A welded joint of steel plates having a plate thickness of 50 mm or more and a method for manufacturing the welded joint are disclosed.
A welded joint of steel plates having a plate thickness of 50 mm or more and a method for manufacturing the welded joint are disclosed.
In the welded joint of the steel plates having a plate thickness T of 50 mm or more, the weld metal includes single-pass-per-layer multiple layers, the first ratio [A/p] of the sectional area A of the weld metal in a direction perpendicular to a weld line to the number of weld layers p is 120.0 mm2/layer or less, and the second ratio [H/W] of the height H to the width of each of the layers of the weld metal is 1.00 or less.
NATIONAL UNIVERSITY CORPORATION UNIVERSITY OF TOYAMA (Japan)
Inventor
Doi, Makoto
Tsubaki, Noritatsu
Guo, Xiaoyu
Abstract
A method for supplying a synthesis gas containing hydrogen gas and carbon oxide gas to a catalyst capable of producing a hydrocarbon from the synthesis gas includes supplying the synthesis gas to the catalyst as a gas containing a poisoning substance that is poisonous to the catalyst.
B01J 8/02 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds
B01D 53/34 - Chemical or biological purification of waste gases
C07C 1/04 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of carbon from carbon monoxide with hydrogen
3.
DIMENSION MEASUREMENT METHOD, DIMENSION MEASUREMENT SYSTEM, AND CONSTRUCTION PREPARATION METHOD
The present invention makes it possible to measure a dimension of a portion without installing a scaffold even if the portion is at high elevation where the dimension cannot be visually measured unless a scaffold is installed. One embodiment of the present invention comprises: a first placement step for moving a first movable body (12) having a dimension portion with at least one dimension known in advance to place the first movable body (12) at a location in the vicinity of an object (80) to be measured; a second placement step for moving a second movable body (14) equipped with an imaging means (14A) to place the second movable body (14) in a photographable area in which a photograph of the object (80) to be measured can be taken; and an imaging step for taking a photograph at each of a first position and a second position different from the first position within the photographable area in which the second movable body (14) has been placed in the second placement step, the photograph including both the object (80) to be measured and the dimension portion as subjects.
NATIONAL UNIVERSITY CORPORATION UNIVERSITY OF TOYAMA (Japan)
Inventor
Doi, Makoto
Hashimoto, Yukako
Urabe, Haruki
Iwasaki, Toshihiko
Tsubaki, Noritatsu
Guo, Xiaoyu
Abstract
Provided is a catalyst which is capable of producing a hydrocarbon from a synthesis gas. The catalyst includes: a metallic catalyst containing a metal compound having activity in a Fischer-Tropsch synthesis reaction, the metallic catalyst being configured to produce the hydrocarbon from the synthesis gas; and a carrier catalyst containing zeolite supporting the metallic catalyst, the metal compound containing cobalt, and at least one metal selected from the group consisting of manganese and ruthenium, and a supported amount of the ruthenium being 0.5 wt % or more and 2 wt % or less.
B01J 37/02 - Impregnation, coating or precipitation
B01J 23/89 - Catalysts comprising metals or metal oxides or hydroxides, not provided for in group of the iron group metals or copper combined with noble metals
This waste treatment device comprises: a gasification/reforming furnace in which waste is thermally decomposed and gasified and a generated gas is reformed to produce a reformed gas; a cooling/cleaning water circulation device for cooling and cleaning the reformed gas produced in the gasification/reforming furnace; a gas purification device for purifying the reformed gas cooled and cleaned in the cooling/cleaning water circulation device; and a chemical-product production device for producing liquid chemical products from, as a raw material, the gas purified in the gas purification device. The cooling/cleaning water circulation device includes a heat collector for collecting some of the sensible heat of the reformed gas and is configured so that the sensible heat collected by the heat collector is supplied to the chemical-product production device.
B09B 3/40 - Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
C10J 3/00 - Production of gases containing carbon monoxide and hydrogen, e.g. synthesis gas or town gas, from solid carbonaceous materials by partial oxidation processes involving oxygen or steam
C10K 1/08 - Purifying combustible gases containing carbon monoxide by washing with liquidsReviving the used wash liquors
6.
GAS PURIFICATION DEVICE, WASTE TREATMENT DEVICE, GAS PURIFICATION METHOD, AND METHOD FOR OPERATING WASTE TREATMENT DEVICE
A gas purification device according to the present invention is provided with: an acid cleaning device that performs cleaning by bringing acid cleaning water into contact with a gas that is generated by thermally decomposing and gasifying a waste; an alkali cleaning device that cleans the gas that has been cleaned by the acid cleaning device, by bringing alkali cleaning water into contact with the gas; and a desulfurization device that removes hydrogen sulfide from the gas that has been cleaned by the alkali cleaning device. The desulfurization device is provided with: a first desulfurization tower which internally comprises a first spray device that sprays a desulfurization liquid onto the gas supplied from the alkali cleaning device; a second desulfurization tower which internally comprises a fluidized bed through which the gas supplied from the first desulfurization tower passes, and a second spray device that sprays the desulfurization liquid toward the fluidized bed; and a regeneration tank which supplies the desulfurization liquid to the first spray device and the second spray device, and recovers the desulfurization liquid used in the first desulfurization tower and the second desulfurization tower. The desulfurization device is also provided with: a first liquid feed pipe for sending the desulfurization liquid from the first desulfurization tower to the regeneration tank; and a second liquid feed pipe for sending the desulfurization liquid from the second desulfurization tower to the regeneration tank.
C10K 1/08 - Purifying combustible gases containing carbon monoxide by washing with liquidsReviving the used wash liquors
C10J 3/00 - Production of gases containing carbon monoxide and hydrogen, e.g. synthesis gas or town gas, from solid carbonaceous materials by partial oxidation processes involving oxygen or steam
7.
EXHAUST GAS PRETREATMENT FACILITY, EXHAUST GAS TREATMENT FACILITY, AND CO2 SEPARATION/RECOVERY METHOD FOR EXHAUST GAS PRETREATMENT FACILITY
B01D 53/82 - Solid phase processes with stationary reactants
B01D 53/83 - Solid phase processes with moving reactants
B01D 53/96 - Regeneration, reactivation or recycling of reactants
B01J 20/08 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group comprising aluminium oxide or hydroxideSolid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group comprising bauxite
This cooling and cleaning system comprises: a cooling and cleaning device for cooling and cleaning a reformed gas discharged from a high-temperature reaction furnace by spraying cooling water onto the reformed gas; and a water seal tank comprising a hollow cylindrical body, a tapered part inclining downward from the inner surface of the body toward the center and having a hole at the center, and a hollow cylindrical internal pipe which is connected to the tapered part, has a hollow portion continuous with the hole of the tapered part, and is disposed inside the body, wherein the reformed gas that has flowed out of the cooling and cleaning device and the cooling water flow to the upper side of the tapered part. The cooling water flows spirally at the tapered part and then flows into the internal pipe.
This cooling cleaning system comprises: a cooling device that sprays first cooling water into a reformed gas discharged from a gasification melting furnace, evaporates the first cooling water, and cools the reformed gas; a sedimentation tank that stores the first cooling water discharged from the cooling device and separates a solid contained in the first cooling water; a cleaning device that sprays second cooling water into the reformed gas cooled by the cooling device and discharged, condenses water vapor contained in the reformed gas, and cools and cleans the reformed gas; and a heat exchanger that cools the second cooling water discharged from the cleaning device. The first cooling water from which the solid has been separated in the sedimentation tank is sent to the cooling device and sprayed into the reformed gas, and part of the second cooling water sprayed into the reformed gas in the cleaning device merges with the first cooling water.
A waste feeding device according to the present invention comprises: a hollow casing that has an insertion port into which waste is inserted, and that is connected to a melting furnace; a screw shaft that is disposed in the casing, has a spiral blade, and feeds the waste toward the melting furnace; a forming unit that is provided more toward the melting furnace side than the spiral blade and in which waste is compressed and formed into a cylindrical shape; and a holding unit that is provided more toward the melting furnace side than the forming unit and holds waste that is formed into a cylindrical shape by the forming unit. The compressed waste can prevent heat and gas from the melting furnace.
B09B 3/40 - Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
B65G 33/14 - Screw or rotary spiral conveyors for fluent solid materials comprising a screw or screws enclosed in a tubular housing
F23G 5/027 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels including pretreatment pyrolising or gasifying
A method for operating a waste treatment device according to the present invention operates a waste treatment device comprising a gasification/reforming furnace that thermally decomposes waste, gasifies the product, and reforms the produced gas to generate reformed gas, a gas purification device that purifies the reformed gas generated by the gasification/reforming furnace, and a chemical product production device that produces a liquid chemical product using the purified gas purified by the gas purification device as a raw material, wherein carbon dioxide remaining in the exhaust gas from the process for producing the chemical product by the chemical product production device is supplied to the gasification/reforming furnace.
B09B 3/40 - Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
C10K 3/00 - Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
Provided is a multiple-tube type reaction container which is excellent in cooling efficiency and in which a filling catalyst can be easily and efficiently replaced. A multiple-tube type reaction container 1 according to the present invention comprises: a catalyst-provided inner-side cooling tube 3 through which a cooling fluid flows and which is provided with a catalyst 9 on the outer circumferential surface; a reaction gas flow tube 5 into which the catalyst-provided inner-side cooling tube 3 is removably inserted and through which a reaction gas flows; and an outer-side cooling container 7 which is provided around the outer circumference of the reaction gas flow tube 5 and through which a cooling fluid flows to cool the outer circumferential surface of the reaction gas flow tube 5. The catalyst 9 is provided to be divided, in the flow direction of the cooling fluid, into a plurality of pieces, which are set to be replaceable individually.
B01J 8/06 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds in tube reactorsChemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the solid particles being arranged in tubes
The present invention achieves a multiple-tube type reaction container which has excellent cooling efficiency and facilitates replacement of a filling catalyst. A multiple-tube type reaction container 1 according to the present invention is characterized by comprising: a catalyst filling container 3 through which a reaction gas flows and which is filled with a catalyst; an inside cooling tube 5 which vertically penetrates the inside of the catalyst filling container 3, is arranged movably in the vertical direction, and cools the catalyst in the catalyst filling container 3 from the inside by having a cooling fluid passing thereinside; and an outer shell container 7 which is provided on the outer circumference of the catalyst filling container 3 and cools the catalyst filling container 3 from the outside by having a cooling fluid passing thereinside. The multiple-tube type reaction container is also characterized in that: the catalyst filling container 3 has, in the upper end surface thereof, a filling port 13 for filling a catalyst, and has, in the lower end surface thereof, a discharge port 15 for discharging the catalyst; and the inside cooling tube 5 functions as a plug for opening and closing the discharge port 15 of the catalyst filling container 3.
B01J 8/06 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds in tube reactorsChemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the solid particles being arranged in tubes
The present invention provides a multi-tube-type reaction vessel that has exceptional cooling efficiency and facilitates replacement of a catalyst to be filled. A multi-tube-type reaction vessel 1 according to the present invention is characterized by comprising: a catalyst fixed inner-side cooling pipe 3 through which a cooling fluid flows in the interior, and in which a porous catalyst layer 9 is fixed to an outer peripheral surface; a reaction gas passage pipe 5 into which the catalyst fixed inner-side cooling pipe 3 is removably inserted, and through which a reaction gas flows in the interior; and an outer-side cooling container 7 that is provided to the outer periphery of the reaction gas passage pipe 5 and cools the outer peripheral surface of the reaction gas passage pipe 5 by allowing the cooling fluid to flow therethrough.
The purposes of the present invention are to obtain a multi-tubular reaction vessel having excellent cooling efficiency and to obtain a multi-tubular reaction vessel in which a packed catalyst can be easily replaced. A multi-tubular reaction vessel 1 according to the present invention is characterized by comprising: a catalyst packing vessel 3 in which a reaction gas flows and into which a catalyst is packed; an inner cooling pipe 5 which is provided to the inside of the catalyst packing vessel 3 along the packing direction and in which a cooling fluid flows to cool the catalyst within the catalyst packing vessel 3; and an outer-shell vessel 7 which is provided around the outer periphery of the catalyst packing vessel 3 and in which a cooling fluid flows to cool the catalyst packing vessel 3 from outside.
