KR970020946A - 농축 공기 개질 및 합성 루프에로의 질소 주입에 의한 암모니아 제법 - Google Patents

농축 공기 개질 및 합성 루프에로의 질소 주입에 의한 암모니아 제법 Download PDF

Info

Publication number
KR970020946A
KR970020946A KR1019960045115A KR19960045115A KR970020946A KR 970020946 A KR970020946 A KR 970020946A KR 1019960045115 A KR1019960045115 A KR 1019960045115A KR 19960045115 A KR19960045115 A KR 19960045115A KR 970020946 A KR970020946 A KR 970020946A
Authority
KR
South Korea
Prior art keywords
stream
ammonia
nitrogen
oxygen
synthesis
Prior art date
Application number
KR1019960045115A
Other languages
English (en)
Other versions
KR100419763B1 (ko
Inventor
죠셉 레이 르블랑
슈탄 에이. 네쯔
Original Assignee
왈포드 크레이그 더블유.
더 엠. 더블유. 켈로그 컴패니
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 왈포드 크레이그 더블유., 더 엠. 더블유. 켈로그 컴패니 filed Critical 왈포드 크레이그 더블유.
Publication of KR970020946A publication Critical patent/KR970020946A/ko
Application granted granted Critical
Publication of KR100419763B1 publication Critical patent/KR100419763B1/ko

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/025Preparation or purification of gas mixtures for ammonia synthesis
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/382Multi-step processes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0482Process control; Start-up or cooling-down procedures
    • 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
    • F25J3/04Processes 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 for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04539Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels
    • 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
    • F25J3/04Processes 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 for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04563Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating
    • F25J3/04587Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating for the NH3 synthesis, e.g. for adjusting the H2/N2 ratio
    • 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
    • F25J3/04Processes 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 for air
    • F25J3/04521Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04593The air gas consuming unit is also fed by an air 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
    • F25J3/04Processes 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 for air
    • F25J3/04763Start-up or control of the process; Details of the apparatus used
    • F25J3/04866Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04969Retrofitting or revamping of an existing air fractionation unit
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/14Details of the flowsheet
    • C01B2203/142At least two reforming, decomposition or partial oxidation steps in series
    • C01B2203/143Three or more reforming, decomposition or partial oxidation steps in series
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/14Details of the flowsheet
    • C01B2203/146At least two purification steps in series
    • C01B2203/147Three or more purification steps in series
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/80Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
    • C01B2203/82Several process steps of C01B2203/02 - C01B2203/08 integrated into a single apparatus
    • 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
    • F25J2215/50Oxygen or special cases, e.g. isotope-mixtures or low purity O2
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Automation & Control Theory (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

연속한 제1 및 제2개질기 및 탄화수소 공급 재료, 증기 및 공기를 반응시켜 화학양론적 설계로 수소 및 질소로 이루어진 조성 합성 가스 스트림을 생성하기 위한 이동 전환기를 포함한 앞공정 및 재순환 합성 가스 스트림을 조성 가스와 배합하여 합성 가스 공급 재료를 생성하여 암모니아 전환기로 보내는 합성 루프를 갖는, 암모니아 공장의 생산 용량을 증가시키기 위한 레트로피트(retrofit)방법. 레트로피트 방법은 공기 분리 장치를 설치하여 산소 및 질소 스트림을 공급하는 것을 수반한다. 산소는 제2개질기로 공급되는 공기를 농축하는데 사용되어 실질적으로 설계 화학양론 및 용량을 능가하는 조성 가스의 수소 함량을 증가 시킨다. 질소 스트림을 합성루프로 공급하여 합성 가스 공급 재료 내에서 원하는 수소 대 질소비를 수득하여 암모니아 전환기로 보내어 조성 가스에서 과잉 수소를 보충한다. 원한다면, 합성 루프를 개선하여 고 활성 촉매 전환기를 포함시켜 암모니아 생산을 증가 시킨다.

Description

농축 공기 개질 및 합성 루프에로의 질소 주입에 의한 암모니아 제법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명에 따른 공기 분리 장치를 포함하는 암모니아 공정의 농축 공기/질소를 주입하는 것을 도식적으로 나타낸 것이다.

