CN113819669B - A low-temperature refrigeration device and method based on the gravity oil separation effect of carbon nanotubes - Google Patents

A low-temperature refrigeration device and method based on the gravity oil separation effect of carbon nanotubes Download PDF

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CN113819669B
CN113819669B CN202111081590.1A CN202111081590A CN113819669B CN 113819669 B CN113819669 B CN 113819669B CN 202111081590 A CN202111081590 A CN 202111081590A CN 113819669 B CN113819669 B CN 113819669B
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何一坚
赵恒庆
丁佳敏
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Taizhou Institute of Zhejiang University
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/005Compression machines, plants or systems with non-reversible cycle of the single unit type
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    • C01B32/15Nano-sized carbon materials
    • C01B32/158Carbon nanotubes
    • C01B32/168After-treatment
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/02Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for separating lubricants from the refrigerant

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Abstract

The invention discloses a low-temperature refrigeration device and a low-temperature refrigeration method based on a carbon nano tube gravity oil separation effect, wherein the device is based on single-machine compression single-stage fractional condensation self-cascade refrigeration and comprises a compressor, a condenser, a gas-liquid separator, a capillary tube and a throttle valve; saturated liquid-phase high-temperature refrigerant in the gas-liquid separator enters a condensing evaporator through a throttling device to complete the evaporation process; meanwhile, saturated gas working refrigerant generated in the gas-liquid separator enters the condensing evaporator to finish the condensation process, enters the evaporator after being throttled by a capillary tube, and finally enters a compression cycle after low-temperature refrigerant exiting the evaporator is mixed with high-temperature refrigerant gas which finishes the evaporation process in the condensing evaporator; in the circulation process, a proper amount of carbon nano tubes are added to the refrigerant, so that the content of lubricating oil in the low-boiling-point refrigerant in the gas-liquid separator is greatly reduced, the capillary tube is prevented from being blocked by the lubricating oil, and meanwhile, the heat exchange performance of the refrigerant, the lubricating performance of the lubricating oil and the abrasion of a compressor can be improved.

Description

一种基于碳纳米管重力油分离效应的低温制冷装置及方法A low-temperature refrigeration device and method based on the gravity oil separation effect of carbon nanotubes

技术领域technical field

本发明涉及制冷设备领域,特别是涉及一种基于碳纳米管重力油分离效应的低温制冷装置及方法。The invention relates to the field of refrigeration equipment, in particular to a low-temperature refrigeration device and method based on the gravity oil separation effect of carbon nanotubes.

背景技术Background technique

碳纳米管自1991年被发现以来,由于其独特的结构特点使其具有良好的传热性能、奇异的导电性以及优异的力学性能,从而引起了专家学者的广泛关注,在各个领域都呈现了广阔的应用前景。碳纳米管不仅具有纳米材料的一些共性特征,还具有极高的机械强度,在润滑领域被应用于润滑油添加剂,起到改善和提升减磨抗磨性能的作用。碳纳米管的多孔结构、较大的比表面积和较轻的质量密度也使其在吸附作用上展现出良好的性能。Since the discovery of carbon nanotubes in 1991, due to their unique structural characteristics, they have good heat transfer performance, singular electrical conductivity and excellent mechanical properties, which have attracted widespread attention from experts and scholars, and have shown great promise in various fields. Broad application prospects. Carbon nanotubes not only have some common characteristics of nanomaterials, but also have extremely high mechanical strength. They are used in lubricating oil additives in the field of lubrication to improve and enhance anti-wear properties. The porous structure, large specific surface area and light mass density of carbon nanotubes also make them exhibit good performance in adsorption.

在自复叠制冷系统中,不同蒸发温度的制冷剂在经过冷凝器冷凝作用后,低温制冷剂处于气态,而高沸点制冷剂已冷凝为液态,此时通过设置气液分离器使得这两种状态的制冷剂分离,使液态的高沸点制冷剂节流后继续冷凝低温制冷剂。但目前气相低沸点制冷剂在分离时常常会夹带一些润滑油液滴,严重的,这些液滴进入低温管路中,会造成毛细管堵塞,严重影响系统的运行状况。In the self-cascading refrigeration system, after the refrigerants with different evaporation temperatures are condensed by the condenser, the low-temperature refrigerant is in a gaseous state, while the high-boiling point refrigerant has been condensed into a liquid state. At this time, the gas-liquid separator is set to make the two The refrigerant in the liquid state is separated, so that the liquid high-boiling point refrigerant is throttled and continues to condense the low-temperature refrigerant. However, at present, when the gas-phase low-boiling point refrigerant is separated, some lubricating oil droplets are often entrained. Seriously, these droplets enter the low-temperature pipeline, which will cause capillary blockage and seriously affect the operation of the system.

目前为了实现低温制冷系统的气液分离器中气相低沸点制冷剂与润滑油的高效分离,主要通过对气液分离器进行改进,但此类工艺对于一些与制冷剂互溶的乳化油的分离效果依旧不明显,因此需要一种能够高效分离气相低沸点制冷剂中的油成分的装置及方法。At present, in order to realize the high-efficiency separation of the gas-phase low-boiling point refrigerant and the lubricating oil in the gas-liquid separator of the low-temperature refrigeration system, the gas-liquid separator is mainly improved. It is still not obvious, so there is a need for a device and method capable of efficiently separating oil components in gas-phase low-boiling point refrigerants.

发明内容Contents of the invention

本发明的目的是解决现有技术的不足,提供一种基于碳纳米管重力油分离效应的低温制冷装置及方法。The purpose of the present invention is to solve the deficiencies of the prior art, and provide a low-temperature refrigeration device and method based on the gravity oil separation effect of carbon nanotubes.

