TW526088B - Dehumidifying method for compressed gas and its apparatus - Google Patents

Dehumidifying method for compressed gas and its apparatus Download PDF

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Publication number
TW526088B
TW526088B TW089110511A TW89110511A TW526088B TW 526088 B TW526088 B TW 526088B TW 089110511 A TW089110511 A TW 089110511A TW 89110511 A TW89110511 A TW 89110511A TW 526088 B TW526088 B TW 526088B
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TW
Taiwan
Prior art keywords
suction
moisture
dew point
drying
cylinder
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Application number
TW089110511A
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Chinese (zh)
Inventor
Toru Takeuchi
Hideo Tamai
Ota Koichi
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Orion Machine Co Ltd
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Publication date
Priority claimed from JP16236499A external-priority patent/JP3483797B2/en
Priority claimed from JP16236399A external-priority patent/JP3517157B2/en
Application filed by Orion Machine Co Ltd filed Critical Orion Machine Co Ltd
Application granted granted Critical
Publication of TW526088B publication Critical patent/TW526088B/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/16Filtration; Moisture separation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/06Control using electricity
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B51/00Testing machines, pumps, or pumping installations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B2207/00External parameters
    • F04B2207/01Load in general
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B2207/00External parameters
    • F04B2207/04Settings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/10Adaptations or arrangements of distribution members

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Gases (AREA)

Abstract

This invention is to reduce running costs both a dehumidifying method for compressed gas and its apparatus; in which during an energy saving operation, adsorbents in both absorbing cylinders are concurrently deteriorated to suppress variation in dew point when a normal operation is restored; thereby replacement operations of adsorbents of both cylinders are simultaneously carried out. In a method for dehumidifying compressed air: a drying process, in which gas is adsorbed and dried in one of two adsorbing cylinders 3, 4 each charged with adsorbents, and a regenerating process, in which a part of the obtained dried gas is led to the other adsorbing cylinder to desorb the moisture from the adsorbents concurrently performed, and these processes are alternately performed by switching from one cylinder to the other to continuously supply dry gas; under predetermined conditions, for example, if the relationship between the dew point (dew point under pressure) Ta and a set dew point (dew point under pressure) Ts is Ta ≤ Ts in dried gas, the drying process is continued alternately between both cylinders, while a process for purging of desorbed moisture from each cylinder that is suspended is provided.

Description

526088 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(1 ) 【本發明所屬之技術領域】526088 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the Invention (1) [Technical Field to which the Invention belongs]

I 本發明係關於爲了使用吸著劑來將濕的壓縮氣體吸著 除濕且乾燥之除濕方法以及其裝置,特別是有關於爲了防 止吸著劑之早期劣化之省能源運轉。 【先前之技術】 在以往之除濕裝置,爲了連續供給乾燥的空氣準備有 2座在容器充塡活性礬土(activated alumina)、砂凝膠(silica gel)、合成沸石(zeolite)或者是氯化鋰(lithium chloride)等吸 著劑之吸著筒。 在一方的吸著筒導入濕的壓縮空氣予以吸著乾燥,供 給到指定之供給處。在同時將所得到之乾燥空氣的一部分 導入另一方之吸著筒,從在前階段吸收濕氣而使得除濕能 力減低之吸著劑將濕氣除去,更將這個濕氣從吸著筒中除 去而再生。在這個再生過程所得到之乾燥空氣,將有2 1 %的量會放出大氣之中。 此種在一方的吸著筒做壓縮空氣的乾燥,而同時在另 一方吸著筒進行吸著劑的再生之同時,在指定的時間經過 之後,切換設置於兩個吸著筒之間的切換開關,連續地供 給乾燥空氣。 但是,因除濕裝置係以使周圍溫度、進氣溫度上昇的 最嚴酷的夏季之條件爲基本所設計,因此例如冬季的使用 或者當供給處之負擔減輕時,將吸著劑之吸著作用減輕, 希望可以達到廷長壽命之目的。 (請先閱讀背面之注意事項再填寫本頁) 裝!丨訂. 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) · 4 - 526088 A7 _ B7 五、發明說明(2 ) 以往係如同第1 1圖之省能源運轉來進行。即使是當 切換開關之切換動作停止,被接續在各個吸著筒之排氣閥 全部將呈關閉狀態,例如:只要繼續在B筒導入濕的壓縮 空氣將以除濕並乾燥,A、B兩筒均停止再生動作。 【發明所欲解決之課題】 、 在省能源運轉時,切換開關之切換動作停止,接續在 各吸著筒之排氣閥全部呈關閉狀態之情形,因排氣而使得 乾燥空氣的排出量減少。但是,因條件之原因上述省能源 運轉有可能長時間繼續。在此時只有在一方的吸著筒內之 吸著劑進行吸著作用,另一方的吸著筒內之吸著劑並不會 有任何作用。 因此,當回復到標準運轉之後,在吸著筒已繼續除濕 乾燥之吸著劑的水分,吸著量與在沒有任何作用之另一方 吸著筒的吸著劑之水分吸著量將沒有平衡。實際上從已繼 續除濕乾燥的一方供給出來之乾燥空氣之露點溫度要較另 一方,供給出來之乾燥空氣的露點溫度要來得高。 結果,長時間繼續吸著作用側之吸著劑’要較另一方 之吸著劑早期劣化,而產生更換新的吸著劑之必要。當任 何一方的吸著劑劣化之後,一般來說兩邊要同時更換’對 另一方來說造成不必要的更煥’對運轉成本有不好的影響 ° ! 本發明係爲了解決上述之課題’其目的爲提供在省能 源運轉時,藉由排氣而抑制乾燥空氣之排出量,使得兩邊 (請先閱讀背面之注意事項再填寫本頁) 裝---I---—訂---- 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -5 · 經濟部智慧財產局員工消費合作社印製 526088 Α7 Β7 五、發明說明(3 ) 之吸著筒內的吸著劑之劣化能均等進行,當回復到標準運 轉時,能抑制在各個吸著筒間之露點溫度的變動,使得各 個吸著劑之交換時間能夠一致,排除不必要之交換’達到 減低運轉成本的效果之壓縮氣體之除濕方法及其裝置。 【解決課題之手段】 爲解決上述課題並達成目的,本發明之壓縮氣體之除 濕方法及其裝置係由下記所構成。 (1 )具備有在充塡吸著劑之2座吸著之其中一方, 導入濕的壓縮氣體作吸著除濕之乾燥過程,及藉由此乾燥 過程所得之乾燥氣體之一部分導入在前階段之乾燥過程而 造成吸濕能力減低之另一方吸著筒,從吸著劑將濕氣脫離 ,而將此脫離之濕氣從吸著筒排出進行再生過程,將這些 乾燥過程與再生過程在兩吸著筒之間交互地切換連續地供 給乾燥氣體之除濕方法,其特徵爲:在指定的條件之下在 兩吸著筒之間,交互地繼續進行乾燥過程之同時可以停止 ,將濕氣脫離;έ各吸著筒的排氣之停止過程。 (2 )如上述(1 )之壓縮氣體之除濕方法,上述指 定之條件係爲在乾燥過程所得之乾燥氣體之露點溫度(壓 力下露點)T a係與設定露點溫度(壓力下露點)The present invention relates to a dehumidification method and a device for dehumidifying and drying a wet compressed gas by using an adsorbent, and more particularly to an energy-saving operation to prevent early deterioration of the adsorbent. [Previous technology] In conventional dehumidifiers, two containers were filled with activated alumina, silica gel, synthetic zeolite, or chlorinated chloride for continuous supply of dry air. Sorbents for sorbents such as lithium chloride. Wet compressed air is introduced into one of the suction cylinders to be sucked and dried, and supplied to a designated supply place. At the same time, a part of the obtained dry air is introduced into the other suction tube, and the moisture is removed from the sorbent which absorbed moisture in the previous stage and the dehumidifying ability is reduced, and this moisture is removed from the suction tube. regeneration. 21% of the dry air obtained in this regeneration process will be released into the atmosphere. This type of drying of compressed air is performed on one suction tube, while the other suction tube is used to regenerate the adsorbent, and after a specified time has passed, the switching between the two suction tubes is switched. Open and close to supply dry air continuously. However, since the dehumidifier is designed based on the most severe summer conditions in which ambient temperature and intake air temperature rise, for example, use in winter or when the burden on the supply site is reduced, the absorption function of the adsorbent is reduced. I hope that the purpose of long life can be achieved. (Please read the precautions on the back before filling this page) Install!丨 Order. This paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) · 4-526088 A7 _ B7 V. Description of the invention (2) In the past, it was performed as energy-saving operation as shown in Figure 11. Even when the switching action of the switch is stopped, the exhaust valves connected to each suction cylinder will be closed. For example, as long as the wet compressed air is continuously introduced into the B cylinder, it will be dehumidified and dried. Both stop the regeneration operation. [Problems to be Solved by the Invention] During the energy-saving operation, the switching operation of the switch is stopped, and the exhaust valves of the suction cylinders are all closed, and the exhaust air reduces the amount of dry air. . However, due to conditions, the above energy-saving operation may continue for a long time. At this time, only the sorbent in one sorption tube performs the absorbing function, and the sorbent in the other sorption tube has no effect. Therefore, after returning to standard operation, the moisture content of the adsorbent that has been dehumidified and dried in the adsorption cartridge will not be balanced with the moisture adsorption amount of the adsorbent in the other adsorption cartridge that has no effect. . In fact, the dew point temperature of the dry air supplied from the party that has continued to dehumidify and dry is higher than the dew point temperature of the dry air supplied. As a result, the sorbent on the application side for a long period of time is deteriorated earlier than the sorbent on the other side, and it becomes necessary to replace the sorbent with a new one. When the sorbent on either side deteriorates, in general, both sides must be replaced at the same time, which will cause "unnecessary renewal for the other side", which will have a bad influence on the running cost. The purpose is to provide the two sides (please read the precautions on the back before filling this page) by suppressing the discharge of dry air by exhausting during energy-saving operation. Printed on the paper by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. The paper size is applicable to the Chinese National Standard (CNS) A4 specification (210 X 297 mm) -5. Printed by the Employees’ Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 526088 Α7 Β7 V. Description of the invention ( 3) The degradation of the sorbent in the sorption tube can be carried out uniformly. When returning to the standard operation, it can suppress the fluctuation of the dew point temperature between the sorption tubes, so that the exchange time of each sorbent can be consistent and eliminated. Unnecessary exchange 'A method and device for dehumidifying compressed gas to achieve the effect of reducing operating costs. [Means for solving the problem] In order to solve the above-mentioned problems and achieve the object, the dehumidification method and device of the compressed gas of the present invention are constituted by the following. (1) Equipped with one of two sorbents filled with sorbent, a wet compressed gas is introduced into the drying process for adsorption and dehumidification, and a part of the dry gas obtained from the drying process is introduced into the previous stage. The other absorption tube, which reduces the moisture absorption capacity during the drying process, detaches the moisture from the sorbent, and discharges the separated moisture from the absorption tube for the regeneration process. The drying process and the regeneration process are absorbed in two ways. The dehumidification method of continuously supplying dry gas is alternately switched between the cylinders, which is characterized in that: under the specified conditions, the drying process can be stopped and the moisture can be stopped interactively while continuing between the two suction cylinders; The process of stopping the exhaust of each suction tube. (2) According to the dehumidification method of compressed gas (1) above, the above-specified conditions are the dew point temperature (dew point under pressure) of the dry gas obtained during the drying process, T a and the set dew point temperature (dew point under pressure).

