TW397903B - The freezing-type low-dew-point drying control method for compressed air - Google Patents
The freezing-type low-dew-point drying control method for compressed air Download PDFInfo
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- TW397903B TW397903B TW87114514A TW87114514A TW397903B TW 397903 B TW397903 B TW 397903B TW 87114514 A TW87114514 A TW 87114514A TW 87114514 A TW87114514 A TW 87114514A TW 397903 B TW397903 B TW 397903B
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五 、發明説明(1 A7 B7 經濟部中央標準局員工消費合作社印製 本,明,有關於一種將壓縮空氣中之水份凝結排出之 控制方法,尤指一種低壓冷媒蒸發溫度可低於〇艺以下, 藉巧溫麟含之水紐制完全之凝結排出, 同時亦不會導致壓縮空氣管路產生結冰阻塞之『凍式壓 縮空氣低露點乾燥控制方法』。 壓縮空^之應用非常廣泛,舉凡各式氣動工具、氣壓 缸、氣動馬達…等等,然而壓縮空氣中所含之水蒸氣卻會 造成各種應用元件或設備之銹蝕,而影響其使用4命及運 轉精度,因此在工廠内必需加裝一空氣乾燥機,排除壓縮 空氣内之水份,得到乾燥度品質較佳之壓縮空氣。 請今閱圖一、二、三所示係為習用冷凍式空氣乾燥機 之結構示意掘及冷媒、壓縮空氣之流程圖,其中 一、 壓縮空氣之流程係輸入蒸發器15内,藉由低溫液態冷 媒吸收壓縮空氣之熱量,並將水蒸氣凝結成水而排出 〇 二、 冷媒流程 (1) 冷媒壓縮機 冷媒經由冷媒壓縮機11之壓縮形成高壓之氣態冷 媒。 (2) 冷凝器 冷媒輸入冷凝器12内散熱,並形成高壓常溫液態 冷媒》 (3) 過濾器 高壓常溫液態冷媒藉由過濾器13濾除雜質。 本·紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83.3.10,000 (请先閱讀背面之注意事項存填寫本頁)V. Description of the invention (1 A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs, which states that there is a control method for condensing and discharging water in compressed air, especially a low-pressure refrigerant whose evaporation temperature can be lower than 0 ° C. In the following, the "frozen compressed air low dew point drying control method" will be completely condensed and discharged by using the water and button system of Wen Lin, which will not cause ice blockage in the compressed air pipeline. The application of compressed air ^ is very wide, For example, all kinds of pneumatic tools, pneumatic cylinders, air motors, etc., but the water vapor contained in the compressed air will cause corrosion of various application components or equipment, affecting its life and operating accuracy, so it is necessary in the factory Install an air dryer to remove the moisture in the compressed air to obtain compressed air with better dryness. Please refer to Figures 1, 2, and 3 shown here for the structure of a conventional refrigerated air dryer. Flow chart of compressed air, one of which is that the flow of compressed air is input into the evaporator 15, and the heat of the compressed air is absorbed by the low-temperature liquid refrigerant. The water vapor is condensed into water and discharged. 2. Refrigerant flow (1) Refrigerant compressor The refrigerant is compressed by the refrigerant compressor 11 to form a high-pressure gaseous refrigerant. (2) Condenser The refrigerant is input into the condenser 12 to dissipate heat and form a high pressure. Liquid refrigerant at normal temperature》 (3) Filter High-pressure liquid refrigerant at normal temperature removes impurities through filter 13. This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 83.3.10,000 (Please read the notes on the back first (Please fill in this page)
