Produits et services

Procurement, namely, purchasing of equipment, machinery, process units, supplies and associated equipment for utility, industrial, commercial, governmental, public works, public accommodation, and infrastructure facilities, structures, and plants for others; business management services, namely, contract administration and project management services. Construction, installation, repair, renovation, and replacement services for public and private accommodations and infrastructure facilities, building structures, plants, equipment; maintenance services, namely, building maintenance services in the public and private sectors, namely, utility, industrial, and commercial companies and governments; inspection and supervisory services in connection with the forgoing in the public and private sectors, namely, utility, industrial, and commercial companies and government; construction, maintenance, and/or repair services for buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; construction, maintenance, and/or repair services for buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries. Biomass gasification services, treatment of waste water; waste to energy generation services. Architectural and engineering services for the design of buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; engineering services in the field of reducing carbon dioxide emissions; engineering services in the field of reducing nitrogen oxide emissions; engineering in the public and private sectors, namely, utility, industrial, and commercial companies and governments; design services, namely, architectural design in the public and private sectors, namely, utility, industrial, and commercial companies and governments; information technology consultation services, namely, enterprise IT consolidation, help desk and network management, telecommunications sustainment and modernization, information assurance and computer network defense; engineering services and computer engineering services in the field of cybersecurity; developing computer software for others; and scientific research services in the field of aerospace development, national defense, and commercial nuclear power; research, engineering, and testing in the fields of aerospace development, national defense, and commercial nuclear power provided to firms in those industries; engineering services for computer security purposes, namely, protecting data and information from unauthorized access.

Abrégé

A method for treating effluent from hydrothermal liquification of feedstock that contains plastic oil, pyrolysis oil, synthetic oil or hydrocarbons distillates in a plastic recycle process using supercritical water as a reaction medium into a finished liquid hydrocarbon fuel by removing impurities such as i.e. silicon, chlorides, metals, heteroatoms, etc., in a pre-treatment zone and may be passed into a feed drum or a continuous mixed settler vessel. The feed is introduced into a hydrogen atmosphere reactor. The reactor effluent is passed to a separator for extracting product mixture by addition of make-up or recycled hydrogen to the separator. The overhead product mixture is water washed to remove sour water or salt. The separator effluent is passed to a distillation section for extracting a liquid fuel product stream. A portion of the hydro processing product stream may be recycled to the feed drum or the continuous mixed settler vessel, which reduces concentration of diolefins.

Classes IPC  ?

• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction

Abrégé

A method for treating effluent from hydrothermal liquification of feedstock that contains plastic oil, pyrolysis oil, synthetic oil or hydrocarbons distillates in a plastic recycle process using supercritical water as a reaction medium into a finished liquid hydrocarbon fuel by removing impurities such as i.e. silicon, chlorides, metals, heteroatoms, etc., in a pre-treatment zone and may be passed into a feed drum or a continuous mixed settler vessel. The feed is introduced into a hydrogen atmosphere reactor. The reactor effluent is passed to a separator for extracting product mixture by addition of make-up or recycled hydrogen to the separator. The overhead product mixture is water washed to remove sour water or salt. The separator effluent is passed to a distillation section for extracting a liquid fuel product stream. A portion of the hydro processing product stream may be recycled to the feed drum or the continuous mixed settler vessel, which reduces concentration of diolefins.

Classes IPC  ?

• C10G 45/32 - Hydrogénation sélective des composés dioléfiniques ou acétyléniques
• C10G 65/06 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en série ne comprenant que des étapes de raffinage au moins une étape étant une hydrogénation sélective des dioléfines
• C08J 11/04 - Récupération ou traitement des résidus des polymères
• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression

Produits et services

Chemicals for use in industry, science and photography, as well as in agriculture, horticulture and forestry; unprocessed artificial resins, unprocessed plastics; fire extinguishing and fire prevention compositions; tempering and soldering preparations; substances for tanning animal skins and hides; adhesives for use in industry; putties and other paste fillers; compost, manures, fertilizers; biological preparations for use in industry and science; accelerators for organic chemical reactions; accelerators for speeding up chemical reactions; chemicals in the nature of activators; chemical additives; chemicals in the nature of buffers; chemical absorbents; chemical adjuvants; chemical agents; chemical coatings; chemical compositions; chemical compounds; chemical diagnostic reagents; chemical emulsifiers; chemical extenders; chemical preparations; chemical products for biotechnological purposes; chemical products for laboratory use other than for medical or veterinary use; chemical products for scientific purposes; chemical products for research purposes; purification chemicals; chemicals in the nature of sealing preparations. Industrial oils and greases, wax; lubricants; dust absorbing, wetting and binding compositions; fuels and illuminants; biofuel; additives for oil, fuel, lubricants, greases, petroleum products; alcohol fuel; biodiesel fuel; biomass fuels; emulsions of oil for use as a fuel; emulsions of bitumen for use as fuel; fuel mixtures. Unprocessed and semi-processed rubber, gutta-percha, gum, asbestos, mica and substitutes for all these materials; plastics and resins in extruded form for use in manufacture; packing, stopping and insulating materials; recycled plastic; recycled rubber; semi-finished chemical resins. Materials, not of metal, for building and construction; asphalt, pitch, tar and bitumen; composite bitumen; mixtures of bitumen and plastics for building purposes; mixtures of bitumen and plastics for making roads; bitumen binding material; bituminous coatings and coverings; bituminous materials other than paint; bituminous preparations other than paint; bituminous products other than paint; acrylic coatings other than paint; coating preparations other than paints or oils; coating materials. Treatment of materials; recycling; recycling of waste and trash; recycling of plastic; recycling of materials; recycling plants; air purification and treatment of water; catalytic conversion of chemical compounds; chemical processing of liquids; chemical treatment of waste products; chemical treatment of plastics; chemical recycling; treatment of chemicals in the nature of recycling; treatment of waste in the nature of recycling; upcycling; carbon offsetting services in the nature of recycling. Scientific and technological services and research and design relating thereto; industrial analysis, industrial research and industrial design services; quality control and authentication services; testing of chemicals; chemistry services; measurement services; providing information, including online, about industrial analysis and research services; material testing; services for assessing the efficiency of chemicals; services for monitoring industrial processes; technical data analysis services; technical diagnostic testing services; technological analysis services; technological consultation services; chemical analysis; chemical information; chemical technological research; preparation of reports relating to chemical research; research relating to chemicals; research relating to chemistry; scientific research relating to chemical products; scientific research relating to chemistry; testing of chemicals; biotechnological research; biotechnology research; biotechnology testing; research relating to biotechnology.

Abrégé

A steam cracking unit including one or more electric resistance heating tubes electrically connected to a current source to generate heat via electrical resistance heating. Each resistance heating tube may include two or more tube sections. Each tube section may be independently supplied with a current. A controller may be configured to adjust the application of the current to one or more tube sections to control the electrical resistance heating of the one or more resistance heating tubes. In examples, the one or more electric heating tubes may be used as preheating tubes, cracking tubes, or both.

Classes IPC  ?

• C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
• B01J 19/24 - Réacteurs fixes sans élément interne mobile

Abrégé

A steam cracking unit including one or more electric resistance heating tubes electrically connected to a current source to generate heat via electrical resistance heating. Each resistance heating tube may include two or more tube sections. Each tube section may be independently supplied with a current. A controller may be configured to adjust the application of the current to one or more tube sections to control the electrical resistance heating of the one or more resistance heating tubes. In examples, the one or more electric heating tubes may be used as preheating tubes, cracking tubes, or both.

Classes IPC  ?

• C10G 9/00 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures
• C08F 2/01 - Procédés de polymérisation caractérisés par des éléments particuliers des appareils de polymérisation utilisés
• C08F 6/00 - Traitements postérieurs à la polymérisation
• C08F 10/02 - Éthylène

Abrégé

A first stream containing 1,3-butadiene, C4 acetylenes, and optionally C3 hydrocarbons, is mixed with a portion of the liquid recycle stream from a C4 acetylene hydrogenation reactor containing hydrogenated C4 acetylenes and a molecular hydrogen-containing stream, the resulting mixed stream is then fed to a C4 acetylene hydrogenation reactor to selectively hydrogenate the C4 acetylenes in the crude butadiene stream without appreciable 1,3-butadiene conversion.

Classes IPC  ?

• C07C 7/167 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par traitement provoquant une modification chimique d'au moins un composé par hydrogénation pour éliminer les composés comportant une triple liaison carbone-carbone
• B01J 19/00 - Procédés chimiques, physiques ou physico-chimiques en généralAppareils appropriés
• C07C 5/09 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant le même nombre d'atomes de carbone par hydrogénation de liaisons triples carbone-carbone en liaisons doubles carbone-carbone
• C07C 11/167 - Butadiène-1,3

Abrégé

A syngas reforming exchanger reactor design is described. The reforming exchanger has a head, a shell, and a tubesheet secured a tube bundle. The tubesheet is bolted to the shell, after which the head is bolted to the shell. A seal is configured between the tubesheet and components of the shell. Another seal is configured between components of the head and the tubesheet. In the reformer exchanger design, those seals are maintained under bolted pressure via the bolting of both the tubesheet and the head to the shell. This design improves the integrity of sealing, thereby preventing escape of hot reformed gases from the reformer exchanger reactor during operation.

