WO2011088763A1 - Self-cleaning reactor for high viscosity stream - Google Patents

Self-cleaning reactor for high viscosity stream Download PDF

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Publication number
WO2011088763A1
WO2011088763A1 PCT/CN2011/070195 CN2011070195W WO2011088763A1 WO 2011088763 A1 WO2011088763 A1 WO 2011088763A1 CN 2011070195 W CN2011070195 W CN 2011070195W WO 2011088763 A1 WO2011088763 A1 WO 2011088763A1
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Prior art keywords
drum
casing
housing
cleaning reactor
shaft
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PCT/CN2011/070195
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French (fr)
Chinese (zh)
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严旭明
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扬州惠通化工技术有限公司
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Publication of WO2011088763A1 publication Critical patent/WO2011088763A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/20Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/625Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis the receptacle being divided into compartments, e.g. with porous divisions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/72Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices
    • B01F27/721Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices with two or more helices in the same receptacle
    • B01F27/722Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices with two or more helices in the same receptacle the helices closely surrounded by a casing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/72Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices
    • B01F27/725Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices with two or more helices in respective separate casings, e.g. one casing inside the other
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/785Preparation processes characterised by the apparatus used

Definitions

  • the present invention relates to a production facility for the polyester industry, and more particularly to a reaction apparatus for use in a polycondensation reaction.
  • a reactor the structure mainly comprises a casing, the top of the casing is provided with a feed inlet and a vacuum suction port, and the bottom of the casing is provided with a discharge port, and the casing is located at the feed.
  • the present invention provides a technical solution for a high-viscosity self-cleaning reactor in view of the deficiencies of the prior art, and aims to solve the problems of poor film forming effect and low work efficiency in the prior art.
  • a high-viscosity self-cleaning reactor comprising a casing, the casing is provided with a vacuum suction port communicating with the inner cavity thereof, and the top of the casing is provided with a feeding port, and the bottom of the casing
  • the utility model is provided with a discharge port, wherein the casing is a horizontally arranged cylinder closed at both ends, the feeding port is arranged at one end of the top of the casing, and the discharging port is arranged at the other end of the bottom of the casing, and the casing is provided in the inner cavity
  • a rotatable drum extending from below the feed port to above the discharge port.
  • the vacuum pumping port is connected to the vacuum pump, and the gas escaping during the reaction of the material can be continuously taken away, the central shaft and the drum are rotated, the material enters from the feeding port, and some materials are fed from the outer propelling blade.
  • One end of the mouth moves toward one end of the discharge port, and some materials pass through the through hole to enter the drum.
  • the material can move toward the discharge port or can advance toward the feed port, depending on the central axis.
  • the material is propelled and agitated by the propelling blade, the enthusiasm of the evaporation surface increases, and the reaction by-products are quickly extracted from the vacuum suction port, and the polycondensation reaction of the material can be further carried out, and the material after the reaction will eventually Leave the unit from the spout.
  • the device is small in volume, large in processing capacity and low in energy consumption, and can be used in the production of polyesters such as PET, PEN, PBT, PTT, etc.
  • the invention is particularly suitable for processing high viscosity materials.
  • the outer propulsion blade is a spiral blade
  • the inner propulsion blade may also be a spiral blade.
  • the spiral blade described above may also be a propeller blade. When it is working, it can make the material fully agitate and evaporate quickly.
  • the drum shafts disposed at both ends of the drum are supported on the casing via the outer bearing, and both ends of the central shaft are supported by the inner bearing in the drum shaft.
  • the input end of the drum shaft and the input end of the center shaft are respectively disposed at both ends of the casing.
  • Figure 1 is a schematic view of the structure of the present invention.
  • FIG. 1 it is a high-viscosity self-cleaning reactor, and its structure mainly comprises a casing 4 which is a cylinder, which is horizontally arranged and closed at both ends, and the casing 4 is provided with a cavity communicating with the inner cavity thereof.
  • the vacuum suction port 10 is provided with a feed port 3 at the top of the casing 4, the feed port 3 is disposed at one end of the top of the casing 4, and a discharge port 15 is provided at the bottom of the casing 4, and the discharge port 15 is disposed at the casing At the other end of the bottom of the casing 4, a rotatable drum 8 is disposed in the inner cavity of the casing 4.
  • the drum shafts 2, 11 at both ends of the drum 8 are supported on the casing 4 through the outer bearing 14, and the drum 8 is continuously from below the inlet port 3.
  • the outer circumference of the drum 8 is provided with an outer propulsion blade 6 adapted to the inner wall of the casing 4, and the outer propulsion blade 6 is a spiral blade.
  • the center of the drum 8 is coaxially disposed with a central shaft 9 and two central shafts 9
  • the inner end bearing 13 is supported in the drum shaft 2, 11 and the inner shaft 9 is fixedly provided with an inner propelling blade 7 adapted to the inner wall of the drum 8.
  • the inner propelling blade 7 is also a spiral blade, and the roller surface is provided with a plurality of through holes. 5; the input end of the drum shaft 2, 11 and the input end of the central shaft 9 are respectively disposed at two ends of the casing 4, and can be input through the pulleys 1, 12 provided at both ends Power.