五 、發明説明(2 A7 B7 經濟部中央標準局員工消費合作社印製 (4) 毛細管 1 高壓常溫液態冷媒經由毛細管14膨脹蒸發,產生 製冷作用。 (5) 蒸發器 低溫冷媒輸入蒸發器15内,吸收流經蒸發器15内 壓縮空氣之熱量,並使壓縮空氣之水蒸氣因低溫 而凝結成水並排出,該冷媒吸收壓縮空氣之熱量 後而形成飽和之氣態冷媒。 (6) 回流至冷媒塵縮機 吸枚壓縮空氣熱量後成為徵和之氣能冷媒回輸入 冷媒壓縮機11内,再度循環作動。 前述冷媒壓縮機11之高、低壓侧設一熱氣旁路閥16主 要係控制低壓侧之冷媒蒸發溫度保持約攝氏2 °c,以避免 。蒸發器15嚴重結冰阻塞壓縮空氣之通路,此乃因為水於〇.4 °C時即會有薄冰之逐漸形成,然而因為無法有效將形成之 冰層清除,不但無法長時間穩定運轉,終將導致冷媒及空 氣管路之阻塞,冷媒及壓縮空氣無法通^而產生極大的壓 卞’且蒸發器15内之冷媒無法吸收壓縮空氣之熱量,其液 態冷媒不完全蒸發而回流至冷媒壓縮機U,導致液壓縮而 損毀之缺點〇 此外,該熱氣旁路閥16係擔任穩定冷媒蒸發溫度之工 作’其係將南壓側之高壓高溫氣態冷媒直接旁路至低麼侧, 以避免冷媒之蒸發溫度過低,但卻造成冷媒壓縮機丨丨作虚 功,因而降限冷媒壓縮機11之冷凍能力,形成能源之粍費。 (請先閱讀背面之注意事項#填寫本頁)V. Description of the invention (2 A7 B7 Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (4) Capillary 1 The high-pressure and normal-temperature liquid refrigerant expands and evaporates through the capillary 14 to produce a cooling effect. (5) The evaporator low-temperature refrigerant is input into the evaporator 15, It absorbs the heat of the compressed air flowing through the evaporator 15 and causes the water vapor of the compressed air to condense into water due to low temperature and discharge. The refrigerant absorbs the heat of the compressed air to form a saturated gaseous refrigerant. (6) Return to the refrigerant dust The compressed air absorbs the heat of the compressed air and becomes the energy gas of the reconciliation. The refrigerant is returned to the refrigerant compressor 11 and circulates again. The hot gas bypass valve 16 on the high and low pressure side of the refrigerant compressor 11 is mainly used to control the low pressure side. Refrigerant evaporation temperature is maintained at about 2 ° C to avoid. Severe freezing of evaporator 15 blocks the path of compressed air. This is because water will gradually form thin ice at 0.4 ° C. The formed ice layer will not only be able to run stably for a long time, but will eventually lead to the blockage of the refrigerant and the air pipeline. Pressure and the refrigerant in the evaporator 15 cannot absorb the heat of the compressed air, its liquid refrigerant does not completely evaporate and returns to the refrigerant compressor U, resulting in the disadvantage of liquid compression and damage. In addition, the hot gas bypass valve 16 serves as stability The work of refrigerant evaporation temperature 'is to directly bypass the high pressure and high temperature gaseous refrigerant on the south pressure side to the low side to avoid the refrigerant evaporation temperature being too low, but it will cause the refrigerant compressor to perform virtual work and reduce the refrigerant limit. The refrigerating capacity of compressor 11 forms the cost of energy. (Please read the note on the back first # Fill this page)
泰紙張適用中國國家標準(CNS)八猶^ (210><297公羞) 83.3.10,000Thai paper conforms to Chinese National Standard (CNS) Ba Ju ^ (210 > < 297 public shame) 83.3.10,000
五、發明説明含) 經濟部中央標準局員工消費合作社印製 因此由上述說可知其就實際使用而言實非一灰好之運 作模式及方法,無法得到良好的乾燥效果,且無形中浪費 尚多之能源。 請參閱圖四’係另一種空氣乾燥設備之流程示意圖, 如圖所示其係將化學吸濕藥劑分別置於兩吸著桶耵、^内, 於空氣入口處設一四位閥61’其閥口分別連接兩吸著桶τι、 T2之入口與排氣口,配合連接於兩吸著桶出口之逆止闊1、 2動作,且於逆止閥兩侧各設一較小管徑之旁路管62、63, 如此可使兩吸著桶T1、T2交替工作及將吸濕藥劑還原(當 吸著桶Τ1進行乾燥工作時,吸著桶Τ2之吸濕藥劑則為還原 之狀態,其乾燥後之大氣露點可達一 4 (TC,圖一方式約 為一 2 3°C,然此一乾燥效果雖較圖一方式良好,但其還 原側之吸著桶T2將消耗15%之壓縮空氣,以利其吸濕藥劑 達成還原目的,且乾燥侧内之吸濕藥劑因吸收水蒸氣逐漸 飽=,故其空氣乾燥效果隨之變化,且其兩吸著桶耵、T2 之交替工作為固定時間週期,並無法提供使用者實際使用 風,大小做調整,因而其處理後之乾燥品質變化較大,又 空子壓縮機於建立壓縮空氣之同時,亦產生油霧,隨壓縮 空氣流出,因而在入口處需加裝過濾器,將油霧濾除,以 免油霧進入後附著於吸濕藥劑表面,影響乾燥效果與使用 责命’且就實際使用而言,其所購置費用高,且化學吸濕 藥劑仍有一使用時間壽命,必需將兩吸著桶用之吸濕藥劑 完全換新,故不但造成使用者不便,且成本提高更有癀棄 化學吸濕藥劑污染環境之慮,故亦非良好之創作。 个卿从卿渊W ( CNS ) Μ呢21〇χ297公石 83. 