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公开(公告)号：US20210131727A1
公开(公告)日：2021-05-06
申请号：US16670281
申请日：2019-10-31
IPC分类号： F25J3/02
摘要： Light gases such as helium are extacted from a carbon dioxide-containing feed stream by distillation. Costly dehydration steps are avoided by pumping the liquid bottoms stream leaving the distillation column without vaporization so as to ensure that any water present in the feed remains in solution with the bulk stream leaving the process. This prevents any liquid phase water causing corrosion or solid ice or hydrates forming to plug the flow.
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公开(公告)号：US20150184932A1
公开(公告)日：2015-07-02
申请号：US14143781
申请日：2013-12-30
IPC分类号： F25J3/08
CPC分类号： F25J3/08 , B01D3/143 , C10G5/06 , C10G7/00 , C10G70/041 , E21B43/164 , E21B43/40 , F25J3/0209 , F25J3/0242 , F25J3/0266 , F25J2200/02 , F25J2200/04 , F25J2200/30 , F25J2200/50 , F25J2200/72 , F25J2200/74 , F25J2200/76 , F25J2205/50 , F25J2215/02 , F25J2220/84 , F25J2260/60 , F25J2260/80 , F25J2270/12 , F25J2270/60 , F25J2270/88 , Y02C10/12 , Y02P90/70
摘要： The power required to recover C3+ hydrocarbons from crude carbon dioxide comprising C1+ hydrocarbons and hydrogen sulfide may be reduced by distilling the crude carbon dioxide to produce carbon dioxide-enriched overhead vapor and C3+ hydrocarbon-enriched bottoms liquid such that the hydrogen sulfide is rejected with the overhead vapor. Power consumption reductions may be achieved by incorporating a heat pump cycle using carbon dioxide vapor as working fluid to provide at least a part of the refrigeration duty and using a side reboiler to reduce the bottom reboiler duty. Where the bottoms liquid is further processed to produce “lighter” and “heavier” hydrocarbon fractions, the process enables optimization of upgrading crude oil on the basis of API gravity, Reid Vapor pressure and/or viscosity.
摘要翻译： 通过蒸馏粗二氧化碳以产生富含二氧化碳的塔顶蒸气和C3 +烃富集的塔底液，可以减少从包含C1 +烃和硫化氢的粗二氧化碳中回收C3 +烃所需的功率，从而使硫化氢与 塔顶蒸气。 可以通过将使用二氧化碳蒸气作为工作流体的热泵循环结合以提供至少一部分制冷功能并使用侧再沸器来减少底部再沸器的负荷来实现功率消耗降低。 当底部液体被进一步加工以产生“较轻”和“较重”的烃馏分时，该方法能够根据API重力，Reid蒸气压力和/或粘度优化升级原油。
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公开(公告)号：US10655912B2
公开(公告)日：2020-05-19
申请号：US14521062
申请日：2014-10-22
摘要： Impurities that are less volatile than carbon dioxide, e.g. hydrogen sulfide, are removed from crude carbon dioxide by processes involving distillation of said crude carbon dioxide in a distillation column system operating at super-atmospheric pressure(s) to produce carbon dioxide-enriched overhead vapor and bottoms liquid enriched with said impurities. Where such processes involve a single heat pump cycle, significant savings in power consumption are realized when the distillation column system is re-boiled by at least partially vaporizing liquid in or taken from an intermediate location in the column system.
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公开(公告)号：US10060348B2
公开(公告)日：2018-08-28
申请号：US14496240
申请日：2014-09-25
CPC分类号： F02C3/22 , B01D53/22 , B01D53/229 , B01D2053/221 , B01D2256/245 , B01D2257/504 , C10L3/104 , F02C9/28 , F02C9/40 , F23R3/36 , Y02C10/04 , Y02C10/10 , Y02E20/16
摘要： Carbon dioxide is separated from natural gas using a single stage membrane separation system to produce a retentate gas that typically meets the specification for pipeline distribution of natural gas, and a permeate gas comprising methane that is combusted to generate power and/or heat, e.g. for use in providing the utility requirements of the process itself or for export to an integrated process. Advantages include an overall reduction in power consumption and improvement in process efficiency.
