AR078438A1 - Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogeno - Google Patents
Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogenoInfo
- Publication number
- AR078438A1 AR078438A1 ARP100103467A ARP100103467A AR078438A1 AR 078438 A1 AR078438 A1 AR 078438A1 AR P100103467 A ARP100103467 A AR P100103467A AR P100103467 A ARP100103467 A AR P100103467A AR 078438 A1 AR078438 A1 AR 078438A1
- Authority
- AR
- Argentina
- Prior art keywords
- elimination
- gas stream
- scrs
- hydrogen sulfide
- stream
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0209—Natural gas or substitute natural gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
- C10L3/101—Removal of contaminants
- C10L3/102—Removal of contaminants of acid contaminants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0233—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 1 carbon atom or more
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0266—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of carbon dioxide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0295—Start-up or control of the process; Details of the apparatus used, e.g. sieve plates, packings
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/74—Refluxing the column with at least a part of the partially condensed overhead gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/76—Refluxing the column with condensed overhead gas being cycled in a quasi-closed loop refrigeration cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/90—Details relating to column internals, e.g. structured packing, gas or liquid distribution
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/40—Processes or apparatus using other separation and/or other processing means using hybrid system, i.e. combining cryogenic and non-cryogenic separation techniques
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/50—Processes or apparatus using other separation and/or other processing means using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
- F25J2205/66—Regenerating the adsorption vessel, e.g. kind of reactivation gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/04—Recovery of liquid products
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2260/00—Coupling of processes or apparatus to other units; Integrated schemes
- F25J2260/80—Integration in an installation using carbon dioxide, e.g. for EOR, sequestration, refrigeration etc.
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2280/00—Control of the process or apparatus
- F25J2280/40—Control of freezing of components
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Gas Separation By Absorption (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Separation Of Gases By Adsorption (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Un sistema para la eliminacion de gases ácidos de una corriente de gas crudo incluye un sistema de eliminacion de gases ácidos (AGRS, segun su sigla en inglés) y un sistema de eliminacion de componentes sulfurosos (SCRS, segun su sigla en inglés). El sistema de eliminacion de gas ácido recibe una corriente de gas amargo y la separa en una corriente de gas superior compuesta principalmente por metano, y una corriente de gas ácido inferior compuesta principalmente por dioxido de carbono. El sistema de eliminacion de componentes sulfurosos se coloca o bien corriente ascendente o corriente descendente del sistema de eliminacion de gases ácidos. El SCRS recibe una corriente de gas y separa generalmente la corriente de gas en una primera corriente de fluido que comprende sulfuro de hidrogeno, y una segunda corriente de fluido que comprende dioxido de carbono. Cuando el SCRS se encuentra corriente ascendente del AGRS, la segunda corriente de fluido además comprende principalmente metano. Cuando el SCRS se encuentra corriente descendente del AGRS, la segunda corriente de fluido es principalmente dioxido de carbono. Pueden utilizarse diversos tipos de sistemas de eliminacion de componentes sulfurosos.