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 dioxideInfo
- 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
Links
Classifications
-
- 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
- C01B17/48—Sulfur dioxide; Sulfurous acid
- C01B17/50—Preparation of sulfur dioxide
- C01B17/60—Isolation of sulfur dioxide from gases
-
- 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
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
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) |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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)
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 |
-
2000
- 2000-11-01 JP JP2001538282A patent/JP2003517419A/en active Pending
- 2000-11-01 WO PCT/US2000/030095 patent/WO2001036324A1/en not_active Application Discontinuation
- 2000-11-01 EP EP00975531A patent/EP1230150A1/en not_active Withdrawn
- 2000-11-01 CN CN00815111A patent/CN1384805A/en active Pending
- 2000-11-01 MX MXPA02004408A patent/MXPA02004408A/en unknown
- 2000-11-01 CA CA002387988A patent/CA2387988A1/en not_active Abandoned
- 2000-11-01 BR BR0015265-0A patent/BR0015265A/en not_active Application Discontinuation
- 2000-11-01 AU AU13573/01A patent/AU1357301A/en not_active Abandoned
- 2000-11-01 EA EA200200516A patent/EA200200516A1/en unknown
- 2000-11-01 KR KR1020027005602A patent/KR20020049001A/en not_active Application Discontinuation
-
2002
- 2002-03-26 ZA ZA200202425A patent/ZA200202425B/en unknown
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EA200200516A1 (en) | Method of producing sulfur trioxide, sulfuric acid and oleum from sulfur dioxide | |
RU2394813C2 (en) | Method of producing urea from ammonia and carbon dioxide | |
JPH01180841A (en) | Production of methanol | |
RU2196767C2 (en) | Method of combined production of ammonia and carbamide, plant for method embodiment, method of modernization of ammonia and carbamide synthesis plants | |
SK280897B6 (en) | Process for the removal of sulphur dioxide from waste gases | |
WO2020233030A1 (en) | Device and method for synergistic recover of sulfur and hydrogen resources from hydrogen sulfide acid gas | |
WO2013108191A9 (en) | A method of forming urea by integration of an ammonia production process in a urea production process and a system therefor | |
US3825657A (en) | Process for the cracking of sulfuric acid | |
JP2005507844A5 (en) | ||
US4186181A (en) | Process for the production of hydrogen | |
JPS6126481B2 (en) | ||
JPS62167207A (en) | Manufacture of concentrated sulfuric acid and sulfur trioxide absorbing equipment therefor | |
US3880983A (en) | Flue gas desulfurization with ammonium sulfite-bisulfite solution | |
YU49456B (en) | A process for the continuous preparation of aqueous formaldehyde solutions | |
RU2531181C2 (en) | Method of oxidising spent alkali under higher pressure | |
JPH04228406A (en) | Manufacture of oleum and sulfuric acid | |
RU2045471C1 (en) | Method and apparatus for obtaining hydroxilamine sulfate | |
KR20000023700A (en) | Process of producing sulfuric acid | |
AU2010280931B2 (en) | Method and installation for producing sulphuric acid | |
JP2001039911A (en) | Production of methanol | |
SU793931A1 (en) | Method of obtaining elementary sulphur from gases | |
RU2151736C1 (en) | Nitric acid production process | |
SU614098A1 (en) | Method of obtaining urea | |
JPH0397613A (en) | Method for recovering gaseous carbon dioxide from waste combustion gas of cogeneration equipment | |
RU2127224C1 (en) | Method of producing nitric acid |