CN100482692C - Agitator of polymerizer for producing PVC resin paste by emulsion polymerization - Google Patents
Agitator of polymerizer for producing PVC resin paste by emulsion polymerization Download PDFInfo
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- CN100482692C CN100482692C CNB2006101343409A CN200610134340A CN100482692C CN 100482692 C CN100482692 C CN 100482692C CN B2006101343409 A CNB2006101343409 A CN B2006101343409A CN 200610134340 A CN200610134340 A CN 200610134340A CN 100482692 C CN100482692 C CN 100482692C
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- 239000011347 resin Substances 0.000 title claims abstract description 19
- 229920005989 resin Polymers 0.000 title claims abstract description 19
- 238000007720 emulsion polymerization reaction Methods 0.000 title claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 49
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 24
- 239000000498 cooling water Substances 0.000 claims abstract description 20
- 229920000915 polyvinyl chloride Polymers 0.000 claims abstract description 15
- 239000004800 polyvinyl chloride Substances 0.000 claims abstract description 15
- 238000012856 packing Methods 0.000 claims abstract description 4
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims abstract description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 claims abstract description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 12
- 230000005540 biological transmission Effects 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 230000001105 regulatory effect Effects 0.000 claims description 3
- -1 polytetrafluoroethylene Polymers 0.000 claims description 2
- 238000012546 transfer Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 4
- 239000000126 substance Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 3
- 238000013019 agitation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000010117 shenhua Substances 0.000 description 1
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Abstract
用于乳液法聚合生产聚氯乙烯糊树脂聚合釜的搅拌器,包括聚合釜、搅拌器,在聚合釜内安装有搅拌器,搅拌器包括搅拌轴、环管式搅拌桨,搅拌轴为空心式,搅拌轴上安装有环管式搅拌桨,搅拌器设置有冷却水进口和冷却水出口,冷却水进口和冷却水出口采用聚四氟填料密封;搅拌器的环管式搅拌桨直径与釜体直径比为0.45-0.50∶1,搅拌器的环管式搅拌桨的环管中心线与搅拌轴之间的夹角为3-5°,环管式搅拌桨与搅拌轴通过可拆式沉头螺钉连接,搅拌轴下部与环管式搅拌桨连接处设置有冷却水流通口。本发明优点是:采用最佳桨径比的环管式搅拌器,提高了搅拌混合和传热效果,尤其是具有倾角的搅拌器使搅拌混合和传热效果更高,从而提高聚氯乙烯糊树脂质量和聚合釜的产能。
The agitator used for the emulsion polymerization to produce polyvinyl chloride paste resin polymerization kettle, including the polymerization kettle and the agitator, the agitator is installed in the polymerization kettle, the agitator includes the stirring shaft, the ring-type stirring paddle, and the stirring shaft is hollow , the stirring shaft is equipped with a ring-type stirring paddle, the agitator is provided with a cooling water inlet and a cooling water outlet, and the cooling water inlet and cooling water outlet are sealed with PTFE packing; the diameter of the ring-type stirring paddle of the agitator is the same as that of the kettle body The diameter ratio is 0.45-0.50:1, the angle between the center line of the ring tube of the agitator's ring tube type impeller and the stirring shaft is 3-5°, the ring tube type impeller and the stirring shaft pass through the detachable countersunk head Screw connection, cooling water flow port is set at the connection between the lower part of the stirring shaft and the ring-type stirring paddle. The advantages of the present invention are: adopting the ring-tube type agitator with the optimal paddle-diameter ratio improves the mixing and heat transfer effect, especially the agitator with an inclination angle makes the mixing and heat transfer effect higher, thereby improving the efficiency of polyvinyl chloride paste. Resin quality and polymerizer capacity.
Description
技术领域 technical field
本发明涉及一种聚合釜用搅拌器,具体涉及一种用于乳液法聚合生产聚氯乙烯糊树脂聚合釜的搅拌器。The invention relates to a stirrer for a polymerization tank, in particular to a stirrer for a polymerization tank for producing polyvinyl chloride paste resin by emulsion polymerization.
背景技术 Background technique
搅拌器是聚合釜最关键的部件,直接影响化工物料在釜内的反应速度、传热速率和产品质量。The agitator is the most critical part of the polymerization kettle, which directly affects the reaction speed, heat transfer rate and product quality of chemical materials in the kettle.
我国聚氯乙烯糊树脂生产始于上世纪八十年代末,采用日本钟渊公司的乳液聚合生产工艺。至今糊树脂生产企业较少,规模不大,生产技术陈旧。现在聚氯乙烯糊树脂需求不断增加,上下温度不匀,致使聚合釜的产能较低。沈阳化工股份公司迫切需要对糊树脂聚合釜进行技术改造和设备更新,以达到高产能、高效益的经济目的。以沈化、天化为代表的聚氯乙烯糊树脂生产企业正在进行扩大规模和技术改造,一批新的糊树脂生产企业正在建设中。The production of polyvinyl chloride paste resin in my country began in the late 1980s, using the emulsion polymerization production process of Japan Zhongyuan Company. So far, there are few paste resin production enterprises with small scale and outdated production technology. Now the demand for polyvinyl chloride paste resin continues to increase, and the upper and lower temperatures are uneven, resulting in low production capacity of the polymerization kettle. Shenyang Chemical Industry Co., Ltd. urgently needs to carry out technical transformation and equipment renewal on the paste resin polymerization kettle, so as to achieve the economic purpose of high production capacity and high benefit. The polyvinyl chloride paste resin production enterprises represented by Shenhua and Tianhua are expanding their scale and undergoing technical transformation, and a batch of new paste resin production enterprises are under construction.