Ts相等,或者較之爲低(TaSTs)。 (3 )具備有2座充塡有吸著劑之吸著筒,與藉著切 換手段將這兩座吸著筒相連通之通路以及排氣手段,其中 將濕的壓縮氣體導入一方之吸著筒吸著除濕並乾燥,將此 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 7〇Ζ " — II-------JAW — — — — — — — ^« — — — — 1 — I a^_wi (請先閱讀背面之注意事項再填寫本頁) 526088 A7 B7 五、發明說明(4 ) 乾燥氣體的一部分導入在前階段使吸濕能力減低之另一方Ts is equal or lower (TaSTs). (3) It is provided with two suction tubes filled with a sorbent, and a passage and an exhaust means for communicating the two suction tubes by a switching means, in which a wet compressed gas is introduced into one suction The tube is dehumidified and dried by suction. This paper size is in accordance with Chinese National Standard (CNS) A4 (210 X 297 mm) 7〇Z " — II ------- JAW — — — — — — — ^ «— — — — 1 — I a ^ _wi (Please read the notes on the back before filling this page) 526088 A7 B7 V. Description of the invention (4) Part of the dry gas is introduced in the previous stage to reduce the moisture absorption capacity. Party

I 吸著筒,從吸著劑將濕氣脫離,並且藉由排氣手段將脫離 之濕氣,從吸著筒排出進行再生之過程,以在上述切換手 段之切換動作爲基礎,於兩吸著筒之間交互作乾燥與再生 之切換,連續地供應乾燥氣體之除濕裝置中,其特徵爲: 在指定之條件下切換手段之繼續切換,一方面在兩吸著筒 間交互地繼續將濕的壓縮氣體除濕乾燥,具有控制各吸著 筒停止排氣手段之控制手段。 由於採用顯示於(1 )〜(3 )之手段,在指定的條 件下便開始所謂之省能源運轉,此時排氣量抑制成少量之 同時,使兩方之筒內的吸著劑之劣化作均等進行,當回復 到標準運轉時,能夠抑制在各吸著筒間之露點溫度,使各 個吸著劑之交換時間相同。 (4 )在充塡有吸著劑之2座吸著筒之中的一方,導 入濕的壓縮氣體作吸著除濕之乾燥過程,以及將由此乾燥 過程所得到之乾燥氣體之一部分導入在前階段乾燥過程使 吸濕能力,減低之他方吸著筒從吸著劑中將濕氣脫離,且 所脫離之濕氣由吸著劑排出進行再生過程,在這些在兩吸 著筒之間交互地切換乾燥過程與再生過程,使其連續供給 乾燥氣體之除濕方法中,其特徵爲:在指定條件下停止上 述再生過程之同時,在此停止過程中於指定之頻率將再進 行再生過程。 t (5 )如上述(4 )之壓縮氣體之除濕方法,其中在 上述指定條件下再生過程停止過程中,上述乾燥過程係在 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁) ·1111111 一5J馨— — _ 經濟部智慧財產局員工消費合作社印製 526088 A7 B7 五、發明說明(5 ) 兩吸著筒間交互地繼續進行,或是只在一方之吸著筒上繼 續。 (請先閱讀背面之注意事項再填寫本頁) (6 )具備有2座充塡有吸著劑之吸著筒,與藉由切 換手段將這些吸著筒相連通之路以及排氣手段,其中將濕 的壓縮氣體導入一方之吸著筒,吸著除濕並乾燥,將此乾 燥氣體的一部分導入在前階段使吸濕能力減低之另一方吸 著筒,從吸著劑將濕氣脫離,並且藉由排氣手段將脫離之 濕氣從吸著筒排出進行再生之過程,以在上述切換手段之 切換動作爲基礎,於兩吸著筒之間交互作乾燥與再生之切 換,連續地供應乾燥氣體之除濕裝置中,其特徵爲:在指 定之條件下進行停止上述再生過程之省能源運轉時·,具備 有控制在此省能源運轉中於指定之週期下進行再生過程之 控制手段^ 經濟部智慧財產局員工消費合作社印製 因採用顯示於(4)〜(6)之手段,在指定之條件 下停止再生過程即使是進行省能源運轉,此時由於亦在指 定之週期下對於兩方之吸著筒進行強制性排氣,因此排氣 量可抑制於少量之同時可使吸著劑之劣化呈均等進行,而 當回復到標準運轉時,能抑制在各吸著筒間之露點溫度, 能使各個吸著筒之交換時相同。 【發明之實施形態】 以下,將本發明之實施形態作以圖面說明。在第1圖 顯示壓縮氣體之除濕裝置的外觀斜視圖。 此除濕裝置係由下部側之架台1 ,與裝設於此架台1 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -8 - 經濟部智慧財產局員工消費合作社印製 526088 A7 B7 五、發明說明(9 ) 3 3,以及從此通口連通路徑3 3的中途部分岐而連通在 \ 上述排氣閥2 7之排氣分岐路徑3 4。 上述排氣閥2 7係爲一般之電磁開關閥,與上述控制 電路2 5電氣性的接續在一起。對應從這個控制電路2 5 之控制信號而作開關動作,使從排氣分岐路徑3 4所導入 之排氣氣體通過或者遮斷。從這裏導出之排氣氣體係因被 導向消音裝置2 8而被消音後再向外部放出。 上述控制電路2 5係具備有接受從上述溫度感應器 2 3來之檢測信號而換算成露點溫度(壓力下露點)T a 之電路,將此露點溫度T a與預先記憶之設定露點溫度( 壓力下露點)T s相比較之電路,以及根據這個比較的結 果來控制切換上述切換閥2 6與控制排氣閥的開閉之電路 〇 由上述構成所成之吸著裝置來完成下述之作用。並且 ,壓縮氣體係以壓縮空氣代以說明。 當切換閥2 6之閥體f在第2圖所顯示之位置上時, 在B筒4作乾燥過程,在A筒3作昇壓過程或者再生過程 〇 即是,供向除濕裝置之濕的壓縮空氣,係從輸入接頭 1 5之導入口 1 0藉著導入路徑3 0導向切換閥2 6之第 3通口 c,並且藉由第4通口 d從B筒連通路徑3 2導向 B筒4之內。 , 當濕的壓縮空氣在B筒4內從下部往上部通過時,因 充塡在此之吸著劑17使之吸著除濕進而乾燥化之乾燥過 ----— — — — — — I i I I I I I I e illll· — —· <請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -12 - 經濟部智慧財產局員工消費合作社印製 526088 A7 --B7 五、發明說明(1〇 ) 程被進行。並且,推押設於此上部之逆止閥1 8 B而導向I The suction tube removes moisture from the sorbent, and exhausts the detached moisture from the suction tube for regenerating by means of exhaust. Based on the switching action of the above switching means, The dehumidification device that alternately switches between drying and regeneration between the cylinders and continuously supplies dry gas is characterized by: the continued switching of the switching means under the specified conditions, on the one hand, the humidity is alternately continued between the two cylinders. The compressed gas is dehumidified and dried, and it has control means to control each suction tube to stop the exhausting means. Since the means shown in (1) to (3) are adopted, the so-called energy-saving operation starts under the specified conditions. At this time, the amount of exhaust gas is suppressed to a small amount, and the sorbent in the two cylinders is degraded. The operation is performed uniformly. When returning to the standard operation, the dew point temperature between the adsorption tubes can be suppressed, and the exchange time of each adsorbent can be the same. (4) In one of the two suction cylinders filled with the sorbent, a wet compressed gas is introduced for the drying process of adsorption and dehumidification, and a part of the dry gas obtained from the drying process is introduced in the previous stage. The drying process makes the hygroscopic ability reduce the other sorbent cylinders to detach the moisture from the sorbent, and the detached moisture is discharged by the sorbent for the regeneration process. These are switched alternately between the two sorption cylinders. In the dehumidification method in which the drying process and the regeneration process are performed so as to continuously supply the drying gas, it is characterized in that, while the regeneration process is stopped under the specified conditions, the regeneration process will be performed at the specified frequency during the stop process. t (5) The dehumidification method of compressed gas as described in (4) above, in which the regeneration process is stopped under the above-mentioned specified conditions, and the above-mentioned drying process is in accordance with the Chinese National Standard (CNS) A4 (210 X 297) (%) (Please read the notes on the back before filling this page) · 1111111-5J Xin-_ Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs's Consumer Cooperatives 526088 A7 B7 V. Description of the invention (5) The two suction cups are interactively Continue, or continue on only one suction tube. (Please read the precautions on the back before filling out this page) (6) There are two suction tubes filled with sorbent, and the way to connect these suction tubes by switching means and exhaust means, Among them, the wet compressed gas is introduced into one suction tube, sucked and dehumidified and dried, and a part of this dry gas is introduced into the other suction tube, which reduces the moisture absorption capacity in the previous stage, and the moisture is separated from the adsorbent. In addition, the exhausted moisture is exhausted from the suction tube by the exhaust means for regeneration. Based on the switching action of the switching means described above, the two suction tubes are alternately switched between drying and regeneration, and continuously supplied. The dry gas dehumidification device is characterized in that when the energy-saving operation of stopping the regeneration process is performed under specified conditions, it is provided with a control means to control the regeneration process at a specified period during the energy-saving operation ^ Economic Printed by the Ministry of Intellectual Property Bureau's Consumer Cooperative because it uses the means shown in (4) to (6) to stop the regeneration process under specified conditions, even if it is an energy-saving operation. Mandatory exhaust is performed for the two suction cylinders at a specified period, so the exhaust volume can be suppressed to a small amount while the deterioration of the adsorbent can be uniformly performed. When returning to the standard operation, it can be suppressed in each The dew point temperature between the suction tubes can make the exchange of each suction tube the same. [Embodiment of the invention] Hereinafter, embodiments of the present invention will be described with reference to the drawings. Figure 1 shows a perspective view of the appearance of a compressed gas dehumidifier. This dehumidifying device is printed by the stand 1 on the lower side, and the paper size installed on this stand 1 is in accordance with the Chinese National Standard (CNS) A4 specification (210 X 297 mm) -8-Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 526088 A7 B7 V. Description of the invention (9) 3 3, and the halfway part of the communication path 33 from this port is connected to the exhaust branch path 34 of the above-mentioned exhaust valve 27. The exhaust valve 27 is a general electromagnetic on-off valve, and is electrically connected to the control circuit 25. In response to a control signal from this control circuit 25, a switching operation is performed to pass or block the exhaust gas introduced from the exhaust branch path 34. The exhaust gas system derived from here is silenced by being guided to the muffler 28, and then released to the outside. The control circuit 25 is provided with a circuit that receives a detection signal from the temperature sensor 23 and converts it into a dew point temperature (dew point under pressure) T a. This dew point temperature T a is stored with a preset dew point temperature (pressure). Lower dew point) T s comparison circuit, and a circuit for controlling the switching of the switching valve 26 and the opening and closing of the exhaust valve based on the result of this comparison. The adsorption device formed by the above structure performs the following functions. And, the compressed gas system is explained by compressed air. When the valve body f of the switching valve 26 is in the position shown in FIG. 2, the drying process is performed in the B cylinder 4, and the boosting process or the regeneration process is performed in the A cylinder 3. That is, the wet The compressed air is guided from the inlet 10 of the input joint 15 through the introduction path 30 to the third port c of the switching valve 2 6 and from the B cylinder communication path 32 to the B cylinder through the fourth port d. Within 4 When the wet compressed air passes from the lower part to the upper part in the B cylinder 4, it is dried because it is adsorbed and dehumidified by the adsorbent 17 filled therein. i IIIIII e illll · — — · < Please read the notes on the back before filling this page) This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) -12-Employees of Intellectual Property Bureau, Ministry of Economic Affairs Printed by the Consumer Cooperative 526088 A7 --B7 V. Description of Invention (1〇) The process was carried out. In addition, the check valve 1 8 B provided on the upper part is pushed and guided

