M355357 五、新型說明： 【新型所屬之技術領域】 種利用化學吸附劑之乾燥設備 本創作係關於一種乾燥設備，尤其指一 【先前技術】 習知之氣體除濕乾燥設備大致可分為兩類，一類為係利用冷媒除濕原 理，另-類則利用化學藥劑吸附原理。化學吸附乾燥設備係以化學吸附劑， 如氧脑等’直接·«㈣水分。傳_觸設備—般包含兩個乾燥 桶，一個祕進行氣_観反應，另—個_於化學吸_的再生反應。 當含水氣體雜，進人糾-個細叫，氣财齡分會被桶内 所含有的乾燥_所吸收，並以乾燥狀態從排氣嶋出。當_的化學藥 劑反應完畢、無法再韻水分時，就必須進行再生侧，藉靖化學吸附 劑中所含有的水分絲，使其_再度恢復蘭水分姐力。目前多是將 外部的再生氣源導人再生桶中，儀未達飽和濕度的再生氣源將化學吸附 劑中所含的水分帶h但是，由於其所導人的再线職往因溫度較低， 飽和濕度亦較低，吸附水分的能力不佳，除濕效率有限，故再生過程中需 耗費大量的能源成本及咖。m此如何提高乾_水效率以及再生設備化 學藥劑的反應能力，乃為產業界之一迫切課題。 【新型内容】 為克服上述之缺點，本創作係提供一種吸附式乾燥設備，包含有兩個 内部盛有乾燥劑之反應桶及再生桶，其中反應桶係用於進行氣體之乾燥反 應，而再生桶則用於進行乾燥劑的再生反應。吸附式乾燥設備亦包含有與 反應桶和再生桶相互連接的進氣裝置及出氣裝置；進氣裝置係將乾燥前之 潮濕氣體導入反應桶，而出氣裝置則係將乾燥完成後之再生氣源自反應桶 3 M355357 排出。此外，在反應桶及再生桶上均裝設有加熱裝置，用以加熱再生桶。 而吸附式乾燥設備還包含有與反應桶及再生桶連接的排水裝置，以及與排 水襞置連接的真空裝置》 一 本創作之主要目的在於提供一種吸附式乾燥設備，由於具有加熱裝 置’可提高其乾燥藥劑之再生效率。 本創作之次要目的在於提供一種吸附式乾燥設備，由於具有與排水裴 置連接的真空裝置，可提高乾燥排水效率。 义 本創作亦提供另一種吸附式乾燥設備，包含有兩個内部盛有乾燥劑之 _反應滅再錢，其巾反賴侧於進行纽之鶴反應，而再生桶則用 於進行乾燥劑的再生反應。吸附式乾燥設備亦包含有與反應桶和再生桶相 互連接的進氣裝置及出氣裝置；進氣裝置係將乾燥前之潮濕氣體導入反應 桶’而出氣裝置則係將乾燥完成後之再生氣源自反應桶排出。此外，在^ 應桶及再生桶上均裝設有加絲置，⑽加熱再生桶。而吸附式乾燥設備 還包含有與反應桶及再生桶連接的排水裝置。 本創作之另-目的在於提供-種吸附式乾燥設備，由於具有加熱裝 置’可提高其乾燥藥劑之再生效率。 梢作雜供再-觀喊錢設備，包含有确崎盛有乾燥劑之 反應桶及再生桶，其巾反躺剌於進行驗之乾燥反應，而再生桶則用 於進行乾燥劑的再生反應。吸附式乾燥設備亦包含有與反應桶和再生桶相 互連接的進氣裝置及出氣裝置；進綠置係將乾祕之潮濕氣體導入反應 桶’而出氣裝置職將乾燥完紐之再錢源自反脑排出。此外，吸附 式乾燥α又備還包含有與反應桶及再生桶連接的排水裝置，以及與排水裝置 連接的真空裝置。 本創作之又-目的在於提供另-麵赋賴設備，由於具有與排水 裝置連接的真空裝置，可提高乾燥排水效率。 M355357 【實施方式】 由於本創作係揭露-種吸附式乾燥設備，其中所利用到的乾燥設備元 件之結合方式與化學_乾_理，闕於該領域具#專業知識之人士所 能輕易理解者’故以下文中之說明，不再作完整描述。而以下文中所對照 之圖式係表達與本創作特徵有關之結構示意，並未亦不需要依據實際尺 寸完整繪製，合先敘明。 ”M355357 V. New description: [New technology field] Drying equipment using chemical adsorbent This paper is about a drying equipment, especially one [prior art]. The conventional gas dehumidifying drying equipment can be roughly divided into two categories, one type In order to utilize the principle of refrigerant dehumidification, the other class uses the principle of chemical adsorption. The chemical adsorption drying equipment is a chemical adsorbent such as oxygen brain or the like. The _ touch device generally contains two drying barrels, one for the gas _ 観 reaction, and the other for the chemical absorption _ regeneration reaction. When the water-containing gas is mixed, the person is squeaked and screamed, and the gas-aged age is absorbed by the dry _ contained in the barrel, and is taken out from the exhaust in a dry state. When the chemical reaction of _ is completed and the water cannot be re-grined, it is necessary to carry out the regeneration side, and the moisture contained in the chemical adsorbent of Jingjing is used to restore the blue water. At present, most of the external regenerative gas source is introduced into the regenerative barrel. The regenerative gas source that does not reach the saturation humidity brings the moisture contained in the chemical adsorbent to h. However, due to the temperature of the re-routed person Low, saturated humidity is also low, the ability to absorb water is not good, and the dehumidification efficiency is limited, so it takes a lot of energy costs and coffee in the regeneration process. m How to improve the dry_water efficiency and the reaction ability of the chemical equipment for recycling equipment is an urgent issue in the industry. [New content] In order to overcome the above shortcomings, the present invention provides an adsorption drying apparatus comprising two reaction tanks and a regeneration tank containing a desiccant therein, wherein the reaction barrel is used for gas drying reaction