Classes IPC  ?

• F28D 7/16 - Appareils échangeurs de chaleur comportant des ensembles de canalisations tubulaires fixes pour les deux sources de potentiel calorifique, ces sources étant en contact chacune avec un côté de la paroi d'une canalisation les canalisations étant espacées parallèlement
• B01J 19/00 - Procédés chimiques, physiques ou physico-chimiques en généralAppareils appropriés
• B01J 19/24 - Réacteurs fixes sans élément interne mobile
• C01B 3/34 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants
• F28F 9/00 - CartersBoîtes de distributionSupports auxiliaires pour les élémentsÉléments auxiliaires dans les carters

Abrégé

A syngas reforming exchanger reactor design is described. The reforming exchanger has a head, a shell, and a tubesheet secured a tube bundle. The tubesheet is bolted to the shell, after which the head is bolted to the shell. A seal is configured between the tubesheet and components of the shell. Another seal is configured between components of the head and the tubesheet. In the reformer exchanger design, those seals are maintained under bolted pressure via the bolting of both the tubesheet and the head to the shell. This design improves the integrity of sealing, thereby preventing escape of hot reformed gases from the reformer exchanger reactor during operation.

Classes IPC  ?

• B01J 8/06 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes dans des réacteurs tubulairesProcédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes les particules solides étant disposées dans des tubes
• F28F 9/013 - Supports auxiliaires pour les éléments pour les tubes ou les assemblages de tubes

Abrégé

A reactor system and method for catalytic dehydrogenation of saturated C3-C6 hydrocarbons within a reactor placed within a reactor disengager, where the reactor is open at the bottom thereof and open to the disengager, and the exit riser from the reactor is not hard coupled to at least one downstream cyclone. This configuration permits controlling the amount of catalyst within the reactor by varying the level of catalyst in the reactor disengager outside the reactor and permits controlling total catalyst hold-up and/or weight hourly space velocity (WHSV) independently from catalyst flow from the catalyst regenerator.

Classes IPC  ?

• B01J 8/00 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés
• B01J 8/18 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées
• C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"

Abrégé

A process and system to deasphalt used motor oil distillate residue including VTAE the process including feeding the used motor oil distillate residue and a supercritical solvent to an asphaltene separator that outputs an overhead having deasphalted oil and a bottoms that includes pitch.

Classes IPC  ?

• C10G 21/00 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par extraction au moyen de solvants sélectifs
• C10G 67/02 - Traitement des huiles d'hydrocarbures, uniquement par au moins un procédé d'hydrotraitement et au moins un procédé de raffinage en l'absence d'hydrogène uniquement par plusieurs étapes en série
• C10G 67/04 - Traitement des huiles d'hydrocarbures, uniquement par au moins un procédé d'hydrotraitement et au moins un procédé de raffinage en l'absence d'hydrogène uniquement par plusieurs étapes en série comprenant une extraction par solvant comme étape de raffinage en l'absence d'hydrogène

Abrégé

A process and system to deasphalt used motor oil distillate residue including VTAE the process including feeding the used motor oil distillate residue and a supercritical solvent to an asphaltene separator that outputs an overhead having deasphalted oil and a bottoms that includes pitch.

Classes IPC  ?

• C10G 21/00 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par extraction au moyen de solvants sélectifs

Abrégé

A system for controlling a steam cracking furnace may include a controller configured to control an electric heater to pre-heat a combustion air feed to a radiation section of the cracking furnace, and one or more sensors configured to sense properties of a recovered pure hydrogen stream fed to the radiation section of the cracking furnace as fuel. The controller can be configured to receive the sensed properties from the one or more sensors and control the electric heater based on the one or more sensed properties.

Classes IPC  ?

• C07C 4/04 - Procédés thermiques
• B01J 6/00 - CalcinationCuisson
• C10G 47/36 - Commande ou régulation

Abrégé

A process and system for integrating a steam cracking unit with a blue hydrogen unit in which a methane-rich gas stream, a hydrogen-rich gas stream, or both from the steam cracking unit are fed to the blue hydrogen unit and a high purity hydrogen gas stream from the blue hydrogen unit is directed to the steam cracking unit.

Classes IPC  ?

• C07C 4/02 - Préparations d'hydrocarbures à partir d'hydrocarbures contenant un plus grand nombre d'atomes de carbone par craquage d'un hydrocarbure unique ou d'un mélange d'hydrocarbures individuellement définis ou d'une fraction d'hydrocarbures normalement gazeux
• C07C 4/04 - Procédés thermiques
• C10G 69/02 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série
• C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène

Abrégé

A process and system to integrate a steam cracking unit with a blue ammonia unit such that a methane-rich gas stream and/or a hydrogen-rich gas stream is directed from the steam cracking unit to the blue ammonia unit while a hydrogen gas containing stream is directed from the blue ammonia unit to the steam cracking unit.

Classes IPC  ?

• C01B 3/04 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés inorganiques, p. ex. de l'ammoniac
• C01B 3/56 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification par contact avec des solidesRégénération des solides usés
• C01B 3/52 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification par contact avec des liquidesRégénération des liquides usés
• B01D 3/32 - Autres caractéristiques de colonnes de fractionnement

Abrégé

A process and system for integrating a steam cracking unit with a blue hydrogen unit in which a methane-rich gas stream, a hydrogen-rich gas stream, or both from the steam cracking unit are fed to the blue hydrogen unit and a high purity hydrogen gas stream from the blue hydrogen unit is directed to the steam cracking unit.

Classes IPC  ?

• C01B 3/36 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec l'oxygène ou des mélanges contenant de l'oxygène comme agents gazéifiants
• C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
• C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
• C10G 70/04 - Post-traitement de mélanges non définis normalement gazeux obtenus par des procédés couverts par les groupes , , , , par des procédés physiques

Abrégé

A process and system to integrate a steam cracking unit with a blue ammonia unit such that a methane-rich gas stream and/or a hydrogen-rich gas stream is directed from the steam cracking unit to the blue ammonia unit while a hydrogen gas containing stream is directed from the blue ammonia unit to the steam cracking unit.

Classes IPC  ?

• C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
• C01B 3/04 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés inorganiques, p. ex. de l'ammoniac
• C01C 1/02 - Préparation ou séparation d'ammoniac

Abrégé

A method and apparatus for high-purity hydrogen fired liquid hydrocarbon cracking. In one embodiment, the method may include preheating a liquid hydrocarbon feedstock in a first heat exchanger that is external to a furnace, adding steam to the preheated liquid hydrocarbon feedstock to create a fully or substantially fully vaporized stream, heating the fully or substantially fully vaporized stream in a second heat exchanger that is external to the furnace, and cracking the heated fully or substantially fully vaporized stream after it is preheated in the furnace to create a cracked gas stream comprising ethylene and hydrogen.

Classes IPC  ?

• C07C 11/04 - Éthylène
• C07C 4/04 - Procédés thermiques

Abrégé

A method and apparatus for high-purity hydrogen fired liquid hydrocarbon cracking. In one embodiment, the method may include preheating a liquid hydrocarbon feedstock in a first heat exchanger that is external to a furnace, adding steam to the preheated liquid hydrocarbon feedstock to create a fully or substantially fully vaporized stream, heating the fully or substantially fully vaporized stream in a second heat exchanger that is external to the furnace, and cracking the heated fully or substantially fully vaporized stream after it is preheated in the furnace to create a cracked gas stream comprising ethylene and hydrogen.

Classes IPC  ?

• C07C 11/04 - Éthylène
• C07C 4/02 - Préparations d'hydrocarbures à partir d'hydrocarbures contenant un plus grand nombre d'atomes de carbone par craquage d'un hydrocarbure unique ou d'un mélange d'hydrocarbures individuellement définis ou d'une fraction d'hydrocarbures normalement gazeux
• C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds

Abrégé

A system for controlling a steam cracking furnace may include a controller configured to control an electric heater to pre-heat a combustion air feed to a radiation section of the cracking furnace, and one or more sensors configured to sense properties of a recovered pure hydrogen stream fed to the radiation section of the cracking furnace as fuel. The controller can be configured to receive the sensed properties from the one or more sensors and control the electric heater based on the one or more sensed properties.

Classes IPC  ?