3.10,000 (請先閲讀背面之注意事項再填寫本頁}V. Description of the invention Including) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. From the above, it can be seen that it is not a good operation mode and method in terms of practical use. It cannot obtain good drying effects, and it is virtually wasteful. More energy. Please refer to Figure 4 'for a schematic flow chart of another type of air drying equipment. As shown in the figure, the chemical hygroscopic agent is placed in two adsorption buckets 耵 and ^, and a four-position valve 61' is provided at the air inlet. The valve ports are respectively connected to the inlets and exhaust ports of the two suction buckets τι, T2, and cooperate with the check valves 1 and 2 connected to the outlets of the two suction buckets, and a small pipe diameter is provided on each side of the check valve. Bypass pipes 62 and 63, so that the two suction buckets T1 and T2 can work alternately and reduce the hygroscopic agent (when the suction bucket T1 performs drying work, the hygroscopic agent in the suction bucket T2 is in a reduced state. After drying, the atmospheric dew point can reach 4 (TC, the method in Figure 1 is about 23 ° C, although the drying effect is better than that in Figure 1, but the absorption bucket T2 on the reducing side will consume 15% of the Compress the air in order to achieve the reduction purpose of its hygroscopic agent, and the hygroscopic agent in the dry side is gradually saturated due to absorption of water vapor, so its air drying effect changes accordingly, and its two suction buckets, T2 work alternately It is a fixed time period and cannot provide users with the actual wind. The size is adjusted because After treatment, the drying quality changes greatly. At the same time that the air compressor creates compressed air, it also generates oil mist, which flows out with the compressed air. Therefore, a filter must be installed at the inlet to filter out the oil mist to avoid oil mist. After entering, it adheres to the surface of the hygroscopic agent, which affects the drying effect and the use of the command. In terms of actual use, the purchase cost is high, and the chemical hygroscopic agent still has a life span. It is necessary to absorb the two suction buckets. Wet medicine is completely renewed, so it not only causes inconvenience to the user, but also raises the cost and abandons the concern that the chemical hygroscopic agent pollutes the environment, so it is not a good creation. Ge Qingcong Qingyuan W (CNS) M? 21〇χ297 Gongshi 83. 3.10,000 (Please read the notes on the back before filling this page}
五、發明説明(4 五、發明説明(4V. Description of the invention (4 V. Description of the invention (4
媒' 4 &考量故必需設法穩定其冷卻溫度於2。〇左右 9羽,_齡之空氣乾燥導 ’設容ίίί式=絲方絲避免冷卻溫想下,需加 q控制,故間接形成能源之耗費。 好之乾燥效果,但其還原則需消 4 縮空氣風4,極不符轉效益。 衰Si=質§g效果隨化,及濕藥劑逐雜和而 式麵機,其崎之化學賴細,雖亦有還原之 但仍隨使用時間逐漸降低效果,故需將其吸滿藥 ifΐ二不但造成保養不便,成本提高,更易造成廢棄 之吸濕藥劑污染環境。 本案發明人有鑑於上述壓縮空氣乾燥方持之缺失,乃 依其多年從事冷凍式空氣乾燥機製作之經驗,予以潛心研 究,經不斷試作與改進,終於研究出本發明,本種「冷凍 式壓縮空氣低露點乾燥控制方法」,而為讓鈞局貴審查委 員及熟於此項技藝之人士,能完全明瞭本發明之功效、步 驟’兹配合圖示及圖號說明於后: 圖式簡單說明 經濟部中央標準局J工消費合作社印製 ---------------if (請先閲讀背面之注意事項再填寫本頁)The media '4 & needs to be managed to stabilize its cooling temperature at 2. 〇 About 9 birds, _ age of air drying guide ‘Set capacity ίί = silk square wire to avoid cooling temperature, you need to add q control, so indirect energy consumption. Good drying effect, but its principle also needs to eliminate air contraction, which is not consistent with the benefits. The effect of decaying Si = quality §g varies, and the wet medicament mixes and blends the dough machine. Its chemical chemistry is detailed, although there is a reduction, but the effect gradually decreases with use time, so it needs to be filled with medicine if 药Second, it will not only cause