因此,改进后的搅拌器和开发出新型搅拌器,生产出优质高效的聚合釜必将产生巨大经济效益和社会效益。Therefore, the improved agitator and the development of a new type of agitator to produce a high-quality and efficient polymerization kettle will surely produce huge economic and social benefits.
锦西化工机械(集团)有限责任公司拥有国内企业唯一的搅拌试验研究室,能应用激光测速仪等先进试验手段进行科学实验,完成了大量的搅拌试验研究项目,积累了不少的实践经验,具备了开发能力。锦西化工机械(集团)有限责任公司已研制开发了乳液法聚合生产聚氯乙烯糊树脂大型聚合釜LF系列产品。Jinxi Chemical Machinery (Group) Co., Ltd. has the only mixing test laboratory among domestic enterprises. It can use advanced testing methods such as laser velocimeters to carry out scientific experiments. It has completed a large number of mixing test research projects and accumulated a lot of practical experience. With the ability to develop. Jinxi Chemical Machinery (Group) Co., Ltd. has developed the LF series of large polymerization kettles for the production of polyvinyl chloride paste resin by emulsion polymerization.
发明内容 Contents of the invention
本发明要解决的技术问题,是提供一种传热效率高、搅拌强度大的用于乳液法聚合生产聚氯乙烯糊树脂聚合釜的搅拌器。The technical problem to be solved by the present invention is to provide an agitator for a polyvinyl chloride paste resin polymerization tank with high heat transfer efficiency and high agitation strength for emulsion polymerization.
采用的技术方案为:The technical solutions adopted are:
用于乳液法聚合生产聚氯乙烯糊树脂聚合釜的搅拌器,包括搅拌轴、环管式搅拌桨,在聚合釜内安装有搅拌器,搅拌轴为空心式,搅拌轴上安装有环管式搅拌桨,搅拌器内部通入循环冷却水,搅拌器设置有冷却水进口和冷却水出口,冷却水进口和冷却水出口采用聚四氟填料密封;搅拌器的环管式搅拌桨直径与釜体直径比为0.45-0.50:1,这样,有利于提高搅拌强度和传热效果;搅拌器的环管式搅拌桨的环管中心线与搅拌轴之间的夹角为3-5°,这样加强了流体的轴向流动,有利于提高搅拌混合效果和传热效果;环管式搅拌桨与搅拌轴通过可拆式沉头螺钉连接,便于安装和维修保养,不影响物料流动,不易结垢;搅拌轴下部与环管式搅拌桨连接处设置有冷却水流通口。The agitator used for the production of polyvinyl chloride paste resin polymerization kettle by emulsion polymerization includes a stirring shaft and a ring-type stirring paddle. A stirrer is installed in the polymerization kettle. The stirring shaft is hollow and a ring-type stirring shaft is installed on the stirring shaft Stirring paddle, the inside of the stirrer is fed with circulating cooling water, the stirrer is equipped with a cooling water inlet and a cooling water outlet, and the cooling water inlet and cooling water outlet are sealed with polytetrafluoroethylene packing; The diameter ratio is 0.45-0.50:1, which is conducive to improving the stirring strength and heat transfer effect; the angle between the centerline of the ring tube of the ring tube type stirring impeller of the agitator and the stirring shaft is 3-5°, which strengthens the The axial flow of the fluid is improved, which is conducive to improving the mixing effect and heat transfer effect; the ring-type stirring impeller and the stirring shaft are connected by detachable countersunk screws, which is convenient for installation and maintenance, does not affect the flow of materials, and is not easy to scale; A cooling water flow port is provided at the joint between the lower part of the stirring shaft and the annular stirring paddle.
上述的聚合釜包括釜体、传动装置,釜体容积为40~150立米、长径比2.5~3.5、高度8~30米、公称直径为2~5米,釜体直段外壁上固设有螺旋半管夹套,釜体底部固设有螺旋导流夹套;在釜体顶部设计联锁装置的快开人孔;上述的釜体底部装有底轴承,该底轴承具有调节偏心结构,并可起到支撑搅拌轴的作用,釜体上部安装有传动装置。The above-mentioned polymerization kettle includes a kettle body and a transmission device. The volume of the kettle body is 40-150 cubic meters, the aspect ratio is 2.5-3.5, the height is 8-30 meters, and the nominal diameter is 2-5 meters. Spiral half-pipe jacket, the bottom of the kettle body is fixed with a spiral diversion jacket; a quick-opening manhole with an interlock device is designed on the top of the kettle body; the bottom of the above-mentioned kettle body is equipped with a bottom bearing, and the bottom bearing has an adjustable eccentric structure. It can also play the role of supporting the stirring shaft, and a transmission device is installed on the upper part of the kettle body.
