PE20090450A1 - Configuracion de caldera para columna de eliminacion de nitrogeno - Google Patents

Configuracion de caldera para columna de eliminacion de nitrogeno

Info

Publication number
PE20090450A1
PE20090450A1 PE2008001043A PE2008001043A PE20090450A1 PE 20090450 A1 PE20090450 A1 PE 20090450A1 PE 2008001043 A PE2008001043 A PE 2008001043A PE 2008001043 A PE2008001043 A PE 2008001043A PE 20090450 A1 PE20090450 A1 PE 20090450A1
Authority
PE
Peru
Prior art keywords
current
column
stage
natural gas
liquefied
Prior art date
Application number
PE2008001043A
Other languages
English (en)
Inventor
Adam Adrian Brostow
Original Assignee
Air Prod & Chem
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 Air Prod & Chem filed Critical Air Prod & Chem
Publication of PE20090450A1 publication Critical patent/PE20090450A1/es

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0228Processes 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
    • F25J3/0233Processes 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0204Processes 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
    • F25J3/0209Natural gas or substitute natural gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0228Processes 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
    • F25J3/0257Processes 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 nitrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/02Processes or apparatus using separation by rectification in a single pressure main column system
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/40Features relating to the provision of boil-up in the bottom of a column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/70Refluxing the column with a condensed part of the feed stream, i.e. fractionator top is stripped or self-rectified
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2215/00Processes characterised by the type or other details of the product stream
    • F25J2215/04Recovery of liquid products
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2235/00Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
    • F25J2235/60Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being (a mixture of) hydrocarbons
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2240/00Processes or apparatus involving steps for expanding of process streams
    • F25J2240/30Dynamic liquid or hydraulic expansion with extraction of work, e.g. single phase or two-phase turbine
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2240/00Processes or apparatus involving steps for expanding of process streams
    • F25J2240/40Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/02Bath type boiler-condenser using thermo-siphon effect, e.g. with natural or forced circulation or pool boiling, i.e. core-in-kettle heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2270/00Refrigeration techniques used
    • F25J2270/02Internal refrigeration with liquid vaporising loop

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

REFERIDO A UN PROCESO PARA LA DESNITROGENACION DE UNA ALIMENTACION DE GAS NATURAL LICUADO, EL CUAL CONTIENE 1-10 MOLES POR CIENTO DE NITROGENO, QUE COMPRENDE: A) EXPANDIR A LA CORRIENTE DE ALIMENTACION DE GAS NATURAL LICUADO A TRAVES DE MEDIOS DISPUESTOS PARA EXPANDIR A DICHA CORRIENTE Y ENFRIARLA EN UN PERMUTADOR TERMICO CON CALDERA; B) INTRODUCIR A LA CORRIENTE DE GAS NATURAL LICUADO ENFRIADO Y EXPANDIDO HACIA UNA COLUMNA DE ELIMINACION DE NITROGENO; C) RETIRAR UNA CORRIENTE DE VAPOR DE LA PARTE SUPERIOR DESDE LA COLUMNA; D) RETIRAR UNA CORRIENTE LIQUIDA RESIDUAL DESDE LA COLUMNA; E) HACER PASAR A LA CORRIENTE RESIDUAL DESDE LA ETAPA (D) A TRAVES DE UNA BOMBA PARA AUMENTAR LA PRESION DE LA CORRIENTE LIQUIDA RESIDUAL; F) DIVIDIR A LA CORRIENTE RESIDUAL EN UNA PRIMERA CORRIENTE Y UNA SEGUNDA CORRIENTE; G) VAPORIZAR POR LO MENOS PARCIALMENTE A LA SEGUNDA CORRIENTE MEDIANTE LA REDUCCION DE PRESION DE ESTA ULTIMA Y HACIENDOLA PASAR LUEGO A TRAVES DEL PERMUTADOR TERMICO CON CALDERA DE LA ETAPA (A); Y H) INYECTAR A LA SEGUNDA CORRIENTE PARCIALMENTE VAPORIZADA DE LA ETAPA (G) A LA COLUMNA
PE2008001043A 2007-06-19 2008-06-18 Configuracion de caldera para columna de eliminacion de nitrogeno PE20090450A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US11/764,975 US20080314079A1 (en) 2007-06-19 2007-06-19 Nitrogen Rejection Column Reboiler Configuration