为了解决上述问题,本发明采用如下技术方案:In order to solve the above problems, the present invention adopts the following technical solutions:

一种基于碳纳米管重力油分离效应的低温制冷装置,包括压缩机、冷凝器、气液分离器、节流阀、毛细管、冷凝蒸发器、蒸发器以及充注口;其中压缩机出口与冷凝器进口连接,冷凝器出口与气液分离器进口连接;气液分离器的高沸点制冷剂通道通过节流阀与冷凝蒸发器的蒸发侧通道连接;气液分离器的低沸点制冷剂通道与冷凝蒸发器的冷凝侧通道连接;冷凝蒸发器的冷凝侧出口通过毛细管与蒸发器的进口连接;冷凝蒸发器的蒸发侧出口与蒸发器的出口相连,并与压缩机的进口连接;在冷凝器和气液分离器之间设置有充注口,充注口用于充注碳纳米管。A low-temperature refrigeration device based on the gravity oil separation effect of carbon nanotubes, including a compressor, a condenser, a gas-liquid separator, a throttle valve, a capillary tube, a condensing evaporator, an evaporator, and a filling port; wherein the outlet of the compressor is connected to the condensing The inlet of the condenser is connected, and the outlet of the condenser is connected to the inlet of the gas-liquid separator; the high-boiling point refrigerant channel of the gas-liquid separator is connected to the evaporation side channel of the condensing evaporator through a throttle valve; the low-boiling point refrigerant channel of the gas-liquid separator is connected to the The condensing side channel of the condensing evaporator is connected; the condensing side outlet of the condensing evaporator is connected to the inlet of the evaporator through a capillary tube; the evaporating side outlet of the condensing evaporator is connected to the outlet of the evaporator and connected to the inlet of the compressor; in the condenser A filling port is arranged between the gas-liquid separator and the gas-liquid separator, and the filling port is used for filling carbon nanotubes.

进一步的,还包括制冷剂,制冷剂采用自复叠混合制冷剂。Further, it also includes a refrigerant, and the refrigerant is a self-cascading mixed refrigerant.

进一步的,所述自复叠混合制冷剂包括高沸点制冷剂中的一种或者其组合,以及低沸点制冷剂中的一种或者其组合;其中高沸点制冷剂包括R134A、R600A、R1234YF、R1234ZE(Z)、R1234ZE(E)、R142B以及R22,低沸点制冷剂包括R23、R14、R1150、R290、R170、R125以及R32。Further, the self-cascading mixed refrigerant includes one or a combination of high-boiling refrigerants, and one or a combination of low-boiling refrigerants; wherein the high-boiling refrigerants include R134A, R600A, R1234YF, R1234ZE (Z), R1234ZE(E), R142B and R22, low boiling point refrigerants include R23, R14, R1150, R290, R170, R125 and R32.

一种基于碳纳米管重力油分离效应的低温制冷方法,所述制冷方法基于上述的制冷装置,制冷方法包括如下步骤:A low-temperature refrigeration method based on the gravity oil separation effect of carbon nanotubes, the refrigeration method is based on the above-mentioned refrigeration device, and the refrigeration method includes the following steps:

步骤1:压缩机停止工作,将设定量的碳纳米管通过充注口充注到制冷装置中;Step 1: The compressor stops working, and the set amount of carbon nanotubes is filled into the refrigeration device through the filling port;

步骤2:启动压缩机;碳纳米管和制冷剂混合进入冷凝器;Step 2: Start the compressor; carbon nanotubes and refrigerant are mixed into the condenser;

步骤3:经过冷凝器冷凝,获得部分液化的制冷剂;高沸点制冷剂经过放热冷凝形成液态,低沸点制冷剂保持气态;其中由于润滑油的粘度高,而碳纳米管存在相见迁移机制,因此碳纳米管吸附润滑油并发生沉积,与液态的高沸点制冷剂混合;Step 3: After condensing in the condenser, a partially liquefied refrigerant is obtained; the high-boiling point refrigerant is condensed to form a liquid state after exothermic condensation, and the low-boiling point refrigerant remains in a gaseous state; due to the high viscosity of the lubricating oil, the carbon nanotubes have a migration mechanism , so carbon nanotubes absorb lubricating oil and deposit, and mix with liquid high-boiling point refrigerant;

步骤4:部分液化的制冷剂进入气液分离器,进行气相低沸点制冷剂和高沸点制冷剂的分离过程;分离后的高沸点制冷剂经过节流阀进入冷凝蒸发器的蒸发侧通道,低温制冷剂进入冷凝蒸发器的冷凝侧通道;Step 4: The partially liquefied refrigerant enters the gas-liquid separator for the separation process of gas-phase low-boiling point refrigerant and high-boiling point refrigerant; the separated high-boiling point refrigerant enters the evaporation side channel of the condensing evaporator through the throttle valve, and the low-temperature The refrigerant enters the condensing side channel of the condensing evaporator;

步骤5:在冷凝蒸发器中,含润滑油和碳纳米管的高沸点制冷剂与饱和气相低沸点制冷剂进行换热,使得高沸点制冷剂吸热蒸发,形成蒸汽,低沸点制冷剂放热冷凝成为液态;其中含有碳纳米管的高沸点制冷剂由于沸腾换热作用产生大量气泡,碳纳米管在沸腾过程产生气泡的作用下再悬浮于制冷剂中,使得碳纳米管分散,避免循环过程中由于碳纳米管的沉积和团聚作用使冷凝蒸发效果变差;Step 5: In the condensing evaporator, the high-boiling point refrigerant containing lubricating oil and carbon nanotubes exchanges heat with the saturated gas-phase low-boiling point refrigerant, so that the high-boiling point refrigerant absorbs heat and evaporates to form steam, and the low-boiling point refrigerant releases heat Condensation becomes liquid; the high-boiling point refrigerant containing carbon nanotubes produces a large number of bubbles due to the heat transfer effect of boiling, and the carbon nanotubes are resuspended in the refrigerant under the action of bubbles generated during the boiling process, so that the carbon nanotubes are dispersed and the cycle process is avoided. Due to the deposition and agglomeration of carbon nanotubes, the condensation and evaporation effect becomes worse;

