TWI242629B - Absorption-type air conditioner system - Google Patents

Absorption-type air conditioner system Download PDF

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TWI242629B
TWI242629B TW093101409A TW93101409A TWI242629B TW I242629 B TWI242629 B TW I242629B TW 093101409 A TW093101409 A TW 093101409A TW 93101409 A TW93101409 A TW 93101409A TW I242629 B TWI242629 B TW I242629B
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Taiwan
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pipe
water
temperature
solution
air
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TW093101409A
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Chinese (zh)
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TW200525123A (en
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Yau Jang
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Yau Jang
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Abstract

An absorption-type air conditioner system using lithium bromide solution as absorbent is provided, which has a small volume and compact structure. The system includes an upper vessel 26, a lower vessel 27, a cooling heat exchanger 10, a self-induced air circulation device 11, an outdoor system controller 9 and a water heater 8. The upper vessel 26 includes a high temperature generator 1, a low temperature generator 2 and a condenser 3. The lower vessel 27 includes a high temperature heat exchanger 4, a low temperature heat exchanger 5, an evaporator 7 and an absorber 6. The upper vessel 26 is connected to the lower vessel 27 by a refrigerant water outlet pipe 28, a low temperature generator dilute solution inlet pipe 29, a low temperature generator concentrate solution outlet pipe 30, a high temperature generator dilute solution inlet pipe 31, a high temperature generator concentrate solution outlet pipe 32, a high temperature generator steam outlet pipe 56, a heating steam switch valve 55 and a high temperature generator steam inlet pipe 57. The system is an ideal central air conditioner system for large houses.

