WO2021115010A1 - Environmentally friendly circulating discharging distillation tower - Google Patents
Environmentally friendly circulating discharging distillation tower Download PDFInfo
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- WO2021115010A1 WO2021115010A1 PCT/CN2020/128224 CN2020128224W WO2021115010A1 WO 2021115010 A1 WO2021115010 A1 WO 2021115010A1 CN 2020128224 W CN2020128224 W CN 2020128224W WO 2021115010 A1 WO2021115010 A1 WO 2021115010A1
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- distillation tower
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/02—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in boilers or stills
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B7/00—Combinations of two or more condensers, e.g. provision of reserve condenser
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
Definitions
- the utility model relates to the technical field of industrial standard devices, in particular to an environmentally-friendly circulating discharge distillation tower.
- the distillation tower is a chemical equipment made of rare metal titanium and other materials and its alloy materials. It has the characteristics of high strength, high toughness, high temperature resistance, corrosion resistance, and light specific gravity; therefore, it is widely used in chemical, petrochemical, metallurgy, light industry, textiles, etc.
- the function of the distillation tower is mainly to separate mixed liquids in the fields of, alkali production, pharmaceuticals, pesticides, electroplating, electronics, etc., using different liquids under different conditions, such as different temperatures and different volatility (boiling points). The purification effect is achieved.
- an environmentally friendly circulating discharge distillation tower including a tower kettle, a distillation tower body is fixed at the top of the tower kettle, and a side of the distillation tower body is welded with an inlet For the material port, a reboiler is plugged and fixed on one side of the tower kettle through a pipe, a multi-mode rapid condensation structure is fixed on the top of the tower kettle, and the lower end of the multi-mode rapid condensation structure is connected with a cooler through a pipe, so A finished product tank is fixed on one side of the lower end of the cooler, a semi-finished product pipe is welded on the other side of the lower end of the cooler, and one end of the reboiler is connected with a waste water recovery storage structure through a pipe.
- the multi-mode rapid condensing structure includes a sheet-shaped heat conduction plate, an air-cooled fixing frame, an air-cooled fan blade, an assembly fixing sleeve, a dispersed rapid liquefaction tube, a miniature booster pump, a steam circulation duct, an immersion water-cooled box, and a centralized
- an air-cooled fixing frame is fixed on both sides of the sheet-shaped heat-conducting plate by screws
- an air-cooled fan blade is fixed inside the air-cooled fixing frame
- the sheet-shaped heat-conducting plate and the air-cooled fixing frame are fixed
- An assembly fixing sleeve is sleeved on the outside
- a dispersion rapid liquefaction tube is fixed inside the sheet-shaped heat conduction plate
- the bottom end of one end of the dispersion rapid liquefaction tube is connected with a miniature booster pump through a separate water pipe, the miniature booster pump One end of the pipe is plugged with a steam circulation pipe, the outside of the steam circulation
- the waste water recovery and storage structure includes a first water pump, a filtering and purification structure, a second water pump, and a recovery storage tank.
- One side of the first water pump is connected with a filtering and purification structure through a diversion tube.
- One side is connected with a second water pump through a diversion tube, and one end of the second water pump is connected with a recovery storage tank through a diversion tube.
- the filter purification structure includes a filter water tank, a sterilization filter plate, an organic matter removal filter plate, and a particle removal filter plate.
- the interior of the filter water tank is respectively inserted with a sterilization filter plate and an organic matter removal filter plate from one end to the other end. And particle removal filter plate.
- the material of the sterilization filter plate is high-purity nano silver
- the material of the organic matter removal filter plate is honeycomb activated carbon
- the material of the particle removal filter plate is PP fiber.
- one end of the recovery storage tank is provided with a waste water outlet, and the diameter of the waste water outlet is 20 cm.
- an output motor is fixed at one end of the air-cooled fan blade, and the output motor and the air-cooled fan blade are fixedly connected by a flat key.
- the material of the dispersing rapid liquefaction tube is copper
- the sheet-shaped heat conducting plate is provided with a placement groove inside, and the top end of the dispersing rapid liquefaction tube is completely attached to the upper surface of the placement groove.
- one end of the reboiler is provided with a steam inlet, and the diameter of the steam inlet is five centimeters.
- the volatile gas generated in the utility model is pumped and driven by the micro booster pump through the steam circulation duct, so that the volatile gas moves in the transmission direction of the micro booster pump, and passes through the inside of the immersed water-cooled box, due to the immersed water cooling
- the cooling liquid is stored inside the tank, and part of the heat in the volatile gas is taken away by the characteristics of heat transfer to form a preliminary liquefaction.
- the preliminary liquefied gas is transferred to the dispersed rapid liquefaction tube through the micro booster pump, and enters the smaller In the space, it is convenient to compress and cool down.