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US25727709P | 2009-11-02 | 2009-11-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AR078438A1 true AR078438A1 (es) | 2011-11-09 |
Family
ID=43922440
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ARP100103467A AR078438A1 (es) | 2009-11-02 | 2010-09-23 | Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogeno |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US20120204599A1 (es) |
| EP (1) | EP2496901A4 (es) |
| JP (1) | JP2013509300A (es) |
| CN (1) | CN102597671B (es) |
| AR (1) | AR078438A1 (es) |
| AU (1) | AU2010313733B2 (es) |
| BR (1) | BR112012009867A2 (es) |
| CA (1) | CA2777760C (es) |
| EA (1) | EA023174B1 (es) |
| MX (1) | MX337923B (es) |
| MY (1) | MY159666A (es) |
| SG (1) | SG10201407019PA (es) |
| WO (1) | WO2011053400A1 (es) |
Families Citing this family (81)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EA021006B1 (ru) | 2009-04-20 | 2015-03-31 | Эксонмобил Апстрим Рисерч Компани | Способ удаления кислотных газов из потока углеводородного газа |
| CN102905772A (zh) | 2010-02-17 | 2013-01-30 | 氟石科技公司 | 在制备超低硫气体中清除高压酸气体的构造和方法 |
| GB2507233B (en) * | 2011-08-09 | 2019-07-10 | Exxonmobil Upstream Res Co | Natural gas liquefaction process |
| CA2772479C (en) | 2012-03-21 | 2020-01-07 | Mackenzie Millar | Temperature controlled method to liquefy gas and a production plant using the method. |
| AU2013235610B2 (en) | 2012-03-21 | 2015-11-19 | Exxonmobil Upstream Research Company | Separating carbon dioxide and ethane from a mixed stream |
| CA2790961C (en) | 2012-05-11 | 2019-09-03 | Jose Lourenco | A method to recover lpg and condensates from refineries fuel gas streams. |
| EP2685189A1 (en) * | 2012-07-13 | 2014-01-15 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Process for storing liquid rich in carbon dioxide in solid form |
| WO2014066539A1 (en) | 2012-10-24 | 2014-05-01 | Fluor Technologies Corporation | Integration methods of gas processing plant and nitrogen rejection unit for high nitrogen feed gases |
| CA2798057C (en) | 2012-12-04 | 2019-11-26 | Mackenzie Millar | A method to produce lng at gas pressure letdown stations in natural gas transmission pipeline systems |
| MX368367B (es) | 2013-01-25 | 2019-09-30 | Exxonmobil Upstream Res Co | Contacto de una corriente de gas con una corriente de liquido. |
| CA2813260C (en) | 2013-04-15 | 2021-07-06 | Mackenzie Millar | A method to produce lng |
| AR096078A1 (es) | 2013-05-09 | 2015-12-02 | Exxonmobil Upstream Res Co | Separación de impurezas de una corriente de gas usando un sistema de contacto en equicorriente orientado verticalmente |
| AR096132A1 (es) | 2013-05-09 | 2015-12-09 | Exxonmobil Upstream Res Co | Separar dióxido de carbono y sulfuro de hidrógeno de un flujo de gas natural con sistemas de co-corriente en contacto |
| RU2522155C1 (ru) * | 2013-07-04 | 2014-07-10 | Андрей Владиславович Курочкин | Сверхкритический сепаратор |
| EP3046653B1 (en) * | 2013-09-16 | 2020-10-28 | Savannah River Nuclear Solutions, LLC | Mass transfer apparatus and method for separation of gases |
