CN201579894U - Melt polycondensation macromolecular waste material regeneration device - Google Patents

Melt polycondensation macromolecular waste material regeneration device Download PDF

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Publication number
CN201579894U
CN201579894U CN2010201078689U CN201020107868U CN201579894U CN 201579894 U CN201579894 U CN 201579894U CN 2010201078689 U CN2010201078689 U CN 2010201078689U CN 201020107868 U CN201020107868 U CN 201020107868U CN 201579894 U CN201579894 U CN 201579894U
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CN
China
Prior art keywords
cylindrical shell
melt polycondensation
source material
regeneration device
liquid level
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Expired - Fee Related
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CN2010201078689U
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Chinese (zh)
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成强
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Individual
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Individual
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Priority to CN2010201078689U priority Critical patent/CN201579894U/en
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

The utility model relates to a melt polycondensation macromolecular regeneration device which belongs to the chemical fiber and plastic processing equipment technical field; a stirring shaft with stirring discs is arranged in a cylindrical barrel body; the utility model enables the purer melt obtained from the melt polycondensation macromolecular waste material by a physical method to finish the relative technique process of alcoholysis or hydrolysis so that the molecular chain structure can be essentially changed, the polyolefin and derivant organic impurities such as PVC, PP and PE in the recovered source material are eliminated, the purity and quality of the regenerated source material are accordingly improved, the uniformity, impurity content and the final quality of the polyester formed by the regenerative source material are greatly higher than the same indexes of the source material; thereby, the melt polycondensation macromolecular regeneration device is widely applicable to the industrial fields with higher quality requirement of source material, including POY long yarn, three-dimensional sandwich, FDY, non-woven cloth, moderate-strength industrial yarn and recycled bottle, reduces the demands on original source material and the consumption of petroleum resource, and facilitates realizing recycle economy.