- the sheet-shaped heat-conducting plate After the material conduction of the dispersed rapid liquefaction tube and the adsorption of the sheet-shaped heat-conducting plate, the remaining heat is discharged, and the sheet-shaped heat-conducting plate is air-cooled at the same time through the air-cooled fan blades on both sides of the sheet-shaped heat-conducting plate. Its own heat can ensure that the heat in the dispersed rapid liquefaction tube is quickly transferred and sucked out, so that the preliminary liquefied gas can be heated to form a discharge liquid, which is discharged through the collection of the centralized liquefaction outlet tube, so that the device can be The discharging material of multiple distillations is rapidly cooled, thereby speeding up the efficiency of circulating discharging;
- the utility model connects a large amount of polluted waste water produced by the reboiler during operation to the first water pump through a pipe.
- the waste water in the pipe is guided into the interior of the filtering and purification structure by the power of the first water pump.
- the waste water is filtered and purified.
- the particle removal filter plate, the organic matter removal filter plate, and the sterilization filter plate are multi-layered and filtered.
- the particle removal filter plate uses the characteristics of its own material to isolate the particles doped in the wastewater, and the organic matter removal filter plate uses the characteristics of its own material.
- the organic matter in the wastewater is adsorbed, and finally the wastewater is sterilized and disinfected again through the sterilization characteristics of the sterilization filter plate material to reduce the harm of the wastewater.
- the second water pump is pulled to the recycling storage box for storage, so that the device is in use. To reduce the impact on the environment.
- Figure 1 is a schematic diagram of the overall structure of the utility model
- Figure 2 is a side view of the utility model as a whole
- Figure 3 is a side view of the multi-mode rapid condensation structure of the utility model
- Figure 4 is an exploded view of the multi-mode rapid condensation structure of the utility model
- Figure 5 is a partial structural diagram of the waste water recycling and storage structure of the utility model
- Figure 6 is a cross-sectional view of the filter purification structure of the present invention.
- an environmentally-friendly circulating discharge distillation tower including a tower kettle 1, a distillation tower main body 2 is fixed at the top of the tower kettle 1, and a feed inlet 3 welded on one side of the distillation tower main body 2, and the tower kettle
- a reboiler 4 is inserted and fixed on one side of the reboiler 4 through a pipe.
- One end of the reboiler 4 is provided with a steam inlet.
- the diameter of the steam inlet is five centimeters to facilitate the introduction of mixed steam into the reboiler 4.
- a multi-mode rapid condensing structure 14 is fixed at the top.
- the lower end of the multi-mode rapid condensing structure 14 is connected with a cooler 15 through a pipe.
- One side of the lower end of the cooler 15 is fixed with a finished product tank 16, and the other side of the lower end of the cooler 15 is welded with
- the multi-mode rapid condensing structure 14 includes a sheet-shaped heat conduction plate 5, an air-cooled fixing frame 6, an air-cooled fan blade 7, an assembly fixing sleeve 8, a dispersed rapid liquefaction tube 9, a miniature booster pump 10, a steam circulation duct 11, and an immersion type water cooling
- the box 12 and the centralized liquefaction outlet pipe 13, the sheet-shaped heat conduction plate 5 is fixed with an air-cooled fixing frame 6 by screws.
- the inside of the air-cooled fixing frame 6 is fixed with an air-cooled fan blade 7, and one end of the air-cooled fan blade 7
- the output motor is fixed, and the output motor and the air-cooled fan blade 7 are fixedly connected by a flat key, which is convenient to drive the air-cooled fan blade 7 to rotate, thereby generating air cooling.
- the outer sides of the sheet-shaped heat conducting plate 5 and the air-cooling fixing frame 6 are sleeved Assemble the fixing sleeve 8, the inside of the sheet-shaped heat-conducting plate 5 is fixed with a dispersion rapid liquefaction tube 9, the material of the dispersion rapid-liquefaction tube 9 is copper, and the inside of the sheet-shaped heat-conducting plate 5 is provided with a placement groove to disperse the top of the rapid liquefaction tube 9 and The upper surface of the placement tank is completely attached to facilitate the rapid dissipation of heat inside the dispersion rapid liquefaction tube 9.
- the bottom end of one end of the dispersion rapid liquefaction tube 9 is connected to a micro booster pump 10 through a separate water pipe, and one end of the micro booster pump 10 is plugged in There is a steam circulation duct 11, the outside of the steam circulation duct 11 is fixed with an immersion water-cooled box 12, and the bottom end of the other end of the dispersion rapid liquefaction pipe 9 is fixed with a concentrated liquefaction outlet pipe 13, which is convenient for the circulation distilled to contain a large amount of volatile substances. Rapid cooling of the discharged steam;
- the waste water recovery storage structure 22 includes a first water pump 18, a filtering and purification structure 19, a second water pump 20, and a recovery storage tank 21.
- One side of the first water pump 18 is connected to a filtering and purification structure 19 through a diversion tube.
