CN207487452U - For the heat-exchanger rig of ClO 2 solution heating - Google Patents

For the heat-exchanger rig of ClO 2 solution heating Download PDF

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Publication number
CN207487452U
CN207487452U CN201721270865.5U CN201721270865U CN207487452U CN 207487452 U CN207487452 U CN 207487452U CN 201721270865 U CN201721270865 U CN 201721270865U CN 207487452 U CN207487452 U CN 207487452U
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China
Prior art keywords
clo
solution
filtrate
temperature
heat
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CN201721270865.5U
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Chinese (zh)
Inventor
詹磊
徐萃声
黄丙贵
刘良青
班飞
李忠平
谭浪
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Anhui Boshike Environmental Protection Technology Co ltd
Guangxi Boshike Environmental Technology Co ltd
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Guangxi Bossco Environmental Protection Technology Co Ltd
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Abstract

The utility model discloses a kind of heat-exchanger rigs for ClO 2 solution heating, it includes tubular heat exchanger, the continuous tubulation of multistage is equipped in the housing of tubular heat exchanger, shell side and tube side are formed in housing, the inlet and outlet piping body contact journey of ClO 2 solution, the inlet and outlet piping take over journey of filtrate is equipped with temperature transmitter and pressure relief device on the outlet conduit of ClO 2 solution, temperature control valve (TCV) is equipped on the inlet pipeline of filtrate.Using the utility model, filtrate after tubulation inner wall forms incrustation, cleared up by the conveniently physical cleaning mode that can be selected;Can control the ClO 2 solution temperature after heating by the temperature control device being configured, the pressure relief device of installation can ensure that ClO 2 solution pressure in safe range, avoids safety accident in device in the range of technological requirement.

Description

For the heat-exchanger rig of ClO 2 solution heating
Technical field
It is specifically a kind of to be heated for ClO 2 solution the utility model is related to chlorine dioxide heating equipment technical field Heat-exchanger rig.
Technical background
Chlorine dioxide is extremely strong oxidant, can corrode all metals in addition to platinum, tantalum and titanium.In normal temperature and pressure Under, chlorine dioxide is orange-yellow gas, has the irritation pungent similar to chlorine and ozone mixture, and boiling point is 11 DEG C, freezing point It is -59 DEG C.Gaseous chlorine dioxide is unstable, and chlorine dioxide gas concentration cannot be too high, and partial pressure will be controlled in 100mmHg (absolute pressure) Hereinafter, it even explodes if partial pressure can be decomposed more than 100mmHg.Aqueous solution of chlorine dioxide is then relatively stable, and aqueous temperature is got over Low chlorine dioxide dissolving degree is higher, more stable.Association with pulp bleaching production line needs the higher ClO 2 solution of concentration, therefore prepares ClO 2 solution temperature it is relatively low (generally 10-14 DEG C), and ClO 2 bleaching technological requirement reaction temperature is generally 70 DEG C or so, steam consumption is bleached to save, needs to carry out using the waste heat of filtrate before ClO 2 solution enters bleaching process Heating.
Since ClO 2 solution has strong corrosive, and temperature is excessively high that chlorine dioxide partial pressure can be caused high, Yi Fa Therefore raw safety accident, is badly in need of manufacture one kind and is not only resistant to chlorine dioxide corrosion, but also can effectively control ClO 2 solution after heating Temperature ensures heat-exchanger rig of the chlorine dioxide pressure in safe range after heating.
Utility model content
The technical problem to be solved by the utility model is to provide it is a kind of for ClO 2 solution heating heat-exchanger rig, The heat-exchanger rig had not only been resistant to chlorine dioxide corrosion, incrustation easy to clean, but also can effectively control the ClO 2 solution temperature after heating Degree ensures that ClO 2 solution pressure is in safe range in device.
The utility model adopts the following technical solution solves above-mentioned technical problem:
The utility model is used for the heat-exchanger rig of ClO 2 solution heating, it includes tubular heat exchanger, tubular heat exchanger Housing in be equipped with the continuous tubulation of multistage, shell side and tube side, the inlet and outlet piping connection shell of ClO 2 solution are formed in housing Journey, the inlet and outlet piping of filtrate connect tube side, temperature transmitter and pressure relief device are equipped on the outlet conduit of ClO 2 solution, Temperature control valve (TCV) is installed on the inlet pipeline of filtrate.
Housing, the tubulation of the tubular heat exchanger are made of titanium.
The utility model device has the advantages that:
1) tubulation for the heat-exchanger rig that the utility model uses and housing are made of titanium, anti-chlorine dioxide corrosion It can be strong;
2) shell side of the tubular heat exchanger of the utility model walks ClO 2 solution, and tube side walks filtrate, and filtrate is in tubulation Conveniently physical cleaning mode can be selected in inner wall incrustation, when cleaning;
3) a set of temperature control device is configured in the utility model heat-exchanger rig, can effectively control the ClO 2 solution temperature after heating Degree is in the range of technological requirement;
4) a set of pressure relief device is configured as emergency service in the utility model heat-exchanger rig, when ClO 2 solution temperature tune Valve or temperature transmitter failure are saved, when causing ClO 2 solution temperature after heating excessively high, and then enabling pressure superelevation in device Timely pressure release, avoids safety accident.
Description of the drawings
Fig. 1 is structure diagram of the utility model for the heat-exchanger rig of ClO 2 solution heating.
In figure:1- tubular heat exchangers, 2- temperature control valve (TCV)s, 3- temperature transmitters, 4- pressure relief devices, 5- chlorine dioxide feed liquors Pipe, 6- chlorine dioxide outlet tubes, 7- filtrate inlet tubes, 8- filtrate outlet tubes.
Specific embodiment
As shown in Figure 1, the utility model is used for the heat-exchanger rig of ClO 2 solution heating, including tubular heat exchanger 1, temperature Spend regulating valve 2, temperature transmitter 3, pressure relief device 4, chlorine dioxide inlet tube 5, chlorine dioxide outlet tube 6, filtrate inlet tube 7, Filtrate outlet tube 8.The continuous tubulation of multistage is equipped in the housing of tubular heat exchanger 1, shell side and tube side, titanium dioxide are formed in housing Chlorine inlet tube 5 and chlorine dioxide outlet tube 6 are connected with shell side, and filtrate inlet tube 7 and filtrate outlet tube 8 are connected with tube side, Temperature transmitter 3 and pressure relief device 4 are installed, filtrate inlet tube 7 is equipped with temperature control valve (TCV) 2 on chlorine dioxide outlet tube 6.
During work, low temperature ClO 2 solution (temperature is 10-14 DEG C) enters tubular heat exchanger from chlorine dioxide inlet tube 5 1 shell side, filtrate (about 70 DEG C) enter the tube side of tubular heat exchanger 1 from filtrate inlet tube 7, and ClO 2 solution is being arranged with filtrate It exchanges heat in heat exchange of heat pipe 1.ClO 2 solution after heat exchange enters bleaching process through chlorine dioxide outlet tube 6, and filtrate is then through filter Liquid outlet tube 8 drains into trench.
In device operational process, the ClO 2 solution temperature after heat exchange passes through 2 groups of temperature transmitter 3 and temperature control valve (TCV) Into temperature control device be monitored, control, the ClO 2 solution temperature stabilization after heat exchange can be made in the range of technological requirement.If There is the temperature control valve (TCV) of ClO 2 solution or temperature transmitter failure, cause ClO 2 solution excessively high, and make in device During pressure superelevation, pressure relief device 4 will releasing pressure automatically, it is ensured that system safety.
Housing, the tubulation for the tubular heat exchanger 1 that the utility model uses are titanium, and resistance to chlorine dioxide corrosion is strong.When After the tubulation inner wall incrustation of tubular heat exchanger 1, both ends end socket is split out, directly tubulation is cleaned with giant, both facilitated It is again quick.

