TWM351333U - Coolant free drying refrigeration system - Google Patents

Coolant free drying refrigeration system Download PDF

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Publication number
TWM351333U
TWM351333U TW97202444U TW97202444U TWM351333U TW M351333 U TWM351333 U TW M351333U TW 97202444 U TW97202444 U TW 97202444U TW 97202444 U TW97202444 U TW 97202444U TW M351333 U TWM351333 U TW M351333U
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Taiwan
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gas
cold
hot
air outlet
inlet
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TW97202444U
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Chinese (zh)
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Zhi-Min Li
Bo-Huei Chen
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Bo-Huei Chen
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Priority to TW97202444U priority Critical patent/TWM351333U/en
Publication of TWM351333U publication Critical patent/TWM351333U/en

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  • Drying Of Solid Materials (AREA)

Description

M351333 八、新型說明: 【新型所屬之技術領域】 種無冷媒乾燥 本創作係關於-種冷; 東系統,特別是指 冷康系統。 【先前技術】 士了因應產業對壓縮氣體的需求(例如加工機於作動拒 而,门£4’但未經處理的壓缩氣體,不僅渔度高且溫方 也兩;,為了解決前述問題,進而發展出—種冷象式乾燥系舍 =,該冷;東室乾燥系統9Q(請參閱第1圖所示)包含-儲氣相 二二管路萄器92、—冷料乾燥機93、—油霧過遽器叫 4达過濾态95及一除臭過濾器% ; 但上述習用結構進—步分析,仍存在下列問題: 該t料乾燥线%必須透㈣冷料㈣進朽 ",目刖的該冷凍式乾燥機93係運用 :=的,油氣凝結排除’但此冷媒正是破動二 地:表:氧_壞將造成大量的紫外線肆無忌.憚 宝,』3 :、 對於居住於地球表面的生物皆直接鸟 告,不淪是生理或心理都將遭受雙重傷害丨 又 濟,氣體必須安裝複數個過“龍縮氣體進行過 及維二 皆屬耗材’為了前述耗材所耗費的安裝成本 、’、U成本,僅會加重使用者的負擔; .M351333 故如何解決上述問題正是目前極需改良研發之問題所 在。 - 有鑑於此,本案創作人乃經詳思細索,遂以多年的經驗 - 加以設計,經多方探討並試作樣品試驗,及多次修正改良, 終而開發出一種無冷媒乾燥冷;東系統。 • 【新型内容】 本創作係一種無冷媒乾燥冷凍系統,其目的在於透過氣 • 水分離器對壓縮氣體進行氣水分離,以及冷熱分離器對壓縮 - 氣體進行冷熱分離,並混合冷氣體與熱氣體進行供給。 為達上述目的,本創作包含至少一氣體除水器及至少一 冷熱分離器,其中:該氣體除水器具有一導入口及一導出口, 奉 且於内設有一容置空間,該導入口係供壓縮氣體導入,該容 置空間中設置一氣水分離室,該氣水分離室隔設至少二導流 空間,讓導流空間相互連通,該導入口與導出口分別與該氣 水分離室連接進行氣水分離;該冷熱分離器於内設有一冷熱 分離室,且具有一入口、一冷出風口及一熱出風口,前述三 者分別與該冷熱分離室相連通,該入口與該氣體除水器的導 出口連接進行冷熱分離;該冷熱分離器的熱出風口及冷出風 口作管路連結進行氣體混合。 6 M351333 藉由前述進一步分析將可獲得下述功效: 1. 該無冷媒乾燥冷凍系統無須冷媒為媒介,即可對壓縮 氣體進行氣水分離及冷熱分離,不僅合乎環保,且降低地球 環境及生物的傷害。 2. 該無冷媒乾燥系統無須安裝複數個過濾器,即可對壓 縮氣體進行濾除,降低耗材更換的成本負擔,相對的維修成 本也隨著降低。。 【實施方式】 有關本創作所採用之技術、手段及其他之功效,茲舉一 較佳實施例,並配合圖示詳細說明如下,相信本創作上述之 目的、特徵及其他優點,當可由之得一深入而具體瞭解; 本創作無冷媒乾燥冷凍系統包含包括複數個氣體除水器 10及一冷熱分離器20 ; 該氣體除水器1〇(請參閱第2圖所示)具有一筒11及一蓋 12,該筒11與該蓋12—侧皆具有一組合部111、121,前述該 組合部111、121相對設有螺紋段,該筒11的組合部111螺紋段 相對該蓋12的組合部121螺紋段螺鎖結合,該蓋12上另具有一 導入口 121及一導出口 122,該筒11與該蓋12結合後形成一容 置空間13 ;上述該筒11與蓋12係可一體成型,該筒11與蓋12 即可不用設計組合部1Π、121,同樣於内部成型一容置空間 M351333 — 該容置空間13中設置一氣水分離室14,該氣水分離室14 具有至少一片狀的分隔件141,該氣水分離室14透過該分隔件 141形成至少二導流空間142,該分隔件141設有一氣孔143, - 讓導流空間142相互連通,該分隔件141的氣孔143設置位置必 - 須錯開,藉此讓壓縮氣體於導流空間142迂迴前進產生碰撞, 藉此增加水氣及油氣的附著量,該蓋12的導入口 121與導出口 122分別與該氣水分離室14二端連接,讓壓縮氣體(本創作採 • 用空壓機A提供壓縮氣體)由該蓋12的導入口 121導入,接著通 過該氣水分離室14之各分隔件141的氣孔143,最後由該蓋12 - 的導出口 122導出。 該冷熱分離器20於内設有一冷熱分離室201,且具有一入 口 21、一冷出風口22及一熱出風口23,前述三者分別與該冷 熱分離室201相連通,該冷出風口22與該熱出風口23分別設置 • 於該冷熱分離室201二端,該入口 21設置於該冷熱分離室201 一侧,該入口21與該氣體除水器10的導出口 122連接; 當該氣體經由該冷熱分離器20的入口 21導入該冷熱分離 室201,該氣體順沿該入口 21朝著該冷熱分離室201喷出,於 該冷熱分離室201中高速旋轉,藉由旋轉產生離心力,且透過 離心力的作用,靠近該冷熱分離室201外壁的氣體其壓力與密 度將上升,遠離該冷熱分離室201内壁的氣體其壓力與密渡將 下降,讓高壓力與高密度的氣體朝低壓力與低密度的氣體流 8 M351333 - 動,因著該冷熱分離室201内的壓力變化,讓熱氣體經由該熱 出風口23導出,讓冷氣體經由該冷出風口22導出,且該冷熱 分離器20的熱出風口23及冷出風口22最後再做管路連結進行 - 混合。 為了調整該冷熱分離器20(請參閱第2圖所示)的熱出風口 23及冷出風口 22的氣體流量,可以視需求對該熱出風口 23與 # 冷出風口 22安裝的管路作不同管徑的變化進行限流,譬如該 冷熱分離器20的熱出風口23口徑約大於、約小於或等於該冷 - 出風口22 口徑;另可視需求於該熱出風口23與冷出風口22安 - 裝控制閥30作閥門開口的變化進行限流。 為了處理大流量的壓縮氣體,該冷出風口 22(請參閱第3 圖所示)送出的冷氣體將容易含有水,此時該冷出風口22就必 • 須另安裝一氣體除水器10’ ;該熱出風口23送出的熱氣體將容 易含有油’此時該熱出風口 2 3就必須另安裝一油氣分離器(圖 式中並未予以繪出)。 為了處理兩溫度的壓縮氣體,該氣體除水器10 (請爹閱弟 4圖所示)於導入口 121連接的管路上安裝一儲氣桶40,將壓縮 氣體導入該儲氣桶40,讓壓縮氣體由小空間導入大空間,造 成壓縮氣體流速變慢達到降溫的效果,且該儲氣桶40亦提供 9 M351333 壓縮孔疋壓降’另可於該館氣桶4〇(請參閱第所示)金 該氣體除水㈣的管路上安裝—風扇5q,讓該風扇帅對管 路吹風進行散熱,經由上述得知❹者可以視壓縮氣體的流 罝及溫度’選擇性使㈣儲氣⑽及風㈣(請相第5圖所 不),更—有些空壓機A於内部,已經針對壓縮氣體提供降溫的 設計,前述賴氣躺或該風_也就不需要安裝·。 綜上所述,本創作係一— '、種I々媒乾燥冷(:東系統,包含: /h ”有提仏乱水分離之氣水分離室的氣體除水器,至 有-^供冷熱分離之冷熱分離室的冷熱分離器,該冷 J刀“另提供管路連結進行冷熱氣體混合。 除此之外本一具有產業之可利用性』應已毋庸置疑, : ^ *貫施例所揭露出的特徵技術,於申請之前 功效增進之事實,更且有^^使用’不但具有如上所述 作的『新穎性』以及、牛Ρ忽的附加功效,是故,本創 提出新型專利之巾請,Si已符合專利法規,麦依法 德便。 〜、予審查並早曰賜准專利,實感 10 M351333 【圖式簡單說明】 第1圖係習用之系統示意圖。 第2圖係本創作安裝一個氣體除水器之組合示意圖。 第3圖係本創作安裝二個氣體除水器之組合示意圖。 第4圖係本創作安裝二個氣體水器、一個散熱風扇及一個 儲氣桶之組合示意圖。 第5圖係本創作安裝二個氣體水器及一散熱風扇之組合示M351333 VIII. New description: [New technical field] Non-refrigerant drying This creation is about - cold; East system, especially cold-cold system. [Prior Art] In response to the demand for compressed gas in the industry (for example, the processing machine refuses to operate, the untreated compressed gas is not only high in fishing but also warm in temperature; in order to solve the aforementioned problems, Further developed a cold image drying system =, the cold; East Chamber drying system 9Q (see Figure 1) includes - a gas phase two-two pipe 92, a cold material dryer 93, - The oil mist filter is called 4 to filter state 95 and a deodorizing filter%; but the above-mentioned conventional structure further analysis has the following problems: The dry line of the t material must pass through (4) the cold material (4) into the decay " The frozen dryer 93 witnessed the use of: =, oil and gas condensation to eliminate 'but this refrigerant is broken two places: Table: oxygen _ bad will cause a lot of ultraviolet ray 肆 惮 惮. For the creatures living on the surface of the earth, they are directly reported to the birds. It is not only physiological or psychological that they will suffer from double injuries. The gas must be installed in a number of "long-shrinking gas and all-dimensional consumables" for the aforementioned consumables. The installation cost, ', U cost, will only increase the user The burden of ;M351333 Therefore, how to solve the above problems is precisely the problem that needs to be improved at present. - In view of this, the creator of this case has been carefully studied and designed with many years of experience, and has been explored and tried by many parties. The sample test, and many corrections and improvements, finally developed a refrigerant-free drying cold; East system. • [New content] This creation is a refrigerant-free drying and freezing system, the purpose of which is to compress the gas through a gas-water separator. Gas-water separation, and cold-hot separator for cold-hot separation of compression-gas, and mixing cold gas and hot