JPS5835919U - Dry desulfurization equipment - Google Patents

Dry desulfurization equipment

Info

Publication number
JPS5835919U
JPS5835919U JP12791781U JP12791781U JPS5835919U JP S5835919 U JPS5835919 U JP S5835919U JP 12791781 U JP12791781 U JP 12791781U JP 12791781 U JP12791781 U JP 12791781U JP S5835919 U JPS5835919 U JP S5835919U
Authority
JP
Japan
Prior art keywords
heat exchanger
sulfur dioxide
dioxide gas
indirect contact
heat
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.)
Pending
Application number
JP12791781U
Other languages
Japanese (ja)
Inventor
野沢 滋
西村 士
修 神田
晃三 小幡
Original Assignee
バブコツク日立株式会社
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 バブコツク日立株式会社 filed Critical バブコツク日立株式会社
Priority to JP12791781U priority Critical patent/JPS5835919U/en
Publication of JPS5835919U publication Critical patent/JPS5835919U/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の乾式脱硫装置の系統図、第2図は乾式脱
硫装置に使用される炭素系還元剤のSO2還元特性を説
明する図、第3図はこの考案の実施例を説明する系統図
である。 11、 16. 19・・・導管、17・・・燃焼器、
18・・・熱交換器。 −第1図 第2図
Figure 1 is a system diagram of a conventional dry desulfurization equipment, Figure 2 is a diagram explaining the SO2 reduction characteristics of the carbon-based reducing agent used in the dry desulfurization equipment, and Figure 3 is a diagram explaining an embodiment of this invention. It is a diagram. 11, 16. 19... conduit, 17... combustor,
18... Heat exchanger. -Figure 1Figure 2

Claims (4)

【実用新案登録請求の範囲】[Scope of utility model registration request] (1)排ガスを粒状炭素系吸着剤と接触させて含有亜硫
酸ガスを吸着除去する吸着装置と、亜硫酸ガスを吸着し
た炭素系吸着剤を加熱して亜硫酸ガスを追い出すととも
に炭素系吸着剤を再生する脱離装置と、脱離装置から追
い出された亜硫酸ガスを炭素系還元剤と接触させて硫黄
に還元する還元装置とを備えた乾式脱硫装置において、
上記脱離装置と還元装置の間に、脱離装置から追い出さ
れた亜硫酸ガスを前記還元装置における還元反応開始温
度まで上昇させるための間接接触式熱交換器を設けたこ
とを特徴とする乾式脱硫装置。
(1) An adsorption device that brings exhaust gas into contact with a granular carbon-based adsorbent to adsorb and remove the sulfur dioxide gas contained therein, and heats the carbon-based adsorbent that has adsorbed sulfur dioxide gas to expel the sulfur dioxide gas and regenerate the carbon-based adsorbent. In a dry desulfurization device equipped with a desorption device and a reduction device that brings sulfur dioxide gas expelled from the desorption device into contact with a carbon-based reducing agent to reduce it to sulfur,
Dry desulfurization characterized in that an indirect contact heat exchanger is provided between the desorption device and the reduction device to raise the sulfur dioxide gas expelled from the desorption device to the reduction reaction starting temperature in the reduction device. Device.
(2)実用新案登録請求の範囲第1項において、間接接
触式熱交換器の熱源は還元装置から排出される還元剤残
渣の燃焼熱であることを特徴とする乾式脱硫装置。
(2) Scope of Utility Model Registration The dry desulfurization device according to claim 1, characterized in that the heat source of the indirect contact heat exchanger is the combustion heat of reducing agent residue discharged from the reducing device.
(3)  実用新案登録請求の範囲第1項において、間
接接触式熱交換器の熱源は、吸着装置または脱離装置か
ら分離除去される微粒状吸着剤の燃焼熱であることを特
徴とする乾式脱硫装置。
(3) In claim 1 of the utility model registration claim, the heat source of the indirect contact heat exchanger is a dry type heat exchanger characterized in that the heat source of the indirect contact heat exchanger is the combustion heat of fine particulate adsorbent separated and removed from an adsorption device or a desorption device. Desulfurization equipment.
(4)実用新案登録請求の範囲第1項において、間接接
触式熱交換器の熱源は、吸着装置から排出される亜硫酸
ガス吸着除去後の清浄排ガスの処理用に設けられる集じ
ん装置で捕集される微粒状吸着剤の燃焼熱であることを
特徴とする乾式(5)実用新案登録請求の範囲第1項に
おいて、間接接触式熱交換器の熱源は、還元装置から生
成するS02の有する排熱であることを特徴とする乾式
脱硫装置。
(4) Scope of Utility Model Registration Claims In paragraph 1, the heat source of the indirect contact heat exchanger is collected by a dust collection device provided for processing clean exhaust gas after adsorption and removal of sulfur dioxide gas discharged from an adsorption device. In Claim 1, the heat source of the indirect contact heat exchanger is the heat of combustion of the particulate adsorbent produced by the reduction device. Dry desulfurization equipment characterized by heat.
JP12791781U 1981-08-31 1981-08-31 Dry desulfurization equipment Pending JPS5835919U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12791781U JPS5835919U (en) 1981-08-31 1981-08-31 Dry desulfurization equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12791781U JPS5835919U (en) 1981-08-31 1981-08-31 Dry desulfurization equipment

Publications (1)

Publication Number Publication Date
JPS5835919U true JPS5835919U (en) 1983-03-09

Family

ID=29921631

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12791781U Pending JPS5835919U (en) 1981-08-31 1981-08-31 Dry desulfurization equipment

Country Status (1)

Country Link
JP (1) JPS5835919U (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56163734A (en) * 1980-05-23 1981-12-16 Mitsubishi Heavy Ind Ltd Treatment for waste gas of combustion

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56163734A (en) * 1980-05-23 1981-12-16 Mitsubishi Heavy Ind Ltd Treatment for waste gas of combustion

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