步骤6:将液态的低沸点制冷剂经过毛细管送入蒸发器;经蒸发器完成蒸发过程的低沸点制冷剂与经冷凝蒸发器的高沸点制冷剂混合后进入压缩机进行下一次循环过程,结束步骤。Step 6: Send the liquid low-boiling point refrigerant into the evaporator through the capillary tube; the low-boiling point refrigerant that has completed the evaporation process through the evaporator is mixed with the high-boiling point refrigerant that has passed through the condensing evaporator, and then enters the compressor for the next cycle process, ending step.

进一步的,所述步骤1中碳纳米管为制冷剂的0.8~10wt%。Further, in the step 1, the carbon nanotubes are 0.8-10 wt% of the refrigerant.

进一步的,所述碳纳米管为表面改性的。Further, the carbon nanotubes are surface-modified.

进一步的,所述碳纳米管的表面通过共价键的性质嫁接与烷烃化学性质相似的功能集团。Further, the surface of the carbon nanotubes is grafted with functional groups having chemical properties similar to alkanes through covalent bonds.

进一步的,所烷烃化学性质相似的功能集团包括C16TMS、C8TMS、C3TMS。Further, the functional groups with similar chemical properties to alkanes include C 16 TMS , C 8 TMS , and C 3 TMS .

进一步的,所述碳纳米管的表面改性,包括如下步骤:Further, the surface modification of the carbon nanotubes includes the following steps:

步骤11:选10-30g的碳纳米管与600ml酒精溶液混合均匀,并水浴超声60~80分钟,使颗粒表面形成羟基;Step 11: Mix 10-30g of carbon nanotubes with 600ml of alcohol solution evenly, and ultrasonicate in a water bath for 60-80 minutes to form hydroxyl groups on the surface of the particles;

步骤12:将碳纳米管/水悬浮液中加入5-15g的C16TMS、C8TMS或C3TMS形成共价键,完成羟基的嫁接;Step 12: adding 5-15 g of C 16 TMS , C 8 TMS or C 3 TMS to the carbon nanotube/water suspension to form a covalent bond to complete the grafting of hydroxyl groups;

步骤13:对悬浮液进行离心,并用酒精对改性的颗粒进行清洗设定次数;Step 13: Centrifuge the suspension, and wash the modified particles with alcohol for a set number of times;

步骤14:将所得的颗粒放入真空烤箱中干燥,去除有机溶剂。Step 14: Dry the obtained particles in a vacuum oven to remove the organic solvent.

进一步的,所述步骤14中真空烤箱的烘干温度为100℃~120℃。Further, the drying temperature of the vacuum oven in step 14 is 100°C-120°C.

本发明的有益效果为:The beneficial effects of the present invention are:

通过在冷凝器和气液分离器之间设置充注碳纳米管,利用碳纳米管的多孔结构和较大的比表面积等特性,实现对自复叠制冷系统中气液分离器中气相低沸点制冷剂夹带的雾沫状的润滑油滴吸附,增加润滑油的密度,促使润滑油在气液分离器以及冷凝蒸发器中重力沉降,减少低沸点制冷剂中的润滑油含量,避免润滑油跟随低沸点制冷剂进入毛细管造成堵塞;By setting and filling carbon nanotubes between the condenser and the gas-liquid separator, the porous structure and large specific surface area of carbon nanotubes are used to realize the low boiling point refrigeration of the gas phase in the gas-liquid separator in the self-cascading refrigeration system The mist-like lubricating oil droplets entrained by the refrigerant absorb, increase the density of the lubricating oil, promote the gravitational sedimentation of the lubricating oil in the gas-liquid separator and condensing evaporator, reduce the lubricating oil content in the low boiling point refrigerant, and prevent the lubricating oil from following the low The boiling point refrigerant enters the capillary and causes blockage;

通过添加碳纳米管,并且碳纳米管跟随制冷剂在制冷装置中进行循环,其中碳纳米管在进入压缩机后,对压缩机的工作起到了润滑作用,减少压缩机的机械损耗,减少压缩机中润滑油的使用量,进一步促进气相低沸点制冷剂中的油沫减少;By adding carbon nanotubes, and the carbon nanotubes follow the refrigerant to circulate in the refrigeration device. After the carbon nanotubes enter the compressor, they can lubricate the compressor, reduce the mechanical loss of the compressor, and reduce the The use of medium lubricating oil further promotes the reduction of oil foam in the gas phase low boiling point refrigerant;

通过添加碳纳米管提高制冷装置的换热效率和制冷量;Improve the heat transfer efficiency and cooling capacity of refrigeration devices by adding carbon nanotubes;

通过步骤1的充注碳纳米管的过程中,停止压缩机工作,便于进行碳纳米管的充注;During the process of filling the carbon nanotubes in step 1, the compressor is stopped to facilitate the filling of the carbon nanotubes;

通过对碳纳米管的表面改性,提高碳纳米管与矿物油成分的润滑油的亲和性,更好的实现吸附润滑油的目的,同时减少碳纳米管颗粒在润滑油中的团聚作用,降低颗粒的沉积比例,从而达到提高油相迁移的目的。Through the surface modification of carbon nanotubes, the affinity between carbon nanotubes and lubricating oil composed of mineral oil can be improved, the purpose of absorbing lubricating oil can be better achieved, and the agglomeration of carbon nanotube particles in lubricating oil can be reduced at the same time. Reduce the sedimentation ratio of particles, so as to achieve the purpose of improving oil phase migration.