Abstract

A self-cleaning reactor for high viscosity stream in the field of polyester production apparatus comprises a housing (4). The housing (4) is a horizontal cylinder, both ends of which are closed. A gas evacuation outlet (10) is arranged on the housing (4) and connected with the inner cavity thereof. A material inlet (3) is arranged at one end of the top of the housing (4), and a material outlet (15) is arranged at the other end of the bottom of the housing (4). A rotatable rolling drum (8) is arranged in the inner cavity of the housing (4) and extends from the bottom of the material inlet (3) to the top of the material outlet (15). External propeller blades (6) are installed around the external circumference of the rolling drum (8) and adapted to the internal wall of the housing (4). A central shaft (9) is coaxially arranged at the center of the rolling drum (8). Internal propeller blades (7) are fixedly installed outside of the central shaft (9) and adapted to the inner wall of the rolling drum (8). A plurality of through holes (5) is arranged on the surface of the rolling drum (8).

Description

高粘度自洁反应器  High viscosity self-cleaning reactor 技术领域Technical field
本发明涉及聚酯行业的一种生产设备,特别涉及缩聚反应中使用的一种反应装置。 The present invention relates to a production facility for the polyester industry, and more particularly to a reaction apparatus for use in a polycondensation reaction.
背景技术Background technique
现有聚酯生产中,随着缩聚反应的进行,物料的粘度逐渐加大,高粘度的物料会阻碍反应副产物的快速逸出,延缓反应的进行,需要使物料在真空状态下形成较大表面积的膜,这样,反应副产物才能从物料中顺利逸出,反应才能更好地进行下去。为使反应能继续进行,目前,采用一种反应器,其结构主要包括有壳体,壳体顶部设有进料口和真空抽气口,壳体底部设有出料口,壳体内位于进料口下方设有一对或多对相对转动的压辊,压辊之间留间隙,物料从进料口进入,从转动的压辊隙缝之间经过形成膜状,并被不断蒸发,最后从出料口离开装置。其不足之处在于:压辊的成膜效率低,物料粘度大时,容易在壳体内堆积,堵塞,致使装置的工作效能降低;采用双压辊相对转动成膜,其功耗高,处理能力小。In the existing polyester production, as the polycondensation reaction proceeds, the viscosity of the material gradually increases, and the high viscosity material hinders the rapid escape of the reaction by-products, delays the progress of the reaction, and requires the material to form a large under vacuum. The surface area of the membrane, so that the reaction by-products can escape smoothly from the material, and the reaction can proceed better. In order to continue the reaction, at present, a reactor is adopted, the structure mainly comprises a casing, the top of the casing is provided with a feed inlet and a vacuum suction port, and the bottom of the casing is provided with a discharge port, and the casing is located at the feed. There are one or more pairs of relatively rotating press rolls under the mouth, leaving a gap between the press rolls, the material enters from the feed port, passes through the gap between the rotating press rolls, and is continuously evaporated, and finally discharged. The mouth leaves the device. The disadvantage is that the film forming efficiency of the pressure roller is low, and when the viscosity of the material is large, it is easy to be accumulated and blocked in the casing, so that the working efficiency of the device is lowered; the film is relatively rotated by the double pressure roller, and the power consumption is high, and the processing capability is high. small.
发明内容Summary of the invention
本发明针对现有技术的不足,提供一种高粘度自洁反应器的技术方案,旨在解决现有技术中物料成膜效果差,工作效率低下的问题。The present invention provides a technical solution for a high-viscosity self-cleaning reactor in view of the deficiencies of the prior art, and aims to solve the problems of poor film forming effect and low work efficiency in the prior art.
