CN202439173U - Modified carbon dioxide injection system for producing foaming extruded sheets - Google Patents

Modified carbon dioxide injection system for producing foaming extruded sheets Download PDF

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Publication number
CN202439173U
CN202439173U CN2011205368952U CN201120536895U CN202439173U CN 202439173 U CN202439173 U CN 202439173U CN 2011205368952 U CN2011205368952 U CN 2011205368952U CN 201120536895 U CN201120536895 U CN 201120536895U CN 202439173 U CN202439173 U CN 202439173U
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CN
China
Prior art keywords
carbon dioxide
pipeline
links
high pressure
promoter
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Expired - Fee Related
Application number
CN2011205368952U
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Chinese (zh)
Inventor
马少云
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NINGXIA DINGSHENG YANGGUANG THERMAL INSULATION MATERIAL CO Ltd
Original Assignee
NINGXIA DINGSHENG YANGGUANG THERMAL INSULATION MATERIAL CO Ltd
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Priority to CN2011205368952U priority Critical patent/CN202439173U/en
Application granted granted Critical
Publication of CN202439173U publication Critical patent/CN202439173U/en
Anticipated expiration legal-status Critical
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Abstract

The utility model relates to production of foaming extruded sheets, particularly a modified carbon dioxide injection system for producing foaming extruded sheets, which is characterized in that liquid carbon dioxide and an accelerator are mixed under high pressure and injected into an extruder to perform foaming. The modified carbon dioxide injection system for producing foaming extruded sheets comprises a carbon dioxide delivery system and an accelerator delivery system, wherein the two systems are connected with a high-pressure mixer; and the liquid outlet of the high-pressure mixer is connected with an extruder through a pipeline. The utility model solves the problems of unstable physical shape, low foaming ratio and the like in the carbon dioxide injection process, thereby greatly enhancing the comprehensive properties of the extruded sheet products and achieving or exceeding the Chinese standard. The carbon dioxide and the accelerator are accurately and quantitatively delivered into the extruder system in a liquid form, so that the cells of the extruded sheet product are distributed uniformly and finely, and the performance indexes of the product achieve the requirements in Chinese Standard. The modified carbon dioxide injection system for producing foaming extruded sheets has the characteristics of reasonable structure configuration and the like, and is convenient to use.