| US9764272B2 (en) * | 2013-10-28 | 2017-09-19 | Energy Recovery, Inc. | Systems and methods for utilizing turbine systems within gas processing systems |
| CA2924402C (en) | 2013-12-06 | 2017-11-21 | Exxonmobil Upstream Research Company | Method and device for separating a feed stream using radiation detectors |
| WO2015084495A2 (en) * | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of maintaining a liquid level in a distillation tower |
| US9803918B2 (en) | 2013-12-06 | 2017-10-31 | Exxonmobil Upstream Research Company | Method and system of dehydrating a feed stream processed in a distillation tower |
| US9562719B2 (en) | 2013-12-06 | 2017-02-07 | Exxonmobil Upstream Research Company | Method of removing solids by modifying a liquid level in a distillation tower |
| CA2924695C (en) * | 2013-12-06 | 2018-10-02 | Exxonmobil Upstream Research Company | Method and system for separating a feed stream with a feed stream distribution mechanism |
| WO2015084499A2 (en) | 2013-12-06 | 2015-06-11 | Exxonmobil Upstream Research Company | Method and system of modifying a liquid level during start-up operations |
| US9874395B2 (en) | 2013-12-06 | 2018-01-23 | Exxonmobil Upstream Research Company | Method and system for preventing accumulation of solids in a distillation tower |
| MY177768A (en) | 2013-12-06 | 2020-09-23 | Exxonmobil Upstream Res Co | Method and device for separating hydrocarbons and contaminants with a heating mechanism to destabilize and/or prevent adhesion of solids |
| AU2014357663B2 (en) | 2013-12-06 | 2016-12-22 | Exxonmobil Upstream Research Company | Method and device for separating hydrocarbons and contaminants with a spray assembly |
| WO2015089446A1 (en) | 2013-12-12 | 2015-06-18 | Fluor Technologies Corporation | Configurations and methods of flexible co2 removal |
| US9504984B2 (en) * | 2014-04-09 | 2016-11-29 | Exxonmobil Upstream Research Company | Generating elemental sulfur |
| WO2015163997A2 (en) | 2014-04-22 | 2015-10-29 | Exxonmobil Upstream Research Company | Method and system for starting up a distillation tower |
| MY183001A (en) | 2014-06-11 | 2021-02-05 | Exxonmobil Upstream Res Co | Method for separating a feed gas in a column |
| US9739529B2 (en) | 2014-07-08 | 2017-08-22 | Exxonmobil Upstream Research Company | Method and system for separating fluids in a distillation tower |
| WO2016023098A1 (en) | 2014-08-15 | 2016-02-18 | 1304338 Alberta Ltd. | A method of removing carbon dioxide during liquid natural gas production from natural gas at gas pressure letdown stations |
| US9823017B2 (en) | 2014-10-22 | 2017-11-21 | Exxonmobil Upstream Research Company | Method and system of controlling a temperature within a melt tray assembly of a distillation tower |
| CA2966991C (en) | 2014-11-17 | 2019-04-09 | Exxonmobil Upstream Research Company | Heat exchange mechanism for removing contaminants from a hydrocarbon vapor stream |
| AU2015374634B2 (en) | 2014-12-30 | 2018-05-31 | Exxonmobil Upstream Research Company | Accumulation and melt tray assembly for a distillation tower |
| CN107106969B (zh) | 2015-01-09 | 2020-03-03 | 埃克森美孚上游研究公司 | 使用多个同流接触器从流体流分离杂质 |
| KR101964584B1 (ko) | 2015-02-17 | 2019-04-03 | 엑손모빌 업스트림 리서치 캄파니 | 병류 컨택터에 대한 내부 표면 특징 |
| RU2576934C1 (ru) * | 2015-02-24 | 2016-03-10 | Андрей Владиславович Курочкин | Фракционирующий холодильник-конденсатор |
| US10495379B2 (en) | 2015-02-27 | 2019-12-03 | Exxonmobil Upstream Research Company | Reducing refrigeration and dehydration load for a feed stream entering a cryogenic distillation process |