附图说明Description of drawings

图1为本发明实施例一的结构框图。FIG. 1 is a structural block diagram of Embodiment 1 of the present invention.

具体实施方式Detailed ways

以下通过特定的具体实例说明本发明的实施方式,本领域技术人员可由本说明书所揭露的内容轻易地了解本发明的其他优点与功效。本发明还可以通过另外不同的具体实施方式加以实施或应用,本说明书中的各项细节也可以基于不同观点与应用,在没有背离本发明的精神下进行各种修饰或改变。需说明的是,在不冲突的情况下,以下实施例及实施例中的特征可以相互组合。Embodiments of the present invention are described below through specific examples, and those skilled in the art can easily understand other advantages and effects of the present invention from the content disclosed in this specification. The present invention can also be implemented or applied through other different specific implementation modes, and various modifications or changes can be made to the details in this specification based on different viewpoints and applications without departing from the spirit of the present invention. It should be noted that, in the case of no conflict, the following embodiments and features in the embodiments can be combined with each other.

需要说明的是,以下实施例中所提供的图示仅以示意方式说明本发明的基本构想,遂图式中仅显示与本发明中有关的组件而非按照实际实施时的组件数目、形状及尺寸绘制,其实际实施时各组件的型态、数量及比例可为一种随意的改变,且其组件布局型态也可能更为复杂。It should be noted that the diagrams provided in the following embodiments are only schematically illustrating the basic ideas of the present invention, and only the components related to the present invention are shown in the diagrams rather than the number, shape and shape of the components in actual implementation. Dimensional drawing, the type, quantity and proportion of each component can be changed arbitrarily during actual implementation, and the component layout type may also be more complicated.

实施例一:Embodiment one:

如图1所示,一种基于碳纳米管重力油分离效应的低温制冷装置,包括压缩机、冷凝器、气液分离器、节流阀、毛细管、冷凝蒸发器、蒸发器以及充注口;其中压缩机出口与冷凝器进口连接,冷凝器出口与气液分离器进口连接;气液分离器的高沸点制冷剂通道通过节流阀与冷凝蒸发器的蒸发侧通道连接;气液分离器的低沸点制冷剂通道与冷凝蒸发器的冷凝侧通道连接;冷凝蒸发器的冷凝侧出口通过毛细管与蒸发器的进口连接;冷凝蒸发器的蒸发侧出口与蒸发器的出口相连,并与压缩机的进口连接;在冷凝器和气液分离器之间设置有充注口,充注口用于充注碳纳米管,需要说明的是在一些其他实施方式中,也可以将充注口直接设置于冷凝器上或者设置于其他装置之间。制冷装置中的制冷剂为现有的自复叠混合制冷剂,自复叠混合制冷剂包括高沸点制冷剂中的一种或者其组合,以及低沸点制冷剂中的一种或者其组合,其中高沸点制冷剂包括R134A、R600A、R1234YF、R1234ZE(Z)、R1234ZE(E)、R142B、R22等,低沸点制冷剂包括R23、R14、R1150、R290、R170、R125、R32等。二元混合工质类型的自复叠混合制冷剂包括R134A和R23以60:40进行配比的组合、R134A/R744以65:35进行配比的组合、R600A/R744以65:35进行配比的组合以及R170/R600A以8:92进行配比的组合;三元混合工质包括R290、R600A和R123以50:10:40进行配比的组合,R23、R143A和R134A以10:70:20进行配比的组合;四元混合工质包括R23、R125、R134A和R32以10:45:40:5进行配比的组合。在本例中采用R744与R134A混合的制冷剂,配比为35:65。As shown in Figure 1, a low-temperature refrigeration device based on the gravity oil separation effect of carbon nanotubes, including a compressor, a condenser, a gas-liquid separator, a throttle valve, a capillary tube, a condensation evaporator, an evaporator and a filling port; The outlet of the compressor is connected to the inlet of the condenser, and the outlet of the condenser is connected to the inlet of the gas-liquid separator; the high-boiling point refrigerant channel of the gas-liquid separator is connected to the evaporation side channel of the condensing evaporator through a throttle valve; The low-boiling point refrigerant channel is connected to the condensing side channel of the condensing evaporator; the condensing side outlet of the condensing evaporator is connected to the inlet of the evaporator through a capillary tube; the evaporating side outlet of the condensing evaporator is connected to the outlet of the evaporator and connected to the compressor Inlet connection; a charging port is provided between the condenser and the gas-liquid separator, and the charging port is used for filling carbon nanotubes. It should be noted that in some other embodiments, the charging port can also be directly arranged on the condenser device or placed between other devices. The refrigerant in the refrigeration device is an existing self-cascading mixed refrigerant, and the self-cascading mixed refrigerant includes one or a combination of high-boiling point refrigerants and one or a combination of low-boiling point refrigerants, wherein High boiling point refrigerants include R134A, R600A, R1234YF, R1234ZE(Z), R1234ZE(E), R142B, R22, etc., and low boiling point refrigerants include R23, R14, R1150, R290, R170, R125, R32, etc. The self-cascading mixed refrigerant of the binary mixed refrigerant type includes a combination of R134A and R23 at a ratio of 60:40, a combination of R134A/R744 at a ratio of 65:35, and a combination of R600A/R744 at a ratio of 65:35 and the combination of R170/R600A at a ratio of 8:92; the ternary mixed working medium includes the combination of R290, R600A and R123 at a ratio of 50:10:40, and the ratio of R23, R143A and R134A at a ratio of 10:70:20 Combination of ratios; quaternary mixed working fluids include R23, R125, R134A and R32 in a ratio of 10:45:40:5. In this example, the refrigerant mixed with R744 and R134A is used, and the ratio is 35:65.

