CN205182735U - Hydrogen chloride removes chlorine device - Google Patents
Hydrogen chloride removes chlorine device Download PDFInfo
- Publication number
- CN205182735U CN205182735U CN201520999653.5U CN201520999653U CN205182735U CN 205182735 U CN205182735 U CN 205182735U CN 201520999653 U CN201520999653 U CN 201520999653U CN 205182735 U CN205182735 U CN 205182735U
- Authority
- CN
- China
- Prior art keywords
- cyclone separator
- hydrogen chloride
- cyclone
- discharge nozzle
- reactor
- 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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- 229910000041 hydrogen chloride Inorganic materials 0.000 title claims abstract description 22
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 title claims abstract description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 239000000460 chlorine Substances 0.000 title abstract description 9
- 229910052801 chlorine Inorganic materials 0.000 title abstract description 9
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 title abstract description 8
- 239000012188 paraffin wax Substances 0.000 claims abstract description 19
- 239000003595 mist Substances 0.000 claims abstract description 15
- 238000006298 dechlorination reaction Methods 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 abstract description 6
- 239000007789 gas Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 5
- 238000004321 preservation Methods 0.000 abstract 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses a hydrogen chloride removes chlorine device, the control unit comprises a reaction vessel, the reation kettle upper end is equipped with the inlet pipe, the reation kettle outside is equipped with the heat preservation device, the reation kettle upper end is equipped with the mist discharging pipe, the mist discharging pipe is connected with the filled tower lower extreme, vice cauldron inlet pipe is connected to filled tower lower extreme one side, the paraffin discharging pipe is connected to the filled tower upper end, filled tower upper end one side is connected with a cyclone, a cyclone is connected with the 2nd cyclone the upper end, the 2nd cyclone upper end is equipped with the hydrogen chloride outlet duct, a cyclone is connected with reation kettle with the 2nd cyclone lower extreme, reation kettle lower extreme discharging pipe communicates with the paraffin discharging pipe of filled tower upper end, the utility model discloses novel structure makes mixture gas volatilize through reation kettle, gets rid of chlorine through the filled tower, and rethread secondary cyclone separates hydrogen chloride gas, the utility model discloses satisfied the operation requirement, the treatment effect is good.
Description
Technical field
The utility model relates to a kind of gas treatment equipment, specifically a kind of hydrogen chloride dechlorination device.
Background technology
Chlorinated paraffin wax is a kind of important raw material of industry, is widely used in the industries such as polyvinyl chloride, polyurethane, rubber and plastic, oil product.
Chlorinated paraffin wax produced for more than 20 years at home, produce from interruption now and be progressively transitioned into the continuous prodution stage, Chinese patent CN02148592.5 and CN1824737A disclosed continuous production device patent has single advance, but its defect is fairly obvious, one is chlorine skewness, chlorination reactor " black material " phenomenon cannot effectively solve, two is rely on power-forced circulation, to solve chlorine skewness problem, once run out of steam suddenly, environmental pollution and " black material " problem can be caused, energy resource consumption is simultaneously high, be unfavorable for the environmental protection of the whole society.
Can produce now the mixture of a large amount of hydrogen chloride and paraffin and chlorine in the production of chlorinated paraffin wax, need now to process this mixture, thus Isolating chlorinated hydrogen and atoleine, and remove chlorine.
Utility model content
The purpose of this utility model is to provide a kind of hydrogen chloride dechlorination device, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of hydrogen chloride dechlorination device, comprise reactor, described reactor upper end is provided with feed pipe, described reactor outside is provided with attemperator, described reactor upper end is provided with mist discharge nozzle, described mist discharge nozzle is connected with packed tower lower end, side, described packed tower lower end auxiliary connection still feed pipe, described packed tower upper end connects paraffin discharge nozzle, side, described packed tower upper end is connected with the first cyclone separator, described first cyclone separator upper end is connected with the second cyclone separator, described second cyclone separator upper end is provided with hydrogen chloride escape pipe, described first cyclone separator is connected with reactor with the second cyclone separator lower end, described reactor lower end discharge nozzle is communicated with the paraffin discharge nozzle of packed tower upper end.
As further program of the utility model: described attemperator comprises incubator, described incubator is fitted in reactor outer surface, and described incubator upper end is provided with liquid outlet, and described incubator lower end is provided with inlet.
As further program of the utility model: described reactor upper end is also provided with thermometer.
As further program of the utility model: described first cyclone separator and the second cyclone separator lower end are provided with looks cup.
As further program of the utility model: described first cyclone separator, the second cyclone separator lower end and discharge nozzle, mist discharge nozzle and paraffin discharge nozzle are equipped with control valve.
Compared with prior art, the beneficial effects of the utility model are: the utility model novel structure, by reactor, gas mixture are volatilized, chlorine is removed by packed tower, again by the Isolating chlorinated hydrogen of secondary cyclone, the utility model meets instructions for use, and treatment effect is good.
Accompanying drawing explanation
Fig. 1 is the structural representation of hydrogen chloride dechlorination device.
