CN107362661A - A kind of gas cleaning plant and its application - Google Patents
A kind of gas cleaning plant and its application Download PDFInfo
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- CN107362661A CN107362661A CN201710827383.3A CN201710827383A CN107362661A CN 107362661 A CN107362661 A CN 107362661A CN 201710827383 A CN201710827383 A CN 201710827383A CN 107362661 A CN107362661 A CN 107362661A
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- 238000004140 cleaning Methods 0.000 title claims 13
- 238000000746 purification Methods 0.000 claims abstract description 130
- 239000007789 gas Substances 0.000 claims abstract description 128
- 239000001301 oxygen Substances 0.000 claims abstract description 37
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 37
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 36
- 238000010438 heat treatment Methods 0.000 claims abstract description 33
- 230000001681 protective effect Effects 0.000 claims abstract description 25
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000000956 alloy Substances 0.000 claims abstract description 19
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 19
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 14
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052802 copper Inorganic materials 0.000 claims abstract description 14
- 239000010949 copper Substances 0.000 claims abstract description 14
- 239000010936 titanium Substances 0.000 claims abstract description 14
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000011733 molybdenum Substances 0.000 claims abstract description 9
- 229910052750 molybdenum Inorganic materials 0.000 claims abstract description 9
- 238000002474 experimental method Methods 0.000 claims abstract description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 16
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 14
- 239000000523 sample Substances 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 238000012360 testing method Methods 0.000 claims description 8
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 7
- 229910052786 argon Inorganic materials 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 6
- 239000000741 silica gel Substances 0.000 claims description 6
- 229910002027 silica gel Inorganic materials 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- 238000007254 oxidation reaction Methods 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 3
- 229910000906 Bronze Inorganic materials 0.000 claims 2
- 230000001590 oxidative effect Effects 0.000 claims 1
- 238000006392 deoxygenation reaction Methods 0.000 abstract description 35
- 239000003795 chemical substances by application Substances 0.000 abstract description 16
- 238000007791 dehumidification Methods 0.000 abstract description 14
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000011825 aerospace material Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000004643 material aging Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000012629 purifying agent Substances 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
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- 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
- B01D53/261—Drying gases or vapours by adsorption
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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
- B01D53/28—Selection of materials for use as drying agents
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- 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
- B01D53/30—Controlling by gas-analysis apparatus
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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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
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- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
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- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/81—Solid phase processes
- B01D53/82—Solid phase processes with stationary reactants
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/10—Oxidants
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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
- B01D2253/106—Silica or silicates
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D2257/104—Oxygen
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Abstract
本发明公开了一种气体净化装置及其应用,包括通过管道串联连接的除湿净化室、第一脱氧净化室、第二脱氧净化室和第三脱氧净化室,除湿净化室的入口与保护气体的气瓶连接;除湿净化室内部填装有硅胶除湿剂,第一脱氧净化室内部填装铜单质或铜基合金中的一种作为脱氧净化剂,第二脱氧净化室内部填装钼单质或钼基合金中的一种作为脱氧净化剂,第三脱氧净化室内部填装钛单质、海绵钛或钛基合金中的一种作为脱氧净化剂;第一脱氧净化室、第二脱氧净化室和第三脱氧净化室分别设有加热单元。本发明可对气体中的水蒸气和氧气进行吸附脱除,可以满足实验和生产中对于气氛环境的各项要求,并且具有操作简单、净化速度快、净化剂使用寿命长、成本低的特点。
The invention discloses a gas purification device and its application, comprising a dehumidification purification room, a first deoxygenation purification room, a second deoxygenation purification room and a third deoxygenation purification room connected in series through pipelines, the entrance of the dehumidification purification room and the protective gas The gas cylinder is connected; the dehumidification and purification chamber is filled with silica gel desiccant, the interior of the first deoxidation purification chamber is filled with copper element or copper-based alloy as a deoxidation purifier, and the interior of the second deoxidation purification chamber is filled with molybdenum element or molybdenum One of the base alloys is used as a deoxidation purification agent, and the third deoxidization purification chamber is filled with titanium element, sponge titanium or titanium-based alloy as a deoxidation purification agent; the first deoxidation purification chamber, the second deoxidation purification chamber and the second The three deoxygenation purification chambers are respectively equipped with heating units. The invention can absorb and remove water vapor and oxygen in the gas, can meet various requirements for the atmosphere environment in experiments and production, and has the characteristics of simple operation, fast purification speed, long service life of the purification agent and low cost.
