A kitchen waste recycling method and a treatment system that uses said method, the method comprising the following steps: 1) carrying out hydraulic cleaning and preliminary separation on kitchen waste; 2) selecting waste metal, waste plastic, bones, glass, and ceramic from the separated out residue material, processing the bones into bone meal and packaging same for selling, packaging the waste plastic for selling, and subjecting the remaining food residue material to dry distillation after crushing, dehydrating, and drying; 3) further separating out biological oil, fine residue, and sewage from the separated liquid, storing the biological oil, performing dry distillation on the fine residue to convert same into biochar, and biogas produced after carrying out anaerobic treatment on the sewage is used as fuel of a dry distillation unit after being subjected to desulfurization; 4) performing dry distillation on biogas residue after drying same; and 5) condensing dry distillation gas produced during dry distillation, separating out a combustible gas to serve as dry distillation unit fuel, and subjecting the remaining liquid to oil-water separation to separate out biomass oil and pyroligneous acid.
This disclosure discloses an apparatus of treating a river, comprising a river bed sludge suction device, a container-type sand-stone refuse separation device, a container-type dehydration device, a container-type pulverization device, a storage container, a container-type drying device, a container-type carbonization device, a container-type flocculation device, a container-type precipitation device, a container-type activated coke filtration and adsorption device, a container-type power generation device, a container-type operation and control chamber, and a cleaning ship for floating debris and river bank refuse. This disclosure discloses a method of treating a river using the apparatus described above where a biochar is produced from the separated, dehydrated and dried sludge. The biochar is then delivered back to the river bed to adsorb nitrogen and phosphorus, cleaning the river water, followed by purification treatments on sewage discharged from the dehydration apparatus and discharging the treated sewage water back to the river.
Disclosed are a method and system for environmentally friendly dredging of a large reservoir and a lake. The method for environmentally friendly dredging comprises: on a water surface of a lake or a reservoir where sludge cleaning is implemented, using a module floating box (31), a drive floating box (3), a domestic water floating box (5), a sewage floating box (22), etc. to assemble a floating platform (1); arranging equipment, such as a sludge pumping device (8), a sand waste separating device (12), a dehydrating device (9), a drying device (15), a dry distillation device (16), a sewage purification device (17), a diesel generator (2), a diesel storage tank (21), a steam boiler (19), a fuel depot (20), an anchor windlass and an anchor (23) and living facilities on the floating platform (1); and carrying out pretreatment on sludge pumped by the sludge pumping device (8) and then carrying out dry distillation, thus implementing sludge cleaning on the water surface on the spot, land is not occupied, the water body is not disturbed, no sludge is transported outward, no secondary pollution of the water body and the environment is caused, and resource recovery, rendering harmless, stabilization and reduction of sludge treatment are realised.
A method and devices for remediating contaminated soil. The method comprises: determining a contaminated arrange of a region where contaminated soil is located; digging out soil in the determined contaminated arrange to carry out dry distillation; on the surface of a bottom soil layer in the region in which the contaminated soil has been dug out, preparing an isolation protective layer by using a carbon adsorption material; backfilling the remediated soil on which dry distillation has been carried out, to the region in which the contaminated soil has been dug out and on the bottom of which the isolation protective layer is prepared by using the carbon adsorption material, and adding biochar to the upper backfilled soil; and planting green plants on the soil on which remediation backfill has been carried out and to which the biochar is added, so as to carry out green remediation. The devices comprise a digging device, a conveying device, a breaking device, a screening device and a dry distillation device, used for respectively digging, conveying, breaking, screening and dry-distilling the contaminated soil. The devices also comprise a gas treatment device, used for purifying and separating dry-distilled gas generated in the process of dry-distilling the contaminated soil.
