A method comprising partially condensing and separating a feed stream comprising helium and hydrogen to produce a first medium-pressure vapor stream and a first medium-pressure liquid stream; reducing the pressure of the first medium-pressure liquid stream or a stream derived from the first medium-pressure liquid stream to produce a low-pressure vapor stream and a low-pressure liquid stream; cooling the first medium-pressure vapor stream by indirect heat exchange against the low-pressure liquid stream to produce a first partially condensed medium-pressure stream; and separating the first partially condensed medium-pressure stream to produce a second medium-pressure vapor stream and a second medium-pressure liquid stream.
A method of operating a hydrogen supply network responsive to carbon intensity (CI) requirements comprising: determining the CI for hydrogen produced at the hydrogen production facilities; determining a network flow solution for the hydrogen supply network, the network flow solution defining a network solution space specifying a range of values for production rates of the hydrogen production facilities and a range of values of delivery rates for the hydrogen delivery points which satisfy predefined operational constraints of the hydrogen supply network; allocating production rates from the hydrogen production facilities to each of the plurality of delivery points based on predetermined criteria associated with the delivery points to define an allocation mapping for the hydrogen supply network; generating control variables for controlling the production rates of each of the hydrogen production facilities; and controlling the hydrogen production facilities in accordance with the determined control variables.
G05B 19/4155 - Commande numérique [CN], c.-à-d. machines fonctionnant automatiquement, en particulier machines-outils, p. ex. dans un milieu de fabrication industriel, afin d'effectuer un positionnement, un mouvement ou des actions coordonnées au moyen de données d'un programme sous forme numérique caractérisée par le déroulement du programme, c.-à-d. le déroulement d'un programme de pièce ou le déroulement d'une fonction machine, p. ex. choix d'un programme
3.
System and Method for Combusting High-Moisture Fuel to Generate Steam
A process for combusting a high-moisture fuel to generate steam in which the high-moisture solid fuel is first dried by contacting with an oxygen-depleted gas stream while being heated by indirect heat exchange with a recirculating thermal fluid. The dried fuel is then combusted with a combustion air stream to produce a combustion products stream whose heat first is used to generate steam, and then to preheat the combustion air stream by indirect heat exchange in which a portion of the combustion air stream and/or a portion of the combustion products stream bypasses the heat exchanger. The combustion products stream also provides heat to dry the solid fuel via the recirculating thermal fluid.
A method comprising: heating a refractory surface in a combustion chamber to produce a heated refractory surface; contacting a stream comprising ammonia with the heated refractory surface to dissociate at least a portion of the ammonia to form nitrogen and hydrogen and produce an at least partially dissociated ammonia stream; and combusting the at least partially dissociated ammonia stream with a primary oxidant to produce an at least partially combusted ammonia stream.
A method of operating a hydrogen production facility to meet carbon intensity (CI) requirements, the method comprising: receiving operational parameter data from the hydrogen production facility, the operational parameter data being representative of measured and/or determined time-dependent values of operational parameters of the hydrogen production facility; processing the operational parameter data to define one or more linear terms, wherein the linear terms are linear with respect to one or more CI reference models; generating, from the linear terms, control system CI values representative of the CI of hydrogen produced by the hydrogen production facility; generating control variables for controlling one or more operational parameters of the hydrogen production facility; and controlling the hydrogen production facility in accordance with the determined control variables.
In a process in which ammonia is cracked to form a hydrogen gas product and an offgas comprising nitrogen gas, residual hydrogen gas and residual ammonia gas, residual ammonia is recovered from the offgas from the hydrogen recovery process by partial condensation and phase separation, and hydrogen is recovered from the resultant ammonia-lean offgas by partial condensation and phase separation. The recovered ammonia may be recycled the cracking process and the recovered hydrogen may be recycled to the hydrogen recovery process to improve hydrogen recovery from the cracked gas. Overall hydrogen recovery from the ammonia may thereby be increased to over 99%.
C01B 3/04 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés inorganiques, p. ex. de l'ammoniac
B01D 53/00 - 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
B01D 53/04 - 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 avec adsorbants fixes
B01J 3/04 - Récipients sous pression, p. ex. autoclaves
C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
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
7.
APPARATUS AND PROCESS FOR PROVIDING NITROGEN AND OXYGEN
An apparatus and process for providing nitrogen and oxygen can include a multicolumn tower that includes a lower pressure column (LP) positioned in alignment with an intermediate pressure (MP) column. At least one of these columns and at least one higher pressure (HP) column can receive air from a feed intake system. Embodiments can be adapted so that the diameter of the LP and MP columns are similar, if not the same so that the columns can be aligned with each other in the tower. Embodiments can be adapted to allow for high purity nitrogen recovery from at least one HP column while also obtaining at least one oxygen stream from the LP column with equipment that has an overall lower height, or length, that can be easier to fabricate and install.
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
8.
METHOD AND APARATUS FOR DIRECT ENERGY DEPOSITION OF METAL
A method for direct energy deposition comprising: (f) moving a tool head and/or a metal structure one relative to the other so that the tool head moves relative to the metal structure in an advance direction on a deposition path along the metal structure; (g) directing energy to an energy input location of the metal structure to create a melt-pool that moves in the advance direction along the deposition path; (h) supplying a feedstock metal from the tool head in a discharge direction directed toward the advancing melt-pool to deposit a new layer of metal on the structure; and (i) directing one or more cryogenic coolant jets of cryogenic fluid with a directional component counter to the advance direction towards the new layer so that the cryogenic fluid impinges on the new layer in a coolant impingement region trailing the melt-pool in the advance direction.
An apparatus and process for drying a product gas for feeding the gas to a downstream user so that product gas can be dried to remove water from the gas that may be absorbed or adsorbed during an initial start-up phase of the product gas production and/or delivery (e.g. from conduits that may have been exposed to water during installation) so the product gas can be passed downstream to the user instead of being vented. Some embodiments can be configured to utilize a removable, mobile water redistribution device that can be transported to a new site after an initial start-up phase of product gas delivery is completed and the product gas providing conduit arrangement has been dried via operation for an initial start-up period of time.
B01D 53/04 - 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 avec adsorbants fixes
B01D 53/28 - Emploi de substances spécifiées comme agents desséchants
e.g.e.g., methane or hydrogen, by separating the gaseous mixture into a carbon dioxide-enriched gas and a second gas-enriched fluid, compressing the carbon dioxide-enriched gas, cooling and partially condensing the compressed gas, phase separating the partially condensed fluid, reducing the pressure of the crude carbon dioxide liquid and distilling the reduced pressure liquid to produce liquid carbon dioxide product. Costs may be reduced and efficiency improved by using the vaporous products from the phase separation and distillation to help cool and partially condense the compressed gas.
Liquid carbon dioxide is produced from a gaseous mixture comprising carbon dioxide and methane by separating the gaseous mixture into a carbon dioxide-enriched gas and a methane-enriched gas, compressing the carbon dioxide-enriched gas, cooling and partially condensing the compressed gas, phase separating the partially condensed fluid, reducing the pressure of the crude carbon dioxide liquid and distilling the reduced pressure liquid to produce liquid carbon dioxide product. Costs are reduced and efficiency improved by using the vaporous products from the phase separation and distillation to help cool and partially condense the compressed gas.
Disclosed herein are membrane-based gas separation methods and systems. The methods and systems may, in particular, be used for separating a feed stream comprising methane and carbon dioxide (such as for example a biogas feed stream) in order to provide a methane product stream (such as for example a biomethane stream).
B01D 53/22 - 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 diffusion
C10L 3/10 - Post-traitement de gaz naturel ou de gaz naturel de synthèse
13.
4-Stage Membrane Process with Sweep for Biogas Upgrading
Disclosed herein are membrane-based gas separation methods and systems. The methods and systems may, in particular, be used for separating a feed stream comprising methane and carbon dioxide (such as for example a biogas feed stream) in order to provide a methane product stream (such as for example a biomethane stream).
B01D 53/22 - 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 diffusion
14.
APPARATUS AND PROCESS FOR ELECTROLYTE SOLUTION PURIFICATION FOR HYDROGEN PRODUCTION VIA ELECTROLYSIS
An apparatus and process for electrolyte purification can be configured to remove iron from a solution to purify an electrolyte solution for feeding to one or more electrolyzers for use in producing hydrogen from water via electrolysis. Embodiments can utilize a reactor having an iron removing agent positioned therein such that the electrolyte solution can be passed through a vessel of the reactor for removal of iron. Other embodiments can include inclusion of an iron removing agent in a tank being agitated with water and electrolytic material (e.g. KOH material) for forming the electrolyte solution and subsequently filtering out iron containing materials included in the formed solution via the iron removing agent. Embodiments can be configured to provide an electrolyte solution having a pre-selected iron concentration to help prevent fouling of electrodes utilized in electrolysis processing.
A method for treating a water stream comprising reacting a carbonaceous feedstock with oxygen in a reactor section of a gasifier to produce a syngas stream; contacting the syngas stream with water in a quench section of the gasifier to produce a quenched syngas stream and a water bath; withdrawing a black water stream from the water bath; removing solids from at least a portion of the black water stream to produce a solids-depleted stream; and recycling at least a portion of the solids-depleted stream to the quench section.
