CN111359367A - SF (sulfur hexafluoride)6Gas micro-water treatment device - Google Patents
SF (sulfur hexafluoride)6Gas micro-water treatment device Download PDFInfo
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 39
- 229910018503 SF6 Inorganic materials 0.000 title 1
- SFZCNBIFKDRMGX-UHFFFAOYSA-N sulfur hexafluoride Chemical compound FS(F)(F)(F)(F)F SFZCNBIFKDRMGX-UHFFFAOYSA-N 0.000 title 1
- 229960000909 sulfur hexafluoride Drugs 0.000 title 1
- 238000001035 drying Methods 0.000 claims abstract description 38
- 230000006835 compression Effects 0.000 claims abstract description 16
- 238000007906 compression Methods 0.000 claims abstract description 16
- 238000001914 filtration Methods 0.000 claims abstract description 15
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 13
- 238000001179 sorption measurement Methods 0.000 claims description 33
- 230000008929 regeneration Effects 0.000 claims description 23
- 238000011069 regeneration method Methods 0.000 claims description 23
- 238000006243 chemical reaction Methods 0.000 claims description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 238000012545 processing Methods 0.000 claims description 7
- 230000003472 neutralizing effect Effects 0.000 claims description 3
- 210000003437 trachea Anatomy 0.000 claims description 2
- 239000003513 alkali Substances 0.000 claims 1
- 239000003607 modifier Substances 0.000 claims 1
- 238000005516 engineering process Methods 0.000 abstract description 6
- 125000004122 cyclic group Chemical group 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 8
- 238000000034 method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- XGCDHPDIERKJPT-UHFFFAOYSA-N [F].[S] Chemical class [F].[S] XGCDHPDIERKJPT-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/302—Sulfur oxides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
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- B01D2257/304—Hydrogen sulfide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
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Abstract
本发明提供了一种SF6气体微水处理装置,包括通过气管依次串联的第一接头、第一水分测量仪、第一压力表、手动阀、气体流量计、过滤机构、干燥机构、气体压缩单元和第二接头。本发明提供了一种SF6气体微水处理装置,通过设置串联结构实现对SF6气体中水分和分解物的循环处理,不仅能够保证设备中SF6气体始终处在稳定的范围中,更好地保护设备中的电路,而且还能够长期与设备连接实现实时处理,水分和分解物随时处理,避免了现有技术处理滞后带来的风险隐患。
The invention provides an SF 6 gas micro-water treatment device, comprising a first joint connected in series through a gas pipe, a first moisture measuring instrument, a first pressure gauge, a manual valve, a gas flow meter, a filtering mechanism, a drying mechanism, and a gas compression mechanism. unit and second connector. The invention provides an SF 6 gas micro-water treatment device, which can realize the cyclic treatment of moisture and decomposition products in SF 6 gas by setting up a series structure, which can not only ensure that the SF 6 gas in the equipment is always in a stable range, but also better It can protect the circuit in the equipment, and can also be connected with the equipment for a long time to realize real-time treatment, and the moisture and decomposition products can be treated at any time, avoiding the hidden risks caused by the lag in the treatment of the existing technology.
Description
技术领域technical field
本发明属于电气设备领域,具体涉及一种SF6气体微水处理装置。The invention belongs to the field of electrical equipment, in particular to an SF 6 gas micro-water treatment device.
背景技术Background technique
SF6气体是一种稳定的惰性化合物,具有极好的绝缘和灭弧性能,广泛应用于电力系统设备中。SF 6 gas is a stable inert compound with excellent insulating and arc extinguishing properties, and is widely used in power system equipment.
SF6气体中含有空气、水分等杂质,在一定条件下,如电弧、火花放电,被电解产生的氟硫化合物与水反应可以生成腐蚀性很强的化学物质,其中包含SO2和H2S,会腐蚀金属部件与绝缘材料,缩短设备使用寿命,影响SF6气体纯度及其电气性能。而且水分过量会凝结在固体介质表面,在设备运行后发生闪络,严重时甚至会造成爆炸。因此,微水试验作为SF6电器设备的必试项目,已广泛受到重视。SF 6 gas contains impurities such as air and moisture. Under certain conditions, such as arc and spark discharge, the fluorine-sulfur compounds produced by electrolysis can react with water to form highly corrosive chemicals, including SO 2 and H 2 S. , it will corrode metal parts and insulating materials, shorten the service life of equipment, and affect the purity of SF 6 gas and its electrical properties. Moreover, excessive moisture will condense on the surface of the solid medium, and flashover will occur after the equipment is running, and even an explosion may occur in severe cases. Therefore, the micro-water test, as a must-test item for SF 6 electrical equipment, has been widely paid attention to.