and regeneration The barrel is used to carry out the regeneration reaction of the desiccant. The adsorption drying device also includes an air inlet device and an air outlet device connected to the reaction barrel and the regeneration barrel; the air inlet device introduces the humid gas before drying into the reaction barrel, and the air outlet device is the regeneration gas source after the drying is completed. Discharged from the reaction tank 3 M355357. In addition, heating means are arranged on the reaction barrel and the regeneration barrel to heat the regeneration barrel. The adsorption drying device further comprises a drainage device connected to the reaction barrel and the regeneration barrel, and a vacuum device connected to the drainage device. The main purpose of the creation is to provide an adsorption drying device which can be improved by having a heating device. The regeneration efficiency of the dried medicament. The secondary objective of this creation is to provide an adsorption drying apparatus that has improved vacuum drainage efficiency due to a vacuum unit connected to the drain. Yiben Creation also offers another type of adsorption drying equipment, which contains two internal dehumidification agents, which are used to carry out the desiccant. Regeneration reaction. The adsorption drying device also includes an air inlet device and an air outlet device connected to the reaction barrel and the regeneration barrel; the air inlet device introduces the humid gas before drying into the reaction barrel, and the air outlet device is the regeneration gas source after the drying is completed. Exhausted from the reaction tank. In addition, a wire setting device is installed on both the barrel and the regeneration barrel, and (10) the regeneration barrel is heated. The adsorption drying device also includes a drainage device connected to the reaction tank and the regeneration tank. Another object of the present invention is to provide an adsorption drying apparatus which has improved regeneration efficiency of the dried medicament by having a heating means. The tip of the miscellaneous supply and re-examination of the money equipment, including the reaction tank and the regenerative barrel containing the desiccant, the towel is lying on the drying reaction for the test, and the regeneration tank is used for the regeneration reaction of the desiccant. . The adsorption drying device also includes an air inlet device and an air outlet device connected to the reaction barrel and the regeneration barrel; the green setting system introduces the dry moist gas into the reaction barrel, and the outlet device is dried and the money is derived from the money. Anti-brain discharge. In addition, the adsorption drying alpha further includes a drain connected to the reaction tank and the regeneration tank, and a vacuum connected to the drain. The purpose of this creation is to provide an additional surface-receiving device that has improved vacuum drainage efficiency due to a vacuum device connected to the drain. M355357 [Embodiment] Since this creation system discloses an adsorption drying device, the combination of the drying device components and the chemical used in the field can be easily understood by those who have expertise in the field. 'Therefore, the description in the following text will not be fully described. The drawings in the following texts express the structural schematics related to the creative features, and do not need to be completely drawn according to the actual dimensions. ”
