CN203577603U - Chlorine gas treatment device - Google Patents
Chlorine gas treatment device Download PDFInfo
- Publication number
- CN203577603U CN203577603U CN201320591042.8U CN201320591042U CN203577603U CN 203577603 U CN203577603 U CN 203577603U CN 201320591042 U CN201320591042 U CN 201320591042U CN 203577603 U CN203577603 U CN 203577603U
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- China
- Prior art keywords
- chlorine
- gas
- treatment device
- outlet
- liquid
- 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.)
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- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 238000011282 treatment Methods 0.000 title claims abstract description 27
- 239000007788 liquid Substances 0.000 claims abstract description 53
- 239000000203 mixture Substances 0.000 claims abstract description 21
- 239000006096 absorbing agent Substances 0.000 claims abstract description 17
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 84
- 239000000460 chlorine Substances 0.000 claims description 77
- 229910052801 chlorine Inorganic materials 0.000 claims description 77
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 74
- 239000003513 alkali Substances 0.000 claims description 49
- 239000012528 membrane Substances 0.000 claims description 16
- 239000004743 Polypropylene Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- -1 polypropylene Polymers 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- 239000007921 spray Substances 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 4
- 239000010865 sewage Substances 0.000 abstract description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract description 6
- 239000011780 sodium chloride Substances 0.000 abstract description 6
- 238000003915 air pollution Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 21
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001804 chlorine Chemical class 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Degasification And Air Bubble Elimination (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a chlorine gas treatment device. The chlorine gas treatment device comprises a chlorine gas separator which is provided with a liquid inlet for enabling a gas-liquid mixed liquid to enter and a gas outlet for outputting chlorine gas, and a chlorine gas absorber of which a gas inlet is connected with the gas outlet of the chlorine gas separator for absorbing chlorine gas output by the chlorine gas separator, wherein the chlorine gas absorber comprises an alkaline liquid tank for containing an alkaline liquid and a jet flow structure connected with the alkaline liquid tank for mixing chlorine gas and the alkaline liquid and injecting the mixture into the alkaline liquid, and the gas inlet is an entrance arranged on the jet flow structure. The chlorine gas treatment device has simple structure and convenience for use, and can separate out chlorine gas in a gas-liquid mixed liquid generated by electrochemical treatment of saline sewage and completely absorb the chlorine gas, thereby reducing air pollution and improving the safety.
Description
Technical field
The utility model relates to technical field of waste gas treatment, relates in particular to the device that a kind of chlorine that saline sewage is produced after electrochemical treatments is processed.
Background technology
Catalytic oxidation sewage disposal technology, owing to not adding medicine, does not produce new solid contaminant, is often called as environmentally friendly new technology, but, in processing the process of saline sewage, but can produce free chlorine, both pollute air, worsened working environment, or a unsafe factor.
Summary of the invention
For overcoming above-mentioned the deficiencies in the prior art, the utility model provides a kind of chlorine treatment device, it is simple in structure, easy to use, chlorine in the gas and liquid mixture that saline sewage can be produced after electrochemical treatments is separated, and absorb completely, therefore reduce the pollution to air, and improved security.
For realizing above-mentioned purpose of the present utility model, chlorine treatment device of the present utility model comprises: have for making inlet that gas and liquid mixture enters and for exporting the chlorine separator of the gas outlet of chlorine; Its air inlet is connected with the gas outlet of chlorine separator for absorbing the chlorine gas absorber of chlorine separator output chlorine; Wherein, described chlorine gas absorber comprises the alkali liquid tank for splendid attire alkali lye, and tank connected for described chlorine being mixed with described alkali lye and mixture being injected to the fluidic architecture in described alkali lye with alkali lye; Wherein, described air inlet is the entrance being arranged on described fluidic architecture.
Wherein, described chlorine gas absorber also comprises: its entrance is communicated with described alkali liquid tank and for making the NaOH solution circulating pump of described alkali lye circulation, its outlet is communicated with another entrance of described fluidic architecture; The mixed liquor conduit that its entrance is communicated with the outlet of described fluidic architecture; The mixed liquor jet member that its entrance is communicated with the outlet of described mixed liquor conduit, it has for being immersed in the outlet in described alkali lye.
Wherein, described chlorine separator also comprises: Membrane Separator Cylinder for CFB Boiler, and described gas outlet is opened in its top, and described inlet is opened in its sidewall; Be arranged on the separated umbrella in Membrane Separator Cylinder for CFB Boiler, for by the chlorine of gas and liquid mixture and fluid separation applications; The liquid outlet that is opened in Membrane Separator Cylinder for CFB Boiler bottom, the liquid in described gas and liquid mixture flows into settling tank from liquid outlet.
