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
6.
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
7.
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
8.
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
15.
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
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 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.
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.
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.
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.
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
38.
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.
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.
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.
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
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
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
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
55.
CATHODE FOR LITHIUM SECONDARY BATTERY, METHOD OF FABRICATING THE SAME AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
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
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
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
58.
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
59.
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
61.
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
62.
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.
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
64.
SEPARATOR AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
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.
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.
An anode active material for a lithium secondary battery comprising magnesium-silicon composite oxide particles comprising MgSiO3 and silicon and having a ratio of magnesium to total magnesium, silicon, and oxygen of about 0.07 to about 0.17. A secondary lithium battery comprising the anode active material is provided having enhanced capacity and lifespan.
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 4/02 - Electrodes composed of, or comprising, active material
H01M 4/36 - Selection of substances as active materials, active masses, active liquids
H01M 4/587 - Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
A cathode for a lithium secondary battery includes lithium metal oxide particles having CM defined by D*(EIT/HIT)/[(Li/Me)2] of of 70 or more. D is an average particle diameter value calculated in micrometers after measuring diameters of particles with a diameter of 4 μm or more in the lithium metal oxide particles included in a scanning electron microscope (SEM) image showing a thickness*width cross-section of the cathode active material layer. EIT is a modulus value of the lithium metal oxide particles measured by a nano indentation method. HIT is a hardness value of the lithium metal oxide particles measured by a nano indentation method. Li/Me is a molar ratio of lithium to metals other than lithium in the lithium metal oxide particles.
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
71.
METHOD FOR REDUCING WASTE BY RECOVERING LITHIUM PRECURSOR FROM WASTE LITHIUM SECONDARY BATTERY POSITIVE ELECTRODE MATERIAL
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.
Provided is a separator having an intensity ratio of peaks corresponding to a (020) plane and a (110) plane in an X-ray diffraction (XRD) analysis graph of 2.6 to 5.7. The separator according to an embodiment has excellent stability at high temperature by satisfying the peak intensity ratio of the XRD analysis graph.
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 50/446 - Composite material consisting of a mixture of organic and inorganic materials
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
Provided is an ammonia synthesis system including an ammonia synthesis reactor; at least two catalyst beds included in the ammonia synthesis reactor; a backflow prevention plate disposed downstream from each one of the catalyst beds except for the catalyst bed disposed at the lowest of the at least two catalyst beds for preventing a backflow of mixed gas; a distribution device disposed upstream from each one of the at least two 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 at least two catalyst beds.
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
74.
GAS DISTRIBUTION SYSTEM AND AMMONIA SYNTHESIS SYSTEM USING THE SAME
Provided are a gas distribution system for an ammonia synthesis system, the gas distribution system comprising: three or more distribution plates disposed upstream from a catalyst bed disposed inside an ammonia synthesis reactor of the ammonia synthesis system; three or more distribution devices, each disposed upstream from a corresponding one of the distribution plates for distributing a mixed gas to the distribution plates; and three or more mixed gas supply lines, each arranged to supply the mixed gas to a respective one of the distribution devices, wherein the three or more distribution plates have different opening ratios.
B01J 8/02 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds
Provided is an ammonia synthesis system including an ammonia synthesis reactor; a single or two or more catalyst beds included in the ammonia synthesis reactor; a distribution device disposed upstream from each of the catalyst beds and distributing mixed gas to the catalyst bed; a mixed gas supply line disposed to supply the mixed gas to the distribution device; and each mixed gas distribution plate is disposed between the catalyst bed and the distribution device and includes a plurality of openings, wherein some openings among the plurality of openings are mounted with a cover at the bottom, and the opening mounted with the cover normally maintains the cover to be closed and to be opened under a fluid pressure.
The present disclosure provides a method for producing aviation fuel, the method including: a first step of subjecting waste plastic pyrolysis oil to an olefin migration reaction; a second step of subjecting a product obtained in the first step to an olefin branching reaction; a third step of hydrotreating a product obtained in the second step in the presence of a hydrotreating catalyst; and a fourth step of hydrocracking a product obtained in the third step in the presence of a hydrocracking catalyst.
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 69/02 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
77.
METHOD FOR PREPARING ZIEGLER-NATTA CATALYST FOR POLYMERIZATION OF LOW-DENSITY COPOLYMER
The present disclosure relates to a method for preparing a Ziegler-Natta catalyst for polymerization of a low-density copolymer, and in particular, to a method for preparing a Ziegler-Natta catalyst including preparing a magnesium chloride support using an inorganic chloride as a halogen source of the magnesium chloride support. In the method for preparing a Ziegler-Natta catalyst according to an embodiment, an inorganic chloride is used when preparing the magnesium chloride support, such that reaction conditions are mild and generation of impurities is minimized, which is preferable for large-scale preparation of catalysts.
