CN109920581B - A kind of mixed insulating medium of liquid nitrogen and liquefied carbon tetrafluoride and preparation method thereof - Google Patents
A kind of mixed insulating medium of liquid nitrogen and liquefied carbon tetrafluoride and preparation method thereof Download PDFInfo
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title claims abstract description 221
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 106
- 239000007788 liquid Substances 0.000 title claims abstract description 97
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 title claims abstract description 35
- 238000002360 preparation method Methods 0.000 title abstract description 7
- 239000007789 gas Substances 0.000 claims abstract description 49
- 238000007710 freezing Methods 0.000 claims abstract description 18
- 230000008014 freezing Effects 0.000 claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 12
- 229910001873 dinitrogen Inorganic materials 0.000 claims abstract description 9
- 239000003949 liquefied natural gas Substances 0.000 claims abstract description 8
- 238000003860 storage Methods 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 15
- 238000005303 weighing Methods 0.000 claims description 6
- 238000005259 measurement Methods 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims 2
- 238000009835 boiling Methods 0.000 abstract description 5
- 239000003507 refrigerant Substances 0.000 description 6
- 238000009413 insulation Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000001307 helium Substances 0.000 description 4
- 229910052734 helium Inorganic materials 0.000 description 4
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 4
- 239000011810 insulating material Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 229910052754 neon Inorganic materials 0.000 description 4
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 description 4
- 238000010292 electrical insulation Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000374 eutectic mixture Substances 0.000 description 1
- 238000003384 imaging method Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 229910021521 yttrium barium copper oxide Inorganic materials 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02E40/00—Technologies for an efficient electrical power generation, transmission or distribution
- Y02E40/60—Superconducting electric elements or equipment; Power systems integrating superconducting elements or equipment
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Abstract
一种液氮和液化四氟化碳的混合绝缘介质及其配制方法,由纯度均大于等于99%的氮气和纯度均大于等于99%的四氟化碳气体配制。液氮和液化四氟化碳的比例为(2%~90%):(98%~10%),为摩尔比。在液氮和液化四氟化碳的摩尔比为45%‑90%的情况下,所制备的混合绝缘介质的凝固点可调控到52K‑60K,满足液氮以下温区电工装备冷却要求;在液氮和液化四氟化碳的摩尔比为2%‑20%的情况下,所制备的混合绝缘介质的常压沸点可调控到89K‑120K,满足液化天然气温区电工装备冷却需求。本发明混合绝缘介质采用液氮换热器或液氮温区的制冷机对高纯氮气和高纯CF4进行液化;根据混合绝缘介质凝固点和泡点的要求确定高纯氮气和高纯CF4气的比例。所述的混合绝缘介质可用于液氮以下温区和液化天然气温区电工装备。
A mixed insulating medium of liquid nitrogen and liquefied carbon tetrafluoride and a preparation method thereof are prepared from nitrogen gas with a purity greater than or equal to 99% and carbon tetrafluoride gas with a purity greater than or equal to 99%. The ratio of liquid nitrogen and liquefied carbon tetrafluoride is (2% to 90%): (98% to 10%), which is a molar ratio. When the molar ratio of liquid nitrogen and liquefied carbon tetrafluoride is 45%-90%, the freezing point of the prepared mixed insulating medium can be adjusted to 52K-60K, which meets the cooling requirements of electrical equipment in the temperature area below liquid nitrogen; When the molar ratio of nitrogen and liquefied carbon tetrafluoride is 2%-20%, the normal pressure boiling point of the prepared mixed insulating medium can be adjusted to 89K-120K, which meets the cooling requirements of electrical equipment in the liquefied natural gas temperature zone. The mixed insulating medium of the invention adopts a liquid nitrogen heat exchanger or a refrigerator in a liquid nitrogen temperature zone to liquefy high-purity nitrogen and high-purity CF 4 ; the high-purity nitrogen and high-purity CF 4 are determined according to the requirements of the freezing point and bubble point of the mixed insulating medium gas ratio. The mixed insulating medium can be used for electrical equipment in the sub-temperature zone of liquid nitrogen and the temperature zone of liquefied natural gas.
