MD1020C2 - Method for separating gaseous polluants from hot process gases - Google Patents
Method for separating gaseous polluants from hot process gasesInfo
- Publication number
- MD1020C2 MD1020C2 MD97-0166A MD970166A MD1020C2 MD 1020 C2 MD1020 C2 MD 1020C2 MD 970166 A MD970166 A MD 970166A MD 1020 C2 MD1020 C2 MD 1020C2
- Authority
- MD
- Moldova
- Prior art keywords
- polluants
- mixer
- process gases
- dust
- gaseous
- Prior art date
Links
- 239000007789 gas Substances 0.000 title abstract 5
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 abstract 8
- 239000000428 dust Substances 0.000 abstract 5
- 230000002745 absorbent Effects 0.000 abstract 4
- 239000002250 absorbent Substances 0.000 abstract 4
- 239000000292 calcium oxide Substances 0.000 abstract 4
- 235000012255 calcium oxide Nutrition 0.000 abstract 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 abstract 2
- 239000000920 calcium hydroxide Substances 0.000 abstract 2
- 235000011116 calcium hydroxide Nutrition 0.000 abstract 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 abstract 2
- 239000000463 material Substances 0.000 abstract 2
- 239000003546 flue gas Substances 0.000 abstract 1
- 235000010269 sulphur dioxide Nutrition 0.000 abstract 1
- 239000004291 sulphur dioxide Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- 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
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/508—Sulfur oxides by treating the gases with solids
-
- 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
- B01D53/81—Solid phase processes
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The invention relates to the method for separating gaseous polluants, such as sulphur dioxide, from hot process gases, such as flue gases, where the hot gases are passing through a contact reactor, in which is introduced the moistened absorbent material, which is reactive with gaseous polluants, to convert the gaseous polluants into separable dust, the process gases are then passing through a dust separator. The major part of the dust separated in the dust separator is passing to a mixer, in which it is mixed and moistened with a fresh absorbent, whereupon it is recirculated as absorbent material by being introduced. Into the process gases burnt lime is added as fresh absorbent. The dust is kept so long in the mixer and recirculated so many times that the total residence time of the burnt lime in the mixer in moistened state is sufficiently long for the burnt lime to react substantially completely with water supplied to the mixer and form slaked lime.The technical result of the invention consists in reducing the price of method by means of application of the slaked lime instead of the burnt lime.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE9404105A SE504440C2 (en) | 1994-11-28 | 1994-11-28 | Ways to separate gaseous pollutants from hot process gases |
| PCT/SE1995/001403 WO1996016722A1 (en) | 1994-11-28 | 1995-11-24 | Method for separating gaseous pollutants from hot process gases |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MD1020C2 true MD1020C2 (en) | 1999-07-31 |
Family
ID=20396125
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MD97-0166A MD1020C2 (en) | 1994-11-28 | 1995-11-24 | Method for separating gaseous polluants from hot process gases |
Country Status (20)
| Country | Link |
|---|---|
| EP (1) | EP0804273A1 (en) |
| JP (1) | JP3640674B2 (en) |
| KR (1) | KR100384589B1 (en) |
| CN (1) | CN1080137C (en) |
| AU (1) | AU692014B2 (en) |
| BR (1) | BR9509831A (en) |
