CA2156411A1 - Process and apparatus for absorbing hydrogen sulphide - Google Patents
Process and apparatus for absorbing hydrogen sulphideInfo
- Publication number
- CA2156411A1 CA2156411A1 CA002156411A CA2156411A CA2156411A1 CA 2156411 A1 CA2156411 A1 CA 2156411A1 CA 002156411 A CA002156411 A CA 002156411A CA 2156411 A CA2156411 A CA 2156411A CA 2156411 A1 CA2156411 A1 CA 2156411A1
- Authority
- CA
- Canada
- Prior art keywords
- gas
- stage
- solution
- stages
- carbonate
- 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.)
- Granted
Links
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 title abstract 3
- 238000000034 method Methods 0.000 title abstract 3
- 239000007789 gas Substances 0.000 abstract 7
- 239000000243 solution Substances 0.000 abstract 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 abstract 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract 3
- 239000007788 liquid Substances 0.000 abstract 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 abstract 2
- 238000010521 absorption reaction Methods 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 abstract 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 abstract 1
- 239000012670 alkaline solution Substances 0.000 abstract 1
- 239000001569 carbon dioxide Substances 0.000 abstract 1
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 230000008020 evaporation Effects 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 229910000029 sodium carbonate Inorganic materials 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
- B01D53/52—Hydrogen sulfide
-
- 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
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/06—Treatment of pulp gases; Recovery of the heat content of the gases; Treatment of gases arising from various sources in pulp and paper mills; Regeneration of gaseous SO2, e.g. arising from liquors containing sulfur compounds
- D21C11/08—Deodorisation ; Elimination of malodorous compounds, e.g. sulfur compounds such as hydrogen sulfide or mercaptans, from gas streams
-
- 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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
A process and an apparatus in black-liquor evaporation for the selective removal, by liquid absorption, of hydrogen sulphide from the generated gas (3) containing hydrogen sulphide as well as carbon dioxide, are disclosed. In the process, the gas is counter-currently brought into multistage contact, preferably comprising three stages (6, 7, 8), with circulating carbonate-containing alkaline solutions, preferably sodium carbonate solutions (25), the pH of which is adjusted during the absorption to about 9-12 by the addition of a hydroxide, preferably a sodium hydroxide solution (26, 27, 28). It is preferred that the gas flow is turbulent and the liquid flow is laminar when contacted with one another.
The apparatus comprises a container (1) having a gas inlet (2), a gas outlet (4), and a packing (9) arranged in several successive stages (6, 7, 8). The apparatus has means (25) for supplying a carbonate-containing solution to the last stage and through this stage countercurrently to the gas, and for recycling the solution across this stage; conduits (29, 30) arranged between the stages for supplying a partial flow of the solution from one stage to a preceding stage; means (26, 27, 28) for supplying a hydroxide to the carbonate-containing solution in at least one of the stages (6, 7, 8); and an outlet conduit (31) from the first stage, as seen in the feed direction of the gas, for discharging a sulphide-containing liquid.
The apparatus comprises a container (1) having a gas inlet (2), a gas outlet (4), and a packing (9) arranged in several successive stages (6, 7, 8). The apparatus has means (25) for supplying a carbonate-containing solution to the last stage and through this stage countercurrently to the gas, and for recycling the solution across this stage; conduits (29, 30) arranged between the stages for supplying a partial flow of the solution from one stage to a preceding stage; means (26, 27, 28) for supplying a hydroxide to the carbonate-containing solution in at least one of the stages (6, 7, 8); and an outlet conduit (31) from the first stage, as seen in the feed direction of the gas, for discharging a sulphide-containing liquid.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9300533A SE9300533L (en) | 1993-02-18 | 1993-02-18 | Methods and apparatus for the absorption of hydrogen sulphide |
SE9300533-8 | 1993-02-18 | ||
PCT/SE1994/000030 WO1994019091A1 (en) | 1993-02-18 | 1994-01-18 | Process and apparatus for absorbing hydrogen sulphide |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2156411A1 true CA2156411A1 (en) | 1994-09-01 |
