CN109059365A - A kind of air-conditioning freon recycling purification system - Google Patents
A kind of air-conditioning freon recycling purification system Download PDFInfo
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- CN109059365A CN109059365A CN201810786159.9A CN201810786159A CN109059365A CN 109059365 A CN109059365 A CN 109059365A CN 201810786159 A CN201810786159 A CN 201810786159A CN 109059365 A CN109059365 A CN 109059365A
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- 238000000746 purification Methods 0.000 title claims abstract description 18
- 238000004378 air conditioning Methods 0.000 title claims abstract description 11
- 238000004064 recycling Methods 0.000 title description 11
- 239000007788 liquid Substances 0.000 claims abstract description 107
- 238000011084 recovery Methods 0.000 claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 101
- 229910052757 nitrogen Inorganic materials 0.000 claims description 49
- 239000002184 metal Substances 0.000 claims description 3
- 238000001125 extrusion Methods 0.000 abstract description 11
- 238000010521 absorption reaction Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 6
- 238000001179 sorption measurement Methods 0.000 abstract description 5
- 238000000605 extraction Methods 0.000 abstract description 3
- 230000009471 action Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000009833 condensation Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 5
- 230000006378 damage Effects 0.000 description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
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- Separating Particles In Gases By Inertia (AREA)
- Gas Separation By Absorption (AREA)
Abstract
本发明属于回收氟利昂技术领域,具体的说是一种空调氟利昂回收提纯系统,包括保温箱、加热盒、一号管、二号管和空调;还包括螺旋管、三号管和恒压单元;所述保温箱的内部设有恒压单元;所述三号管包括内管和外管,内管、外管间有一号吸油海绵、二号吸油海绵和吸油层。通过在内管处设置螺旋板,液态氟利昂按照螺旋板的轨迹路线流动,增大了液态氟利昂与吸油层的接触面积,使得吸油层更充分的对液态氟利昂中的油进行吸附,从而提高了对液态氟利昂的吸油吸附效果;同时在外管内壁上设置挤压块,挤压块对一号吸油海绵进行挤压,使得油更便于抽离,从而提高了油被抽离的效率。
The present invention belongs to the technical field of recovering freon, and is specifically an air-conditioning freon recovery and purification system, including an incubator, a heating box, No. 1 pipe, No. 2 pipe and an air conditioner; and a spiral pipe, No. 3 pipe and a constant pressure unit; The inside of the incubator is provided with a constant pressure unit; the No. 3 tube includes an inner tube and an outer tube, and there is a No. 1 oil-absorbing sponge, No. 2 oil-absorbing sponge and an oil-absorbing layer between the inner tube and the outer tube. By setting the spiral plate at the inner tube, the liquid freon flows according to the trajectory of the spiral plate, which increases the contact area between the liquid freon and the oil-absorbing layer, and makes the oil-absorbing layer more fully adsorb the oil in the liquid freon, thus improving the performance of the liquid freon. The oil absorption and adsorption effect of liquid freon; at the same time, an extrusion block is set on the inner wall of the outer tube, and the extrusion block squeezes the No. 1 oil-absorbing sponge, making it easier to extract the oil, thereby improving the efficiency of oil extraction.
Description
技术领域technical field
本发明属于回收氟利昂技术领域,具体的说是一种空调氟利昂回收提纯系统。The invention belongs to the technical field of Freon recovery, in particular to an air conditioner Freon recovery and purification system.
背景技术Background technique
氟利昂广泛用于家用电器、泡沫塑料、日用化学品、汽车、消防器材等领域,特别是作为制冷剂在空调、空调里大量使用。目前,全国在用空调约计上亿台,电空调也有几千万台。据有关部门统计,每年仅空调、空调的维修保养数量在上千万台,同时报废的也有近千万台左右。这些报废的空调、空调类产品每年排放的氟利昂上万吨,其危害不可估量。Freon is widely used in household appliances, foam plastics, daily chemicals, automobiles, fire-fighting equipment and other fields, especially as a refrigerant in air conditioners and air conditioners. At present, there are hundreds of millions of air conditioners in use nationwide, and tens of millions of electric air conditioners. According to the statistics of relevant departments, only tens of millions of air conditioners and air conditioners are repaired and maintained every year, and nearly ten million units are scrapped at the same time. These discarded air-conditioners and air-conditioning products emit tens of thousands of tons of Freon every year, and the harm is immeasurable.
解决氟利昂排放问题主要有两种方式:一是大力发展无氟替代产品;二是加强氟利昂的回收再利用。无氟替代技术,目前刚应用于新研发的空调,而对大量的、已在用的老款空调、空调等,加强氟利昂的回收再利用就显得非常重要。There are two main ways to solve the problem of Freon emissions: one is to vigorously develop fluorine-free alternative products; the other is to strengthen the recycling and reuse of Freon. The fluorine-free alternative technology has just been applied to newly developed air conditioners, but it is very important to strengthen the recovery and reuse of freon for a large number of old air conditioners and air conditioners that are already in use.