Claims (20)

  1. 연속된 제1 및 제2개질기 및 탄화수소 공급 재료, 증기 및 공기를 반응시켜 화학양론적 설계상 수소 및 질소로 이루어진 조성 합성 가스 스트림을 생성하기 위한 고온 및 저온 이동 전환기를 포함하는 앞공정, 및 재순환 합성 가스 스트림을 조성 가스와 배합하여 합성 가스 공급 재료를 형성하고 암모니아 전환기로 보내는 합성 루프를 갖는 암모니아 공장의 생산 용량을 증가 시키기 위한 레트로피트 방법으로서 : 제2개질기에로 공급되는 공기를 산소로써 농축시키고 실질적으로 설계 양론 이상으로 조성 가스의 수소 함량을 증가시키는 단계; 실질적으로 순수한 질소 스트림을 합성 루프에 공급하여 합성 공급 재료내에 원하는 수소 대 질소비를 수득하여 암모니아 전환기로 보내는 단계로 이루어지는 레트로피트 방법.
  2. 제1항에 있어서, 농축-단계에서 공기에 첨가되는 산소-농축 스트림 및 실질적으로 순수한 질소 스트림원으로서 사용된 질소-농축 스트림을 생성하기 위한 공기 분리 장치의 설치를 포함하는 방법.
  3. 제2항에 있어서, 암모니아 공장의 현재 합성 루프 용량이 레트로피트 이전의 현재 앞공정의 용량을 초과하는 방법.
  4. 제1항에 있어서, 레트로피트 전에 현재 앞 공정의 용량을 초과하도록 합성 루프의 용량을 증가 시키기 위한 합성 루프 변형 단계를 더 포함하는 방법.
  5. 제1항에 있어서, 암모니아 공장이 합성 루프에 대한 조성 합성 가스 스트림을 좌우하는 탄소 산화물을 제거하기 위한 메탄 발생 장치를 포함하고, 질소 공급 단계는 질소 스트림을 메탄 발생 장치로부터 상류에서 보정 합성 가스 스트림내로 주입하는 것으로 이루어지는 방법.
  6. 제1항에 있어서, 질소 스트림에 필수적으로 산소 및 산소 화합물이 없고 질소 스트림을 조성 합성 가스 스트림에 첨가하는 방법.
  7. 제1항에 있어서, 질소 스트림에 필수적으로 산소 및 산소 화합물이 없고 질소 스트림을 합성 가스 공급 재료에 주입하는 방법.
  8. (1) 탄화수소 공급 재료 스트림을 증기 및 압축된 공기와 반응시켜 선재하는 용량으로 설계 HN 비를 갖는 조성 합성 가스 스트림을 생산하는 제1개질기, 제2개질기, 공기 압축기 및 CO2제거 장치를 포함하는 앞공정, 및(2) 선재하는 용량으로 암모니아를 생산하기 위해 재순환 합성 가스 스트림을 조성 합성 가스 스트림과 배합하여 합성 가스 공급 재료를 생성하여 암모니아 전환기로 보내는 합성 루프를 갖은 암모니아 공장의 생산을 증가시키기 위한, 하기의 단계로 이루어진 레트로피트 방법으로서;공기 분리 장치를 설치하여 산소-농축 및 질소-농축 스트림을 생산하고; 산소-농축 스트림을 압축된 공기에 주입하여, CO2제거 장치로부터 원료 합성 가스 스트림이 설계 비보다 상대적으로 증가된 NH 비를 가지는 선재하는 용량에 비해 상대적으로 증가된 용량으로, 앞공정을 조작하고, 질소-농축 스트림을 합성 루프로 공급하며; 합성 루프를 변형하여 합성루프의 암모니아 용량을 증가시키는 단계들로 이루어진 레트로피트 방법.
  9. 제8항에 있어서, 주입 단계에서 산소-농축 공기 스트림을 생성하여 25 내지 40 부피 퍼센트 산소를 함유한 제2개질기로 공급하는 레트로피트 방법.
  10. 제9항에 있어서 산소-농축 스트림이 40 내지 100 부피 퍼센트 산소를 함유하는 레트로피트 방법.
  11. 제9항에 있어서, 산소-농축 스트림이 50 내지 80 부피 퍼센트 산소를 함유하는 레트로피트 방법.
  12. 제8항에 있어서, 질소-농축 스트림이 1 부피 피센트 이하의 산소를 포함하고, 질소-농축 스트림이 원료 합성 가스 스트림내로 주입되고, 상기 방법은 질소-농축된 원료 합성 가스 스트림을 메탄 발생 장치로 통과시켜 필수적으로 산소 및 산소-함유 화합물이 없는 조성 합성 가스 스트림을 생성하는 단계를 포함하는 레트로피트 방법.
  13. 제11항에 있어서, 질소-농축 스트림이 필수적으로 산소가 없고 질소-농축 스트림을 메탄 발생 장치로부터 하류에 있는 조성 합성 가스 스트림내로 주입하는 레트로피트 방법.
  14. 제11항에 있어서, 질소-농축 스트림에 필수적으로 산소가 없고 질소-농축 스트림을 합성 가스 공급재료로 주입하여 암모니아 전환기로 보내는 레트로피트 방법.
  15. 제8항에 있어서, 합성 루프의 변형에 흑연-함유 탄소 상에 지지된 플라티늄 족 금속으로 이루어진 고활성 촉매 기재의 암모니아 전환 용량의 설치가 포함되는 레트로피트 방법.
  16. 하기의 단계로 이루어진 암모니아 합성 방법; (a) 공기를 산소-농축 및 질소-농축 스트림으로 분리하는 단계, (b) 공기를 단계 (a)로부터의 산소-농축 스트림과 혼합하여 25-40 몰퍼센트 산소를 함유한 산소-농축된 스트림을 생성하는 단계; (c) 단계(b)로부터의 산소-농축 스트림을 자열식 개질기로부터 상류에 제1개질기 및 하류에 이동 전환기, CO2제거 장치 및 메탄 발생 장치를 포함하는 합성 가스 장치의 자열식 개질기로 주입하여 합성 스트림을 생산하는 단계; 및 (d) 단계(c)로부터의 합성 가스 스트림 및 단계(a)로부터의 질소-농축 스트림을 조성 가스로서 암모니아 합성 루프로 공급하는 단계;(e) 암모니아 합성 루프를 작동시켜 (1) 암모니아 합성 반응기 공급 재료 스트림내 질소 및 수소를 전환시켜 암모니아-농축 스트림을 생성,(2) 암모니아-농축 스트림으로부터 암모니아를 회수하여 재순환 가스 스트림을 생성,(3) 합성 루프로부터 배출 스트림을 제거, (4) 배출 스트림으로부터 수소-농축 가스를 회수하고, 및 (5) 단계(d)로부터 재순환 스트림 및 조성 가스를 수소-농축 가스와 배합하여 암모니아 합성 반응기 공급 재료 스트림을 생성하는 단계.
  17. 제1항의 방법에 의해 수득된 레트로피트된 암모니아 공장.
  18. 제8항의 방법에 의해 수득된 레트로피트된 암모니아 공장.
  19. 제12항의 방법에 의해 수득된 레트로피트된 암모니아 공장.
  20. 제15항의 방법에 의해 수득된 레트로피트된 암모니아 공장.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019960045115A 1995-10-25 1996-10-10 농축공기개질및합성루프에로의질소주입에의한암모니아제법 KR100419763B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/547,853 1995-10-25
US08/547,853 US5736116A (en) 1995-10-25 1995-10-25 Ammonia production with enriched air reforming and nitrogen injection into the synthesis loop

