經濟部中央標準局員工消費合作社印製 A7 B7 ____ 五、發明説明（1 ) 發明背景 發明領域 本發明係一種空調機之熱循環，尤係一種熱循環結構 ，使用一種氫氟碳化物（HF C )基之冷媒取代習知有害 之氟碳化合物基之冷媒。 習知技術說明 近來，有關含一空調機之熱循環所有之冷媒，已廣泛 使用氫氟碳化物（H FJL )基之冷媒取代習知含C ( 氟氯碳化物）之有害化物，尤從環保觀點，如同溫厝 之臭氧層破壊。使用H F C基冷媒之熱循環採用各 ，如用於熱循環中一壓縮機所用之冷凍機械油，考 慮冷媒特性。酯基潤滑油之特例可如Japan Sun Oi 1銷售 之 HAF 56D1 或 SL — 68。 另一方面，已知一冷凍循環具一乾燥器用於與上述 H F C基冷媒不同之習知氟碳化物基之冷媒，如日本新型 公告昭55 — 2678 (1980)號揭示，其中提供可 由習知有害多私|物蓬媒除去水分；^燥^可防止因水 分凍結於冷。此冷凍周期亦具有 一乾燥器充滿一乾燥劑於一凝結器及一降壓單元（毛細管 )間以吸收冷凍循環中水分。此外，通常一冷凍用冷 凍循_罗中冷媒流速g 。 但以上習知技術具以下問題。 本紙張尺度適用中國國家標準（《：阳）八4規格（21〇\ 297公瘦） - * ' ί I - It I - - Ι^ϋ - -I I HI ^ii (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消费合作社印製 A7 ____ B7 __ 五、發明説明（2 ) 首先，不同於與習知冷媒一起使用之輝_ϋΐϋ，使以 上H 熱循環所用之迪因水 解，產生易腐蝕含以上熱循環中壓縮機機械部分之酸，降 低含壓縮機之機械部可靠性。 /-^ 另一方面，以上日本新型公告昭5 5 — 2 6 7 8號指 出熱循環中因冷媒水分凍題；但其未教授使用以上 H F C之熱循環中所用酯基潤題。尤其’此文件 未了解酯基潤滑油（如Japan Sun Oil銷售之HAF 5 6 D 1或SL - 6 8)與冷媒中水分氧化，其貌良防止此現 皂。 尤其，構冷熱式(:空之熱循環中，通過一降壓單元 ___ 、.·Γ々 後，分成液體及氣成分之冷媒如雙相位流體流動’因此冷 媒之流速更髙，與以上文件所示f凍#之冷凍循環不同。 例如，冷凍器中冷媒之流率約爲2 k g/h ;然而’本發 明之冷熱空調機之熱循環中冷媒流率約5 0至1 5 0 k g / h。 若此具高速度之雙相位（液/氣）流體進入一乾燥器 ，乾燥器中合粒焚動並以相 互碰擦而碎成細粉。合成沸石之碎片及/或粉末經熱循環 移至壓縮機，破壤其可動部，因而降低壓縮機可靠性’一 用於四向閥之控制部因此流動控制之零件隨時間劣化° 發明概述 因此，爲解決以上問題，本發明目的提供一種空調機 本紙張尺度適用中國國家標準（CNS > Λ4規格（210X 297公釐） -^ϋ i^— ^^1 : d^i tn^i mi ml -1 -I ^^^1 im J. ，^. i (請先閲讀背面之注意事項再填寫本頁) -5 - 305920 A7 B7 五、發明説明（3 ) 的熱循環，使用，HF C，可由所用冷媒除去水分（脫水） ’以防止冷媒中所含酯基潤滑油因水而氧化，因而解決因 潤滑油氧化致含壓縮機之機械部於熱循環中腐蝕降低可靠 性之問題；即使當冷媒於熱循環中高速流動時乾燥劑於乾 燥器中發生碎片及/或粉末之情況亦可防止，因而防止因 乾燥劑成碎片及/或粉末使含壓縮機之熱循環隨時間劣化 或降低可靠性之問題。 圖式簡要說明 圖1顯示一熱循環用於本發明空調機之實施例系統圖A7 B7 ____ printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of the invention (1) Background of the invention Field of the invention The present invention is a thermal cycle of an air conditioner, especially a thermal cycle structure, using a hydrofluorocarbon (HF C) ) Based refrigerant to replace the conventional harmful fluorocarbon based refrigerant. Known technical description Recently, with regard to all refrigerants containing a heat cycle of an air conditioner, hydrofluorocarbon (H FJL) based refrigerants have been widely used to replace the conventional harmful substances containing C (fluorochlorocarbide), especially from environmental protection The point of view is like the warming of the ozone layer. The H F C-based refrigerant is used for the thermal cycle, such as the refrigeration mechanical oil used in a compressor in the thermal cycle, considering the characteristics of the refrigerant. Special examples of ester-based lubricants can be HAF 56D1 or SL-68 sold by Japan Sun Oi 1. On the other hand, it is known that a refrigeration cycle has a dryer for conventional fluorocarbon-based refrigerants different from the above-mentioned HFC-based refrigerants, as disclosed in Japanese New Publication No. Sho 55-2678 (1980), which provides a harmful Multi-private | Wu Peng media removes moisture; ^ dryness ^ can prevent freezing due to moisture. This freezing cycle also has a dryer filled with a desiccant between a condenser and a pressure-reducing unit (capillary) to absorb moisture in the freezing cycle. In addition, usually a refrigeration cycle for freezing-Luozhong refrigerant flow rate g. However, the above conventional techniques have the following problems. The size of this paper is in accordance with Chinese National Standard (《： 阳） 八 4 号 （21〇 \ 297 公 瘦）-* 'ί I-It I--Ι ^ ϋ--II HI ^ ii (Please read the notes on the back first (Fill in this page again) A7 ____ B7 __ printed by the Employees ’Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy V. Description of the invention (2) First, it is different from the glow used with conventional refrigerants _ ϋll ϋ, which is used for the above heat cycle. Hydrolysis produces acids that easily corrode the mechanical parts of the compressor in the above thermal cycle, reducing the reliability of the mechanical parts containing the compressor. /-^ On the other hand, the above-mentioned Japanese New Announcement No. 5 5-2 6 7 8 pointed out the problem of freezing of refrigerant moisture in the thermal cycle; however, it did not teach the ester-based moisturizing problem used in the thermal cycle