inconvenience to maintenance, increase the cost, but also easily cause waste hygroscopic agents to pollute the environment. In view of the above-mentioned shortcomings in compressed air drying, the inventor of this case has made intensive research based on his many years of experience in the production of refrigerated air dryers. After continuous trial and improvement, he finally developed the present invention, this "frozen compressed air "Low dew point drying control method", and in order to allow Jun Jugui's review members and those who are familiar with this technology to fully understand the efficacy, steps of the present invention, the illustrations and figure numbers are described later: Printed by the Ministry of Central Standards Bureau J Industry Consumer Cooperatives ---- if (Please read the precautions on the back before filling this page)
1T 圖一係習知冷凍式空氣乾燥機流程示意圖 圖二係圖一習知冷凍式空氣乾燥機之冷媒流程圖 圖三係圖一習知冷凍式空氣乾燥機之壓縮空氣流程圖 0 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83. 3.10,000 五 、發明説明(5 A7 B7 程示意圖 圖六係機之配置圖 圖七係本發明冷媒流程圖 圖八〜十係本發明之流程示意圖 圖號簡單說明: 16熱氣旁路閥 A、B、15蒸發器 21空氣前置冷卻器 33、12冷凝器 22、23自動排水器 24熱交換器 41、411、42、43、44空氣管路 31、 11冷媒壓縮機32、 34、241、242冷媒管路 36、B卜38、38卜39冷媒管路 35、13過濾器 37、14毛細管 51三位閥 52電磁閥 53、61四位閥 62、63旁路管 I、Π壓力感測器 m溫度感測器 p微處理器 H、T2吸著桶 係本發明之冷凍式空氣乾 經濟部中央標準局員工消費合作社印裝 請參閱圖五、六、七所示 配Η ’其主要係於壓縮空氣之管路财二只蒸發 fi丄並藉由三位闕51控制®縮空氣之流向,於冷媒系 交換器24,可提供出σ壓縮空氣之溫升及冷媒散 ,所需外,其熱交換器24之前段更可供給高壓液態冷媒更 多之過冷溫度,並藉由四位閥控制兩只蒸發器A、Β輪流製 冷之動作,並由電磁閥52之控制,得導入高溫冷媒於結冰 之蒸發器Α内,使其迅速融解並排出;另設有—只'一’度感 8- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83.3.10,000 (請先閲讀背面之注意事項再填寫本頁)1T Figure 1 is a flow chart of a conventional refrigerated air dryer. Figure 2 is a flow chart of a refrigerant of a conventional refrigerated air dryer. Figure 3 is a flow chart of a compressed air of a conventional refrigerated air dryer. Applicable to China National Standard (CNS) A4 specification (210X297 mm) 83. 3.10,000 V. Description of the invention (5 A7 B7 schematic diagram Figure 6 series machine configuration diagram Figure 7 is the refrigerant flow chart of the present invention Figure 8 ~ 10 series The process flow diagram of the invention is as follows: The hot air bypass valve A, B, 15 evaporator 21 air pre-cooler 33, 12 condenser 22, 23 automatic drain 24 heat exchanger 41, 411, 42, 43, 44 Air line 31, 11 Refrigerant compressor 32, 34, 241, 242 Refrigerant line 36, B 38, 38 39 39 Refrigerant line 35, 13 Filter 37, 14 Capillary 51 Three-position valve 52 Solenoid valve 53, 61 Four-position valve 62, 63 Bypass pipe I, Π Pressure sensor m Temperature sensor p Microprocessor H, T2 Suction barrel is printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Refrigerated Air Dry Economy of the present invention Please refer to the distribution shown in Figures 5, 6, and 7. The air-condensing pipelines only have two evaporating fi 丄 s and are controlled by the three-position 阙 51. The air-condensing flow direction can provide the σ compressed air temperature rise and refrigerant dispersion in the refrigerant-based exchanger 24. The front section of the heat exchanger 24 can supply more high-temperature liquid refrigerant with more subcooling temperature, and the two evaporators A and B are controlled by the four-position valve to take turns to cool, and is controlled by the solenoid valve 52 to introduce high-temperature refrigerant. In the icing evaporator A, it melts and discharges quickly; there is also-only 'a' sense of degree 8- This paper size applies to China National Standard (CNS) A4 specification (210X297 mm) 83.3.10,000 (please (Read the notes on the back before filling out this page)
