Proposed is an electrode, which includes a first frame and a second frame, wherein the first and second frames are non-conductors, and at least one of the first and second frames includes a plurality of cavities, a packing member disposed between the first and second frames and attached to one of the first and second frames, wherein the first frame, the second frame, and the packing member define an inner space that is open in one direction, a current-collecting member interposed in the inner space, and a powdered electrode active material with which the plurality of cavities is filled, the electrode active material contacting the current-collecting member. The electrode is usable for various purposes by changing the electrode active material alone, and the current-collecting member and the frames are reusable, which is economically advantageous.
A separator, a method of manufacturing the separator, and an electrochemical device including the separator. The separator includes: a porous substrate; and an inorganic particle layer formed on at least one surface of the porous substrate, wherein a release rate of the inorganic particle layer is 70% or more when measured by immersing the separator in a water tank at room temperature and then subjecting the separator to sonication under conditions of a frequency of 40 kHz, an output of 1,000 W, and an application time of 60 seconds.
Embodiments of the present disclosure relate to an ion conductive polymer including a repeating unit of formula 1.
Embodiments of the present disclosure relate to an ion conductive polymer including a repeating unit of formula 1.
Embodiments of the present disclosure relate to an ion conductive polymer including a repeating unit of formula 1.
wherein in Formula 1, A+ is quaternary ammonium, B+ is an anion, a is an integer of 1 to 3, R1 is an organic group having 1 to 10 carbon atoms, R2 is H or an organic group having 1 to 10 carbon atoms, R3 is an organic group having 1 to 20 carbon atoms which includes at least one of an alkylene group or an arylene group, and Ar is a benzene ring.
CARBON DIOXIDE ABSORBENT CONTAINING IONIC MATERIAL CONTAINING SPIRO AMMONIUM CATION AND HYDROXIDE ANION, AND CARBON DIOXIDE SEPARATION METHOD USING THE SAME
The embodiments of the present disclosure relate to a carbon dioxide absorbent containing an ionic material containing a spiro ammonium cation and a hydroxide anion. The carbon dioxide absorbent according to an embodiment contains a hydroxide anion having a small molecular weight and high basicity, such that absorption performance per unit volume of the absorbent may be effectively improved. Further, the carbon dioxide absorbent according to an embodiment is soluble in water and thus may not cause layer separation problems.
B01J 20/22 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising organic material
B01D 53/14 - 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 absorption
A polyolefin-based microporous membrane, a separator for a secondary battery, and manufacturing method thereof are provided. The polyolefin-based microporous membrane has a puncture strength of 0.3 N/μm or more, a gas permeability of 0.8×10−5 Darcy or more, a porosity of 30.0% or more, and a surface roughness of 2.1 μm or less, the surface roughness being obtained by selecting 5 random points on a front surface and 5 random points on a back surface, each random point having an area of 284 μm wide×220 μm long, measuring a maximum height difference (μm, Rmax) which is a difference between the highest surface height and the lowest surface height in the area of each point, and adding an average value of values measured in each of the 5 points on the front surface and an average value of values measured in each of the 5 points on the back surface.
A method and a device for generating recipes of a polymer composite material are provided which include acquiring a prediction recipe based on a preset target property of a target polymer composite material and a recipe prediction model; acquiring a result property of a polymer composite material generated based on the prediction recipe; calculating a difference value between the target property and the result property; and outputting or modifying the prediction recipe based on a result of comparing the difference value with a preset reference value.
The mixed refrigerant composition according to embodiments of the present disclosure includes carbon dioxide (R-744), trifluoroiodomethane (R-13I1), and 1,1-difluoroethane (R-152a), wherein a sum of contents of the trifluoroiodomethane (R-13I1) and the 1,1-difluoroethane (R-152a) based on a total weight of the mixed refrigerant composition may be 60 wt. % or more and less than 100 wt. %. Accordingly, environmental pollution caused by the mixed refrigerant composition may be suppressed, and the cooling performance of the mixed refrigerant composition may be improved.
An electrolyte for a lithium secondary battery according to the present disclosure includes: a lithium salt; an organic solvent; an additive comprising a compound including a carbon-carbon triple bond, a linear ether group, and a 4- or 5-membered cyclic ether group; and a sulfur compound including a sulfur-containing heterocyclic structure.
An electrolyte for a lithium secondary battery according to embodiments of the present disclosure comprises a lithium salt and a compound containing at least two sulfonate groups and at least one cyclic group. A lithium secondary battery according to embodiments of the present disclosure comprises: an electrode assembly including at least one positive electrode and at least one negative electrode; and the electrolyte.
A fixed bed reactor for desulfurization is provided, the fixed bed reactor including an outlet collector that is located at a lower end portion of the fixed bed reactor; and a lower baffle that is formed spaced apart from an upper portion of the outlet collector. The fixed bed reactor efficiently lowers a surface temperature of the outlet collector located at a lower end portion of the fixed bed reactor.
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
11.
MONOMER FOR ELECTROLYTE, ELECTROLYTE FOR SECONDARY BATTERY INCLUDING THE SAME, METHOD OF PREPARING THE SAME AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
A monomer for an electrolyte according to the embodiments of the present disclosure may include a compound represented by Formula 1. A lithium secondary battery according to the embodiments of the present disclosure includes a cathode, an anode, and an electrolyte, wherein the electrolyte may include a polymer of the compound represented by Formula 1.
A monomer for an electrolyte according to the embodiments of the present disclosure may include a compound represented by Formula 1. A lithium secondary battery according to the embodiments of the present disclosure includes a cathode, an anode, and an electrolyte, wherein the electrolyte may include a polymer of the compound represented by Formula 1.
A monomer for an electrolyte according to the embodiments of the present disclosure may include a compound represented by Formula 1. A lithium secondary battery according to the embodiments of the present disclosure includes a cathode, an anode, and an electrolyte, wherein the electrolyte may include a polymer of the compound represented by Formula 1.
wherein X1, X2 and X3 are each independently a halogen element,
R1, R2 and R3 are each independently hydrogen, a halogen element, a substituted or unsubstituted C1 to C6 alkyl group, or a polymerizable group, and
at least one of R1, R2 or R3 is a polymerizable group.
A method for manufacturing a separator for a secondary battery, and a lithium secondary battery comprising same. A separator for a lithium secondary battery, and a lithium secondary battery comprising same, the separator having excellent heat resistance, adhesive strength, air permeability and high-temperature shrinkage characteristics, which are significantly improved, and having an inorganic particle layer formed on one surface or both surfaces of a porous substrate layer, the inorganic particle layer being prepared from a slurry comprising inorganic particles and a condensation-suppressed silane-based hydrocondensate having excellent binding force between organic and inorganic materials.
H01M 50/449 - Separators, membranes or diaphragms characterised by the material having a layered structure
H01M 50/451 - Separators, membranes or diaphragms characterised by the material having a layered structure comprising layers of only organic material and layers containing inorganic material
H01M 50/489 - Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
A method for manufacturing a separator for a secondary battery, and a lithium secondary battery comprising same. A separator for a lithium secondary battery, and a lithium battery comprising same, the separator having 5 secondary excellent heat resistance, adhesive strength, air permeability and high-temperature shrinkage characteristics, which are significantly improved, and having an inorganic particle layer formed on one surface or both surfaces of a porous substrate layer, the inorganic particle layer being prepared from a slurry comprising inorganic particles and a condensation-suppressed silane-based hydrocondensate having excellent binding force between organic and inorganic materials.
H01M 50/449 - Separators, membranes or diaphragms characterised by the material having a layered structure
H01M 50/451 - Separators, membranes or diaphragms characterised by the material having a layered structure comprising layers of only organic material and layers containing inorganic material
H01M 50/489 - Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
An electrolyte for a lithium secondary battery according to embodiments of the present disclosure may include an organic solvent, a lithium salt, and a phosphonate-based additive represented by Formula 1. The lithium secondary battery according to embodiments of the present disclosure may include a cathode, an anode disposed opposite to the cathode, and the electrolyte for a lithium secondary battery including a phosphonate-based additive represented by Formula 1.
An electrolyte for a lithium secondary battery according to exemplary embodiments includes an additive including a compound having a structure represented by Formula 1, an organic solvent and a lithium salt. The electrolyte for a lithium secondary battery according to exemplary embodiments may form a uniform and stable solid electrolyte interphase (SEI) with high ionic conductivity on the electrode surface. Accordingly, a lithium secondary battery including the electrolyte for a lithium secondary battery may exhibit improved low-temperature performance and high-temperature stability.