B01J 8/06 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds in tube reactorsChemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the solid particles being arranged in tubes
B01J 8/02 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds
Provided is a welded joint of a steel plate having a plate thickness of 50-160 mm, the welded joint having a sound welded metal with no weld defects such as high-temperature cracking and fusion defects, and being provided with both high strength and excellent low-temperature toughness. Also provided is a method for manufacturing the same. The welded joint of a steel plate having a plate thickness T of 50-160 mm is configured such that the welded metal is composed of three or more layers and the width W of each layer excluding the first layer and the outermost surface layer of the welded metal is in the range from 5.0 mm to 0.4 T mm.
Provided are: a welded joint of steel plates having a plate thickness of at least 50 mm, the welded joint including sound welded metal without welding defects such as high-temperature cracking and incomplete fusion, and having both high strength and excellent low-temperature toughness; and a method for manufacturing the welded joint. In the welded joint of steel plates having a plate thickness T of at least 50 mm, the weld metal comprises multiple layers having of one pass per layer, wherein a first ratio [A/p] between a cross-sectional area A in a direction perpendicular to a welding line of the weld metal and a number p of weld layers is at most equal to 120.0 mm2/layer, and a second ratio [H/W] between a height H and a width W of each layer in the weld metal is at most equal to 1.00.
NATIONAL UNIVERSITY CORPORATION UNIVERSITY OF TOYAMA (Japan)
Inventor
Doi, Makoto
Hashimoto, Yukako
Urabe, Haruki
Iwasaki, Toshihiko
Tsubaki, Noritatsu
Guo, Xiaoyu
Abstract
The purpose of the present invention is to improve the yield of C5 or higher hydrocarbons that are manufactured using carbon monoxide and hydrogen as raw materials. The present invention provides a catalyst having a metal-based catalyst that contains a metal compound having activity in a Fischer-Tropsch synthesis reaction and that generates hydrocarbons from a synthesized gas, and a carrier catalyst that includes a zeolite carrying the metal-based catalyst, said catalyst enabling hydrocarbons to be manufactured from the synthesized gas, wherein the metal compound contains at least one type of metal selected from the group consisting of cobalt, manganese, and ruthenium, the amount of manganese carried being 1-3 wt%, the amount of Ru carried being 0.5-2 wt%, and the amount of Co carried being 10-30 wt%. The zeolite includes a porous zeolite that breaks down carbon chains in the generated hydrocarbons, the pores in the porous zeolite being mesopores having an opening diameter of 2-50 nm inclusive, and the ratio of silicon to aluminum in the zeolite being 2.5-3.5 inclusive.
C07C 1/04 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of carbon from carbon monoxide with hydrogen
C07C 9/14 - Acyclic saturated hydrocarbons with five to fifteen carbon atoms
C07C 9/22 - Acyclic saturated hydrocarbons with more than fifteen carbon atoms
The present invention increases the feasibility of carbon-neutrality of slag. The present disclosure is an information processing method performed by an information processing device 1, wherein: the information processing device 1 includes a control unit 11, a communication unit 12, and a storage unit 13 and is communicably connected with a network via the communication unit 12; and the control unit 11 associates slag slip information that pertains to produced slag and verification information that verifies that the electric power used in producing the slag is electric power for which a non-fossil value or zero-emission value is defined, and stores the slag slip information and the verification information in the storage unit 13.
This diesel engine comprises a combustion chamber and a fuel injection means for injecting a fuel oil and gaseous ammonia, which serve as an ignition source, into the combustion chamber, wherein an ammonia premixed gas is formed in the combustion chamber from the fuel oil and gaseous ammonia, which are injected into the combustion chamber by the fuel injection means, to be subjected to mixed combustion. The diesel engine comprises a setting means capable of setting a plurality of different ammonia mixing ratio values and a control means for adjusting an excess air ratio value in the total sum of the fuel oil and ammonia, which are injected by the injection means, on the basis of the ammonia mixing ratio value set by the setting means.
F02M 25/00 - Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
F02D 19/08 - Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with pluralities of fuels, e.g. alternatively with light and heavy fuel oil, other than engines indifferent to the fuel consumed simultaneously using pluralities of fuels
23.
POWER GENERATION SYSTEM, CONTROL DEVICE, CONTROL METHOD, AND PROGRAM
The purpose of the present invention is to continue the supply of power to a load facility without stopping, even when system power enters a power failure state. This power generation system comprises: a power generator that controls generated power by driving of an internal combustion engine having a speed governor; a power load configured to be able to supply external power from an external commercial power system and the generated power of the power generator; a simulated load that consumes the generated power of the power generator together with the power load; and a control unit that can control the power consumption of the simulated load. The control unit performs control to set the power consumption of the simulated load to a prescribed power consumption before acquiring a power failure signal indicating detection or prediction of a power failure of the commercial power system, as power increase/decrease control that can change the power consumption of the simulated load to any power value in a state in which the power generation device of the power generator is being continuously performed. When the power failure signal is acquired, the control unit performs control to change the power consumption of the simulated load from the prescribed power consumption to another power consumption.
H02J 9/08 - Circuit arrangements for emergency or stand-by power supply, e.g. for emergency lighting in which the distribution system is disconnected from the normal source and connected to a standby source with automatic change-over requiring starting of a prime-mover
24.
ELECTRIC POWER GENERATION SYSTEM, CONTROL DEVICE, CONTROL METHOD, AND PROGRAM
A purpose of the present invention is to activate and operate in a stable manner an electric power generator that is required after a supply of electric power from a commercial electric power grid or a commercial electric power supply has stopped. The present invention comprises: an electric power generator that controls generated electric power by being driven by an engine provided with a speed regulator; a dummy load having a load capacity that is set such that the dummy load is capable of consuming generated electric power of the electric power generator when the engine is driving, and is capable of regulating electric power consumption; a dummy-load-regulating unit configured so as to be capable of regulating the electric power consumption of the dummy load; and a control unit capable of controlling the electric power consumption of the dummy load by controlling the dummy-load-regulating unit. A plurality of pairs of dummy loads and dummy-load-regulating units are provided. At an activation time of the electric power generator, the control unit controls at least part of the dummy loads among the plurality of dummy loads, so as to power on said dummy loads with respect to the electric power generator, said dummy loads having a load capacity set to be equal to or greater than a load having a predetermined electric power consumption that does not cause tripping to occur in an activation operation of the electric power generator.
H02P 9/04 - Control effected upon non-electric prime mover and dependent upon electric output value of the generator
H02J 9/08 - Circuit arrangements for emergency or stand-by power supply, e.g. for emergency lighting in which the distribution system is disconnected from the normal source and connected to a standby source with automatic change-over requiring starting of a prime-mover
25.
POWER GENERATION SYSTEM, CONTROL DEVICE, CONTROL METHOD, AND PROGRAM
The purpose of the present invention is to perform, with high responsiveness, control for maintaining reverse flow power equal to or lower than a prescribed upper limit. The present invention comprises: a power generator which is configured to be capable of reverse flow in which generated power is controlled by driving an internal combustion engine including a governor, and at least some of the generated power is output to a commercial power system; a simulated load which consumes the generated power from the power generator together with a power load, when the generated power from the power generator is supplied to the power load in a state where the internal combustion engine is being driven; a reverse flow power measurement unit which can measure the reverse flow power from the power generator to the commercial power system; and a control unit which can control the power consumption of the simulated load on the basis of a value of the reverse flow power measured by the reverse flow power measurement unit, wherein, when some of the generated power from the power generator is made to reversely flow, in the case where the reverse flow power measured by the reverse flow power measurement unit is equal to or greater than a preset upper limit, control is performed such that the power that has exceeded the upper limit of the reverse flow power of the generated power from the power generator is consumed by the simulated load.
The purpose of the present invention is stable activation and driving a power generator, which is required after stoppage of the reception of electric power from a commercial electric power system or a normal power supply. The present invention comprises: a power generator which controls generated power by the driving of an internal combustion engine provided with a speed governor; simulated loads in which a load capacity is set so as to be able to consume the generated power of the power generator and be able to adjust power consumption in a state in which the internal combustion engine is driven; simulated load adjustment units which are capable of adjusting the power consumption of the simulated loads; and a control unit which is capable of controlling the power consumption of the simulated load by controlling the simulated load adjustment unit. The simulated loads and the simulated load adjustment units are provided in a plurality of pairs. When the power generator is activated, the control unit performs control to introduce, with respect to the power generator, at least some of the simulated loads, among the plurality of simulated loads, in which load capacities are set to be equal to or greater than a load of prescribed power consumption that does not cause tripping in the activation operation of the power generator.
A method for synthesizing a zirconium complex includes setting a temperature of a mixed solution at a certain temperature or more to synthesize a zirconium complex, the mixed solution being obtained by mixing: an organic solvent containing an organic substance having water miscibility; a chelating agent solution in which a chelating agent is dissolved; and zirconium dissolved in an acidic solution.
The present invention increases the feasibility of a carbon-neutral steel product. The present disclosure is a method for producing a steel product using an electric furnace that employs power defined by a non-fossil fuel value or a zero-emissions value.
This hanging scaffold comprises: a post 120 that can be inserted from a ceiling opening 21 of a hollow structure (boiler 10), and is provided in the vertical direction inside the hollow structure (10); a frame 130 capable of vertical movement along the post 120; a beam 140 mounted on the frame 130 and capable of extending/contracting and rotating in a plane orthogonal to the post 120; a wall abutment unit 142 provided at an end of the beam 140 for supporting the beam 140 by abutting on an inner wall surface 20W of the hollow structure (10); a floor panel 160, 162, 164 attached to the beam 140; and a handrail 170, 172 attached to the floor panel 160, 162, 164. Consequently, a hanging scaffold which can be installed very easily regardless of the installation position or place is provided.
E04G 3/24 - Scaffolds essentially supported by building constructions, e.g. adjustable in height specially adapted for particular parts of buildings or for buildings of particular shape, e.g. chimney stacks or pylons
E04G 3/28 - Mobile scaffoldsScaffolds with mobile platforms
A method for synthesizing a zirconium complex includes: mixing a solvent containing an organic substance having a dipole moment of 3.0 D or more, a chelating agent solution in which a chelating agent containing a structure represented by General Formula (1) or General Formula (2) is dissolved, and zirconium dissolved in an acidic solution, to obtain a mixed solution; and setting the mixed solution at a predetermined temperature or more to synthesize a zirconium complex.
C07D 255/02 - Heterocyclic compounds containing rings having three nitrogen atoms as the only ring hetero atoms, not provided for by groups not condensed with other rings
The purpose of the present invention is to improve water recovery rate while suppressing generation of scale in the case of extracting water from treatment-target water including impurities. This water treatment device is provided with: a plurality of flocculation and sedimentation parts that flocculate and eliminate at least a portion of impurities from treatment-target water; and a plurality of water extraction parts that each have a forward osmosis membrane and/or a reverse osmosis membrane capable of extracting water from a water-containing solution, containing water as a solvent, so as to extract permeable water from the treatment-target water, and that also discharge concentrated water obtained as a result of extraction of the permeable water from the treatment-target water. Along the flow direction of the treatment-target water, a first water extraction part is disposed at the stage after a first flocculation and sedimentation part, a second flocculation and sedimentation part is disposed at the stage after the first water extraction part, and a second water extraction part is disposed at the stage after the second flocculation and sedimentation part. The second water extraction part extracts permeable water from the concentrated water discharged from the first water extraction part, and discharges highly concentrated water which is obtained by further concentrating the concentrated water discharged from the first water extraction part, whereas the first flocculation and sedimentation part and the second flocculation and sedimentation part flocculate and eliminate at least a portion of silica.