| WO2016148780A1 (en) | 2015-03-13 | 2016-09-22 | Exxonmobil Upstream Research Company | Coalescer for co-current contactors |
| WO2016209404A1 (en) | 2015-06-22 | 2016-12-29 | Exxonmobil Upstream Research Company | Purge to intermediate pressure in cryogenic distillation |
| US9808755B2 (en) * | 2015-07-24 | 2017-11-07 | Air Products And Chemicals, Inc. | Sour pressure swing adsorption process |
| CN108431184B (zh) * | 2015-09-16 | 2021-03-30 | 1304342阿尔伯塔有限公司 | 在气体减压站制备天然气以生产液体天然气(lng)的方法 |
| CA2994812C (en) | 2015-09-18 | 2020-03-10 | Exxonmobil Upstream Research Company | Heating component to reduce solidification in a cryogenic distillation system |
| US10569219B2 (en) | 2015-09-21 | 2020-02-25 | Exxonmobil Upstream Research Company | Systems and methods for separating hydrogen sulfide from carbon dioxide in a high-pressure mixed stream |
| CA2998466C (en) * | 2015-09-24 | 2021-06-29 | Exxonmobil Upstream Research Company | Treatment plant for hydrocarbon gas having variable contaminant levels |
| CN106608618A (zh) * | 2015-10-21 | 2017-05-03 | 中国石油化工股份有限公司 | 酸气净化工艺 |
| BR112018008451A2 (pt) * | 2015-10-27 | 2018-12-11 | Fluor Tech Corp | configurações e métodos para processar gases ácidos de alta pressão sem emissões |
| US10173389B2 (en) * | 2015-12-15 | 2019-01-08 | Bloom Energy Corporation | Carbon dioxide shielded natural gas line and method of using thereof |
| WO2017143215A1 (en) * | 2016-02-19 | 2017-08-24 | Exxonmobil Upstream Reasrch Company | Cold solvent gas treating system for selective h2s removal |
| EA201892054A1 (ru) | 2016-03-30 | 2019-02-28 | Эксонмобил Апстрим Рисерч Компани | Поступающая из собственных источников пластовая текучая среда для повышения нефтеотдачи |
| CN105771539A (zh) * | 2016-03-31 | 2016-07-20 | 四川天采科技有限责任公司 | 一种适用于炼厂的高浓度硫化氢尾气的脱除工艺 |
| US11634651B2 (en) * | 2016-09-08 | 2023-04-25 | Waste to Energy Systems, LLC | System and method for biogasification |
| US10539364B2 (en) * | 2017-03-13 | 2020-01-21 | General Electric Company | Hydrocarbon distillation |
| CN107051125A (zh) * | 2017-05-03 | 2017-08-18 | 海湾环境科技(北京)股份有限公司 | 油气回收系统 |
| CN110740795B (zh) | 2017-06-15 | 2022-02-25 | 埃克森美孚上游研究公司 | 使用成束的紧凑并流接触系统的分馏系统 |
| US11000795B2 (en) | 2017-06-15 | 2021-05-11 | Exxonmobil Upstream Research Company | Fractionation system using compact co-current contacting systems |
| US10876052B2 (en) | 2017-06-20 | 2020-12-29 | Exxonmobil Upstream Research Company | Compact contacting systems and methods for scavenging sulfur-containing compounds |
| AU2018322436B2 (en) | 2017-08-21 | 2021-07-22 | Exxonmobil Upstream Research Company | Integration of cold solvent and acid gas removal |
| CN107880946B (zh) * | 2017-12-13 | 2023-05-16 | 中冶焦耐(大连)工程技术有限公司 | 一种煤气冷却分离装置及方法 |
| US20190194551A1 (en) * | 2017-12-22 | 2019-06-27 | Clariant International, Ltd. | Synergized acetals composition and method for scavenging sulfides and mercaptans |
| WO2019195570A1 (en) * | 2018-04-06 | 2019-10-10 | Baker Hughes, A Ge Company, Llc | In-line pipe contactor |
| US11306267B2 (en) | 2018-06-29 | 2022-04-19 | Exxonmobil Upstream Research Company | Hybrid tray for introducing a low CO2 feed stream into a distillation tower |
| WO2020005553A1 (en) | 2018-06-29 | 2020-01-02 | Exxonmobil Upstream Research Company (Emhc-N1.4A.607) | Mixing and heat integration of melt tray liquids in a cryogenic distillation tower |
| CN108744565B (zh) * | 2018-07-31 | 2023-07-14 | 中国大唐集团科学技术研究院有限公司西北分公司 | 一种蒸发结晶换热装置与燃煤厂脱硫废水零排放系统 |
