TWI826680B - Adsorption treatment device - Google Patents
Adsorption treatment device Download PDFInfo
- Publication number
- TWI826680B TWI826680B TW109113123A TW109113123A TWI826680B TW I826680 B TWI826680 B TW I826680B TW 109113123 A TW109113123 A TW 109113123A TW 109113123 A TW109113123 A TW 109113123A TW I826680 B TWI826680 B TW I826680B
- Authority
- TW
- Taiwan
- Prior art keywords
- adsorption
- desorption
- cylindrical rotor
- sealing
- area
- Prior art date
Links
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 106
- 238000007789 sealing Methods 0.000 claims abstract description 99
- 238000003795 desorption Methods 0.000 claims abstract description 64
- 239000003463 adsorbent Substances 0.000 claims description 23
- 238000005192 partition Methods 0.000 claims description 19
- 239000003960 organic solvent Substances 0.000 claims description 9
- 238000012545 processing Methods 0.000 abstract description 22
- 230000002093 peripheral effect Effects 0.000 description 54
- 239000012530 fluid Substances 0.000 description 27
- 239000003566 sealing material Substances 0.000 description 11
- 239000000126 substance Substances 0.000 description 10
- 238000010586 diagram Methods 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 239000000428 dust Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 229910021536 Zeolite Inorganic materials 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- 241000264877 Hippospongia communis Species 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012805 post-processing Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
Classifications
-
- 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
- B01D53/02—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
- B01D53/06—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 moving adsorbents, e.g. rotating beds
-
- 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
- B01D53/38—Removing components of undefined structure
- B01D53/44—Organic components
-
- 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
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/81—Solid phase processes
- B01D53/83—Solid phase processes with moving reactants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16J—PISTONS; CYLINDERS; SEALINGS
- F16J15/00—Sealings
- F16J15/16—Sealings between relatively-moving surfaces
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Separation Of Gases By Adsorption (AREA)
- Treating Waste Gases (AREA)
Abstract
一種吸附處理裝置,該吸附處理裝置的密封體(40),包含:並設於圓筒狀轉子的旋轉方向之複數之密封構件(430)、與用來固持複數之密封構件(430)之固持構件(411);密封體(40),其複數之密封構件(430),欲分隔出吸附區域(R2)與脫附區域(R1),就在圓筒狀轉子(90)旋轉之際,可和分隔體(20)滑動並接觸,以此方式設置於脫附入口通道構件(4)以及脫附出口通道構件(5);藉由複數之密封構件(430)中之和分隔體(20)接觸滑動之密封構件(430),將吸附區域(R2)與脫附區域(R1)以氣密方式區隔。An adsorption processing device. The sealing body (40) of the adsorption processing device includes: a plurality of sealing members (430) arranged in the rotation direction of a cylindrical rotor, and a holding member for holding the plurality of sealing members (430). Component (411); the sealing body (40), whose plural sealing components (430) want to separate the adsorption area (R2) and the desorption area (R1), can be rotated when the cylindrical rotor (90) rotates. The separator (20) slides and contacts, and is disposed in the desorption inlet channel member (4) and the desorption outlet channel member (5) in this manner; by combining the plurality of sealing members (430) and the separator (20) The contact sliding seal member (430) separates the adsorption area (R2) and the desorption area (R1) in an airtight manner.
Description
本發明係關於一種吸附處理裝置。The present invention relates to an adsorption treatment device.
藉由吸附濃縮來處理含VOC之工場排放氣體之情況下,該排放氣體中除VOC以外還包含使吸附性能降低之氣狀物質。吸附性能降低之吸附體,必須進行更換。When VOC-containing factory exhaust gas is treated by adsorption and concentration, the exhaust gas contains gaseous substances that reduce adsorption performance in addition to VOC. The adsorbent whose adsorption performance is reduced must be replaced.
碟型吸附處理裝置所具備之吸附體,係特殊一體成形所以製造成本偏高。再者,更換該吸附體之際,必須全體性更換,更換作業會耗費勞力。The adsorption body of the disc-type adsorption treatment device is specially formed in one piece, so the manufacturing cost is relatively high. Furthermore, when replacing the adsorbent body, the entire adsorbent body must be replaced, and the replacement operation is labor-intensive.
另一方面,缸型吸附處理裝置所具備之複數之吸附體,分別具有定型,所以可使其製造成本減少。該吸附體更換之際,可部分地更換,所以可更輕易進行更換作業。On the other hand, the plurality of adsorbents included in the cylinder-type adsorption treatment device each have a fixed shape, so the manufacturing cost can be reduced. When the adsorbent body is replaced, it can be partially replaced, so the replacement operation can be performed more easily.
氣狀物質以外的因素當中,也有吸附性能降低之情況,例如作為該因素之一,可舉出水氣、粉塵。水氣、粉塵存在被處理流體中之情況下,其等會導致吸附材料的堵塞。Factors other than gaseous substances may also reduce adsorption performance. Examples of such factors include water vapor and dust. When water vapor and dust exist in the fluid to be processed, they will cause clogging of the adsorbent material.
碟型吸附處理裝置當中,將吸附區段與脫附區段加以區隔之密封構件和吸附體直接接觸之狀態下,使吸附體旋轉。因此,或許會使被處理流體中所含之水氣、粉塵藉由密封構件而緊貼吸附體,助長吸附體的堵塞。In the disk-type adsorption treatment device, the sealing member that separates the adsorption section and the desorption section causes the adsorption body to rotate in a state of direct contact with the adsorption body. Therefore, water vapor and dust contained in the fluid to be processed may be caused to adhere to the adsorbent through the sealing member, thereby promoting clogging of the adsorbent.
另一方面,缸型吸附處理裝置當中,將吸附區段與脫附區段加以區隔之密封構件不會和吸附體直接接觸,所以不會因水氣、粉塵來助長吸附體的堵塞。On the other hand, in the cylinder-type adsorption treatment device, the sealing member that separates the adsorption section and the desorption section does not come into direct contact with the adsorbent, so moisture and dust do not contribute to clogging of the adsorbent.
