SE441150B - PROCEDURE FOR WATER EXHAUST FROM COMBUSTION PLANTS AT THE SAME TIME DISPOSING NITROGEN OXIDES AND SULFUR OXIDES UNDER ADDITION OF AMMONIA - Google Patents

PROCEDURE FOR WATER EXHAUST FROM COMBUSTION PLANTS AT THE SAME TIME DISPOSING NITROGEN OXIDES AND SULFUR OXIDES UNDER ADDITION OF AMMONIA

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Publication number
SE441150B
SE441150B SE7909735A SE7909735A SE441150B SE 441150 B SE441150 B SE 441150B SE 7909735 A SE7909735 A SE 7909735A SE 7909735 A SE7909735 A SE 7909735A SE 441150 B SE441150 B SE 441150B
Authority
SE
Sweden
Prior art keywords
ammonia
sulfur oxides
process step
procedure
addition
Prior art date
Application number
SE7909735A
Other languages
Swedish (sv)
Other versions
SE7909735L (en
Inventor
H Bechthold
U Mohn
Original Assignee
Walther & Cie Ag
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Walther & Cie Ag filed Critical Walther & Cie Ag
Publication of SE7909735L publication Critical patent/SE7909735L/en
Publication of SE441150B publication Critical patent/SE441150B/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/60Simultaneously removing sulfur oxides and nitrogen oxides
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Description

lysen icke omsatt "*"enen@ Till grund för uppfinningen ligger up giften att tillhandahålla ett förfarande där nan arbetar med en överdosering av ammoniak för att bortföra HOX och avlägsna ammoniaköverskottet u de kvarblivande av- gaserna utan extra kostnad, Uppgiften löses genom att avgaserna tillsammans med förfarandets hela annoniaxtillsats först tillförs till ett första processteg, som avlägsnar HDX, och som är av ett s'ag, där ett överskott av ammoniak utöver förbrukningen i prooessteget leder till ökad reaktionshastighet i proeessteget, och att avgaserna efter behandlingen i det första prooessteget tillförs tillsammans ned icke förbrukad ammoniak till ett andra prooessteg, som i närvaro av ammoniak avlägsnar svaveloxider, varvid nämnda hela ammoniaktillsats sätts att motsvara den totala förbrukningen i båda prooesstegene Föreliggande uppfinning grundar sig följaktligen på idén att man kombinerar ett godtyckligt med NH; arbetande förfarande för att avlägsna HDX med ett förfarande för rökgasavsvavling - exempelvis enligt den tyska patentskriften 24 31 130. Detta förut kända avsvav- lingsförfarande arbetar medelst tillsats av gasformig ammoniak, varvid ænnoniunsulfat framställes ur svaveloxiderna. Enligt uppfinningen till- sattes den härför erforderliga sanmoniakmängden på ett ställe - sett i gasströmmens riktning - vilket ligger före påbörjandet av NOx-förfaran- deto Den för KO:-borttagningen erforderliga ammoniakmängden höjes följ- ektligen enligt uppfinningen till det belopp som behövs för reaktionen med i rökgasen förhandenvarande SOX under den efterföljande avsvav- lingenq Därigenom ernås de ovan angivna fördelarna beträffande jäm- viktsinställningenø För NOK-borttagningen kan vilket som helst förfarande användas där man arbetar ned ammoniak och där vid processens slut jämviktstill- ståndet mellan ammoniak och H03 (resp andra komponenter) påverkar bort- tagningsgraden av HDX; då är nämligen ett ammoniaköverskott till fördel eftersom det leder till en avsevärd höjning av reaktionshastigheten. ärigenom ernås lägre investeringskostnader resp mindre omfattande anpar tur, eller vid samma storlek på anparaturen en högre grad av NOK-avlägsnandec För ett avlägsne,FOï kan man använda katalytiska re- duktionsförfaranden, eller adsorptions= och absorptionsprocesser, för- utsatt att dessa arbetar med ammoniaktillsats. lysen not sold "*" enen @ The invention is based on the information provided a process in which nan works with an overdose of ammonia to remove the HOX and remove the excess ammonia from the remaining the gases at no extra cost, The task is solved by the exhaust gases together with the procedure the whole anonyx additive is first added to a first process step, which removes HDX, and which is of a s'ag, where an excess of ammonia in addition to the consumption in the prooes step leads to increased reaction rate in the proees stage, and that the exhaust gases after the treatment in the first the prooes step is added together with unused ammonia to a second process step, which in the presence of ammonia removes sulfur oxides, wherein said whole ammonia additive is set to correspond to the total consumption in both prooesstegene Accordingly, the present invention is based on the idea that one combines an arbitrary with NH; working procedure to remove HDX with a flue gas desulphurisation procedure - for example according to German Patent Specification 24 31 130. This previously known desulphurisation The process works by adding gaseous ammonia, wherein Annonium sulphate is prepared from the sulfur oxides. According to the invention the amount of ammonia required for this was placed in one place - seen in direction of the gas flow - which is before the start of the NOx The amount of ammonia required for KO removal is increased accordingly. according to the invention to the amount needed for the reaction with SOX present in the flue gas during the subsequent desulphurisation This achieves the above advantages in terms of weight settingø For NOK removal, any procedure can be used where ammonia is worked down and where at the end of the process equilibrium the position between ammonia and H03 (respectively other components) affects the the degree of capture of HDX; then an excess of ammonia is advantageous as it leads to a significant increase in the reaction rate. thereby achieving lower investment costs or less extensive ones anpar luck, or at the same size of the anparatur a higher degree of NOK removal For a distance, FOï, one can use catalytic production processes, or adsorption = and absorption processes, exposed that these work with ammonia additive.

