CN204783671U - Novel liquid ring vacuum pump system - Google Patents
Novel liquid ring vacuum pump system Download PDFInfo
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- CN204783671U CN204783671U CN201520415735.0U CN201520415735U CN204783671U CN 204783671 U CN204783671 U CN 204783671U CN 201520415735 U CN201520415735 U CN 201520415735U CN 204783671 U CN204783671 U CN 204783671U
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Abstract
本实用新型涉及一种新型液环真空泵系统,包括真空设备、液环真空泵、气液分离槽、冷凝器、高位槽、尾气吸收系统,高位槽从上到下依次设置有溢流口、回流口、进液口;真空设备通过真空气相管与液环真空泵的吸气口相连,液环真空泵的气液排出口与气液分离槽的进口相连,气液分离槽的出气口与尾气吸收系统相连;工艺系统中的工艺液体通过管道进入气液分离槽内,分离后的液体依次经过循环泵、冷凝器进入高位槽,高位槽的溢流口与工艺系统相连,高位槽的回流口与气液分离槽相连,高位槽的出液口与液环真空泵的进液口相连。通过将工艺液体代替循环水,避免废水产生,减少废水处理费用;工艺液体吸收工艺真空气体,减少大气污染,回收工艺物料。
The utility model relates to a novel liquid ring vacuum pump system, comprising vacuum equipment, a liquid ring vacuum pump, a gas-liquid separation tank, a condenser, a high position tank, and an exhaust gas absorption system. The high position tank is sequentially provided with an overflow port and a return port from top to bottom , liquid inlet; the vacuum equipment is connected to the suction port of the liquid ring vacuum pump through the vacuum gas phase tube, the gas-liquid discharge port of the liquid ring vacuum pump is connected to the inlet of the gas-liquid separation tank, and the gas-liquid separation tank outlet is connected to the tail gas absorption system ;The process liquid in the process system enters the gas-liquid separation tank through the pipeline, and the separated liquid enters the high-level tank through the circulating pump and the condenser in turn. The overflow port of the high-level tank is connected with the process system, and the return port of the high-level tank is connected with the gas-liquid The separation tanks are connected, and the liquid outlet of the head tank is connected with the liquid inlet of the liquid ring vacuum pump. By replacing circulating water with process liquid, waste water is avoided and waste water treatment costs are reduced; process liquid absorbs process vacuum gas, reduces air pollution, and recycles process materials.
Description
技术领域 technical field
本实用新型涉及一种真空泵系统,具体涉及一种新型液环真空泵系统。 The utility model relates to a vacuum pump system, in particular to a novel liquid ring vacuum pump system.
背景技术 Background technique
化工装置经常采用水环式真空泵取得真空,该工艺系统主要是从所需真空的设备中连接管道至真空泵,另对真空泵提供循环水,利用循环水的离心带动气相,制取真空。从真空泵排出的气水混合物经气水分离罐,气至尾气吸附系统,被工艺气体污染的循环水至污水处理装置。 Chemical plants often use water ring vacuum pumps to obtain vacuum. This process system is mainly to connect pipes from the equipment required for vacuum to the vacuum pump, and to provide circulating water to the vacuum pump, and use the centrifugal force of the circulating water to drive the gas phase to produce vacuum. The gas-water mixture discharged from the vacuum pump passes through the gas-water separation tank, the gas goes to the tail gas adsorption system, and the circulating water polluted by the process gas goes to the sewage treatment device.
现有的水环式真空系统的缺点在于:1、循环水量消耗大,增加装置公用工程费用;2、气水分离后的被工艺气体污染的循环水需经废水处理,增加装置废水处理费用;3、溶解于循环水中工艺物料未被回收利用,增加工艺物料耗损。 The disadvantages of the existing water ring vacuum system are: 1. The consumption of circulating water is large, which increases the utility cost of the device; 2. The circulating water polluted by the process gas after gas-water separation needs to be treated with wastewater, which increases the cost of wastewater treatment of the device; 3. Process materials dissolved in circulating water are not recycled, increasing the consumption of process materials.
实用新型内容 Utility model content
本实用新型的目的在于:提供一种绿色环保、成本低的新型液环真空泵系统。 The purpose of the utility model is to provide a novel liquid ring vacuum pump system which is green, environment-friendly and low in cost.