如上所述,若考慮到吸附性能,在對於包含有會對吸附體造成影響的物質之被處理流體進行處理之情況,可以說缸型吸附處理裝置比碟型吸附處理裝置更為適當。As mentioned above, when considering the adsorption performance, it can be said that a cylinder-type adsorption treatment device is more suitable than a dish-type adsorption treatment device when processing a fluid to be processed containing substances that may affect the adsorbent.
這種缸型吸附處理裝置,揭示於國際專利公開第2017/006785號(專利文獻1)。 [習知技術文獻] [專利文獻]This type of cylinder-type adsorption treatment device is disclosed in International Patent Publication No. 2017/006785 (Patent Document 1). [Known technical documents] [Patent Document]
專利文獻1:國際專利公開第2017/006785號Patent Document 1: International Patent Publication No. 2017/006785
[發明所欲解決之課題][Problem to be solved by the invention]
近年來,吸附處理裝置之中,隨著大型化使得構成該吸附處理裝置之構件也變大。因此,關於上述的密封構件等的耗材,被要求可輕易更換。In recent years, as adsorption treatment apparatuses have become larger in size, components constituting the adsorption treatment apparatus have also become larger. Therefore, it is required that the above-mentioned consumable materials such as the sealing member can be easily replaced.
上述專利文獻1當中,揭示了一種構成,可更換於被滑動構件滑動的密封構件。The above-mentioned Patent Document 1 discloses a structure in which a sealing member slid by a sliding member can be replaced.
可是,密封構件,設置於旋轉驅動之旋轉體側的全周,所以密封構件的安裝、更換仍然需要許多的作業量。However, the sealing member is provided all around the rotating body side of the rotational drive, so the installation and replacement of the sealing member still requires a lot of work.
此發明,係有鑒於如上述的問題所完成,目的在於提供一種吸附處理裝置,其所具備之構成可輕易進行密封構件的安裝等。 [解決課題之技術手段]This invention was made in view of the above-mentioned problems, and aims at providing an adsorption processing apparatus which is comprised so that a sealing member can be easily installed. [Technical means to solve the problem]
依據本發明之吸附處理裝置,包含:圓筒狀轉子,成環狀而可繞其軸線旋轉,交互配置有具空氣流路之吸附體與不具空氣流路之分隔體;吸附區域,使被處理氣體從該圓筒狀轉子的外側往該吸附體流通,再將所含有機溶劑被吸附於該吸附體之清淨氣體,從該圓筒狀轉子的內側排出;脫附區域,使加熱氣體從該圓筒狀轉子的內側往該吸附體流通,再將該有機溶劑從該吸附體脫附之濃縮氣體,從該圓筒狀轉子的外側排出;旋轉機構,藉由該圓筒狀轉子之該繞其軸線的旋轉,在該圓筒狀轉子的周向從該吸附區域移行至該脫附區域;密封體,將該吸附區域與該脫附區域分隔;脫附入口通道構件,形成了供該脫附區域的該加熱氣體流通之通道;脫附出口通道構件,形成了供該脫附區域的該濃縮氣體流通之通道。The adsorption treatment device according to the present invention includes: a cylindrical rotor, which is annular and can rotate around its axis; an adsorption body with an air flow path and a separator without an air flow path are alternately arranged; an adsorption area allows the treated material to be processed The gas flows from the outside of the cylindrical rotor to the adsorption body, and then the clean gas containing the organic solvent adsorbed on the adsorption body is discharged from the inside of the cylindrical rotor; the desorption area allows the heated gas to flow from the The inside of the cylindrical rotor flows to the adsorption body, and then the concentrated gas desorbed from the adsorption body is discharged from the outside of the cylindrical rotor; the rotating mechanism uses the winding of the cylindrical rotor. The rotation of its axis moves from the adsorption area to the desorption area in the circumferential direction of the cylindrical rotor; the sealing body separates the adsorption area from the desorption area; the desorption inlet channel member forms a space for the desorption area. The channel for the circulation of the heated gas in the attached area; the desorption outlet channel member forms a channel for the circulation of the concentrated gas in the desorption area.
上述密封體,包含:並設於上述圓筒狀轉子的旋轉方向之複數之密封構件、與固持複數之上述密封構件之固持構件;上述密封體,其複數之上述密封構件,欲分隔出上述吸附區域與上述脫附區域,就在上述圓筒狀轉子旋轉之際,可和上述分隔體滑動並接觸,以此方式設置於上述脫附入口通道構件以及上述脫附出口通道構件;藉由複數之上述密封構件中之和上述分隔體接觸滑動之上述密封構件,將上述吸附區域與上述脫附區域以氣密方式區隔。The above-mentioned sealing body includes: a plurality of sealing members disposed in parallel in the rotation direction of the above-mentioned cylindrical rotor, and a holding member that holds the plurality of the above-mentioned sealing members; the above-mentioned sealing body includes a plurality of the above-mentioned sealing members to separate the above-mentioned adsorption The area and the above-mentioned desorption area can slide and contact the above-mentioned partition when the above-mentioned cylindrical rotor rotates, and are provided in the above-mentioned desorption inlet channel member and the above-mentioned desorption outlet channel member in this way; by plural The sealing member among the sealing members that is in contact and sliding with the partition separates the adsorption area and the desorption area in an airtight manner.
其他形態當中,上述分隔體,係上述密封構件的接觸面往上述密封構件側膨起之形狀。In another aspect, the partition body has a shape in which the contact surface of the sealing member bulges toward the sealing member.
其他形態當中,上述密封體,係以可裝卸方式設於上述脫附入口通道構件以及上述脫附出口通道構件。 [發明之功效]In other forms, the sealing body is detachably provided on the desorption inlet channel member and the desorption outlet channel member. [The effect of invention]
根據此吸附處理裝置,可提供一種吸附處理裝置,所具備之構成可輕易進行密封構件的安裝等。According to this adsorption treatment device, it is possible to provide an adsorption treatment device having a structure that allows easy installation of the sealing member and the like.