Publications (2)

Publication Number Publication Date
KR970020946A true KR970020946A (ko) 1997-05-28
KR100419763B1 KR100419763B1 (ko) 2004-05-17

Family

ID=24186420

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019960045115A KR100419763B1 (ko) 1995-10-25 1996-10-10 농축공기개질및합성루프에로의질소주입에의한암모니아제법

Country Status (10)

Country Link
US (1) US5736116A (ko)
EP (1) EP0770578B1 (ko)
JP (1) JP4053103B2 (ko)
KR (1) KR100419763B1 (ko)
BR (1) BR9605221A (ko)
CA (1) CA2184126C (ko)
DE (1) DE69617878T2 (ko)
ES (1) ES2166853T3 (ko)
MX (1) MX9604151A (ko)
NO (1) NO964526L (ko)

Families Citing this family (51)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2164425T3 (es) * 1997-04-10 2002-02-16 Air Liquide Inyeccion de oxigeno y nitrogeno para aumentar la produccion de amoniaco.
US5775128A (en) * 1997-05-02 1998-07-07 Praxair Technology, Inc. Process for producing ammonia and recovering argon using low purity oxygen
NO308398B1 (no) * 1997-06-06 2000-09-11 Norsk Hydro As Fremgangsmate for utforelse av katalytiske eller ikke-katalytiske prosesser hvori oksygen er ±n av reaktantene
US6306917B1 (en) * 1998-12-16 2001-10-23 Rentech, Inc. Processes for the production of hydrocarbons, power and carbon dioxide from carbon-containing materials
WO2001009038A2 (en) 1999-07-29 2001-02-08 Sasol Technology (Pty) Ltd Natural gas conversion to hydrocarbons and ammonia
US6632846B2 (en) * 1999-08-17 2003-10-14 Rentech, Inc. Integrated urea manufacturing plants and processes
US6192707B1 (en) 1999-11-12 2001-02-27 Praxair Technology, Inc. Cryogenic system for producing enriched air
US6620399B1 (en) 2000-04-10 2003-09-16 Robert Rudolf Josef Jungerhans Purification of gases, in synthesis gas production process
DE10055818A1 (de) * 2000-11-10 2002-05-23 Ammonia Casale Sa Verfahren zum Herstellen von Ammoniak aus einem Stickstoff-Wasserstoff-Gemisch aus Erdgas
US6976362B2 (en) * 2001-09-25 2005-12-20 Rentech, Inc. Integrated Fischer-Tropsch and power production plant with low CO2 emissions
US20040020239A1 (en) * 2002-03-08 2004-02-05 Laforce Craig Steven Method of producing an oxygen-enriched air stream
US6793910B1 (en) 2002-10-02 2004-09-21 K. David Lyons Process to accomplish autothermal or steam reforming via a reciprocating compression device
US7081230B2 (en) * 2002-11-15 2006-07-25 Kellogg Brown & Root Llc Split-flow, vertical ammonia converter
US20040219088A1 (en) * 2003-04-29 2004-11-04 Harvey Wen Mini ammonia plant
US7892511B2 (en) * 2004-07-02 2011-02-22 Kellogg Brown & Root Llc Pseudoisothermal ammonia process
US7435401B2 (en) * 2004-07-02 2008-10-14 Kellogg Brown & Root Llc Pseudoisothermal ammonia process
US7094384B1 (en) * 2005-09-19 2006-08-22 University Of Central Florida Research Foundation, Inc. Combined methane decomposition and ammonia formation cell
US20080016768A1 (en) 2006-07-18 2008-01-24 Togna Keith A Chemically-modified mixed fuels, methods of production and used thereof
EP2065337A1 (en) * 2007-11-27 2009-06-03 Ammonia Casale S.A. Process for producing ammonia synthesis gas
US7687041B2 (en) * 2008-02-27 2010-03-30 Kellogg Brown & Root Llc Apparatus and methods for urea production
US7967896B2 (en) * 2008-03-26 2011-06-28 Uop Llc Use of hydraulic turbocharger for recovering energy from high pressure solvents in gasification and natural gas applications
US7867465B2 (en) * 2008-05-29 2011-01-11 Kellogg Brown & Root Llc Cold wall horizontal ammonia converter
EP2172417A1 (en) * 2008-10-02 2010-04-07 Ammonia Casale S.A. Process for the production of ammonia synthesis gas
EP2199253A1 (en) * 2008-12-18 2010-06-23 Ammonia Casale S.A. Process and equipment for the production of ammonia make-up syngas with an air separation unit as nitrogen source
