DE2654843C2 - Process for cleaning flue gases and other exhaust gases - Google Patents
Process for cleaning flue gases and other exhaust gasesInfo
- Publication number
- DE2654843C2 DE2654843C2 DE19762654843 DE2654843A DE2654843C2 DE 2654843 C2 DE2654843 C2 DE 2654843C2 DE 19762654843 DE19762654843 DE 19762654843 DE 2654843 A DE2654843 A DE 2654843A DE 2654843 C2 DE2654843 C2 DE 2654843C2
- Authority
- DE
- Germany
- Prior art keywords
- added
- calcium
- gas
- liquid
- washing
- 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.)
- Expired
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
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
-
- 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
- B01D53/14—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 by absorption
- B01D53/1456—Removing acid components
-
- 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
- B01D53/14—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 by absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F11/00—Compounds of calcium, strontium, or barium
- C01F11/46—Sulfates
- C01F11/464—Sulfates of Ca from gases containing sulfur oxides
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C3/00—Fertilisers containing other salts of ammonia or ammonia itself, e.g. gas liquor
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Treating Waste Gases (AREA)
Description
Die Erfindung betrifft ein Verfahren zum Reinigen vorr Rauchgasen und anderen Abgasen, die Schwefeldioxyd enthalten, bei dem das Gas mit einer im Kreislauf gefahrenen Waschflüssigkeit in Kontakt gebracht wird, der Kalziumkarbonat und/oder Kalziumoxyd und/ock Kalziumhydroxyd zugesetzt werden und deren in Lösung befindliche Kalziumionen beim Waschvorgang das Schwefeldioxyd des Gases binden, und bei dem die gebildeten Verbindungen mittels Luftsauerstoff zu Kalziumsulfat oxydiert werden und aus dem Kreislauf ab geschieden werden, wobei der Waschflüssigkeit als Zusatz Salze und/oder eine Mineralsäure zugegeben werden und die Waschflüssigkeit vordem Kontakt mit dem Gas von Feststoffen befreit wird und der Waschflüssigkeit vor dem Kontakt mit dem Gas zusätzlich eine zur Pufferung dienende Karbonsäure und/oder deren Salz zugegeben wird nach Patent 25 32 373. The invention relates to a method for cleaning vorr flue gases and other exhaust gases containing sulfur dioxide, in which the gas is brought into contact with a circulating scrubbing liquid to which calcium carbonate and / or calcium oxide and / or calcium hydroxide are added and their calcium ions in solution bind the sulfur dioxide of the gas during the washing process, and in which the compounds formed are oxidized to calcium sulfate by means of atmospheric oxygen and are separated from the circuit, the washing liquid being added as an additive, salts and / or a mineral acid and the washing liquid before contact with the gas solids and is freed of the washing liquid prior to contact with the gas additionally serving for buffering carboxylic acid and / or salt thereof is added to Patent 25 32 373rd
Das Verfahren nach dem Hauptpatent hat sich bewährt. In Abhängigkeit von der Schwcfcldioxydkonzentration im Rauchgas werden außer bestimmten Mengen Salzsäure und Ameisensäure auch eine als Pufferung dienei.de einbasische Karbonsäurc und/oder deren Salze zugegeben.The procedure according to the main patent has proven itself. Depending on the low-carbon dioxide concentration In addition to certain quantities of hydrochloric acid and formic acid, the flue gas also acts as a buffer dienei.de monocarboxylic acids and / or their salts admitted.
Aufgabe der Erfindung ist die Verbesserung des Verfahrens nach dem Hauptpatent.The object of the invention is to improve the method according to the main patent.
Diese Aufgabe wird dadurch gelöst, daß die Waschflüssigkeit mit einem Additiv, das aus einer mehrbasischen Karbonsäurc und Chlorioncn besteht, versetzt wird.This object is achieved in that the washing liquid with an additive that consists of a polybasic Carboxylic acid and chlorine ions is added.