Description
技术领域technical field
本发明涉及一种气体净化装置及其应用,属于化学反应净化气体技术领域。The invention relates to a gas purification device and its application, belonging to the technical field of chemical reaction gas purification.
背景技术Background technique
保护气制备方面、特别是在超大规模集成电路、激光材料、光导纤维和航空航天材料等航域,要求生产过程在超净环境体系内进行,例如半导体制造工艺要求把气体中的氧降低到10-6ppm,甚至10-15~10-23ppm,这就要求采用合适的脱氧剂将氧脱除以达到要求。In terms of protective gas preparation, especially in the fields of ultra-large-scale integrated circuits, laser materials, optical fibers, and aerospace materials, the production process is required to be carried out in an ultra-clean environment system. For example, the semiconductor manufacturing process requires that the oxygen in the gas be reduced to 10 -6 ppm, or even 10 -15 ~ 10 -23 ppm, which requires the use of a suitable deoxidizer to remove oxygen to meet the requirements.
因此,在工厂的产品生产过程中或者实验室的实验过程中,有较多过程需要在气氛保护后才能进行。保护性气氛的衡量标准主要包括气氛的湿度和气氛的含氧量。例如,在钢铁的生产过程中,氧元素的存在降低了钢的热脆性能的同时,显著降低了钢液的表面张力。也就证明了氧含量对于钢产品的质量有很大影响。又如,在电子产品的生产过程中,气体湿度过大会引起通路、漏电、击穿及材料老化等问题。因此,控制气氛的湿度及氧含量对于各种产品的生产有着重要意义。而目前为止,这种气体净化装置还比较少。Therefore, in the process of product production in the factory or in the experimental process of the laboratory, many processes need to be carried out after the atmosphere is protected. The measuring standard of protective atmosphere mainly includes the humidity of the atmosphere and the oxygen content of the atmosphere. For example, in the production process of steel, the presence of oxygen reduces the hot brittleness of steel and significantly reduces the surface tension of molten steel. It also proves that the oxygen content has a great influence on the quality of steel products. Another example is that in the production process of electronic products, excessive gas humidity will cause problems such as pathways, leakage, breakdown, and material aging. Therefore, controlling the humidity and oxygen content of the atmosphere is of great significance for the production of various products. And so far, there are relatively few such gas purification devices.
公开号为CN104694705A的中国专利文件中公开了一种深度脱氧装置及其应用,气体经过加热装置加热到一定温度后通过铜、镁、钛三种脱氧剂达到脱氧目的,可以在常压下进行脱氧处理,精度可以达到10-21ppm。然而,这个装置并不能控制气体的湿度,也不能实现气体在不同温度下与不同的脱氧剂进行接触,因此也就影响了此装置的脱氧效率及脱氧质量。此外,该装置由于镁系脱氧剂的存在,不能完成氮气N2的深度脱氧工作。The Chinese patent document with the publication number CN104694705A discloses a deep deoxidation device and its application. After the gas is heated to a certain temperature by the heating device, it can be deoxidized by copper, magnesium and titanium deoxidizers. It can be deoxidized under normal pressure. processing, the accuracy can reach 10 -21 ppm. However, this device cannot control the humidity of the gas, nor can it realize the contact of the gas with different deoxidizers at different temperatures, thus affecting the deoxidation efficiency and quality of the device. In addition, due to the presence of magnesium-based deoxidizers, this device cannot complete the deep deoxidation work of nitrogen N2 .
公开号为CN205700091U的中国专利文件中公开了一种工业生产酸性气体过滤净化装置,采用活性炭过滤与碱液喷洒除酸相结合的方式,提高了酸性气体过滤化的效率,并采用pH继电控制排液系统,可以智能控制精华液的排放。具有较高的净化效率。但是,这项专利只能对酸性气体进行净化,不能有效的处理中性或者碱性气体。The Chinese patent document with the publication number CN205700091U discloses an acid gas filtration and purification device for industrial production, which adopts the combination of activated carbon filtration and lye spraying to remove acid, improves the efficiency of acid gas filtration, and adopts pH relay control The drainage system can intelligently control the discharge of essence. It has high purification efficiency. However, this patent can only purify acidic gases, and cannot effectively deal with neutral or alkaline gases.
综上所述,现有的气体净化、脱氧装置的适用范围较小,精度及效率较低,且无法实时监测气体净化后的湿度及氧含量。然而,对于精密实验设备,针对进入设备内不同保护气体的全面净化是十分必要的。To sum up, the existing gas purification and deoxygenation devices have a small scope of application, low precision and efficiency, and cannot monitor the humidity and oxygen content of the purified gas in real time. However, for precision experimental equipment, comprehensive purification of different protective gases entering the equipment is very necessary.
发明内容Contents of the invention
本发明解决的技术问题是:针对现有气体净化设备净化效率低,气体适用范围小,难以脱除气体内水分,且没有实时监测设备出口的湿度及氧分压等问题,提供了一种净化气体的方法,用于工厂和实验室中低氧含量保护气体的制备。The technical problem solved by the present invention is: to solve the problems of low purification efficiency of existing gas purification equipment, small scope of gas application, difficulty in removing moisture in the gas, and no real-time monitoring of humidity and oxygen partial pressure at the outlet of the equipment, etc., a purification method is provided. Gas method for the preparation of protective gases with low oxygen content in factories and laboratories.
本发明采用如下技术方案实现:The present invention adopts following technical scheme to realize:
一种气体净化装置,包括通过管道串联连接的除湿净化室2、第一脱氧净化室31、第二脱氧净化室32和第三脱氧净化室33,所述除湿净化室2的入口与保护气体的气瓶1连接;A gas purification device, comprising a dehumidification purification chamber 2, a first deoxygenation purification chamber 31, a second deoxygenation purification chamber 32 and a third deoxygenation purification chamber 33 connected in series through pipelines, the entrance of the dehumidification purification chamber 2 is connected to the protective gas Cylinder 1 connection;
所述除湿净化室2内部填装有硅胶除湿剂,所述第一脱氧净化室31内部填装铜单质或铜基合金中的一种作为脱氧净化剂,所述第二脱氧净化室32内部填装钼单质或钼基合金中的一种作为脱氧净化剂,所述第三脱氧净化室33内部填装钛单质、海绵钛或钛基合金中的一种作为脱氧净化剂;The interior of the dehumidification and purification chamber 2 is filled with a silica gel desiccant, the interior of the first deoxygenation purification chamber 31 is filled with a copper element or a copper-based alloy as a deoxidation purifier, and the interior of the second deoxygenation purification chamber 32 is filled with One of molybdenum element or molybdenum-based alloy is installed as a deoxidizing agent, and the third deoxidation purification chamber 33 is filled with one of titanium element, sponge titanium or titanium-based alloy as a deoxidizing agent;
所述第一脱氧净化室31、第二脱氧净化室32和第三脱氧净化室33分别设有加热单元。The first deoxygenation purification chamber 31 , the second deoxygenation purification chamber 32 and the third deoxygenation purification chamber 33 are respectively provided with heating units.
进一步的,所述硅胶除湿剂和脱氧净化剂分别占对应净化室内部体积的50%-80%。Further, the silica gel dehumidifier and the deoxygenation purifier account for 50%-80% of the corresponding internal volume of the clean room respectively.
进一步的,所述第一脱氧净化室31、第二脱氧净化室32和第三脱氧净化室33分别设置在三个独立的加热炉内,分别对三个脱氧净化室内部的脱氧净化剂加热至相应的氧化温度。Further, the first deoxygenation purification chamber 31, the second deoxygenation purification chamber 32 and the third deoxygenation purification chamber 33 are respectively arranged in three independent heating furnaces, and the deoxidation purification agents inside the three deoxidation purification chambers are respectively heated to corresponding oxidation temperature.
进一步的,所述三个独立的加热炉分别设有独立的PID反馈控制温度仪表。Further, the three independent heating furnaces are respectively equipped with independent PID feedback control temperature instruments.