• C07C 4/04 - Procédés thermiques
• C07C 11/04 - Éthylène
• F27D 19/00 - Aménagement des dispositifs de commande

Produits et services

(1) Chemicals for use in industry, science and photography, as well as in agriculture, horticulture and forestry; unprocessed artificial resins, unprocessed plastics; fire extinguishing and fire prevention compositions; tempering and soldering preparations; substances for tanning animal skins and hides; adhesives for use in industry; putties and other paste fillers; compost, manures, fertilizers; biological preparations for use in industry and science; accelerators for organic chemical reactions; accelerators for speeding up chemical reactions; chemicals in the nature of activators; chemical additives; chemicals in the nature of buffers; chemical absorbents; chemical adjuvants; chemical agents; chemical coatings; chemical compositions; chemical compounds; chemical diagnostic reagents; chemical emulsifiers; chemical extenders; chemical preparations; chemical products for biotechnological purposes; chemical products for laboratory use other than for medical or veterinary use; chemical products for scientific purposes; chemical products for research purposes; purification chemicals; chemicals in the nature of sealing preparations. (2) Industrial oils and greases, wax; lubricants; dust absorbing, wetting and binding compositions; fuels and illuminants; biofuel; additives for oil, fuel, lubricants, greases, petroleum products; alcohol fuel; biodiesel fuel; biomass fuels; emulsions of oil for use as a fuel; emulsions of bitumen for use as fuel; fuel mixtures. (3) Unprocessed and semi-processed rubber, gutta-percha, gum, asbestos, mica and substitutes for all these materials; plastics and resins in extruded form for use in manufacture; packing, stopping and insulating materials; recycled plastic; recycled rubber; semi-finished chemical resins. (4) Materials, not of metal, for building and construction; asphalt, pitch, tar and bitumen; composite bitumen; mixtures of bitumen and plastics for building purposes; mixtures of bitumen and plastics for making roads; bitumen binding material; bituminous coatings and coverings; bituminous materials other than paint; bituminous preparations other than paint; bituminous products other than paint; acrylic coatings other than paint; coating preparations other than paints or oils; coating materials. (1) Treatment of materials; recycling; recycling of waste and trash; recycling of plastic; recycling of materials; recycling plants; air purification and treatment of water; catalytic conversion of chemical compounds; chemical processing of liquids; chemical treatment of waste products; chemical treatment of plastics; chemical recycling; treatment of chemicals in the nature of recycling; treatment of waste in the nature of recycling; upcycling; carbon offsetting services in the nature of recycling. (2) Scientific and technological services and research and design relating thereto; industrial analysis, industrial research and industrial design services; quality control and authentication services; testing of chemicals; chemistry services; measurement services; providing information, including online, about industrial analysis and research services; material testing; services for assessing the efficiency of chemicals; services for monitoring industrial processes; technical data analysis services; technical diagnostic testing services; technological analysis services; technological consultation services; chemical analysis; chemical information; chemical technological research; preparation of reports relating to chemical research; research relating to chemicals; research relating to chemistry; scientific research relating to chemical products; scientific research relating to chemistry; testing of chemicals; biotechnological research; biotechnology research; biotechnology testing; research relating to biotechnology.

Produits et services

Engineering services relating to ammonia production process

Abrégé

A separation process and system to separate highly pure polymer grade propylene product from a liquefied petroleum gas stream combined. In examples, the system and method as combine the functions of a deethanizer and of a depropanizer, with a C3 splitter system to separate highly pure polymer grade propylene product from a liquefied petroleum gas stream, thus eliminating the need for separate dethanizer, depropanizer, and C3-splitter.

Classes IPC  ?

• B01D 3/14 - Distillation fractionnée
• C07C 11/06 - Propène
• C07C 7/04 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par distillation
• C07C 9/08 - Propane
• C10C 3/12 - Dispositifs à cet effet

Abrégé

In a Fluid Catalytic Cracker (FCC) unit being operated in petrochemical mode that has an increased dry gas and LPG production that creates a bottleneck in product flow, a method for full or partial separation of light gas components from a wet gas compressor suction stream and routing it directly to an untreated fuel gas header using a parallel system to an existing wet gas compressor, which parallel system includes an auxiliary compressor and a membrane separation system.

Classes IPC  ?

• C10G 70/04 - Post-traitement de mélanges non définis normalement gazeux obtenus par des procédés couverts par les groupes , , , , par des procédés physiques
• C10G 55/08 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par au moins un procédé de raffinage et par au moins un procédé de craquage uniquement par plusieurs étapes en parallèle

Abrégé

Methods and systems for alkylate production involving a multi-zone alkylation reactor. The multi-zone alkylation reactor includes a plurality of alkylation zones spaced vertically in a series configuration and a partition splitting the plurality of alkylation zones into at least two mechanically separated catalytic volumes.

Classes IPC  ?

• B01J 8/04 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes le fluide passant successivement à travers plusieurs lits
• C07C 2/76 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un plus petit nombre d'atomes de carbone par condensation d'hydrocarbures avec élimination partielle d'hydrogène

Abrégé

Methods and systems are provided for delimiting a gas plant during fluid catalytic cracking unit (FCCU) revamp as part of the olefin production system. These methods and system include a chiller unit in the gas concentration unit downstream of the FCCU. Other measures also include installing a stripper unit downstream of the regenerator of the FCCU or installing a quench line in a reactor of a FCCU to reduce the contact time of the hydrocarbon feedstock with the catalyst. These methods and systems may also lead to an increase in the propylene yield of the olefin production system

Classes IPC  ?

• C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"
• C10G 7/00 - Distillation des huiles d'hydrocarbures
• B01D 3/14 - Distillation fractionnée
• C10G 70/04 - Post-traitement de mélanges non définis normalement gazeux obtenus par des procédés couverts par les groupes , , , , par des procédés physiques
• C10G 35/24 - Commande ou régulation des opérations de réformage
• F28F 19/00 - Prévention de la formation de dépôts ou de la corrosion, p. ex. en utilisant des filtres
• F28D 7/16 - Appareils échangeurs de chaleur comportant des ensembles de canalisations tubulaires fixes pour les deux sources de potentiel calorifique, ces sources étant en contact chacune avec un côté de la paroi d'une canalisation les canalisations étant espacées parallèlement

Abrégé

Methods and systems are provided for delimiting a gas plant during fluid catalytic cracking unit (FCCU) revamp as part of the olefin production system. These methods and system include a chiller unit in the gas concentration unit downstream of the FCCU. Other measures also include installing a stripper unit downstream of the regenerator of the FCCU or installing a quench line in a reactor of a FCCU to reduce the contact time of the hydrocarbon feedstock with the catalyst. These methods and systems may also lead to an increase in the propylene yield of the olefin production system.

Classes IPC  ?

• B01J 8/18 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées
• B01D 3/14 - Distillation fractionnée
• B01D 5/00 - Condensation de vapeursRécupération de solvants volatils par condensation
• B01J 8/24 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé"

Abrégé

In a Fluid Catalytic Cracker (FCC) unit being operated in petrochemical mode that has an increased dry gas and LPG production that creates a bottleneck in product flow, a method for full or partial separation of light gas components from a wet gas compressor suction stream and routing it directly to an untreated fuel gas header using a parallel system to an existing wet gas compressor, which parallel system includes an auxiliary compressor and a membrane separation system.

Classes IPC  ?

• C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"
• C07C 4/06 - Procédés catalytiques
• C10G 11/02 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures caractérisé par le catalyseur utilisé
• C10G 55/06 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par au moins un procédé de raffinage et par au moins un procédé de craquage uniquement par plusieurs étapes en série comprenant au moins une étape de craquage catalytique
• B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération

Abrégé

A multi-tier integrated power-to-ammonia system includes a converter for generating ammonia and heat through a reaction involving a compressed mixture of hydrogen and nitrogen gases. The system includes a steam generator that can generate steam using the heat from the reaction, and a reversible solid-oxide system in fluid communication with the steam generator that can separate the steam into oxygen gas and hydrogen gas.

Classes IPC  ?

• C01C 1/04 - Préparation d'ammoniac par synthèse
• C25B 1/042 - Hydrogène ou oxygène par électrolyse de l'eau par électrolyse de la vapeur
• C25B 15/08 - Alimentation ou vidange des réactifs ou des électrolytesRégénération des électrolytes

Abrégé

A multi-tier integrated power-to-ammonia system includes a converter for generating ammonia and heat through a reaction involving a compressed mixture of hydrogen and nitrogen gases. The system includes a steam generator that can generate steam using the heat from the reaction, and a reversible solid-oxide system in fluid communication with the steam generator that can separate the steam into oxygen gas and hydrogen gas.

Classes IPC  ?

• C01C 1/04 - Préparation d'ammoniac par synthèse
• C25B 1/042 - Hydrogène ou oxygène par électrolyse de l'eau par électrolyse de la vapeur
• F25J 3/04 - Procédés ou appareils pour séparer les constituants des mélanges gazeux impliquant l'emploi d'une liquéfaction ou d'une solidification par rectification, c.-à-d. par échange continuel de chaleur et de matière entre un courant de vapeur et un courant de liquide pour l'air
• H01M 8/20 - Éléments à combustible indirects, p. ex. éléments à combustible avec un couple REDOX irréversible
• C01B 3/02 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène

Produits et services

Engineering services relating to the treatment of materials, namely, hydrometallurgical extraction of battery metals.

Abrégé

A piping connection system and method to connect a double pipe system such as a double pipe heat changer to a housing, for example a housing of a manifold. In examples, the piping connection system and method may include a transition member configured to bond or connect to the double pipe system and to the housing. In examples, the piping connection system may include a baffle configured to redirect flow from the housing to the double pipe system through an opening and towards the transition member. In examples, the piping connection system and method may be used to manufacture a quench exchanger such as a primary quench exchanger.

