CN204768715U - Chemical industry distillation plant - Google Patents
Chemical industry distillation plant Download PDFInfo
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- CN204768715U CN204768715U CN201520490265.4U CN201520490265U CN204768715U CN 204768715 U CN204768715 U CN 204768715U CN 201520490265 U CN201520490265 U CN 201520490265U CN 204768715 U CN204768715 U CN 204768715U
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- 238000004821 distillation Methods 0.000 title claims abstract description 15
- 239000000126 substance Substances 0.000 title claims abstract description 13
- 238000003756 stirring Methods 0.000 claims abstract description 56
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- 238000009775 high-speed stirring Methods 0.000 claims abstract description 12
- 239000000498 cooling water Substances 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000000463 material Substances 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 2
- 239000002904 solvent Substances 0.000 abstract description 19
- 238000001816 cooling Methods 0.000 abstract description 8
- 239000002994 raw material Substances 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 4
- 229920005862 polyol Polymers 0.000 description 3
- 150000003077 polyols Chemical class 0.000 description 3
- 239000007921 spray Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
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Abstract
本实用新型公开了一种化工蒸馏装置,包括反应釜,反应釜设有带设备法兰的釜盖以及釜体,釜体内设有高速搅拌轴和低速搅拌轴,高速搅拌轴上由上至下设有搅拌叶片,低速搅拌轴的下端连接一刮板机构,刮板机构包括釜壁刮板和底刮板,在釜壁刮板的内侧设有与搅拌叶片相同个数的搅拌齿,反应釜还置竖直冷凝管,竖直冷凝管的外部设有套管,竖直冷凝管的上端通过管路连接横冷凝管,横冷凝管靠近管路的位置设有温度传感器,温度传感器连接温度显示屏。本实用新型在搅拌的同时,能够对釜体内侧壁进行有效的清理,防止原料粘在所述釜体内侧壁上;通过控制隔膜泵加大低温溶剂的加入量,对高温溶剂蒸汽进行冷却降温,降温冷却效果好。
The utility model discloses a chemical distillation device, which comprises a reaction kettle. The reaction kettle is provided with a kettle cover with equipment flanges and a kettle body. The kettle body is provided with a high-speed stirring shaft and a low-speed stirring shaft. The high-speed stirring shaft is arranged from top to bottom. Stirring blades are provided, and a scraper mechanism is connected to the lower end of the low-speed stirring shaft. The scraper mechanism includes a kettle wall scraper and a bottom scraper. The inside of the kettle wall scraper is provided with the same number of stirring teeth as the stirring blades. A vertical condensing pipe is also installed, and the outside of the vertical condensing pipe is provided with a sleeve. The upper end of the vertical condensing pipe is connected to the horizontal condensing pipe through a pipeline. The position of the horizontal condensing pipe close to the pipeline is provided with a temperature sensor. Screen. The utility model can effectively clean the inner wall of the kettle body while stirring, and prevent the raw materials from sticking to the inner wall of the kettle body; increase the amount of low-temperature solvent by controlling the diaphragm pump, and cool the high-temperature solvent vapor , good cooling effect.
Description
技术领域technical field
本实用新型涉及化工设备领域体是一种化工蒸馏装置。The utility model relates to the field of chemical equipment, which is a chemical distillation device.
背景技术Background technique
反应釜反应中的多元醇和多元酸酯化反应生成的水蒸汽和反应器内未反应的多元醇会形成高温溶剂蒸汽,高温溶剂蒸汽经过初次降温后进入蒸馏器蒸馏形成低温溶剂,再进入分水器,水蒸气从分水器分离出冷凝水和多元醇,冷凝水和多元醇经分离后再次分别利用。但是,现有高温溶剂蒸汽的初次降温效果不佳,进入蒸馏器时仍然温度过高,有效控温难;而且反应时要不停的搅拌反应液以使其反应充分,由于搅拌叶片和反应液接触的面积不够,搅拌不够均匀,往往导致反应不够彻底,此外粘在釜体侧壁上的原料若得不到及时刮除易产生高温结碳现象,进一步影响反应效率,降低原料利用率。The polyalcohol in the reactor reaction and the water vapor generated by the polybasic esterification reaction and the unreacted polyol in the reactor will form a high-temperature solvent vapor. After the initial cooling, the high-temperature solvent vapor enters the distiller to distill to form a low-temperature solvent, and then enters the water separation The water vapor is separated from the water separator to separate condensed water and polyols, and the condensed water and polyols are separated and reused separately. However, the primary cooling effect of the existing high-temperature solvent vapor is not good, and the temperature is still too high when it enters the distiller, so it is difficult to effectively control the temperature; Insufficient contact area and uneven stirring often lead to incomplete reaction. In addition, if the raw materials sticking to the side wall of the kettle body are not scraped off in time, high-temperature carbon formation will easily occur, which will further affect the reaction efficiency and reduce the utilization rate of raw materials.
