CN102093590A - Waste plastic conditioning and viscosity modifying system - Google Patents
Waste plastic conditioning and viscosity modifying system Download PDFInfo
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- CN102093590A CN102093590A CN2010105740447A CN201010574044A CN102093590A CN 102093590 A CN102093590 A CN 102093590A CN 2010105740447 A CN2010105740447 A CN 2010105740447A CN 201010574044 A CN201010574044 A CN 201010574044A CN 102093590 A CN102093590 A CN 102093590A
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- separation tower
- vacuum
- vacuum separation
- raw material
- viscosity
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Abstract
The invention relates to a reaction system for polymers in chemical fiber industry, in particular to a waste plastic conditioning and viscosity modifying system, which comprises a vacuum separation tower (1), wherein a raw material inlet (3) and a vacuum opening (2) are formed above the vacuum separation tower (1); a discharge opening (6) is formed below the vacuum separation tower (1); the outside surface of the vacuum separation tower (1) is provided with a hot medium coil (4); porous plates (5) are arranged at intervals in the vertical direction in the vacuum separation tower (1); and the discharge opening (6) is also connected with a two-stage conditioning and viscosity modifying device. With the additional two-stage conditioning and viscosity modifying device with a screw arranged inside, raw material can be pushed and stirred to improve viscosity; a vacuum pump is adopted to further improve vacuum degree, and a reaction environment is provided for improving the viscosity of the raw material; and the combination of the factors promotes the obvious improvement on the production efficiency of high-viscosity poly(ethylene terephthalate) (PET) plastic raw material.
Description
Technical field
The present invention relates to a kind of reactive system of chemical fibre industry polymkeric substance, relate in particular to the sticking system of the modified accent of a kind of plastic waste.
Background technology
The sticking technology of modified accent that is used for the plastic waste raw material of terylene short fiber production at present mainly is: the liquid plastic waste raw material after the fusion is sent into its special-purpose vacuum separation tower, multi-layer porous plate is arranged in the vacuum separation tower, liquid raw material successively increases surface-area by porous plate, low molecular impurity gasification is separated, improve the purity and the viscosity of raw material, promote the quality of finished product product greatly.
By above method, can be with the viscosity system of raw material 0.5 0.68 when being increased to discharging when beginning to import.Can satisfy processing requirement fully though the PET plastic raw materials that this technology is produced is made common silk, when making high strength silk or industry silk, need viscous modulus to reach more than 0.7.Test through tackify:, can increase the vacuum tightness in the vacuum separation tower in order to improve the viscous modulus of PET raw material.After material viscosity increases, the rapid variation of fluidity of molten, flow velocity is slow, increases discharging time greatly, has a strong impact on production efficiency.If viscous modulus is increased to more than 0.75, will cause melt feed to flow downward, make parturient paresis.
Therefore, how to improve the production high viscosity especially the production efficiency of the PET plastic raw materials of viscous modulus more than 0.7 become a technical barrier.
Summary of the invention
The invention provides the sticking system of the modified accent of a kind of plastic waste, can high efficiency production high viscosity the PET plastic raw materials of viscous modulus more than 0.7 especially.In order to realize the foregoing invention purpose, the present invention has adopted following technique means:
The modified accent of a kind of plastic waste glues system, comprises the vacuum separation tower; Described vacuum separation tower top is provided with feed(raw material)inlet and vacuum port; Described vacuum separation tower below is provided with discharge port; Described vacuum separation tower appearance is provided with the heating agent coil pipe; Be arranged at intervals with porous plate on the described vacuum separation tower internal vertical direction; Described discharge port also connects the sticking device of a modified accent of secondary.
The sticking device of the modified accent of described secondary comprises casing and the vacuum pump that is interconnected; Described casing appearance is provided with heating coil, and inside is provided with the screw rod of screw-blade, and described screw rod is by electric motor driving; Position near the screw rod two ends on the described casing is provided with opening for feed and delivery port respectively, and described opening for feed is communicated with the discharge port sealing, and described delivery port is connected with transferpump;
The heating coil of casing appearance coils along screw axial.
Beneficial effect of the present invention is: owing to added the sticking device of a modified accent of secondary, be provided with screw rod in this device, not only can promote raw material, and can stir raw material and improve viscosity; Singly add a vacuum pump, further gas clean-up is for material viscosity provides reaction environment.More than these factor in conjunction with having facilitated the obvious raising of High Viscosity PET plastic raw materials production efficiency.
Description of drawings
Fig. 1 is the structural representation of the sticking system of the modified accent of plastic waste of the present invention.
Embodiment
Below in conjunction with accompanying drawing, the preferred implementation of the sticking system of the modified accent of plastic waste of the present invention is made detailed description:
As shown in Figure 1, the sticking system of the modified accent of this plastic waste comprises vacuum separation tower 1 and the sticking device of the modified accent of secondary.Vacuum separation tower 1 is identical with prior art, and tower body is a round shape, and the top is provided with feed(raw material)inlet 3 and vacuum port 2, and the below is provided with discharge port 6; Coiling is provided with heating agent coil pipe 4 on the outside surface, and coil direction is axially identical with vacuum separation tower 1; Be arranged at intervals with a plurality of porous plates 5 on the tower body internal vertical direction.