- the filtering and purification structure 19 includes filtering.
- the inside of the filter water tank 23 is respectively inserted with the sterilization filter plate 24, the organic matter removal filter plate 25 and the particle removal filter plate from one end to the other end. 26.
- the material of the sterilization filter plate 24 is high-purity nano silver
- the material of the organic matter removal filter plate 25 is honeycomb activated carbon
- the material of the particle removal filter plate 26 is PP fiber to facilitate the filtration of wastewater with different effects.
- a second water pump 20 is connected to the side through a diversion tube. One end of the second water pump 20 is connected to a recovery storage box 21 through a diversion tube. One end of the recovery storage box 21 is provided with a waste water outlet. The diameter of the waste water outlet is 20 cm. , It is convenient to discharge the filtered waste water stored in the inside to facilitate the filtering and recycling of the waste water generated by the reboiler 4.
- the preliminarily liquefied gas is transferred to the dispersion rapid liquefaction tube 9 through the micro booster pump 10, and is divided into a smaller space to facilitate compression and cooling.
- the remaining heat is exported, and it is air-cooled by the air-cooled fan blades 7 on both sides of the sheet-shaped heat-conducting plate 5, reducing the self-heat of the sheet-shaped heat-conducting plate 5, and can ensure that the heat in the dispersed rapid liquefaction tube 9 is quickly transferred and sucked out.
- the preliminary liquefied gas can be heated to form a discharging liquid, which flows out through the collection of the centralized liquefaction outlet pipe 13, so that the device can quickly cool the multiple distilled discharging materials containing a large amount of volatile substances, thereby speeding up the circulation of discharging materials.
- Efficiency the large amount of polluted waste water generated by the reboiler 4 during operation is connected to the first water pump 18 through a pipe, and the waste water in the pipe is guided into the interior of the filter purification structure 19 by the power of the first water pump 18, and the waste water is filtered and purified
- the particle removal filter plate 26, the organic matter removal filter plate 25, and the sterilization filter plate 24 are multi-layered and filtered.
- the particle removal filter plate 26 uses the characteristics of its own material to isolate the particles doped in the wastewater, and the organic matter removal filter plate 25 Use the characteristics of its own material to adsorb the organic matter in the waste water, and finally sterilize and disinfect the waste water again through the sterilization characteristics of the sterilization filter plate 24 material to reduce the harm of the waste water. Finally, it is pulled to the recycling storage tank by the second water pump 20. 21 for storage, so that the device reduces the impact on the environment during use.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
本实用新型涉及工业制式装置技术领域,具体为一种环保型循环出料蒸馏塔。The utility model relates to the technical field of industrial standard devices, in particular to an environmentally-friendly circulating discharge distillation tower.
蒸馏塔是稀有金属钛等材料及其合金材料制造的化工设备具有强度高、韧性大、耐高温、耐腐蚀、比重轻等特性;因此被广泛应用与化工、石油化工、冶金、轻工、纺织、制碱、制药、农药、电镀、电子等领域,蒸馏塔的功能主要是为了分离混合液体,利用不同液体在不同条件下,如温度不同,挥发性(沸点)不同的原理进行液体分离,从而达到提纯效果,但是,现有的装置在进行分离后的冷却回流收集时,冷凝器的冷却方式单一,导致冷凝液化效率较慢,降低循环出料的效率,且使用过程中产生的废水未经过净化,对环境有较大的影响。The distillation tower is a chemical equipment made of rare metal titanium and other materials and its alloy materials. It has the characteristics of high strength, high toughness, high temperature resistance, corrosion resistance, and light specific gravity; therefore, it is widely used in chemical, petrochemical, metallurgy, light industry, textiles, etc. The function of the distillation tower is mainly to separate mixed liquids in the fields of, alkali production, pharmaceuticals, pesticides, electroplating, electronics, etc., using different liquids under different conditions, such as different temperatures and different volatility (boiling points). The purification effect is achieved. However, when the existing device performs cooling and reflux collection after separation, the cooling method of the condenser is single, resulting in slow condensing and liquefaction efficiency, reducing the efficiency of recycling and discharging, and the waste water generated during use is not passed through Purification has a greater impact on the environment.
实用新型内容Utility model content
为实现上述目的,本实用新型提供如下技术方案:一种环保型循环出料蒸馏塔,包括塔釜,所述塔釜的顶端固定有蒸馏塔主体,所述蒸馏塔主体的一侧焊接有进料口,所述塔釜的一侧通过导管插接固定有重沸器,所述塔釜顶端固定有多方式快速冷凝结构,所述多方式快速冷凝结构的下端通过导管连接有冷却器,所述冷却器下端的一侧固定有成品罐,所述冷却器下端的另一侧焊接有半成品管,所述重沸器的一端通过导管连接有废水回收存储结构。In order to achieve the above object, the present invention provides the following technical solution: an environmentally friendly circulating discharge distillation tower, including a tower kettle, a distillation tower body is fixed at the top of the tower kettle, and a side of the distillation tower body is welded with an inlet For the material port, a reboiler is plugged and fixed on one side of the tower kettle through a pipe, a multi-mode rapid condensation structure is fixed on the top of the tower kettle, and the lower end of the multi-mode rapid condensation structure is connected with a cooler through a pipe, so A finished product tank is fixed on one side of the lower end of the cooler, a semi-finished product pipe is welded on the other side of the lower end of the cooler, and one end of the reboiler is connected with a waste water recovery storage structure through a pipe.