国内外目前的回收方法基本分为压缩回收法、吸附再分离法、冷却凝缩回收等,普遍因为技术成熟度不高、工艺流程复杂、回收成本高等因素的制约,空调、空调的安装维修企业及汽车维修站使用回收设备的极少,再加上受短期经济利益的趋动、维修企业环保意识淡薄等因素的影响,氟利昂制冷剂任意排放的现象非常严重。众所周知,氟利昂是臭氧层破坏的元凶,一千克氟利昂可以捕捉消灭约七万千克臭氧,臭氧层被大量损耗后,吸收紫外线辐射的能力大大减弱,导致到达地球表面的紫外线明显增加,给人类健康和生态环境带来多方面的危害。因此,加强氟利昂的回收利用亦刻不容缓。The current recovery methods at home and abroad are basically divided into compression recovery method, adsorption re-separation method, cooling condensation recovery, etc. Generally, due to the constraints of low technology maturity, complex process flow, and high recovery costs, air conditioners, air conditioner installation and maintenance companies Few recovery equipments are used in auto repair stations, and due to the influence of short-term economic interests and weak environmental protection awareness of maintenance companies, the phenomenon of arbitrary discharge of Freon refrigerants is very serious. As we all know, freon is the culprit of the destruction of the ozone layer. One kilogram of freon can capture and eliminate about 70,000 kilograms of ozone. After the ozone layer is depleted, the ability to absorb ultraviolet radiation is greatly weakened, resulting in a significant increase in ultraviolet rays reaching the earth's surface, which is harmful to human health and the ecological environment. cause multiple hazards. Therefore, it is urgent to strengthen the recycling of Freon.
现有技术中也出现了一些一种空调氟利昂回收提纯系统的技术方案,如申请号为201410810882的一项中国专利公开了一种回收空调中氟利昂的设备及方法,包括冷凝分离器,冷凝分离器的侧面开设有气态氟利昂进口和液氮进口;冷凝分离器的顶部开设有氮气出口,底部开设有用于回收液态氟利昂的液态氟利昂出口;冷凝分离器内设置有换热盘管,换热盘管的入口通过液氮进口与外界液氮源相连通,出口通过一路保冷管道与空调的换热管的一端相连,换热管的另一端与气态氟利昂进口相连通;氮气由连接在氮气出口的另一路保冷管道外排。In the prior art, there are also some technical solutions for the recovery and purification system of Freon in air conditioners. For example, a Chinese patent with application number 201410810882 discloses a device and method for recovering Freon in air conditioners, including a condensation separator and a condensation separator There are gaseous Freon inlets and liquid nitrogen inlets on the side of the condensing separator; a nitrogen outlet is opened on the top of the condensation separator, and a liquid Freon outlet for recovering liquid Freon is opened at the bottom; a heat exchange coil is arranged in the condensation separator, and the heat exchange coil The inlet is connected to the external liquid nitrogen source through the liquid nitrogen inlet, the outlet is connected to one end of the heat exchange tube of the air conditioner through a cold insulation pipe, and the other end of the heat exchange tube is connected to the gaseous Freon inlet; the nitrogen is connected to the other end of the nitrogen outlet. The cooling pipe is discharged outside.
该技术方案的一种回收空调中氟利昂的设备及方法,发明运用物理冷却方法,采用无污染的液氮做冷却剂,便捷高效地实施了氟利昂的回收。但是该方案不能对液态氟利昂中的油进行充分的吸附,使得含有油的液态氟利昂与无油的液态氟利昂混合,使得回收利用的液态氟利昂的纯净度不足;同时,在保温箱中不能对氟利昂的挥发做出有效的改进;从而使得该技术方案受到限制。The equipment and method for recovering freon in the air conditioner of the technical proposal, the invention uses a physical cooling method, uses non-polluting liquid nitrogen as the coolant, and implements the recovery of freon conveniently and efficiently. However, this scheme cannot fully absorb the oil in the liquid Freon, so that the oil-containing liquid Freon is mixed with the oil-free liquid Freon, so that the purity of the recovered liquid Freon is insufficient; at the same time, the Freon cannot be recovered in the incubator. Volatility is effectively improved; thus the technical solution is limited.
发明内容Contents of the invention
为了弥补现有技术的不足,本发明提出的一种空调氟利昂回收提纯系统,通过在内管处设置螺旋板,液态氟利昂按照螺旋板的轨迹路线流动,增大了液态氟利昂与吸油层的接触面积,使得吸油层更充分的对液态氟利昂中的油进行吸附,从而提高了对液态氟利昂的吸油吸附效果;同时在外管内壁上设置挤压块,挤压块对一号吸油海绵进行挤压,使得油更便于抽离,从而提高了油被抽离的效率。In order to make up for the deficiencies of the existing technology, the present invention proposes a Freon recovery and purification system for air conditioners. By setting the spiral plate at the inner pipe, the liquid Freon flows according to the trajectory of the spiral plate, which increases the contact area between the liquid Freon and the oil-absorbing layer. , so that the oil-absorbing layer can more fully absorb the oil in the liquid freon, thereby improving the oil-absorbing effect on the liquid freon; at the same time, an extrusion block is set on the inner wall of the outer tube, and the extrusion block squeezes the No. 1 oil-absorbing sponge, so that The oil is more easily drawn off, thereby increasing the efficiency with which the oil is drawn off.