I 排出接頭5之供輸路徑2 0,從供輸口 9供輸到指定之供 輸處。 另外,從B筒4上端開口部送出之乾燥空氣之一部分 將導入排氣室2 2,並且因排氣孔1 2而將流量關小,藉 著A筒3上部之排氣室2 2導入A筒3之內。接著通過充 塡在A筒3內之吸著劑1 7,在前階段的乾燥過程中被吸 著劑1 7吸著之濕氣將被脫除。 這個濕氣脫除之後的排氣空氣,係從A筒連通路徑 3 1藉著第2通口上,從第1通口 a被導引出來,而導向 通口連通路徑3 3。因第5通口 e係處於閉塞狀態.,因此 排氣空氣將從通口連通路徑3 3導向排氣分岐路徑3 4。 當排氣閥2 7處於關閉狀態時,排氣空氣將在這裹 被遮斷,因此A筒3內之壓力將上昇而造成昇壓過程。當 排氣閥2 7處於開放狀態時,排氣空氣將通過排氣閥2 7 導向消音裝置2 8,在此被消音之後向外部放.出形成再生 過程。 當切換閥2 6之閥體f處於第3圖所顯示之位置時, 在A筒3形成乾燥過程、B筒4形成昇壓過程或者再生過 程。 也就是,向除濕裝置供給之濕的壓縮空氣,係從輸入 接頭1 5的導入口 1 0藉由導人路徑3 0導向切換閥2 6 之第3通口 c ,並且藉著第2通口 b從A筒連通路徑3 1 導向A筒3之內。 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -13 · — —— — — — — — — — ---I I I I I — — — — — — — a^nwi (請先閱讀背面之注意事項再填寫本頁) 526088 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(11 ) 濕的壓縮空氣在A筒內從下部往上部通過時,因充塡 在此之吸著劑17使之吸著除濕進而乾燥之乾燥過程被進 行。並且,推押設置於此上部之逆止閥1 8 A,而導向排 出接頭5之供輸路徑2 0,從供輸口 9供輸到指定之供輸 處。 另外,從A筒上端開口部送出之乾燥空氣的一部分, 將導入排氣室22並因排氣孔1 2而將流量關小,藉著B 筒4上部之排氣室2 2導入B筒4之內。 這個乾燥空氣將通過充塡在B筒4內之吸著劑1 7, 在前階段的乾燥過程中被吸收劑1 7吸著之濕氣將被脫除 。這個濕氣脫除之後的排氣空氣,係從B筒連通路徑3 2 藉著第4通口 d從第5通口 e被導引出來,而導向通口連 通路徑3 3 〇 因爲第1通口係處於閉塞狀態,因此排氣空氣將從通 口連通路徑3 3導向排氣分岐路徑3 4。當排氣閥2 7處 於關閉狀態時,排氣空氣將在這裹被遮斷,因此B筒4內 之壓力將上昇而形成昇壓過程。當排氣閥2 7處於開放狀 態時,排氣空氣將通過排氣閥2 7導向消音裝置2 8,在 此被消音之後向外部放出形成再生過程。 接下來,如第4圖(A )到(D )所顯示將上述除濕 作用的流路構成之切換面作順序說明。 第4圖(A)係將濕的壓縮空氣通過切換閥2,6而導 向B筒4,藉由充塡在此之吸著劑1 7將它吸著乾燥。乾 燥後之壓縮空氣將通過逆止閥1 8 B向供輸處供輸。 — — — — — — — — — — —Aw · I I I I I I I ^ ·1111111· (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -14 - 526088 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(12 ) 另外,從B筒4排出之乾燥空氣的一部分將藉著排氣 1 孔1 2導向A筒3,可是因排氣閥2 7‘處於關閉狀態,因 此入筒3內將昇壓到運轉壓力。即是,在B筒4形成乾燥 ^程,而在A筒3形成昇壓過程 在第4圖(B),係在切換切換閥26之同時,放變 排氣閥2 7至開放狀態。濕的壓縮空氣將通過切換閥2 6 而導向A筒3,藉由吸著劑1 7而將它吸著乾燥。 乾燥後之壓縮空氣將通過逆止閥1 8 A被供給出來。 另外,從A筒3供出之乾燥空氣的一部分將藉著排氣孔 1 2導向B筒4,而從吸著劑中將濕氣脫除。 這個排氣空氣將通過開放的排氣閥2 7,而導向消音 裝置2 8從這裹向外部排放出去。即是,在A筒3進行乾 燥過程,而在B筒4進行再生過程。 在第4圖(C),係在將切換閥2 6保持在原狀態之 下’將排氣閥2 7變成關閉狀態。因此,在A筒3將持續 進行乾燥過程,而在B筒4內將進行昇壓至運轉壓力之昇 壓過程。 在第4圖(D),係在切換切換閥26之同時,將排 氣閉2 7變成開放之狀態。濕的壓縮空氣將藉著切換閥 2 6導向B筒4,經過再生之後藉由吸著劑1 7而進行吸 著乾燥之過程。 乾燥後之壓縮空氣係藉著逆止閥1 8 B被供給出來。 另外’從B筒4排出之乾燥空氣的一部分將通過排氣孔 1 2而導向A筒3,形成從吸著劑將濕氣脫除之排氣空氣 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -15 - — — — — — — — — — — ^ — — — — — — — ^» — — — — 1 — (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 526088 A7 ____ B7 五、發明說明(13 ) ’藉著排氣閥2 7從消音裝置2 8向外部排放出來。即是I Discharge the supply path 20 of connector 5 and supply it from supply port 9 to the designated supply and delivery place. In addition, part of the dry air sent from the upper opening of the B cylinder 4 will be introduced into the exhaust chamber 22, and the flow rate will be reduced due to the exhaust hole 12. The exhaust chamber 22 at the upper part of the A cylinder 3 will be introduced into A Within tube 3. Then, by filling the sorbent 17 in the A cylinder 3, the moisture absorbed by the sorbent 17 during the previous stage of drying will be removed. The exhaust air after the moisture is removed is guided from the first port a through the second port through the A tube communication path 3 1 and is guided to the port communication path 33. Since the fifth port e is closed, the exhaust air is guided from the port communication path 3 3 to the exhaust branch path 34. When the exhaust valve 27 is closed, the exhaust air will be blocked here, so the pressure in the A cylinder 3 will rise and cause a boosting process. When the exhaust valve 27 is in the open state, the exhaust air will be guided to the muffler 28 through the exhaust valve 27, and after it is silenced, it will be released to the outside to form a regeneration process. When the valve body f of the switching valve 26 is in the position shown in Fig. 3, a drying process is formed in the A cylinder 3, and a boosting process or a regeneration process is formed in the B cylinder 4. That is, the wet compressed air supplied to the dehumidifier is introduced from the inlet 10 of the input connector 15 to the third port c of the switching valve 2 6 through the guide path 30 and through the second port b is guided into the A cylinder 3 from the A cylinder communication path 3 1. This paper size applies to the Chinese National Standard (CNS) A4 specification (210 X 297 mm) -13 · — —— — — — — — — — --IIIII — — — — — — — a ^ nwi (Please read first Note on the back, please fill in this page again) 526088 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (11) When the wet compressed air passes from the bottom to the top of the A tube, it is filled here. A drying process in which the sorbent 17 adsorbs, dehumidifies, and dries is performed. In addition, a check valve 18 A provided in this upper part is pushed and pushed, and the supply and delivery path 20 of the guide discharge connector 5 is supplied from the supply and supply port 9 to the designated supply and output place. In addition, a part of the dry air sent from the opening at the upper end of the A cylinder is introduced into the exhaust chamber 22 and the flow rate is reduced due to the exhaust hole 12. The exhaust chamber 22 at the upper part of the B cylinder 4 is introduced into the B cylinder 4 within. This dry air will pass through the sorbent 17 filled in the B cylinder 4, and the moisture absorbed by the absorbent 17 during the previous stage of the drying process will be removed. The exhaust air after the moisture is removed is guided from the B-tube communication path 3 2 through the fourth port d from the fifth port e, and the guide port communication path 3 3 〇 because the first port Since the port system is closed, the exhaust air is guided from the port communication path 33 to the exhaust branch path 34. When the exhaust valve 27 is in the closed state, the exhaust air will be blocked in this package, so the pressure in the B cylinder 4 will rise to form a boosting process. When the exhaust valve 27 is in the open state, the exhaust air will be guided to the muffler 28 through the exhaust valve 27, and after it is silenced, it is released to the outside to form a regeneration process. Next, as shown in Figs. 4 (A) to (D), the switching surfaces of the flow path structure of the dehumidification function described above will be sequentially explained. Fig. 4 (A) shows that the wet compressed air is guided to the B cylinder 4 through the switching valves 2, 6 and is sucked and dried by the adsorbent 17 filled therein. The dried compressed air will be supplied to the supply and delivery point through the check valve 18 B. — — — — — — — — — — — — Aw · IIIIIII ^ · 1111111 · (Please read the notes on the back before filling out this page) This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) -14-526088 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the Invention (12) In addition, a part of the dry air discharged from the B tube 4 will be guided to the A tube 3 through the exhaust 1 hole 12 but Since the exhaust valve 27 'is closed, the pressure in the cylinder 3 will be increased to the operating pressure. That is, the drying process is formed in the B cylinder 4 and the pressure increasing process is formed in the A cylinder 3. In FIG. 4 (B), the switching valve 26 is switched and the exhaust valve 27 is opened to open. The wet compressed air will be directed to the A cylinder 3 through the switching valve 2 6, and it will be sucked and dried by the adsorbent 17. The dried compressed air will be supplied through the check valve 18 A. In addition, a part of the dry air supplied from the A cylinder 3 is guided to the B cylinder 4 through the exhaust hole 12 to remove moisture from the sorbent. This exhaust air will pass through the open exhaust valve 27, and the guide muffler 28 will be discharged from this package to the outside. That is, the drying process is performed in the A cylinder 3, and the regeneration process is performed in the B cylinder 4. In Fig. 4 (C), the exhaust valve 27 is closed when the switching valve 26 is maintained in its original state. Therefore, in the A cylinder 3, the drying process will be continuously performed, and in the B cylinder 4, the pressure increasing process to the operating pressure will be performed. In Fig. 4 (D), the switching valve 26 is switched, and the exhaust gas closed 27 is opened. The wet compressed air is guided to the B cylinder 4 through the switching valve 26, and after the regeneration, the adsorption drying process is performed by the adsorbent 17. The dried compressed air is supplied through a check valve 18 B. In addition, a part of the dry air discharged from the B cylinder 4 will be guided to the A cylinder 3 through the exhaust hole 12 to form exhaust air for removing moisture from the sorbent. This paper applies the Chinese National Standard (CNS) A4 Specifications (210 X 297 mm) -15-— — — — — — — — — — ^ — — — — — — ^ »— — — 1 — (Please read the notes on the back before filling out this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 526088 A7 ____ B7 V. Description of the invention (13) 'Exhaust valve 2 7 is discharged from the muffler 2 8 to the outside. That is