以下,參照圖,同步對本實施形態的吸附處理裝置做說明。以下所說明之實施形態以及實施例當中,提及個數、數量等之情況下,除了有特別記載之情況外,本發明的範圍未必限定於該個數、數量等。對於同樣的零件,相等的零件,或許會賦予同樣的元件符號,不再重複說明。圖面當中,有幾處並未依照實際寸法的比率所圖示出,而是為了易於構造的理解,便以構造明確之方式,將比率變更所圖示出。Hereinafter, the adsorption processing device of this embodiment will be described simultaneously with reference to the drawings. In the embodiments and examples described below, when the number, quantity, etc. are mentioned, the scope of the present invention is not necessarily limited to the number, quantity, etc., unless otherwise stated. For the same parts, equal parts may be given the same component symbol, and the description will not be repeated. In the drawings, there are several parts that are not shown according to the actual scale ratios. Instead, in order to facilitate the understanding of the structure, the ratios are changed in a way that makes the structure clear.
圖1,係本實施形態相關吸附處理裝置的縱剖面圖;圖2,係圖1中的II-II線箭頭方向剖面圖;圖3,係圖1所示之圓筒狀轉子主要部位的放大剖面圖。參照圖1至圖3,針對本實施形態相關吸附處理裝置100做說明。Figure 1 is a longitudinal sectional view of the adsorption treatment device related to this embodiment; Figure 2 is a sectional view in the direction of the arrow line II-II in Figure 1; Figure 3 is an enlargement of the main parts of the cylindrical rotor shown in Figure 1 Sectional view. Referring to FIGS. 1 to 3 , the adsorption processing device 100 related to this embodiment will be described.
如圖1所示,本實施形態相關吸附處理裝置100,係將供給至處理室1內之大風量被處理流體F1中所含的被處理物質,利用後述之吸附體30加以吸附除去,再將淨化之清淨空氣F2排出。吸附處理裝置100,對吸附了經吸附除去之被處理物質的吸附體30噴吐少量的加熱流體F3,使被處理物質從該吸附體30脫附,作為濃縮流體F4排出。As shown in FIG. 1 , the adsorption processing device 100 according to this embodiment adsorbs and removes the to-be-processed substances contained in the fluid F1 with a large air volume supplied into the processing chamber 1 using an adsorbent 30 to be described later, and then removes the substances to be processed. The purified clean air F2 is discharged. The adsorption processing device 100 sprays a small amount of heated fluid F3 onto the adsorbent body 30 that has adsorbed the adsorbed and removed substance to be processed, so that the substance to be processed is desorbed from the adsorbent body 30 and discharged as a concentrated fluid F4.
被處理物質的吸附處理,係在後述之圓筒狀轉子90的吸附區域R2(參照圖3)進行。吸附區域R2,相當於吸附區域。被處理物質的脫附處理,係在後述之圓筒狀轉子90的脫附區域R1(參照圖3)進行。The adsorption process of the substance to be processed is performed in the adsorption area R2 (refer to FIG. 3) of the cylindrical rotor 90 mentioned later. The adsorption area R2 is equivalent to the adsorption area. The desorption process of the to-be-processed substance is performed in the desorption area R1 (refer FIG. 3) of the cylindrical rotor 90 mentioned later.
圓筒狀轉子90,設有用以使圓筒狀轉子90繞筒軸C旋轉的旋轉機構M1。藉由圓筒狀轉子90繞筒軸C的旋轉,對於通過脫附區域R1位於吸附區域R2之吸附體30進行吸附處理,對於吸附處理後通過吸附區域R2位於脫附區域R1之吸附體30進行脫附處理。像這樣,吸附處理裝置100當中,連續實施吸附處理以及脫附處理。The cylindrical rotor 90 is provided with a rotation mechanism M1 for rotating the cylindrical rotor 90 around the cylindrical axis C. By the rotation of the cylindrical rotor 90 about the cylindrical axis C, the adsorbent 30 passing through the desorption region R1 and located in the adsorption region R2 is adsorbed. Desorption treatment. In this way, in the adsorption processing apparatus 100, adsorption processing and desorption processing are continuously performed.
如圖1至圖3所示,吸附處理裝置100,包含:作為旋轉體的圓筒狀轉子90、第1流路形成構件2、作為入口部側流路形成構件的內周側流路形成構件4、以及作為出口部側流路形成構件的外周側流路形成構件5。As shown in FIGS. 1 to 3 , the adsorption processing device 100 includes a cylindrical rotor 90 as a rotating body, a first flow path forming member 2 , and an inner peripheral side flow path forming member as an inlet side flow path forming member. 4. And the outer peripheral side flow path forming member 5 as the outlet side flow path forming member.
圓筒狀轉子90,設置於處理室1內。圓筒狀轉子90,設置成可使流體往徑向流動。圓筒狀轉子90,設置成可繞筒軸C旋轉。本實施形態中,圓筒狀轉子90,令筒軸C方向朝向鉛直方向,由支柱等的複數之支持構件6以可旋轉方式所支持。The cylindrical rotor 90 is installed in the processing chamber 1 . The cylindrical rotor 90 is configured to allow fluid to flow in a radial direction. The cylindrical rotor 90 is provided rotatably around the cylindrical axis C. In the present embodiment, the cylindrical rotor 90 is rotatably supported by a plurality of supporting members 6 such as pillars with the cylindrical axis C directed in the vertical direction.
圓筒狀轉子90,由一對圓盤10、複數之分隔體20以及複數之吸附體30所構成。The cylindrical rotor 90 is composed of a pair of discs 10 , a plurality of partitions 20 and a plurality of adsorption bodies 30 .
一對圓盤10,係以互相面對之方式配置。一對圓盤10,包含第1圓盤11與第2圓盤12。第1圓盤11的中央部,設有開口部11a。第1圓盤11與第2圓盤12,從圓筒狀轉子90的筒軸C方向觀察之情況下,中心位置重疊,以此方式互相面對所配置。第1圓盤11以及第2圓盤12,係於兩者之間可配置分隔體20以及吸附體30之方式,隔出距離所設置。A pair of discs 10 are arranged to face each other. The pair of disks 10 includes a first disk 11 and a second disk 12 . The opening 11a is provided in the center of the first disk 11 . The first disk 11 and the second disk 12 are arranged to face each other so that their centers overlap when viewed from the direction of the cylindrical axis C of the cylindrical rotor 90 . The first disk 11 and the second disk 12 are installed at a distance so that the partition body 20 and the adsorption body 30 can be arranged therebetween.