of the above H F C. In particular, this document does not understand the oxidation of moisture in ester-based lubricants (such as HAF 5 6 D 1 or SL-6 8 sold by Japan Sun Oil) and the refrigerant, and its good appearance prevents this soap. In particular, the structured cooling and heating type (: in the empty thermal cycle, after passing through a pressure-reducing unit ___,. · Γ々, the refrigerant, which is divided into liquid and gas components, such as a two-phase fluid flows, so the flow rate of the refrigerant is higher, and the above The freezing cycle of f # is different. For example, the flow rate of the refrigerant in the freezer is about 2 kg / h; however, the flow rate of the refrigerant in the thermal cycle of the cold and hot air conditioner of the present invention is about 50 to 150 kg / h. If the high-speed dual-phase (liquid / gas) fluid enters a dryer, the pellets in the dryer are incinerated and crushed into fine powder by rubbing against each other. The fragments and / or powder of the synthetic zeolite undergo thermal cycling Move to the compressor, breaking its movable part, thus reducing the reliability of the compressor.-The control part for the four-way valve therefore the flow control parts deteriorate over time. SUMMARY OF THE INVENTION Therefore, in order to solve the above problems, the purpose of the present invention is to provide a The paper size of the air conditioner is applicable to the Chinese National Standard (CNS> Λ4 specification (210X 297 mm)-^ ϋ i ^ — ^^ 1: d ^ i tn ^ i mi ml -1 -I ^^^ 1 im J. , ^. I (please read the precautions on the back before filling in this page) -5-305920 A7 B7 5. Invention Description (3) Thermal cycle, use, HF C, can remove moisture (dehydration) from the refrigerant used to prevent the oxidation of the ester-based lubricating oil contained in the refrigerant due to water, thus solving the mechanical part containing the compressor due to oxidation of the lubricating oil Corrosion reduces the problem of reliability in the thermal cycle; even when the refrigerant flows at high speed in the thermal cycle, the occurrence of debris and / or powder in the desiccant can be prevented, thus preventing the debris from becoming debris and / or powder The problem of deteriorating the thermal cycle including the compressor over time or reducing reliability. Brief description of the drawings FIG. 1 shows a system diagram of an embodiment of a thermal cycle used in the air conditioner of the present invention
I 圖2顯示一熱循環用於習知空調機之系統圖以供比較I Figure 2 shows a system diagram of a thermal cycle used in conventional air conditioners for comparison
I 圖3顯示冷媒流動於一通用乾燥器中之速度圖表； 圖4(a)及4(b)顯示另一實施例之熱循環用於 本發明熱循環；及 »3 5顯示再一實施例之熱循環用於本發明空調機。 本發明由以下較佳實施例說明可完全了解。 較佳實施例說明 以下參考附圖說明本發明· (實施例1 ) 參考圖1本發明一實施例，數字1代表一壓縮機；2 本紙張尺度適用中國國家鮮（CNS ) A4规格（210X 297公釐） 1^1 nn In ml - I - nn n^— mt nn ^ J J^、v* (請先閏讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 -6 _ 經濟部t央標準局員工消費合作社印袋 A7 B7五、發明説明（4 ) 爲一四向閥：3爲一室外側熱交換器：4爲一降壓單元（ 如擴張閥）：5 ，9爲叉管（分支機構）；6 ，7爲連接 管，形成二流道用以分開冷媒於二部分一段距離於叉管5 ，9間；6 a，7 a分別位於連接管6 ，7中之毛細管以 如所需降壓；8爲一乾燥器位於熱循環6側之流道中； 1 Oa，1 Ob，1 1 a，1 lb爲冷媒管線之接頭； 12爲一室內側熱交換器。數字13代表乾燥器8中合成 沸石，其中含顆粒直徑1至2mm之多孔材料，且平均孔 尺寸成爲2. 8至3. 3A範圍：數字14代爲一彈簧， 供與合成沸石1 3緊密塡入多孔板中間隙。 圖2顯示用於習知空調機之習知熱循環系統圖，與本 發明熱循環比較，習知熱循環缺乏叉管5 ，9及旁通乾燥 器8之連接管7。圖1及2 ，相同數字代表相似部件，實 線箭頭及虛線箭頭分別代表冷媒冷卻及加熱時之流向。 圖3顯示乾燥器8柱筒部中流動之冷媒，條件爲冷媒 流率定爲5 0 kg/h (冷媒R— 2 2 )，乾燥器8柱筒 部內徑定爲2 5mm。此圖中，橫座檫爲乾燥度'， 縱座標爲冷媒之流速Αν# (m/s)。 首先，參考圖1說明冷卻操作。首先以壓縮機1壓縮 冷媒。高溫及高壓之冷媒於實線箭頭方向流動至室外側熱 交換器3 ，經過四向閥2。冷媒於室外側熱交換器3與室 外空氣熱交換而凝結液化。以擴張閥4將液化之冷媒減壓 成液/氣混合冷媒（乾燥度或氣質X，代表相對總量所含 氣體部分約0 . 2 )。液/氣混合冷媒由叉管5分開而至- „ ------訂--..----^ I (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準（CNS ) A4規格（210X 297公釐） 經濟部中央橾準局員工消費合作社印製 A7 ___ B7__ 五、發明説明（5 ) 連接管6 ，7。此時，連接管6 ，7因彼此內徑'"d*1及 長度 ％ ，乃興管 6， 7中液/氣混合冷媒分支^率。 關於液/氣混合冷媒，低流速之液體冷媒以其重力作 用通過連接管6 ’並流過乾燥器8中合成沸石1 3。因此 ，以合成沸石1 3除去冷凍循環中水分》此外，液/氣混 合冷媒之氣體冷媒流動於連接管7中。液體冷媒通過乾燥 器8後與通過連接管7後之氣體冷媒合併於叉管9。如此 混合之冷媒抵至室內側熱交換器1 2 ’並與室內空氣熱交 換而因室內側熱交換器1 2蒸發。蒸發潛熱乃冷卻室內空 間。 此處圖2所示習知熱循環中，因乾燥器8中流動之冷 媒乾燥度或氣質'X#約爲0. 2 ’根據圖3，冷媒速度 約爲0. 2m/s。若乾燥器位於擴張閥4前，冷媒處於 液態（乾燥度或氣質ιχ"爲0)，因此，根據圓3，乾 燥器8中流動之冷媒速度爲0. 〇25m/s。 