BRPI0718270A8 - Processo e dispositivo para oxidação catalítica de gases que contêm so2 por meio de oxigênio. - Google Patents

Processo e dispositivo para oxidação catalítica de gases que contêm so2 por meio de oxigênio.

Info

Publication number
BRPI0718270A8
BRPI0718270A8 BRPI0718270A BRPI0718270A BRPI0718270A8 BR PI0718270 A8 BRPI0718270 A8 BR PI0718270A8 BR PI0718270 A BRPI0718270 A BR PI0718270A BR PI0718270 A BRPI0718270 A BR PI0718270A BR PI0718270 A8 BRPI0718270 A8 BR PI0718270A8
Authority
BR
Brazil
Prior art keywords
catalytic oxidation
oxygen
catalyst
partial
continuous
Prior art date
Application number
BRPI0718270A
Other languages
English (en)
Inventor
Kürten Martin
Haverkamp Verena
Erkes Bernd
Original Assignee
Bayer Technology Services Gmbh
Bayer Ip Gmbh
Bayer Ag
Chemetics Inc
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 Bayer Technology Services Gmbh, Bayer Ip Gmbh, Bayer Ag, Chemetics Inc filed Critical Bayer Technology Services Gmbh
Publication of BRPI0718270A2 publication Critical patent/BRPI0718270A2/pt
Publication of BRPI0718270A8 publication Critical patent/BRPI0718270A8/pt
Publication of BRPI0718270B1 publication Critical patent/BRPI0718270B1/pt

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    • 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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00—Sulfur; Compounds thereof
    • C01B17/69—Sulfur trioxide; Sulfuric acid
    • C01B17/74—Preparation
    • C01B17/76—Preparation by contact processes
    • C01B17/765—Multi-stage SO3-conversion
    • C01B17/7655—Multi-stage SO3-conversion with intermediate absorption
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75—Multi-step processes
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8603—Removing sulfur compounds
    • B01D53/8609—Sulfur oxides
    • 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
    • B01J8/0476—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 otherwise shaped beds
    • B01J8/048—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 otherwise 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
    • B01J8/0476—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 otherwise shaped beds
    • B01J8/0488—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 otherwise shaped beds the beds being placed in separate 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
    • B01J8/0496—Heating or cooling the reactor
    • 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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00—Sulfur; Compounds thereof
    • C01B17/69—Sulfur trioxide; Sulfuric acid
    • C01B17/74—Preparation
    • C01B17/76—Preparation by contact processes
    • C01B17/765—Multi-stage SO3-conversion
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00—Sulfur; Compounds thereof
    • C01B17/69—Sulfur trioxide; Sulfuric acid
    • C01B17/74—Preparation
    • C01B17/76—Preparation by contact processes
    • C01B17/78—Preparation by contact processes characterised by the catalyst used
    • C01B17/79—Preparation by contact processes characterised by the catalyst used containing vanadium
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00—Sulfur; Compounds thereof
    • C01B17/69—Sulfur trioxide; Sulfuric acid
    • C01B17/74—Preparation
    • C01B17/76—Preparation by contact processes
    • C01B17/80—Apparatus
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00—Sulfur; Compounds thereof
    • C01B17/69—Sulfur trioxide; Sulfuric acid
    • C01B17/74—Preparation
    • C01B17/76—Preparation by contact processes
    • C01B17/80—Apparatus
    • C01B17/803—Converters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2255/00—Catalysts
    • B01D2255/20—Metals or compounds thereof
    • B01D2255/207—Transition metals
    • B01D2255/20723—Vanadium
    • 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
    • B01J2208/00176—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles outside the reactor
    • 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
    • B01J2208/00203—Coils
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Epoxy Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PROCESSO E DISPOSITIVO PARA A OXIDAÇÃO CATALÍTICA DE GASES QUE CONTÊM 502 POR MEIO DE OXIGÊNIO. A presente invenção refere-se a um processo para a oxidação catalítica contínua, completa ou parcial, de um gás básico, que contém O,1 a 66% em volume de dióxido de enxofre, além de oxigênio, sendo que o catalisador é mantido ativo com uma condução de processo pseudoisotérmica, sob introdução ou remoção de energia. Além disso, a presente invenção refere-se a um dispositivo pra a oxidação catalítica continua, completa ou parcial, de um gás básico, que contém dióxido de enxofre e oxigênio, caracterizado por pelo menos um aparelho de contato de tubos, que é um trocador de calor em posição vertical, de pelo menos um tubo de paredes duplas, cujo tubo interno, enchido com catalisador, forma um tubo de reação, sendo que calor em torno do tubo de reação é transferido em corrente contínua e um absorvedor para separação de S03 é ligado a jusante do aparelho de contato de tubos. O catalisador está ajustado previamente em sua reatividade por mistura com material inerte. O dispositivo de acordo com a invenção é particularmente apropriado para realização do processo de acordo com a invenção.
BRPI0718270-8A 2006-10-31 2007-10-13 Processo e dispositivo para oxidação catalítica de gases que contêm so2 por meio de oxigênio. BRPI0718270B1 (pt)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102006051899.3 2006-10-31
DE102006051899A DE102006051899A1 (de) 2006-10-31 2006-10-31 Verfahren und Vorrichtung zur katalytischen Oxidation von SO2-haltigen Gasen mit Sauerstoff
PCT/EP2007/008910 WO2008052649A1 (de) 2006-10-31 2007-10-13 Verfahren und vorrichtung zur katalytischen oxidation von so2-haltigen gasen mit sauerstoff