複數之分隔體20,將一對圓盤10間的空間,分隔成在周向互相獨立之複數之空間部S(參照圖3)。具體而言,複數之分隔體20,從筒軸C方向觀察之情況下,第1圓盤11與第2圓盤12重疊部分當中一對圓盤10間的空間,分隔成在周向互相獨立之複數之空間部S。The plurality of partitions 20 divides the space between the pair of disks 10 into a plurality of space portions S that are mutually independent in the circumferential direction (see FIG. 3 ). Specifically, when viewed from the direction of the cylinder axis C of the plurality of partitions 20, the space between a pair of disks 10 in the overlapping portion of the first disk 11 and the second disk 12 is separated into independent spaces in the circumferential direction. The spatial part S of the complex number.
複數之分隔體20,其等的中心O(參照圖3)以既定的間距於周向並列之方式配置。複數之分隔體20,以於筒軸C方向氣密以及/或是液密之方式安裝於一對圓盤10間。A plurality of partitions 20 are arranged so that their centers O (see FIG. 3 ) are juxtaposed in the circumferential direction with a predetermined spacing. A plurality of partitions 20 are installed between the pair of discs 10 in an airtight and/or liquidtight manner in the direction of the cylinder axis C.
複數之吸附體30,分別收納於互相獨立之複數之空間部S。複數之吸附體30,以既定的間距於周向並列。吸附體30,具有例如方塊狀。The plurality of adsorption bodies 30 are respectively accommodated in a plurality of mutually independent space portions S. A plurality of adsorption bodies 30 are juxtaposed in the circumferential direction at a predetermined distance. The adsorption body 30 has, for example, a square shape.
吸附體30,由含有活性氧化鋁、矽膠、活性碳、沸石的任一者之吸附材料所構成。較佳的是,吸附體30,利用粒狀、紛體狀、蜂巢狀等的活性碳、沸石。活性碳、沸石,優於吸附以及脫附低濃度的有機化合物。令其為蜂巢狀,藉此可使流體的壓力損失減少,可使處理能力增加。再者,可抑制塵粒等的固形物之堵塞。The adsorbent 30 is composed of an adsorbent material containing any one of activated alumina, silica gel, activated carbon, and zeolite. Preferably, the adsorbent 30 is made of activated carbon or zeolite in the form of granules, powders, honeycombs, or the like. Activated carbon and zeolite are better at adsorbing and desorbing low-concentration organic compounds. By making it a honeycomb shape, the pressure loss of the fluid can be reduced and the processing capacity can be increased. Furthermore, clogging by solid matter such as dust particles can be suppressed.
在一對圓盤10間,由複數之分隔體20與複數之吸附體30交互於周向複數之並列而成圓筒狀所構成之圓筒狀轉子90當中,以和第1圓盤11的開口部11a連通之方式,形成了中央空間部90a。Between a pair of disks 10 , a plurality of partitions 20 and a plurality of adsorption bodies 30 alternate in a cylindrical rotor 90 composed of a plurality of parallel cylindrical shapes in the circumferential direction. The openings 11a communicate with each other to form a central space 90a.
第1流路形成構件2的一端側,讓第1流路形成構件2的內部與圓筒狀轉子90的中央空間部90a維持氣密,並且容許圓筒狀轉子90繞筒軸C旋轉。具體而言,例如,於第1流路形成構件2的一端側設有凸緣部,藉由位於該凸緣部與開口部11a周緣之部分的第1圓盤11,來挾持環狀的密封構件。第1流路形成構件2的另一端側,引出處理室1外。One end side of the first flow path forming member 2 allows the cylindrical rotor 90 to rotate around the cylindrical axis C while maintaining airtightness between the inside of the first flow path forming member 2 and the central space 90 a of the cylindrical rotor 90 . Specifically, for example, a flange is provided on one end side of the first flow path forming member 2, and an annular seal is held by the first disk 11 located between the flange and the periphery of the opening 11a. component. The other end side of the first flow path forming member 2 is led out of the processing chamber 1 .
圓筒狀轉子90的內周側即中央空間部90a,配設有構成脫附入口通道構件之內周側流路形成構件4。圓筒狀轉子90的外周側,配設有構成脫附出口通道構件之外周側流路形成構件5。內周側流路形成構件4以及外周側流路形成構件5,以夾入周向當中圓筒狀轉子90的一部分之方式,在圓筒狀轉子90的內周側以及外周側當中互相面對所配設。The inner circumferential side flow
內周側流路形成構件4,在中央空間部90a內沿著筒軸C方向延設,從開口部11a朝圓筒狀轉子90的外側伸出,以此方式設置。The inner circumferential side flow
內周側流路形成構件4的一端側,設有面向圓筒狀轉子90的內周側之內周側開口端部4a。內周側開口端部4a當中的開口面,以面對周向當中圓筒狀轉子90的內周側的一部分區域之方式設置。該開口面,在內周側流路形成構件4的第1圓盤11以及第2圓盤12之間,於筒軸C方向面對圓筒狀轉子90的內周側,以此方式設置。內周側流路形成構件4的另一端側,從設於第1流路形成構件2之開口部2a往第1流路形成構件2的外側突出。One end side of the inner peripheral side flow
外周側流路形成構件5的一端側,設有面向圓筒狀轉子90的外周側之外周側開口端部5a。外周側開口端部5a的開口面,以面對周向當中圓筒狀轉子的外周側的一部分區域之方式設置。該開口面,在第1圓盤11以及第2圓盤12之間,於筒軸C方向面對圓筒狀轉子90的外周側之方式設置。One end side of the outer peripheral side flow path forming member 5 is provided with an outer peripheral side opening end portion 5 a facing the outer peripheral side of the cylindrical rotor 90 . The opening surface of the outer peripheral side open end 5a is provided so as to face a part of the outer peripheral side area of the cylindrical rotor in the circumferential direction. This opening surface is provided between the first disk 11 and the second disk 12 so as to face the outer peripheral side of the cylindrical rotor 90 in the direction of the cylindrical axis C.
