A multi-layer drop tube falling film devolatilization reactor

A reactor and drop-tube technology, applied in the field of multi-layer drop-tube falling film devolatilization reactor, can solve the problems of simplicity and low heat transfer efficiency, and achieve large flow rate, large specific surface area and good film-forming property Effect

Active Publication Date: 2017-10-31
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, because the internal components of the reactor are too simple, there is not enough heating circulation pipeline, and only rely on the outer heating jacket of the outer tower for heat supply, the heat transfer efficiency is relatively low; and because the viscosity of the material is too high, it usually flows in a laminar state. It is difficult to form a sufficient surface renewal effect on the surface of the material only by gravity

Method used

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  • A multi-layer drop tube falling film devolatilization reactor
  • A multi-layer drop tube falling film devolatilization reactor
  • A multi-layer drop tube falling film devolatilization reactor

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Embodiment 1

[0032] Embodiment 1: PET final polycondensation process.

[0033] The structure and principle of the reactor are as described above, and the structural parameters of some reactors are as follows: the number of openings is 10-100, the width of the leakage channel is 2-15mm, the vertical distance between two adjacent umbrella skirts is 20-100mm, and the falling film The taper of the umbrella skirt on the drop tube is from 2:1 to 1:5, the bottom diameter of the umbrella skirt is 20-100mm, and the number of layers is 10-30.

Embodiment 2

[0034] Example 2: Polymer devolatilization process.

[0035] The structure and principle of the reactor are as described above, and some structural parameters and operating parameters of the reactor are as follows: melt viscosity 10-100Pa·s, small molecule volatile content 2-5%, number of openings 10-100, leakage channel width 2 -10mm, the vertical distance between two adjacent umbrella skirts is 20-100mm, the taper of the umbrella skirt on the falling film drop tube is 2:1-1:5, and the bottom diameter of the umbrella skirt is 20- 50mm, the number of layers is 10-30; compared with the smooth drop tube devolatilizer under the same structural parameters, the volatilization removal efficiency is increased by 10-30%.

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Abstract

The invention relates to a multilayer falling pipe type falling film devolatilization reactor, which mainly comprises an outer tower and a plurality of tower cores, wherein the outer tower consists of a tower top, a tower body and a tower bottom; the plurality of tower cores arranged inside the outer tower are in sequential arrangement from top to bottom; each tower core consists of a tower plate and a plurality of falling film falling pipes in parallel arrangement; each falling film falling pipe consists of hollow pipes and a plurality of umbrella skirt-shaped falling sleeves which are provided with downward openings and are fixed on the outer side wall of the hollow pipes; the hollow pipes are mutually connected; heat media are introduced into the hollow pipes; a heat exchange pipeline is used for connection. Compared with a conventional reactor, the multilayer falling pipe type falling film devolatilization reactor has the advantages that the structure is simple; a large gas-liquid interface is realized; the stretching effect is generated on the film surface; the surface updating speed is high; the flow rate is high; the dwell time is controllable; the structure is simple; the additional power equipment is not used; the reaction energy consumption is low; the heat transfer efficiency is high.

Description

technical field [0001] The invention relates to a novel multilayer falling tube type falling film devolatilization reactor. Background technique [0002] The characteristic of the polycondensation process is that through the reaction between the terminal functional groups, the small molecule products are gradually removed but the molecular weight of the polymer is gradually increased. For the whole reaction process, the viscosity of the system increases continuously with the progress of the reaction, with tens of milliPascal seconds and finally even hundreds of thousands of milliPascal seconds. At this time, the removal of small molecular substances becomes extremely difficult. difficulty. Due to the relatively low thermal efficiency of the reaction, it is difficult for us to change the temperature to make the polycondensation reaction proceed effectively in the direction of the positive reaction to obtain qualified products. Therefore, we need to remove the small molecule ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J19/24
CPCB01J19/0013B01J19/0053B01J19/247B01J2219/00081B01J2219/00094B01J2219/0072
Inventor 赵思维王嘉骏冯连芳顾雪萍刘钰余翔翔程层
Owner ZHEJIANG UNIV
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