为了实现上述目的,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:
一种新型液环真空泵系统,包括真空设备、液环真空泵、气液分离槽、冷凝器、高位槽、尾气吸收系统,所述的高位槽从上到下依次设置有溢流口、回流口、进液口; A new liquid ring vacuum pump system, including vacuum equipment, a liquid ring vacuum pump, a gas-liquid separation tank, a condenser, an elevated tank, and an exhaust gas absorption system. The elevated tank is sequentially provided with an overflow port, a return port, liquid inlet;
所述的真空设备通过真空气相管与液环真空泵的吸气口相连,液环真空泵的气液排出口与气液分离槽的进口相连,气液分离槽的出气口与尾气吸收系统相连; The vacuum equipment is connected to the suction port of the liquid ring vacuum pump through the vacuum gas phase tube, the gas-liquid discharge port of the liquid ring vacuum pump is connected to the inlet of the gas-liquid separation tank, and the gas outlet of the gas-liquid separation tank is connected to the tail gas absorption system;
工艺系统中的工艺液体通过管道进入气液分离槽内,经气液分离槽分离后的液体依次经过循环泵、冷凝器进入到高位槽,所述的高位槽的溢流口与工艺系统相连,高位槽的回流口与气液分离槽相连,高位槽的出液口与液环真空泵的进液口相连。 The process liquid in the process system enters the gas-liquid separation tank through the pipeline, and the liquid separated by the gas-liquid separation tank sequentially passes through the circulating pump and the condenser and enters the head tank, and the overflow port of the head tank is connected with the process system. The return port of the elevated tank is connected with the gas-liquid separation tank, and the liquid outlet of the elevated tank is connected with the liquid inlet of the liquid ring vacuum pump.
优选地,所述的气液分离槽的出气口设置在槽的顶部。 Preferably, the gas outlet of the gas-liquid separation tank is arranged on the top of the tank.
优选地,所述的高位槽的溢流口与工艺系统之间设置开关阀。 Preferably, a switching valve is provided between the overflow port of the elevated tank and the process system.
本实用新型的有益效果在于: The beneficial effects of the utility model are:
1、工艺液体物料代替循环水,减少装置公用工程费用。2、工艺液体物料代替循环水,避免废水产生,减少废水处理费用。3、工艺液体物料吸收工艺真空气体,减少大气污染,回收工艺物料。 1. The process liquid material replaces the circulating water, reducing the cost of public works for the installation. 2. The process liquid material replaces the circulating water to avoid the generation of waste water and reduce the cost of waste water treatment. 3. The process liquid material absorbs process vacuum gas, reduces air pollution and recycles process materials.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
具体实施方式 Detailed ways
结合附图1对本实用新型作进一步说明: The utility model is further described in conjunction with accompanying drawing 1:
一种新型液环真空泵系统,包括真空设备1、液环真空泵2、气液分离槽3、冷凝器4、高位槽5、尾气吸收系统6,所述的高位槽5从上到下依次设置有溢流口、回流口、进液口; A new type of liquid ring vacuum pump system, including vacuum equipment 1, liquid ring vacuum pump 2, gas-liquid separation tank 3, condenser 4, high level tank 5, tail gas absorption system 6, the high level tank 5 is sequentially arranged with Overflow port, return port, liquid inlet;
所述的真空设备1通过真空气相管与液环真空泵2的吸气口相连,液环真空泵2的气液排出口与气液分离槽3的进口相连,气液分离槽3的出气口与尾气吸收系统6相连; The vacuum device 1 is connected to the suction port of the liquid ring vacuum pump 2 through a vacuum gas phase tube, the gas-liquid outlet of the liquid ring vacuum pump 2 is connected to the inlet of the gas-liquid separation tank 3, and the gas outlet of the gas-liquid separation tank 3 is connected to the tail gas The absorption system 6 is connected;
工艺系统7中的工艺液体通过管道进入气液分离槽3内,经气液分离槽3分离后的液体依次经过循环泵8、冷凝器4进入到高位槽5,所述的高位槽5的溢流口与工艺系统7相连,高位槽5的回流口与气液分离槽3相连,高位槽5的出液口与液环真空泵2的进液口相连。 The process liquid in the process system 7 enters the gas-liquid separation tank 3 through the pipeline, and the liquid separated by the gas-liquid separation tank 3 enters the head tank 5 through the circulation pump 8 and the condenser 4 successively, and the overflow of the head tank 5 The orifice is connected to the process system 7 , the return port of the head tank 5 is connected to the gas-liquid separation tank 3 , and the liquid outlet of the head tank 5 is connected to the liquid inlet of the liquid ring vacuum pump 2 .