I ’在B筒4進行乾燥過程,而在A筒3進行再生過程。 之後再切換至第4圖(A)之狀態,順次重覆以上之 4個過程。 在標準運轉時,將形成如第6圖所顯示之控制。即便 是’上述控制電路2 5係將切換閥分成分鐘間隔來控制, 在A筒3的吸著除濕之乾燥過程,與在B筒4的吸著除濕 的乾燥過程3間的切換,大約間隔兩分鐘被進行。 並且,控制電路2 5係當將切換切換閥排氣閥2 7開 放時,幾乎配合時間來進行,且控制成能使每次排氣閥 2 7的關閉後,將切換切換閥2 6到以前之狀態。 例如,因爲在A筒3進行吸著除濕之乾燥過程,因此 將控制排氣閥2 7於切換切換閥2 6數秒之後被開放,而 控制在B筒4之再生排氣開始時之壓力變動。 上述排氣閥2 7大約設定只有開放9 0秒,在這之間 ,在B筒4將繼續進行再生過程。而且,當在A筒3的除 濕乾燥開始約9 0秒後,排氣閥將被關閉,因此在B筒4 中將進行昇壓過程。 在B筒4的昇壓過程將繼續約3 0秒,合計約1 2 0 秒之後(2分鐘),切換閥2 6將切換到B筒4進行吸著 除濕之乾燥過程約12 0秒(2分鐘)。從這個切換約數 秒後,排氣閥2 7被控制開放出來,於A筒3繼續進行再 生過程約9 0秒後,有約3 0秒的時間排氣閥2 7將關閉 ,在A筒3變成昇壓過程。 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -16 · — — — — — — — — — — JAW- ·1111111 ^ ·11111111 (請先閱讀背面之注意事項再填寫本頁) 526088 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(14 ) 結果,繼續約1 2 0秒(2分鐘)後,在如同先前之 \ 說明在A筒3側行吸著除濕之乾燥過程,與B筒4側變成 再生及昇壓過程,如以下順序反覆循環。 上述溫度感知器2 3係檢測吸著除濕乾燥後之壓縮空 氣之溫度,並將檢測信號傳送到控制電路2 5,在此計算 出露點溫度(壓力下露點)T a ,.其結果以感應出力電壓 來輸出。- 例如從供輸口 9到供輸處所必要之空氣量,極端的變 少等,也是負荷很小的情形,或者從導入口 1 0導入之壓 縮空氣的溫度非常的低。而且乾燥的情形,將移至省能源 運轉。 實際上,以顯示於第5圖之流程圖爲基本,相對於全 流量之標準運轉,當流量少時’將切換至省能源運轉。 也就是,從開始到階段S1,將開始標準運轉。從這 個標準運轉移到階段S 2,溫度感應器2 3將檢測供給出 來的乾燥空氣的溫度^ 在階段3,接到從溫度感應器送來的檢測信號之控制 電路25,將換算成露點溫度(壓力下露點)Ta。接著 ,在階段S 4,控制電路將把預先記億之設定露點溫度( 壓力下露點)T s與計算後之露點溫度T a來比較。 當計算後之露點溫度T a比設定露點溫度T s要低, 或者相等的情形,(Ta<Ts) ’將形成Yes而向階 段S 5移動,而後述之省能源運轉將開始。另外’當計算 後之露點溫度T a比設定露點溫度T s要高時’將成N 〇 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公f -17- " I I I I--------------— — — — — — — (請先閱讀背面之注意事項再填寫本頁) 526088 經濟部智慧財產局員工消費合作社印製 B7 五、發明說明(15 ) 。而回到階段S1之標準運轉。I 'performs the drying process in the B cylinder 4 and the regeneration process in the A cylinder 3. After that, switch to the state shown in Figure 4 (A) and repeat the above 4 processes in sequence. In standard operation, the control shown in Figure 6 will be formed. Even if the above-mentioned control circuit 25 and 5 control the switching valve in minute intervals, the switching between the drying process of the absorption and dehumidification of the A cylinder 3 and the drying process 3 of the absorption and dehumidification of the B cylinder 4 is about two intervals. Minutes are carried out. In addition, the control circuit 25 is performed almost in accordance with the time when the switching valve exhaust valve 27 is opened, and is controlled so that each time the exhaust valve 27 is closed, the switching valve 26 is switched to the previous state. Of the state. For example, since the drying process of suction and dehumidification is performed in the A cylinder 3, the control exhaust valve 27 is opened after switching the switching valve 26 for a few seconds, and the pressure fluctuation at the start of the regeneration exhaust of the B cylinder 4 is controlled. The above-mentioned exhaust valve 27 is only set to open for 90 seconds, and in between, the B cylinder 4 will continue the regeneration process. Moreover, when about 90 seconds after the dehumidification and drying of the A cylinder 3 starts, the exhaust valve will be closed, so the pressure increasing process will be performed in the B cylinder 4. After the pressure increasing process of the B cylinder 4 will continue for about 30 seconds, after a total of about 120 seconds (2 minutes), the switching valve 26 will switch to the B cylinder 4 for the drying process of adsorption and dehumidification for about 120 seconds (2 minute). After a few seconds from this switching, the exhaust valve 27 is controlled to open. After the A cylinder 3 continues the regeneration process for about 90 seconds, the exhaust valve 27 will be closed for about 30 seconds. It becomes a boost process. This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) -16 · — — — — — — — — — JAW- · 1111111 ^ · 11111111 (Please read the precautions on the back before filling in this Page) 526088 A7 B7 printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of the invention (14) As a result, after about 120 seconds (2 minutes), it was sucked on the side of A tube 3 as described previously. The drying process of dehumidification and the 4 side of the B cylinder become a regeneration and boosting process, and the cycle is repeated as follows. The above-mentioned temperature sensor 2 3 detects the temperature of the compressed air after absorption, dehumidification and drying, and transmits the detection signal to the control circuit 25, where the dew point temperature (dew point under pressure) T a is calculated, and the result is induced by the output force. Voltage to output. -For example, the amount of air required from supply port 9 to the supply site is extremely reduced, and the load is small, or the temperature of the compressed air introduced from the inlet 10 is very low. In addition, dry conditions will move to energy-saving operation. Actually, the flow chart shown in Figure 5 is used as a basis. Compared with the standard full-flow operation, when the flow is low, it will switch to energy-saving operation. That is, from the beginning to the stage S1, the standard operation will be started. Moving from this standard operation to stage S 2, the temperature sensor 23 will detect the temperature of the supplied dry air ^ In stage 3, the control circuit 25 receiving the detection signal sent from the temperature sensor will convert it into the dew point temperature (Dew point under pressure) Ta. Next, at stage S4, the control circuit will compare the set dew point temperature (dew point under pressure) T s, which is recorded in advance, to the calculated dew point temperature T a. When the calculated dew point temperature T a is lower than the set dew point temperature T s or equal, (Ta < Ts) ′ will form Yes and move to stage S 5, and the energy-saving operation to be described later will begin. In addition, 'when the calculated dew point temperature T a is higher than the set dew point temperature T s', it will become N 〇 This paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 male f -17- " III I- ------------- — — — — — — — (Please read the notes on the back before filling out this page) 526088 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs B7 V. Invention Description ( 15) Return to the standard operation of stage S1.