公开号为CN106000022B的中国专利提供了一种通过对SF6电气设备气室的气体进行循环干燥以及分解物过滤,从而使得SF6电气设备能够进行不停电检修的SF6电气设备在线微水处理方法及其处理装置,但是该装置进出气共用一个接头,这就使得从设备抽取SF6气体和回充SF6气体过程只能单独进行,不能进行循环处理,在抽取SF6气体进行处理的过程中,势必会导致设备中的SF6气体产生压力下降,导致绝缘和灭弧效果降低,不利于设备的长期运行,因此在实际生产中,SF6气体微水干燥处理为定期进行,或是设备中微水指标达到一定程度时进行,并非实时进行,具有滞后性,设备中不可避免地存在微量SO2和H2S,若腐蚀设备中的电路,造成损失则是巨大的。The Chinese patent with the publication number CN106000022B provides an on-line micro-water treatment method for SF 6 electrical equipment, which enables the SF 6 electrical equipment to perform non-stop maintenance by circulating and drying the gas in the gas chamber of the SF 6 electrical equipment and filtering the decomposed products. and its processing device, but the inlet and outlet of the device share a joint, which makes the process of extracting SF 6 gas from the equipment and backfilling SF 6 gas only carried out separately, and cannot be recycled. In the process of extracting SF 6 gas for processing , it will inevitably lead to the pressure drop of SF 6 gas in the equipment, resulting in the reduction of insulation and arc extinguishing effect, which is not conducive to the long - term operation of the equipment. When the micro water index reaches a certain level, it is not carried out in real time and has a hysteresis. There are inevitably traces of SO 2 and H 2 S in the equipment. If the circuit in the equipment is corroded, the loss will be huge.
发明内容SUMMARY OF THE INVENTION
为解决上述技术问题,本发明提供了一种SF6气体微水处理装置,通过设置串联结构实现对SF6气体中水分和分解物的循环处理,不仅能够保证设备中SF6气体始终处在稳定的范围中,更好地保护设备中的电路,而且还能够长期与设备连接实现实时处理,水分和分解物随时处理,避免了现有技术处理滞后带来的风险隐患。In order to solve the above technical problems, the present invention provides a SF 6 gas micro-water treatment device, which can realize the cyclic treatment of moisture and decomposition products in SF 6 gas by setting up a series structure, which can not only ensure that the SF 6 gas in the equipment is always in a stable state. It can better protect the circuits in the equipment, and it can also be connected with the equipment for a long time to realize real-time treatment, and the moisture and decomposition products can be treated at any time, avoiding the hidden risks caused by the lag of the existing technology.
本发明通过以下技术方案得以实现:The present invention is achieved through the following technical solutions:
一种SF6气体微水处理装置,包括通过气管依次串联的第一接头、第一水分测量仪、第一压力表、手动阀、气体流量计、过滤机构、干燥机构、气体压缩单元和第二接头,设置双接头串联结构实现对设备中的微水和分解物进行循环处理,通过过滤机构吸附SF6气体产生的分解物,干燥机构过滤水分,不仅能够保证设备中SF6气体始终处在稳定的范围中,更好地保护设备中的电路,而且还能够长期与设备连接实现实时处理,水分和分解物随时处理,避免了现有技术处理滞后带来的风险隐患。An SF 6 gas micro-water treatment device, comprising a first joint connected in series through a gas pipe, a first moisture measuring instrument, a first pressure gauge, a manual valve, a gas flow meter, a filtering mechanism, a drying mechanism, a gas compression unit and a second Joints, set up a double-joint series structure to realize the circulatory treatment of micro water and decomposed products in the equipment, adsorb the decomposed products generated by SF 6 gas through the filtering mechanism, and filter the moisture by the drying mechanism, which can not only ensure that the SF 6 gas in the equipment is always in a stable state It can better protect the circuits in the equipment, and it can also be connected with the equipment for a long time to realize real-time treatment, and the moisture and decomposition products can be treated at any time, avoiding the hidden risks caused by the lag of the existing technology.