CN102449124A (zh) * 2009-05-26 2012-05-09 巴斯夫欧洲公司 由流体料流,尤其是由合成气回收二氧化碳的方法
EP2284125A1 (en) 2009-08-13 2011-02-16 Ammonia Casale S.A. Process for revamping an ammonia plant with nitrogen-based washing of a purge stream
EP2292554A1 (en) 2009-09-02 2011-03-09 Ammonia Casale S.A. Production of ammonia make-up syngas with cryogenic purification
US9083020B2 (en) * 2009-09-04 2015-07-14 Lg Fuel Cell Systems Inc. Reducing gas generators and methods for generating reducing gas
US8377154B2 (en) * 2010-05-18 2013-02-19 Kellogg Brown & Root Llc Gasification system and process for maximizing production of syngas and syngas-derived products
CN102145900A (zh) * 2011-02-22 2011-08-10 安徽淮化股份有限公司 合成氨原料气中氢氮比的调节方法
EP2662327A1 (en) 2012-05-07 2013-11-13 Ammonia Casale S.A. Method of revamping of an ammonia plant fed with natural gas
AU2013282904B2 (en) 2012-06-27 2016-11-03 Grannus, Llc Polygeneration production of power and fertilizer through emissions capture
BR112014032417B1 (pt) 2012-06-29 2021-05-18 Dow Global Technologies Llc solução aquosa de alcanolamina e processo para remover sulfeto de hidrogênio de uma mistura gasosa
EP2867345B1 (en) 2012-06-29 2018-08-01 Dow Global Technologies LLC Aqueous alkanolamine absorbent composition comprising piperazine for enhanced removal of hydrogen sulfide from gaseous mixtures and method for using the same
WO2014028623A1 (en) 2012-08-17 2014-02-20 Vinod Kumar Arora Ammonia plant upgrading-multistage integrated chilling of process air compressor with ammonia compressor followed by air flow split and multistage air preheating to secondary ammonia reformer
DE102013004341A1 (de) 2013-03-14 2014-09-18 Thyssenkrupp Uhde Gmbh Verfahren zur Oxidation von Ammoniak und dafür geeignete Anlage
US9643856B2 (en) 2013-08-07 2017-05-09 Kellogg Brown+Root LLC Methods and systems for making ammonia in a double ammonia converter system
EP2957544A1 (en) * 2014-06-18 2015-12-23 Casale SA Process for production of ammonia and derivatives, in particular urea
CA2867731C (en) * 2014-10-15 2022-08-30 Nova Chemicals Corporation High conversion and selectivity odh process
EP3026016A1 (en) 2014-11-27 2016-06-01 Casale SA A method for revamping an ammonia plant
CA2986035C (en) 2015-05-20 2023-08-22 Dow Global Technologies Llc An aqueous alkanolamine composition and process for the selective removal of hydrogen sulfide from gaseous mixtures
EP3336061A1 (en) 2016-12-14 2018-06-20 Casale SA A process for the synthesis of ammonia
EP3366645A1 (en) * 2017-02-28 2018-08-29 Casale Sa Ammonia-urea integrated process and plant
DE102017204208A1 (de) * 2017-03-14 2018-09-20 Thyssenkrupp Ag Verfahren und Anlage zur Erzeugung und Aufbereitung eines Synthesegasgemisches
US11370658B2 (en) 2017-07-25 2022-06-28 Topsoe A/S Method for the preparation of ammonia synthesis gas
NZ760484A (en) 2017-07-25 2024-05-31 Haldor Topsoee As Method for the preparation of ammonia synthesis gas
DE102018108989A1 (de) 2018-04-16 2019-10-17 Thyssenkrupp Ag Industrieanlage mit Anfahrofen und Verfahren zum Initiieren chemischer Reaktionen
US11834333B2 (en) 2020-04-22 2023-12-05 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation Procédés Georges Claude Nitrogen process for production of ammonia and liquid hydrogen
WO2022112497A1 (en) * 2020-11-27 2022-06-02 Basf Se A process for separating h2 from a gas mixture
BE1029787B1 (de) * 2021-09-22 2023-04-24 Thyssenkrupp Ind Solutions Ag Verfahren zur Ammoniaksynthese und Anlage zur Herstellung von Ammoniak
EP4334242A1 (de) * 2021-09-22 2024-03-13 thyssenkrupp Uhde GmbH Verfahren zur ammoniaksynthese und anlage zur herstellung von ammoniak