优选的,所述多方式快速冷凝结构包括片状导热板、风冷固定架、风冷扇叶、装配固定套、分散快速液化管、微型增压泵、蒸汽循环导管、浸泡式水冷箱和集中液化导出管,所述片状导热板的两侧均通过螺钉固定有风冷固定架,所述风冷固定架的内部固定有风冷扇叶,所述片状导热板及 风冷固定架的外侧均套接有装配固定套,所述片状导热板的内部固定有分散快速液化管,所述分散快速液化管一端的底端通过分离水管连接有微型增压泵,所述微型增压泵的一端插接有蒸汽循环导管,所述蒸汽循环导管的外侧固定有浸泡式水冷箱,所述分散快速液化管另一端的底端固定有集中液化导出管。Preferably, the multi-mode rapid condensing structure includes a sheet-shaped heat conduction plate, an air-cooled fixing frame, an air-cooled fan blade, an assembly fixing sleeve, a dispersed rapid liquefaction tube, a miniature booster pump, a steam circulation duct, an immersion water-cooled box, and a centralized In the liquefaction outlet pipe, an air-cooled fixing frame is fixed on both sides of the sheet-shaped heat-conducting plate by screws, an air-cooled fan blade is fixed inside the air-cooled fixing frame, and the sheet-shaped heat-conducting plate and the air-cooled fixing frame are fixed An assembly fixing sleeve is sleeved on the outside, a dispersion rapid liquefaction tube is fixed inside the sheet-shaped heat conduction plate, and the bottom end of one end of the dispersion rapid liquefaction tube is connected with a miniature booster pump through a separate water pipe, the miniature booster pump One end of the pipe is plugged with a steam circulation pipe, the outside of the steam circulation pipe is fixed with an immersion type water-cooled box, and the bottom end of the other end of the dispersed rapid liquefaction pipe is fixed with a concentrated liquefaction outlet pipe.
优选的,所述废水回收存储结构包括第一水泵、过滤净化结构、第二水泵和回收存储箱,所述第一水泵的一侧通过导流管连接有过滤净化结构,所述过滤净化结构的一侧通过导流管连接有第二水泵,所述第二水泵的一端通过导流管连接有回收存储箱。Preferably, the waste water recovery and storage structure includes a first water pump, a filtering and purification structure, a second water pump, and a recovery storage tank. One side of the first water pump is connected with a filtering and purification structure through a diversion tube. One side is connected with a second water pump through a diversion tube, and one end of the second water pump is connected with a recovery storage tank through a diversion tube.
优选的,所述过滤净化结构包括过滤水箱、杀菌滤板、有机物去除滤板和颗粒去除滤板,所述过滤水箱的内部分别从一端到另一端依次插接有杀菌滤板、有机物去除滤板和颗粒去除滤板。Preferably, the filter purification structure includes a filter water tank, a sterilization filter plate, an organic matter removal filter plate, and a particle removal filter plate. The interior of the filter water tank is respectively inserted with a sterilization filter plate and an organic matter removal filter plate from one end to the other end. And particle removal filter plate.
优选的,所述杀菌滤板的材质为高纯纳米银,所述有机物去除滤板的材质为蜂窝活性炭,所述颗粒去除滤板的材质为PP纤维。Preferably, the material of the sterilization filter plate is high-purity nano silver, the material of the organic matter removal filter plate is honeycomb activated carbon, and the material of the particle removal filter plate is PP fiber.
优选的,所述回收存储箱的一端开设有废水导出口,所述废水导出口的直径为二十厘米。Preferably, one end of the recovery storage tank is provided with a waste water outlet, and the diameter of the waste water outlet is 20 cm.
优选的,所述风冷扇叶的一端固定有输出马达,所述输出马达与风冷扇叶通过平键固定连接。Preferably, an output motor is fixed at one end of the air-cooled fan blade, and the output motor and the air-cooled fan blade are fixedly connected by a flat key.
优选的,所述分散快速液化管的材质为铜,所述片状导热板的内部开设有放置槽,所述分散快速液化管的顶端与放置槽的上表面完全贴合。Preferably, the material of the dispersing rapid liquefaction tube is copper, the sheet-shaped heat conducting plate is provided with a placement groove inside, and the top end of the dispersing rapid liquefaction tube is completely attached to the upper surface of the placement groove.