所述第一接头和第二接头分别连接在电力系统设备的两端,使得设备中的气体形成循环流动,设备中各处的SF6气体能够得到充分的处理,进一步提高SF6气体微水处理的效果。The first joint and the second joint are respectively connected to the two ends of the power system equipment, so that the gas in the equipment forms a circulating flow, and the SF 6 gas in the equipment can be fully treated, which further improves the SF 6 gas micro-water treatment. Effect.
所述过滤机构包括第一电磁阀和固定床吸附反应装置,气体流量计、第一电磁阀、固定床吸附反应装置和干燥机构通过气管依次串联,固定床吸附反应装置中设置有用来中和并吸附SF6气体分解物的碱改性活性炭,能够过滤掉SF6气体中SO2和H2S等分解物,第一电磁阀用来控制气路的通断,切断气路时,便于更换活性炭。The filtering mechanism includes a first solenoid valve and a fixed bed adsorption reaction device. The gas flow meter, the first solenoid valve, the fixed bed adsorption reaction device and the drying mechanism are connected in series through a gas pipe. The fixed bed adsorption reaction device is provided with a device for neutralizing and drying. The alkali-modified activated carbon that adsorbs the decomposition products of SF 6 gas can filter out the decomposition products such as SO 2 and H 2 S in the SF 6 gas. The first solenoid valve is used to control the on-off of the gas circuit. When the gas circuit is cut off, it is easy to replace the activated carbon. .
所述干燥机构包括通过气管依次首尾相连的伴热式吸附再生单元、气体储存单元和气体循环动力单元,并且过滤机构、伴热式吸附再生单元、气体储存单元、气体压缩单元通过气管依次串联,伴热式吸附再生单元能够将抽取的SF6气体中的水分进行吸收,再通过加热将这些水分释放到外环境中,能够反复使用;气体储存单元对干燥后的SF6气体中水气含量进行监控,不达标则通过气体循环动力单元送回伴热式吸附再生单元再次干燥,直至SF6气体中水气含量达标后送入下道环节。The drying mechanism comprises a heat tracing adsorption regeneration unit, a gas storage unit and a gas circulation power unit which are connected end to end in sequence through a gas pipe, and the filter mechanism, the heat tracing adsorption regeneration unit, the gas storage unit and the gas compression unit are connected in series through the gas pipe in sequence, The heat tracing adsorption regeneration unit can absorb the moisture in the extracted SF 6 gas, and then release the moisture into the external environment through heating, which can be used repeatedly ; If it does not meet the standard, it will be sent back to the heat tracing adsorption regeneration unit through the gas circulation power unit to be dried again until the water vapor content in the SF 6 gas reaches the standard and then sent to the next link.
所述气体储存单元包括气缸、第二水分测量仪和第二压力表,第二水分测量仪和第二压力表通过气管与气缸相连,第二水分测量仪对干燥后的SF6气体进行监控,保证干燥后送入设备中的SF6气体的水气含量达标,第二压力表保证抽入进行干燥处理的SF6气压与设备中SF6气压相当,避免出现抽取过多引起设备中SF6气压偏低,更好地维持设备中的SF6气压始终处于最佳的范围内。The gas storage unit comprises a cylinder, a second moisture measuring instrument and a second pressure gauge, the second moisture measuring instrument and the second pressure gauge are connected to the cylinder through a gas pipe, and the second moisture measuring instrument monitors the dried SF gas, Ensure that the moisture content of the SF 6 gas fed into the equipment after drying is up to standard, and the second pressure gauge ensures that the SF 6 gas pressure pumped for drying treatment is equivalent to the SF 6 gas pressure in the equipment, so as to avoid the SF 6 gas pressure in the equipment caused by excessive extraction Lower, to better maintain the SF 6 air pressure in the equipment is always in the optimal range.
所述气体循环动力单元包括气泵和气泵两端连接的第三电磁阀和第四电磁阀,通常第三电磁阀和第四电磁阀处于关闭状态,当经过伴热式吸附再生单元干燥的SF6气体中水气含量不达标时,第三电磁阀和第四电磁阀打开,气泵将水气含量检测不达标的SF6气体送回伴热式吸附再生单元再次干燥。The gas circulation power unit includes an air pump and a third solenoid valve and a fourth solenoid valve connected to both ends of the air pump. Usually, the third solenoid valve and the fourth solenoid valve are in a closed state. When the SF 6 dried by the heat tracing adsorption regeneration unit When the moisture content in the gas does not meet the standard, the third solenoid valve and the fourth solenoid valve are opened, and the air pump sends the SF 6 gas whose moisture content does not meet the standard to the heat tracing adsorption regeneration unit to be dried again.