在本发明的一种气体净化装置中,所述第三脱氧净化室33的出口管道上设有氧含量测试探头5。In a gas purification device of the present invention, the outlet pipe of the third deoxygenation purification chamber 33 is provided with an oxygen content testing probe 5 .
进一步的,所述第三脱氧净化室33的出口管道上还设有湿度计6。Further, a hygrometer 6 is also provided on the outlet pipeline of the third deoxygenation purification chamber 33 .
本发明的一种气体净化装置用于净化的气体为氩气、氢气、氮气、硫化氢气体中的一种或多种混合气体。A gas purifying device of the present invention is used to purify one or more mixed gases of argon, hydrogen, nitrogen and hydrogen sulfide.
本发明还公开了一种上述气体净化装置的应用,将该气体净化装置用于保护气体的制备,具体包括如下步骤:The present invention also discloses an application of the above-mentioned gas purification device. The gas purification device is used for the preparation of protective gas, which specifically includes the following steps:
第一步,配置初始气体,将氩气、氢气、氮气、硫化氢中的一种或几种混合成实验所需保护气体,并装入气瓶1;The first step is to configure the initial gas, mix one or more of argon, hydrogen, nitrogen, and hydrogen sulfide into the protective gas required for the experiment, and put it into the gas cylinder 1;
第二步,气体干燥,将配置好的保护气体通入装有硅胶除湿剂的除湿净化室2,在气体通过硅胶除湿剂的过程中,除去保护气体中的水分,达到气体干燥的目的;The second step is to dry the gas. The configured protective gas is passed into the dehumidification and purification chamber 2 equipped with silica gel desiccant. When the gas passes through the silica gel desiccant, the moisture in the protective gas is removed to achieve the purpose of gas drying;
第三步,气体脱氧,开启三组加热炉,保持三组脱氧净化室内的温度为设定的脱氧剂目标脱氧温度,保护气体依次通过第一脱氧净化室31中的铜单质或铜基合金、第二脱氧净化室32中的钼单质或钼基合金、第三脱氧净化室33中的钛单质、海绵钛或钛基合金,保护气体中的氧会在高温条件下与脱氧净化剂发生氧化反应达到脱氧目的;In the third step, gas deoxidation, three groups of heating furnaces are turned on, and the temperature in the three groups of deoxidation purification chambers is kept at the set deoxidation agent target deoxidation temperature, and the protective gas passes through the copper element or copper-based alloy in the first deoxidation purification chamber 31 in turn, The molybdenum element or molybdenum-based alloy in the second deoxidation purification chamber 32, the titanium element substance, sponge titanium or titanium-based alloy in the third deoxidation purification chamber 33, the oxygen in the protective gas will oxidize with the deoxidation purification agent under high temperature conditions To achieve the purpose of deoxidation;
第四步,测量氧含量及湿度,开启装置末端的氧含量测试探头5和湿度计6,对净化后保护气体的氧含量和适度进行测量,达到要求值即可通入所需设备中进行实验。The fourth step is to measure the oxygen content and humidity, open the oxygen content test probe 5 and the hygrometer 6 at the end of the device, and measure the oxygen content and appropriateness of the purified protective gas. When the required value is reached, it can be passed into the required equipment for experimentation .
进一步的,通入该气体净化装置的气体流量为100-300mL/min。Further, the gas flow rate passed into the gas purification device is 100-300mL/min.
进一步的,所述第一加热炉41的温度范围为500-700℃,所述第二加热炉42的温度范围为350-550℃,所述第三加热炉43的温度为50-200℃。Further, the temperature range of the first heating furnace 41 is 500-700°C, the temperature range of the second heating furnace 42 is 350-550°C, and the temperature of the third heating furnace 43 is 50-200°C.
本发明具有以下有益效果:The present invention has the following beneficial effects:
1)气体净化彻底,不仅可以控制并检测气体内部的氧含量,同时还可以对气体进行干燥,降低气体湿度,提高了气体的净化质量。1) Thorough gas purification, not only can control and detect the oxygen content inside the gas, but also can dry the gas, reduce the humidity of the gas, and improve the purification quality of the gas.