所述的气液分离槽3的出气口设置在槽的顶部。 The gas outlet of the gas-liquid separation tank 3 is arranged on the top of the tank.
所述的高位槽5的溢流口与工艺系统7之间设置开关阀。 An on-off valve is set between the overflow port of the elevated tank 5 and the process system 7 .
本实用新型的工作原理:自真空设备1的工艺气体通过真空气相管接至液环真空泵2,气液混合从液环真空泵2的气液排出口至气液分离槽3,气相从气液分离槽3顶部至尾气吸附系统6。液相经循环泵8、冷凝器4后至液高位槽5。高位槽5液位高位设置溢流口,管路设置开关阀回工艺系统7,当气液分离槽3的液位达到高限度时,开关阀由关状态开启,工艺液体流向工艺系统7,气液分离槽3液位回归正常状态范围,开关阀关闭。高位槽5液位次高位设置回流口,工艺液体回气液分离槽3。高位槽5液位低位设置出液口,至液环真空泵2,代替循环水,吸收真空气体,不产生废水量。吸收工艺气体的工艺液体至工艺系统,减少物料排放,保护大气环境,回收工艺物料。 The working principle of the utility model: the process gas from the vacuum equipment 1 is connected to the liquid ring vacuum pump 2 through the vacuum gas phase pipe, the gas and liquid are mixed from the gas and liquid outlet of the liquid ring vacuum pump 2 to the gas and liquid separation tank 3, and the gas phase is separated from the gas and liquid Tank 3 top to tail gas adsorption system 6. The liquid phase goes through the circulating pump 8 and the condenser 4 to the liquid high level tank 5. An overflow port is set at the high liquid level of the high level tank 5, and a switch valve is set in the pipeline to return to the process system 7. When the liquid level of the gas-liquid separation tank 3 reaches the upper limit, the switch valve is opened from the closed state, and the process liquid flows to the process system 7, and the gas The liquid level of the liquid separation tank 3 returns to the normal state range, and the on-off valve is closed. A reflux port is set at the second highest level of the liquid level in the upper tank 5, and the process liquid returns to the gas-liquid separation tank 3. A liquid outlet is set at the lower level of the liquid level of the upper tank 5, and reaches the liquid ring vacuum pump 2 to replace circulating water and absorb vacuum gas without generating waste water. The process liquid that absorbs the process gas is sent to the process system to reduce material discharge, protect the atmospheric environment, and recycle process materials.
上述结合附图对实用新型进行了示例性描述,显然本实用新型具体实现并不受上述方式的限制,只要采用了实用新型的方法构思和技术方案进行的这种非实质改进,或未经改进将实用新型的构思和技术方案直接应用于其他场合的,均在本实用新型的保护范围之内。 The utility model has been described as an example in conjunction with the accompanying drawings. Obviously, the specific implementation of the utility model is not limited by the above-mentioned method, as long as the method concept and technical solution of the utility model are used for this insubstantial improvement, or without improvement Directly applying the ideas and technical solutions of the utility model to other occasions falls within the protection scope of the utility model.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520415735.0U CN204783671U (en) | 2015-06-16 | 2015-06-16 | Novel liquid ring vacuum pump system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520415735.0U CN204783671U (en) | 2015-06-16 | 2015-06-16 | Novel liquid ring vacuum pump system |
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| CN204783671U true CN204783671U (en) | 2015-11-18 |
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| CN201520415735.0U Expired - Lifetime CN204783671U (en) | 2015-06-16 | 2015-06-16 | Novel liquid ring vacuum pump system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106640650A (en) * | 2016-12-30 | 2017-05-10 | 哈尔滨天顺化工科技开发有限公司 | Liquid recovery device of water ring vacuum pump for producing carbon fiber precursors |
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2015
- 2015-06-16 CN CN201520415735.0U patent/CN204783671U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106640650A (en) * | 2016-12-30 | 2017-05-10 | 哈尔滨天顺化工科技开发有限公司 | Liquid recovery device of water ring vacuum pump for producing carbon fiber precursors |
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Granted publication date: 20151118 |
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| CX01 | Expiry of patent term |