TW500902B - Refrigeration system using non-azeotropic mixing refrigerants - Google Patents

Refrigeration system using non-azeotropic mixing refrigerants Download PDF

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Publication number
TW500902B
TW500902B TW90107315A TW90107315A TW500902B TW 500902 B TW500902 B TW 500902B TW 90107315 A TW90107315 A TW 90107315A TW 90107315 A TW90107315 A TW 90107315A TW 500902 B TW500902 B TW 500902B
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Taiwan
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temperature
refrigerant
compressor
low
pressure
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TW90107315A
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Chinese (zh)
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Toshio Seion
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Dairei Co Ltd
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Abstract

Disclosed is to provide a refrigerant mixture system having more than two components. Superlow temperature can be achieved by using simple refrigerator system construction. When using non-azeotropic mixing refrigerant of more than two refrigerant components, low temperature operation fluid which pass through compressor 1, condenser 2, throttling valve 4, evaporator 5 and feedback to the circulation path of said compressor can be cooled down by the operation fluid flowed between the said condenser and said throttling valve using heat exchanger 10, this cause the temperature and vapor pressure of refrigerant depressed and by using the depressed temperature and vapor pressure in the compression and condensation to make the operation pressure of refrigerator system lowered down, while to promote the refrigerant component of high vapor pressure and low boiling point to condense, liquefy. Lowering down the operation pressure of refrigerator system, meanwhile using refrigerant of high critical pressure and low critical temperature as mixing refrigerant components can easily achieve superlow temperature.

Description

500902 五、發明說明(1) 產業上之利用領绝 本發明係有關冷庾趟。 v東機早位等的冷凍系統 習知技冬好 由冷康庫 冷(flon)被廣 破壞大氣層上 体而對地球暖 象而成為不可 壞且較少溫室 又轉變成此等 著。 然而,除 滑油間之相溶 關係需具有足 要求臨界溫度 點對臨界溫度 範圍内,故欲 冷媒係有困難 溫用冷凍機用 所需的壓力亦 之架構係有困 因此,對 藉由選定其混 ^凍機用冷凍劑之優特 泛採用著,妙 规疋,雖U亂 層的臭氧芦Γέ氣之所謂的特定氟冷會 化有影塑7姓夕f,I冷係作為溫室效應氣 使用的I斜料t等氟冷即成為國際管制的對 效應等影绝的娃乃有不導致臭氧層之破 氟冷系A二的所,替代氟冷被嘗試使用著, “令、之烴系新冷凍劑的開發正被進行 使用作冷媒需為化學上藉宗曰益主以 性良好等特性::上穩疋且無毒性,與潤 夠低的標‘ 卜,與目的之冷;東劑溫度間的 需汽,妙'弗點及為在室溫環境下動作雖被 ::值C臨通Λ以絕對溫度刻度言十,標準彿 得可在官H界彿點值)係大致在〇.6〜7之 的,尤Α ^ 作大幅降低冷凍庫内部溫度之 冷凍劑二°c以下的庫内溫度之超低 鲈古私2 I界溫度需低一事相結合,液化 難的。 、出具有貫用性之新穎冷凍系統 由二個以上 合組成可調整之混合冷”而言, /弗點荨特性即被嘗試著。此500902 V. Description of the invention (1) Industrial use and leadership This invention relates to cold heading. v Tokiji ’s refrigeration system in the early stage, etc. Known skills Winter is good. From cold storage, cold (flon) has been widely destroyed by the upper body of the atmosphere, and it has become an indestructible and less greenhouse for the planet. However, in addition to the compatibility relationship between oils, the critical temperature point must be sufficient to the critical temperature range. Therefore, if the refrigerant is difficult, the pressure required for warming the refrigerator is difficult. Therefore, the The special features of the refrigerants used in its freezers are widely used. Although the U-layers of ozone are so-called specific fluorine cooling, they will be affected by the plastic film. The cooling system is the greenhouse effect. Fluoride cooling, such as I, slant, t, etc., which has become an internationally controlled effect, is a fluorine-free cooling system that does not cause the ozone layer. It is an attempt to replace fluorine cooling. The development of new refrigerants is being carried out. As a refrigerant, it needs to be borrowed from the chemical industry. The characteristics are good: it is stable, non-toxic, and low in moisture, and it is cold with purpose. The steam needs between the temperature of the agent, the magic point and the action at room temperature are: although the value of C Lintong Λ is ten on an absolute temperature scale, the standard Buddha is in the official H boundary. 〇 ~ 6 ~ 7 , Especially A ^ It is used to reduce the refrigerant temperature below 2 ° C. The internal temperature is very low. The temperature of the I world needs to be low, and it is difficult to liquefy. The novel refrigerating system with consistent usability is composed of two or more adjustable cold mixes. Nettle properties were tried. this