The sticking device main body of the modified accent of secondary is a horizontally disposed cylindrical box 11, and it is connected with vacuum pump 14; The two ends of casing 11 are offered opening for feed 12 and delivery port 9 respectively, and the discharge port of opening for feed 12 and vacuum separation tower 16 is connected delivery port 9 external transferpumps 8 by flange; Casing 11 outside surfaces coil vertically heating coil 7 are set; Be parallel in the casing 11 screw rod 10 that has screw-blade axially is set, it is near the inwall bottom surface of casing 11, opening for feed 11 is positioned at the top of screw rod 9, delivery port 9 is positioned at the below of screw rod 10, screw rod 10 is driven by motor 14, and the screw rod 10 of band screw-blade and motor 13 are formed a stirring puopulsion unit.
Liquid PET raw material enters vacuum separation tower 1 inside of high temperature (4 heating of heating agent coil pipe) high vacuum by feed(raw material)inlet 3, liquid raw material increases surface-area through the multi-layer porous plate 5 of vacuum separation tower 1 inside, low molecular impurity gasification back is detached by vacuum port 2, improve material purity, simultaneously under action of gravity by some porous plate 5 preliminary purification tackifies, when making viscous modulus by pan feeding 0.5 is increased to 0.68, reach the sticking purpose of elementary modified accent, enter the sticking device of the modified accent of secondary by discharge port 6 outflows then.
When flowing in the casing 11 through the sticking liquid raw material of elementary modified accent, and the vacuum pump 14 of casing 11 by the outside makes its internal vacuum than vacuum separation tower 1 higher one-level, thereby the interior low molecular impurity of liquid raw material of inflow is further gasified, fully detach, make the purity of raw material higher, simultaneously under high vacuum state, the stirring of the screw-blade by screw rod 10, the raw molecule structure realizes rearranging, (coefficient is promoted to more than 0.70 to increase material viscosity, reach the processing requirement of production high strength silk), the sticking work of the modified accent of secondary is finished.At last, again by the pushing effect of the screw-blade of screw rod 10, mobile variation and viscosity enhanced liquid raw material is delivered to transferpump 8, transferpump 8 output raw material production spinning.
Claims (3)
1. the sticking system of the modified accent of plastic waste comprises vacuum separation tower (1); Described vacuum separation tower (1) top is provided with feed(raw material)inlet (3) and vacuum port (2); Described vacuum separation tower (1) below is provided with discharge port (6); Described vacuum separation tower (1) appearance is provided with heating agent coil pipe (4); Be arranged at intervals with porous plate (5) on described vacuum separation tower (1) the internal vertical direction; It is characterized in that: described discharge port (6) also connects the sticking device of a modified accent of secondary.
2. the modified accent of plastic waste according to claim 1 glues system, it is characterized in that: the sticking device of the modified accent of described secondary comprises casing (11) and the vacuum pump (14) that is interconnected; Described casing (11) appearance is provided with heating coil (7), and inside is provided with the screw rod (10) of screw-blade, and described screw rod (10) is driven by motor (13); The position that described casing (11) is gone up near screw rod (10) two ends is provided with opening for feed (12) and delivery port (9) respectively, and described opening for feed (12) is communicated with discharge port (6) sealing, and described delivery port (9) is connected with transferpump (8).