| EP3616774A1 (de) * | 2018-09-03 | 2020-03-04 | L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude | Verfahren und vorrichtung zur abtrennung von metallcarbonylen aus einem gasgemisch |
| CN109387030B (zh) * | 2018-11-17 | 2023-08-01 | 杭州宏盛中弘新能源有限公司 | 一种低浓度煤矿瓦斯液化提浓甲烷制lng的系统及方法 |
| WO2020205750A1 (en) | 2019-03-29 | 2020-10-08 | Bright Energy Storage Technologies, Llp | Co2 separation & liquefaction system and method |
| RU2723874C1 (ru) * | 2019-11-21 | 2020-06-17 | Сергей Леонидович Терентьев | Установка десорбции (испарения) с глубокой рекуперацией тепла |
| CN111760546A (zh) * | 2020-07-13 | 2020-10-13 | 江西庞泰环保股份有限公司 | 一种气液分布支撑平衡装置 |
| US11745136B2 (en) | 2020-10-14 | 2023-09-05 | Bcck Holding Company | System and method for treating a methane system to remove carbon dioxide, hydrogen sulfide, and water in a single process |
| RU2761705C1 (ru) * | 2021-04-13 | 2021-12-13 | федеральное государственное бюджетное образовательное учреждение высшего образования "Нижегородский государственный технический университет им. Р.Е. Алексеева" (НГТУ) | Способ удаления диоксида углерода из природного газа |
| CN115691688A (zh) * | 2021-07-30 | 2023-02-03 | 中国石油化工股份有限公司 | 一种酸性气体中硫溶解行为的分子模拟方法及其应用 |
| CN113491883B (zh) * | 2021-08-12 | 2022-06-28 | 江西全兴化工填料有限公司 | 用于分离可燃性气体的金属填料分馏塔 |
| AU2022390169A1 (en) * | 2021-11-18 | 2024-06-27 | Dvo Licensing, Inc. | Method and apparatus for anaerobic digestion of liquid waste streams |
| CN114272724B (zh) * | 2021-12-31 | 2024-04-02 | 南京亿碳科技有限公司 | 一种新型节能co2回收装置 |
| CN114653184B (zh) * | 2022-04-01 | 2023-10-27 | 北京建筑大学 | 一种去除恶臭气体和生物气溶胶的系统和方法 |
| US11629571B1 (en) * | 2022-12-05 | 2023-04-18 | Capwell Seavices Llc | Modular well capping system, kit, and methods |
| GB202302933D0 (en) * | 2023-02-28 | 2023-04-12 | Caloritum Nv | System and method preventing leakage from industrial equipment operating in corrosive environments |
| CN116731760B (zh) * | 2023-07-20 | 2024-01-02 | 北京化工大学 | 一种低浓度煤层气气水合物法循环提纯系统 |
| CN117553516A (zh) * | 2023-12-29 | 2024-02-13 | 江苏正丹化学工业股份有限公司 | 一种偏三甲苯连续氧化尾气制氮生产装置 |
| CN118256334B (zh) * | 2024-05-30 | 2025-06-24 | 山东中创健康科技集团有限公司 | 微生物添加剂发酵空气多级过滤除菌装置 |
Family Cites Families (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4222991A (en) * | 1978-05-18 | 1980-09-16 | Union Oil Company Of California | Process for removing SOx and NOx compounds from gas streams |
| US4370156A (en) * | 1981-05-29 | 1983-01-25 | Standard Oil Company (Indiana) | Process for separating relatively pure fractions of methane and carbon dioxide from gas mixtures |
| US4459142A (en) * | 1982-10-01 | 1984-07-10 | Standard Oil Company (Indiana) | Cryogenic distillative removal of CO2 from high CO2 content hydrocarbon containing streams |
| CA1219731A (en) * | 1983-05-02 | 1987-03-31 | John Happel | Process for desulfurizing fuel gases |
| US4563202A (en) * | 1984-08-23 | 1986-01-07 | Dm International Inc. | Method and apparatus for purification of high CO2 content gas |
| US4831206A (en) * | 1987-03-05 | 1989-05-16 | Uop | Chemical processing with an operational step sensitive to a feedstream component |
| EP0398952A4 (en) * | 1988-01-15 | 1991-05-22 | Chevron Research Company | Composition, method and apparatus for removal of hydrogen sulfide |
| US4874524A (en) * | 1988-03-30 | 1989-10-17 | The Curators Of The University Of Missouri | Separation of adsorbed components by variable temperature desorption |
| DE3828227A1 (de) * | 1988-08-19 | 1990-02-22 | Basf Ag | Verfahren zum entfernen von co(pfeil abwaerts)2(pfeil abwaerts) und gegebenenfalls h(pfeil abwaerts)2(pfeil abwaerts) aus gasen |