Wherein, described fluidic architecture is jet pump.
Wherein, described mixed liquor jet member is four-way pipe.
Preferably, every of described four-way pipe pipe is provided with a plurality of spray apertures.
Preferably, described alkali liquid tank is made by polypropylene material.
Preferably, described Membrane Separator Cylinder for CFB Boiler is made by polypropylene material.
Wherein, a described entrance of described fluidic architecture is communicated with the gas outlet of described chlorine separator by chlorine conduit.
Compared with prior art, chlorine treatment device tool of the present utility model has the following advantages:
1) chlorine treatment device of the present utility model comprises chlorine separator and chlorine gas absorber, chlorine in the gas and liquid mixture that chlorine separator produces saline sewage after electrochemical treatments is separated, and chlorine gas absorber fully absorbs this chlorine, thereby can not produce free chlorine, therefore can contaminated air, eliminated unsafe factor, and simple in structure, easy to use;
2) chlorine separator of the present utility model has separated umbrella, and it guarantees the chlorine in gas-liquid mixture fully separated with liquid;
3) chlorine gas absorber of the present utility model has fluidic architecture, and it can be guaranteed that chlorine is without leakage, and be absorbed completely by alkali lye importing to alkali liquid tank bottom from the stress-free chlorine of chlorine separator output, has eliminated the pollution to air;
4) the utlity model has mixed liquor jet member, it is the four-way pipe with a plurality of spray apertures, it is immersed in alkali lye, each outlet that makes chlorine pass through four-way pipe fully mixes with alkali lye and by alkali liquor absorption, guarantee that chlorine is without leakage, eliminate the pollution to air, and avoided the generation of clogging.
Below in conjunction with accompanying drawing, the utility model is described in more detail.
Accompanying drawing explanation
Fig. 1 is the structural representation of chlorine treatment device of the present utility model;
Fig. 2 is the structural representation of chlorine gas absorber of the present utility model;
Fig. 3 is the top view of chlorine gas absorber shown in Fig. 2;
Fig. 4 is that the A-A shown in Fig. 3 is to cutaway view;
Fig. 5 is the structural representation of mixed liquor jet member of the present utility model;
Fig. 6 is the structural representation of chlorine separator of the present utility model;
Fig. 7 is that the B-B of the separator of chlorine shown in Fig. 6 is to cutaway view.
Description of reference numerals: 1-chlorine separator; 11-gas outlet; 12-Membrane Separator Cylinder for CFB Boiler; 13-inlet; The separated umbrella of 14-; 15-liquid outlet; 2-chlorine gas absorber; 22-alkali liquid tank; 23-fluidic architecture; 24-NaOH solution circulating pump; 25-mixed liquor conduit; 26-mixed liquor jet member; 26a-spray apertures; 3-chlorine conduit.
The specific embodiment
As shown in Figure 1, chlorine treatment device of the present utility model comprises: have for making inlet 13 that gas and liquid mixture enters and for exporting the chlorine separator 1 of the gas outlet 11 of chlorine; Its air inlet is connected with the gas outlet 11 of chlorine separator 1 for absorbing the chlorine gas absorber 2 of chlorine separator 1 output chlorine; Wherein, chlorine gas absorber 2 comprises the alkali liquid tank 22 for splendid attire alkali lye, and be connected with alkali liquid tank 22 for chlorine being mixed with alkali lye and mixture being injected to the fluidic architecture 23 in alkali lye; Wherein, air inlet is the entrance being arranged on fluidic architecture 23.
Wherein, as shown in Fig. 2-Fig. 4, chlorine gas absorber 2 of the present utility model, except alkali liquid tank 22 and fluidic architecture 23, also comprises: its entrance is communicated with alkali liquid tank 22 and for making the NaOH solution circulating pump 24 of alkali lye circulation, its outlet is communicated with another entrance of fluidic architecture 23; The mixed liquor conduit 25 that its entrance is communicated with the outlet of fluidic architecture 23; The mixed liquor jet member 26 that its entrance is communicated with the outlet of mixed liquor conduit 25, it has for being immersed in the outlet in alkali lye.
Concrete, in alkali liquid tank 22 of the present utility model, fill the alkali lye that concentration is 15%---20%.And as shown in Figure 5, fluidic architecture 23 is jet pump, it has two entrances and an outlet, an one entrance is communicated with the gas outlet 11 of chlorine separator 1 by chlorine conduit 3, its another entrance is connected with the outlet of NaOH solution circulating pump 24, and its outlet connects a mixed liquor conduit 25, thereby the mixture producing after chlorine is mixed with alkali lye is transported in the mixed liquor jet member 26 being communicated with mixed liquor conduit 25, and mixed liquor jet member 26 is four-way pipe, on every pipe of four-way pipe, be provided with a plurality of spray apertures 26a, and every Guan Jun is immersed in alkali lye, thereby described mixture is infused in alkali lye completely, chlorine is absorbed by alkali lye completely, thereby can not produce nomadic nitrogen, can contaminated air, eliminated unsafe factor.