H01M 10/0567 - Liquid materials characterised by the additives
H01M 4/02 - Electrodes composed of, or comprising, active material
H01M 4/58 - Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFySelection of substances as active materials, active masses, active liquids of polyanionic structures, e.g. phosphates, silicates or borates
A separator for a secondary battery, a method of manufacturing the separator, and a secondary battery including the separator, where these separator includes: a porous substrate and an inorganic particle layer formed on at least one surface of the porous substrate, wherein a heat shrinkage rate S of the separator is 8% or less may be provided.
H01M 50/403 - Manufacturing processes of separators, membranes or diaphragms
H01M 50/449 - Separators, membranes or diaphragms characterised by the material having a layered structure
H01M 50/489 - Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
17.
ANODE ACTIVE MATERIAL FOR LITHIUM SECONDARY BATTERY, METHOD OF PREPARING THE SAME AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
An anode active material for a lithium secondary battery according to the embodiments of the present disclosure includes composite particles comprising carbon-based particles and silicon-containing particles including silicon and hydrogen disposed on the surface of the carbon-based particles and an H/Si ratio of the composite particles, defined by Equation 2, is 0.5% to 5.3%.
A mixed refrigerant composition includes carbon dioxide (R-744), 2,3,3,3-tetrafluoropropene (R-1234yf) and trifluoroiodomethane (R-13I1). A content of the carbon dioxide (R-744) ranges from 1 to 10 wt. % based on a total weight of the mixed refrigerant composition, and a sum of a content of the 2,3,3,3-tetrafluoropropene (R-1234yf) and a content of the trifluoroiodomethane (R-13I1) ranges from 90 to 99 wt. % based on the total weight of the mixed refrigerant composition. A boiling point at 1 atm of the mixed refrigerant composition ranges from −76 to −35° C.
The present disclosure relates to a method for preparing a Ziegler-Natta catalyst for polymerization of linear low-density polyethylene (LLDPE), and specifically, the method for preparing a Ziegler-Natta catalyst for polymerization of linear low-density polyethylene according to an embodiment includes preparing a magnesium chloride support containing magnesium chloride alcoholate obtained by mixing an excessive amount of alcohol with magnesium chloride. In the method for preparing a Ziegler-Natta catalyst according to an embodiment, a catalyst composition is easily controlled, such that it is possible to effectively produce linear low-density polyethylene having various physical properties and excellent copolymerization performance.
An electrolyte for the lithium secondary battery according to embodiments of the present disclosure includes an additive including a complex containing a boroxine compound, a lithium salt and an organic solvent. Accordingly, a lithium secondary battery including the electrolyte for a lithium secondary battery exhibits improved high-temperature storage characteristics and cycle life characteristics.
H01M 10/0567 - Liquid materials characterised by the additives
H01M 4/02 - Electrodes composed of, or comprising, active material
H01M 4/38 - Selection of substances as active materials, active masses, active liquids of elements or alloys
H01M 4/525 - Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
H01M 4/583 - Carbonaceous material, e.g. graphite-intercalation compounds or CFx
A cathode active material for a lithium secondary battery according to embodiments of the present disclosure comprises a lithium-sulfur-metal-containing portion and lithium-transition metal oxide particles having a minimum particle diameter (Dmin) of greater than 1 μm, wherein a relative standard deviation of the sulfur signal values of the lithium-transition metal oxide particles, as measured repeatedly ten times by X-ray photoelectron spectroscopy (XPS) analysis, is 10.5% or less.
C01G 53/506 - Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2 containing manganese of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2 containing lithium and cobalt with the molar ratio of nickel with respect to all the metals other than alkali metals higher than or equal to 0.5, e.g. Li(MzNixCoyMn1-x-y-z)O2 with x ≥ 0.5 with the molar ratio of nickel with respect to all the metals other than alkali metals higher than or equal to 0.8, e.g. Li(MzNixCoyMn1-x-y-z)O2 with x ≥ 0.8
A system for regenerating a lithium precursor includes an electrode active material mixture supply unit, a dry rotary heating reactor for reacting the electrode active material mixture supplied from the electrode active material mixture supply unit with a reductive gas, and a lithium precursor recovery unit for collecting a lithium precursor from a reaction product generated by a reduction reaction of the electrode active material mixture in the dry rotary heating reactor. A lithium precursor is selectively recovered from the preliminary precursor mixture. Recovery yield and selectivity can be improved using the dry rotary heating reactor.
A method for evaluating corrosion resistance of a thermal spray coating, the method including (a) coating one or more sides of a sample by a thermal spray coating method to form a thermal spray coated sample; (b) immersing the thermal spray coated sample in an acid solution; and (c) analyzing the components of the acid solution by collecting the acid solution at regular intervals after immersion. The analysis is performed by an inductively coupled plasma (ICP) analysis method. Based on the method, accuracy of evaluating the corrosion resistance of the thermal spray coating can be improved, and the method of evaluating the corrosion resistance of the thermal spray coating can be simplified.
G01N 17/00 - Investigating resistance of materials to the weather, to corrosion or to light
C23C 4/01 - Selective coating, e.g. pattern coating, without pre-treatment of the material to be coated
C23C 4/12 - Coating by spraying the coating material in the molten state, e.g. by flame, plasma or electric discharge characterised by the method of spraying
24.
ELECTROCHEMICAL WATER TREATMENT METHOD USING SELECTIVE ION SEPARATION
A method of removing pollutants from wastewater, the method including a) separating the wastewater into first treated water containing monovalent ions and second treated water containing multivalent ions, b) concentrating the monovalent ions in the first treated water to produce concentrated water, c) electrochemically reducing nitric acid in the concentrated water, and d) electrochemically oxidizing organic matter in the second treated water. According to the above method, the pollutants in the wastewater can be removed efficiently and environmentally.
A apparatus for analyzing a composition of an intermetallic compound includes a database storing data of a plurality of feature areas matched to respective composition ratios, a plurality of brightness range data corresponding to the plurality of respective feature areas, and color data, for an intermetallic compound generated during welding of dissimilar metals, a microscope image acquisition unit acquiring an electron microscope image including a brightness value for the intermetallic compound to be analyzed, a signal processor extracting a unit brightness value corresponding to each preset image basic unit from the electron microscope image and searching for color data of a corresponding feature area from the database based on the unit brightness value, and an image processor applying searched color data to the electron microscope image and generating a colorization image.
G01N 23/04 - Investigating or analysing materials by the use of wave or particle radiation, e.g. X-rays or neutrons, not covered by groups , or by transmitting the radiation through the material and forming images of the material
G01N 23/06 - Investigating or analysing materials by the use of wave or particle radiation, e.g. X-rays or neutrons, not covered by groups , or by transmitting the radiation through the material and measuring the absorption
G01N 23/2251 - Investigating or analysing materials by the use of wave or particle radiation, e.g. X-rays or neutrons, not covered by groups , or by measuring secondary emission from the material using electron or ion microprobes using incident electron beams, e.g. scanning electron microscopy [SEM]
G06T 7/90 - Determination of colour characteristics
G06V 10/56 - Extraction of image or video features relating to colour
26.
Negative Electrode Active Material For Secondary Battery, Method of Manufacturing the Same, Negative Electrode Comprising the Same, and Secondary Battery Comprising the Same
The present disclosure relates to a negative electrode active material for a secondary battery, including a silicon-based oxide particle, and a carbon coating layer coating at least a portion of the silicon-based oxide particle, in which the carbon coating layer has a surface roughness of greater than or equal to 4 nm and less than or equal to 30 nm.
Provided are a polyethylene microporous membrane, a method for manufacturing the same, and a separator including the microporous membrane. According to an embodiment, a polyethylene microporous membrane which has a thickness of 3 μm to 30 μm, a puncture strength of 0.15 N/μm or more, a shrinkage rate in the transverse direction of 5% or less as measured after being allowed to stand at 121° C. for 1 hour, and a PS index represented by the following Equation 1 of 110 or more is provided:
Provided are a polyethylene microporous membrane, a method for manufacturing the same, and a separator including the microporous membrane. According to an embodiment, a polyethylene microporous membrane which has a thickness of 3 μm to 30 μm, a puncture strength of 0.15 N/μm or more, a shrinkage rate in the transverse direction of 5% or less as measured after being allowed to stand at 121° C. for 1 hour, and a PS index represented by the following Equation 1 of 110 or more is provided:
[
Equation
1
]
PS
index
=
[
gas
permeability
(
×
10
-
5
Darcy
)
×
porosity
(
%
)
]
÷
[
shrinkage
rate
(
%
)
in
the
transverse
direction
at
12
1
°
C
.