2)提高了脱氧能力及脱氧效率,本发明使用三个加热炉分别对不同的脱氧净化室的内部空间进行加热,使每个脱氧净化室内的脱氧剂均可以在最优的环境下进行工作,即提高了脱氧能力,同时也提升了脱氧效率。2) The deoxidation capacity and deoxidation efficiency are improved. The present invention uses three heating furnaces to heat the interior spaces of different deoxidation purification chambers, so that the deoxidizers in each deoxidation purification chamber can work in an optimal environment. That is, the deoxidation capacity is improved, and the deoxidation efficiency is also improved.
3)扩大了适用脱氧气体的范围,氩气、氮气、氢气、硫化氢等气体的一种或几种混合气体均可以在该装置中进行净化,净化后的气体氧含量可降低至10-26ATM。3) The range of applicable deoxidizing gases has been expanded. One or several mixed gases of argon, nitrogen, hydrogen, hydrogen sulfide and other gases can be purified in this device, and the oxygen content of the purified gas can be reduced to 10 -26 ATMs.
4)净化剂可以循环使用,降低了气体净化的成本。4) The purifying agent can be recycled, which reduces the cost of gas purification.
由上所述,本发明可以满足实验和生产中对于气氛环境的各项要求,并且具有操作简单、净化速度快、净化剂使用寿命长、成本低等特点。From the above, the present invention can meet various requirements for the atmosphere environment in experiments and production, and has the characteristics of simple operation, fast purification speed, long service life of the purification agent, and low cost.
以下结合附图和具体实施方式对本发明作进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments.
附图说明Description of drawings
图1为实施例中的气体净化装置的连接结构示意图。Fig. 1 is a schematic diagram of the connection structure of the gas purification device in the embodiment.
图中标号:1-气瓶,2-除湿净化室,31-第一脱氧净化室,32-第二脱氧净化室,33-第三脱氧净化室,41-第一加热炉,42-第二加热炉,43-第三加热炉,5-氧含量测试探头,6-湿度计。Labels in the figure: 1-gas cylinder, 2-dehumidification and purification room, 31-first deoxygenation and purification room, 32-second deoxygenation and purification room, 33-third deoxygenation and purification room, 41-first heating furnace, 42-second Heating furnace, 43-third heating furnace, 5-oxygen content test probe, 6-humidity meter.
具体实施方式detailed description
实施例Example
参见图1,图示中的一种气体净化装置为本发明的优选方案,具体包括气瓶1、除湿净化室2、第一脱氧净化室31、第二脱氧净化室32、第三脱氧净化室33、第一加热炉41、第二加热炉42、第三加热炉43、氧含量测试探头5和湿度计6。气瓶1和除湿净化室2、第一脱氧净化室31、第二脱氧净化室32、第三脱氧净化室33通过管道串联连接,分别对气瓶内的气体进行除湿和三次脱氧净化。Referring to Fig. 1, a gas purification device in the illustration is a preferred solution of the present invention, specifically comprising a gas cylinder 1, a dehumidification purification chamber 2, a first deoxygenation purification chamber 31, a second deoxygenation purification chamber 32, and a third deoxygenation purification chamber 33. The first heating furnace 41 , the second heating furnace 42 , the third heating furnace 43 , the oxygen content testing probe 5 and the hygrometer 6 . The gas cylinder 1 is connected in series with the dehumidification and purification chamber 2, the first deoxygenation purification chamber 31, the second deoxygenation purification chamber 32, and the third deoxygenation purification chamber 33 through pipelines to dehumidify and deoxygenate the gas in the gas cylinder three times.
气瓶1用于储存待净化的气体,连接在除湿净化室2的进口端管路上,可将单独一种气体的气瓶与净化装置的进口连接,也可将若干不同气体的气瓶并联连接,实现多种混合气体的净化。The gas cylinder 1 is used to store the gas to be purified, and is connected to the inlet pipeline of the dehumidification and purification chamber 2. A single gas cylinder can be connected to the inlet of the purification device, or several gas cylinders of different gases can be connected in parallel , to achieve the purification of a variety of mixed gases.
除湿净化室2内填装的净化剂为硅胶,主要作用是用来吸收通过气体中的水分。The purification agent filled in the dehumidification and purification chamber 2 is silica gel, and its main function is to absorb moisture in the passing gas.