优选的,所述重沸器的一端开设有蒸汽导入口,所述蒸汽导入口的直径为五厘米。Preferably, one end of the reboiler is provided with a steam inlet, and the diameter of the steam inlet is five centimeters.
与现有技术相比,本实用新型的有益效果是:Compared with the prior art, the beneficial effects of this utility model are:
1、本实用新型中产生的易挥发气体通过蒸汽循环导管被微型增压泵进行抽取带动,使得易挥发气体跟随微型增压泵的传输方向运动,通过浸 泡式水冷箱的内部,由于浸泡式水冷箱的内部存储有冷却液体,通过热传递的特性将易挥发气体中一部分的热量进行带走,形成初步液化,初步液化气体通过微型增压泵传递至分散快速液化管中,经过分流进入较小的空间内,便于压缩降温,经过分散快速液化管的材质传导与片状导热板的吸附,将剩余热量导出,经过片状导热板两侧风冷扇叶的同时风冷,降低片状导热板的自身热量,可以保证将分散快速液化管内的热量快速传导吸出,从而使得初步液化气体可以去热形成出料液体,通过集中液化导出管的汇总进行流出,使得装置可以对含有较多量易挥发物质的多次蒸馏出料进行快速冷却,从而加快循环出料的效率;1. The volatile gas generated in the utility model is pumped and driven by the micro booster pump through the steam circulation duct, so that the volatile gas moves in the transmission direction of the micro booster pump, and passes through the inside of the immersed water-cooled box, due to the immersed water cooling The cooling liquid is stored inside the tank, and part of the heat in the volatile gas is taken away by the characteristics of heat transfer to form a preliminary liquefaction. The preliminary liquefied gas is transferred to the dispersed rapid liquefaction tube through the micro booster pump, and enters the smaller In the space, it is convenient to compress and cool down. After the material conduction of the dispersed rapid liquefaction tube and the adsorption of the sheet-shaped heat-conducting plate, the remaining heat is discharged, and the sheet-shaped heat-conducting plate is air-cooled at the same time through the air-cooled fan blades on both sides of the sheet-shaped heat-conducting plate. Its own heat can ensure that the heat in the dispersed rapid liquefaction tube is quickly transferred and sucked out, so that the preliminary liquefied gas can be heated to form a discharge liquid, which is discharged through the collection of the centralized liquefaction outlet tube, so that the device can be The discharging material of multiple distillations is rapidly cooled, thereby speeding up the efficiency of circulating discharging;
2、本实用新型通过将重沸器在工作时产生的大量污染废水通过导管连接至第一水泵处,导管中的废水通过第一水泵的动力引导进入过滤净化结构的内部,该废水在过滤净化结构中经过颗粒去除滤板、有机物去除滤板、杀菌滤板的多层分工过滤,颗粒去除滤板利用自身材质的特性对废水中掺杂的颗粒进行隔离,有机物去除滤板利用自身材质的特性对废水中的有机物进行吸附,最后通过杀菌滤板材质的杀菌特性对废水进行再次的杀菌、消毒,降低废水的危害,最后通过第二水泵的牵引到回收存储箱进行存储,使得装置在使用过程中减少对环境的影响。2. The utility model connects a large amount of polluted waste water produced by the reboiler during operation to the first water pump through a pipe. The waste water in the pipe is guided into the interior of the filtering and purification structure by the power of the first water pump. The waste water is filtered and purified. In the structure, the particle removal filter plate, the organic matter removal filter plate, and the sterilization filter plate are multi-layered and filtered. The particle removal filter plate uses the characteristics of its own material to isolate the particles doped in the wastewater, and the organic matter removal filter plate uses the characteristics of its own material. The organic matter in the wastewater is adsorbed, and finally the wastewater is sterilized and disinfected again through the sterilization characteristics of the sterilization filter plate material to reduce the harm of the wastewater. Finally, the second water pump is pulled to the recycling storage box for storage, so that the device is in use. To reduce the impact on the environment.
图1为本实用新型整体的结构示意图;Figure 1 is a schematic diagram of the overall structure of the utility model;
图2为本实用新型整体的侧视图;Figure 2 is a side view of the utility model as a whole;
图3为本实用新型多方式快速冷凝结构的侧视图;Figure 3 is a side view of the multi-mode rapid condensation structure of the utility model;
图4为本实用新型多方式快速冷凝结构的爆炸图;Figure 4 is an exploded view of the multi-mode rapid condensation structure of the utility model;
图5为本实用新型废水回收存储结构的局部结构示意图;Figure 5 is a partial structural diagram of the waste water recycling and storage structure of the utility model;
图6为本实用新型过滤净化结构的剖视。Figure 6 is a cross-sectional view of the filter purification structure of the present invention.