gas supply. To achieve the above purpose, the present invention comprises at least one gas eliminator and at least one hot and cold separator, wherein: The gas eliminator has an inlet port and an outlet port, and is provided with an accommodating space therein, wherein the inlet port is for introducing compressed gas, and a gas-water separation chamber is disposed in the accommodating space, and the gas-water separation chamber is at least separated The second flow guiding space allows the flow guiding spaces to communicate with each other, and the inlet and the outlet are respectively connected with the gas-water separation chamber for gas-water separation; The hot and cold separator is provided with a cold and hot separation chamber, and has an inlet, a cold air outlet and a hot air outlet. The three are respectively connected to the cold and heat separation chamber, and the inlet is connected with the outlet of the gas water separator. The hot and cold separation is performed; the hot air outlet and the cold air outlet of the cold and hot separator are connected by a pipeline for gas mixing. 6 M351333 The following effects can be obtained by further analysis as described above: 1. The refrigerant-free drying system does not require a refrigerant medium. The gas can be separated from the compressed gas and separated from the hot and cold, which is not only environmentally friendly, but also reduces the damage of the earth environment and organisms. 2. The refrigerant-free drying system can filter the compressed gas without installing a plurality of filters. The cost burden of consumable replacement is reduced, and the relative maintenance cost is also reduced. [Embodiment] The techniques, means, and other functions used in the present invention are described in detail with reference to the accompanying drawings. I believe that the above purpose, characteristics and other advantages of this creation can be understood in detail by the in-depth; The medium drying and freezing system comprises a plurality of gas water eliminators 10 and a hot and cold water separator 20; the gas eliminator 1 〇 (see FIG. 2) has a cylinder 11 and a cover 12, the cylinder 11 and the The cover 12 - the side has a combination portion 111 , 121 , the combination portion 111 , 121 is oppositely provided with a threaded segment, and the threaded portion of the combination portion 111 of the sleeve 11 is screw-locked with respect to the threaded portion of the combination portion 121 of the cover 12 , The cover 12 further has an introduction port 121 and an outlet port 122. The tube 11 is combined with the cover 12 to form an accommodating space 13; the tube 11 and the cover 12 are integrally formed, and the tube 11 and the cover 12 are Instead of designing the combination parts 1 and 121, an accommodating space M351333 is formed in the interior. A gas-water separation chamber 14 is provided in the accommodating space 13, and the gas-water separation chamber 14 has at least one piece-shaped partition member 141. The water separation chamber 14 forms at least two flow guiding spaces 142 through the partitioning member 141. The