WO1986004260A1 - Process for scrubbing raw gases laden with sulphur oxides and nitrogen oxides - Google Patents
Process for scrubbing raw gases laden with sulphur oxides and nitrogen oxides Download PDFInfo
- Publication number
- WO1986004260A1 WO1986004260A1 PCT/EP1986/000027 EP8600027W WO8604260A1 WO 1986004260 A1 WO1986004260 A1 WO 1986004260A1 EP 8600027 W EP8600027 W EP 8600027W WO 8604260 A1 WO8604260 A1 WO 8604260A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- washing
- redox potential
- washing liquid
- stage
- iron
- Prior art date
Links
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
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen oxides
-
- 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
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Definitions
- the invention relates to a process for the purification of raw gases loaded with sulfur and nitrogen oxides, in which the raw gases contain at least one washing step in at least one washing step with an absorbent for the sulfur oxides as well as metal complex compounds, in particular iron-II complex compounds, for the absorption of the nitrogen oxides Is brought into contact.
- So-called wet processes have become known for cleaning raw gases loaded with sulfur and nitrogen oxides, in which the raw gases have been brought into contact with scrubbing liquids which are enriched with appropriate absorbents for the pollutants.
- Soluble alkali or alkaline earth compounds are particularly suitable for absorbing the SO.
- CaSO calcium sulfite
- Ca (HSO ⁇ ) calcium hydrogen sulfite
- gypsum stable end product
- the object of the invention is to develop a method of the type mentioned at the outset which, with constant high efficiency, enables economical separation of sulfur and nitrogen oxides from raw gases.
- This object is achieved in that the redox potential of the washing liquid is set negatively.
- complex compounds which contain carboxylic acid groups or their alkali metal or alkaline earth metal salts in the complex-forming anions, in particular those complexes in which aminocarboxylic acids or their salts are present.
- An essential representative of such chelate complexes is from ethylene - Diaminotetraacetic acid (EDTA) or its alkali or alkaline earth salts.
- Examples include: ethylene diamine, diethylene triamine, triethylene tetra in, tetraethylene pentamine and higher polyethylene amines; also 1,2-diamines such as propylenediamine, dipropylenetria in etc., and 1,2-, 3,4-tetramines such as butadiene tetramine etc.
- the value of the negative redox potential is generally below -50 mV, preferably between -100 mV and -300 mV.
- the setting of the 'negative redox potential takes place by means of an iron cracker, in which under
- the iron reactor can be connected in the bypass to the washing stage, ie part of the washing liquid is withdrawn from the washing stage, via the iron led reactor and then fed again into the washing stage.
- the iron reactor then advantageously consists of various bulk beds or it is designed as a steel tube bundle.
- a further advantageous development of the invention consists in designing the iron reactor as a metal granulate fluidized bed reactor, which is either connected to the washing stage in the bypass, or else the washing liquid in the sump of the washing stage is mixed directly with metallic iron or cast granules which very ' inexpensive to get on the market.
- the swirling of the metal balls can in this case by means of a rotary piston blower, which is connected to the raw gas, or by means of an O-poor gas ⁇ or by a water-gas mixture.
- the setting of the negative redox potential can be supported by additionally washing the washing liquid inside the iron reactor.
- the container wall is to be insulated accordingly or made of plastic, while the respective iron core has the function of the anode.
- the negative redox potential can also be set in whole or in part by adding suitable reducing agents to the washing liquid, such as sodium dithionite.
- the part of the washing liquid treated for setting the negative redox potential is contacted again with the raw gas stream before the rest of the washing liquid.
- the nitrogen released in the course of the treatment of the washing liquid can be drawn off directly from the system together with the clean gas.
- the upstream scrubber can be designed as a countercurrent scrubber or as a cocurrent scrubber, or both washing stages are integrated in a single two-stage scrubber.
- This washing liquid is conveyed from a container 7 into the washing stage 11 by means of a pump 6 via two nozzle levels in the present case.
- the container 7 is designed as an oxidation container in which, with a positive redox potential, the calcium sulfite or calcium hydrogen sulfite washed out in the washing stage 11 is oxidized to calcium sulfate (gypsum).
- the moist gypsum, including any calcium chloride still present, is drawn off from the system via a line 8 and fed to a treatment unit (not shown here).
- the crude gas obtained in the head of washing stage 11 and still containing almost all of the NO and residual amounts of SO is fed to a further washing stage 3 via a hood system and is washed there with a further washing liquid which has a negative redox potential.