  为解决上述技术问题,本发明的技术方案如下:高粘度自洁反应器,包括壳体,壳体上设有与其内腔相通的真空抽气口,壳体顶部设有进料口,壳体底部设有出料口,所述壳体为卧式设置且两端封闭的圆筒,进料口设置在壳体顶部的一端,出料口设置在壳体底部的另一端,壳体内腔中设有一个可转动的滚筒,滚筒从进料口下方一直延伸到出料口上方,滚筒外周设有与壳体内壁相适配的外推进叶片,滚筒中心同轴设置有中心轴,中心轴外固定设有与滚筒内壁相适配的内推进叶片,滚筒表面设有若干通孔。In order to solve the above technical problem, the technical solution of the present invention is as follows: a high-viscosity self-cleaning reactor, comprising a casing, the casing is provided with a vacuum suction port communicating with the inner cavity thereof, and the top of the casing is provided with a feeding port, and the bottom of the casing The utility model is provided with a discharge port, wherein the casing is a horizontally arranged cylinder closed at both ends, the feeding port is arranged at one end of the top of the casing, and the discharging port is arranged at the other end of the bottom of the casing, and the casing is provided in the inner cavity There is a rotatable drum extending from below the feed port to above the discharge port. The outer circumference of the drum is provided with an outer propeller blade adapted to the inner wall of the casing. The center of the drum is coaxially arranged with a central shaft, and the central shaft is fixed externally. An inner propulsion blade is provided which is adapted to the inner wall of the drum, and the roller surface is provided with a plurality of through holes.
  本发明在使用时,真空抽气口接真空泵,可不断抽走物料反应过程中逸出的气体,中心轴和滚筒均转动,物料从进料口进入,部分物料在外推进叶片的推动下从进料口一端向出料口一端运动,部分物料穿过所述通孔进入滚筒内,在内推进叶片作用下,物料可以向出料口方向运动,也可以向进料口方向推进,视中心轴的转向而定;在上述过程中,物料被推进叶片推进、搅动,自身蒸发面积极度增大,反应副产物迅速被从真空抽气口抽出,物料的缩聚反应能进一步深入进行,反应后的物料最终会从出料口离开装置。该装置体积小、处理量大、能耗低,可用于PET、PEN、PBT、PTT等聚酯的生产中,本发明特别适合处理高粘度的物料。When the invention is used, the vacuum pumping port is connected to the vacuum pump, and the gas escaping during the reaction of the material can be continuously taken away, the central shaft and the drum are rotated, the material enters from the feeding port, and some materials are fed from the outer propelling blade. One end of the mouth moves toward one end of the discharge port, and some materials pass through the through hole to enter the drum. Under the action of the inner propulsion blade, the material can move toward the discharge port or can advance toward the feed port, depending on the central axis. In the above process, the material is propelled and agitated by the propelling blade, the enthusiasm of the evaporation surface increases, and the reaction by-products are quickly extracted from the vacuum suction port, and the polycondensation reaction of the material can be further carried out, and the material after the reaction will eventually Leave the unit from the spout. The device is small in volume, large in processing capacity and low in energy consumption, and can be used in the production of polyesters such as PET, PEN, PBT, PTT, etc. The invention is particularly suitable for processing high viscosity materials.
  所述外推进叶片为螺旋叶片,内推进叶片也可为螺旋叶片。上述螺旋叶片还可以是推进桨叶。其工作时,均能使物料充分搅动,蒸发迅速。The outer propulsion blade is a spiral blade, and the inner propulsion blade may also be a spiral blade. The spiral blade described above may also be a propeller blade. When it is working, it can make the material fully agitate and evaporate quickly.
  为保证该装置结构简单紧凑,所述滚筒两端设置的滚筒轴经外轴承支撑在壳体上,中心轴两端经内轴承支撑在滚筒轴内。为进一步保证其动力布置合理,滚筒轴的输入端和中心轴的输入端分设在壳体两端。In order to ensure that the structure of the device is simple and compact, the drum shafts disposed at both ends of the drum are supported on the casing via the outer bearing, and both ends of the central shaft are supported by the inner bearing in the drum shaft. In order to further ensure that the power arrangement is reasonable, the input end of the drum shaft and the input end of the center shaft are respectively disposed at both ends of the casing.