CA2156411C CA2156411C (en) | 2004-05-11 |
Family
ID=20388935
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002156411A Expired - Fee Related CA2156411C (en) | 1993-02-18 | 1994-01-18 | Process and apparatus for absorbing hydrogen sulphide |
Country Status (11)
Country | Link |
---|---|
JP (1) | JPH08506993A (en) |
KR (1) | KR100286384B1 (en) |
CN (1) | CN1050527C (en) |
AU (1) | AU6158694A (en) |
BR (1) | BR9406271A (en) |
CA (1) | CA2156411C (en) |
FI (1) | FI114084B (en) |
PL (1) | PL180733B1 (en) |
RU (1) | RU2103050C1 (en) |
SE (1) | SE9300533L (en) |
WO (1) | WO1994019091A1 (en) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE501782C2 (en) * | 1993-09-17 | 1995-05-15 | Flaekt Ab | Method and apparatus for selectively removing hydrogen sulfide from a gas |
JPH09183618A (en) * | 1995-12-28 | 1997-07-15 | Kansai Electric Power Co Inc:The | Production of gypsum |
KR100347970B1 (en) * | 1999-08-11 | 2002-08-07 | 대경기계기술주식회사 | System for eliminating malodorous substance from malodorous gas |
KR100415917B1 (en) * | 2001-11-14 | 2004-01-24 | 주식회사 포스코 | Method for cleaning expanded metal packing in hydrogen sulfide collecting tank |
US7662215B2 (en) | 2004-07-12 | 2010-02-16 | Exxonmobil Upstream Research Company | Methods for removing sulfur-containing compounds |
US7727374B2 (en) * | 2004-09-23 | 2010-06-01 | Skyonic Corporation | Removing carbon dioxide from waste streams through co-generation of carbonate and/or bicarbonate minerals |
EP2030670A1 (en) * | 2007-08-31 | 2009-03-04 | Intega GmbH | Method and apparatus for removing at least one hydrogen chalcogen compound from an exhaust gas stream |
KR100943537B1 (en) | 2008-05-27 | 2010-02-22 | 주식회사 애니텍 | An Air Cleaner with Function Capable of CO2 Removal |
DE102009009476A1 (en) * | 2009-02-19 | 2010-08-26 | Linde-Kca-Dresden Gmbh | Process and apparatus for purifying a carbon dioxide-containing gas stream |
US8617494B2 (en) * | 2012-03-30 | 2013-12-31 | Alstom Technology Ltd | Condenser and method for cleaning flue gases |
CN105056709A (en) * | 2015-07-30 | 2015-11-18 | 江苏金曼科技有限责任公司 | Tail gas processing method |
CN105854549A (en) * | 2016-05-06 | 2016-08-17 | 铜仁学院 | Mercury-containing waste gas treatment method |
KR102325084B1 (en) * | 2019-10-04 | 2021-11-10 | 서정봉 | Composition for neutralizing acidic waste water or harmful gas having low freezing point |
CN111330413A (en) * | 2020-02-13 | 2020-06-26 | 东营联合石化有限责任公司 | Petroleum cracking gasification substance desulfurization device |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE319078B (en) * | 1968-06-07 | 1969-12-22 | British Columbia Res Council | |
SE448173B (en) * | 1985-06-03 | 1987-01-26 | Croon Inventor Ab | PROCEDURE FOR THE RECOVERY OF CELLULOSA DISPOSAL CHEMICALS BY PYROLYSIS |
SE9001957L (en) * | 1990-05-31 | 1991-12-01 | Chemrec Ab | Purification of process gas from partial combustion of black liquor |
US5284550A (en) * | 1992-06-18 | 1994-02-08 | Combustion Engineering, Inc. | Black liquier gasification process operating at low pressures using a circulating fluidized bed |
-
1993
- 1993-02-18 SE SE9300533A patent/SE9300533L/en not_active Application Discontinuation
-
1994
- 1994-01-18 RU RU95118712A patent/RU2103050C1/en not_active IP Right Cessation
- 1994-01-18 AU AU61586/94A patent/AU6158694A/en not_active Abandoned
- 1994-01-18 WO PCT/SE1994/000030 patent/WO1994019091A1/en active IP Right Grant
- 1994-01-18 PL PL94310320A patent/PL180733B1/en not_active IP Right Cessation
- 1994-01-18 BR BR9406271A patent/BR9406271A/en not_active IP Right Cessation
- 1994-01-18 JP JP6518871A patent/JPH08506993A/en active Pending
- 1994-01-18 CA CA002156411A patent/CA2156411C/en not_active Expired - Fee Related
- 1994-01-18 KR KR1019950703518A patent/KR100286384B1/en not_active IP Right Cessation
- 1994-01-18 CN CN94191218A patent/CN1050527C/en not_active Expired - Fee Related
-
1995
- 1995-08-17 FI FI953882A patent/FI114084B/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
KR960700799A (en) | 1996-02-24 |
FI953882A (en) | 1995-08-17 |
BR9406271A (en) | 1996-01-02 |
FI114084B (en) | 2004-08-13 |
JPH08506993A (en) | 1996-07-30 |
PL180733B1 (en) | 2001-03-30 |
CN1118146A (en) | 1996-03-06 |
AU6158694A (en) | 1994-09-14 |
CA2156411C (en) | 2004-05-11 |
KR100286384B1 (en) | 2001-04-16 |
SE9300533D0 (en) | 1993-02-18 |
FI953882A0 (en) | 1995-08-17 |
WO1994019091A1 (en) | 1994-09-01 |
SE9300533L (en) | 1994-08-19 |
PL310320A1 (en) | 1995-12-11 |
CN1050527C (en) | 2000-03-22 |
RU2103050C1 (en) | 1998-01-27 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |