DE3318252A1 - Process for flue gas desulphurisation having a gas distributor in the cooling tower without a bottom surface - Google Patents

Process for flue gas desulphurisation having a gas distributor in the cooling tower without a bottom surface

Info

Publication number
DE3318252A1
DE3318252A1 DE19833318252 DE3318252A DE3318252A1 DE 3318252 A1 DE3318252 A1 DE 3318252A1 DE 19833318252 DE19833318252 DE 19833318252 DE 3318252 A DE3318252 A DE 3318252A DE 3318252 A1 DE3318252 A1 DE 3318252A1
Authority
DE
Germany
Prior art keywords
flue gas
cooling tower
distributor
gas
water
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.)
Ceased
Application number
DE19833318252
Other languages
German (de)
Inventor
Heribert Dipl.-Ing. 4390 Gladbeck Dewert
Georg Dr.-Ing. 5226 Reichshof Gebhard
Heinrich Ing.(grad.) 4600 Dortmund Gresch
Klaus R.G. Dr.-Ing. 5010 Bergheim Hein
Heinz Dipl.-Ing. Hölter
Heinrich Dipl.-Ing. 4390 Gladbeck Igelübscher
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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
Priority claimed from DE3314678A external-priority patent/DE3314678C2/en
Application filed by Individual filed Critical Individual
Priority to DE19833318252 priority Critical patent/DE3318252A1/en
Publication of DE3318252A1 publication Critical patent/DE3318252A1/en
Ceased legal-status Critical Current

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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
    • F28C1/003—Direct-contact trickle coolers, e.g. cooling towers comprising outlet ducts for exhaust gases
    • 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
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (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)
  • Chimneys And Flues (AREA)

Abstract

The invention relates to a process for flue gas desulphurisation, preferably downstream of old power stations having low cooling towers. According to the main application P 3314678.0, the scrubbed flue gas from the flue gas desulphurisation plant is passed via a large surface area distributor into the vicinity of the bottom of the cooling tower. In order to achieve design distribution in the vicinity of the bottom to be on as large a surface area as possible, according to the invention it is proposed to design the gas feed (1) in the shape of a ring, that is to arrange it open towards the water flume (9) and to immerse and support this in the water flume so that the trickling water from the cooling tower (3) flows through the ring arrangement downward into the water flume and in the course of this at the same time washes out the entrained droplets from the scrubbed dirty gas. The boundary surfaces of the distributor (4) are perforated. <IMAGE>

Description

Beschreibung und Erläuterung zur Zusatz-Description and explanation of the additional

Patentanmeldung "Verfahren zur Rauchgasentschwefelung mit Gasverteiler im Kiihlturm ohne Bodenfläche" Zusatzpatentanmeldung zu P 33 14 678.0 In der Hauptanmeldung P 33 14 e 8.O wird ein Verfahren zur Rauchgasentschweßeiung vorzugsweise hinter Altkraftwerken mit niedrigem Kühlturm beschrieben, wobei das gewaschene Rauchgas aus der Rauchgasentschwefelungsanlage über einen großflächigen Verteiler in Bodennähe des Kühlturms eingeleitete wird.Patent application "Process for flue gas desulphurization with gas distributor in the cooling tower without floor space "additional patent application to P 33 14 678.0 in the main application P 33 14 e 8.O a process for flue gas removal is preferred Old power plants with low cooling towers described, with the scrubbed flue gas from the flue gas desulphurisation system via a large-area distributor close to the ground of the cooling tower is initiated.