本发明解决其技术问题所采用的技术方案是:本发明所述的一种空调氟利昂回收提纯系统,包括保温箱、加热盒、一号管、二号管和空调;还包括螺旋管、三号管和恒压单元;所述保温箱的内部设有恒压单元,保温箱的外壁固连安装有螺旋管;所述螺旋管一端与一号管连通,螺旋管另一端作为液氮入口;所述一号管中部连接有加热盒;所述二号管一端与空调连通,二号管另一端与一号管连通;所述保温箱的左侧设有一号孔,保温箱的右侧设有二号孔,保温箱的顶部设有三号孔;所述空调通过三号管与一号孔连通,一号孔位于恒压单元的下方;其中,The technical scheme adopted by the present invention to solve the technical problem is: a kind of air-conditioning Freon recovery and purification system according to the present invention, comprising an incubator, a heating box, No. 1 pipe, No. 2 pipe and air conditioner; tube and constant pressure unit; the interior of the incubator is provided with a constant pressure unit, and the outer wall of the incubator is fixedly installed with a spiral tube; one end of the spiral tube is connected to the No. 1 tube, and the other end of the spiral tube is used as the liquid nitrogen inlet; The middle part of the No. 1 pipe is connected with a heating box; one end of the No. 2 pipe is connected with the air conditioner, and the other end of the No. 2 pipe is connected with the No. 1 pipe; a No. 1 hole is provided on the left side of the incubator, and a No. 2 hole, the top of the incubator is provided with No. 3 hole; the air conditioner communicates with No. 1 hole through No. 3 pipe, and No. 1 hole is located below the constant pressure unit; wherein,
所述恒压单元包括一号板、滑动伸缩杆和二号板;所述一号板通过滑动伸缩杆与二号板固定连接,滑动伸缩杆外侧套设有弹簧,一号板位于二号板的下方,一号板与保温箱侧壁固定连接,一号板上开设有四号孔。工作时,将液氮从液氮入口输送到螺旋管中,液氮从螺旋管的端头到达一号管,经过一号管中的加热盒加热,使得液氮汽化,汽化后的液氮通过二号管输送到空调中,汽化后的液氮对空调中的气态氟利昂进行冷凝,气态氟利昂形液态氟利昂和氮气;液态氟利昂和氮气通过三号管从一号孔输送到保温箱中,在恒压单元的作用下,避免氟利昂的挥发,使得液态氟利昂从二号孔处抽离保温箱进行回收利用,氮气通过恒压单元从三号孔处排出保温箱。The constant pressure unit includes the No.1 plate, the sliding telescopic rod and the No.2 plate; the No.1 plate is fixedly connected with the No. Below, the No. 1 plate is fixedly connected with the side wall of the incubator, and No. 4 holes are opened on the No. 1 plate. When working, the liquid nitrogen is transported from the liquid nitrogen inlet to the spiral tube, and the liquid nitrogen reaches the No. 1 tube from the end of the spiral tube, and is heated by the heating box in the No. 1 tube to vaporize the liquid nitrogen. The No. 2 pipe is transported to the air conditioner, and the vaporized liquid nitrogen condenses the gaseous Freon in the air conditioner, and the gaseous Freon is in the form of liquid Freon and nitrogen; the liquid Freon and nitrogen are transported from the No. 1 hole to the incubator through the No. 3 pipe. Under the action of the pressure unit, the volatilization of Freon is avoided, so that the liquid Freon is drawn out of the incubator from the second hole for recycling, and the nitrogen gas is discharged from the incubator from the third hole through the constant pressure unit.
优选的,所述三号管包括内管和外管,内管与外管均为金属管,内管与外管之间设有一号吸油海绵;所述一号吸油海绵与内管外壁接触,一号吸油海绵在内管与外管间滑动;所述外管开设有五号孔,内管开设有一组六号孔;所述六号孔中设有二号吸油海绵;所述二号吸油海绵一端与一号吸油海绵固连,二号吸油海绵另一端固连设有吸油层。工作时,液态氟利昂自左向右通过三号管时,一号吸油海绵、二号吸油海绵和吸油层对液态氟利昂中的油进行吸附,使得对液态氟利昂进行吸附提纯,从而提高了液态氟利昂的纯净度,进而提高了液态氟利昂的回收利用率。Preferably, the No. 3 tube includes an inner tube and an outer tube, both of which are metal tubes, and a No. 1 oil-absorbing sponge is arranged between the inner tube and the outer tube; the No. 1 oil-absorbing sponge is in contact with the outer wall of the inner tube, The No. 1 oil-absorbing sponge slides between the inner tube and the outer tube; the outer tube has a No. 5 hole, and the inner tube has a set of No. 6 holes; the No. 2 oil-absorbing sponge is arranged in the No. 6 hole; the No. 2 oil-absorbing sponge One end of the sponge is fixedly connected with No. 1 oil-absorbing sponge, and the other end of No. 2 oil-absorbing sponge is fixedly connected with an oil-absorbing layer. When working, when the liquid Freon passes through the No. 3 pipe from left to right, the No. 1 oil-absorbing sponge, the No. 2 oil-absorbing sponge and the oil-absorbing layer absorb the oil in the liquid Freon, so that the liquid Freon can be adsorbed and purified, thereby improving the efficiency of the liquid Freon. Purity, thereby improving the recycling rate of liquid freon.
优选的,所述内管处设有螺旋板,所述螺旋板通过支架固定安装在内管的内壁上。工作时,液态氟利昂自左向右通过三号管,在液态氟利昂流过内管时,由于内管处设置有螺旋板,使得液态氟利昂按照螺旋板的轨迹路线流动,增大了液态氟利昂与吸油层的接触面积,使得吸油层更充分的对液态氟利昂中的油进行吸附,从而提高了对液态氟利昂的吸油吸附效果。Preferably, the inner tube is provided with a spiral plate, and the spiral plate is fixedly installed on the inner wall of the inner tube through a bracket. When working, the liquid Freon passes through the No. 3 tube from left to right. When the liquid Freon flows through the inner tube, because the inner tube is equipped with a spiral plate, the liquid Freon flows according to the trajectory of the spiral plate, which increases the relationship between the liquid Freon and the oil absorption. The contact area of the layer makes the oil-absorbing layer more fully adsorb the oil in the liquid freon, thereby improving the oil absorption and adsorption effect on the liquid freon.