Description
技术领域technical field
本发明涉及一种液氮和液化CF4混合绝缘介质及其配制方法。 The invention relates to a liquid nitrogen and liquefied CF4 mixed insulating medium and a preparation method thereof.
背景技术Background technique
液氮是一种重要的低温制冷剂,也是一种液体绝缘材料,主要用于各种超导电缆、超导变压器、超导限流器、超导储能装置等电工装备中。通过浸泡冷却超导电工装备,为超导电工装备提供一个正常工作的低温环境,同时也起到提高电气绝缘强度的作用,对超导电工装备的正常运行有着直接的影响。Liquid nitrogen is an important low-temperature refrigerant and a liquid insulating material. It is mainly used in electrical equipment such as various superconducting cables, superconducting transformers, superconducting current limiters, and superconducting energy storage devices. By immersing and cooling the superconducting electrical equipment, it provides a low-temperature environment for the superconducting electrical equipment to work normally, and also plays a role in improving the electrical insulation strength, which has a direct impact on the normal operation of the superconducting electrical equipment.
四氟化碳(CF4)常温下是一种无色、无臭、不燃、不溶于水的可压缩性气体,可用作低温制冷剂和绝缘气体。四氟化碳常压下的沸点约为145K,熔点89.6K,液化四氟化碳有良好的电气绝缘性能,能够和液氮形成共晶混合物,如图1所示,其凝固点可以达到52K左右,如图2所示,其泡点最高可以达到145K左右。Carbon tetrafluoride (CF 4 ) is a colorless, odorless, non-flammable, water-insoluble compressible gas at room temperature, which can be used as low-temperature refrigerant and insulating gas. The boiling point of carbon tetrafluoride under normal pressure is about 145K and the melting point is 89.6K. Liquefied carbon tetrafluoride has good electrical insulation properties and can form a eutectic mixture with liquid nitrogen. As shown in Figure 1, its freezing point can reach about 52K , as shown in Figure 2, the highest bubble point can reach about 145K.
常压下,液氮的沸点大约是77K,大部分高温超导材料在此温度都能够正常工作。超导电缆、超导限流器、超导变压器、超导电机等电工装备当前通常采用液氮直接冷却,而超导储能(SMES)、磁共振(MRI/NMR)成像系统等利用了强磁场的电工装备,则主要采用液氦(4.2K)、液氖(20K)、以及制冷机直接传导的方式来冷却。氦气和氖气在地球上含量很低,液化成本高昂,限制了其大规模推广。制冷机直接传导冷却的电工装备相对液体直接浸泡其热稳定性较差,且存在低真空下的绝缘问题,也限制了大规模推广。一般而言,高温超导材料在液氮凝固点65K的临界电流是77K下的2倍,如果继续降温,则当前没有合适的低温液体绝缘材料,利用液氮和液化CF4混合绝缘介质,其凝固点可继续降低到52K左右,高温超导材料在50K自场下临界电流是77K下的3-4倍,如图3所示,超导电工装备的载流能力和磁场都会得到很大提升,另外,氮气和CF4气体的成本较低,绝缘能力比氦气和氖气耐压高很多,对于超导电工装备的小型化及降低成本具有重要意义。Under normal pressure, the boiling point of liquid nitrogen is about 77K, and most high-temperature superconducting materials can work normally at this temperature. Superconducting cables, superconducting current limiters, superconducting transformers, superconducting motors and other electrical equipment are currently directly cooled by liquid nitrogen, while superconducting energy storage (SMES), magnetic resonance (MRI/NMR) imaging systems, etc. The electrical equipment of the magnetic field is mainly cooled by liquid helium (4.2K), liquid neon (20K), and the direct conduction of the refrigerator. Helium and neon are in very low concentrations on Earth and are expensive to liquefy, limiting their large-scale deployment. Compared with the direct immersion of liquid, the electrical equipment directly cooled by the refrigerator has poor thermal stability, and has insulation problems under low vacuum, which also limits its large-scale promotion. Generally speaking, the critical current of high-temperature superconducting materials at the freezing point of liquid nitrogen at 65K is twice that at 77K. If the temperature continues to drop, there is currently no suitable low - temperature liquid insulating material. Using liquid nitrogen and liquefied CF4 mixed insulating medium, its freezing point It can be further reduced to about 52K. The critical current of high-temperature superconducting materials at 50K self-field is 3-4 times that at 77K. As shown in Figure 3, the current-carrying capacity and magnetic field of superconducting electrical equipment will be greatly improved. , Nitrogen and CF 4 gas have lower cost, and the insulating ability is much higher than that of helium and neon gas, which is of great significance for the miniaturization and cost reduction of superconducting electrical equipment.