An apparatus for treating a black and odorous river, comprising a river bed silt suction device (2), a container-type sandstone waste separation device (38), a container-type dehydration device (5), a container-type crushing device (11), a storage container (6), a container-type drying device (37), a container-type dry distillation device (7), a container-type flocculation device (13), a container-type sedimentation device (14), a container-type active coke filtration and adsorption device (15), a container-type power generation device (18), a container-type operation control chamber (19) and a cleaning boat for objects floating on the surface of a river and river bank waste(9). The silt suction device (2) is connected to the container-type sandstone waste separation device (38) via a silt delivery pipe laid on the surface of the water. Bulky materials discharged from the container-type sandstone waste separation device (38) and objects floating on the surface of the river and/or river bank waste collected by the cleaning boat (9) are delivered to and treated in the container-type crushing device (11). Then, same, together with the silt treated by the container-type sandstone waste separation device (38), enter the container-type dehydration device (5) for dehydration. Discharged waste water sequentially enters the container-type flocculation device (13), the container-type sedimentation device (14) and the container-type active coke filtration and adsorption device (15) for flocculation, sedimentation, and filtration, adsorption and purification treatments by active coke, and is then discharged into the river. The dehydrated silt and residues enter the container-type drying device (37) for treatment, and after treatment, are then delivered to the container-type dry distillation device (7) to prepare biochar, and the biochar is delivered back to the bottom of the river via a delivery pipe. Black and odorous river water is extracted by a water pump from one end of a river treatment section, sequentially enters the container-type flocculation device (13), the container-type sedimentation device (14) and the container-type active coke filtration and adsorption device (15) for flocculation, sedimentation, and filtration, adsorption and purification treatments by active coke, and is then discharged back into the river from the other end of the river treatment section. The operation of each of the above-mentioned devices is controlled by the container-type operation control chamber (19). Disclosed is a method for treating a black and odorous river using the above-mentioned apparatus.
An organic refuse disposal apparatus and a method for disposing organic refuse by using the disposal apparatus. The apparatus comprises: a dehydration device (2), a steam drying device (3), an organic refuse drying bin (5), a dry distillation device (7), a biomass fuel combustion engine (34), a cooling device (7), an exhaust gas waste heat vapor generator (12), a gas purification and separation device (22), an oil-water separation device (23), a sewage treatment device (30), and an oil storage device (25). By using the apparatus to dispose the organic refuse, the advantages of reclamation, harmlessness and environmental friendliness of a dry distillation method for disposing the organic refuse are preserved; a combined process of dehydration, drying and dry distillation is utilized; waste heat is recycled, expensive natural gas is replaced by biomass fuels, and defects that the operation costs are high when the organic refuse is independently disposed by the dry distillation method are overcome.
AMAZON ENVIRONMENTAL PROTECTION TECHNOLOGY AND EQUIPMENT PTE. LTD (Singapore)
Inventor
Zhang, Dawei
Abstract
A device for reversing and discharging active coke in a sewage treatment device (20); two neighboring partition walls are provided with branch discharge troughs (10) thereabove; one end of each branch discharge trough (10) is sealed by a plug, and the other end is connected to a main discharge trough (11); the main discharge trough (11) is provided at one side of the sewage treatment device (20) inclining in a walking direction of an electric operation platform (22); the upper end of the main discharge trough (11) is sealed by the plug, and the discharge port of the main discharge trough (11) is connected to a dehydrating device (12); the bottom portion of each water treatment unit (21) is connected to parallel delivery pipes (26); the upper ends of the parallel delivery pipes (26) are sealed by the plugs, and the other ends are connected to the main discharge trough (11); the middle portion of each water treatment unit (21) is provided with a vertical delivery pipe (7); the top portion of the vertical delivery pipe (7) is detachably installed with a material reversing cap (8) or a third connection hose (9); each water treatment unit (21) is provided with a first air pipe (6) and a second air pipe (25) therein; one end of the first air pipe (6) is connected to the bottom portion of the vertical delivery pipe (7), and one end of the second air pipe (25) extends into the parallel delivery pipes (26); and an air storage tank (1) is connected to a control box (4) of the electric operation platform (22). Also disclosed is a method for reversing and discharging the active coke.
C02F 1/28 - Treatment of water, waste water, or sewage by sorption
B01D 53/02 - Separation of gases or vapoursRecovering vapours of volatile solvents from gasesChemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases or aerosols by adsorption, e.g. preparative gas chromatography
8.
SANDY AND DEGRADED SOIL MODIFIER AND PREPARATION METHOD AND DEVICE THEREFOR
A sandy and degraded soil modifier is formed by mixing organic carbon with active coke powder according to a weight ratio of 1:0.1-0.3, wherein the organic carbon is formed by conducting dry distillation on organic wastes. A method for preparing the soil modifier comprises: A) pretreating organic wastes; B) conducting dry distillation on the pretreated organic wastes to form organic carbon; and C) mixing the organic carbon with active coke powder according to a weight ratio of 1:0.1-0.3 to obtain the sandy and degraded soil modifier. Also disclosed is a device for preparing the sandy and degraded soil modifier.