优选的,所述外管处设有挤压块;所述挤压块一端固定在外管的内壁上,挤压块另一端与一号吸油海绵接触。工作时,液态氟利昂自左向右流过三号管时,一号海绵对液态氟利昂中的油进行吸附后,通过设置在外管内壁的挤压块,通过挤压块对一号吸油海绵进行挤压,使得油更便于从五号孔处抽离出三号管,从而提高了油被抽离的效率。Preferably, an extruding block is provided at the outer tube; one end of the extruding block is fixed on the inner wall of the outer tube, and the other end of the extruding block is in contact with No. 1 oil-absorbing sponge. When working, when the liquid Freon flows through the No. 3 pipe from left to right, the No. 1 sponge absorbs the oil in the liquid Freon, and then squeezes the No. 1 oil-absorbing sponge through the extrusion block arranged on the inner wall of the outer pipe. The pressure makes it easier for the oil to be extracted from the fifth hole to the third pipe, thereby improving the efficiency of oil extraction.
优选的,所述二号吸油海绵的外侧设有套筒。工作时,液态氟利昂自左向右通过三号管时,二号吸油海绵长时间的对液态氟利昂中的油进行吸附,使得二号吸油海绵容易损坏,通过在二号吸油海绵的两侧设置套筒,套筒对二号吸油海绵进行保护,从而减小了对二号吸油海绵的损坏。Preferably, a sleeve is provided on the outside of the No. 2 oil-absorbing sponge. When working, when the liquid Freon passes through the No. 3 pipe from left to right, the No. 2 oil-absorbing sponge absorbs the oil in the liquid Freon for a long time, which makes the No. 2 oil-absorbing sponge easy to be damaged. The sleeve protects the No. 2 oil-absorbing sponge, thereby reducing the damage to the No. 2 oil-absorbing sponge.
优选的,所述二号板底部设有挡板;所述挡板一端固连在二号板的底部,挡板另一端位于一号板的上方,挡板的长度向两侧逐渐增大,挡板在二号板底部围成圆弧形。工作时,液态氟利昂和氮气输送到保温箱后,由于保温箱中的压力不恒定,容易造成氟利昂挥发,使得液态氟利昂不能从二号孔处进行回收利用,通过在二号板的底部设置挡板,挡板长度向两侧逐渐增大,开始挡板将四号板堵住,在液态氟利昂和氮气的持续输送,使得一号板下方的保温箱压力增大,在压力的作用下,推动二号板向上运动,来维持保温箱内的压力一定,避免了氟利昂的挥发,从而提高了液态氟利昂的回收利用率。Preferably, a baffle is provided at the bottom of the No. 2 board; one end of the baffle is fixedly connected to the bottom of the No. 2 board, and the other end of the baffle is located above the No. 1 board, and the length of the baffle gradually increases toward both sides. The baffle forms an arc shape at the bottom of the No. 2 plate. When working, after the liquid Freon and nitrogen are transported to the incubator, due to the unstable pressure in the incubator, it is easy to cause Freon to volatilize, so that the liquid Freon cannot be recycled from the No. 2 hole. By setting the baffle at the bottom of the No. 2 plate , the length of the baffle gradually increases to both sides, and the baffle blocks the No. The number plate moves upward to maintain a constant pressure in the incubator, avoiding the volatilization of Freon, thereby improving the recycling rate of liquid Freon.
优选的,所述一号板底部设有平衡块,所述平衡块位于四号孔的下方,平衡块通过连接杆与挡板固连,平衡块围成与挡板相同的圆弧形;所述平衡块通过弹簧固连在一号板的底部,平衡块的上下两面设有圆弧凹槽,平衡块的两侧设有七号孔;所述七号孔与圆弧凹槽连通。工作时,在液态氟利昂和氮气持续输送到保温箱中,二号板在气压的作用下向上运动,通过设置平衡块,平衡块将四号孔开口堵住,氮气从平衡块两侧的七号孔逸到四号孔处,用于平衡氮气的流出量。Preferably, a balance weight is provided at the bottom of the No. 1 plate, and the balance weight is located below the No. 4 hole. The balance weight is fixedly connected to the baffle through a connecting rod, and the balance weight is surrounded by the same arc shape as the baffle; The balance weight is fixedly connected to the bottom of the No. 1 plate through a spring, the upper and lower sides of the balance weight are provided with arc grooves, and both sides of the balance weight are provided with No. 7 holes; the No. 7 holes communicate with the arc grooves. When working, when the liquid freon and nitrogen are continuously delivered to the incubator, the No. 2 plate moves upward under the action of air pressure. By setting the balance weight, the balance block will block the opening of the No. 4 hole, and the nitrogen gas will flow from No. 7 on both sides of the balance weight. The hole escapes to the No. 4 hole, which is used to balance the outflow of nitrogen.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
1.本发明所述的一种空调氟利昂回收提纯系统,液氮沿着螺旋管到达一号管,经过一号管中的加热盒加热,使得液氮汽化,汽化后的液氮通过二号管输送到空调中,汽化后的液氮对空调中的气态氟利昂进行冷凝,气态氟利昂形液态氟利昂和氮气。1. An air-conditioning Freon recovery and purification system according to the present invention, liquid nitrogen reaches the No. 1 tube along the spiral tube, and is heated by the heating box in the No. 1 tube to vaporize the liquid nitrogen, and the vaporized liquid nitrogen passes through the No. 2 tube Transported to the air conditioner, the vaporized liquid nitrogen condenses the gaseous Freon in the air conditioner, and the gaseous Freon forms liquid Freon and nitrogen.
