公开(公告)号：US12129170B2

公开(公告)日：2024-10-29

申请号：US17712551

申请日：2022-04-04

申请人： Casale SA

发明人： Iacopo Cerea ,  Jean Francois Granger

IPC分类号： C01B21/28 ,  B01D53/14 ,  B01D53/56 ,  B01D53/78 ,  C01B21/46

CPC分类号： C01B21/46 ,  B01D53/1493 ,  B01D53/56 ,  B01D53/78 ,  C01B21/28 ,  B01D2252/103 ,  B01J2219/00024

摘要： A dual-pressure plant for the synthesis of nitric acid comprising: a reactor (4) providing a gaseous effluent (15) containing nitrogen oxides; an absorption tower (6) nitrogen oxides react with water providing raw nitric acid and, said absorption tower operating at a pressure greater than the pressure of the reactor; a compressor (5) elevating the pressure of the reactor effluent (15) to the absorption pressure; said plant also comprising a first bleacher (37) and a second bleacher (7), said first bleacher (37) stripping with air (39) nitrogen oxides from the output stream (27) of the absorption tower (6) providing a partially stripped nitric acid stream (40) and a nitrogen oxides-loaded air stream (41), the former being fed to the second bleacher (7) and the latter being recycled to the delivery-side of said compressor (5).

公开(公告)号：US20240343593A1

公开(公告)日：2024-10-17

申请号：US18133611

申请日：2023-04-12

申请人： L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude

发明人： Michael LUTZ ,  Lorenzo VICARI ,  Swatantra Kumar SHRIVASTAVA ,  Dieter ULBER

IPC分类号： C01C1/12 ,  B01D53/14 ,  C01B3/04 ,  C01B3/52

CPC分类号： C01C1/12 ,  B01D53/1418 ,  C01B3/047 ,  C01B3/52 ,  B01D2252/103 ,  B01D2257/406 ,  C01B2203/0415 ,  C01B2203/0465

摘要： A method of separating and reusing unconverted ammonia from cracked ammonia gas provided by an ammonia cracking unit is provided. The method includes introducing a cracked ammonia gas stream into a water wash column, thereby producing a clean gas stream and a water-containing effluent stream and introducing the water-containing effluent stream into a stripping column, thereby producing a cleaned wash water stream and a recovered ammonia stream. Wherein the cracked ammonia gas stream has an ammonia concentration of between 0.003 mol % and 10 mol %. Wherein the clean gas stream has an ammonia concentration of between 1 10 ppm and 2500 ppm. And wherein at least a portion of the recovered ammonia stream is used as fuel within the ammonia cracking unit.

公开(公告)号：US20240335787A1

公开(公告)日：2024-10-10

申请号：US18575802

申请日：2022-06-30

申请人： Hans Gude GUDESEN

发明人： Hans Gude GUDESEN

IPC分类号： B01D53/14

CPC分类号： B01D53/1475 ,  B01D2252/103 ,  B01D2257/504 ,  B01D2258/0283

摘要： A method for extracting CO2 from a gas mixture comprising CO2 is disclosed. The method comprises dispensing the gas mixture in water in a first water volume, dissolving CO2 in the first water volume resulting in water enriched in dissolved 5CO2, and passing the water enriched in dissolved CO2 through a turbine. A corresponding system is also disclosed.

公开(公告)号：US20240318090A1

公开(公告)日：2024-09-26

申请号：US18547269

申请日：2022-03-04

申请人： ExxonMobil Chemical Patents Inc.

发明人： Mark A. Nierode ,  James L. Kendall

IPC分类号： C10G70/04 ,  B01D53/04 ,  B01D53/14 ,  C10G9/36 ,  C10G70/06

CPC分类号： C10G70/046 ,  B01D53/04 ,  B01D53/1493 ,  C10G9/36 ,  C10G70/06 ,  B01D2251/60 ,  B01D2252/103 ,  B01D2252/204 ,  B01D2256/24 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/308 ,  B01D2259/4009 ,  C10G2300/207

摘要： Processes and systems for upgrading a hydrocarbon. In some embodiments, the process for upgrading a hydrocarbon, can include contacting a gas that can include one or more C1-C4 hydrocarbons and carbonyl sulfide with a sorbent under conditions sufficient to cause at least a portion of the carbonyl sulfide to sorb onto the sorbent to produce a treated gas lean in carbonyl sulfide and a sorbent rich in carbonyl sulfide. The process can also include contacting the sorbent rich in carbonyl sulfide with a regenerating gas that can include molecular hydrogen, one or more C1-C4 hydrocarbons, or a mixture thereof to produce a regenerated sorbent and a desorb effluent that can include a sulfur-based contaminant. The process can also include introducing at least a portion of the desorb effluent into a pyrolysis zone of a steam cracker and recovering a steam cracker effluent from the pyrolysis zone.