An anode active material for a lithium secondary battery includes a composite particle. The composite particle includes a carbon-based particle including pores, and a silicon-containing coating formed on a surface of the carbon-based particle. A crystallite size of silicon included in the silicon-containing coating after a heat treatment of the composite particle at a temperature of 900° C. to 1200° C. for 6 hours to 9 hours measured by an X-ray diffraction (XRD) analysis is 10 nm or less.
An anode for a lithium secondary battery includes an anode current collector, and an anode active material layer disposed on at least one surface of the anode current collector. The anode active material layer includes an anode active material and a conductive material. An electrode peak intensity ratio obtained by a pair distribution function (PDF) analysis of the anode active material layer is in a range from 1.1 to 2.7.
A biodegradable resin composition according to of the present disclosure includes thermoplastic starch, a biodegradable polymer having a melt flow index of greater than 30 g/10 min under conditions of 190° C. and a load of 2.16 kg, and a plasticizer, wherein a content of the biodegradable polymer is 30 wt % based on a total weight of the biodegradable resin composition. The melt flow index of the biodegradable resin composition measured under conditions of 190° C. and a load of 2.16 kg is 2.5 g/10 min to 20 g/10 min. A biodegradable film and a multilayer barrier film according to embodiments of the present disclosure include a resin layer formed from the biodegradable resin composition.
B32B 9/02 - Layered products essentially comprising a particular substance not covered by groups comprising animal or vegetable substances
B32B 9/04 - Layered products essentially comprising a particular substance not covered by groups comprising such substance as the main or only constituent of a layer, next to another layer of a specific substance
81.
ANODE FOR LITHIUM SECONDARY BATTERY AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
An anode for a lithium secondary battery includes an anode current collector, a first anode active material layer disposed on at least one surface of the anode current collector and including a first anode active material, and a second anode active material layer disposed on the first anode active material layer and including a second anode active material. The first anode active material includes a graphite-based active material, and the second anode active material includes a composite particle including silicon. A diffusivity of the first anode active material layer obtained by an X-ray microscope (XRM) analysis is 3.87 or less.
A carbon nanotube production system according to the present disclosure includes a reactor configured to generate a carbon nanotube fluid in a first direction; a conveyor unit which is arranged spaced apart from the reactor in the first direction, and comprises a mesh belt configured to capture carbon nanotube structures from the carbon nanotube fluid while continuously traveling in a second direction perpendicular to the first direction; and a collection unit configured to collect carbon nanotube units from the carbon nanotube structures.
The present disclosure relates to a method for preparing a porous catalyst for the production of a pyrolytically synthesized gas, the method comprising the steps of: mixing a metal precursor including a Group VIIIA element, a ceramic support, and a solvent to prepare a mixed solution; adding an acid to the mixed solution to prepare a precursor gel; mixing the precursor gel with clay to prepare a mixture; adding an inorganic binder to the mixture to prepare a composite catalyst sol; and drying and calcining the composite catalyst sol.
An anode active material for a lithium secondary battery includes a composite particle. The composite particle includes a carbon-based particle including pores, and a silicon-containing coating formed on a surface of the carbon-based particle. A particle peak distance of the composite particle measured by a pair distribution function (PDF) analysis is 0.6 Å or less.
An anode for a lithium secondary battery includes an anode current collector, a first anode active material layer disposed on at least one surface of the anode current collector and including a first anode active material, and a second anode active material layer disposed on the first anode active material layer and including a second anode active material. The first anode active material includes a graphite-based active material, and the second anode active material includes a composite particle including silicon. A tortuosity of the second anode active material layer obtained by an X-ray microscope (XRM) analysis is 2.32 or less.
A mordenite zeolite having excellent particle uniformity and a method for preparing the same are provided. The method includes dissolving a pH-adjusting material and a silica precursor in water to provide a basic silica suspension; dissolving a structure-directing agent and an alumina precursor in water to provide an aqueous solution; dissolving a surfactant in water to provide an aqueous solution; mixing and stirring the basic silica suspension and an alumina aqueous solution to prepare a silica-alumina aqueous solution; adding an surfactant aqueous solution to the silica-alumina aqueous solution to prepare a zeolite synthesis composition; gelating the zeolite synthesis composition; and crystallizing.
