200525122 坎、發明說明： 【發明所屬之技術領域】 本發明涉及-種用漠化鐘溶液作吸收劑，以 5 10 15 劑的空調，呈I#菩扣駚接,為表々 主體。-體疋才曰體積小、結構緊凑的—種吸收式空調 【先前技術】 傳統的吸收式空調的高溫發生器爲獨立㈣體 發生器與冷凝器爲-個筒體，蒸發器與吸收器爲一個； 體’南、低溫熱交換器置於它們之外，這樣各筒體的焊縫 多’對外泄漏的機率大，真空度相應較低熱傳導的 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 夕真工狀1、好’熱傳導的熱損失小的一種吸收式空調主 體。 本發明的設計方案^，它主要由上筒體和下筒體組 成’上筒體和下筒體之間用溶液管盒罩、冷劑水管、冷卻 水e、制熱瘵汽管連接，溶液管盒罩内有兩根濃溶液管和 兩根稀溶液管，上筒體由高溫發生器（簡稱高發，下同）、 2〇 低溫發生器（簡稱低發，下同）、冷凝器組成，高發與低 發由尚發與低發間隔板丨、丨丨隔開，高發上面有低發，低 發上面有冷凝器，高發與低發之間，低發與冷凝器之間均 有非金屬隔熱層，下筒體由板式熱交換器、蒸發器、吸收 器組成，板式熱交換器在下筒體上部，蒸發器和吸收器在 200525122 板式熱交換器下面，蒸發器在下筒體中部，吸收器在蒸發 器週邊，冷凝器、低發、蒸發器、吸收器的換熱管均爲螺 旋形銅管。 【實施方式】 5 下面結合附圖對本發明加以詳細說明。 實施例： 參見圖1，本發明它主要由上筒體24和下筒體21組 成，上筒體24和下筒體21之間用溶液管盒罩23、冷劑水 管22、冷卻水管7、制熱蒸汽管5連接，溶液管盒罩^ 1〇 内有兩根濃溶液管和兩根稀溶液管，上筒體24由高發4、 低發2、冷凝器1組成，高發4與低發2由高發與低發間 隔板135、高發與低發間隔板1133隔開，高發彳上有低發 2’低發2上有冷凝器i，高發4與低發2之間，低發之與 冷凝器1之間均有非金屬隔熱層34，下筒體21由板式熱 15交換器8、蒸發器1G、吸收器Π組成，板式熱交換器8 在下同體24上部’蒸發器1〇和吸收器u在板式熱交換 器8下面’蒸發器10在下筒體21中部吸收器^在塞 發器10週邊’冷凝器卜低發2、_ 10、吸收器η 的換熱官30、39、6卜73均爲螺旋形銅管。 2〇 參見圖卜圖2、圖3、圖8、圖U、圖17,冷凝器i 由冷凝器換熱管30、冷凝押38細a 人t 7坑價d8組成，冷凝器換熱管3〇置 於冷凝槽38内，冷卻水出口管28通向冷卻器，冷卻水入 口管、29Λ冷卻水^ 7及吸收器11的冷卻水出口管74相 、7 U的劑水25通過冷劑水出管μ、冷劑水管 200525122 2 2與蒸發器10的冷劑水一次入管6 4相通。 參見圖1、圖4、圖5、圖6、圖7、圖8,低發2由 低發蒸汽入管37、低發前蒸汽室48、低發管板42、低發 換熱管39、低發後水室43、低發壓差毛細管31、低發濃 5 溶液出盒44、低發隔板45、濃溶液出管27、稀溶液入管 46組成，低發蒸汽入管37 —端與低發前蒸汽室48相通， 另一端處在高發的上部的高發蒸汽腔内，低發蒸汽入管37 入口下設置高發擋液板41，低發換熱管39兩端與低發管 板42固接，並分別與低發前蒸汽室48、低發後水室43相 10 通，低發隔板45將低發濃溶液出盒44與稀溶液入管46 隔開，低發壓差毛細管31連通低發後水室43與冷凝器1， 濃溶液出管27經板式熱交換器8與吸收器11的低發濃溶 液入管81相通，稀溶液入管4 6與稀溶液管8 2相通。 參見圖1、圖9、圖10、圖11，高發4由高發爐膛55、 15 高發煙管管板60、高發煙管59、波紋片56、高發稀溶液 入管52、高發濃溶液盒53、高發濃溶液入管58、高發濃 溶液出管57、平衡管51及高發制熱蒸汽管50組成，高發 4底部爲錐面鍋底形，高發煙管管板60在左側及後部形成 高發爐膛55及後封頭，在前、後方固定高發煙管59束， 20 在高發煙管59束内置有波紋片56，高發稀溶液入管52 — 端接板式熱交換器8稀溶液出端，高發稀溶液入管52另 一端進入高發煙管59上方，高發濃溶液盒53在高發爐膛 55另一側，高發濃溶液入管58貼近高發4的底部，使濃 溶液進入高發濃溶液盒53，高發濃溶液出管57經板式熱 200525122 交換器8與吸收器U的高發濃溶液入管8〇相通平衡管 51 —端與咼發濃溶液盒53相通，另一端通向高發蒸汽腔， 高發制熱蒸汽管50連通高發蒸汽腔及制熱裝置。 5 10 15 參見圖卜圖…圖^圖…蒸發器^由蒸㈣ 換熱管61、冷劑水喷淋管66、外擋液罩67、内擋水罩68、 側擋液擋水板69、水盤7卜冷劑水一次入管=、冷劑水 二次入管65組成，冷劑水二次入管65與冷劑水噴淋66 相通’水盤中的冷劑水72由冷劑水出f 83進入冷劑 士二次入管65’冷劑水—次人管64與冷劑水管Μ及冷凝 器，1的冷劑水出管49相通，它們的喷口均處在蒸發器換 熱管61之上，在冷劑水噴淋管66外側至可罩蓋墓發哭換 熱管的有内擋水罩68，蒸發器換熱管61外側_撞液 擋水板69，内擋水罩68外側有外擋液罩67，水盤η處 在蒸發器換歸61下面，其水盤71邊沿處在側擋液撞水 板69中間。 士見圖卜圖15、圖16、圖17,吸收器11ώ吸收器 換熱管73、吸收器溶液喷淋f 77、撐液罩76、冷卻水入 口管75、冷卻水出口 #74组成，吸收器換熱管73上方有 吸收器溶液噴淋管77，吸收器溶液喷淋管77與低發濃溶 液入管8卜高發濃溶液人㈣相通，低發濃溶液入管8卜 馬發濃溶液入管80與板式熱交換器8的濃溶液出管相 通’在吸收器溶液噴淋管77外側至可罩蓋 73的有擋液罩76,冷卻水入口其7ς *人 … , 〜部水入口官75與冷卻器出管相通， 冷部水出π官74與冷卻水管7、冷凝器}的冷卻水入口管 20 200525122 29相通。 本發明的工作過程是··參見圖1、圖9、圖1 〇、圖11， 高發4的高發爐膛55的熱源燃燒到12〇〇°c時，將在高發 煙官59、高發爐膛55周圍的由板式熱交換器8經高發稀 溶液入管52的稀溶液加熱到158°C，溶液沸騰，産生大量 水蒸A ’爲防止溶液進入低發蒸汽入管3 7，高發播液板 41隔阻溶液濺入，同時煙氣從高發煙管59經波紋片56緩 ίο 15 忮排出，這時57%的稀溶液被濃縮到μ%，沈入高發4錐 面鍋底，由高發濃溶液入管58進入板式熱交換器8參與 換熱，進入吸收器Π參與喷淋；參見圖4、圖8，高發4 産生的大I水蒸汽經由低發蒸汽入管37進入低發2的低 發換熱官39，將管外的稀溶液加熱到9〇〇c，溶液産生的 低發冷劑蒸汽及經低發壓差毛細管31的高發冷劑蒸汽進 入冷减為1 ’釋放熱量後被冷凝爲水，57%的稀溶液被濃縮 到63%再次經濃溶液出；g； 27進人板式熱交換器8參與換 熱，進入吸收器11參與噴淋；參見圖丨、圖8、圖14，從 吸收器η冷卻水出口管74、經冷卻水管7到冷卻水入口管 29的冷卻水流經冷凝器換熱f 3()，將管外的水蒸汽冷凝 爲水’把低發2的熱量由冷卻水經冷卻水出口 # 28帶入 冷卻器，而冷凝水作爲製冷杳，丨由；人亦丨 衣〜^甶冷劑水出管49，經冷劑水 管22、冷劑水一次入管64谁入咳欢口。 進入療^斋10進行製冷；參見 圖1、圖14，從空調系統來的14°c 63進入蒸發器換熱管61，被冷凝p 水一次入管64、水盤71的冷劑水 空調水經空調水入口管 1的4°C冷劑水由冷劑 72經冷劑水二次入管 20 200525122 T向蒸發器換熱管61嘴淋，蒸發器換熱管61㈣空調水 ^降概至7C，經空調出水管62進入空調系統的風機換 …吕冷刈水獲得空调系統的熱量，變成水蒸汽被吸收器 ^吸收’·參見圖卜圖17，濃度63%、溫度37。