所述气体压缩单元包括气体驱动器和气体驱动器两端连接的第五电磁阀和第六电磁阀,当经过伴热式吸附再生单元干燥的SF6气体中水气含量达标时,第五电磁阀和第六电磁阀打开,气体驱动器将干燥合格的SF6气体送回设备中。The gas compression unit includes a gas driver and a fifth solenoid valve and a sixth solenoid valve connected at both ends of the gas driver. When the moisture content in the SF 6 gas dried by the heat tracing adsorption regeneration unit reaches the standard, the fifth solenoid valve and the sixth solenoid valve reach the standard. The sixth solenoid valve opens, and the gas driver sends the dry and qualified SF 6 gas back to the equipment.
所述第一接头和第二接头均为快速插拔接口,便于连接操作。Both the first connector and the second connector are quick-plug interfaces, which are convenient for connection operation.
与上述方案不同,所述干燥机构还包括第二电磁阀,第二电磁阀设置在过滤机构与伴热式吸附再生单元之间,便于在补充SF6气体时控制气路通断。Different from the above solution, the drying mechanism further includes a second solenoid valve, which is arranged between the filter mechanism and the heat tracing adsorption and regeneration unit, so as to control the on-off of the gas path when SF 6 gas is supplemented.
所述第二电磁阀与伴热式吸附再生单元之间还通过三通连接有单向输入气路,单向输入气路上设置有第一单向阀实现气源向所述处理装置中单向输入气体,当第一压力表监测到SF6气压偏低时,关闭第二电磁阀,SF6气源通过单向输入气路向干燥机构充入SF6气体,经过干燥达标后,补充到设备中,进一步保证设备中的SF6气压始终处于最佳的范围内。A one-way input gas path is also connected between the second solenoid valve and the heat tracing adsorption regeneration unit through a three-way, and a first one-way valve is arranged on the one-way input gas path to realize one-way flow of the gas source to the processing device. Input gas, when the first pressure gauge detects that the air pressure of SF 6 is low, close the second solenoid valve, and the SF 6 gas source fills the drying mechanism with SF 6 gas through the one-way input gas path. After drying up to the standard, it is added to the equipment , to further ensure that the SF 6 air pressure in the equipment is always in the best range.
所述气体压缩单元和第二接头之间还设置有防止设备中SF6气体通过第二接头向微水处理装置回流的第二单向阀,保证设备与微水处理装置之间形成单向循环,进而保证过滤和干燥的效果。There is also a second one - way valve between the gas compression unit and the second joint to prevent the SF gas in the equipment from flowing back to the micro-water treatment device through the second joint, so as to ensure that a one-way circulation is formed between the equipment and the micro-water treatment device. , thereby ensuring the effect of filtration and drying.
与上述方案不同,又一方案中还包括溢流阀,溢流阀通过三通连接在过滤机构与第二电磁阀之间,当SF6气源充入气体过多导致设备内SF6气压过高时,能够通过溢流阀排除多余的气体,实现气压动态平衡,更进一步保证设备中的SF6气压始终处于最佳的范围内,同时排放的SF6气体经过过滤,避免了对环境的污染。Different from the above scheme, another scheme also includes an overflow valve, which is connected between the filter mechanism and the second solenoid valve through a three - way connection. When it is high, excess gas can be removed through the overflow valve to achieve dynamic balance of air pressure, which further ensures that the SF 6 air pressure in the equipment is always in the best range, and the discharged SF 6 gas is filtered to avoid environmental pollution. .