如圖2以及圖3所示,圓筒狀轉子90,包含於周向區隔之脫附區域R1以及吸附區域R2。複數之吸附體30,藉由圓筒狀轉子90的旋轉,使脫附區域R1與吸附區域R2交互移動。As shown in FIGS. 2 and 3 , the cylindrical rotor 90 includes a desorption region R1 and an adsorption region R2 separated in the circumferential direction. The plurality of adsorption bodies 30 alternately move the desorption region R1 and the adsorption region R2 by the rotation of the cylindrical rotor 90 .
圓筒狀轉子90,於內周側開口端部4a以及外周側開口端部5a,設有密封體40。該密封體40的詳細構成則於後述之。密封體40,並設於圓筒狀轉子90的旋轉方向(圖2,圖3中箭頭方向)。密封體40,包含內側密封體41與外側密封體42。The cylindrical rotor 90 is provided with a sealing
內側密封體41,係以將內周側開口端部4a從圓筒狀轉子90的上游側以及下游側夾入之方式,成對設置。外側密封體42,也是以將外周側開口端部5a從圓筒狀轉子90的上游側以及下游側夾入之方式,成對設置。The
分隔體20,包含和密封體40所設之密封構件430(參照圖6)滑動並接觸之接觸面21、22。分隔體20,從筒軸C方向觀察之情況下,具有梯形狀。The partition body 20 includes contact surfaces 21 and 22 that slide and come into contact with the sealing member 430 (see FIG. 6 ) provided in the sealing
接著,參照圖4至圖7,針對本實施形態的密封體40的構成做說明。圖4,係密封體的放大立體圖;圖5,係內側密封體41的構成之示圖;圖6,係密封構件430的構成之示圖;圖7,係外側密封體42的構成之示圖。Next, the structure of the sealing
如上所述,密封體40,包含:配置於內周側開口端部4a側之一對內側密封體41、與配置於外周側開口端部5a側之一對外側密封體42。As described above, the sealing
內側密封體41,預先設有複數之螺孔BH,利用螺絲等扣接固定於內周側開口端部4a側。外側密封體42,也予先設有複數之螺孔BH,利用螺絲等扣接固定於內周側開口端部4a側。The
如圖5以及圖6所示,內側密封體41,包含:往筒軸C的軸向延伸之基底構件411、與利用螺絲B等固定於該基底構件411之複數之密封構件430。基底構件411,包含:往筒軸C的軸向延伸之基底411b、筒軸C的軸向的基底411b的端部所設之端部托架411a、與基底411b的側部所設之側部托架411c。基底411b,係以沿著圓筒狀轉子90內側的圓弧狀之方式設置成彎曲狀。端部托架411a以及側部托架411c,設有上述之螺孔BH。As shown in FIGS. 5 and 6 , the
內側密封體41,有5處固定有密封構件430。內側密封體41所設之密封構件430的數量,可因應對吸附處理裝置100要求之規格做適當選擇。The
如圖6所示,為密封構件430的橫剖面,以沿著筒軸C的軸向延伸之方式設置。密封構件430,具有以下構成:由橡膠構件等所構成之片狀的密封材料431,被夾入剖面為C字狀的內側夾入板432以及外側夾入板433,使得密封材料431成2列直立。直立之密封材料431的間距,最好是,比分隔體20內側的接觸面21的寬度更小為宜。這是因為,即使一方的密封材料431故障,也可藉由另一方的密封材料431來確保氣密性。密封材料431,被夾入內側夾入板432以及外側夾入板433之狀態下,利用螺絲扣接,藉由一齊鎖緊來固定於基底411b。As shown in FIG. 6 , it is a cross section of the sealing member 430 and is provided so as to extend along the axial direction of the cylindrical axis C. The sealing member 430 has the following structure: a sheet-shaped sealing material 431 made of a rubber member or the like is sandwiched between an inner sandwiching plate 432 and an outer sandwiching plate 433 having a C-shaped cross section, so that the sealing materials 431 are arranged in two rows. upright. The distance between the upright sealing materials 431 is preferably smaller than the width of the contact surface 21 on the inside of the partition 20 . This is because even if one of the sealing materials 431 fails, the airtightness can be ensured by the other sealing material 431 . The sealing material 431 is fixed to the base 411b by locking together with screws in a state of being sandwiched between the inner sandwich plate 432 and the outer sandwich plate 433.
參照圖7,外側密封體42,包含:往筒軸C的軸向延伸之基底構件421、與利用螺絲B等固定於該基底構件421之複數之密封構件430。基底構件421,包含:往筒軸C的軸向延伸之基底421b、筒軸C的軸向之基底421b的端部所設之端部托架421a、與基底421b的側部所設之側部托架421c。基底421b,係以沿著圓筒狀轉子90外側的圓弧狀之方式設置成彎曲狀。端部托架421a以及側部托架421c,設有上述之螺孔BH。Referring to FIG. 7 , the
外側密封體42,有5處固定有密封構件430。外側密封體42所設之密封構件430,和內側密封體41只有寬度不同,構成係相同。直立之密封材料431的間距,最好是,比分隔體20外側的接觸面22的寬度更小為宜。這是因為,即使一方的密封材料431故障,也可藉由另一方的密封材料431來確保氣密性。內側密封體41所設之密封構件430的數量,可因應對吸附處理裝置100要求之規格做適當選擇。The
具備以上構成之密封體40,其複數之密封構件430,欲分隔出吸附區域R2與脫附區域R1,就在圓筒狀轉子90旋轉之際,可和分隔體20滑動並接觸,以此方式設置於脫附入口通道構件即內周側流路形成構件4以及脫附出口通道構件即外周側流路形成構件5,藉由複數之密封構件430中之和分隔體20接觸滑動之密封構件430,將吸附區域R2與脫附區域R1以氣密方式區隔。In the sealing
再次,參照圖1至圖3,圓筒狀轉子90,區隔成脫附區域R1與吸附區域R2。脫附區域R1,對於內周側流路形成構件4以及外周側流路形成構件5氣密連通。吸附區域R2,未和內周側流路形成構件4以及外周側流路形成構件5連通,構成了和脫附區域R1不同之流路。Again, referring to FIGS. 1 to 3 , the cylindrical rotor 90 is divided into a desorption region R1 and an adsorption region R2. The desorption region R1 is in airtight communication with the inner peripheral flow
脫附區域R1以及吸附區域R2,分別導入流體。通過吸附區域R2之流體的流動方向、與通過脫附區域R1之流體的流動方向,在圓筒狀轉子90的徑向的方向當中為逆向,為較佳者。Fluid is introduced into the desorption region R1 and the adsorption region R2 respectively. It is preferable that the flow direction of the fluid passing through the adsorption region R2 and the flow direction of the fluid passing through the desorption region R1 be opposite to each other in the radial direction of the cylindrical rotor 90 .