五、發明說明(2) :類非= Π可廣泛選擇纽成或各成分物質之 度=及彿點曲線分離並在壓力固^的條件下液化開始溫 又^曰束溫度或氣化開始溫度及氣化結束溫度不同Γ 撣力二^,在等壓下的冷凝機内氣液各相之組成變化,若 ϋ; ϊ ΐ ί充量!且提高冷卻能力•’則在保持濕潤的 统循二:⑯4發器已殘存的狀態下,即成為使冷凍機系 、、死循衣並降低冷凍機系統之效率。 又,在超低溫用冷凍機系統,至於已採用由二個以上 分而成之非共滞混合冷媒的冷凍機系統,在室溫環境 八作的冷凝器之能力由於在低沸點時臨界溫度之較低的 1之液化係較困難,乃對每一成分冷凍劑採用可使多階 叙冷凝的多元方式等。 噙添第3圖所示者為其一例’採用由沸點不同的三種類冷 \ d而成之混合冷媒’將用一台壓縮機1予以壓縮的混合 冷凍劑經由冷凝器2使其放熱後,供沸點較高沸點之第一 冷束d低的第二冷·柬劑之冷凝時使用,再供實現以第二冷 凍劑為目的之冷卻溫度的低沸點冷凍劑之冷凝時使用者, 内此等第一、第二冷凍劑係以氣液分離器6· 8予以各 並經由節流閥4予以氣化,使於熱交換器?·8冷凝成 、父低^的冷凍劑。沸點最低的第三冷凍劑係經由節流閥 溫度在蒸發器5氣化並予冷卻冷卻槽(冷凍庫)50内至目的V. Description of the invention (2): quasi-indicator = Π can be widely selected or the degree of each component substance = and the bud point curve is separated and under the condition of pressure solidification, the liquefaction start temperature and the beam temperature or gasification start temperature And the gasification end temperature is different Γ 掸 force two ^, the composition of the gas-liquid phases in the condenser under equal pressure changes, if ϋ; ϊ ΐ ΐ charge! And to improve the cooling capacity • ’In the second system of keeping the moist: In the state where the 4 hair dryers have been left, it will become a refrigerator system, and reduce the efficiency of the refrigerator system. In addition, in the ultra-low temperature refrigerator system, as for the refrigerator system that has adopted two or more non-co-hysteresis mixed refrigerants, the capacity of the condenser in the room temperature environment is eight due to the critical temperature at low boiling point. The liquefaction system with a low value of 1 is more difficult. For each component refrigerant, a multivariate method capable of condensing in multiple stages is used. Adding the one shown in Fig. 3 is an example of "using a mixed refrigerant composed of three kinds of refrigerants with different boiling points". After the mixed refrigerant compressed by a compressor 1 is passed through the condenser 2 to release heat, It is used for condensing the second cold coolant with low boiling point and the first cold bundle with higher boiling point, and it is also used by the user for the condensation of low boiling point refrigerant with cooling temperature for the purpose of the second refrigerant. Wait for the first and second refrigerants to be separated by gas-liquid separators 6 and 8 and gasified through the throttle valve 4 to be used in the heat exchanger? · 8 condensed into a low parent refrigerant. The third refrigerant with the lowest boiling point is vaporized in the evaporator 5 through a throttle valve and pre-cooled in a cooling tank (freezer) 50 to the purpose.