Publications (3)

Publication Number Publication Date
BRPI0718270A2 BRPI0718270A2 (pt) 2013-11-12
BRPI0718270A8 true BRPI0718270A8 (pt) 2017-02-21
BRPI0718270B1 BRPI0718270B1 (pt) 2018-05-02

Family

ID=38984433

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0718270-8A BRPI0718270B1 (pt) 2006-10-31 2007-10-13 Processo e dispositivo para oxidação catalítica de gases que contêm so2 por meio de oxigênio.

Country Status (25)

Country Link
US (1) US7871593B2 (pt)
EP (2) EP2256085B1 (pt)
JP (2) JP5570216B2 (pt)
KR (1) KR101420127B1 (pt)
CN (1) CN101573291B (pt)
AT (1) ATE503721T1 (pt)
AU (1) AU2007315318B2 (pt)
BR (1) BRPI0718270B1 (pt)
CA (1) CA2668059C (pt)
CL (1) CL2007003153A1 (pt)
CY (2) CY1112064T1 (pt)
DE (2) DE102006051899A1 (pt)
DK (2) DK2256085T3 (pt)
ES (2) ES2361951T3 (pt)
MA (1) MA30915B1 (pt)
MX (1) MX2009004483A (pt)
NO (1) NO342026B1 (pt)
PL (2) PL2256085T3 (pt)
PT (2) PT2256085E (pt)
RU (2) RU2456232C2 (pt)
SI (2) SI2256085T1 (pt)
TN (1) TN2009000150A1 (pt)
UA (2) UA97381C2 (pt)
WO (1) WO2008052649A1 (pt)
ZA (1) ZA200902892B (pt)

