EA201691182A1 - METHOD AND DEVICE FOR SEPARATION OF HYDROCARBONS AND POLLUTION SUBSTANCES THROUGH SURFACE TREATMENT MECHANISM - Google Patents
METHOD AND DEVICE FOR SEPARATION OF HYDROCARBONS AND POLLUTION SUBSTANCES THROUGH SURFACE TREATMENT MECHANISMInfo
- Publication number
- EA201691182A1 EA201691182A1 EA201691182A EA201691182A EA201691182A1 EA 201691182 A1 EA201691182 A1 EA 201691182A1 EA 201691182 A EA201691182 A EA 201691182A EA 201691182 A EA201691182 A EA 201691182A EA 201691182 A1 EA201691182 A1 EA 201691182A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- freezing zone
- wall
- section
- feed stream
- distillation column
- Prior art date
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/008—Liquid distribution
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- 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
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- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/141—Fractional distillation or use of a fractionation or rectification column where at least one distillation column contains at least one dividing wall
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
- B01D3/146—Multiple effect distillation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
- B01D3/148—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step in combination with at least one evaporator
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D3/16—Fractionating columns in which vapour bubbles through liquid
- B01D3/22—Fractionating columns in which vapour bubbles through liquid with horizontal sieve plates or grids; Construction of sieve plates or grids
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- B01D3/24—Fractionating columns in which vapour bubbles through liquid with sloping plates or elements mounted stepwise
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- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
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- B01D3/324—Tray constructions
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
- C07C7/05—Purification; Separation; Use of additives by distillation with the aid of auxiliary compounds
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- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
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- F25J2280/40—Control of freezing of components
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- 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/12—Particular process parameters like pressure, temperature, ratios
-
- 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/40—Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/44—Particular materials used, e.g. copper, steel or alloys thereof or surface treatments used, e.g. enhanced surface
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- General Chemical & Material Sciences (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
Abstract
Раскрытие изобретения включает в себя способ разделения подаваемого потока в дистилляционной колонне, который может включать обеспечение функционирования секции с зоной регулируемого замораживания в дистилляционной колонне, которая обеспечивает образование твердых веществ из подаваемого потока, при этом секция с зоной регулируемого замораживания включает в себя один или более элементов, расположенных внутри, и стенку зоны регулируемого замораживания, имеющую внутреннюю поверхность стенки, находящуюся внутри дистилляционной колонны, модифицирование по меньшей мере одного из элементов, расположенных внутри, внутренней поверхности стенки или как по меньшей мере одного из элементов, расположенных внутри, так и внутренней поверхности стенки посредством механизма обработки, который включает по меньшей мере одно из (а) удаления участков внутренней поверхности стенки и (b) нанесения покрывающей поверхности, ввод подаваемого потока в секцию с зоной регулируемого замораживания, образование твердых веществ из подаваемого потока в секции с зоной регулируемого замораживания, и по меньшей мере одну операцию из предотвращения и дестабилизации прилипания твердых веществ к внутренней поверхности стенки посредством механизма обработки.The disclosure of the invention includes a method of separating the feed stream in a distillation column, which may include ensuring the operation of a section with an adjustable freezing zone in a distillation column that provides for the formation of solids from the feed stream, while the section with an adjustable freezing zone includes located inside and the wall of the controlled freezing zone, having an internal wall surface inside the distillation column modifying at least one of the elements located inside the inner surface of the wall or at least one of the elements located inside and the internal surface of the wall by means of a processing mechanism that includes at least one of (a) removing the inner parts wall surface and (b) applying a covering surface, injecting the feed stream into the section with a controlled freezing zone, forming solids from the feed stream in the section with a controlled freezing zone and at least one operation to prevent and destabilize the adhesion of solids to the inner wall surface through a treatment mechanism.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201361912987P | 2013-12-06 | 2013-12-06 | |