]
.
B01D 67/00 - Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
B01D 69/02 - Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or propertiesManufacturing processes specially adapted therefor characterised by their properties
The present disclosure provides a method for producing hydrocarbons, comprising the steps of: (S1) heat treating organic waste in the presence of a heat transfer medium so as to generate a first mixed gas; (S2) steam reforming the first mixed gas in a first fluidized bed reactor so as to generate a second mixed gas; (S3) separating the second mixed gas into a first stream including carbon dioxide and a second stream including hydrogen and carbon monoxide; (S4) introducing, into a second fluidized bed reactor, the first stream separated out in step (S3), and converting same into carbon monoxide through reverse Boudouard reaction; (S5) mixing the second stream and the carbon monoxide obtained through conversion in step (S4), so as to produce a third mixed gas; (S6) generating syngas from the third mixed gas through a water-gas shift reaction; and (S7) generating hydrocarbons from the syngas through a catalytic reaction, wherein the heat transfer medium comprises 1-40 mass% of iron (Fe) and comprises 5-50 mass% of an alkaline earth metal oxide.
C10J 3/58 - 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 combined with pre-distillation of the fuel
C01B 3/44 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts using moving solid particles using the fluidised bed technique
C01B 3/48 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
Disclosed are a recarburizer based on a solid iron-containing carbonaceous product derived from a process of pyrolyzing methane in a methane-containing feedstock in the presence of an iron-based catalyst and a method of producing the same, where a solid, iron-containing carbonaceous material formed during methane pyrolysis using the iron-based catalyst can be produced into a molded product having a predetermined shape without a costly purification process, and can thus be employed in high value-added applications such as recarburizers.
Cathodes and lithium secondary batteries including the cathodes are disclosed. In some implementations, a cathode may include a cathode current collector and a cathode active material layer disposed on the cathode current collector and including cathode active material particles such that the cathode active material layer satisfies a specific equation. The cathode active material particles may include lithium metal oxide particles that include nickel, and may have a mole fraction of cobalt of 0.02 or less with respect to all elements except for lithium and oxygen.
H01M 4/525 - Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
H01M 4/02 - Electrodes composed of, or comprising, active material
H01M 4/62 - Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
An electrolyte for a lithium secondary battery according to the embodiments of the present disclosure includes a lithium salt, an organic solvent, a phosphate-based additive including a compound represented by the following Formula 1, and a halogenated benzene. A lithium secondary battery including the electrolyte and having improved flame retardancy and high-temperature stability of the electrolyte, as well as improved high-temperature lifespan characteristics and high-temperature storage characteristics may be provided.
A lubricant composition according to embodiments of the present disclosure may include a base oil, a friction-reducing agent which includes oleic acid, and an antiwear agent which includes a phosphoric acid compound. The friction-reducing agent may be included in the lubricant composition in a predetermined amount such as an amount of 0.02 wt % to 0.9 wt % based on a total weight of the lubricant composition.
C10M 129/40 - Carboxylic acidsSalts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having 8 or more carbon atoms monocarboxylic
C10M 141/10 - Lubricating compositions characterised by the additive being a mixture of two or more compounds covered by more than one of the main groups , each of these compounds being essential at least one of them being an organic phosphorus-containing compound
C10N 30/06 - OilinessFilm-strengthAnti-wearResistance to extreme pressure
An anode active material for a lithium secondary battery according to embodiments of the present disclosure includes composite particles which comprise a silicon-containing coating formed on a surface of carbon-based particles comprising porous, wherein the composite particles have a C/SiC peak intensity ratio of 1.0 to 4.5, which is measured through X-ray diffraction analysis after performing heat treatment on the composite particles at 900° C. to 1200° C. for 6 hours to 9 hours. The anode active material for a lithium secondary battery has improved capacity characteristics, output characteristics and lifespan characteristics.
H01M 4/587 - Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
C01B 32/324 - Preparation characterised by the starting materials from waste materials, e.g. tyres or spent sulfite pulp liquor
C01B 32/336 - Preparation characterised by gaseous activating agents
C01B 33/029 - Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material by decomposition of monosilane
A method of preparing a nickel sulfate salt including preparing a fooding solution including a nickel salt and an aqueous sulfuric acid solution, subjecting the feeding solution to crystallization to produce a mixed liquid containing a nickel sulfate solid. The mixed liquid is then subjected to solid-liquid separation to collect the nickel sulfate salt. The filtrate produced from the solid-liquid separation is recycled together with purging.
An anode for a lithium secondary battery includes an anode current collector, and an anode active material layer formed on at least one surface of the anode current collector. The anode active material layer includes an anode active material and an anode binder. The anode active material includes a plurality of composite particles, each of the composite particles include a silicon-based active material particle, and a solid electrolyte interphase (SEI) layer formed on at least a portion of a surface of the silicon-based active material particle. A relative standard deviation of thickness values of the SEI layer of the composite particles, which are measured by an X-ray photoelectron spectroscopy (XPS) from 9 different composite particles among the plurality of composite particles after repeating 100 cycles of charging and discharging is 20% or less.
H01M 4/13 - Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulatorsProcesses of manufacture thereof
H01M 4/133 - Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
H01M 4/136 - Electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
H01M 4/1393 - Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
H01M 4/1395 - Processes of manufacture of electrodes based on metals, Si or alloys
H01M 4/36 - Selection of substances as active materials, active masses, active liquids
H01M 4/38 - Selection of substances as active materials, active masses, active liquids of elements or alloys
H01M 4/48 - Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
H01M 4/58 - Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFySelection of substances as active materials, active masses, active liquids of polyanionic structures, e.g. phosphates, silicates or borates
H01M 4/587 - Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
H01M 4/62 - Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
36.
COMPOSITE SEPARATOR AND SECONDARY BATTERY USING THE SAME
Composite separators and secondary batteries are disclosed. In an embodiment, a composite separator includes a porous substrate and an adhesive layer formed on an outermost layer of at least one surface of the porous separator. The adhesive layer includes first organic particles with a first average particle diameter (D50) and a first glass transition temperature and second organic particles with a second average particle diameter (D50) and a second glass transition temperature. The first glass transition temperature is lower than the second glass transition temperature, and the first average particle diameter is smaller than the second average particle diameter, and the first organic particles and the second organic particles satisfy a specific relation.
H01M 50/449 - Separators, membranes or diaphragms characterised by the material having a layered structure
H01M 50/489 - Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
37.
METHOD FOR PRODUCING RECYCLED LUBRICATING BASE OIL FROM WASTE LUBRICATING OIL AND RECYCLED LUBRICATING BASE OIL PRODUCED THEREBY
According to an embodiment, a method for producing a recycled lubricating base oil from waste lubricating oil is proposed, the method including a) first pretreating the waste lubricating oil, b) performing distillation to recover a fraction having a specific boiling point from the first pretreated waste lubricating oil, c) second pretreating the fraction recovered in the distillation operation, and d) hydroprocessing the second pretreated fraction in the presence of a catalyst. The recycled lubricating base oil produced by the above method has a viscosity index (VI) equal to or greater than 130. The proposed method makes it possible to produce a high-grade lubricating base oil using only waste lubricating oil as a feed, thereby reducing the cost of raw materials for production of lubricating base oil, and having the advantage of being environmentally friendly.
C10M 175/00 - Working-up used lubricants to recover useful products
C10G 67/14 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including at least two different refining steps in the absence of hydrogen
C10N 30/00 - Specified physical or chemical property which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
38.
ZEOLITE WITH IMPROVED HYDRO-ISOMERIZATION ACTIVITY
According to an aspect of the present invention, provided is a zeolite catalyst having an MRE structure for hydro-isomerization. The zeolite catalyst has an adsorption volume ratio of lutidine to collidine measured by Fourier-transform infrared spectroscopy (FTIR) using lutidine and collidine as adsorbents of greater than 3 and less than or equal to 10. According to an aspect of the present invention, provided is a method of hydro-isomerization for a hydrocarbon feedstock, including subjecting the hydrocarbon feedstock to a hydro-isomerization reaction under conditions of a temperature of 200° C. to 500° C., a hydrogen pressure of 1 to 200 atmospheres, a liquid space velocity (LHSV) of 1.0 to 10.0 hr−1, and the hydrogen/feedstock ratio of 45 to 1780 Nm3/m3 in the presence of the zeolite catalyst.
