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21.
公开(公告)号:US20190201830A1
公开(公告)日:2019-07-04
申请号:US16326920
申请日:2018-05-04
发明人: Zhaoxiang ZHONG , Feng ZHANG , Junwei WU
IPC分类号: B01D46/54 , B01D46/42 , B01D46/00 , B01D46/44 , B01D46/46 , B01D39/20 , B01D39/16 , B01D53/78 , B01D53/48 , B01D53/80 , F23G7/00 , F23G5/50 , F23G5/08 , F23G5/16
CPC分类号: B01D46/543 , B01D39/16 , B01D39/2068 , B01D46/0027 , B01D46/0071 , B01D46/4263 , B01D46/448 , B01D46/46 , B01D53/48 , B01D53/78 , B01D53/80 , B01D2239/1216 , B01D2251/2062 , B01D2251/304 , B01D2251/404 , B01D2251/606 , B01D2251/608 , B01D2257/30 , B01D2273/20 , B01D2275/10 , F23G5/08 , F23G5/16 , F23G5/50 , F23G7/008 , F23G7/04 , F23J15/02
摘要: A membrane method processing system and process for a high-concentration salt-containing organic waste liquid incineration exhaust gas is described. The system consists essentially of a waste liquid incinerator (I), a gas-solid separator (II), a heat exchanger (III), an air blower (IV), an anti-caking agent storage tank (V), a membrane method dust cleaner (VI), an induced draft fan (VII), a check valve (VIII), and a desulfurization tower (IX). The present invention introduces the dust collecting membrane into the tail gas treatment system and utilizes the small pore size and high porosity of the dust collecting membrane to prevent inorganic salt particles from entering the internal of the filter material and agglomerating there. When the humidity of the gas entering the dust collector increases during the dust removing process, the anti-caking agent is also introduced into the tail gas treatment system to change the surface structure of the inorganic salt crystal to prevent the crystal from agglomeration.
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公开(公告)号:US10316257B2
公开(公告)日:2019-06-11
申请号:US15965228
申请日:2018-04-27
申请人: NexoSolutions LLC
IPC分类号: C10G53/12 , B01D53/75 , C10L3/12 , B01D53/54 , C10G29/22 , C10G31/08 , B01D53/48 , B01D53/62 , B01D53/78 , B01D53/79 , C10L3/10
摘要: A system for removing mercaptan contaminants from both liquid and gaseous hydrocarbon streams and methods thereof are described. An additive that reacts with said contaminant to form water-soluble compounds is injected into the hydrocarbon streams.
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23.
公开(公告)号:US20190118137A1
公开(公告)日:2019-04-25
申请号:US16222344
申请日:2018-12-17
申请人: START-CATALYST LLC
发明人: Liudmila Aleksandrovna TYURINA , Alexander Ivanovich TYURIN , Irina Gennadievna TARKHANOVA , Alexey Aleksandrovich TYURIN
CPC分类号: B01D53/52 , B01D53/26 , B01D53/263 , B01D53/48 , B01D53/86 , B01D53/8603 , B01D2251/102 , B01D2255/20738 , B01D2255/20761 , B01D2255/705 , B01D2256/24 , B01D2257/304 , B01D2257/306 , B01J27/122 , B01J31/00
摘要: This application is in the field of technologies for desulfurization and demercaptanization of gaseous hydrocarbons. The device includes a catalytic reactor loaded with a catalyst solution in an organic solvent, a means of withdrawal sulfur solution from the reactor into the sulfur-separating unit, and a sulfur-separating unit. The said device has at least means of supplying gaseous hydrocarbon medium to be purified and oxygen-containing gas into the reactor, and a means of outletting the purified gas from the reactor. The sulfur-separation unit includes a means of sulfur extraction. The reactor design and the catalyst composition provide conversion of at least 99.99% of hydrogen sulfide and mercaptans into sulfur and disulfides. The catalyst is composed of mixed-ligand complexes of transition metals. The technical result achieved by use of claimed invention is single-stage purification of gaseous hydrocarbons from hydrogen sulfide and mercaptans with remaining concentration of —SH down up to 0.001 ppm.