上述的传动装置包括电动机、减速机、变频调速装置、机械密封、油站,电动机与减速机间采用直联形式,电动机接有变频调速装置,实现设备运转调速;传动装置机架上安装有减速机、电动机、上部轴承盒,减速机与链条连接器连接,在釜体顶部安装有机械密封,机械密封与油站连接,提供循环机械油实现密封和冷却。The above-mentioned transmission device includes electric motor, reducer, frequency conversion speed control device, mechanical seal, oil station, the direct connection form is adopted between the motor and the reducer, and the motor is connected with frequency conversion speed control device to realize the speed regulation of equipment operation; A reducer, motor, and upper bearing box are installed, the reducer is connected with the chain connector, and a mechanical seal is installed on the top of the kettle body, which is connected with an oil station to provide circulating mechanical oil for sealing and cooling.
本发明优点是:采用最佳桨径比的环管式搅拌器,提高了搅拌混合和传热The advantage of the present invention is: adopting the ring-tube type agitator with the optimal paddle-diameter ratio improves the stirring mixing and heat transfer
效果,尤其是具有倾角的搅拌器使搅拌混合和传热效果更高,从而提高聚氯乙烯糊树脂质量和聚合釜的产能。The effect, especially the agitator with an inclination angle, makes the agitation mixing and heat transfer effect higher, thereby improving the quality of the PVC paste resin and the productivity of the polymerization tank.
附图说明 Description of drawings
图1为本发明的一种实施例的结构示意图。Fig. 1 is a structural schematic diagram of an embodiment of the present invention.
图2为本发明的一种实施例的搅拌器结构示意图。Fig. 2 is a schematic structural diagram of an agitator according to an embodiment of the present invention.
图3为本发明的一种实施例的搅拌器结构剖面示意图Fig. 3 is a schematic cross-sectional view of an agitator structure of an embodiment of the present invention
具体实施方式 Detailed ways
实施例一Embodiment one
用于乳液法聚合生产聚氯乙烯糊树脂聚合釜的搅拌器,搅拌器15包括搅拌轴18、环管式搅拌桨17,在聚合釜1内安装有搅拌器15,搅拌轴18为空心式,搅拌轴18上安装有环管式搅拌桨17,搅拌器15内部通入循环冷却水,搅拌器15设置有冷却水进口12和冷却水出口11,冷却水进口12和冷却水出口11采用聚四氟填料密封10;搅拌器15的环管式搅拌桨17直径与釜体2直径比为0.48:1,搅拌器15的环管式搅拌桨17的环管中心线与搅拌轴18之间的夹角为3°;环管式搅拌桨17与搅拌轴18通过可拆式沉头螺钉22连接;搅拌轴18下部与环管式搅拌桨17连接处设置有冷却水流通口21;The agitator used for emulsion method polymerization to produce polyvinyl chloride paste resin polymerization kettle, agitator 15 includes
上述的聚合釜包括釜体2、传动装置4,釜体2容积为48立米、长径比2.8、高15米、公称直径为2.68米,釜体2直段外壁上固设有螺旋半管夹套16,釜体2底部固设有螺旋导流夹套19;在釜体2顶部设置有联锁装置的快开入孔14;上述的釜体2底部装有底轴承20,该底轴承20具有调节偏心结构;上述的釜体2上部安装有传动装置4。The above-mentioned polymerization kettle includes a kettle body 2 and a transmission device 4. The volume of the kettle body 2 is 48 cubic meters, the aspect ratio is 2.8, the height is 15 meters, and the nominal diameter is 2.68 meters. The outer wall of the straight section of the kettle body 2 is fixed with a spiral half pipe clamp. Cover 16, the bottom of the kettle body 2 is fixed with a
上述的传动装置4包括电动机6、减速机7、变频调速装置5、机械密封13、油站3,电动机6与减速机7间采用直联形式,减速机7与链条连接器8连接,电动机6接有变频调速装置5;传动装置机架23上安装有减速机7、电动机6、上部轴承盒9,在釜体2顶部安装有机械密封13,机械密封13与油站3连接。The above-mentioned transmission device 4 includes a
实施例二Embodiment two
实施例二与实施例一基本相同,不同之处在于搅拌器15的环管式搅拌桨17直径与釜体2直径比为0.45:1,搅拌器15的环管式搅拌桨17的环管中心线与搅拌轴18中心线之间的夹角为4°;Embodiment 2 is basically the same as Embodiment 1, except that the ratio of the diameter of the ring-
釜体2容积为130立米、长径比2.6、高30米、公称直径为4.0米。The kettle body 2 has a volume of 130 cubic meters, an aspect ratio of 2.6, a height of 30 meters, and a nominal diameter of 4.0 meters.
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| CN108247882B (en) * | 2018-02-01 | 2024-03-19 | 辽宁华远石化科技有限公司 | Stirring device for chloroethylene by bulk method |
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