使流體,通過位於內周側流路形成構件4周圍之部分圓筒狀轉子90的中央空間部90a,從第1圓盤11的開口部11a流出,以此方式從圓筒狀轉子90的外周側往內周側導入吸附區域R2。The fluid passes through the central space 90a of the cylindrical rotor 90 located around the inner peripheral side flow
另一方面,使流體,穿過通過第1圓盤11的開口部11a之內周側流路形成構件4後,從圓筒狀轉子90的內周側通往外周側,以此方式導入脫附區域R1。On the other hand, the fluid passes through the inner circumferential side flow
導入吸附區域R2之流體,係排放氣體等的被處理流體。該被處理流體,包含作為被處理物質的有機溶劑。吸附區域R2當中,進行被處理流體的淨化。The fluid introduced into the adsorption region R2 is a fluid to be processed such as exhaust gas. The fluid to be processed contains an organic solvent as a substance to be processed. In the adsorption area R2, the fluid to be processed is purified.
在淨化之際,首先,對於圓筒狀轉子90的吸附區域R2,以從圓筒狀轉子90的外周側往內周側之方式,導入排放氣體。已導入吸附區域R2之排放氣體,沿著徑向通過圓筒狀轉子90之際,藉由位於吸附區域R2之複數之吸附體30將有機溶劑吸附除去,得到淨化。During purification, first, the exhaust gas is introduced into the adsorption region R2 of the cylindrical rotor 90 from the outer circumferential side to the inner circumferential side of the cylindrical rotor 90 . When the exhaust gas introduced into the adsorption area R2 passes through the cylindrical rotor 90 in the radial direction, the organic solvent is adsorbed and removed by the plurality of adsorption bodies 30 located in the adsorption area R2, and is purified.
淨化過的排放氣體,作為清淨空氣從吸附區域R2流入圓筒狀轉子90的中央空間部90a。已流入圓筒狀轉子90的中央空間部90a之清淨空氣,通過位於內周側流路形成構件4周圍之部分圓筒狀轉子的中央空間部90a,從第1圓盤11的開口部11a流出。從開口部11a流出之清淨空氣,通過第1流路形成構件2往處理室1外排出。The purified exhaust gas flows from the adsorption region R2 into the central space 90 a of the cylindrical rotor 90 as clean air. The clean air that has flowed into the central space 90 a of the cylindrical rotor 90 passes through the central space 90 a of the cylindrical rotor located around the inner peripheral flow
導入脫附區域R1之流體,係加熱空氣等的加熱流體。脫附區域R1當中,將吸附體30所吸附之有機溶劑脫附,藉以進行吸附體30的再生,並且產生有機溶劑濃度變高之濃縮流體。The fluid introduced into the desorption region R1 is a heating fluid such as heated air. In the desorption region R1, the organic solvent adsorbed by the adsorbent 30 is desorbed, thereby regenerating the adsorbent 30 and generating a concentrated fluid with a higher concentration of organic solvent.
為了進行有機溶劑的脫附,便從內周側流路形成構件4的另一端側導入加熱空氣。從內周側流路形成構件4的另一端側導入之加熱空氣,穿過通過第1圓盤11的開口部11a之內周側流路形成構件4的內部,從內周側流路形成構件4的一端側,導入脫附區域R1。In order to desorb the organic solvent, heated air is introduced from the other end side of the inner peripheral flow
已導入脫附區域R1之加熱空氣,從圓筒狀轉子90的內周側往外周側通過圓筒狀轉子90之際,藉熱使位於脫附區域R1之複數之吸附體30所吸附之有機溶劑脫附。含有有機溶劑之加熱空氣,作為濃縮流體,從脫附區域R1往外周側流路形成構件5排出。往外周側流路形成構件5排出之濃縮流體,導入進行回收或是燃燒等後段處理之後處理裝置。When the heated air introduced into the desorption area R1 passes through the cylindrical rotor 90 from the inner circumferential side to the outer circumferential side, the organic matter adsorbed by the plurality of adsorbents 30 located in the desorption area R1 is heated. Solvent desorption. The heated air containing the organic solvent is discharged from the desorption region R1 to the outer peripheral flow path forming member 5 as a concentrated fluid. The concentrated fluid discharged from the outer peripheral side flow path forming member 5 is introduced into a post-processing device for post-processing such as recovery or combustion.
在此之際,密封體40所設之複數之密封構件430,欲分隔出吸附區域R2與脫附區域R1,就在圓筒狀轉子90旋轉之際,可和分隔體20滑動並接觸,以此方式設置於脫附入口通道構件即內周側流路形成構件4以及脫附出口通道構件即外周側流路形成構件5。因此,藉由複數之密封構件430中之和分隔體20接觸滑動之密封構件430,將吸附區域R2與脫附區域R1以氣密方式區隔。At this time, the plurality of sealing members 430 provided in the sealing
密封體40,因為複數之密封構件430以一體構成,所以吸附處理裝置100的組裝時,可輕易將密封體40安裝於內周側開口端部4a以及外周側開口端部5a。Since the sealing
吸附處理裝置100的運轉後,密封構件430有損傷之情況下,來到密封構件430的更換時期之情況下,都將密封體40作為零件處置,藉此可輕易更換成新的密封體40。After the operation of the adsorption processing device 100 , if the sealing member 430 is damaged or when it is time to replace the sealing member 430 , the sealing
(其他的分隔體20A) 參照圖8,針對其他形態的分隔體20A做說明。圖8,係其他形態的分隔體20A的構成之示圖。上述實施形態中,分隔體20的接觸面21以及接觸面22,為平坦面,但如圖8所示之分隔體20A所示,亦可為往密封構件430側膨起之接觸面21a以及接觸面22a的形狀。因此,與密封材料431的接觸面積擴大,能藉由密封構件430更加確保氣密性。(Other dividers 20A) Referring to FIG. 8 , another form of partition 20A will be described. FIG. 8 is a diagram showing the structure of another form of partition body 20A. In the above embodiment, the contact surface 21 and the contact surface 22 of the separator 20 are flat surfaces. However, as shown in the separator 20A shown in FIG. 8, they may also be the contact surface 21a and the contact surface 21a that bulge toward the sealing member 430 side. The shape of surface 22a. Therefore, the contact area with the sealing material 431 is enlarged, and the airtightness of the sealing member 430 can be further ensured.
