WO2015154786A3 - Anlage zur verringerung eines kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen gasstroms und entsprechendes verfahren - Google Patents

Anlage zur verringerung eines kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen gasstroms und entsprechendes verfahren Download PDF

Info

Publication number
WO2015154786A3
WO2015154786A3 PCT/EP2014/001244 EP2014001244W WO2015154786A3 WO 2015154786 A3 WO2015154786 A3 WO 2015154786A3 EP 2014001244 W EP2014001244 W EP 2014001244W WO 2015154786 A3 WO2015154786 A3 WO 2015154786A3
Authority
WO
WIPO (PCT)
Prior art keywords
carbon dioxide
rich
gas flow
segregating unit
hydrocarbons
Prior art date
Application number
PCT/EP2014/001244
Other languages
English (en)
French (fr)
Other versions
WO2015154786A2 (de
Inventor
Robert Adler
Sascha Dorner
Ekkehardt Klein
Christoph Nagl
Original Assignee
Linde Aktiengesellschaft
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Linde Aktiengesellschaft filed Critical Linde Aktiengesellschaft
Priority to EP14879279.9A priority Critical patent/EP2997320A2/de
Publication of WO2015154786A2 publication Critical patent/WO2015154786A2/de
Publication of WO2015154786A3 publication Critical patent/WO2015154786A3/de

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
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
    • F25J3/067—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • 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
    • C10L3/104—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
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/0605—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the feed stream
    • F25J3/061—Natural gas or substitute natural 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
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
    • F25J3/0635—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of CnHm with 1 carbon atom or more
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2256/00—Main component in the product gas stream after treatment
    • B01D2256/24—Hydrocarbons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2256/00—Main component in the product gas stream after treatment
    • B01D2256/24—Hydrocarbons
    • B01D2256/245—Methane
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/05—Biogas
    • 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
    • F25J2205/20—Processes or apparatus using other separation and/or other processing means using solidification of components
    • 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
    • F25J2205/24—Processes or apparatus using other separation and/or other processing means using regenerators, cold accumulators or reversible heat exchangers
    • 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
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/42—Nitrogen
    • 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
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/62—Liquefied natural gas [LNG]; Natural gas liquids [NGL]; Liquefied petroleum gas [LPG]
    • 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
    • F25J2270/904—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by liquid or gaseous cryogen in an open loop
    • 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
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

Die Erfindung betrifft eine Anlage (1), die zur Verringerung eines Kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen Gasstroms (A) eingerichtet ist, mit einer ersten und einer zweiten Abscheideeinheit (10, 20), die jeweils einen in einem Abscheideraum (12, 22) angeordneten und mit einem Kältemittel (C) speisbaren Kryokondensator (11, 21) aufweist, wobei Mittel (30, 40) vorgesehen sind, die dafür eingerichtet sind, in einem ersten Betriebsmodus das Kältemittel (C) durch den Kryokondensator (11 ) nur der ersten Abscheideeinheit (10) und den kohlendioxidhaltigen und kohlenwasserstoffreichen Gasstrom (A) durch den Abscheideraum (12) nur der ersten Abscheideeinheit (10) zu führen und die zweite Abscheideeinheit (20) zu erwärmen und aus der zweiten Abscheideeinheit (20) einen kohlendioxidreichen Strom (D) abzuziehen, und die ferner dafür eingerichtet sind, in einem zweiten Betriebsmodus das Kältemittel (C) durch den Kryokondensator (21) nur der zweiten Abscheideeinheit (20) und den kohlendioxidhaltigen und kohlenwasserstoffreichen Gasstrom (A) durch den Abscheideraum (22) nur der zweiten Abscheideeinheit (20) zu führen und die erste Abscheideeinheit (10) zu erwärmen und aus dieser einen kohlendioxidreichen Strom (D) abzuziehen. Ein entsprechendes Verfahren ist ebenfalls Gegenstand der vorliegenden Erfindung.
PCT/EP2014/001244 2013-05-16 2014-05-08 Anlage zur verringerung eines kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen gasstroms und entsprechendes verfahren WO2015154786A2 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP14879279.9A EP2997320A2 (de) 2013-05-16 2014-05-08 Anlage zur verringerung eines kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen gasstroms und entsprechendes verfahren

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102013008535.7A DE102013008535A1 (de) 2013-05-16 2013-05-16 Anlage zur Verringerung eines Kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen Gasstroms und entsprechendes Verfahren
DE102013008535.7 2013-05-16

Publications (2)

Publication Number Publication Date
WO2015154786A2 WO2015154786A2 (de) 2015-10-15
WO2015154786A3 true WO2015154786A3 (de) 2016-01-28

Family

ID=51831180

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2014/001244 WO2015154786A2 (de) 2013-05-16 2014-05-08 Anlage zur verringerung eines kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen gasstroms und entsprechendes verfahren

Country Status (3)