图中:1、塔釜;2、蒸馏塔主体;3、进料口;4、重沸器;5、片状 导热板;6、风冷固定架;7、风冷扇叶;8、装配固定套;9、分散快速液化管;10、微型增压泵;11、蒸汽循环导管;12、浸泡式水冷箱;13、集中液化导出管;14、多方式快速冷凝结构;15、冷却器;16、成品罐;17、半成品管;18、第一水泵;19、过滤净化结构;20、第二水泵;21、回收存储箱;22、废水回收存储结构;23、过滤水箱;24、杀菌滤板;25、有机物去除滤板;26、颗粒去除滤板。In the picture: 1. Tower kettle; 2. Distillation tower main body; 3. Feed inlet; 4. Reboiler; 5. Sheet heat conducting plate; 6. Air-cooled fixing frame; 7. Air-cooled fan blade; 8. Assembly Fixed sleeve; 9. Dispersed rapid liquefaction pipe; 10. Mini booster pump; 11. Steam circulation duct; 12. Immersion water-cooled box; 13. Centralized liquefaction outlet pipe; 14. Multi-mode rapid condensation structure; 15. Cooler; 16. Finished product tank; 17. Semi-finished product pipe; 18. First water pump; 19. Filter purification structure; 20. Second water pump; 21. Recycling storage tank; 22. Waste water recycling storage structure; 23. Filter water tank; 24. Sterilization filter Plate; 25, organic matter removal filter plate; 26, particle removal filter plate.
下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本实用新型一部分实施例,而不是全部的实施例。The following will clearly and completely describe the technical solutions in the embodiments of the present utility model with reference to the accompanying drawings in the embodiments of the present utility model. Obviously, the described embodiments are only a part of the embodiments of the present utility model, not all implementations. example.
请参阅图1-6,一种环保型循环出料蒸馏塔,包括塔釜1,塔釜1的顶端固定有蒸馏塔主体2,蒸馏塔主体2的一侧焊接有进料口3,塔釜1的一侧通过导管插接固定有重沸器4,重沸器4的一端开设有蒸汽导入口,蒸汽导入口的直径为五厘米,便于将混合蒸汽导入重沸器4的内部,塔釜1顶端固定有多方式快速冷凝结构14,多方式快速冷凝结构14的下端通过导管连接有冷却器15,冷却器15下端的一侧固定有成品罐16,冷却器15下端的另一侧焊接有半成品管17,重沸器4的一端通过导管连接有废水回收存储结构22;Please refer to Figure 1-6, an environmentally-friendly circulating discharge distillation tower, including a
多方式快速冷凝结构14包括片状导热板5、风冷固定架6、风冷扇叶7、装配固定套8、分散快速液化管9、微型增压泵10、蒸汽循环导管11、浸泡式水冷箱12和集中液化导出管13,片状导热板5的两侧均通过螺钉固定有风冷固定架6,风冷固定架6的内部固定有风冷扇叶7,风冷扇叶7的一端固定有输出马达,输出马达与风冷扇叶7通过平键固定连接,便于带动风冷扇叶7进行旋转,从而产生空冷,片状导热板5及风冷固定架6的外侧均套接有装配固定套8,片状导热板5的内部固定有分散快速液 化管9,分散快速液化管9的材质为铜,片状导热板5的内部开设有放置槽,分散快速液化管9的顶端与放置槽的上表面完全贴合,便于分散快速液化管9内部的热量快速导出,分散快速液化管9一端的底端通过分离水管连接有微型增压泵10,微型增压泵10的一端插接有蒸汽循环导管11,蒸汽循环导管11的外侧固定有浸泡式水冷箱12,分散快速液化管9另一端的底端固定有集中液化导出管13,便于对循环蒸馏出的含有较多量易挥发物质的出料蒸汽进行快速冷却;The multi-mode
废水回收存储结构22包括第一水泵18、过滤净化结构19、第二水泵20和回收存储箱21,第一水泵18的一侧通过导流管连接有过滤净化结构19,过滤净化结构19包括过滤水箱23、杀菌滤板24、有机物去除滤板25和颗粒去除滤板26,过滤水箱23的内部分别从一端到另一端依次插接有杀菌滤板24、有机物去除滤板25和颗粒去除滤板26,杀菌滤板24的材质为高纯纳米银,有机物去除滤板25的材质为蜂窝活性炭,颗粒去除滤板26的材质为PP纤维便于对废水进行不同效果的过滤,过滤净化结构19的一侧通过导流管连接有第二水泵20,第二水泵20的一端通过导流管连接有回收存储箱21,回收存储箱21的一端开设有废水导出口,废水导出口的直径为二十厘米,便于将内部存储的过滤后废水排出便于对重沸器4产生的废水进行过滤回收。The waste water
工作原理:在混合蒸汽通过重沸器4到蒸馏塔主体2内部后,经过热蒸汽与冷却液的相互碰撞,产生了含有较多量易挥发物质的出料蒸汽易挥发体和含有较多量的高沸点组分的气体不易挥发气体,易挥发气体通过蒸馏塔主体2的顶端传递至多方式快速冷凝结构14处,该气体通过蒸汽循环导管11被微型增压泵10进行抽取带动,使得易挥发气体跟随微型增压泵10的传输方向运动,通过浸泡式水冷箱12的内部,由于浸泡式水冷箱12的内部存储有冷却液体,通过热传递的特性将易挥发气体中一部分的 热量进行带走,形成初步液化,初步液化气体通过微型增压泵10传递至分散快速液化管9中,经过分流进入较小的空间内,便于压缩降温,经过分散快速液化管9的材质传导与片状导热板5的吸附,将剩余热量导出,经过片状导热板5两侧风冷扇叶7的同时风冷,降低片状导热板5的自身热量,可以保证将分散快速液化管9内的热量快速传导吸出,从而使得初步液化气体可以去热形成出料液体,通过集中液化导出管13的汇总进行流出,使得装置可以对含有较多量易挥发物质的多次蒸馏出料进行快速冷却,从而加快循环出料的效率;将重沸器4在工作时产生的大量污染废水通过导管连接至第一水泵18处,导管中的废水通过第一水泵18的动力引导进入过滤净化结构19的内部,该废水在过滤净化结构19中经过颗粒去除滤板26、有机物去除滤板25、杀菌滤板24的多层分工过滤,颗粒去除滤板26利用自身材质的特性对废水中掺杂的颗粒进行隔离,有机物去除滤板25利用自身材质的特性对废水中的有机物进行吸附,最后通过杀菌滤板24材质的杀菌特性对废水进行再次的杀菌、消毒,降低废水的危害,最后通过第二水泵20的牵引到回收存储箱21进行存储,使得装置在使用过程中减少对环境的影响。Working principle: After the mixed steam passes through the reboiler 4 to the inside of the distillation tower