Description

Produce the foaming extruded sheet with modification carbon dioxide injected system
Technical field
The utility model relates to the production of foaming extrusion molding sheet material, with particularly producing the foaming extruded sheet with modification carbon dioxide injected system.
Background technology
Traditional XPS extruded plastic foam warming plate production line is to use fluorine series blowing agent and chain hydrocarbon.As everyone knows, freon is the main cause that causes ozone hole, uses freon to be unfavorable for environmental protection, by international community is forbidden; And chain hydrocarbon has inflammability, influences production safety.
At present; The XPS plastic extrusion heated board that in the production of extruded plastic foam warming plate, has used carbon dioxide foaming agent to produce; But; Existing carbon dioxide foaming agent in injection process, gets into the carbon dioxide of body and the melt resolution is low, diffusance is high, cause and be difficult to mixing or mixing inhomogeneously with melt, and causing can't the ordinary production qualified product.And the boiling point of carbon dioxide is-78 ℃, in injection process, receives the influence of environment temperature and transient pressure, is prone to cause gasification or knot dry ice, causes carbon dioxide can not stablize injection, can't reach the purpose of smooth foaming.The insulation extruded sheet unit weight for building that the most generally uses according to national requirements requires 30kg/m 3More than, below the thermal conductivity factor 0.030w/mk, still, existing titanium dioxide carbon foaming extruded sheet just adds the use amount of carbon dioxide with reduction freon in freon, or the simple ethanol that adds is as auxiliary agent in carbon dioxide.The product unit weight of being produced is all at 36kg/m 3More than, cause the raw materials for production cost to increase by 20%; Thermal conductivity factor is greater than 0.030w/mk, and heat-insulating property can not be up to state standards fully, and this is that the technical staff knows together in the present technique field.
Summary of the invention
The purpose of the utility model is to solve the problem that prior art exists, and provides a kind of carbon dioxide foaming agent to inject the production foaming extruded sheet stable, that expansion ratio is high with modification carbon dioxide injected system.
For addressing the above problem, the utility model adopts following technical scheme:
A kind of production foaming extruded sheet is with modification carbon dioxide injected system; Comprise carbon dioxide fluid reservoir, measuring pump, vacuum tank; The liquid outlet that it is characterized in that the carbon dioxide fluid reservoir links to each other with the inlet of CO 2 high pressure delivery pump; The liquid outlet of CO 2 high pressure delivery pump links to each other with the carbon dioxide vacuum tank through pipeline; The inlet of CO 2 high pressure measuring pump links to each other with the carbon dioxide vacuum tank through pipeline, and the liquid outlet of CO 2 high pressure measuring pump links to each other with the high pressure mixing device through pipeline; The inlet of promoter voltage stabilizing measuring pump links to each other with the promoter fluid reservoir through pipeline; The liquid outlet of promoter voltage stabilizing measuring pump links to each other with the inlet of promoter high-pressure metering pump through pipeline, and the liquid outlet of the promoter high-pressure metering pump pipeline that was connected links to each other with the high pressure mixing device; The liquid outlet of high pressure mixing device links to each other with extruder through pipeline, on high pressure mixing device and pipeline that extruder links to each other, check valve is installed.
On the liquid outlet of above-mentioned promoter voltage stabilizing measuring pump and the pipeline between the promoter high-pressure metering pump, stable-pressure device is installed.
On the liquid outlet of above-mentioned CO 2 high pressure measuring pump and the pipeline that the high pressure mixing device links to each other the carbon dioxide check valve is installed.
On the liquid outlet of above-mentioned promoter high-pressure metering pump and the pipeline that the high pressure mixing device links to each other the promoter check valve is installed.
The characteristics of the utility model are following: 1, with liquid carbon dioxide with after promoter is mixed in the high pressure mixing device; Inject extruder; Solve carbon dioxide problems such as physical aspect is unstable in injection process, expansion ratio is on the low side, also goods unit weight has been reduced to 32 kg/m 3Or below, thermal conductivity factor is reduced to below the 0.028w/mk, thereby improves the combination property of extruded sheet goods greatly, reaches or is superior to national standard.2, adopt voltage stabilizing measuring pump and high-pressure metering pump with accurately quantitative being transported in the extruder system of form with liquid state of blowing agent carbon dioxide and promoter, thereby make extruded sheet goods distribution of cells uniform and delicate, the product properties index all reaches the GB requirement.3, this system has characteristics such as structure configuration is reasonable, easy to use.
Description of drawings
Fig. 1 is the utility model system architecture sketch map.
Among the figure: 1 carbon dioxide fluid reservoir, 2 CO 2 high pressure delivery pumps, 3 carbon dioxide vacuum tanks; 4 promoter voltage stabilizing measuring pumps, 5 promoter fluid reservoirs, 6 promoter check valves; 7 promoter high-pressure metering pumps, 8 CO 2 high pressure measuring pumps, 9 carbon dioxide check valves; 10 high pressure mixing devices, 11 check valves, 12 extruders.
The specific embodiment
As shown in Figure 1; The liquid outlet of carbon dioxide fluid reservoir 1 links to each other with the inlet of CO 2 high pressure delivery pump 2; The liquid outlet of CO 2 high pressure delivery pump 2 links to each other with carbon dioxide vacuum tank 3 through pipeline; The inlet of CO 2 high pressure measuring pump 8 links to each other with carbon dioxide vacuum tank 3 through pipeline; The liquid outlet of CO 2 high pressure measuring pump links to each other with high pressure mixing device 10 through pipeline, on CO 2 high pressure measuring pump and pipeline that the high pressure mixing device links to each other, carbon dioxide check valve 9 is installed; The inlet of promoter voltage stabilizing measuring pump 4 links to each other with promoter fluid reservoir 5 through pipeline; The liquid outlet of promoter voltage stabilizing measuring pump links to each other with the inlet of promoter high-pressure metering pump 7 through pipeline; The liquid outlet of the promoter high-pressure metering pump pipeline that was connected links to each other with the high pressure mixing device, on promoter high-pressure metering pump and pipeline that the high pressure mixing device links to each other, promoter check valve 6 is installed; The liquid outlet of high pressure mixing device links to each other with extruder 12 through pipeline, on high pressure mixing device and pipeline that extruder links to each other, check valve 11 is installed.For the pressure stability of the accelerator systems that guarantees, on the liquid outlet of voltage stabilizing measuring pump and the pipeline between the promoter high-pressure metering pump, stable-pressure device is installed.