Publications (1)

Publication Number Publication Date
PE20090450A1 true PE20090450A1 (es) 2009-04-27

Family

ID=40135079

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2008001043A PE20090450A1 (es) 2007-06-19 2008-06-18 Configuracion de caldera para columna de eliminacion de nitrogeno

Country Status (12)

Country Link
US (1) US20080314079A1 (es)
EP (1) EP2179235A2 (es)
JP (1) JP2011513503A (es)
KR (1) KR20100021443A (es)
CN (1) CN102084199A (es)
AU (1) AU2008264885A1 (es)
BR (1) BRPI0812568A2 (es)
CA (1) CA2687886A1 (es)
PE (1) PE20090450A1 (es)
RU (1) RU2010101417A (es)
TW (1) TW200902703A (es)
WO (1) WO2008155653A2 (es)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090139263A1 (en) * 2007-12-04 2009-06-04 Air Products And Chemicals, Inc. Thermosyphon reboiler for the denitrogenation of liquid natural gas
US8522574B2 (en) * 2008-12-31 2013-09-03 Kellogg Brown & Root Llc Method for nitrogen rejection and or helium recovery in an LNG liquefaction plant
CN102994184B (zh) * 2012-12-03 2013-10-30 中国石油集团工程设计有限责任公司 一种液化天然气联产液氮的装置及方法
KR101550618B1 (ko) 2014-01-14 2015-09-07 현대자동차 주식회사 리보일링 장치 및 이를 구비한 재생탑
US10488105B2 (en) * 2015-12-14 2019-11-26 Exxonmobil Upstream Research Company Method and system for separating nitrogen from liquefied natural gas using liquefied nitrogen
FR3075658B1 (fr) * 2017-12-21 2022-01-28 Air Liquide Procede de limitation de la concentration d'oxygene contenu dans un courant de biomethane
US11221176B2 (en) * 2018-08-14 2022-01-11 Air Products And Chemicals, Inc. Natural gas liquefaction with integrated nitrogen removal
US20200378682A1 (en) * 2019-05-29 2020-12-03 Uop Llc Use of dense fluid expanders in cryogenic natural gas liquids recovery

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB968019A (en) * 1963-08-19 1964-08-26 Alexander Harmens Cold separation of gas mixtures
GB1288762A (es) * 1968-09-16 1972-09-13
DE2154965A1 (de) * 1971-06-24 1973-05-10 Linde Ag Verfahren zur zerlegung von gasgemischen
DE2202206A1 (de) * 1972-01-18 1973-07-26 Messer Griesheim Gmbh Verfahren zur zerlegung von gasgemischen durch zweistufige rektifikation
US4451275A (en) * 1982-05-27 1984-05-29 Air Products And Chemicals, Inc. Nitrogen rejection from natural gas with CO2 and variable N2 content
AU572890B2 (en) * 1983-09-20 1988-05-19 Costain Petrocarbon Ltd. Separation of hydrocarbon mixtures
US4592767A (en) * 1985-05-29 1986-06-03 Union Carbide Corporation Process for separating methane and nitrogen
US4732598A (en) * 1986-11-10 1988-03-22 Air Products And Chemicals, Inc. Dephlegmator process for nitrogen rejection from natural gas
US5041149A (en) * 1990-10-18 1991-08-20 Union Carbide Industrial Gases Technology Corporation Separation of nitrogen and methane with residue turboexpansion
FR2682964B1 (fr) * 1991-10-23 1994-08-05 Elf Aquitaine Procede de deazotation d'un melange liquefie d'hydrocarbures consistant principalement en methane.
US5339641A (en) * 1993-07-07 1994-08-23 Praxair Technology, Inc. Cryogenic liquid nitrogen production system
MY113525A (en) * 1995-10-05 2002-03-30 Bhp Petroleum Pty Ltd Liquefaction process
US5927103A (en) * 1998-06-17 1999-07-27 Praxair Technology, Inc. Carbon dioxide production system with integral vent gas condenser
MY117066A (en) * 1998-10-22 2004-04-30 Exxon Production Research Co Process for removing a volatile component from natural gas
GB0111961D0 (en) * 2001-05-16 2001-07-04 Boc Group Plc Nitrogen rejection method
US6393866B1 (en) * 2001-05-22 2002-05-28 Praxair Technology, Inc. Cryogenic condensation and vaporization system
FR2885679A1 (fr) * 2005-05-10 2006-11-17 Air Liquide Procede et installation de separation de gaz naturel liquefie