| US5062270A (en) * | 1990-08-31 | 1991-11-05 | Exxon Production Research Company | Method and apparatus to start-up controlled freezing zone process and purify the product stream |
| US5120338A (en) * | 1991-03-14 | 1992-06-09 | Exxon Production Research Company | Method for separating a multi-component feed stream using distillation and controlled freezing zone |
| US5126118A (en) * | 1991-04-08 | 1992-06-30 | Ari Technologies, Inc. | Process and apparatus for removal of H2 S with separate absorber and oxidizer and a reaction chamber therebetween |
| CA2133302A1 (en) * | 1993-10-06 | 1995-04-07 | Ravi Kumar | Integrated process for purifying and liquefying a feed gas mixture with respect to its less strongly adsorbed component of lower volatility |
| DE19704173C1 (de) * | 1997-02-05 | 1998-04-16 | Webasto Karosseriesysteme | Flexibles Verdeck eines Fahrzeugs |
| ID24280A (id) * | 1997-07-01 | 2000-07-13 | Exxon Production Research Co | Proses untuk memisahkan aliran gas multi-komponen yang mengandung paling tidak satu komponen yang dapat membeku |
| TW366409B (en) * | 1997-07-01 | 1999-08-11 | Exxon Production Research Co | Process for liquefying a natural gas stream containing at least one freezable component |
| US6416729B1 (en) * | 1999-02-17 | 2002-07-09 | Crystatech, Inc. | Process for removing hydrogen sulfide from gas streams which include or are supplemented with sulfur dioxide |
| GB0015997D0 (en) * | 2000-06-29 | 2000-08-23 | Norske Stats Oljeselskap | Method for mixing fluids |
| GB0031710D0 (en) * | 2000-12-27 | 2001-02-07 | Dyno Oil Field Chemicals | Process for the reduction or elimination of hydrogen sulphide |
| FR2848121B1 (fr) * | 2002-12-04 | 2005-01-28 | Inst Francais Du Petrole | Procede de traitement d'un gaz naturel acide |
| JP2005097542A (ja) * | 2003-08-28 | 2005-04-14 | Kobe Steel Ltd | 炭化水素含有ガス処理装置および炭化水素含有ガス処理方法 |
| PL2402068T5 (pl) * | 2004-01-20 | 2017-09-29 | Fluor Tech Corp | Sposoby i konfiguracje do wzbogacania gazu kwaśnego |
| CA2583120C (en) * | 2004-12-03 | 2014-03-25 | Exxonmobil Upstream Research Company | Integrated acid gas and sour gas reinjection process |
| US20100018248A1 (en) * | 2007-01-19 | 2010-01-28 | Eleanor R Fieler | Controlled Freeze Zone Tower |
| US20080256977A1 (en) * | 2007-04-20 | 2008-10-23 | Mowrey Earle R | Hydrocarbon recovery and light product purity when processing gases with physical solvents |
| US8529664B2 (en) * | 2007-05-18 | 2013-09-10 | Exxonmobil Research And Engineering Company | Removal of a target gas from a mixture of gases by swing adsorption with use of a turboexpander |
| JP2010536573A (ja) * | 2007-08-30 | 2010-12-02 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 酸ガス流からの硫化水素及び二酸化炭素の除去方法 |
| US20090090049A1 (en) * | 2007-10-09 | 2009-04-09 | Chevron U.S.A. Inc. | Process for producing liqefied natural gas from high co2 natural gas |
| US20090220406A1 (en) * | 2008-02-29 | 2009-09-03 | Greatpoint Energy, Inc. | Selective Removal and Recovery of Acid Gases from Gasification Products |
| US7955496B2 (en) * | 2008-04-22 | 2011-06-07 | Kellogg Brown & Root Llc | Systems and methods for upgrading hydrocarbons |
-
2010
- 2010-08-02 EP EP10827299.8A patent/EP2496901A4/en not_active Withdrawn
- 2010-08-02 US US13/395,619 patent/US20120204599A1/en not_active Abandoned
- 2010-08-02 AU AU2010313733A patent/AU2010313733B2/en active Active
- 2010-08-02 JP JP2012537871A patent/JP2013509300A/ja active Pending
- 2010-08-02 BR BR112012009867A patent/BR112012009867A2/pt not_active IP Right Cessation
- 2010-08-02 SG SG10201407019PA patent/SG10201407019PA/en unknown