(：的溴化鋰 々液具有極強的吸收水蒸汽的能力，從板式熱交換器8的 =洛液經吸收器溶液喷淋管77向吸收器換熱管Μ喷淋， §匕及收了蒸發為1 〇的水蒸汽後，溫度上升，濃度變稀， 從冷卻器來的經冷卻水人口管75進人吸收器換熱管73的 冷卻水將溶液吸收來的熱量帶走，而變稀爲57%的溶液則 1〇 被溶液泵19經板式熱交換器8進行熱交換，分別送到高 毛4低發2加溫濃縮。以上過程，由此不斷迴圈，來維 繫空調的正常運行。 本發明的優點是： 1、 突破了傳統的吸收式空調的結構，冷凝器1、低發 15 2、同發4在一個筒體内，高發4上有低發2，低發2上有 4綾斋1，對外泄漏大幅度降低，上筒體24只有一條長焊 縫，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，高發4溫度最高，低發2的溫度第二，冷 凝器1的溫度最低，冷凝器1、低發2、蒸發器10和吸收 -〇 器11的換熱官均採用螺旋形銅管，熱傳導效率高； 2、 上筒體24的高發4與低發2、低發2與冷凝器1 之間都有非金屬隔熱層34 ; 3、 低發2的水蒸汽凝結成水以後進入冷凝器1，其壓 差非常大’用很長的螺旋形低發壓差毛細管31增加阻力 200525122 進入冷凝器，以調節低發2與冷凝器之間的壓力； 4 '高發4的濃溶液出、稀溶液入，低發2的稀溶液 出、濃溶液入的結構能使溶液高進、高出，液位非常穩定， 既能保證高發煙管59不被燒壞，也不會使上筒體24被燒 5 壞，更不會出現溶液過濃和過稀的狀況，能保證每根高發 煙管59充分換熱； 5、 高發4有偏心的高發爐膛55，有後封頭可使煙氣 經高發煙管59,而高發4的底部有像鍋底的錐度，能有效 地使濃溶液與稀溶液分離，濃溶液可從鍋底取出，平衡管 10 51能將濃溶液中的氣體排出到高發蒸汽腔中，高發擋液板 41此隔阻沸騰的溶液濺入低發蒸汽入管3 7内； 6、 蒸發器10和吸收器U分別有内擋水罩⑽、擋液 罩76,蒸發器1〇還有外擋液罩67,這樣可確保冷劑水喷 不出去，同時外面的溶液也進不來，同時在蒸發器1〇和 15 吸收器11之間有側擋液擋水板69,吸收器u的溶液也無 法進到蒸發器10中來，溶液不會污染冷劑水，保障系統 製冷； 7、 板式熱交換器8處在下筒體21内，吸收器u的 濃溶液入和稀溶液出的四根管子都在下筒體2ι内，即使 2〇 彳少量泄漏也不會影響整個系統的真空度，同時在上筒體 24、下筒體21之間有四根溶液管道處在溶液管盒罩^的 包圍之中，溶液管盒罩23便於焊接； 8、上筒體24、下筒體21及溶液管盒草㈣縫少， 能滿足南度真空的要求。 200525122 本發明由於結構緊湊、體積小，焊縫少、真空度高， 冷凝器1、低發2、蒸發器10和吸收器11的換熱管（30、 39、61、73)，均採用螺旋形銅管，其熱傳導效率高。 【圖式簡單說明】 5 圖1爲本發明系統示意圖； 圖2爲本發明上筒體低發、冷凝器外殼示意圖； 圖3爲圖2A-A剖面示意圖； 圖4爲圖3B-B剖面示意圖； 圖5爲圖4C-C剖面示意圖； 10 圖6爲圖5D-D剖面示意圖； 圖7爲圖5E-E剖面示意圖； 圖8爲圖5F-F剖面示意圖； 圖9爲本發明上筒體高發透視示意圖； 圖10爲圖9俯視透視示意圖； 15 圖11爲圖10G-G剖面示意圖； 圖12爲本發明下筒體蒸發器換熱管示意圖； 圖13爲本發明下筒體蒸發器俯視透視示意圖； 圖14爲圖13H-H剖面示意圖； 圖15爲本發明下筒體吸收器換熱管示意圖； 20 圖16爲圖15俯視透視示意圖；及 圖17爲圖16I-I剖面示意圖。 200525122 【圖式之主要元件代表符號說明】 I 一冷凝器 2—低發 3 一溶液 4一高發 5—制熱蒸汽管 6 一冷熱切換閥 7— 冷卻水管 8— 板式熱交換器 9一空調水管 10 —蒸發器 II 一吸收器 12— 水盤 13— 冷劑旁通閥 14一冷卻水泵 15—空調水泵 16 —篩檢程式 17—冷劑泵 18 —薛檢程式 19一溶液泵 20—溶液 21 —下筒體 22— 冷劑水管 23— 溶液管盒罩 24— 上筒體 25— 冷劑水 26— 低發、冷凝器外殼 27— 濃溶液出管 28— 冷卻水出口管 29— 冷卻水入口管 30 —冷凝器換熱管 31— 低發壓差毛細管 32— 冷劑水出擋罩 33— 高發與低發間隔板II 34 —非金屬隔熱層 35—高發與低發間隔板I 36一冷凝換熱管支板 37 —低發蒸汽入管 38— 冷凝槽 39— 低發換熱管 40— 冷凝器管板 41 一高發擋液板 42— 低發管板 43— 低發後水室 44一低發濃溶液出盒， 45— 低發隔板 46— 稀溶液入管200525122 Description of the invention: [Technical field to which the invention belongs] The present invention relates to a kind of air conditioner using a desertification bell solution as an absorbent, 5 10 15 doses, and it is presented as I # bamboo buckle as the main body of the watch. -The body is small and compact—a kind of absorption air conditioner [Previous technology] The high temperature generator of the traditional absorption air conditioner is an independent body generator and the condenser is a cylinder, the evaporator and the absorber It is a body; the south and low temperature heat exchangers are placed outside them, so that the welds of each cylinder are more likely to leak to the outside, and the degree of vacuum is relatively low, and the heat conduction is relatively large. [Summary of the Invention] The object of the present invention is to provide an absorption air-conditioning main body with a very compact structure and an external welded seam 1. It's good. The design scheme of the present invention is mainly composed of an upper cylinder and a lower cylinder. The upper cylinder and the lower cylinder are connected with a solution tube box cover, a refrigerant water pipe, a cooling water e, and a heating steam tube. There are two concentrated solution tubes and two dilute solution tubes in the tube