ES2030467T3 - Proceso mejorado para sintesis heterogenea y reactores relacionados. - Google Patents

Proceso mejorado para sintesis heterogenea y reactores relacionados.

Info

Publication number
ES2030467T3
ES2030467T3 ES198888110174T ES88110174T ES2030467T3 ES 2030467 T3 ES2030467 T3 ES 2030467T3 ES 198888110174 T ES198888110174 T ES 198888110174T ES 88110174 T ES88110174 T ES 88110174T ES 2030467 T3 ES2030467 T3 ES 2030467T3
Authority
ES
Spain
Prior art keywords
synthesis
improved process
heterogenous
bed
gas
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
ES198888110174T
Other languages
English (en)
Inventor
Umberto Zardi
Giorgio Pagani
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Casale SA
Original Assignee
Ammonia Casale SA
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 Ammonia Casale SA filed Critical Ammonia Casale SA
Application granted granted Critical
Publication of ES2030467T3 publication Critical patent/ES2030467T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00—Ammonia; Compounds thereof
    • C01C1/02—Preparation, purification or separation of ammonia
    • C01C1/04—Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0417—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor
    • C01C1/0423—Cold wall reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0403—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal
    • B01J8/0407—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds
    • B01J8/0415—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more cylindrical annular shaped beds the beds being superimposed one above the other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0461—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds
    • B01J8/0469—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds the beds being superimposed one above the other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/152—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00194—Tubes
    • 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
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PROCEDIMIENTO MEJORADO PARA SINTESIS HETEROGENEA Y REACTORES RELACIONADOS, SEGUN EL CUAL EL REACTOR DE SINTESIS SE DISTRIBUYE EN TRES LECHOS CATALITICOS AXIAL-RADIALES O RADIALES, SIENDO LLEVADO A CABO EL CONTROL DE LA TEMPERATURA ENTRE LECHOS POR MEDIO DEL GAS FRIO NUEVO ENTRE EL PRIMERO Y SEGUNDO LECHOS, Y POR MEDO DE ENFRIAMIENTO INDIRECTO CON UN CAMBIADOR ENTRE EL SEGUNDO Y TERCER LECHOS DEL GAS QUE DEJA EL SEGUNDO LECHO, UTILIZANDO GAS NUEVO QUE SE CALIENTA DENTRO DE LOS TUBOS DE DICHO CAMBIADOR.
ES198888110174T 1987-07-03 1988-06-25 Proceso mejorado para sintesis heterogenea y reactores relacionados. Expired - Lifetime ES2030467T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH252987 1987-07-03

Publications (1)

Publication Number Publication Date
ES2030467T3 true ES2030467T3 (es) 1992-11-01

Family

ID=4235852

Family Applications (1)

Application Number Title Priority Date Filing Date
ES198888110174T Expired - Lifetime ES2030467T3 (es) 1987-07-03 1988-06-25 Proceso mejorado para sintesis heterogenea y reactores relacionados.

Country Status (8)