另外,随着超导技术的发展,超导材料的临界温度不断提高,可以在液化天然气温区(90K-120K)乃至更高温区工作。在这个温区,可以用比液氮制冷机效率更高的混合工质节流制冷机或逆布雷顿制冷机来冷却。然而,在更高的温度下,缺少相应的液体绝缘材料来进行超导电工装备的绝缘和冷却。液氮在90K时,其压力超过0.3MPa,在100K时,压力超过0.6Mpa,给压力容器和超导电工装备的设计、制造和运维带来困难。急需一种可以运行在90K-120K温区的低温绝缘冷却介质。目前有很多氟利昂制冷剂如R124、R32、R125、R134a及其混合制冷剂的低温绝缘性能都比较差,在强电场下存在析碳现象,而且有些低温制冷剂对臭氧层有破坏,无法广泛应用于高压电工装备中。In addition, with the development of superconducting technology, the critical temperature of superconducting materials continues to increase, and it can work in the LNG temperature region (90K-120K) or even higher temperature regions. In this temperature region, a mixed refrigerant throttling refrigerator or an inverse Brayton refrigerator, which is more efficient than a liquid nitrogen refrigerator, can be used for cooling. At higher temperatures, however, corresponding liquid insulating materials are lacking for the insulation and cooling of superconducting electrical equipment. When liquid nitrogen is at 90K, its pressure exceeds 0.3MPa, and at 100K, the pressure exceeds 0.6Mpa, which brings difficulties to the design, manufacture and operation and maintenance of pressure vessels and superconducting electrical equipment. There is an urgent need for a low-temperature insulating cooling medium that can operate in the temperature range of 90K-120K. At present, many Freon refrigerants such as R124, R32, R125, R134a and their mixed refrigerants have poor low-temperature insulation performance, and carbon deposition occurs in strong electric fields, and some low-temperature refrigerants damage the ozone layer and cannot be widely used. high-voltage electrical equipment.
因此,有必要开发一种绿色环保、制备工艺简便、工作温度为50K~140K的新型低温液体绝缘材料。Therefore, it is necessary to develop a new low-temperature liquid insulating material that is green and environmentally friendly, has a simple preparation process, and has a working temperature of 50K to 140K.
发明内容SUMMARY OF THE INVENTION
本发明的目的是针对现有的低温液体绝缘介质难以工作在50K~60K等液氮以下温区和90K-120K液化天然气温区、电气绝缘性能差、且制备工艺复杂等缺陷,提供一种液氮和液化四氟化碳混合绝缘介质及其配制方法。The purpose of the present invention is to provide a liquid insulation medium for the defects of the existing low-temperature liquid insulating medium that it is difficult to work in the temperature region below liquid nitrogen such as 50K-60K and the temperature region of 90K-120K liquefied natural gas, the electrical insulation performance is poor, and the preparation process is complicated. Nitrogen and liquefied carbon tetrafluoride mixed insulating medium and preparation method thereof.
