EA200200516A1 - Method of producing sulfur trioxide, sulfuric acid and oleum from sulfur dioxide - Google Patents

Method of producing sulfur trioxide, sulfuric acid and oleum from sulfur dioxide

Info

Publication number
EA200200516A1
EA200200516A1 EA200200516A EA200200516A EA200200516A1 EA 200200516 A1 EA200200516 A1 EA 200200516A1 EA 200200516 A EA200200516 A EA 200200516A EA 200200516 A EA200200516 A EA 200200516A EA 200200516 A1 EA200200516 A1 EA 200200516A1
Authority
EA
Eurasian Patent Office
Prior art keywords
gas
sulfuric acid
conversion
oleum
heat
Prior art date
Application number
EA200200516A
Other languages
Russian (ru)
Inventor
Адам В. Менон
Original Assignee
Монсанто Компани
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 Монсанто Компани filed Critical Монсанто Компани
Publication of EA200200516A1 publication Critical patent/EA200200516A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00Sulfur; Compounds thereof
    • C01B17/48Sulfur dioxide; Sulfurous acid
    • C01B17/50Preparation of sulfur dioxide
    • C01B17/60Isolation of sulfur dioxide from gases
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B17/00Sulfur; Compounds thereof
    • C01B17/69Sulfur trioxide; Sulfuric acid
    • C01B17/74Preparation
    • C01B17/76Preparation by contact processes
    • C01B17/765Multi-stage SO3-conversion

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Treating Waste Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

Получают конверсионный исходный газ, содержащий первую часть обогащенного SOдесорбированного газа. Конверсионный газ, содержащий SOи остаточный SO, образуют пропусканием конверсионного исходного газа через множество последовательно размещенных каталитических слоев, причем множество включает, по меньшей мере, 2 и не более 4 каталитических слоев. Вторую часть обогащенного SOгаза вводят, по меньшей мере, в один каталитический слой, размещенный ниже по потоку относительно вышележащего каталитического слоя в указанном множестве слоев, для повышения концентрации SOв газе, подаваемом в слой, расположенный ниже по потоку. Настоящее изобретение относится также к способу получения серной кислоты и/или олеума из источника газа, содержащего SO. Конверсионный газ, содержащий SOи остаточный SO, образуют пропусканием обогащенного SOдесорбированного газа через множество последовательно размещенных каталитических слоев. Конверсионный газ объединяют с водяным паром с образованием кислотного газового продукта, содержащего: (а) серную кислоту, образованную реакцией в газовой фазе между SOиз конверсионного газа и водяным паром, вследствие чего генерируется теплота образования серной кислоты в газовой фазе; (b) SOи (с) SO. Тепловую энергию из теплоты образования серной кислоты в газовой фазе извлекают переносом теплоты от кислотного газового продукта в водяной пар или питающую воду в непрямом теплообменнике. Затем охлажденный кислотный газовый продукт контактируют с жидкой серной кислотой в зоне абсорбции SOс образованием дополнительного количества серной кислоты и/или олеума и обедненного SOгаза, содержащего SO.Международная заявка была опубликована вместе с Get conversion source gas containing the first part of the enriched SO desorbed gas. Conversion gas containing SO and residual SO is formed by passing a conversion source gas through a plurality of catalytic beds arranged in series, the manifold comprising at least 2 and no more than 4 catalytic beds. The second part of the enriched SOgas is introduced into at least one catalytic layer located downstream of the overlying catalytic layer in said plurality of layers to increase the concentration of SO in the gas fed to the layer located downstream. The present invention also relates to a method for producing sulfuric acid and / or oleum from a source of gas containing SO. Conversion gas containing SO and residual SO is formed by passing the enriched SO to the desorbed gas through a plurality of sequentially placed catalytic beds. Conversion gas is combined with steam to form an acidic gas product containing: (a) sulfuric acid formed by the reaction in the gas phase between SO of the conversion gas and water vapor, thereby generating the heat of formation of sulfuric acid in the gas phase; (b) SO and (c) SO. Heat energy from the heat of formation of sulfuric acid in the gas phase is extracted by transferring heat from the acid gas product to water vapor or feed water in an indirect heat exchanger. The cooled acid gas product is then contacted with liquid sulfuric acid in the SO absorption zone to form an additional amount of sulfuric acid and / or oleum and depleted SO gas containing SO. The international application was published together with

EA200200516A 1999-11-01 2000-11-01 Method of producing sulfur trioxide, sulfuric acid and oleum from sulfur dioxide EA200200516A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US16306199P 1999-11-01 1999-11-01
PCT/US2000/030095 WO2001036324A1 (en) 1999-11-01 2000-11-01 Method for making sulfur trioxide, sulfuric acid, and oleum from sulfur dioxide

Publications (1)

Publication Number Publication Date
EA200200516A1 true EA200200516A1 (en) 2002-10-31

Family

ID=22588320

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200200516A EA200200516A1 (en) 1999-11-01 2000-11-01 Method of producing sulfur trioxide, sulfuric acid and oleum from sulfur dioxide

Country Status (11)