box cover. The upper cylinder is composed of a high temperature generator (referred to as high-fabrication, the same below), a 20 low-temperature generator (referred to as low-fabrication, the same below), and a condenser. High hair and low hair are separated by Shangfa and low hair spacers 丨, 丨 丨, high hair has low hair, low hair has condenser, high hair and low hair, low hair and condenser are non-metal Insulation layer, the lower cylinder is composed of a plate heat exchanger, an evaporator, and an absorber. The plate heat exchanger is above the lower cylinder. The evaporator and absorber are under the 200525122 plate heat exchanger. The evaporator is in the middle of the lower cylinder. The evaporator is around the evaporator, and the heat exchanger tubes of the condenser, low temperature generator, evaporator and absorber are spiral copper tubes. [Embodiment] 5 The present invention will be described in detail below with reference to the drawings. Embodiment: Referring to FIG. 1, the present invention is mainly composed of an upper cylinder 24 and a lower cylinder 21. A solution tube box cover 23, a coolant water pipe 22, and a cooling water pipe 7 are arranged between the upper cylinder 24 and the lower cylinder 21. The heating steam tube 5 is connected, and the solution tube box cover ^ 10 contains two concentrated solution tubes and two dilute solution tubes. The upper cylinder 24 is composed of high hair 4, low hair 2, and condenser 1, high hair 4 and low hair. 2 is separated by a high hair and low hair spacer plate 135, a high hair and low hair spacer plate 1133, low hair on the high hair 2 'low hair 2 has a condenser i, high hair 4 and low hair 2 between, low hair and There is a non-metal heat insulation layer 34 between the condensers 1, and the lower cylinder 21 is composed of a plate heat exchanger 15, an evaporator 1G, and an absorber Π. The plate heat exchanger 8 is above the same body 24 as the evaporator 1. And the absorber u under the plate heat exchanger 8 'the evaporator 10 is in the middle of the lower cylinder 21 the absorber ^ is around the plugging device 10' the condenser is a low temperature 2, 10, the heat exchangers 30, 39 of the absorber η 6 and 73 are spiral copper pipes. 20 Refer to Figure 2, Figure 3, Figure 8, Figure 8, Figure U, Figure 17, condenser i is composed of condenser heat exchange tube 30, condensing charge 38 fine a person t 7 pit price d8, condenser heat exchange tube 30 In the condensation tank 38, the cooling water outlet pipe 28 leads to the cooler. The cooling water inlet pipe, 29Λ cooling water ^ 7, and the cooling water outlet pipe 74 of the absorber 11 and the 7U agent water 25 pass through the refrigerant water outlet pipe. The refrigerant water pipe 200525122 22 is in communication with the refrigerant water inlet pipe 64 of the evaporator 10 at one time. Referring to Fig. 1, Fig. 4, Fig. 5, Fig. 6, Fig. 7, and Fig. 8, low-generation 2 consists of low-generation steam inlet pipe 37, low-generation steam chamber 48, low-generation tube plate 42, low-generation heat exchange tube 39, and low-generation Back water chamber 43, low pressure differential capillary 31, low hair concentration 5 solution outlet box 44, low hair separator 45, concentrated