TWI682894B - Hydrogen recovery and reuse system - Google Patents

Hydrogen recovery and reuse system Download PDF

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TWI682894B
TWI682894B TW107130405A TW107130405A TWI682894B TW I682894 B TWI682894 B TW I682894B TW 107130405 A TW107130405 A TW 107130405A TW 107130405 A TW107130405 A TW 107130405A TW I682894 B TWI682894 B TW I682894B
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hydrogen
electrochemical
gas
mixed gas
recovery
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TW107130405A
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TW202009212A (en
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閻明宇
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鼎佳能源股份有限公司
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一種氫氣回收再利用系統,係包括一處理裝置、一電化學氫氣純化裝置及一除水裝置,該處理裝置用以接收並處理一混合氣體並用以移除有害物質,該電化學氫氣純化裝置與所述處理裝置相連接並用以清除所述混合氣體內的非氫氣的氣體及雜質,該除水裝置與所述電化學氫氣純化裝置相連接並用以去除純化後之氫氣內的水分。 A hydrogen recovery and reuse system includes a processing device, an electrochemical hydrogen purification device, and a water removal device. The processing device is used to receive and process a mixed gas and remove harmful substances. The processing device is connected and used to remove non-hydrogen gas and impurities in the mixed gas. The water removal device is connected to the electrochemical hydrogen purification device and used to remove moisture in the purified hydrogen.

Description

氫氣回收再利用系統 Hydrogen recovery and reuse system

本發明係有關於一種氫氣回收再利用系統,尤指一種可有效回收氫氣並再利用且可純化出純度高的氫氣之氫氣回收再利用系統。 The invention relates to a hydrogen recovery and reuse system, in particular to a hydrogen recovery and reuse system that can effectively recover and reuse hydrogen and can purify hydrogen with high purity.

在一般的半導製程體與光電製程結束後,剩餘的製程氣體(即廢氣)中通常含有氨氣(NH3)、矽甲烷(SiH4)、二矽甲烷(Si2H6)、磷化氫(PH3)、砷化氫(AsH3)、三甲基鎵(Ga(CH3)3)與高濃度的氫氣,其中氨氣、矽甲烷、二矽甲烷、磷化氫、砷化氫、三甲基鎵皆為環境污染物。 After the general semiconducting process body and the photoelectric process are completed, the remaining process gas (i.e., exhaust gas) usually contains ammonia (NH 3 ), silicon methane (SiH 4 ), disilyl methane (Si 2 H 6 ), phosphating Hydrogen (PH 3 ), arsine (AsH 3 ), trimethylgallium (Ga(CH 3 ) 3 ) and high-concentration hydrogen, including ammonia, silane, methane, phosphine, arsenide And trimethylgallium are environmental pollutants.

目前,對於上述環境污染物的處理方式通常是將廢氣經過硫酸或次氯酸水洗之後直接排放至大氣中。然而,此處理方式具有許多缺點。例如,經處理後的廢水中的氮濃度達數萬ppm,遠高於法規標準。此外,氫氣被直接排放至大氣中具有爆炸的風險,且造成氫氣的浪費。 At present, the treatment method for the above environmental pollutants is usually to directly discharge the exhaust gas into the atmosphere after being washed with sulfuric acid or hypochlorous acid. However, this approach has many disadvantages. For example, the nitrogen concentration in the treated wastewater reaches tens of thousands of ppm, which is far higher than the legal standards. In addition, hydrogen is directly discharged into the atmosphere with the risk of explosion and waste of hydrogen.

此外,於半導體製程或光電製程或化工廠製程中,相關行業業者通常是將剩餘的製程廢氣(如前述之各種氣體)透過燃燒的方式處理,因此,製程較為複雜且設備及處理費用也相對較昂貴。 In addition, in the semiconductor process, the photoelectric process or the chemical plant process, the relevant industry players usually treat the remaining process waste gas (such as the aforementioned various gases) through combustion, so the process is more complicated and the equipment and processing costs are relatively relatively high. expensive.