实用新型内容Utility model content
本实用新型的目的在于提供一种降温冷却效果好的化工蒸馏装置,以解决上述背景技术中提出的问题。The purpose of the utility model is to provide a chemical distillation device with good cooling effect to solve the problems raised in the above-mentioned background technology.
为实现上述目的,本实用新型提供如下技术方案:In order to achieve the above object, the utility model provides the following technical solutions:
一种化工蒸馏装置,包括反应釜,反应釜设有带设备法兰的釜盖以及釜体,釜体外侧设有夹套,夹套上部设有导热油出口,夹套的下端设有导热油进口,釜盖上设有进料口和出料口,釜体内设有高速搅拌轴和低速搅拌轴,高速搅拌轴上由上至下设有搅拌叶片,低速搅拌轴的下端连接一刮板机构,所述刮板机构包括釜壁刮板和底刮板,在釜壁刮板的内侧设有与搅拌叶片相同个数的搅拌齿,所述搅拌叶片与搅拌齿交错排列,搅拌叶片伸入相邻两层搅拌齿的空隙中,搅拌齿和搅拌叶片表面还设置有搪玻璃,釜盖上还设有高速电机与低速电机,高速搅拌轴与低速搅拌轴的另一端伸出釜体外部分别与高速电机和低速电机连接;所述反应釜还置竖直冷凝管,竖直冷凝管的外部设有套管,套管连通冷却水装置,竖直冷凝管的上端通过管路连接横冷凝管,横冷凝管远离竖直冷凝管的一端连接分水器,分水器连接隔膜泵,隔膜泵通过管道连接喷头,喷头通入管路,横冷凝管靠近管路的位置设有温度传感器,温度传感器连接温度显示屏。A chemical distillation device, including a reaction kettle, the reaction kettle is provided with a kettle cover with an equipment flange and a kettle body, a jacket is arranged on the outside of the kettle body, a heat transfer oil outlet is arranged on the upper part of the jacket, and a heat transfer oil is arranged at the lower end of the jacket The inlet, the lid of the kettle is equipped with a feed port and a discharge port, and the kettle body is equipped with a high-speed stirring shaft and a low-speed stirring shaft. The high-speed stirring shaft is equipped with stirring blades from top to bottom, and the lower end of the low-speed stirring shaft is connected to a scraper mechanism , the scraper mechanism includes a kettle wall scraper and a bottom scraper, the inside of the kettle wall scraper is provided with the same number of stirring teeth as the stirring blades, the stirring blades and the stirring teeth are arranged in a staggered manner, and the stirring blades extend into the corresponding In the gap between the adjacent two layers of stirring teeth, the surfaces of the stirring teeth and the stirring blades are also equipped with glass-lined, and the kettle cover is also equipped with a high-speed motor and a low-speed motor. The other ends of the high-speed stirring shaft and the low-speed stirring shaft extend out of the kettle body respectively The high-speed motor is connected with the low-speed motor; the reaction kettle is also provided with a vertical condensing pipe, and the outside of the vertical condensing pipe is provided with a casing, the casing is connected to the cooling water device, and the upper end of the vertical condensing pipe is connected to the horizontal condensing pipe through a pipeline. The end of the horizontal condensing pipe away from the vertical condensing pipe is connected to the water separator, and the water separator is connected to the diaphragm pump. The diaphragm pump is connected to the nozzle through the pipeline, and the nozzle is connected to the pipeline. temperature display.
作为本实用新型进一步的方案:所述釜体上还设有观测孔。As a further solution of the utility model: the kettle body is also provided with an observation hole.
作为本实用新型再进一步的方案:所述冷却水装置包括和套管连通的冷却水进水管和冷却水出水管,冷却水出水管设于冷却水进水管的上方。As a further solution of the utility model: the cooling water device includes a cooling water inlet pipe and a cooling water outlet pipe connected with the casing, and the cooling water outlet pipe is arranged above the cooling water inlet pipe.