C10J 3/84 - Moyens d'extraction des gaz avec moyens de dépoussiérage ou de dégoudronnage du gaz
C10K 1/10 - Purification des gaz combustibles contenant de l'oxyde de carbone par lavage avec des liquidesRégénération des liqueurs de lavage avec des liquides aqueux
A burner comprising a first channel surrounding a centerline and terminating in a first tip; a second channel surrounding the first channel and terminating in a second tip, the second channel comprising a convergent conical section forming a first angle with respect to the centerline; a third channel surrounding the second channel and terminating in a third tip, the third channel comprising a convergent conical section forming a second angle with respect to the centerline;wherein the third tip comprises one or more slots.
An apparatus for nitrogen generation for methanol powered maritime vehicles can include a compression system for compressing air and feeding compressed air to a separation unit for separation of nitrogen and oxygen from the compressed air. The nitrogen can be output from the separation unit for storage at an elevated pre-selected pressure suitable for feeding to a methanol engine of a maritime vehicle (e.g. a ship) for use in purging, leak testing, inerting, or other uses. Embodiments can be configured so there is no heat exchanger or booster compressor positioned between the separation unit and the nitrogen storage unit.
B01D 53/22 - 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 diffusion
B63H 21/38 - Appareils ou procédés spécialement adaptés à la manipulation de liquides pour l'appareil moteur d'un navire ou pour l'un de ses éléments, p. ex. lubrifiants, réfrigérants, carburants ou analogues
F02D 19/06 - Commande des moteurs caractérisés par l'emploi de combustible non liquide, de combustibles multiples ou de substances non combustibles ajoutées au mélange carburant particulière aux moteurs fonctionnant avec des combustibles multiples, p. ex. alternativement du fuel léger et du fuel lourd, et autres que les moteurs indifférents au combustible utilisé
F02M 37/00 - Appareils ou systèmes pour transférer le combustible liquide des réservoirs de stockage aux carburateurs ou aux injecteursDispositions d'épuration du combustible liquide spécialement conçues pour les moteurs à combustion interne ou aménagées sur ceux-ci
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
18.
REDUCING ENERGY CONSUMPTION IN NITROGEN PRODUCTION USING A TURBOEXPANDER
An air separation system using a membrane separation unit to produce a nitrogen-enriched product stream from a feed air stream is described herein. A nitrogen-enriched non-permeate stream is expanded in a turboexpander and the energy recovered during expansion is used to further compress the feed air stream prior to membrane separation. Expanded nitrogen-enriched non-permeate stream is also used to cool the compressed feed air upstream from membrane separation.
B01D 53/22 - 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 diffusion
19.
Apparatus and Method for Nitrogen Generation for Methanol Powered Maritime Vehicle
An apparatus for nitrogen generation for methanol powered maritime vehicles can include a compression system for compressing air and feeding compressed air to a separation unit for separation of nitrogen and oxygen from the compressed air. The nitrogen can be output from the separation unit for storage at an elevated pre-selected pressure suitable for feeding to a methanol engine of a maritime vehicle (e.g. a ship) for use in purging, leak testing, inerting, or other uses. Embodiments can be configured so there is no heat exchanger or booster compressor positioned between the separation unit and the nitrogen storage unit.
An air separation system using a membrane separation unit to produce a nitrogen-enriched product stream from a feed air stream is described herein. A nitrogen-enriched non-permeate stream is expanded in a turboexpander and the energy recovered during expansion is used to further compress the feed air stream prior to membrane separation. Expanded nitrogen-enriched non-permeate stream is also used to cool the compressed feed air upstream from membrane separation.
B01D 53/22 - 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 diffusion
Disclosed herein are methods and systems for storing and withdrawing a light gas such as helium or hydrogen in an underground formation. The method includes pumping a cryogenic liquid stream to produce a pumped liquid stream, and vaporizing the pumped liquid stream to produce a first-high pressure gas steam. The method further includes feeding the first high-pressure gas stream to a gas storage cavern.
F17C 1/00 - Récipients sous pression, p. ex. bouteilles de gaz, réservoirs de gaz, cartouches échangeables
F17C 5/06 - Procédés ou appareils pour remplir des récipients sous pression de gaz liquéfiés, solidifiés ou comprimés pour le remplissage avec des gaz comprimés
22.
APPARATUS AND PROCESS FOR COOLING PRESSURIZED GAS FOR FUELING
An apparatus and process for cooling a pressurized gas for feeding to one or more vehicle fuel tanks for fueling a vehicle can be configured so that a pressurized gas (e.g. hydrogen or natural gas) for fueling one or more vehicles can be cooled prior to dispensing via a heat transfer fluid that cools the pressurized gas and transfers the heat of the pressurized gas toward fluid of a heat sink source. The transfer of the heat to the heat sink source fluid can occur via a refrigerant in some embodiments.
Adsorbent material for use in pressure swing adsorption (PSA) related processing can provide improved purification processing with reduced temperature differentials between adsorption and desorption processing of the bed of adsorbent material. Embodiments can be configured so that adsorbent material has occluded micropores or macropores. The occlusion of the micropores or macropores can be up to 42% of the micropores the adsorbent material in some embodiments. At least one metal acetate can be utilized for the occlusion of the micropores or macropores. Utilization of the adsorbent material having occluded micropores or macropores was surprisingly found to increase the yield for purification of a product gas in spite of the occlusion of the micropores or macropores.
B01J 20/20 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone libreCompositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone obtenu par des procédés de carbonisation
B01J 20/22 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance organique
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
25.
APPARATUS AND PROCESS FOR AMMONIA CRACKING CATALYST ACTIVATION
An apparatus and process for the activation of catalyst material utilized in ammonia cracking can include an initial use of hydrogen and heat to perform an initial stage of catalyst activation and a subsequent use of ammonia and heat to perform a subsequent state of catalyst activation. The subsequent use of ammonia can be configured so that different catalytic material at different plant elements are activated in a pre-selected sequence to provide activation of the catalytic material utilized in different plant elements. Some embodiments can be configured to avoid excess temperatures that can be detrimental to equipment that can be positioned upstream of a furnace in some embodiments while also avoiding sintering of the catalytic material.
Disclosed herein are methods and systems for producing a liquefied methane product from a methane- and carbon dioxide-containing feed stream, in which a plurality of membrane stages comprising gas separation membranes that are more permeable to carbon dioxide than methane are used to remove carbon dioxide from the feed and form a retentate stream that is enriched in methane, said retentate stream being then cooled and liquefied to provide the liquefied methane product. In particular, the disclosed methods and systems may be used for producing liquefied biomethane from a biogas feed.
B01D 53/22 - 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 diffusion
27.
SYSTEM AND METHOD FOR COMBUSTING HIGH-MOISTURE FUEL TO GENERATE STEAM
A process for combusting a high-moisture fuel to generate steam, the process comprising heating a high-moisture solid fuel while contacting the high-moisture solid fuel with an oxygen-depleted gas stream to produce a dried solid fuel and a moist oxygen-depleted gas stream; combusting the dried solid fuel with a combustion air stream to produce a combustion products stream; transferring heat to generate steam by indirect heat exchange with the combustion products stream; dividing the combustion products stream into a first portion and a second portion; transferring heat to the recirculating thermal fluid by indirect heat exchange with the first portion of the combustion products stream; and transferring heat to preheat the combustion air stream by indirect heat exchange with the second portion of the combustion products stream; and recombining the first portion of combustion products stream and the second portion of the combustion products stream.
F01K 13/00 - Dispositions générales ou processus généraux de fonctionnement des installations complètes d'ensembles fonctionnels de machines à vapeur
F23G 5/04 - Procédés ou appareils, p. ex. incinérateurs, spécialement adaptés à la combustion de déchets ou de combustibles pauvres comportant un traitement préalable consistant en un séchage
F23K 1/04 - Réchauffage du combustible avant son introduction dans l'appareil à combustion
F23L 7/00 - Alimentation du foyer en liquides ou gaz non combustibles autres que l'air, p. ex. oxygène, vapeur d'eau
An adsorption system having at least one adsorber retaining a bed of adsorbent material can be configured to provide enhanced purification of fees having relatively low concentrations of hydrogen or helium. Embodiments can utilize an activated carbon layer between at least one upstream layer and at least one downstream layer. The activate carbon layer can include activated carbon can have a pre-selected surface area (SA), bulk density, total open pore volume (TOPV), and/or ratio of TOPV to surface area (TOPV/SA).
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
B01D 53/04 - 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 avec adsorbants fixes
B01J 20/20 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone libreCompositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone obtenu par des procédés de carbonisation
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
29.
ADSORBENT MATERIAL, ADSORPTION SYSTEM, AND ADSORPTION PROCESS FOR HYDROGEN RECOVERY
An adsorption system having at least one adsorber retaining a bed of adsorbent material can be configured to provide enhanced purification of fees having relatively low concentrations of hydrogen or helium. Embodiments can utilize an activated carbon layer between at least one upstream layer and at least one downstream layer. The activate carbon layer can include activated carbon can have a pre-selected surface area (SA), bulk density, total open pore volume (TOPV), and/or ratio of TOPV to surface area (TOPV/SA).
B01J 20/20 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone libreCompositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone obtenu par des procédés de carbonisation
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
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
B01J 20/30 - Procédés de préparation, de régénération ou de réactivation
30.