- This washing liquid consists of an aqueous solution of, for example, hydrated lime, EDTA-iron-II-chelate and optionally sodium dithionite.
- the redox potential is preferably between -100 mV and -300 mV.
- the loaded washing liquid collected via the hood system is fed to a container 4, in which the desired redox potential is set, for example, in the manner described above.
- the correspondingly prepared washing liquid is fed again into the upper region of washing stage 3 by means of a pump 5 and in the present case two nozzle levels.
- part of the washing liquid collected in the container 4 is transferred to the oxidation container 7 of the washing stage 11 via a line 9.
- the calcium sulfite or hydrogen sulfite carried along from washing stage 3 is oxidized to sulfate at a positive redox potential and is likewise drawn off from the system via line 8.
- a corresponding amount of liquid can be returned from the container 7 to the container 4 at the same time.
- the cleaned raw gas After passing through a droplet separator system 10, the cleaned raw gas is withdrawn from the system via an outlet 2.
- the chemicals for the washing liquid of the washing stage 11 are fed into the container 7 and for the washing liquid of the washing stage 11 into the container 4.
- FIG. 2 shows a two-stage washer in which both the first washing stage 1 operated at a positive redox potential and the second washing stage 3 operated at a negative redox potential are operated in direct current.
- FIG. 3 finally shows a further embodiment in which the two washing stages 11 and 3 are designed as spatially separate washers, the washer 11 being operated in cocurrent and the scrubber 3 in countercurrent.
- the droplet separator system 10 is arranged in the gas-carrying connection channel between the two washers.
- the scrubber system shown in FIG. 3, in which the scrubber 3 can of course also be designed as a countercurrent scrubber or the scrubber 11 as a cocurrent scrubber, is particularly suitable for raw gases with high SO and NO contents, for example behind melting chamber boilers or chemical processes.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Description
Claims
Applications Claiming Priority (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3502208A DE3502208C2 (de) | 1985-01-24 | 1985-01-24 | Verfahren zur simultanen Abscheidung von SO↓2↓ und NO↓x↓ aus Rohgas |
DE19853502207 DE3502207A1 (de) | 1984-12-24 | 1985-01-24 | Elektrochemisches verfahren zur reinigung von abgasen in verbindung mit einem eisenreaktor |
DEP3502207.8 | 1985-01-24 | ||
DEP3502208.6 | 1985-01-24 | ||
DEP3502732.0 | 1985-01-28 | ||
DE3502732A DE3502732C2 (de) | 1985-01-28 | 1985-01-28 | Verfahren zur Rauchgasreinigung |
DE19853503889 DE3503889A1 (de) | 1985-02-06 | 1985-02-06 | Verfahren zur waschung von so(pfeil abwaerts)2(pfeil abwaerts) und no(pfeil abwaerts)x(pfeil abwaerts) |
DEP3503889.6 | 1985-02-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1986004260A1 true WO1986004260A1 (en) | 1986-07-31 |
Family
ID=27433282
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1986/000027 WO1986004260A1 (en) | 1985-01-24 | 1986-01-24 | Process for scrubbing raw gases laden with sulphur oxides and nitrogen oxides |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0210238A1 (de) |
WO (1) | WO1986004260A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0361895A2 (de) * | 1988-09-28 | 1990-04-04 | The Dow Chemical Company | Regenerierung von chelierten polyvalenten Metall-Lösungen durch kontrollierte Potential-Elektrolyse |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3268127B2 (ja) * | 1994-07-11 | 2002-03-25 | 三菱重工業株式会社 | 亜硫酸塩の酸化制御方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4126529A (en) * | 1977-08-05 | 1978-11-21 | Southern California Edison Company | Ferrous ion scrubbing of flue gas |
US4331639A (en) * | 1981-03-11 | 1982-05-25 | Union Oil Company Of California | Process for removing SOx and NOx compounds from gas streams |
WO1985003238A2 (en) * | 1984-01-25 | 1985-08-01 | Hoelter Heinz | Process for stripping nitrogen oxides and sulphur oxides as well as optionally other noxious elements of flue gas from combustion plants |