C02F 1/44 - Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
B01D 61/00 - Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltrationApparatus, accessories or auxiliary operations specially adapted therefor
The purpose of the present invention is to reduce the added amount of a flocculant when treating a silica-containing water. A water treatment device for removing silica from silica-containing water to be treated, the device comprising: a reaction part which retains the water to be treated and in which silica contained in the water to be treated is reacted with a chemical agent; a flocculant addition part that is provided to the reaction part for adding a flocculant that contains an aluminum salt and that is capable of flocculating silica; a precipitation part which is provided downstream of the reaction part in the flow direction of the water being treated and in which the silica and the chemical agent which have reacted in the reaction part flocculate and precipitate as a flocculent precipitation sludge; a sludge transport part that introduces the flocculent precipitation sludge precipitated in the precipitation part, as a chemical agent, into the reaction part; and a pH adjustment part for adjusting, to 8-12, the pH of the water being treated that is retained in at least one of the reaction part and the precipitation part.
06 - Common metals and ores; objects made of metal
07 - Machines and machine tools
11 - Environmental control apparatus
37 - Construction and mining; installation and repair services
40 - Treatment of materials; recycling, air and water treatment,
Goods & Services
Large metal containers for environmental and energy
technology as well as systems formed from them; buildings,
transportable, of metal; chimneys made of metal for energy
technology, for the power plant industry, lignite power
plants, waste incineration plants; ventilation ducts
(chimney pipes); inner cables (tubes) made of stainless
steel; metal pipes, large pipelines, exhaust steam and
dephlegmator pipes; compensator pipes, flue gas ducts in the
form of gas pipes, superheated steam pipes; steel buildings;
common metals and their alloys; goods of metal, included in
this class; metal building materials (not for electrical
purposes). Machines and machine-driven devices as well as systems
formed from them for energy generation; blowing engines;
sound absorbers being parts of machines; heat exchangers (as
machine parts); lifting devices (machines), cranes; pressing
machines; engines, other than for land vehicles; turbines,
couplings and transmission components (except for land
vehicles); filters (included in this class). Gas / heating boilers, including industrial steam boilers,
water tube boilers, saturated steam and superheated steam
boilers, hot water boilers, waste heat boilers, smoke tube
boilers, special boilers for thermal disposal and
afterburning; torches, ventilation systems, in particular
exhaust air chimneys and exhaust air systems; cooling
chimneys. Construction, in particular steel construction, structural
steel construction, prefabricated steel construction,
construction and assembly work, as well as maintenance and
repair of (turnkey) industrial and functional buildings, of
boiler and container systems, of compressed air systems, of
heating and cooling systems, of air conditioning and
ventilation systems, of energy generation systems; pipeline
laying; insulation construction work; insulation work,
sealing work, preservation work, namely being corrosion
protection (included in this class); installation services. Welding of steel structures for constructional purposes.
The objective of the present invention is to synthesize a zirconium complex by making even a low concentration of 1,4,7,10-tetraazacyclododecane-1,4,7,10-tetraacetic acid (DOTA) react with radioactive zirconium at a high reaction rate. A mixed solution, obtained by finally mixing zirconium dissolved in an acidic solution into a solution in which a solution containing 40-95 vol% of an organic substance having water miscibility is mixed with a compound containing a chelating agent represented by DOTA, etc., is heated to a prescribed temperature of 35°C or higher to thereby synthesize a zirconium complex. The acidic solution is a hydrochloric acid, and the organic substance is methanol or ethanol.
C07D 255/02 - Heterocyclic compounds containing rings having three nitrogen atoms as the only ring hetero atoms, not provided for by groups not condensed with other rings
C07D 257/02 - Heterocyclic compounds containing rings having four nitrogen atoms as the only ring hetero atoms not condensed with other rings
An object is to synthesize a zirconium complex by reacting 1,4,7,10-tetraazacyclododecane-1,4,7,10- tetraacetic acid (DOTA), even with a small concentration, and radioactive zirconium with a high reaction rate. A mixed solution obtained by lastly mixing zirconium dissolved in an acidic solution into a solution in which a solution containing an organic substance having water miscibility in an amount of 40% by volume or more and 95% by volume or less and a compound containing a chelating agent represented by DOTA or the like are mixed together is heated up to a certain temperature of 35°C or more to synthesize a zirconium complex. The acidic solution is hydrochloric acid, and the organic substance is methanol or ethanol.
C07D 255/02 - Heterocyclic compounds containing rings having three nitrogen atoms as the only ring hetero atoms, not provided for by groups not condensed with other rings
C07D 257/02 - Heterocyclic compounds containing rings having four nitrogen atoms as the only ring hetero atoms not condensed with other rings
C22B 3/44 - Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
The purpose of the present invention is to react radioactive zirconium at a high reaction rate to synthesize a zirconium complex even using low-concentration DOTA or NOTA. A mixed solution, obtained by finally mixing zirconium dissolved in an acidic solution into a solution obtained by mixing a solution that includes 1-95 vol% (inclusive) of an organic substance having a dipole moment of 3.0D or higher and a compound that includes a chelating agent represented by 1,4,7,10-tetraazacyclododecane-1,4,7,10-tetraacetic acid (DOTA), etc., is heated to a prescribed temperature of 35°C or higher to synthesize a zirconium complex. The acidic solution is hydrochloric acid, and the organic substance is at least one selected from the group consisting of dimethyl sulfoxide (DMSO), N,N-dimethylformamide (DMF), N-methylformamide (NMF), N-methylpyrrolidone (NMP), and urea.
C07D 255/02 - Heterocyclic compounds containing rings having three nitrogen atoms as the only ring hetero atoms, not provided for by groups not condensed with other rings
C07D 257/02 - Heterocyclic compounds containing rings having four nitrogen atoms as the only ring hetero atoms not condensed with other rings
C07D 403/06 - Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, not provided for by group containing two hetero rings linked by a carbon chain containing only aliphatic carbon atoms
C07D 403/12 - Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, not provided for by group containing two hetero rings linked by a chain containing hetero atoms as chain links
The purpose of the present invention is to react radioactive zirconium at a high reaction rate to synthesize a zirconium complex even using low-concentration DOTA or NOTA. A mixed solution, obtained by finally mixing zirconium dissolved in an acidic solution into a solution obtained by mixing a solution that includes 1-95 vol% (inclusive) of an organic substance having a dipole moment of 3.0D or higher and a compound that includes a chelating agent represented by 1,4,7,10-tetraazacyclododecane-1,4,7,10-tetraacetic acid (DOTA), etc., is heated to a prescribed temperature of 35°C or higher to synthesize a zirconium complex. The acidic solution is hydrochloric acid, and the organic substance is at least one selected from the group consisting of dimethyl sulfoxide (DMSO), N,N-dimethylformamide (DMF), N-methylformamide (NMF), N-methylpyrrolidone (NMP), and urea.
C07D 255/02 - Heterocyclic compounds containing rings having three nitrogen atoms as the only ring hetero atoms, not provided for by groups not condensed with other rings
C07D 257/02 - Heterocyclic compounds containing rings having four nitrogen atoms as the only ring hetero atoms not condensed with other rings
C07D 403/12 - Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, not provided for by group containing two hetero rings linked by a chain containing hetero atoms as chain links
The purpose of the invention is to provide a reinforcement beam for reinforcing a plurality of post members of a structure. A reinforcement beam has a reinforcement beam body 10 comprising a tube, a first cover 6 provided on one end of the reinforcement beam body 10, and a second cover 7 provided on the other end of the reinforcement beam body 10, and is configured such that: a first post member coupling part 4 for mounting to a first post member from among a plurality of post members is formed by the first cover 6 and the one end side of the reinforcement beam body on which the first cover is provided, and a second post member coupling part 5 for mounting to a second post member different than the first post member from among the plurality of post members is formed by the second cover 7 and the other end of the reinforcement beam body 10 on which the second cover 7 is provided; and, when the reinforcement beam is coupled to the first post member, the first post member can be enclosed with the first post member coupling part 4 and a first post member coupling part 4 of another reinforcement beam mounted on the first post member.
The present invention relates to a reinforcement beam for reinforcing a post member of a structure. The reinforcement beam is used for a structure that has a first post member the bottom end of which is fixed to the ground, a second post member that is adjacent to the first post member, a third post member that is adjacent to the first post member and that is in a position so that the direction that the first post member and the third post member are arranged intersects the direction that the first post member and the second post member are arranged, and an upper structure that is supported by a plurality of post members including the first to the third post members. The reinforcement beam has a reinforcement beam body, a first junction that is provided on one end of the reinforcement beam body and that is mounted to the first post member, and a second junction that is provided on the other end of the reinforcement beam body and that is mounted to the second post member. The first junction is configured so as to enclose the first post member in conjunction with another reinforcement beam mounted between the first post member and the third post member when the first junction is mounted to the first post member, and the second junction is configured so as to enclose the second post member in conjunction with another reinforcement beam mounted to the second post member when the second junction is mounted to the second post member.
22 is reduced. This diesel engine has a combustion chamber and a fuel supply means that supplies gas-form ammonia and fuel oil serving as an ignition source into the combustion chamber, and a premixed ammonia gas is formed and co-fired in the combustion chamber by the fuel supply means. The combustion chamber interior has a control means that performs control so as to form a premixed ammonia gas such that the ammonia concentration at the inner side wall surface of the combustion chamber is higher than in the center of the combustion chamber, and the control means makes adjustments so that the excess air ratio is lower than the excess air ratio during operation performed using only fuel oil.
F02M 25/00 - Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
JAPAN ASSOCIATION OF CARGO-HANDLING MACHINERY SYSTEMS (Japan)
MITSUI E&S MACHINERY CO., LTD. (Japan)
JFE ENGINEERING CORPORATION (Japan)
Inventor
Kiyohara Hideto
Shiraishi Tetsuya
Noguchi Hitoshi
Yoshida Yoshiharu
Inui Ryoma
Murano Kenichi
Abstract
Provided is an operation method for container terminals that allows efficient operation by improving operation in a transfer area. The operation method for container terminals that have a storage area of storage blocks 14 disposed vertically is characterized in that: a container transport vehicle 24 circles around between a storage block 14 and an apron or the like; a container 30 is transferred between the container transport vehicle 24 and the storage block 14 on a lengthwise side thereof; a transfer area 28 to transfer a container 30 between the container transport vehicle 24 and an external vehicle 34 is established in an area further inland than the land side end; external vehicles 34 have an external travel lane 36 established; and the transfer of a container 30 in the transfer area 28 is performed in a state in which the container transport vehicle 24 and the external vehicle 34 are both facing a direction intersecting the lengthwise direction of the storage block 14.
A temperature-sensitive water absorbent which comprises a polyoxyalkylene adduct represented by general formula R1nnR2(1), the water absorbent being intended to attain a high osmotic pressure and a lower cloud point. In general formula (1), R16-136-13 monohydric alcohol; R21-132-42-4 oxyalkylene group; and n, indicating the average number of moles of the alkylene oxide added, is 1-235, and when n is 2 or larger, then the two or more AO moieties may be the same or different. R16-136-13 aliphatic monohydric alcohol residue, aliphatic linear monohydric alcohol residue, or aliphatic branched monohydric alcohol residue.
B01D 61/00 - Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltrationApparatus, accessories or auxiliary operations specially adapted therefor
C02F 1/44 - Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
Provided is a gas absorption/refinement device that selectively absorbs and refines, by means of an absorbing liquid, a specific gas component from within a gas to be treated, wherein the gas absorption/refinement device makes it possible to reduce the number of pumps and other such machines for sending the absorbing liquid and any remaining gas to a subsequent process, and/or to reduce the number of operations of said machines. A gas absorption/refinement device 1 according to the present invention comprises: an injector 3 that brings a concentrated absorbing liquid into contact with a gas to be absorbed and raises the pressure to cause a specific gas component from within the gas to be absorbed to be absorbed by the concentrated absorbing liquid and produce a diluted absorbing liquid; a gas-liquid separator 5 that receives a supply of the diluted absorbing liquid of which the pressure was raised by the injector 3, as well as a supply of the remaining gas, and performs gas-liquid separation; a regeneration tower 7 that receives the diluted absorbing liquid separated by the gas-liquid separator 5 and regenerates the diluted absorbing liquid to the concentrated absorbing liquid; a concentrated-absorbing-liquid supply line 9 that supplies the concentrated absorbing liquid regenerated in the regeneration tower 7 to the injector 3; and a flow rate adjustment valve 11 provided to the concentrated-absorbing-liquid supply line 9, the flow rate adjustment valve 11 adjusting the flow rate of the concentrated absorbing liquid being supplied.