3. the modified accent of plastic waste according to claim 2 glues system, it is characterized in that: the heating coil (7) of casing (11) appearance is along axially coiling of screw rod (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010105740447A CN102093590B (en) | 2010-12-01 | 2010-12-01 | Waste plastic conditioning and viscosity modifying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010105740447A CN102093590B (en) | 2010-12-01 | 2010-12-01 | Waste plastic conditioning and viscosity modifying system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102093590A true CN102093590A (en) | 2011-06-15 |
| CN102093590B CN102093590B (en) | 2012-05-30 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010105740447A Active CN102093590B (en) | 2010-12-01 | 2010-12-01 | Waste plastic conditioning and viscosity modifying system |
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| CN (1) | CN102093590B (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102877156A (en) * | 2012-10-19 | 2013-01-16 | 宁波大发化纤有限公司 | Preparation method of anti-flaming recyle polyester staple fiber |
| CN102877157A (en) * | 2012-10-19 | 2013-01-16 | 宁波大发化纤有限公司 | Preparation method of antibacterial flame-retardant sound-insulation heat-insulation polyester staple fibers |
| CN102899729A (en) * | 2012-10-19 | 2013-01-30 | 宁波大发化纤有限公司 | Method for processing regenerated polyester staple fiber by using waste polyester textile |
| CN103147162A (en) * | 2013-03-21 | 2013-06-12 | 宁波大发化纤有限公司 | Sheath-core type polyester short fiber with core layer made of recycled polyester and preparation method thereof |
| CN103147163A (en) * | 2013-03-21 | 2013-06-12 | 宁波大发化纤有限公司 | Skin-core type recycled polyester staple fiber and preparation method thereof |
| WO2014146588A1 (en) * | 2013-03-21 | 2014-09-25 | 宁波大发化纤有限公司 | Method for preparing high-melting-point recycled polyester used for sheath-core polyester staple fiber layer, and application thereof |
| CN106279757A (en) * | 2016-08-15 | 2017-01-04 | 宁波大发化纤有限公司 | The method that glycolysis alcoholysis Waste Polyester textile preparation height joins quality melt |
| CN106279656A (en) * | 2016-08-15 | 2017-01-04 | 宁波大发化纤有限公司 | The method that 1.4 butanediol alcoholysis Waste Polyester textile preparation height join quality melt |
| CN106279758A (en) * | 2016-08-15 | 2017-01-04 | 宁波大发化纤有限公司 | The method that 2,2'-ethylenedioxybis(ethanol). alcoholysis Waste Polyester textile preparation height joins quality melt |
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| CN201890854U (en) * | 2010-12-01 | 2011-07-06 | 宁波大发化纤有限公司 | Quality and viscosity regulation system for waste plastic |
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Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102877157B (en) * | 2012-10-19 | 2014-08-27 | 宁波大发化纤有限公司 | Preparation method of antibacterial flame-retardant sound-insulation heat-insulation polyester staple fibers |
| CN102877157A (en) * | 2012-10-19 | 2013-01-16 | 宁波大发化纤有限公司 | Preparation method of antibacterial flame-retardant sound-insulation heat-insulation polyester staple fibers |
| CN102899729A (en) * | 2012-10-19 | 2013-01-30 | 宁波大发化纤有限公司 | Method for processing regenerated polyester staple fiber by using waste polyester textile |
| CN102899729B (en) * | 2012-10-19 | 2015-08-26 | 宁波大发化纤有限公司 | The method of Waste Polyester textile processing Regenerated Polyester Staple Fiber dimension |
| CN102877156A (en) * | 2012-10-19 | 2013-01-16 | 宁波大发化纤有限公司 | Preparation method of anti-flaming recyle polyester staple fiber |
| CN102877156B (en) * | 2012-10-19 | 2014-08-13 | 宁波大发化纤有限公司 | Preparation method of anti-flaming recyle polyester staple fiber |
| WO2014146590A1 (en) * | 2013-03-21 | 2014-09-25 | 宁波大发化纤有限公司 | Sheath-core polyester staple fiber employing recycled polyester as core layer and method for manufacturing the fiber |
| WO2014146588A1 (en) * | 2013-03-21 | 2014-09-25 | 宁波大发化纤有限公司 | Method for preparing high-melting-point recycled polyester used for sheath-core polyester staple fiber layer, and application thereof |
| CN103147163A (en) * | 2013-03-21 | 2013-06-12 | 宁波大发化纤有限公司 | Skin-core type recycled polyester staple fiber and preparation method thereof |
| WO2014146591A1 (en) * | 2013-03-21 | 2014-09-25 | 宁波大发化纤有限公司 | Skin-core type recycled polyester staple fiber and preparation method thereof |
| CN103147163B (en) * | 2013-03-21 | 2015-03-18 | 宁波大发化纤有限公司 | Skin-core type recycled polyester staple fiber and preparation method thereof |
| CN103147162A (en) * | 2013-03-21 | 2013-06-12 | 宁波大发化纤有限公司 | Sheath-core type polyester short fiber with core layer made of recycled polyester and preparation method thereof |
| CN103147162B (en) * | 2013-03-21 | 2015-09-16 | 宁波大发化纤有限公司 | Sandwich layer adopts core-skin type polyester staple fiber of recycled polyester and preparation method thereof |
| CN106279757A (en) * | 2016-08-15 | 2017-01-04 | 宁波大发化纤有限公司 | The method that glycolysis alcoholysis Waste Polyester textile preparation height joins quality melt |
| CN106279656A (en) * | 2016-08-15 | 2017-01-04 | 宁波大发化纤有限公司 | The method that 1.4 butanediol alcoholysis Waste Polyester textile preparation height join quality melt |
| CN106279758A (en) * | 2016-08-15 | 2017-01-04 | 宁波大发化纤有限公司 | The method that 2,2'-ethylenedioxybis(ethanol). alcoholysis Waste Polyester textile preparation height joins quality melt |
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| CN102093590B (en) | 2012-05-30 |
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Effective date of registration: 20220809 Address after: No.266 Binhai 2nd Road, Hangzhou Bay New District, Ningbo City, Zhejiang Province Patentee after: Ningbo Dafa New Material Co.,Ltd. Address before: Ningbo Dafa Chemical Fiber Co., Ltd., Haibin 2nd Road, Hangzhou Bay New District, Ningbo City, Zhejiang Province, 315323 Patentee before: NINGBO DAFA CHEMICAL FIBER Co.,Ltd. |