Classes IPC  ?

• F28F 9/18 - Dispositions pour obturer des éléments dans les boîtes de distribution ou plaques d'extrémité par joints permanents, p. ex. par dudgeonnage par soudage
• F28D 7/10 - Appareils échangeurs de chaleur comportant des ensembles de canalisations tubulaires fixes pour les deux sources de potentiel calorifique, ces sources étant en contact chacune avec un côté de la paroi d'une canalisation les canalisations étant disposées l'une dans l'autre, p. ex. concentriquement
• F28F 1/00 - Éléments tubulairesEnsembles d'éléments tubulaires
• F28F 9/02 - Boîtes de distributionPlaques d'extrémité

Abrégé

A piping connection system and method to connect a double pipe system such as a double pipe heat changer to a housing, for example a housing of a manifold. In examples, the piping connection system and method may include a transition member configured to bond or connect to the double pipe system and to the housing. In examples, the piping connection system may include a baffle configured to redirect flow from the housing to the double pipe system through an opening and towards the transition member. In examples, the piping connection system and method may be used to manufacture a quench exchanger such as a primary quench exchanger.

Classes IPC  ?

• F28D 7/10 - Appareils échangeurs de chaleur comportant des ensembles de canalisations tubulaires fixes pour les deux sources de potentiel calorifique, ces sources étant en contact chacune avec un côté de la paroi d'une canalisation les canalisations étant disposées l'une dans l'autre, p. ex. concentriquement
• F28D 7/12 - Appareils échangeurs de chaleur comportant des ensembles de canalisations tubulaires fixes pour les deux sources de potentiel calorifique, ces sources étant en contact chacune avec un côté de la paroi d'une canalisation les canalisations étant disposées l'une dans l'autre, p. ex. concentriquement le tube extérieur étant fermé à une extrémité, c.-à-d. du type à retour
• F28D 7/00 - Appareils échangeurs de chaleur comportant des ensembles de canalisations tubulaires fixes pour les deux sources de potentiel calorifique, ces sources étant en contact chacune avec un côté de la paroi d'une canalisation
• F28F 9/02 - Boîtes de distributionPlaques d'extrémité

Produits et services

Business feasibility studies; Business project management services; Business project management services for construction projects; Business risk management; business services, namely, logistics management in the refinery, crude and refinery product blending, liquid natural gas storage and shipping, and batch processing industries; Procurement, namely, purchasing equipment, machinery, supplies and associated equipment for utility, industrial, transportation, buildings, mining, commercial, governmental, public works, public accommodation and infrastructure facilities, structures and plants for others; Operational business assistance to enterprises Construction, maintenance, and/or repair services for buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, coal gasification, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; Building construction observation, namely, static inspection, functional verification inspection, performance verification inspection; Construction consultation; Construction project management services; Inspection services in the course of construction of utilities, industrial facilities, transportation systems, buildings, mining facilities, commercial buildings, governmental facilities, public works plants, public accommodations, infrastructure facilities, structures, chemical and industrial plants, and construction equipment; Maintenance and/or repair of utilities, industrial facilities, transportation systems, buildings, mining facilities, commercial buildings, governmental facilities, public works plants, public accommodations, infrastructure facilities, structures, chemical and industrial plants, and construction equipment Architectural and engineering services for the design of buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, coal gasification, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; engineering services in the field of reducing carbon dioxide emissions; Computer-aided engineering services for others; Computer software development and computer programming development for others; Consulting in the field of information technology; Design, deployment and management of wireless computer networks for others; Engineering design services; Engineering services in the field of reducing nitrogen oxide emissions; Engineering services, namely, engineering for the utility, industrial, transportation, building, mining, commercial, aerospace, power, defense and government industries; Professional computer services, namely, network analysis, LAN/WAN design, wireless engineering, virtualization and computer project management; Scientific research and development; Information technology consulting services

Abrégé

A system for hydrogenation C3 and C4 acetylenes contained within a hydrocarbon stream generated in a stream cracker unit where a debutanizer is placed upstream of a depropanizer for more economical processing of the hydrocarbon stream to produce lighter hydrocarbons, where the system requires only one stripper tower downstream of hydrogenation to remove residual hydrogen.

Classes IPC  ?

• C10G 70/04 - Post-traitement de mélanges non définis normalement gazeux obtenus par des procédés couverts par les groupes , , , , par des procédés physiques
• C10G 51/06 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, uniquement par plusieurs procédés de craquage uniquement par plusieurs étapes en parallèle

Produits et services

Engineering services in the field of reducing carbon emissions within the catalytic cracking process

Produits et services

Consulting in the field of engineering; electrical engineering; engineering design services; engineering drawing services; engineering services, namely, engineering for the design and construction of facilities to store electricity; technology advisory services related to civil engineering and construction.

Produits et services

Consultancy in the field of artificial intelligence technology; providing temporary use of on-line non-downloadable software and applications using artificial intelligence for engineering and design of processes and facilities in the utility, industrial, transportation, building, mining, commercial, aerospace, power, defense and government industries; research in the field of artificial intelligence technology; software as a service (SAAS) services featuring software using artificial intelligence for engineering and design of processes and facilities in the ammonia, aviation, biofuel, carbon capture, carbon storage, chemical, coal gasification, coal monetization, fertilizer, gas, gas-to-liquids, hydrogen, liquified natural gas, manufacturing, minerals, mining, oil, olefins, organic chemical, paper, petrochemical, pipeline, power generation, power transmission, pulp, refining, renewable energy, synthesis gas, transportation, water supply and wastewater handling industries.

Produits et services

Chemicals for use in industry, science and photography, as well as in agriculture, horticulture and forestry; unprocessed artificial resins, unprocessed plastics; fire extinguishing and fire prevention compositions; tempering and soldering preparations; substances for tanning animal skins and hides; adhesives for use in industry; putties and other paste fillers; compost, manures, fertilizers; biological preparations for use in industry and science; accelerators for organic chemical reactions; accelerators for speeding up chemical reactions; chemicals in the nature of activators; chemical additives; chemicals in the nature of buffers; chemical absorbents; chemical adjuvants; chemical agents; chemical coatings; chemical compositions; chemical compounds; chemical diagnostic reagents; chemical emulsifiers; chemical extenders; chemical preparations; chemical products for biotechnological purposes; chemical products for laboratory use other than for medical or veterinary use; chemical products for scientific purposes; chemical products for research purposes; semi-finished chemical resins; purification chemicals; chemicals in the nature of sealing preparations Industrial oils and greases, wax; lubricants; dust absorbing, wetting and binding compositions; fuels and illuminants; biofuel; additives for oil, fuel, lubricants, greases, petroleum products; alcohol fuel; biodiesel fuel; biomass fuels; emulsions of oil for use as a fuel; emulsions of bitumen for use as fuel; fuel mixtures Treatment of materials; recycling; recycling of waste and trash; recycling of plastic; recycling of materials; recycling plants; air purification and treatment of water; catalytic conversion of chemical compounds; chemical processing of liquids; chemical treatment of waste products; chemical treatment of plastics; chemical recycling; treatment of chemicals in the nature of recycling; treatment of waste in the nature of recycling; upcycling; carbon offsetting services in the nature of recycling Unprocessed and semi-processed rubber, gutta-percha, gum, asbestos, mica and substitutes for all these materials; plastics and resins in extruded form for use in manufacture; packing, stopping and insulating materials; recycled plastic; recycled rubber Materials, not of metal, for building and construction; asphalt, pitch, tar and bitumen; composite bitumen; mixtures of bitumen and plastics for building purposes; mixtures of bitumen and plastics for making roads; bitumen binding material; bituminous coatings and coverings; bituminous materials other than paint; bituminous preparations other than paint; bituminous products other than paint; acrylic coatings other than paint; coating preparations other than paints or oils; coating materials Scientific and technological services and research and design relating thereto; industrial analysis, industrial research and industrial design services; quality control and authentication services; testing of chemicals; chemistry services; measurement services; providing information, including online, about industrial analysis and research services; material testing; services for assessing the efficiency of chemicals; services for monitoring industrial processes; technical data analysis services; technical diagnostic testing services; technological analysis services; technological consultation services; chemical analysis; chemical information; chemical technological research; preparation of reports relating to chemical research; research relating to chemicals; research relating to chemistry; scientific research relating to chemical products; scientific research relating to chemistry; testing of chemicals; biotechnological research; biotechnology research; biotechnology testing; research relating to biotechnology

Produits et services

Procurement, namely, purchasing of equipment, machinery, process units, supplies related to engineering and construction equipment, and associated equipment for utility, industrial, commercial, governmental, public works, public accommodation, and infrastructure facilities, structures, and plants for others; business management services, namely, contract administration and project management services Biomass gasification services, treatment of waste water; waste to energy generation services Construction, installation, repair, renovation, and replacement services of public and private accommodations and infrastructure facilities, building structures, plants, equipment; maintenance services, namely, building maintenance services in the public and private sectors, namely, utility, industrial, and commercial companies and governments; inspection and supervisory services associated therewith in the course of construction, installation, repair, renovation and replacement of the forgoing in the public and private sectors, namely, utility, industrial, and commercial companies and government; construction, maintenance, and repair services for buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries. Architectural and engineering services for the design of buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; engineering services in the field of reducing carbon dioxide emissions; engineering services in the field of reducing nitrogen oxide emissions; Engineering in the public and private sectors, namely, utility, industrial, and commercial companies and governments; design services, namely, architectural design in the public and private sectors, namely, utility, industrial, and commercial companies and governments; Information technology consultation services, namely, enterprise IT consolidation, help desk and network management, telecommunications sustainment and modernization, information assurance and computer network defense; Engineering services and computer engineering services in the field of cybersecurity; Developing computer software for others; and Scientific research services in the field of aerospace development, national defense, and commercial nuclear power; Scientific and technical research, engineering, and testing in the fields of aerospace development, national defense, and commercial nuclear power provided to firms in those industries; Engineering services for computer security purposes, namely, protecting data and information from unauthorized access

Produits et services

Fuels; aviation fuel; hydrocarbon fuels; non-chemical additives for fuels.