本发明的有益效果在于:The beneficial effects of the present invention are:
与现有技术相比,通过设置双接头串联结构实现对设备中的微水和分解物进行循环处理,通过过滤机构吸附SF6气体产生的分解物,干燥机构过滤水分,不仅能够保证设备中SF6气体始终处在稳定的范围中,更好地保护设备中的电路,而且还能够长期与设备连接实现实时处理,水分和分解物随时处理,避免了现有技术处理滞后带来的风险隐患。通过设置第一压力表和第二压力表,保证每次干燥过程抽取的SF6气体量,更好地维持设备中的SF6气压始终处于最佳的范围内。通过在干燥机构前设置单向输入气路,在设备中SF6气压偏低时,SF6气源通过单向输入气路向干燥机构充入SF6气体,经过干燥达标后,补充到设备中,进一步保证设备中的SF6气压始终处于最佳的范围内。通过在气体压缩单元和第二接头之间设置单向阀,保证设备与微水处理装置之间形成单向循环,进而保证过滤和干燥的效果。通过在过滤机构与第二电磁阀之间设置溢流阀,实现气压动态平衡,更进一步保证设备中的SF6气压始终处于最佳的范围内,同时排放的SF6气体经过过滤,避免了对环境的污染。Compared with the prior art, by setting up a double-joint series structure to realize the circulatory treatment of micro - water and decomposed products in the equipment, the decomposed products generated by SF gas are adsorbed by the filtering mechanism, and the drying mechanism filters the moisture, which can not only ensure the SF in the equipment. 6. The gas is always in a stable range, which better protects the circuits in the equipment, and can also be connected to the equipment for a long time to realize real-time treatment, and the moisture and decomposition products can be treated at any time, avoiding the hidden risks caused by the lag of the existing technology. By setting the first pressure gauge and the second pressure gauge, the amount of SF 6 gas extracted in each drying process can be ensured, and the SF 6 gas pressure in the equipment can be better maintained within the optimal range. By setting a one-way input gas circuit in front of the drying mechanism, when the SF 6 gas pressure in the equipment is low, the SF 6 gas source fills the drying mechanism with SF 6 gas through the one-way input gas path. Further ensure that the SF 6 air pressure in the equipment is always in the optimal range. By arranging a one-way valve between the gas compression unit and the second joint, it is ensured that a one-way circulation is formed between the equipment and the micro-water treatment device, thereby ensuring the effect of filtration and drying. By setting an overflow valve between the filter mechanism and the second solenoid valve, the dynamic balance of air pressure is realized, which further ensures that the SF 6 air pressure in the equipment is always in the best range, and the discharged SF 6 gas is filtered, avoiding the need for air pressure. pollution of the environment.
附图说明Description of drawings
图1是本发明实施例一的结构示意图;1 is a schematic structural diagram of Embodiment 1 of the present invention;
图2是本发明实施例二的结构示意图;2 is a schematic structural diagram of
图3是本发明实施例三的结构示意图。FIG. 3 is a schematic structural diagram of
图中:1-第一接头,2-第一水分测量仪,3-第一压力表,4-手动阀,5-气体流量计,6-第一电磁阀,7-固定床吸附反应装置,8-第二电磁阀,9-伴热式吸附再生单元,10-气体储存单元,11-气体循环动力单元,12-气体压缩单元,13-气缸,14-第二水分测量仪,15-第二压力表,16-气泵,17-第三电磁阀,18-第四电磁阀,19-气体驱动器,20-第五电磁阀,21-第六电磁阀,22-第二接头,23-单向输入气路,24-第一单向阀,25-第三接头,26-第二单向阀,27-溢流阀。In the figure: 1-first joint, 2-first moisture measuring instrument, 3-first pressure gauge, 4-manual valve, 5-gas flow meter, 6-first solenoid valve, 7-fixed bed adsorption reaction device, 8-Second solenoid valve, 9-Heat tracing adsorption regeneration unit, 10-Gas storage unit, 11-Gas circulation power unit, 12-Gas compression unit, 13-Cylinder, 14-Second moisture measuring instrument, 15-No. Two pressure gauges, 16-air pump, 17-third solenoid valve, 18-fourth solenoid valve, 19-gas driver, 20-fifth solenoid valve, 21-sixth solenoid valve, 22-second connector, 23-single To the input gas path, 24-the first one-way valve, 25-the third joint, 26-the second one-way valve, 27-relief valve.
具体实施方式Detailed ways
下面进一步描述本发明的技术方案,但要求保护的范围并不局限于所述。The technical solutions of the present invention are further described below, but the claimed scope is not limited to the description.