所述充注口用于充注碳纳米管,通过碳纳米管,吸附气液分离器分离出的气相低沸点制冷剂中的雾沫状的油滴。碳纳米管跟随制冷剂在制冷装置中循环。The filling port is used for filling carbon nanotubes, through which the mist-like oil droplets in the gas-phase low-boiling point refrigerant separated by the gas-liquid separator are absorbed. The carbon nanotubes follow the refrigerant as it circulates through the refrigeration unit.

在实施的过程中,通过在冷凝器和气液分离器之间设置充注碳纳米管的充注口,利用碳纳米管的多孔结构和较大的比表面积等特性,实现对自复叠制冷系统中气液分离器中气相低沸点制冷剂夹带的雾沫状的润滑油滴吸附,增加润滑油的密度,促使润滑油在气液分离器以及冷凝蒸发器中重力沉降,避免润滑油跟随低沸点制冷剂进入毛细管造成堵塞;通过添加碳纳米管,并且碳纳米管跟随制冷剂在制冷装置中进行循环,其中碳纳米管在进入压缩机后,对压缩机的工作起到了润滑作用,减少压缩机的机械损耗,减少压缩机中润滑油的使用量,进一步促进低沸点制冷剂中的油沫减少;通过添加碳纳米管提高制冷装置的换热效率和制冷量。In the process of implementation, by setting a filling port filled with carbon nanotubes between the condenser and the gas-liquid separator, the self-cascading refrigeration system is realized by utilizing the porous structure and large specific surface area of carbon nanotubes. The mist-like lubricating oil droplets entrained by the gas-phase low-boiling point refrigerant in the gas-liquid separator are adsorbed to increase the density of the lubricating oil, and promote the gravitational settlement of the lubricating oil in the gas-liquid separator and condensing evaporator, preventing the lubricating oil from following the low boiling point The refrigerant enters the capillary and causes blockage; by adding carbon nanotubes, and the carbon nanotubes follow the refrigerant to circulate in the refrigeration device, where the carbon nanotubes enter the compressor, lubricate the compressor, and reduce the compressor reduce the amount of lubricating oil used in the compressor, and further promote the reduction of oil foam in low-boiling refrigerants; increase the heat exchange efficiency and cooling capacity of the refrigeration device by adding carbon nanotubes.

一种基于碳纳米管重力油分离效应的低温制冷方法,包括如下步骤:A low-temperature refrigeration method based on the gravity oil separation effect of carbon nanotubes, comprising the steps of:

步骤1:压缩机停止工作,将设定量的碳纳米管通过充注口充注到制冷装置中;Step 1: The compressor stops working, and the set amount of carbon nanotubes is filled into the refrigeration device through the filling port;

步骤2:启动压缩机;碳纳米管和制冷剂混合进入冷凝器;Step 2: Start the compressor; carbon nanotubes and refrigerant are mixed into the condenser;

步骤3:经过冷凝器冷凝,获得部分液化的制冷剂;需要说明的是经过冷凝器的冷凝效果,高沸点制冷剂放热形成液态,低沸点制冷剂保持气态;Step 3: Condensate through the condenser to obtain partially liquefied refrigerant; it should be noted that after the condensation effect of the condenser, the high-boiling point refrigerant releases heat to form a liquid state, and the low-boiling point refrigerant remains in a gaseous state;

步骤4:部分液化的制冷剂进入气液分离器,进行气相低沸点制冷剂和高沸点制冷剂的分离过程;分离后的高沸点制冷剂经过节流阀进入冷凝蒸发器的蒸发侧通道,低温制冷剂进入冷凝蒸发器的冷凝侧通道;Step 4: The partially liquefied refrigerant enters the gas-liquid separator for the separation process of gas-phase low-boiling point refrigerant and high-boiling point refrigerant; the separated high-boiling point refrigerant enters the evaporation side channel of the condensing evaporator through the throttle valve, and the low-temperature The refrigerant enters the condensing side channel of the condensing evaporator;

步骤5:在冷凝蒸发器中,含润滑油和碳纳米管的高沸点制冷剂与饱和气相低沸点制冷剂进行换热,使得高沸点制冷剂吸热蒸发,形成蒸汽,低沸点制冷剂放热冷凝成为液态;Step 5: In the condensing evaporator, the high-boiling point refrigerant containing lubricating oil and carbon nanotubes exchanges heat with the saturated gas-phase low-boiling point refrigerant, so that the high-boiling point refrigerant absorbs heat and evaporates to form steam, and the low-boiling point refrigerant releases heat condense into a liquid state;

步骤6:将液态的低沸点制冷剂经过毛细管送入蒸发器;经蒸发器完成蒸发过程的低沸点制冷剂与经冷凝蒸发器的高沸点制冷剂混合后进入压缩机进行下一次循环过程,结束步骤;其中高沸点制冷剂中含有润滑油、碳纳米管。Step 6: Send the liquid low-boiling point refrigerant into the evaporator through the capillary tube; the low-boiling point refrigerant that has completed the evaporation process through the evaporator is mixed with the high-boiling point refrigerant that has passed through the condensing evaporator, and then enters the compressor for the next cycle process, ending Step; wherein the high boiling point refrigerant contains lubricating oil and carbon nanotubes.