Separator for a secondary battery and secondary battery comprising the separator. The separator comprises a porous substrate, and an inorganic particle layer on at least one surface of the porous substrate, wherein the inorganic particle layer has a surface roughness (Ra) of 180 nm to 230 nm. The separator improves heat resistance, charge/discharge characteristics, and life characteristics of the secondary battery.
Embodiments of the present disclosure relate to a separator comprising a porous substrate, and an inorganic particle layer comprising inorganic particles on at least one surface of the porous substrate, wherein the inorganic particle layer has a surface roughness (Ra) of 100 nm to 160 nm. The separator according to the embodiments may improve heat resistance, charge/discharge characteristics, and life characteristics of a battery, by having the above surface roughness.
A separator and a secondary battery including the separator, the separator including a porous substrate and an adhesive layer disposed on at least one surface of the porous substrate. The adhesive layer includes a binder and anisotropic particles. The adhesive layer includes 1.2 parts by weight or more of the anisotropic particles with respect to 100 parts by weight of the binder. The anisotropic particles have an aspect ratio of 4 to 1,000 and include one or more selected from first inorganic particles and organic particles. The separator according to the embodiments of the present disclosure may have significantly improved adhesion to an electrode of the secondary battery.
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
90.
METHOD FOR REMOVING CHLORINE FROM WASTE PLASTIC PYROLYSIS OIL
The present disclosure relates to a method for removing chlorine from waste plastic pyrolysis oil, the method including: (S1) mixing and reacting waste plastic pyrolysis oil with a neutralizing solution that contains a neutralizer containing M-OR1 and a solvent; and (S2) subjecting a fluid generated in the step (S1) to a water treatment to remove chlorine, wherein M is an alkali metal or an alkaline earth metal, and R1 is a C1 to C10 alkyl group.
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
C10G 53/04 - Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only including at least one extraction step
The present disclosure relates to a method and a system for producing hydrogen, the method comprising the steps of: (S1) purifying landfill gas, thereby generating a first mixed gas; (S2) performing steam reforming on the first mixed gas in a first reactor, thereby generating a second mixed gas; (S3) separating the second mixed gas into a first stream comprising carbon dioxide and a second stream comprising hydrogen and carbon monoxide; (S4) introducing the first stream, separated out in step (S3), into a second reactor and converting same into carbon monoxide through reverse Boudouard reaction; (S5) mixing the second stream and the carbon monoxide converted in step (S4), thereby preparing a third mixed gas; (S6) generating syngas from the third mixed gas through water-gas shift reaction; and (S7) separating carbon dioxide from the syngas, thereby obtaining hydrogen.
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
C01B 3/50 - Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
A method of preparing an EPDM copolymer by solution polymerization using a Ziegler-Natta catalyst system, in which the Ziegler-Natta catalyst system includes VOCl3, ethylaluminum sesquichloride (EASC), and a straight chain or branched chain C4-C6 alkyl amine as a catalyst modifier. The method includes performing polymerization by adding the catalyst modifier before injecting VOCl3 or by adding VOCl3 and the catalyst modifier simultaneously.
C08F 4/20 - Metallic compounds other than hydrides and other than metallo-organic compoundsBoron halide or aluminium halide complexes with organic compounds containing oxygen of antimony, bismuth, vanadium, niobium, or tantalum
A separator and an electrochemical device comprising the separator are provided, the separator comprising a porous substrate, and an inorganic particle layer formed on at least one surface of the porous substrate and comprises a binder and inorganic particles. The separator has a peak shown in a range of 1082.5 to 1086.5 cm−1 in a spectrum by Fourier-transform infrared spectroscopy (FT-IR), and a saturated moisture content measured by a Karl Fischer method of 350 to 1000 ppm.
A method for removing a pulverized bumper surface material includes a peeling operation of cutting a pulverized bumper by a cutting blade to peel a surface material as a rotating drum rotates by using peeling machine including the rotating drum on which the cutting blade is formed, a transfer operation of transferring the pulverized bumper to which the surface material peeled in the peeling operation is attached to a separation region, and a separation operation of separating the peeled surface material from the pulverized bumper in the separation region, wherein, in the peeling operation, steam is sprayed on the pulverized bumper to peel the surface material from the pulverized bumper due to a difference in a coefficient of thermal expansion between the surface material and the pulverized bumper.
B26D 3/28 - Splitting layers from workMutually separating layers by cutting
B26D 7/06 - Arrangements for feeding or delivering work of other than sheet, web, or filamentary form
B26D 1/40 - Cutting through work characterised by the nature or movement of the cutting memberApparatus or machines thereforCutting members therefor involving a cutting member which does not travel with the work having a cutting member moving about an axis with a non-circular cutting member moving about an axis parallel to the line of cut and coacting with a rotary member
B26D 5/08 - Means for actuating the cutting member to effect the cut
B26D 7/00 - Details of apparatus for cutting, cutting-out, stamping-out, punching, perforating, or severing by means other than cutting
95.