C07C 5/22 - Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
B01J 29/70 - Crystalline aluminosilicate zeolitesIsomorphous compounds thereof of types characterised by their specific structure not provided for in groups
B01J 35/50 - Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
Electrochemical devices are disclosed for various applications such as secondary batteries. In an embodiment, an electrochemical device includes a positive electrode, a negative electrode, a separator, and an electrolyte. The separator includes a porous membrane including a core-shell structure that includes formed on at least one polyolefin strand. The coating shell includes one or more of a hydrophilic inorganic material or a hydrophilic polymer. The electrolyte includes a nitrile-based compound. The electrochemical device exhibits high ionic conductivity by including the porous separator having wettability to the electrolyte.
H01M 50/454 - Separators, membranes or diaphragms characterised by the material having a layered structure comprising a non-fibrous layer and a fibrous layer superimposed on one another
H01M 10/0525 - Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodesLithium-ion batteries
H01M 10/0567 - Liquid materials characterised by the additives
H01M 10/0568 - Liquid materials characterised by the solutes
H01M 10/0569 - Liquid materials characterised by the solvents
H01M 10/42 - Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
Electrochemical devices are disclosed for various applications such as secondary batteries. In an embodiment, an electrochemical device includes a positive electrode, a negative electrode, a separator, and an electrolyte. The separator includes a porous separator including inorganic fibers or including inorganic particles and a polymer binder, and the electrolyte includes a nitrile-based compound. The electrochemical device exhibits high ionic conductivity by including the porous separator having wettability to the electrolyte.
Electrochemical devices are disclosed for various applications such as secondary batteries. In an embodiment, an electrochemical device including a positive electrode, a negative electrode, a separator, and an electrolyte. Specifically, the separator includes a porous polymer membrane including one or more of hydrophilic inorganic particles or a hydrophilic polymer that are blended in a porous substrate, and the electrolyte includes a nitrile-based compound. The electrochemical device exhibits high ionic conductivity by including the porous separator having wettability to the electrolyte.
Electrochemical devices are disclosed for various applications such as secondary batteries. In an embodiment, an electrochemical device includes a positive electrode, a negative electrode, a separator, and an electrolyte. The separator includes a porous hydrophilic polymer membrane, and the electrolyte includes a nitrile-based compound. The electrochemical device exhibits high ionic conductivity by including the porous separator having wettability to the electrolyte.
A composition for vehicle parts based on recycled polypropylene includes: 15 wt % to 55 wt % of recycled polypropylene containing a first filler, a high crystallinity polypropylene, an impact modifier, and a second filler. In particular, the weight ratio of the high crystallinity polypropylene to the impact modifier is in a range of 3:1 to 11:1, the combined weight of the first filler and the second filler is from 20 wt % to 25 wt % based on the total weight of the composition, and the recycled polypropylene has a melt index in a range of 5 g/10 min to 35 g/10 min measured at 230° C. and 21.2 N according to ISO 1133-1.
The present disclosure relates to a method and a system for producing hydrogen, wherein the method comprises the steps of: (S1) introducing a feed gas containing C1 to C4 hydrocarbons into a first reactor and performing dry reforming to produce a first mixed gas; (S2) introducing carbon dioxide and carbon into a second reactor and converting same into a second mixed gas containing carbon monoxide via a reverse Boudouard reaction; (S3) mixing the first mixed gas and the second mixed gas to prepare a third mixed gas; (S4) generating synthetic gas from the third mixed gas through a water gas conversion reaction; and (S5) separating carbon dioxide from the synthetic gas to obtain hydrogen, wherein the carbon dioxide separated in step (S5) is recycled to the second reactor.
C01B 3/38 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
C01B 3/44 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts using moving solid particles using the fluidised bed technique
C01B 3/48 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
C01B 3/50 - Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
C01B 3/40 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts characterised by the catalyst
45.
Method for Predicting Characteristic of Polymer Composite Materials Based on Material and Device Thereof
A method for predicting characteristics of a polymer composite material and a device thereof may be provided, wherein the method includes inputting a recipe including two or more materials containing at least one polymer and a mixing ratio for each of the two or more materials; predicting properties of the polymer composite material according to the recipe based on a recipe and property prediction model; and outputting the properties of the polymer composite material.
According to the embodiments of the present disclosure, an ammonia decomposition catalyst may be prepared by performing heat treatment on alumina, a lanthanum compound and a cerium compound in a reducing gas atmosphere to form a composite oxide on an alumina support, and supporting an active metal including ruthenium on the composite oxide.
B01J 35/70 - Catalysts, in general, characterised by their form or physical properties characterised by their crystalline properties, e.g. semi-crystalline
A method for predicting recipes of a polymer composite material and a device thereof may be provided, wherein the method includes: obtaining at least one property for a target polymer composite material; predicting a recipe including at least two materials including at least one polymer for synthesizing the target polymer composite material and a mixing ratio for each of the at least two materials based on at least one property and recipe prediction model; and outputting the recipe.
A cathode active material for a lithium secondary battery according to an embodiment of the present disclosures a plurality of composite particles, each of which comprises a lithium metal phosphate particle, and a carbon coating formed on at least a portion of a surface of the lithium metal phosphate particle. A standard deviation of thickness values of the carbon coating measured by an X-ray photoelectron spectroscopy (XPS) for five different composite particles of the plurality of composite particles is 15 nm or less.
H01M 4/58 - Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFySelection of substances as active materials, active masses, active liquids of polyanionic structures, e.g. phosphates, silicates or borates
H01M 4/62 - Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
Ammonia synthesis system including an ammonia synthesis reactor; two or more catalyst beds included in the ammonia synthesis reactor; one or more backflow prevention plates disposed, downstream from each of the catalyst beds except not below a lowest catalyst bed of the two or more catalyst beds, and preventing a gas backflow; distribution devices disposed upstream from each of the two or more catalyst beds and distributing gas to the catalyst bed;
Ammonia synthesis system including an ammonia synthesis reactor; two or more catalyst beds included in the ammonia synthesis reactor; one or more backflow prevention plates disposed, downstream from each of the catalyst beds except not below a lowest catalyst bed of the two or more catalyst beds, and preventing a gas backflow; distribution devices disposed upstream from each of the two or more catalyst beds and distributing gas to the catalyst bed;
hydrogen gas supply lines arranged to supply hydrogen gas to each of the distribution devices; and at least one microwave heating device for emitting microwaves to each of the two or more catalyst beds, and further including a nitrogen gas supply line disposed to supply nitrogen gas to a top-most distribution device of the distribution devices.
A composite laminate according to embodiments of the present disclosure includes a unidirectional tape layer including a thermoplastic resin and continuous fibers, and a first metal layer formed on the unidirectional tape layer. A content of the continuous fibers is 40 wt % or more based on the total weight of the unidirectional tape layer. The flame resistance and lightness of the composite laminate may be improved.
B32B 15/085 - Layered products essentially comprising metal comprising metal as the main or only constituent of a layer, next to another layer of a specific substance of synthetic resin comprising polyolefins
B32B 5/08 - Layered products characterised by the non-homogeneity or physical structure of a layer characterised by structural features of a layer comprising fibres or filaments the fibres or filaments of a layer being specially arranged or being of different substances
B32B 15/14 - Layered products essentially comprising metal next to a fibrous or filamentary layer
B32B 15/18 - Layered products essentially comprising metal comprising iron or steel
B32B 15/20 - Layered products essentially comprising metal comprising aluminium or copper
In a method of producing an ethylene-based copolymer according to the embodiments of the present disclosure, a monomer solution including a comonomer and monomethyl ether hydroquinone is discharged into a reactor through a first discharge unit. An ethylene monomer reacts with the comonomer by injecting the ethylene monomer into the reactor. A content of the monomethyl ether hydroquinone in the monomer solution is adjusted to be 210 ppm or more based on a total weight of the comonomer.
A poly(lactic-co-glycolic acid)-containing resin composition according to exemplary embodiments may include a poly(lactic-co-glycolic acid) (PLGA) polymer, a zinc-containing ionomer (Zn ionomer) and an ethylene terpolymer. The PLGA polymer may be 65 wt % or more and less than 100 wt % based on a total weight of the poly(lactic-co-glycolic acid)-containing resin composition.