。月參考第1圖’係為本創作第—較佳實施例的吸附式乾燥設備示意圖。 吸附式乾燥設備1包含有兩個内部盛有乾燥劑之反應桶u再生桶丨2，其中 反應桶11係用於進行氣體之賴反應，㈣生桶12則用於進行乾燥劑的 再生反應。在反應㈣内之乾燥劑使用$畢後，藉由一閥體的切換，則可 將此反應桶轉為再生桶，進行再生侧，而再生完畢之再生桶Ο即切換為 反應桶，以再度進行氣體的乾燥反應。. The reference to Fig. 1 is a schematic view of the adsorption drying apparatus of the first preferred embodiment. The adsorption drying apparatus 1 comprises two reaction tanks u regenerating drums 2 containing a desiccant therein, wherein the reaction tank 11 is used for the reaction of the gas, and (4) the barrel 12 is used for the regeneration reaction of the desiccant. After the use of the desiccant in the reaction (4), after switching through a valve body, the reaction tank can be converted into a regeneration tank to carry out the regeneration side, and the regenerated regeneration tank is switched to the reaction barrel to be re-used. The drying reaction of the gas is carried out.
吸附式乾軸11亦包含有航_ u和再生桶12相互連接的進氣裝 置13及y裝置14 ;進綠置13係將乾燥前之潮濕氣體A叫入反應桶 1卜而出氣裝置14則係將乾燥完成後之再生氣源A1自反應桶u排出。此 外，在反應桶11及再生桶12上均裝設有加熱裝置16，用以加速進行乾燥 劑的再生反應。而吸附式乾燥設備1G進—步包含有與反應桶u及再生桶 12連接的排水裝置15，以及與排水裝置15連接的真空裝置η。 在進行乾_ ’ _氣體AG係由進紐置13導人反應桶n。潮濕氣 體0通過反應桶Π後，由反應桶u内所含的乾燥劑將潮濕氣體中所 帶有的水分吸走’藉_成再生並經由域錢14輸出。進氣 可進—步裝設有至少一個第一控制間131，藉以控制潮濕氣體A0 化向反應桶U，而第—控制闕⑶為電磁閥。而出氣裝置i4上則可進一步 裝設有至少-個第二控綱141，藉以控制再生氣源ai的 制閥141為逆止閥。 弟一控 請繼續參考第丨圖，反應桶u在進行再生反應時，利用裝設於再生桶 5 M355357 、一 裝置16將再生桶12加熱而使再生桶i2中的乾燥劑及氣體 ’皿，升四Μ速乾補峰水分，並且由於溫度升高，紐峨和濕度也 升门因此氣體錢承载更多的水分，藉以將由再生桶U中乾燥劑脫除的 水刀由排水農置I5排出再生桶⑵此外，排水裝置b連接有真空裝置17, 藉由真空乾燥原理改變水之相態，使排水裝置ls中的水蒸氣變化成水，加 速水分自排水裝置15排出，因此提升再生桶12的再生效率。而排水襄置 15可進-步包含至少—第三控糊i5i，且第三控侧⑸為電磁間。 上述之加綠置I6可_置在再錢U外部或是_。不論是裝設 於再生桶的12⑴卩或外部，其結構可包含有石英加熱管、石英加熱片或加 熱線，而加絲的鶴又以線圈狀圍繞再生桶U設置紐。社述之真空 裝置17可包含有真空產生料是真空槽。、 除上述的吸附式乾燥設備之外，本創作亦提供另一種吸附式乾燥設 備。請參考第2圖，係為本創作第二較佳實施例的吸附式乾燥設備示意圖。 吸附式乾燥設備2包含有兩個内部盛有乾燥劑之反應桶21及再生桶22，其 中反應桶21 _於進行氣體之乾燥反應，而再生桶22顧於輯乾燥劑 的再生反應。在反應桶21内之乾制使用完畢後，則定義其由反應桶轉為 再生桶，進行再生作用’而再生完畢之再生桶22即定義其轉為反應桶，以 再度進行氣體的乾燥反應。 吸附式乾燥設備2亦包含有與反應桶21和再生桶22相互連接的進氣 裝置23及出氣裝置24 ;進氣裝置23係將乾燥前之潮濕氣體A0導入反應 桶21’而出氣裝置24則係將乾燥完成後之再生氣源入丨自反應桶21排出。 此外，在反應桶21及再生桶22上均裝設有加熱裝置26，用以加熱再生桶 22。而吸附式乾燥設備2還包含有與反應桶21及再生桶22連接的排水裝 置 25。 、 在進行乾燥時，潮濕氣體A0係由進氣裝置23導入反應桶21。潮濕氣 體A〇通過反應桶21後，由反應桶2丨内所含的乾燥劑將潮濕、氣體A0中所 6 M355357 ==走生氣源A1，並經由出氣裝置24輪出。進氣 至卜娜—控糊231，如控彻《氣體 机向反應桶21，而弟一控制閥231為電磁閥。m出氣裝置24上則 裝設有至少-個第二控制閥241，藉以控制再生氣源Al的流向 = 制閥241為逆止閥。 二The adsorption type dry shaft 11 also includes an air intake device 13 and a y device 14 which are connected to each other by the air _ u and the regeneration drum 12; the green gas 13 system calls the humid gas A before drying into the reaction tank 1 and the air outlet device 14 The regeneration gas source A1 after the completion of drying is discharged from the reaction tank u. Further, heating means 16 are provided on both the reaction tank 11 and the regeneration tank 12 for accelerating the regeneration reaction of the desiccant. The adsorption drying apparatus 1G further includes a drain 15 connected to the reaction tank u and the regeneration tank 12, and a vacuum unit η connected to the drain unit 15. In the process of performing the dry _ _ gas AG, the reaction tank n is guided by the inlet 13 . After the humid gas 0 passes through the reaction tank, the moisture contained in the moist gas is sucked away by the desiccant contained in the reaction tank u, and is regenerated and output via the money 14. The intake air can be stepped into at least one first