YU44692A - DRY TYPE APPARATUS AND PROCEDURE FOR EXHAUST GAS DESULFURIZATION - Google Patents

DRY TYPE APPARATUS AND PROCEDURE FOR EXHAUST GAS DESULFURIZATION

Info

Publication number
YU44692A
YU44692A YU44692A YU44692A YU44692A YU 44692 A YU44692 A YU 44692A YU 44692 A YU44692 A YU 44692A YU 44692 A YU44692 A YU 44692A YU 44692 A YU44692 A YU 44692A
Authority
YU
Yugoslavia
Prior art keywords
exhaust gas
desulfurization
desulfurizing agent
exhaust
dry type
Prior art date
Application number
YU44692A
Other languages
Serbo-Croatian (sh)
Other versions
YU48360B (en
Inventor
H. Kikkawa
Y. Nishimura
H. Kaku
K. Yokoyama
H. Nosaka
F. Nakajima
S. Takamoto
T. Kurumaji
T. Hashimoto
H. Ishizaka
T. Nishimura
T. Nosaka
Original Assignee
Babcock-Hitachi Kabushiki Kaisha
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 JP27063191A external-priority patent/JP3308286B2/en
Application filed by Babcock-Hitachi Kabushiki Kaisha filed Critical Babcock-Hitachi Kabushiki Kaisha
Publication of YU44692A publication Critical patent/YU44692A/en
Publication of YU48360B publication Critical patent/YU48360B/en

Links

Classifications

    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Landscapes

  • Treating Waste Gases (AREA)

Abstract

UREDJAJ I POSTUPAK SUVOG TIPA ZA DESULFURIZACIU IZDUVNOG GASA, sprečava taloženje unutar uredjaja i sprečava koroziju uredjaja, a ipak održava visoko dejstvo desulfurizacije. Kod uredjaja suvog tipa za desulfurizaciju izduvnog gasa za uklanjanje sumpornih oksida iz izduvnog gasa, sredstvo za desulfurizaciju kao što je gašeni kreč, dovodi se u ložište (1) uredjaja za sagorevanje ili u izduvni gasovod (6, 13), a voda se uprskava u stub (4) za desulfurizaciju na njegovom ulazu. Na pola puta u smeru tokagasa predvidjen je unutar stuba (4) za desulfurizaciju deo (16) za stvaranje vrtloga, tako da se stvaraju zone visoke relativne vlažnosti unutar stuba (4) za desulfurizaciju. Sredstvo za desulfurizaciju se umešava u svaku od zona visoke relativne vlažnosti. Sredstvo za desulfurizaciju se dovodi u zonu izduvnog gasa čija je temperatura niža od 200В°C, a sredstvo za desulfurizaciju koje je reagovalo sa sumpornim oksidima iz izduvnog gasa skuplja se pomoću uredjaja (8) za skupljanje praha, a zatim se ove zaustavljene čestice pnovo dovode u deo izduvnog cevovoda (13) gde je temperatura od 500 do 900В°C.DEVICE AND DRY TYPE PROCESS FOR EXHAUST GAS DESULFURIZATION, prevents deposition inside the device and prevents corrosion of the device, while maintaining a high desulfurization effect. In the case of a dry exhaust desulfurization device for removing sulfur oxides from the exhaust gas, a desulfurizing agent such as slaked lime is fed to the combustion chamber (1) or to the exhaust pipe (6, 13) and the water is sprayed into a desulfurization column (4) at its inlet. Halfway in the direction of the tokagas, a vortex-forming part (16) is provided inside the desulfurization column (4), so that zones of high relative humidity are created inside the desulfurization column (4). The desulfurizing agent is mixed into each of the zones of high relative humidity. The desulfurizing agent is introduced into the exhaust gas zone whose temperature is lower than 200V ° C, and the desulfurizing agent which has reacted with sulfur oxides from the exhaust gas is collected by means of a powder collecting device (8), and then these stopped particles are brought back. in the part of the exhaust pipeline (13) where the temperature is from 500 to 900V ° C.

YU44692A 1991-04-24 1992-04-24 DRY TYPE APPARATUS AND PROCEDURE FOR EXHAUST GAS DESULFURIZATION YU48360B (en)

Applications Claiming Priority (7)

Application Number Priority Date Filing Date Title
JP9387891 1991-04-24
JP17708491 1991-07-18
JP21505991 1991-08-27
JP21775591 1991-08-29
JP26248791 1991-10-11
JP26248691 1991-10-11
JP27063191A JP3308286B2 (en) 1990-11-10 1991-10-18 Dry flue gas desulfurization apparatus and method

Publications (2)

Publication Number Publication Date
YU44692A true YU44692A (en) 1995-03-27
YU48360B YU48360B (en) 1998-07-10

Family

ID=27565536

Family Applications (1)

Application Number Title Priority Date Filing Date
YU44692A YU48360B (en) 1991-04-24 1992-04-24 DRY TYPE APPARATUS AND PROCEDURE FOR EXHAUST GAS DESULFURIZATION

Country Status (5)

Country Link
CN (1) CN1041994C (en)
CZ (1) CZ290636B6 (en)
ID (1) ID1036B (en)
SK (1) SK124392A3 (en)
YU (1) YU48360B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102430449A (en) * 2011-12-14 2012-05-02 江苏科行环境工程技术有限公司 Water spray humidifying device in horizontal roller mill
CN105664688A (en) * 2016-04-15 2016-06-15 北京宜泽环保科技有限责任公司 Flue gas comprehensive denitration treatment system and treatment technology
WO2018184702A1 (en) * 2017-04-07 2018-10-11 S.A. Lhoist Recherche Et Developpement Process for flue gas treatment and products for use in said process
CN114011234B (en) * 2021-11-10 2024-04-23 山东鲁碧建材有限公司 Dry desulfurization method for treating low-temperature flue gas

Also Published As

Publication number Publication date
CN1041994C (en) 1999-02-10
CZ290636B6 (en) 2002-09-11
CN1066803A (en) 1992-12-09
ID1036B (en) 1996-10-24
CZ9201243A3 (en) 2002-05-15
YU48360B (en) 1998-07-10
SK124392A3 (en) 1993-12-08

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