C09K 17/04 - Soil-conditioning materials or soil-stabilising materials containing inorganic compounds only applied in a physical form other than a solution or a grout, e.g. as granules or gases
9.
WASTE TREATMENT METHOD AND APPARATUS FOR SOLID/LIQUID SEPARATION AND ORGANIC/INORGANIC MATERIAL SEPARATION
AMAZON ENVIRONMENTAL PROTECTION TECHNOLOGY AND EQUIPMENT PTE. LTD (Singapore)
Inventor
Zhang, Dawei
Abstract
A waste treatment method for solid/liquid separation and organic/inorganic material separation, the process thereof being: 1) city household waste is subjected to bag-breaking and washing with water; 2) after bag-breaking, the city household waste is washed with water; 3) after washing, the city household waste is subjected to solid/liquid separation; 4) after sorting, water-soluble organic waste is crushed, then dehydrated; 5) after the wastewater generates biogas, the biogas residue is dehydrated and made into biochar. The present application also discloses an apparatus for implementing the described method.
AMAZON ENVIRONMENTAL PROTECTION TECHNOLOGY AND EQUIPMENT PTE. LTD (Singapore)
Inventor
Zhang, Dawei
Abstract
Disclosed is a method for the anaerobic pyrolysis treatment of dead livestock and urban organic wastes by using an anaerobic pyrolysis device to perform a harmlessness treatment on dead pigs, the treatment being a chemical reaction process performed under a sealed, oxygen-free, non-combustible, high-temperature state, comprising heating the bodies of the pigs to high temperature under an anaerobic state, and by the action of thermal decomposition through reactions such as vaporization, pyrolysis, dehydrogenation, thermal condensation and carbonization, evaporating the moisture from the bodies of the pigs, converting the organics therein into combustible gases and organic carbon, and killing various types of bacteria in the bodies of the dead pigs via the high temperature. Then, the dead livestock have been obtained by a harmlessness resource treatment, avoiding environmental pollution and avoiding the spread of major animal diseases such as foot-and-mouth disease, highly pathogenic avian influenza, highly pathogenic blue-ear pig disease, and swine fever. Also disclosed is a device for realizing the above-mentioned method.
C05F 15/00 - Mixtures of fertilisers covered by more than one of main groups Fertilisers from mixtures of starting materials, all the starting materials being covered by this subclass but not by the same main group
B09B 3/00 - Destroying solid waste or transforming solid waste into something useful or harmless
11.
METHOD AND APPARATUS FOR UTILIZING WASTE HEAT OF HIGH-TEMPERATURE FLUE GAS
Provided is an apparatus and method for utilizing the waste heat of a high-temperature flue gas. An apparatus for utilizing the waste heat of a high-temperature flue gas comprises a steam heating device (5), an activated gas mixer (6), a steam generator from waste heat of the flue gas (1), a recovery device for waste heat of activated coke (2), a heat preservation water tank (3), a heat storage tank (4) and a control cabinet (8). The high-temperature flue gas generated by an activated coke preparing unit (7) enters a flue gas chamber (11) of the steam heating device (5) to heat the steam in a steam heating tube bundle (12); the hot flue gas flowing out of the steam heating device (5) flows through the steam generator from waste heat of the flue gas (1) to heat the water therein, thereby generating steam, the steam being conveyed to the heat storage tank (4), and the cooled flue gas is discharged; the steam in the heat storage tank (4) flows into the steam heating device (5) when the activated coke preparing device (7) enters an activation stage, the saturated steam is heated into a high-temperature steam and delivered into the activated gas mixer (6), where the steam is mixed with the high-temperature flue gas, before being conveyed to the activated coke preparing unit (7) to complete the activation procedure; the prepared activated coke is sent to the recovery device for waste heat of activated coke (2) to heat the water in the cooling pipe thereof, and the heated water is sent to the heat preservation water tank (3), thereby cyclically heating the water in the heat preservation water tank (3).
An operation control system for sludge dry distillation equipment, comprising: a control layer, a power terminal layer and a field layer; the control layer is an electric control cabinet (16) installed with a programmable logic controller therein for operating the entire sludge dry distillation equipment; the power terminal layer comprises a power distribution cabinet (15) for distributing power for the sludge dry distillation equipment, a main-engine control cabinet (13) and an auxiliary-engine control cabinet (14); the main-engine control cabinet (13) and the auxiliary-engine control cabinet (14) being remote IO stations for controlling the collection and conversion of field data; the field layer comprises a field device and a push button station (7), a field instrument (24) and a display operation station. The push button station (7) is electrically connected with the power distribution cabinet (15) for manually operating the device, and the display operation station is electrically connected with the main-engine control cabinet (13) and the auxiliary-engine control cabinet (14) for displaying system operation parameters via the field instrument (24). The system can perform chain operations, control and management on various devices of the sludge dry distillation equipment, thus improving system operation stability, reducing work intensity of an operator, improving the quality of dry distilled biochar, saving energy and reducing costs for biochar dry distillation.