Kombinationen enligt unpfinningen har fördelen att graden NOX- borttagning påverkas fördelaktigt utan att otillåtligt höga mängderThe combination according to the invention has the advantage that the degree of NOX removal is favorably affected without excessively high amounts

Claims (1)

vso9vzs~a ammoniak avgår genom eldstadens skorsten. Kombinationsförfarandet en- ligt uppfinningen är baserat på en för avsvavling under ammoniaktill- sats anordnad anläggning vid vilken den avgående rengasen blott har så ringa halt ammoniak att denna ligger under tillåtna gränser och miljökraven sålunda tillfredsställes. Ett sådant förfarande beskrives i DE-PS 24 31 130. Den medelst kombinationen enligt uppfinningen genomförda om- sättningen kan exempelvis förlöpa enligt följande kemiska reaktion: 2110 + 2NH3 + 1/2 02 <---9 3H2o + 2N2 Till följd av åtgärderna enligt uppfinningen åstadkommes även den ekonomiskt fördelaktiga effekten att anläggningen för NOX-borttagande kan byggas med mindre dimensioner än förut kända anläggningar, efter- som en högre proportion ammoniak vid inträdet i systemet fördelaktigt påverkar reaktionen som avlägsnar NOX-föroreningen. Patentkrav: Förfarande för att ur avgaser från förbrännlngsanläggnlngar sarntidigt avlägsna kväveoxider och svaveloxider under tillsats av ammoniak, kännetecknat av att avgaserna tillsammans med förfarandets hela ammoniaktillsats först tillförs till ett första processteg, som avlägsnar NOX, och som är av ett slag, där ett överskott av ammoniak utöver förbrukningen i processteget leder till ökad reaktionshastighet i processteget, och att avgaserna efter behandüngen i det första processteget tfllförs tiüsanunans rned icke förbrukad anunoniak tül ett andra processteg, sonw i närvaro av ammoniak avlägsnar svaveloxider, varvid nämnda hela ammoniaktillsats sätts att motsvara den totala förbrukningen i bada processtegen.vso9vzs ~ a ammonia escapes through the fireplace chimney. The combination process according to the invention is based on a plant arranged for desulphurisation under ammonia addition at which the effluent purge gas has only such a low content of ammonia that it is below permissible limits and the environmental requirements are thus satisfied. Such a process is described in DE-PS 24 31 130. The reaction carried out by means of the combination according to the invention can proceed, for example, according to the following chemical reaction: 2110 + 2NH 3 + 1/2 O 2 <--- 9 3H 2 O + 2N 2 As a result of the measures according to The invention also provides the economically advantageous effect that the NOX removal plant can be built with smaller dimensions than previously known plants, since a higher proportion of ammonia upon entering the system advantageously affects the reaction which removes the NOX contaminant. Claim: Process for the simultaneous removal of nitrogen oxides and sulfur oxides from combustion gases from combustion plants with the addition of ammonia, characterized in that the exhaust gases together with the entire ammonia additive of the process are first fed to a first process stage, which removes NOX, and which is of one kind, ammonia in addition to the consumption in the process step leads to an increased reaction rate in the process step, and that the exhaust gases after the treatment in the first process step are carried to the unused ammonia to a second process step, sonw in the presence of ammonia removes sulfur oxides to which the said whole in both process steps.
SE7909735A 1978-12-04 1979-11-26 PROCEDURE FOR WATER EXHAUST FROM COMBUSTION PLANTS AT THE SAME TIME DISPOSING NITROGEN OXIDES AND SULFUR OXIDES UNDER ADDITION OF AMMONIA SE441150B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2852336A DE2852336C2 (en) 1978-12-04 1978-12-04 Process for the separation of NO? X? and SO? x? from combustion exhaust gases