作为本实用新型再进一步的方案:所述隔膜泵为气动隔膜泵,气动隔膜泵设有电磁气动阀。As a further solution of the utility model: the diaphragm pump is a pneumatic diaphragm pump, and the pneumatic diaphragm pump is provided with an electromagnetic pneumatic valve.
作为本实用新型再进一步的方案:所述温度显示屏和电磁气动阀之间设有温控仪。As a further solution of the utility model: a temperature controller is provided between the temperature display screen and the electromagnetic pneumatic valve.
与现有技术相比,本实用新型的有益效果是:本实用新型中反应釜通过搅拌叶片自上而下的设置保证了与反应物料的接触面积,搅拌叶片与搅拌齿的交错设置,使搅拌的更加均匀彻底,在低速搅拌轴的下端还设有刮板机构,在搅拌的同时,能够对釜体内侧壁进行有效的清理,防止原料粘在所述釜体内侧壁上,提高了原料利用率;且分水器中的部分低温溶剂通入管路,对高温溶剂蒸汽进行冷却降温,操作人员通过观察温度显示屏操作或者温控器控制,通过控制隔膜泵加大低温溶剂的加入量,对高温溶剂蒸汽进行冷却降温,降温冷却效果好。Compared with the prior art, the beneficial effect of the utility model is: in the utility model, the contact area between the reactor and the reaction material is ensured through the setting of the stirring blades from top to bottom, and the staggered setting of the stirring blades and the stirring teeth makes the stirring It is more uniform and thorough. There is also a scraper mechanism at the lower end of the low-speed stirring shaft. While stirring, it can effectively clean the inner wall of the kettle body, prevent the raw materials from sticking to the inner wall of the kettle body, and improve the utilization of raw materials. rate; and part of the low-temperature solvent in the water separator is passed into the pipeline to cool the high-temperature solvent vapor. The operator controls the operation of the temperature display screen or the temperature controller, and increases the amount of low-temperature solvent added by controlling the diaphragm pump. The high-temperature solvent vapor is used for cooling, and the cooling effect is good.
附图说明Description of drawings
图1为化工蒸馏装置的结构示意图;Fig. 1 is the structural representation of chemical industry distillation unit;
图中:1-高速电机、2-高速搅拌轴、3-搅拌齿、4-搅拌叶片、5-刮板机构、6-低速电机、7-釜盖、8-釜体、9-导热油出口、10-夹套、11-低速搅拌轴、12-导热油进口、13-竖直冷凝管、14-管路、15-横冷凝管、16-分水器、17-开口、18-气动隔膜泵、19-第一阀门、20-电磁气动阀、21-套管、22-第二阀门、23-喷头、24-热电阻、25-温度显示屏、26-温控仪、27-冷却水进水管、28-冷却水出水管、29-管道。In the figure: 1-high-speed motor, 2-high-speed stirring shaft, 3-stirring teeth, 4-stirring blade, 5-scraper mechanism, 6-low-speed motor, 7-kettle cover, 8-kettle body, 9-heat transfer oil outlet , 10-jacket, 11-low-speed stirring shaft, 12-heat transfer oil inlet, 13-vertical condenser, 14-pipeline, 15-horizontal condenser, 16-water separator, 17-opening, 18-pneumatic diaphragm Pump, 19-first valve, 20-electromagnetic pneumatic valve, 21-casing, 22-second valve, 23-nozzle, 24-thermal resistance, 25-temperature display, 26-temperature controller, 27-cooling water Water inlet pipe, 28-cooling water outlet pipe, 29-pipeline.
具体实施方式Detailed ways
下面结合具体实施方式对本专利的技术方案作进一步详细地说明。The technical solution of this patent will be further described in detail below in conjunction with specific embodiments.