solution outlet tube 27, dilute solution inlet tube 46, low hair vapor inlet tube 37-end and before low hair The steam chamber 48 is in communication, and the other end is located in the high-temperature steam chamber at the upper part of the high-frequency generator. A low-frequency steam inlet plate 37 is provided under the inlet of the high-frequency shield 41. Both ends of the low-frequency heat exchange tube 39 are fixedly connected to the low-frequency tube plate 42 and are It communicates with the steam chamber 48 before the low hair and the water chamber 43 after the low hair. The low hair partition 45 separates the low hair concentrated solution exit box 44 from the dilute solution inlet pipe 46. The low hair pressure differential capillary 31 communicates with the low hair water. The chamber 43 communicates with the condenser 1 and the concentrated solution outlet pipe 27 communicates with the low-intensity concentrated solution inlet pipe 81 of the absorber 11 through the plate heat exchanger 8 and the dilute solution inlet pipe 46 communicates with the dilute solution pipe 82. Referring to FIG. 1, FIG. 9, FIG. 10, and FIG. 11, Gaofa 4 consists of Gao Furnace 55, 15 Gao Fu tube sheet 60, Gao Fu 59, corrugated sheet 56, Gao Di dilute solution inlet tube 52, Gao concentrated solution box 53, Gao concentrated solution It consists of an inlet pipe 58, a high-concentration solution outlet pipe 57, a balance pipe 51, and a high-fat heating steam pipe 50. The bottom of the high-fat 4 is a cone-shaped bottom of the pot. The high-fume pipe tube sheet 60 forms a high-fat furnace chamber 55 and a rear head on the left and rear. 59 bundles of high-smoke pipes are fixed at the front and rear. 20 The high-smoke pipes 59 have a built-in corrugated sheet 56, and the high-temperature dilute solution inlet pipe 52 is terminated at the end of the plate heat exchanger 8 dilute solution. The other end of the high-temperature dilute solution inlet pipe 52 enters the high-smoke pipe 59. Above, the high concentration solution box 53 is on the other side of the high temperature furnace 55. The high concentration solution inlet pipe 58 is close to the bottom of the high concentration solution 4, so that the concentrated solution enters the high concentration solution box 53. The high concentration solution outlet tube 57 passes the plate heat 200525122 exchanger 8 and The high-intensity solution inlet pipe 80 of the absorber U communicates with the balance tube 51 at one end and communicates with the high-concentration solution box 53 at the other end, and the high-end steam heating tube 50 communicates with the high-temperature steam cavity and the heating device. 5 10 15 See the figure ... Picture ^ Picture ... Evaporator ^ By steaming heat exchange pipe 61, coolant water spray pipe 66, outer liquid shield 67, inner water shield 68, side liquid shield 69, The water pan 7 is composed of the refrigerant water primary inlet pipe =, the refrigerant water secondary inlet pipe 65, and the refrigerant water secondary inlet pipe 65 communicates with the refrigerant water spray 66. The refrigerant water 72 in the water pan is entered by the refrigerant water f 83. Refrigerant secondary inlet pipe 65 'refrigerant