ADSORBENT MATERIAL, ADSORPTION SYSTEM, AND ADSORPTION PROCESS
Adsorbent material for use in pressure swing adsorption (PSA) related processing can provide improved purification processing with reduced temperature differentials between adsorption and desorption processing of the bed of adsorbent material. Embodiments can be configured so that adsorbent material has occluded micropores or macropores. The occlusion of the micropores or macropores can be up to 42% of the micropores the adsorbent material in some embodiments. At least one metal acetate can be utilized for the occlusion of the micropores or macropores. Utilization of the adsorbent material having occluded micropores or macropores was surprisingly found to increase the yield for purification of a product gas in spite of the occlusion of the micropores or macropores.
B01J 20/04 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant des composés des métaux alcalins, des métaux alcalino-terreux ou du magnésium
B01J 20/08 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant des oxydes ou des hydroxydes des métaux non prévus dans le groupe contenant de l'oxyde ou de l'hydroxyde d'aluminiumCompositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant des oxydes ou des hydroxydes des métaux non prévus dans le groupe contenant de la bauxite
B01J 20/10 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant de la silice ou un silicate
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
B01J 20/30 - Procédés de préparation, de régénération ou de réactivation
Disclosed herein are methods and systems for producing a liquefied methane product from a methane- and carbon dioxide-containing feed stream, in which a plurality of membrane stages comprising gas separation membranes that are more permeable to carbon dioxide than methane are used to remove carbon dioxide from the feed and form a retentate stream that is enriched in methane, said retentate stream being then cooled and liquefied to provide the liquefied methane product. In particular, the disclosed methods and systems may be used for producing liquefied biomethane from a biogas feed.
A process for combusting a high-moisture fuel to generate steam, the process comprising heating a high-moisture solid fuel while contacting the high-moisture solid fuel with an oxygen-depleted gas stream to produce a dried solid fuel and a moist oxygen-depleted gas stream; combusting the dried solid fuel with a combustion air stream to produce a combustion products stream; transferring heat to generate steam by indirect heat exchange with the combustion products stream; dividing the combustion products stream into a first portion and a second portion; transferring heat to the recirculating thermal fluid by indirect heat exchange with the first portion of the combustion products stream; and transferring heat to preheat the combustion air stream by indirect heat exchange with the second portion of the combustion products stream; and recombining the first portion of combustion products stream and the second portion of the combustion products stream.
e.g.e.g., consisting of, hopcalite is improved where the hopcalite has a zero-point-of-charge (ZPC) in a range from about 6.9 to about 7.7 and/or an ionic conductivity as a 10 wt % slurry in deionized water of no more than about 500 µS/cm.
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
34.
MULTI-WELL PAD STORAGE OF H2 AND/OR NH3 WITH SIMULTANEOUS CO2 SEQUESTRATION
Disclosed herein are systems and methods of gas sequestration of carbon dioxide from a fossil-fueled hydrogen production plant. The method includes producing at least hydrogen and carbon dioxide above ground from a fossil-fueled hydrogen production plant, injecting at least a portion of the hydrogen and carbon dioxide produced from the fossil-fueled hydrogen production plant into a geological hydrogen storage unit and a geological carbon dioxide storage unit, respectively, wherein the portion of the carbon dioxide is injected concurrently with the portion of the hydrogen. The injection of the portion of carbon dioxide and hydrogen underground are performed through carbon dioxide injection well(s) and hydrogen injection well(s), respectively, wherein a hydrogen injection wellhead(s) and a carbon dioxide injection wellhead(s) are located on a multi-well pad proximate the fossil-fueled hydrogen production plant.
B65G 5/00 - Emmagasinage des fluides dans des excavations ou cavités naturelles ou artificielles souterraines
E21B 41/00 - Matériel ou accessoires non couverts par les groupes
C01B 3/22 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés organiques gazeux ou liquides
C01B 3/32 - 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
C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
C10J 3/00 - Production de gaz contenant de l'oxyde de carbone et de l'hydrogène, p. ex. du gaz de synthèse ou du gaz de ville, à partir de matières carbonées solides par des procédés d'oxydation partielle faisant intervenir de l'oxygène ou de la vapeur
35.
APPARATUSES AND PROCESSES FOR DISTILLATION AND DISTILLATION COLUMN ASSEMBLY
An apparatus and process for distillation column fabrication can include forming multiple distillation column packing units that are positionable in a column to define a single packing section so that multiple columns of packing can be positioned in parallel with each other within a single distillation pressure vessel. Each of these multiple columns can have a pre-selected cross-sectional shape, such as a hexagonal shape, and each packing unit can have the same cross-sectional shape (e.g. hexagonal). Each column can include a riser, or distributor, attached to its upper or top portion. A plurality of outer jigsaw seal elements can be arranged between the outer portion of the columns and the inner wall of the pressure vessel. Each packing unit can include a plurality of layered corrugated sheets that are provided in a pre-selected arrangement to facilitate gas and liquid separation via the packing.
B01D 3/32 - Autres caractéristiques de colonnes de fractionnement
B01J 19/32 - Éléments de remplissage en forme de grille ou d'éléments composés de plusieurs pièces pour constituer une unité ou un module dans l'appareil de transfert de chaleur ou de matière
36.
APPARATUSES AND PROCESSES FOR DISTILLATION AND DISTILLATION COLUMN ASSEMBLY
An apparatus and process for distillation column fabrication can include forming multiple distillation column packing units that are positionable in a column to define a single packing section so that multiple columns of packing can be positioned in parallel with each other within a single distillation pressure vessel. Each of these multiple columns can have a pre-selected cross-sectional shape, such as a hexagonal shape, and each packing unit can have the same cross-sectional shape (e.g. hexagonal). Each column can include a riser, or distributor, attached to its upper or top portion. A plurality of outer jigsaw seal elements can be arranged between the outer portion of the columns and the inner wall of the pressure vessel. Each packing unit can include a plurality of layered corrugated sheets that are provided in a pre-selected arrangement to facilitate gas and liquid separation via the packing.
B01J 19/32 - Éléments de remplissage en forme de grille ou d'éléments composés de plusieurs pièces pour constituer une unité ou un module dans l'appareil de transfert de chaleur ou de matière
B01D 3/32 - Autres caractéristiques de colonnes de fractionnement
37.
APPARATUS AND PROCESS FOR CONTROLLING A DISPLAY FOR FUEL DISPENSING
Systems, apparatuses, controllers, and processes that are configured to facilitate controlling visual information provided via a display at a dispenser while a vehicle is being fueled can be adapted so no use of communication protocols is needed for control of the display. For instance, a controller can be connected with a payment terminal having a screen via multiple different physical connections (e.g. wiring for conveying electricity, optical fiber cables, etc.). One or more of these connections can be activated while others are deactivated in an accordance with a pre-defined scheme to indicate to the payment terminal which of a number of different pre-defined display graphics should be displayed during fueling. Embodiments can be adapted so no payment information or other information is shared between a payment processing device and a fuel dispensing controller and no communication protocol is needed for transport of data between such devices.
G05B 19/416 - Commande numérique [CN], c.-à-d. machines fonctionnant automatiquement, en particulier machines-outils, p. ex. dans un milieu de fabrication industriel, afin d'effectuer un positionnement, un mouvement ou des actions coordonnées au moyen de données d'un programme sous forme numérique caractérisée par la commande de vitesse, d'accélération ou de décélération
G06Q 20/18 - Architectures de paiement impliquant des terminaux en libre-service, des distributeurs automatiques, des bornes ou des terminaux multimédia
38.
MULTI-WELL PAD STORAGE OF H2 AND/OR NH3 WITH SIMULTANEOUS CO2 SEQUESTRATION
Disclosed herein are systems and methods of gas sequestration of carbon dioxide from a fossil-fueled hydrogen production plant. The method includes producing at least hydrogen and carbon dioxide above ground from a fossil-fueled hydrogen production plant, injecting at least a portion of the hydrogen and carbon dioxide produced from the fossil-fueled hydrogen production plant into a geological hydrogen storage unit and a geological carbon dioxide storage unit, respectively, wherein the portion of the carbon dioxide is injected concurrently with the portion of the hydrogen. The injection of the portion of carbon dioxide and hydrogen underground are performed through carbon dioxide injection well(s) and hydrogen injection well(s), respectively, wherein a hydrogen injection wellhead(s) and a carbon dioxide injection wellhead(s) are located on a multi-well pad proximate the fossil-fueled hydrogen production plant.
A nozzle for a pressure vessel can include a lip design that facilitates an improved reduction in stress at a location at which the nozzle can be joined to the vessel. Embodiments can include a contoured annular lip element for attachment to an end of a vessel to position a nozzle within an opening at an end of the vessel for fluidly connecting the vessel to another plant element. The nozzle can include one or more geometries to position a weld for joining the nozzle to the end of the vessel so that the weld is located at a pre-selected location to experience a pre-selected level of stress during operation of the vessel to facilitate use of a vessel having a reduced overall wall thickness to provide a vessel having an overall lower weight and capital cost while also improving the ease with which maintenance can be performed.
