CN105692558A - Method for vaporizing liquid chlorine by using heat energy produced from sulfur combustion - Google Patents

Method for vaporizing liquid chlorine by using heat energy produced from sulfur combustion Download PDF

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Publication number
CN105692558A
CN105692558A CN201510528347.8A CN201510528347A CN105692558A CN 105692558 A CN105692558 A CN 105692558A CN 201510528347 A CN201510528347 A CN 201510528347A CN 105692558 A CN105692558 A CN 105692558A
Authority
CN
China
Prior art keywords
heat
sulfur
liquid chlorine
chlorine
exchanger
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
CN201510528347.8A
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Chinese (zh)
Inventor
赵红
杨金水
张连军
张颖
左玉伟
王法
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.)
Tianjin Changlu Haijing Group Co Ltd
Original Assignee
Tianjin Changlu Haijing Group Co Ltd
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 Tianjin Changlu Haijing Group Co Ltd filed Critical Tianjin Changlu Haijing Group Co Ltd
Priority to CN201510528347.8A priority Critical patent/CN105692558A/en
Publication of CN105692558A publication Critical patent/CN105692558A/en
Pending legal-status Critical Current

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    • 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
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Abstract

The invention discloses a method for vaporizing liquid chlorine by using heat energy produced from sulfur combustion. The method includes the following steps: (i) carrying out mixed combustion of sulfur and air; (ii) carrying out heat exchange with a jacketed heat exchanger; and (iii) vaporizing the liquid chlorine. A water medium is heated by the heat energy produced from sulfur combustion in a bromine production process by an air blowing-out method, and then the heated water medium is used for vaporizing the liquid chlorine; the method fully applies the heat energy produced from the sulfur combustion, effectively reduces the energy consumption and realizes energy-saving and environmental-protection purposes.

Description

The method that liquid chlorine is vaporized by the heat energy produced with sulfur burning
Technical field
The invention belongs to the gasification process of a kind of liquid chlorine, be specifically related to the method that liquid chlorine is vaporized by the heat energy of a kind of sulfur burning generation。
Background technology
In prior art in the method for closed acid system Air blowing bromine, adopt the sulfur dioxide gas that sulfur burning is produced to participate in reaction, finally the bromide ion in sea water is replaced as molecular bromine, obtains bromine product。In process of production, the chlorine owing to participating in reaction is in a liquid state, it is necessary to so as to carry out the reaction of oxidation salt after vaporization, generally uses steam and is vaporized heating, and steam-heated method can not meet the current requirement reducing energy resource consumption。The heat energy that sulfur burning produces is not utilized, and waste in vain。
Summary of the invention
The present invention proposes to overcome the shortcoming existed in prior art, the method that its objective is to provide the heat energy that a kind of sulfur burning produces that liquid chlorine is vaporized。
The technical scheme is that
The method that liquid chlorine is vaporized by the heat energy that a kind of sulfur burning produces, comprises the following steps:
() sulfur and air carry out mixed combustion
Using drusen and air as raw material, in combustion furnace, carry out burning produce sulfur dioxide gas;
() carries out heat exchange with jacket heat-exchanger
Sulfur dioxide gas step () obtained, is passed in the pipeline with multiple jacket heat-exchangers, and sulfur dioxide gas carries out heat exchange with the medium in jacket heat-exchanger;
() vaporization liquid chlorine
Medium through heat exchange in jacket heat-exchanger is passed into chlorine water bath, the tubular heat exchanger in chlorine water bath is heated, makes the liquid chlorine in tubular heat exchanger vaporize, obtain gaseous state chlorine。
It is 300 DEG C~600 DEG C that described step () obtains sulfur dioxide gas temperature。
The plurality of jacket heat-exchanger connects in series。
Medium in described jacket heat-exchanger is water。
Described chlorine water bath is provided with temperature measurer。
The bath temperature of described chlorine water bath controls at 40 DEG C~65 DEG C。
The invention has the beneficial effects as follows:
The present invention utilizes the energy heats aqueous medium that in bromine by air blowing-out process technique, sulfur burning produces, then the method carrying out liquid chlorine vaporization with heating aqueous medium again, the heat energy that sulfur burning is produced by the method is applied fully, effectively reduce energy resource consumption, it is achieved the purpose of energy-conserving and environment-protective。
Detailed description of the invention
Method liquid chlorine being vaporized by the heat energy that present invention sulfur burning produces below in conjunction with embodiment is described in detail:
The method that liquid chlorine is vaporized by the heat energy that a kind of sulfur burning produces, comprises the following steps:
() sulfur and air carry out mixed combustion
Using drusen and air as raw material, in combustion furnace, carry out fully burning according to reaction ratio and produce sulfur dioxide gas;
() carries out heat exchange with jacket heat-exchanger
Step () obtaining the sulfur dioxide gas of 500 DEG C, is passed in the pipeline being provided with 2 series connection jacket heat exchanger, sulfur dioxide gas carries out heat exchange with the aqueous medium in jacket heat-exchanger;Sulfur dioxide gas participates in after cooling to 100 DEG C in the reduction reaction of closed acid system Air blowing bromine;
() vaporization liquid chlorine
Aqueous medium through heat exchange in jacket heat-exchanger is passed into chlorine water bath, the tubular heat exchanger in chlorine water bath is heated, makes the liquid chlorine in tubular heat exchanger vaporize, obtain gaseous state chlorine。Being provided with temperature measurer in chlorine water bath, when in water bath, temperature reaches 65 DEG C, the temperature that pipeline pump is fed back controls and stops circulation;After temperature arrives 40 DEG C, the temperature that pipeline pump is fed back controls and starts circulation, and the water in water bath is heated。
The present invention utilizes the energy heats aqueous medium that in bromine by air blowing-out process technique, sulfur burning produces, then the method carrying out liquid chlorine vaporization with heating aqueous medium again, the heat energy that sulfur burning is produced by the method is applied fully, effectively reduce energy resource consumption, it is achieved the purpose of energy-conserving and environment-protective。