I 在第七圖顯示省能源運轉的控制之第一例子。 預先記憶在控制電路2 5之設定露點T s ,例如在壓 力下露點爲4 0°C,當計算後之露點溫度T a與這個設定 露點溫度T s相等,或者比它低時,省能源運轉開始的信 號將被送出來。 切換閥2 8係將A筒3的除濕乾燥與B筒4的除濕乾 燥,如同先前之說明每間隔兩分鐘進行切換。並且,對於 A筒3,切換除濕乾燥時,幾乎配合其時間開放排氣閥 2 7使B筒4進行再生排氣,之後排氣閥2 7關閉而昇壓 。二分鐘後,B筒4切換成除濕乾燥時幾乎配合其時間使 A筒3進行再生排氣,之後再進行昇壓。 當因負荷非常小,或者導入壓縮空氣的溫度非常低時 ,露點溫度將從一 4 0 °C下降到一 4 5 °C。並且雖然針對 切換閥2 6之切換,控制成繼續兩分鐘,但是排氣閥係保 持在關閉之狀態。因此,A筒3與B筒4將有幾乎均等的 濕的壓縮氣體被導入’各筒3、4內之吸著劑1 7彼此間 將進行相等之吸著作用。如此之下’供輸出來的乾燥空氣 之乾燥度將不會有所變動而保持爲一定。 因爲排氣閥2 7的關閉,而因爲沒有從吸著劑1 7脫 除之濕氣排氣’露點溫度T a將再從一 4 5 °C緩緩上升。 如此,切換閥2 6之切換係爲指定之週期(例如,,3週期 :12分)進行之後’排氣閥27將被開放。 此排氣閥2 7之開放,係指被進行在切換閥2 6之一 本紙張尺度適用中國國家標準(CNS)A4規格(210 x 297公釐) -18 - -----------^—I—I—11 (請先閱讀背面之注意事項再填$頁) 526088 A7 _ B7 五、發明說明(16 ) (請先閱讀背面之注意事項再填寫本頁) 週期。也就是,當切換A筒3的除濕乾燥時,幾乎配合時 間在B筒4將進行再生排氣,而當切換B筒4的除濕乾燥 時,幾乎配合時間在A筒3進行再生排氣。 但是,在省能源運轉中因除濕乾燥之反覆操作,積存 於A、B各筒3、4內之濕氣將被排氣,吸著劑1 7的吸 著度將有一定程度的回覆。此後,在如同上述般繼續控制 切換切換閥2 6」便回到在指定的週期中之排氣閥的關閉 狀態。 因爲這樣的切換到省能源運轉,排氣量將減少而使得 能源損失減少。並且,因爲在個使定之週期進行於各筒3 、4,所以可將吸著劑1 7的劣化仰制到最小限度。· 當負荷回到原來之狀態,或者導入之壓縮空氣的溫度 再上昇時,因爲計算後的露點溫度要比設定露點溫度T s 要來得高,控制電路2 5將再控制回到先前所說明之全流 量的標準運轉。 ' 經濟部智慧財產局員工消費合作社印製 就算回到標準運轉,在省能源運轉中於A、B各筒3 、4已繼續均等的除濕乾燥,所以彼此之間從除濕乾燥過 程所得到之乾燥空氣幾乎沒有露點變動。 另外,在省能源運轉中A、B各筒3、4之吸著劑 1 7的劣化係均等的進行,因此在有必要更換時,便只要 同時更換A、B各筒3、4的吸著劑即可。 以上係說明當負荷非常小只要將少量之除濕乾燥後的 壓縮空氣供給出來即可使省能源運轉,但是以下要說明在 此種少流量之省能源運轉與先前以說明之全流量運轉之間 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -怊_ 526088 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(17 ) ,所謂的在中流量之省能源運轉。 1 如同第八圖所顯示,切換閥2 6係每隔2分鐘被切換 ,而交互在A、B各筒3、4繼續進行除濕乾燥過程。在 一方面,當判斷計算後的露點溫度T a與設定露點溫度 T s相等,或者在其之下時,便進入省能源運轉。也就是 ,配合A筒3的除濕乾燥之切換,在幾乎相同之時間,排 氣閥2 7將關閉在B筒4的再生排氣將中斷。 但是,因負荷大得一些程度,因此因爲再生排氣之中 斷,而使得露點溫度T a變成要比設定露點溫度T s高。 在那裡,配合B筒4的除濕乾燥之切換,在幾乎相同之時 間,排氣閥2 7將開放,在A筒3進行再生排氣。- 所以因爲露點溫度T a再次變成比設定露點溫度低, 因此針對A筒3之除濕切換,幾乎配合在同一時間將排氣 閥27關閉,中斷B筒4之再生排氣。 以下,中流量之省能源運轉係在針對切換閥2 6之A 、B各筒3、4之除濕乾燥的四個週期中,當只要露點溫 度T a要比設定露點溫度T s上昇時,將排氣閥2 7開放 ,而在相對應之各筒3、4進行再生排氣。因此,可極力 控制當回到標準運轉時之露點溫度等·,與先前所說明之少 流量之省能源運轉完全相同。 而且,在圖上雖然沒有特別顯示,依據條件,在少流 量之能源運轉中,也可以分等級來進行。 , 也就是,先前已說明之少流量省能源運轉,於針對切 換閥26之A、B各筒3、4,每四個週期之除濕乾燥的 I----------^ — — — — — — I— ^- — — — — — — 1— (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -20 - 526088 A7 ----B7 五、發明說明(18 ) 切換中,而將排氣閥2 7開放,但是不限定於此。 t (請先閱讀背面之注意事項再填寫本頁) 預先記億之設定露點溫度T s達到更低時,例如以壓 力下露點一 6 0°C或者一 8 Ot:爲基準,切換閥2 6之除 濕乾燥切換爲每6週期、或者8週期將排氣閥2 7開放一 次’便得進行流量更少之省能源運轉。 在第9圖’顯示在省能源運轉之控制的第2個例子, 與上述現況相同省能源運轉的開始信號被送出來。 切換閥2 8係將A筒3的除濕乾燥與B筒4的除濕乾 燥’如同先前之說明作間隔2分鐘之切換。並且,針對A 筒3之除濕切換幾乎配合在同一時間將排氣閥2 7開放, 使B筒4進行再生排氣之後關閉排氣閥2 7而昇壓。2分 鐘後,配合B筒4之除濕切換幾乎在同一時間使A筒3進 行再生排氣,之後進行昇壓。 經濟部智慧財產局員工消費合作社印製 當在負荷變小,或者導入之壓縮空氣的溫度非常低的 地方,露點溫度將從一 4 0 °C下降到一 4 5 °C。接著雖然 針對切換閥2 6控制切換繼續在間隔2分鐘之下,但是排 氣閥是保持在關閉之狀態。因此,在A筒3與B筒4幾乎 均等地導入壓縮空氣,各筒3、4內的吸著劑1 7彼此之 間進行相等之吸著作用。因此供給出來的乾燥空氣之乾燥 度將不會變動而保持一定。 因爲排氣閥2 7的關閉,不會將從吸著劑1 7脫除之 濕氣排除,所以露溫度T a將從一 4 5 °C再度徐徐上昇。 如此切換閥2 6之切換以指定之週期(例如3個週期:I Figure 7 shows the first example of control for energy saving operation. Set the dew point T s in the control circuit 25 in advance. For example, the dew point under pressure is 40 ° C. When the calculated dew point temperature T a is equal to or lower than the set dew point temperature T s, energy-saving operation The start signal will be sent. The switching valves 2 and 8 switch the dehumidification and drying of the A cylinder 3 and the dehumidification and drying of the B cylinder 4 as described above. In addition, for the A cylinder 3, when the dehumidification and drying are switched, the exhaust valve 27 is opened at almost the same time to regenerate the exhaust of the B cylinder 4, and then the exhaust valve 27 is closed to increase the pressure. After two minutes, the B cylinder 4 was switched to dehumidification and drying for almost the time required to regenerate and exhaust the A cylinder 3, and then pressurize. When the load is very small, or the temperature of the compressed air is very low, the dew point temperature will drop from-40 ° C to -45 ° C. Also, although the switching of the switching valve 26 is controlled to continue for two minutes, the exhaust valve is kept closed. Therefore, the A and B cylinders 3 and 4 will have almost equal wet compressed gas to be introduced into the sorbents 17 in each of the cylinders 3 and 4, and they will perform equal suction functions. In this way, the dryness of the dry air supplied will not change and will remain constant. Because the exhaust valve 27 is closed, and because the moisture is not removed from the sorbent 17, the dew point temperature T a will gradually rise again from a temperature of 45 ° C. In this way, the switching of the switching valve 26 is performed at a designated cycle (for example, 3 cycles: 12 minutes), and the exhaust valve 27 is opened. The opening of this exhaust valve 2 7 means that one of the switching valves 2 6 is used. The paper size applies the Chinese National Standard (CNS) A4 (210 x 297 mm) -18--------- --- ^ — I—I—11 (Please read the precautions on the back before filling in the $ page) 526088 A7 _ B7 V. Description of the invention (16) (Please read the precautions on the back before filling in this page) Cycle. That is, when the dehumidification and drying of the A cylinder 3 is switched, the regenerative exhaust will be performed in the B cylinder 4 at almost the matching time, and when the dehumidification and drying of the B cylinder 4 is switched, the regenerative exhaust will be performed in the A cylinder 3 at almost the matching time. However, due to the repeated operation of dehumidification and drying during energy-saving operation, the moisture stored in the barrels 3 and 4 of A and B will be exhausted, and the absorption of the sorbent 17 will have a certain degree of response. After that, the control of the switching valve 2 6 ″ is continued as described above, and the exhaust valve is closed in the specified period. Because switching to energy-saving operation like this, the exhaust volume will be reduced and the energy loss will be reduced. In addition, since each of the tubes 3 and 4 is performed at a fixed period, the deterioration of the sorbent 17 can be minimized. · When the load returns to