water-secondary pipe 64 communicates with the refrigerant water pipe M and the condenser, and the refrigerant water outlet pipe 49 communicates with each other, and their nozzles are all located above the evaporator heat exchange pipe 61. There is an inner water shield 68 on the outside of the refrigerant water spray pipe 66 to cover the tomb crying heat exchange pipe, the outer side of the evaporator heat exchange pipe 61 _ collision liquid flap 69, and the outer water shield 68 has an outer liquid shield 67. The water pan η is under the evaporator replacement 61, and the edge of the water pan 71 is in the middle of the side liquid-impacting water plate 69. Figure 15, Figure 16, Figure 17, absorber 11 absorber heat exchanger tube 73, absorber solution spray f 77, liquid support hood 76, cooling water inlet pipe 75, cooling water outlet # 74, absorber Above the heat exchange tube 73, there is an absorber solution spraying pipe 77. The absorber solution spraying pipe 77 communicates with the low-intensity solution inlet tube 8 and the high-intensity solution inlet tube. The low-intensity solution inlet tube 8 and the Bima-rich solution inlet tube 80 are connected to the plate. The concentrated solution outlet pipe of the heat exchanger 8 is connected to the outside of the absorber solution spraying pipe 77 to a liquid blocking cover 76 which can cover the cover 73. The cooling water inlet is 7 persons., ~ ~ Water inlet officer 75 and the cooler The outlet pipes communicate with each other, and the cold part water outlet π and 74 are in communication with the cooling water pipes 7 and the cooling water inlet pipes 20 200525122 29 of the condenser. The working process of the present invention is as shown in FIG. 1, FIG. 9, FIG. 10, and FIG. 11. When the heat source of the high-temperature furnace 55 of the high-temperature furnace 4 is burned to 1200 ° C., it will be around the high-temperature furnace 59 and the high-temperature furnace 55. The dilute solution of the plate heat exchanger 8 through the high-intensity dilute solution inlet tube 52 is heated to 158 ° C, and the solution is boiled to generate a large amount of water vapor. At the same time, the flue gas is slowly discharged from the high smoke pipe 59 through the corrugated sheet 56. At this time, 57% of the dilute solution is concentrated to μ%, sinking into the bottom of the high-fat 4 cone surface, and the high-concentration solution enters the pipe 58 into the plate heat exchange. Heater 8 participates in heat exchange and enters the absorber Π to participate in the shower; see Figures 4 and 8; the large I water vapor generated by Gaofa 4 enters the low-heat heat exchanger 39 of Low-fat 2 through the low-heat steam inlet pipe 37, The dilute solution was heated to 900 ° C. The low-temperature refrigerant vapor produced by the solution and the high-temperature refrigerant vapor passing through the low-pressure differential capillary 31 entered the cold reduction to 1 'and were condensed into water after releasing heat. The solution was concentrated to 63% and re-exported through the concentrated solution; g; 27 into the plate heat exchanger 8 to participate The heat enters the absorber 11 to participate in the shower; see FIG. 