PCT/US2014/061039 WO2015084501A2 (en) | 2013-12-06 | 2014-10-17 | Method and device for separating hydrocarbons and contaminants with a surface treatment mechanism |
Publications (1)
Publication Number | Publication Date |
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EA201691182A1 true EA201691182A1 (en) | 2016-09-30 |
Family
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Family Applications (1)
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EA201691182A EA201691182A1 (en) | 2013-12-06 | 2014-10-17 | METHOD AND DEVICE FOR SEPARATION OF HYDROCARBONS AND POLLUTION SUBSTANCES THROUGH SURFACE TREATMENT MECHANISM |
Country Status (9)
Country | Link |
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US (1) | US20150159942A1 (en) |
CN (1) | CN105705213A (en) |
AU (1) | AU2014357670B2 (en) |
CA (1) | CA2925410C (en) |
EA (1) | EA201691182A1 (en) |
MX (1) | MX2016004188A (en) |
MY (1) | MY175300A (en) |
NO (1) | NO20160889A1 (en) |
WO (1) | WO2015084501A2 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
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MY166180A (en) | 2012-03-21 | 2018-06-07 | Exxonmobil Upstream Res Co | Separating carbon dioxide and ethane from mixed stream |
CA2962608C (en) | 2014-10-22 | 2019-01-08 | Exxonmobil Upstream Research Company | Method and system of controlling a temperature within a melt tray assembly of a distillation tower |
MX2017005037A (en) | 2014-11-17 | 2017-06-30 | Exxonmobil Upstream Res Co | Heat exchange mechanism for removing contaminants from a hydrocarbon vapor stream. |
CA2972696C (en) | 2014-12-30 | 2019-06-11 | Nicholas F. Urbanski | Accumulation and melt tray assembly for a distillation tower |
MX2017008683A (en) | 2015-02-27 | 2017-10-11 | Exxonmobil Upstream Res Co | Reducing refrigeration and dehydration load for a feed stream entering a cryogenic distillation process. |
US10274252B2 (en) | 2015-06-22 | 2019-04-30 | Exxonmobil Upstream Research Company | Purge to intermediate pressure in cryogenic distillation |
CA2994812C (en) | 2015-09-18 | 2020-03-10 | Exxonmobil Upstream Research Company | Heating component to reduce solidification in a cryogenic distillation system |
WO2017052922A2 (en) | 2015-09-24 | 2017-03-30 | Exxonmobil Upstream Research Company | Treatment plant for hydrocarbon gas having variable contaminant levels |
WO2017172321A1 (en) | 2016-03-30 | 2017-10-05 | Exxonmobil Upstream Research Company | Self-sourced reservoir fluid for enhanced oil recovery |
US11378332B2 (en) | 2018-06-29 | 2022-07-05 | Exxonmobil Upstream Research Company | Mixing and heat integration of melt tray liquids in a cryogenic distillation tower |
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 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2821323A (en) * | 1955-12-07 | 1958-01-28 | Lee Co | Pin plug |
US4533372A (en) * | 1983-12-23 | 1985-08-06 | Exxon Production Research Co. | Method and apparatus for separating carbon dioxide and other acid gases from methane by the use of distillation and a controlled freezing zone |
US5265428A (en) * | 1990-10-05 | 1993-11-30 | Exxon Production Research Company | Bubble cap tray for melting solids and method for using same |
US7594414B2 (en) * | 2001-05-04 | 2009-09-29 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of natural gas and methods relating to same |
WO2003062725A1 (en) * | 2002-01-18 | 2003-07-31 | Curtin University Of Technology | Process and device for production of lng by removal of freezable solids |
US20100018248A1 (en) * | 2007-01-19 | 2010-01-28 | Eleanor R Fieler | Controlled Freeze Zone Tower |
CA2771566C (en) * | 2009-09-09 | 2017-07-18 | Exxonmobil Upstream Research Company | Cryogenic system for removing acid gases from a hydrocarbon gas stream |
US20110272830A1 (en) * | 2010-05-07 | 2011-11-10 | Bayer Materialscience Llc | Downcomers for mass transfer column |
-
2014
- 2014-10-17 WO PCT/US2014/061039 patent/WO2015084501A2/en active Application Filing
- 2014-10-17 US US14/516,731 patent/US20150159942A1/en not_active Abandoned
- 2014-10-17 MX MX2016004188A patent/MX2016004188A/en unknown
- 2014-10-17 CA CA2925410A patent/CA2925410C/en active Active
- 2014-10-17 CN CN201480060334.6A patent/CN105705213A/en active Pending
- 2014-10-17 AU AU2014357670A patent/AU2014357670B2/en active Active
- 2014-10-17 MY MYPI2016000537A patent/MY175300A/en unknown
- 2014-10-17 EA EA201691182A patent/EA201691182A1/en unknown
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2016
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CA2925410C (en) | 2018-02-06 |
US20150159942A1 (en) | 2015-06-11 |
CA2925410A1 (en) | 2015-06-11 |
AU2014357670B2 (en) | 2017-08-03 |
MY175300A (en) | 2020-06-18 |
MX2016004188A (en) | 2016-07-07 |
NO20160889A1 (en) | 2016-05-25 |
WO2015084501A3 (en) | 2016-02-25 |
CN105705213A (en) | 2016-06-22 |
WO2015084501A2 (en) | 2015-06-11 |
AU2014357670A1 (en) | 2016-07-07 |
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