06 - Common metals and ores; objects made of metal
07 - Machines and machine tools
11 - Environmental control apparatus
35 - Advertising and business services
37 - Construction and mining; installation and repair services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Large containers of metal for environmental engineering and energy technology, and installations composed thereof; Transportable buildings of metal; Chimneys of metal for use in energy technology, for the power plant industry, lignite power plants, waste incineration installations; Ventilation funnels (chimney shafts); Internal flues (pipes) of stainless steel; Metal pipes, Large pipelines, exhaust steam pipes and dephlegmator pipes; Compensator pipes, flue gas ducts in the form of gas pipes, superheated steam pipes; Steel buildings; Common metals and their alloys; Unprocessed and semi-processed materials of metal, not specified for use; Non-electric building materials of metal. Machines and mechanically driven apparatus, and installations composed thereof for generating energy; Blowing engines; Sound absorbers being parts of machines; Heat exchangers (parts of machines); Elevating apparatus (machines), Cranes [lifting and hoisting apparatus]; Pressing machines; Engines and motors; Turbines, machine coupling and transmission components, except for land vehicles; Filters (included in class 7). Gas/heating boilers, including industrial steam boilers, water tube boilers, saturated steam boilers and superheated steam boilers, Hot water boilers, waste heat recuperators, fire-tube boilers, Special boilers for thermal disposal and post-combustion; Flaming torches, Ventilating installations, In particular exhaust air chimneys and exhaust air installations; Cooling chimneys; Hot water and steam generator and boiler installation and their fittings; Steam generators for incinerators and their fittings; Installations for exhaust/ventilating gas scrubbing, in particular for flue gas scrubbing. Trading in hot water and steam generators, steam boiler installations and related apparatus and aggregates of all types including components therefor, hot water boilers of all types, steam generators for incinerators including components therefor, industry and thermal power stations, installations for exhaust/ventilating gas scrubbing and flue gas purification. Building, installation and repair of gas/heating boilers, ventilating installations and heat exchangers; Construction and repair of electricity or gas generating installations and coal extraction installations; Construction and repair of electrical power, gas and water distribution networks and telecommunication lines and networks; Construction and repair of environmental protection installations; Boiler cleaning and repair; Building consultancy; Assembling, commissioning of hot water and steam generators, steam boiler installations and related apparatus and aggregates of all types including components therefor, hot water boilers of all types, steam generators for incinerators including components therefor, industry and thermal power stations, installations for exhaust/ventilating gas scrubbing and flue gas purification; Maintenance, modernisation, repair, assembling and commissioning of energy generation, installations for the chemical and petrochemical industry, installations for wood, waste and surplus disposal, installations for water treatment. Treatment of materials, Namely surface treatment; Mechanical processing of materials made of metal or chemical processing or chemical conversion of materials; Rental of generators; Recycling of waste and trash; Boilermaking; Generating of energy, in particular electricity; Generation of gas and electricity; Incineration of waste and trash; Recycling of waste and valuable materials; Recycling of chemicals; Waste treatment [transformation]; Selection of waste and recovered raw materials (for processing); Steam and electricity generating from biomass. Engineering services; Technical research; Technical project studies; Technical planning, evaluation, estimation, reports and research in relation to electrical energy; Research and development relating to the generation and distribution of electricity and gas, water distribution, coal extraction, telecommunications and environmental protection; Testing and quality inspection of electric apparatus, equipment and instruments; Engineering in the field of production of energy; Planning and construction of hot water and steam generators, steam boiler installations and related apparatus and aggregates of all types including components therefor, hot water boilers of all types, steam generators for incinerators including components therefor, industry and thermal power stations, installations for exhaust/ventilating gas scrubbing and flue gas purification; Engineering services in the field of engineering/machine construction; Technical consulting services in the field of industry installations.
06 - Common metals and ores; objects made of metal
07 - Machines and machine tools
11 - Environmental control apparatus
35 - Advertising and business services
37 - Construction and mining; installation and repair services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Large containers of metal for environmental engineering and energy technology, and installations composed thereof; Transportable buildings of metal; Chimneys of metal for use in energy technology, for the power plant industry, lignite power plants, waste incineration installations; Ventilation funnels (chimney shafts); Internal flues (pipes) of stainless steel; Metal pipes, Large pipelines, exhaust steam pipes and dephlegmator pipes; Compensator pipes, flue gas ducts in the form of gas pipes, superheated steam pipes; Steel buildings; Common metals and their alloys; Unprocessed and semi-processed materials of metal, not specified for use; Non-electric building materials of metal; all the aforementioned goods in the fields of energy supply, thermal waste treatment and production of process steam for industrial processes. Machines and mechanically driven apparatus, and installations composed thereof for generating energy; Blowing engines; Sound absorbers being parts of machines; Heat exchangers (parts of machines); Elevating apparatus (machines), Cranes [lifting and hoisting apparatus]; Pressing machines; Engines and motors; Turbines, machine coupling and transmission components, except for land vehicles; Filters (included in class 7); all the aforementioned goods in the fields of energy supply, thermal waste treatment and production of process steam for industrial processes. Gas/heating boilers, including industrial steam boilers, water tube boilers, saturated steam boilers and superheated steam boilers, Hot water boilers, waste heat recuperators, fire-tube boilers, Special boilers for thermal disposal and post-combustion; Flaming torches, Ventilating installations, In particular exhaust air chimneys and exhaust air installations; Cooling chimneys; Hot water and steam generator and boiler installation and their fittings; Steam generators for incinerators and their fittings; Installations for exhaust/ventilating gas scrubbing, in particular for flue gas scrubbing. Trading in hot water and steam generators, steam boiler installations and related apparatus and aggregates of all types including components therefor, hot water boilers of all types, steam generators for incinerators including components therefor, industry and thermal power stations, installations for exhaust/ventilating gas scrubbing and flue gas purification. Building, installation and repair of gas/heating boilers, ventilating installations and heat exchangers; Construction and repair of electricity or gas generating installations and coal extraction installations; Construction and repair of electrical power, gas and water distribution networks and telecommunication lines and networks; Construction and repair of environmental protection installations; Boiler cleaning and repair; Building consultancy; Assembling, commissioning of hot water and steam generators, steam boiler installations and related apparatus and aggregates of all types including components therefor, hot water boilers of all types, steam generators for incinerators including components therefor, industry and thermal power stations, installations for exhaust/ventilating gas scrubbing and flue gas purification; Maintenance, modernisation, repair, assembling and commissioning of energy generation, installations for the chemical and petrochemical industry, installations for wood, waste and surplus disposal, installations for water treatment; all the aforementioned services in the fields of energy supply, thermal waste treatment and production of process steam for industrial processes. Treatment of materials, Namely surface treatment; Mechanical processing of materials made of metal or chemical processing or chemical conversion of materials; Rental of generators; Recycling of waste and trash; Boilermaking; Generating of energy, in particular electricity; Generation of gas and electricity; Incineration of waste and trash; Recycling of waste and valuable materials; Recycling of chemicals; Waste treatment [transformation]; Selection of waste and recovered raw materials (for processing); Steam and electricity generating from biomass. Engineering services; Technical research; Technical project studies; Technical planning, evaluation, estimation, reports and research in relation to electrical energy; Research and development relating to the generation and distribution of electricity and gas, water distribution, coal extraction, telecommunications and environmental protection; Testing and quality inspection of electric apparatus, equipment and instruments; Engineering in the field of production of energy; Planning and construction of hot water and steam generators, steam boiler installations and related apparatus and aggregates of all types including components therefor, hot water boilers of all types, steam generators for incinerators including components therefor, industry and thermal power stations, installations for exhaust/ventilating gas scrubbing and flue gas purification; Engineering services in the field of engineering/machine construction; Technical consulting services in the field of industry installations; all the aforementioned services in the fields of energy supply, thermal waste treatment and production of process steam for industrial processes.
46.
WATER TREATMENT APPARATUS, WATER TREATMENT METHOD, AND METHOD OF STARTING WATER TREATMENT APPARATUS
A water treatment apparatus is configured to: allow a diluted draw solution to flow out, which is obtained by causing water to move to a draw solution having a cloud point from a water-containing solution containing water as a solvent via a semipermeable membrane to dilute the draw solution, and discharges the water-containing solution as a concentrated water-containing solution that is concentrated; heat the diluted draw solution to a temperature equal to or higher than the cloud point; separate the heated diluted draw solution into a water-rich solution and the draw solution having water content lower than that of the water-rich solution; cool a liquid and allows the liquid to flow out as a coolant; perform heat exchange between the coolant and the draw solution; and perform heat exchange between the diluted draw solution and the water-rich solution.
B01D 61/00 - Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltrationApparatus, accessories or auxiliary operations specially adapted therefor
C02F 1/44 - Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
C02F 1/02 - Treatment of water, waste water, or sewage by heating
B01D 21/00 - Separation of suspended solid particles from liquids by sedimentation
HTT of the tapered pipe 14 is substantially 1.5/100. An antenna 24 is provided to an upper section of the iron tower 10. The iron tower 10 is provided with the function of emitting gas.
E04H 12/00 - TowersMasts or polesChimney stacksWater-towersMethods of erecting such structures
E04H 9/14 - Buildings, groups of buildings or shelters adapted to withstand or provide protection against abnormal external influences, e.g. war-like action, earthquake or extreme climate against other dangerous influences, e.g. tornadoes, floods
48.
Ballast water treatment device and ballast water treatment method
A ballast water treatment device includes an oxidant supply amount control device in which a storage unit stores a relationship between an absorbance of a raw water for a ballast and a dissolved organic carbon concentration thereof and another relationship between the dissolved concentration and a residual oxidant concentration required after a predetermined time from an oxidant supply, to kill organisms and to suppress their regrowth in the ballast. A calculation unit derives the required residual oxidant concentration corresponding to the absorbance measured by a meter by referring to the relationships and calculates a target oxidant supply amount using the required residual oxidant concentration. For the target, a control unit controls an oxidant supply device.
06 - Common metals and ores; objects made of metal
07 - Machines and machine tools
11 - Environmental control apparatus
37 - Construction and mining; installation and repair services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Large containers of metal for environmental engineering and energy technology, and installations composed thereof; Transportable buildings of metal; Chimneys of metal for use in energy technology, for the power plant industry, lignite power plants, waste incineration installations; Ventilation funnels (chimney shafts); Internal flues (pipes) of stainless steel; Metal pipes, Large pipelines, exhaust steam pipes and dephlegmator pipes; Compensator pipes, flue gas ducts in the form of gas pipes, superheated steam pipes; Steel buildings; Common metals and their alloys; Unprocessed and semi-processed materials of metal, not specified for use; Non-electric building materials of metal. Machines and mechanically driven apparatus, and installations composed thereof for generating energy; Blowing engines; Sound absorbers being parts of machines; Heat exchangers (parts of machines); Elevating apparatus (machines), Cranes [lifting and hoisting apparatus]; Pressing machines; Engines and motors; Turbines, machine coupling and transmission components, except for land vehicles; Filters (included in class 7). Gas/heating boilers, including industrial steam boilers, water tube boilers, saturated steam boilers and superheated steam boilers, Hot water boilers, waste heat recuperators, fire-tube boilers, Special boilers for thermal disposal and post-combustion; Flaming torches, Ventilating installations, In particular exhaust air chimneys and exhaust air installations; Cooling chimneys. Building, installation and repair of gas/heating boilers, ventilating installations and heat exchangers; Construction and repair of electricity or gas generating installations and coal extraction installations; Construction and repair of electrical power, gas and water distribution networks and telecommunication lines and networks; Construction and repair of environmental protection installations; Boiler cleaning and repair; Building consultancy. Treatment of materials, Namely surface treatment; Mechanical or chemical treatment or processing of materials; Rental of generators; Recycling of waste and trash; Boilermaking; Generating of energy, in particular electricity; Generation of gas and electricity; Incineration of waste and trash; Recycling of waste and valuable materials; Recycling of chemicals; Waste treatment [transformation]; Selection of waste and recovered raw materials (for processing); Steam and electricity generating from biomass. Engineering services; Technical research; Studies (Technical project -); Technical planning, evaluation, estimation, reports and research in relation to electrical energy; Research and development relating to the generation and distribution of electricity and gas, water distribution, coal extraction, telecommunications and environmental protection; Testing and quality inspection of electric apparatus, equipment and instruments; Engineering in the field of production of energy.