The present invention relates to a method and a system for producing aviation fuel. This method comprises the steps of: preparing FT synthetic oil as a feed; introducing the feed into a first distillation column for separating the feed into a plurality of fractions including an aviation fuel boiling point range fraction and an aviation fuel boiling point range exceeding fraction; introducing the aviation fuel boiling point range exceeding fraction into an HCK reactor to produce an HCK reaction product; recycling at least a portion of the HCK reaction product into the first distillation column; introducing the aviation fuel boiling point range fraction into an HDI reactor to produce an HDI reaction product; and recovering aviation fuel from the HDI reaction product.
C10G 65/10 - Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
C10G 45/58 - Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour pointSelective hydrocracking of normal paraffins
A lubricant composition for preparing an ethylene copolymer according to embodiments of the present disclosure includes a base oil including a white mineral oil, and an oxidation stabilizer represented by Formula 1. The oxidation stabilizer may have a solubility of 0.1 g/100 g or more in the white mineral oil at 25° C.
Provided are an ammonia synthesis system and its operation method, the system including an ammonia synthesis reactor; two or more catalyst beds included in the ammonia synthesis reactor; a backflow prevention plate disposed downstream from each of the catalyst beds except for the catalyst bed disposed at the lowest of the two or more catalyst beds for preventing a backflow of mixed gas; a distribution device disposed upstream from each of the two or more catalyst beds for distributing the mixed gas to the catalyst bed; mixed gas supply lines arranged to supply the mixed gas to each distribution device; and a mixed gas heat exchanger for supplying heat to the mixed gas by heat-exchanging the mixed gas fed through the mixed gas supply line with a heat storage medium.
An electrode manufacturing system is disclosed. In some implementations, the electrode manufacturing system may include a coating station configured to coat a coating material on a coating substrate traveling along a path, and a drying station configured to dry the coating material. The drying station may include at least one linear infrared lamp configured to irradiate the coating material with infrared light, and opposite ends of the infrared lamp may be disposed to be vertically aligned with opposite edges of the coating material.
F26B 3/30 - Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements
F26B 3/04 - Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour circulating over, or surrounding, the materials or objects to be dried
F26B 13/00 - Machines or apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
Provided is a refining apparatus of a waste plastic pyrolysis oil including a reactor where a waste plastic pyrolysis oil is introduced and hydrotreated, wherein the reactor includes Area 1 including a hydrotreating catalyst having a Mo content of 1 to 15 wt % with respect to the total weight; and Area 2 including a hydrotreating catalyst having a Mo content of 5 to 40 wt % and a Ni or Co content of 4 to 50 wt % with respect to the total weight, and the waste plastic pyrolysis oil is refined by passing through Area 1 and Area 2 sequentially.
C10G 49/04 - Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups , , , , or characterised by the catalyst used containing nickel, cobalt, chromium, molybdenum, or tungsten metals, or compounds thereof
B01J 8/04 - 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 the fluid passing successively through two or more beds
An aqueous dispersion composition according to embodiments of the present disclosure includes a first ethylene-based copolymer having a melting temperature of 84° C. or higher and a second ethylene-based copolymer having a melting temperature of less than 80° C., wherein a content of the second ethylene-based copolymer is 70 wt % to 90 wt % based on a total weight of the first ethylene-based copolymer and the second ethylene-based copolymer, and a total content of the first ethylene-based copolymer and the second ethylene-based copolymer is 50 wt % or more based on a total solid content weight of the aqueous dispersion composition.
C08L 23/0869 - Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen with unsaturated acids, e.g. [meth]acrylic acidCopolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen with unsaturated esters, e.g. [meth]acrylic acid esters
Disclosed is a method for producing hydrocarbons, the method comprising the steps of: S1) thermally decomposing a mixed waste to produce a first mixed gas; S2) steam-reforming the first mixed gas, removed of impurities, in a first fluidized bed reactor to produce a second mixed gas; S3) separating the second mixed gas into a first stream containing carbon dioxide and a second stream containing hydrogen and carbon monoxide; S4) introducing the first stream, separated in step S3), into a second fluidized bed reactor and converting the first stream into carbon monoxide through a reverse Boudouard reaction; S5) mixing the second stream and the carbon monoxide, converted in step S4), to produce a third mixed gas, and producing a synthesis gas (Syngas) through a water-gas conversion reaction using the third mixed gas; and S6) producing hydrocarbons from the synthetic gas through a catalytic reaction.
C01B 3/38 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
C01B 3/48 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
C07C 1/20 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as hetero atoms
C07C 29/151 - Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
The present disclosure provides a method for preparing hydrocarbons, comprising the steps of: (S1) heat treating organic waste so as to generate a first mixed gas; (S2) dry reforming the first mixed gas in a first fluidized bed reactor so as to generate a second mixed gas; (S3) separating the second mixed gas into a first stream that comprises carbon dioxide and a second stream that comprises hydrogen and carbon monoxide; (S4) introducing the first stream, which was separated out in step (S3), to a second fluidized bed reactor and converting same into carbon monoxide through a reverse Boudouard reaction; (S5) mixing the second stream and the carbon monoxide, which was converted in step (S4), so as to prepare a third mixed gas; (S6) generating syngas from the third mixed gas through a water-gas shift reaction; and (S7) preparing hydrocarbons from the syngas through a catalytic reaction.
C01B 3/38 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
C01B 3/48 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
C07C 1/20 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as hetero atoms
C07C 29/151 - Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
An anode active material for a lithium secondary battery includes a silicon-based active material particle doped with a metal element and including pores. A porosity of the silicon-based active material particle is in a range from 0.4% to 3.5%. A lithium secondary battery includes the anode and a cathode facing the anode.
A ammonia synthesis system, an operation method thereof, and an ammonia synthesis method are provided. The system includes a compressor for compressing mixed gas; a feed supply line for supplying the mixed gas to the compressor; an ammonia synthesis reactor for synthesizing ammonia by feeding the mixed gas compressed by the compressor into the reactor; an ammonia separation device for separating syngas produced by the ammonia synthesis reactor into ammonia and a regeneration stream; a feed recirculation line for recirculating the regeneration stream to the feed supply line; and a buffer tank installed in the feed recirculation line.
An ammonia synthesis system, an operation method thereof, and an ammonia synthesis method are provided. The system includes a compressor for compressing mixed gas; a feed supply line for supplying the mixed gas to the compressor; an ammonia synthesis reactor for synthesizing ammonia by feeding the mixed gas compressed by the compressor into the reactor; an air separation unit for separating nitrogen from air; a first cooler for cooling syngas including ammonia discharged from the ammonia synthesis reactor; and a second cooler for heat-exchanging gaseous nitrogen separated by the air separation unit with the syngas cooled by the first cooler, wherein gaseous nitrogen heat-exchanged by the second cooler is supplied to the feed supply line.
An ammonia synthesis system, an operation method thereof, and an ammonia synthesis method are provided. The system includes a compressor for compressing mixed gas; a feed supply line for supplying the mixed gas to the compressor; an ammonia synthesis reactor for synthesizing ammonia by feeding the mixed gas compressed by the compressor into the reactor; a first ammonia separation device for separating syngas produced by the ammonia synthesis reactor into a sweep gas including nitrogen and hydrogen and into an ammonia rich gas; a second ammonia separation device for separating the ammonia rich gas into the ammonia and a regeneration stream including the nitrogen and the hydrogen; a feed recirculation line for recirculating the regeneration stream to the feed supply line; and a sweep gas recirculation line for recirculating the sweep gas to the ammonia synthesis reactor.
Proposed is a pump failure prediction apparatus which includes at least one processor, a storage, which is communicably connected with the processor and stores a program code which operates in the processor, and a communicator, which is communicably connected with the processor, wherein the program code includes a data collection module, and an abnormality detection module which detects three abnormalities. The first abnormality appears before failure occurrence by inputting the real-time data into a first model which has performed supervised learning of history data. The second abnormality appears outside of a normal operation range of the pump by inputting the real-time data to a second, which has performed unsupervised learning of normal operation data. The third abnormality appears outside an initial normal operation range of the pump by inputting the real-time data to a third model, which has performed unsupervised learning of initial operation data.