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4122040A (en) * 1974-09-02 1978-10-24 The British Petroleum Company Limited Platinum group metal catalyst
US4055628A (en) * 1974-09-02 1977-10-25 The British Petroleum Company Limited Method for preparing graphite containing carbon
GB1565074A (en) * 1976-11-03 1980-04-16 British Petroleum Co Process for the production of ammonia
US4230669A (en) * 1978-07-17 1980-10-28 Pullman Incorporated Radial ammonia converter
FR2473032A1 (fr) * 1980-01-07 1981-07-10 Banquy David Procede de production d'ammoniac et du gaz de synthese correspondant
US4414191A (en) * 1981-08-07 1983-11-08 Union Carbide Corporation Process for the production of ammonia
EP0093502B2 (en) * 1982-04-14 1988-11-17 Imperial Chemical Industries Plc Ammonia production process
GB8414491D0 (en) * 1984-06-07 1984-07-11 Humphreys & Glasgow Ltd Ammonia plant re-vamp process
US4568532A (en) * 1984-10-16 1986-02-04 The M. W. Kellogg Company Supplemental ammonia synthesis
US4568530A (en) * 1984-10-16 1986-02-04 The M. W. Kellogg Company Ammonia synthesis
US4568531A (en) * 1984-10-16 1986-02-04 The M. W. Kellogg Company Ammonia purge gas conversion
US4696799A (en) * 1986-07-15 1987-09-29 The M. W. Kellogg Company Ammonia synthesis converter
US4735780A (en) * 1986-07-15 1988-04-05 The M. W. Kellogg Company Ammonia synthesis converter
US4792441A (en) * 1988-01-19 1988-12-20 Air Products And Chemicals, Inc. Ammonia synthesis
US4886651A (en) * 1988-05-18 1989-12-12 Air Products And Chemicals, Inc. Process for co-production of higher alcohols, methanol and ammonia
US5011625A (en) * 1989-12-11 1991-04-30 The M. W. Kellogg Company Autothermal steam reforming process
US5180570A (en) * 1992-01-23 1993-01-19 Lee Jing M Integrated process for making methanol and ammonia
US5250270A (en) * 1992-07-17 1993-10-05 The M. W. Kellogg Company Catalytic reactor bed