所述步骤1中设定量的碳纳米管为制冷剂的0.8~10wt%。在本例中碳纳米管为表面改性的;在碳纳米管的表面通过共价键的性质嫁接与烷烃化学性质相似的功能集团,包括C16TMS、C8TMS、C3TMS,实现碳纳米管的改性。通过表面改性的碳纳米管,提高与矿物油成分的润滑油的亲和性,更好的实现吸附润滑油的目的,同时减少碳纳米管颗粒在润滑油中的团聚作用,降低颗粒的沉积比例,从而达到提高油相迁移的目的。对于碳纳米管的表面改性通过如下步骤获得,以C16TMS为例:The set amount of carbon nanotubes in the step 1 is 0.8-10 wt% of the refrigerant. In this example, the carbon nanotubes are surface-modified; on the surface of the carbon nanotubes, functional groups with similar chemical properties to alkanes are grafted on the surface of the carbon nanotubes, including C 16 TMS, C 8 TMS, and C 3 TMS. Modification of nanotubes. Through surface-modified carbon nanotubes, the affinity with lubricating oil composed of mineral oil can be improved, and the purpose of absorbing lubricating oil can be better achieved, while reducing the agglomeration of carbon nanotube particles in lubricating oil and reducing particle deposition Ratio, so as to achieve the purpose of improving oil phase migration. The surface modification of carbon nanotubes is obtained through the following steps, taking C 16 TMS as an example:

步骤11:选用20g的碳纳米管与600ml酒精溶液混合均匀,并水浴超声60~80分钟,使颗粒表面形成羟基;Step 11: Mix 20g of carbon nanotubes with 600ml of alcohol solution evenly, and ultrasonicate in a water bath for 60-80 minutes to form hydroxyl groups on the surface of the particles;

步骤12:将碳纳米管/水悬浮液中加入10g的C16TMS形成共价键,完成羟基的嫁接;Step 12: adding 10 g of C 16 TMS to the carbon nanotube/water suspension to form a covalent bond to complete the grafting of hydroxyl groups;

步骤13:对悬浮液进行离心,并用酒精对改性的颗粒进行清洗数次;Step 13: Centrifuge the suspension and wash the modified particles several times with alcohol;

步骤14:将所得的颗粒放入真空烤箱中干燥3小时去除有机溶剂。Step 14: The obtained particles were dried in a vacuum oven for 3 hours to remove the organic solvent.

所述步骤14中真空烤箱的烘干温度为100℃~120℃,优选为110℃。The drying temperature of the vacuum oven in step 14 is 100°C-120°C, preferably 110°C.

所述步骤3中,由于润滑油的粘度高,而碳纳米管存在相见迁移机制,因此碳纳米管相比制冷剂,更容易与润滑油相结合,润滑油被吸附后,由于重量增加发生沉积,因此碳纳米管和润滑油更多存在于液态的高沸点制冷剂中;In the step 3, due to the high viscosity of the lubricating oil, carbon nanotubes have a phase migration mechanism, so carbon nanotubes are easier to combine with the lubricating oil than refrigerants. After the lubricating oil is absorbed, due to the increase in weight, the Deposition, so carbon nanotubes and lubricating oil are more present in liquid high-boiling point refrigerants;

所述步骤5中,含有碳纳米管的高沸点制冷剂由于沸腾换热作用产生大量气泡,碳纳米管在沸腾过程产生气泡的作用下再悬浮于制冷剂中,使得碳纳米管分散,避免循环过程中由于碳纳米管的沉积和团聚作用使冷凝蒸发效果变差,有助于装置长时间高效运行。In the step 5, the high-boiling point refrigerant containing carbon nanotubes produces a large number of bubbles due to the heat transfer effect of boiling, and the carbon nanotubes are resuspended in the refrigerant under the action of the bubbles generated during the boiling process, so that the carbon nanotubes are dispersed and the circulation is avoided. During the process, due to the deposition and agglomeration of carbon nanotubes, the effect of condensation and evaporation is deteriorated, which helps the device to run efficiently for a long time.

在实施过程中,通过步骤1的充注碳纳米管的过程中,停止压缩机工作,便于进行碳纳米管的充注;通过对碳纳米管的表面改性,提高碳纳米管与矿物油成分的润滑油的亲和性,更好的实现吸附润滑油的目的,同时减少碳纳米管颗粒在润滑油中的团聚作用,降低颗粒的沉积比例,从而达到提高油相迁移的目的。During the implementation process, during the process of filling carbon nanotubes in step 1, the compressor is stopped to facilitate the filling of carbon nanotubes; by surface modification of carbon nanotubes, the composition of carbon nanotubes and mineral oil is improved. Improve the affinity of lubricating oil, better achieve the purpose of absorbing lubricating oil, reduce the agglomeration of carbon nanotube particles in lubricating oil, reduce the sedimentation ratio of particles, so as to achieve the purpose of improving oil phase migration.

实施例二:Embodiment two:

本实施例是基于实施例一进行改进获得的,其中碳纳米管的改性过程包括如下步骤:This embodiment is obtained based on the improvement of Embodiment 1, wherein the modification process of carbon nanotubes includes the following steps:

步骤21:将甲基丙烯酸甲酷加入盛有甲醇、碳纳米管的三颈瓶中;其中甲基丙烯酸甲酷和碳纳米管的质量比为20:1,甲基丙烯酸甲酷与甲醇的比例为1g/20ml~1g/40ml;Step 21: Add methyl methacrylate into a three-necked bottle filled with methanol and carbon nanotubes; wherein the mass ratio of methyl methacrylate to carbon nanotubes is 20:1, and the ratio of methyl methacrylate to methanol 1g/20ml~1g/40ml;

步骤22:对三颈瓶进行超声处理,处理10~30min;Step 22: ultrasonically treat the three-neck bottle for 10-30 minutes;