The embodiments of this disclosure are related to a water treatment system comprising a flotation tank, a shell-tube inlet conduit connected to the flotation tank and comprising a shell configured to supply a gas and at least one tube configured to supply untreated water, wherein each of the shell and the tube has a first part exposed to an outside of the flotation tank and a second part extending into the flotation tank, a microbubble forming means positioned on or adjacent to the second part of the shell, and a treated water outlet connected to the flotation tank and configured to allow treated water separated from solids in the flotation tank to be discharged therethrough.
A cathode active material for a lithium secondary battery has a structure of a lithium transition metal oxide. A ratio of a crystallite size of a (003) plane to a crystallite size of a (110) plane measured by an X-ray diffraction (XRD) analysis is in a range from 0.7 to 2.0, and a ratio of the crystallite size of the (003) plane to a crystallite size of a (104) plane measured by the XRD analysis is in a range from 0.7 to 2.0. A cathode for a lithium secondary battery and a lithium secondary battery include the cathode active material for a lithium secondary battery.
H01M 4/525 - Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
C01G 53/50 - Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2 containing manganese of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2
C01G 53/504 - Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2 containing manganese of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2 containing lithium and cobalt with the molar ratio of nickel with respect to all the metals other than alkali metals higher than or equal to 0.5, e.g. Li(MzNixCoyMn1-x-y-z)O2 with x ≥ 0.5
C01G 53/506 - Complex oxides containing nickel and at least one other metal element containing alkali metals, e.g. LiNiO2 containing manganese of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2 containing lithium and cobalt with the molar ratio of nickel with respect to all the metals other than alkali metals higher than or equal to 0.5, e.g. Li(MzNixCoyMn1-x-y-z)O2 with x ≥ 0.5 with the molar ratio of nickel with respect to all the metals other than alkali metals higher than or equal to 0.8, e.g. Li(MzNixCoyMn1-x-y-z)O2 with x ≥ 0.8
H01M 4/02 - Electrodes composed of, or comprising, active material
H01M 4/131 - Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
H01M 10/0525 - Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodesLithium-ion batteries
68.
ANODE FOR LITHIUM SECONDARY BATTERY AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
An anode for a lithium secondary battery according to embodiments of the present disclosure includes an anode current collector, a first anode active material layer formed on at least one surface of the anode current collector and including first pores, a second anode active material layer formed on the first anode active material layer and including artificial graphite and second pores, wherein a difference between the first pore aspect ratio and the second pore aspect ratio is 0.5 to 3.0.
A method and a system for recycling a metal from a lithium secondary battery are provided. In the method for recycling a metal from a lithium secondary battery, a cathode active material mixture containing lithium is prepared. A lithium precursor is produced by reducing the cathode active material mixture. A lithium precursor aqueous solution is formed by dissolving the lithium precursor in water. The lithium precursor aqueous solution is passed through an aluminum adsorption resin column to adsorb aluminum to the aluminum adsorption resin column. A first treatment liquid including distilled water is injected into the aluminum adsorption resin column at a flow rate of 100 L/hr to 1,200 L/hr to obtain a regenerated aluminum adsorption resin column from which aluminum is desorbed.
C22B 3/24 - Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means by adsorption on solid substances, e.g. by extraction with solid resins
A polyolefin microporous membrane, a method for manufacturing the same, and a separator including the microporous membrane are provided. The polyolefin microporous membrane including 60 wt % to 80 wt % of a polypropylene having a viscosity average molecular weight of 1×106 g/mol to 3×106 g/mol and 20 wt % to 40 wt % of a polyethylene having a weight average molecular weight of 1×105 g/mol to 10×105 g/mol is provided, wherein the polyolefin microporous membrane has a puncture strength of 0.25 N/μm or more, a gas permeability of 1.0×10−5 Darcy or more, a porosity of 30% to 70%, an average pore size of 20 nm to 40 nm, a shutdown temperature of 150° C. or lower, and a meltdown temperature of 180° C. or higher.
H01M 50/489 - Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
B29C 48/00 - Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired formApparatus therefor
B29C 48/08 - Flat, e.g. panels flexible, e.g. films
A negative electrode for a lithium secondary battery, according to embodiments of the present disclosure, comprises: a negative electrode current collector; a first negative electrode active material layer formed on at least one surface of the negative electrode current collector; and a second negative electrode active material layer which is formed on the first negative electrode active material layer and includes artificial graphite, wherein the first Raman peak area ratio of the first negative electrode active material layer is 1 to 2 and the second Raman peak area ratio of the second negative electrode active material layer is 0.2 to 0.5.
Embodiments of the present disclosure provide a system, apparatus, and method for providing a recycling service for a plastic using a blockchain. The system includes a first electronic device of a collection company for collecting recycled materials from waste products; a second electronic device of a recycling company for compounding the recycled material with at least one additive to prepare a composite material; and a third electronic device of a production company for producing a product using the composite material.
Proposed is a method of analyzing microplastic particles in a water system. The method includes providing raw water containing microplastic particles, freezing and thawing the raw water at least once to generate microplastic aggregates in the raw water, recovering the microplastic aggregates, and analyzing the recovered microplastic aggregates. According to the method, the microplastic particles are precipitated in the water system without the use of an additional coagulant, whereby the effect of coagulants on the subsequently recovered microplastic aggregates may be ruled out. In addition, the process configuration is simple because the aggregates can be separated from the supernatant without using any additional treatment process.
A method for manufacturing carbon nanotubes according to embodiments of the present disclosure includes injecting a carbon source, a metal catalyst, a cocatalyst and a transport gas into a reactor, and heating the reactor to manufacture carbon nanotubes. A ratio of a molar flow rate of the carbon source to a molar flow rate of the metal catalyst is 350 to 1,300.
According to one embodiment, a method and an apparatus for verifying the quantity of scaffolding materials by using augmented reality can be provided, the method comprising: a mode selection step of selecting a virtual scaffold installation mode or an on-site scaffold measurement mode; a scaffold input step of inputting a scaffold structure by using the virtual scaffold installation mode or the on-site scaffold measurement mode; and a quantity calculation step of calculating a quantity of materials required for the scaffold structure.
G06T 19/00 - Manipulating 3D models or images for computer graphics
G06V 10/40 - Extraction of image or video features
G06F 30/13 - Architectural design, e.g. computer-aided architectural design [CAAD] related to design of buildings, bridges, landscapes, production plants or roads
G06F 111/18 - Details relating to CAD techniques using virtual or augmented reality
A lithium secondary battery includes a cathode including a cathode active material, the cathode active material including a lithium metal oxide that has a form of a secondary particle in which a plurality of primary particles are aggregated and is doped with a doping element, and an anode facing the cathode and including an anode active material, the anode active material including a composite active material of a silicon-containing material and a first carbon-based material, and a second carbon-based active material. An aspect ratio of the primary particles is in a range from 1.4 to 7.0, and a content of the composite active material based on a total weight of the anode active material is in a range from 1 wt % to 50 wt %.
H01M 4/62 - Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
H01M 4/02 - Electrodes composed of, or comprising, active material
H01M 4/36 - Selection of substances as active materials, active masses, active liquids
H01M 4/38 - Selection of substances as active materials, active masses, active liquids of elements or alloys
H01M 4/525 - Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
H01M 4/587 - Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
Provided is an ammonia synthesis system including an ammonia synthesis reactor; two or more catalyst beds included in the ammonia synthesis reactor; a backflow prevention plate disposed downstream from each of the catalyst beds except for the catalyst bed disposed at the lowest of the two or more catalyst beds for preventing a backflow of mixed gas; a distribution device disposed upstream from each of the two or more catalyst beds for distributing the mixed gas to the catalyst bed; mixed gas supply lines arranged to supply the mixed gas to each distribution device; and a microwave heating device for emitting microwaves to each of the two or more catalyst beds, wherein the catalyst bed contains a microwave reactive catalyst mixture including a catalyst and a carbon body.
B01J 8/04 - 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 the fluid passing successively through two or more beds
Provided is an ammonia synthesis system including an ammonia synthesis reactor; two or more catalyst beds included in the ammonia synthesis reactor; a backflow prevention plate disposed downstream from each of the catalyst beds except for the catalyst bed disposed at the lowest of the two or more catalyst beds and preventing a backflow of mixed gas; a distribution device disposed upstream from each of the two or more catalyst beds and distributing the mixed gas to the catalyst bed; mixed gas supply lines arranged to supply the mixed gas to each distribution device; and a microwave heating device for emitting microwaves to each of the two or more catalyst beds, wherein the catalyst bed includes a metal nitride catalyst.