Claims (4)

1. produce the foaming extruded sheet with modification carbon dioxide injected system for one kind; Comprise carbon dioxide fluid reservoir, measuring pump, vacuum tank; The liquid outlet that it is characterized in that carbon dioxide fluid reservoir (1) links to each other with the inlet of CO 2 high pressure delivery pump (2); The liquid outlet of CO 2 high pressure delivery pump (2) links to each other with carbon dioxide vacuum tank (3) through pipeline; The inlet of CO 2 high pressure measuring pump (8) links to each other with carbon dioxide vacuum tank (3) through pipeline, and the liquid outlet of CO 2 high pressure measuring pump (8) links to each other with high pressure mixing device (10) through pipeline; The inlet of promoter voltage stabilizing measuring pump (4) links to each other with promoter fluid reservoir (5) through pipeline; The liquid outlet of promoter voltage stabilizing measuring pump (4) links to each other with the inlet of promoter high-pressure metering pump (7) through pipeline, and the liquid outlet of promoter high-pressure metering pump (7) links to each other with the high pressure mixing device through pipeline; The liquid outlet of high pressure mixing device links to each other with extruder (12) through pipeline, on high pressure mixing device and pipeline that extruder links to each other, check valve is installed.
2. production according to claim 1 foaming extruded sheet is with modification carbon dioxide injected system, it is characterized in that on the liquid outlet of above-mentioned promoter voltage stabilizing measuring pump (4) and the pipeline between the promoter high-pressure metering pump (7), stable-pressure device being installed.
3. production according to claim 2 foaming extruded sheet is with modification carbon dioxide injected system, on the liquid outlet that it is characterized in that above-mentioned CO 2 high pressure measuring pump (8) and the pipeline that high pressure mixing device (10) links to each other carbon dioxide check valve (9) is installed.
4. production according to claim 3 foaming extruded sheet is with modification carbon dioxide injected system, on the liquid outlet that it is characterized in that above-mentioned promoter high-pressure metering pump (7) and the pipeline that the high pressure mixing device links to each other promoter check valve (6) is installed.
CN2011205368952U 2011-12-20 2011-12-20 Modified carbon dioxide injection system for producing foaming extruded sheets Expired - Fee Related CN202439173U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011205368952U CN202439173U (en) 2011-12-20 2011-12-20 Modified carbon dioxide injection system for producing foaming extruded sheets

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011205368952U CN202439173U (en) 2011-12-20 2011-12-20 Modified carbon dioxide injection system for producing foaming extruded sheets

Publications (1)

Publication Number Publication Date
CN202439173U true CN202439173U (en) 2012-09-19

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CN2011205368952U Expired - Fee Related CN202439173U (en) 2011-12-20 2011-12-20 Modified carbon dioxide injection system for producing foaming extruded sheets

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102490306A (en) * 2011-12-20 2012-06-13 宁夏鼎盛阳光保温材料有限公司 Injection method and system of modified carbon dioxide for producing foamed extruded sheet
CN103231458A (en) * 2013-04-28 2013-08-07 宁夏鼎盛阳光保温材料有限公司 Device for manufacturing modified carbon dioxide foaming agent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102490306A (en) * 2011-12-20 2012-06-13 宁夏鼎盛阳光保温材料有限公司 Injection method and system of modified carbon dioxide for producing foamed extruded sheet
CN103231458A (en) * 2013-04-28 2013-08-07 宁夏鼎盛阳光保温材料有限公司 Device for manufacturing modified carbon dioxide foaming agent

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120919

Termination date: 20151220

EXPY Termination of patent right or utility model