2.本发明所述的一种空调氟利昂回收提纯系统,通过一号吸油海绵、二号吸油海绵和吸油层对液态氟利昂中的油进行吸附,使得对液态氟利昂进行吸附提纯,从而提高了液态氟利昂的纯净度,进而提高了液态氟利昂的回收利用率。2. An air-conditioning Freon recovery and purification system according to the present invention, the oil in the liquid Freon is adsorbed by the No. 1 oil-absorbing sponge, the No. 2 oil-absorbing sponge and the oil-absorbing layer, so that the liquid Freon is adsorbed and purified, thereby improving the liquid Freon. Purity, thereby improving the recycling rate of liquid freon.
3.本发明所述的一种空调氟利昂回收提纯系统,通过在内管处设置螺旋板,液态氟利昂按照螺旋板的轨迹路线流动,增大了液态氟利昂与吸油层的接触面积,使得吸油层更充分的对液态氟利昂中的油进行吸附,从而提高了对液态氟利昂的吸油吸附效果;同时在外管内壁上设置挤压块,挤压块对一号吸油海绵进行挤压,使得油更便于抽离,从而提高了油被抽离的效率。3. In the air-conditioning Freon recovery and purification system of the present invention, the spiral plate is arranged at the inner pipe, and the liquid Freon flows according to the trajectory of the spiral plate, which increases the contact area between the liquid Freon and the oil-absorbing layer, making the oil-absorbing layer more Sufficiently absorb the oil in the liquid freon, thereby improving the oil absorption and adsorption effect on the liquid freon; at the same time, an extrusion block is set on the inner wall of the outer tube, and the extrusion block squeezes the No. 1 oil-absorbing sponge, making it easier to extract the oil , thereby improving the efficiency of oil extraction.
4.本发明所述的一种空调氟利昂回收提纯系统,通过一号板、二号板、挡板和平衡块间的相互配合,既平衡氮气流出量,又使得氟利昂不易挥发,从而提高了液态氟利昂的回收利用率。4. An air-conditioning Freon recovery and purification system according to the present invention, through the mutual cooperation between the No. 1 plate, the No. 2 plate, the baffle plate and the balance weight, not only balances the outflow of nitrogen, but also makes Freon less volatile, thereby improving the liquid state. Freon recycling rate.
附图说明Description of drawings
下面结合附图对本发明作进一步说明。The present invention will be further described below in conjunction with accompanying drawing.
图1是本发明的主视图;Fig. 1 is the front view of the present invention;
图2是图1中三号管的剖视图;Fig. 2 is the sectional view of pipe No. 3 in Fig. 1;
图3是图1中A处的局部放大图;Fig. 3 is a partial enlarged view of place A in Fig. 1;
图中:保温箱1、一号孔11、二号孔12、三号孔13、加热盒2、一号管3、二号管4、空调5、螺旋管6、三号管7、内管71、六号孔711、外管72、五号孔721、一号吸油海绵73、二号吸油海绵74、吸油层75、螺旋板76、挤压块77、套筒78、恒压单元8、一号板81、四号孔811、滑动伸缩杆82、二号板83、挡板84、平衡块85、七号孔851、圆弧凹槽852、连接杆86。In the figure: incubator 1, No. 1 hole 11, No. 2 hole 12, No. 3 hole 13, heating box 2, No. 1 tube 3, No. 2 tube 4, air conditioner 5, spiral tube 6, No. 3 tube 7, inner tube 71. No. 6 hole 711, outer tube 72, No. 5 hole 721, No. 1 oil-absorbing sponge 73, No. 2 oil-absorbing sponge 74, oil-absorbing layer 75, spiral plate 76, extrusion block 77, sleeve 78, constant pressure unit 8, No. 1 plate 81, No. 4 hole 811, sliding telescopic rod 82, No. 2 plate 83, baffle plate 84, balance weight 85, No. 7 hole 851, arc groove 852, connecting rod 86.
具体实施方式Detailed ways
为了使本发明实现的技术手段、创作特征、达成目的与功效易于明白了解,下面结合具体实施方式,进一步阐述本发明。In order to make the technical means, creative features, goals and effects achieved by the present invention easy to understand, the present invention will be further described below in conjunction with specific embodiments.