| CZ (1) | CZ157497A3 (en) |
| EE (1) | EE04049B1 (en) |
| FI (1) | FI972233A7 (en) |
| HU (1) | HU220402B (en) |
| MD (1) | MD1020C2 (en) |
| PL (1) | PL320426A1 (en) |
| RO (1) | RO115421B1 (en) |
| RU (1) | RU2147919C1 (en) |
| SE (1) | SE504440C2 (en) |
| SI (1) | SI9520141A (en) |
| SK (1) | SK66197A3 (en) |
| UA (1) | UA52592C2 (en) |
| WO (1) | WO1996016722A1 (en) |
| ZA (1) | ZA959876B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2286836C1 (en) * | 2005-04-11 | 2006-11-10 | Константин Владимирович Зелинский | Method of removing sulfur dioxide from gas |
Families Citing this family (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT404565B (en) * | 1997-06-05 | 1998-12-28 | Scheuch Alois Gmbh | METHOD FOR PURIFYING POLLUTANT-GASES |
| JP3395036B2 (en) | 1997-10-06 | 2003-04-07 | 日立造船株式会社 | Method and apparatus for removing acid gas from exhaust gas |
| JP3395035B2 (en) | 1997-10-06 | 2003-04-07 | 日立造船株式会社 | Method and apparatus for removing acid gas from exhaust gas |
| SE514592C2 (en) * | 1998-05-18 | 2001-03-19 | Flaekt Ab | Method and apparatus for flue gas purification with extinguishing lime in immediate connection with flue gas purification |
| SE512227C2 (en) * | 1998-06-24 | 2000-02-14 | Flaekt Ab | Ways to clean flue gases during the start-up of a boiler |
| US6290921B1 (en) | 1999-11-03 | 2001-09-18 | Foster Wheeler Enegeria Oy | Method and apparatus for binding pollutants in flue gas |
| SE523667C2 (en) * | 2002-09-20 | 2004-05-11 | Alstom Switzerland Ltd | Method and apparatus for separating gaseous pollutants from hot gases by particulate absorbent material and mixer for wetting the absorbent material |
| DE602006002103D1 (en) * | 2006-02-06 | 2008-09-18 | Alstom Technology Ltd | Method and device for controlling the absorption of gaseous impurities from hot process gases |
| DE602006020030D1 (en) | 2006-07-04 | 2011-03-24 | Alstom Technology Ltd | Method and device for separating gaseous pollutants from hot exhaust gases |
| AT504426B8 (en) * | 2006-10-24 | 2008-09-15 | Scheuch Gmbh | APPARATUS FOR MOISTURIZING A SORPTION AGENT |
| US7766997B2 (en) | 2007-12-21 | 2010-08-03 | Alstom Technology Ltd | Method of reducing an amount of mercury in a flue gas |
| US7850936B2 (en) | 2008-02-18 | 2010-12-14 | Alstom Technology Ltd | Dry sulfur dioxide (SO2) scrubbing |
| CN101513589B (en) * | 2009-03-03 | 2011-07-20 | 桑德环境资源股份有限公司 | Method and device for purification of flue gases by semidry process |
| US8192529B2 (en) * | 2009-03-10 | 2012-06-05 | Gatton Jr Lawrence H | Integrated dry scrubber system |
| ES2593812T3 (en) | 2010-11-24 | 2016-12-13 | General Electric Technology Gmbh | Method of purifying a combustion gas rich in carbon dioxide and a boiler system |
| US8728211B2 (en) | 2012-03-30 | 2014-05-20 | Alstom Technology Ltd | Nozzle for spraying liquid and a mixer comprising the nozzle |
| US9457366B2 (en) * | 2012-07-13 | 2016-10-04 | General Electric Technology Gmbh | Spray lance arrangement |
| US8663586B1 (en) | 2012-08-07 | 2014-03-04 | Alstom Technology Ltd | High performance mercury capture |
| US9108152B2 (en) * | 2013-11-26 | 2015-08-18 | Alstom Technology Ltd | Dry scrubber system with low load distributor device |
| US8906333B1 (en) * | 2013-11-27 | 2014-12-09 | Alstom Technology Ltd | Dry scrubber system with air preheater protection |
| CN105617851B (en) * | 2016-03-16 | 2018-08-28 | 中国科学院城市环境研究所 | A kind of method and its device of efficient double tower semi-dry desulphurization |