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公开(公告)号：US20150114034A1
公开(公告)日：2015-04-30
申请号：US14063067
申请日：2013-10-25
IPC分类号： F25J3/08
CPC分类号： F25J3/08 , B01D53/002 , B01D53/75 , B01D2257/302 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/404 , B01D2257/406 , B01D2257/7022 , C01B17/167 , C01B32/50 , F25J2200/02 , F25J2200/04 , F25J2200/40 , F25J2200/50 , F25J2200/74 , F25J2200/76 , F25J2200/78 , F25J2205/02 , F25J2215/80 , F25J2220/82 , F25J2220/84 , F25J2230/80 , F25J2235/02 , F25J2235/80 , F25J2240/40 , F25J2245/02 , F25J2260/20 , F25J2260/80 , F25J2270/02 , F25J2270/80 , F25J2270/88 , F25J2290/40 , Y02P20/129 , Y02P20/152
摘要： In a process for separating “heavy” impurities such as hydrogen sulfide from crude carbon dioxide comprising significant quantities of “light” impurities such as non-condensable gases, involving at least one heat pump cycle using as working fluid a fluid from the “heavy” impurity separation, the “light” impurities are removed from carbon dioxide-enriched gas generated in the “heavy” impurity separation. The carbon dioxide-enriched gas, or a compressed carbon dioxide-enriched gas produced therefrom, is at least partially condensed by indirect heat exchange against intermediate liquid also generated in the “heavy” impurity separation. Total and specific energy consumption is reduced compared to conventional processes in which “light” impurities are removed from carbon dioxide product gas.
摘要翻译： 在从包含大量“轻”杂质如不可冷凝气体的粗二氧化碳中分离“重”杂质如硫化氢的方法中，涉及使用作为工作流体的至少一个热泵循环，来自“重” 杂质分离，从“重”杂质分离产生的富含二氧化碳的气体中除去“轻”杂质。 由二氧化碳富集的气体或由其产生的压缩的富含二氧化碳的气体通过与在“重”杂质分离中也产生的中间体液体的间接热交换至少部分地冷凝。 与从二氧化碳产品气体中除去“轻”杂质的常规方法相比，总的和比能量消耗降低。
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公开(公告)号：US20130127163A1
公开(公告)日：2013-05-23
申请号：US13674189
申请日：2012-11-12
发明人： John Eugene Palamara , Fabrice Amy
CPC分类号： F02C3/30 , C01B3/382 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/0475 , C01B2203/148 , C01B2203/84 , F01K17/025 , F01K23/067 , Y02E20/14 , Y02E20/16 , Y02E20/18 , Y02P20/129 , Y02P20/13
摘要： Systems and methods are provided for generating and using decarbonized fuel for power generation. In particular, the integrated systems and methods are provided for generating a synthesis gas, removing carbon dioxide from the synthesis gas and using the synthesis gas for producing power.
摘要翻译： 提供用于产生和使用脱碳燃料用于发电的系统和方法。 特别地，集成的系统和方法被提供用于产生合成气，从合成气中除去二氧化碳并使用合成气来产生电力。
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公开(公告)号：US10267560B2
公开(公告)日：2019-04-23
申请号：US14143781
申请日：2013-12-30
IPC分类号： F25J3/00 , F25J3/02 , F25J3/08 , E21B43/16 , E21B43/40 , C10G70/04 , C10G7/00 , B01D3/14 , C10G5/06
摘要： The power required to recover C3+ hydrocarbons from crude carbon dioxide comprising C1+ hydrocarbons and hydrogen sulfide may be reduced by distilling the crude carbon dioxide to produce carbon dioxide-enriched overhead vapor and C3+ hydrocarbon-enriched bottoms liquid such that the hydrogen sulfide is rejected with the overhead vapor. Power consumption reductions may be achieved by incorporating a heat pump cycle using carbon dioxide vapor as working fluid to provide at least a part of the refrigeration duty and using a side reboiler to reduce the bottom reboiler duty. Where the bottoms liquid is further processed to produce “lighter” and “heavier” hydrocarbon fractions, the process enables optimization of upgrading crude oil on the basis of API gravity, Reid Vapor pressure and/or viscosity.