Description

1242629 玖、發明說明: 【發明所屬之技術領域】 本發明涉及一種用溴化鋰溶液作吸收劑,以水爲製冷 劑的空調,具體是指體積小、結構緊湊的一種吸收式空調 5 系統。 【先前技術】 傳統的吸收式空調的高溫發生器爲獨立的筒體,低溫 發生器與冷凝器爲一個筒體,蒸發器與吸收器爲一個筒 體,高、低溫熱交換器置於它們之外,這樣各筒體的焊縫 10 多,對外泄漏的機率大,真空度相應較低,熱傳導的損失 也相對較大。 【發明内容】 本發明的目的是提供一種結構非常緊湊,對外焊縫 少,真空狀態好,熱傳導的熱損失小的一種吸收式空調系 15 統。 本發明的設計方案是,它主要由上筒體、下筒體、冷 卻器、自動抽氣裝置、室外機控制器孤、熱水器組成,上 筒體内有高溫發生器、低溫發生器、冷凝器,下筒體内有 高溫熱交換器、低溫熱交換器、蒸發器、吸收器,上筒體 20 與下筒體由冷劑水出管、低發稀溶液入管、低發濃溶液出 管、高發稀溶液入管、高發濃溶液出管以及高發蒸汽出 管、冷熱切換閥、高發蒸汽入管串連連通,冷卻器的冷卻 水喷淋管由冷卻水出管與冷凝器的冷凝器換熱管連通,冷 卻器的冷卻器水槽和溢流管與排水管連通,補水浮球閥裝 1242629 置與補水管、補水電磁閥連通,冷卻器的過濾器由冷卻水 出管、冷卻泵、冷卻水入管與下筒體吸收器的吸收器換熱 管相通,自動抽氣裝置上端由抽氣管與下筒體吸收器相 通,上部由稀溶液出管與下筒體稀溶液出管連通,下部由 5 稀溶液入管與下筒體吸收器的稀溶液槽相通,熱水器的熱 水器換熱管一端與熱水入管II、熱水泵、熱水入管I相通, 另一端與熱水出管相通,熱水器的燃燒器與熱水器控制 器、過濾器、燃料入管相通,室外機控制器的控制線與空 調入口溫度感測器、空調出口溫度感測器、冷卻水入口溫 10 度感測器、冷卻水出口溫度感測器、高發溫度感測器、環 境溫度感測器、高發溫度開關、排氣溫度開關、冷水流量 控制器、冷水流量控制器、熱水流量控制器、高發液位感 測器、冷劑液位感測器、貯氣量感測器、低發結晶感測器、 冷卻水液位元感測器用導線連通。 15 【實施方式】 實施例: 參見圖1 — 3,本發明它主要由上筒體26、下筒體27、 冷卻器10、自動抽氣裝置11、室外機控制器9、熱水器8 組成,上筒體26内有高溫發生器1、低溫發生器2、冷凝 20 器3,下筒體27内有高溫熱交換器4、低溫熱交換器5、 蒸發器7、吸收器6,上筒體26與下筒體27由冷劑水出 管28、低發稀溶液入管29、低發濃溶液出管30、高發稀 溶液入管31、高發濃溶液出管32以及高發蒸汽出管56、 冷熱切換閥55、高發蒸汽入管57串連連通,冷卻水管40 1242629 6的吸收器換 連通冷凝器3的冷凝器換熱管24和吸收器 熱管38。 …冷卻1、1的冷卻水喷淋管64由冷卻水出管22與冷 旋為3的"减„。換熱&24連通,冷卻器1()的冷卻器水槽 79和溢流官69與排水管46連通,補水浮球閱裝置67與 補水管45、補水電磁閥49、過渡器%、補水端連通,冷 卻器10的過渡器70由冷卻水出f 8〇、冷卻果η、♦卻 水入管44與下筒體27吸收器6的吸收器換熱管3“通。 自動抽氣裝置U上端由抽氣管41與直接抽氣閥6〇 及下筒體27的吸收器6連通’上部由稀溶液出管42與下 筒體27稀溶液出管82連通,下部由稀溶液入管43與下 筒體27吸收器6的稀溶液槽83連通。 ίο 15 熱水器8的熱水器換熱管85 一端與熱水入管獅、熱 水泵2卜熱水入管153連通,另一端與熱水出管M連通’ 熱水器8的燃燒器84與熱水器控制器51、過濾器%、燃 料入管72連通,同時通過燃燒機控制器52與燃燒機14 連通。 室外機控制器9的控制線與空調入口溫度感測器τ卜 空调出口溫度感測器T2、冷卻水入口溫度感測器T3、冷 部水出口溫度感測器T4、高發溫度感測器T5、環境溫度 感測器T6、排氣溫度感測器T7、熱水溫度感測器T8、冷 水溫度感測器T9、高發溫度開關w卜熱水溫度開關W2、 冷水流量控制器B1、冷水流量控制器B2、熱水流量控制 裔B3、咼發液位感測器υι、冷劑液位感測器U2、貯氣量 20 1242629 感測器U3、低發結晶感測器U4、冷卻水液位元感測器U5 用導線連通。 參見圖1、2,高溫發生器1的燃燒器14與燃燒機控 制器52、過濾器50、燃料入管72連通,高發濃溶液出管 5 32與高溫熱交換器4連通,高發稀溶液入管31與高溫熱 交換管87連通,高發冷劑蒸汽通過低溫發生器2的低發 換熱管25從冷凝器3的高發冷劑蒸汽出管89出。 參見圖1、2,低溫發生器2的低發稀溶液入管29與 低溫熱交換器5的低溫熱交換管8 8連通,低發濃溶液出 10 管30與低溫熱交換器5相通。 參見圖1、2,冷凝器3的冷劑水盤23通過冷劑水出 管28與蒸發器7的冷劑水箱34連通,冷凝器3的冷凝器 換熱管24的另一端通過冷卻水管40與吸收器6的吸收器 換熱管3 8連通。 15 參見圖1、2,高發溶液液位元裝置12的溶液溢流管 62、溶液入管63與高溫發生器1連通,溶液溢流管62約 高於溶液液面,溶液入管63處於溶液中層偏下位置。 參見圖1、2,吸收器6的濃溶液喷淋管33兩端與高 溫熱交換器4、低溫熱交換器5連通,高溫熱交換管87和 20 低溫熱交換管88的另一端通過稀溶液出管82與溶液泵 18、稀溶液入管81、過濾器47、稀溶液槽83連通。 參見圖1、2,蒸發器7的蒸發器換熱管36 —端與空 調水入管190、空調水泵19、空調水入管1191、過濾器48、 空調水入管III92連通,另一端與空調水出管93連通。 1242629 參見圖1、2,冷劑水盤37 —方面通過冷劑水出管 1174、冷劑水泵20、冷劑水入管39與冷劑水箱34連通, 另一方面通過冷劑水出管173、冷劑液液位元裝置13、冷 劑水回管76與下筒體27内腔連通,冷劑液液位元裝置13 5 的下端通過冷劑旁通閥75、冷劑液回管94與稀溶液槽83 連通。 參見圖1、2,旁通閥95兩端與空調水入管III92,空 調水出管93連通。 參見圖1、2,溶液再生器77 —端通過貯氣室抽氣閥 10 61與自動抽氣裝置11連通,另一端通過溶液閥97與稀溶 液出管82連通。 本發明的工作過程是: 高溫發生器1 :高溫發生器1的燃燒機14在爐膛15 中燃燒,1200°C的火焰將溶液加熱到158°C,産生大量水 15 蒸汽,水蒸汽進入低溫發生器2的低發換熱管25,高溫發 生器1將57%的稀溶液被濃縮到63%,經高發濃溶液出管 32、進入高溫熱交換器4,經濃溶液噴淋管33向吸收器換 熱管38喷淋; 低溫發生器2 :高溫發生器1來的水蒸汽進入低發換 20 熱管25内,將管外的稀溶液加熱到90°C,溶液産生的水 蒸汽經高發冷劑蒸汽出管89進入冷凝器3,57%的稀溶液 被濃縮到63%,經低發濃溶液出管30進入低溫熱交換器 5,經濃溶液噴淋管33向吸收器換熱管38喷淋; 冷凝器3 :冷卻水流經冷凝器換熱管24,將管外的水 1242629 蒸汽冷凝爲水,把低溫發生器2的熱量由冷卻水出管22 帶進冷卻器10,而冷凝水作爲製冷劑經冷劑水出管28進 入蒸發器7的冷劑水箱3 4,由冷劑水噴淋管3 5向蒸發器 換熱管36喷淋製冷; 5 高溫熱交換器4 :將高溫發生器1經高發濃溶液出管 32來的158°C的濃溶液與吸收器6經稀溶液槽83、過濾器 47、稀溶液入管81、溶液泵18、稀溶液出管82來的38 °C的稀溶液進行熱交換,使稀溶液升溫,濃溶液降溫,158 °C濃溶液經交換後進入吸收器6時變爲42°C,回收了 116 10 C溫差的熱ϊ, 低溫熱交換器5 :將低溫發生器2經低發濃溶液出管 30來的90°C濃溶液與吸收器6經稀溶液槽83、過濾器47、 稀溶液入管81、溶液泵18、稀溶液出管82來的38°C的稀 溶液進行熱交換,90°C濃溶液經熱交換後進入吸收器6時 15 變爲41°C,回收了 49°C溫差的熱量;高溫熱交換器4與 低溫熱交換器5,大幅度減少了高、低溫發生器4、5加溫 所需的熱量,同時也減少了溶液降溫所需的冷卻水負荷, 其性能優劣對機組節能指標起決定性作用。 蒸發器7:從空調系統經空調水入管11192、過濾器48、 20 空調水入管1191、空調水泵19來的14°C冷水流經蒸發器 換熱管36,被蒸發器換熱管36外的真空環境下的4°C的 冷劑水喷淋,冷劑水蒸發吸熱,使冷水降溫到7 °C,冷劑 水獲得了空調系統的熱量,變成水蒸汽進入吸收器6 ; 吸收器6 :濃度63%、溫度41°C的溴化鋰溶液具有極 1242629 度強的吸收水蒸汽能力,它經濃溶液喷淋管33向吸收器 換熱管38時,它吸收了蒸發器7的水蒸汽後,溫度上升、 濃度變稀,存於稀溶液槽83,從冷卻器10經過濾器70、 冷卻水出管80、冷卻泵17、冷卻水入管44、進入吸收器 5 換熱管3 8的冷卻水將溶液吸收來的熱量帶走,而變稀爲 57%的溶液則被溶液泵18經稀溶液出管82分別送到高溫 熱交換器4和低溫熱交換器5的高溫熱交換管87、低溫熱 交換管88加溫濃縮; 本發明的優點是: 10 突破了傳統的吸收式空調的結構,冷凝器3、低溫發 生器2、高溫發生器1在一個筒體内,高溫發生器1上有 低溫發生器2,低溫發生器2上有冷凝器3,對外泄漏大 幅度降低,上筒體26只有一條長焊缝,真空狀態非常好, 結構非常緊湊,它們之間的熱傳導的梯度關係好,高溫發 15 生器1溫度最高,低溫發生器2的溫度第二,冷凝器3的 溫度最低;高溫熱交換器4、低溫熱交換器5共處在下筒 體27内,吸收器6的濃溶液入和稀溶液出的四根管子都 在下筒體27内,即使有少量泄漏也不會影響整個系統的 真空度;上筒體26、下筒體27焊縫少,能滿足高度真空 20 的要求。 本發明由於結構緊湊、體積小,焊縫少、真空度高, 自動控制水平高,是家庭大戶型、別墅的理想中央空調。 【圖式簡單說明】 1242629 圖1爲本發明結構原理示意圖; 圖2爲圖1部分結構原理放大示意圖;及 圖3爲圖1部分結構原理放大示意圖。1242629 发明 Description of the invention: [Technical field to which the invention belongs] The present invention relates to an air conditioner using a lithium bromide solution as an absorbent and water as a refrigerant, and specifically refers to an absorption air conditioner 5 system having a small volume and a compact structure. [Previous technology] The high temperature generator of the traditional absorption air conditioner is an independent cylinder, the low temperature generator and the condenser are one cylinder, the evaporator and the absorber are one cylinder, and the high and low temperature heat exchangers are placed on them. In addition, if there are more than 10 welds in each cylinder, the probability of external leakage is large, the degree of vacuum is correspondingly low, and the loss of heat conduction is relatively large. [Summary of the Invention] The purpose of the present invention is to provide an absorption air conditioning system with a very compact structure, few external welds, good vacuum conditions, and low heat loss due to heat conduction. The design scheme of the present