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24.
公开(公告)号:US10213740B2
公开(公告)日:2019-02-26
申请号:US15539867
申请日:2016-07-04
申请人: START-CATALYST LLC
发明人: Liudmila Aleksandrovna Tyurina , Alexander Ivanovich Tyurin , Irina Gennadievna Tarkhanova , Alexey Aleksandrovich Tyurin
IPC分类号: B01D53/52 , B01D53/86 , B01D53/26 , B01D53/48 , B01J27/122
摘要: This application is in the field of technologies for desulfurization and demercaptanization of gaseous hydrocarbons. The device includes a catalytic reactor loaded with a catalyst solution in an organic solvent, a means of withdrawal sulfur solution from the reactor into the sulfur-separating unit, and a sulfur-separating unit. The said device has at least means of supplying gaseous hydrocarbon medium to be purified and oxygen-containing gas into the reactor, and a means of outletting the purified gas from the reactor. The sulfur-separation unit includes a means of sulfur extraction. The reactor design and the catalyst composition provide conversion of at least 99.99% of hydrogen sulfide and mercaptans into sulfur and disulfides. The catalyst is composed of mixed-ligand complexes of transition metals. The technical result achieved by use of claimed invention is single-stage purification of gaseous hydrocarbons from hydrogen sulfide and mercaptans with remaining concentration of —SH down up to 0.001 ppm.
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25.
公开(公告)号:US20190010052A1
公开(公告)日:2019-01-10
申请号:US16128586
申请日:2018-09-12
摘要: A method for increasing sulfur recovery from an acid gas feed comprising the steps of introducing the acid gas feed and a sulfur dioxide enriched air stream to a Claus process to produce a product gas stream, introducing the product gas stream to a thermal oxidizer to produce a flue gas stream, cooling the flue gas stream to produce a cooled take-off stream, separating the cooled take-off stream into a saturated gas stream, heating the saturated gas stream to produce a membrane gas stream, introducing the membrane gas stream to a membrane sweeping unit, the membrane sweeping unit comprises a membrane, the sulfur dioxide in the membrane gas stream permeates the membrane of the membrane sweeping unit, introducing a sweep air stream, the sweep air stream collects the sulfur dioxide to create the sulfur dioxide enriched air stream.
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公开(公告)号:US10065148B2
公开(公告)日:2018-09-04
申请号:US14382108
申请日:2013-03-01
发明人: Marty Lail , Luke Coleman
摘要: A solvent system for the removal of acid gases from mixed gas streams is provided. Also provided is a process for removing acid gases from mixed gas streams using the disclosed solvent systems. The solvent systems may be utilized within a gas processing system.
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公开(公告)号:US20180245005A1
公开(公告)日:2018-08-30
申请号:US15965075
申请日:2018-04-27
申请人: NexoSolutions LLC
IPC分类号: C10G53/12 , C10L3/10 , B01D53/48 , B01D53/62 , B01D53/75 , B01D53/78 , B01D53/79 , B01D53/54 , C10G29/22 , C10G31/08 , C10L3/12
CPC分类号: C10G53/12 , B01D53/485 , B01D53/54 , B01D53/62 , B01D53/75 , B01D53/78 , B01D53/79 , B01D2251/10 , B01D2251/21 , B01D2256/24 , B01D2257/306 , B01D2257/308 , B01D2257/40 , B01D2257/504 , C10G29/22 , C10G31/08 , C10G2300/202 , C10L3/101 , C10L3/103 , C10L3/12 , C10L2290/141 , C10L2290/146 , C10L2290/24 , C10L2290/541 , C10L2290/544 , C10L2290/547 , Y02C10/04
摘要: A method for removing amine contaminants from both liquid and gaseous hydrocarbon streams and methods thereof are described. An additive that reacts with said contaminant to form water-soluble compounds is injected into the hydrocarbon streams.