B01J 8/04 - 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 the fluid passing successively through two or more beds
79.
COMPOSITE SEPARATOR AND SECONDARY BATTERY USING THE SAME
A composite separator including an adhesive layer and a secondary battery including the same. In the composite separator, the adhesive layer contains a particulate organic binder having a glass transition temperature of 60 to 80° C., and when the adhesive layers are brought into contact with each other, pressurized at a temperature of 50° C. and a pressure of 1.7 MPa for 2 hours, and then peeled at a speed of 300 mm/min and an angle of 180°, blocking does not occur between the adhesive layers, and an adhesive strength to a positive electrode is 5 gf/cm or more.
The present invention relates to a curtain-type fire response system for an electric vehicle and, more specifically, to a curtain-type fire response system for an electric vehicle, the system comprising: a fire checking unit for checking if a fire is occurring or predicted in an electric vehicle parked in a parking space; fire response curtain units installed above the parking space and configured to, when in operation, lower flame retardant curtains such that at least one portion of at least one side of the parking space is open and at least one of the other sides is blocked; and a fire response control unit which, when a fire is detected or predicted in the electric vehicle parked in the parking space by the fire checking unit, operates the fire response curtain units to prevent the spread of the fire ignited from the electric vehicle.
E04H 6/42 - Devices or arrangements peculiar to garages, not covered elsewhere, e.g. securing devices, safety devices
G08B 17/12 - Actuation by presence of radiation or particles, e.g. of infrared radiation or of ions
G08B 3/10 - Audible signalling systemsAudible personal calling systems using electric transmissionAudible signalling systemsAudible personal calling systems using electromagnetic transmission
G08B 25/14 - Central alarm receiver or annunciator arrangements
The present disclosure provides a method for producing hydrocarbon, comprising the steps of: (S1) generating a first mixed gas by heat-treating organic waste; (S2) generating a second mixed gas by steam-reforming the first mixed gas in a first fixed-bed reactor; (S3) separating the second mixed gas into a first stream including carbon dioxide and a second stream including hydrogen and carbon monoxide; (S4) introducing the first stream obtained by separation in step (S3) into a second fixed-bed reactor and converting the first stream into carbon monoxide through a reverse Boudouard reaction; (S5) producing a third mixed gas by mixing the second stream and the carbon monoxide obtained by conversion in step (S4); (S6) generating a synthetic gas from the third mixed gas through a water gas conversion reaction; and (S7) producing hydrocarbon from the synthetic gas through a catalytic reaction.
C01B 3/38 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
C01B 3/48 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
C07C 1/20 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as hetero atoms
C07C 29/151 - Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
The present disclosure relates to a method for producing light olefins and, more particularly, to a method for producing light olefins which can increase the production yield of light olefins and minimize the generation of carbon dioxide. The method for producing light olefins according to the present disclosure comprises the steps of: S1) pyrolyzing waste plastics to produce pyrolysis oil and pyrolysis gas; S2) separating the pyrolysis oil and pyrolysis gas; S3) producing a first gas from which impurities are removed by purifying the separated pyrolysis gas; S4) steam-reforming the first gas to manufacture a second gas; S5) producing a first synthesis gas from the second gas; S6) producing a second synthesis gas by converting carbon monoxide in the synthesis gas into hydrogen and carbon dioxide through a water gas shift reaction; S7) preparing a first mixed solution containing methanol by converting the second synthesis gas into methanol through a hydrogenation reaction; and (S8) preparing a second mixed solution containing light olefins through an olefin conversion reaction of methanol contained in the first mixed solution, and recovering the light olefins from the second mixed solution.
C07C 1/20 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as hetero atoms
C07C 29/151 - Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
C01B 3/40 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts characterised by the catalyst
C01B 3/48 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
C10J 3/84 - Gas withdrawal means with means for removing dust or tar from the gas
C10G 1/10 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
The present disclosure provides a method for producing hydrocarbon, comprising the steps of: (S1) generating a first mixed gas by heat-treating organic waste; (S2) generating a second mixed gas by dry-reforming the first mixed gas in a first fixed-bed reactor; (S3) separating the second mixed gas into a first stream including carbon dioxide and a second stream including hydrogen and carbon monoxide; (S4) introducing the first stream obtained by separation in step (S3) into a second fixed-bed reactor and converting the first stream into carbon monoxide through a reverse Boudouard reaction; (S5) producing a third mixed gas by mixing the second stream and the carbon monoxide obtained by conversion in step (S4); (S6) generating a synthetic gas from the third mixed gas through a water gas conversion reaction; and (S7) producing hydrocarbon from the synthetic gas through a catalytic reaction.
C01B 3/38 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
C01B 3/48 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
C07C 1/20 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as hetero atoms
C07C 29/151 - Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
A method for recovering active metals of a lithium secondary battery may supply a cathode active material mixture to a fluidized bed reactor including a reactor body. A reaction gas may be introduced from a lower portion of the fluidized bed reactor to form a fluidized bed including a preliminary precursor mixture within the reactor body. The fluidized bed portion that has entered the upper portion of the fluidized bed reactor may be cooled to descend it into the reactor body, and then a lithium precursor may be recovered from the preliminary precursor mixture. Accordingly, a terminal velocity of the preliminary precursor is reduced, such that even if the particle size of the preliminary precursor is fine, loss due to scattering may be prevented.
C22B 5/14 - Dry processes by gases fluidised material
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
A cathode for a lithium secondary battery and a lithium secondary battery including the same are provided. The cathode includes a cathode active material layer including a cathode active material and a conductive material, and having a Raman R1 value represented by A1D/A1G and measured on a surface of the cathode active material layer in a range from 1.5 and 4.
H01M 4/525 - Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
Embodiments of the present disclosure relate to a separator having pore diameters D10, D50, and D90 satisfies all of 180 nm≤D10≤350 nm, 380 nm≤D50≤650 nm, and 670 nm≤D90≤1000 nm. The separator according to an embodiment has improved heat resistance by satisfying the predetermined pore diameter ranges, and a battery comprising the separator may have improved performance.
Provided are a separator having significantly improved withstand voltage characteristics and a lithium secondary battery including the same. The separator includes a porous substrate and an inorganic particle layer including a binder and inorganic particles formed on at least one surface of the porous substrate, wherein the separator has a ratio of a breakdown voltage (kV) of the separator to an overall average thickness (μm) of the separator of 0.15 kV/μm or more, has a peak in a range of 1070 cm−1 to 1082 cm−1 in a spectrum by Fourier transform infrared spectroscopy (FT-IR), has heat shrinkage rates in the machine direction and in the transverse direction of 5% or less as measured after being allowed to stand at 150° C. for 60 minutes, and has ΔGurley permeability of 100 sec/100 cc or less.
H01M 50/489 - Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
H01M 10/0525 - Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodesLithium-ion batteries
H01M 50/414 - Synthetic resins, e.g. .thermoplastics or thermosetting resins
H01M 50/451 - Separators, membranes or diaphragms characterised by the material having a layered structure comprising layers of only organic material and layers containing inorganic material
88.
WATER-TANK-TYPE FIRE RESPONSE SYSTEM FOR ELECTRIC VEHICLE
The present invention relates to a water-tank-type fire response system for an electric vehicle and, more specifically, to a water-tank-type fire response system for an electric vehicle, the system comprising: a fire checking unit for checking if a fire is occurring or predicted in an electric vehicle parked in a parking space; a fire response water tank unit installed to be placed on the ground along the edges of the parking space and configured to, when in operation, be elevated by a predetermined height from the bottom of the parking space so as to surround the electric vehicle parked in the parking space, and supply and store firewater therein; and a fire response control unit for operating the fire response water tank unit to flood the battery of the electric vehicle when a fire is detected or predicted in the electric vehicle parked in the parking space by the fire checking unit.
E04H 6/42 - Devices or arrangements peculiar to garages, not covered elsewhere, e.g. securing devices, safety devices
G08B 3/10 - Audible signalling systemsAudible personal calling systems using electric transmissionAudible signalling systemsAudible personal calling systems using electromagnetic transmission
G08B 25/14 - Central alarm receiver or annunciator arrangements
A62C 99/00 - Subject matter not provided for in other groups of this subclass
G09F 19/22 - Advertising or display means on roads, walls or similar surfaces, e.g. illuminated
89.