Description

The melt polycondensation high polymer old material regeneration device
Technical field
The utility model relates to a kind of melt polycondensation high polymer old material regeneration device, improve the quality quality of melt polycondensation high polymer old material recovery regeneration by this device, be specifically related to the regeneration of macromolecule waste and scraps such as polyester, polyamide, Merlon, belong to chemical fibre, device of plastic processing technical field.
Background technology
The reclaiming of existing high polymer old material realizes by the physics method or by chemical method.
The characteristics of physics method be exactly whole process be core with the physical change, pass through processes such as pulverizing, screening, clear, oven dry usually, regenerative raw materials carries out chemical fibre, processing of plastic with regard to directly fusion, after filtering then.
The characteristics of chemical method be exactly whole process be core with the chemical reaction, reclaimed materials needs after chemical reaction further to improve some quality index or several quality index.Chemical method can improve some inherent quality index of raw material from changing structure in essence; Chemical method not only can be removed the organic impurities that mechanical admixture can also be removed other non-PET classes, thereby improves the quality of product.
There are following some shortcomings in existing physics method: it is very high that (1) requires to reclaim material quality, " particular about food " phenomenon of originating highly stable; (2) even reached the quality requirements of raw material, also because reclaimed materials has always passed through processing, the quality that causes in process descends and cannot repair; (3) quality uniformity of raw material does not reach the high-quality of industrialized unit, successional requirement.
Summary of the invention
The purpose of this utility model is the physics method above shortcomings that reclaim raw material regeneration at existing, provide and to change molecular chain structure, polyolefin and derivative class organic impurities thereof such as PVC, the PP in the removal recovery raw material, PE, thereby a kind of melt polycondensation high polymer old material regeneration device that the chemical method of the purity of raising regenerative raw materials and quality uses.
The purpose of this utility model is achieved through the following technical solutions, a kind of melt polycondensation high polymer old material regeneration device, it is characterized in that, described regeneration uses device by cylindrical tube, the cylindrical shell two ends are through the bolted end cap of lip weldering sealing flange, the oblique anti-blocking liquid level gauge mouth down that end cap is provided with near the bottom, the combination vacuum seal mechanism that tape spool that respective end covers holds is passed at the shaft two ends that are provided with in the cylindrical shell, the stirring disc of fixed interval successively from front to back on the shaft, an end is fixed on the baffle plate that has opening on the cylinder inboard wall between the stirring disc, the heating agent chuck of the cylindrical shell outside and the welding of end cap outer face, the charging aperture of the bottom solid welding of the close front end of cylindrical shell and cylindrical shell are near the discharging opening of the bottom solid welding of rear end, and the gas phase mouth of the cylindrical shell top solid welding of corresponding discharging opening constitutes; Bottom near an end end cap is provided with anti-blocking liquid level gauge mouth, inserts liquid level gauge in the anti-blocking liquid level gauge mouth.
The front and rear cover center slightly is provided with the stirring axis hole to the bottom eccentric part.
Stir the open-celled structure that adopts gradual change successively on the disc.
The utility model is finished alcoholysis or hydrolysis with melt polycondensation high polymer old material at the comparatively pure melt that the physics method obtains under the cooperation of related system, homogenizing, decontamination, remove little molecule, the several technical process of reaggregation, help from having changed molecular chain structure in essence, removed the PVC that reclaims in the raw material, PP, polyolefin and derivative class organic impurities thereof such as PE, thereby the purity and the quality of regenerative raw materials have been improved, the polyester fondant of Xing Chenging is in uniformity thus, impurity content and final quality just are higher than these indexs of raw material far away, thereby be widely used in the POY long filament, three-dimensional hollow, FDY, nonwoven, in strong industry silk, regeneration bottles etc. are to reclaiming the higher occasion of raw material quality requirement, minimizing realizes recycling economy to the demand and the consumption of petroleum resources of former raw material.The utlity model has following beneficial effect:
(1) adaptability to waste and old raw material is strong, can process extremely greatly to count markets and reclaim waste and old raw material and produce high-quality raw product again;
(2) core of the present utility model is homogenizing reaggregation process, has solved the quality problem of non-uniform between the raw material of separate sources, and the raw material same with the physics method handled through the utility model, can produce the product that quality is more stable, quality is higher;
(3) the utility model macromolecule melt quality of producing can online adjustment quality index, and steady production, satisfies the different industries quality requirement different to of a sort raw material;
(4) present technique is follow-up can use by supporting direct melt continuously, and does not need regeneration to produce middle product (high polymer particle), reduces production process and energy consumption.
Description of drawings
Fig. 1 is the utility model structural representation;
Among the figure, 1 heating agent chuck, 2 baffle plates, 3 stir disc, 4 cylindrical shells, 5 shafts, 6 discharging openings, 7 combination vacuum seals, 8 gas phase mouths, 9 anti-blocking liquid level gauge mouths, 10 end caps, 11 charging apertures.
The specific embodiment
Further specify the utility model in conjunction with the accompanying drawings and embodiments, as shown in Figure 1, the utility model is horizontal cylindrical structural, hull outside is a cylindrical shell 4, two ends are front and rear cover 10, end cap 10 is oblique down near bottom direction, have anti-blocking liquid level gauge mouth 9, be connected with lip weldering sealing flange bolt between cylindrical shell 4 and the front and rear cover 10, cylindrical shell 4 and the end cap 10 outer one deck heating agent chucks 1 that all are provided with, heating agent chuck 1 is welded on cylindrical shell 4 and the end cap 10, and near drive end bearing bracket 10 perforates welding charging aperture 11, the bottom is near rear end cap 10 perforates welding discharging opening 6 in cylindrical shell 4 bottoms, cylindrical shell 4 tops are welded with gas phase mouth 8 near the rear end cap perforate, end cap 10 centers slightly are provided with the stirring axis hole to the bottom eccentric part, and shaft 5 passes front and rear cover 10 and stirs axis holes, and the combination vacuum seal 7 of holding of the tape spool by two ends couples together shaft 5 and end cap 10 respectively.Be nested with the fixedly stirring disc 3 of different structure on the shaft 5 from front to back successively, shaft 5 one ends connect motor-driven reductor, stirring disc 3 is fixed on the shaft 5 by key and positioning sleeve, and between several groups of stirring discs 3, be provided with polylith baffle plate 2, have opening on the baffle plate 2, resistance difference and partition functionality zone before and after baffle plate 2 is used for increasing, baffle plate 2 usefulness bolts are connected on cylindrical shell 4 inwalls, and spot welding fixes, and also leaves the seam of 10-50mm with cylindrical shell 4 junctions.The inner flow direction of this device adopted partitioned organization, also dividing plate can be set, stir the open-celled structure that disc 3 adopts gradual change successively, adapt to different viscosity and flow, axle system is eccentric installs, and integral body inclination angle slightly, inner barrel does not have the dead angle, form the laminar flow effect that macromolecule melt flows, finish alcoholysis (hydrolysis), homogenizing, decontamination smoothly, remove the integrated of low molecule, the several technical process of reaggregation, and realize serialization production.
Anti-blocking liquid level gauge mouth 9 is open joints with well, along the sleeve pipe trend, is equipped with one on the top and stops up poker, and just often poker is pulled upwardly, and liquid level gauge is in normal operating conditions; When taking place to stop up, poker can move from top to bottom along interior pipe, the tamper in the cleaning sleeve pipe, and cleaning is withdrawn into original position again after finishing.
The utility model in use, its shaft 5 one ends connect motor-driven reductor, gas phase mouth 8 connects impurity piece-rate system and vacuum systems; Exit 6 connects melt vacuum self priming pump and in-line viscometer; Each heating agent chuck 1 connects the heating agent heating system; Bottom near the integrated horizontal reactor end cap of homogenizing reaggregation is provided with anti-blocking liquid level gauge mouth, inserts liquid level gauge in the anti-blocking liquid level gauge mouth.
Existing product is adopted in combination vacuum seal 7 in the utility model.