Abrégé

A system for reactivating a catalyst having a predetermined heat content includes a reactor, a regenerator, and an electrically energized heater. The reactor is configured to generate a spent catalyst. The regenerator is configured to receive the spent catalyst from the reactor. The electrically energized heater has a plurality of energy emitting members at least partially immersed in the spent catalyst. The heater is configured to provide a supplemental heat content to obtain the predetermined heat content.

Classes IPC  ?

• B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération
• B01J 8/18 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées
• B01J 38/02 - Traitement thermique

Produits et services

Fuels; aviation fuel; hydrocarbon fuels; non-chemical additives for fuels. Providing fuel business management services in the field of aviation. Fuel treatment services; processing of fuel materials; production, treatment and refinement of fuel, diesel fuel, biofuel and biodiesel fuel for others. Engineering services in the field of reducing fuel consumption; technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels.

Abrégé

A system for reactivating a catalyst having a predetermined heat content includes a reactor, a regenerator, and an electrically energized heater. The reactor is configured to generate a spent catalyst. The regenerator is configured to receive the spent catalyst from the reactor. The electrically energized heater has a plurality of energy emitting members at least partially immersed in the spent catalyst. The heater is configured to provide a supplemental heat content to obtain the predetermined heat content.

Classes IPC  ?

• B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération
• B01J 38/02 - Traitement thermique
• B01J 38/22 - Lit mobile, p. ex. la charge se déplaçant verticalement ou horizontalement
• B01J 38/30 - Traitement avec un gaz contenant de l'oxygène libre en suspension gazeuse, p. ex. lits fluidisés

Produits et services

(1) Fuels; aviation fuel; hydrocarbon fuels; non-chemical additives for fuels.

Abrégé

A method of evaluating one or more aspects of a low carbon ammonia production facility uses a digital twin implemented on a computer system. The digital twin includes a low carbon energy source component and one or more of: a hydrogen source component, a nitrogen source component, and an ammonia synthesis loop component.

Classes IPC  ?

• G06Q 10/04 - Prévision ou optimisation spécialement adaptées à des fins administratives ou de gestion, p. ex. programmation linéaire ou "problème d’optimisation des stocks"
• G06Q 50/06 - Fourniture d’énergie ou d’eau

Abrégé

A method of evaluating one or more aspects of a low carbon ammonia production facility uses a digital twin implemented on a computer system. The digital twin includes a low carbon energy source component and one or more of: a hydrogen source component, a nitrogen source component, and an ammonia synthesis loop component.

Classes IPC  ?

• C01C 1/04 - Préparation d'ammoniac par synthèse
• G05B 17/02 - Systèmes impliquant l'usage de modèles ou de simulateurs desdits systèmes électriques
• G05B 24/02 - Systèmes de commande automatique à boucle ouverte non prévus ailleurs électriques
• G06N 5/022 - Ingénierie de la connaissanceAcquisition de la connaissance
• G06Q 10/04 - Prévision ou optimisation spécialement adaptées à des fins administratives ou de gestion, p. ex. programmation linéaire ou "problème d’optimisation des stocks"
• G05B 15/02 - Systèmes commandés par un calculateur électriques
• G06N 3/08 - Méthodes d'apprentissage

Abrégé

A system for processing a selected feedstock using a catalyst includes a reactor, a catalyst recovery system, and a conduit. The reactor receives the catalyst and the selected feedstock. A reaction between the selected feedstock and the catalyst generates a spent catalyst. The catalyst recovery system processes the spent catalyst. The conduit connects the reactor to the catalyst recovery system and has a lateral section. The spent catalyst flows from the reactor through a flow space defined by an inner wall of the lateral section to the catalyst recovery system. The system also includes a fluidizer positioned at the lateral section. The fluidizer includes at least one nozzle. The at least one nozzle is completely inside the flow space. The at least one nozzle forms and directs a jet of a fluidizing agent into the spent catalyst in the lateral section.

Classes IPC  ?

• B01J 8/00 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés
• B01J 38/00 - Régénération ou réactivation des catalyseurs, en général

Abrégé

A system for processing a selected feedstock using a catalyst includes a reactor, a catalyst recovery system, and a conduit. The reactor receives the catalyst and the selected feedstock. A reaction between the selected feedstock and the catalyst generates a spent catalyst. The catalyst recovery system processes the spent catalyst. The conduit connects the reactor to the catalyst recovery system and has a lateral section. The spent catalyst flows from the reactor through a flow space defined by an inner wall of the lateral section to the catalyst recovery system. The system also includes a fluidizer positioned at the lateral section. The fluidizer includes at least one nozzle. The at least one nozzle is completely inside the flow space. The at least one nozzle forms and directs a jet of a fluidizing agent into the spent catalyst in the lateral section.

Classes IPC  ?

• C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"
• B01J 8/18 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées
• B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération

Abrégé

7 aromatic rich hydrocarbons that is recycled and mixed with quench water going to the quench water separator drum to assist in removing tar molecules out of the quench water.

Classes IPC  ?

• C10G 53/04 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en série comprenant au moins une étape d'extraction

Abrégé

Advanced control and related methods for a low carbon ammonia facility having an ammonia synthesis loop that includes systems to carry out the steps of supplying energy to the facility, wherein at least a portion of the supplied energy is from a low carbon energy source, receiving a forecasted energy profile for the low carbon energy source over a time period, predicting, using an advanced regulatory controller (ARC), the operating conditions of the facility based on the forecasted energy profile for the low carbon energy source, generating, by the ARC, one or more set points to control the facility; controlling the generating of the hydrogen feed using the ARC; and producing ammonia by feeding the generated hydrogen feed to the ammonia synthesis loop in accordance with one or more set points generated by the ARC.

Classes IPC  ?

• H02J 3/00 - Circuits pour réseaux principaux ou de distribution, à courant alternatif
• H02J 3/38 - Dispositions pour l’alimentation en parallèle d’un seul réseau, par plusieurs générateurs, convertisseurs ou transformateurs

Abrégé

Advanced control and related methods for a low carbon ammonia facility having an ammonia synthesis loop that includes systems to carry out the steps of supplying energy to the facility, wherein at least a portion of the supplied energy is from a low carbon energy source, receiving a forecasted energy profile for the low carbon energy source over a time period, predicting, using an advanced regulatory controller (ARC), the operating conditions of the facility based on the forecasted energy profile for the low carbon energy source, generating, by the ARC, one or more set points to control the facility; controlling the generating of the hydrogen feed using the ARC; and producing ammonia by feeding the generated hydrogen feed to the ammonia synthesis loop in accordance with one or more set points generated by the ARC.

Classes IPC  ?

• C01C 1/02 - Préparation ou séparation d'ammoniac
• C01C 1/04 - Préparation d'ammoniac par synthèse

Produits et services

Construction project management services; construction project management services in the field of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; construction project management services in the field of reducing carbon dioxide emissions. Consulting services for others in the field of design, planning, and implementation project management of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; engineering services in the field of reducing carbon dioxide emissions; measurement and verification of carbon dioxide and other greenhouse gas emission offsets; research in the reduction of carbon emissions.

Abrégé

Methods and systems for alkylate production involving a multi-zone alkylation reactor. The multi-zone alkylation reactor includes a plurality of alkylation zones spaced vertically in a series configuration and a partition splitting the plurality of alkylation zones into at least two mechanically separated catalytic volumes.

Classes IPC  ?

• B01J 8/04 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes le fluide passant successivement à travers plusieurs lits
• C07C 2/54 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un plus petit nombre d'atomes de carbone par addition d'hydrocarbures non saturés à des hydrocarbures saturés, ou à des hydrocarbures contenant un cycle aromatique à six chaînons ne comportant pas d'autre insaturation que celle du cycle aromatique
• C07C 2/56 - Addition à des hydrocarbures acycliques
• C07C 2/58 - Procédés catalytiques
• C07C 2/76 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un plus petit nombre d'atomes de carbone par condensation d'hydrocarbures avec élimination partielle d'hydrogène

Abrégé

7 rich bottoms stream are directed to a dimerizer where the CPD is thermally dimerized to dicyclopentadiene (DCPD). DCPD is more stable than CPD and thus safer to handle.