partitioning member 141 is provided with an air hole 143, and the air guiding holes 142 are connected to each other. The air holes 143 of the partitioning member 141 are disposed at a position necessary to be staggered. This causes the compressed gas to move forward in the flow guiding space 142 to generate a collision. Thereby, the water vapor and the adhesion amount of the oil and gas are increased, and the inlet 121 and the outlet 122 of the lid 12 are respectively connected to the two ends of the gas-water separation chamber 14 to allow compressed gas (the compressed air is supplied by the air compressor A). The introduction is carried out from the introduction port 121 of the lid 12, and then passes through the pores 143 of the separators 141 of the gas-water separation chamber 14, and finally is led out from the outlet 122 of the lid 12-. The hot and cold separator 20 is provided with a cold and hot separation chamber 201, and has an inlet 21, a cold air outlet 22 and a hot air outlet 23, and the three are respectively connected to the cold and heat separation chamber 201, and the cold air outlet 22 is connected. And the hot air outlet 23 is respectively disposed at two ends of the cold and hot separation chamber 201, the inlet 21 is disposed at one side of the cold and hot separation chamber 201, and the inlet 21 is connected to the outlet 122 of the gas eliminator 10; The hot and cold separation chamber 201 is introduced through the inlet 21 of the cold-hot separator 20, and the gas is ejected along the inlet 21 toward the cold-hot separation chamber 201, and is rotated at a high speed in the cold-hot separation chamber 201 to generate centrifugal force by rotation, and Through the action of the centrifugal force, the pressure and density of the gas close to the outer wall of the cold-hot separation chamber 201 will rise, and the pressure and the density of the gas away from the inner wall of the cold-hot separation chamber 201 will decrease, and the high-pressure and high-density gas will be directed toward the low pressure. The low-density gas flow 8 M351333 - moves, the hot gas is led out through the hot air outlet 23 due to the pressure change in the cold-hot separation chamber 201, and the cold gas is led out through the cold air outlet 22, and the The hot air outlet 23 and the cold air outlet 22 of the hot and cold separator 20 are finally connected by a pipe to be mixed. In order to adjust the gas flow rate of the hot air outlet 23 and the cold air outlet 22 of the cold and hot separator 20 (refer to FIG. 2), the piping installed in the hot air outlet 23 and the # cold air outlet 22 may be made as needed. The flow of the different diameters is limited, for example, the diameter of the hot air outlet 23 of the cold and hot separator 20 is greater than, about less than or equal to the diameter of the cold-air outlet 22; the hot air outlet 23 and the cold air outlet 22 may be optionally required. The safety control valve 30 is used to limit the flow of the valve opening. In order to handle a large flow of compressed gas, the cold gas sent out by the cold air outlet 22 (see Fig. 3) will easily