its original state, or the temperature of the compressed air introduced again rises, because the calculated dew point temperature is higher than the set dew point temperature T s, the control circuit 25 will re-control back to the previous description Full flow standard operation. '' Even if the consumer cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs prints it back to standard operation, in the energy-saving operation, the dehumidification and drying of the A and B cylinders 3 and 4 have continued to be uniform, so the drying obtained from the dehumidification and drying process between each other There is almost no dew point change in the air. In addition, during the energy-saving operation, the degradation of the sorbent 17 of the barrels 3 and 4 of A and B is uniformly performed. Therefore, if it is necessary to replace, the adsorption of the barrels 3 and 4 of A and B can be replaced at the same time. Agent. The above is that when the load is very small, only a small amount of compressed air after dehumidification and drying can be supplied to enable energy-saving operation. However, the following explains the difference between this low-flow energy-saving operation and the full-flow operation previously described. Paper size applies Chinese National Standard (CNS) A4 specification (210 X 297 mm)-怊 _ 526088 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 5. Invention Description (17), the so-called energy saving in medium flow Operational. 1 As shown in the eighth figure, the switching valve 2 6 is switched every 2 minutes, and the dehumidification and drying process is continued in the barrels 3 and 4 of A and B. On the one hand, when it is judged that the calculated dew point temperature T a is equal to or lower than the set dew point temperature T s, it enters an energy-saving operation. That is, in conjunction with the dehumidification and drying switching of the A cylinder 3, the exhaust valve 27 will close at the same time, and the regeneration exhaust of the B cylinder 4 will be interrupted. However, the load is so large that the dew point temperature T a becomes higher than the set dew point temperature T s because the regeneration exhaust gas is interrupted. There, in accordance with the dehumidification and drying switching of the B cylinder 4, the exhaust valve 27 will be opened at almost the same time, and the A cylinder 3 will be regenerated and exhausted. -Because the dew point temperature T a becomes lower than the set dew point temperature again, for the dehumidification switching of the A cylinder 3, the exhaust valve 27 is closed at the same time, and the regeneration exhaust of the B cylinder 4 is interrupted. In the following, the energy-saving operation of the medium flow rate is performed in the four cycles of dehumidification and drying of the A and B barrels 3 and 4 of the switching valve 26. When the dew point temperature T a is higher than the set dew point temperature T s, the The exhaust valve 27 is opened, and regenerative exhaust is performed in the corresponding cylinders 3 and 4. Therefore, it is possible to control the dew point temperature and the like when returning to the standard operation as much as possible. In addition, although it is not particularly shown in the figure, depending on the conditions, it can also be carried out in different levels in a low-flow energy operation. That is, the low-flow and energy-saving operation that has been described previously, for the four and four cycles of the dehumidification and drying of the A and B barrels 3 and 4 of the switching valve 26 ---------- ^- — — — — — I— ^-— — — — — — 1— (Please read the notes on the reverse side before filling out this page) This paper size applies to China National Standard (CNS) A4 (210 X 297 mm)- 20-526088 A7 ---- B7 V. Description of the invention (18) The exhaust valve 2 7 is opened, but it is not limited to this. t (Please read the precautions on the back before filling in this page) When the set dew point temperature T s recorded beforehand reaches 100%, for example, the dew point under pressure-60 ° C or-8 Ot: as the reference, the switching valve 2 6 The dehumidification and drying is switched to opening the exhaust valve 27 every 6 cycles or 8 cycles, and energy-saving operation with less flow is required. Fig. 9 'shows a second example of the control of the energy-saving operation, and the start signal of the energy-saving operation is transmitted in the same manner as the above-mentioned current situation. The switching valves 2 and 8 switch between the dehumidification and drying of the A cylinder 3 and the dehumidification and drying of the B cylinder 4 as described above. In addition, the dehumidification switching for the A cylinder 3 is almost matched with opening the exhaust valve 27 at the same time, and the B cylinder 4 is regenerated and exhausted, and the exhaust valve 27 is closed to increase the pressure. After 2 minutes, in conjunction with the dehumidification switch of the B tube 4, the A tube 3 is regenerated and exhausted at about the same time, and then boosted. Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. When the load becomes small or the temperature of the compressed air introduced is very low, the dew point temperature will drop from-40 ° C to -45 ° C. Next, although the control switching for the switching valve 26 continues below the interval of 2 minutes, the exhaust valve is kept closed. Therefore, compressed air is introduced into the A and B cylinders 3 and 4 almost evenly, and the sorbents 17 in the cylinders 3 and 4 perform equal suction functions with each other. Therefore, the dryness of the supplied dry air will not change and remain constant. Because the exhaust valve 27 is closed, the moisture removed from the sorbent 17 will not be removed, so the dew temperature T a will gradually rise again from 45 ° C. In this way, the switching of the switching valves 26 is performed at a specified cycle (for example, 3 cycles:

1 2分)來進行之後,排氣閥2 7將被控制在接下來的A 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) · 21 經濟部智慧財產局員工消費合作社印製 526088 A7 __ B7 五、發明說明(19 ) 、B雨筒3、4之除濕乾燥之切換的1個週期中。1 2 points), the exhaust valve 2 7 will be controlled at the next A. This paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm). 21 Employees ’Cooperatives, Intellectual Property Bureau, Ministry of Economic Affairs Print 526088 A7 __ B7 V. Description of the invention (19), B rain tube 3, 4 is switched in a cycle of dehumidification and drying.

I 也就是,以開始切換切換閥2 6之切換週期爲基準, 在第4個週期排氣閥2 7將被控制。具體來說,配合A筒 3之除濕乾燥的切換,幾乎在同一時間B筒4將進行再生 排氣,而配合B筒4之除濕乾燥的切換,幾乎在同一時間 A筒3將進行再生排氣。 由此,在省能源運轉之中除濕乾燥之反覆操作,積存 在A、B各筒3、4內之濕氣將被強制地排除,吸著劑 17的吸著度將回復到某一個程度。 之後,再繼續進行控制如上述控制切換閥2 6之切換 ,與每4個週期的排氣閥2 7之控制。在繼續省能·源運轉 中上述之模式不會放變。 減少排氣量將可使能量損失減少,進行所謂省能源運 轉。而且,在指定之週期針對各筒3、4內之吸著劑進行 強制排氣,所以可以將吸著劑1 7之劣化抑制到最小限度 〇 當負荷回復到原狀態,或者所導入之壓縮空氣的溫度 再度上昇時,因爲計算後的露點溫度變成要比設定露點溫 度高,所以控制電路2 5將再控制回到先前已說明之全流 量的標準運轉。 就算回到標準運轉,在省能源運轉中針對A、B各筒 3、4之脫著劑1 7,均等地將脫除之濕氣強制排,除進行 再生過程,所以所得到之乾燥空氣之露點幾乎沒有變動。 另外,在省能源運轉中於A、B個筒3、4之吸著劑 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 22- ' I--I JAW ·1111111 ^-1111111 (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 526088 A7 _ B7 五、發明說明(2〇 ) 1 7之劣化將均等進行,因在有交換之必要時,只要同時 將A、B各筒3、4之吸著劑1 7交換即可。 並且,在先前已說明之停止再生過程之省能源運轉中 ’雖然將排氣閥1 7控制開放成針對每4個切換閥2 6之 A、B各筒3、4之除濕乾燥切換之週期,但並不局限於 此。 、 第1 0圖(A ) ( B )係顯示省能源運轉控制之第3 個例子。 如同第1 0圖(A )所顯示,將排氣閥2 7控制成於 每5個除濕乾燥切換週期開放亦可,此週期數係判斷對應 於例如因吸著乾燥後的空氣之露點所造成了負荷等種種條 件來作適當之變更。 另外,在省能源運轉之中,必不限定一定要針對切換 閥2 6之A、B各筒3、4交互進行除濕乾燥切換。例如 第1 0圖(B )所顯示,在關閉排氣閥2 7停止再生過程 之時,亦可以將切換閥2 6保持切換從A筒3到B筒4之 狀態下,進行省能源運轉。 但是,就算在這種狀態下,也一定要控制排氣閥2 7 在指定之週期開放使針對各筒3、4之吸著劑1 7進行均 等的強制性排氣。 【發明之效果】 , 根據記載於申請專利範圍第1項〜第3項之發明,在 所謂省能源運轉時,一方面於兩吸著筒繼續進行除濕乾燥 本纸張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) · 23 · ----------^丨1·裝--------訂--- (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 526088 A7 B7 五、發明說明(21 ) 之切換,因爲停止在各筒之再生排氣,因排氣而抑制乾燥That is, based on the start of the switching cycle of the switching valve 26, the exhaust valve 27 will be controlled in the fourth cycle. Specifically, with the switching of the dehumidification and drying of the A cylinder 3, the B cylinder 4 will be regenerated and exhausted at about the same time, and with the switching of the dehumidification and drying of the B cylinder 4, the A cylinder 3 will be regenerated and exhausted at about the same time. . Therefore, in the repeated operation of dehumidification and drying during energy-saving operation, the moisture accumulated in the barrels 3 and 4 of A and B will be forcibly removed, and the adsorption of the sorbent 17 will be restored to a certain level. After that, control such as the switching of the control switching valve 26 and the control of the exhaust valve 27 every 4 cycles are continued. The above-mentioned mode will not be changed during the continuous energy saving and source operation. Reducing the amount of exhaust gas will reduce energy loss and perform so-called energy-saving operations. In addition, the sorbent in each cylinder 3 and 4 is forcedly vented in a specified period, so the degradation of the sorbent 17 can be suppressed to a minimum. When the load returns to the original state, or the compressed air is introduced When the temperature rises again, since the calculated dew point temperature becomes higher than the set dew point temperature, the control circuit 25 will return to the standard operation of the full flow rate previously explained. Even when returning to standard operation, in the energy-saving operation, for the release agents 17 of the barrels 3 and 4 of A and B, the removed moisture is forcibly discharged evenly, and the regeneration process is performed, so the dry air obtained The dew point has hardly changed. In addition, in the energy-saving operation of the sorbents in the A and B cylinders 3 and 4, the paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) 22- 'I--I JAW · 1111111 ^ -1111111 (Please read the notes on the back before filling out this page) Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs, Employee Consumption Cooperative, 526088 A7 _ B7 V. Description of the invention (20) The degradation of 7 will be carried out evenly, as there are exchanges If necessary, it is only necessary to exchange the sorbents 17 of the barrels 3 and 4 of A and B at the same time. In addition, in the energy-saving operation of stopping the regeneration process described previously, 'Although the exhaust valve 17 is controlled to be opened to a cycle of dehumidification and drying switching for each of A, B barrels 3, 4 of 4 switching valves 26, But it is not limited to this. Figure 10 (A) (B) shows the third example of energy-saving operation control. As shown in Fig. 10 (A), it is also possible to control the exhaust valve 27 to open every five dehumidification and drying switching cycles. The number of cycles is determined to correspond to, for example, the dew point caused by absorption of dry air. Various conditions such as load were changed to make appropriate changes. In addition, in energy-saving operation, there is no limitation on dehumidifying and drying switching for the A, B cylinders 3, 4 of the switching valve 26. For example, as shown in FIG. 10 (B), when the exhaust valve 27 is closed to stop the regeneration process, the switching valve 26 can also be switched from the A cylinder 3 to the B cylinder 4 for energy-saving operation. However, even in this state, it is necessary to control the exhaust valve 2 7 to be opened at a designated period so that the sorbent 17 for each of the cylinders 3 and 4 is uniformly and compulsorily exhausted. [Effects of the invention] According to the inventions described in claims 1 to 3 of the scope of the patent application, during the so-called energy-saving operation, on the one hand, the dehumidification and drying are continued on the two suction cylinders. This paper applies the Chinese national standard (CNS) ) A4 size (210 X 297 mm) · 23 · ---------- ^ 丨 1 · Packing -------- Order --- (Please read the notes on the back before filling (This page) Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs, Employee Consumer Cooperatives. 526088 A7 B7 V. Switching of the description of invention (21), because the regenerative exhaust in each cylinder is stopped, and the drying is inhibited by the exhaust.

I 空氣之排出量之同時,兩吸著筒的吸著劑之劣化將呈均等 進行,抑制於回到標準運轉時在各吸著筒間之露點溫度的 變動,使得信賴性增加之同時,兩吸著筒的吸著劑交換的 時間將相同,排除不必要的交換達到降低運轉成本之效果 〇 ^ 根據記載於申請專利範圍第4項〜第6項之發明,在 所謂省能源運轉時,因爲在指定之週期針對各吸著筒之吸 著劑進行強制排氣,所以藉由排氣而將乾燥空氣的排氣量 維持在少量,並且兩吸著筒之吸著劑之劣化將均等進行, 抑制在回到標準運轉時,在各吸著筒間之露點溫度之變動 ,使得信賴性提高之同時,兩吸著筒的吸著劑之交換時間 將相同,排除不必要的交換達到降件運轉成本之效果。 【圖面之簡單說明】 第1圖有關本發明的一實施例形態之除濕裝置的外觀 斜視圖。 第2圖同實施形態之除濕裝置的槪略斷面圖。 第3圖說明同實施形態之除濕裝置的槪略斷面圖,而 與第2圖屬不同過程之圖。 第4圖A〜D係說明同實施形態之構成除濕作用之流 路之切換順序。 , 第5圖同實施形態之從標準運轉到切換至省能源運轉 之流程圖。 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -24 - --— — — — — — — — — — — — — — I— ^ ·11111111 (請先閱讀背面之注意事項再填寫本頁) 526088 A7 B7 五、發明說明(22 ) 第6圖同實施形態之標準運轉時的控制說明圖。 第7圖同實施形態之少流量時之省能源運轉時的控制 之第1例子說明圖。 第8圖同實施形態之中流量時之省能源運轉時的控制 之說明。 第9圖同實施形態之少流量時之省能源運轉時的控制 之第2例子說明圖。 第1 0圖A、B係同實施形態之少流量時之省能源運 轉時的控制之第3例子說明圖。 第1 1圖以往之省能源運轉時的控制說明圖。 【圖號說明】 (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 3 吸著 筒 ( A 筒 ) 4 吸著 筒 ( B 筒 ) 1 7 吸著 劑 2 3 溫度 感 應 器 2 5 控制 電 路 ( 控 制 手 段) 2 6 切換 閥 ( 切 換 手 段 ) 2 7 排氣 手 段 ( 排 氣 閥 ) 3 0 導入 路 徑 3 1 A筒 連 通 路 徑 3 2 B筒 連 通 路 徑 3 3 通口 連 通 路 徑 3 4 排氣 分岐路 徑 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -25-I At the same time as the amount of air is discharged, the degradation of the sorbent in the two sorption cartridges will progress uniformly, and the fluctuation in the dew point temperature between the sorption cartridges will be suppressed when returning to standard operation. The sorbent exchange time of the suction tube will be the same. Eliminating unnecessary exchange will reduce the cost of operation. ^ According to the inventions described in the fourth to sixth aspects of the patent application scope, in the so-called energy-saving operation, because Forcibly evacuate the sorbent of each sorbent cartridge at a specified period, so the amount of dry air is kept at a small amount by exhausting, and the degradation of the sorbent of the two sorbent cartridges is evenly performed. When the return to standard operation is suppressed, the change in the dew point temperature between the suction tubes improves the reliability. At the same time, the exchange time of the sorbents of the two suction tubes will be the same, eliminating unnecessary exchanges to achieve the drop operation. The effect of cost. [Brief Description of the Drawings] FIG. 1 is a perspective view showing an external appearance of a dehumidifying device according to an embodiment of the present invention. Fig. 2 is a schematic sectional view of a dehumidifier of the same embodiment. Fig. 3 is a schematic cross-sectional view of the dehumidifier according to the same embodiment, and Fig. 3 is a diagram of a different process from Fig. 2. Figures 4 to 4 show the switching sequence of the flow path constituting the dehumidification function in the same embodiment. Fig. 5 is the same flowchart of switching from standard operation to energy-saving operation in the embodiment. This paper size applies to China National Standard (CNS) A4 specifications (210 X 297 mm) -24---- — — — — — — — — — — — — — 11111111 (Please read the note on the back first Please fill in this page again for the matters) 526088 A7 B7 V. Description of the invention (22) Figure 6 is the same as the control explanatory diagram of the standard operation of the embodiment. Fig. 7 is a diagram illustrating a first example of control during energy-saving operation at a low flow rate in the same embodiment. Fig. 8 illustrates the control during the energy-saving operation during the flow rate in the embodiment. Fig. 9 is a diagram illustrating a second example of the control during the energy-saving operation when the flow rate is small in the embodiment. Fig. 10 A and B are explanatory diagrams of a third example of control during energy-saving operation at a low flow rate in the same embodiment. Fig. 11 is an explanatory diagram of control during conventional energy-saving operation. [Illustration of drawing number] (Please read the notes on the back before filling this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 3 Suction tube (A tube) 4 Suction tube (B tube) 1 7 Suction agent 2 3 Temperature sensor 2 5 Control circuit (control means) 2 6 Switching valve (switching means) 2 7 Exhaust means (exhaust valve) 3 0 Introduction path 3 1 A tube communication path 3 2 B tube communication path 3 3 Port Communication path 3 4 Exhaust divergence path This paper size is applicable to China National Standard (CNS) A4 specification (210 X 297 mm) -25-

