CN201534827U - Oxidized polyethylene wax producing device - Google Patents
Oxidized polyethylene wax producing device Download PDFInfo
- Publication number
- CN201534827U CN201534827U CN200920240368XU CN200920240368U CN201534827U CN 201534827 U CN201534827 U CN 201534827U CN 200920240368X U CN200920240368X U CN 200920240368XU CN 200920240368 U CN200920240368 U CN 200920240368U CN 201534827 U CN201534827 U CN 201534827U
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- kettle
- polymeric kettle
- polymerization
- fusion
- still
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Abstract
The utility model relates to a producing facility of chemical products, in particular to an oxidized polyethylene wax producing device which comprises a polymerization kettle, wherein a polymerization kettle charging port of the polymerization kettle is connected with a fusion kettle discharging port of a fusion kettle through a pipeline, the fusion kettle discharging port is positioned higher than the fusion kettle discharging port, a polymerization kettle discharging port of the polymerization kettle is connected with a discharging pipeline, a hot oil output pipeline of a warming-up device is respectively connected with a polymerization kettle oil inlet valve on the lower portion of a polymerization kettle jacket and a fusion kettle oil inlet valve on the lower portion of a fusion kettle jacket through a transfer pump, moreover, a polymerization kettle oil outlet valve on the upper portion of the polymerization kettle jacket and a fusion kettle oil outlet valve on the upper portion of the fusion kettle jacket are respectively connected with a hot oil input pipeline of the warming-up device. The oxidized polyethylene wax producing device has simple structure and convenient operation, the temperature is constant when melting materials are added, and the control of adding quantity is accurate, thus the quality of polymerization products is guaranteed, and the working efficiency is enhanced.
Description
Technical field:
The utility model relates to a kind of Chemicals production unit, especially a kind of oxidized polyethlene wax production equipment.
Background technology:
At present, in the production preparation process of traditional oxidized polyethlene wax, earlier partial material is added in the polymeric kettle, then polymeric kettle is heated, in reaction process, in polymeric kettle, add all the other again and melt good material in advance, carry out polyreaction to cooperate the material in the polymeric kettle by opening for feed, this production process efficient is low, and adopt and to manually add material, can't accurately control its addition, impact for easily the polyreaction of material.In addition, be to heat in advance to melt well by the material that manually adds, in the interpolation process, can't keep the homoeostasis of its temperature, cause certain influence also can for the polyreaction of material in the polymeric kettle, finally influence the quality of polyreaction product.
The utility model content:
The utility model provides a kind of oxidized polyethlene wax production equipment, and it is simple in structure, and is easy to operate, the homo(io)thermism when material that melts adds, the addition precise control has guaranteed the quality of polyreaction product, improve production efficiency, solved problems of the prior art.
The utility model is to solve the problems of the technologies described above the technical scheme that is adopted to be: it comprises polymeric kettle, the polymeric kettle opening for feed of polymeric kettle is higher than the thawing still of polymeric kettle opening for feed by pipeline and position thawing still discharge port links to each other, and the polymeric kettle discharge port of polymeric kettle links to each other with the discharging pipeline; The deep fat delivery conduit of warming apparatus links to each other with the thawing still fuel charging valve that melts still chuck bottom with the polymeric kettle fuel charging valve of jacket of polymerization bottom respectively through transferpump, and the polymeric kettle delivery valve on jacket of polymerization top links to each other with the deep fat intake line of warming apparatus respectively with the thawing still delivery valve that melts still chuck top.
The utility model adopts such scheme, simple in structure, easy to operate, during work, in polymeric kettle, add the partial reaction material earlier, the reaction mass that all the other are to be melted adds in the thawing still, open warming apparatus, by transferpump about 200 ℃ deep fat being sent into jacket of polymerization by transfer line heats to material with melting in the still chuck, after waiting to melt the material thawing in the still, open and melt the still discharge port and control its flow, be higher than the polymeric kettle opening for feed owing to melt still discharge port position, material relies on own wt progressively to be added drop-wise in the polymeric kettle through the polymeric kettle opening for feed by pipeline, carries out polyreaction with material in the polymeric kettle, compare with the existing artificial production equipment that melts material that adds, temperature when having guaranteed to melt material in the still and entering in the polymeric kettle and drip speed has alleviated labor intensity of operating personnel, and after the polyreaction quality of product is better, production efficiency of products is higher, has saved production cost.
