CN208193715U - Slow down the device of vinyl chloride low boiling point rectifying column autohemagglutination blocking - Google Patents
Slow down the device of vinyl chloride low boiling point rectifying column autohemagglutination blocking Download PDFInfo
- Publication number
- CN208193715U CN208193715U CN201820544226.1U CN201820544226U CN208193715U CN 208193715 U CN208193715 U CN 208193715U CN 201820544226 U CN201820544226 U CN 201820544226U CN 208193715 U CN208193715 U CN 208193715U
- Authority
- CN
- China
- Prior art keywords
- polymerization inhibitor
- low boiling
- rectifying column
- boiling point
- charge pump
- 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
- Polymerisation Methods In General (AREA)
Abstract
Provided by the utility model is the device for slowing down the blocking of vinyl chloride low boiling point rectifying column autohemagglutination.Polymerization inhibitor basin is connect by the pipeline equipped with polymerization inhibitor charge pump inlet valve with polymerization inhibitor charge pump, counterbalance valve is installed on the pipeline exported on the upside of polymerization inhibitor basin, for the pipeline exported by polymerization inhibitor charge pump and counterbalance valve through being conveyed to low boiling point rectifying column by check (non-return) valve and low boiling point rectifying column polymerization inhibitor inlet valve after polymerization inhibitor charge pump outlet valve, another pipeline of polymerization inhibitor charge pump is also conveyed to low boiling point rectifying column via runic list slot.The utility model passes through the process units for increasing and being continuously added to polymerization inhibitor to low boiling point rectifying column compared with prior art, slows down the blocking of low boiling point rectifying column autohemagglutination, can run steadily in the long term, ensure that vinyl chloride stable high yield.It is suitable to be used as the device for slowing down the blocking of vinyl chloride low boiling point rectifying column autohemagglutination.
Description
Technical field
The utility model relates to the technical fields of carbide acetylene method production vinyl chloride, specifically slow down vinyl chloride low boiling
The device of point rectifying column autohemagglutination blocking.
Background technique
Currently, domestic PVC industry is mainly based on carbide acetylene method synthesis vinyl chloride thereof, wherein VCM synthesis
It is intermediate extremely important production link.In process of production, vinyl chloride autohemagglutination can occur often for vinyl chloride low boiling point rectifying column
Phenomenon will gradually block the tower tray of rectifying column with the progress of production, once blocking is serious, low tower is just unable to control and just
Often operation, seriously destroys production process, extreme influence polyvinyl chloride product quality, or even product transformation occur, causes larger warp
Ji loss.In the past, autohemagglutination blockage problem can often occur in vinyl chloride low boiling point rectifying column, and sudden very strong, give vinyl chloride
Normal production causes very big puzzlement.
Utility model content
In order to overcome the problems, such as that autohemagglutination blocking can often occur in vinyl chloride low boiling point rectifying column, the utility model, which provides, to be subtracted
The device of slow vinyl chloride low boiling point rectifying column autohemagglutination blocking.The device passes through polymerization inhibitor basin and polymerization inhibitor charge pump to low boiling point
Rectifying column conveys polymerization inhibitor, solves vinyl chloride low boiling point rectifying column and the technical issues of autohemagglutination blocking often occurs.
The utility model solves scheme used by technical problem:
Polymerization inhibitor basin is connect by the pipeline equipped with polymerization inhibitor charge pump inlet valve with polymerization inhibitor charge pump, polymerization inhibitor storage
Counterbalance valve is installed on the pipeline exported on the upside of tank, is added by the pipeline that polymerization inhibitor charge pump and counterbalance valve export by polymerization inhibitor
Through being conveyed to low boiling point rectifying column, polymerization inhibitor charging by check (non-return) valve and low boiling point rectifying column polymerization inhibitor inlet valve after material pump discharge valve
Another pipeline of pump is also conveyed to low boiling point rectifying column via runic list slot.