In figure: 1-hydrogen chloride escape pipe, 2-second cyclone separator, 3-visor, 4-packed tower, 5-look cup, 6-feed pipe, 7-thermometer, 8-control valve, 9-reactor, 10-flowmeter, the secondary still feed pipe of 11-, 12-first cyclone separator, 13-liquid outlet, 14-inlet, 15-attemperator, 16-mist discharge nozzle.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, in the utility model embodiment, a kind of hydrogen chloride dechlorination device, comprise reactor 9, reactor 9 upper end is provided with feed pipe 6, reactor 9 outside is provided with attemperator 15, reactor 9 upper end is provided with mist discharge nozzle 16, mist discharge nozzle 16 is connected with packed tower 4 lower end, side, packed tower 4 lower end auxiliary connection still feed pipe 11, packed tower 4 upper end connects paraffin discharge nozzle, side, packed tower 4 upper end is connected with the first cyclone separator 12, first cyclone separator 12 upper end is connected with the second cyclone separator 2, second cyclone separator 2 upper end is provided with hydrogen chloride escape pipe 1, first cyclone separator 12 is connected with reactor 9 with the second cyclone separator 2 lower end, reactor 9 lower end discharge nozzle is communicated with the paraffin discharge nozzle of packed tower 4 upper end, attemperator 15 comprises incubator, incubator is fitted in reactor 9 outer surface, incubator upper end is provided with liquid outlet 13, incubator lower end is provided with inlet 14, reactor 9 upper end is also provided with thermometer 7, first cyclone separator 12 and the second cyclone separator 2 lower end are provided with looks cup 5, first cyclone separator 12, second cyclone separator 2 lower end and discharge nozzle, mist discharge nozzle 16 and paraffin discharge nozzle are equipped with control valve 8.
The utility model novel structure, mixture enters reactor by feed pipe, pass through attemperator, mixture is volatilized, packed tower is entered into by mist, secondary still feed pipe also enters mist, chlorine is removed by packed tower, the paraffin removing gas flows out from paraffin discharge nozzle, remaining hydrogen chloride and the mist of paraffin are again by the first cyclone separator and the Isolating chlorinated hydrogen of the second cyclone separator, the paraffin that non-separating hydrogen chloride is clean enters in reactor again, volatilizing, the utility model meets instructions for use, separating treatment is effective.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this description is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of description is only for clarity sake, those skilled in the art should by description integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (5)
1. a hydrogen chloride dechlorination device, comprise reactor, it is characterized in that, described reactor upper end is provided with feed pipe, described reactor outside is provided with attemperator, described reactor upper end is provided with mist discharge nozzle, described mist discharge nozzle is connected with packed tower lower end, side, described packed tower lower end auxiliary connection still feed pipe, described packed tower upper end connects paraffin discharge nozzle, side, described packed tower upper end is connected with the first cyclone separator, described first cyclone separator upper end is connected with the second cyclone separator, described second cyclone separator upper end is provided with hydrogen chloride escape pipe, described first cyclone separator is connected with reactor with the second cyclone separator lower end, described reactor lower end discharge nozzle is communicated with the paraffin discharge nozzle of packed tower upper end.
2. hydrogen chloride dechlorination device according to claim 1, is characterized in that, described attemperator comprises incubator, and described incubator is fitted in reactor outer surface, and described incubator upper end is provided with liquid outlet, and described incubator lower end is provided with inlet.
3. hydrogen chloride dechlorination device according to claim 1, is characterized in that, described reactor upper end is also provided with thermometer.
4. hydrogen chloride dechlorination device according to claim 1, is characterized in that, described first cyclone separator and the second cyclone separator lower end are provided with looks cup.
5. hydrogen chloride dechlorination device according to claim 1, is characterized in that, described first cyclone separator, the second cyclone separator lower end and discharge nozzle, mist discharge nozzle and paraffin discharge nozzle are equipped with control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520999653.5U CN205182735U (en) | 2015-12-03 | 2015-12-03 | Hydrogen chloride removes chlorine device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520999653.5U CN205182735U (en) | 2015-12-03 | 2015-12-03 | Hydrogen chloride removes chlorine device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205182735U true CN205182735U (en) | 2016-04-27 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520999653.5U Active CN205182735U (en) | 2015-12-03 | 2015-12-03 | Hydrogen chloride removes chlorine device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205182735U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113893677A (en) * | 2021-09-29 | 2022-01-07 | 封丘县龙润精细化工有限公司 | Method and device for refining and purifying ethyl chloride byproduct hydrochloric acid |
-
2015
- 2015-12-03 CN CN201520999653.5U patent/CN205182735U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113893677A (en) * | 2021-09-29 | 2022-01-07 | 封丘县龙润精细化工有限公司 | Method and device for refining and purifying ethyl chloride byproduct hydrochloric acid |
| CN113893677B (en) * | 2021-09-29 | 2022-10-18 | 河南嘉颖生物科技有限公司 | Method and device for refining and purifying ethyl chloride byproduct hydrochloric acid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240122 Address after: 330300 Xinghuo Industrial Park, Yongxiu County, Jiujiang City, Jiangxi Province Patentee after: JIANGXI AIDIER NEW ENERGY Co.,Ltd. Country or region after: China Address before: 332000 Xinghuo Industrial Park, Yongxiu County, Jiujiang City, Jiangxi Province Patentee before: JIANGXI EAST HUGE DRAGON CHEMICAL Co.,Ltd. Country or region before: China |
|
| TR01 | Transfer of patent right |