丨, FIG. 8 and FIG. 14, the cooling water from the cooling water outlet pipe 74 of the absorber η, the cooling water pipe 7 to the cooling water inlet pipe 29 flows through the condenser to exchange heat f 3 (), The water vapor outside the tube is condensed into water. The heat of low heat 2 is brought from the cooling water to the cooler through the cooling water outlet # 28, and the condensed water is used as a cooling unit. The refrigerant water outlet pipe 49 passes through the refrigerant water pipe 22, and the refrigerant water enters the pipe 64 once. Enter the therapy room 10 for refrigeration; see Figure 1 and Figure 14, 14 ° c 63 from the air conditioning system enters the evaporator heat exchanger tube 61, and the condensed water enters the pipe 64 once, and the refrigerant water from the water pan 71 is conditioned by the air conditioning water. The 4 ° C refrigerant water in the inlet pipe 1 flows from the refrigerant 72 through the refrigerant water to the secondary pipe 20 200525122 T. The evaporator heat exchanger tube 61 is sprayed to the mouth of the evaporator, and the evaporator heat exchanger tube 61㈣air-conditioning water is reduced to 7C. 62 Fans entering the air-conditioning system are replaced ... Lu Leng's water obtains the heat from the air-conditioning system and becomes water vapor absorbed by the absorber ^ See Fig. 17, concentration 63%, temperature 37. (: Lithium bromide mash has a strong ability to absorb water vapor, spraying from the Luo liquid of the plate heat exchanger 8 through the absorber solution spraying pipe 77 to the absorber heat-exchanging tube M, After 10% water vapor, the temperature rises and the concentration becomes thinner. The cooling water from the cooler passing through the cooling water pipe 75 into the absorber heat exchange pipe 73 takes away the heat absorbed by the solution and becomes 57% thinner. The solution 10 is heat-exchanged by the solution pump 19 through the plate heat exchanger 8 and sent to the high-hair 4 low-heat 2 and heated and concentrated. The above process is continuously looped to maintain the normal operation of the air conditioner. The advantages are: 1. Breakthrough the structure of traditional absorption air conditioner, condenser 1, low hair 15 2, same hair 4 in a tube, high hair 4 with low hair 2, low hair 2 with 4 fast 1. The external leakage is greatly reduced. The upper cylinder 24 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 temperature of high temperature 4 is the highest, and the temperature of low temperature 2 is the second. Condenser 1 has the lowest temperature, Condenser 1, Low temperature 2, Evaporator 10 The heat exchangers of the absorber 11 are all made of spiral copper tubes, which have high heat conduction efficiency; 2. There is a non-metal heat insulation layer between the high and low hairs 2 and 2 of the upper cylinder 24 and the condenser 1 34; 3. The water vapor of low temperature 2 condenses into water and enters condenser 1. The pressure difference is very large. Use a long spiral low pressure differential capillary 31 to increase the resistance 200525122 into the condenser to adjust the low temperature 2 and The pressure between the condensers; 4 'high-fat 4 concentrated solution out, dilute solution in, low-fat 2 dilute solution out, concentrated solution in structure can make the solution high in and high out, and the liquid level is very stable, which can guarantee The high smoke pipe 59 will not be burned out, nor will the upper cylinder 24 be burned. 