爰此,為有效解決上述之問題,本發明之主要目的在於提供 一種有效回收氫氣並再利用之氫氣回收再利用系統。 So, in order to effectively solve the above problems, the main purpose of the present invention is to provide A hydrogen recovery and reuse system that efficiently recovers and reuses hydrogen.

本發明之次要目的,在於提供一種可純化出純度高的氫氣之氫氣回收再利用系統。 The secondary object of the present invention is to provide a hydrogen recovery and reuse system that can purify hydrogen with high purity.

本發明之次要目的,在於提供一種回收製程成本較低之氫氣回收再利用系統。 The secondary objective of the present invention is to provide a hydrogen recovery and reuse system with a relatively low recovery process cost.

為達上述目的,本發明係提供一種氫氣回收再利用系統,係包括一處理裝置、一電化學氫氣純化裝置及一除水裝置,該處理裝置用以接收並處理一混合氣體並用以移除有害電化學處裡裝置之物質,該電化學氫氣純化裝置與所述處理裝置相連接並用以去除所述混合氣體內的非氫氣的氣體,該除水裝置與所述電化學氫氣純化裝置相連接並用以去除純化後之氫氣內的水分。 To achieve the above object, the present invention provides a hydrogen recovery and reuse system, which includes a processing device, an electrochemical hydrogen purification device and a water removal device, the processing device is used to receive and process a mixed gas and to remove harmful Substances in the electrochemical treatment unit. The electrochemical hydrogen purification device is connected to the treatment device and used to remove non-hydrogen gas in the mixed gas. The water removal device is connected to the electrochemical hydrogen purification device and used To remove the water in the purified hydrogen.

透過本發明此系統的設計,先以所述處理裝置接收並處理一製程中所排出的混合氣體,並且移除該混合氣體內的有害物質如含氮化物、硫化物…)等,然後利用所述電化學氫氣純化裝置清除混合氣體內的非氫氣的氣體及雜質,再利用所述泵浦裝置提供壓力以將所述電化學氫氣純化裝置內的氫氣推出至所述除水裝置,最後利用該除水裝置以去除純化後之氫氣內的水分,如此得以分離出純度較高的氫氣,因此,可以有效地達成回收氫氣並再利用。 Through the design of the system of the present invention, the processing device first receives and processes the mixed gas discharged in a process, and removes harmful substances such as nitrides, sulfides, etc. in the mixed gas, and then uses the The electrochemical hydrogen purification device removes non-hydrogen gas and impurities in the mixed gas, and then uses the pump device to provide pressure to push the hydrogen in the electrochemical hydrogen purification device to the water removal device, and finally uses the The water removal device removes the water in the purified hydrogen, so that the hydrogen with higher purity can be separated, so that the hydrogen can be recovered and reused effectively.

2‧‧‧氫氣回收再利用系統 2‧‧‧Hydrogen recovery and reuse system

20‧‧‧處理裝置 20‧‧‧Processing device

21‧‧‧電化學氫氣純化裝置 21‧‧‧Electrochemical hydrogen purification device

22‧‧‧泵浦裝置 22‧‧‧Pump device

23‧‧‧除水裝置 23‧‧‧water removal device

24‧‧‧吸附元件 24‧‧‧Adsorption components

3‧‧‧混合氣體 3‧‧‧ Mixed gas

4‧‧‧氫氣 4‧‧‧hydrogen

40‧‧‧氫離子 40‧‧‧ hydrogen ion

41‧‧‧電子 41‧‧‧Electronics

5‧‧‧管路 5‧‧‧Pipeline

6‧‧‧氮氣 6‧‧‧ Nitrogen

7‧‧‧質子交換膜 7‧‧‧ Proton exchange membrane

70‧‧‧陽極觸媒反應層 70‧‧‧Anode catalyst reaction layer

71‧‧‧陰極觸媒反應層 71‧‧‧ Cathode catalyst reaction layer

8‧‧‧外部電源 8‧‧‧External power supply

90‧‧‧進氣通道 90‧‧‧ Intake channel

91‧‧‧出氣通道 91‧‧‧ Outlet channel

第1圖係為本發明氫氣回收再利用系統之較佳實施例之方塊示意圖;第2圖係為本發明氫氣回收再利用系統之較佳實施例之電化學氫氣純 化裝置之實施示意圖;第3圖係為本發明氫氣回收再利用系統之另一實施例之方塊示意圖。 Figure 1 is a block schematic diagram of a preferred embodiment of the hydrogen recovery and reuse system of the present invention; Figure 2 is a electrochemical hydrogen purification of a preferred embodiment of the hydrogen recovery and reuse system of the present invention 3 is a block diagram of another embodiment of the hydrogen recovery and reuse system of the present invention.