invention is that it mainly consists of an upper cylinder, a lower cylinder, a cooler, an automatic air extraction device, an outdoor unit controller, and a water heater. The upper cylinder has a high temperature generator, a low temperature generator, and a condenser. There are high temperature heat exchangers, low temperature heat exchangers, evaporators, and absorbers in the lower cylinder. The upper cylinder 20 and the lower cylinder are discharged from the refrigerant water pipe, the low-temperature dilute solution into the pipe, and the low-temperature concentrated solution. The tube, high-intensity dilute solution inlet pipe, high-intensity concentrated solution outlet pipe, and high-intensity steam outlet pipe, hot and cold switching valve, and high-intensity steam inlet pipe are connected in series. The cooling water spray pipe of the cooler consists of the cooling water outlet pipe and the condenser heat exchange pipe of the condenser. The cooler water tank and overflow pipe of the cooler communicate with the drain pipe. The makeup water float ball valve 1242629 is connected with the makeup water pipe and the makeup water solenoid valve. The filter of the cooler is composed of the cooling water outlet pipe, the cooling pump and the cooling water inlet pipe. The absorber heat exchange tube of the lower cylinder absorber is connected. The upper end of the automatic air extraction device is connected to the lower cylinder absorber by an exhaust pipe. The upper part is connected with the dilute solution outlet pipe and the lower cylinder dilute solution outlet pipe. The lower part is composed of 5 dilute solutions. The tube communicates with the dilute solution tank of the lower cylinder absorber. One end of the heat exchanger tube of the water heater of the water heater is connected to the hot water inlet pipe II, the hot water pump, and the hot water inlet pipe I. The other end is connected to the hot water outlet pipe. The burner of the water heater is controlled by the water heater. Filters, filters, and fuel inlet pipes, the control line of the outdoor unit controller and the air conditioner inlet temperature sensor, air conditioner outlet temperature sensor, cooling water inlet temperature 10 degree sensor, cooling water outlet temperature sensor, high Temperature sensor, ambient temperature sensor, high temperature switch, exhaust temperature switch, cold water flow controller, cold water flow controller, hot water flow controller, high temperature liquid level sensor, refrigerant liquid level sensor The air storage sensor, low-emitting crystal sensor, and cooling water level sensor are connected by wires. 15 [Embodiment] Example: Referring to FIGS. 1-3, the present invention is mainly composed of an upper cylinder 26, a lower cylinder 27, a cooler 10, an automatic air extraction device 11, an outdoor unit controller 9, and a water heater 8. Inside the cylinder 26 is a high-temperature generator 1, a low-temperature generator 2, a condenser 20, and a lower cylinder 27, and a high-temperature heat exchanger 4, a low-temperature heat exchanger 5, an evaporator 7, an absorber 6, and an upper cylinder. The body 26 and the lower cylinder 27 are composed of a refrigerant water outlet pipe 28, a low-fat dilute solution inlet pipe 29, a low-fat dilute solution outlet pipe 30, a high-fat dilute solution inlet pipe 31, a high-thickness concentrated solution outlet pipe 32, and a high-emission steam outlet pipe 56, cold and hot The switching valve 55 and the high-pressure steam inlet pipe 57 are connected in series, and the absorber of the cooling water pipe 40 1242629 6 is replaced by the condenser heat exchange pipe 24 and the absorber heat pipe 38 of the condenser 3. … The cooling water spray pipe 64 for cooling 1, 1 is cooled by the cooling water outlet pipe 22 to the "minus" of the cold spin 3. The heat exchanger & 24 communicates with the cooler water tank 79 and the overflow officer of the cooler 1 () 69 is in communication with the drainage pipe 46, and the water-supplying floating ball reading device 67 is in communication with the water-supplying pipe 45, the water-supplying solenoid valve 49, the transition device%, and the water-supply end. ♦ However, the water inlet pipe 44 communicates with the absorber heat exchange pipe 3 of the absorber 6 of the lower cylinder 27. The upper end of the automatic air extraction device U is connected by the air suction pipe 41 to the direct air suction valve 60 and the absorber 6 of the lower cylinder 27. The upper part is communicated with the dilute solution outlet pipe 42 and the lower cylinder 27 and the dilute solution outlet pipe 82. The solution inlet pipe 43 communicates with the dilute solution tank 83 of the absorber 6 of the lower cylinder 27. ίο 15 One end of the water heater heat exchanger tube 85 of the water heater 8 is connected to the hot water inlet pipe, the hot water pump 2 and the hot water inlet pipe 153, and the other end is connected to the hot water outlet pipe M 'The burner 84 of the water heater 8 and the water heater controller 51 and the filter The fuel inlet pipe 72 communicates with the combustor 14 through the combustor controller 52. The control line of the outdoor unit controller 9 and the air conditioner inlet temperature