contain water, and the cold air outlet 22 must be additionally equipped with a gas eliminator 10. The hot gas sent from the hot air outlet 23 will easily contain oil. At this time, the hot air outlet 23 must be additionally equipped with an oil separator (not shown in the drawings). In order to process the compressed gas at two temperatures, the gas eliminator 10 (shown in FIG. 4) is provided with a gas storage tank 40 on the pipeline connected to the inlet 121, and the compressed gas is introduced into the gas storage tank 40. The compressed gas is introduced into the large space from a small space, causing the flow rate of the compressed gas to slow down to achieve the effect of cooling, and the gas storage tank 40 also provides a pressure drop of 9 M351333, which is also available in the gas cylinder of the museum (see the first section). Show) gold gas is installed in the pipeline of water (4) - fan 5q, let the fan cool the pipe to dissipate heat, through the above, the latter can see the flow and temperature of the compressed gas 'selectively (4) gas storage (10) Wind (4) (please do not correspond to Figure 5), more - some air compressor A is inside, has been designed to provide cooling for the compressed gas, the above lying or the wind _ does not need to be installed. In summary, the creation department is a gas dewatering device for the gas-water separation chamber of the water-separating chamber of the water-separating chamber of the water-cooling system. The cold and hot separator of the cold and hot separation cold and hot separation chamber, the cold J knife "provides another pipeline connection for mixing hot and cold gas. In addition, the industry has the availability of the industry" should be undoubtedly: ^ * The feature technology revealed, the fact that the effect is improved before the application, and the use of '^ not only has the "novelty" as described above, and the additional effect of the ox, the original patent Please contact, Si has complied with the patent regulations, McDonald's will. ~, review and early grant of patents, real sense 10 M351333 [Simple diagram of the diagram] Figure 1 is a schematic diagram of the system used. Figure 2 is the creation of this A schematic diagram of the installation of a gas eliminator is provided. Figure 3 is a schematic diagram of the combination of two gas eliminators installed in this creation. Figure 4 is a combination of two gas water heaters, one cooling fan and one gas storage tank. Schematic diagram. Figure 5 is the original The mounting assembly two gas water heater, and a heat-dissipating fan shown

意圖。 【主要元件符號說明】 《習用》 冷凍式乾燥系統90 儲氣桶91 管路過濾器92 • 冷凍式乾燥機93 油霧過遽器94 精密過濾器95 除臭過濾器96 〔本創作〕 氣體除水器10 筒11 組合部111 蓋12 組合部121 M351333 ^ 導入口 122 容置空間13 氣水分離室14 - 導流空間142 - 冷熱分離器20 冷熱分離室201 冷出風口 22 • 控制閥30intention. [Main component symbol description] "Utility" Freeze drying system 90 Gas storage tank 91 Pipeline filter 92 • Refrigerated dryer 93 Oil mist filter 94 Precision filter 95 Deodorizing filter 96 [This creation] Gas removal Water tank 10 Cartridge 11 Combination part 111 Cover 12 Combination part 121 M351333 ^ Guide inlet 122 accommodating space 13 Gas-water separation chamber 14 - Diversion space 142 - Cooling and cooling separator 20 Cooling and cooling separation chamber 201 Cold air outlet 22 • Control valve 30