圖1實施例之冷凍循環中，乾燥器8中流動之冷媒速 度決定於連接管6 ，7之流阻。以下公式指出連接管6 ， 7中流動之冷媒流率：I Figure 3 shows the velocity chart of the refrigerant flowing in a universal dryer; Figures 4 (a) and 4 (b) show another embodiment of the thermal cycle used in the thermal cycle of the present invention; and »3 5 shows yet another embodiment The thermal cycle is used in the air conditioner of the present invention. The invention can be fully understood from the following description of preferred embodiments. DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the drawings. (Embodiment 1) Referring to FIG. 1, an embodiment of the present invention, the number 1 represents a compressor; 2 The paper size is applicable to China National Fresh (CNS) A4 specification (210X 297 Mm) 1 ^ 1 nn In ml-I-nn n ^ — mt nn ^ JJ ^, v * (please read the notes on the back before filling this page) Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs-6 _ Printed bags A7 B7 of the Employee Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of invention (4) is a four-way valve: 3 is an outdoor side heat exchanger: 4 is a pressure-reducing unit (such as an expansion valve): 5, 9 is a fork pipe (branch); 6, 7 is a connecting pipe, forming a two-channel to separate the refrigerant in the two parts at a distance from the fork pipe 5, 9; 6 a, 7 a are located in the connecting pipe 6, 7 respectively The capillary tube is depressurized as required; 8 is a dryer located in the flow channel on the 6 side of the thermal cycle; 1 Oa, 1 Ob, 1 1 a, and 1 lb are the connectors of the refrigerant line; 12 is an indoor side heat exchanger. The number 13 represents the synthetic zeolite in the dryer 8, which contains a porous material with a particle diameter of 1 to 2 mm, and the average pore size becomes the range of 2.8 to 3.3 A: the number 14 is a spring for supplying the synthetic zeolite 13 Into the gap in the perforated plate. Fig. 2 shows a diagram of a conventional thermal cycle system used in a conventional air conditioner. Compared with the thermal cycle of the present invention, the conventional thermal cycle lacks the fork tubes 5, 9 and the connecting tube 7 of the bypass dryer 8. In Figures 1 and 2, the same numbers represent similar parts, and the solid arrows and dotted arrows represent the flow direction of the refrigerant during cooling and heating, respectively. Figure 3 shows the refrigerant flowing in the cylinder part of the dryer 8 under the condition that the refrigerant flow rate is set at 50 kg / h (refrigerant R 2 2) and the inner diameter of the cylinder part of the dryer 8 is set at 25 mm. In this figure, the horizontal sassafras is the dryness', and the vertical coordinate is the refrigerant flow rate Αν # (m / s). First, the cooling operation will be described with reference to FIG. First, the compressor 1 compresses the refrigerant. The high-temperature and high-pressure refrigerant flows to the outdoor heat exchanger 3 in the direction of the solid arrow and passes through the four-way valve 2. The refrigerant exchanges heat with the outdoor air in the outdoor heat exchanger 3 to condense and liquefy. The expansion valve 4 is used to decompress the liquefied refrigerant into a liquid / gas mixed refrigerant (dryness or gas quality X, which represents the relative total amount of gas contained in about 0.2). The liquid / gas mixed refrigerant is separated from the fork tube 5 to-"------ order --..---- ^ I (please read the precautions on the back before filling in this page) Standard (CNS) A4 specification (210X 297 mm) A7 ___ B7__ printed by the Employee Consumer Cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs 5. Description of the invention (5) Connecting pipes 6, 7, At this time, connecting pipes 6, 7 are due to each other The diameter 'D'1 and the length% are the branching rate of the liquid / gas mixed refrigerant in the Xing pipe 6, 7. With regard to the liquid / gas mixed refrigerant, the liquid refrigerant with low flow rate flows through the connecting pipe 6' by its gravity The zeolite 13 is synthesized in the dryer 8. Therefore, the synthetic zeolite 13 is used to remove water in the refrigeration cycle. In addition, the gas refrigerant of the liquid / gas mixed refrigerant flows in the connecting pipe 7. The liquid refrigerant passes through the dryer 8 and is connected The gas refrigerant after the tube 7 is merged into the fork tube 9. The refrigerant thus mixed reaches the indoor heat exchanger 12 'and exchanges heat with the indoor air to evaporate due to the indoor heat exchanger 12. The latent heat of evaporation cools the indoor space. In the conventional thermal cycle shown in FIG. 2 here, the refrigerant flowing in the dryer 8 Dryness or temperament 'X # is about 0.2' According to Figure 3, the refrigerant speed is about 0.2m / s. If the dryer is located before the expansion valve 4, the refrigerant is in a liquid state (dryness or temperament ιχ " is 0), so According to circle 3, the speed of the refrigerant flowing in the dryer 8 is 0.02 m / s. In the refrigeration cycle of the embodiment of FIG. 1, the speed of the refrigerant flowing in the dryer 8 is determined by the flow resistance of the connecting pipes 6, 7. The following The formula indicates the flow rate of the refrigerant flowing in the connecting pipes 6 and 7:
Dp = A · r * i/d5* G2 (1)Dp = A · r * i / d5 * G2 (1)
Dp爲叉管5及9間壓力差；A爲摩擦係數：r爲流動液 體及/或氣體之比重；β爲管長；d爲管之內徑；G爲流 率。 假設冷媒流率爲5 0 k g/h ;乾燥度或氣質（X) 本紙張尺度適用中國國家標準（CNS ) Μ規格（210 X 297公釐Ί ' -8 ~ I ί— I -- .^ϋ —^1 I^' --- i— —^― — I- -li ...... —I -- I (請先閱讀背面之注意事項再填寫本頁) 3〇592〇 A7 B7 五、發明説明（6 ) ^__, 爲0. 2 ;連接管6中流動之厗體媒流率爲4 0 k g/ h ;連接管6中流動之冷媒流率爲10kg/h;液 體冷媒比重爲1 1 3 0 k g/m3;氣體冷媒之比重爲 66kg/m3;連接管6 ，7內徑彼此相間。如此，連 接管6，7間長度比（$7/ $β)根據公式（1)約爲 1/3。使用如此長度比之連接管6 ’ 7，液體冷媒可於 0. 02m/s之低速流動於乾燥器8中》 此處亦可假設液/氣混合冷媒（乾燥度或氣質 爲0. 2)流動於連接管6，7中，未由叉舌5分開液/ 氣混合冷媒成液體冷媒及氣體冷媒。然而如此，爲設定流 動於乾燥器8中液/氣混合冷媒速度爲約0. 025m/ s ，即爲流動於乾燥器8中液體冷媒速度，假設連接管6 ，7內徑彼此相同，根據公式（1)連接管6，7間長度 比（約爲1/4 9。此長度比適用實際設備。 因此較佳爲含叉管5及9之結構以分開液氣體。 加熱時流動於虛線方向之冷媒因室內熱交換器1 2而 液化’並由叉管9分開。冷媒分支部分由連接管6 ，7調 整之流率流動於連接管6，7中。流動於連接管6中冷媒 通過乾澡器8中合成沸石1 3，因而除去冷凍循環中水分 。如此’液體冷媒流動於連接管6 ，7中。假設連接管6 ’ 7間長度比約爲1/13 ，液體冷媒之流 率比（G7/Ge，Ge爲連接管6中流率；G7爲連接管7 中流率）約爲1 . 7/1。亦即，連接管6中流率〇8約 爲19kg/h，連接管7中流率約31kg/h。 本紙張尺度適用中國國家標準（CNS ) M現格（21〇χ297公釐) ~ -9 - — l·-------f .,4 — _^-----訂-------A 丨 (請先閲讀背面之注意事項再填寫本頁) 經汫部中央標準局員工消费合作杜印製 經 部 中 央 揉 準 員 工 消 費 合 作 杜 印 製 A7 B7 五、發明説明 ( 7 ) 1 因 此 » 液 體 冷 媒 以 0 0 1 m / S 之 低 速 流 動 於 乾 燥 器 8 1 I 中 〇 1 I 此 實 施 例 中 t 加 熱 及 冷 卻 時 > 流 動 於 乾 燥 器 8 中 液 體 1 \ 冷 媒 速 度 定 爲 0 0 2 5 m / S 以 下 0 如 此 可 防 止 乾 燥 器 請 先 1 8 中 合 成 沸 石 1 3 顆 粒 破 裂 保 持 壓 縮 機 1 可 靠 性 〇 阅 ik 背 1 L 具 有 — 乾 燥 器 之 空 調 機 之 熱 循 環 尤 適 用 冷 凍 循 環 使 用 之 注 1 I 意 1 | Η F C 冷 媒 ( Η F C — 3 2 Η F C — 1 2 5 Η F C — 事 1 '1 1 3 4 a 等 ) 以 取 代 冷 媒 R 一 2 2 ( Η C F C — 2 2 ) 填 寫 1 0 理 由 如 下 0 —· 酯 基 油 作 爲 使 用 Η F C 基 冷 媒 之 冷 凍 循 環 本 頁 1 I 中 壓 縮 機 1 所 用 冷 凍 機 油 引 起 與 水 分 水 解 產 生 酸 易 腐 1 1 * 独 壓 縮 機 1 機 械 部 分 降 低 壓 縮 機 1 可 靠 性 〇 因 此 爲 除 1 1 去 冷 凍 循 rga 壞 中 水 分 乾 燥 器 填 有 主 要 /nr： 撕 法 吸 收 Η F C 基 之 1 訂 冷 媒 之 合 成 沸 石 1 3 ( 如 Η F C — 3 2 之 分 子 直 徑 爲 1 1 3 2 A ; Η F C — 1 2 5 之 分 子 直 徑 爲 4 2 A ; 而 1 | Η F C — 1 3 4 a 分 子 直 徑 爲 4 2 A ) 但 主 要 可 吸 水 1 I ( 分 子 直 徑 爲 2 8 A ) 〇 1 合 成 沸 石 1 3 顆 粒 尤 爲 有 效 其 中 平 均 孔 大 小 介 於 1 1 2 8 至 3 * 2 A 9 此 外 合 成 沸 石 1 3 顆 粒 中 孔 尺 寸 變 1 1 異 亦 如 以 上 界 定 者 最 有 效 〇 1 1 合 成 沸 石 基 本 化 學 式 如 下 1 | Μ 2 / n〇 Α ί 1 2 0 3 _ X S 〇 2 • Υ Η 2〇 ((c 1 ) Μ 爲 金 屬 陽 離 子 9 η 歸 爲 價 位 0 合 成 m 石 主 要 含 鉀 I 爲 金 屬 陽 離 子 > 如 Vn i 〇 η SHOWA銷售之Μ 〇 1 ec u 1 a r She a v e s X Η — 1 0 C 〇 - I I 本紙張尺度適用中國國家標準（CNS> A4規格（210X 297公釐） A7 B7 經濟部中央標準局員工消費合作社印裝 五、發明説明（8 ) 1 1 ( 實 施 例 2 ) 1 I 圖 4 ( a ) 及 4 ( b ) 顯 示 具 有 乾 燥 器 之 空 調 機 之 熱 1 1 I 循 環 > 爲 本 發 明 另 一 實 施 例 t 其 中 4 ( a ) 爲 基 本 部 分 系 請 先 統 圖 > 圖 4 ( b ) 爲 由 圖 4 ( a ) 箭 頭 方 向 觀 察 之 放 大 截 閲 背 面 圚 〇 此 ΓΒ1 m 中 i 與 前 例 同 之 部 件 以 相 同 數 字 表 示 0 此 外 » 面 1 I * 1 1 圖 4 ( a ) » 4 ( b ) 主 要 顯 示 — 分 配 器 熱 循 環 其 他 部 事 項 1 I 分 ( 未 HHI1 圖 示 ) 與 圖 1 者 同 0 再 填 寫 本 1 人 -- 分 配 器 1 5 可 降 低 部 件 數 以 低 成 本 達 成 圖 1 前 述 實 頁 1 I 施 例 相 同 功 效 〇 1 1 1 具 圖 4 ( a ) 及 4 ( b ) 所 示 乾 燥 器 之 熱 循 環 中 使 1 1 用 分 配 器 1 5 爲 分 支 機 稱 〇 分 配 器 1 5 包 含 上 及 下 件 7 P 1 訂 9 6 P 以 分 隔 分 配 器 1 5 內 部 並 保 持 分 隔 部 分 相 通 一 1 1 連 接 埠 1 5 a 連 接 至 降 壓 單 元 4 其 位 於 上 下 件 7 P 1 Ί 6 P 間 一 連 接 埠 1 5 d 相 通 於 乾 燥 器 8 側 之 連 接 管 6 * 1 I 其 位 於 下 件 6 P 側 分 配 器 1 5 端 一 連 接 埠 1 5 d 連 接 至 1 J·|—k*·. 