control room 131 to control the humid gas A0 to the reaction tank U, and the first control port (3) is a solenoid valve. Further, at least one second control unit 141 is further disposed on the air outlet unit i4, whereby the valve 141 for controlling the regeneration air source ai is a check valve. For the first control, please continue to refer to the figure. When the regeneration reaction is carried out, the reaction tank is heated in the regeneration tank 5 M355357 and a device 16 to heat the regeneration tank 12 to make the desiccant and the gas in the regeneration tank i2. Ascending the four squats to dry the peak moisture, and because of the temperature rise, the sputum and humidity also rise to the door, so the gas money carries more water, so that the water knives removed by the desiccant in the regeneration tank U are discharged by the drainage farm I5. In addition, the drainage device b is connected to the vacuum device 17, and the phase of the water is changed by the vacuum drying principle, so that the water vapor in the drainage device ls is changed into water, and the moisture is accelerated from the drainage device 15, thereby lifting the regeneration bucket 12 Regeneration efficiency. The draining device 15 can further include at least a third control paste i5i, and the third control side (5) is an electromagnetic room. The above-mentioned green setting I6 can be placed outside the money U or _. Whether it is installed in the 12(1) 再生 or the outside of the regenerative barrel, the structure may include a quartz heating tube, a quartz heating sheet or a heating wire, and the wired crane is arranged in a coil shape around the regeneration barrel U. The vacuum device 17 of the present invention may comprise a vacuum generating material which is a vacuum tank. In addition to the above-described adsorption drying equipment, this creation also provides another adsorption drying apparatus. Please refer to FIG. 2, which is a schematic diagram of the adsorption drying apparatus according to the second preferred embodiment of the present invention. The adsorption drying apparatus 2 comprises two reaction tanks 21 containing a desiccant therein and a regeneration tank 22, wherein the reaction tank 21 is subjected to a gas drying reaction, and the regeneration tank 22 is subjected to a regeneration reaction of the desiccant. After the dry use in the reaction tank 21 is completed, it is defined that it is converted from a reaction tank to a regeneration tank to carry out regeneration. The regeneration drum 22, which has been regenerated, is defined as a reaction tank, and the gas drying reaction is again performed. The adsorption drying device 2 also includes an air intake device 23 and an air outlet device 24 connected to the reaction tub 21 and the regeneration tub 22; the air intake device 23 introduces the humid gas A0 before drying into the reaction tub 21' and the air outlet device 24 The regeneration gas source after the completion of drying is discharged from the reaction tank 21. Further, heating means 26 are provided on the reaction tank 21 and the regeneration tank 22 for heating the regeneration tank 22. The adsorption drying apparatus 2 further includes a drain device 25 connected to the reaction tub 21 and the regeneration tub 22. When drying is performed, the humid gas A0 is introduced into the reaction tub 21 by the air intake device 23. After the humid gas A 〇 