为了实现上述目的,本发明采取如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
本发明混合绝缘介质采用纯度均大于等于99%的氮气和纯度均大于等于99%的四氟化碳气体配制,液氮和液化四氟化碳的比例为(2%~90%):(98%~10%),为摩尔比。在液氮和液化四氟化碳的摩尔比为45%-90%的情况下,所制备的混合绝缘介质的凝固点可调控到52K-60K,满足液氮以下温区电工装备冷却要求。在液氮和液化四氟化碳的摩尔比为2%-20%的情况下,所制备的混合绝缘介质的常压沸点可调控到89K-120K,满足液化天然气温区电工装备冷却需求。混合绝缘介质的凝固点和泡点通过量热仪或相平衡装置测定,绝缘性能依据国标GB/T 507-2002,采用高压试验电源和标准液体耐压试验电极测定。本发明混合液体绝缘介质不仅能够达到和液氮相当的绝缘强度,而且液化温度也能够满足52K-145K的工程应用要求。The mixed insulating medium of the present invention is prepared by using nitrogen gas with a purity greater than or equal to 99% and carbon tetrafluoride gas with a purity greater than or equal to 99%, and the ratio of liquid nitrogen and liquefied carbon tetrafluoride is (2% to 90%): (98 %~10%), which is a molar ratio. When the molar ratio of liquid nitrogen and liquefied carbon tetrafluoride is 45%-90%, the freezing point of the prepared mixed insulating medium can be adjusted to 52K-60K, which meets the cooling requirements of electrical equipment in the lower temperature area of liquid nitrogen. When the molar ratio of liquid nitrogen and liquefied carbon tetrafluoride is 2%-20%, the normal pressure boiling point of the prepared mixed insulating medium can be adjusted to 89K-120K, which meets the cooling requirements of electrical equipment in the liquefied natural gas temperature zone. The freezing point and bubble point of the mixed insulating medium are measured by a calorimeter or a phase balance device, and the insulation performance is measured according to the national standard GB/T 507-2002, using a high-voltage test power supply and a standard liquid withstand voltage test electrode. The mixed liquid insulating medium of the invention can not only achieve the dielectric strength equivalent to that of liquid nitrogen, but also can meet the engineering application requirements of 52K-145K in liquefaction temperature.
本发明液氮和液化CF4混合绝缘介质可采用以下两种方法制备: The liquid nitrogen and liquefied CF mixed insulating medium of the present invention can be prepared by the following two methods:
方法一:method one:
利用液氮换热器对氮气瓶中的高纯氮气和CF4气瓶中的高纯CF4气体进行液化。液氮换热器由低温容器、液氮盘管和混合绝缘介质盘管构成。液氮盘管的一端连接液氮储罐,另一端排空;混合绝缘介质盘管的一端连接高纯氮气瓶和高纯CF4气瓶,另一端连接混合绝缘介质储罐,通过液氮盘管冷却混合绝缘介质盘管。液氮盘管的两端分别设置有进液阀和排空阀,混合绝缘介质盘管的两端分别设置有进气阀和出液阀。氮气瓶和CF4气瓶的出气量通过各自的减压阀门进行控制,高纯氮气和高纯CF4气的比例通过电子秤称重或气相色谱仪测量来确定。混合绝缘介质的出液管连接到混合绝缘介质储罐,混合绝缘介质储罐为低温密闭容器,低温密闭容器的顶部装有真空阀门和进液阀门。首先通过真空机组将封闭容器抽真空至0.1Pa以下真空态,然后混合绝缘介质通过进液管流入绝缘介质储罐中。The high-purity nitrogen in the nitrogen cylinder and the high-purity CF 4 gas in the CF 4 cylinder are liquefied using a liquid nitrogen heat exchanger. The liquid nitrogen heat exchanger consists of a cryogenic vessel, a liquid nitrogen coil and a mixed insulating medium coil. One end of the liquid nitrogen coil is connected to the liquid nitrogen storage tank, and the other end is empty ; Tube cooling mixed insulating medium coil. Both ends of the liquid nitrogen coil are respectively provided with a liquid inlet valve and an emptying valve, and both ends of the mixed insulating medium coil are respectively provided with an intake valve and a liquid outlet valve. The gas output of nitrogen cylinder and CF 4 gas cylinder is controlled by their respective pressure reducing valves, and the ratio of high-purity nitrogen gas and high-purity CF 4 gas is determined by weighing with electronic scale or measuring by gas chromatograph. The liquid outlet pipe of the mixed insulating medium is connected to the mixed insulating medium storage tank. The mixed insulating medium storage tank is a low temperature airtight container, and the top of the low temperature airtight container is equipped with a vacuum valve and a liquid inlet valve. First, the closed container is evacuated to a vacuum state below 0.1Pa through the vacuum unit, and then the mixed insulating medium flows into the insulating medium storage tank through the liquid inlet pipe.