COVER-TYPE FIRE RESPONSE SYSTEM FOR ELECTRIC VEHICLE
The present invention relates to a cover-type fire response system for an electric vehicle and, more specifically, to a cover-type fire response system for an electric vehicle, the system comprising: a fire checking unit for checking if a fire is occurring or predicted in an electric vehicle parked in a parking space; a fire response cover unit installed on one side of the parking space and configured to, when in operation, be deployed along the parking space so as to surround the electric vehicle parked in the parking space; and a fire response control unit which, when a fire is detected or predicted in the electric vehicle parked in the parking space by the fire checking unit, operates the fire response cover unit to prevent the spread of the fire ignited from the electric vehicle.
A62C 3/07 - Fire prevention, containment or extinguishing specially adapted for particular objects or places in vehicles, e.g. in road vehicles
A62C 3/16 - Fire prevention, containment or extinguishing specially adapted for particular objects or places in electrical installations, e.g. cableways
G08B 25/10 - Alarm systems in which the location of the alarm condition is signalled to a central station, e.g. fire or police telegraphic systems characterised by the transmission medium using wireless transmission systems
G08B 17/00 - Fire alarmsAlarms responsive to explosion
A62C 99/00 - Subject matter not provided for in other groups of this subclass
90.
AVIATION FUEL COMPOSITION AND METHOD FOR PRODUCING SAME
The present disclosure provides a method for producing an aviation fuel composition, and also provides an aviation fuel produced by the method, the method for producing an aviation fuel composition comprising the steps of: (a) introducing a feed into a fluid catalytic cracking (FCC) reaction to produce an FCC reaction product; (b) separating the FCC reaction product into a plurality of fractions including a first fraction and a second fraction, wherein the first fraction is a fraction having a boiling point of 70°C or less, and the second fraction is a fraction having a boiling point of more than 150°C; (c) converting the first fraction into a first oil, wherein the first oil has a boiling point of more than 150°C; (d) hydrotreating the second fraction to produce a second oil; and (e) blending the first oil and the second oil in a predetermined ratio.
C10G 69/04 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of catalytic cracking in the absence of hydrogen
C10G 69/12 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
C10G 57/00 - Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process
C10G 45/58 - Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour pointSelective hydrocracking of normal paraffins
C01B 3/34 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
C10L 1/04 - Liquid carbonaceous fuels essentially based on blends of hydrocarbons
The present disclosure provides a method for producing hydrocarbons, comprising steps of: (S1) heat-treating organic waste in a pyrolysis reactor to generate a first mixed gas; (S2) methane reforming the first mixed gas in a reforming reactor to generate a second mixed gas; (S3) separating the second mixed gas into a first stream containing carbon dioxide and a second stream containing hydrogen and carbon monoxide; (S4) injecting the first stream and carbon into a reverse Boudouard reactor and converting same into carbon monoxide through a reverse Boudouard reaction; (S5) generating a third mixed gas by mixing the second stream and the carbon monoxide converted in step (S4); (S6) producing synthesis gas from the third mixed gas through a water gas shift reaction; and (S7) producing hydrocarbons from the synthesis gas through a catalytic reaction, wherein the reforming reactor in step (S2) includes a fluidized bed reforming reactor and a fixed bed reforming reactor connected in parallel, and the first mixed gas is switched and supplied to the fluidized bed reforming reactor or the fixed bed reforming reactor.
C01B 3/24 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
C01B 3/30 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using moving solid particles using the fluidised bed technique
C01B 3/26 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using catalysts
92.
ELECTROLYTE FOR LITHIUM SECONDARY BATTERY AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
An electrolyte for a lithium secondary battery including an organic solvent, a lithium salt, and a phosphate-based additive including a compound represented by Formula 1. A lithium secondary battery according to embodiments of the present disclosure may include a cathode, an anode opposite to the cathode, and an electrolyte including the phosphate-based additive represented by Formula 1.
H01M 10/0567 - Liquid materials characterised by the additives
C07F 9/06 - Phosphorus compounds without P—C bonds
H01M 4/02 - Electrodes composed of, or comprising, active material
H01M 4/58 - Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFySelection of substances as active materials, active masses, active liquids of polyanionic structures, e.g. phosphates, silicates or borates
H01M 10/0525 - Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodesLithium-ion batteries
H01M 10/0568 - Liquid materials characterised by the solutes
H01M 10/0569 - Liquid materials characterised by the solvents
93.
METHOD AND DEVICE FOR PRODUCING WASTE PLASTIC PYROLYSIS OIL WITH REDUCED CHLORINE
Embodiments of the present disclosure provide a method for producing waste plastic pyrolysis oil with reduced chlorine, the method including a first operation of charging a waste plastic feedstock and modified red mud into a reactor, and a second operation of pyrolyzing the waste plastic feedstock in the reactor and recovering pyrolysis oil, wherein when the modified red mud is subjected to X-ray diffraction (XRD) analysis, an intensity of a first peak at a 2θ diffraction angle of 14±0.1° is higher than an intensity of a second peak at a 2θ diffraction angle of 14.5±0.1°.
C10B 57/06 - Other carbonising or coking processesFeatures of destructive distillation processes in general using charges of special composition containing additives
C10B 53/02 - Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
C10B 53/07 - Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of synthetic polymeric materials, e.g. tyres
C10G 1/02 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
94.
SILICON-CARBON-CONTAINING ELECTRODE MATERIAL AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
A silicon-carbon-containing electrode material including a porous carbon structure and a silicon-containing coating layer formed on the porous carbon structure. A volume ratio of micropores in the porous carbon structure having a pore diameter of 2 nm or less in a total pore volume is greater than 50% and less than 90%. A lithium secondary battery comprising the anode which comprises the silicon-carbon-containing electrode material and a cathode disposed to face to the anode. The lithium secondary battery employing the silicon-containing electrode exhibits improved lifespan and efficiency characteristics.
Provided are a separator having significantly improved heat resistance and a lithium secondary battery including the same. According to an aspect of the present disclosure, a separator including: a porous substrate; and an inorganic particle layer which is formed on at least one surface of the porous substrate and includes a binder and inorganic particles, wherein the separator has a ratio of a total thickness of the inorganic particle layer to a thickness of the porous substrate of 0.2 to 0.6, has a peak shown in a range of 1070 cm−1 to 1082 cm−1 in a spectrum by Fourier transform infrared spectroscopy (FT-IR), and has heat shrinkage rates in the machine direction and in the transverse direction of 5% or less as measured after being allowed to stand at 150° C. for 60 minutes is provided.
A separator for a secondary battery and a secondary battery comprising the same. The separator comprises a porous substrate, and an inorganic particle layer which is formed on at least one surface of the porous substrate and comprises a binder and inorganic particles. The separator has a first peak shown in a range of 3800 to 3400 cm−1 and a second peak shown in a range of 1800 to 1500 cm−1 in a spectrum by Fourier-transform infrared spectroscopy (FT-IR) measured after performing 600 cycles of charge and discharge.
A system for reducing waste by recovering a lithium precursor, the system comprising: a first mixer for mixing a waste lithium secondary battery positive electrode material with urea to prepare a first mixture; an oven for firing the first mixture to prepare a second mixture containing lithium hydroxide; and a second mixer for subjecting the second mixture to water washing to separate a lithium precursor.
Embodiments of the present disclosure provide a method for producing waste plastic pyrolysis oil with reduced chlorine, the method including a first operation of charging a waste plastic raw material and an accelerator containing char into a reactor; a second operation of pyrolyzing the waste plastic raw material in the reactor and recovering pyrolysis oil; and a third operation of recovering the accelerator from the reactor.
C10G 1/10 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
C10G 1/00 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
Provided is an ammonia synthesis system including an ammonia synthesis reactor; two or more catalyst beds; a distribution plate; a backflow prevention plate; a distribution device; and mixed gas supply lines, wherein the distribution plate has a plurality of openings formed independently of each other, and a percentage of a total region of the openings to a total region of each distribution plate is referred to as an opening ratio, wherein the opening ratio of the distribution plate is decreased toward a lower part.
Provided are a mixed gas distribution system and an ammonia synthesis system comprising the mixed gas distribution system, the mixed gas distribution system comprising a gas distribution device; a mixed gas supply line connected to the gas distribution device; a flow induction guide; an upper area; and a plurality of mixed gas flow pipes fixed to a circumference part of a bottom surface of the upper area, and connected to a plurality of openings formed in the circumference part of the bottom surface to enable a movement of mixed gas.