Classes IPC  ?

• C07C 2/38 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un plus petit nombre d'atomes de carbone par addition d'hydrocarbures non saturés entre eux par oligomérisation d'hydrocarbures non saturés bien définis, sans formation de cycle de diènes ou d'alcynes
• B01J 19/00 - Procédés chimiques, physiques ou physico-chimiques en généralAppareils appropriés
• C07C 7/04 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par distillation
• C07C 13/61 - Indènes pontés, p. ex. dicyclopentadiène

Abrégé

A method of estimating a carbon emission lifecycle footprint of an infrastructure project includes compiling a rules set that include carbon emission rules and engineering rules, wherein each carbon emission rule and each engineering rule represent a predetermined decision; encoding the rules set in a database; obtaining non-project specific information from suppliers and manufacturers; storing non-project specific information in the database; obtaining project specific information for the energy project; conveying the project specific information via a user interface to the database; generating deliverables using at least the rules set, the non-project specific information, and the project specific information; using the deliverables to estimate the carbon emission lifecycle footprint of the project; and using the workshop and interactive engineering facility to deliver a lower overall carbon emission footprint of the infrastructure project.

Classes IPC  ?

• G06Q 10/063 - Recherche, analyse ou gestion opérationnelles
• G06Q 10/10 - BureautiqueGestion du temps
• G06Q 50/06 - Fourniture d’énergie ou d’eau
• G06Q 50/08 - Construction

Produits et services

Engineering services relating to the treatment of materials, namely, hydrometallurgical extraction of battery metals

Produits et services

(1) Construction project management services; construction project management services in the field of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; construction project management services in the field of reducing carbon dioxide emissions. (2) Consulting services for others in the field of design, planning, and implementation project management of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; engineering services in the field of reducing carbon dioxide emissions; measurement and verification of carbon dioxide and other greenhouse gas emission offsets; research in the reduction of carbon emissions.

Abrégé

Low carbon dioxide-emitting processes and systems for steam cracking hydrocarbons to produce products such as ethylene are described. The processes and systems involve cracking the feed in a furnace that is configured to burn a hydrogen-rich fuel, which produces less carbon dioxide than methane, which is typically used as fuel for such furnaces. The hydrogen-rich stream can be isolated and recycled from the cracker tail gas.

Classes IPC  ?

• C07C 4/04 - Procédés thermiques

Abrégé

Low carbon dioxide-emitting processes and systems for steam cracking hydrocarbons to produce products such as ethylene are described. The processes and systems involve cracking the feed in a furnace that is configured to burn a hydrogen-rich fuel, which produces less carbon dioxide than methane, which is typically used as fuel for such furnaces. The hydrogen-rich stream can be isolated and recycled from the cracker tail gas.

Classes IPC  ?

• C07C 4/04 - Procédés thermiques

Abrégé

Low carbon dioxide-emitting processes and systems for steam cracking hydrocarbons to produce products such as ethylene are described. The processes and systems involve cracking the feed in a furnace that is configured to burn a hydrogen-rich fuel, which produces less carbon dioxide than methane, which is typically used as fuel for such furnaces. The hydrogen-rich stream can be isolated and recycled from the cracker tail gas.

Classes IPC  ?

• C07C 4/04 - Procédés thermiques

Produits et services

Consulting services in the field of design and development of engineering processes; engineering design services; engineering services in the field of energy efficiency; engineering services in the field of hydrogen production.

Produits et services

(1) Fuels; aviation fuel; hydrocarbon fuels; non-chemical additives for fuels. (1) Providing fuel business management services in the field of aviation. (2) Fuel treatment services; processing of fuel materials; production, treatment and refinement of fuel, diesel fuel, biofuel and biodiesel fuel for others. (3) Engineering services in the field of reducing fuel consumption; technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels.

Abrégé

A process of dissociating ammonia into a dissociated hydrogen/nitrogen stream in catalyst tubes within a radiant tube furnace and an adiabatic or isothermal unit containing catalyst, along with downstream purification process units to purify the dissociated hydrogen/nitrogen stream into high purity hydrogen product.

Classes IPC  ?

• C01B 3/04 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés inorganiques, p. ex. de l'ammoniac
• B01J 19/24 - Réacteurs fixes sans élément interne mobile
• B01J 15/00 - Procédés chimiques généraux faisant réagir des milieux gazeux avec des solides non particulaires, p. ex. des matériaux en feuillesAppareillage spécialement adapté à cet effet
• B01J 19/00 - Procédés chimiques, physiques ou physico-chimiques en généralAppareils appropriés
• B01D 3/32 - Autres caractéristiques de colonnes de fractionnement
• B01D 3/00 - Distillation ou procédés d'échange apparentés dans lesquels des liquides sont en contact avec des milieux gazeux, p. ex. extraction
• B01D 53/14 - Séparation de gaz ou de vapeursRécupération de vapeurs de solvants volatils dans les gazÉpuration chimique ou biologique des gaz résiduaires, p. ex. gaz d'échappement des moteurs à combustion, fumées, vapeurs, gaz de combustion ou aérosols par absorption
• B01D 53/18 - Unités d'absorptionDistributeurs de liquides

Abrégé

Processes and systems for fluid catalytic cracking (FCC) of hydrocarbon feeds using a multiple riser FCC reactor are described. The conditions in each riser can be tailored for handling a different feed. For example, one riser may be configured to crack heavy hydrocarbons, such as vacuum gas oil (VGO) to yield medium and light products. Other risers may be configured to crack low and/or medium hydrocarbons to yield light olefins. Embodiments of the disclosed processes and systems may be used to provide a product spectrum that has greater amounts of light olefins.

Classes IPC  ?

• C10G 11/05 - Alumino-silicates cristallins, p. ex. tamis moléculaires
• C10G 51/04 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, uniquement par plusieurs procédés de craquage uniquement par plusieurs étapes en série ne comprenant que des étapes de craquage thermique et catalytique

Abrégé

Processes and systems for fluid catalytic cracking (FCC) of hydrocarbon feeds using a multiple riser FCC reactor are described. The conditions in each riser can be tailored for handling a different feed. For example, one riser may be configured to crack heavy hydrocarbons, such as vacuum gas oil (VGO) to yield medium and light products. Other risers may be configured to crack low and/or medium hydrocarbons to yield light olefins. Embodiments of the disclosed processes and systems may be used to provide a product spectrum that has greater amounts of light olefins.

Classes IPC  ?

• C10G 11/05 - Alumino-silicates cristallins, p. ex. tamis moléculaires
• B01D 3/14 - Distillation fractionnée

Abrégé

A process of dissociating ammonia into a dissociated hydrogen/nitrogen stream in catalyst tubes within a radiant tube furnace and an adiabatic or isothermal unit containing catalyst, along with downstream purification process units to purify the dissociated hydrogen/nitrogen stream into high purity hydrogen product.

Classes IPC  ?

• C01B 3/04 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés inorganiques, p. ex. de l'ammoniac
• B01J 19/14 - Production de mélanges de gaz inertesUtilisation des gaz inertes en général
• C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification

Produits et services

Fuels; Aviation fuel; Hydrocarbon fuels; Non-chemical additives for fuels

Produits et services

Engineering services, namely, engineering for the design of steam cracking-based ethylene production processes combining a furnace and recovery section process; engineering services in the field of reducing emissions in ethylene production.

Produits et services

(1) Consulting services in the field of design and development of engineering processes; engineering design services; engineering services in the field of energy efficiency; engineering services in the field of hydrogen production.

Abrégé

A reactor system and method for catalytic dehydrogenation of saturated C3-C6 hydrocarbons within a reactor placed within a reactor disengager, where the reactor is open at the bottom thereof and open to the disengager, and the exit riser from the reactor is not hard coupled to at least one downstream cyclone. This configuration permits controlling the amount of catalyst within the reactor by varying the level of catalyst in the reactor disengager outside the reactor and permits controlling total catalyst hold-up and/or weight hourly space velocity (WHSV) independently from catalyst flow from the catalyst regenerator.

Classes IPC  ?

• B01J 8/24 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé"
• B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération
• B01J 38/04 - Traitement avec un gaz ou une vapeurTraitement avec des liquides vaporisables au contact du catalyseur épuisé
• C07C 5/327 - Formation de liaisons doubles carbone-carbone uniquement non aromatiques
• C07C 5/333 - Procédés catalytiques

Abrégé

Methods and systems for treating an olefin-containing stream are disclosed. The disclosed methods and systems are particularly suitable for treating an off-gas stream in a refining or petrochemical process, such as from a fluid catalytic cracker (FCC), coker, steam cracker, and the like. The stream is treated in an absorber column to reject lighter stream components and to absorb ethylene and/or propylene into a solvent. The solvent is typically isobutane. The enriched solvent stream from the absorber column is fed to an alkylation reactor, which reacts the dissolved olefin with the isobutane solvent to produce an alkylate product.

Classes IPC  ?