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f型化係無法避免的,有製造成本高漲,或维蠖作案蓉t 、 耗費維持成本,在謀求推廣之上常受限制。 發明欲解決 本發明係採用非 構成可較容易的實現 冷凍機系統。 共沸混合系冷凍劑,藉由簡單的系統 出高效率之冷凍系統,尤指超低溫用 解決課顳 本發明之 冷凍劑成分之 壓縮機、冷凝 路徑内的由蒸 冷凝器至節流 又,藉由 的低溫動作流 狀態,可有效 饋至壓縮機之 的動作流体, 低0 冷凍系統, 非共沸系混 器、節流閥 發器反饋至 閥間之動作 將冷卻由上 体,依液狀 的提.高冷卻 低溫動作流 可使來自壓 其特徵在於 合冷凍劑之 、蒸發器而 壓縮機之低 流体以促進 述蒸發器至 的高彿點成 能力,再者 体,冷卻由 縮機之動 乍 採用含 冷凍系 反饋至 溫動作 低沸點 節流閥分之不 藉由由 冷凝器 流体的 有二個統,藉 壓縮機 流体, 成分之 間之動 同使成 上述蒸 至節流 吐出壓 以上的 由經過 之循環 冷卻由 液化。 作流体 為濕潤 發器反 閥之間 力降 又’藉由使上述 界溫度在約略室溫以 凍機系統。 非共彿系混合冷媒之至少一 下,可實現出容易達成超低 成分的臨 溫度之冷The f-type system is unavoidable. There are high manufacturing costs, or maintenance costs for maintenance and repair. They are often limited in their promotion. The invention is to be solved The present invention is a refrigerator system that can be easily realized by using a non-structure. An azeotropic mixed refrigerant, through a simple system to produce a high-efficiency refrigeration system, especially a compressor for the cryogenic component of the present invention that solves the cryogenic component of the present invention, the steam condenser to the throttling in the condensation path. The low-temperature operating flow state can effectively feed the working fluid of the compressor. The low-zero refrigeration system, non-azeotropic mixer, and throttle valve send feedback to the valve. The action will be cooled from the upper body, depending on the liquid state. The high-cooling and low-temperature action flow can make the low fluid which is characterized by refrigerant, evaporator and compressor low to promote the high Buddha point of the evaporator, and the body is cooled by the shrinking machine. At first glance, there are two systems of low-boiling-point throttle valves with feedback from the refrigeration system to warm-action operation. The condenser fluid has two systems. By using the compressor fluid, the movement between the components is adjusted to the above-mentioned steaming to throttling and discharge pressure. The above is cooled by passing through the liquefaction. The working fluid is to reduce the force between the valve of the hair dryer and the freezer system by setting the above-mentioned boundary temperature to about room temperature. At least one of the non-common Buddhist mixed refrigerants can achieve the temperature of the ultra-low composition easily.

由Μ Ξ L圖^\本么明之冷凍機系統之一實施例的概念圖, 機匕予隔Λ咖非共彿系混合編^ 而、夜彳卜飢妳±妒、冷凝态2放熱並予冷卻至約略室溫為止 予以月二,2燥器3並通過節流閥4而被送入蒸發器5内 回復ί壓1 ΐ夕叙吸收冷凍庫内的熱再回復至壓縮機,惟 略体係在其穩定狀態運㈣ 置埶交旅溫度,於節流閥之間的路徑上設 4之1的曰^ 可有效的冷卻由圖中的乾燥器進入節流閥 別的化口冷凍劑並可降低溫度至室溫以下的溫度為 ^ 於此種壓縮機及蒸發 系統本身系長久以來即予 山田治夫著,養賢堂股份 10曰第7版發行,第77頁) 流出的氣体係藉由液狀的 飽和溫度以下且於其中完 内’於壓縮機及蒸發器之 ^ 然而,此等係於由單 藉由顯熱之利用並非可使 者0 器之間已設置熱交換器之冷凍機 瘙見者(例如·「冷涞及空調」 有限公司、昭和4 5 ( 1 9 7 0 )年6月 ’惟若如此進行時,則由蒸發器 高溫冷凍劑予以妥善的過冷卻至 全不夾雜殘存氣体下進入節流閥 兩者均可進行順利的運轉。 一成分而成的冷媒予以進行者, 此種冷凍機之運轉循環順利進行 ,—— 如本發明般,於由二個以上的成分% Λ、> & 4 谦会浪人、人 从刀而成之非多 >、此。》來劑,若如此進行予以有效的冷 , 奴'弗點曲綠及露點曲線由於會分離’在冷凝過程之冷浴From the M Ξ L picture ^ \ Ben Moming concept illustration of an embodiment of the freezer system, the machine tool is prepared by a mixture of non-common Buddha system ^, and the night 彳 jealous, condensed state 2 exotherm and give Cool to about room temperature and give it on the second month, 2 dryer 3 and send it to the evaporator 5 through the throttle valve 4 to restore the pressure. 1 Xi Xishu absorbs the heat in the freezer and returns it to the compressor, but the system is omitted. Set the travel temperature in its steady state, and set 1 of 4 on the path between the throttles to effectively cool the refrigerant entering the other port of the throttle from the dryer in the figure and Lowering the temperature to below room temperature is ^ This compressor and the evaporation system itself has been written by Haruyamada for a long time, issued by Yakendo Co., Ltd. 10th, 7th edition, page 77) The outflowing gas system uses liquid The saturation temperature is below and within the range of 'compressor and evaporator ^ However, this is due to the fact that the use of sensible heat alone does not make it possible for a refrigerator to have a heat exchanger installed between the appliances. (For example, "Cold Coil and Air Conditioning" Co., Ltd., Showa June 5 (1970)) During the process, the high-temperature refrigerant in the evaporator is properly supercooled to enter the throttle valve without any residual gas. Both components can run smoothly. The operation cycle goes smoothly, as in the present invention, in the case of two or more ingredients,% Λ, > & For effective cooling, the slave's green point and dew point curve will separate due to the cold bath in the condensation process

