CN203763881U - Energy-saving device for rectification of chloroethylene high-boiling substances - Google Patents
Energy-saving device for rectification of chloroethylene high-boiling substances Download PDFInfo
- Publication number
- CN203763881U CN203763881U CN201420028594.2U CN201420028594U CN203763881U CN 203763881 U CN203763881 U CN 203763881U CN 201420028594 U CN201420028594 U CN 201420028594U CN 203763881 U CN203763881 U CN 203763881U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- vinyl chloride
- water pipe
- chloroethylene
- temperature
- 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.)
- Expired - Fee Related
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- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical group ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 title claims abstract description 65
- 238000009835 boiling Methods 0.000 title claims abstract description 31
- 239000000126 substance Substances 0.000 title abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 230000008676 import Effects 0.000 claims description 12
- 238000003860 storage Methods 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 14
- 238000005265 energy consumption Methods 0.000 abstract description 8
- 230000008901 benefit Effects 0.000 abstract description 3
- 239000002440 industrial waste Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical class CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000011982 device technology Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model relates to the technical field of an energy-saving device for rectification of chloroethylene high-boiling substances. The energy-saving device for rectification of chloroethylene high-boiling substances comprises an intermittent chloroethylene rectifying column, a high-temperature hot water pipe for delivering circulating water heated by heat emitted by a chloroethylene section, and a chloroethylene section circulating water device, wherein a column kettle heat exchanger is fixedly arranged on the column kettle of the intermittent chloroethylene rectifying column, a heat exchanger heat source inlet and a heat exchanger heat source outlet are arranged on the column kettle heat exchanger respectively, the inlet of the high-temperature hot water pipe and an outlet end of the chloroethylene section circulating water device are fixedly assembled together, and the outlet of the high-temperature hot water pipe and the heat exchanger heat source inlet are fixedly arranged together. The energy-saving device has a reasonable and compact structure and convenience in use, can fully utilize the circulating water heated by heat emitted by the chloroethylene section to achieve the effect of effectively saving energy consumption, prolonging the production cycle and realizing safety production, can further improve the rectifying benefit of the chloroethylene high-boiling substances and has great economic value.
Description
Technical field
the utility model relates to vinyl chloride high-boiling components rectifying heating device technology area, is a kind of vinyl chloride high-boiling components Finestill energy-saving apparatus.
Background technology
the great function that chemical industry alarming development speed is brought into play in social progress is self-evident, but is accompanied by chemical industry and the three-waste pollution that produces is also on the rise, and becomes a large crisis of human survival, has obtained the concern of the whole society.China has promulgated " three industrial wastes discharge tentative standard " in 1973; within 1989, formally promulgate the Law on Environmental Protection of the People's Republic of China; therefore, the Resource analysis of the comprehensive regulation to three industrial wastes and refuse has become scientific worker's popular research topic.
in Production of PVC, the refining step of monomer all needs to remove low-boiling-point substance and high-boiling components.Big-and-middle-sized Production of PVC producer all recycles for low-boiling-point substance, after the VCM reclaiming wherein, bleeds off or incinerates for high-boiling components, causes environmental pollution.Each medium and small Production of PVC producer is coarse especially to the processing of high-boiling components, and even monomer is not reclaimed.According to the constituent and properties of high-boiling components and application prospect, the recycling of vinyl chloride high-boiling components is at present generally to adopt batch fractionating, and feed liquid is dropped into rectifying still in batch, and progressively heating and gasifying is once discharged it after still liquid composition is down to setting.According to the boiling point difference of vinyl chloride high-boiling components composition, can make the composition in high-boiling components progressively obtain recycling by the temperature and the reflux ratio that change tower bottom of rectifying tower.This processing method equipment and process is simple, but needs more external energy to heat tower reactor.The rectifying of vinyl chloride high-boiling components, although can obtain the product in a part of high-boiling components, if but energy consumption is too high, production cost increases, and makes a lot of enterprises hang back, therefore, in the distillation process of vinyl chloride high-boiling components, how to reduce energy consumption, make full use of other heats more than needed of vinyl chloride production process, the production cost that reduces the rectifying of vinyl chloride high-boiling components is very necessary.