方法二:Method Two:
利用液氮温区的制冷机对氮气瓶中的氮气和CF4气瓶中的CF4气体进行液化。液氮温区的制冷机由压缩机和冷头构成,通过制冷机冷头对氮气和CF4气体进行冷却。氮气瓶和CF4气瓶的出气量通过各自的减压阀门进行控制,高纯氮气和高纯CF4气的比例通过电子秤称重或气相色谱仪测量来确定。高纯氮气瓶和高纯CF4气瓶的气体通过出气管连接到混合绝缘介质储罐,混合绝缘介质储罐为低温密闭容器,低温密闭容器的顶部装有真空阀门和进气阀门;制冷机的冷头安装在混合绝缘介质储罐的顶部,首先通过真空机组将封闭容器抽真空至0.1Pa以下真空态,然后氮气和CF4气体通过进气管流入绝缘介质储罐中,由制冷机冷头冷凝后存储在储罐中。The nitrogen in the nitrogen cylinder and the CF 4 gas in the CF 4 cylinder are liquefied by using the refrigerator in the liquid nitrogen temperature zone. The refrigerator in the liquid nitrogen temperature zone is composed of a compressor and a cold head, and nitrogen and CF 4 gas are cooled by the cold head of the refrigerator. The gas output of nitrogen cylinder and CF 4 gas cylinder is controlled by their respective pressure reducing valves, and the ratio of high-purity nitrogen gas and high-purity CF 4 gas is determined by weighing with electronic scale or measuring by gas chromatograph. The gas of the high-purity nitrogen cylinder and the high-purity CF 4 gas cylinder is connected to the mixed insulating medium storage tank through the gas outlet pipe. The mixed insulating medium storage tank is a low-temperature airtight container, and the top of the low-temperature airtight container is equipped with a vacuum valve and an intake valve; a refrigerator; The cold head is installed on the top of the mixed insulating medium storage tank. First, the closed container is evacuated to a vacuum state below 0.1Pa through the vacuum unit, and then nitrogen gas and CF4 gas flow into the insulating medium storage tank through the intake pipe, and the cold head of the refrigerator Store in storage tanks after condensation.
本发明与其他方法相比,具有以下优点:Compared with other methods, the present invention has the following advantages:
(1)混合绝缘介质成本低,凝固点最低可达52K左右,且其绝缘能力比液氦液氖等低温液体耐压高很多,可方便用于55K-65K液氮以下温区超导电工装备的冷却,对于超导电工装备的小型化及降低成本具有重要意义。(1) The cost of the mixed insulating medium is low, the freezing point can be as low as about 52K, and its insulating capacity is much higher than that of low-temperature liquids such as liquid helium and liquid neon. Cooling is of great significance for the miniaturization and cost reduction of superconducting electrical equipment.
(2)混合绝缘介质的沸点最高可达145K左右,可方便用于90K-120K液化天然气温区电工设备的冷却,对于液化天然气温区电工设备的开发和推广具有重要意义。(2) The boiling point of the mixed insulating medium can reach up to about 145K, which can be easily used for the cooling of electrical equipment in the temperature range of 90K-120K liquefied natural gas, and is of great significance for the development and promotion of electrical equipment in the temperature range of liquefied natural gas.