Claims (2)

1. for the heat-exchanger rig of ClO 2 solution heating, which is characterized in that it includes tubular heat exchanger, tubular heat exchanger The continuous tubulation of multistage is equipped in housing, shell side and tube side, the inlet and outlet piping body contact journey of ClO 2 solution, filter are formed in housing The inlet and outlet piping take over journey of liquid is equipped with temperature transmitter and pressure relief device on the outlet conduit of ClO 2 solution, filtrate Temperature control valve (TCV) is installed on inlet pipeline.
2. according to claim 1 for the heat-exchanger rig of ClO 2 solution heating, which is characterized in that the tubulation heat exchange Housing, the tubulation of device are made of titanium.
CN201721270865.5U 2017-09-29 2017-09-29 For the heat-exchanger rig of ClO 2 solution heating Active CN207487452U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721270865.5U CN207487452U (en) 2017-09-29 2017-09-29 For the heat-exchanger rig of ClO 2 solution heating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721270865.5U CN207487452U (en) 2017-09-29 2017-09-29 For the heat-exchanger rig of ClO 2 solution heating

Publications (1)

Publication Number Publication Date
CN207487452U true CN207487452U (en) 2018-06-12

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721270865.5U Active CN207487452U (en) 2017-09-29 2017-09-29 For the heat-exchanger rig of ClO 2 solution heating

Country Status (1)

Country Link
CN (1) CN207487452U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110579120A (en) * 2019-08-30 2019-12-17 安徽池州九华发电有限公司 Shell-and-tube heat exchanger and control method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110579120A (en) * 2019-08-30 2019-12-17 安徽池州九华发电有限公司 Shell-and-tube heat exchanger and control method thereof
CN110579120B (en) * 2019-08-30 2020-11-24 安徽池州九华发电有限公司 Shell-and-tube heat exchanger and control method thereof

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Address after: 242300 intersection of Dongcheng Avenue and Dongcheng Road, heli Park, Ningguo Economic and Technological Development Zone, Ningguo City, Xuancheng City, Anhui Province

Patentee after: Anhui Boshike Environmental Protection Technology Co.,Ltd.

Country or region after: China

Address before: 530007 12 Kexing Road, hi tech Zone, Nanning, the Guangxi Zhuang Autonomous Region

Patentee before: GUANGXI BOSSCO ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd.

Country or region before: China

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Effective date of registration: 20240524

Address after: 242300 intersection of Dongcheng Avenue and Dongcheng Road, heli Park, Ningguo Economic and Technological Development Zone, Ningguo City, Xuancheng City, Anhui Province

Patentee after: Anhui Boshike Environmental Protection Technology Co.,Ltd.

Country or region after: China

Patentee after: Guangxi Boshike Environmental Technology Co.,Ltd.

Address before: 242300 intersection of Dongcheng Avenue and Dongcheng Road, heli Park, Ningguo Economic and Technological Development Zone, Ningguo City, Xuancheng City, Anhui Province

Patentee before: Anhui Boshike Environmental Protection Technology Co.,Ltd.

Country or region before: China

TR01 Transfer of patent right