Publications (2)

Publication Number Publication Date
SE7909735L SE7909735L (en) 1980-06-05
SE441150B true SE441150B (en) 1985-09-16

Family

ID=6056242

Family Applications (1)

Application Number Title Priority Date Filing Date
SE7909735A SE441150B (en) 1978-12-04 1979-11-26 PROCEDURE FOR WATER EXHAUST FROM COMBUSTION PLANTS AT THE SAME TIME DISPOSING NITROGEN OXIDES AND SULFUR OXIDES UNDER ADDITION OF AMMONIA

Country Status (10)

Country Link
JP (1) JPS5581729A (en)
AT (1) AT376584B (en)
CH (1) CH641057A5 (en)
CS (1) CS222289B2 (en)
DE (1) DE2852336C2 (en)
DK (1) DK512679A (en)
FR (1) FR2443274B1 (en)
NL (1) NL7908531A (en)
PL (1) PL123282B1 (en)
SE (1) SE441150B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992008541A1 (en) * 1990-11-12 1992-05-29 A/S Miljøutvikling METHOD AND APPARATUS FOR PURIFYING EXHAUST WITH RESPECT TO SO2, NOx AND DUST

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT384958B (en) * 1985-05-28 1988-02-10 Waagner Biro Ag Process and device for the purification of exhaust gases which are contaminated with dusts and pollutant gases
DE3610942A1 (en) * 1985-11-26 1987-08-13 Lothar Dipl Ing Mueller Process for the simultaneous removal of pollutants from flue gases and reactor for carrying out the process
US4853193A (en) * 1986-01-10 1989-08-01 Exxon Research And Engineering Company Process for removing NOx and SOx from a gaseous mixture

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1007829A (en) * 1972-09-01 1977-04-05 Exxon Research And Engineering Company Removal of nitrogen oxides and sulfur oxides from gases
JPS5636971B2 (en) * 1974-05-08 1981-08-27
DE2431130C3 (en) * 1974-06-28 1979-07-26 Maschinenfabrik Burkau R. Wolf Kg, 4048 Grevenbroich Process for removing acidic components from exhaust gases
FR2299071A1 (en) * 1974-07-20 1976-08-27 Mitsubishi Chem Ind PROCESS FOR THE CHEMICAL REMOVAL OF NITROGEN OXIDES AND SULFUR OXIDES
JPS535984B2 (en) * 1974-09-04 1978-03-03
FR2368987A1 (en) * 1976-11-01 1978-05-26 Mitsubishi Chem Ind CATALYTIC REDUCTION OF NITROGEN OXIDES

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992008541A1 (en) * 1990-11-12 1992-05-29 A/S Miljøutvikling METHOD AND APPARATUS FOR PURIFYING EXHAUST WITH RESPECT TO SO2, NOx AND DUST

Also Published As

Publication number Publication date
NL7908531A (en) 1980-06-06
FR2443274A1 (en) 1980-07-04
SE7909735L (en) 1980-06-05
CH641057A5 (en) 1984-02-15
PL220110A1 (en) 1980-09-22
CS222289B2 (en) 1983-06-24
DE2852336C2 (en) 1986-10-16
AT376584B (en) 1984-12-10
ATA699379A (en) 1984-05-15
JPS5581729A (en) 1980-06-20
PL123282B1 (en) 1982-10-30
DE2852336A1 (en) 1980-06-26
DK512679A (en) 1980-06-05
FR2443274B1 (en) 1987-01-23

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