步骤23:对三颈瓶持续通入氮气,持续25~35minStep 23: Continuously inject nitrogen into the three-neck bottle for 25-35 minutes

步骤24:在三颈瓶中添加1g自由基引发剂,在55℃~70℃环境下反应6-10h;在本例中自由基引发剂采用偶氮二异丁睛,通过自由基引发剂能够促使碳纳米管和甲基丙烯酸甲酷形成共价键,并且保证反应更彻底;Step 24: Add 1g of free radical initiator to the three-necked bottle, and react for 6-10 hours at 55°C to 70°C; in this example, azobisisobutyronitrile is used as the free radical initiator, which can Promote the formation of covalent bonds between carbon nanotubes and methyl methacrylate, and ensure a more thorough reaction;

步骤25:通过过滤获得反应后的产物,并通过乙酸乙酷超声洗涤3~5次;Step 25: Obtain the reacted product by filtration, and ultrasonically wash with ethyl acetate for 3 to 5 times;

步骤26:将洗涤后的颗粒放入真空烤箱中,设定温度为40℃~50℃,干燥16~20h,去除有机溶剂。Step 26: Put the washed particles into a vacuum oven, set the temperature at 40°C-50°C, dry for 16-20 hours, and remove the organic solvent.

以上描述仅是本发明的一个具体实例,不构成对本发明的任何限制。显然对于本领域的专业人员来说,在了解了本发明内容和原理后,都可能在不背离本发明原理、结构的情况下,进行形式和细节上的各种修改和改变,但是这些基于本发明思想的修正和改变仍在本发明的权利要求保护范围之内。The above description is only a specific example of the present invention, and does not constitute any limitation to the present invention. Obviously, for those skilled in the art, after understanding the content and principle of the present invention, it is possible to make various modifications and changes in form and details without departing from the principle and structure of the present invention, but these are based on the present invention. The modification and change of the inventive concept are still within the protection scope of the claims of the present invention.

Claims (5)