Country Link
EP (1) EP1230150A1 (en)
JP (1) JP2003517419A (en)
KR (1) KR20020049001A (en)
CN (1) CN1384805A (en)
AU (1) AU1357301A (en)
BR (1) BR0015265A (en)
CA (1) CA2387988A1 (en)
EA (1) EA200200516A1 (en)
MX (1) MXPA02004408A (en)
WO (1) WO2001036324A1 (en)
ZA (1) ZA200202425B (en)

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WO2005106034A1 (en) * 2004-04-29 2005-11-10 Agency For Science, Technology And Research Method and device for detection of nucleic acids and/or polypeptides
DE102005008109A1 (en) * 2005-02-21 2006-08-24 Outokumpu Technology Oy Process and plant for the production of sulfuric acid
EP1918248A3 (en) * 2006-10-29 2010-06-09 Silicon Fire AG Provision of H2O2 from sulphuric acid which is produced from the sulphur residue during combustion of fossil fuels, and utilisation of H2O2 as an energy carrier
DE102007027841B4 (en) * 2007-06-13 2012-02-16 Outotec Oyj Method and apparatus for mixing gases
CN102741158B (en) * 2009-12-01 2015-10-21 拜尔技术服务有限责任公司 For the apparatus and method of burn sulphur and sulfur-containing compound
JOP20200123A1 (en) * 2010-01-20 2017-06-16 Mecs Inc Energy recovery in manufacture of sulfuric acid
WO2011147431A1 (en) 2010-05-27 2011-12-01 Haldor Topsoe A/S Process and apparatus for sulphuric acid production
WO2012096817A2 (en) * 2011-01-11 2012-07-19 Albemarle Corporation Process for producing sulfur dioxide and sulfur trioxide
CN102351156B (en) * 2011-07-28 2013-03-27 湖南科技大学 Sulfuric acid plant production device without discharge of tail gas and process method therefor
CN102530888B (en) * 2012-01-31 2013-11-27 刘立文 Method for preparing sulfuric acid by using sulfur dioxide
CN103058147B (en) * 2013-01-07 2015-08-12 刘立文 A kind of absorption unit and method utilizing gypsum production sulphur trioxide
CN103405997A (en) * 2013-07-29 2013-11-27 中国恩菲工程技术有限公司 Equipment for preparing sulfuric acid
CN103405998A (en) * 2013-07-29 2013-11-27 中国恩菲工程技术有限公司 Equipment and method for preparing sulfuric acid
WO2018015138A1 (en) * 2016-07-21 2018-01-25 Haldor Topsøe A/S Method for production of sulfuric acid from sulfur containing feeds with gas quenching
CN106512980B (en) * 2016-08-31 2018-11-13 上海奥威日化有限公司 The catalyst of sulfur trioxide is produced by oxidizing sulfur dioxide
CN106744714A (en) * 2016-11-18 2017-05-31 上海东化环境工程有限公司 A kind of technique that sulfur dioxide Sulphuric acid is reclaimed from flue gas
EP3691991A1 (en) * 2017-10-05 2020-08-12 Haldor Topsøe A/S A novel layout for inter-bed cooling in sulfuric acid plants
CN109603429B (en) * 2018-11-14 2021-03-05 惠州宇新新材料有限公司 Raw material air pretreatment method
CN111533092A (en) * 2020-05-09 2020-08-14 山东合生固废处置工程有限公司 Method for treating and recycling sulfur-phosphorus-containing organic waste
CN111747382B (en) * 2020-05-25 2022-04-15 惠州宇新化工有限责任公司 Method and system for concentrating and recycling dilute acid by using alkylation waste acid recycling device
CA3236228A1 (en) * 2021-10-28 2023-05-04 Marten Nils Rickard Granroth Production of sulfuric acid employing an o2 rich stream
WO2023234318A1 (en) * 2022-05-31 2023-12-07 日本管機工業株式会社 Sulfuric acid production apparatus, and sulfuric acid production method

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB475120A (en) * 1935-05-24 1937-11-15 Grasselli Chemical Co Improvements in or relating to the production of sulphuric acid
IT500174A (en) * 1951-02-09
US3475119A (en) * 1966-12-23 1969-10-28 Richard L Hummel Production of sulphuric acid
NO131417L (en) * 1970-05-01
BE792061A (en) * 1971-12-02 1973-05-29 Bayer Ag PRODUCTION OF SULFURIC ANHYDRIDE AND SULFURIC ACID
US5130112A (en) * 1990-03-23 1992-07-14 Monsanto Company Method for recovering high grade process energy from a contact sulfuric acid process
US5118490A (en) * 1989-06-21 1992-06-02 Monsanto Company Absorption of wet conversion gas
DK61892D0 (en) * 1992-05-12 1992-05-12 Haldor Topsoe As METHOD OF PRODUCING SULFURIC ACID

Also Published As

Publication number Publication date
BR0015265A (en) 2002-06-18
WO2001036324A1 (en) 2001-05-25
CN1384805A (en) 2002-12-11
ZA200202425B (en) 2003-09-23
MXPA02004408A (en) 2002-09-02
CA2387988A1 (en) 2001-05-25
AU1357301A (en) 2001-05-30
EP1230150A1 (en) 2002-08-14
KR20020049001A (en) 2002-06-24
JP2003517419A (en) 2003-05-27

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