1 室 內 側 熱 交 換 器 1 2 側 一 冷 凍 循 環 管 其 位 於 上 件 7 P 側 1 1 分 配 器 1 5 另 一 端 及 一 合 併 埠 1 5 C 併 入 乾 燥 器 8 側 連 1 1 接 管 6 其 位 於 上 件 7 P 與 連 接 墙 1 5 d 間 中 部 〇 上 下 件 1 1 7 P 及 6 P 具 相 通 孔 7 h 6 h 以 分 別 調 整 連 接 管 中 流 動 1 I 之 冷 媒 流 率 0 I 尤 其 上 件 7 P 於 中 央 具 相 通 孔 7 h 賦 予 由 連 接 埠 1 I 1 5 a 位 擴 張 閥 4 進 入 分 配 器 1 5 之 液 / 氣 混 合 冷 媒 —· 定 之 流 阻 » 而 允 許 氣 體 冷 媒 流 動 於 分 配 器 1 5 之 合 併 埠 1 5 1 本紙浪尺度適用中國國家標準（CNS ) A4規格（210X 297公釐） -11 - A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明（ 9 ) 1 C 及 連 接 埠 1 5 d 中 0 另 方 向 * 下 件 6 P 於 中 央 具 相 通 1 I 孔 6 h 以 賦 予 液 / 氣 混 合 冷 媒 — 定 流 阻 ， 以 允 許 液 體 冷 媒 1 1 流 動 於 分 配 器 1 5 之 連 接 埠 1 5 b 及 連 接 管 6 中 〇 1 流 動 於 連 接 管 6 中 之 冷 媒 通 1® 乾 燥 器 8 中 合 成 沸 石 请 先 1 4 以 除 去 冷 凍 循 環 中 水 分 ， 如 1 PI 園 1 例 所 示 〇 閱 讀 背 1 面 I 圖 4 ( a ) » 4 ( b ) 所 示 冷 凍 循 環 設 備 中 » 合 成 沸 I I 意 1 | 石 1 3 顆 粒 平 均 孔 大 小 設 定 » 液 體 冷 媒 流 動 於 乾 燥 器 8 中 事 XS 1 I 之 調 整 及 冷 凍 循 環 設 備 之 功 效 與 9B 1 前 例 同 0 再 填 1 一 寫 本 頁 取 1 I ( 實 施 例 3 ) 1 1 I 圖 5 爲 具 一 乾 燥 器 之 空 調 機 之 熱 循 環 系 統 圖 根 據 本 1 1 發 明 另 — 實 施 例 此 圖 中 以 相 同 數 字 代 表 與 第 — 例 對 應 者 訂 1 不 再 赘 述 其 說 明 0 圚 5 所 示 例 中 一 乾 燥 器 位 於 冷 凍 循 1 環 一 部 分 其 中 冷 卻 時 壓 力 很 高 0 換 言 之 用 以 分 開 冷 媒 1 | 於 一 定 範 圍 經 過 二 叉 管 5 9 之 二 連 接 晋 6 7 置 於 — 降 1 I 壓 單 元 4 與 一 室 外 側 熱 交 換 器 3 間 乾 燥 器 8 位 於 連 接 管 1 6 側 〇 1 1 冷 卻 時 冷 媒 流 動 於 實 線 箭 頭 所 示 方 向 因 室 外 側 熱 交 1 1 換 器 液 化 » 並 由 叉 管 5 分 開 9 冷 媒 然 後 流 動 於 高 流 阻 之 連 1 1 接 管 6 > 7 中 t 以 連 接 Αι¥·τ 営 6 9 7 調 節 流 率 〇 此 時 液 體 冷 1 媒 低 速 流 動 於 乾 燥 器 8 中 〇 .1 加 熱 時 冷 媒 流 動 於 虛 線 箭 頭 方 向 > 受 室 內 側 熱 交 換 器 ! 1 I 1 2 液 化 1 由 一 降 壓 單 元 ( 擴 張 閥 ) 4 降 壓 成 液 / 氣 混 合 冷 媒 0 液 / 氣 混 合 冷 媒 由 叉 管 9 分 開 > 液 體 冷 媒 流 動 於 連 1 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） -12 - 經濟部中央標準局員工消費合作社印製 A7 _______B7 五、發明説明（10 ) 接管6中，而氣體冷媒流動於連接管7中，即藉由圖1前 例所述連接管6 ，7之流阻。 圖5所示熱循環中，合成沸石1 3平均孔大小設定， 液體冷媒流動於乾燥器8中調整，及冷凍循環設備之功效 與圖1前例同。 雖未圖示，圖5實例中熱循環具有一乾燥器8於冷凍 循環一部分，其中冷卻時壓力變高，當然可具圖4分配器 1 5以降低成本" 如上述，根據本發明，提供之熱循環尤適用具乾燥器 之空調機，，防止 器 中合成沸多{，因而防止壓縮機 受合成沸石碎或__粉^.褒藉以提高壓縮機可靠性。 此外，根據本發明，提供之熱循環具有使用H F C基 冷媒之乾燥器，包含一壓縮機，一四向閥，一室外側熱交 換器，及彼此連接部件之管線，特徵在於用以分開冷媒於 一特定長度經過分支機構之流道位於降壓單元與室內側熱 交換器間；及一乾澡器充滿主_$含1^ 陽離子之合成 '沸石之乾燥流道之一。 此外，根據本發明，合成沸石顆粒包含多孔性，平均 孔大小介於2 . 8至3 . 2 A。 再者’根據本發明，較佳地二流道使用一叉管爲分支 機構將冷媒分成液體冷媒及氣體冷媒，利用二連接管形成 二流道率，使液體冷媒主要流過;具 乾燥器之流道。 本紙張尺度適用中國國家標準（CNS ) Λ4規格（210X 297公釐） ^ ·: ^ 冬 I ^-----訂------^ I (請先閱讀背面之注意事項再填寫本頁) 13 - Α7 Β7 ^〇S92〇 五、發明説明（11 ) 以上技術機構可防止合成沸石於/乾，即使 乾燥器中冷媒流數費JI，並消除由冷媒作用引起合成沸石 移動。尤其，就雙相位（液/氣）流體之冷媒高速流動時 ，可提供一流道旁通乾燥器而低速流動於乾燥器中。 - .......—^ ----- 換言之，以下技術機構功效如下： 提供一流道旁通一乾澡器，及一流道確定流動於乾燥 器側及旁通側冷媒..分nig間比Μ，即具流阻供液體流動 於乾燥器中之流道，通過降壓單元前後於乾燥器中流動之 Γ 液體冷媒流率定爲允許合成沸石破成粉末之數值以下。如 此可防止合成沸石於乾燥器中破裂，提高壓縮機可靠性。 (請先閱讀背面之注意事項再填寫本頁) 笨. 訂 經濟部中央標準局員工消費合作杜印製 本紙張尺度適用中國國家標準（CNS ) Α4規格（210X2W公釐）Dp is the pressure difference between the fork tubes 5 and 9; A is the friction coefficient: r is the specific gravity of the flowing liquid and / or gas; β is the tube length; d is the inner diameter of the tube; G is the flow rate. Assuming that the refrigerant flow rate is 50 kg / h; dryness or temperament (X) This paper scale applies the Chinese National Standard (CNS) Μ specification (210 X 297 mm Ί '-8 ~ I ί— I-. ^ Ϋ — ^ 1 I ^ '--- i— — ^ ― — I- -li ...... —I-I (Please read the precautions on the back before filling this page) 3〇592〇A7 B7 5 , Description of the invention (6) ^ __, is 0.2; the flow rate of the medium flowing in the connecting pipe 6 is 40 kg / h; the flow rate of the refrigerant flowing in the connecting pipe 6 is 10kg / h; the specific gravity of the liquid refrigerant is 1 1 3 0 kg / m3; the specific gravity of the gas refrigerant is 66kg / m3; the inner diameters of the connecting pipes 6 and 7 are spaced from each other. Thus, the length ratio between the connecting pipes 6 and 7 ($ 7 / $ β) is approximately according to formula (1) 1/3. Using the connecting tube 6'7 with this length ratio, the liquid refrigerant can flow in the dryer 8 at a low speed of 0.02m / s. Here, it can also be assumed that the liquid / gas mixed refrigerant (dryness or temperament is 0 2) Flowing through the connecting pipes 6 and 7, the liquid / gas mixed refrigerant is not separated into the liquid refrigerant and the gas refrigerant by the prongs 5. However, in order to set the speed of the liquid / gas mixed refrigerant flowing in the dryer 8 to about 0 . 