06 - Common metals and ores; objects made of metal
07 - Machines and machine tools
40 - Treatment of materials; recycling, air and water treatment,
Goods & Services
Common metals and their alloys; Unprocessed and semi-processed materials of metal, not specified for use; Non-electric building materials of metal. Elevating apparatus (machines), Cranes [lifting and hoisting apparatus]. Rental of generators; Recycling of waste and trash; Boilermaking; Generating of energy, in particular electricity; Generation of gas and electricity; Incineration of waste and trash; Recycling of waste and valuable materials; Recycling of chemicals; Waste treatment [transformation]; Selection of waste and recovered raw materials (for processing).
06 - Common metals and ores; objects made of metal
07 - Machines and machine tools
11 - Environmental control apparatus
37 - Construction and mining; installation and repair services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Large containers of metal for environmental engineering and energy technology, and installations composed thereof; Transportable buildings of metal; Chimneys of metal for use in energy technology, for the power plant industry, lignite power plants, waste incineration installations; Ventilation funnels (chimney shafts); Internal flues (pipes) of stainless steel; Metal pipes, Large pipelines, exhaust steam pipes and dephlegmator pipes; Compensator pipes, flue gas ducts in the form of gas pipes, superheated steam pipes; Steel buildings; Common metals and their alloys; Unprocessed and semi-processed materials of metal, not specified for use; Non-electric building materials of metal. Machines and mechanically driven apparatus, and installations composed thereof for generating energy; Blowing engines; Sound absorbers being parts of machines; Heat exchangers (being parts of machines); Elevating apparatus (machines), Cranes [lifting and hoisting apparatus]; Pressing machines; Engines and motors; Turbines, Machine coupling and transmission components (except for land vehicles); Filters (included in class 7). Gas/heating boilers, including industrial steam boilers, water tube boilers, saturated steam boilers and superheated steam boilers, Hot water boilers, waste heat recuperators, fire-tube boilers, Special boilers for thermal disposal and post-combustion; Flaming torches, Ventilating installations, In particular exhaust air chimneys and exhaust air installations; Cooling chimneys. Building, installation and repair of gas/heating boilers, ventilating installations and heat exchangers; Construction and repair of electricity or gas generating installations and coal extraction installations; Construction and repair of electrical power, gas and water distribution networks and telecommunication lines and networks; Construction and repair of environmental protection installations; Boiler cleaning and repair; Building consultancy. Treatment of materials, Namely surface treatment; Mechanical or chemical treatment or processing of materials; Rental of generators; Recycling of waste and trash; Boilermaking; Generating of energy, in particular electricity; Generation of gas and electricity; Incineration of waste and trash; Recycling of waste and valuable materials; Recycling of chemicals; Waste treatment [transformation]; Selection of waste and recovered raw materials (for processing); Steam and electricity generating from biomass. Engineering services; Technical research; Studies (Technical project -); Technical planning, evaluation, estimation, reports and research in relation to electrical energy; Research and development relating to the generation and distribution of electricity and gas, water distribution, coal extraction, telecommunications and environmental protection; Testing and quality inspection of electric apparatus, equipment and instruments; Engineering in the field of production of energy.
The purpose of the present invention is to stabilize energy balance by controlling energy consumption required for cooling and heating while simplifying pipe structure. A water treatment device is provided with: a forward osmosis means for forming a diluted draw solution by moving water through a semipermeable membrane from an aqueous solution that includes water as a solvent in a draw solution having a cloud point; a heating means for heating the diluted draw solution to a temperature at the cloud point or greater; a water separation means for separating the diluted draw solution heated by the heating means into a water-rich solution and a regenerated draw solution wherein the water content is lower than the water-rich solution; an inflow-side heat exchange means for carrying out heat exchange between the aqueous solution and the regenerated draw solution flowing out of the water separation means; and an outflow-side heat exchange means for carrying out heat exchange between the diluted draw solution flowing out of the forward osmosis means and the water-rich solution flowing out of the water separation means.
C02F 1/44 - Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
B01D 61/00 - Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltrationApparatus, accessories or auxiliary operations specially adapted therefor
An objective of the present invention is to provide a ballast water treatment device capable of preventing reduction reaction heat which is generated when detoxifying bactericide residue, from adversely affecting bactericide supplying devices and the like. The ballast water treatment device is provided with: a bactericide supplying device (20) which supplies a chlorine-type bactericide to a ballast water pipe (3) circulating ballast water towards a ballast tank (2); a reduction agent supplying device (30) which supplies a reduction agent, which reacts with the chlorine-type bactericide, to the ballast water pipe; a first pipe (22) which transfers, into the ballast water pipe (3), the chlorine-type bactericide remaining in the bactericide supplying device (20); a second pipe (32) which transfers the reduction agent into the ballast pipe (3); and an injection part (7) which injects, into the ballast water pipe, the chlorine-type bactericide transferred from the first pipe (22). The second pipe (32) is connected to the injection part (7), and the chlorine-type bactericide remaining in the bactericide supplying device (20) is injected, with the reduction agent, into the ballast water pipe (3) from an opening (7a) provided in the injection part (7).
Provided is condensing equipment which is capable of operating stably, and which inhibits a pulsation phenomenon caused by gas pressure fluctuation in a gas supply flow path upstream of a condenser. Condensing equipment 1 according to the present invention is provided with a condenser 7 which brings a gas into direct or indirect contact with a liquid, to condense the gas. The condensing equipment is further provided with: an adjustment valve 11 which is provided upstream of the condenser 7, and which adjusts the supply amount of the gas supplied to the condenser 7; and a gas supply pipe 13 for supplying the gas from the adjustment valve 11 to the condenser 7. The condenser 7 is provided with a gas supply portion 17 which is connected to the gas supply pipe 13, and in which the gas is temporarily stored before being brought into direct or indirect contact with the liquid. The total volume of the gas supply pipe 13 and the gas supply portion 17 is set so as to be equal to or greater than the amount of the gas which is condensed in one second.
Provided is a gas-liquid mixer which is not damaged as a result of deformation caused by a temperature difference between a supplied liquid and a supplied gas, and in which the liquid does not flow into the side of a gas supply pipe. A gas-liquid mixer 1 according to the present invention is provided with: a main body 2 provided with a cylindrical fluid flow path-forming part 9, a liquid supply port 11, and a mixed fluid discharge port 13; a gas supply part 3 which is provided to the outside or the inside of the fluid flow path-forming part 9, and which supplies a gas to a liquid flowing through the fluid flow path-forming part 9; and a gas supply pipe connecting part 7 to which a gas supply pipe 5 is connected. The gas supply part 3 is provided with a partition wall 21 which is provided so as to form a partition between the liquid flowing through the inside of the fluid flow path-forming part 9 and the gas supplied to the gas supply part 3. The partition wall 21 is provided with one or more gas supply holes 23 for supplying the supplied gas to the liquid. The gas supply pipe connecting part 7 is provided in a position higher than the positions of all of the gas supply holes 23 in an installed state.
Provided are: a bubble detection device which is capable of detecting, with high sensitivity, bubbles present in a liquid; and condensing equipment which uses said bubble detection device. A bubble detection device 1 according to the present invention is provided to a flow path through which a liquid which may include bubbles flows, and detects bubbles included in the liquid. The bubble detection device is provided with: a vertical container 3 which has, connected to a side wall part, a supply pipe 9 for supplying the liquid, and has, connected to a lower part, a discharge pipe 11 for discharging the liquid; a liquid return pipe 5 which is provided to an upper part of the vertical container 3, and which returns the liquid flowing therein to a constant liquid source; and a differential pressure gauge 7 which detects a pressure difference in the vertical container 3, or in the vertical container 3 and in an area where bubbles may be present in a portion of the liquid return pipe 5.
G01N 9/26 - Investigating density or specific gravity of materialsAnalysing materials by determining density or specific gravity by measuring pressure differences
G01N 7/00 - Analysing materials by measuring the pressure or volume of a gas or vapour
G01N 9/36 - Analysing materials by measuring the density or specific gravity, e.g. determining quantity of moisture
57.
BALLAST WATER TREATMENT DEVICE AND BALLAST WATER TREATMENT METHOD
Provided are a ballast water treatment device and treatment method with which it is possible to supply, in accordance with the quality of raw water taken in for ballast water, an appropriate amount of an oxidant required for ensuring an adequate concentration of the oxidant to sterilize living organisms in the raw water, even after a long period of time has elapsed from when the supply of the oxidant to the raw water was stopped. In the treatment device, a storage means (23) stores: a first correspondence relationship of the light absorption of the raw water and the concentration of dissolved organic carbon in the raw water; and a second correspondence relationship of the concentration of the dissolved organic carbon and a required residual oxidant concentration required, as a residual oxidant concentration at the point in time when a prescribed amount of time has elapsed since the oxidant was supplied, in order to sterilize the living organisms in the raw water and to suppress the repopulation of living organisms in the water stored in the ballast tank. On the basis of the correspondence relationships, a calculation means (24) derives the required residual oxidant concentration corresponding to the light absorption of the raw water as measured by a light absorption meter 21, and calculates the amount of oxidant required to be supplied using the required residual oxidant concentration as a control target value. A control means (25) controls an oxidant supply device 5 in accordance with the calculation.
Provided is a ship in which it is possible to minimize or prevent the incidence of faults in the treatment of ballast water caused by a chlorine-based sterilizing agent remaining after not being used in treating ballast water. A ship (VSL) is provided with a ballast pump (Pm) that is provided with a first driving mode in which sea water (Wo) acquired from outside the ship is circulated toward a ballast tank (T) so as to be accommodated in the ballast tank or filled thereinto, and a second driving mode in which the sea water acquired from outside the ship is circulated without being routed the ballast tank to discharge the sea water to outside the ship. The ship is further provided with a ballast water treatment device provided with: a sterilizing-agent injection opening (Is) via which, during the first driving mode, a chlorine-based sterilizing agent (As) is injected into the sea water circulated toward the ballast tank; and a remainder injection opening (Id) via which, during the second driving mode, at least a portion of the remainder (Re) of the chlorine-based sterilizing agent is injected into the sea water circulated toward the outside of the ship, the remainder (Re) of the chlorine-based sterilizing agent being what remains thereof without having been injected into the sea water during the first driving mode.
A buckling pattern steel pipe for being buried in ground in which flexure occurs includes: a steel pipe straight portion; and a buckling pattern portion. The buckling pattern portion is in a shape expressed by a sine wave determined based on: a buckling wavelength which is 2.05 to 4.32 times a compression local buckling half wavelength expressed by 1.72√(r·T); and a crest height expressed by a value 8.00 to 16.25 times a pipe thickness of the steel pipe straight pipe portion, and the buckling pattern portion absorbs bending compression deformation caused by faulting of the ground and axial compression deformation caused by the flexure so as to avoid deformation of the steel pipe straight pipe portion, where r is a pipe thickness center radius of the steel pipe straight pipe portion and T is the pipe thickness of the steel pipe straight pipe portion.