五、發明説明(6 ) A7 B7 經濟部中央標準局貞工消費合作社印製 測器]Π於冷媒低壓回流管路上,二只壓力感測器I、, Η於 壓縮空氣之入、出口’各感應器I、it、m所偵測得之溫 度或壓力變化而改變三位閥51、四位閥53及電磁闕52之控 制時序’改變壓縮空氣及冷媒之流動方向,俾能達到低溫 乾燥壓縮空氣之功效,提昇壓縮空氣之品質。茲就其二蒸 發器A結冰前、後之冷媒流程及壓縮空氣流程之步雜說明 於后··(請搭配圖五、圖七所示) (一)蒸發器A結冰前之冷媒流程,請參閱圖七所示: (1) 冷媒壓縮機之壓縮: 首先冷媒壓縮機31内壓縮而成為高壓高溫之氣態 冷媒。 (2) 熱交換器内與空氣熱交換: 高溫高壓之氣態冷媒經冷媒管路32輸入熱交換器 24後端之冷媒管路241,令壓縮空氣與高壓^溫 之氣態冷媒進行熱交換,使壓縮空氣成為常溫之 乾燥空氣排出。 (3) 冷凝器散熱: 高溫高壓之氣態冷媒經由冷凝器33散熱,成為高 壓常溫之液態冷媒。 (4) 過濾器過濾雜質: 高壓常溫之液態冷媒經冷媒管路34輸入過濾器35 内濾除雜質》 (5) 熱交換器内增加飽和液態之過冷溫度: 濾除雜質之高壓常溫冷媒輸入熱交換器24前端之 (請先閲讀背面之注意事項再填寫本頁) 尽紙Λ尺度適用中國國家標準(CNS ) A4規格(21 ox297公釐) 83· 3· 1〇,〇〇〇 B7 五、發明説明(7 ) 經濟部中央標準局員工消費合作社印製 冷媒管路242,令冷媒得以增加飽和液態之過冷 溫度。 (6) 四位閥之流向控制: 冷媒經四位閥53控制流入蒸發器B内。 (7) 毛細管之膨脹蒸發: 冷媒經蒸發器B導流入毛細管37内膨脹蒸發。 (8) 蒸發器A内吸熱 冷媒流入蒸發器A,内對流經蒸發器A内之壓縮空 氣降溫排熱,令空氣之水蒸氣凝結,同時冷媒吸 熱後成為飽和之氣態冷媒。 (9) 回流至冷媒壓縮機内循環使用: 飽和氣態冷媒經由冷媒管路38之西位闊53導流入 冷媒管路381,回入冷媒壓縮機31内再循環使用〇 (二)蒸發器A結冰前壓縮空氣之流程:(請搭配合圖五、 六所示) (1) 前置冷卻器降溫: 壓縮機首先流入空氣前置冷卻器21内冷卻降至常 溫。 (2) 蒸發器A内凝結水份: 常溫之壓縮空氣經空氣管路41之三位閥51控制而 導流入蒸發器A内,流經蒸發器A内之冷媒吸收壓 縮空氣之熱量,使得壓縮空氣内含水蒸氣於低溫 下凝結成水份,水份並由自動排水器22排出,使 得壓縮空氣冷卻並乾燥。 —本紙張適用中關家標準(CNS ) ( 210X297公釐)"~~ 83.3.10,000 (請先閲讀背面之注意事項再填寫本頁)V. Description of the invention (6) A7 B7 Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Zhengong Consumer Cooperative Co., Ltd.] On the refrigerant low-pressure return line, two pressure sensors I and I are placed on the inlet and outlet of the compressed air. The temperature or pressure changes detected by the sensors I, it, and m change the control sequence of the three-position valve 51, four-position valve 53, and the electromagnetic 阙 52 to change the flow direction of compressed air and refrigerant, which can achieve low-temperature dry compression The effectiveness of air improves the quality of compressed air. The steps of refrigerant flow before and after freezing of evaporator A and the compressed air flow are explained later (please show as shown in Figures 5 and 7) (1) Refrigerant flow before evaporator A is frozen Please refer to Figure VII: (1) Compressor of refrigerant compressor: First, the refrigerant compressor 31 compresses to become high-pressure high-temperature gaseous refrigerant. (2) Heat exchange with air in the heat exchanger: The high-temperature and high-pressure gaseous refrigerant is input into the refrigerant pipe 241 at the rear end of the heat exchanger 24 through the refrigerant pipe 32, so that the compressed air and the high-pressure gaseous refrigerant exchange heat, so that The compressed air is discharged as dry air at room temperature. (3) Condenser heat dissipation: The high-temperature and high-pressure gaseous refrigerant is radiated through the condenser 33 and becomes a high-pressure and normal-temperature liquid refrigerant. (4) Filters filter impurities: liquid refrigerant at high pressure and normal temperature is input to filter 35 through refrigerant pipe 34 to filter out impurities. (5) Increase the supercooled temperature of saturated liquid in heat exchanger: Input high pressure normal temperature refrigerant to remove impurities The front end of the heat exchanger 24 (please read the precautions on the back before filling this page) The paper Λ scale is applicable to the Chinese National Standard (CNS) A4 specification (21 ox297 mm) 83 · 3 · 1〇, 〇〇〇〇7 (7) Description of the invention (7) The central government bureau of the Ministry of Economic Affairs has printed the refrigerant medium pipe 242 in the Consumer Cooperatives, so that the refrigerant can increase the supercooled temperature of the saturated liquid. (6) Flow direction control of four-position valve: Refrigerant is controlled to flow into evaporator B through four-position valve 53. (7) Expansion and evaporation of the capillary tube: The refrigerant is introduced into the capillary tube 37 via the evaporator B to expand and evaporate. (8) Heat absorption in evaporator A The refrigerant flows into evaporator A, and the condensed air passing through evaporator A cools and exhausts heat, condenses water vapor in the air, and the refrigerant absorbs heat and becomes a saturated gaseous refrigerant. (9) Return to the refrigerant compressor for recycling: Saturated gaseous refrigerant is conducted into the refrigerant pipeline 381 through the west position 53 of the refrigerant pipeline 38 and returned to the refrigerant compressor 31 for recycling. (2) Evaporator A freezes The flow of the front compressed air: (please match as shown in Figures 5 and 6) (1) Cooling of the front cooler: The compressor first flows into the air precooler 21 to cool down to normal temperature. (2) Condensed water in evaporator A: Compressed air at normal temperature is controlled by three-position valve 51 of air pipe 41 and guided into evaporator A. The refrigerant flowing through evaporator A absorbs the heat of compressed air, making it compressed. The water vapor in the air is condensed into water at low temperature, and the water is discharged by the automatic drainer 22, so that the compressed air is cooled and dried. —This paper applies CNS (210X297mm) " ~~ 83.3.10,000 (Please read the precautions on the back before filling this page)
經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明g ) (3)熱父換器内提高為常溫之乾燥之空氣:> 壓縮空氣冷卻後而成乾燥之空氣,輸入熱交換器 it j壓常溫液態冷媒的熱量,因吸收“壓 尚=氣l冷媒之熱量後而成為常溫且乾燥高品質 之壓縮空氣,排出高品質常溫之乾燥壓縮空氣即 得以輸入各式氣動工具、機具…等内使用。 另’設於空氣入、出口之壓力感測器jπ及設低塵 冷媒管路381之溫度感測器瓜將其所測得之壓力及溫度數 值回授至微處理器Ρ内比較運算,當入口壓力與出口塵力 產生些許差時’即表示蒸發器Α内結聚冰層,微處理器ρ即 會令四位閥53作動’改變冷媒之流向,使蒸發器a不再製 冷,如圖八所示,由熱交換器24前端冷媒;^路242輸出之 冷媒經由四位閥53導流入蒸發器A内,再經毛細管37之膨 脹蒸發流入蒸發器B内製冷,冷媒再由四位閥53導丨兔入冷 媒壓縮機31循環使闬;此時由於蒸發器a内之冰層尚未融 化’仍保有適當之冷度’故壓縮空氣仍導流入蒸發器A内, 並不會影響壓縮空氣乾燥之品質,且因蒸發ί'Β之溫度尚 未降至所需之低溫,故溫度感測器ffl所測得之溫度較高, 待蒸發器B内之溫度下降至所需之工作溫度時,微處理器ρ 回授得到訊號後即作動三位闊51及電磁閥52,如圖九所示, 使壓縮空氣流向改變進入蒸發器B,同時高壓高溫氣態冷 媒經電磁閥52,並通過四位間53直接進入蒸發器 A,藉 此將所結之冰唐快速融解並藉由自動排水器22排出,又蒸 發器A内之冰層若完全融解時,因高壓冷媒亦無法再得到 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇><297公釐) (請先閱讀背面之注意事項再填寫本頁)Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention g) (3) Dry air raised to normal temperature in the heat exchanger: > Compressed air is cooled to form dry air and input into the heat exchanger It j presses the heat of the liquid refrigerant at normal temperature, which absorbs the heat of the "pressure = air l refrigerant" and becomes the normal temperature and dry high-quality compressed air. The high-pressure normal temperature dry compressed air can be input into various types of pneumatic tools, machinery ... In addition, the pressure sensor jπ provided at the air inlet and outlet and the temperature sensor provided with the low-dust refrigerant pipeline 381 return the measured pressure and temperature values to the microprocessor