Claims (3)

1. melt polycondensation high polymer old material regeneration device, it is characterized in that, described regeneration uses device by cylindrical tube, the cylindrical shell two ends are through the bolted end cap of lip weldering sealing flange, the oblique anti-blocking liquid level gauge mouth down that end cap is provided with near the bottom, the combination vacuum seal mechanism that tape spool that respective end covers holds is passed at the shaft two ends that are provided with in the cylindrical shell, the stirring disc of fixed interval successively from front to back on the shaft, an end is fixed on the baffle plate that has opening on the cylinder inboard wall between the stirring disc, the heating agent chuck of the cylindrical shell outside and the welding of end cap outer face, the charging aperture of the bottom solid welding of the close front end of cylindrical shell and cylindrical shell are near the discharging opening of the bottom solid welding of rear end, and the gas phase mouth of the cylindrical shell top solid welding of corresponding discharging opening constitutes; Bottom near an end end cap is provided with anti-blocking liquid level gauge mouth, inserts liquid level gauge in the anti-blocking liquid level gauge mouth.
2. melt polycondensation high polymer old material regeneration device according to claim 1 is characterized in that, the front and rear cover center slightly is provided with the stirring axis hole to the bottom eccentric part.
3. melt polycondensation high polymer old material regeneration device according to claim 1 is characterized in that, stirs the open-celled structure that adopts gradual change successively on the disc.
CN2010201078689U 2010-01-29 2010-01-29 Melt polycondensation macromolecular waste material regeneration device Expired - Fee Related CN201579894U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010201078689U CN201579894U (en) 2010-01-29 2010-01-29 Melt polycondensation macromolecular waste material regeneration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010201078689U CN201579894U (en) 2010-01-29 2010-01-29 Melt polycondensation macromolecular waste material regeneration device

Publications (1)

Publication Number Publication Date
CN201579894U true CN201579894U (en) 2010-09-15

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CN2010201078689U Expired - Fee Related CN201579894U (en) 2010-01-29 2010-01-29 Melt polycondensation macromolecular waste material regeneration device

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102330305A (en) * 2011-08-18 2012-01-25 天津工业大学 Filament bundle fiber chemical modification production device
CN105153460A (en) * 2015-07-01 2015-12-16 福建百宏聚纤科技实业有限公司 FDY oil-free waste silk intelligent online adding reuse device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102330305A (en) * 2011-08-18 2012-01-25 天津工业大学 Filament bundle fiber chemical modification production device
CN102330305B (en) * 2011-08-18 2013-03-06 天津工业大学 Filament bundle fiber chemical modification production device
CN105153460A (en) * 2015-07-01 2015-12-16 福建百宏聚纤科技实业有限公司 FDY oil-free waste silk intelligent online adding reuse device
CN105153460B (en) * 2015-07-01 2016-07-06 福建百宏聚纤科技实业有限公司 Reclamation set is added in FDY oil-free waste silk intellectuality online

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GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100915

Termination date: 20130129