In order to effectively condense an evaporated gas and mix same into a low-temperature fluid, a condensing and mixing device 2 comprises: a storage means 18 that stores the correspondence between mixed fluid pressure and the saturation temperature at said pressure, as a first correspondence relationship A, and the correspondence between a permissible minimum value for the degree of overcooling of the mixed fluid and an auxiliary flow rate ratio obtained by dividing the total flow rate for a main flow and an auxiliary flow by the flow rate for the auxiliary flow, as a second correspondence relationship B; and a control means 17 that adjusts the opening of an auxiliary flow adjustment valve 14 and controls the flow rate of the auxiliary flow, such that the degree of overcooling of the mixed fluid is greater than the minimum value, said adjustment and control being performed on the basis of the measurement values for the flow rate for the main flow, the flow rate for the auxiliary flow, the temperature of the mixed fluid, and the pressure and also while referring to the first correspondence relationship A and the second correspondence relationship B.
In order to effectively re-liquefy evaporated gas, the present invention comprises: a Venturi tube-type flow pipe 7 having formed therein, from an upstream side towards a downstream side, a reduced-diameter section 7A having an inner diameter that gradually reduces, followed by a throat section 7B having the smallest diameter, and then an enlarged-diameter section 7C having an inner diameter that gradually increases from the throat section 7B, said Venturi tube-type flow pipe injecting steam into a low-temperature fluid that flows downstream, condensing the steam, and mixing same into the low-temperature fluid; stepped enlarged-diameter sections 7C-1, 7C-2, ... having stepped sections 10B-1, 10B-2, … formed at a plurality of positions in the axial direction of the enlarged-diameter section 7C and having inner peripheral surfaces that gradually increase in diameter at each step and extend toward the downstream side in the axial direction; and vapor holes 10--1, 10-2, … formed so as to face towards the radial direction of the flow pipe 7 and the downstream side in order to inject steam from outside the flow pipe 7 into the low-temperature fluid flowing downstream inside the flow pipe 7 and formed so as to have injection openings 10A-1, 10A-2, … in the inner circumferential surface of the enlarged-diameter section 7C at a plurality of positions in the axial direction of the flow pipe 7.
A buckling waveform steel pipe (1) with buckling waveform sections (3). The buckling waveform steel pipe (1) is characterized in that said buckling waveform sections (3) have a shape represented by a sine wave determined on the basis of a buckling wavelength (Ln) that is 2.05-4.32 times the local compression buckling half-wavelength (L), which is represented by 1.72v(r·T), and a peak height (h) that is represented as 8.00-16.25 times the pipe thickness (T) of the straight steel pipe sections (2), r being the radius from the center of a straight steel pipe section (2) to the middle of the pipe thickness and (T) being the pipe thickness of the straight steel pipe section (2).
A buckling waveform steel pipe (1) with buckling waveform sections (3). The buckling waveform steel pipe (1) is characterized in that said buckling waveform sections (3) have a shape represented by a sine wave determined on the basis of a buckling wavelength (Ln) that is 2.05-4.32 times the local compression buckling half-wavelength (L), which is represented by 1.72√(r∙T), and a peak height (h) that is represented as 8.00-16.25 times the pipe thickness (T) of the straight steel pipe sections (2), r being the radius from the center of a straight steel pipe section (2) to the middle of the pipe thickness and (T) being the pipe thickness of the straight steel pipe section (2).
Crude oil composition estimation method, absorption process simulation method in absorption and liquefaction system, process simulation method in recovery system, and method of producing absorption and liquefaction system
A crude oil composition estimation method estimates a composition of crude oil for use in simulation of a material balance in an absorption and liquefaction system that absorbs vapors emitted from the crude oil with the crude oil. The crude oil composition estimation method includes: comparing a calculated concentration of a treated gas with a measured concentration of the treated gas; estimating, when the calculated concentration agrees with the measured concentration, that the concentration included in the crude oil is a correct crude oil composition; and repeating, when the calculated concentration does not agree with the measured concentration, a process of correcting the concentration included in the crude oil and then comparing the calculated concentration with the measured concentration, until the calculated concentration agrees with the measured concentration, and when they agree, estimating that the corrected concentration in the crude oil is a correct crude oil composition.
The problem addressed by the present invention is to provide an exhaust gas treatment device and method for reliable absorption and removal of mercury in exhaust gas from a furnace, and for providing activated carbon thereto in a suitable activated carbon quantity even if the mercury concentration in the exhaust gas varies. Provided is an exhaust gas treatment device that has a dust collection device 4, which carries out dust elimination treatment on the exhaust gas that contains mercury from a furnace 1, provided in a position downstream from the furnace 1 and is provided with an activated carbon supply device 3 for blowing activated carbon into an exhaust gas flow path wherein exhaust gas is guided from the furnace 1 to the dust collection device 4, wherein the exhaust gas treatment device has a mercury concentration gauge 5, which measures mercury concentration in the exhaust gas, provided on the downstream side of the dust collection device 4 and is provided with a control device 7 which maintains and controls the activated carbon supply amount to a prescribed minimum value such that the mercury concentration in the exhaust gas on the downstream side of the dust collection device 4 is a setting value or less on the basis of a value measured by the mercury concentration gauge 5.
The purpose of the present invention is to provide a petroleum purification waste-processing apparatus (10) and method capable of processing alkaline waste liquid (AW) and oil sludge (OS) comprised in waste discharged from a petroleum purification device (12) at lower cost than in the past and of reducing the amount ultimately discarded. One processing apparatus comprises: an oil extraction device (14), which is connected to the petroleum purification device and is for separating oil sludge into oil (OI) and sludge (SL); a combustion furnace (16), which is connected to the petroleum purification device and the oil extraction device and is for burning the oil from the oil extraction device and oxidatively decomposing alkaline waste liquid from the petroleum purification device; and a gasification melting furnace (20), which is connected to the oil extraction device and is for thermolyzing sludge from the oil extraction device into gas (CG) and melted solids (MS) and discharging said gas and melted solids.
This filtration device has: a casing 1 having a fluid inlet 6, a fluid outlet 7, a raw material liquid chamber 8, and a filtered liquid chamber 9; a filter element 3 (3a, 3b) which has a filtration material 31, is formed in a box shape or a cylinder shape, is removably installed within the casing 1, receives fluid from one open face or two facing faces and causes the fluid to flow from the inside to the outside, thereby filtering the fluid, and has a backwash mechanism therein; and a backwash fluid discharge pipe 4 for discharging backwash fluid, which flows from the backwash mechanism, to the outside of the casing. The backwash mechanism has: a stationary pipe 33 affixed to the inside the filter element; a movable pipe 34 fitted over the outside of the stationary pipe and movable in the axial direction of the stationary pipe; and a backwash head 35 mounted to the movable pipe and backwashing the filtration material. The stationary pipe and the movable pipe movably guide the backwash head and form a discharge passage for backwash fluid.
B01D 29/50 - Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
B01D 29/11 - Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
B01D 29/66 - Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
68.
Waste gasification melting apparatus and waste gasification melting method using the same
Problem to be Solved
To provide a waste gasification melting apparatus which, even if a fuel gas is used as an alternative to a part of the coke, the temperature of the coke bed can be sufficiently raised, and a method using the same.
Solution
A waste gasification melting apparatus including an oxygen rich air supply apparatus 14 for blowing oxygen rich air into a tuyere 5, and a fuel gas supply apparatus 15 for supplying a fuel gas to the tuyere 5, and a controller 16 for controlling the oxygen rich air supply apparatus 14; the oxygen rich air supply apparatus 14 mixing air and oxygen to prepare oxygen rich air and supply the oxygen rich air to the tuyere 5; and the controller 16 controlling the amount of air to be mixed and the amount of oxygen to be mixed in the oxygen rich air supply apparatus 14 so as to give an oxygen concentration of the oxygen rich air in accordance with the amount of fuel gas supplied to the tuyere 5 from the fuel gas supply apparatus 15.
F23L 7/00 - Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
F23G 5/027 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels including pretreatment pyrolising or gasifying
F23G 5/24 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels with combustion in a vertical, substantially cylindrical, combustion chamber
This filtration device is provided with: a casing (1); a first separating wall (2) which separates the inside of the casing into a first raw liquid chamber (9a) in which a fluid is held before filtration and a filtered liquid chamber (10) in which the fluid is held after filtration; tubular filter elements (3a, 3b) which communicate internally with the first raw liquid chamber, are provided in the filtered liquid chamber and filter fluid by passing said fluid from the inside outwards; a second separating wall (4) which is disposed at the other, second end of the filter elements and which forms a second raw liquid chamber which is in communication with the first raw liquid chamber; a cleaning pipe (5) which is connected to at least the first end of a filter element and which cleans the fluid by passing the same from the raw liquid chamber in the axial direction of the filter element; and a cleaning fluid drain pipe (6) which discharges captured matter to the outside. The second end of the filter element (3b) connected to the cleaning pipe (5) is always opened to the raw liquid chamber (9a).
B01D 29/62 - Regenerating the filter material in the filter
B01D 29/50 - Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
B63B 13/00 - Conduits for emptying or ballastingSelf-bailing equipmentScuppers
70.
TEMPERATURE-SENSITIVE ABSORBENT, WATER TREATMENT METHOD, AND WATER TREATMENT APPARATUS
This temperature-sensitive absorbent is employed as an attractant in the manufacture of fresh water by a forward osmosis process, the temperature-sensitive absorbent having a cloud point, and being designed to agglomerate when heated. This temperature-sensitive absorbent includes at least a hydrophobic portion and a hydrophilic portion, and is a block copolymer that has a glycerol skeleton as the basic skeleton thereof, and that includes an ethylene oxide group and a group comprising propylene oxide and/or butylene oxide. Alternatively, the temperature-sensitive absorbent is a block copolymer that has a trimethylolpropane skeleton as the basic skeleton thereof, and that includes ethylene oxide and butylene oxide.
B01D 61/00 - Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltrationApparatus, accessories or auxiliary operations specially adapted therefor
C02F 1/44 - Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
In accordance with the present invention, steel having a prescribed component composition, in particular, one in which the total amount of Cu + Ni is at least 15 mass%, with the remainder being Fe and unavoidable impurities, is brought to a crystal grain size, measured subsequent to being shaped to stabilizer shape and quenched, such that the prior austenitic grain size number is in the range of 7.5-10.5, whereby a high-durability stabilizer steel having tensile strength of 1,200 MPa grade or above, and excellent normal temperature/low temperature ductility, can be obtained at lower cost, through an environmentally-friendly manufacturing process.
A method and apparatus for removing soluble silica efficiently from accompanied water, produced from wells containing calcium ion, soluble silica, and sulfate ion, and not clogging a reverse osmosis membrane in the reverse osmosis membrane treatment process after that, includes adding a magnesium salt to mix with the accompanied water under alkaline conditions to produce insoluble silica and calcium sulfate. A microfiltration (MF) membrane treatment process includes treating a first reaction solution obtained in said magnesium salt adding process, with a microfiltration membrane to separate insolubilized silica and calcium sulfate by filtration. An acid adding process includes adding an acid to and mixing with filtrate obtained in the MF membrane treatment process to render a pH value of the filtrate on the range from 5 to 9 and a negative Langeliar saturation index. A reverse osmosis membrane treatment process includes treating a second reaction solution, obtained in the acid adding process, with a reverse osmosis membrane to obtain fresh water and membrane concentrates.
Provided is a waste gasification and melting device and method capable of increasing the temperature of a coke bed sufficiently even when using fuel gas as a substitute for a portion of the coke. A waste gasification and melting device having an oxygen-rich air supplying device (14) that supplies oxygen-rich air, by blowing, to a tuyere (5), a fuel gas supplying device (15) that supplies fuel gas to the tuyere (5), and a controlling device (5) that controls the oxygen-rich air supplying device (14), wherein the oxygen-rich air supplying device (14) prepares the oxygen-rich air by mixing air with oxygen and then supplies the oxygen-rich air to the tuyere (5), and the control device (16) controls the amount of air and the amount of oxygen that are mixed by the oxygen-rich air supplying device (14) so as to set the concentration of oxygen in the oxygen-rich air according to the amount of gas fuel supplied to the tuyere (5) from the fuel gas supplying device (15).
