CN112108097B - Novel tubular tackifying equipment - Google Patents
Novel tubular tackifying equipment Download PDFInfo
- Publication number
- CN112108097B CN112108097B CN202010950122.2A CN202010950122A CN112108097B CN 112108097 B CN112108097 B CN 112108097B CN 202010950122 A CN202010950122 A CN 202010950122A CN 112108097 B CN112108097 B CN 112108097B
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- Prior art keywords
- tackifying
- charging
- tubular
- equipment
- charging bin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
Abstract
The invention discloses novel tubular tackifying equipment. The tubular tackifying equipment comprises a tackifying kettle; a plurality of charging bins are arranged in the tackifying kettle, and the charging bins are straight pipelines; and a plurality of heating pore channels are arranged on the outer wall of the charging bin along the axial direction of the charging bin and used for placing heat conducting wires or heat conducting oil. The invention enables the polymer melt to be fully and uniformly heated in each level of charging bin by arranging the distributed charging bins, and enables the cross sections of all parts to have the same temperature basically, thereby ensuring that the tackifying process of the polymer in the device is basically consistent. The tackifying equipment is not only suitable for tackifying polyamide, but also suitable for other macromolecules. The charging bin of the novel tubular tackifying equipment is reasonable in design, so that a polymer melt is uniformly heated, the tackifying process is stable, the tackifying time is saved by more than 20-40%, and the viscosity uniformity error is within 5%.
Description
Technical Field
The invention relates to novel tubular tackifying equipment, and belongs to the field of chemical fiber equipment.
Background
Solid-phase tackifying, also called solid-phase polycondensation, is characterized in that during tackifying, high molecules undergo polycondensation reaction in a solid state, thereby increasing the molecular weight. The method aims to improve the spinnability of spinning macromolecules. At present, a drum method is mostly adopted for tackifying equipment, and the problems of long tackifying time, uneven viscosity, uneven subsequent spinning and the like are caused due to the problems of uneven heating, large particle damage, much ash and the like in the method. It is therefore desirable to provide a new viscosity increasing device.
Disclosure of Invention
The invention aims to provide tubular tackifying equipment, which is used for uniformly heating and fully reacting tackifying particles in a small space through the tubular equipment so as to achieve the aim of tackifying and solve the technical problems that the particle damage is large and the ash content is high to cause the subsequent high-molecular spinning difficulty due to low tackifying speed or non-uniform tackifying in the prior art.
The pipe type tackifying equipment provided by the invention comprises a tackifying kettle; the charging bin is a straight pipeline;
and a plurality of heating pore channels are arranged on the outer wall of the charging bin along the axial direction of the charging bin and used for placing heat conducting wires or heat conducting oil.
In the tubular tackifying equipment, the diameter of the charging bin is 0.2-0.4 m.
In the tubular tackifying equipment, the cross section of the charging bin is circular, square, hexagonal or triangular, so that the problem of material accumulation of the polymer melt in the pipeline can be reduced when the cross section of the charging bin is circular, and the temperature difference between the center and the edge of the polymer melt can be reduced when the cross section of the charging bin is square, hexagonal or triangular.
In the tubular tackifying equipment, 5-10 charging bins are arranged in the tackifying kettle.
In the tubular tackifying device, the heating pore channels are uniformly distributed on the outer wall of the charging bin.
The invention enables the polymer melt to be fully and uniformly heated in each level of charging bin by arranging the distributed charging bins, and enables the cross sections of all parts to have the same temperature basically, thereby ensuring that the tackifying process of the polymer in the device is basically consistent.
The tackifying equipment is not only suitable for tackifying polyamide, but also suitable for other polymers.
The invention has the following beneficial effects:
the charging bin of the novel tubular tackifying equipment is reasonable in design, so that a polymer melt is uniformly heated, the tackifying process is stable, the tackifying time is saved by more than 20-40%, and the viscosity uniformity error is within 5%.
Drawings
FIG. 1 is a schematic view of the construction of a tubular tackifying apparatus of the present invention.
FIG. 2 is a sectional view of a loading bin of the tubular viscosifying apparatus of the present invention.
The respective symbols in the figure are as follows:
1 tackifying kettle, 2 charging bin and 3 heating pore channel.
Detailed Description
The present invention will be further described with reference to the accompanying drawings, but the present invention is not limited to the following embodiments.
As shown in figure 1, the structural schematic diagram of the pipe-type tackifying equipment provided by the invention comprises a tackifying kettle 1, wherein 5-10 charging bins 2 which are dispersedly arranged are arranged in the tackifying kettle 1, the charging bins 2 are straight pipelines with the diameter of 0.2-0.4 m, and the cross section of the charging bins can be circular, square, hexagonal or triangular. The outer wall of the charging bin 2 is uniformly provided with heating pore canals 3 along the axial direction of the charging bin, and the heating pore canals are used for placing heating wires or heating oil so as to heat the charging bin 2.