Families Citing this family (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009025510A1 (de) 2008-12-20 2010-06-24 Bayer Technology Services Gmbh Verfahren zur Herstellung von Schwefeltrioxid
DE102010018172A1 (de) 2010-04-22 2011-10-27 Bayer Technology Services Gmbh Verfahren zur Aufarbeitung schwefelwasserstoffhaltiger Abgase
PL2507165T3 (pl) 2009-12-01 2017-10-31 Chemetics Inc Sposób obróbki związków siarki
SI2330075T1 (sl) * 2009-12-01 2015-12-31 Bayer Intellectual Property Gmbh Postopek izdelave žveplove kisline
EP2507164B1 (de) 2009-12-01 2017-10-18 Chemetics, Inc. Verfahren zur herstellung von schwefelsäure
EP2694177B1 (en) * 2011-04-06 2016-10-05 Haldor Topsøe A/S Process for production of sulphuric acid
US8790611B2 (en) * 2012-07-05 2014-07-29 Basf Se Reactor for carrying out an exothermic reaction in the gas phase
RU2502546C1 (ru) * 2012-07-20 2013-12-27 Андрей Владиславович Курочкин Способ очистки углеводородных газов
AT513414B1 (de) * 2012-10-08 2014-06-15 Kanzler Walter Verfahren zur zweistufigen katalytischen Oxidation von Schwefel-Verbindungen in Abgasen
US20150315022A1 (en) * 2012-12-17 2015-11-05 Chemetics Inc. Contact apparatus for oxidizing sulfur dioxide and systems for producing sulfuric acid
US9994451B2 (en) 2014-06-09 2018-06-12 Chemetics Inc. Single contact, single absorption system for producing sulfuric acid with high conversion efficiency
DE102014108272A1 (de) * 2014-06-12 2015-12-17 Basf Se Anlage und Verfahren zur Durchführung von heterogen katalysierten Gasphasen-Reaktionen
CN104084094A (zh) * 2014-07-17 2014-10-08 科洋环境工程（上海）有限公司 一种转化so2浓度的装置及so2转化系统及转化方法
LU92547B1 (de) * 2014-09-17 2016-03-18 Cppe Carbon Process & Plant Engineering S A Verfahren zur katalytischen entfernung von schwefeldioxid aus abgasen
US9958211B2 (en) 2015-03-12 2018-05-01 Bayotech, Inc. Nested-flow heat exchangers and chemical reactors
EP3075434A1 (de) 2015-04-02 2016-10-05 Bayer Technology Services GmbH Kontinuierliches verfahren zur reinigung von so2-haltigen gasen
EA034697B1 (ru) * 2015-07-02 2020-03-10 Хальдор Топсёэ А/С Способ производства серной кислоты
DE102016103976A1 (de) * 2016-03-04 2017-09-07 Thyssenkrupp Ag Verfahren und Vorrichtung zur Herstellung von Schwefelsäure
LU93014B1 (en) 2016-04-04 2017-10-05 Ajo Ind S A R L Catalyst mixture for the treatment of waste gas
LU93013B1 (en) 2016-04-04 2017-11-08 Cppe Carbon Process & Plant Eng S A En Abrege Cppe S A Process for the removal of heavy metals from fluids
LU93012B1 (en) * 2016-04-04 2017-11-08 Cppe Carbon Process & Plant Eng S A En Abrege Cppe S A Sulfur dioxide removal from waste gas
CN105967150A (zh) * 2016-07-08 2016-09-28 华能国际电力股份有限公司 一种铂催化剂制取so3气体的设备及方法
JP6747167B2 (ja) * 2016-08-18 2020-08-26 住友金属鉱山株式会社 硫酸製造システム
CN107973278A (zh) * 2016-10-25 2018-05-01 中国石油化工股份有限公司 一种连续产生so3气体的方法
CN106915731B (zh) * 2017-04-14 2023-08-08 双盾环境科技有限公司 一种可调式应用惰性触媒处理高浓度so2烟气生产so3气体的装置
CN107020053A (zh) * 2017-04-18 2017-08-08 北京清新环境技术股份有限公司 一种产生三氧化硫并维持其气体状态的系统及其方法
FR3070016B1 (fr) * 2017-08-10 2019-08-23 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procede et installation de purification d'un flux gazeux d'alimentation comprenant au moins 90% de co2
CN107537316A (zh) * 2017-09-19 2018-01-05 中国大唐集团科学技术研究院有限公司华中分公司 烟道脱硫系统及方法、烟气催化反应装置
CN111164046B (zh) * 2017-10-05 2023-06-06 托普索公司 用于硫酸设备中的床间冷却的新型布局
CN108046220A (zh) * 2018-01-16 2018-05-18 山东润银生物化工股份有限公司 一种用合成气脱硫所得h2s生产浓硫酸的装置以及生产方法
CN110606795A (zh) * 2018-06-15 2019-12-24 孔繁昇 一种利用含硫燃料燃烧烟气制备有机磺酸的方法
CN110615407B (zh) * 2018-06-19 2023-07-07 盐城市恒星石油化学有限公司 一种基础油磺化用三氧化硫的转化工艺
CN110615408B (zh) * 2018-06-19 2023-08-04 盐城市恒星石油化学有限公司 一种白油生产用三氧化硫转化工艺
WO2021089217A1 (en) * 2019-11-04 2021-05-14 Outotec (Finland) Oy Process and plant for producing sulphuric acid
ES3053808T3 (en) 2019-12-13 2026-01-26 Chemetics Inc Integrated ammonia and sulfuric acid production plant and process
EP4211073B1 (en) 2020-09-09 2024-10-30 Chemetics Inc. System and method for producing sulfur dioxide and associated sulfuric acid plant
CA3238318A1 (en) 2021-12-03 2023-06-08 Rene Dijkstra Systems and methods for producing sulfuric acid or liquefied sulfur dioxide
US12264066B2 (en) 2022-04-25 2025-04-01 Messer Industries Usa, Inc. Process and apparatus for acid regeneration
US12607352B2 (en) 2023-04-20 2026-04-21 Messer Industries Usa, Inc. Process and burner apparatus for acid regeneration
US20240351879A1 (en) * 2023-04-20 2024-10-24 Messer Industries Usa, Inc. Process and apparatus for preparing sulfur trioxide from sulfur dioxide
US12600627B2 (en) 2023-04-20 2026-04-14 Messer Industries Usa, Inc. Process and apparatus for oxygen injection in a sulfur furnace
US12577103B2 (en) 2023-04-20 2026-03-17 Messer Industries Usa, Inc. Process and redox furnace for acid regeneration
WO2025170980A1 (en) 2024-02-06 2025-08-14 Chemetics Inc. Method for producing concentrated oleum or sulfur trioxide