Country Link
EP (1) EP2997320A2 (de)
DE (1) DE102013008535A1 (de)
WO (1) WO2015154786A2 (de)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3050656B1 (fr) * 2016-04-27 2019-11-29 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procede de production de biomethane liquide par separation cryogenique
FR3050655B1 (fr) * 2016-04-27 2020-03-27 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procede de production de biomethane mettant en œuvre un flux d'azote
EP3339785A1 (de) * 2016-12-20 2018-06-27 Linde Aktiengesellschaft Verfahren und anlage zum abkühlen eines mediums
FR3086187B1 (fr) * 2018-09-25 2021-02-26 Air Liquide Procede de production de biomethane a partir d'un flux de biogaz comprenant une solidification des impuretes

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6082133A (en) * 1999-02-05 2000-07-04 Cryo Fuel Systems, Inc Apparatus and method for purifying natural gas via cryogenic separation
DE19940371A1 (de) * 1999-08-25 2001-03-01 Messer Griesheim Gmbh Verfahren und Vorrichtung zur Gewinnung von Kohlendioxid aus Abgasen
US20120000242A1 (en) * 2010-04-22 2012-01-05 Baudat Ned P Method and apparatus for storing liquefied natural gas
WO2012029021A1 (fr) * 2010-09-03 2012-03-08 Total S.A. Procede de traitement d'un gaz naturel contenant du dioxyde de carbone

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW200914115A (en) 2007-05-14 2009-04-01 Shell Int Research Process for producing purified natural gas from natural gas comprising water and carbon dioxide
DE102009017228A1 (de) 2009-04-09 2010-10-14 Linde-Kca-Dresden Gmbh Verfahren und Vorrichtung zur Behandlung von Rauchgasen

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6082133A (en) * 1999-02-05 2000-07-04 Cryo Fuel Systems, Inc Apparatus and method for purifying natural gas via cryogenic separation
DE19940371A1 (de) * 1999-08-25 2001-03-01 Messer Griesheim Gmbh Verfahren und Vorrichtung zur Gewinnung von Kohlendioxid aus Abgasen
US20120000242A1 (en) * 2010-04-22 2012-01-05 Baudat Ned P Method and apparatus for storing liquefied natural gas
WO2012029021A1 (fr) * 2010-09-03 2012-03-08 Total S.A. Procede de traitement d'un gaz naturel contenant du dioxyde de carbone

Also Published As

Publication number Publication date
EP2997320A2 (de) 2016-03-23
DE102013008535A1 (de) 2014-11-20
WO2015154786A2 (de) 2015-10-15

Similar Documents

Publication Publication Date Title
MX2018007771A (es) Metodo para producir biometano al purificar biogas de instalaciones de almacenamiento de desechos no peligrosos e instalacion para implementar el metodo.
RU2014140213A (ru) Упорядоченная насадка
AU2018200946B2 (en) Method and system for removing carbon dioxide from hydrocarbons
WO2015011566A3 (en) Split line system, method and process for co2 recovery
EP2938425A4 (de) System und verfahren zur integrierten kohlendioxidabscheidung aus verbrennungsgasen
PL2788104T3 (pl) Sposób obróbki zanieczyszczeń zawartych w gazach spalinowych statków, statek ze skruberem gazu spalinowego
WO2015154786A3 (de) Anlage zur verringerung eines kohlendioxidgehalts eines kohlendioxidhaltigen und kohlenwasserstoffreichen gasstroms und entsprechendes verfahren
CO7101226A2 (es) Método para separación de gases
IN2015DN03309A (de)
WO2013025645A3 (en) Systems and methods for collecting and processing permafrost gases, and for cooling permafrost
GB2462555B (en) Process and apparatus for separation of Nitrogen from LNG
BR112015012441A2 (pt) produção de gás natural liquefeito
WO2012078564A3 (en) Process for transferring heat or modifying a tube in a heat exchanger
MX2014003880A (es) Metodos y sistemas para condensacion de co2.
MY183465A (en) Method for separating off acid gases from natural gas
EA201491246A1 (ru) Способ облагораживания газа
WO2014067652A3 (de) Verfahren zum abkühlen einer kohlenwasserstoff-reichen fraktion
EA201890610A1 (ru) Способ и система для осуществления короткоцикловой адсорбции с использованием головного потока метаноотгонной колонны в качестве продувочного газа
WO2010132323A3 (en) Method of removing hydrocarbon impurities from a gas
WO2013135993A3 (fr) Procédé et appareil de séparation d'un mélange contenant du dioxyde de carbone par distillation
CA3010925A1 (en) Carbon dioxide separation/recovery device, combustion system using same, thermal power generation system using same, and method for separating and recovering carbon dioxide
WO2015055939A3 (fr) Procédé et appareil de séparation d'air par distillation cryogénique
WO2013135802A3 (de) Kombinierte gasaufbereitung
WO2015044575A3 (fr) Procede et appareil de separation cryogenique d'un melange contenant au moins du monoxyde de carbone, de l'hydrogene et de l'azote
WO2014155108A3 (en) Method and apparatus in a cryogenic liquefaction process

Legal Events

Date Code Title Description
NENP Non-entry into the national phase

Ref country code: DE

REEP Request for entry into the european phase

Ref document number: 2014879279

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 2014879279

Country of ref document: EP