本發明之上述目的及其結構與功能上的特性,將依據所附圖式之較佳實施例予以說明。 The above objects, structural and functional characteristics of the present invention will be described based on the preferred embodiments of the accompanying drawings.

請參閱第1、2圖,係為本發明氫氣回收再利用系統2之較佳實施例之方塊示意圖及電化學氫氣純化裝置之實施示意圖,如圖所示,一種氫氣回收再利用系統2,係包括一處理裝置20、一氫氣純化裝置21及一除水裝置23,於本發明中,所述氫氣回收再利用系統2係自含有氫氣4、氮氣6、氨氣與其他氣體形成一混合氣體3中回收氫氣4並且再利用,該混合氣體3例如是半導體製程或光電製程進行完成之後所剩餘的廢氣,其包含有氫氣4、氮氣6、氨氣、矽甲烷、二矽甲烷、磷化氫、砷化氫、三甲基鎵或其組合;首先,前述之混合氣體3會先透過一管路5排出至所述處理裝置20,該處理裝置20係選擇為一區域洗滌塔(local scrubber),透過該區域洗滌塔先行初步處裡所述混合氣體3,以將該混合氣體3內的有毒氣體或物體顆粒(如粉塵…)或有害物質(如含氮化物、硫化物…)等先行去除,留下無害氣體進入所述電化學氫氣純化裝置21,尤須說明的是,該區域洗滌塔依原理可分為電熱水洗式、填充水洗式、乾式吸附式等,而於本發明氫氣回收再利用系統2中,端視使用者的需求決定該混合氣體3需使用何種型式進行處理,因此前述處理裝置20之各型式接包含於本發明之範圍內,合先敘明;然後,將清洗過後的混合氣體3透過所述管路5傳送至所述電 化學氫氣純化裝置21,並利用該電化學氫氣純化裝置21來清除混合氣體3內的非氫氣4的氣體及其餘雜質,尤須說明的是,所述電化學氫氣純化裝置21係選擇利用電化學方式以清除所述混合氣體3內的非氫氣4的氣體及雜質,換句話說,所述混合氣體3於該電化學氫氣純化裝置21內透過電化學的方式將氫氣4以外的氣體(如氫氣4、氮氣6、氨氣…)及雜質進行去除分離的動作,以只保留氫氣4於該電化學氫氣純化裝置21內,至此,所述混合氣體3內除了氫氣4以外的氣體皆已被分離而不存在,而氫氣4則經由所述管路5進入所述除水裝置23;請一併參閱第2圖,更進一步說明,該電化學氫氣純化裝置更具有一進氣通道90、一質子交換膜7、一陽極觸媒反應層70、一陰極觸媒反應層71、一出氣通道91及一外部電源8,該進氣通道90與前述處理裝置20相連通,於該處理裝置20內處理過後的混合氣體3會透過進氣通道90進入該電化學氫氣純化裝置21,接著利用該質子交換膜7隔阻氫氣4以外之氣體,並可透過該質子交換膜7傳送複數氫離子40並隔離複數電子41通過,所述陽極觸媒反應層70及陰極觸媒反應層71係分設於該質子交換膜7之相對兩側,於所述陽、陰極觸媒反應層70、71提供鉑(Pt)或釕(Ru)或其他貴金屬為一觸媒進行一電化學反應後並將一生成物(該生成物係指氫氣4)經由所述出氣通道91擴散排出,進而完成去除所述混合氣體3內的非氫氣4的氣體及雜質;接著,於該氫氣4進入除水裝置23之前先行經過一泵浦裝置22,並利用所述泵浦裝置22提供壓力將所述氫氣4純化裝置21內的氫氣4推送至所述除水裝置23,由於在該電化學氫氣純化裝置21分離出來的氫氣4仍然 會存有部分的水分,因此需透過該除水裝置23將水分去除,而該除水裝置23選擇利用冷凍除水的方式去除純化後之氫氣4內的水分,如此得以分離出純度較高的氫氣4;此外,請一併參閱第3圖,尤須說明的是,於本發明中可更進一步包括一吸附元件24與所述除水裝置23相連接,該吸附元件24用以吸附純化後之氫氣4內的水分,也就是說,該吸附元件24可作為所述除水裝置23的輔助元件,以令分離後之氫氣4內的水分去除速率更快且氫氣4純度更高,達到具有加乘之功效,該吸附元件24係可選擇為下列材質:活性碳、沸石、矽膠、活性氧化鋁、分子篩、氧化錳、氫氧化鈣、石墨烯或中空纖維其中任一種;如此一來,透過前述之各裝置的各功用,進以達到分離出高純度的氫氣4,形成具有高效率之回收氫氣4並再利用的系統,並且,回收製程與習知氫氣回收之方式相比之下其成本也相對較為低廉,大幅降低氫氣4回收的成本。 Please refer to Figures 1 and 2 for a block schematic diagram of a preferred embodiment of the hydrogen recovery and recycling system 2 of the present invention and an implementation schematic diagram of an electrochemical hydrogen purification device. It includes a processing device 20, a hydrogen purification device 21 and a water removal device 23. In the present invention, the hydrogen recovery and reuse system 2 is a mixed gas 3 that contains hydrogen 4, nitrogen 6, ammonia and other gases The hydrogen gas 4 is recovered and reused. The mixed gas 3 is, for example, the waste gas remaining after the semiconductor process or the photoelectric process is completed, which includes hydrogen gas 4, nitrogen gas 6, ammonia gas, silane, dimethan, phosphine, Arsenide, trimethylgallium, or a combination thereof; first, the aforementioned mixed gas 3 is first discharged through a pipeline 5 to the processing device 20, which is selected as a local scrubber, The mixed gas 3 is preliminarily preliminarily passed through the scrubber in this area, so as to remove the toxic gas or object particles (such as dust...) or harmful substances (such as nitrides, sulfides, etc.) in the mixed gas 3, Leaving harmless gas into the electrochemical hydrogen purification device 21, it should be noted that the area of the washing tower can be divided into electric hot water washing type, filled water washing type, dry adsorption type, etc. according to the principle, and the hydrogen recovery and reuse of the present invention In the system 2, the type of the mixed gas 3 needs to be processed depending on the user's needs. Therefore, the types of the aforementioned processing device 20 are included in the scope of the present invention, which will be described first; then, after cleaning The mixed gas 3 is sent to the electricity through the pipeline 5 Chemical hydrogen purification device 21, and use the electrochemical hydrogen