passes through the reaction tank 21, the desiccant contained in the reaction tank 2 is wet, and the gas M0 357 is replaced by the gas source A1 and is rotated through the gas outlet device 24. Intake to the buna-control paste 231, such as control "gas machine to the reaction barrel 21, and the second control valve 231 is a solenoid valve. The m air outlet device 24 is provided with at least one second control valve 241 for controlling the flow direction of the regeneration air source A1. The valve 241 is a check valve. two
明繼續參考第2圖’反顧22在進行再生反應時，_裝設於再生桶 22上的加Μ置26，將再絲22加熱，峨再生桶η巾的鶴劑及氣體 溫度升高，加速乾_脫除水分’並使簡承載更㈣水分。氣體通 過再生桶22之後會經由排水裝置25排出，藉以將由再生桶22中乾燥劑脫 除的水分排出再生桶22。而排水裝置15可進—步包含至少—第三控制闕 251 ’且第三控制閥251為電磁閥。 ' 上述之加熱裝置26可以裝置在再生桶22外部或是内部。不論是裝設 於再生桶的22内部或外部，其結構可包含有;δ英加熱管、；5英加熱片或加 熱線，而加熱線的型態又以線圈狀圍繞再生桶22設置為佳。 除上述兩種吸附式乾燥設備之外，本創作亦提供再一種吸附式乾燥設 備。請參考H 3目’絲摘作第三較佳實關的麵錢燥設備示意圖。 吸附式乾燥設備3包含有兩個内部盛有乾燥劑之反應桶31及再生桶幻，其 中反應桶31係用於進行氣體之乾燥反應，而再生桶32則用於進行乾燥劑 的再生反應。在反應桶31内之乾燥劑使用完畢後，則定義其由反應桶轉為 再生桶，進行再生作用，而再生完畢之再生桶32即定義其轉為反應桶，以 再度進行氣體的乾燥反應。 吸附式乾燥設備3亦包含有與反應桶31和再生桶32相互連接的進氣 裝置33及出氣裝置34 ;進氣裝置33係將乾燥前之潮濕氣體Α0導入反應 桶31 ’而出氣裝置34則係將乾燥完成後之再生氣源Α1自反應桶31排出。 而吸附式乾燥設備3還包含有與反應桶3丨及再生桶32連接的排水裝置35, 以及與排水裝置35連接的真空簌置37。 7 M355357 體AO通過 她繼33導从输！。継氣 帶有的水31内所含的乾燥劑將潮濕氣體Α〇中所 =上;再生氣源"’並經由出氣裝置34輸出。進氣 tit 3 f 一個第一控制_，藉以控制潮濕氣體Α〇 應桶31，而第-控制閥331為電磁閥。而出氣裝置 裝設有至少一個第二控制閥341，藉 7 制闕341紐閥。 藉侧再生減則流向，而第二控 ^續參考第3圖，反應桶32在進行再生反應時，氣體通過再生桶％ ^會經由排水裝置35排出，藉以將由再生桶32中乾燥劑脫除的水分排 神徽生桶32此外’排水裝置35連接有真空裝置37，藉由真空乾燥原理 改變水之相態，使排水裝置35中的水蒸氣變化成水，加速水分自排水裝置 丨排出ϋ此提升再生桶32的再生效率。而排水裝置35可進一步包含至 ^第二控綱35卜且第三控制閥3S1為電磁間。又，真空裝置37可包 含有真空產生器或是真空槽。 以上所述者’僅為本創作之較佳實施例，並非用以限定本創作之申請 專利權利；同時以上的描述，對於本技術領域之具有通常知識者應可明瞭 及實施’目此其絲雌摘作簡示之精神下所完躺等效改變或修 飾，均應包含在以下所列之申請專利範圍中。 一 【圖式簡單說明】 第1圖，為本創作第一較佳實施例吸附式乾燥設備示意圖。 第2圖，為本創作第二較佳實施例吸附式乾燥設備示意圖。 第3圖，為本創作第三較佳實施例吸附式乾燥設備示意圖。 【主要元件符號說明】 吸附式乾燥設備 丨，2,3 M355357 反應桶 11,21,31 再生桶 12,22,32 進氣裝置 13,23,33 第一控制閥 131,231,331 出氣裝置 14,24,34 第二控制閥 141,241,341 排水裝置 15,25,35 第三控制閥 151,251,351 加熱裝置 16,26 真空裝置 17,37 潮濕氣體 A0 再生氣源 A1Continuing to refer to Fig. 2, when the regeneration reaction is carried out, the twisting device 26 installed on the regeneration tank 22 heats the wire 22, and the temperature of the crane and the gas in the regeneration drum is increased. Accelerate the dry_removal of moisture' and make the simple load more (iv) moisture. After passing through the regeneration tub 22, the gas is discharged through the drain device 25, whereby the moisture removed by the desiccant in the regeneration tub 22 is discharged to the regeneration tub 22. The drain device 15 may further include at least a third control port 251 ' and the third control valve 251 is a solenoid valve. The above-described heating device 26 can be disposed outside or inside the regeneration tub 22. Whether it is installed inside or outside the regeneration bucket 22, the structure may include; δ 英 heating tube; 5 inch heating sheet or heating wire, and the shape of the heating wire is preferably arranged in a coil shape around the regeneration barrel 22 . In addition to the above two types of adsorption drying equipment, this creation also provides an additional adsorption drying apparatus. Please refer to the H 3 head's wire for the third best practice. The adsorption drying apparatus 3 comprises two reaction tanks 31 containing a desiccant inside and a regeneration tank, wherein the reaction tank 31 is used for the drying reaction of the gas, and the regeneration tank 32 is used for the regeneration