Um die Verteilung in Bodennähe größtflächig auszubilden, wird erfindungsgemäß vo-rgeschlagen, die Gaseinleitung ringförmig vorzunehmen -wie in der beiliegenden Zeichnung mit (1) dargestellt - und ohne Boden auszubilden und tunlichst in der Wassertasse anzutauchen und abzustützen, so da1d das Rieselwasser aus dem Kühlturm durch die Ringanordnung nach unten in die Wassertasse abfließt und dabei gleichzeitig erfindungsgemäß den Tropfendurchriß aus dem gewaschenen Rohgas auswäscht - wie in der beiliegenden Zeichnung dargestellt.In order to develop the distribution over a large area near the ground, according to the invention suggested, to introduce the gas in a ring -as in the accompanying drawing with (1) - and train without a bottom and to submerge and support it in the water cup if possible, so that the trickling water flows down from the cooling tower through the ring arrangement into the water cup and at the same time, according to the invention, the teardrop opening from the scrubbed raw gas washes out - as shown in the accompanying drawing.

Es ist vorteilhaft, die Verteiler-Begrenzungsflächen zu perforieren, um eine bestmögliche Flächenverteilung des eingeleiteten Gases zu erzielen.It is advantageous to perforate the distributor boundary surfaces, in order to achieve the best possible area distribution of the gas introduced.

In der beiliegenden Zeichnung ist dargestelt: mit (1) die Gaseinleitung mit (2) der Gasaustritt aus dem Diffusorbereich mit (3) der Kühlturm mit (4) die diffusorartige Darstellung -rund oder eckig mit (5) die Tropfenabscheider mit (6) z.B. die Rieseldüsen mit (7) das Rieselwasser mit (8) das ankommende, gewaschene Rohgas mit (9) das sich auf dem Kühlturm-Boden ansammelnde Kühlwasser mit (10) der Ablauf des Kühlwassers.The accompanying drawing shows: with (1) the gas inlet with (2) the gas outlet from the diffuser area with (3) the cooling tower with (4) the diffuser-like Representation - round or square with (5) the droplet separators with (6) e.g. the trickle nozzles with (7) the trickling water with (8) the incoming, washed raw gas with (9) the itself Cooling water accumulating on the cooling tower floor with (10) the drainage of the cooling water.

Erfindungsgemäß wird hiermit weiter erreicht, daß noch eine zusätzliche Nachwaschung der bereits gereinigten Gase, die aber immerhin noch einen Rest an Schwefeldioxid enthalten, in der Berieselungszone des Kühlturms zwangsläufig erfolgt.According to the invention it is hereby further achieved that an additional Post-washing of the already cleaned gases, but they still show a residue Containing sulfur dioxide, inevitably occurs in the irrigation zone of the cooling tower.

Durch diese Anordnung ist die Gewähr gegeben, daß geringstmöglicher S02-haltiger Nebelauswurf aus dem Kühlturm erreicht wird.This arrangement ensures that the least possible S02-containing fog is achieved from the cooling tower.

Zusatz-Patentanspriiche: - Leerseite -Additional claims: - blank page -

Claims (1)

Zusatz-P a t e n t a n s p r ü c h e: Anspruch 1 Verfahren zur Rauchgasentschwefelung vorzugsweise hinter Altkrattwerken mit niedrigen Kühltürmen nach Hauptpatentanmeldung P 53 14 67880 dadurch gekennzeichnet, daß das gewaschene Rauchgas aus der Rauchgasentschwefelungsanlage ber einen großflächigen Verteiler in Bodennähe des kühlturms eingeleitet wird, wobei dieser Verteiler erfindungsgemäß keinen Boden besitzt, sondern nach unten zur Wassertasse (9) offen ausgebildet ist und vorzugsweise aufgeständert ausgeführt wird.Additional P a t e n t a n s p r ü c h e: Claim 1 method for flue gas desulfurization preferably behind Altkrattwerke with low cooling towers according to the main patent application P 53 14 67880 characterized in that the scrubbed flue gas from the flue gas desulfurization system is introduced via a large-area distributor near the bottom of the cooling tower, whereby this distributor according to the invention has no bottom, but down to the water cup (9) is designed to be open and is preferably carried out raised. Anspruch 2 Verfahren zur Hauchgasentschwefelung nach Anspruch 1 dadurch gekennzeichnet, daß die Begrenzungsflächen des Verteilers perforiert ausgebildet sind.Claim 2 method for breath gas desulphurization according to claim 1 thereby characterized in that the boundary surfaces of the distributor are perforated are.
DE19833318252 1983-04-22 1983-05-19 Process for flue gas desulphurisation having a gas distributor in the cooling tower without a bottom surface Ceased DE3318252A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE19833318252 DE3318252A1 (en) 1983-04-22 1983-05-19 Process for flue gas desulphurisation having a gas distributor in the cooling tower without a bottom surface