purification device 21 to remove the non-hydrogen 4 gas and other impurities in the mixed gas 3, in particular, the electrochemical hydrogen purification device 21 chooses to use electrochemical In order to remove the non-hydrogen 4 gas and impurities in the mixed gas 3, in other words, the mixed gas 3 in the electrochemical hydrogen purification device 21 electrochemically removes gases other than hydrogen 4 (such as hydrogen 4. Nitrogen 6, ammonia...) and impurities are removed and separated to keep only hydrogen 4 in the electrochemical hydrogen purification device 21, so far, all gases except hydrogen 4 in the mixed gas 3 have been separated It does not exist, and hydrogen 4 enters the water removal device 23 through the pipeline 5; please refer to FIG. 2 for further explanation. The electrochemical hydrogen purification device further has an air inlet passage 90 and a proton The exchange membrane 7, an anode catalyst reaction layer 70, a cathode catalyst reaction layer 71, an outlet channel 91 and an external power source 8, the inlet channel 90 communicates with the aforementioned processing device 20 and is processed in the processing device 20 Afterwards, the mixed gas 3 will enter the electrochemical hydrogen purification device 21 through the air inlet channel 90, and then use the proton exchange membrane 7 to block the gas other than the hydrogen 4, and can transmit a plurality of hydrogen ions 40 through the proton exchange membrane 7 and isolate When a plurality of electrons 41 pass through, the anode catalyst reaction layer 70 and the cathode catalyst reaction layer 71 are disposed on opposite sides of the proton exchange membrane 7, and platinum is provided on the anode and cathode catalyst reaction layers 70 and 71 ( Pt) or ruthenium (Ru) or other precious metals are used as a catalyst to perform an electrochemical reaction and diffuse a product (the product refers to hydrogen 4) through the gas outlet channel 91 to complete the removal of the mixed gas Non-hydrogen 4 gas and impurities in 3; then, before the hydrogen 4 enters the water removal device 23, it first passes through a pump device 22, and uses the pump device 22 to provide pressure to the hydrogen 4 purification device 21 Hydrogen 4 is pushed to the water removal device 23, because the hydrogen 4 separated in the electrochemical hydrogen purification device 21 is still Part of the water will exist, so the water needs to be removed through the water removal device 23, and the water removal device 23 chooses to use the method of freezing and water removal to remove the water in the purified hydrogen 4, so that the higher purity can be separated Hydrogen 4; In addition, please refer to FIG. 3 together. It should be noted that, in the present invention, an adsorption element 24 may further be connected to the water removal device 23. The adsorption element 24 is used to adsorb and purify The moisture in the hydrogen gas 4, that is to say, the adsorption element 24 can be used as an auxiliary element of the water removal device 23, so that the moisture removal rate in the separated hydrogen gas 4 is faster and the purity of the hydrogen gas 4 is higher. For the effect of multiplication, the adsorption element 24 can be selected from the following materials: activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide, graphene or hollow fiber; in this way, through The various functions of the aforementioned devices are used to separate high-purity hydrogen 4 to form a highly efficient system for recycling hydrogen 4 and reusing it, and the cost of the recovery process is compared with the conventional hydrogen recovery method. It is also relatively inexpensive, greatly reducing the cost of hydrogen 4 recovery.