G05B 19/418 - Total factory control, i.e. centrally controlling a plurality of machines, e.g. direct or distributed numerical control [DNC], flexible manufacturing systems [FMS], integrated manufacturing systems [IMS] or computer integrated manufacturing [CIM]
C02F 11/10 - Treatment of sludgeDevices therefor by pyrolysis
13.
OPERATION CONTROL SYSTEM FOR ACTIVE COKE REGENERATION EQUIPMENT
An operation control system for an active coke regeneration equipment and operation process thereof, the operation control system comprising: a control layer, a power terminal layer and a field layer. The control layer is an electric control cabinet (17) installed with a programmable logic controller therein for operating the entire active coke regeneration equipment; the power terminal layer comprises a power distribution cabinet (15) for distributing power for the entire active coke regeneration equipment, and distributed terminal cabinets (13, 14, 16) are remote IO stations for controlling the collection and conversion of the field data; the field layer comprises field equipment and a push button station (42), a field instrument (30) and a display operation station. The push button station (42) is electrically connected with the power distribution cabinet (15) for manually operating the equipment, and the display operation station is electrically connected with the distributed terminal cabinets (13, 14, 16) for displaying system operation parameters via the field instrument (30).
B01J 20/20 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbonSolid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising carbon obtained by carbonising processes
14.
ACTIVE COKE REGENERATION MIXED VAPOR TREATMENT METHOD AND APPARATUS
An active coke regeneration mixed vapor treatment method comprises a process of: A) performing fist water condensation on a mixed vapor produced in an active coke regeneration process in a first condensation area by spray water; B) performing second water condensation on the mixed vapor after the first water condensation in a second condensation area, to further condensate and purify the mixed vapor; C) removing moisture in the gas through mist removal from a gas part in the mixed vapor after the second water condensation, and discharging the remaining gas from the top of the second condensation area; and D) discharging active coke micro powder in the mixed vapor after the second water condensation with condensation water. Also an apparatus for implementing the method.
B01J 20/20 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbonSolid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising carbon obtained by carbonising processes
B01D 50/00 - Combinations of methods or devices for separating particles from gases or vapours
A de-dusting and cooling method for an active coke regeneration apparatus comprises: when an active coke regeneration apparatus runs, generating a negative pressure region at each of a discharge end and a feeding end, the negative pressure region absorbing leaked gas and dust; and cooling the active coke regeneration apparatus by using gas flow generated by the negative pressure region. Also provided is a device for implementing a de-dusting and cooling method for an active coke regeneration device. A feeding chamber (29) is disposed at one end of the active coke apparatus, and a discharge chamber (7) is disposed at the other end. A front mechanical room (23) is between the feeding chamber (29) and a burning chamber (22). A rear mechanical room (18) is between the discharge chamber (7) and the burning chamber (22). The burning chamber (22) is between the front mechanical room (23) and the rear mechanical room (18). A roller (20) is connected from the feeding chamber (29) to the discharge chamber (7). A front negative pressure dust-absorbing chamber (27) is between the feeding chamber (29) and the front mechanical room (23). A vent pipe (9) is disposed in the front mechanical room (23). An air inlet (16) of the vent pipe (9) is at an upper portion in the front mechanical room (23). An air outlet (11) of the vent pipe (9) is in the front negative pressure dust-absorbing chamber (27). A rear negative pressure dust-absorbing chamber (5) is between the discharge chamber (7) and the rear mechanical room (18). A vent pipe (9) disposed in the rear mechanical room (18). An air inlet (16) of the vent pipe (9) is at an upper portion in the rear mechanical room (18). An air outlet (11) of the vent pipe (9) is in the rear negative pressure dust-absorbing chamber (5). A dust-absorbing port (4) is disposed at the top of the front negative pressure dust-absorbing chamber (27) and the rear negative pressure dust-absorbing chamber (5). The dust-absorbing port (4) is connected onto a dust-absorbing apparatus (1) by a dust-absorbing pipeline (2). The feeding chamber (29) is provided with a gas outlet (30).
