CN205253078U - Continuous type halogen -containing salt reaction unit - Google Patents
Continuous type halogen -containing salt reaction unit Download PDFInfo
- Publication number
- CN205253078U CN205253078U CN201520528601.XU CN201520528601U CN205253078U CN 205253078 U CN205253078 U CN 205253078U CN 201520528601 U CN201520528601 U CN 201520528601U CN 205253078 U CN205253078 U CN 205253078U
- Authority
- CN
- China
- Prior art keywords
- cooler bin
- reaction
- pipeline
- reaction chamber
- continous way
- 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.)
- Active
Links
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model is suitable for a halogen -containing salt reaction unit technical field provides a continuous type halogen -containing salt reaction unit, including elevated tank, reaction box, cooler bin, reaction liquid storage device and product collection device, the reaction box is connected the cooler bin, the cooler bin is kept away from the one end upper portion of reaction box is connected with reaction liquid storage device, the cooler bin is close to the one end sub -unit connection of reaction box has the conveyer pipe, duct connections the elevated tank, be equipped with in reaction box and the cooler bin and connect pipeline as an organic whole, pipe connection in the reaction box the elevated tank, pipe connection in the cooler bin product collection device. Therefore, the utility model discloses rational in infrastructure, easy operation can improve work efficiency with consecutive reaction, can also utilize the product waste heat to preheat reaction liquid, and is energy -concerving and environment -protective.
Description
Technical field
The utility model relates to halohydrocarbons reaction device technique field, relates in particular to a kind of continous way halogenated hydrocarbons anti-Should install.
Background technology
At present, the reaction unit of halogenated hydrocarbons reacts after mostly being and adding reactant liquor, reacts complete collection product,After product-collecting, could add new reactant liquor and carry out the reaction of next round, be interrupted reaction, when operating costEffort, inefficiency. And by cooling water, its temperature is reduced more than the heat of products obtained therefrom, causeThe waste of waste heat needs the reactant liquor that improves temperature to need the energy to heat simultaneously, and energy resource consumption is large, increasesThe production cost of product.
In summary, obviously there is in actual use inconvenience and defect in prior art, so be necessary in additionImprove.
Utility model content
For above-mentioned defect, the purpose of this utility model is to provide a kind of continous way halohydrocarbons reaction device,It is rational in infrastructure, simple to operate, both can successive reaction, increase work efficiency, and can utilize again more than productHot preheating reactant liquor, energy-conserving and environment-protective.
To achieve these goals, the utility model provides a kind of continous way halohydrocarbons reaction device, comprises heightPosition groove, reaction chamber, cooler bin, reactant liquor storage device and product collecting device, described reaction chamber connects instituteState cooler bin, described cooler bin is connected with reactant liquor storage device away from the top, one end of described reaction chamber, instituteState cooler bin and be connected with carrier pipe near the bottom, one end of described reaction chamber, described carrier pipe connects a described high positionGroove, is provided with the pipeline connecting as one in described reaction chamber and cooler bin, the pipeline in described reaction chamber connectsDescribed head tank, the pipeline in described cooler bin connects described product collecting device.
As preferred technical scheme, described carrier pipe is provided with delivery pump.
As preferred technical scheme, described pipeline is linear pattern, spirality or waveform.
As preferred technical scheme, described pipeline is waveform.
As preferred technical scheme, the upper inside wall of described cooler bin and described reaction chamber is provided with opening, instituteStating opening matches with described pipeline.
As preferred technical scheme, the junction of described opening and described pipeline is provided with sealing device.
As preferred technical scheme, described pipeline is 150 meters～200 meters.
As preferred technical scheme, the Length Ratio of described pipeline in length and the cooler bin of reaction chamber insideFor: 2:1 or 3:1.
The utility model provides a kind of continous way halohydrocarbons reaction device, comprises head tank, reaction chamber, coolingCase, reactant liquor storage device and product collecting device, described reaction chamber connects described cooler bin, described coolingCase is connected with reactant liquor storage device away from the top, one end of described reaction chamber, and described cooler bin is near described anti-Answer the bottom, one end of case to be connected with carrier pipe, such arranging can make reactant liquor fully in cooler bin with productProduct carry out thermal energy exchange, and product temperature is reduced, and reach collection storage temperature required, make to react liquid temperature simultaneouslyDegree improves, and reaches the effect of preheating, makes full use of waste heat, saves the energy. Described carrier pipe connects described heightPosition groove, is provided with the pipeline connecting as one in described reaction chamber and cooler bin, the pipeline in described reaction chamber connectsConnect described head tank, the pipeline in described cooler bin connects described product collecting device, and described pipeline is integratedFormula structure, reactant liquor enters pipeline by head tank, reacts, cold in the pipeline of reaction chamber insideBut directly cooling reacted product of the pipeline of case inside, continued operation, do not need to interrupt collecting product orAdd reactant liquor, improved operating efficiency, increased production capacity.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model one embodiment.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with accompanying drawingAnd embodiment, the utility model is further elaborated. Should be appreciated that described herein concreteEmbodiment is only in order to explain the utility model, and is not used in restriction the utility model.