A gasifier for converting a carbonaceous feedstock to produce syngas comprising a cone section and a throat section; wherein the throat section comprises a throat refractory material having an inside surface and a substantially cylindrical cooling element having an inner face and an outer face in a radial direction, and a top face and a bottom face in the vertical direction, wherein the inner, outer, top, and bottom faces define a cooling cavity; and wherein the cooling element is in thermal contact with the throat refractory material on the inner face, the top face, and the outer face.
A coil wound heat exchanger utilizing a deformable support system and method for making a tube bundle for the same includes a mandrel, a first tube layer formed by winding one or more tubes around the mandrel, and a plurality of supports and spacers circumferentially-arranged in an alternating pattern on an outer surface of the first tube layer. A second tube layer is formed by winding one or more tubes around the mandrel, whereby the second tube layer contacts an opposite side of the supports. A deforming force is applied to the second tube layer in a direction normal to the outer surface of each support, which causes the one or more tubes forming the second tube layer to deform the outer support surface of each support.
F28D 7/02 - 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 enroulées en hélice
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
F28F 9/013 - Supports auxiliaires pour les éléments pour les tubes ou les assemblages de tubes
A gasifier for converting a carbonaceous feedstock to produce syngas comprising a cone section and a throat section; wherein the throat section comprises a throat refractory material having an inside surface and a substantially cylindrical cooling element having an inner face and an outer face in a radial direction, and a top face and a bottom face in the vertical direction, wherein the inner, outer, top, and bottom faces define a cooling cavity; and wherein the cooling element is in thermal contact with the throat refractory material on the inner face, the top face, and the outer face.
A nozzle for a pressure vessel can include a lip design that facilitates an improved reduction in stress at a location at which the nozzle can be joined to the vessel. Embodiments can include a contoured annular lip element for attachment to an end of a vessel to position a nozzle within an opening at an end of the vessel for fluidly connecting the vessel to another plant element. The nozzle can include one or more geometries to position a weld for joining the nozzle to the end of the vessel so that the weld is located at a pre-selected location to experience a pre-selected level of stress during operation of the vessel to facilitate use of a vessel having a reduced overall wall thickness to provide a vessel having an overall lower weight and capital cost while also improving the ease with which maintenance can be performed.
A system for exchanging heat comprising a header oriented vertically within a pressure vessel, the header configured to receive a coolant stream from a coolant source or deliver a coolant stream to a coolant sink; one or more platen tubes in fluid flow communication with the header; wherein the one or more platen tubes comprise a vertical section and a non-vertical section; wherein the non-vertical section of the one or more platen tubes is configured to receive the coolant stream from or discharge the coolant stream to the header.
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
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
F28D 9/00 - Appareils échangeurs de chaleur comportant des ensembles de canalisations fixes en forme de plaques ou de laminés 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
An apparatus and process for fog mitigation can be include a mechanism to reduce fog formation and/or condense the fog into water to avoid fog being formed and moving through a site. Embodiments can be configured to utilize at least one fog collection mechanism positioned adjacent a vaporizer utilized to vaporizer a cryogenic liquid so that fog that may form adjacent the vaporizer is removed from air surrounding the vaporizer and prevented from spreading beyond the vaporizer to other areas of a site having the vaporizer (e.g. a hydrogen fueling station, etc.).
An apparatus and process for warming a cryogenic liquid and re-cooling gas for recapture and recovery of that cryogenic gas can include recovery cryogenic gas and storing that gas in at least one storage device to avoid venting such gas to atmosphere. The stored gas can be fed to at least one heat exchanger to vaporize a cryogenic liquid being fed from at least one storage tank for dispending of that cryogenic fluid. The stored cryogenic gas can be cooled as a result of its use as a heating medium for vaporization of the cryogenic liquid and can be subsequently fed to one or more cryogenic liquid storage tanks as a cooled cryogenic gas, partially liquefied fluid that includes cryogenic liquid and cryogenic gas, or a fully liquefied cryogenic liquid for storage and subsequent use.
F17C 9/02 - Procédés ou appareils pour vider les gaz liquéfiés ou solidifiés contenus dans des récipients non sous pression avec changement d'état, p. ex. vaporisation
47.
APPARATUS AND PROCESS FOR CRYOGENIC FLUID ENERGY RECOVERY
An apparatus and process for utilization of the cold provided by a cryogenic fluid so that the energy is not lost via exchange with ambient air etc. Embodiments can be configured for utilization of at least one working fluid and/or thermoelectric generation device for use of such energy extractable from a cryogenic fluid to generate electricity for powering one or more elements. Embodiments can also be configured to provide direct cooling. Embodiments can be utilized in various different environments, such as industrial plants, stationary facilities, or mobile devices (e.g. ships, trains, vehicles, etc.).
F01K 25/10 - Ensembles fonctionnels ou machines motrices caractérisés par l'emploi de fluides énergétiques particuliers non prévus ailleursEnsembles fonctionnant selon un cycle fermé, non prévus ailleurs utilisant des vapeurs particulières ces vapeurs étant froides, p. ex. ammoniac, gaz carbonique, éther
F02M 21/02 - Appareils pour alimenter les moteurs en combustibles non liquides, p. ex. en combustibles gazeux stockés sous forme liquide en combustibles gazeux
F02B 43/10 - Moteurs ou ensembles fonctionnels caractérisés par l'utilisation d'autres gaz spécifiques, p. ex. l'acétylène, le gaz oxhydrique
F17C 13/00 - Détails des récipients ou bien du remplissage ou du vidage des récipients
F17C 13/12 - Aménagements ou montage de dispositifs pour prévenir ou atténuer les effets d'explosion
A method for corrosion control is disclosed, wherein the method includes limiting all components involved in sulfuric acid formation to low levels. The components include, but may not be limited to oxygen, nitrogen oxides, sulfur oxides, and H2S. The method may also include maintaining the H2S level above typical pipeline concentrations to inhibit the reactions to form sulfuric acid in the pipeline.
A computer-implemented method of providing hydrogen having a defined carbon intensity (CI) value to an end user location, the process comprising: selecting a total end-to-end maximum CI value for the hydrogen from production to delivery of the hydrogen to an end user location; receiving one or more feedstocks; receiving product CI values associated with each feedstock and/or the produced hydrogen; receiving demand data defining the end user demand for the hydrogen; receiving renewable power data; defining, in an optimization model, a plurality of constraints; generating, using the optimization model, a control strategy for control of the one or more industrial plants; and controlling the industrial plants in accordance with the values of the control variables to process the one or more feedstocks in order to provide a required quantity of hydrogen meeting the selected total end-to-end maximum CI value for use by an end user.
G06Q 10/06 - Ressources, gestion de tâches, des ressources humaines ou de projetsPlanification d’entreprise ou d’organisationModélisation d’entreprise ou d’organisation
A method for separating a raw feed gas stream utilizes a compressor, a chiller, a membrane drying stage, and a plurality of membrane separation stages. The raw feed gas stream may comprise biogas. In one example, the raw feed gas stream is supplied to the chiller where it is cooled to a target operating temperature to separate out condensed water. The gas stream is then supplied to a membrane drying stage to separate out water vapor. An off-gas from one of the membrane module stages may be recycled as a low pressure sweep gas on the low pressure side of the membrane drying stage to increase the driving force for water permeation within the membrane drying stage. The gas stream is then supplied to the plurality of membrane separation stages where it is upgraded into a high purity methane stream.
A method for corrosion control is disclosed, wherein the method includes limiting all components involved in sulfuric acid formation to low levels. The components include, but may not be limited to oxygen, nitrogen oxides, sulfur oxides,and H2S. The method may also include maintaining the H2S level above typical pipeline concentrations to inhibit the reactions to form sulfuric acid in the pipeline.
The invention relates to particular burners, particularly to non-premixed or partially-premixed dual-fuel burners with flexibility to change the heat input from the two fuels. Accordingly, said burners may be used in applications that needs operation of a bummer in both single-fuel, and/or duel-fuel mode depending on furnace operation needs. The invention further relates to methods of operating the burners.
F23D 14/32 - Brûleurs pour la combustion d'un gaz, p. ex. d'un gaz stocké sous pression à l'état liquide utilisant un mélange de combustible gazeux et d'oxygène pur ou d'air enrichi d'oxygène
F23D 14/22 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant
The invention relates to particular burners, particularly to non-premixed or partially-premixed dual-fue burners with flexibility to change the heat input from the two fuels. Accordingly, said burners may be used in applications that needs operation of a burner in both single-fuel, and/or duel-fuel mode depending on furnace operation needs. The invention further relates to furnaces including the burners and methods of operating the burners.
F23D 14/24 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant au moins un des fluides étant soumis à un mouvement tourbillonnant
F23D 14/58 - Buses caractérisés par la forme ou la disposition de l'orifice ou des orifices des buses, p. ex. en couronne
F23C 1/00 - Appareils à combustion spécialement adaptés à la combustion de plusieurs sortes de combustibles simultanément ou alternativement, au moins un des combustibles étant fluide ou étant un combustible solide en suspension dans l’air
54.
BURNER, METHOD OF OPERATION AND COMBUSTION APPARATUS
Burners having the flexibility to change the heat input from multiple fuels can be configured to facilitate stable flame formation with low nitrous oxide (NOx) emissions. Processes of combustion that can be utilized via one or more burners can provide for improved flame formation that can provide reduced NOx emissions as well. Embodiments can be configured for use in ammonia cracker implementations, reforming applications, metal remelt furnace applications, as well as other furnace applications and/or combustor applications.