公开(公告)号：US12077435B2

公开(公告)日：2024-09-03

申请号：US18233028

申请日：2023-08-11

申请人： ThermoChem Recovery International, Inc.

发明人： Ravi Chandran ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC分类号： C01B3/52 ,  B01D5/00 ,  B01D17/02 ,  B01D29/27 ,  B01D29/66 ,  B01D46/00 ,  B01D47/10 ,  B01D50/60 ,  B01D53/04 ,  B01D53/047 ,  B01D53/12 ,  B01D53/14 ,  B01D53/18 ,  B01D53/26 ,  B01D53/32 ,  B01D53/48 ,  B01D53/76 ,  B01D61/36 ,  C01B3/24 ,  C01B3/38 ,  C01B3/56 ,  C01B3/58

CPC分类号： C01B3/52 ,  B01D5/0027 ,  B01D5/006 ,  B01D5/0072 ,  B01D5/0075 ,  B01D5/009 ,  B01D17/0208 ,  B01D29/27 ,  B01D29/66 ,  B01D46/0036 ,  B01D47/10 ,  B01D50/60 ,  B01D53/0423 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/0476 ,  B01D53/12 ,  B01D53/1406 ,  B01D53/1412 ,  B01D53/1431 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1487 ,  B01D53/18 ,  B01D53/265 ,  B01D53/326 ,  B01D53/48 ,  B01D53/76 ,  B01D61/3621 ,  C01B3/24 ,  C01B3/38 ,  C01B3/382 ,  C01B3/386 ,  C01B3/56 ,  C01B3/58 ,  H05K999/99 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/20436 ,  B01D2252/504 ,  B01D2252/602 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2257/60 ,  B01D2257/708 ,  B01D2259/402 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/0877 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/147 ,  C01B2203/84 ,  Y02P20/129 ,  Y02P30/00

摘要： A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

公开(公告)号：US20240239454A1

公开(公告)日：2024-07-18

申请号：US18561519

申请日：2022-05-27

申请人： Maersk A/S

发明人： Jorn KAHLE ,  Toby AUSTIN-FRASER

IPC分类号： B63B81/00 ,  B01D53/18 ,  B01D53/50 ,  F16L7/02 ,  F16L55/165 ,  F16L58/10

CPC分类号： B63B81/00 ,  F16L7/02 ,  F16L55/1657 ,  F16L58/1036 ,  B01D53/18 ,  B01D53/50 ,  B01D2252/103 ,  B01D2257/302 ,  B01D2259/4566 ,  B63B2221/10

摘要： Disclosed is a method (200) of assembling a vessel overboard discharge assembly (600), the method (200) comprising: inserting (210) a tubular insert (500) into an overboard discharge pipe (300) so that a space (400) is defined between the tubular insert (500) and the overboard discharge pipe (300): blocking (221) an outboard opening (401) into the space (400) at an outboard end (301) of the space (400): and providing (280) in the space (400) an adhesive (450) and/or chocking material (450) for adhering and/or chocking the tubular insert (500) in the overboard discharge pipe (300).

公开(公告)号：US20240198280A1

公开(公告)日：2024-06-20

申请号：US18279366

申请日：2022-03-03

申请人： Greenlyte Carbon Technologies GmbH

发明人： Peter Behr

IPC分类号： B01D53/14

CPC分类号： B01D53/1475 ,  B01D53/1493 ,  B01D2252/103 ,  B01D2257/504

摘要： In an embodiment a method includes loading an absorbent with a carbon dioxide in a first device, wherein a hydrogen carbonate-containing solution is formed, feeding the hydrogen carbonate-containing solution from the first device into an electrolysis unit, electrolyzing the hydrogen carbonate-containing solution in the electrolysis unit to release carbon dioxide, wherein a carbonate-rich solution is formed in the electrolysis unit, forming oxygen, hydrogen and carbon dioxide in the electrolysis unit, and recycling the carbonate-rich solution from the electrolysis unit to the first device.

公开(公告)号：US20240181379A1

公开(公告)日：2024-06-06

申请号：US18423450

申请日：2024-01-26

申请人： Karim SALEHPOOR

发明人： Karim SALEHPOOR

IPC分类号： B01D46/58 ,  A01G15/00 ,  B01D45/18 ,  B01D46/00 ,  B01D46/12 ,  B01D46/42 ,  B01D46/62 ,  B01D47/02 ,  B01D47/06 ,  B01D50/60 ,  B01D53/14 ,  B01D53/18 ,  E03B3/28 ,  F01N3/04 ,  F23J15/04