(其他的吸附處理裝置100A) 上述實施形態的吸附處理裝置100,係圓筒狀轉子90的筒軸C沿著鉛直方向延伸之方式所配置之縱型吸附處理裝置。可是,並不限於此構成,上述構成,如圖9的吸附處理裝置100A所示,即使是圓筒狀轉子90的筒軸C沿著水平方向延伸之方式所配置橫型吸附處理裝置100A,也可得到和縱型吸附處理裝置100同樣的作用效果。(Other adsorption treatment device 100A) The adsorption treatment device 100 of the above embodiment is a vertical adsorption treatment device arranged so that the cylindrical axis C of the cylindrical rotor 90 extends in the vertical direction. However, the configuration is not limited to this configuration. As shown in the adsorption processing device 100A in FIG. 9 , even if the horizontal adsorption processing device 100A is arranged such that the cylindrical axis C of the cylindrical rotor 90 extends in the horizontal direction, The same functions and effects as those of the vertical adsorption treatment device 100 can be obtained.
以上,針對本發明的實施形態做了說明,但本此所揭示之實施形態在所有面向中僅為例示,並非加以限制。本發明的範圍係由申請專利範圍所表示,與申請專利均等的意思以及範圍內的所有變更均包含在內。The embodiments of the present invention have been described above. However, the embodiments disclosed here are only illustrative in all respects and are not restrictive. The scope of the present invention is represented by the scope of the patent application, and all changes within the scope are intended to be equivalent to the patent application.
1:處理室 2:第1流路形成構件 2a,11a:開口部 4:內周側流路形成構件 4a:內周側開口端部 5:外周側流路形成構件 5a:外周側開口端部 6:支持構件 10:圓盤 11:第1圓盤 12:第2圓盤 20,20A:分隔體 21,21a,22,22a:接觸面 30:吸附體 40:密封體 41:內側密封體 42:外側密封體 90:圓筒狀轉子 90a:中央空間部 100,100A:吸附處理裝置 411,421:基底構件 411a,421a:端部托架 411b,421b:基底 411c,421c:側部托架 430:密封構件 431:密封材料 432,433:夾入板 B:螺絲 BH:螺孔 C:筒軸 F1:被處理流體 F2:清淨空氣 F3:加熱流體 F4:濃縮流體 M1:旋轉機構 O:中心 R1:脫附區域 R2:吸附區域 S:空間部1: Processing room 2: First flow path forming member 2a,11a: opening 4: Inner peripheral side flow path forming member 4a: Inner peripheral side open end 5: Outer peripheral side flow path forming member 5a: Open end on outer peripheral side 6: Support components 10: disc 11: 1st disc 12: 2nd disc 20,20A: Divider 21,21a,22,22a: Contact surface 30: Adsorption body 40:Sealed body 41:Inner sealing body 42:Outside sealing body 90: Cylindrical rotor 90a: Central Space Department 100,100A: Adsorption treatment device 411,421: Base component 411a, 421a: end bracket 411b, 421b: Base 411c, 421c: Side bracket 430:Sealing component 431:Sealing materials 432,433: Clamping plate B:Screw BH: screw hole C:Thru shaft F1: Fluid to be processed F2: Clean air F3: Heating fluid F4: Concentrated fluid M1: Rotating mechanism O:center R1: desorption area R2: adsorption area S: Space Department
圖1係實施形態的吸附處理裝置的縱剖面圖。 圖2係圖1中的II-II線箭頭方向剖面圖。 圖3係圖1所示之圓筒狀轉子主要部位的放大剖面圖。 圖4係密封體的放大立體圖。 圖5係內側密封體的構成之示圖。 圖6係密封構件的構成之示圖。 圖7係外側密封體的構成之示圖。 圖8係其他形態的分隔體的構成之示圖。 圖9係其他實施形態的吸附處理裝置的外觀圖。Fig. 1 is a longitudinal sectional view of the adsorption treatment device according to the embodiment. Figure 2 is a cross-sectional view in the direction of the arrow on line II-II in Figure 1. Figure 3 is an enlarged cross-sectional view of the main parts of the cylindrical rotor shown in Figure 1. Figure 4 is an enlarged perspective view of the sealing body. Figure 5 is a diagram showing the structure of the inner sealing body. Fig. 6 is a diagram showing the structure of the sealing member. Figure 7 is a diagram showing the structure of the outer seal body. Figure 8 is a diagram illustrating the structure of another form of separator. Fig. 9 is an external view of an adsorption treatment device according to another embodiment.