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公开(公告)号:US09982201B2
公开(公告)日:2018-05-29
申请号:US14557684
申请日:2014-12-02
申请人: NexoSolutions LLC
IPC分类号: C10G53/12 , B01D53/54 , B01D53/62 , B01D53/78 , B01D53/79 , C10G31/08 , C10L3/12 , C10G29/22 , B01D53/48 , B01D53/75 , C10L3/10
CPC分类号: C10G53/12 , B01D53/485 , B01D53/54 , B01D53/62 , B01D53/75 , B01D53/78 , B01D53/79 , B01D2251/10 , B01D2251/21 , B01D2256/24 , B01D2257/306 , B01D2257/308 , B01D2257/40 , B01D2257/504 , C10G29/22 , C10G31/08 , C10G2300/202 , C10L3/101 , C10L3/103 , C10L3/12 , C10L2290/141 , C10L2290/146 , C10L2290/24 , C10L2290/541 , C10L2290/544 , C10L2290/547 , Y02C10/04
摘要: A system for removing contaminants from both liquid and gaseous hydrocarbon streams and methods thereof are described. An additive that reacts with said contaminant to form water-soluble compounds is injected into the hydrocarbon streams.
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公开(公告)号:US09957029B2
公开(公告)日:2018-05-01
申请号:US15417244
申请日:2017-01-27
CPC分类号: B63H21/32 , B01D53/18 , B01D53/48 , B01D53/50 , B01D53/78 , B01D2258/0283 , B01D2259/4566 , F01N3/04 , F01N3/08
摘要: An exhaust gas processing apparatus that processes exhaust gas, including a reaction tower that includes an internal space extending in a height direction; a trunk tube that extends in the height direction in the internal space of the reaction tower and transports a liquid; and a plurality of branch tubes that are provided extending from an outer side surface of the trunk tube toward an inner side surface of the reaction tower, each include an ejecting section that ejects the liquid supplied from the trunk tube, and are provided at positions at different heights. Ejection regions of the liquid where the liquid is ejected from the respective ejecting sections of branch tubes that are adjacent in the height direction include a region in which the ejection regions partially overlap in an overhead view as seen from the height direction.
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公开(公告)号:US20180038642A1
公开(公告)日:2018-02-08
申请号:US15414170
申请日:2017-01-24
CPC分类号: F25J1/023 , B01D53/047 , B01D53/48 , B01D2256/16 , B01D2256/24 , B01D2257/30 , B01D2259/40086 , C01B3/34 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/042 , C01B2203/043 , C01B2203/046 , C01B2203/061 , C01B2203/1241 , C01B2203/1258 , F25J1/001 , F25J1/0015 , F25J1/0022 , F25J1/0037 , F25J1/004 , F25J1/0045 , F25J1/005 , F25J1/0072 , F25J1/0204 , F25J1/0221 , F25J1/0229 , F25J1/0232 , F25J1/0234 , F25J1/0236 , F25J1/0244 , F25J1/0245 , F25J1/0282 , F25J1/0288 , F25J1/0292 , F25J1/0294 , F25J3/04018 , F25J3/04024 , F25J3/04121 , F25J3/04412 , F25J3/04563 , F25J3/04593 , F25J3/046 , F25J2205/66 , F25J2210/06 , F25J2210/12 , F25J2210/40 , F25J2210/42 , F25J2210/60 , F25J2215/40 , F25J2220/64 , F25J2230/20 , F25J2230/30 , F25J2230/32 , F25J2230/40 , F25J2230/42 , F25J2230/60 , F25J2245/02 , F25J2245/40 , F25J2245/42 , F25J2260/44 , F25J2270/04 , F25J2270/06 , F25J2270/14 , F25J2270/16
摘要: It is proposed to integrate a gas processing unit with a liquefaction unit. The industrial gas stream may be but is not limited to air gases of oxygen, nitrogen argon, hydrocarbon, LNG, syngas or its components, CO2, or any other molecule or combination of molecules. It is proposed to integrate the underutilized process inefficiencies of a gas processing unit into the liquefaction unit to produce a liquid at a reduced operating cost. The gas processing unit may be any system or apparatus which alters the composition of a feed gas. Examples could be, but are not limited to, a methanol plant, steam methane reformer, cogeneration plant, and partial oxidation unit.
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