在三组脱氧净化室内分别填装易于氧化反应的金属脱氧剂,其中,在第一脱氧净化室31内填装的脱氧净化剂为铜单质或铜基合金中的一种,通过铜的氧化反应吸收空气中的氧气,第二脱氧净化室32内填装的脱氧净化剂为钼单质或钼基合金中的一种,通过钼的氧化反应吸收空气中的氧气,第三脱氧净化室33内填装的脱氧净化剂为钛单质、海绵钛或钛基合金中的一种,在设定的氧化温度下,三种脱氧净化剂均可以脱去通过气体中的氧,降低气体氧含量。The metal deoxidizers that are easy to oxidize are filled in the three groups of deoxidation purification chambers respectively, wherein the deoxidation purification agent filled in the first deoxidation purification chamber 31 is a copper element or a copper-based alloy, and the oxidation reaction of copper To absorb oxygen in the air, the deoxidizing agent filled in the second deoxidation purification chamber 32 is a kind of molybdenum element or molybdenum-based alloy, and absorbs oxygen in the air through the oxidation reaction of molybdenum, and the third deoxidation purification chamber 33 is filled with The deoxidizing agent installed is one of titanium element, sponge titanium or titanium-based alloy. At the set oxidation temperature, all three deoxidizing agents can remove the oxygen in the passing gas and reduce the oxygen content of the gas.
为了保证气体在净化室内的通过效率以及与净化剂(除湿剂)的接触效率,除湿净化室2内填装的硅胶除湿剂以及脱氧净化室内填装的脱氧净化剂分别占相应净化室内部体积的50%-80%。In order to ensure the passing efficiency of the gas in the clean room and the contact efficiency with the purifier (dehumidifier), the silica gel desiccant filled in the dehumidification clean room 2 and the deoxygen purifier filled in the deoxygen clean room respectively account for 30% of the inner volume of the corresponding clean room. 50%-80%.
为了保证脱氧净化剂的最佳脱氧效果,本实施例的第一加热炉41、第二加热炉42、第三加热炉43分别作为第一脱氧净化室31、第二脱氧净化室32、第三脱氧净化室33的加热单元,第一脱氧净化室31、第二脱氧净化室32、第三脱氧净化室33分别设置在三个独立的加热炉中,三个加热炉分别受独立的PID反馈控制温度仪表控制,最高可加热至700℃并保持恒温。In order to ensure the best deoxidation effect of the deoxidation purifier, the first heating furnace 41, the second heating furnace 42, and the third heating furnace 43 of this embodiment are respectively used as the first deoxidation purification chamber 31, the second deoxidation purification chamber 32, and the third deoxidation purification chamber. The heating unit of the deoxygenation purification chamber 33, the first deoxygenation purification chamber 31, the second deoxygenation purification chamber 32, and the third deoxygenation purification chamber 33 are respectively arranged in three independent heating furnaces, and the three heating furnaces are respectively controlled by independent PID feedback Temperature instrument control, can heat up to 700 ℃ and keep constant temperature.
在第三脱氧净化室33的出口端连接的管道上分别设有氧含量测试探头5和湿度计6,氧探头7可以测量气体经过净化装置后、进入实验设备的气体氧含量,湿度计10可以测量气体经过净化装置后,进入实验设备的气体的湿度。The pipeline connected to the outlet of the third deoxygenation purification chamber 33 is respectively provided with an oxygen content test probe 5 and a hygrometer 6. The oxygen probe 7 can measure the oxygen content of the gas entering the experimental equipment after the gas passes through the purification device. The hygrometer 10 can Measure the humidity of the gas entering the experimental equipment after the gas passes through the purification device.
本实施例的气体净化装置可用于净化氩气、氢气、氮气、硫化氢等惰性气体中的一种气体或者按一定比例组成的混合气体,待净化的气体依次通过除湿净化室2、第一脱氧净化室31、第二脱氧净化室32、第三脱氧净化室33,实现气体中水蒸气和氧气的净化脱除。The gas purification device of this embodiment can be used to purify one of the inert gases such as argon, hydrogen, nitrogen, and hydrogen sulfide, or a mixed gas composed of a certain proportion. The purification chamber 31, the second deoxygenation purification chamber 32, and the third deoxygenation purification chamber 33 realize the purification and removal of water vapor and oxygen in the gas.