如图1至图3所示,本发明所述的一种空调氟利昂回收提纯系统,包括保温箱1、加热盒2、一号管3、二号管4和空调5;还包括螺旋管6、三号管7和恒压单元8;所述保温箱1的内部设有恒压单元8,保温箱1的外壁固连安装有螺旋管6;所述螺旋管6一端与一号管3连通,螺旋管6另一端作为液氮入口;所述一号管3中部连接有加热盒2;所述二号管4一端与空调5连通,二号管4另一端与一号管3连通;所述保温箱1的左侧设有一号孔11,保温箱1的右侧设有二号孔12,保温箱1的顶部设有三号孔13;所述空调5通过三号管7与一号孔11连通,一号孔11位于恒压单元8的下方;其中,As shown in Fig. 1 to Fig. 3, a kind of air-conditioning freon recovery and purification system of the present invention includes incubator 1, heating box 2, No. 1 pipe 3, No. 2 pipe 4 and air conditioner 5; also includes spiral pipe 6, No. 3 pipe 7 and constant pressure unit 8; the interior of the incubator 1 is provided with a constant pressure unit 8, and the outer wall of the incubator 1 is fixedly connected with a spiral pipe 6; one end of the spiral pipe 6 communicates with the No. 1 pipe 3, The other end of the spiral tube 6 is used as the liquid nitrogen inlet; the middle part of the No. 1 tube 3 is connected with a heating box 2; one end of the No. 2 tube 4 is connected with the air conditioner 5, and the other end of the No. 2 tube 4 is connected with the No. 1 tube 3; The left side of the incubator 1 is provided with a No. 1 hole 11, the right side of the incubator 1 is provided with a No. 2 hole 12, and the top of the incubator 1 is provided with a No. 3 hole 13; the air conditioner 5 passes through the No. 3 pipe 7 and the No. 1 hole 11 connected, the No. 1 hole 11 is located below the constant pressure unit 8; wherein,
所述恒压单元8包括一号板81、滑动伸缩杆82和二号板83;所述一号板81通过滑动伸缩杆82与二号板83固定连接,滑动伸缩杆82外侧套设有弹簧,一号板81位于二号板83的下方,一号板81与保温箱1侧壁固定连接,一号板81上开设有四号孔811。工作时,将液氮从液氮入口输送到螺旋管6中,液氮从螺旋管6的端头到达一号管3,经过一号管3中的加热盒2加热,使得液氮汽化,汽化后的液氮通过二号管4输送到空调5中,汽化后的液氮对空调5中的气态氟利昂进行冷凝,气态氟利昂形液态氟利昂和氮气;液态氟利昂和氮气通过三号管7从一号孔11输送到保温箱1中,在恒压单元8的作用下,避免氟利昂的挥发,使得液态氟利昂从二号孔12处抽离保温箱1进行回收利用,氮气通过恒压单元8从三号孔13处排出保温箱1。The constant pressure unit 8 includes a No.1 plate 81, a sliding telescopic rod 82 and a No. , the No. 1 plate 81 is located below the No. 2 plate 83 , the No. 1 plate 81 is fixedly connected with the side wall of the incubator 1 , and the No. 4 hole 811 is opened on the No. 1 plate 81 . When working, the liquid nitrogen is transported from the liquid nitrogen inlet to the spiral tube 6, and the liquid nitrogen reaches the No. 1 tube 3 from the end of the spiral tube 6, and is heated by the heating box 2 in the No. 1 tube 3, so that the liquid nitrogen is vaporized and vaporized The final liquid nitrogen is delivered to the air conditioner 5 through the second pipe 4, and the vaporized liquid nitrogen condenses the gaseous freon in the air conditioner 5, and the gaseous freon is in the form of liquid freon and nitrogen; the liquid freon and nitrogen pass through the third pipe 7 from the first The hole 11 is transported to the incubator 1, and under the action of the constant pressure unit 8, the volatilization of Freon is avoided, so that the liquid Freon is extracted from the incubator 1 from the No. The incubator 1 is discharged from the hole 13.
作为本发明的一种实施方式,所述三号管7包括内管71和外管72,内管71与外管72均为金属管,内管71与外管72之间设有一号吸油海绵73;所述一号吸油海绵73与内管71外壁接触,一号吸油海绵73在内管71与外管72间滑动;所述外管72开设有五号孔721,内管71开设有一组六号孔711;所述六号孔711中设有二号吸油海绵74;所述二号吸油海绵74一端与一号吸油海绵73固连,二号吸油海绵74另一端固连设有吸油层75。工作时,液态氟利昂自左向右通过三号管7时,一号吸油海绵73、二号吸油海绵74和吸油层75对液态氟利昂中的油进行吸附,使得对液态氟利昂进行吸附提纯,从而提高了液态氟利昂的纯净度,进而提高了液态氟利昂的回收利用率。As an embodiment of the present invention, the No. 3 pipe 7 includes an inner pipe 71 and an outer pipe 72. Both the inner pipe 71 and the outer pipe 72 are metal pipes. A No. 1 oil-absorbing sponge is arranged between the inner pipe 71 and the outer pipe 72. 73; the No. 1 oil-absorbing sponge 73 is in contact with the outer wall of the inner tube 71, and the No. 1 oil-absorbing sponge 73 slides between the inner tube 71 and the outer tube 72; the outer tube 72 is provided with a fifth hole 721, and the inner tube 71 is provided with a set of No. 6 hole 711; No. 2 oil-absorbing sponge 74 is arranged in No. 6 hole 711; one end of No. 2 oil-absorbing sponge 74 is fixedly connected with No. 1 oil-absorbing sponge 73, and the other end of No. 2 oil-absorbing sponge 74 is fixedly connected with an oil-absorbing layer 75. When working, when the liquid Freon passes through the No. 3 pipe 7 from left to right, the No. 1 oil-absorbing sponge 73, the No. 2 oil-absorbing sponge 74 and the oil-absorbing layer 75 absorb the oil in the liquid Freon, so that the liquid Freon is adsorbed and purified, thereby improving The purity of liquid freon is improved, and the recycling rate of liquid freon is improved.