CPC分类号： B01D46/58 ,  A01G15/00 ,  B01D46/0031 ,  B01D46/0087 ,  B01D46/12 ,  B01D46/4218 ,  B01D46/4254 ,  B01D46/645 ,  B01D47/02 ,  B01D47/021 ,  B01D47/06 ,  B01D50/60 ,  B01D53/14 ,  B01D53/145 ,  B01D53/1475 ,  B01D53/18 ,  E03B3/28 ,  F01N3/04 ,  F23J15/04 ,  B01D45/18 ,  B01D2252/103 ,  B01D2252/20 ,  B01D2279/30 ,  B01D2279/40 ,  Y02C20/40

摘要： Disclosed are a pollutant capturer and mobilizer and method of mobilizing a polluted gaseous substance from one location towards another location and capturing one or multiple types of polluting substances, such as CO2, from an atmospheric body of polluted gaseous substance or from exhaust of vehicles, chimneys, or stacks and thereby combat the negative health, environmental, and economic impacts of the of the polluting substances on communities. Wet or dry embodiments of the pollutant capturer and mobilizer utilize wet or dry pollutant capturing components, respectively, to capture one or multiple types of polluting substances from a body of polluted gaseous substance. Flow-establishing devices can be used to set the body of polluted gaseous substance in motion through the pollutant capturing component. The pollutant capturer and mobilizer may also be mounted on any type of vehicle, with or without using flow-establishing devices.

公开(公告)号：US20240109776A1

公开(公告)日：2024-04-04

申请号：US17958938

申请日：2022-10-03

申请人： Saudi Arabian Oil Company

发明人： Mohammad Saad AlQahtani ,  Seung-Hak Choi

IPC分类号： C01B17/04 ,  B01D19/00 ,  B01D53/14 ,  B01D53/86

CPC分类号： C01B17/0456 ,  B01D19/0031 ,  B01D53/1481 ,  B01D53/8612 ,  B01D53/864 ,  C01B17/0413 ,  C01B17/0426 ,  B01D2252/103

摘要： A system and method for removing sulfur compounds from gas, including discharging tail gas having sulfur compounds from a sulfur recovery unit (SRU) to a non-thermal plasma (NTP) catalytic unit including an NTP reactor, providing oxidant to the NTP reactor and placing the oxidant in an NTP state in the NTP reactor to give an oxidative reactive species formed from the oxidant, converting (oxidizing) the sulfur compounds with the oxidative reactive species and catalyst in the NTP catalytic unit into sulfur oxides (SOx) to discharge the tail gas as treated having the formed SOx without the sulfur compounds that were converted. The SOx is absorbed into water in a quench tower to give the tail gas beneficially having only small amounts (e.g., less than 200 ppmv) of sulfur compounds. SOx may be degassed from water discharged from the quench tower and sent to the SRU furnace.

公开(公告)号：US20240091702A1

公开(公告)日：2024-03-21

申请号：US18509956

申请日：2023-11-15

申请人： Robert George Richardson

发明人： Robert George Richardson

IPC分类号： B01D53/60 ,  B01D19/00 ,  B01D53/14 ,  B01D53/50 ,  B01D53/56 ,  B01D53/62 ,  B01D53/73 ,  B01D53/76 ,  B01D53/78 ,  B01D53/96 ,  C01D5/02 ,  C01D7/07 ,  C01D7/12 ,  C01D9/06 ,  C01D13/00 ,  C25B1/34

CPC分类号： B01D53/60 ,  B01D19/0005 ,  B01D53/1406 ,  B01D53/1425 ,  B01D53/1475 ,  B01D53/1481 ,  B01D53/1493 ,  B01D53/502 ,  B01D53/56 ,  B01D53/62 ,  B01D53/73 ,  B01D53/76 ,  B01D53/78 ,  B01D53/96 ,  C01D5/02 ,  C01D7/07 ,  C01D7/12 ,  C01D9/06 ,  C01D13/00 ,  C25B1/34 ,  B01D2251/302 ,  B01D2251/304 ,  B01D2251/306 ,  B01D2251/604 ,  B01D2252/103 ,  B01D2252/2021 ,  B01D2252/205 ,  B01D2252/504 ,  B01D2257/302 ,  B01D2257/404 ,  B01D2257/504

摘要： The disclosure provides seven integrated methods for the chemical sequestration of carbon dioxide (CO2), nitric oxide (NO), nitrogen dioxide (NO2) (collectively NO2, where x=1, 2) and sulfur dioxide (SO2) using closed loop technology. The methods recycle process reagents and mass balance consumable reagents that can be made using electrochemical separation of sodium chloride (NaCl) or potassium chloride (KCl). The technology applies to marine and terrestrial exhaust gas sources for CO2, NOx and SO2. The integrated technology combines compatible and green processes that capture and/or convert CO2, NOx and SO2 into compounds that enhance the environment, many with commercial value.