sensor τb The air conditioner outlet temperature sensor T2, the cooling water inlet temperature sensor T3, the cold water outlet temperature sensor T4, and the high-temperature temperature sensor T5 , Ambient temperature sensor T6, exhaust temperature sensor T7, hot water temperature sensor T8, cold water temperature sensor T9, high temperature switch w, hot water temperature switch W2, cold water flow controller B1, cold water flow Controller B2, hot water flow control B3, burst liquid level sensor υι, refrigerant liquid level sensor U2, air storage 20 1242629 sensor U3, low emission crystal sensor U4, cooling water level The element sensor U5 is connected by a wire. 1 and 2, the burner 14 of the high temperature generator 1 is in communication with the burner controller 52, the filter 50, and the fuel inlet pipe 72, and the high-intensity solution outlet pipe 5 32 is in communication with the high-temperature heat exchanger 4 and the high-intensity dilute solution is in the pipe. 31 communicates with the high-temperature heat exchange tube 87, and the high-temperature refrigerant vapor exits the high-temperature refrigerant vapor outlet pipe 89 of the condenser 3 through the low-temperature heat exchange tube 25 of the low-temperature generator 2. 1 and 2, the low-temperature dilute solution inlet pipe 29 of the low-temperature generator 2 communicates with the low-temperature heat exchange pipe 8 8 of the low-temperature heat exchanger 5, and the low-temperature concentrated solution outlet pipe 30 communicates with the low-temperature heat exchanger 5. . Referring to FIGS. 1 and 2, the refrigerant water pan 23 of the condenser 3 communicates with the refrigerant water tank 34 of the evaporator 7 through the refrigerant water outlet pipe 28, and the other end of the condenser heat exchange pipe 24 of the condenser 3 communicates with the absorption through the cooling water pipe 40. The absorber heat exchange tubes 38 of the heat exchanger 6 communicate with each other. 15 Referring to FIGS. 1 and 2, the solution overflow pipe 62 and the solution inlet pipe 63 of the high-level solution liquid level device 12 are in communication with the high-temperature generator 1. The solution overflow pipe 62 is about higher than the solution liquid level, and the solution inlet pipe 63 is in the middle of the solution. Down position. Referring to FIGS. 1 and 2, both ends of the concentrated solution spray pipe 33 of the absorber 6 are in communication with the high-temperature heat exchanger 4 and the low-temperature heat exchanger 5. One end communicates with the solution pump 18, the dilute solution inlet pipe 81, the filter 47, and the dilute solution tank 83 through the dilute solution outlet pipe 82. 1 and 2, one end of the evaporator heat exchange pipe 36 of the evaporator 7 is connected to the air conditioning water inlet pipe 190, the air conditioning water pump 19, the air conditioning water inlet pipe 1191, the filter 48, and the air conditioning water inlet pipe III92, and the other end is connected to the air conditioning water outlet pipe 93 Connected. 1242629 Referring to FIGS. 1 and 2, the refrigerant water pan 37 communicates with the refrigerant water tank 34 through the refrigerant water outlet pipe 1174, the refrigerant water pump 20, and the refrigerant water inlet pipe 39, and on the other hand, the refrigerant water outlet pipe 173, the cold water The coolant liquid level device 13, the coolant water return pipe 76 communicates with the inner cavity of the lower cylinder 27. The lower end of the coolant liquid level device 13 5 passes through the coolant bypass valve 75, the coolant liquid return pipe 94, and the diluent. The solution tank 83 communicates. Referring to Figs. 1 and 2, both ends of the bypass valve 95 communicate with the air-conditioning water inlet pipe III92 and the air-conditioning water outlet pipe 93. Referring to Figs. 1 and 2, the solution regenerator 77 is communicated with the automatic gas extraction device 11 through an air storage chamber suction valve 1061, and the other end is communicated with the dilute solution outlet pipe 82 through a solution valve 97. The working process of the present invention is: High temperature generator 1: The burner 14 of the high temperature generator 1 burns in the furnace 15, the flame of 1200 ° C heats the solution to 158 ° C, and generates a large amount of water 15 steam, which occurs at low temperature. The low-temperature heat transfer tube 25 of the heat exchanger 2 and the high-temperature generator 1 concentrate 57% of the dilute solution to 63%. The high-temperature concentrated solution exits the pipe 32, enters the high-temperature heat exchanger 4, and is absorbed by the concentrated solution spray pipe 33. Heat exchanger tube 38 sprays; Low temperature generator 2: Water vapor from high temperature generator 1 enters low heat exchange 20 heat pipe 25 and heats the dilute solution outside the pipe to 90 ° C. The water vapor generated by the solution is cooled by high heat The agent vapor exit pipe 89 enters the condenser 3, and the 57% dilute solution is concentrated to 63%. It passes through the low-concentration solution exit pipe 30 and enters the low-temperature heat exchanger 5, and then passes through the