因此,本实施例的气体净化装置可用于实验室或生产中的保护气体的制备,具体包括如下步骤:Therefore, the gas purification device of this embodiment can be used for the preparation of protective gas in laboratories or production, and specifically includes the following steps:
本发明还公开了一种气体净化装置的使用方法,包括如下步骤:The invention also discloses a method for using the gas purification device, which includes the following steps:
第一步,配置初始气体,将氩气、氢气、氮气、硫化氢中的一种或几种混合成实验所需保护气体,并装入气瓶1。The first step is to configure the initial gas, mix one or more of argon, hydrogen, nitrogen, and hydrogen sulfide into the protective gas required for the experiment, and fill it into the gas cylinder 1.
第二步,气体干燥,将配置好的保护气体通入装有硅胶除湿剂的除湿净化室2,在气体通过硅胶除湿剂的过程中,除去保护气体中的水分,达到气体干燥的目的,通入的气体流量为100-300mL/min,进一步优选在150mL/min。The second step is to dry the gas. The configured protective gas is passed into the dehumidification and purification chamber 2 equipped with silica gel desiccant. When the gas passes through the silica gel desiccant, the moisture in the protective gas is removed to achieve the purpose of gas drying. The gas flow rate that enters is 100-300mL/min, more preferably at 150mL/min.
第三步,气体脱氧,开启三组加热炉,保持三组脱氧净化室内的温度为设定的脱氧剂目标脱氧温度,保护气体依次通过第一脱氧净化室31中的铜单质或铜基合金、第二脱氧净化室32中的钼单质或钼基合金、第三脱氧净化室33中的钛单质、海绵钛或钛基合金,保护气体中的氧会在高温条件下与脱氧净化剂发生氧化反应达到脱氧目的。在该步骤中,第一加热炉41的温度范围控制在500-700℃,优选600℃,第二加热炉42的温度范围控制在350-550℃,优选450℃,第三加热炉43的温度范围控制在50-200℃,优选100℃。In the third step, gas deoxidation, three groups of heating furnaces are turned on, and the temperature in the three groups of deoxidation purification chambers is kept at the set deoxidation agent target deoxidation temperature, and the protective gas passes through the copper element or copper-based alloy in the first deoxidation purification chamber 31 in turn, The molybdenum element or molybdenum-based alloy in the second deoxidation purification chamber 32, the titanium element substance, sponge titanium or titanium-based alloy in the third deoxidation purification chamber 33, the oxygen in the protective gas will oxidize with the deoxidation purification agent under high temperature conditions To achieve the purpose of deoxidation. In this step, the temperature range of the first heating furnace 41 is controlled at 500-700°C, preferably 600°C, the temperature range of the second heating furnace 42 is controlled at 350-550°C, preferably 450°C, and the temperature of the third heating furnace 43 The range is controlled at 50-200°C, preferably 100°C.
第四步,测量氧含量及湿度,开启装置末端的氧含量测试探头5和湿度计6,对净化后保护气体的氧含量和适度进行测量,达到要求值即可通入所需设备中进行实验。The fourth step is to measure the oxygen content and humidity, open the oxygen content test probe 5 and the hygrometer 6 at the end of the device, and measure the oxygen content and appropriateness of the purified protective gas. When the required value is reached, it can be passed into the required equipment for experimentation .
以上对本发明实施例所提供的技术方案进行了详细介绍,本文中应用了具体个例对本发明实施例的原理以及实施方式进行了阐述,以上实施例的说明只适用于帮助理解本发明实施例的原理;同时,对于本领域的一般技术人员,依据本发明实施例,在具体实施方式以及应用范围上均会有改变之处,综上,本说明书内容不应理解为对本发明的限制。The technical solutions provided by the embodiments of the present invention have been introduced in detail above, and the principles and implementation modes of the embodiments of the present invention have been explained by using specific examples in this paper. The descriptions of the above embodiments are only applicable to help understand the embodiments of the present invention At the same time, for those of ordinary skill in the art, according to the embodiment of the present invention, there will be changes in the specific implementation and application scope. In summary, the content of this specification should not be construed as limiting the present invention.