Good effect, the utility model pass through increase compared with prior art and are continuously added to polymerization inhibitor to low boiling point rectifying column
Process units, slow down low boiling point rectifying column autohemagglutination blocking, can run steadily in the long term, ensure that vinyl chloride high yield is steady
It produces.It is suitable to be used as the device for slowing down the blocking of vinyl chloride low boiling point rectifying column autohemagglutination.
Detailed description of the invention
Fig. 1 is utility model device structure configuration diagram.
In figure: 1. polymerization inhibitor basins, 2. polymerization inhibitor charge pump inlet valves, 3. polymerization inhibitor charge pumps, 4. runic list slots, 5. back
Pressure valve, 6. polymerization inhibitor charge pump outlet valves, 7. check (non-return) valves, 8. low boiling point rectifying column polymerization inhibitor inlet valves, 9. low boiling point rectifying columns.
Specific embodiment
Embodiment:
Polymerization inhibitor basin 1 is connect by the pipeline equipped with polymerization inhibitor charge pump inlet valve 2 with polymerization inhibitor charge pump 3, is inhibited
Counterbalance valve 5 is installed on the pipeline exported on the upside of agent basin, the pipeline exported by polymerization inhibitor charge pump and counterbalance valve is by resistance
Through being conveyed to low boiling point rectifying column 9 by check (non-return) valve 7 and low boiling point rectifying column polymerization inhibitor inlet valve 8 after poly- agent charge pump outlet valve 6,
Another pipeline of polymerization inhibitor charge pump is also conveyed to low boiling point rectifying column via runic list slot 4.
The liquid feeding higher boiling rectifying column of low boiling point rectifying column lower part, further rectifying, and the gaseous state of the output on top
Substance is sent into compressor and is compressed.
The polymerization inhibitor is liquid.
The substance of the rectifying is vinyl chloride.
The polymerization inhibitor charge pump uses plunger type metering pump.
The course of work:
A kind of liquid polymerization inhibitor is selected, is continuously added in vinyl chloride low boiling point rectifying column by polymerization inhibitor charge pump.Liquid
Polymerization inhibitor is stored in a canister, enters polymerization inhibitor charging pump intake by polymerization inhibitor charge pump inlet valve by bottom nozzles,
It pressurizes through charge pump, it, will in low boiling point rectifying column charging inlet by pump discharge through polymerization inhibitor charge pump outlet valve and check (non-return) valve
Polymerization inhibitor is added in rectifying column.It is equipped with counterbalance valve in pump discharge, when hypertonia, counterbalance valve is opened, and polymerization inhibitor flows back to basin,
To guarantee output pressure safety.
Operating method:
(1) polymerization inhibitor is filled into basin.
(2) polymerization inhibitor charge pump inlet valve is opened.
(3) start polymerization inhibitor charge pump.
(4) after pressure rises, counterbalance valve is adjusted to certain pressure, low boiling point essence can be added in polymerization inhibitor enough
It evaporates in tower.
(5) charge pump outlet valve is opened.
(6) low boiling point rectifying column polymerization inhibitor inlet valve is opened.
In this way, liquid polymerization inhibitor can keep uninterruptedly being added in low boiling point rectifying column, pass through polymerization inhibitor
Inhibition slows down the blocking of low boiling point rectifying column autohemagglutination, can continuous and steady operation.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims.
Claims (4)
1. slow down the device of vinyl chloride low boiling point rectifying column autohemagglutination blocking, it is characterized in that:
Polymerization inhibitor basin (1) is connect by the pipeline equipped with polymerization inhibitor charge pump inlet valve (2) with polymerization inhibitor charge pump (3), is hindered
Counterbalance valve (5) are installed on the pipeline exported on the upside of poly- agent basin, are passed through by the pipeline that polymerization inhibitor charge pump and counterbalance valve export
It crosses polymerization inhibitor charge pump outlet valve (6) and is conveyed to low boiling by by check (non-return) valve (7) and low boiling point rectifying column polymerization inhibitor inlet valve (8)
Point rectifying column (9), another pipeline of polymerization inhibitor charge pump are also conveyed to low boiling point rectifying column via runic list slot (4).