1.一种基于碳纳米管重力油分离效应的低温制冷装置,其特征在于,包括压缩机、冷凝器、气液分离器、节流阀、毛细管、冷凝蒸发器、蒸发器以及充注口;其中压缩机出口与冷凝器进口连接,冷凝器出口与气液分离器进口连接;1. A low-temperature refrigeration device based on the gravity oil separation effect of carbon nanotubes, characterized in that it comprises a compressor, a condenser, a gas-liquid separator, a throttle valve, a capillary tube, a condensation evaporator, an evaporator and a filling port; The outlet of the compressor is connected to the inlet of the condenser, and the outlet of the condenser is connected to the inlet of the gas-liquid separator; 气液分离器的高沸点制冷剂通道通过节流阀与冷凝蒸发器的蒸发侧通道连接;气液分离器的低沸点制冷剂通道与冷凝蒸发器的冷凝侧通道连接;冷凝蒸发器的冷凝侧出口通过毛细管与蒸发器的进口连接;冷凝蒸发器的蒸发侧出口与蒸发器的出口相连,并与压缩机的进口连接;在冷凝器和气液分离器之间设置有充注口,充注口用于充注碳纳米管;通过碳纳米管吸附润滑油,使润滑油重力沉降,碳纳米管跟随制冷剂在制冷装置中循环,还包括制冷剂,制冷剂采用自复叠混合制冷剂,所述自复叠混合制冷剂包括高沸点制冷剂中的一种或者其组合,以及低沸点制冷剂中的一种或者其组合;其中高沸点制冷剂包括R134A、R600A、R1234YF、R1234ZE(Z)、R1234ZE(E)、R142B以及R22,低沸点制冷剂包括R23、R14、R1150、R290、R170、R125以及R32,所述碳纳米管为表面改性的,所述碳纳米管的表面通过共价键的性质嫁接与烷烃化学性质相似的功能集团,烷烃化学性质相似的功能集团包括C16TMS、C8TMS、C3TMS。The high-boiling point refrigerant channel of the gas-liquid separator is connected to the evaporating side channel of the condensing evaporator through a throttle valve; the low-boiling point refrigerant channel of the gas-liquid separator is connected to the condensing side channel of the condensing evaporator; the condensing side of the condensing evaporator The outlet is connected to the inlet of the evaporator through a capillary tube; the outlet of the evaporation side of the condensing evaporator is connected to the outlet of the evaporator and connected to the inlet of the compressor; a charging port is provided between the condenser and the gas-liquid separator, and the charging port It is used to fill carbon nanotubes; the lubricating oil is adsorbed by carbon nanotubes to make the lubricating oil settle by gravity. The self-cascade mixed refrigerant includes one or a combination of high-boiling refrigerants, and one or a combination of low-boiling refrigerants; wherein the high-boiling refrigerants include R134A, R600A, R1234YF, R1234ZE(Z), R1234ZE (E), R142B and R22, low-boiling point refrigerants include R23, R14, R1150, R290, R170, R125 and R32, the carbon nanotubes are surface-modified, and the surface of the carbon nanotubes is covalently bonded Grafting functional groups with similar chemical properties to alkanes, including C 16 TMS , C 8 TMS , and C 3 TMS . 2.一种基于碳纳米管重力油分离效应的低温制冷方法,其特征在于,所述制冷方法基于权利要求1所述的制冷装置,制冷方法包括如下步骤:2. a low-temperature refrigeration method based on carbon nanotube gravity oil separation effect, it is characterized in that, described refrigeration method is based on the refrigeration unit described in claim 1, and refrigeration method comprises the steps: 步骤1:压缩机停止工作,将设定量的碳纳米管通过充注口充注到制冷装置中;Step 1: The compressor stops working, and the set amount of carbon nanotubes is filled into the refrigeration device through the filling port; 步骤2:启动压缩机;碳纳米管和制冷剂混合进入冷凝器;Step 2: Start the compressor; carbon nanotubes and refrigerant are mixed into the condenser; 步骤3:经过冷凝器冷凝,获得部分液化的制冷剂;高沸点制冷剂经过放热冷凝形成液态,低沸点制冷剂保持气态;其中由于润滑油的粘度高,而碳纳米管存在相见迁移机制,因此碳纳米管吸附润滑油并发生沉积,与液态的高沸点制冷剂混合;Step 3: After condensing in the condenser, a partially liquefied refrigerant is obtained; the high-boiling point refrigerant is condensed to form a liquid state after exothermic condensation, and the low-boiling point refrigerant remains in a gaseous state; due to the high viscosity of the lubricating oil, the carbon nanotubes have a migration mechanism , so carbon nanotubes absorb lubricating oil and deposit, and mix with liquid high-boiling point refrigerant; 步骤4:部分液化的制冷剂进入气液分离器,进行气相低沸点制冷剂和高沸点制冷剂的分离过程;分离后的高沸点制冷剂经过节流阀进入冷凝蒸发器的蒸发侧通道,低温制冷剂进入冷凝蒸发器的冷凝侧通道;Step 4: The partially liquefied refrigerant enters the gas-liquid separator for the separation process of gas-phase low-boiling point refrigerant and high-boiling point refrigerant; the separated high-boiling point refrigerant enters the evaporation side channel of the condensing evaporator through the throttle valve, and the low-temperature The refrigerant enters the condensing side channel of the condensing evaporator; 步骤5:在冷凝蒸发器中,含润滑油和碳纳米管的高沸点制冷剂与饱和气相低沸点制冷剂进行换热,使得高沸点制冷剂吸热蒸发,形成蒸汽,低沸点制冷剂放热冷凝成为液态;其中含有碳纳米管的高沸点制冷剂由于沸腾换热作用产生大量气泡,碳纳米管在沸腾过程产生气泡的作用下再悬浮于制冷剂中,使得碳纳米管分散,避免循环过程中由于碳纳米管的沉积和团聚作用使冷凝蒸发效果变差;Step 5: In the condensing evaporator, the high-boiling point refrigerant containing lubricating oil and carbon nanotubes exchanges heat with the saturated gas-phase low-boiling point refrigerant, so that the high-boiling point refrigerant absorbs heat and evaporates to form steam, and the low-boiling point refrigerant releases heat Condensation becomes liquid; the high-boiling point refrigerant containing carbon nanotubes produces a large number of bubbles due to the heat transfer effect of boiling, and the carbon nanotubes are resuspended in the refrigerant under the action of bubbles generated during the boiling process, so that the carbon nanotubes are dispersed and the cycle process is avoided. Due to the deposition and agglomeration of carbon nanotubes, the condensation and evaporation effect becomes worse; 步骤6:将液态的低沸点制冷剂经过毛细管送入蒸发器;经蒸发器完成蒸发过程的低沸点制冷剂与经冷凝蒸发器的高沸点制冷剂混合后进入压缩机进行下一次循环过程,结束步骤。Step 6: Send the liquid low-boiling point refrigerant into the evaporator through the capillary tube; the low-boiling point refrigerant that has completed the evaporation process through the evaporator is mixed with the high-boiling point refrigerant that has passed through the condensing evaporator, and then enters the compressor for the next cycle process, ending step. 3.根据权利要求2所述的一种基于碳纳米管重力油分离效应的低温制冷方法,其特征在于,所述步骤1中碳纳米管为制冷剂的0.8~10wt%。3. A low-temperature refrigeration method based on the gravity oil separation effect of carbon nanotubes according to claim 2, characterized in that, in the step 1, the carbon nanotubes are 0.8-10 wt% of the refrigerant. 4.根据权利要求2所述的一种基于碳纳米管重力油分离效应的低温制冷方法,其特征在于,所述碳纳米管的表面改性,包括如下步骤:4. a kind of cryogenic refrigeration method based on carbon nanotube gravity oil separation effect according to claim 2, is characterized in that, the surface modification of described carbon nanotube comprises the steps: 步骤11:选用10-30g的碳纳米管与600ml酒精溶液混合均匀,并水浴超声60~80分钟,使颗粒表面形成羟基;Step 11: Select 10-30g of carbon nanotubes and mix them evenly with 600ml of alcohol solution, and ultrasonicate in a water bath for 60-80 minutes to form hydroxyl groups on the surface of the particles; 步骤12:将碳纳米管/水悬浮液中加入5-15g的C16TMS、C8TMS或C3TMS形成共价键,完成羟基的嫁接;Step 12: adding 5-15 g of C 16 TMS , C 8 TMS or C 3 TMS to the carbon nanotube/water suspension to form a covalent bond to complete the grafting of hydroxyl groups; 步骤13:对悬浮液进行离心,并用酒精对改性的颗粒进行清洗设定次数;Step 13: Centrifuge the suspension, and wash the modified particles with alcohol for a set number of times; 步骤14:将所得的颗粒放入真空烤箱中干燥,去除有机溶剂。Step 14: Dry the obtained particles in a vacuum oven to remove the organic solvent. 5.根据权利要求4所述的一种基于碳纳米管重力油分离效应的低温制冷方法,其特征在于,所述步骤14中真空烤箱的烘干温度为100℃~120℃。5 . The low-temperature refrigeration method based on the gravity oil separation effect of carbon nanotubes according to claim 4 , wherein the drying temperature of the vacuum oven in the step 14 is 100° C. to 120° C. 5 .
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