F23C 7/00 - Appareils à combustion caractérisés par des dispositions pour l'amenée d'air
F23C 9/00 - Appareils à combustion caractérisés par des dispositions pour renvoyer les produits de combustion ou les gaz de fumée dans la chambre de combustion
F02C 7/22 - Systèmes d'alimentation en combustible
F23K 3/00 - Alimentation ou distribution de combustible en morceaux ou pulvérulent à l'appareil à combustion
F23N 3/00 - Régulation de l'amenée d'air ou du tirage
F23C 1/12 - Appareils à combustion spécialement adaptés à la combustion de plusieurs sortes de combustibles simultanément ou alternativement, au moins un des combustibles étant fluide ou étant un combustible solide en suspension dans l’air du combustible gazeux et du combustible pulvérulent
F23C 7/02 - Amenées d'air ne traversant pas le brûleur
A controller, process, and apparatus can be configured to provide backup electrical power to various equipment used in hydrogen and/or ammonia production in response to a loss of power condition being detected. The loss of power can be due to unavailable power from renewable sources (e.g. cloudy day, non-windy conditions) or due to other power transmission problems. The backup electrical power can be provided in a way that can reduce the carbon intensity associated with the providing of the backup power. The backup power can also be provided to help avoid degradation of equipment that can occur from sudden losses of electrical power. In some embodiments, hydrogen powered turbines, hydrogen fuel cells, biofuel generators, and/or hydrogen powered engines can be utilized for providing the backup power.
H02J 9/06 - Circuits pour alimentation de puissance de secours ou de réserve, p. ex. pour éclairage de secours dans lesquels le système de distribution est déconnecté de la source normale et connecté à une source de réserve avec commutation automatique
The invention relates to particular burners, and e.g. to a burner comprising a central main fuel lance, a pilot fuel conduit, a main oxidant conduit, an auxiliary oxidant conduit, and optionally a secondary fuel conduit, which are arranged in a particular and advantageous way to surround each other at least in their downstream sections. The invention further relates to furnaces including the burners and methods of operating the burners. Among others, the burners of the present invention allow a particularly advantageous way of including a pilot burner as an integral part of the main burner to ignite liquid fuel flame in a cold furnace. If required, the pilot flame can assist in extending the flammability limit or operating range of the liquid fuel burner.
F23D 17/00 - Brûleurs pour la combustion simultanée ou alternative de combustibles gazeux, liquides ou pulvérulents
F23C 1/08 - Appareils à combustion spécialement adaptés à la combustion de plusieurs sortes de combustibles simultanément ou alternativement, au moins un des combustibles étant fluide ou étant un combustible solide en suspension dans l’air du combustible liquide et du combustible gazeux
F23C 7/00 - Appareils à combustion caractérisés par des dispositions pour l'amenée d'air
F23D 11/38 - AjutagesDispositifs de nettoyage des ajutages
F23G 7/06 - Procédés ou appareils, p. ex. incinérateurs, spécialement adaptés à la combustion de déchets particuliers ou de combustibles pauvres, p. ex. des produits chimiques de gaz d'évacuation ou de gaz nocifs, p. ex. de gaz d'échappement
The invention relates to particular burners, particularly to non-premixed or partially-premixed fuel burners with flexibility to oxygen enrich the burner. Accordingly, said burners may be used in applications that needs operation of a burner in both air-fuel, and/or oxy-fuel and/or air-oxy-fuel mode depending on furnace operation needs. The invention further relates to furnaces including the burners and methods of operating the burners.
F23D 14/24 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant au moins un des fluides étant soumis à un mouvement tourbillonnant
F23C 1/00 - Appareils à combustion spécialement adaptés à la combustion de plusieurs sortes de combustibles simultanément ou alternativement, au moins un des combustibles étant fluide ou étant un combustible solide en suspension dans l’air
F23C 7/00 - Appareils à combustion caractérisés par des dispositions pour l'amenée d'air
The invention relates to particular burners, particularly to non-premixed or partially-premixed dual-fue burners with flexibility to change the heat input from the two fuels. Accordingly, said burners may be used in applications that needs operation of a burner in both single-fuel, and/or duel-fuel mode depending on furnace operation needs. The invention further relates to furnaces including the burners and methods of operating the burners.
F23D 14/24 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant au moins un des fluides étant soumis à un mouvement tourbillonnant
F23C 1/00 - Appareils à combustion spécialement adaptés à la combustion de plusieurs sortes de combustibles simultanément ou alternativement, au moins un des combustibles étant fluide ou étant un combustible solide en suspension dans l’air
F23C 3/00 - Appareils à combustion caractérisés par la forme de la chambre de combustion
F23C 7/00 - Appareils à combustion caractérisés par des dispositions pour l'amenée d'air
In a reactor comprising a cylindrical combustion chamber, at least one burner and a circular array of catalyst-containing tubes, there is provided a ring baffle on the wall opposite the burner(s) extending into the combustion chamber which redirects combustion gas around the combustion chamber, thereby enabling more even heat distribution and an increase in overall heat transfer.
An apparatus and process for processing of a fluid (e.g. hydrogen) for liquefaction can permit a reduction in power consumption and also an improvement in operational efficiency in flexibility. Embodiments can be configured to account for large variations in feed to be provided for liquefaction and also permit operational cost reductions associated with liquefaction processing so the overall power consumption and operational cost for liquefaction can be greatly reduced while also providing improved operational flexibility. For instance, embodiments can be configured to feed a fluid to multiple liquefiers of a train of liquefiers based on a pre-selected set of feed routing criteria for improving power consumption and providing greater operational flexibility for liquefaction operations.
F25J 1/02 - Procédés ou appareils de liquéfaction ou de solidification des gaz ou des mélanges gazeux nécessitant l'emploi d'une réfrigération, p. ex. de l'hélium, de l'hydrogène
F25J 1/00 - Procédés ou appareils de liquéfaction ou de solidification des gaz ou des mélanges gazeux
G05B 13/04 - Systèmes de commande adaptatifs, c.-à-d. systèmes se réglant eux-mêmes automatiquement pour obtenir un rendement optimal suivant un critère prédéterminé électriques impliquant l'usage de modèles ou de simulateurs
61.
Apparatus and Process for Pre-Liquefaction Fluid Processing for Improved Liquefaction Operations
An apparatus and process for pre-liquefaction processing of a fluid (e.g. hydrogen) can permit a reduction in capital costs and also an improvement in operational efficiency in flexibility. Embodiments can be configured to account for large variations in feed to be provided for liquefaction and also permit capital cost reductions associated with pre-liquefaction processing so the overall capital cost for liquefaction can be greatly reduced while also providing improved operational flexibility. For instance, embodiments can be configured to utilize one or more common pre-liquefaction processing elements to treat a fluid for pre-cooling of a fluid to a pre-selected liquefaction feed temperature.
F25J 1/02 - Procédés ou appareils de liquéfaction ou de solidification des gaz ou des mélanges gazeux nécessitant l'emploi d'une réfrigération, p. ex. de l'hélium, de l'hydrogène
F25J 1/00 - Procédés ou appareils de liquéfaction ou de solidification des gaz ou des mélanges gazeux
62.
CONTROL SYSTEM FOR CARBON INTENSITY MANAGEMENT IN A HYDROGEN SUPPLY NETWORK
A computer-implemented method of providing hydrogen having a defined carbon intensity (CI) value to an end user location, the process comprising: selecting a total end-to-end maximum CI value for the hydrogen from production to delivery of the hydrogen to an end user location; receiving one or more feedstocks; receiving product CI values associated with each feedstock and/or the produced hydrogen; receiving demand data defining the end user demand for the hydrogen; receiving renewable power data; defining, in an optimization model, a plurality of constraints; generating, using the optimization model, a control strategy for control of the one or more industrial plants; and controlling the industrial plants in accordance with the values of the control variables to process the one or more feedstocks in order to provide a required quantity of hydrogen meeting the selected total end-to-end maximum CI value for use by an end user.
G05B 13/02 - Systèmes de commande adaptatifs, c.-à-d. systèmes se réglant eux-mêmes automatiquement pour obtenir un rendement optimal suivant un critère prédéterminé électriques
G06Q 10/0832 - Marchandises spéciales ou procédures de manutention spéciales, p. ex. manutention de marchandises dangereuses ou fragiles
In a reactor comprising a cylindrical combustion chamber, at least one burner and a circular array of catalyst-containing tubes, there is provided a ring baffle on the wall opposite the burner(s) extending into the combustion chamber which redirects combustion gas around the combustion chamber, thereby enabling more even heat distribution and an increase in overall heat transfer.
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
C01B 3/38 - 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 des catalyseurs
The invention relates to particular burners, and e.g. to a burner comprising a central main fuel lance, a pilot fuel conduit, a main oxidant conduit, an auxiliary oxidant conduit, and optionally a secondary fuel conduit, which are arranged in a particular and advantageous way to surround each other at least in their downstream sections. The invention further relates to furnaces including the burners and methods of operating the burners. Among others, the burners of the present invention allow a particularly advantageous way of including a pilot burner as an integral part of the main burner to ignite liquid fuel flame in a cold furnace. If required, the pilot flame can assist in extending the flammability limit or operating range of the liquid fuel burner.