91057-DR-P001.ptd91057-DR-P001.ptd

玉、發明說明(5)Jade, invention description (5)

係使液 使蒸氣 促進此 沸點成 進行而 最大限 再 劑,係 低壓下 作成為 相之組成朝向、 壓降低係可2如沸點冷凍劑側移行,又隨著冷卻而 作用。另一制隔熱壓縮之際之溫度上升,且可再 分側組成之ίI丄沸點係隨著液相之組成而異,低 已移行至低;;二…的沸點係變成較低,故如此 度的發揮出;!^纟且成的冷康劑,則在蒸發過程可 7 /果能力。 者,如此進杆& + Α 阳庙兮、田=在冷凝過程經予冷卻的混合冷凍 1^ 便蒸虱壓降低之故,冷凝過程成為在較 可迅速進杆,h 平又The system promotes the boiling point of the liquid to promote the progress of the boiling point and minimizes the recirculation. The system is oriented at low pressure and the pressure of the phase is reduced. The pressure can be reduced, such as the boiling point of the refrigerant side, and it acts with cooling. The temperature of the other system is increased when the insulation is compressed, and the boiling point of the composition that can be subdivided is different with the composition of the liquid phase, and the low has shifted to low; the boiling point of the second has become lower, so Degree of exertion;! ^ 纟 and formed cold health agent, it can be 7 / fruit capacity in the evaporation process. In this way, the stroke & + Α Yangmiaoxi, Tian = mixed cooling that has been pre-cooled during the condensation process 1 ^ will reduce the pressure of steam lice, the condensation process becomes faster and faster, h flat and

在車乂低壓力下使冷;東機系統全体之動 可能。 M 、亦即’長久以來提高冷凝過程之壓力並進行低沸點冷 來劑側組成之液化時,成為可降低壓縮機之吐出壓力且 減輕其負載。 由此事實’採用相同能力之壓縮機,係可使用含有蒸 氣壓較高的冷凍劑成分之混合冷媒者,欲謀提高冷凍機之 能力即成為可能的。 又藉由利用此.熱交換器之冷卻混合冷凍劑,使混和冷 凍劑中之沸點降低,促使臨界溫度較低的成分冷凝,而藉 由冷卻此混合冷凍劑之溫度至室溫以下,在室溫之動作環 境下未能使直接冷凝之臨界溫度較低的冷凍劑即成為可予 使用。對此種沸點較低的冷凍劑,採用沸點及臨界溫度較 高且在室溫環境下動作的冷凝器,並組合可容易冷凝的冷 凍劑,藉由作成由二個以上的多數冷媒而成之混合冷凍 劑,藉由已採用在室溫環境下動作的冷凝器之單元方式的Cooling under low pressure on the car; the overall system of the Dongji system is possible. M, that is, when the pressure of the condensation process is increased for a long time and the low-boiling-point refrigerant side composition is liquefied, it becomes possible to reduce the discharge pressure of the compressor and reduce its load. From this fact, the use of compressors of the same capacity means that a mixed refrigerant containing a refrigerant component having a relatively high vapor pressure can be used, and it is possible to increase the capacity of the refrigerator. By using this heat exchanger to cool the mixed refrigerant, the boiling point of the mixed refrigerant is reduced, and the components with a lower critical temperature are condensed. By cooling the temperature of the mixed refrigerant to below room temperature, In the warm operating environment, the refrigerant that fails to make the critical temperature of direct condensation lower can be used. For this kind of refrigerant with a low boiling point, a condenser with a high boiling point and a critical temperature and operating at room temperature is used, and a refrigerant that can be easily condensed is combined to make it from two or more refrigerants. Mixed refrigerant, by means of a unit that has adopted a condenser that operates at room temperature