concentrated solution spray pipe 33 to the absorber heat exchange pipe 38. Spraying; Condenser 3: Cooling water flows through condenser heat exchange tube 24, condenses the water outside the tube 1242629 steam into water, and brings the heat of low temperature generator 2 from cooling water outlet tube 22 to cooler 10, and the condensed water is used as The refrigerant enters the refrigerant water tank 3 4 of the evaporator 7 through the refrigerant water outlet pipe 28 and is sprayed with the refrigerant water. Pipe 3 5 sprays cooling to evaporator heat exchange pipe 36; 5 High temperature heat exchanger 4: Passes the concentrated solution of 158 ° C from high temperature generator 1 through high-concentration solution outlet pipe 32 and absorber 6 through dilute solution tank 83 , Filter 47, dilute solution inlet tube 81, solution pump 18, dilute solution outlet tube 82. The dilute solution at 38 ° C is heat exchanged to increase the temperature of the dilute solution and reduce the temperature of the concentrated solution. After the exchange, the concentrated solution at 158 ° C enters the absorption. The temperature of the reactor 6 became 42 ° C, and the heat of the temperature difference of 116 10 C was recovered. The low-temperature heat exchanger 5: The 90 ° C concentrated solution from the low-temperature generator 2 through the low-concentration solution outlet pipe 30 and the absorber 6 After the dilute solution tank 83, the filter 47, the dilute solution inlet tube 81, the solution pump 18, and the dilute solution outlet tube 82, the dilute solution at 38 ° C is heat exchanged, and the concentrated solution at 90 ° C enters the absorber 6 after heat exchange. 15 becomes 41 ° C, and recovers the heat with a temperature difference of 49 ° C; the high temperature heat exchanger 4 and the low temperature heat exchanger 5 greatly reduce the heat required for heating the high and low temperature generators 4, 5 and at the same time It also reduces the cooling water load required for solution cooling, and its performance is decisive for the unit's energy saving index. Evaporator 7: The 14 ° C cold water from the air conditioning system through the air conditioning water inlet pipe 11192, filters 48, 20 air conditioning water inlet pipe 1191, the air conditioning water pump 19 flows through the evaporator heat exchange pipe 36, and the vacuum environment outside the evaporator heat exchange pipe 36 Coolant water spray at 4 ° C, the refrigerant water evaporates and absorbs heat, cooling the cold water to 7 ° C, the refrigerant water gains the heat of the air conditioning system, and turns into water vapor into the absorber 6; absorber 6: concentration 63 %, Lithium bromide solution with a temperature of 41 ° C has a strong absorption capacity of 1242629 degrees. When it passes the concentrated solution spray pipe 33 to the absorber heat exchange tube 38, it absorbs the water vapor of the evaporator 7, the temperature rises, The concentration becomes diluted and stored in the dilute solution tank 83. The cooling water absorbed from the cooler 10 through the filter 70, the cooling water outlet pipe 80, the cooling pump 17, the cooling water inlet pipe 44 and the absorber 5 and the heat exchange pipe 38 is absorbed by the solution. The heat is taken away, and the solution diluted to 57% is sent by the solution pump 18 to the high-temperature heat exchanger 4 and the low-temperature heat exchanger 5 and the low-temperature heat exchanger 87 through the dilute solution outlet pipe 82, respectively. The exchange tube 88 is heated and concentrated; the advantages of the present invention are: 10 breaks through the traditional suction The structure of the air conditioner is that the condenser 3, the low temperature generator 2 and the high temperature generator 1 are in one cylinder. The high temperature generator 1 has a low temperature generator 2 and the low temperature generator 2 has a condenser 3, which greatly reduces external leakage. The upper cylinder 26 has only one long welding seam. The vacuum state is very good and the structure is very compact. The gradient of heat conduction between them is good. The high temperature generator 1 has the highest temperature, the low temperature generator 2 has the second temperature, and the condenser. The temperature of 3 is the lowest; the high temperature heat exchanger 4 and the low temperature heat exchanger 5 are co-located in the lower cylinder 27, and the four tubes of the concentrated solution entering and diluting solution of the absorber 6 are all in the lower cylinder 27, even if there are A small amount of leakage will not affect the vacuum of the entire system; the upper cylinder 26 and lower cylinder 27 have fewer welds, which can meet the requirements of high vacuum 20. The invention has the advantages of compact structure, small volume, few welds, high vacuum, and high level of automatic control, and is an ideal central air conditioner for large households and villas. [Schematic description] 1242629 FIG. 1 is a schematic diagram of the structure principle of the present invention; FIG. 2 is an enlarged schematic diagram of the structure principle of FIG. 1; and FIG. 3 is an enlarged schematic diagram of the structure principle of FIG. 1.