儲氣桶40 風扇5 0 空壓機A 導出口 123 分隔件141 氣孔143 入口 21 熱出風口 23 12Gas storage tank 40 Fan 5 0 Air compressor A Outlet 123 Separator 141 Air hole 143 Entrance 21 Hot air outlet 23 12

Claims (1)

M351333 九、申請專利範圍: 1. 一種無冷媒乾燥冷涞系統,包含: 至少一氣體除水器,係具有一導入口及一導出口,且於 -内設有一容置空間,該導入口係供壓縮氣體導入,該容置空 '間中設置一氣水分離室,該氣水分離室具有至少一分隔件, 該氣水分離室透過該分隔件形成至少二導流空間,該分隔件 設有一氣孔,讓導流空間相互連通,該導入口與導出口分別 籲與該氣水分離室連接進行氣水分離;以及 至少一冷熱分離器,於内設有一冷熱分離室,且具有一 入口、一冷出風口及一熱出風口,前述三者分別與該冷熱分 離室相連通,該入口與該氣體除水器的導出口連接進行冷熱 分離;該冷熱分離器的熱出風口及冷出風口作管路連結進行 氣體混合。 2.如申請專利範圍第1項所述之無冷媒乾燥冷凍系統,其 中該冷熱分離器的熱出風口或冷出風口另設有一控制閥進行 限流。 3. 如申請專利範圍第1項所述之無冷媒乾燥冷凍系統,其 中該冷熱分離器之冷出風口的管路上另設有一氣體除水器。 4. 如申請專利範圍第1項所述之無冷媒乾燥冷凍系統,其 13 M351333 3 %?凡丨3 : i ' : / , 1 中該冷熱分離器之熱出風口的管路1°另~~設畜=商貪分離器。 5. 如申請專利範圍第1項所述之無冷媒乾燥冷凍系統,其 -中該氣體除水器之導入口的官路上另設有一儲氣桶。 6. 如申請專利範圍第1項所述之無冷媒乾燥冷凍系統,其 中該氣體除水器之導入口的管路另設有一風扇。 7. 如申請專利範圍第1項所述之無冷媒乾燥冷凍系統,其 中該氣體除水器之導入口的管路另設有一儲氣桶及一風扇。 8. —種無冷媒乾燥冷凍系統,包含: 至少二氣體除水器,係具有一導入口及一導出口,且於 内設有一容置空間,該導入口係供壓縮氣體導入,該容置空 籲間中設置一氣水分離室,該氣水分離室具有至少一分隔件, 該氣水分離室透過該分隔件形成至少二導流空間’該分隔件 設有一氣孔,讓導流空間相互連通,該導入口與導出口分別 與該氣水分離室連接進行氣水分離;以及 至少一冷熱分離器,於内設有一冷熱分離室,且具有一 入口、一冷出風口及一熱出風口,前述三者分別與該冷熱分 離室相連通,該入口與該氣體除水器的導出口連接進行冷熱 分離;該冷熱分離器的熱出風口及冷出風口作管路連結進行 14 M351333 氣體混合,該冷熱分離器之冷I,咸 除水器進行氣水分離。 口韵管路上另設有 氣 9.如申請專利範圍第δ項 中該冷熱分離㈣熱“ 口以㈣、統,其 限流。 7出風口另权有一控制閥進行 其::::::::8項所述之無冷媒乾燥冷㈣ 統 器 風口的管路上另設有一油氣分離 .如U利feu第8項所述之無冷媒乾燥冷;東系統 其中該氣體除水器之導入口的管路上另設有一儲氣桶。 复申請專利範圍第8項所述之無冷媒乾燥冷凍系統 其中该氣體除水器之導人口的管路上料有一風扇。 3.如申请專利範圍第8項所述之無冷媒乾燥冷殊系統, 其中该氣體除水器之導入口的管路上另設有一儲氣桶及一風 扇。 15M351333 IX. Patent application scope: 1. A non-refrigerant drying and cooling system, comprising: at least one gas water eliminator having an inlet port and an outlet port, and having an accommodating space therein, the inlet port a gas-water separation chamber is disposed between the accommodating chambers, and the gas-water separation chamber has at least one partition member, and the gas-water separation chamber forms at least two flow guiding spaces through the partitioning member, and the partitioning member is provided with a The air vents allow the flow guiding spaces to communicate with each other, and the inlet and the outlet are respectively connected to the gas-water separation chamber for gas-water separation; and at least one of the cold and hot separators is provided with a cold and heat separation chamber, and has an inlet and a a cold air outlet and a hot air outlet, wherein the three are respectively connected to the cold and hot separation chamber, and the inlet is connected to the air outlet of the gas water separator for hot and cold separation; the hot air outlet and the cold air outlet of the cold and hot separator are used for The pipeline is connected for gas mixing. 2. The non-refrigerant drying and freezing system according to claim 1, wherein the hot air outlet or the cold air outlet of the cold and hot separator is further provided with a control valve for current limiting. 3. The non-refrigerant drying and freezing system according to claim 1, wherein a gas eliminator is further disposed on the pipeline of the cold air outlet of the cold and hot separator. 