实施例一Example 1
如图1所示,一种SF6气体微水处理装置,包括通过气管依次串联的第一接头1、第一水分测量仪2、第一压力表3、手动阀4、气体流量计5、过滤机构、干燥机构、气体压缩单元12和第二接头22,设置双接头串联结构实现对设备中的微水和分解物进行循环处理,通过过滤机构吸附SF6气体产生的分解物,干燥机构过滤水分,不仅能够保证设备中SF6气体始终处在稳定的范围中,更好地保护设备中的电路,而且还能够长期与设备连接实现实时处理,水分和分解物随时处理,避免了现有技术处理滞后带来的风险隐患。As shown in Fig. 1, a SF 6 gas micro-water treatment device includes a first joint 1, a first
所述第一接头1和第二接头22分别连接在电力系统设备的两端,使得设备中的气体形成循环流动,设备中各处的SF6气体能够得到充分的处理,进一步提高SF6气体微水处理的效果。The first joint 1 and the second joint 22 are respectively connected to the two ends of the power system equipment, so that the gas in the equipment forms a circulating flow, and the SF 6 gas everywhere in the equipment can be fully treated, which further improves the SF 6 gas microscopicity. effect of water treatment.
所述过滤机构包括第一电磁阀6和固定床吸附反应装置7,气体流量计5、第一电磁阀6、固定床吸附反应装置7和干燥机构通过气管依次串联,固定床吸附反应装置7中设置有用来中和并吸附SF6气体分解物的碱改性活性炭,能够过滤掉SF6气体中SO2和H2S等分解物,第一电磁阀6用来控制气路的通断,切断气路时,便于更换活性炭。The filtering mechanism includes a
所述干燥机构包括通过气管依次首尾相连的伴热式吸附再生单元9、气体储存单元10和气体循环动力单元11,并且过滤机构、伴热式吸附再生单元9、气体储存单元10、气体压缩单元12通过气管依次串联,伴热式吸附再生单元9能够将抽取的SF6气体中的水分进行吸收,再通过加热将这些水分释放到外环境中,能够反复使用;气体储存单元10对干燥后的SF6气体中水气含量进行监控,不达标则通过气体循环动力单元11送回伴热式吸附再生单元9再次干燥,直至SF6气体中水气含量达标后送入下道环节。The drying mechanism includes a heat tracing adsorption and
所述气体储存单元10包括气缸13、第二水分测量仪14和第二压力表15,第二水分测量仪14和第二压力表15通过气管与气缸相连,第二水分测量仪14对干燥后的SF6气体进行监控,保证干燥后送入设备中的SF6气体的水气含量达标,第二压力表15保证抽入进行干燥处理的SF6气压与设备中SF6气压相当,避免出现抽取过多引起设备中SF6气压偏低,更好地维持设备中的SF6气压始终处于最佳的范围内。The
所述气体循环动力单元11包括气泵16和气泵16两端连接的第三电磁阀17和第四电磁阀18,通常第三电磁阀17和第四电磁阀18处于关闭状态,当经过伴热式吸附再生单元9干燥的SF6气体中水气含量不达标时,第三电磁阀17和第四电磁阀18打开,气泵16将水气含量检测不达标的SF6气体送回伴热式吸附再生单元9再次干燥。The gas
所述气体压缩单元12包括气体驱动器19和气体驱动器19两端连接的第五电磁阀20和第六电磁阀21,当经过伴热式吸附再生单元9干燥的SF6气体中水气含量达标时,第五电磁阀20和第六电磁阀21打开,气体驱动器19将干燥合格的SF6气体送回设备中。The
所述第一接头1和第二接头22均为快速插拔接口,便于连接操作。The first connector 1 and the
实施例二
如图2所示,在实施例一的结构基础上,作出如下改进:As shown in Figure 2, on the basis of the structure of the first embodiment, the following improvements are made:
所述干燥机构还包括第二电磁阀8,第二电磁阀8设置在过滤机构与伴热式吸附再生单元9之间,便于在补充SF6气体时控制气路通断。The drying mechanism also includes a
所述第二电磁阀8与伴热式吸附再生单元9之间还通过三通连接有单向输入气路23,单向输入气路23上设置有第一单向阀24,实现气源向所述处理装置中单向输入气体,单向输入气路23端部设置有第三接头25,当第一压力表3监测到SF6气压偏低时,关闭第二电磁阀8,SF6气源通过单向输入气路23向干燥机构充入SF6气体,经过干燥达标后,补充到设备中,进一步保证设备中的SF6气压始终处于最佳的范围内。A one-way
所述气体压缩单元12和第二接头22之间还设置有防止设备中SF6气体通过第二接头22向微水处理装置回流的第二单向阀26,保证设备与微水处理装置之间形成单向循环,进而保证过滤和干燥的效果。A
现有技术中,因密封无法做到绝对,总会存在泄漏,电力系统设备考虑气压泄漏,只设置有一个接口,来降低泄漏的影响;而本发明通过实时监控并补气,实现气压的动态平衡,设备不必再考虑增加接口对泄漏的影响,设备能容易地进行改造增加一个接口,配合本发明所提供的微水处理装置,更好地保护设备中的电气电路。In the prior art, since the seal cannot be absolute, there will always be leakage. The power system equipment considers air pressure leakage and only has one interface to reduce the impact of leakage. The present invention realizes dynamic air pressure by monitoring and replenishing air in real time. Balance, the equipment does not need to consider the effect of adding an interface on leakage, the equipment can be easily modified to add an interface, and the micro water treatment device provided by the present invention can better protect the electrical circuit in the equipment.