附图说明Description of drawings
图1为N2和CF4的固液相平衡图;Fig. 1 is the solid-liquid phase equilibrium diagram of N 2 and CF 4 ;
图2为N2和CF4的气液相平衡图;Fig. 2 is the gas-liquid phase equilibrium diagram of N 2 and CF 4 ;
图3为YBCO超导带材临界电流随温度和磁场的变化曲线;Fig. 3 is the change curve of the critical current of YBCO superconducting tape with temperature and magnetic field;
图4为本发明具体实施例1利用液氮换热器进行混合绝缘介质配制方法的示意图;4 is a schematic diagram of a method for preparing a mixed insulating medium by utilizing a liquid nitrogen heat exchanger in
图5为本发明具体实施例2利用制冷机进行混合绝缘介质配制方法的示意图。FIG. 5 is a schematic diagram of a method for preparing a mixed insulating medium using a refrigerator according to
具体实施方式Detailed ways
下面结合附图和具体实施例进一步说明本发明。The present invention will be further described below with reference to the accompanying drawings and specific embodiments.
本发明混合绝缘介质采用的氮气和四氟化碳气体的纯度均大于等于99%。混合绝缘介质不同液氮和液化四氟化碳(CF4)比例的凝固点、泡点以及直流耐压参数如表1所示。本发明混合液体绝缘介质,不仅能够达到和液氮相当的绝缘强度,而且液化温度也能够满足55K-145K的工程应用要求。The purity of nitrogen gas and carbon tetrafluoride gas used in the mixed insulating medium of the present invention are both greater than or equal to 99%. Table 1 shows the freezing point, bubble point and DC withstand voltage parameters of the mixed insulating medium with different ratios of liquid nitrogen and liquefied carbon tetrafluoride (CF 4 ). The mixed liquid insulating medium of the invention can not only achieve the dielectric strength equivalent to that of liquid nitrogen, but also can meet the engineering application requirements of 55K-145K in liquefaction temperature.
实施例1Example 1
以90%摩尔比的液氮和10%摩尔比的液化CF4制备混合绝缘介质。采用液氮换热器方法对高纯氮气和高纯CF4进行液化。所制备的混合绝缘介质的凝固点为59K,常压泡点为78K,直流耐压大于10kV/mm。制备方法具体如下:The mixed insulating medium was prepared with 90% molar ratio of liquid nitrogen and 10 % molar ratio of liquefied CF4. The high-purity nitrogen and high-purity CF4 were liquefied by the liquid nitrogen heat exchanger method. The freezing point of the prepared mixed insulating medium is 59K, the bubble point at normal pressure is 78K, and the DC withstand voltage is greater than 10kV/mm. The preparation method is as follows:
利用液氮换热器对氮气瓶中的高纯氮气和CF4气瓶中的高纯CF4气体进行液化。通过液氮换热器的由低温容器、液氮盘管和混合绝缘介质盘管构成。液氮盘管的一端连接液氮储罐,另一端排空;混合绝缘介质盘管的一端连接高纯氮气瓶和高纯CF4气瓶,另一端连接混合绝缘介质储罐,通过液氮盘管对混合绝缘介质盘管进行冷却。液氮盘管两端设置进液阀和排空阀,混合绝缘介质盘管的两端设置进气阀和出液阀。通过高纯氮气瓶和高纯CF4气瓶的减压阀门控制出气量。通过电子秤称重或气相色谱仪测量确定高纯氮气和高纯CF4气的比例。混合绝缘介质的出液管连接到混合绝缘介质储罐,混合绝缘介质储罐为低温密闭容器,低温密闭容器的顶部有真空阀门和进液阀门。首先将封闭容器抽真空至0.1Pa以下,混合绝缘介质通过进液管流入绝缘介质储罐中。The high-purity nitrogen in the nitrogen cylinder and the high-purity CF 4 gas in the CF 4 cylinder are liquefied using a liquid nitrogen heat exchanger. The liquid nitrogen heat exchanger is composed of a cryogenic vessel, a liquid nitrogen coil and a mixed insulating medium coil. One end of the liquid nitrogen coil is connected to the liquid nitrogen storage tank, and the other end is empty ; The tube cools the mixed insulating medium coil. Both ends of the liquid nitrogen coil are provided with a liquid inlet valve and an emptying valve, and both ends of the mixed insulating medium coil are provided with an intake valve and a liquid outlet valve. The gas output is controlled by the pressure reducing valve of the high-purity nitrogen cylinder and the high-purity CF 4 gas cylinder. Determine the ratio of high-purity nitrogen gas and high - purity CF gas by weighing with electronic scale or measuring by gas chromatograph. The liquid outlet pipe of the mixed insulating medium is connected to the mixed insulating medium storage tank, and the mixed insulating medium storage tank is a low temperature airtight container, and the top of the low temperature airtight container is provided with a vacuum valve and a liquid inlet valve. First, the closed container is evacuated to below 0.1Pa, and the mixed insulating medium flows into the insulating medium storage tank through the liquid inlet pipe.