请参阅图1,一种化工蒸馏装置,包括反应釜,反应釜设有带设备法兰的釜盖7以及釜体8,釜盖7和釜体8通过设备法兰螺栓连接,釜体8外侧设有夹套10,夹套10上部设有导热油出口9,夹套10的下端设有导热油进口12,釜盖7上还设有进料口和出料口。釜体8内设有高速搅拌轴2和低速搅拌轴11,高速搅拌轴2上由上至下设有若干搅拌叶4,防止搅拌叶片与反应物料的接触面积不够,釜盖7上设有与高速搅拌轴2相连的高速电机1以及与所述低速搅拌轴11相连的低速电机6,高速电机1和低速电机6通过各自下端的机架固装在釜盖7上,低速搅拌轴11的下端连接一刮板机构5,所述刮板机构5包括釜壁刮板52和底刮板51,在釜壁刮板52的内侧设有与搅拌叶片4相同个数的搅拌齿3,所述搅拌叶片4与搅拌齿3交错排列,搅拌叶片4伸入相邻两层搅拌齿3的空隙中,使得搅拌叶片4与搅拌齿3之间的切割运动将反应物料进行均匀混合,反应彻底;反应釜还设置竖直冷凝管13,反应釜产生的高温溶剂蒸汽进入竖直冷凝管13,竖直冷凝管13的外部设有套管21。Please refer to Figure 1, a chemical distillation device, including a reaction kettle, the reaction kettle is provided with a kettle cover 7 and a kettle body 8 with equipment flanges, the kettle cover 7 and the kettle body 8 are connected by equipment flange bolts, and the outside of the kettle body 8 A jacket 10 is provided, the upper part of the jacket 10 is provided with a heat transfer oil outlet 9, the lower end of the jacket 10 is provided with a heat transfer oil inlet 12, and the kettle lid 7 is also provided with a feed port and a discharge port. The kettle body 8 is provided with a high-speed stirring shaft 2 and a low-speed stirring shaft 11. The high-speed stirring shaft 2 is provided with a number of stirring blades 4 from top to bottom to prevent the contact area between the stirring blades and the reaction material from being insufficient. The high-speed motor 1 connected to the high-speed stirring shaft 2 and the low-speed motor 6 connected to the low-speed stirring shaft 11, the high-speed motor 1 and the low-speed motor 6 are fixed on the kettle cover 7 by the frame at the lower end respectively, and the lower end of the low-speed stirring shaft 11 Connect a scraper mechanism 5, said scraper mechanism 5 comprises kettle wall scraper 52 and bottom scraper 51, is provided with the same number of stirring teeth 3 as stirring blade 4 in the inner side of kettle wall scraper 52, said stirring The blades 4 and the stirring teeth 3 are alternately arranged, and the stirring blades 4 extend into the gap between the two adjacent layers of stirring teeth 3, so that the cutting movement between the stirring blades 4 and the stirring teeth 3 can uniformly mix the reaction materials, and the reaction is thorough; A vertical condensing pipe 13 is also provided, and the high-temperature solvent vapor generated by the reaction kettle enters the vertical condensing pipe 13 , and a casing 21 is provided outside the vertical condensing pipe 13 .
套管21与冷却水进水管27和冷却水出水管28连通,冷却水出水管28设置于冷却水进水管27的上方。竖直冷凝管13的上端通过管路14连接横冷凝管15,横冷凝管15远离管路14的一端连接分水器16,分水器16的底部设有开口17,分水器16连接气动隔膜泵18,分水器16和气动隔膜泵18之间设有第一阀门19,气动隔膜泵18设有电磁气动阀20,电磁气动阀20用于操作人员操作。The sleeve pipe 21 communicates with the cooling water inlet pipe 27 and the cooling water outlet pipe 28 , and the cooling water outlet pipe 28 is arranged above the cooling water inlet pipe 27 . The upper end of the vertical condensing pipe 13 is connected to the horizontal condensing pipe 15 through the pipeline 14, and the end of the horizontal condensing pipe 15 away from the pipeline 14 is connected to the water separator 16, and the bottom of the water separator 16 is provided with an opening 17, and the water separator 16 is connected to the pneumatic A first valve 19 is provided between the diaphragm pump 18 , the water separator 16 and the pneumatic diaphragm pump 18 , and the pneumatic diaphragm pump 18 is provided with an electromagnetic pneumatic valve 20 for operation by the operator.
气动隔膜泵18将分水器16中的低温溶剂抽出,气动隔膜泵18通过管道29连接喷头23,喷头23通入管路14,喷头23向下喷水,对高温溶剂蒸汽进行冷却,部分低温溶剂随着高温溶剂蒸汽上升进入横冷凝管15,部分通过竖直冷凝管13流入反应釜,管道29设有第二阀门22,横冷凝管15靠近管路14的位置设有热电阻24,热电阻24连接温度显示屏25。The pneumatic diaphragm pump 18 pumps out the low-temperature solvent in the water separator 16. The pneumatic diaphragm pump 18 is connected to the nozzle 23 through the pipeline 29. The nozzle 23 is connected to the pipeline 14. The nozzle 23 sprays water downward to cool the high-temperature solvent vapor, and part of the low-temperature solvent As the high-temperature solvent vapor rises into the horizontal condensing pipe 15, part of it flows into the reaction kettle through the vertical condensing pipe 13, the pipeline 29 is provided with a second valve 22, and the horizontal condensing pipe 15 is provided with a thermal resistor 24 near the position of the pipeline 14. 24 connect the temperature display 25.