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2026816A1 (de) 1970-06-02 1971-12-16 Farbwerke Hoechst AG, vorm Meister Lucius & Brumng, 6000 Frankfurt Verfahren zur Herstellung von Faden aus Poly beta amiden
DE2307973A1 (de) * 1973-02-17 1974-08-29 Metallgesellschaft Ag Verfahren zur katalytischen umsetzung von so tief 2 zu so tief 3
DE2418216C2 (de) * 1974-04-13 1983-02-17 Hoechst Ag, 6000 Frankfurt Verfahren zur Herstellung von Schwefeltrioxyd aus Schwefeldioxyd und Sauerstoff
DE2711897C3 (de) * 1977-03-18 1980-01-10 Davy International Ag, 6000 Frankfurt Verfahren und Vorrichtung zur katalytischen Oxidation von gasförmigen Schwefelverbindungen zu Schwefeltrioxid
SU1011229A1 (ru) * 1982-01-27 1983-04-15 Государственный Ордена Трудового Красного Знамени Научно-Исследовательский Институт Цветных Металлов Контактный аппарат дл окислени двуокиси серы
DK167242B1 (da) * 1989-02-16 1993-09-27 Topsoe Haldor As Apparat og fremgangsmaade til exoterme reaktioner
DE4217317A1 (de) * 1992-05-26 1993-12-02 Metallgesellschaft Ag Kontaktkessel zur quasi-isothermen katalytischen Umsetzung von SO¶2¶ zu SO¶3¶ und Verfahren zum Betreiben desselben
BG61107B1 (bg) * 1994-08-29 1996-11-29 Институт По Инженерна Химия При Бан Метод за получаване на серен триокис
DE4443774A1 (de) * 1994-12-08 1996-06-13 Basf Ag Vorrichtung und Verfahren zur Durchführung exothermer Reaktionen
DE10249782A1 (de) * 2002-10-24 2004-05-06 Outokumpu Oyj Verfahren und Anlage zur Herstellung von Schwefelsäure aus schwefeldioxidreichen Gasen
US20090258259A1 (en) * 2008-04-14 2009-10-15 Michael Leshchiner Catalytic heat exchangers and methods of operation

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AU2007315318A1 (en) 2008-05-08
CA2668059A1 (en) 2008-05-08
PL2256085T3 (pl) 2013-01-31
PL1979270T3 (pl) 2011-09-30
MX2009004483A (es) 2009-05-20
EP1979270B1 (de) 2011-03-30
DE102006051899A1 (de) 2008-05-15
WO2008052649A8 (de) 2009-05-22
PT2256085E (pt) 2012-11-06
CN101573291B (zh) 2014-04-23
EP1979270A1 (de) 2008-10-15
MA30915B1 (fr) 2009-11-02
RU2009120402A (ru) 2010-12-10
US20100092374A1 (en) 2010-04-15
ATE503721T1 (de) 2011-04-15
WO2008052649A1 (de) 2008-05-08
EP2256085A2 (de) 2010-12-01
US7871593B2 (en) 2011-01-18
ES2394635T3 (es) 2013-02-04
CN101573291A (zh) 2009-11-04
SI1979270T1 (sl) 2011-07-29
BRPI0718270A2 (pt) 2013-11-12
NO20091768L (no) 2009-05-29
DK2256085T3 (da) 2012-12-17
JP5570216B2 (ja) 2014-08-13
RU2012109567A (ru) 2013-09-20
UA97381C2 (ru) 2012-02-10
JP2010508222A (ja) 2010-03-18
AU2007315318B2 (en) 2013-05-30
CL2007003153A1 (es) 2008-05-23
RU2456232C2 (ru) 2012-07-20
DE502007006834D1 (de) 2011-05-12
PT1979270E (pt) 2011-06-01
JP2014240347A (ja) 2014-12-25
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BRPI0718270B1 (pt) 2018-05-02
UA111809C2 (uk) 2016-06-24
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DK1979270T3 (da) 2011-07-25
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CA2668059C (en) 2016-07-12

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