对于本领域技术人员而言,显然本实用新型不限于上述示范性实施例的细节,而且在不背离本实用新型的精神或基本特征的情况下,能够以其他的具体形式实现本实用新型。因此,无论从哪一点来看,均应将实施例看作是示范性的,而且是非限制性的,本实用新型的范围由所附权利要求而不是上述说明限定,因此旨在将落在权利要求的等同要件的含义和范围内的所有变化囊括在本实用新型内。不应将权利要求中的任何附图标记视为限制所涉及的权利要求。For those skilled in the art, it is obvious that the present invention is not limited to the details of the above exemplary embodiments, and the present invention can be implemented in other specific forms without departing from the spirit or basic characteristics of the present invention. Therefore, no matter from which point of view, the embodiments should be regarded as exemplary and non-restrictive. The scope of the present invention is defined by the appended claims rather than the above description, so it is intended to fall on the rights. All the changes in the meaning and scope of the required equivalent elements are included in the present invention. Any reference signs in the claims should not be regarded as limiting the claims involved.
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| CN211635256U (en) * | 2019-12-12 | 2020-10-09 | 倪治荣 | Environment-friendly circulation ejection of compact distillation column |
| CN112973159A (en) * | 2019-12-12 | 2021-06-18 | 江苏民生特种设备集团有限公司 | Environment-friendly circulation ejection of compact distillation column |
| CN113856228B (en) * | 2021-09-26 | 2024-02-06 | 冠县新瑞实业有限公司 | Alcohol distillation system |
| CN115581934B (en) * | 2022-10-08 | 2023-06-16 | 山东信谊制药有限公司 | Separation and purification device for drug synthesis |
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| CN116059669A (en) * | 2022-11-14 | 2023-05-05 | 江西佰康药业有限责任公司 | Chinese herbal medicine distillation purification kettle and purification method thereof |
| CN115541648B (en) * | 2022-12-05 | 2023-03-10 | 埃森农机常州有限公司 | Plant protection machine mixes medicine concentration on-line measuring device |
| CN116083202B (en) * | 2023-04-11 | 2023-06-16 | 山东青州云门酒业(集团)有限公司 | Continuous distillation device |
| CN119633426B (en) * | 2024-11-29 | 2025-04-15 | 湖南奔骥环保能源科技有限责任公司 | Semi-continuous crude oil rectifying device combined with energy balls |
| CN119390297A (en) * | 2024-12-14 | 2025-02-07 | 江苏鑫淮环保设备有限公司 | A multi-stage treatment device for wastewater filtration and purification |
| CN119909399B (en) * | 2025-04-03 | 2025-06-13 | 盘锦鑫海源生物科技有限公司 | A stills for vegetable oil acid production |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4249386A (en) * | 1978-06-16 | 1981-02-10 | Smith Otto J | Apparatus for providing radiative heat rejection from a working fluid used in a Rankine cycle type system |
| CN2495646Y (en) * | 2001-08-28 | 2002-06-19 | 王成东 | Multi-functional apparatus for recovering and concentrating alcohol |
| CN201959581U (en) * | 2010-12-29 | 2011-09-07 | 东营万通橡胶助剂有限公司 | Improved device for old type condenser system |
| CN203612971U (en) * | 2013-12-18 | 2014-05-28 | 河南心连心化肥有限公司 | Ammonia distillation device |
| CN203928789U (en) * | 2014-06-10 | 2014-11-05 | 安阳市福士德锅炉有限责任公司 | A kind of boiler combined condenser |
| CN204251451U (en) * | 2013-05-01 | 2015-04-08 | 因温斯特技术公司 | For the manufacture of the device of polymeric amide |
| CN206222959U (en) * | 2016-11-02 | 2017-06-06 | 湖南博雅智能装备股份有限公司 | The condenser system that water wind is combined |