Summary of the invention
the utility model provides a kind of vinyl chloride high-boiling components Finestill energy-saving apparatus, has overcome the deficiency of above-mentioned prior art, and it can effectively solve the too high problem of rectifying energy consumption of vinyl chloride high-boiling components.
the technical solution of the utility model realizes by following measures: a kind of vinyl chloride high-boiling components Finestill energy-saving apparatus, comprises vinyl chloride batch fractionating tower, carries high-temperature-hot-water pipe and vinyl chloride workshop section circulating water device by the recirculated water of vinyl chloride workshop section liberated heat heating; In the tower reactor of vinyl chloride batch fractionating tower, be installed with tower reactor heat exchanger, on tower reactor heat exchanger, there are respectively the import of heat exchanger thermal source and the outlet of heat exchanger thermal source, the port of export of the import of high-temperature-hot-water pipe and vinyl chloride workshop section circulating water device is fixedly installed togather, the outlet of high-temperature-hot-water pipe and the import of heat exchanger thermal source are fixedly installed togather, in the outlet of heat exchanger thermal source, be installed with outlet pipe, on high-temperature-hot-water pipe, be installed with delivery pump, the entrance point of delivery pump is communicated with high-temperature-hot-water pipe respectively with the port of export.
the further optimization and/or improvements to above-mentioned utility model technical scheme below:
above-mentionedly on high-temperature-hot-water pipe, be installed with storage tank, be installed with cold water pipe on storage tank, on the high-temperature-hot-water pipe between the import of heat exchanger thermal source and storage tank, be installed with delivery pump, the entrance point of delivery pump is communicated with high-temperature-hot-water pipe respectively with the port of export.
above-mentioned tower reactor heat exchanger is tubular heat exchanger or finned heat exchanger or jacketed type exchanger.
the utility model reasonable and compact in structure, easy to use, by making full use of the recirculated water by the liberated heat heating of vinyl chloride workshop section, can effectively save energy consumption, extended the production cycle, realize safety in production, the benefit that has further improved the rectifying of vinyl chloride high-boiling components, has larger economic worth.
Brief description of the drawings
accompanying drawing 1 is the main TV structure schematic diagram of the utility model most preferred embodiment.
coding in accompanying drawing is respectively: 1 is vinyl chloride batch fractionating tower, and 2 is high-temperature-hot-water pipe, and 3 is storage tank, and 4 is outlet pipe, and 5 is cold water pipe, and 6 is vinyl chloride workshop section circulating water device, and 7 is delivery pump.
Detailed description of the invention
the utility model is not subject to the restriction of following embodiment, can determine concrete embodiment according to the technical solution of the utility model and actual conditions.
in the utility model, for convenience of description, the description of the relative position relation of each parts is to be all described according to the Butut mode of Figure of description 1, as: the position relationship of upper and lower, left and right etc. is to determine according to the Butut direction of Figure of description.
below in conjunction with embodiment and accompanying drawing, the utility model is further described:
as shown in Figure 1, this vinyl chloride high-boiling components Finestill energy-saving apparatus comprises vinyl chloride batch fractionating tower 1, carries high-temperature-hot-water pipe 2 and vinyl chloride workshop section circulating water device 6 by the recirculated water of vinyl chloride workshop section liberated heat heating; In the tower reactor of vinyl chloride batch fractionating tower 1, be installed with tower reactor heat exchanger, on tower reactor heat exchanger, there are respectively the import of heat exchanger thermal source and the outlet of heat exchanger thermal source, the port of export of the import of high-temperature-hot-water pipe 2 and vinyl chloride workshop section circulating water device 6 is fixedly installed togather, the outlet of high-temperature-hot-water pipe 2 and the import of heat exchanger thermal source are fixedly installed togather, in the outlet of heat exchanger thermal source, be installed with outlet pipe 4, on high-temperature-hot-water pipe 2, be installed with delivery pump 7, the entrance point of delivery pump 7 is communicated with high-temperature-hot-water pipe respectively with the port of export.Vinyl chloride workshop section liberated heat is taken out of by recirculated water, recirculated water becomes high-temperature-hot-water like this, enter vinyl chloride workshop section circulating water device 6 with the recirculated water of heat, by high-temperature-hot-water pipe 2 in delivery pump 7 is delivered to tower reactor heat exchanger, as the thermal source of vinyl chloride batch fractionating tower 1 tower reactor, avoid adopting separately steam to heat as thermal source, like this, by utilizing the waste heat that produces in the course of production of chloroethylene thermal source as vinyl chloride batch fractionating tower 1 tower reactor, can save energy consumption, the recirculated water being heated by vinyl chloride workshop section liberated heat is after the tower reactor heating to vinyl chloride batch fractionating tower 1, send through outlet pipe 4.