Überraschenderweise hat sich gezeigt, daß dabei die Aufnahmefähigkeit von SO>etwa 3 χ höher liegt, d. h. es können etwa 3 χ soviel Kal/.iuininnen über d:is Kal/ium/ilial in Losung gebracht werden als bei der Zugabe von /.. H. einbasischer Ameisensäure mit HCI. Das beik-ulLt einen wesentlich niedrigeren Waschflüssigkeit*· f.iktor (l.iicr Hüssii'keit /u ni' Rohgas), so daß eine wesentlich geringere I liissigkeit zur Waschung in das Gaswaschsystem eingepumpt werden muß. somit nur einSurprisingly, it has been shown that the absorption capacity of SO is> about 3 higher, ie. H. it can have about 3 χ as many Kal / .iuininnen over d: is Kal / ium / ilial be brought into solution than with the addition of / .. H. monobasic formic acid with HCl. That beik-ulLt a much lower scrubbing liquid * · f.iktor (l.iicr Hüssii'keit / u ni 'raw gas), so that a substantially less liquid for washing in the gas washing system must be pumped in. thus only one
3030th Bruchteil der bisher erforderlichen Pumpenleistung. Die Waschflüssigkeitsbehälter, wie Sinkabscheider und OxydationsgefäBe, können wesentlich kleiner ausgelegt werden, da ja eine wesentlich geringere Waschflüssigkeitsmenge im Waschkreislauf gefahren wird.Fraction of the previously required pump output. the Washing liquid containers, such as sink separators and oxidation vessels, can be designed to be much smaller because a much smaller amount of washing liquid is run in the washing cycle.
Die ph-Wert-Absenkung der aufgegebenen Waschflüssigkeit in den Waschprozeß von pH 12 bis auf pH 2.8 erfolgt ohne Ausfällung (keine Kalziumsulfitbildung und Kalziumcarbonatbildung). Es entstehen absolut keine Inkrustierungen innerhalb der Wafchapparatur. Verluste durch Verdampfung beim Einsprühen in heiße Rauchgase um 200° C entstehen nichtThe lowering of the pH value of the applied washing liquid in the washing process from pH 12 to pH 2.8 takes place without precipitation (no calcium sulfite formation and calcium carbonate formation). There are absolutely none Incrustations within the washing machine. Losses due to evaporation when spraying into hot Flue gases around 200 ° C do not arise
Die Zitronensäure liegt zur Dosierung in fester Form vor. Das Salz wird in Wasser gelöst der Waschflüssigkeit zugegeben. Durch die Zugabe dieser dreibasischen Zitronensäure wird eine Waschlösung gebiliet, die im alkalischen sowie im sauren Bereich als Pufferlösung wirkt Die starke Pufferwirkung der Waschlösung bewirkt auch in dem pH-Bereich von z. B. pH 5 bis pH 7 einen weitgehenden Korrosionsschutz für die Anlagenteile der Gaswascheinrichtung. Eine gute Oxydation von Kalziumsulfit zu Kalziumsulfat wirr1; im pH-Wert-Bereich zwischen pH 6 bis pH 63 vorteilhaft erzieltCitric acid is available in solid form for dosing. The salt is dissolved in water and added to the washing liquid. The addition of this tribasic citric acid creates a washing solution that acts as a buffer solution in the alkaline and acidic range. B. pH 5 to pH 7 an extensive corrosion protection for the system parts of the gas scrubbing device. A good oxidation of calcium sulphite to calcium sulphate confused 1 ; advantageously achieved in the pH range between pH 6 to pH 63
Als weiterer Vorteil darf gewertet werden, daß überraschenderweise die Kristallausbildung der Gipskristalle nach der Oxydation wesentlich größer ist als bei den bekannten Waschflüssigkeiten, so daß hierdurch eine wesentlich bessere Absenkung des Wassergehaltes im abzufilternden CaSO*-Rückstand durch Trommelvakuumfilter oder Zentrifugen gewährleistet wird.Another advantage is that, surprisingly, the crystal formation of the gypsum crystals after the oxidation is significantly greater than that of the known washing liquids, so that this results in a much better lowering of the water content in the CaSO * residue to be filtered off is guaranteed by drum vacuum filters or centrifuges.