And, on every pipe of four-way pipe, being equipped with a plurality of spray apertures, four-way pipe is immersed in alkali lye, making chlorine pass through its each outlet fully mixes with alkali lye and by alkali liquor absorption, guarantee that chlorine is without leakage, eliminated the pollution to air, and avoided the generation of clogging.
Preferably, alkali liquid tank 22, mixed liquor conduit 25 are made by polypropylene material.
And as shown in Figure 6, Figure 7, chlorine separator 1 of the present utility model, except inlet 13 and gas outlet 11, also comprises: Membrane Separator Cylinder for CFB Boiler 12, and gas outlet 11 is opened in its top, and inlet 13 is opened in its sidewall; Be arranged on the separated umbrella 14 in Membrane Separator Cylinder for CFB Boiler 12, for by the chlorine of gas and liquid mixture and fluid separation applications; Be opened in the liquid outlet 15 of Membrane Separator Cylinder for CFB Boiler 12 bottoms, the liquid that gas and liquid mixture produces after separated umbrella 14 separation is from the dirty settling tank that enters of liquid outlet 15.
Preferably, Membrane Separator Cylinder for CFB Boiler 12 is made by polypropylene material.
Chlorine treatment device of the present utility model, the gas and liquid mixture of exporting through apparatus for electrochemical treatment processing saline sewage is input in Membrane Separator Cylinder for CFB Boiler 12 from the inlet 13 of Membrane Separator Cylinder for CFB Boiler 12, and by separated umbrella 14 by the chlorine in gas and liquid mixture and fluid separation applications, chlorine after separation is flowed out from the gas outlet 11 of Membrane Separator Cylinder for CFB Boiler 12, and by chlorine conduit 3, chlorine is outputed to a described porch of fluidic architecture 23.
Because the chlorine of a described porch that outputs to fluidic architecture 23 is without pressure, the utility model is installed a NaOH solution circulating pump 24 on alkali liquid tank 22, and the entrance of NaOH solution circulating pump 24 is communicated with the alkali lye in alkali liquid tank 22, and described another entrance of fluidic architecture is communicated with the outlet of NaOH solution circulating pump 24, when NaOH solution circulating pump 24 work, the chlorine that makes on the one hand to output to a described porch of fluidic architecture 23 is inhaled in fluidic architecture 23, on the other hand the alkali lye in alkali liquid tank 22 is outputed in fluidic architecture 23 by described another entrance, and the mixture that mixes rear formation is outputed in mixed liquor conduit 25 from the outlet of fluidic architecture, thereby by mixed liquor conduit 25, chlorine is absorbed by alkali lye completely.
Although above the utility model is explained in detail; but be not limited to this; the interior perhaps principle that those skilled in the art can record according to the utility model is modified; therefore the various modifications that, all interior perhaps principles of recording according to the utility model are carried out all should be understood to include in protection domain of the present utility model.
Claims (9)
1. a chlorine treatment device, is characterized in that, comprising:
There is inlet (13) for gas and liquid mixture is entered and for exporting the chlorine separator (1) of the gas outlet (11) of chlorine;
Its air inlet is connected the chlorine gas absorber (2) that is used for absorbing chlorine separator (1) output chlorine with the gas outlet (11) of chlorine separator (1);
Wherein, described chlorine gas absorber (2) comprises the alkali liquid tank (22) for splendid attire alkali lye, and be connected with alkali liquid tank (22) for described chlorine being mixed with described alkali lye and mixture being injected to the fluidic architecture (23) in described alkali lye;
Wherein, described air inlet is for being arranged at an entrance on described fluidic architecture (23).
2. chlorine treatment device according to claim 1, is characterized in that, described chlorine gas absorber (2) also comprises:
Its entrance is communicated with described alkali liquid tank (22) and for making the NaOH solution circulating pump (24) of described alkali lye circulation, its outlet is communicated with another entrance of described fluidic architecture (23);
The mixed liquor conduit (25) that its entrance is communicated with the outlet of described fluidic architecture (23);
The mixed liquor jet member (26) that its entrance is communicated with the outlet of described mixed liquor conduit (25), it has for being immersed in the outlet in described alkali lye.