作为本发明的一种实施方式,所述内管71处设有螺旋板76,所述螺旋板76通过支架固定安装在内管71的内壁上。工作时,液态氟利昂自左向右通过三号管7,在液态氟利昂流过内管71时,由于内管71处设置有螺旋板76,使得液态氟利昂按照螺旋板76的轨迹路线流动,增大了液态氟利昂与吸油层75的接触面积,使得吸油层75更充分的对液态氟利昂中的油进行吸附,从而提高了对液态氟利昂的吸油吸附效果。As an embodiment of the present invention, the inner tube 71 is provided with a spiral plate 76, and the spiral plate 76 is fixedly installed on the inner wall of the inner tube 71 through a bracket. When working, the liquid Freon passes through the No. 3 tube 7 from left to right. When the liquid Freon flows through the inner pipe 71, since the inner pipe 71 is provided with a spiral plate 76, the liquid Freon flows according to the trajectory of the spiral plate 76, increasing The contact area between the liquid freon and the oil-absorbing layer 75 is increased, so that the oil-absorbing layer 75 can more fully absorb the oil in the liquid freon, thereby improving the oil absorption and adsorption effect on the liquid freon.
作为本发明的一种实施方式,所述外管72处设有挤压块77;所述挤压块77一端固定在外管72的内壁上,挤压块77另一端与一号吸油海绵73接触。工作时,液态氟利昂自左向右流过三号管7时,一号海绵对液态氟利昂中的油进行吸附后,通过设置在外管72内壁的挤压块77,通过挤压块77对一号吸油海绵73进行挤压,使得油更便于从五号孔721处抽离出三号管7,从而提高了油被抽离的效率。As an embodiment of the present invention, the outer tube 72 is provided with an extruding block 77; one end of the extruding block 77 is fixed on the inner wall of the outer tube 72, and the other end of the extruding block 77 is in contact with No. 1 oil-absorbing sponge 73 . When working, when the liquid freon flows through the No. 3 tube 7 from left to right, after the No. 1 sponge absorbs the oil in the liquid freon, it passes through the extrusion block 77 arranged on the inner wall of the outer tube 72, and the No. 1 sponge passes through the extrusion block 77. The oil-absorbing sponge 73 squeezes, making it easier for the oil to be drawn out of the No. 3 pipe 7 from the No. 5 hole 721, thereby improving the efficiency of the oil being drawn out.
作为本发明的一种实施方式,所述二号吸油海绵74的外侧设有套筒78。工作时,液态氟利昂自左向右通过三号管7时,二号吸油海绵74长时间的对液态氟利昂中的油进行吸附,使得二号吸油海绵74容易损坏,通过在二号吸油海绵74的两侧设置套筒78,套筒78对二号吸油海绵74进行保护,从而减小了对二号吸油海绵74的损坏。As an embodiment of the present invention, a sleeve 78 is provided on the outside of the No. 2 oil-absorbing sponge 74 . When working, when liquid freon passes through No. 3 pipe 7 from left to right, No. 2 oil-absorbing sponge 74 absorbs the oil in liquid freon for a long time, making No. 2 oil-absorbing sponge 74 easily damaged. Sleeves 78 are arranged on both sides, and the sleeves 78 protect the No. 2 oil-absorbing sponge 74, thereby reducing damage to the No. 2 oil-absorbing sponge 74.
作为本发明的一种实施方式,所述二号板83底部设有挡板84;所述挡板84一端固连在二号板83的底部,挡板84另一端位于一号板81的上方,挡板84的长度向两侧逐渐增大,挡板84在二号板83底部围成圆弧形。工作时,液态氟利昂和氮气输送到保温箱1后,由于保温箱1中的压力不恒定,容易造成氟利昂挥发,使得液态氟利昂不能从二号孔12处进行回收利用,通过在二号板83的底部设置挡板84,挡板84长度向两侧逐渐增大,开始挡板84将四号板堵住,在液态氟利昂和氮气的持续输送,使得一号板81下方的保温箱1压力增大,在压力的作用下,推动二号板83向上运动,来维持保温箱1内的压力一定,避免了氟利昂的挥发,从而提高了液态氟利昂的回收利用率。As an embodiment of the present invention, the bottom of the No. 2 board 83 is provided with a baffle 84; , the length of the baffle plate 84 gradually increases toward both sides, and the baffle plate 84 forms an arc shape at the bottom of the second plate 83 . During work, after the liquid Freon and nitrogen are transported to the incubator 1, since the pressure in the incubator 1 is not constant, it is easy to cause the volatilization of Freon, so that the liquid Freon cannot be recycled from the second hole 12. A baffle 84 is set at the bottom, and the length of the baffle 84 gradually increases toward both sides. At the beginning, the baffle 84 blocks the No. 4 plate. The continuous delivery of liquid freon and nitrogen makes the pressure of the incubator 1 under the No. 1 plate 81 increase. , under the action of pressure, the No. 2 plate 83 is pushed upward to maintain a constant pressure in the incubator 1, avoiding the volatilization of Freon, thereby improving the recycling rate of liquid Freon.
作为本发明的一种实施方式,所述一号板81底部设有平衡块85,所述平衡块85位于四号孔811的下方,平衡块85通过连接杆86与挡板84固连,平衡块85围成与挡板84相同的圆弧形;所述平衡块85通过弹簧固连在一号板81的底部,平衡块85的上下两面设有圆弧凹槽852,平衡块85的两侧设有七号孔851;所述七号孔851与圆弧凹槽852连通。工作时,在液态氟利昂和氮气持续输送到保温箱1中,二号板83在气压的作用下向上运动,通过设置平衡块85,平衡块85将四号孔811开口堵住,氮气从平衡块85两侧的七号孔851逸到四号孔811处,用于平衡氮气的流出量。As an embodiment of the present invention, the bottom of the No. 1 plate 81 is provided with a balance weight 85, the balance weight 85 is located below the No. The block 85 is surrounded by the same arc shape as the baffle plate 84; the balance block 85 is fixedly connected to the bottom of the No. 1 plate 81 by a spring, and the upper and lower sides of the balance block 85 are provided with arc grooves 852, and the two sides of the balance block 85 There is a No. 7 hole 851 on the side; the No. 7 hole 851 communicates with the arc groove 852 . During work, when the liquid freon and nitrogen are continuously delivered to the incubator 1, the No. 2 plate 83 moves upward under the action of air pressure. By setting the balance weight 85, the opening of the fourth hole 811 is blocked by the balance weight 85, and the nitrogen gas flows from the balance weight. No. 7 hole 851 on both sides of 85 escapes to No. 4 hole 811 to balance the outflow of nitrogen.