Claims (1)

526088 A8 B8 C8 D8 六、申請專利範圍 第89 1 105 1 1號專利申請案 中文申請專利範圍修正本 (請先閱讀背面之注意事項再填寫本頁) 民國91年5月修正 1 · 一種壓縮氣體之除濕方法,是在2座充塡有吸著 劑之吸著筒之中在一方導入濕的壓縮氣體,進行吸著除濕 之乾燥過程,以及將藉此乾燥過程所得到之乾燥氣體的一 部分導入在前階段之乾燥過程使吸濕能力減低之另一方吸 著筒,而從吸著劑將濕氣脫除,並且將脫除之濕氣從吸著 筒中排除之再生過程同時被進行,而在此種將乾燥過程與 再生過程交互切換於兩吸著筒之間,以便連續供給乾燥氣 體之壓縮氣體之除濕方法,其特徵爲: 具備有在所定之條件下一方面在兩吸著筒之間交互地 繼續乾燥過程之同時,停止脫除之濕氣從各吸著筒排出之 停止過程。 經濟部智慧財產局員工消費合作社印製 2 ·如申請專利範圍第1項之壓縮氣體之除濕方法, 其中上述所定之條件爲在乾燥過程所得之乾燥氣體的露點 溫度(壓力露點)T a係與設定露點溫度(壓力下露點) Ts相等,或者較之爲低(TaSTs)。 3 · —種壓縮氣體除濕裝置,是2座充塡有吸著劑之 吸著筒,與藉由切換手段將這此吸著筒連通之連通路徑以 及排氣手段,其中將濕的壓縮氣體導入一方之吸著筒吸著 除濕而乾燥,將此乾燥氣體之一部分導入另一方之吸著筒 從在前階段使吸濕能力減低之吸著劑中將濕氣脫除,並且 藉由排氣手段將脫除之濕氣從吸著筒排除同時進行再:生, 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 一 526088 A8 B8 C8 D8 六、申請專利範圍 (請先閱讀背面之注意事項再填寫本頁) 以上述切換手段之切換爲基準,在兩吸著筒之間交互切換 乾燥與再生,使其能連續地供給乾燥氣體,其特徵爲: 具備有在所定之條件,一方面繼續切換手段之切換, 使在兩吸著筒之間交互地繼續將濕的壓縮氣體除濕乾燥, 而控制針對各吸著筒停止排氣手段之控制手段。 4 · 一種壓縮氣體之除濕方法,在2座充塡有吸著劑 之吸著筒之一方,導入濕的壓縮氣體進行吸著除濕之乾燥 過程,以及藉此乾燥過程所得之乾燥氣體之一部分導入在 前階段之乾燥過程,使吸濕能力減低之另一方吸著筒從吸 著劑中將濕氣脫除,並且將脫除之濕氣從吸著筒排除同時 進行再生過程,這些乾燥過程與再生過程交互切換於兩吸 著筒之間使之能連續地供給乾燥氣體,其特徵爲: 具有在所定之條件下進行停止上述再生過程之省能源 運轉之同時,在此省能源運轉中以所定之週期來進行再生 過程。 經濟部智慧財產局員工消費合作社印製 5 .如申請專利範圍第4項之壓縮氣體之除濕方法, 其中在上述省能源運轉中,上述乾燥過程係交互地繼續在 兩吸著筒之間,或者只繼續在一方之吸著筒。 6 . —種壓縮氣體之除濕裝置,2座充塡有吸著劑之 吸著筒,與藉由切換手段將這些吸著筒連通之連通路徑及 排氣手段,將濕的壓縮氣體導入一方之吸著筒,使之吸著 除濕且乾燥,另將此乾燥氣體之一部分導入另一方之吸著 筒從在前階段使吸濕能力減低之吸著劑中將濕氣脫除,且 藉由排氣手段將脫除之濕氣從吸著筒排氣同時進行再生, 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 526088 A8 B8 C8 D8 々、申請專利範圍 並以上述切換手段之切換爲基準,在兩吸著筒之間交互地 切換乾燥與再生使之能連續地供給乾燥氣體,其特徵爲: 具備有在所定之條件下,停止上述再生過程而呈省肯g 源運轉之同時,控制在該省能源運轉中以所定週期進行再 生過程之控制手段。 --------·裝-- (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐)526088 A8 B8 C8 D8 VI. Application for Patent Scope No. 89 1 105 1 No. 1 Patent Application in Chinese Revised Patent Scope (Please read the precautions on the back before filling out this page) Amended in May 91 of the Republic of China1. A compressed gas The dehumidification method is to introduce wet compressed gas into one of two sorption cylinders filled with sorbent, perform a drying process of adsorption and dehumidification, and introduce a part of the dry gas obtained by the drying process. The drying process in the previous stage reduces the moisture absorption capacity of the other suction tube, and the moisture is removed from the adsorbent, and the regeneration process of removing the removed moisture from the suction tube is performed simultaneously, and in the This dehumidification method that alternately switches the drying process and the regeneration process between the two suction cylinders so as to continuously supply the compressed gas of the drying gas is characterized in that it is provided with one side between the two suction cylinders under the predetermined conditions. While the drying process is continued alternately, the stopping process of the discharged moisture from each suction cylinder is stopped. Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs2. If the compressed gas dehumidification method of item 1 of the scope of patent application, the above-mentioned conditions are the dew point temperature (pressure dew point) of the dry gas obtained during the drying process. Set dew point temperature (dew point under pressure) Ts is equal or lower (TaSTs). 3. A type of compressed gas dehumidification device, which is two suction tubes filled with an adsorbent, and a communication path that connects the suction tubes with a switching means and an exhaust means, in which the wet compressed gas is introduced One suction tube absorbs moisture and dries, and then introduces a part of this dry gas into the other suction tube to remove moisture from the sorbent that has reduced the moisture absorption capacity in the previous stage, and exhausts it by means of exhaust. The removed moisture is removed from the suction tube and reprocessed at the same time: Regeneration, the paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm)-526088 A8 B8 C8 D8 VI. Application for patent scope (please read the back first (Notes for filling in this page, please fill in this page) Based on the above-mentioned switching method, the drying and regeneration are alternately switched between the two suction cylinders, so that it can continuously supply dry gas. It is characterized by: On the one hand, the switching of the switching means is continued, so that the wet compressed gas is continuously dehumidified and dried alternately between the two suction cylinders, and the control means for stopping the exhaust means for each suction cylinder is controlled. 4 · A method for dehumidifying compressed gas, in which one of the two suction cylinders filled with an adsorbent is introduced with a wet compressed gas for adsorption and dehumidification drying process, and a part of the drying gas obtained by the drying process is introduced In the previous stage of the drying process, the other suction tube that reduced the moisture absorption capacity removes moisture from the sorbent, and removes the removed moisture from the suction tube while performing a regeneration process. These drying processes are related to The regeneration process is alternately switched between the two suction cylinders so that it can continuously supply dry gas. It is characterized by having the energy-saving operation of stopping the regeneration process under predetermined conditions, and in the energy-saving operation with the predetermined Cycle to carry out the regeneration process. Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. If the compressed gas dehumidification method of item 4 of the patent application scope, in the above energy-saving operation, the above-mentioned drying process is continued between the two suction cups interactively, or Only continue to suck the tube on one side. 6. A kind of compressed gas dehumidification device, 2 suction tubes filled with sorbent, and the communication path that connects these suction tubes by switching means and exhaust means to introduce wet compressed gas to one side The suction tube is made to absorb and dehumidify and dry, and a part of this dry gas is introduced into the other suction tube to remove the moisture from the absorbing agent that has reduced the moisture absorption capacity in the previous stage, and by exhausting Removal of the removed moisture from the suction tube at the same time by air means. The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 526088 A8 B8 C8 D8 々, the scope of patent application and the above switching means The switching is used as a reference, and the drying and regeneration are alternately switched between the two suction cylinders so that the dry gas can be continuously supplied. It is characterized by having the above-mentioned regeneration process stopped under a predetermined condition and operated in a ken-g source. At the same time, control means to perform the regeneration process at a predetermined cycle in the energy-saving operation of the province. -------- · Installation-- (Please read the precautions on the back before filling out this page) Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs, Employee Consumer Cooperatives This paper is sized to the Chinese National Standard (CNS) A4 (210X 297) Mm)
TW089110511A 1999-06-09 2000-05-30 Dehumidifying method for compressed gas and its apparatus TW526088B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP16236499A JP3483797B2 (en) 1999-06-09 1999-06-09 Method and apparatus for dehumidifying compressed gas
JP16236399A JP3517157B2 (en) 1999-06-09 1999-06-09 Method and apparatus for dehumidifying compressed gas

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TW526088B true TW526088B (en) 2003-04-01

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9109807B2 (en) 2011-12-21 2015-08-18 Industrial Technology Research Institute Device for desorption and dehumidification and system using the same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN203598672U (en) * 2013-10-28 2014-05-21 郭应辉 Adsorption drying device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9109807B2 (en) 2011-12-21 2015-08-18 Industrial Technology Research Institute Device for desorption and dehumidification and system using the same

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CN1115188C (en) 2003-07-23
KR20010007322A (en) 2001-01-26
KR100586775B1 (en) 2006-06-08
CN1277074A (en) 2000-12-20

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