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公开(公告)号：US20150114033A1
公开(公告)日：2015-04-30
申请号：US14063047
申请日：2013-10-25
IPC分类号： F25J3/08
CPC分类号： F25J3/08 , B01D53/002 , B01D53/75 , B01D2257/302 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/404 , B01D2257/406 , B01D2257/7022 , C01B17/167 , C01B32/50 , F25J3/0266 , F25J3/029 , F25J2200/04 , F25J2200/08 , F25J2200/10 , F25J2200/40 , F25J2200/50 , F25J2200/70 , F25J2200/74 , F25J2200/76 , F25J2200/78 , F25J2205/02 , F25J2205/30 , F25J2205/40 , F25J2205/80 , F25J2220/82 , F25J2220/84 , F25J2230/80 , F25J2235/02 , F25J2235/80 , F25J2240/40 , F25J2245/02 , F25J2260/20 , F25J2260/80 , F25J2270/02 , F25J2270/80 , F25J2270/88 , F25J2290/40 , Y02B30/52 , Y02C10/12 , Y02P20/124 , Y02P20/129 , Y02P20/152
摘要： In a process for separating at least one “heavy” impurity such as hydrogen sulfide from crude carbon dioxide comprising significant quantities of at least one “light” impurity such as non-condensable gases, involving at least one heat pump cycle using carbon dioxide-containing fluid from the process as the working fluid, the “light” impurity is removed from the crude carbon dioxide and carbon dioxide is subsequently recovered from the removed “light” impurity, thereby improving overall carbon dioxide recovery and efficiency in terms of energy consumption.
摘要翻译： 在从包含大量至少一种“轻”杂质如不可冷凝气体的粗二氧化碳中分离至少一种“重”杂质如硫化氢的方法中，涉及使用含二氧化碳的至少一个热泵循环 作为工作流体的流体，从粗二氧化碳中除去“轻”杂质，随后从去除的“轻”杂质中回收二氧化碳，从而改善总体二氧化碳回收率和能量消耗方面的效率。
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公开(公告)号：US20150114032A1
公开(公告)日：2015-04-30
申请号：US14521062
申请日：2014-10-22
IPC分类号： F25J1/00
CPC分类号： F25J1/0027 , B01D53/002 , B01D2256/22 , B01D2257/304 , C01B17/167 , F25J3/0266 , F25J3/08 , F25J2200/02 , F25J2200/04 , F25J2200/30 , F25J2200/40 , F25J2200/50 , F25J2200/74 , F25J2200/76 , F25J2200/78 , F25J2210/06 , F25J2215/80 , F25J2220/84 , F25J2230/80 , F25J2235/02 , F25J2235/80 , F25J2240/02 , F25J2240/30 , F25J2245/02 , F25J2260/20 , F25J2260/80 , F25J2270/02 , F25J2270/80 , F25J2270/88 , F25J2290/40 , Y02P20/129 , Y02P20/152
摘要： Impurities that are less volatile than carbon dioxide, e.g. hydrogen sulfide, are removed from crude carbon dioxide by processes involving distillation of said crude carbon dioxide in a distillation column system operating at super-atmospheric pressure(s) to produce carbon dioxide-enriched overhead vapor and bottoms liquid enriched with said impurities. Where such processes involve a single heat pump cycle, significant savings in power consumption are realized when the distillation column system is re-boiled by at least partially vaporizing liquid in or taken from an intermediate location in the column system.
摘要翻译： 比二氧化碳挥发性低的杂质，例如 硫化氢通过涉及在超大气压下运行的蒸馏塔系统中蒸馏所述粗二氧化碳的方法从粗二氧化碳中除去以产生富含二氧化碳的塔顶蒸气和富含所述杂质的塔底液。 当这种方法涉及单个热泵循环时，当蒸馏塔系统通过在塔系统中的中间位置至少部分蒸发液体或从其中的中间位置进行蒸发而将蒸馏塔系统重沸时，实现了功率消耗的显着节省。
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公开(公告)号：US11353261B2
公开(公告)日：2022-06-07
申请号：US16670281
申请日：2019-10-31
摘要： Light gases such as helium are extracted from a carbon dioxide-containing feed stream by distillation. Costly dehydration steps are avoided by pumping the liquid bottoms stream leaving the distillation column without vaporization so as to ensure that any water present in the feed remains in solution with the bulk stream leaving the process. This prevents any liquid phase water causing corrosion or solid ice or hydrates forming to plug the flow.
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