025m / s, which is the liquid flowing in the dryer 8 Refrigerant speed, assuming that the inner diameters of the connecting pipes 6, 7 are the same as each other, according to the formula (1), the length ratio between the connecting pipes 6, 7 (approximately 1/4 9. This length ratio applies to actual equipment. Therefore, it is preferable to include the fork pipe 5 And 9 are structured to separate liquid gas. The refrigerant flowing in the dashed direction during heating is liquefied by the indoor heat exchanger 12 and is separated by the fork tube 9. The refrigerant branch part is flowed through the connection by the flow rate adjusted by the connecting tubes 6 and 7. In pipes 6, 7. The refrigerant flowing in the connecting pipe 6 passes through the dry bath 8 to synthesize zeolite 13 and thus removes the water in the refrigeration cycle. Thus, the 'liquid refrigerant flows in the connecting pipes 6, 7. Assuming the connecting pipe 6' 7 The length-to-length ratio is about 1/13, and the flow rate ratio of the liquid refrigerant (G7 / Ge, Ge is the flow rate in the connecting pipe 6; G7 is the flow rate in the connecting pipe 7) is about 1.7 / 1. That is, the connecting pipe 6 The mid-flow rate is about 19kg / h, and the mid-flow rate is about 31kg / h in the connecting tube 7. The paper size is applicable to the Chinese National Standard (CNS) M present grid (21〇 × 297mm) ~ -9--l · --- ---- f., 4 — _ ^ ----- Subscribe ------ A 丨 (please read the precautions on the back before filling this page) Employee consumption cooperation of the Central Bureau of Standards As a member of the Du Printing Department of the Ministry of Economic Development, the company ’s consumer cooperation is du printing A7 B7. 5. Description of the invention (7) 1 Therefore, the liquid refrigerant flows at a low speed of 0 0 1 m / S in the dryer 8 1 I 〇1 I this In the example, t during heating and cooling > the liquid flowing in the dryer 8 1 \ the refrigerant speed is set to 0 0 2 5 m / S below 0. This can prevent the dryer from synthesizing the zeolite in 1 8 1 3 The particles are broken and kept compressed Machine 1 Reliability 〇 Reading ik back 1 L The heat cycle of the air conditioner with-dryer is especially suitable for the use of refrigeration cycle Note 1 I Italian 1 | Η FC refrigerant (Η FC — 3 2 Η FC — 1 2 5 Η FC — Matter 1 '1 1 3 4 a etc.) to replace the refrigerant R 1 2 2 (H CFC — 2 2) Fill in 1 0 Reasons are as follows 0 — · Ester-based oil as a refrigeration cycle using HFC-based refrigerants Page 1 I Compressed Machine 1 caused by the use of refrigeration oil and moisture Hydrolysis produces acid perishable 1 1 * The unique compressor 1 mechanical part reduces the reliability of the compressor 1 so it is divided by 1 1 to defrost cycle rga bad medium moisture dryer is filled with main / nr: tearing method absorbs HF FC 1 of the set The synthetic zeolite 1 3 of the refrigerant (for example, the molecular diameter of H FC — 3 2 is 1 1 3 2 A; the molecular diameter of H FC — 1 2 5 is 4 2 A; and the molecular diameter of 1 | H FC — 1 3 4 a is 4 2 A) but mainly absorbs water 1 I (the molecular diameter is 2 8 A) 〇1 synthetic zeolite 1 3 particles are particularly effective. The average pore size is between 1 1 2 8 and 3 * 2 A 9 In addition, synthetic zeolite 1 3 particles The change in mesopore size 1 1 is also the most effective as defined above. The basic chemical formula of synthetic zeolite is as follows 1 | Μ 2 / n〇Α ί 1 2 0 3 _ XS 〇2 • Υ Η 2〇 ((c 1) Μ It is a metal cation 9 η is classified as a valence of 0. Synthesis m Stone mainly contains potassium I is a metal Cation > such as Μ 〇1 ec u 1 ar She aves X Η-1 0 C 〇- II sold by Vn i 〇η SHOWA This paper size is applicable to Chinese national standards (CNS> A4 specifications (210X 297 mm) A7 B7 economy Printed by the Ministry of Standards and Staff Consumer Cooperatives V. Description of Invention (8) 1 1 (Example 2) 1 I Figure 4 (a) and 4 (b) shows the heat of the air conditioner with dryer 1 1 I cycle> It is another embodiment of the invention t where 4 (a) is the basic part, please make a drawing first> FIG. 4 (b) is an enlarged view of the back side view from the arrow direction of FIG. 4 (a). This ΓΒ1 m in i Parts that are the same as the previous example are represented by the same number 0. In addition »Surface 1 I * 1 1 Figure 4 (a)» 4 (b) Main display — Distributor thermal cycle other matters 1 I points (not shown in HHI1) and Figure 1 If it is the same as 0, then fill in this 1 person-Distributor 1 5 can reduce the number of parts to Achieving low cost Figure 1 The same effect as in the previous page 1 I Example 〇1 1 1 With the heat cycle of the dryer shown in Figures 4 (a) and 4 (b), let 1 1 be the distributor 1 5 for the branch machine. Distributor 1 5 contains upper and lower parts 7 P 1 Order 9 6 P to separate the inside of the distributor 1 5 and keep the partition part connected to one 1 1 Port 1 5 a Connected to the pressure reducing unit 4 It is located on the upper and lower parts 7 P 1 Ί 6 P one port 1 5 d connects to the connecting pipe 6 on the 8 side of the dryer 6 * 1 I which is located in the lower part 6 P side distributor 1 5 end one port 1 5 d connects to 1 J · | —k * · . 1 indoor side heat exchanger 1 2 side a refrigerating cycle pipe located on the upper part 7 P side 1 1 distributor 1 5 the other end and a merge port 1 5 C merged into the dryer 8 side connection 1 1 takeover 6 it is located on the top Part 7 P and the middle of the connecting wall for 15 d. Upper and lower parts 1 1 7 P and 6 P have through holes 7 h 6 h to adjust the flow of the connecting pipe 1 I's refrigerant flow rate 0 I Especially the upper part 7 P has a through hole 7 h in the center to give the liquid / gas mixed refrigerant from the port 1 I 1 5 a position expansion valve 4 into the distributor 1 5 · fixed flow resistance » The gas refrigerant is allowed to flow through the merger port of the distributor 1 5 1 The paper wave scale is applicable to the Chinese National Standard (CNS) A4 specification (210X 297 mm) -11-A7 B7 Printed by the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 1. Description of the invention (9) 1 C and port 1 5 d in the other direction 0 The lower part 6 P has a communication in the center 1 I hole 6 h to give the liquid / gas mixed refrigerant a constant flow resistance to allow the liquid refrigerant 1 1 Flow through the port 1 5 b of the distributor 1 5 b and the connection tube 6 〇1 Flow through the connection tube 6 Refrigerant pass 1® Dryer 8 Synthesize the zeolite in the first 1 4 to remove the water in the refrigeration cycle, such as 1 PI 1 example of a garden. Reading 1 Face I Figure 4 (a) »4 (b) shown in the refrigeration cycle equipment» Synthetic Boiling II Italian 1 | Stone 1 3 Particle average pore size setting »Liquid refrigerant flowing in the dryer 8 Adjustment and freezing of XS 1 I The function of the circulation device is the same as the previous example of 9B 1 0 and then fill in 1 Write this page and take 1 I (Example 3) 1 1 I Figure 5 is a diagram of the thermal cycle system of the air conditioner with a dryer according to this 1 1 invention and another- Example In this figure, the same number represents the same as the first example. Order 1 will not repeat its description. 0 圚 5 In the example shown, a dryer is located in a part of the freezing cycle 1 and the pressure during cooling is very high. In other words, it is used to separate the refrigerant. | Within a certain range, through a bifurcated tube 5 9 bis connected to Jin 6 7 placed-drop 1 I pressure unit 4 and an outdoor side heat exchanger 3 between the dryer 8 is located on the side of the connecting tube 1 6 〇1 1 Refrigerant flows in the direction indicated by the solid arrow during cooling due to heat exchange on the outdoor side 1 1 Liquefaction of the changer »and is separated by the fork tube 5 9 Refrigerant then flows in the connection with high flow resistance 1 1 Takes over 6 &7; t Connect Αι ¥ · τ 営 6 9 7 to adjust the flow rate. At this time, the liquid cooling medium flows at a low speed in the dryer 8. The cooling medium flows in the direction of the dashed arrow during heating.