P. Comparative calculation, when there is a slight difference between the inlet pressure and the dust force at the outlet, 'it means that the ice layer has accumulated in the evaporator A, and the microprocessor ρ will actuate the four-position valve 53' to change the refrigerant flow direction, so that the evaporator a is no longer Refrigeration, as shown in Fig. 8, the refrigerant at the front end of the heat exchanger 24; the refrigerant output from the circuit 242 is guided into the evaporator A through the four-position valve 53, and then expanded into the evaporator B through the expansion and evaporation of the capillary tube 37, and the refrigerant is refrigerated. By four Guide 53 into the refrigerant compressor 31 to circulate; at this time, because the ice layer in the evaporator a has not yet melted, 'the proper coldness is still maintained', the compressed air is still guided into the evaporator A, and it will not affect the compressed air. Dry quality, and because the temperature of evaporation Γ′Β has not fallen to the required low temperature, the temperature measured by the temperature sensor ffl is high. When the temperature in evaporator B drops to the required operating temperature, After receiving the signal, the microprocessor ρ will actuate the Sanwei 51 and the solenoid valve 52, as shown in Figure 9, to change the direction of the compressed air into the evaporator B. At the same time, the high-pressure high-temperature gaseous refrigerant passes through the solenoid valve 52 and passes through the four-position The space 53 directly enters the evaporator A, thereby quickly melting the frozen ice and discharging it through the automatic drainage device 22. When the ice layer in the evaporator A is completely melted, the paper size can no longer be obtained due to the high-pressure refrigerant. Applicable to Chinese National Standard (CNS) A4 specification (21〇 > < 297mm) (Please read the precautions on the back before filling this page)
A7 B7 五 發明説明g ,當之散熱:故其低壓之回、流冷媒溫度隨之微升 停此動作(如圖十所示t如此微 f 53、電磁闕52等,使蒸發器A、Β交 π二乾燥機品質高,且可減少能源之損耗。依前 令’可得知本發明可歸納以下優點: L 3造严阻塞之慮,故其蒸發溫度可建立低於〇。。 t 採微處理器監控自H吏用,故其空氣乾 ===環’可重覆敎操細,故其空氣 線®— 經濟部中央標準局員工消費合作社印製 > .itA7 B7 Five invention descriptions g, when it dissipates heat: Therefore, its low pressure returns, and the temperature of the flow refrigerant rises and stops slightly (as shown in Figure 10, t is so small, such as f 53, electromagnetic 阙 52, etc., which makes the evaporators A and B The cross-pier dryer has high quality and can reduce energy consumption. According to the preamble, the following advantages can be summarized in the present invention: L 3 is considered to be strictly blocked, so its evaporation temperature can be established below 0. t mining Microprocessor monitoring is used by officials, so its air-drying === ring can be repeated, so its air line ®-printed by the Staff Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs > .it
Ns 6 I準 # 公 7 9 2Ns 6 I Standard # Male 7 9 2
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TW87114514A TW397903B (en) | 1998-09-01 | 1998-09-01 | The freezing-type low-dew-point drying control method for compressed air |
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TW87114514A TW397903B (en) | 1998-09-01 | 1998-09-01 | The freezing-type low-dew-point drying control method for compressed air |
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