91057-DR-POOl.ptd 第8頁 五、發明說明(6) ,單構造之冷;東㈣統,可容易的發揮超低溫之冷束能 途的ΐϊΐΐίί:,比較上述習用的多元方式,在中 過程之延長上换利用恰在節流閥正前方的冷凝 熱及顯熱,進行促進: = =程;冷,之潛 極有效的冷卻。恰在此 ;間:二 低,可抑制隔熱壓縮之反壓力降 = :熱及顯熱’並與提高冷卻能力-= 且迅迷的進入穩定狀態運轉—事即有可能的。進仃了谷易 卻動冷束機系統之特徵,係在節流閥之前冷 換;r 1 /瓜^ t至壓縮機之混合冷凍劑的溫度藉由数交 产方雖然會上升,但在壓縮機= 上度及?力可觀察出均會降低”亦即,由於 :壓力顯著的降低’ &由隔熱壓縮度升 限制,此種過程會立即回饋至冷珠循環内所致度上升曰又 予以的混合冷束劑,係利用熱交換方式 相亦^$彳^ ^牦加,惟殘存的高沸點成分較多的液 相亦經予齓化而成為不妨礙壓縮機之運轉的狀離。 至第二確:此:厂本發明之冷;東系統之動作,與不具有回復 至第2圖所不的壓縮機之前之由回復冷束劑而成的熱交換91057-DR-POOl.ptd Page 8 V. Description of the invention (6), the single structure is cold; the Eastern Orthodox system can easily use the ultra-low temperature cold beam energy. Ϊ́ϊΐΐ: Compare the above-mentioned conventional multiple methods, in the middle The extension of the process uses the condensation heat and sensible heat directly in front of the throttle valve to promote: = = course; cold, latent extremely effective cooling. Just here; between: two low, can suppress the reverse pressure drop of thermal insulation compression =: heat and sensible heat 'and increase cooling capacity-= and quickly enter the steady state operation-things are possible. Into the characteristics of the Guyi dynamic cooling beam machine system, it is cold-replaced before the throttle; the temperature of the mixed refrigerant from r 1 / melon to the compressor will increase, but the Compressor = Upper Degree and? Force can be observed to all decrease ", that is, due to: a significant reduction in pressure '& limited by the insulation compression degree rise, this process will immediately return to the mixed cold beam caused by the increase in the cold bead cycle The agent is added in the same way by heat exchange, but the remaining liquid phase with more high-boiling components is also converted into a liquid that does not hinder the operation of the compressor. To the second true: This: The cold of the present invention; the operation of the East system, and the heat exchange between the return of the cooling beam agent without the compressor before returning to the compressor not shown in Figure 2.