can according to actual needs, above-mentioned vinyl chloride high-boiling components Finestill energy-saving apparatus be made further optimization and/or improvements:
as shown in Figure 1, on high-temperature-hot-water pipe 2, be installed with storage tank 3, on storage tank 3, be installed with cold water pipe 5, on the high-temperature-hot-water pipe between the import of heat exchanger thermal source and storage tank 3, be installed with delivery pump 7, the entrance point of delivery pump 7 is communicated with high-temperature-hot-water pipe respectively with the port of export.The circulating water temperature being heated by vinyl chloride workshop section liberated heat is conventionally 95 DEG C of left and right, excess Temperature, easily cause vinyl chloride coking, polymerization, can be by first will being delivered to storage tank 3 by high-temperature-hot-water pipe 2 by the recirculated water of vinyl chloride workshop section liberated heat heating, in storage tank 3, pass into cold water by cold water pipe 5 again, the temperature of water is reduced to and delivers to tower reactor heat exchanger by high-temperature-hot-water pipe 2 through delivery pumps 7 again behind 55 DEG C of left and right the tower reactor of vinyl chloride batch fractionating tower 1 is heated, so not only increase the input that enters heating hot water in vinyl chloride batch fractionating tower 1 tower reactor, and make the temperature of recirculated water more suitable, can obtain vinyl chloride and dichloroethanes in vinyl chloride high-boiling components, can not cause vinyl chloride batch fractionating tower 1 tower reactor excess Temperature simultaneously, make vinyl chloride coalescent, also reduced the number of times of cleaning during shutdown, extend the production cycle, realize safety in production, improve the benefit of vinyl chloride high-boiling components rectifying.
as required, tower reactor heat exchanger is tubular heat exchanger or finned heat exchanger or jacketed type exchanger.
if calculate taking the annual production of vinyl chloride as 500,000 tons, the high-boiling components that obtains 2000 tons/year, adopt the present invention can save 10000 tons/year of vapours, be converted into 1,000,000 yuan/year of operating costs.Can find out, the present invention not only can reduce energy consumption, and in reducing energy consumption, can reduce operating cost, has larger economic worth.
above technical characterictic has formed most preferred embodiment of the present utility model, and it has stronger adaptability and best implementation result, can increase and decrease according to actual needs non-essential technical characterictic, meets the demand of different situations.
Claims (3)
1. a vinyl chloride high-boiling components Finestill energy-saving apparatus, is characterized in that comprising vinyl chloride batch fractionating tower, carries high-temperature-hot-water pipe and vinyl chloride workshop section circulating water device by the recirculated water of vinyl chloride workshop section liberated heat heating; In the tower reactor of vinyl chloride batch fractionating tower, be installed with tower reactor heat exchanger, on tower reactor heat exchanger, there are respectively the import of heat exchanger thermal source and the outlet of heat exchanger thermal source, the port of export of the import of high-temperature-hot-water pipe and vinyl chloride workshop section circulating water device is fixedly installed togather, the outlet of high-temperature-hot-water pipe and the import of heat exchanger thermal source are fixedly installed togather, in the outlet of heat exchanger thermal source, be installed with outlet pipe, on high-temperature-hot-water pipe, be installed with delivery pump, the entrance point of delivery pump is communicated with high-temperature-hot-water pipe respectively with the port of export.
2. vinyl chloride high-boiling components Finestill energy-saving apparatus according to claim 1, it is characterized in that being installed with storage tank on high-temperature-hot-water pipe, on storage tank, be installed with cold water pipe, on the high-temperature-hot-water pipe between the import of heat exchanger thermal source and storage tank, be installed with delivery pump, the entrance point of delivery pump is communicated with high-temperature-hot-water pipe respectively with the port of export.
3. vinyl chloride high-boiling components Finestill energy-saving apparatus according to claim 1 and 2, is characterized in that tower reactor heat exchanger is tubular heat exchanger or finned heat exchanger or jacketed type exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420028594.2U CN203763881U (en) | 2014-01-17 | 2014-01-17 | Energy-saving device for rectification of chloroethylene high-boiling substances |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420028594.2U CN203763881U (en) | 2014-01-17 | 2014-01-17 | Energy-saving device for rectification of chloroethylene high-boiling substances |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203763881U true CN203763881U (en) | 2014-08-13 |
Family
ID=51281131
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420028594.2U Expired - Fee Related CN203763881U (en) | 2014-01-17 | 2014-01-17 | Energy-saving device for rectification of chloroethylene high-boiling substances |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203763881U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106866860A (en) * | 2017-03-31 | 2017-06-20 | 四川永祥股份有限公司 | The technique that a kind of crude product vinyl chloride produces macromolecular material polyvinyl chloride |
-
2014
- 2014-01-17 CN CN201420028594.2U patent/CN203763881U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106866860A (en) * | 2017-03-31 | 2017-06-20 | 四川永祥股份有限公司 | The technique that a kind of crude product vinyl chloride produces macromolecular material polyvinyl chloride |
| CN106866860B (en) * | 2017-03-31 | 2019-08-16 | 四川永祥股份有限公司 | A kind of technique of crude product vinyl chloride production high molecular material polyvinyl chloride |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140813 Termination date: 20210117 |