Claims (10)
- A kind of 1. gas cleaning plant, it is characterised in that:Including the dehumidifying clean room (2), first de- connected by placed in series Oxygen clean room (31), the second deoxidizing purification room (32) and the 3rd deoxidizing purification room (33), it is described dehumidifying clean room (2) entrance with Gas cylinder (1) connection of protective gas;Silica gel dehumidizer is filled with inside dehumidifying clean room (2), copper list is loaded inside the first deoxidizing purification room (31) For one kind in matter or acid bronze alloy as deoxidation purificant, the second deoxidizing purification room (32) is internal to load molybdenum simple substance or molybdenum base For one kind in alloy as deoxidation purificant, the 3rd deoxidizing purification room (33) is internal to load titanium simple substance, titanium sponge or titanium-based One kind in alloy is as deoxidation purificant;The first deoxidizing purification room (31), the second deoxidizing purification room (32) and the 3rd deoxidizing purification room (33) are respectively equipped with heating Unit.
- 2. a kind of gas cleaning plant according to claim 1, the silica gel dehumidizer and deoxidation purificant account for pair respectively Answer the 50%-80% of clean room's internal volume.
- 3. a kind of gas cleaning plant according to claim 1, the first deoxidizing purification room (31), the second deoxidizing purification Room (32) and the 3rd deoxidizing purification room (33) are separately positioned in three independent heating furnaces, respectively in three deoxidizing purification rooms The deoxidation purificant in portion is heated to corresponding oxidizing temperature.
- 4. a kind of gas cleaning plant according to claim 3, three independent heating furnaces are respectively equipped with independent PID/feedback controls thermometric instrument.
- 5. a kind of gas cleaning plant according to any one of claim 1-4, the 3rd deoxidizing purification room (33) Outlet conduit is provided with oxygen content test probe (5).
- 6. a kind of gas cleaning plant according to claim 5, on the outlet conduit of the 3rd deoxidizing purification room (33) It is additionally provided with hygrometer (6).
- 7. a kind of gas cleaning plant according to claim 1, the gas of purification is argon gas, hydrogen, nitrogen, stink damp One or more mixed gas in body.
- A kind of 8. application of the gas cleaning plant described in claim 6, it is characterised in that:The gas cleaning plant is used to protect The preparation of gas, specifically comprises the following steps:The first step, initial gas is configured, the one or more in argon gas, hydrogen, nitrogen, hydrogen sulfide are mixed into needed for experiment and protected Gas is protected, and loads gas cylinder (1);Second step, gas are dried, and the protective gas configured are passed through into the dehumidifying clean room (2) equipped with silica gel dehumidizer, in gas During body is by silica gel dehumidizer, the moisture in protective gas is removed, reaches the purpose of gas drying;3rd step, gas deoxidation, three groups of heating furnaces are opened, keep deoxidier mesh of the temperature in three groups of deoxidizing purification rooms for setting Mark deoxidation temperature, it is net that protective gas passes sequentially through copper simple substance in the first deoxidizing purification room (31) or acid bronze alloy, the second deoxidation Change the molybdenum simple substance in room (32) or titanium simple substance, titanium sponge or titanium-base alloy in molybdenum-base alloy, the 3rd deoxidizing purification room (33), protect Oxygen in shield gas can occur oxidation reaction with deoxidation purificant under the high temperature conditions and reach deoxidation purpose;4th step, measure oxygen content and humidity, the oxygen content test probe (5) and hygrometer (6) of opening device end, to purification The oxygen content of protective gas and appropriateness measure afterwards, reach required value can be passed through needed for tested in equipment.
- 9. a kind of application of gas cleaning plant according to claim 8, it is passed through the gas flow of the gas cleaning plant For 100-300mL/min.
- 10. a kind of application of gas cleaning plant according to claim 8, the temperature range of first heating furnace (41) For 500-700 DEG C, the temperature range of second heating furnace (42) is 350-550 DEG C, the temperature of the 3rd heating furnace (43) For 50-200 DEG C.
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CN113155252A (en) * | 2021-04-25 | 2021-07-23 | 上海海事大学 | Weighing system with deoxidization function and capable of achieving cyclic dehumidification simultaneously |
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