91057-DR-pnni ntH91057-DR-pnni ntH

第9頁 五 發明說明(7) I用形式之冷珠系統而成者對比,並進〜每 於把握此等特性之實驗方面,並不一 ^貫驗。 冷凍劑之詳細物性,藉由實際機器之運轉可;:,析:心合 機二面係使用市售的UNIMD公司製造的製品機’冷凍 院二=機種名:GL99EJ) ’…合冷來劑係使用丁 、R_116(c6F6)45%之混合冷束劑,在2〇〇~237g 之耗圍内改變對冷束機之填充量’料於冷來機系統之 Ab的各部分之溫度、壓力值。 至於熱交換器ίο,則亦採用市售品之銅製雙層管3111長 度者’以外管為回復冷凍劑之流路。 此等的實際機器之壓力、溫度示於表1。 吐出壓Λ (kg/cm2) 吐出溫度 (°C ) 吸入壓力 (cmHg) 回復溫度 (°c ) 熱交換器 入口溫度 (°C ) 熱交換器 出口溫度 (°C ) 蒸發器 入口溫度 (°C ) 塡充量 (g) 本 發 明 16.5 62.7 10 35.9 29.8 23.9 -70.0 200 15.0 63.4 10 35.3 29.5 18.6 -71.6 219 8.0 Ί 62.2 0 32.1 31 -12.3 1 -68.9 237 比 較 例 19.5 66.9 0 26.5 1 -55.0 200 19.0 68.9 0 22.4 -70.0 219 19.5 69.4 0.05 18.9 -70.7 237 表内之數值的測定點係如下所示 91057-DR-P001.ptd 第10頁 500902 五、發明說明(8) 吐出壓力(A)、吐出溫度(a)、吸入壓 卜、 度(B)、熱交換器出口溫度(E)、蒗$ 、回復溫 “、、知态入口溫度(G ) 如表1所示,冷卻恰在節流閥正前 的回復冷珠劑,係吸收來自冷凝器之冷^齊;^劑旦所使用 復溫度之欄所示般,恰在壓縮機正前 里並如回 度U.W.4X;,而利用壓縮機使此= =上升溫 反之卻降低7.2〜4.2。(:。又同時隨著\^熱壓山缩後的溫度 N 4丨思有熱父換器屮 、、西 降低,冷;東劑之恰在節流7正前 出壓力之降低及吐丄:=]…壓降低,生成吐 237 ί乂 ΪΪ效可藉由使冷;東劑之填充量由2〇〇g增加至 ^ ^ 1 ,此冷凍劑填充量之增加係直接提高恰在節 &閥正刖方的冷;東劑之冷卻作用,可知使於該熱交換器出 口之’里度會降低。至於到達溫度,係隨著冷凝溫度之降 低,沸點曲線之斜度呈緩坡狀,.故在填充氣体之組成的沸 點附近,到達溫度差會變小,而即使在填充量或吐出壓力 之較小的範圍内亦有效的達成指定的低溫度。 y ,此,為觀察此冷媒填充量及此等的冷卻作用間之關 係,右將熱交換器入口及出口之冷凍劑的溫度及填充量間 之關係予以對比時,則如表2所示。Page 9 5 Description of the invention (7) I use a form of cold bead system to make comparisons, and progress ~ every experimental aspect of grasping these characteristics is not consistent. The detailed physical properties of the refrigerant can be achieved by the operation of the actual machine.:, Analysis: The second side of the machine is a commercial machine made by the UNIMD company, which is a commercially available machine 'Freezing House II = Model Name: GL99EJ)' ... It uses D, R_116 (c6F6) 45% mixed cold beam agent, and the filling amount of the cold beam machine is changed within the consumption range of 2000 ~ 237g. It is expected that the temperature and pressure of each part of the Ab of the cold machine system value. As for the heat exchanger ί, a commercially-available copper double-layer pipe 3111 length 'outer pipe is also used as the refrigerant return flow path. The pressure and temperature of these actual machines are shown in Table 1. Discharge pressure Λ (kg / cm2) Discharge temperature (° C) Suction pressure (cmHg) Recovery temperature (° c) Heat exchanger inlet temperature (° C) Heat exchanger outlet temperature (° C) Evaporator inlet temperature (° C ) 塡 Charge (g) The present invention 16.5 62.7 10 35.9 29.8 23.9 -70.0 200 15.0 63.4 10 35.3 29.5 18.6 -71.6 219 8.0 Ί 62.2 0 32.1 31 -12.3 1 -68.9 237 Comparative Example 19.5 66.9 0 26.5 1 -55.0 200 19.0 68.9 0 22.4 -70.0 219 19.5 69.4 0.05 18.9 -70.7 237 The measurement points of the values in the table are as follows 91057-DR-P001.ptd Page 10 500902 V. Description of the invention (8) Discharge pressure (A), discharge temperature (A), suction pressure, degree (B), heat exchanger outlet temperature (E), 蒗 $, recovery temperature ", and state inlet temperature (G) As shown in Table 1, the cooling is just at the throttle valve positive The previous recovery cold bead agent absorbs the cold from the condenser; as shown in the column of the complex temperature used by the agent, it is directly in front of the compressor and returns to UW4X; and the compressor is used to make This = = the temperature rises but decreases by 7.2 ~ 4.2. (:. At the same time, the temperature N 4 after shrinking with \ ^ There is a hot parent converter, and the west and the west are reduced and cold; the east agent is just before the throttling 7 and the pressure is reduced and spitting: =] ... the pressure is reduced and the spit is generated. The effect can be made cold; The filling amount of the agent is increased from 200g to ^^ 1. The increase in the filling amount of the refrigerant is to directly improve the cooling effect of the agent at the node &valve; the cooling effect of the agent is known to make the heat exchange The temperature at the outlet of the device will decrease. As for the arrival temperature, the slope of the boiling point curve will gradually decrease as the condensation temperature decreases. Therefore, near the boiling point of the filling gas composition, the difference in the arrival temperature will become smaller, and even if The specified low temperature can also be effectively achieved within a relatively small range of the filling amount or the discharge pressure. Y, this is to observe the relationship between the refrigerant filling amount and the cooling effect. When the relationship between the temperature of the refrigerant and the filling amount is compared, it is shown in Table 2.