Examples 1,
Approximately two thirds of the polyamide (viscosity 2.01) were added per tube in a tubular viscosifying device for viscosification: 10 charging bins 2 are arranged in the tackifying kettle, the charging bins 2 are straight circular pipelines with the diameter of 0.2m, heating pore channels 3 are uniformly distributed at intervals outside the circumference of the charging bins, the tackifying temperature is 180 ℃, the tackifying time is 12h, and the performance of the tackified polyamide is shown in table 1.
Examples 2,
Approximately two thirds of the polyamide (viscosity 2.01) were added per tube in a tubular viscosifying device for viscosification: 10 charging bins 2 are arranged in the tackifying kettle, the charging bins 2 are straight triangular pipelines with the diameter of 0.4m, heating pore channels 3 are uniformly distributed at intervals outside the circumference of the charging bins, the tackifying temperature is 180 ℃, the tackifying time is 12h, and the performance of the tackified polyamide is shown in table 1.
Examples 3,
Approximately two thirds of the polyamide (viscosity 2.01) were added per tube in a tubular viscosifying device for viscosification: 8 charging bins 2 are arranged in the tackifying kettle, the charging bins 2 are straight hexagonal pipelines with the diameter of 0.3m, heating pore channels 3 are uniformly distributed at intervals outside the circumference of the charging bins, the tackifying temperature is 180 ℃, the tackifying time is 12h, and the performance of the tackified polyamide is shown in table 1.
Comparative example 1 (conventional adhesion promotion),
Adding polyamide (the viscosity is 2.01) into a tackifying kettle, and tackifying in a conventional tackifying kettle at 180 ℃ for 16h, wherein the performance of the tackified polyamide is shown in Table 1.
As can be seen from the data in Table 1, the tackifying process by adopting the tackifying equipment of the invention is stable, the tackifying time is saved by more than 33.3%, and the uniformity error of the viscosity is within +/-3%.
TABLE 1 tackifying material Properties
Claims (3)
1. A tubular tackifying device comprises a tackifying kettle; a plurality of charging bins are arranged in the tackifying kettle, and the charging bins are straight pipelines;
a plurality of heating pore channels are arranged on the outer wall of the charging bin along the axial direction of the charging bin and used for placing heat conducting wires or heat conducting oil;
the diameter of the charging bin is 0.2-0.4 m;
the cross section of the charging bin is circular, square, hexagonal or triangular.
2. The tubular tackifying apparatus of claim 1, wherein: and 5-10 charging bins are arranged in the tackifying kettle.
3. The tubular tackifying apparatus of claim 1 or 2, wherein: the heating pore channels are uniformly distributed on the outer wall of the charging bin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202010950122.2A CN112108097B (en) | 2020-09-10 | 2020-09-10 | Novel tubular tackifying equipment |
Applications Claiming Priority (1)
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---|---|---|---|
CN202010950122.2A CN112108097B (en) | 2020-09-10 | 2020-09-10 | Novel tubular tackifying equipment |
Publications (2)
Publication Number | Publication Date |
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CN112108097A CN112108097A (en) | 2020-12-22 |
CN112108097B true CN112108097B (en) | 2022-05-24 |
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CN202010950122.2A Active CN112108097B (en) | 2020-09-10 | 2020-09-10 | Novel tubular tackifying equipment |
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Citations (4)
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EP0702033A1 (en) * | 1994-09-14 | 1996-03-20 | Shin-Etsu Chemical Co., Ltd. | Process of producing vinyl chloride type polymer |
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CN106390897A (en) * | 2016-11-03 | 2017-02-15 | 扬州惠通化工科技股份有限公司 | Polymer tackifying reaction kettle |
CN111617727A (en) * | 2020-06-29 | 2020-09-04 | 上海博氢新能源科技有限公司 | Electrical heating type reforming reactor and reforming hydrogen production system |
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EP0702033A1 (en) * | 1994-09-14 | 1996-03-20 | Shin-Etsu Chemical Co., Ltd. | Process of producing vinyl chloride type polymer |
CN1475301A (en) * | 2001-07-02 | 2004-02-18 | 中国石油化工股份有限公司 | Constant temperature heat insulating dual purpose reactor |
CN106390897A (en) * | 2016-11-03 | 2017-02-15 | 扬州惠通化工科技股份有限公司 | Polymer tackifying reaction kettle |
CN111617727A (en) * | 2020-06-29 | 2020-09-04 | 上海博氢新能源科技有限公司 | Electrical heating type reforming reactor and reforming hydrogen production system |
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