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Claims (2)
Priority Applications (15)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19762654843 DE2654843C2 (en) | 1975-07-19 | 1976-12-03 | Process for cleaning flue gases and other exhaust gases |
DE19772730845 DE2730845A1 (en) | 1975-07-19 | 1977-07-08 | Purificn. of gas contg. sulphur di:oxide by washing - using an additive contg. a poly:carboxylic acid |
AT0783577A AT367318B (en) | 1976-12-03 | 1977-11-03 | METHOD FOR PURIFYING RAW GAS AND OTHER EXHAUST GASES CONTAINING SULFUR DIOXIDE AND DEVICE FOR CARRYING OUT THE METHOD |
NL7712450A NL7712450A (en) | 1976-12-03 | 1977-11-11 | PROCESS FOR PURIFYING CRUDE GAS AND OTHER EXHAUST GASES CONTAINING SULFUR DIOXIDE AND EQUIPMENT FOR PERFORMING THIS PROCESS. |
SE7712900A SE431939B (en) | 1976-12-03 | 1977-11-15 | SET TO CLEAN RAGAS AND OTHER EXHAUSTS INCLUDING SULFUR Dioxide AND DEVICE IMPLEMENTATION |
GB4849677A GB1545175A (en) | 1974-09-19 | 1977-11-22 | Removal of noxious contaminants from gas |
FR7735441A FR2372651A1 (en) | 1976-12-03 | 1977-11-24 | PROCESS FOR PURIFYING CRUDE GASES AND OTHER WASTE GASES WHICH CONTAIN SULPHUROUS ANHYDRIDE AND DEVICE FOR CARRYING OUT THIS PROCESS |
AU31026/77A AU515100B2 (en) | 1976-12-03 | 1977-11-28 | Gas washing process |
US05/855,268 US4222993A (en) | 1974-09-19 | 1977-11-28 | Removal of noxious contaminants from gas |
CH1461177A CH630814A5 (en) | 1976-12-03 | 1977-11-29 | Process for cleaning waste gases containing sulphur dioxide, and appliance for carrying out the process |
BE2056472A BE861329A (en) | 1976-12-03 | 1977-11-30 | METHOD AND DEVICE FOR PURIFYING CRUDE GASES AND OTHER RESIDUAL GASES CONTAINING SULPHUROUS ANHYDRIDE |
IT30251/77A IT1089312B (en) | 1976-12-03 | 1977-12-01 | DEVICE TO PURIFY GEGGI GAS OR EXHAUST GASES, WHICH CONTAIN SULFUR DIOXIDE |
JP14492377A JPS5370981A (en) | 1976-12-03 | 1977-12-02 | Method and apparatus for purifying raw gas and sulfur dioxideecontaining waste gas |
DK539277A DK539277A (en) | 1976-12-03 | 1977-12-02 | PROCEDURE FOR PURIFICATION OF RAAGAS AND OTHER EXHAUST GASES CONTAINING SULFUR DIOXIDE AND APPLIANCE FOR PERFORMING THE PROCEDURE |
CA292,308A CA1100122A (en) | 1976-12-03 | 1977-12-02 | Removal of noxious contaminants from gas |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2532373A DE2532373C3 (en) | 1975-07-19 | 1975-07-19 | Method and device for cleaning flue gases and other exhaust gases containing sulfur dioxide |
DE19762654843 DE2654843C2 (en) | 1975-07-19 | 1976-12-03 | Process for cleaning flue gases and other exhaust gases |
Publications (2)
Publication Number | Publication Date |
---|---|
DE2654843A1 DE2654843A1 (en) | 1978-06-08 |
DE2654843C2 true DE2654843C2 (en) | 1989-11-23 |
Family
ID=25769175
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19762654843 Expired DE2654843C2 (en) | 1974-09-19 | 1976-12-03 | Process for cleaning flue gases and other exhaust gases |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE2654843C2 (en) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3632306A (en) * | 1969-02-18 | 1972-01-04 | Chemical Construction Corp | Removal of sulfur dioxide from waste gases |
JPS5017318B1 (en) * | 1970-12-29 | 1975-06-19 |
-
1976
- 1976-12-03 DE DE19762654843 patent/DE2654843C2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE2654843A1 (en) | 1978-06-08 |
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