• C07C 7/11 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par absorption, c.-à-d. purification ou séparation d'hydrocarbures gazeux à l'aide de liquides
• C07C 2/12 - Procédés catalytiques avec des alumino-silicates cristallins, p. ex. avec des tamis moléculaires
• C07C 7/00 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs
• C07C 7/09 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par condensation fractionnée
• B01J 8/02 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules immobiles, p. ex. dans des lits fixes
• B01D 53/14 - Séparation de gaz ou de vapeursRécupération de vapeurs de solvants volatils dans les gazÉpuration chimique ou biologique des gaz résiduaires, p. ex. gaz d'échappement des moteurs à combustion, fumées, vapeurs, gaz de combustion ou aérosols par absorption
• B01D 53/18 - Unités d'absorptionDistributeurs de liquides

Abrégé

A reactor system and method for catalytic dehydrogenation of saturated C3-C6 hydrocarbons within a reactor placed within a reactor disengager, where the reactor is open at the bottom thereof and open to the disengager, and the exit riser from the reactor is not hard coupled to at least one downstream cyclone. This configuration permits controlling the amount of catalyst within the reactor by varying the level of catalyst in the reactor disengager outside the reactor and permits controlling total catalyst hold-up and/or weight hourly space velocity (WHSV) independently from catalyst flow from the catalyst regenerator.

Classes IPC  ?

• B01J 8/00 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés
• B01J 8/18 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées
• C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"

Abrégé

A reactor system and method for catalytic dehydrogenation of saturated C3-C6 hydrocarbons within a reactor placed within a reactor disengager, where the reactor is open at the bottom thereof and open to the disengager, and the exit riser from the reactor is not hard coupled to at least one downstream cyclone. This configuration permits controlling the amount of catalyst within the reactor by varying the level of catalyst in the reactor disengager outside the reactor and permits controlling total catalyst hold-up and/or weight hourly space velocity (WHSV) independently from catalyst flow from the catalyst regenerator.

Classes IPC  ?

• B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération
• C07C 5/333 - Procédés catalytiques
• B01J 38/04 - Traitement avec un gaz ou une vapeurTraitement avec des liquides vaporisables au contact du catalyseur épuisé
• C07C 5/327 - Formation de liaisons doubles carbone-carbone uniquement non aromatiques
• B01J 8/24 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé"

Abrégé

Carbon capture of carbon dioxide (CO2) gives an extracted CO2 stream that is reacted with hydrogen to produce methanol (MeOH), which can in turn be fed to catalytic production of olefins such as ethylene and propylene to give an integrated process.

Classes IPC  ?

• C01B 3/34 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants
• C07C 1/12 - Préparation d'hydrocarbures à partir d'un ou plusieurs composés, aucun d'eux n'étant un hydrocarbure à partir d'oxydes de carbone à partir d'anhydride carbonique avec de l'hydrogène

Abrégé

222 stream that is reacted with hydrogen to produce methanol (MeOH), which can in turn be fed to catalytic production of olefins such as ethylene and propylene to give an integrated process.

Classes IPC  ?

• B01D 53/02 - Séparation de gaz ou de vapeursRécupération de vapeurs de solvants volatils dans les gazÉpuration chimique ou biologique des gaz résiduaires, p. ex. gaz d'échappement des moteurs à combustion, fumées, vapeurs, gaz de combustion ou aérosols par adsorption, p. ex. chromatographie préparatoire en phase gazeuse
• B01D 53/34 - Épuration chimique ou biologique des gaz résiduaires
• B01D 53/73 - Post-traitement des composants éliminés

Produits et services

Consulting in the field of engineering; Electrical engineering; Engineering design services; Engineering drawing services; Engineering services, namely, engineering for the design and construction of facilities to store electricity; Technology advisory services related to civil engineering and construction

Produits et services

Consultancy in the field of artificial intelligence technology; Providing temporary use of on-line non-downloadable software and applications using artificial intelligence for engineering and design of processes and facilities in the utility, industrial, transportation, building, mining, commercial, aerospace, power, defense and government industries; Research in the field of artificial intelligence technology; Software as a service (SAAS) services featuring software using artificial intelligence for engineering and design of processes and facilities in the ammonia, aviation, biofuel, carbon capture, carbon storage, chemical, coal gasification, coal monetization, fertilizer, gas, gas-to-liquids, hydrogen, liquified natural gas, manufacturing, minerals, mining, oil, olefins, organic chemical, paper, petrochemical, pipeline, power generation, power transmission, pulp, refining, renewable energy, synthesis gas, transportation, water supply and wastewater handling industries

Abrégé

A paraffin having 2-8 carbon atoms may be dehydrogenated by contacting the paraffin with metal oxide catalyst(s) to produce light olefins, such as propylene, under certain reaction conditions in a riser, fluidized bed, or fixed-bed swing reactor. The resulting metal oxide catalyst fines contained in the reactor effluent stream formed by the dehydrogenation reaction may be recovered by contacting the reactor effluent stream with a wash fluid to form a catalyst effluent stream that is subsequently slurried and filtered to capture the catalyst fines for potential reuse.

Classes IPC  ?

• C07C 5/32 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant le même nombre d'atomes de carbone par déshydrogénation avec formation d'hydrogène libre
• C07C 5/327 - Formation de liaisons doubles carbone-carbone uniquement non aromatiques
• B01J 23/54 - Catalyseurs contenant des métaux, oxydes ou hydroxydes métalliques non prévus dans le groupe des métaux nobles en combinaison avec des métaux, oxydes ou hydroxydes prévus dans les groupes
• C07C 5/333 - Procédés catalytiques

Abrégé

A method of designing a plastic recycling facility at a selected site includes representing each selected component of the plastic recycling facility a module defined by information relating to at least one of a carbon emission or a cost. The method also includes storing the information represented each module in a database accessible by a processor; programming the processor with a set of engineering rules, wherein each engineering rule is configured to represent a predetermined design decision relating to at least a design of the plastic recycling facility; and generating deliverables using at least the set of engineering rules and the modules. The deliverables may include at least: a cost estimate for the plastic recycling facility, and a carbon emission estimate for the plastic recycling facility.

Classes IPC  ?

• G06Q 10/08 - Logistique, p. ex. entreposage, chargement ou distributionGestion d’inventaires ou de stocks
• G06Q 10/30 - Administration du recyclage ou de l’élimination des produits
• G06Q 50/04 - Fabrication

Abrégé

A method of designing a plastic recycling facility at a selected site includes representing each selected component of the plastic recycling facility a module defined by information relating to at least one of a carbon emission or a cost. The method also includes storing the information represented each module in a database accessible by a processor; programming the processor with a set of engineering rules, wherein each engineering rule is configured to represent a predetermined design decision relating to at least a design of the plastic recycling facility; and generating deliverables using at least the set of engineering rules and the modules. The deliverables may include at least: a cost estimate for the plastic recycling facility, and a carbon emission estimate for the plastic recycling facility.

Classes IPC  ?

• G06Q 10/30 - Administration du recyclage ou de l’élimination des produits
• G06Q 30/018 - Certification d’entreprises ou de produits
• G06Q 30/0283 - Estimation ou détermination de prix

Abrégé

A method of designing a plastic recycling facility at a selected site includes representing each selected component of the plastic recycling facility a module defined by information relating to at least one of a carbon emission or a cost. The method also includes storing the information represented each module in a database accessible by a processor; programming the processor with a set of engineering rules, wherein each engineering rule is configured to represent a predetermined design decision relating to at least a design of the plastic recycling facility; and generating deliverables using at least the set of engineering rules and the modules. The deliverables may include at least: a cost estimate for the plastic recycling facility, and a carbon emission estimate for the plastic recycling facility.

Classes IPC  ?

• G06Q 10/30 - Administration du recyclage ou de l’élimination des produits
• G06Q 50/04 - Fabrication
• G06Q 10/08 - Logistique, p. ex. entreposage, chargement ou distributionGestion d’inventaires ou de stocks

Produits et services

Construction project management services; Construction project management services in the field of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; Construction project management services in the field of reducing carbon dioxide emissions Consulting services for others in the field of design, planning, and implementation project management of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; Engineering services in the field of reducing carbon dioxide emissions; Measurement and verification of carbon dioxide and other greenhouse gas emission offsets; Research in the reduction of carbon emissions

Produits et services

Consulting services in the field of design and development of engineering processes; Engineering design services; Engineering services in the field of energy efficiency; Engineering services in the field of hydrogen production

Abrégé

The present invention relates to debottleneck solution for delayed Coker unit. More particularly, this invention relates to bottoms of vacuum residuum routed to Coker unit through de-asphalting unit to avoid revamp of existing Coker for the processing of heavier feed stock when there is a change in crude slate. Another object of the invention, in particular, relates to improved delayed coking products, a process used in petroleum refineries to crack petroleum residue, thus converting it into gaseous and liquid product streams and leaving behind solid, carbonaceous petroleum coke.

Classes IPC  ?