-
1986
- 1986-01-24 EP EP86901055A patent/EP0210238A1/de not_active Ceased
- 1986-01-24 WO PCT/EP1986/000027 patent/WO1986004260A1/de not_active Application Discontinuation
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4126529A (en) * | 1977-08-05 | 1978-11-21 | Southern California Edison Company | Ferrous ion scrubbing of flue gas |
US4331639A (en) * | 1981-03-11 | 1982-05-25 | Union Oil Company Of California | Process for removing SOx and NOx compounds from gas streams |
WO1985003238A2 (en) * | 1984-01-25 | 1985-08-01 | Hoelter Heinz | Process for stripping nitrogen oxides and sulphur oxides as well as optionally other noxious elements of flue gas from combustion plants |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0361895A2 (de) * | 1988-09-28 | 1990-04-04 | The Dow Chemical Company | Regenerierung von chelierten polyvalenten Metall-Lösungen durch kontrollierte Potential-Elektrolyse |
EP0361895A3 (de) * | 1988-09-28 | 1991-01-02 | The Dow Chemical Company | Regenerierung von chelierten polyvalenten Metall-Lösungen durch kontrollierte Potential-Elektrolyse |
Also Published As
Publication number | Publication date |
---|---|
EP0210238A1 (de) | 1987-02-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE2619145C3 (de) | Verfahren zum Abscheiden von Stickstoffoxiden oder von Stickstoffoxiden und Schwefeloxiden aus Abgasen | |
DE3220403C1 (de) | Verfahren zum Entfernen von sauren Komponenten und Stickoxyden aus Abgasen | |
EP0792186B1 (de) | Verfahren und vorrichtung zum reinigen von verbrennungsabgasen | |
DE3305120C2 (de) | Verfahren zur zweistufigen Rauchgasreinigung mittels Absorption | |
DE3626370A1 (de) | Entschwefelung/denitrifikation von rauchgas unter verwendung von metall-chelatadditiven | |
DE3513544C2 (de) | ||
EP0981022B1 (de) | Verfahren zum Reinigen von Rauchgas | |
DE2735566A1 (de) | Verfahren zum entfernen von fluorverbindungen und schwefeldioxid aus abgasen | |
EP0238811B1 (de) | Verfahren zum Reinigen von S02-haltigen Rauchgasen | |
DE2342861A1 (de) | Verfahren und vorrichtung zum nassentschwefeln von rauchgasen | |
WO1986004260A1 (en) | Process for scrubbing raw gases laden with sulphur oxides and nitrogen oxides | |
WO1985003238A2 (en) | Process for stripping nitrogen oxides and sulphur oxides as well as optionally other noxious elements of flue gas from combustion plants | |
DE3310716C2 (de) | Verfahren zur absorptiven Entfernung von HCL und SO↓2↓ aus Rauchgas | |
DE69905378T2 (de) | Verfahren zur reinigung eines abgases | |
DE1817015B2 (de) | Verfahren zur abtrennung von schwefeldioxyd aus restgasen | |
WO1986005709A1 (en) | Process for the cleansing of fumes | |
DE3732191C1 (en) | Method for treating the heat exchanger impinged with an ammonium sulphate-containing gas on washing | |
DE3821350C2 (de) | ||
EP0706815B1 (de) | Verfahren zur Abscheidung von Quecksilber aus Verbrennungsabgasen von Klärschlammverbrennungsanlagen | |
DE3412955C2 (de) | ||
EP0223803A1 (de) | VERFAHREN ZUM GLEICHZEITIGEN AUSWASCHEN VON SO 2?, NO x? UND GGF. WEITEREN SCHADSTOFFEN AUS DEN RAUCHGASEN VON MIT FOSSILEN BRENNSTOFFEN BETRIEBENEN FEUERUNGSANLAGEN | |
DE4229662C2 (de) | Verfahren zur Entfernung von Quecksilber aus aus Rauchgaswäschern stammenden Abwässern | |
DE2703157C3 (de) | Verfahren zum Entfernen von Stickstoffoxiden und Schwefeloxiden aus Verbrennungsabgasen | |
DE3535172A1 (de) | Verfahren zum regenerieren von kohlenstoffhaltigen adsorptionsmitteln | |
CH630814A5 (en) | Process for cleaning waste gases containing sulphur dioxide, and appliance for carrying out the process |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): JP US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE FR GB IT LU NL SE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1986901055 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1986901055 Country of ref document: EP |
|
WWR | Wipo information: refused in national office |
Ref document number: 1986901055 Country of ref document: EP |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 1986901055 Country of ref document: EP |