实施例2Example 2
以80%摩尔比的液氮和20%摩尔比的液化CF4制备混合绝缘介质。所制备的混合绝缘介质的凝固点为57K,常压泡点为78K,直流耐压大于10kV/mm。采用液氮温区的制冷机对高纯氮气和高纯CF4进行液化,具体如下:The mixed insulating medium was prepared with 80% molar ratio of liquid nitrogen and 20 % molar ratio of liquefied CF4. The prepared mixed insulating medium has a freezing point of 57K, a normal pressure bubble point of 78K, and a DC withstand voltage greater than 10kV/mm. The high-purity nitrogen and high-purity CF 4 are liquefied by a refrigerator in the liquid nitrogen temperature zone, as follows:
液氮温区的制冷机由压缩机和冷头构成,通过制冷机冷头对氮气和CF4气体进行冷却。高纯氮气瓶的减压阀和高纯CF4气瓶的减压阀门控制气瓶的出气量。高纯氮气和高纯CF4气的比例通过电子秤称重或气相色谱仪测量确定。高纯氮气瓶和高纯CF4气瓶的气体通过出气管连接到混合绝缘介质储罐。混合绝缘介质储罐为低温密闭容器,低温密闭容器的顶部有真空阀门和进气阀门。制冷机的冷头安装在混合绝缘介质储罐的顶部。首先将封闭容器抽真空至0.1Pa以下,氮气和CF4气体通过进气管流入绝缘介质储罐中,由制冷机冷头冷凝后存储在储罐中。The refrigerator in the liquid nitrogen temperature zone is composed of a compressor and a cold head, and nitrogen and CF 4 gas are cooled by the cold head of the refrigerator. The pressure reducing valve of the high-purity nitrogen cylinder and the pressure-reducing valve of the high-purity CF 4 cylinder control the gas output of the cylinder. The ratio of high-purity nitrogen and high-purity CF 4 gas is determined by weighing with an electronic scale or by gas chromatograph measurement. The gas of the high-purity nitrogen cylinder and the high-purity CF 4 cylinder is connected to the mixed insulating medium storage tank through the gas outlet pipe. The mixed insulating medium storage tank is a low temperature airtight container with a vacuum valve and an air inlet valve on the top of the low temperature airtight container. The cold head of the refrigerator is installed on the top of the mixed insulating medium storage tank. First, the closed container is evacuated to below 0.1Pa , nitrogen gas and CF4 gas flow into the insulating medium storage tank through the intake pipe, and are stored in the storage tank after being condensed by the cold head of the refrigerator.