B01D 53/02 - Separation of gases or vapoursRecovering vapours of volatile solvents from gasesChemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases or aerosols by adsorption, e.g. preparative gas chromatography
B01J 20/20 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbonSolid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising carbon obtained by carbonising processes
C02F 1/28 - Treatment of water, waste water, or sewage by sorption
Disclosed is destructive distillation equipment: a destructive distillation drum (1), wherein the two ends thereof are respectively a feed drum (2) and a discharge drum (3), the diameter of the destructive distillation drum (1) being greater than the diameter of the feed drum (2) and of the discharge drum (3); rows of reversing and guiding material plates (4) are mounted onto the inner wall of the destructive distillation drum (1), a space remaining between every two rows of reversing and guiding material plates (4); each row of reversing and guiding material plates (4) is composed of reversing and guiding material plates (4), each reversing and guiding plate (4) being composed of a flat face and an inclined face a triangular shape, the flat faces of each row of reversing and guiding material plates (4) being arranged horizontally, and the tip of the triangular shape pointing towards the discharge outlet of the destructive distillation drum (1); the destructive distillation drum (1) is disposed within a combustion chamber (15), and a supporting rolling ring (9) is mounted onto the outer wall of the feed drum (2) and of the discharge drum (3), the supporting rolling ring (9) being located on a supporting roller (12); the outer wall of the discharge drum (3) is provided with a drive gear ring (10), and the discharge drum (3), the destructive distillation drum (1) and the feed drum (2) rotate together forwards or backwards, driven by an electric motor (13). The present invention can control and regulate the residence time of the materials in the destructive distillation drum (1) during each process flow and the whole flow, thus controlling the quality of the product.
Disclosed is a method for preparing an agricultural carbon by pyrolyzing, carbonizing and activating organic waste, which comprises the steps of: feeding the organic substance into heating equipment; using the heating equipment; heating the organic substance using the heating equipment, during which the organic substance is decomposed to produce carbon and a mixed gas which is discharged; at the same time when the heating equipment is heating, feeding the steam and flue gas into the heating equipment to produce the agricultural carbon after activating the carbon for a period, in which case, the steam is water steam and the flue gas is produced after burning a combustible material. The present invention also discloses a device for realizing the abovementioned method, which device at least comprises a heating chamber and a steam boiler which is used for providing the steam and flue gas and for recycling the combustible gas produced after decomposition of the organic substance.
The present invention provides a device for biochar manufacturing. The device comprises a hopper, a rotary preheat chamber, a rotary dry distillation chamber and a cooling chamber. The rotary preheat chamber is located in a hot flue gas chamber, with one end connecting to the hopper through an incoming roller and a first screw conveyor and the other end connecting to the top of a middle hopper through an outgoing roller, used to preheat the biomass raw material; the rotary dry distillation chamber is located inside a combustion chamber, with one end connecting to the bottom of the middle hopper through a front roller and a second screw conveyor and the other end connecting to a discharge chamber through a back roller, and a burner being installed at its bottom; the dry distillation chamber is used for carbonizing the preheated biomass raw material and causing it to undergo an activation reaction with steam and flue gas to form biochar; the cooling chamber is located below the discharge chamber and is used for cooling the biochar formed through the activation reaction. The biochar manufacturing device of the present invention can use livestock manure, crop stalks, bagasse and other biomass as raw material to manufacture biochar in a low-cost and industrialized manner.
C10B 53/02 - Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
C10B 31/08 - Charging devices for coke ovens for charging horizontally coke ovens with horizontal chambers
A method for treating saturated activated carbon comprises the following steps: A) the saturated activated carbon is dewatered so that the water content of the activated carbon is ≤25%. B) The product obtained from the step A is dried at the starting temperatures of 120ºC-150ºC. C) the product obtained from the step B is dried distilled. The dry distillation condition is that heating to 500ºC-600ºC at the rate of 4ºC-10ºC per minute and maintaining for 10-60 minutes. The organic matter on the surface and in the hole of the activated carbon is cracked, volatilized, and carbonized. D) The product obtained from the step C is activated and the activation condition is that heating to 800ºC-950ºC at the rate of 2ºC-8ºC per minute and supplying the vapor. The proportion by weight of the activated carbon and the vapor is 1:0.5-5. The activated time is 0.5-2 hours. The activated carbon may be used as the fuel after many treating processes.
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