Description of drawings:
Fig. 1 is a structural representation of the present utility model.
Among the figure, 1, polymeric kettle; 2, polymeric kettle opening for feed; 3, melt still; 4, melt the still discharge port; 5, polymeric kettle discharge port; 6, warming apparatus; 7, transferpump; 8, jacket of polymerization; 9, polymeric kettle fuel charging valve; 10, melt the still chuck; 11, melt the still fuel charging valve; 12, polymeric kettle delivery valve; 13, melt the still delivery valve.
Embodiment:
For clearly demonstrating the technical characterstic of this programme, below by embodiment, and in conjunction with its accompanying drawing, the utility model is elaborated.
As shown in FIG., the utility model comprises polymeric kettle 1, and the polymeric kettle opening for feed 2 of polymeric kettle 1 is higher than the thawing still 3 of polymeric kettle opening for feed 2 by pipeline and position thawing still discharge port 4 links to each other, and the polymeric kettle discharge port 5 of polymeric kettle 1 links to each other with the discharging pipeline; The deep fat delivery conduit of warming apparatus 6 links to each other with the thawing still fuel charging valve 11 that melts still chuck 10 bottoms with the polymeric kettle fuel charging valve 9 of jacket of polymerization 8 bottoms respectively through transferpump 7, and the polymeric kettle delivery valve 12 on jacket of polymerization 8 tops links to each other with the deep fat intake line of warming apparatus 6 respectively with the thawing still delivery valve 13 that melts still chuck 10 tops.
During use, in polymeric kettle 1, add the partial reaction material earlier, the reaction mass that all the other are to be melted adds in the thawing still 3, open warming apparatus 6, by transferpump 7 about 200 ℃ deep fat being sent into jacket of polymerization 8 by transfer line heats to material with melting in the still chuck 10, after waiting to melt the material thawing in the still 3, open and melt still discharge port 4 and control its mass flow, be higher than polymeric kettle opening for feed 2 owing to melt still discharge port 4 positions, material relies on own wt progressively to be added drop-wise in the polymeric kettle 1 through polymeric kettle opening for feed 2 by pipeline, carries out polyreaction with material in the polymeric kettle 1.Adopt this production equipment, alleviated labor intensity of operating personnel, guaranteed to be added into the accuracy of dripping speed of material in the polymeric kettle 1, the stability of temperature makes after the polyreaction quality of product better, and production efficiency of products is higher, has saved production cost.
The utility model does not describe part in detail, is those skilled in the art of the present technique's known technology.
Claims (1)
1. oxidized polyethlene wax production equipment, comprise polymeric kettle, it is characterized in that: the polymeric kettle opening for feed of polymeric kettle is higher than the thawing still of polymeric kettle opening for feed by pipeline and position thawing still discharge port links to each other, and the polymeric kettle discharge port of polymeric kettle links to each other with the discharging pipeline; The deep fat delivery conduit of warming apparatus links to each other with the thawing still fuel charging valve that melts still chuck bottom with the polymeric kettle fuel charging valve of jacket of polymerization bottom respectively through transferpump, and the polymeric kettle delivery valve on jacket of polymerization top links to each other with the deep fat intake line of warming apparatus respectively with the thawing still delivery valve that melts still chuck top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920240368XU CN201534827U (en) | 2009-10-26 | 2009-10-26 | Oxidized polyethylene wax producing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920240368XU CN201534827U (en) | 2009-10-26 | 2009-10-26 | Oxidized polyethylene wax producing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201534827U true CN201534827U (en) | 2010-07-28 |
Family
ID=42534609
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920240368XU Expired - Fee Related CN201534827U (en) | 2009-10-26 | 2009-10-26 | Oxidized polyethylene wax producing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201534827U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103910814A (en) * | 2013-11-28 | 2014-07-09 | 大连隆星新材料有限公司 | Oxidation device for polyethylene wax |
-
2009
- 2009-10-26 CN CN200920240368XU patent/CN201534827U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103910814A (en) * | 2013-11-28 | 2014-07-09 | 大连隆星新材料有限公司 | Oxidation device for polyethylene wax |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shandong Zouping Dazhan New Materials Co., Ltd. Assignor: Shandong Zouping Jindu Industry Co., Ltd. Contract record no.: 2011370000178 Denomination of utility model: Oxidized polyethylene wax producing device Granted publication date: 20100728 License type: Exclusive License Record date: 20110510 |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100728 Termination date: 20101026 |