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3314678A DE3314678C2 (en) 1983-04-22 1983-04-22 Process for introducing the flue gases of a power plant into a cooling tower
DE19833318252 DE3318252A1 (en) 1983-04-22 1983-05-19 Process for flue gas desulphurisation having a gas distributor in the cooling tower without a bottom surface

Publications (1)

Publication Number Publication Date
DE3318252A1 true DE3318252A1 (en) 1984-11-22

Family

ID=25810224

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19833318252 Ceased DE3318252A1 (en) 1983-04-22 1983-05-19 Process for flue gas desulphurisation having a gas distributor in the cooling tower without a bottom surface

Country Status (1)

Country Link
DE (1) DE3318252A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1986005577A1 (en) * 1985-03-16 1986-09-25 Saarbergwerke Aktiengesellschaft Smoke gas exhaust by way of a cooling tower
RU2453712C2 (en) * 2010-08-20 2012-06-20 Государственное образовательное учреждение высшего профессионального образования Самарский государственный технический университет Power facility combined-cycle plant
RU2704364C1 (en) * 2018-07-09 2019-10-28 федеральное государственное бюджетное образовательное учреждение высшего образования "Самарский государственный технический университет" Combined cycle gas turbine of power plant

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2732580A1 (en) * 1976-08-02 1978-02-09 Mitsubishi Heavy Ind Ltd METHOD FOR TREATMENT OF EXHAUST GAS
DE3008012A1 (en) * 1980-03-01 1981-09-10 Nukem Gmbh, 6450 Hanau METHOD AND DEVICE FOR REMOVING NITROSEN GASES FROM GAS MIXTURES
DE3103399A1 (en) * 1981-02-02 1982-08-05 Saarberg-Fernwärme GmbH, 6600 Saarbrücken Apparatus for producing and purifying gases and vapours

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2732580A1 (en) * 1976-08-02 1978-02-09 Mitsubishi Heavy Ind Ltd METHOD FOR TREATMENT OF EXHAUST GAS
DE3008012A1 (en) * 1980-03-01 1981-09-10 Nukem Gmbh, 6450 Hanau METHOD AND DEVICE FOR REMOVING NITROSEN GASES FROM GAS MIXTURES
DE3103399A1 (en) * 1981-02-02 1982-08-05 Saarberg-Fernwärme GmbH, 6600 Saarbrücken Apparatus for producing and purifying gases and vapours

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1986005577A1 (en) * 1985-03-16 1986-09-25 Saarbergwerke Aktiengesellschaft Smoke gas exhaust by way of a cooling tower
US4784810A (en) * 1985-03-16 1988-11-15 Saarbergwerke Aktiengesellschaft Smoke gas exhaust by way of a cooling tower
US4885011A (en) * 1985-03-16 1989-12-05 Saarbergwerke Aktiengesellschaft Cooling tower for the cooling water that drains/ from the condensor of a steam generator or the condensors/ of a plurality of steam generators
RU2453712C2 (en) * 2010-08-20 2012-06-20 Государственное образовательное учреждение высшего профессионального образования Самарский государственный технический университет Power facility combined-cycle plant
RU2704364C1 (en) * 2018-07-09 2019-10-28 федеральное государственное бюджетное образовательное учреждение высшего образования "Самарский государственный технический университет" Combined cycle gas turbine of power plant

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