> The indoor heat exchanger! 1 I 1 2 Liquefaction 1 by a pressure-reducing unit (expansion valve) 4 Pressure-reducing into liquid / gas mixed refrigerant 0 Liquid / gas mixed refrigerant is separated by the fork tube 9> Liquid refrigerant flows in the connection 1 This paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm) -12-Printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 _______B7 V. Invention description (10) Take over 6, and the gas refrigerant flows through the connecting tube 7, as shown in the previous example in FIG. 1 The flow resistance of the connecting pipes 6 and 7 is described. In the thermal cycle shown in FIG. 5, the average pore size of the synthetic zeolite 13 is set, the liquid refrigerant flow is adjusted in the dryer 8, and the function of the refrigeration cycle device is the same as the previous example in FIG. Although not shown, the thermal cycle in the example of FIG. 5 has a dryer 8 in a part of the refrigeration cycle, where the pressure becomes higher during cooling, of course, the distributor 15 of FIG. 4 can be used to reduce the cost. As mentioned above, according to the present invention, the The thermal cycle is especially suitable for air conditioners with dryers, to prevent the synthesis of more boiling in the device, thus preventing the compressor from being crushed by synthetic zeolite or __powder ^. Praise to improve the reliability of the compressor. In addition, according to the present invention, the heat cycle provided has a dryer using HFC-based refrigerant, including a compressor, a four-way valve, an outdoor heat exchanger, and a pipeline connecting components, which is characterized by A specific length of the flow channel passing through the branch is located between the pressure reduction unit and the indoor side heat exchanger; and a dry bath filled with one of the main flow channels of the synthetic zeolite containing 1 ^ cations. In addition, according to the present invention, the synthetic zeolite particles contain porosity with an average pore size ranging from 2.8 to 3.2 A. Furthermore, according to the present invention, it is preferred that the two-channel use a fork tube as a branch to divide the refrigerant into liquid refrigerant and gas refrigerant, and use the two connecting tubes to form a two-channel rate so that the liquid refrigerant mainly flows through; the flow channel with a dryer . This paper scale is applicable to China National Standard (CNS) Λ4 specification (210X 297mm) ^ ·: ^ Winter I ^ ----- order ------ ^ I (please read the precautions on the back before filling in this Page) 13-Α7 Β7 ^ 〇S92〇 V. Description of the invention (11) The above technical mechanism can prevent the synthetic zeolite from drying, even if the refrigerant flow in the dryer costs JI, and eliminates the movement of the synthetic zeolite caused by the action of the refrigerant. In particular, when the refrigerant of the two-phase (liquid / gas) fluid flows at a high speed, it can provide a first-pass bypass dryer and a low-speed flow in the dryer. -.......— ^ ----- In other words, the functions of the following technical institutions are as follows: Provide a first-rate bypass by a dry bath, and the first-rate bypass determines the flow of refrigerant on the dryer side and the bypass side .. minute nig The ratio M, that is, the flow path for the liquid to flow in the dryer, the flow rate of Γ liquid refrigerant flowing in the dryer before and after passing through the pressure reducing unit is set to a value that allows the synthetic zeolite to break into powder. This prevents the synthetic zeolite from cracking in the dryer and improves compressor reliability. (Please read the precautions on the back before filling in this page) Stupid. Ordered by the Ministry of Economic Affairs, Central Standards Bureau, employee consumption cooperation du printing. This paper standard is applicable to China National Standard (CNS) Α4 specification (210X2W mm)