F23D 14/22 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant
F23D 17/00 - Brûleurs pour la combustion simultanée ou alternative de combustibles gazeux, liquides ou pulvérulents
F23C 6/04 - Appareils à combustion caractérisés par la combinaison d'au moins deux chambres de combustion disposées en série
F23D 14/24 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant au moins un des fluides étant soumis à un mouvement tourbillonnant
The invention relates to particular burners, particularly to non-premixed or partially-premixed fuel burners with flexibility to oxygen enrich the burner. Accordingly, said burners may be used in applications that needs operation of a burner in both air-fuel, and/or oxy-fuel and/or air-oxy-fuel mode depending on furnace operation needs. The invention further relates to furnaces including the burners and methods of operating the burners.
F23D 14/24 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant au moins un des fluides étant soumis à un mouvement tourbillonnant
66.
APPARATUS AND PROCESS FOR STARTING UP AND SHUTTING DOWN A FEED OF FUEL FOR A TURBINE APPARATUS
An apparatus can be arranged and configured so that after a gas turbine is shut down due to a detected condition, a higher autoignition temperature fuel can be utilized to purge a fuel delivery system and facilitate a quicker restart of the turbine. Embodiments can utilize conduits, valves, and a control system for detection of a fault condition warranting a shut down, purging of a lower autoignition temperature fuel via venting and use of a higher autoignition temperature fuel for purging to facilitate subsequent restarting of the turbine. Embodiments can be configured so an inert gas purge is not needed for venting and purging of the fuel delivery system.
An apparatus can be arranged and configured so that after a gas turbine is shut down due to a detected condition, a higher autoignition temperature fuel can be utilized to purge a fuel delivery system and facilitate a quicker restart of the turbine. Embodiments can utilize conduits, valves, and a control system for detection of a fault condition warranting a shut down, purging of a lower autoignition temperature fuel via venting and use of a higher autoignition temperature fuel for purging to facilitate subsequent restarting of the turbine. Embodiments can be configured so an inert gas purge is not needed for venting and purging of the fuel delivery system.
An apparatus for utilization of cooling water can facilitate an improved and more efficient cooling approach. Embodiments can provide an adjustable cooling temperature for the cooling water to account for an operational state of hydrogen producing equipment, which may transition between fully powered to non-powered statuses based on the availability of renewable power. Embodiments can be provided to help limit the amount of water lost during cooling and costs associated with providing cooling water to equipment when the equipment is operating to produce hydrogen.
C25B 15/021 - Commande ou régulation des opérations de chauffage ou de refroidissement
C25B 9/67 - Moyens de chauffage ou de refroidissement
F25D 17/02 - Dispositions pour la circulation des fluides de refroidissementDispositions pour la circulation de gaz, p. ex. d'air, dans les enceintes refroidies pour la circulation des liquides, p. ex. de la saumure
F28C 3/04 - Autres appareils échangeurs de chaleur à contact direct les sources de potentiel calorifique étant toutes deux des liquides
H01M 8/04029 - Échange de chaleur par des liquides
C25B 1/04 - Hydrogène ou oxygène par électrolyse de l'eau
An apparatus and process for oxidant formation can be configured to facilitate improved mixing of for formation of an oxidant. Embodiments can be configured so conduits having a relatively large aspect ratio (e.g., 1.5 to 5 or 1.5 to over 5) can be utilized for improved gas mixing even in situations in which the carrier gas is at a relatively low pressure. Embodiments can also facilitate low nitrogen oxide formation combustion. Some embodiments can additionally provide improved carbon capture.
An apparatus and process for steam reforming can be configured to produce at least one product with reduced carbon dioxide and/or nitrogen oxide emissions. Some embodiments can be better adapted for retrofitting a pre-existing steam reforming process while other embodiments can be better adapted for use in a newly constructed facility. Embodiments can be configured to utilize a synthetic air oxidant to provide combustion that results in formation of a flue gas having relatively high carbon dioxide concentrations that may also have low nitrogen and low nitrogen oxide concentrations. A control system can be configured for utilization in such embodiments to control the steam reforming process and/or oxidant formation process as well. Some embodiments can also be configured to provide carbon dioxide recovery that can permit recovery of a second product stream comprised of carbon dioxide.
C01B 3/38 - 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 des catalyseurs
B01D 53/22 - 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 diffusion
C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
71.
CONTROL SYSTEM FOR AN APPARATUS FOR STEAM REFORMING AND PROCESS FOR CONTROLLING AN APPARATUS FOR STEAM REFORMING
An apparatus and process for steam reforming can be configured to produce at least one product with reduced carbon dioxide and/or nitrogen oxide emissions. Some embodiments can be better adapted for retrofitting a pre-existing steam reforming process while other embodiments can be better adapted for use in a newly constructed facility. Embodiments can be configured to utilize a synthetic air oxidant to provide combustion that results in formation of a flue gas having relatively high carbon dioxide concentrations that may also have low nitrogen and low nitrogen oxide concentrations. A control system can be configured for utilization in such embodiments to control the steam reforming process and/or oxidant formation process as well. Some embodiments can also be configured to provide carbon dioxide recovery that can permit recovery of a second product stream comprised of carbon dioxide.
An apparatus and process for steam reforming can be configured to produce at least one product with reduced carbon dioxide and/or nitrogen oxide emissions. Some embodiments can be better adapted for retrofitting a pre-existing steam reforming process while other embodiments can be better adapted for use in a newly constructed facility. Embodiments can be configured to utilize a synthetic air oxidant to provide combustion that results in formation of a flue gas having relatively high carbon dioxide concentrations that may also have low nitrogen and low nitrogen oxide concentrations. A control system can be configured for utilization in such embodiments to control the steam reforming process and/or oxidant formation process as well. Some embodiments can also be configured to provide carbon dioxide recovery that can permit recovery of a second product stream comprised of carbon dioxide.
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
73.
APPARATUS AND PROCESS FOR REDUCED FORMATION OF NITROGEN OXIDES DURING COMBUSTION
An apparatus and process can be configured for reduced nitrogen oxide formation during combustion. Embodiments can provide synthetic air to a combustion device so that combustion of a fuel can occur with a substantially low amount of NOx. Some embodiments can provide a reduction in NOx formation by at least 75% and as much as greater than 95% as compared to use of ambient air or oxygen enriched air oxidants. Embodiments can also provide a flue gas that has a high concentration of carbon dioxide that can facilitate improved carbon capture and permit efficient formation of at least one carbon dioxide product stream with a high carbon dioxide concentration (e.g. at least 95 mole percent carbon dioxide).
An apparatus and process for steam reforming can be configured to produce at least one product with reduced carbon dioxide and/or nitrogen oxide emissions. Some embodiments can be better adapted for retrofitting a pre-existing steam reforming process while other embodiments can be better adapted for use in a newly constructed facility. Embodiments can be configured to utilize a synthetic air oxidant to provide combustion that results in formation of a flue gas having relatively high carbon dioxide concentrations that may also have low nitrogen and low nitrogen oxide concentrations. A control system can be configured for utilization in such embodiments to control the steam reforming process and/or oxidant formation process as well. Some embodiments can also be configured to provide carbon dioxide recovery that can permit recovery of a second product stream comprised of carbon dioxide.
C01B 3/38 - 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 des catalyseurs
B01D 53/22 - 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 diffusion
B01F 35/221 - Commande ou régulation des paramètres de fonctionnement, p. ex. du niveau de matière dans le mélangeur, de la température ou de la pression
C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
75.
Purification of Concentrated Aqueous Hydroxide Solutions for Electrolysis
Disclosed are novel processes, based on precipitation, settling, and filtration for the removal of critical impurities selected from dissolved transition metals, inorganic anions and dissolved organic compounds, from highly concentrated hydroxide solutions used as electrolytes in alkaline water electrolysis (AEW) to produce hydrogen. The processes comprise adding to the solutions at least one precipitation additive selected from water-soluble salts of alkaline earth metals; nickel (II) hydroxide; and hydroxides or oxides of alkaline earth metals, provided that the surface area of the hydroxides/oxides is more than 5 m2/g, to form at least one inorganic compound (or complex) as a precipitate which is removed from the solution.
An apparatus and process for steam reforming can be configured to produce at least one product with reduced carbon dioxide and/or nitrogen oxide emissions. Some embodiments can be better adapted for retrofitting a pre-existing steam reforming process while other embodiments can be better adapted for use in a newly constructed facility. Embodiments can be configured to utilize a synthetic air oxidant to provide combustion that results in formation of a flue gas having relatively high carbon dioxide concentrations that may also have low nitrogen and low nitrogen oxide concentrations. A control system can be configured for utilization in such embodiments to control the steam reforming process and/or oxidant formation process as well. Some embodiments can also be configured to provide carbon dioxide recovery that can permit recovery of a second product stream comprised of carbon dioxide.
C01B 3/38 - 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 des catalyseurs
B01D 53/00 - 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
77.