2. the device according to claim 1 for slowing down the blocking of vinyl chloride low boiling point rectifying column autohemagglutination, it is characterized in that: the resistance
Poly- agent is liquid.
3. the device according to claim 1 for slowing down the blocking of vinyl chloride low boiling point rectifying column autohemagglutination, it is characterized in that: the essence
The substance evaporated is vinyl chloride.
4. the device according to claim 1 for slowing down the blocking of vinyl chloride low boiling point rectifying column autohemagglutination, it is characterized in that: the resistance
Poly- agent charge pump uses plunger type metering pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820544226.1U CN208193715U (en) | 2018-04-17 | 2018-04-17 | Slow down the device of vinyl chloride low boiling point rectifying column autohemagglutination blocking |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820544226.1U CN208193715U (en) | 2018-04-17 | 2018-04-17 | Slow down the device of vinyl chloride low boiling point rectifying column autohemagglutination blocking |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208193715U true CN208193715U (en) | 2018-12-07 |
Family
ID=64523276
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820544226.1U Active CN208193715U (en) | 2018-04-17 | 2018-04-17 | Slow down the device of vinyl chloride low boiling point rectifying column autohemagglutination blocking |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208193715U (en) |
-
2018
- 2018-04-17 CN CN201820544226.1U patent/CN208193715U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105696654A (en) | Water supply system and container and boost pump thereof and water supply method | |
CN103061384B (en) | Secondary-pressurizing energy-saving water-supply system for high-rise building and energy-saving water supply method | |
CN106224756A (en) | A kind of compression air energy-storing apparatus realizing the storage of gas constant voltage | |
CN109235535B (en) | Non-negative pressure water supply device with small flow control function and control method thereof | |
CN103267403B (en) | A kind of system and method improving liquid argon yield | |
CN208193715U (en) | Slow down the device of vinyl chloride low boiling point rectifying column autohemagglutination blocking | |
CN202082615U (en) | Recovery system for gas emptied by high-pressure output pump in LNG (Liquefied Natural Gas) receiving terminal | |
CN111704518B (en) | Device and method for controlling gaseous ethane condensation rate at top of deethanizer | |
CN201220915Y (en) | Liquid supply apparatus capable of improving stable reliability | |
CN208719857U (en) | A kind of liquefied ammonia recovery system for ammonia ice maker | |
CN113847247B (en) | Spray cooling-assisted oilfield associated gas recovery liquid ring compressor system and method | |
JP2014122284A (en) | Facility for recovering crude lpg from flare gas | |
CN203656578U (en) | Wide-gas inflow constant-flow CNG compression plant | |
CN202674833U (en) | Low-temperature liquid evaporating and transporting device | |
CN202813338U (en) | Steam condensate reclaiming system | |
Suhendar et al. | Gas Well Deliquification for Maximizing Recovery from Mature Gas Assets | |
CN202546250U (en) | Rapid low-temperature liquid vaporization device | |
CN106091575A (en) | A kind of expanded air bypass amount being matched in external compression space division reduces device and reduction method | |
CN201525816U (en) | Rubber double-reactor elutriation coagulation device with low energy consumption | |
CN104998431A (en) | Comprehensive utilization device and method for steam condensate in fluorocarbon alkane production device | |
CN105924326B (en) | It is exclusively used in the flashing pressure stabilising arrangement of isooctane production | |
CN103011266B (en) | Improved titanium tetrachloride distillation process method | |
CN104846945A (en) | Pipe network differential compensation energy-saving water supply equipment with auxiliary pump | |
CN218936035U (en) | Ethylene receiving device | |
CN220229116U (en) | Condensate water recycling system containing flash steam |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20220214 Address after: 125000 office building, building 1-113, chemical Street, Lianshan District, Huludao City, Liaoning Province Patentee after: Hangjin Jinxi Chlor Alkali Chemical Co.,Ltd. Address before: No. 1, Lianshan chemical Street, Huludao, Liaoning Province Patentee before: HANGJIN TECHNOLOGY CO.,LTD. |