11 1242629 【圖式之主要元件代表符號說明】 1 一高溫發生器 24 —冷凝器換熱管 2—低溫發生器 25—低發換熱管 3 —冷凝器 26 —上筒體 4一高溫熱交換器 27 —下筒體 5—低溫熱交換器 28一冷劑水出管 6—吸收器 29—低發稀溶液入管 7 —蒸發器 30—低發濃溶液出管 8 一熱水器 31—高發稀溶液入管 鲁 9一室外機控制器 32—高發濃溶液出管 10 —冷卻器 33 —濃溶液喷淋管 11 一自動抽氣裝置 34—冷劑水箱 12 —高發溶液液位元裝置 35 —冷劑水喷淋管 13—冷劑液液位元裝置 36 —蒸發器換熱管 14 一燃燒機 37一冷劑水盤 15 —爐月堂 38 —吸收器換熱管 16 —冷卻風機 39—冷劑水入管 ® 17 —冷卻泵 40—冷卻水管 18 —溶液泵 41 一抽氣管 19 一空調水泵 42—稀溶液出管 20—冷劑水泵 43—稀溶液入管 21 —熱水泵 44一冷卻水入管 22—冷卻水出管 45一補水管 23 一冷劑水盤 46—排水管 12 1242629 47—過慮器 48 —過慮器 49 —補水電磁閥 50 一過滤1§ 51 —熱水器控制器 52 —燃燒機控制器11 1242629 [Description of the main components of the diagram] 1 A high temperature generator 24 —condenser heat exchange tube 2 —low temperature generator 25 —low heat exchange tube 3 —condenser 26 —upper cylinder 4—high temperature heat exchanger 27—lower cylinder 5—low temperature heat exchanger 28—coolant water outlet pipe 6—absorber 29—low-temperature dilute solution inlet pipe 7—evaporator 30—low-thickness solution outlet pipe 8—water heater 31—high-temperature dilute solution Inlet pipe 9—Outdoor unit controller 32—High-fat concentrated solution outlet pipe 10—Cooler 33—Concentrated solution spray pipe 11—Automatic air extraction device 34—Coolant water tank 12—High-level solution liquid level device 35—Coolant water Spray pipe 13—Refrigerant liquid level device 36—Evaporator heat exchange tube 14—Burner 37—Refrigerant water pan 15—Guan Yuetang 38—Absorber heat exchange tube 16—Cooling fan 39—Coolant water inlet pipe® 17 —Cooling pump 40—Cooling water pipe 18—Solution pump 41—Exhaust pipe 19—Air conditioner water pump 42—Dilute solution outlet pipe 20—Refrigerant water pump 43—Dilute solution inlet pipe 21—Hot water pump 44—Cooling water inlet pipe 22—Cooling water outlet pipe 45 one water pipe 23 one 46- drain water tray agent 12124262947- worrying too much 48 - worrying too much 49 - solenoid valve 50 a replenishment filter 1§ 51 - water heater controller 52 - combustor controller