juuyuz 五、發明說明(9) 回復冷凍劑熱交換器入口溫度CF) 口復冷滚劑熱交換器出口溫度(D ) 亦即,若冷凍劑填充量增加時, 上的適當填充量,㈣發器入 力 低,冷凍庫庫内π许介π攸& 又+曰相*私度的降 劑之溫度會顯著的ϋ。 _惟於熱交換器出口的冷凍 中斷斷蒸發下循環且含有該不 由在熱交換器内與來自壓縮機之3匕換:u ’藉 化,大幅的有助於冷媒之冷卻。州進仃熱父換並予氣 此狀態係於通常採用非共沸系混a 統内,會經常發生稱作結霜的狀•態。東劑之·冷,機系 無助於冷凍機之冷凍能力,不僅冷成為此種狀態時, 由蒸發器至壓縮機之配管周圍會之運轉效率降低, 損之原因。 门固曰…相,亦成為冷凍設備破 本發明係不僅消除此結霜現象, 力之回復冷凍劑成分的冷卻能力並使 ?助於5冷凍能 減輕其負m,可提高冷凍機之運轉效率。壓力顯著降低以 R - 116,丁烧之物理性質示於表3。juuyuz V. Description of the invention (9) Restore the refrigerant heat exchanger inlet temperature CF) The recooling roller heat exchanger outlet temperature (D), that is, if the refrigerant filling amount increases, the appropriate filling amount on the The inlet force of the device is low, and the temperature of π 许 介 π 攸 in the freezer will increase significantly. _ Only the refrigeration at the outlet of the heat exchanger interrupts the circulation under the interruption of evaporation and contains the inevitable replacement in the heat exchanger with the compressor from the compressor: u 'borrowing greatly helps the cooling of the refrigerant. This state is in a non-azeotropic mixed system, and a state called frosting often occurs. The coldness of the agent, the machine system does not help the freezing capacity of the refrigerator. When it is not only in this state, the operating efficiency from the evaporator to the piping around the compressor will be reduced, causing damage. The door solidifies ... phase, also becomes the freezing equipment break. The present invention not only eliminates the frost phenomenon, but also restores the cooling capacity of the refrigerant component and makes? Helping 5 freeze can reduce its negative m, can improve the operating efficiency of the refrigerator. The pressure is significantly reduced by R-116.

500902 五、發明說明(ίο) 如表所述,丁烷之沸點為〜0 · 5 X:,故填充量為2 3 7 g 時,-2 4 · 7 °C之冷凍劑溫度係加上丁烷之潛熱,可知由冷 凍劑之顯熱而成者係較大的。 " 表3 : 丁烷、R-116之物理性質 化學式 沸點 (〇C、latm) 臨界溫度 ΓΟ 蒸氣壓500902 V. Description of the invention (ίο) As stated in the table, the boiling point of butane is ~ 0 · 5 X :, so when the filling amount is 2 3 7 g, the refrigerant temperature of -2 4 · 7 ° C is added with Ding. It is known that the latent heat of alkanes is larger from the sensible heat of the refrigerant. " Table 3: Physical properties of butane and R-116 Chemical formula Boiling point (〇C, laTM) Critical temperature ΓΟ Vapor pressure

丁烷-R116系之混合冷凍劑,因卜116之蒸氣壓較低, 故如上述般,即使不依本發明之系統雖然冷凍機系統亦可 貫際機器運轉,然而本發明之冷凍機系統因會有效的使冷 凝過程之溫f及壓力降低,故在通常的室溫環境下,於冷 凝過程需要咼® ’臨界溫度較低,在習用的冷凍機之能力 方面使用不可液化的冷凍劑,可實現出超低溫。 、因此,對丁 R23系混合冷凍劑取代丁烷—R1丨6系混 合冷凍劑,冷凍系統方面同樣的採用UNIDAD公司製造的機 ,名F^4(冷涞機種名:GL99EJ)之冷束機及由市售的銅製 層官而成^&、、、、父換器,以由丁烷(匕心口冗及卜“㈧叮。 而-成的rW冷凍劑作為混合冷凍劑,在140〜27〇g之範 内’更:V二機之填充量並測定於 A〜 部分的溫度、壓力。The butane-R116 mixed refrigerant has a low vapor pressure as described above. Therefore, even if the system according to the present invention does not comply with the present invention, although the freezer system can be operated continuously, the freezer system of the present invention may Effectively reduce the temperature f and pressure of the condensing process, so under normal room temperature environment, the condensing process requires 咼 ® 'Critical temperature is low, the use of non-liquefiable refrigerant in the capacity of the conventional refrigerator can be achieved Very low temperature. Therefore, instead of butane-R1 丨 6-series mixed refrigerants for butane R23 series refrigerants, the refrigeration system also uses the cold beam machine named F ^ 4 (cold heading machine name: GL99EJ) manufactured by UNIDAD Company. And made of commercially available copper layer officials ^ & ,,,, and parent converters, made of butane (dark heart mouth redundant and Bu "dingding. And-the rW refrigerant as a mixed refrigerant, in 140 ~ Within the range of 27 g, more: The filling amount of the V two machine is measured at the temperature and pressure of part A ~.