F23G 5/00 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels
F23G 5/24 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels with combustion in a vertical, substantially cylindrical, combustion chamber
F23K 5/00 - Feeding or distributing other fuel to combustion apparatus
F23L 7/00 - Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
A rapid charger, comprising: a power reception means connected to a commercial power supply; a storage battery connected to the power reception means; and an output means which is connected to the power reception means and the storage battery, and which outputs power for charging to an external device. The storage amount target value (SOCt) for the storage battery varies depending on the power received via the power reception means. The storage amount target value (SOCt), when the amount of power received via the power reception means is small, is preferably greater than the storage amount target value (SOCt) when the amount of power received via the power reception means is large.
This quick charger (1-1) comprises: a first power receiving means (6) that receives power from a commercial power supply; a second power receiving means (8) that is connected to the first power receiving means and that receives power from a power supply other than the commercial power supply; and a storage battery (10) that is connected to the first power receiving means and the second power receiving means. The quick charger has the function of charging an external device (EV). The maximum input power from the first power receiving means is preferably less than 50% of the maximum output power to the external device. The second power receiving means preferably receives power from a solar power generation device.
This quick charger (1-1) for an electric vehicle comprises: a power receiving means (6) that receives power from an external power supply; and a storage battery (10) that is connected to the power receiving means, and that can supply power to an electric vehicle (EV) when power is not received from the external power supply. When power is not received from the external power supply, power for a control power supply (20a) of a control device (20) and output power (Po) to be supplied to the electric vehicle are preferably output from the storage battery. The quick charger may have a plurality of power receiving means including a commercial power receiving means that receives power from a commercial power supply.
This quick charger comprises: a power receiving means that receives power from a commercial power supply; a storage battery; and an output means that is connected to the power receiving means and the storage battery, and that can output, as charging power (Po) to an external device, power (P1) received from the commercial power supply and power (Pb) discharged by the storage battery. The power (P1) received at the time of charging the external device is changed in accordance with the state of charge (SOC) of the storage battery. It is preferable that the power (P1) received when the state of charge (SOC) is high is smaller than the power (P1) received when the state of charge (SOC) is low.
This quick charger comprises: a power receiving means (6) that receives power from a commercial power supply and a solar power generation system (30); a storage battery (10); an output means (7) that can output, as charging power (Po) to an external device (EV), power (P1) received by the power receiving means and power (Pb) discharged by the storage battery; a switching means (8) that connects or disconnects the commercial power supply; and an acquisition means (20) that acquires power (P2) generated by the solar power generation system. In case of a power failure of the commercial power supply, the commercial power supply is disconnected by the switching means, and the command value of the power received by the power receiving means is set to a value in accordance with the generated power.
Provided is a steel for nitrocarburizing, of which the composition is so adjusted as to comprise, in mass%, 0.01% or more and less than 0.10% of C, 1.0% or less of Si, 0.5 to 3.0% of Mn, 0.02% or less of P, 0.06% or less of S, 0.3 to 3.0% of Cr, 0.005 to 0.4% of Mo, 0.02 to 0.5% of V, 0.003 to 0.15% of Nb, 0.005 to 0.2% of Al, 0.0005 to 0.02% of Sb and a remainder made up by Fe and incidental impurities, and in which the area ratio of a bainite phase makes up more than 50% of the whole area of the structure of the steel. The steel exhibits excellent machine-processing properties before the nitrocarburization of the steel, exhibits excellent fatigue properties after the nitrocarburization of the steel, and can be used suitably for mechanical structure parts for automobiles and the like.
C21D 8/06 - Modifying the physical properties by deformation combined with, or followed by, heat treatment during manufacturing of rods or wires
C21D 9/32 - Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articlesFurnaces therefor for gear wheels, worm wheels, or the like
C22C 38/60 - Ferrous alloys, e.g. steel alloys containing lead, selenium, tellurium or antimony, or more than 0.04% by weight of sulfur
80.
POWDER/LIQUID MIXING AND DISSOLVING DEVICE AND BALLAST WATER TREATMENT APPARATUS USING SAME
A powder/liquid mixing and dissolving device comprises: a storage tank (3) in which mixed liquid obtained by mixing powder into liquid is stored; a liquid cyclone (9) which receives the mixed liquid from the storage tank (3) and separates the mixed liquid into a solution and undissolved portion-containing liquid; a mixed liquid supply line (8) through which the mixed liquid is supplied from a mixed liquid discharge port (3B) of the storage tank (3) to a mixed liquid reception port (9C) of the liquid cyclone (9); and an undissolved portion-containing liquid return line (10) through which the undissolved portion-containing liquid discharged from an undissolved portion-containing liquid discharge port (9B) provided in the liquid cyclone (9) is returned to the mixed liquid supply line (8), and the undissolved portion-containing liquid return line (10) is connected to the mixed liquid supply line (8) to thereby form a circulation line (11).
The purpose of the present invention is to provide a low-price static fluid mixer having a simple shape and capable of quickly and efficiently mixing multiple fluids, and to provide a compact and low-cost ballast water treatment device using said mixer. This static fluid mixer includes a ring portion (5) which is interposed concentrically in a main fluid pipe conduit, and flap portions (6) which protrude towards the central axis of the pipe conduit from multiple positions around the circumference of the inner peripheral surface, and is provided with a mixing member which, by means of a Kármán vortex street generated in the primary fluid by the flap portions, mixes into the primary fluid a secondary fluid supplied to the primary fluid. The ring portion is made as a plate member expanding in the radial direction of said ring portion, and the inner peripheral surface of the ring portion is flush with the inner peripheral surface of the pipe conduit. The flap portion includes two linear side edges (6A-1) which are spaced circumferentially apart from each other and face radially inwards, and an arcuate protruding edge (6B-1) which extends between the ends of the inwardly-facing two side edges and protrudes towards the central axis. An opening (8) defined between the multiple flap portions inside of the inner peripheral surface of the ring portion includes a narrow area (7) between the multiple arcuate protruding edges.
Provided are a method and device with which the soluble silica is efficiently removed from accompanying water that contains calcium ions and soluble silica and that was produced from a well and in which in a reverse osmosis membrane treatment step to be conducted thereafter, the reverse osmosis membrane is not clogged. The method comprises: a magnesium salt addition step in which a magnesium salt is added to and mixed with the accompanying water under alkaline conditions to yield insoluble silica and calcium sulfate; a microfiltration step in which the first liquid reaction mixture obtained in the magnesium salt addition step is treated by microfiltration to separate the insolubilized silica and calcium sulfate therefrom; an acid addition step in which an acid is added to and mixed with the filtrate water obtained in the microfiltration step to thereby regulate the pH of the filtrate water to a value in the range of 5-9 and the Langelier index to a value in the negative range; and a reverse osmosis membrane treatment step in which the second liquid reaction mixture obtained in the acid addition step is treated with a reverse osmosis membrane to obtain fresh water and membrane-concentrated water.
As a method and apparatus for removing soluble silica efficiently from accompanied water produced from wells containing calcium ion and soluble silica, and not clogging a reverse osmosis membrane in the reverse osmosis membrane treatment process after that, it is to provide a method comprising magnesium salt adding process, wherein a magnesium salt is added to mix with the accompanied water contain:mg calcium ion, soluble silica and sulfate ion produced from a well under alkaline conditions to produce insoluble silica and calcium sulfate; a MF membrane treatment process, wherein a first reaction solution obtained in said magnesium salt adding process is treated with a MF membrane to separate the insolubilized silica and calcium sulfate by filtration; an acid adding process, wherein an acid is added to and mixed with filtrate obtained in said MF membrane treatment process to render pH value of said filtrate into the range from 5 to 9 and Langeliar saturation index into the range of minus; and a RO membrane treatment process, wherein a second reaction solution obtained in said acid adding process is treated with a RO membrane to obtain fresh water and RO membrane concentrates, and an apparatus therefore.
Provided is a grate-type waste incinerator that is capable of reducing the amount of hazardous substance generation, and performing combustion of waste with ease using a low air ratio, and a method for incinerating waste. An incinerator (1) includes a combustion chamber (2) that combusts waste (W) while the waste moves on a grate (5); a primary gas blowing unit (FABU) that blows a primary combustion gas (A) from below the grate into the combustion chamber; and a hot gas blowing unit (HGBU) that has a plurality of hot gas blowing ports (13) which blow hot gas (B) down from an upper position one to three meters away from the grate in the combustion chamber toward a predetermined site between a waste combustion initiation area and a main combustion area in the combustion chamber. The hot gas that is blown in inhibits an upward flow of the combustion gas that contains a flammable gas which is generated from the waste, and induces stagnation or circulation of the hot gas or the combustion gas for the waste on the grate to provide a stable planar combustion area for the waste.
F23G 5/14 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels including supplementary heating including secondary combustion
F23G 5/00 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels
F23G 5/027 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels including pretreatment pyrolising or gasifying
85.
STEEL FOR NITROCARBURIZING AND NITROCARBURIZED COMPONENT USING THE STEEL AS MATERIAL
The present invention can provide steel for nitrocarburizing which has a predefined chemical composition and, before nitrocarburizing, excellent machinability by cutting by having a structure in which the bainite area ratio prior to nitrocarburizing is greater than 50%, and after nitrocarburizing, strength/toughness equal to that of a carburized material of conventional steel, for example, SCr420 steel and provides more superior fatigue characteristics.
The purpose is to provide a biomass carbonization device (10) and a biomass carbonization method for thermally degrading a biomass (M) to obtain a carbonized product (C) at a higher yield than in the past. The biomass carbonization device has a temperature control unit (16) for controlling the temperature inside a carbonization furnace (11). The temperature control unit controls the temperature of the lower part of the packed moving bed (P) of the biomass to at or above a tar vapor generation temperature that thermally degrades the biomass and generates tar vapor, and controls the temperature of the upper part of the packed moving bed to at or below a tar condensation temperature that condenses the tar vapor. In the carbonization furnace, tar vapor generated in the lower part of the packed moving bed is condensed in the upper part and made into liquid tar; the liquid tar is trapped by the biomass in the packed moving bed, and the trapped liquid tar is thermally degraded together with the biomass and converted into a carbonized product.
C10B 47/20 - Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge according to the "moving bed" technique
B09B 3/00 - Destroying solid waste or transforming solid waste into something useful or harmless
C10B 53/02 - Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
87.
SAND DISCHARGE DEVICE AND SAND DISCHARGE METHOD FOR BALLAST TANK
A sand discharge device, which discharges mud and sand deposited in ballast tanks (2) comprising multiple tank compartments (5) in a ship (1) equipped with a port-side water injection/drainage pump (21) and a starboard-side water injection/drainage pump (11), which inject water into and drain water from the ballast tanks (2), wherein this sand discharge device is equipped with: nozzles (19) which are provided near the tank floor plate (8) of the tank compartments (5), and which spray water; a water feed pipeline (13) that feeds water to the nozzles (19); a water discharge pipeline (22) that discharges from the ballast tanks (2) muddy water in which mud and sand that has been washed away by the water sprayed from the nozzles (19) has been dispersed and suspended; and a water feed/discharge control means (100) which, when mud and sand is discharged from the port-side ballast tanks (2), opens/closes a valve in the water feed pipeline (13) and operates the starboard-side water injection/drainage pump (11) so as to feed water into the port-side water feed pipeline (13) from the starboard-side water injection/drainage pump (11), and opens/closes a valve in the water discharge pipeline (22) and operates the port-side water injection/drainage pump (21) so as to discharge muddy water from the port-side water discharge pipeline (22) by means of the port-side water injection/drainage pump (21). Thus, the mud and sand accumulated in the ballast tanks (2) can be discharged efficiently.
Provided are a method and device for obtaining fresh water from a liquid to be processed, e.g. seawater, using a forward osmosis membrane, wherein the solution obtained after separating the water from a diluted draw solution that was diluted by the inflow of water from the liquid to be processed can be stably regenerated an re-used as the draw solution. The method and device for preparing fresh water involve: an osmosis process in which a solution having water as a solvent and a draw solution obtained by dissolving a prescribed amount of a volatile substance in water are brought into contact across a semi-permeable membrane, and the water in the solution flows to the draw solution across the semi-permeable membrane; a distillation process in which the diluted draw solution diluted by the water in the osmosis process is set to a prescribed temperature and is supplied to a distillation column, and a gas comprising the volatile substance and water vapor is obtained from the top of the distillation column, while fresh water is obtained from the bottom of the distillation column; and a cooling/regeneration process in which the gas is cooled to regenerate the draw solution.