以上所述,本發明相較於習知具有下列優點:1.有效回收氫氣並再利用;2.可純化出純度高的氫氣;3.回收製程成本較低。 As described above, the present invention has the following advantages over conventional ones: 1. Effectively recover hydrogen and reuse it; 2. Can purify hydrogen with high purity; 3. Lower recovery process cost.

以上已將本發明做一詳細說明,惟以上所述者,僅為本發明之一較佳實施例而已,當不能限定本發明實施之範圍,即凡依本發明申請範圍所作之均等變化與修飾等,皆應仍屬本發明之專利涵蓋範圍。 The present invention has been described in detail above, but the above is only one of the preferred embodiments of the present invention. When the scope of the present invention cannot be limited, that is, all changes and modifications made in accordance with the scope of the application of the present invention Etc., should still be covered by the patent of the present invention.

2‧‧‧氫氣回收再利用系統 2‧‧‧Hydrogen recovery and reuse system

20‧‧‧處理裝置 20‧‧‧Processing device

21‧‧‧電化學氫氣純化裝置 21‧‧‧Electrochemical hydrogen purification device

22‧‧‧泵浦裝置 22‧‧‧Pump device

23‧‧‧除水裝置 23‧‧‧water removal device

3‧‧‧混合氣體 3‧‧‧ Mixed gas

4‧‧‧氫氣 4‧‧‧hydrogen

5‧‧‧管路 5‧‧‧Pipeline

Claims (5)