附图说明DRAWINGS
图1为本发明一种结构示意图。Figure 1 is a schematic view of the structure of the present invention.
  其中,1、12皮带轮,2、11滚筒轴,3进料口,4壳体,5通孔,6外推进叶片,7内推进叶片,8滚筒,9中心轴,10真空抽气口, 13内轴承,14外轴承,15出料口。Among them, 1, 12 pulleys, 2, 11 drum shafts, 3 feed ports, 4 shells, 5 through holes, 6 outer propeller blades, 7 inner propeller blades, 8 rollers, 9 center shafts, 10 vacuum suction ports, 13 inner bearings, 14 outer bearings, 15 discharge ports.
具体实施方式detailed description
如图1所示,为高粘度自洁反应器,其结构主要包括有壳体4,壳体4为圆筒,其卧式设置且两端封闭,壳体4上设有与其内腔相通的真空抽气口10,壳体4顶部设有进料口3,该进料口3设置在壳体4顶部的一端,壳体4底部设有出料口15,该出料口15设置在壳体4底部的另一端,壳体4内腔中设有一个可转动的滚筒8,滚筒8两端的滚筒轴2、11通过外轴承14支撑在壳体4上,滚筒8从进料口3下方一直延伸到出料口15上方,滚筒8外周设有与壳体4内壁相适配的外推进叶片6,外推进叶片6为螺旋叶片,滚筒8中心同轴设置有中心轴9,中心轴9两端经内轴承13支撑在滚筒轴2、11内,中心轴9外固定设有与滚筒8内壁相适配的内推进叶片7,内推进叶片7也为螺旋叶片,滚筒表面设有若干通孔5;滚筒轴2、11的输入端和中心轴9的输入端分设在壳体4两端,可通过两端设置的皮带轮1、12输入动力。As shown in FIG. 1 , it is a high-viscosity self-cleaning reactor, and its structure mainly comprises a casing 4 which is a cylinder, which is horizontally arranged and closed at both ends, and the casing 4 is provided with a cavity communicating with the inner cavity thereof. The vacuum suction port 10 is provided with a feed port 3 at the top of the casing 4, the feed port 3 is disposed at one end of the top of the casing 4, and a discharge port 15 is provided at the bottom of the casing 4, and the discharge port 15 is disposed at the casing At the other end of the bottom of the casing 4, a rotatable drum 8 is disposed in the inner cavity of the casing 4. The drum shafts 2, 11 at both ends of the drum 8 are supported on the casing 4 through the outer bearing 14, and the drum 8 is continuously from below the inlet port 3. Extending above the discharge port 15, the outer circumference of the drum 8 is provided with an outer propulsion blade 6 adapted to the inner wall of the casing 4, and the outer propulsion blade 6 is a spiral blade. The center of the drum 8 is coaxially disposed with a central shaft 9 and two central shafts 9 The inner end bearing 13 is supported in the drum shaft 2, 11 and the inner shaft 9 is fixedly provided with an inner propelling blade 7 adapted to the inner wall of the drum 8. The inner propelling blade 7 is also a spiral blade, and the roller surface is provided with a plurality of through holes. 5; the input end of the drum shaft 2, 11 and the input end of the central shaft 9 are respectively disposed at two ends of the casing 4, and can be input through the pulleys 1, 12 provided at both ends Power.
  工作时,通过真空抽气口10抽真空,动力经皮带轮1、12输入,滚筒8和中心轴9转动,两者可以同向转动,也可以相逆向转动,可视物料的粘度,以及在反应器中需要反应的时间,来确定滚筒8和中心轴9的转动速差,从进料口3进入的物料会在滚筒8内外经通孔5不断相互流动,在外推进叶片6和内推进叶片7的共同作用下,换位、搅拌,自身表面积极度增大,反应副产物充分逸出,使聚合反应更加彻底。During operation, vacuum is drawn through the vacuum suction port 10, the power is input through the pulleys 1, 12, the drum 8 and the central shaft 9 are rotated, and the two can rotate in the same direction, or can be reversely rotated, the viscosity of the material can be seen, and in the reactor The time required for the reaction is determined to determine the rotational speed difference between the drum 8 and the central shaft 9. The material entering from the inlet port 3 will continuously flow through the through hole 5 inside and outside the drum 8, and the outer propeller blade 6 and the inner propeller blade 7 are externally propelled. Under the joint action, the position and the agitation are increased, the surface positivity is increased, and the reaction by-products are fully escaped, so that the polymerization reaction is more thorough.