- 2010-08-02 WO PCT/US2010/044137 patent/WO2011053400A1/en not_active Ceased
- 2010-08-02 EA EA201290277A patent/EA023174B1/ru not_active IP Right Cessation
- 2010-08-02 CN CN201080049495.7A patent/CN102597671B/zh active Active
- 2010-08-02 MX MX2012004788A patent/MX337923B/es active IP Right Grant
- 2010-08-02 CA CA2777760A patent/CA2777760C/en active Active
- 2010-08-02 MY MYPI2012001879A patent/MY159666A/en unknown
- 2010-09-23 AR ARP100103467A patent/AR078438A1/es unknown
Also Published As
| Publication number | Publication date |
|---|---|
| AU2010313733B2 (en) | 2016-05-12 |
| MY159666A (en) | 2017-01-13 |
| MX337923B (es) | 2016-03-28 |
| SG10201407019PA (en) | 2014-12-30 |
| EA023174B1 (ru) | 2016-04-29 |
| JP2013509300A (ja) | 2013-03-14 |
| US20120204599A1 (en) | 2012-08-16 |
| WO2011053400A1 (en) | 2011-05-05 |
| EA201290277A1 (ru) | 2012-10-30 |
| CA2777760A1 (en) | 2011-05-05 |
| CN102597671B (zh) | 2015-11-25 |
| EP2496901A4 (en) | 2013-04-24 |
| MX2012004788A (es) | 2012-06-08 |
| EP2496901A1 (en) | 2012-09-12 |
| AU2010313733A1 (en) | 2012-05-24 |
| CA2777760C (en) | 2017-06-27 |
| CN102597671A (zh) | 2012-07-18 |
| BR112012009867A2 (pt) | 2016-08-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| AR078438A1 (es) | Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogeno | |
| AR077603A1 (es) | Sistemas y metodos para extraer hidrocarburos pesados y gases acidos de una corriente de gases de hidrocarburos | |
| AR080000A1 (es) | Eliminacion de gases acidos de una corriente de gas, con captura y secuestro de co2 | |
| MY153100A (en) | Multi-stage membrane separation process | |
| AR096132A1 (es) | Separar dióxido de carbono y sulfuro de hidrógeno de un flujo de gas natural con sistemas de co-corriente en contacto | |
| MX2012005491A (es) | Sistema de tratamiento de gas de combustion. | |
| WO2010019510A3 (en) | Mercury removal from crude oil | |
| WO2011137020A3 (en) | Methods and apparatus for sulfur recovery from acid gases | |
| GB2464906A (en) | Cryogenic treatment of gas | |
| WO2012092040A3 (en) | Use of gas-separation membranes to enhance production in fields containing high concentrations of hydrogen sulfides | |
| EA201170572A1 (ru) | Удаление кислотных газов из газового потока | |
| IN2012DN03067A (es) | ||
| MY183960A (en) | Contacting a gas stream with a liquid stream | |
| WO2011149660A3 (en) | Integrated process for floating liquefied natural gas pretreatment | |
| BR112012030338A2 (pt) | sistema e processo para tratar uma corrente de gás de alimentação contendo uma quantidade indesejável de co2 | |
| EA200800270A1 (ru) | Способы и конфигурации для извлечения газоконденсатных жидкостей (ngl) | |
| IN2014DN07127A (es) | ||
| MY174878A (en) | Sweetening of natural gas | |
| EA201891266A1 (ru) | Способ и система для очистки природного газа с использованием мембран | |
| EA201991617A1 (ru) | Углеродные молекулярно-ситовые мембраны для разделения агрессивных газов | |
| EA200970762A1 (ru) | Способ очистки газового потока | |
| EA201792668A1 (ru) | Установка, способ и катализатор осушки и очистки газообразного углеводородного сырья от сероводорода и/или меркаптанов | |
| MX2012003737A (es) | Proceso para la remocion de azufre de gases despedidos de refineria. | |
| EA200901522A1 (ru) | Способ удаления диоксида углерода из газового потока | |
| BR112015032266A2 (pt) | Método e sistema para produzir sulfito de dimetila de um fluxo de coque gaseificado |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FB | Suspension of granting procedure |