Claims (3)

1. the method that liquid chlorine is vaporized by the heat energy produced with sulfur burning, it is characterised in that: comprise the following steps:
() sulfur and air carry out mixed combustion
Using drusen and air as raw material, in combustion furnace, carry out burning produce sulfur dioxide gas;
() carries out heat exchange with jacket heat-exchanger
Sulfur dioxide gas step () obtained, is passed in the pipeline with multiple jacket heat-exchangers, and sulfur dioxide gas carries out heat exchange with the aqueous medium in jacket heat-exchanger;
() vaporization liquid chlorine
Aqueous medium through heat exchange in jacket heat-exchanger is passed into chlorine water bath, tubular heat exchanger in chlorine water bath is heated, the bath temperature making chlorine water bath controls at 40 DEG C ~ 65 DEG C, the liquid chlorine vaporization in tubular heat exchanger, obtains gaseous state chlorine。
2. the method that liquid chlorine is vaporized by the heat energy that a kind of sulfur burning according to claim 1 produces, it is characterised in that: it is 300 DEG C ~ 600 DEG C that described step () obtains sulfur dioxide gas temperature。
3. the method that liquid chlorine is vaporized by the heat energy that a kind of sulfur burning according to claim 1 produces, it is characterised in that: the plurality of jacket heat-exchanger connects in series。
CN201510528347.8A 2015-08-26 2015-08-26 Method for vaporizing liquid chlorine by using heat energy produced from sulfur combustion Pending CN105692558A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510528347.8A CN105692558A (en) 2015-08-26 2015-08-26 Method for vaporizing liquid chlorine by using heat energy produced from sulfur combustion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510528347.8A CN105692558A (en) 2015-08-26 2015-08-26 Method for vaporizing liquid chlorine by using heat energy produced from sulfur combustion

Publications (1)

Publication Number Publication Date
CN105692558A true CN105692558A (en) 2016-06-22

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510528347.8A Pending CN105692558A (en) 2015-08-26 2015-08-26 Method for vaporizing liquid chlorine by using heat energy produced from sulfur combustion

Country Status (1)

Country Link
CN (1) CN105692558A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101045528A (en) * 2007-04-24 2007-10-03 天津长芦海晶集团有限公司 Technology for coarse bromine purifying using hydrobomic acid enriched liquid
CN101104532A (en) * 2007-04-24 2008-01-16 天津长芦海晶集团有限公司 Technique for producing refined salt from salt production waste liquid
JP2013086984A (en) * 2011-10-14 2013-05-13 Taiheiyo Cement Corp Treatment method of chlorine bypass exhaust gas

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101045528A (en) * 2007-04-24 2007-10-03 天津长芦海晶集团有限公司 Technology for coarse bromine purifying using hydrobomic acid enriched liquid
CN101104532A (en) * 2007-04-24 2008-01-16 天津长芦海晶集团有限公司 Technique for producing refined salt from salt production waste liquid
JP2013086984A (en) * 2011-10-14 2013-05-13 Taiheiyo Cement Corp Treatment method of chlorine bypass exhaust gas

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
王法: "溴素生产中节能降耗的改进", 《创新技术》 *

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Application publication date: 20160622