53— 熱水入管I 54— 熱水出管 55— 冷熱切換閥 56 —高發蒸汽出管 57 —高發蒸汽入管 58 —排氣管 59— 排氣管 60— 直接抽氣閥 61 —貯氣室抽氣閥 62— 溶液溢流管 63— 溶液入管 64 —冷卻水喷淋管 65 —冷卻器充填料 66一百頁窗 67—補水浮球閥裝置 68 —排水開關 69一溢流管 70 —過濾器 71 —排水塞 72— 燃料入管53— Hot water inlet pipe I 54— Hot water outlet pipe 55—Hot and cold switching valve 56—High steam exit pipe 57—High steam exit pipe 58—Exhaust pipe 59—Exhaust pipe 60—Direct air extraction valve 61—Reservoir extraction Air valve 62—Solution overflow pipe 63—Solution inlet pipe 64—Cooling water spray pipe 65—Cooler filling and filling 66 One hundred windows 67—Water supply float valve device 68—Drain switch 69—Overflow pipe 70—Filter 71 --Drain plug 72-- Fuel inlet pipe

73— 冷劑水出管I 74一冷劑水出管II 75— 冷劑旁通閥 76— 冷劑水回管 77— 溶液再生器 78 —拉繩 79— 冷卻器水槽 80— 冷卻水出管 81— 稀溶液入管 82— 稀溶液出管 83— 稀溶液槽 84— 燃燒器73—Refrigerant water outlet pipe I 74—Coolant water outlet pipe II 75—Refrigerant bypass valve 76—Refrigerant water return pipe 77—Solution regenerator 78—Drawstring 79—Cooler water tank 80—Cooling water outlet pipe 81—dilute solution inlet pipe 82—dilute solution outlet pipe 83—dilute solution tank 84—burner

85 —熱水器換熱管 86—熱水入管II 87 —高溫熱交換管 88 —低溫熱交換管 89— 高發冷劑蒸汽出管85 —Heat exchange pipe for water heater 86 —Hot water pipe II 87 —High temperature heat exchange pipe 88 —Low temperature heat exchange pipe 89—High refrigerant vapor exit pipe

90— 空調水入管I90— Air conditioning water inlet pipe I

91— 空調水入管II91— Air Conditioning Water Inlet Pipe II

92— 空調水入管III 93— 空調水出管 94— 冷劑液回管92—Air conditioner water inlet pipe III 93—Air conditioner water outlet pipe 94—Refrigerant liquid return pipe

13 1242629 95 —旁通閥 T9 一冷水溫度感測裔 96 —過濾器 W1 —高發溫度開關 97 —溶液閥 W2—熱水溫度開關 T1—空調入口溫度感測器 B1 —冷水流量控制裔 T2—空調出口溫度感測器 B2—冷水流量控制器 T3 —冷卻水入口溫度感測器 B 3 —熱水流量控制器 T4 一冷卻水出口溫度感測器 U1—高發液位感測器 T5—高發溫度感測器 U2—冷劑液位感測器 T6—環境溫度感測器 U3 一貯氣量感測 T7 —排氣溫度感測 U4—低發結晶感測器 T8—熱水溫度感測器 U5—冷卻水液位感測器13 1242629 95 —Bypass valve T9—Cold water temperature sensor 96—Filter W1—High temperature switch 97—Solution valve W2—Hot water temperature switch T1—Air conditioner inlet temperature sensor B1—Cold water flow control T2—Air conditioner Outlet temperature sensor B2—Cool water flow controller T3—Cooling water inlet temperature sensor B 3—Hot water flow controller T4—Cooling water outlet temperature sensor U1—High temperature liquid level sensor T5—High temperature temperature Sensor U2—Refrigerant level sensor T6—Environmental temperature sensor U3—Air storage volume sensor T7—Exhaust temperature sensor U4—Low-temperature crystal sensor T8—Hot water temperature sensor U5—Cooling Water level sensor

1414

Claims (1)

