CN202506141U - Monomer recovery system - Google Patents
Monomer recovery system Download PDFInfo
- Publication number
- CN202506141U CN202506141U CN2012200987109U CN201220098710U CN202506141U CN 202506141 U CN202506141 U CN 202506141U CN 2012200987109 U CN2012200987109 U CN 2012200987109U CN 201220098710 U CN201220098710 U CN 201220098710U CN 202506141 U CN202506141 U CN 202506141U
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- CN
- China
- Prior art keywords
- recovery system
- monomer recovery
- exhaust pipe
- heat preservation
- separation device
- 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 - Lifetime
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Abstract
The utility model relates to a monomer recovery system which comprises a measuring tank and a measuring tank exhaust pipe connected with the measuring tank. A heat preservation separation device is connected with the other end of the measuring tank exhaust pipe, a heat preservation separation device exhaust pipe is connected with the upper portion of the heat preservation separation device, and the other end of the heat preservation separation device exhaust pipe is arranged in a condensation water tank. The monomer recovery system enables reacting monomers to be recycled to the greatest degree, saves recourses and cost, is environment-friendly and cannot influence normal production or waste manpower and material resources due to repeated clearing and extracting of crystals in a water storage tank.
Description
Technical field
The utility model relates to a kind of MONOMER RECOVERY system.
Background technology
Aborning, the MONOMER RECOVERY system is to produce the water that contains the 10%-12% monomer in producing extraction, through vapo(u)rization system; Through Steam Heating, discharge water, make concentration reach 50%-60% and put into batch box, continue heating by batch box and improve the process that concentration reaches reuse requirement (80%-90%); In order to make concentration reach the reuse requirement, the temperature of batch box generally is controlled at 125 ℃-130 ℃, because temperature is high; Can take a part of monomer out of when discharging steam,, enter extraction water to the vapour that has monomer and store the bucket reuse for cutting the waste; Because of extraction water storage barrel temperature is low, have only about 80 ℃, be easy to generate partially crystallizable; Will often clear up crystalline solid, waste of manpower, material resources also can have influence on normally carrying out of production.
Be improved to separating barrel that has heat insulation function of installation to above-mentioned defective at present; Batch box is discharged the vapour that contains monomer enter separating barrel; 100 ℃-105 ℃ of separating barrel insulations can let steam continue to discharge like this, and the monomer separation that contains is in bucket; The gas of discharging is through cool back usefulness naturally, and isolated monomer can be recycled in the batch box.
The utility model content
The purpose of the utility model provides a kind of above-mentioned shortcoming that overcomes, and a kind of MONOMER RECOVERY system that can fully reclaim monomer is provided.
The technical scheme that realizes the utility model purpose is: a kind of MONOMER RECOVERY system; Comprise batch box; The batch box blast pipe that is connected with batch box; The batch box blast pipe other end connects the insulation separator, and insulation separator top connects insulation separator blast pipe, and the insulation separator blast pipe other end places condensate draining.
Above-mentioned MONOMER RECOVERY system, said insulation separator is a separating barrel.
Above-mentioned MONOMER RECOVERY system, the holding temperature of said insulation separator is 100 ℃～105 ℃.
The utlity model has positive effect: the monomer in (1) reaction is farthest recycled, and economizes on resources, and cost is saved in environmental protection; (2) can not influence normal production because of the crystalline solid in the cleaning extraction water bucket repeatedly.
Description of drawings
For the content that makes the utility model is expressly understood more easily,, the utility model is done further detailed explanation, wherein below according to specific embodiment and combine accompanying drawing
Fig. 1 is the utility model MONOMER RECOVERY system architecture sketch map.
1 batch box wherein, 2 batch box blast pipes, 3 insulation separators, 4 insulation separator blast pipes, 5 condensate drainings.
The specific embodiment
(embodiment 1)
See Fig. 1; The utility model comprises batch box 1, and the batch box blast pipe 2 that is connected with batch box 1, batch box blast pipe 2 other ends connect insulation separator 3; Insulation separator 3 tops connect insulation separator blast pipe 4; Insulation separator blast pipe 4 other ends place condensate draining 5, and insulation separator 3 is a separating barrel, and holding temperature is 100 ℃～105 ℃.
Above-described specific embodiment; Purpose, technical scheme and beneficial effect to the utility model have carried out further explain, it should be understood that the above is merely the specific embodiment of the utility model; Be not limited to the utility model; All within the spirit and principle of the utility model, any modification of being made, be equal to replacement, improvement etc., all should be included within the protection domain of the utility model.
Claims (3)
1. MONOMER RECOVERY system; Comprise batch box (1); The batch box blast pipe (2) that is connected with batch box (1); It is characterized in that: batch box blast pipe (2) other end connects insulation separator (3), and insulation separator (3) top connects insulation separator blast pipe (4), and insulation separator blast pipe (4) other end places condensate draining (5).
2. according to the said MONOMER RECOVERY of claim 1 system, it is characterized in that: insulation separator (3) is separating barrel.
3. according to the said MONOMER RECOVERY of claim 2 system, it is characterized in that: the holding temperature of insulation separator (3) is 100 ℃～105 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200987109U CN202506141U (en) | 2012-03-16 | 2012-03-16 | Monomer recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200987109U CN202506141U (en) | 2012-03-16 | 2012-03-16 | Monomer recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202506141U true CN202506141U (en) | 2012-10-31 |
Family
ID=47058649
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200987109U Expired - Lifetime CN202506141U (en) | 2012-03-16 | 2012-03-16 | Monomer recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202506141U (en) |
-
2012
- 2012-03-16 CN CN2012200987109U patent/CN202506141U/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20121031 |