Country Link
US (1) US4963338A (es)
EP (1) EP0297474B1 (es)
CN (1) CN1014031B (es)
AT (1) ATE74291T1 (es)
CA (1) CA1306846C (es)
DE (1) DE3869677D1 (es)
ES (1) ES2030467T3 (es)
SU (1) SU1671148A3 (es)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2030467T3 (es) * 1987-07-03 1992-11-01 Ammonia Casale S.A. Proceso mejorado para sintesis heterogenea y reactores relacionados.
DE68900388D1 (de) * 1988-12-09 1991-12-05 Ammonia Casale Sa Reaktor fuer die exotherme heterogene katalytische synthese.
US5254316A (en) * 1988-12-21 1993-10-19 Ammonia Casale S.A. Reactors for heterogeneous synthesis
DE68906006T2 (de) * 1988-12-21 1993-08-12 Ammonia Casale Sa Reaktoren fuer heterogene synthesen.
CH678286A5 (es) * 1989-03-09 1991-08-30 Ammonia Casale Sa
DE4207905A1 (de) * 1992-03-12 1993-09-16 Bayer Ag Festbettreaktoren mit kurzem katalysatorbett in stroemungsrichtung
US5250270A (en) * 1992-07-17 1993-10-05 The M. W. Kellogg Company Catalytic reactor bed
DK169696B1 (da) * 1992-12-07 1995-01-16 Topsoe Haldor As Fremgangsmåde til køling af syntesegas i en katalytisk reaktor
DE4303471A1 (de) * 1993-02-06 1994-08-11 Noell Dbi Energie Entsorgung Reaktor für exotherme katalytische Gasreaktionen
DE4446359A1 (de) * 1993-12-29 1995-07-06 Ammonia Casale Sa Verfahren zur in-situ-Modernisierung eines heterogenen exothermen Synthesereaktors, insbesondere eines sogenannten Kellog-Reaktors
US5427760A (en) * 1994-02-22 1995-06-27 Brown & Root Petroleum And Chemicals Axial-radial reactors in the braun ammonia synloop with extrnal heat sink
DK173023B1 (da) * 1997-04-21 1999-11-15 Topsoe Haldor As Fremgangsmåde og reaktor til fremstilling af ammoniak
US6350614B1 (en) * 2000-02-07 2002-02-26 Concept Sciences, Inc System for the ion exchange purification of hydroxylamine
US7435862B2 (en) 2000-11-30 2008-10-14 Sud-Chemie Inc. Radial reactor loading of a dehydrogenation catalyst
US20020183571A1 (en) * 2000-11-30 2002-12-05 Sud-Chemie Inc. Radial reactor loading of a dehydrogenation catalyst
DE102004003070A1 (de) * 2004-01-21 2005-08-18 Uhde Gmbh Verfahren und Vorrichtung zum Eindüsen von Sauerstoff mit radialer Katalysatordurchströmung
US7435401B2 (en) * 2004-07-02 2008-10-14 Kellogg Brown & Root Llc Pseudoisothermal ammonia process
US7892511B2 (en) * 2004-07-02 2011-02-22 Kellogg Brown & Root Llc Pseudoisothermal ammonia process
CN100377774C (zh) * 2004-10-22 2008-04-02 中国石油化工股份有限公司 一种烃油催化转化反应器
EP2354092A1 (en) * 2010-01-29 2011-08-10 Ammonia Casale S.A. A method for modernizing the synthesis loop of an ammonia plant
WO2019121155A1 (en) * 2017-12-21 2019-06-27 Casale Sa Multi-bed catalytic converter
EP4171793B1 (en) * 2020-06-25 2024-03-20 Casale Sa Multi-bed ammonia converter
WO2021259929A1 (en) * 2020-06-25 2021-12-30 Casale Sa Multi-bed catalytic reactor

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT289847B (de) * 1969-03-18 1971-05-10 Chemie Linz Ag Verfahren und Vorrichtung zur alleinigen oder zusätzlichen Temperaturregelung von Hochdrucksynthesereaktoren, vorzugsweise für die Ammoniaksynthese, durch Kaltgaseinspeisung
AT299981B (de) * 1970-04-21 1972-07-10 Chemie Linz Ag Vorrichtung zur Erzielung einer gleichmäßigen Gasverteilung in radial durchströmten Katalysatorlagen in Reaktoren für katalytische, exotherme Hochdrucksynthesen, vorzugsweise der Ammoniaksynthese
US3751232A (en) * 1971-01-14 1973-08-07 Universal Oil Prod Co Means for effecting a multiple stage contact of a reactant stream
US3957449A (en) * 1972-02-28 1976-05-18 Imperial Chemical Industries Limited Synthesis plant
IT1041778B (it) * 1975-07-15 1980-01-10 Snam Progetti Reattore a flusso radiale per la sintesi dell ammoniaca con produzione di vapore ad alto livello termico
GB1574723A (en) * 1976-03-10 1980-09-10 Haldor Topsoe As Apparatus for the synthesis of ammonia
US4346060A (en) * 1978-07-17 1982-08-24 Pullman Incorporated Radial ammonia converters
SU963951A1 (ru) * 1980-08-01 1982-10-07 Предприятие П/Я Р-6603 Способ синтеза аммиака
US4789527A (en) * 1983-03-07 1988-12-06 Exxon Research & Engineering Co. Catalytic gas synthesis apparatus
US4482523A (en) * 1983-11-14 1984-11-13 The M. W. Kellogg Company Ammonia synthesis converter
CH666198A5 (it) * 1985-09-13 1988-07-15 Ammonia Casale Sa Reattore per sintesi catalitiche dell'ammoniaca, metanolo ed alcoli superiori.
DE8634177U1 (es) * 1986-12-20 1987-05-07 Uhde Gmbh, 4600 Dortmund, De
ES2030467T3 (es) * 1987-07-03 1992-11-01 Ammonia Casale S.A. Proceso mejorado para sintesis heterogenea y reactores relacionados.

Also Published As

Publication number Publication date
EP0297474B1 (en) 1992-04-01
ATE74291T1 (de) 1992-04-15
DE3869677D1 (de) 1992-05-07
US4963338A (en) 1990-10-16
CA1306846C (en) 1992-09-01
SU1671148A3 (ru) 1991-08-15
CN1030878A (zh) 1989-02-08
EP0297474A2 (en) 1989-01-04
EP0297474A3 (en) 1989-04-05
CN1014031B (zh) 1991-09-25

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