MX371385B - Proceso para optimizar la remocion de componentes condensables de un fluido. - Google Patents

Proceso para optimizar la remocion de componentes condensables de un fluido.

Info

Publication number
MX371385B
MX371385B MX2015003390A MX2015003390A MX371385B MX 371385 B MX371385 B MX 371385B MX 2015003390 A MX2015003390 A MX 2015003390A MX 2015003390 A MX2015003390 A MX 2015003390A MX 371385 B MX371385 B MX 371385B
Authority
MX
Mexico
Prior art keywords
stream
gas
condensable components
initial feed
feed stream
Prior art date
Application number
MX2015003390A
Other languages
English (en)
Other versions
MX2015003390A (es
Inventor
Wayne Mckay Norman
Maddocks James
Original Assignee
Gas Liquids Eng Ltd
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 Gas Liquids Eng Ltd filed Critical Gas Liquids Eng Ltd
Publication of MX2015003390A publication Critical patent/MX2015003390A/es
Publication of MX371385B publication Critical patent/MX371385B/es

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0027—Condensation of vapours; Recovering volatile solvents by condensation by direct contact between vapours or gases and the cooling medium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0033—Other features
    • B01D5/0039—Recuperation of heat, e.g. use of heat pump(s), compression
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
    • B01D5/0087—Recirculating of the cooling medium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
    • B01D5/0093—Removing and treatment of non condensable gases
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/20—Reductants
    • B01D2251/21—Organic compounds not provided for in groups B01D2251/206 or B01D2251/208
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/20—Organic absorbents
    • B01D2252/202—Alcohols or their derivatives
    • B01D2252/2021—Methanol
    • 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
    • B01D2257/00—Components to be removed
    • B01D2257/30—Sulfur compounds
    • B01D2257/302—Sulfur oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/30—Sulfur compounds
    • B01D2257/304—Hydrogen sulfide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/40—Nitrogen compounds
    • B01D2257/404—Nitrogen oxides other than dinitrogen oxide
    • 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
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/702—Hydrocarbons
    • B01D2257/7022—Aliphatic hydrocarbons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/80—Water
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Gas Separation By Absorption (AREA)
  • Drying Of Gases (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

La presente invención se relaciona con un método para remover componentes condensables de un fluido que contiene componentes condensables. El método involucra optimizar la temperatura de una corriente de alimentación inicial que incluye los componentes condensables, a través de un intercambio de calor y enfriar para condensar los líquidos ahí. Los líquidos se remueven para formar una corriente de gas que después se comprime y después se enfría para formar una corriente a alta presión. Una porción de la corriente a alta presión se expande para formar una corriente a baja presión enfriada, la cual se mezcla con la corriente de alimentación inicial para aumentar el enfriamiento y la condensación de los componentes condensables en la corriente de alimentación inicial. El método se caracteriza porque, después de mezclar la corriente a baja presión enfriada con la corriente de alimentación inicial, la mezcla formada se separa en una corriente líquida y una corriente gaseosa. La corriente líquida y la corriente gaseosa se ponen en contacto con la corriente de alimentación inicial en un intercambiador de calor gas-líquido y en un intercambiador de calor gas-gas, respectivamente.
MX2015003390A 2012-09-17 2013-09-17 Proceso para optimizar la remocion de componentes condensables de un fluido. MX371385B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CA2790182A CA2790182C (en) 2012-09-17 2012-09-17 Process for optimizing removal of condensable components from a fluid
PCT/CA2013/001094 WO2014075176A1 (en) 2012-09-17 2013-09-17 Process for optimizing removal of condensable components from a fluid

Publications (2)

Publication Number Publication Date
MX2015003390A MX2015003390A (es) 2015-08-12
MX371385B true MX371385B (es) 2020-01-28

Family

ID=47262874

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2015003390A MX371385B (es) 2012-09-17 2013-09-17 Proceso para optimizar la remocion de componentes condensables de un fluido.

Country Status (12)

Country Link
EP (1) EP2895245A4 (es)
JP (1) JP6357155B2 (es)
CN (1) CN104812454A (es)
AR (1) AR092601A1 (es)
AU (1) AU2013344724B2 (es)
BR (1) BR112015005839B1 (es)
CA (1) CA2790182C (es)
EA (1) EA201500312A1 (es)
MX (1) MX371385B (es)
MY (1) MY169920A (es)
SA (1) SA515360153B1 (es)
WO (1) WO2014075176A1 (es)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3044238B1 (fr) * 2015-11-30 2020-11-13 Haffner Energy Dispositif d'epuration par distillation adiabatique
FR3075658B1 (fr) * 2017-12-21 2022-01-28 Air Liquide Procede de limitation de la concentration d'oxygene contenu dans un courant de biomethane
DE102018205890A1 (de) * 2018-04-18 2019-10-24 Röchling Automotive SE & Co. KG Kontinuierlich arbeitende Wasser-Gewinnungsvorrichtung für ein Kraftfahrzeug
CN114111315B (zh) * 2020-08-31 2022-11-29 昆明理工大学 一种粉煤气化磨煤工段煤粉干燥节能方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU9086598A (en) * 1997-09-15 1999-04-05 Den Norske Stats Oljeselskap A.S. Separation of acid gas from natural gas
AU1937999A (en) * 1997-12-16 1999-07-05 Lockheed Martin Idaho Technologies Company Apparatus and process for the refrigeration, liquefaction and separation of gases with varying levels of purity
RU2272973C1 (ru) * 2004-09-24 2006-03-27 Салават Зайнетдинович Имаев Способ низкотемпературной сепарации газа (варианты)
US20080256975A1 (en) * 2006-08-21 2008-10-23 Carrier Corporation Vapor Compression System With Condensate Intercooling Between Compression Stages
CN101406763B (zh) * 2008-10-31 2012-05-23 华南理工大学 一种船运液货蒸发气体的再液化方法
US20120167620A1 (en) * 2009-05-15 2012-07-05 Eva Marfilia Van Dorst Method and system for separating co2 from synthesis gas or flue gas
AU2010273123A1 (en) * 2009-07-13 2011-01-20 James Maddocks Process for removing condensable components from a fluid
GB2489396B (en) * 2011-02-25 2018-08-22 Costain Oil Gas & Process Ltd Process and apparatus for purification of carbon dioxide
CN102407064B (zh) * 2012-01-08 2013-09-11 文闯 一种双喉部型气体超声速旋流分离装置

Also Published As

Publication number Publication date
SA515360153B1 (ar) 2016-06-09
MX2015003390A (es) 2015-08-12
AR092601A1 (es) 2015-04-29
JP6357155B2 (ja) 2018-07-11
CA2790182A1 (en) 2012-11-27
BR112015005839B1 (pt) 2022-03-29
WO2014075176A1 (en) 2014-05-22
MY169920A (en) 2019-06-17
AU2013344724B2 (en) 2017-12-14
JP2015533636A (ja) 2015-11-26
BR112015005839A2 (pt) 2017-07-04
AU2013344724A1 (en) 2015-04-02
CN104812454A (zh) 2015-07-29
EP2895245A1 (en) 2015-07-22
EA201500312A1 (ru) 2015-08-31
CA2790182C (en) 2014-04-29
EP2895245A4 (en) 2016-06-15

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