Referring to Fig. 1, the utility model provides a kind of continous way halohydrocarbons reaction device, comprises head tank 1, anti-Answer case 2, cooler bin 3, reactant liquor storage device 4 and product collecting device 5, described reaction chamber 2 connects instituteState cooler bin 3, described cooler bin 3 is connected with reactant liquor storage device away from the top, one end of described reaction chamber 24, described cooler bin 3 is connected with carrier pipe 6 near the bottom, one end of described reaction chamber 2, and such setting canSo that reactant liquor fully carries out thermal energy exchange with product in cooler bin 3, product temperature is reduced, reach receiptsCollection storage is temperature required, makes reacting liquid temperature improve simultaneously, reaches the effect of preheating, makes full use of waste heat,Save the energy. Described carrier pipe 6 connects described head tank 1, the company of being provided with in described reaction chamber 2 and cooler bin 3Connect the pipeline 7 being integrated, the pipeline 7 in described reaction chamber 2 connects described head tank 1, described cooler bin 3Interior pipeline 7 connects described product collecting device 5, and described pipeline 7 is integral type structure, and reactant liquor is by highPosition groove 1 enters pipeline 7, reacts, at the pipe of cooler bin 3 inside in the pipeline 7 of reaction chamber 2 insideThe direct cooling reacted product in road 7, continued operation, does not need to interrupt collecting product or adding reactant liquor,Improve operating efficiency, increased production capacity.
Preferably, described carrier pipe 6 is provided with delivery pump 8, can be more smoothly by reactant liquor after preheatingSend into head tank.
Preferably, described pipeline 7 is linear pattern, spirality or waveform, and the best is waveform. InstituteThat states wavy shaped configuration arranges that it is simple in structure, and has increased the contact area of pipeline 7 with reactant liquor.
Preferably, the upper inside wall of described cooler bin 3 and described reaction chamber 2 is provided with opening, described openingMatch with described pipeline 7, the junction of described opening and described pipeline 7 is provided with sealing device, described closeSeal apparatus can increase the sealing of cooler bin, and reaction heat is not leaked outside.
Preferably, described pipeline 7 is 150 meters～200 meters, and described pipeline 7 is in the length of reaction chamber 2 insideDegree with the Length Ratio in cooler bin 3 is: 2:1 or 3:1, described pipeline 7 reaction length and cooling Length RatioThe best during for 2:1, can fully react, and has and reacted product effectively can be lowered the temperature.
In sum, the utility model provides a kind of continous way halohydrocarbons reaction device, comprises head tank, anti-Answer case, cooler bin, reactant liquor storage device and product collecting device, described reaction chamber connects described cooler bin,Described cooler bin is connected with reactant liquor storage device away from the top, one end of described reaction chamber, and described cooler bin leans onThe bottom, one end of nearly described reaction chamber is connected with carrier pipe, and such arranging can make reactant liquor fully coolingIn case, carry out thermal energy exchange with product, product temperature is reduced, reach collection storage temperature required, make simultaneouslyReacting liquid temperature improves, and reaches the effect of preheating, makes full use of waste heat, saves the energy. Described carrier pipe connectsConnect described head tank, in described reaction chamber and cooler bin, be provided with the pipeline connecting as one, in described reaction chamberPipeline connect described head tank, the pipeline in described cooler bin connects described product collecting device, described pipeRoad is integral type structure, and reactant liquor enters pipeline by head tank, carries out anti-in the pipeline of reaction chamber insideShould, at the directly cooling reacted product of pipeline of cooler bin inside, continued operation, does not need to interrupt collectingProduct or add reactant liquor, has improved operating efficiency, has increased production capacity.
Certainly, the utility model also can have other various embodiments, do not deviate from the utility model spirit andIn the situation of essence, those of ordinary skill in the art are when making and variously changing accordingly according to the utility modelBecome and distortion, but these corresponding changes and distortion all should belong to the guarantor of the appended claim of the utility modelProtect scope.