APPARATUS AND PROCESS FOR REDUCED FORMATION OF NITROGEN OXIDES DURING COMBUSTION
An apparatus and process can be configured for reduced nitrogen oxide formation during combustion. Embodiments can provide synthetic air to a combustion device so that combustion of a fuel can occur with a substantially low amount of NOx. Some embodiments can provide a reduction in NOx formation by at least 75% and as much as greater than 95% as compared to use of ambient air or oxygen enriched air oxidants. Embodiments can also provide a flue gas that has a high concentration of carbon dioxide that can facilitate improved carbon capture and permit efficient formation of at least one carbon dioxide product stream with a high carbon dioxide concentration (e.g. at least 95 mole percent carbon dioxide).
F23C 9/00 - Appareils à combustion caractérisés par des dispositions pour renvoyer les produits de combustion ou les gaz de fumée dans la chambre de combustion
An apparatus and process for oxidant formation can be configured to facilitate improved mixing of for formation of an oxidant. Embodiments can be configured so conduits having a relatively large aspect ratio (e.g., 1.5 to 5 or 1.5 to over 5) can be utilized for improved gas mixing even in situations in which the carrier gas is at a relatively low pressure. Embodiments can also facilitate low nitrogen oxide formation combustion. Some embodiments can additionally provide improved carbon capture.
F23C 9/00 - Appareils à combustion caractérisés par des dispositions pour renvoyer les produits de combustion ou les gaz de fumée dans la chambre de combustion
F23L 7/00 - Alimentation du foyer en liquides ou gaz non combustibles autres que l'air, p. ex. oxygène, vapeur d'eau
An apparatus and process for steam reforming can be configured to produce at least one product with reduced carbon dioxide and/or nitrogen oxide emissions. Some embodiments can be better adapted for retrofitting a pre-existing steam reforming process while other embodiments can be better adapted for use in a newly constructed facility. Embodiments can be configured to utilize a synthetic air oxidant to provide combustion that results in formation of a flue gas having relatively high carbon dioxide concentrations that may also have low nitrogen and low nitrogen oxide concentrations. A control system can be configured for utilization in such embodiments to control the steam reforming process and/or oxidant formation process as well. Some embodiments can also be configured to provide carbon dioxide recovery that can permit recovery of a second product stream comprised of carbon dioxide.
C01B 3/38 - 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 des catalyseurs
C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
B01D 53/00 - 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
80.
Method and System for Heat Recovery in an Oxy-Fuel Fired Glass Furnace
Processes and systems for glass making can utilize heat recovery to improve operational efficiency and flexibility of operation to provide improved yield, higher quality, or more consistent quality glass, and/or other efficiencies. Some embodiments can utilize adjustments in burner operation to account for different manufacturing conditions to provide improved quality of fabricated glass to provide improved yields of glass with a more efficient utilization of heat, which can improve the environmental impact associated with the manufacturing process in addition to improving the operational efficiency and flexibility of the glass manufacturing process.
Processes and systems for glass making can utilize heat recovery to improve operational efficiency and flexibility of operation to provide improved yield, higher quality, or more consistent quality glass, and/or other efficiencies. Some embodiments can utilize adjustments in burner operation to account for different manufacturing conditions to provide improved quality of fabricated glass to provide improved yields of glass with a more efficient utilization of heat, which can improve the environmental impact associated with the manufacturing process in addition to improving the operational efficiency and flexibility of the glass manufacturing process.
C03B 5/237 - Régénérateurs ou récupérateurs spécialement adaptés aux fours de fusion de verre
C03B 3/02 - Enfournement combiné à un préchauffage, une préfusion ou un prétraitement des ingrédients vitrifiables, des granulés ou des groisils
F23D 14/22 - Brûleurs à gaz sans prémélangeur, c.-à-d. dans lesquels le combustible gazeux est mélangé à l'air de combustion à l'arrivée dans la zone de combustion avec des conduits d'alimentation en air et en gaz séparés, p. ex. avec des conduits disposés parallèlement ou se croisant
A method comprising contacting an offgas stream comprising H2, H2O, CO, CO2, and at least one impurity comprising COS with at least one metal oxide to catalyze a reaction of H2O and COS to form H2S and CO2 in the offgas stream; contacting the offgas stream with an H2S-adsorbent to remove H2S from the offgas stream to produce a treated gas stream; and separating the treated gas stream to produce a carbon dioxide-enriched stream and a carbon dioxide-depleted stream.
Disclosed herein are rotary valve assemblies, comprising a single rotor, for use in adsorption based separation processes. Also disclosed are adsorption based separation apparatuses including said rotary valve assemblies, and adsorption based separation processes using said adsorption based separation apparatuses.
B01D 53/04 - 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 avec adsorbants fixes
84.
ADSORBER, PURIFICATION SYSTEM, AND PURIFICATION METHOD
An adsorber for utilization in purification systems for cryogenic fluid processing can include a first layer of adsorbent material and a second layer of adsorbent material within a bed of adsorbent material within the adsorber. The first layer can include alumina or other water removal adsorbent material while the second layer can include NaMSX or other suitable molecular sieve adsorbent material. The first layer can be sized to be substantially smaller than the second layer to facilitate a pre-selected ratio of water adsorption to molecular sieve adsorption so that water can break through the first layer to the second layer during purification operations while the volume of the adsorber can be provided in a much smaller size with much less adsorbent material utilized in the bed as compared to conventional designs. Embodiments can provide an increased purification operational capacity with reduced need for adsorbent material.
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
B01D 53/04 - 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 avec adsorbants fixes
The invention concerns a process and apparatus for cracking ammonia in which heated ammonia at super-atmospheric pressure is partially cracked in reactor tubes containing a first catalyst in a fired reactor to produce partially cracked ammonia gas which is then cracked over a second catalyst in a reaction zone of an electrically heated reactor to produce cracked gas comprising hydrogen gas, nitrogen gas and residual ammonia. The cracked gas is cooled and hydrogen is recovered from the cooled cracked gas in a hydrogen recovery unit. Offgas from the hydrogen recovery unit, or a cracked offgas derived therefrom, provides at least some, preferably all, of the fuel requirement in the fired reactor. Varying the power input to the second part of the cracking reaction enables direct control of the heat flux profile and hence optimization of the conversion.
The invention concerns a process and apparatus for cracking ammonia in which heated ammonia at super-atmospheric pressure is partially cracked over a first catalyst in a reaction zone of an electrically heated reactor to produce partially cracked ammonia gas which is then cracked in reactor tubes containing a second catalyst in a fired reactor to produce cracked gas comprising hydrogen gas, nitrogen gas and residual ammonia. The cracked gas is cooled and hydrogen is recovered from the cooled cracked gas in a hydrogen recovery unit. Offgas from the hydrogen recovery unit, or a cracked offgas derived therefrom, provides at least some, preferably all, of the fuel requirement in the fired reactor. Varying the power input to the first part of the cracking reaction enables direct control of the heat flux profile and hence accommodate any excess or shortfall in the heat input from the fired reactor.
The invention concerns a process and apparatus for cracking ammonia in which heated ammonia at super-atmospheric pressure is partially cracked in reactor tubes containing a first catalyst in a fired reactor to produce partially cracked ammonia gas which is then cracked over a second catalyst in a reaction zone of an electrically heated reactor to produce cracked gas comprising hydrogen gas, nitrogen gas and residual ammonia. The cracked gas is cooled and hydrogen is recovered from the cooled cracked gas in a hydrogen recovery unit. Offgas from the hydrogen recovery unit, or a cracked offgas derived therefrom, provides at least some, preferably all, of the fuel requirement in the fired reactor. Varying the power input to the second part of the cracking reaction enables direct control of the heat flux profile and hence optimization of the conversion.
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 8/00 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés
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
C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
The invention concerns a process and apparatus for cracking ammonia in which heated ammonia at super-atmospheric pressure is partially cracked over a first catalyst in a reaction zone of an electrically heated reactor to produce partially cracked ammonia gas which is then cracked in reactor tubes containing a second catalyst in a fired reactor to produce cracked gas comprising hydrogen gas, nitrogen gas and residual ammonia. The cracked gas is cooled and hydrogen is recovered from the cooled cracked gas in a hydrogen recovery unit. Offgas from the hydrogen recovery unit, or a cracked offgas derived therefrom, provides at least some, preferably all, of the fuel requirement in the fired reactor. Varying the power input to the first part of the cracking reaction enables direct control of the heat flux profile and hence accommodate any excess or shortfall in the heat input from the fired reactor.
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 8/00 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés
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
C01B 3/50 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification
40 - Traitement de matériaux; recyclage, purification de l'air et traitement de l'eau
42 - Services scientifiques, technologiques et industriels, recherche et conception
Produits et services
Carbon capture for others; consulting services in the field of production of renewable green energy; production of renewable green energy; production of renewable chemicals. Consulting services in the nature of utilizing artificial intelligence for maximizing the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen; Consulting services in the field of energy saving computation; Technological consultancy services in the field of clean hydrogen production and efficient use of renewable energy; Conducting technical project studies in the field of clean hydrogen production and efficient use of renewable energy; Calibration services; Energy auditing services; Engineering services for hydrogen production facilities; Industrial design services; Providing scientific information, advice and consultancy relating to carbon offsetting; Providing scientific information, advice and consultancy relating to net zero emissions; Weather forecasting services; Providing quality control services; research in the field of artificial intelligence technology; Scientific research in the field of environmental protection; Software as a service (SaaS) services featuring software to maximize the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen using advanced computational models to predict available power, performance, and future trends based on historic and predicted weather conditions and plant performance data and enabling optimal design and operation of hydrogen production facilities and efficient use of renewable power available; Computer programming services for utilizing artificial intelligence for maximizing the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen; Design of computer-simulated models; Updating of computer software; Providing online non-downloadable computer software for maximizing the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen using advanced computational models to predict available power, performance, and future trends based on historic and predicted weather conditions and plant performance data and enabling optimal design and operation of hydrogen production facilities and efficient use of renewable power available; Technical support services, namely, troubleshooting of industrial process control computer software problems; Providing technical information updates of industrial process control computer software via the global computer network.