Also Published As

Publication number Publication date
CA2184126A1 (en) 1997-04-26
EP0770578A2 (en) 1997-05-02
NO964526D0 (no) 1996-10-24
US5736116A (en) 1998-04-07
DE69617878T2 (de) 2002-04-25
BR9605221A (pt) 1998-07-21
CA2184126C (en) 2007-04-10
EP0770578A3 (en) 1998-10-28
ES2166853T3 (es) 2002-05-01
AU701282B2 (en) 1999-01-21
EP0770578B1 (en) 2001-12-12
MX9604151A (es) 1997-04-30
KR100419763B1 (ko) 2004-05-17
JP4053103B2 (ja) 2008-02-27
NO964526L (no) 1997-04-28
DE69617878D1 (de) 2002-01-24
AU6432496A (en) 1997-05-01
JPH09165215A (ja) 1997-06-24

Similar Documents

Publication Publication Date Title
KR970020946A (ko) 농축 공기 개질 및 합성 루프에로의 질소 주입에 의한 암모니아 제법
CA2357527C (en) Methanol recycle stream
US6706770B2 (en) Co-production of hydrogen and methanol from steam reformate
US5496859A (en) Gasification process combined with steam methane reforming to produce syngas suitable for methanol production
CN107021450B (zh) 用于制备氨和尿素的方法
EP1434926B1 (en) Method and plant for increasing oil recovery by gas injection
AU2011276058B2 (en) Process for producing ammonia synthesis gas
US6048508A (en) Process for obtaining carbon monoxide and hydrogen
US4578214A (en) Process for ammonia syngas manufacture
EP2994415B1 (en) A process for producing ammonia synthesis gas with high temperature shift and low steam-to-carbon ratio
EP2805914A1 (en) A process for co-production of ammonia, urea and methanol
KR970006922B1 (ko) 일산화탄소가 풍부한 가스의 제조방법
CA2087887A1 (en) An integrated process for making methanol and ammonia
AU2018308586A1 (en) Method for the preparation of ammonia synthesis gas
EP3728112B1 (en) Process for producing a hydrogen-containing synthesis gas
JP2004516219A (ja) 合成ガスの製造のための統合された方法および設備
JP2007536347A (ja) メタノール合成用システム及び方法
EP3083490B1 (en) Process for producing ammonia synthesis gas
WO2023180114A1 (en) Process for co-producing ammonia and methanol with reduced carbon
EP1441981B1 (en) Reactor for reformation of natural gas and simultaneous production of hydrogen
WO2003029174A2 (en) Methanol production process
EA005458B1 (ru) Способ увеличения производительности существующей технологической установки и технологическая установка
JP3947266B2 (ja) 水素製造方法およびそれに用いる装置
SU1111983A1 (ru) Способ совместного производства аммиака и метанола
CN116710394A (zh) 用于甲醇生产的方法和装置

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20130130

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20140129

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20150129

Year of fee payment: 12

FPAY Annual fee payment

Payment date: 20160125

Year of fee payment: 13

EXPY Expiration of term