实施例三
如图3所示,在实施例二的结构基础上,作出如下改进:As shown in Figure 3, on the basis of the structure of the second embodiment, the following improvements are made:
还包括溢流阀27,溢流阀27通过三通连接在过滤机构与第二电磁阀8之间,当SF6气源充入气体过多导致设备内SF6气压过高时,能够通过溢流阀27排除多余的气体,实现气压动态平衡,更进一步保证设备中的SF6气压始终处于最佳的范围内,同时排放的SF6气体经过过滤,避免了对环境的污染。It also includes an
本发明提供的一种SF6气体微水处理装置,通过设置双接头串联结构实现对设备中的微水和分解物进行循环处理,通过过滤机构吸附SF6气体产生的分解物,干燥机构过滤水分,不仅能够保证设备中SF6气体始终处在稳定的范围中,更好地保护设备中的电路,而且还能够长期与设备连接实现实时处理,水分和分解物随时处理,避免了现有技术处理滞后带来的风险隐患。通过设置第一压力表和第二压力表,保证每次干燥过程抽取的SF6气体量,更好地维持设备中的SF6气压始终处于最佳的范围内。通过在干燥机构前设置单向输入气路,在设备中SF6气压偏低时,SF6气源通过单向输入气路向干燥机构充入SF6气体,经过干燥达标后,补充到设备中,进一步保证设备中的SF6气压始终处于最佳的范围内。通过在气体压缩单元和第二接头之间设置单向阀,保证设备与微水处理装置之间形成单向循环,进而保证过滤和干燥的效果。通过在过滤机构与第二电磁阀之间设置溢流阀,实现气压动态平衡,更进一步保证设备中的SF6气压始终处于最佳的范围内,同时排放的SF6气体经过过滤,避免了对环境的污染。The invention provides a SF 6 gas micro-water treatment device, which realizes the circulatory treatment of micro-water and decomposed products in the device by setting up a double-joint series structure, adsorbs the decomposed products generated by SF 6 gas through a filtering mechanism, and filters the moisture through a drying mechanism. , not only can ensure that the SF 6 gas in the equipment is always in a stable range, better protect the circuit in the equipment, but also can be connected to the equipment for a long time to achieve real-time processing, moisture and decomposition products can be processed at any time, avoiding the existing technology. Risks caused by lag. By setting the first pressure gauge and the second pressure gauge, the amount of SF 6 gas extracted in each drying process can be ensured, and the SF 6 gas pressure in the equipment can be better maintained within the optimal range. By setting a one-way input gas circuit in front of the drying mechanism, when the SF 6 gas pressure in the equipment is low, the SF 6 gas source fills the drying mechanism with SF 6 gas through the one-way input gas path. Further ensure that the SF 6 air pressure in the equipment is always in the optimal range. By arranging a one-way valve between the gas compression unit and the second joint, it is ensured that a one-way circulation is formed between the equipment and the micro-water treatment device, thereby ensuring the effect of filtration and drying. By setting an overflow valve between the filter mechanism and the second solenoid valve, the dynamic balance of air pressure is realized, which further ensures that the SF 6 air pressure in the equipment is always in the best range, and the discharged SF 6 gas is filtered, avoiding the need for air pressure. pollution of the environment.
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山西省电力工业局: "《电气设备运行》", 31 October 1997, 中国电力出版社 * |
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