4:內周側流路形成構件 4: Inner peripheral side flow path forming member
4a:內周側開口端部 4a: Inner peripheral side open end
5:外周側流路形成構件 5: Outer peripheral side flow path forming member
5a:外周側開口端部 5a: Open end on outer peripheral side
20:分隔體 20:Divider
21,22:接觸面 21,22: Contact surface
30:吸附體 30: Adsorption body
40:密封體 40:Sealed body
41:內側密封體 41:Inner sealing body
42:外側密封體 42:Outside sealing body
F3:加熱流體 F3: Heating fluid
F4:濃縮流體 F4: Concentrated fluid
O:中心 O:center
R1:脫附區域 R1: desorption area
R2:吸附區域 R2: adsorption area
S:空間部 S: Space Department
Claims (3)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2019-085911 | 2019-04-26 | ||
JP2019085911 | 2019-04-26 |
Publications (2)
Publication Number | Publication Date |
---|---|
TW202108228A TW202108228A (en) | 2021-03-01 |
TWI826680B true TWI826680B (en) | 2023-12-21 |
Family
ID=72942018
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW109113123A TWI826680B (en) | 2019-04-26 | 2020-04-20 | Adsorption treatment device |
Country Status (5)
Country | Link |
---|---|
JP (1) | JPWO2020217857A1 (en) |
KR (1) | KR20220002395A (en) |
CN (1) | CN113747964A (en) |
TW (1) | TWI826680B (en) |
WO (1) | WO2020217857A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2023175463A1 (en) * | 2022-03-18 | 2023-09-21 | Svante Inc. | Scalable sorptive gas separator and method of operation |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04131424U (en) * | 1991-05-23 | 1992-12-03 | 日立造船株式会社 | Purification equipment for NOx-containing gas |
US5169414A (en) * | 1990-07-03 | 1992-12-08 | Flakt, Inc. | Rotary adsorption assembly |
US6447583B1 (en) * | 1999-06-04 | 2002-09-10 | Flair Corporation | Rotating drum adsorber process and system |
CN104941389A (en) * | 2014-03-26 | 2015-09-30 | 株式会社西部技研 | Rotary type gas adsorption concentration device |
CN207254040U (en) * | 2017-08-03 | 2018-04-20 | 可迪尔空气技术(北京)有限公司 | Cartridge type zeolite runner enrichment facility |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57131424U (en) * | 1981-02-12 | 1982-08-16 | ||
JPH0694185B2 (en) * | 1990-02-27 | 1994-11-24 | ダイキン工業株式会社 | Fluorocarbon rubber sponge laminate and honeycomb rotor device using the same |
US5057128A (en) * | 1990-07-03 | 1991-10-15 | Flakt, Inc. | Rotary adsorption assembly |
JP4004195B2 (en) * | 1999-10-29 | 2007-11-07 | 株式会社大気社 | Rotating type adsorption / desorption type gas treatment equipment |
JP2006068582A (en) * | 2004-08-31 | 2006-03-16 | Seibu Giken Co Ltd | Rotary gas adsorption and concentration device |
JP4960985B2 (en) * | 2009-03-27 | 2012-06-27 | 株式会社大気社 | Adsorption rotor type gas processing apparatus and adsorption rotor manufacturing method |
CN107708839B (en) * | 2015-07-03 | 2021-09-24 | 东洋纺株式会社 | Adsorption treatment device |
CN108295620A (en) * | 2018-01-26 | 2018-07-20 | 华北理工大学 | A kind of zeolite rotating cylinder and its adsorption cleaning system |
-
2020
- 2020-03-27 JP JP2020550193A patent/JPWO2020217857A1/ja active Pending
- 2020-03-27 WO PCT/JP2020/014228 patent/WO2020217857A1/en active Application Filing
- 2020-03-27 KR KR1020217037781A patent/KR20220002395A/en active Search and Examination
- 2020-03-27 CN CN202080032166.5A patent/CN113747964A/en active Pending
- 2020-04-20 TW TW109113123A patent/TWI826680B/en active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5169414A (en) * | 1990-07-03 | 1992-12-08 | Flakt, Inc. | Rotary adsorption assembly |
JPH04131424U (en) * | 1991-05-23 | 1992-12-03 | 日立造船株式会社 | Purification equipment for NOx-containing gas |
US6447583B1 (en) * | 1999-06-04 | 2002-09-10 | Flair Corporation | Rotating drum adsorber process and system |
CN104941389A (en) * | 2014-03-26 | 2015-09-30 | 株式会社西部技研 | Rotary type gas adsorption concentration device |
CN207254040U (en) * | 2017-08-03 | 2018-04-20 | 可迪尔空气技术(北京)有限公司 | Cartridge type zeolite runner enrichment facility |
Also Published As
Publication number | Publication date |
---|---|
JPWO2020217857A1 (en) | 2020-10-29 |
WO2020217857A1 (en) | 2020-10-29 |
TW202108228A (en) | 2021-03-01 |
CN113747964A (en) | 2021-12-03 |
KR20220002395A (en) | 2022-01-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6516003B2 (en) | Adsorption processing unit | |
US6514318B2 (en) | Multistage system for separating gas by adsorption | |
CN101927150B (en) | Radial flow continuous reaction/regeneration apparatus | |
JP7244651B2 (en) | Separation device and separation method | |
JPH06343814A (en) | Rotary adsorption and desorption type gas treating device | |
JP6747442B2 (en) | Adsorption processing device | |
US11439934B2 (en) | Capture device for purifying air, purification device and air purifier | |
TWI826680B (en) | Adsorption treatment device | |
JP7028161B2 (en) | Adsorption processing equipment | |
JP7532373B2 (en) | Regenerative separation apparatus for separating impurities from an air stream | |
JP2012020226A (en) | Device for treating organic solvent-containing gas | |
JP3241010U (en) | Adsorption unit, adsorption treatment device, and treatment system | |
WO2023203888A1 (en) | Adsorption rotor and adsorption rotor accommodation device | |
JPH10156128A (en) | Rotary cylinder type gas concentrator | |
TW202218737A (en) | Adsorption unit, adsorption processing device, and processing system | |
CN216909760U (en) | VOCs exhaust purification device | |
KR100526636B1 (en) | Organic solvent adsorption concentration equipment | |
JP2002507477A (en) | Apparatus for processing gas using adsorption disk filter | |
CN114288821A (en) | VOCs exhaust purification device | |
KR20120133846A (en) | Rotary VOC Concentrator using Pellet Adsorbent | |
JP2010051877A (en) | Apparatus and method for manufacturing oxygen enriched air | |
JP3244814B2 (en) | Rotary valve type continuous gas separator | |
JPH05200225A (en) | Pressure swing type gas separator | |
JPS61209025A (en) | Gas adsorbing and separation apparatus | |
JP2022039976A (en) | Organic solvent recovery system |