C02F 1/44 - Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
B01D 61/00 - Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltrationApparatus, accessories or auxiliary operations specially adapted therefor
C02F 1/04 - Treatment of water, waste water, or sewage by heating by distillation or evaporation
Provided is a heat storage agent comprising a clathrate hydrate that is generated by cooling an aqueous solution containing tetra-n-butylammonium bromide as a solute. The invention is characterized in that the heat storage agent is prepared by adding tetra-iso-pentylammonium bromide, an alkali metal phosphate, and a cellulose derivative to the aqueous solution, and the cellulose derivative comprises a carboxyl group and/or carboxymethyl group, or comprises at least a carboxyl group and/or carboxymethyl group together with an alkali metal.
The invention addresses the problem of providing a waste-melting method, with which the amount of coal coke used in a vertical-type waste-melting furnace is reduced to reduce the emission of carbon dioxide and also to enable the suppression of an increase in the running costs of the waste-melting furnace, and also the heat of combustion of volatile matter contained in a biomass starting material can be effectively utilized, and more stable operation can be achieved. A waste-melting method, in which waste is fed into a waste-melting furnace (1), and the waste is thermally decomposed and combusted, and then, thermal decomposition and combustion residues are melted, is characterized in that coal coke and a biomass-molded material obtained by press-molding a biomass starting material while heating the biomass starting material to a temperature lower than the carbonization temperature thereof are fed into the melting furnace, a high-temperature grate is formed with coal coke at the bottom of the melting furnace, and the coal coke and the biomass-molded material are combusted and used as heat sources for melting.
F23G 5/24 - Methods or apparatus, e.g. incinerators, specially adapted for combustion of waste or low-grade fuels with combustion in a vertical, substantially cylindrical, combustion chamber
91.
STEEL FOR AUTOMOTIVE SUSPENSION SPRING COMPONENT, AUTOMOTIVE SUSPENSION SPRING COMPONENT, AND MANUFACTURING METHOD FOR SAME
Disclosed is a steel for automotive suspension spring components that is characterized by: comprising 0.15-0.35 mass% of C, more than 0.6 mass% and at most 1.5 mass% of Si, 1-3 mass% of Mn, 0.3-0.8 mass% of Cr, 0.005-0.080 mass% of sol. Al, 0.005-0.060 mass% of Ti, 0.005-0.060 mass% of Nb, at most 150 ppm of N, at most 0.035 mass% of P, at most 0.035 mass% of S, 0.01-1.00 mass% of Cu, and 0.01-1.00 mass% of Ni, with the remainder consisting of Fe and unavoidable impurities; Ti+Nb≤0.07 mass%; having a tensile strength of at least 1300 MPa; and exhibiting superior corrosion resistance and low-temperature toughness.
C21D 9/02 - Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articlesFurnaces therefor for springs
C22C 38/58 - Ferrous alloys, e.g. steel alloys containing chromium with nickel with more than 1.5% by weight of manganese
C22C 38/60 - Ferrous alloys, e.g. steel alloys containing lead, selenium, tellurium or antimony, or more than 0.04% by weight of sulfur
F16F 1/02 - Springs made of steel or other material having low internal frictionWound, torsion, leaf, cup, ring or the like springs, the material of the spring not being relevant
92.
TOWER-TYPE LIGHT-CONCENTRATING SOLAR POWER GENERATING SYSTEM AND METHOD FOR LIGHT CONCENTRATION THEREOF
In the disclosed solar power generating system, a solar power generating module (101) containing a solar cell assembly (102) is provided to a tower (1) at a position at a predetermined height, and is caused to be struck by sunlight (L) reflected by a plurality of heliostats (5) installed on the ground. As the heliostats (5) are multi-mirror heliostats having a plurality of mirrors (2), it is possible to cause sunlight (L) to strike the solar cell assembly (102) evenly, and it is possible to cause the power generating ability of multi-junction solar cells to be exerted at a maximum level.
H01L 31/052 - Cooling means directly associated or integrated with the PV cell, e.g. integrated Peltier elements for active cooling or heat sinks directly associated with the PV cells
93.
SOLAR POWER GENERATION MODULE AND LIGHT-CONCENTRATING SOLAR POWER GENERATION SYSTEM
In the present disclosures, heat from solar cells and the like arising when receiving light can be cooled by a cooling body (103) being provided in a manner so as to cover the entire back surface of a solar cell assembly (102) to which a plurality of solar cells (120) are rectangularly arranged. The cooling body (103) is an integral cast body having a coolant duct (123) inside, and so is robust with respect to heat shock in situations such as when suddenly hit by sunlight, and can reliably handle high temperatures resulting from a level of light concentration that is increased by around 800-2000 times.
A biomass carbonization device provided with a vertical-type carbonization furnace in which biomass is supplied to the upper part of the carbonization furnace, creating a biomass filling movement layer inside the carbonization furnace; high-temperature gas is supplied to the lower part of the carbonization furnace; and the biomass is brought into contact with the high-temperature gas to induce thermal decomposition. The carbonization device has a temperature control device for controlling the temperature within the carbonization furnace. The temperature control device maintains the lower part of the filling movement layer within a range of temperatures that are not lower than the tar volatization temperature at which the biomass undergoes thermal decomposition and tar is volatized, and no higher than the temperature at which excessive gas is produced when the biomass undergoes thermal decomposition. The temperature control device maintains the upper part of the filling movement layer within a range of temperatures that are not lower than the biomass desiccation temperature at which biomass is desiccated, and no higher than a tar condensing temperature at which the tar condenses.
C10B 53/02 - Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
C10B 47/20 - Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge according to the "moving bed" technique
95.
BALLAST-TANK SAND-REMOVAL DEVICE AND SAND-REMOVAL METHOD
Disclosed is a sand-removal device that removes mud and sand accumulated in a ballast tank in a ship, said ballast tank comprising tank compartments (15) formed by partitioning the space in the ballast tank via garters (13) and floors (14) and provided with a water injection/drainage means (21) that injects and drains seawater. Said sand-removal device is provided with: nozzles (19) that spray water and are arranged near the floor plate (11) of a tank compartment; a water supply pipe (17) that supplies water to the nozzles; and a control unit that has the nozzles spray water, thereby blasting mud and sand accumulated in that tank compartment up into said tank compartment, and has the abovementioned water injection/drainage means drain the resulting water mixture containing suspended/dispersed mud and sand. Mud and sand accumulated in the ballast tank is thus removed efficiently.
In a filtration apparatus, a filtration tank is provided with a raw water inlet, through which raw water is drawn in, and a filtered water outlet, which releases filtered water obtained by filtering raw water with a filter. The internal space of said filtration tank is divided into a plurality of compartments by filters, and said plurality of compartments is arranged alternately as inflow chambers that communicate with the abovementioned raw water inlet, and outflow chambers that communicate with the filtered water outlet. Said filtration apparatus is equipped with: a backwash collection pipe that faces the filters, thereby forming a water collection port in the inflow chamber; and a backwash discharge pipe, which is movably arranged on the surface of said filters, is connected to the backwash collection pipe, and extends outside the filtration tank. The backwash collection pipe receives backwash water, which flows through the filters from the outflow chamber side, from the abovementioned water collection port, uses backwash water to separate deposits that are trapped on the surfaces of the filters on the inflow chamber side, receives trapped deposits and backwash water from the abovementioned water collection port, and discharges the trapped deposits and backwash water as backwash discharge water through the backwash discharge pipe to the outside of the tank, thereby providing a filtration apparatus that is compact and able to filter large volumes.
B01D 29/01 - Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups Filtering elements therefor with flat filtering elements
B01D 29/66 - Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
B63B 13/00 - Conduits for emptying or ballastingSelf-bailing equipmentScuppers
C02F 1/32 - Treatment of water, waste water, or sewage by irradiation with ultraviolet light
C02F 1/44 - Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
C02F 1/50 - Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
97.
QUICK CHARGING DEVICE AND MOBILE CHARGING APPARATUS
Provided is a quick charging device which facilitates control when a storage battery for power of an electric vehicle is charged and achieves compact size and reduced costs even when a storage battery for quick charging is used. A quick charging device (10) is provided with first and second storage batteries for quick charging (12, 13) which are capable of quickly charging a storage battery for power (20), a large-capacity storage battery (14) which has a larger electric capacity than the first and second storage batteries for quick charging (12, 13), and a controller (16) which, when the storage battery for power (20) is charged, connects the first storage battery for quick charging (12) and the large-capacity storage battery (14) in series to add the electric power of the large-capacity storage battery (14) to the electric power of the first storage battery for quick charging (12) and outputs resultant electric power, and when the electric capacity of the first storage battery for quick charging (12) becomes practically zero, connects the second storage battery for quick charging (13) and the large-capacity storage battery (14) in series to add the electric power of the large-capacity storage battery (14) to the electric power of the second storage battery for quick charging (13) and outputs resultant electric power.
Provided is a rapid charger capable of reducing an average power consumption and thereby reducing the size of the contract with an electric power company from which the supply of electric power is received. When an equipment battery (3) is charged, a controller (C1) controls a DC power supplier (2) so that DC power necessary for charging the equipment battery (3) is generated from the AC power of a commercial power supply (20) and supplies the DC power from the DC power supplier (2) to the equipment battery (3). When a power battery (21) is connected as a load, the controller (C1) allows the DC power supplier (2) and the equipment battery (3) to form a series circuit, controls the DC power supplier (2) so that a predetermined DC power is generated from the AC power of the commercial power supply (20), generates DC power necessary for charging the power battery (21) by adding the predetermined DC power to the DC power from the equipment battery (3), and supplies the generated DC power to the power battery (21).
Provided is a novel underground bicycle parking facility with which it is both possible to make the portion of the underground bicycle parking facility exposed aboveground more compact and to store more bicycles by increasing bicycle handling performance. The underground bicycle parking facility is provided with an underground structure (1) that has a storage space to store bicycles underground, an elevating body (14) that has a positioning section (14b) for positioning bicycles, an elevating apparatus (4) that raises and lowers the elevating body (14) vertically inside the underground structure (1), multiple storage shelves (2) disposed radially around the elevating apparatus (4) and vertically at multiple levels in the storage space in the underground structure (1), and a transfer apparatus (22) that transfers the bicycles between the elevating body (14) and the storage shelves (2). A user places a bicycle on the positioning section (14b) of the elevating body (14) that has been lifted aboveground, and the elevating apparatus (4) lowers the elevating body (14) to the height of storage shelves (2) in the underground structure (1) while a holder (22a) of the transfer apparatus (22) grips the bicycle on the elevating body (14).
E04H 6/18 - Garages for many vehicles with mechanical means for shifting or lifting vehicles with means for transport in vertical direction only or independently in vertical and horizontal directions
B62H 3/04 - Separate supports or holders for parking or storing cycles involving forked supports or brackets for holding a wheel
B62H 3/08 - Separate supports or holders for parking or storing cycles involving recesses or channelled rails for embracing the bottom part of a wheel
Provided is a quick charging device that can conduct quick charging even with a conventional meter-rate lighting power supply or a low voltage power service power supply, and, in the case that the storage battery (for example, an electric vehicle's storage battery) to be charged is empty, that can conduct charging up to a charging rate of 30-50% (up to a maximum of about 60%) in a short period of time (a few minutes), in repetition in short intervals. The quick charging device (20) is provided, for charging a storage battery (11) mounted on an electric vehicle (EV) (10), with: a converter (21) having a rectifying function that converts an alternating current supplied by a 100V or 200V AC power supply to a direct current, and a boosting function; a storage battery (high output-density storage battery) (22A) with high output-density and instantaneous power; and a storage battery (high energy-density storage battery) (22B) with high energy-density and a large energy capacity.