| CN208229420U (en) * | 2018-03-21 | 2018-12-14 | 东营石大胜华新材料有限公司 | A kind of continuous production device of methyl ethyl carbonate |
| CN109556422A (en) * | 2018-12-03 | 2019-04-02 | 江苏中宇光伏科技有限公司 | A kind of solar battery sintering condenser and its condensation method |
| CN110260675A (en) * | 2019-06-25 | 2019-09-20 | 吉林大学 | A kind of air-cooled water cooling parallel system and its consumption control method |
| CN211635256U (en) * | 2019-12-12 | 2020-10-09 | 倪治荣 | Environment-friendly circulation ejection of compact distillation column |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5262012A (en) * | 1990-09-19 | 1993-11-16 | Chemical Research & Licensing Company | Catalytic distillation system |
| CN202014951U (en) * | 2011-04-12 | 2011-10-26 | 马媛媛 | Stirrer with filter screen |
| CN203890342U (en) * | 2014-03-12 | 2014-10-22 | 厦门圣尼诺生物科技有限公司 | Porous paddle distillation kettle |
| CN204656056U (en) * | 2015-06-03 | 2015-09-23 | 浙江诚泰化工机械有限公司 | A kind of tasteless Chinese medicine extracting tank |
| CN204841677U (en) * | 2015-07-17 | 2015-12-09 | 福建省伍重机械制造有限公司 | High efficiency reation kettle with cleaning function |
| CN205517488U (en) * | 2016-04-15 | 2016-08-31 | 天津市日航石油科技有限公司 | Novel lubricating oil agitator tank |
| CN206424604U (en) * | 2017-01-21 | 2017-08-22 | 广州市同源化工科技有限公司 | A kind of Chemical Manufacture distillation still |
| CN211635259U (en) * | 2019-12-11 | 2020-10-09 | 倪治荣 | High efficiency distillation column cauldron |
-
2019
- 2019-12-12 CN CN201922216233.6U patent/CN211635256U/en not_active Expired - Fee Related
-
2020
- 2020-11-12 WO PCT/CN2020/128224 patent/WO2021115010A1/en not_active Ceased
- 2020-11-12 WO PCT/CN2020/128223 patent/WO2021115009A1/en not_active Ceased
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4249386A (en) * | 1978-06-16 | 1981-02-10 | Smith Otto J | Apparatus for providing radiative heat rejection from a working fluid used in a Rankine cycle type system |
| CN2495646Y (en) * | 2001-08-28 | 2002-06-19 | 王成东 | Multi-functional apparatus for recovering and concentrating alcohol |
| CN201959581U (en) * | 2010-12-29 | 2011-09-07 | 东营万通橡胶助剂有限公司 | Improved device for old type condenser system |
| CN204251451U (en) * | 2013-05-01 | 2015-04-08 | 因温斯特技术公司 | For the manufacture of the device of polymeric amide |
| CN203612971U (en) * | 2013-12-18 | 2014-05-28 | 河南心连心化肥有限公司 | Ammonia distillation device |
| CN203928789U (en) * | 2014-06-10 | 2014-11-05 | 安阳市福士德锅炉有限责任公司 | A kind of boiler combined condenser |
| CN206222959U (en) * | 2016-11-02 | 2017-06-06 | 湖南博雅智能装备股份有限公司 | The condenser system that water wind is combined |
| CN208229420U (en) * | 2018-03-21 | 2018-12-14 | 东营石大胜华新材料有限公司 | A kind of continuous production device of methyl ethyl carbonate |
| CN109556422A (en) * | 2018-12-03 | 2019-04-02 | 江苏中宇光伏科技有限公司 | A kind of solar battery sintering condenser and its condensation method |
| CN110260675A (en) * | 2019-06-25 | 2019-09-20 | 吉林大学 | A kind of air-cooled water cooling parallel system and its consumption control method |
| CN211635256U (en) * | 2019-12-12 | 2020-10-09 | 倪治荣 | Environment-friendly circulation ejection of compact distillation column |
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|---|---|
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