• C10G 9/00 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures
• C10B 55/00 - Cokéfaction des huiles minérales, bitumes, goudrons ou analogues, ou de leurs mélanges, avec des matières carbonées solides
• C10B 57/04 - Autres procédés de carbonisation ou de cokéfactionCaractéristiques générales des procédés de distillation destructive utilisant des charges de composition spéciale
• C10G 7/00 - Distillation des huiles d'hydrocarbures
• C10G 21/00 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par extraction au moyen de solvants sélectifs
• C10G 55/04 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par au moins un procédé de raffinage et par au moins un procédé de craquage uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique

Produits et services

Fuel treatment services; Processing of fuel materials; Production, treatment and refinement of fuel, diesel fuel, biofuel and biodiesel fuel for others Providing fuel management services in the field of aviation Engineering services in the field of reducing fuel consumption; Technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels

Abrégé

A system for processing a hydrocarbon feed has a final stage reactor and internal separator with cyclone that forms a substantially gas stream and a substantially non-gas stream. The substantially gas stream is sent directly from the final stage reactor and separator to further downstream processing.

Classes IPC  ?

• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• B01J 8/00 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés
• B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"

Abrégé

A method for purifying cumene may include splitting an alkylation reaction product into a first portion and a second portion; feeding the first portion as mostly a liquid into a benzene column; at least partially vaporizing the second portion in a heater; feeding the at least partially vaporized second portion into the benzene column. A method for purifying cumene may also include the steps of providing a benzene column and a cumene column; directing a liquid side draw from the benzene column to the cumene column, the liquid side draw being a liquid substantially free of DIPB; returning a benzene enriched vapor from the cumene column to the benzene column using an overhead line, the benzene enriched vapor having a higher concentration of benzene than the liquid side draw; and drawing purified cumene from the cumene column.

Classes IPC  ?

• C07C 15/085 - Isopropylbenzène
• C07C 15/02 - Hydrocarbures monocycliques
• C07C 6/12 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un nombre différent d'atomes de carbone par des réactions de redistribution par conversion d'une liaison carbone-carbone saturée exclusivement dans les hydrocarbures contenant un cycle aromatique à six chaînons

Abrégé

A method for purifying cumene may include splitting an alkylation reaction product into a first portion and a second portion; feeding the first portion as mostly a liquid into a benzene column; at least partially vaporizing the second portion in a heater; feeding the at least partially vaporized second portion into the benzene column. A method for purifying cumene may also include the steps of providing a benzene column and a cumene column; directing a liquid side draw from the benzene column to the cumene column, the liquid side draw being a liquid substantially free of DIPB; returning a benzene enriched vapor from the cumene column to the benzene column using an overhead line, the benzene enriched vapor having a higher concentration of benzene than the liquid side draw; and drawing purified cumene from the cumene column.

Classes IPC  ?

• C07C 7/05 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par distillation à l'aide de composés auxiliaires

Produits et services

Providing educational mentoring services and programs in the field of sustainability and environmental protection; Providing science educational mentoring services and programs.

Produits et services

Engineering services, namely, engineering for the design of steam cracking-based ethylene production processes combining a furnace and recovery section process; Engineering services in the field of reducing emissions in ethylene production

Produits et services

Chemical engineering, namely, design and production of methane carboxylic acid (acetic acid) from methanol and carbon monoxide; Engineering design services for the production of methane carboxylic acid (acetic acid) from methanol and carbon monoxide

Abrégé

An offshore platform has a hull, a ballast system, and at least one enclosed deck. The hull has a vertical axis and at least one perimeter defining a boundary between an interior and an exterior of the hull. The hull includes at least one set of planar walls that are symmetrically disposed about the vertical axis. The at least one set of planar walls at least partially define a rectilinear shape for the at least one perimeter. The planar walls have substantially the same width dimension. The ballast system has at least one compartment positioned within the at least one perimeter and a fluid mover configured to control a flow of water into the at least one compartment. The at least one enclosed deck is positioned inside the hull. The at least one compartment separates the at least one enclosed deck and the at least one perimeter.

Classes IPC  ?

• B63B 35/44 - Constructions, magasins, plates-formes de forage ou ateliers flottants, p. ex. portant des appareils séparateurs huile-eau

Abrégé

A dividing wall column is used in an alkylation process flow scheme to fractionate an alkylate reactor effluent to produce an iso-butane-rich stream as a recycle feed for the alkylation reactor while also separating iso-butane, normal butane and alkylate as separate product streams depending on the reactor effluent composition. In an optional embodiment, the scheme may contain propane.

Classes IPC  ?

• C07C 2/62 - Procédés catalytiques avec des acides
• B01D 3/14 - Distillation fractionnée
• B01D 3/00 - Distillation ou procédés d'échange apparentés dans lesquels des liquides sont en contact avec des milieux gazeux, p. ex. extraction
• C07C 2/58 - Procédés catalytiques
• C07C 7/04 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par distillation

Abrégé

A desolidification process enables the isolation and extraction of solid additives from an unreacted petroleum residue stream. In a hydrocracking process that mixes a solid additive with a petroleum residue feedstock to convert the petroleum residue to higher-value distillates, the desolidification process enables the recovery of the unreacted petroleum residue for conversion to a saleable product. The desolidification process involves the mixture of one or more solvents with a slurry in which solids are integrated in the petroleum residue to generate a mixture having a decreased density and viscosity as compared to the slurry, which facilitates removal of the solids.

Classes IPC  ?

• C10G 67/04 - Traitement des huiles d'hydrocarbures, uniquement par au moins un procédé d'hydrotraitement et au moins un procédé de raffinage en l'absence d'hydrogène uniquement par plusieurs étapes en série comprenant une extraction par solvant comme étape de raffinage en l'absence d'hydrogène
• C10G 67/14 - Traitement des huiles d'hydrocarbures, uniquement par au moins un procédé d'hydrotraitement et au moins un procédé de raffinage en l'absence d'hydrogène uniquement par plusieurs étapes en série comprenant au moins deux étapes de raffinage différentes, en l'absence d'hydrogène
• C10G 49/22 - Séparation des effluents
• B01D 3/14 - Distillation fractionnée
• B01D 3/10 - Distillation sous vide
• B01D 11/04 - Extraction par solvants de solutions
• C10G 49/10 - Traitement des huiles d'hydrocarbures, en présence d'hydrogène ou de composés donneurs d'hydrogène, non prévu dans un seul des groupes , , , ou avec des particules solides en mouvement

Abrégé

A method of designing a charging station to charge electric vehicles at a selected site includes the steps of compiling a set of engineering rules; encoding the set of engineering rules in a processor; obtaining non-site specific information from suppliers and manufactures; storing non-site specific information in a database; obtaining site specific information for the selected site; conveying the site specific information via a user interface to the database; generating deliverables using at least the set of engineering rules, the non-site specific information and the site specific information; and sending the deliverables to an end user. Each engineering rule represents a predetermined design decision.

Classes IPC  ?

• B60L 53/30 - Détails de construction des stations de charge
• G06F 30/13 - Conception architecturale, p. ex. conception architecturale assistée par ordinateur [CAAO] relative à la conception de bâtiments, de ponts, de paysages, d’usines ou de routes
• G06F 30/20 - Optimisation, vérification ou simulation de l’objet conçu

Abrégé

A method of designing a charging station to charge electric vehicles at a selected site includes the steps of compiling a set of engineering rules; encoding the set of engineering rules in a processor: obtaining non-site specific information from suppliers and manufactures; storing non-site specific information in a database; obtaining site specific information for the selected site; conveying the site specific information via a user interface to the database; generating deliverables using at least the set of engineering rules, the non-site specific information and the site specific information; and sending the deliverables to an end user. Each engineering rule represents a predetermined design decision.

Classes IPC  ?

• B60L 53/62 - Surveillance et commande des stations de charge en réponse à des paramètres de charge, p. ex. courant, tension ou charge électrique
• B60L 53/67 - Commande de plusieurs stations de charge
• B60L 53/64 - Optimisation des coûts énergétiques, p. ex. en répondant aux tarifs d'électricité

Abrégé

A method of designing a charging station to charge electric vehicles at a selected site includes the steps of compiling a set of engineering rules; encoding the set of engineering rules in a processor; obtaining non-site specific information from suppliers and manufactures; storing non-site specific information in a database; obtaining site specific information for the selected site; conveying the site specific information via a user interface to the database; generating deliverables using at least the set of engineering rules, the non-site specific information and the site specific information; and sending the deliverables to an end user. Each engineering rule represents a predetermined design decision.

Classes IPC  ?

• B60L 53/30 - Détails de construction des stations de charge
• G06F 30/13 - Conception architecturale, p. ex. conception architecturale assistée par ordinateur [CAAO] relative à la conception de bâtiments, de ponts, de paysages, d’usines ou de routes
• G06F 30/20 - Optimisation, vérification ou simulation de l’objet conçu

Produits et services

Engineering design services; Engineering services, namely, engineering for the maleic anhydride technology industry; Technology advisory services related to maleic anhydride and ethylene production processes

Produits et services

Engineering design services; Engineering services, namely, engineering for the ethylene oxide and ethylene glycol industry; Technology advisory services related to ethylene oxide and ethylene glycol production processes