工作时,将液氮从液氮入口输送到螺旋管6中,液氮从螺旋管6的端头到达一号管3,经过一号管3中的加热盒2加热,使得液氮汽化,汽化后的液氮通过二号管4输送到空调5中,汽化后的液氮对空调5中的气态氟利昂进行冷凝,气态氟利昂形液态氟利昂和氮气;液态氟利昂和氮气通过三号管7时,一号吸油海绵73和二号吸油海绵74对液态氟利昂中的油进行吸附,液态氟利昂流过内管71时,液态氟利昂按照螺旋板76的轨迹路线流动,增大了液态氟利昂中油与吸油层75的接触面积,从而加大吸油效率;液态氟利昂流过外管72时,外管72内壁设置的挤压块77对二号吸油海绵74进行挤压,从而使得油更便捷的从五号孔721抽离;吸油处理后的液态氟利昂和氮气从一号孔11输送到保温箱1中,在恒压单元8的作用下,避免氟利昂的挥发,使得液态氟利昂从二号孔12处抽离保温箱1进行回收利用,同时通过平衡块85来平衡氮气流量,氮气从三号孔13处排出保温箱1。When working, the liquid nitrogen is transported from the liquid nitrogen inlet to the spiral tube 6, and the liquid nitrogen reaches the No. 1 tube 3 from the end of the spiral tube 6, and is heated by the heating box 2 in the No. 1 tube 3, so that the liquid nitrogen is vaporized and vaporized The final liquid nitrogen is transported to the air conditioner 5 through the second pipe 4, and the vaporized liquid nitrogen condenses the gaseous freon in the air conditioner 5, and the gaseous freon forms liquid freon and nitrogen; when the liquid freon and nitrogen pass through the third pipe 7, a No. 7 oil-absorbing sponge 73 and No. 2 oil-absorbing sponge 74 absorb the oil in the liquid freon. When the liquid freon flows through the inner tube 71, the liquid freon flows according to the trajectory of the spiral plate 76, which increases the distance between the oil in the liquid freon and the oil-absorbing layer 75. The contact area increases the oil absorption efficiency; when liquid freon flows through the outer tube 72, the extrusion block 77 set on the inner wall of the outer tube 72 squeezes the No. 2 oil-absorbing sponge 74, so that the oil can be more conveniently pumped from the No. 5 hole 721 The liquid freon and nitrogen after the oil absorption treatment are transported from the first hole 11 to the incubator 1, and under the action of the constant pressure unit 8, the volatilization of freon is avoided, so that the liquid freon is drawn out of the incubator 1 from the second hole 12 Recycling is carried out, and the nitrogen flow is balanced by the balance weight 85 at the same time, and the nitrogen is discharged from the incubator 1 from the third hole 13 .
上述前、后、左、右、上、下均以说明书附图中的图1为基准,按照人物观察视角为标准,装置面对观察者的一面定义为前,观察者左侧定义为左,依次类推。The above-mentioned front, back, left, right, up, and down are all based on Figure 1 in the accompanying drawings of the specification, and according to the viewing angle of the person as the standard, the side of the device facing the observer is defined as the front, and the left side of the observer is defined as the left. And so on.
以上显示和描述了本发明的基本原理、主要特征和优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。本发明要求保护范围由所附的权利要求书及其等效物界定。The basic principles, main features and advantages of the present invention have been shown and described above. Those skilled in the industry should understand that the present invention is not limited by the above-mentioned embodiments. What are described in the above-mentioned embodiments and the description only illustrate the principle of the present invention. Without departing from the spirit and scope of the present invention, the present invention will also have Variations and improvements are possible, which fall within the scope of the claimed invention. The protection scope of the present invention is defined by the appended claims and their equivalents.
Claims (7)
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| KR20030079474A (en) * | 2002-04-04 | 2003-10-10 | 엠에스모터시스템(주) | Air conditioner recovery recycle recharge evac tank refill system |
| CN104501485A (en) * | 2014-12-23 | 2015-04-08 | 西北工业大学 | Equipment and method for recycling freon in refrigerators |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5090211A (en) * | 1990-03-12 | 1992-02-25 | Reklame, Inc. | Refrigerant recovery and recycling system |
| CN1058090A (en) * | 1990-07-08 | 1992-01-22 | 朱伟民 | Freon recovery device |
| US5072594A (en) * | 1990-10-05 | 1991-12-17 | Squire David C | Method and apparatus for passive refrigerant retrieval and storage |
| KR20030079474A (en) * | 2002-04-04 | 2003-10-10 | 엠에스모터시스템(주) | Air conditioner recovery recycle recharge evac tank refill system |
| CN104501485A (en) * | 2014-12-23 | 2015-04-08 | 西北工业大学 | Equipment and method for recycling freon in refrigerators |
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