3. chlorine treatment device according to claim 1 and 2, is characterized in that, described chlorine separator (1) also comprises:
Membrane Separator Cylinder for CFB Boiler (12), described gas outlet (11) are opened in its top, and described inlet (13) is opened in its sidewall;
Be arranged on the separated umbrella (14) in Membrane Separator Cylinder for CFB Boiler (12), for by the chlorine of gas and liquid mixture and fluid separation applications;
Be opened in the liquid outlet (15) of Membrane Separator Cylinder for CFB Boiler (12) bottom, the liquid in described gas and liquid mixture flows into settling tank from liquid outlet (15).
4. chlorine treatment device according to claim 1 and 2, is characterized in that, described fluidic architecture (23) is jet pump.
5. chlorine treatment device according to claim 1 and 2, is characterized in that, described mixed liquor jet member (26) is four-way pipe.
6. chlorine treatment device according to claim 5, is characterized in that, every pipe of described four-way pipe is provided with a plurality of spray apertures (26a).
7. chlorine treatment device according to claim 2, is characterized in that, described alkali liquid tank (22) is made by polypropylene material.
8. chlorine treatment device according to claim 3, is characterized in that, described Membrane Separator Cylinder for CFB Boiler (12) is made by polypropylene material.
9. chlorine treatment device according to claim 1, is characterized in that, a described entrance of described fluidic architecture (23) is communicated with the gas outlet (11) of described chlorine separator (1) by chlorine conduit (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320591042.8U CN203577603U (en) | 2013-09-24 | 2013-09-24 | Chlorine gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320591042.8U CN203577603U (en) | 2013-09-24 | 2013-09-24 | Chlorine gas treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203577603U true CN203577603U (en) | 2014-05-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320591042.8U Expired - Fee Related CN203577603U (en) | 2013-09-24 | 2013-09-24 | Chlorine gas treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203577603U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104478151A (en) * | 2014-12-18 | 2015-04-01 | 重庆海洲化学品有限公司 | Environment-friendly treatment method of caustic-soda-containing sodium hypochlorite waste liquor |
| CN106395750A (en) * | 2016-08-31 | 2017-02-15 | 惠州市臻鼎环保科技有限公司 | Chlorine treating process and device of system for recycling copper from acidic waste etching solution |
| CN109289464A (en) * | 2018-11-02 | 2019-02-01 | 辽宁新瑞碳材料科技有限公司 | A kind of recovery and processing system of the furnace exhaust gas of high temperature containing chlorine |
| CN110052132A (en) * | 2019-05-23 | 2019-07-26 | 深圳众意远诚环保科技有限公司 | A kind of bipolar jet stream chlorine treatment device of aqueous slkali |
| CN114534480A (en) * | 2022-03-04 | 2022-05-27 | 西藏浏河化工发展有限公司 | Chlorate electrolysis tail gas pretreatment method and oxygen content determination method applying same |
-
2013
- 2013-09-24 CN CN201320591042.8U patent/CN203577603U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104478151A (en) * | 2014-12-18 | 2015-04-01 | 重庆海洲化学品有限公司 | Environment-friendly treatment method of caustic-soda-containing sodium hypochlorite waste liquor |
| CN104478151B (en) * | 2014-12-18 | 2016-08-24 | 重庆海洲化学品有限公司 | Environment-friendly treatment method containing Caustic soda sodium hypochlorite waste liquid |
| CN106395750A (en) * | 2016-08-31 | 2017-02-15 | 惠州市臻鼎环保科技有限公司 | Chlorine treating process and device of system for recycling copper from acidic waste etching solution |
| CN106395750B (en) * | 2016-08-31 | 2019-07-12 | 惠州市臻鼎环保科技有限公司 | A kind of chlorine gas treatment process of acidic etching waste liquid copper recovery system |
| CN109289464A (en) * | 2018-11-02 | 2019-02-01 | 辽宁新瑞碳材料科技有限公司 | A kind of recovery and processing system of the furnace exhaust gas of high temperature containing chlorine |
| CN109289464B (en) * | 2018-11-02 | 2021-06-29 | 辽宁新瑞碳材料科技有限公司 | Recovery processing system of chlorine-containing high-temperature furnace tail gas |
| CN110052132A (en) * | 2019-05-23 | 2019-07-26 | 深圳众意远诚环保科技有限公司 | A kind of bipolar jet stream chlorine treatment device of aqueous slkali |
| CN114534480A (en) * | 2022-03-04 | 2022-05-27 | 西藏浏河化工发展有限公司 | Chlorate electrolysis tail gas pretreatment method and oxygen content determination method applying same |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140507 Termination date: 20160924 |
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| CF01 | Termination of patent right due to non-payment of annual fee |