| CN111032192A (en) * | 2017-09-06 | 2020-04-17 | 勒瓦研究开发股份有限公司 | Method for treating flue gas in CDS flue gas treatment |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3308927A1 (en) | 1983-03-12 | 1984-09-13 | L. & C. Steinmüller GmbH, 5270 Gummersbach | Process for binding gaseous pollutants contained in flue gases |
| FI78401B (en) * | 1985-04-24 | 1989-04-28 | Tampella Oy Ab | FOERFARANDE OCH ANORDNING FOER ATT BRINGA ROEKGASERNAS GASFORMIGA SVAVELFOERENINGAR SAOSOM SVAVELDIOXID ATT REAGERA TILL FASTA FOERENINGAR SOM SEPARERAS FRAON ROEKGASERNA. |
| SE453570B (en) * | 1985-10-09 | 1988-02-15 | Flaekt Ab | Plant for sepg. acid components from gas mixt. |
| SE458095B (en) * | 1986-06-27 | 1989-02-27 | Flaekt Ab | Sepn. system for pollutants from gas-form medium |
| FI76931B (en) * | 1986-12-12 | 1988-09-30 | Imatran Voima Oy | FOERFARANDE FOER RENING AV ROEKGASER. |
| JP3035015B2 (en) * | 1991-08-13 | 2000-04-17 | 三菱重工業株式会社 | Desulfurization method |
-
1994
- 1994-11-28 SE SE9404105A patent/SE504440C2/en not_active IP Right Cessation
-
1995
- 1995-11-21 ZA ZA959876A patent/ZA959876B/en unknown
- 1995-11-24 EP EP95939455A patent/EP0804273A1/en not_active Withdrawn
- 1995-11-24 SI SI9520141A patent/SI9520141A/en not_active IP Right Cessation
- 1995-11-24 SK SK661-97A patent/SK66197A3/en unknown
- 1995-11-24 BR BR9509831A patent/BR9509831A/en not_active IP Right Cessation
- 1995-11-24 KR KR1019970703389A patent/KR100384589B1/en not_active Expired - Fee Related
- 1995-11-24 AU AU41264/96A patent/AU692014B2/en not_active Ceased
- 1995-11-24 HU HU9800501A patent/HU220402B/en not_active IP Right Cessation
- 1995-11-24 UA UA97063196A patent/UA52592C2/en unknown
- 1995-11-24 JP JP51717096A patent/JP3640674B2/en not_active Expired - Lifetime
- 1995-11-24 MD MD97-0166A patent/MD1020C2/en unknown
- 1995-11-24 PL PL95320426A patent/PL320426A1/en unknown
- 1995-11-24 EE EE9700215A patent/EE04049B1/en not_active IP Right Cessation
- 1995-11-24 RU RU97111848A patent/RU2147919C1/en not_active IP Right Cessation
- 1995-11-24 CN CN95196504A patent/CN1080137C/en not_active Expired - Lifetime
- 1995-11-24 CZ CZ971574A patent/CZ157497A3/en unknown
- 1995-11-24 RO RO97-00951A patent/RO115421B1/en unknown
- 1995-11-24 WO PCT/SE1995/001403 patent/WO1996016722A1/en active IP Right Grant
-
1997
- 1997-05-27 FI FI972233A patent/FI972233A7/en not_active IP Right Cessation
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2286836C1 (en) * | 2005-04-11 | 2006-11-10 | Константин Владимирович Зелинский | Method of removing sulfur dioxide from gas |
Also Published As
| Publication number | Publication date |
|---|---|
| SE9404105D0 (en) | 1994-11-28 |
| EE04049B1 (en) | 2003-06-16 |
| HU220402B (en) | 2002-01-28 |
| CN1080137C (en) | 2002-03-06 |
| SE504440C2 (en) | 1997-02-10 |
| RU2147919C1 (en) | 2000-04-27 |
| SK66197A3 (en) | 1997-10-08 |
| JP3640674B2 (en) | 2005-04-20 |
| UA52592C2 (en) | 2003-01-15 |
| HUT77637A (en) | 1998-06-29 |
| JPH10509914A (en) | 1998-09-29 |
| PL320426A1 (en) | 1997-09-29 |
| BR9509831A (en) | 1997-09-30 |
| KR100384589B1 (en) | 2003-08-21 |
| ZA959876B (en) | 1996-07-15 |
| RO115421B1 (en) | 2000-02-28 |
| FI972233A0 (en) | 1997-05-27 |
| CZ157497A3 (en) | 1997-11-12 |
| FI972233A7 (en) | 1997-05-27 |
| SI9520141A (en) | 1997-10-31 |
| CN1167450A (en) | 1997-12-10 |
| SE9404105L (en) | 1996-05-29 |
| EE9700215A (en) | 1998-02-16 |
| AU4126496A (en) | 1996-06-19 |
| EP0804273A1 (en) | 1997-11-05 |
| WO1996016722A1 (en) | 1996-06-06 |
| AU692014B2 (en) | 1998-05-28 |
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