5 The solution will not be too thick and too thin, which can ensure that each high smoke pipe 59 has sufficient heat exchange. The eccentric high-temperature furnace 55 has a back cover to allow the smoke to pass through the high-temperature pipe 59, and the bottom of the high-temperature 4 has a taper like the bottom of the pot, which can effectively separate the concentrated solution from the dilute solution. The concentrated solution can be taken out from the bottom of the pot, and the balance tube 10 51 can discharge the gas in the concentrated solution into the high-temperature steam chamber, and the high-frequency liquid baffle 41 The barrier boiling solution is splashed into the low-temperature steam inlet pipe 37. 6. The evaporator 10 and the absorber U have an inner water shield ⑽, a liquid shield 76, an evaporator 10 and an outer liquid shield 67, respectively. It can ensure that the refrigerant water cannot be sprayed out, and the solution from the outside cannot come in at the same time. At the same time, there is a side liquid blocking plate 69 between the evaporator 10 and the absorber 11, and the solution of the absorber u cannot enter the evaporation. Since the solution comes from the device 10, the solution will not contaminate the refrigerant water to ensure the cooling of the system. 7. The plate heat exchanger 8 is located in the lower tube 21, and the four tubes of the concentrated solution inlet and the dilute solution of the absorber u are in the lower tube. In the body 2m, even a small leakage of 20 彳 will not affect the vacuum of the entire system. At the same time, there are four solution pipes between the upper cylinder 24 and the lower cylinder 21 surrounded by the solution tube box cover. The solution tube box cover 23 is convenient for welding; 8. The upper tube body 24, the lower tube body 21, and the solution tube box have less quilting, which can meet the requirements of the southern vacuum. 200525122 Due to its compact structure, small volume, few welds, and high vacuum, the heat exchanger tubes (30, 39, 61, 73) of condenser 1, low emission 2, evaporator 10, and absorber 11 all adopt a spiral shape Copper tubes have high heat transfer efficiency. [Brief description of the drawings] 5 FIG. 1 is a schematic diagram of the system of the present invention; FIG. 2 is a schematic diagram of the upper cylinder of the present invention with a low temperature and a condenser shell; FIG. 3 is a schematic diagram of a cross-section of FIG. 2A-A; Figure 5 is a schematic sectional view of Figure 4C-C; 10 Figure 6 is a schematic sectional view of Figure 5D-D; Figure 7 is a schematic sectional view of Figure 5E-E; Figure 8 is a schematic sectional view of Figure 5F-F; Figure 9 is the upper cylinder of the present invention High perspective perspective diagram; Figure 10 is a top perspective view of Figure 9; 15 Figure 11 is a schematic sectional view of Figure 10G-G; Figure 12 is a schematic diagram of the heat exchanger tube