Claims (5)

  1. 一种高粘度自洁反应器,包括壳体,壳体上设有与其内腔相通的真空抽气口,壳体顶部设有进料口,壳体底部设有出料口,其特征在于:所述壳体为卧式设置且两端封闭的圆筒,进料口设置在壳体顶部的一端,出料口设置在壳体底部的另一端,壳体内腔中设有一个可转动的滚筒,滚筒从进料口下方一直延伸到出料口上方,滚筒外周设有与壳体内壁相适配的外推进叶片,滚筒中心同轴设置有中心轴,中心轴外固定设有与滚筒内壁相适配的内推进叶片,滚筒表面设有若干通孔。 The utility model relates to a high-viscosity self-cleaning reactor, which comprises a casing, and a vacuum suction port communicating with the inner cavity thereof is arranged on the casing, a feeding inlet is arranged on the top of the casing, and a discharge opening is arranged at the bottom of the casing, and the utility model is characterized in that: The housing is a horizontally disposed cylinder closed at both ends, the feeding opening is arranged at one end of the top of the housing, the discharging opening is arranged at the other end of the bottom of the housing, and a rotatable drum is arranged in the inner cavity of the housing. The drum extends from below the feed port to the top of the discharge port, and the outer circumference of the drum is provided with an outer propeller blade which is matched with the inner wall of the casing. The center of the drum is coaxially arranged with a central shaft, and the central shaft is fixed externally to fit the inner wall of the drum. The inner propeller blade is provided with a plurality of through holes on the surface of the drum.
  2. 根据权利要求1所述的高粘度自洁反应器,其特征在于:所述外推进叶片为螺旋叶片。 The high viscosity self-cleaning reactor of claim 1 wherein said outer propulsion blades are helical blades.
  3. 根据权利要求1所述的高粘度自洁反应器,其特征在于:所述内推进叶片为螺旋叶片。 The high viscosity self-cleaning reactor of claim 1 wherein said inner propulsion blades are helical blades.
  4. 根据权利要求1-3任意一项所述的高粘度自洁反应器,其特征在于:所述滚筒两端设置的滚筒轴经外轴承支撑在壳体上,中心轴两端经内轴承支撑在滚筒轴内。 The high-viscosity self-cleaning reactor according to any one of claims 1 to 3, characterized in that the drum shaft provided at both ends of the drum is supported on the casing via an outer bearing, and both ends of the central shaft are supported by the inner bearing. Inside the roller shaft.
  5. 根据权利要求4所述的高粘度自洁反应器,其特征在于:所述滚筒轴的输入端和中心轴的输入端分设在壳体两端。 The high viscosity self-cleaning reactor according to claim 4, wherein the input end of the drum shaft and the input end of the center shaft are disposed at both ends of the casing.
PCT/CN2011/070195 2010-01-22 2011-01-12 Self-cleaning reactor for high viscosity stream WO2011088763A1 (en)

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Application Number Priority Date Filing Date Title
CN201010110591.X 2010-01-22
CN201010110591XA CN101745361B (en) 2010-01-22 2010-01-22 High-viscosity self-cleaning reactor

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WO2020126311A1 (en) * 2018-12-19 2020-06-25 IFP Energies Nouvelles Tubular reactor having a conveyor screw
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CN113648951A (en) * 2021-08-10 2021-11-16 良德纳米粉体创新科技(安徽)有限公司 Nano calcium carbonate carbonization treatment device and method

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