Claims (7)
1. a continous way halohydrocarbons reaction device, it is characterized in that, comprise head tank, reaction chamber, cooler bin, reactant liquor storage device and product collecting device, described reaction chamber connects described cooler bin, described cooler bin is connected with reactant liquor storage device away from the top, one end of described reaction chamber, described cooler bin is connected with carrier pipe near the bottom, one end of described reaction chamber, described carrier pipe connects described head tank, in described reaction chamber and cooler bin, be provided with the pipeline connecting as one, pipeline in described reaction chamber connects described head tank, pipeline in described cooler bin connects described product collecting device.
2. continous way halohydrocarbons reaction device according to claim 1, is characterized in that, described carrier pipe is provided with delivery pump.
3. continous way halohydrocarbons reaction device according to claim 1, is characterized in that, described pipeline is linear pattern, spirality or waveform.
4. continous way halohydrocarbons reaction device according to claim 1, is characterized in that, the upper inside wall of described cooler bin and described reaction chamber is provided with opening, and described opening matches with described pipeline.
5. continous way halohydrocarbons reaction device according to claim 4, is characterized in that, the junction of described opening and described pipeline is provided with sealing device.
6. continous way halohydrocarbons reaction device according to claim 1, is characterized in that, described pipeline is 150 meters～200 meters.
7. continous way halohydrocarbons reaction device according to claim 6, is characterized in that, the Length Ratio of described pipeline in length and the cooler bin of reaction chamber inside is: 2:1 or 3:1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520528601.XU CN205253078U (en) | 2015-07-20 | 2015-07-20 | Continuous type halogen -containing salt reaction unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520528601.XU CN205253078U (en) | 2015-07-20 | 2015-07-20 | Continuous type halogen -containing salt reaction unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205253078U true CN205253078U (en) | 2016-05-25 |
Family
ID=55994630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520528601.XU Active CN205253078U (en) | 2015-07-20 | 2015-07-20 | Continuous type halogen -containing salt reaction unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205253078U (en) |
-
2015
- 2015-07-20 CN CN201520528601.XU patent/CN205253078U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101865622B (en) | Long-distance waste heat recovery system of drying tail gas | |
| CN205253078U (en) | Continuous type halogen -containing salt reaction unit | |
| CN204939413U (en) | A kind of coal gas waste heat recovery apparatus carrying cleaning function | |
| CN105953298A (en) | High-efficient heat-storage tank semitrailer | |
| CN204345692U (en) | A kind of purifier of Gas Pipe | |
| CN202757462U (en) | Cooling device for nickel-iron particles | |
| CN104496821B (en) | Gasify in methylcarbonate production CO 2with the method reclaiming emptying material | |
| CN204265849U (en) | A kind of heating container of stainless steel blackening process | |
| CN207162579U (en) | A kind of energy saver and boiler energy-saving system | |
| CN205807616U (en) | High-efficiency thermal storage tank type half-trailer | |
| CN205087434U (en) | Alleviate device of coal pile spontaneous combustion | |
| CN202482269U (en) | Heat-conducting oil circulation system in tar distillation | |
| CN203518742U (en) | Economizer provided with parallel-connection heat collecting tubes | |
| CN203494492U (en) | Chloroethylene conversion reactor | |
| CN211739897U (en) | Improved energy-saving heating furnace | |
| CN204514120U (en) | composite heat exchanger | |
| CN204836630U (en) | Frequency conversion heater | |
| CN205037413U (en) | Heat pipe conductive heat hydrophone | |
| CN203281301U (en) | Reaction kettle heating device | |
| CN203518741U (en) | Economizer provided with series-connection heat-collecting heat pipes | |
| CN214095647U (en) | Closed heat exchanger for cooling tower that heat exchange efficiency is good | |
| CN212987639U (en) | Material heating device | |
| CN206337022U (en) | A kind of energy-saving carbon carries deoxidation nitrogen purification equipment | |
| CN210426189U (en) | Heat exchanger with spiral turbulence wire in heat exchange tube | |
| CN207371538U (en) | A kind of catalyst reaction bed |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 262725. Jin Yuan Road 9, Hou Hai Town Chemical Industry Zone, Shouguang City, Shandong, Weifang Patentee after: SHANDONG TONGCHENG MEDICINE CO.,LTD. Address before: 262700 Weifang, Shouguang City, Shouguang City, the town of the project area alliance road, No. 6 Patentee before: SHANDONG TONGCHENG MEDICINE TECHNOLOGY Co.,Ltd. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Continuous halohydrocarbon reaction unit Effective date of registration: 20221222 Granted publication date: 20160525 Pledgee: Postal Savings Bank of China Limited Shouguang sub branch Pledgor: SHANDONG TONGCHENG MEDICINE CO.,LTD. Registration number: Y2022980027268 |