1242629 拾、申請專利範圍: L 種吸收式空調系統,其特徵在於它主要由上筒體(26 )、 下筒體(27)、冷卻器(10)、自動抽氣裝£ (⑴、室外機 控制器(9)、熱水器⑴組成,上筒體(26)内有高溫發 生器(1)、低溫發生器(2)、冷凝器(3),下筒體(27)内 有高溫熱交換器(4)、低溫熱交換器(5)、蒸發器(7)、吸 收器(6),上筒體(26)與下筒體(27)由冷劑水出管(28)、 低發稀溶液入管(29)、低發濃溶液出管(3〇)、高發稀溶液 入官(31)、高發濃溶液出管(32)以及高發蒸汽出管、 鲁 冷熱切換閥(55)、高發蒸汽入管(57)串連連通,冷卻水 官(40)連通冷凝器(3)的冷凝器換熱管(24)和吸收器 (6)的吸收器換熱管(38 )。 2·根據申印專利範圍第1項所述的一種吸收式空調系統,其特 4文在於部^§( 1 〇 )的冷卻水贺淋管(Μ )由冷卻水出管(2 2 ) 與冷凝器(3)的冷凝器換熱管(24)連通,冷卻器(1〇) 的冷卻器水槽(79)和溢流管(69)與排水管(46)連通, 補水浮球閥装置(67)與補水管(45)、補水電磁閥(49)、 · 過濾器(96)、補水端連通,冷卻器(1〇)的過濾器(7〇) 由冷部水出管(80)、冷卻泵(17)、冷卻水入管(44)與下 筒體(27)吸收器(6)的吸收器換熱管連通。 3·根據申请專利範圍第丨項所述的一種吸收式空調系統,其特 徵在於自動抽氣裝置(1〇上端由抽氣管(41)與直接抽氣 閥(6〇)及下筒體(27)的吸收器(6)連通,上部由稀溶 液出管(42)與下筒體(27)稀溶液出管(82)連通,下部 15 1242629 由稀命液入s (43)與下筒體(27)吸收器“)的稀溶液 槽(83 )連通。 ^據申.月專利範圍第j項所述的一種吸收式空調系統,其特 熱水器⑴的熱水器換熱管(85) -端與熱水入管 11 (86)、熱水栗(21)、熱水入管I (μ)連通,另一端與 心水出g (54)連通,熱水器的燃燒器(料)與熱水 器控制器⑸)、過濾器(5〇)、燃料入管(72)連通,同時 通過燃燒機控制器(52)與燃燒機(14)連通。 5·根據申請專利範圍第U所述的一種吸收式空調系統,其肖 # 徵在於室外機控制器(9)的控制線與空調入口溫度感測器 )工凋出口 /孤度感測裔(丁2 )、冷卻水入口溫度感測器 (T3)、冷卻水出口溫度感測器(T4)、高發溫度感測器 (Τ5 )、環^ /皿度感測裔(Τ6 )、排氣溫度感測器(口)、熱 水溫度感測器(Τ8)、冷水溫度感測器(Τ9)、高發溫度開關 (W1)、熱水溫度開關(W2)、冷水流量控制器(βι)、冷 水流量控制器(B2)、熱水流量控制器(B3)、高發液位感 測器(υι)、冷劑液位感測器(U2)、貯氣量感測器(u3)、 · 低發結晶感測器(U4)、冷卻水液位感測器(U5)用導線連 通。 6·根據申請專利範圍第1項所述的一種吸收式空調系統,其特 徵在於高溫發生器(1 )的燃燒器(14)與燃燒機控制器(52)、 ’ 過濾器(50)、燃料入管(72)連通,高發濃溶液出管(32) 與高溫熱交換器(4)連通,高發稀溶液入管(31)與高溫 熱交換管(87)連通,高發冷劑蒸汽通過低溫發生器(2) 16 1242629 的低舍換熱管(25 )從冷凝器(3 )的高發冷劑蒸汽出管(89 ) 7·根據申請專利範圍第1項所述的一種吸收式空調系統,其特 徵在於低溫發生器(2)的低發稀溶液入管(29)與低溫熱 交換器(5)的低溫熱交換管(88)連通,低發濃溶液出管 (3 0 )與低溫熱交換器(5 )相通。 8.根據申請專利範圍第1項所述的一種吸收式空調系統,其特 徵在於冷凝器(3)的冷劑水盤(23)通過冷劑水出管(28) 與瘵發器(7)的冷劑水箱(34)連通,冷凝器(3 )的冷凝 鲁 器換熱管(24)的另一端通過冷卻水管(4〇)與吸收器(6) 的吸收器換熱管(38)連通。 9·根據申請專利範圍第丨項所述的一種吸收式空調系統,其特 徵在於尚發溶液液位元裝置(12)的溶液溢流管(62)、溶 液入笞(63 )與咼溫發生器(1 )連通,溶液溢流管(62 ) 約高於溶液液面,溶液入管(63)處於溶液中層偏下位置。 1 〇·根據申明專利範圍第1項所述的一種吸收式空調系統,其特 徵在於吸收器(6)的濃溶液噴淋管(33)兩端與高溫熱交 籲 換官(87)、低溫熱交換管(88)連通,高溫熱交換管(87) 和低溫熱交換管(88)的另一端通過稀溶液出管(82)與溶 液泵(18)、稀溶液入管(81)、過濾器(47)、稀溶液槽(83) 連通。 U·根據申請專利範圍帛1項所述的一種吸收式空調系統,其特 徵在於蒸發器⑺的蒸發器換熱管(36) _端與空調水入 官1(90)、空調水泵(19)、空調水入管π(91)、過濾器(48)、 17 1242629 空調水入管 通。 III ( 92 )連通 另一端與空調水出管(93)連 .根據申Μ專利第!項所述的—種吸收式空調系統,立特 徵在於冷麻盤(37) _方面通過冷财㈣π(74)^ 劑水泵(20)、冷劑水人管(39)與冷劑水箱(Μ)連通, 另-方面通過冷劑水出管1(73)、冷劑液液位元裝置(⑴、 冷劑水回管(76)盘下r ηπ \ ^ )/、下问體(27)内腔連通,冷劑液液位元1242629 Patent application scope: L types of absorption air-conditioning system, which is characterized in that it is mainly composed of an upper cylinder (26), a lower cylinder (27), a cooler (10), an automatic air extraction unit (⑴, outdoor unit) The controller (9) and the water heater are composed of a high temperature generator (1), a low temperature generator (2), a condenser (3) in the upper cylinder (26), and a high temperature heat exchange in the lower cylinder (27). (4), low-temperature heat exchanger (5), evaporator (7), absorber (6), the upper cylinder (26) and the lower cylinder (27) are cooled by the refrigerant water outlet pipe (28), low Diluted solution inlet pipe (29), low-concentrated solution outlet pipe (30), high-diluted solution inlet pipe (31), high-concentrated solution outlet pipe (32), and high-emission steam outlet pipe, Lu cold heat switching valve (55), The high-pressure steam inlet pipe (57) is connected in series, and the cooling water officer (40) is connected to the condenser heat exchange pipe (24) of the condenser (3) and the absorber heat exchange pipe (38) of the absorber (6). 2 · According to Shenyin An absorption air-conditioning system according to item 1 of the patent scope, the special feature of which is the cooling water shower pipe (Μ) in the section ^ § (10), which is provided by the cooling water outlet pipe (2 2) and the condenser (3). Condensation The heat exchange pipe (24) is in communication, the cooler water tank (79) and overflow pipe (69) in the cooler (10) are in communication with the drain pipe (46), and the water supply float valve device (67) is connected to the water supply pipe (45) and water The solenoid valve (49), the filter (96) and the water supply end are connected, and the filter (70) of the cooler (10) is composed of a cold water outlet pipe (80), a cooling pump (17), and a cooling water inlet pipe ( 44) It communicates with the absorber heat exchange tube of the lower cylinder (27) and the absorber (6). 3. An absorption air-conditioning system according to item 丨 of the patent application scope, which is characterized by an automatic air extraction device (10 upper end The suction pipe (41) communicates with the direct suction valve (60) and the absorber (6) of the lower cylinder (27), and the upper part is connected with the dilute solution outlet pipe (42) and the lower cylinder (27). (82) is connected, and the lower part 15 1242629 is connected to the dilute solution tank (83) of the lower cylinder (27) absorber ") by the diluent solution inlet s (43). An absorption type air-conditioning system has a water heater heat exchange pipe (85) -end of a special water heater connected to a hot water inlet pipe 11 (86), a hot water pump (21), and a hot water inlet pipe I (μ), and the other end is connected to The heart water outlet g (54) communicates with the water heater's burner (material) and the water heater controller ⑸), the filter (50), and the fuel inlet pipe (72). At the same time, the burner controller (52) communicates with the burner ( 14) Connected. 5. According to an absorption air-conditioning system described in U of the scope of the patent application, its characteristics are the control line of the outdoor unit controller (9) and the air-conditioning inlet temperature sensor). Sensing ancestry (Ding 2), cooling water inlet temperature sensor (T3), cooling water outlet temperature sensor (T4), high temperature temperature sensor (T5), ring temperature sensor (T6) , Exhaust temperature sensor (port), hot water temperature sensor (T8), cold water temperature sensor (T9), high temperature switch (W1), hot water temperature switch (W2), cold water flow controller ( βι), cold water flow controller (B2), hot water flow controller (B3), high temperature liquid level sensor (υι), refrigerant liquid level sensor (U2), air storage sensor (u3), · Low-emitting crystal sensor (U4) and cooling water level sensor (U5) are connected by wires. 6. An absorption air-conditioning system according to item 1 of the scope of patent application, which is characterized by a burner (14) and a burner controller (52), a filter (50), and a fuel of a high-temperature generator (1). The inlet pipe (72) communicates with the high-concentration solution outlet pipe (32) and the high-temperature heat exchanger (4). The high-fat dilute solution inlet pipe (31) communicates with the high-temperature heat exchange pipe (87). The high-temperature refrigerant vapor passes through the low temperature. The generator (2) 16 1242629's low-rise heat exchange tube (25) exits the high-refrigerant vapor exit pipe (89) from the condenser (3). 7. An absorption air-conditioning system according to item 1 of the scope of patent application, It is characterized in that the low-temperature dilute solution inlet pipe (29) of the low-temperature generator (2) is in communication with the low-temperature heat exchange pipe (88) of the low-temperature heat exchanger (5), and the low-temperature concentrated solution outlet pipe (30) is The heat exchanger (5) communicates. 8. An absorption air-conditioning system according to item 1 of the scope of the patent application, characterized in that the refrigerant water pan (23) of the condenser (3) passes through the refrigerant water outlet pipe (28) and the hair dryer (7). The refrigerant water tank (34) is in communication, and the other end of the condenser heat exchanger tube (24) of the condenser (3) is in communication with the absorber heat exchanger tube (38) of the absorber (6) through the cooling water pipe (40). 9. An absorption air-conditioning system according to item 丨 in the scope of an applied patent, which is characterized in that a solution overflow pipe (62), a solution inlet (63), and a temperature of the solution liquid level device (12) are generated. The device (1) is in communication, the solution overflow pipe (62) is about higher than the solution liquid level, and the solution inlet pipe (63) is at the lower position of the middle layer of the solution. 1 〇 An absorption air conditioning system according to item 1 of the declared patent scope, characterized in that the concentrated solution spray pipe (33) at both ends of the absorber (6) exchanges heat with high temperature (87), The low-temperature heat exchange tube (88) is in communication, and the other end of the high-temperature heat exchange tube (87) and the low-temperature heat exchange tube (88) is connected to the solution pump (18) and the dilute solution inlet tube (81) through the dilute solution outlet tube (82). ), The filter (47), and the dilute solution tank (83) are connected. U · An absorption air-conditioning system according to item 1 of the scope of the patent application, characterized in that the evaporator heat exchanger tube (36) _ end of the evaporator and the air-conditioning water inlet 1 (90), the air-conditioning water pump (19), Air conditioning water inlet pipe (91), filter (48), 17 1242629 Air conditioning water inlet pipe. III (92) connected The other end is connected to the air conditioning water outlet pipe (93). An absorption air-conditioning system as described in the item, which is characterized in that the cold hemp dish (37) _ is passed through the cold wealth ㈣π (74) ^ agent water pump (20), refrigerant water man pipe (39) and refrigerant water tank (Μ) ) Communication, on the other hand, through the refrigerant water outlet pipe 1 (73), the refrigerant liquid level device (⑴, the refrigerant water return pipe (76) under the plate r ηπ \ ^) /, the lower body (27) Internal cavity communication, coolant liquid level (13)的下端通過冷劑旁通閥(乃)、冷劑液回管(94) 與稀溶液槽(83 )連通。 13=據中請專利範圍第1項所述的—種吸收式空調系統,其特 徵在於旁通閥(95)兩端與空調水入管ΠΙ(92),空調水出 管(93)連通。 14·根射請專利範圍第1項所述的-種吸收式空調系統,其特 徵在於/合液再生益(77) _端通過貯氣室抽氣閥(Μ )與自 才氣農置(11 )連通,另一端通過溶液閥()與稀溶液 出管(82)連通。The lower end of (13) communicates with the dilute solution tank (83) through a refrigerant bypass valve (i.e.,) and a refrigerant liquid return pipe (94). 13 = According to item 1 of the patent scope, an absorption air-conditioning system, characterized in that both ends of the bypass valve (95) communicate with the air-conditioning water inlet pipe (II) and the air-conditioning water outlet pipe (93). 14. · A kind of absorption air-conditioning system as described in item 1 of the patent scope, which is characterized by / heli regeneration (77) _ end through the air chamber exhaust valve (M) and Zicai Farm (11 ), And the other end communicates with the dilute solution outlet pipe (82) through the solution valve (). 1818
TW093101409A 2004-01-19 2004-01-19 Absorption-type air conditioner system TWI242629B (en)

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