4. For the non-refrigerant drying and freezing system described in the first paragraph of the patent application, 13 M351333 3 %? where 丨3 : i ' : / , 1 is the hot air outlet of the hot and cold separator 1 ° another ~ ~ Set the livestock = commercial greed separator. 5. The non-refrigerant drying and freezing system according to claim 1, wherein a gas storage tank is further disposed on the official road of the inlet of the gas eliminator. 6. The non-refrigerant drying and freezing system according to claim 1, wherein the gas inlet of the gas eliminator is further provided with a fan. 7. The non-refrigerant drying and freezing system according to claim 1, wherein the gas inlet of the gas eliminator is further provided with a gas storage tank and a fan. 8. A refrigerant-free drying and freezing system, comprising: at least two gas eliminators having an inlet port and an outlet port, and an accommodating space therein for introducing a compressed gas, the accommodating A gas-water separation chamber is disposed in the air-filling chamber, the gas-water separation chamber has at least one partitioning member, and the gas-water separating chamber forms at least two flow guiding spaces through the partitioning member. The partitioning member is provided with an air hole to allow the guiding space to communicate with each other. The inlet port and the outlet port are respectively connected to the gas-water separation chamber for gas-water separation; and at least one cold-hot separator has a cold-hot separation chamber therein, and has an inlet, a cold air outlet and a hot air outlet. The three are respectively connected to the cold and hot separation chamber, and the inlet is connected to the outlet of the gas eliminator for hot and cold separation; the hot air outlet of the cold and hot separator and the cold air outlet are connected by a pipeline to carry out 14 M351333 gas mixing. The cold and hot separator of the cold and hot separator, the salt water separator performs gas-water separation. There is another gas on the rhythm pipeline. 9. In the δ item of the patent application scope, the hot and cold separation (4) heat “port” (4), system, and its current limit. 7 outlet outlet has another control valve to carry out its :::::: The refrigerant-free drying of the air conditioner is as follows: There is another gas storage tank on the pipeline. The refrigerant-free drying and freezing system described in claim 8 of the patent application has a fan in the pipeline of the gas-removing device. 3. If the patent application scope is the eighth item The refrigerant-free drying system has a gas storage tank and a fan on the pipeline of the gas inlet of the gas eliminator.
TW97202444U 2008-02-04 2008-02-04 Coolant free drying refrigeration system TWM351333U (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW97202444U TWM351333U (en) 2008-02-04 2008-02-04 Coolant free drying refrigeration system

Publications (1)

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TWM351333U true TWM351333U (en) 2009-02-21

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