of the lower barrel evaporator of the present invention; Figure 13 is a top perspective view of the lower barrel evaporator of the present invention 14 is a schematic sectional view of FIG. 13H-H; FIG. 15 is a schematic view of the heat exchange tube of the lower cylinder absorber of the present invention; 20 FIG. 16 is a schematic perspective view of the top view of FIG. 15; and FIG. 17 is a schematic sectional view of FIG. 16I-I. 200525122 [Description of the main symbols of the diagram] I-Condenser 2-Low temperature 3-Solution 4-High temperature 5-Heating steam pipe 6-Hot and cold switching valve 7-Cooling water pipe 8-Plate heat exchanger 9-Air conditioning water pipe 10 — Evaporator II — Absorber 12 — Water tray 13 — Refrigerant bypass valve 14 — Cooling water pump 15 — Air conditioning water pump 16 — Screening program 17 — Refrigerant pump 18 — Xue check program 19 — Solution pump 20 — Solution 21 — Lower tube 22—Refrigerant water pipe 23—Solution tube box cover 24— Upper tube 25—Refrigerant water 26—Low temperature, condenser shell 27—Concentrated solution outlet tube 28—Cooling water outlet tube 29—Cooling water inlet tube 30—Condenser heat exchange tube 31—Low pressure differential capillary 32—Coolant water outlet shield 33—High and low hair spacer plate II 34—Non-metal insulation layer 35—High and low hair spacer plate I 36—Condensation change Heat pipe support plate 37—low-temperature steam inlet pipe 38—condensation tank 39—low-temperature heat exchange tube 40—condenser tube plate 41—high-temperature baffle plate 42—low-temperature tube plate 43—low-temperature water chamber 44—low-temperature solution Out of the box, 45—low hair partition 46—dilute solution into the tube
12 200525122 47— 低發折流板 48— 低發前蒸汽室 49一冷劑水出管 50—高發制熱蒸汽管 51 —平衡管 52— 高發稀溶液入管 53— 高發濃溶液盒 54— 高發外筒體 55— 高發爐膛 56— 波紋片 57— 高發濃溶液出管 58— 高發濃溶液入管 59— 高發煙管 60— 高發煙管管板 61 —蒸發器換熱管 62— 空調水出口管 63— 空調水入口管 64一冷劑水一次入管 65—冷劑水二次入管 66一冷劑水噴淋管 67— 外擋液罩 68— 内擋水罩 69 —側擔液擔水板 70— 蒸發器換熱管支板 71— 水盤 72— 冷劑水 73— 吸收器換熱管 74 —冷卻水出口管 75—冷卻水入口管 76 —擋液罩 77— 吸收器溶液喷淋管 78— 吸收器換熱管支板 79— 吸收器固定板 80— 高發濃溶液入管 81 —低發溶液入官 82— 稀溶液管 83— 冷劑水出管 1312 200525122 47— Low hair baffle 48— Low temperature steam room 49—Refrigerant water outlet tube 50—High hair heating steam tube 51—Balance tube 52—High hair dilute solution inlet tube 53—High hair concentrated solution box 54—High hair outside Cylinder 55—High furnace hearth 56—Corrugated sheet 57—High concentration solution outlet tube 58—High concentration solution inlet tube 59—High smoke tube 60—High smoke tube tube sheet 61—Evaporator heat exchange tube 62—Air conditioner water outlet tube 63—Air conditioner water inlet Tube 64—Coolant water primary inlet tube 65—Refrigerant water secondary inlet tube 66—Coolant water spray tube 67—Outer liquid hood 68—Inner water hood 69—Side liquid carrying water plate 70—Evaporator heat exchange tube Support plate 71—water tray 72—refrigerant water 73—absorber heat exchange pipe 74—cooling water outlet pipe 75—cooling water inlet pipe 76—liquid shield 77—absorber solution spray pipe 78—absorber heat exchange pipe support plate 79 — Absorber fixing plate 80—High-intensity solution inlet tube 81—Low-intensity solution inlet tube 82—Dilute solution tube 83—Refrigerant water outlet tube 13