实施例3Example 3
以60%摩尔比的液氮和40%摩尔比的液化CF4制备混合绝缘介质。所制备的混合绝缘介质的凝固点为54K,常压泡点为79K,直流耐压大于10kV/mm。采用液氮换热器法对高纯氮气和高纯CF4进行液化。The mixed insulating medium was prepared with 60% molar ratio of liquid nitrogen and 40 % molar ratio of liquefied CF4. The freezing point of the prepared mixed insulating medium is 54K, the normal pressure bubble point is 79K, and the DC withstand voltage is greater than 10kV/mm. The high-purity nitrogen and high-purity CF 4 were liquefied by the liquid nitrogen heat exchanger method.
实施例4Example 4
以50%摩尔比的液氮和50%摩尔比的液化CF4制备混合绝缘介质。所制备的混合绝缘介质的凝固点为58K,常压泡点为81K,直流耐压大于10kV/mm。采用液氮温区的制冷机方法对高纯氮气和高纯CF4进行液化。 The mixed insulating medium was prepared with 50% molar ratio of liquid nitrogen and 50% molar ratio of liquefied CF4. The freezing point of the prepared mixed insulating medium is 58K, the normal pressure bubble point is 81K, and the DC withstand voltage is greater than 10kV/mm. The high-purity nitrogen and high-purity CF 4 were liquefied by the refrigerator method in the liquid nitrogen temperature zone.
实施例5Example 5
以40%摩尔比的液氮和60%摩尔比的液化CF4制备混合绝缘介质。所制备的混合绝缘介质的凝固点为62K,常压泡点为82K,直流耐压大于10kV/mm。采用液氮换热器方法对高纯氮气和高纯CF4进行液化。The mixed insulating medium was prepared with 40 % molar ratio of liquid nitrogen and 60% molar ratio of liquefied CF4. The freezing point of the prepared mixed insulating medium is 62K, the normal pressure bubble point is 82K, and the DC withstand voltage is greater than 10kV/mm. The high-purity nitrogen and high-purity CF4 were liquefied by the liquid nitrogen heat exchanger method.
实施例6Example 6
以20%摩尔比的液氮和80%摩尔比的液化CF4制备混合绝缘介质。所制备的混合绝缘介质的凝固点为74K,常压泡点为89K,直流耐压大于10kV/mm。采用液氮温区的制冷机方法对高纯氮气和高纯CF4进行液化。The mixed insulating medium was prepared with 20 % molar ratio of liquid nitrogen and 80% molar ratio of liquefied CF4. The freezing point of the prepared mixed insulating medium is 74K, the normal pressure bubble point is 89K, and the DC withstand voltage is greater than 10kV/mm. The high-purity nitrogen and high-purity CF 4 were liquefied by the refrigerator method in the liquid nitrogen temperature zone.
实施例7Example 7
以10%摩尔比的液氮和90%摩尔比的液化CF4制备混合绝缘介质。所制备的混合绝缘介质的凝固点为81K,常压泡点为97K,直流耐压大于10kV/mm。采用液氮换热器对高纯氮气和高纯CF4进行液化。The mixed insulating medium was prepared with 10 % molar ratio of liquid nitrogen and 90% molar ratio of liquefied CF4. The freezing point of the prepared mixed insulating medium is 81K, the normal pressure bubble point is 97K, and the DC withstand voltage is greater than 10kV/mm. High-purity nitrogen and high-purity CF 4 are liquefied using a liquid nitrogen heat exchanger.
实施例8Example 8
以2%摩尔比的液氮和98%摩尔比的液化CF4制备混合绝缘介质。所制备出的混合绝缘介质的凝固点为89K,常压泡点为121K,直流耐压大于10kV/mm。采用液氮温区的制冷机方法对高纯氮气和高纯CF4进行液化。The mixed insulating medium was prepared with 2 mol% liquid nitrogen and 98 mol% liquefied CF4. The freezing point of the prepared mixed insulating medium is 89K, the normal pressure bubble point is 121K, and the DC withstand voltage is greater than 10kV/mm. The high-purity nitrogen and high-purity CF 4 were liquefied by the refrigerator method in the liquid nitrogen temperature zone.
表1Table 1
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