reaction of the desiccant. After the desiccant in the reaction tank 31 is used, it is defined that it is converted from a reaction tank to a regeneration tank for regeneration, and the regenerated regeneration tank 32 is defined to be converted into a reaction tank to perform a gas drying reaction again. The adsorption drying apparatus 3 also includes an air intake device 33 and an air outlet device 34 connected to the reaction tub 31 and the regeneration tub 32. The air intake device 33 introduces the humid gas Α0 before drying into the reaction tub 31' and the air outlet device 34. The regeneration gas source Α1 after the completion of drying is discharged from the reaction tank 31. The adsorption drying apparatus 3 further includes a drain 35 connected to the reaction tank 3 and the regeneration tank 32, and a vacuum chamber 37 connected to the drain 35. 7 M355357 Body AO through her following 33 guides to lose! . The desiccant contained in the water 31 contained in the helium gas is discharged from the humid gas gas; the regeneration gas source "' is output via the gas outlet device 34. The intake air tit 3 f is a first control _, thereby controlling the humid gas Α〇 tank 31, and the first-control valve 331 is a solenoid valve. The air outlet device is provided with at least one second control valve 341, and the brake valve 341 is used. The borrowing side reduces the flow direction, and the second control refers to FIG. 3, when the reaction tank 32 performs the regeneration reaction, the gas passes through the regeneration tank % ^ and is discharged through the drain device 35, thereby removing the desiccant from the regeneration tank 32. In addition, the drain device 35 is connected with a vacuum device 37, and the phase of the water is changed by the vacuum drying principle, so that the water vapor in the drain device 35 is changed into water, and the water is accelerated from the drain device. This enhances the regeneration efficiency of the regeneration tub 32. The drain device 35 may further include a second control unit 35b and the third control valve 3S1 is an electromagnetic chamber. Further, the vacuum unit 37 may contain a vacuum generator or a vacuum chamber. The above description is only a preferred embodiment of the present invention, and is not intended to limit the patent application rights of the present invention; and the above description should be understood and implemented by those having ordinary knowledge in the art. Equivalent changes or modifications to the lyings in the spirit of the abstract shall be included in the scope of the patent application listed below. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing an adsorption drying apparatus according to a first preferred embodiment of the present invention. Fig. 2 is a schematic view showing the adsorption drying apparatus of the second preferred embodiment of the present invention. Fig. 3 is a schematic view showing the adsorption drying apparatus of the third preferred embodiment of the present invention. [Main component symbol description] Adsorption drying equipment 丨, 2,3 M355357 Reaction tank 11, 21, 31 Regeneration tank 12, 22, 32 Intake unit 13, 23, 33 First control valve 131, 231, 331 Air outlet unit 14, 24, 34 Second control valve 141, 241, 341 Drainage device 15, 25, 35 Third control valve 151, 251, 351 Heating device 16, 26 Vacuum device 17, 37 Moisture gas A0 Regeneration gas source A1