Also Published As

Publication number Publication date
WO2008155653A2 (en) 2008-12-24
CA2687886A1 (en) 2008-12-24
JP2011513503A (ja) 2011-04-28
KR20100021443A (ko) 2010-02-24
CN102084199A (zh) 2011-06-01
AU2008264885A1 (en) 2008-12-24
US20080314079A1 (en) 2008-12-25
RU2010101417A (ru) 2011-07-27
WO2008155653A3 (en) 2011-04-07
BRPI0812568A2 (pt) 2015-02-18
TW200902703A (en) 2009-01-16
EP2179235A2 (en) 2010-04-28

Similar Documents

Publication Publication Date Title
PE20090450A1 (es) Configuracion de caldera para columna de eliminacion de nitrogeno
CL2012000706A1 (es) Proceso para separar una corriente de gas que contiene metano, c2, c3 e hidrocarburos más pesados en una fracción de gas residual volatil y una fraccion relativamente menos volatil.
AR058013A1 (es) Proceso para la hidrogenacion de glicerol
PE20080391A1 (es) Proceso y aparato para licuefaccion de gas natural y recuperacion de componentes mas pesados que el metano del gas natural
AR090327A1 (es) Separacion de dioxodo de carbono y etano de una corriente mixta
PE20151709A1 (es) Eliminacion de nitrogeno integrada en la produccion de gas licuado utilizando circuito de reinyeccion dedicado
BRPI0515295A (pt) método e sistema para o processamento de gás natural liquefeito
AR088784A1 (es) Procedimiento de deshidratacion de etanol en etileno con bajo consumo energetico
CO6470814A2 (es) Procesamiento de gas natural licuado y gas hidrocarburo
CO6270264A2 (es) Procedimiento de gases de hidrocarburos
AR089595A1 (es) Metodo para separar dioxido de carbono de corrientes liquidas de gas acido
PE20040391A1 (es) Proceso para licuar gas natural
CO2019009948A2 (es) Licuefactor de gas natural líquido que utiliza refrigeración mecánica y de nitrógeno líquido
AR020930A1 (es) Un proceso para separar un componente mas volatil que metano, de una corriente de gas natural liquida presurizada.
AR026989A1 (es) Procedimiento para licuar una corriente de gas presurizado rica en metano
PE20040796A1 (es) Procesamiento de gases de hidrocarburos
EP2808634A3 (en) Liquefied gas treatment system
PE20110645A1 (es) Produccion de gas natural licuado
CO2017002298A2 (es) Sistema refrigerante mixto dual
PE20150658A1 (es) Metodo y aparato para la remocion de hidrocarburos de una corriente de gas natural
AR058276A1 (es) Proceso para remover compuestos de azufre y dioxido de carbono de una corriente gaseosa
CO2017002301A2 (es) Sistema refrigerante mixto dual
CO2023017112A2 (es) Fabricante de amoníaco-hidrógeno limpio modular, transportable
AR098489A1 (es) Recuperación de gnl del singás empleando un refrigerante mixto
PE20121792A1 (es) Procesamiento de gases de hidrocarburos

Legal Events

Date Code Title Description
FA Abandonment or withdrawal