HYBRID SEPARATOR AND LITHIUM SECONDARY BATTERY INCLUDING THE SAME
Hybrid separators and lithium secondary batteries including the hybrid separators are disclosed. In an embodiment, a lithium secondary battery includes a negative electrode, a positive electrode, a separator disposed between the negative electrode and the positive electrode, and a liquid electrolyte, wherein the separator is a hybrid separator including a porous substrate and a lithium ion conductive flexible polymer layer disposed on at least one surface of the porous substrate, and a lithium ionic conductivity of the hybrid separator is 10−4 to 10−2 S/cm. The hybrid separator that includes the flexible polymer layer based on some embodiments of the disclosed technology can improve the mechanical strength of the separator and significantly reduce the formation of lithium dendrites during charging and discharging cycles.
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
Embodiments of the present disclosure relate to a separator comprising a porous substrate; and an inorganic particle layer disposed on at least one surface of the porous substrate, the inorganic particle layer comprising a binder and inorganic particles, wherein the separator has a Gurley permeability of 10 to 250 sec/100 cc, a puncture strength of 0.3 N/μm or more, tensile strengths in the machine direction and in the transverse direction of 1500 kgf/cm2 or more, heat shrinkage rates in the machine direction and in the transverse direction measured after being allowed to stand at 130° C. for 60 minutes of 5% or less, and a saturated moisture content measured by a Karl Fischer method of 350 to 1000 ppm.
An ammonia oxidation catalyst and a catalyst system and method using the ammonia oxidation catalyst are provided. The catalyst comprises a metal oxide including titanium and chromium, wherein an energy band gap of the metal oxide measured by UV-Vis DRS is less than 1.4 eV. The catalyst system comprises an ammonia decomposition reactor and a catalyst unit which is located downstream from the ammonia decomposition reactor, and includes the above-described ammonia oxidation catalyst.
C01B 3/04 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of inorganic compounds, e.g. ammonia
H01M 8/0606 - Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
98.
Carbon Dioxide Absorbent Comprising Ionic Liquid and Alcohol Solvent, and Method Of Separating Carbon Dioxide Using the Same
Provided is a carbon dioxide absorbent including an ionic liquid including an imidazole-based anion and an aliphatic alcohol, and since an alcohol solvent included in the carbon dioxide absorbent according to one embodiment has low toxicity and a very high boiling point, the carbon dioxide absorbent has no problem of release into the atmosphere and consequent environmental pollution, and is chemically stable to significantly lower the possibility of release of decomposition products into the atmosphere. In addition, the carbon dioxide absorbent is also effective, since it may absorb carbon dioxide with a higher equivalent than an absorbent input equivalent, and has low regeneration energy so that carbon dioxide is easily desorbed.
B01J 20/22 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising organic material
B01J 20/28 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof characterised by their form or physical properties
99.
GAS INJECTION NOZZLE FOR DRYING ELECTRODE PLATE AND DRYING APPARATUS FOR ELECTRODE PLATE INCLUDING THE SAME
Embodiments of the present disclosure relate to a gas injection nozzle for drying an electrode plate, coupled to a chamber of a drying apparatus for the electrode plate, and including a first nozzle body including at least one inlet opening configured to allow the drying gas to flow therein; a second nozzle body connected to the first nozzle body and including a plurality of injection holes configured to inject the drying gas outside of the gas injection nozzle; and a partition plate disposed between the first nozzle body and the second nozzle body, and including at least one communication hole configured to allow the drying gas to flow from the at least one inlet opening to the plurality of injection holes. At least a portion of the first nozzle body is protruding into a gas supply space of the chamber so as to be disposed inside the chamber.
The present disclosure provides a gas injection nozzle for drying an electrode plate including: a nozzle body including a first plate, a second plate, and a partition plate, wherein the partition plate divides a flow space formed between the first plate and the second plate into a first flow space opposing the first plate and a second flow space opposing the second plate; at least one inlet hole formed in the first plate and configured to allow drying gas to flow into the first flow space; at least one communication hole formed in the partition plate and configured to allow the first flow space and the second flow space to communicate with each other; and a plurality of injection holes formed in the second plate and configured to inject drying gas from the second flow space to the outside.
B05B 1/04 - Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops in flat form, e.g. fan-like, sheet-like
B05D 1/02 - Processes for applying liquids or other fluent materials performed by spraying