所述刮板机构5整体呈U形,并与所述釜体8的端面相配合,低速搅拌轴11转动时,刮板机构5就会跟着转动,从而将粘在釜体8内侧壁的原料刮除。此外,搅拌齿3和搅拌叶片4表面设置有搪玻璃。The scraper mechanism 5 is U-shaped as a whole, and cooperates with the end surface of the kettle body 8. When the low-speed stirring shaft 11 rotates, the scraper mechanism 5 will rotate accordingly, thereby removing the raw materials stuck to the inner wall of the kettle body 8. scrape off. In addition, the surfaces of the stirring teeth 3 and the stirring blades 4 are lined with glass.
操作人员通过控制电磁气动阀20,通过气动隔膜泵18控制喷头23的低温溶剂加入量,进而控制进入蒸馏装置的高温溶剂蒸汽的温度。The operator controls the amount of low-temperature solvent added to the nozzle 23 by controlling the electromagnetic pneumatic valve 20 and the pneumatic diaphragm pump 18, thereby controlling the temperature of the high-temperature solvent vapor entering the distillation device.
温度显示屏25和电磁气动阀20之间设有温控仪26,喷头23喷出低温溶剂对高温溶剂蒸汽进行了冷却控温,而且通过温度显示屏25和温控仪20与气动隔膜泵15实现连动工作,当横冷凝管15内的蒸馏头温度比温控仪20设定的温度高时,温控仪20输出信号启动气动隔膜泵18泵料冷却;当蒸馏头温度比温控仪20设定的温度低时,温控仪20断开输出信号来停止气动隔膜泵18泵料冷却,通过这种方式实现控温的作用。A temperature controller 26 is provided between the temperature display screen 25 and the electromagnetic pneumatic valve 20, and the nozzle 23 sprays out low-temperature solvent to cool and control the temperature of the high-temperature solvent vapor, and through the temperature display screen 25 and the temperature controller 20 and the pneumatic diaphragm pump 15 Realize linked work, when the temperature of the distillation head in the horizontal condensation pipe 15 is higher than the temperature set by the temperature controller 20, the output signal of the temperature controller 20 starts the cooling of the pneumatic diaphragm pump 18; when the temperature of the distillation head is higher than the temperature of the temperature controller When the temperature set by 20 is low, the temperature controller 20 cuts off the output signal to stop the pneumatic diaphragm pump 18 from pumping material for cooling, and in this way realizes the function of temperature control.
上面对本专利的较佳实施方式作了详细说明,但是本专利并不限于上述实施方式,在本领域的普通技术人员所具备的知识范围内,还可以在不脱离本专利宗旨的前提下做出各种变化。The preferred implementation of this patent has been described in detail above, but this patent is not limited to the above-mentioned implementation, and within the knowledge of those of ordinary skill in the art, it can also be made without departing from the purpose of this patent. Variations.
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Cited By (4)
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CN106629940A (en) * | 2016-11-23 | 2017-05-10 | 丽水市人民医院 | Device for temporarily preparing distilled water in operating room |
CN108786700A (en) * | 2018-06-13 | 2018-11-13 | 运城学院 | A kind of chemosynthesis reaction kettle |
CN112980581A (en) * | 2021-04-22 | 2021-06-18 | 江西馨源香料有限公司 | Natural and healthy spice preparation process and device |
CN113082753A (en) * | 2021-04-26 | 2021-07-09 | 江西亚香香料有限公司 | Distillation still is used in production of efficient essence spices |
-
2015
- 2015-07-03 CN CN201520490265.4U patent/CN204768715U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106629940A (en) * | 2016-11-23 | 2017-05-10 | 丽水市人民医院 | Device for temporarily preparing distilled water in operating room |
CN106629940B (en) * | 2016-11-23 | 2019-09-10 | 丽水市人民医院 | A kind of operating room extemporaneous preparation distilled water device |
CN108786700A (en) * | 2018-06-13 | 2018-11-13 | 运城学院 | A kind of chemosynthesis reaction kettle |
CN112980581A (en) * | 2021-04-22 | 2021-06-18 | 江西馨源香料有限公司 | Natural and healthy spice preparation process and device |
CN113082753A (en) * | 2021-04-26 | 2021-07-09 | 江西亚香香料有限公司 | Distillation still is used in production of efficient essence spices |
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