一種氫氣回收再利用系統,係包括:一處理裝置,係用以接收並處理一混合氣體並用以移除有害物質;一電化學氫氣純化裝置,與所述處理裝置相連接,該電化學氫氣純化裝置用以清除所述混合氣體內的非氫氣的氣體;一除水裝置,與所述電化學氫氣純化裝置相連接,該除水裝置係利用冷凍除水方式去除純化後之氫氣內的水分;一泵浦裝置,與所述電化學氫氣純化裝置相連接,該泵浦裝置係用以提供一壓力以將所述電化學氫氣純化裝置內的氫氣推出;及一吸附元件,與所述泵浦裝置相連接,該吸附元件係用以吸附純化後之氫氣內的水分。 A hydrogen recycling system includes: a processing device for receiving and processing a mixed gas and for removing harmful substances; an electrochemical hydrogen purification device connected to the processing device for electrochemical hydrogen purification The device is used to remove the non-hydrogen gas in the mixed gas; a water removal device is connected to the electrochemical hydrogen purification device, the water removal device uses a frozen water removal method to remove the water in the purified hydrogen; A pumping device connected to the electrochemical hydrogen purification device, the pumping device is used to provide a pressure to push out the hydrogen in the electrochemical hydrogen purification device; and an adsorption element, and the pump The device is connected, and the adsorption element is used to adsorb the moisture in the purified hydrogen. 如請求項1所述之氫氣回收再利用系統,其中所述處理裝置係選擇為一區域洗滌塔(local scrubber)。 The hydrogen recovery and reuse system according to claim 1, wherein the treatment device is selected as a local scrubber. 如請求項1所述之氫氣回收再利用系統,其中所述混合氣體包括但不限於氫氣、氮氣、氨氣、氬氣、矽化合物、磷化合物、砷化合物、鎵化合物,銦化合物或其組合。 The hydrogen recovery and reuse system according to claim 1, wherein the mixed gas includes but is not limited to hydrogen, nitrogen, ammonia, argon, silicon compound, phosphorus compound, arsenic compound, gallium compound, indium compound, or a combination thereof. 如請求項1所述之氫氣回收再利用系統,其中該吸附元件係選擇為活性碳、沸石、矽膠、活性氧化鋁、分子篩、氧化錳、氫氧化鈣、石墨烯或中空纖維其中任一。 The hydrogen recovery and reuse system according to claim 1, wherein the adsorption element is selected from activated carbon, zeolite, silica gel, activated alumina, molecular sieve, manganese oxide, calcium hydroxide, graphene, or hollow fiber. 如請求項1所述之氫氣回收再利用系統,其中所述電化學氫氣純化裝置更具有一進氣通道、一質子交換膜、一陽極觸媒反應層、一陰極觸媒反應層、一出氣通道及一外部電源,該進氣通道與所述處理裝置相連通,該質子交換膜用以傳送複數氫離子並隔離複數電子通過,所述陽極觸媒反應層及陰極觸媒反應層係分設於該質子交換膜之相對兩 側,於所述陽、陰極觸媒反應層提供鉑(Pt)或釕(Ru)或其他貴金屬為觸媒進行一電化學反應後並將一生成物經由所述出氣通道擴散排出。 The hydrogen recovery and reuse system according to claim 1, wherein the electrochemical hydrogen purification device further has an inlet channel, a proton exchange membrane, an anode catalyst reaction layer, a cathode catalyst reaction layer, and an outlet channel And an external power supply, the gas inlet channel communicates with the processing device, the proton exchange membrane is used to transmit a plurality of hydrogen ions and isolate the passage of a plurality of electrons, the anode catalyst reaction layer and the cathode catalyst reaction layer are located separately The relative two of the proton exchange membrane On the side, platinum (Pt) or ruthenium (Ru) or other precious metals are provided on the anode and cathode catalyst reaction layers as a catalyst to perform an electrochemical reaction and diffuse a product through the gas outlet channel.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101306302A (en) * 2008-01-31 2008-11-19 上海交通大学 Hydrogen containing industrial waste gas separation and purification method
CN104416163A (en) * 2013-08-31 2015-03-18 天津联一科技有限公司 Novel energy-saving hydrogen recovery device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101306302A (en) * 2008-01-31 2008-11-19 上海交通大学 Hydrogen containing industrial waste gas separation and purification method
CN104416163A (en) * 2013-08-31 2015-03-18 天津联一科技有限公司 Novel energy-saving hydrogen recovery device

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