40 - Traitement de matériaux; recyclage, purification de l'air et traitement de l'eau
42 - Services scientifiques, technologiques et industriels, recherche et conception
Produits et services
Carbon capture for others; consulting services in the field of production of renewable green energy; production of renewable green energy; production of renewable chemicals. Consulting services in the nature of utilizing artificial intelligence for maximizing the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen; Consulting services in the field of energy saving computation; Technological consultancy services in the field of clean hydrogen production and efficient use of renewable energy; Conducting technical project studies in the field of clean hydrogen production and efficient use of renewable energy; Calibration services; Energy auditing services; Engineering services for hydrogen production facilities; Industrial design services; Providing scientific information, advice and consultancy relating to carbon offsetting; Providing scientific information, advice and consultancy relating to net zero emissions; Weather forecasting services; Providing quality control services; research in the field of artificial intelligence technology; Scientific research in the field of environmental protection; Software as a service (SaaS) services featuring software to maximize the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen using advanced computational models to predict available power, performance, and future trends based on historic and predicted weather conditions and plant performance data and enabling optimal design and operation of hydrogen production facilities and efficient use of renewable power available; Computer programming services for utilizing artificial intelligence for maximizing the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen; Design of computer-simulated models; Updating of computer software; Providing online non-downloadable computer software for maximizing the utilization of intermittent renewable energy for optimal production of zero-carbon hydrogen using advanced computational models to predict available power, performance, and future trends based on historic and predicted weather conditions and plant performance data and enabling optimal design and operation of hydrogen production facilities and efficient use of renewable power available; Technical support services, namely, troubleshooting of industrial process control computer software problems; Providing technical information updates of industrial process control computer software via the global computer network.
A method for purifying a crude hydrogen feed stream utilizes an adsorbent having a N2/Ar selectivity ranging from 2 to 4 at 30° C. and a Henry's law coefficient for argon ranging from 0.15 to 1.0 mmole/g/atma at 30° C. The composition of crude hydrogen streams from processes in which carbon dioxide is captured necessitates new criteria for adsorbent selection to improve recovery.
A method for purifying a crude hydrogen feed stream utlizes an adsorbent having a N2/Ar selectivity ranging from 2 to 4 at 30°C and a Henry's law coefficient for argon ranging from 0.15 to 1.0 mmole/g/atma at 30°C. The composition of crude hydrogen streams from processes in which carbon dioxide is captured necessitates new criteria for adsorbent selection to improve recovery.
B01D 53/04 - 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 avec adsorbants fixes
There is provided an electrolyser power system comprising: a transformer arrangement having: at least one primary winding connectable to an AC power source; and a plurality of secondary windings; a first rectifier arrangement comprising: an AC input connected to a first secondary winding of the transformer arrangement; and a first DC output; a second rectifier arrangement comprising: an AC input connected to a second secondary winding of the transformer arrangement; and a second DC output; and a plurality of discrete electrically coupled electrolyser modules, wherein each electrolyser module is electrically connected between the first and second DC outputs.
H02M 7/162 - Transformation d'une puissance d'entrée en courant alternatif en une puissance de sortie en courant continu sans possibilité de réversibilité par convertisseurs statiques utilisant des tubes à décharge avec électrode de commande ou des dispositifs à semi-conducteurs avec électrode de commande utilisant des dispositifs du type thyratron ou thyristor exigeant des moyens d'extinction utilisant uniquement des dispositifs à semi-conducteurs dans une configuration en pont
C25B 1/04 - Hydrogène ou oxygène par électrolyse de l'eau
C25B 9/65 - Dispositifs pour l'alimentation en courantConnexions d'électrodesConnexions électriques intercellulaires
C25B 9/70 - Assemblages comprenant plusieurs cellules
H02M 7/17 - Transformation d'une puissance d'entrée en courant alternatif en une puissance de sortie en courant continu sans possibilité de réversibilité par convertisseurs statiques utilisant des tubes à décharge avec électrode de commande ou des dispositifs à semi-conducteurs avec électrode de commande utilisant des dispositifs du type thyratron ou thyristor exigeant des moyens d'extinction utilisant uniquement des dispositifs à semi-conducteurs agencés pour la marche en parallèle
94.
APPARATUS AND PROCESS TO CONTROL PROVIDING PURIFIED WATER FOR HYDROGEN PRODUCTION
An apparatus to provide purified water to one or more electrolyzers for manufacture of hydrogen can include a polisher positioned to receive at least a minimum flow of water from a demineralization unit to purify the water and output the purified water to at least one electrolyzer of an electrolyzer house. The flow of water can be adjusted to maintain a minimum flow of water passing through one or more beds of the polisher while accounting for the demand of water at the electrolyzers. Flow adjustments can be made between providing all the purified water to the electrolyzers during high demand operations to other configurations in which little or no purified water is fed to the electrolyzers and, instead, that water is recycled back to the water demineralization unit.
Residual ammonia is removed effectively from ammonia cracked gas in a hydrogen PSA system using a non-zeolitic adsorbent such as activated carbon, activated alumina or silica gel.
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
96.
APPARATUS AND PROCESS TO CONTROL PROVIDING OF ELECTROLYZER WATER FOR HYDROGEN PRODUCTION
An apparatus to purify water and provide the purified water to one or more electrolyzers for manufacture of hydrogen can include a purification unit positioned to receive water from a demineralization unit to purify the water and output the purified water to at least one electrolyzer of an electrolyzer house. The flow of water can be adjusted to maintain a minimum flow of water passing through one or more beds of a polisher while accounting for the demand of water at the electrolyzers. Flow adjustments can be made between providing all the purified water to the electrolyzers during high demand operations to other configurations in which little or no purified water is fed to the electrolyzers and, instead, that water is recycled back to the water purification unit.
C25B 15/08 - Alimentation ou vidange des réactifs ou des électrolytesRégénération des électrolytes
C02F 1/28 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par absorption ou adsorption
C02F 1/469 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par des procédés électrochimiques par séparation électrochimique, p. ex. par électro-osmose, électrodialyse, électrophorèse
C25B 1/04 - Hydrogène ou oxygène par électrolyse de l'eau
C25B 9/70 - Assemblages comprenant plusieurs cellules
C25B 15/02 - Commande ou régulation des opérations
97.
Process and Apparatus for Xenon and or Krypton Recovery
Recovering xenon and/or krypton from a feed gas can include utilization of a purge stream from a separation column positioned and configured to output at least one stream of fluid that is substantially nitrogen and at least one stream of fluid that is substantially oxygen. The purge stream can be split so that a first portion of the purge stream is fed as a liquid adjacent to a top of a purge treatment column and a second portion of the purge stream can be fed to a heat exchanger for superheating the second portion to feed a superheated vapor at or adjacent to a bottom of the purge treatment column. The purge treatment column can output a liquid stream that has a relatively high concentration of Xe and/or Kr therein as a feed stream for an Xe and/or Kr recovery system.
A method for pyrolysing a methane-rich stream to produce hydrogen and a solid carbon intermediate. The solid carbon intermediate may then be transported to a second location to be gasified to produce hydrogen and carbon dioxide, the latter of which may be sequestered at the second location. Because the solid carbon intermediate may be transported more easily than carbon dioxide, this allows the decoupling of hydrogen production from carbon dioxide sequestration.
C01B 3/24 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés organiques gazeux ou liquides d'hydrocarbures
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
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
A method for heating reactor using a multi-function burner comprising feeding primary fuel through an annular channel, feeding oxygen through a central channel within the annular channel, and feeding an auxiliary fuel through a central lance within the central channel to produce a flame extending into a furnace having a temperature and a pressure; wherein the flow rate of the auxiliary fuel and oxygen are increased while maintaining an equivalence ratio below 1 to increase the temperature of the furnace; wherein after the furnace temperature exceeds the auto-ignition temperature of the primary fuel, increasing the flow rate of the primary fuel to increase the equivalence ratio to be greater than 1.
F23D 14/32 - Brûleurs pour la combustion d'un gaz, p. ex. d'un gaz stocké sous pression à l'état liquide utilisant un mélange de combustible gazeux et d'oxygène pur ou d'air enrichi d'oxygène
F23D 14/58 - Buses caractérisés par la forme ou la disposition de l'orifice ou des orifices des buses, p. ex. en couronne
An apparatus and process for oxygen production can be configured to utilize flash vapor losses, recovery of regeneration heat and/or utilize a compressor to provide better heat integration and/or less wasteful processing for the recovery of oxygen that can be obtained from electrolysis (e.g., operation of one or more electrolyzers). Some embodiments may utilize all three of these features while other embodiments may use only one of these features or a combination of two of these features.
B01D 53/04 - 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 avec adsorbants fixes