第13頁 500902 五、發明說明(11) 其數據與丁烷及R-23之物理性質示於表4及表5 ° 測定點:回復冷凍劑熱交換器入口(F)、回復冷凍劑 熱交換器出口(D)、庫内溫度(H) 吐出壓力 (kg/cm2) 吸入壓力 (cmHg) 熱交換器 入口溫度 (°C) 熱交換器 出口溫度 CC) 回復冷凍劑 熱父換益 入口 (。〇 a復冷凍爾 熱交換器 出口 rc) 庫內溫度 ΓΟ 塡充量 (g) 本 發 明 仿1 15.5 20 30.4 24.4 17.9 30.2 -27 140 14.5 5 29.8 -0.8 -17.0 29.2 -50 150 11.0 0 29.7 -17.5 -26.7 26.8 -69.7 160 10.0 0 29.8 -22 19.3 r -73.5 170 9.5 0 30.2 -24 -30.9 -0.9 -74.2 180 9.5 0.1 30.3 -23.4 -30.9 -1.9 -73.4 190 9.5 0.2 31.3 -23.3 -30.2 -4.8 -72.0 200 1 10.0 Γ 0.3 32.9 -22.3 -29.2 -2.6 -70.1 210 10.5 0.5 34.6 -21.4 -28.9 -0.4 -67.9 220 11.0 0.6 35.0 -21.6 -28.9 1.7 -66.5 230 11.25 0.6 35.3 -22.5 -29.5 2.8 -66.0 240 12.0 0.7 35.8 -24.2 -30.7 3.4 -65.5 250 ^ 12.25 0.8 35.6 -24.7 -30.7 3.5 -65.0 260 '12.5 1 : n~kLpJif. 0.8 "h、ItR H M 35.3 -25.4 -31.4 3.7 -64.4 270 表5 : 丁院、R-23之物理性質Page 13 500902 V. Description of the invention (11) The data and physical properties of butane and R-23 are shown in Tables 4 and 5 ° Measurement point: Restore the refrigerant heat exchanger inlet (F), restore the refrigerant heat exchange The outlet (D), the temperature in the storehouse (H), the discharge pressure (kg / cm2), the suction pressure (cmHg), the heat exchanger inlet temperature (° C), and the heat exchanger outlet temperature CC) return the refrigerant heat exchange inlet (). 〇a Recooler heat exchanger outlet rc) Temperature in the warehouse Γ 塡 Charge (g) The present invention imitates 1 15.5 20 30.4 24.4 17.9 30.2 -27 140 14.5 5 29.8 -0.8 -17.0 29.2 -50 150 11.0 0 29.7 -17.5 -26.7 26.8 -69.7 160 10.0 0 29.8 -22 19.3 r -73.5 170 9.5 0 30.2 -24 -30.9 -0.9 -74.2 180 9.5 0.1 30.3 -23.4 -30.9 -1.9 -73.4 190 9.5 0.2 31.3 -23.3 -30.2 -4.8- 72.0 200 1 10.0 Γ 0.3 32.9 -22.3 -29.2 -2.6 -70.1 210 10.5 0.5 34.6 -21.4 -28.9 -0.4 -67.9 220 11.0 0.6 35.0 -21.6 -28.9 1.7 -66.5 230 11.25 0.6 35.3 -22.5 -29.5 2.8 -66.0 240 12.0 0.7 35.8 -24.2 -30.7 3.4 -65.5 250 ^ 12.25 0.8 35.6 -24.7 -30.7 3.5 -65.0 260 '12 .5 1: n ~ kLpJif. 0.8 " h, ItR H M 35.3 -25.4 -31.4 3.7 -64.4 270 Table 5: Physical properties of Ding Yuan, R-23

由表5可見,R-23亦較R-116為沸點低,臨界、严 惟另一方面蒸氣壓係相當高,故即使作為μ 二恤X巧’ 束劑,在冷凝過程之溫度、壓力上升而混合系冷 能力而言,則使用上係有困難的。 、冷束機之It can be seen from Table 5 that R-23 also has a lower boiling point than R-116, and is critical and strict. On the other hand, the vapor pressure is quite high. Therefore, even as a μ two-shirt Xqiao 'beam agent, the temperature and pressure of the condensation process rise. As for the cooling capacity of the hybrid system, it is difficult to use the upper system. Of cold beam machine

mm 第14頁 91057-DR-P001.ptd J^9〇2mm Page 14 91057-DR-P001.ptd J ^ 9〇2

五、發明說明(12)V. Description of the invention (12)

於本發明之冷凍系統,由上述表4可見,隨著冷凍劑 填充量增加,於熱交換器之回復冷凍劑的溫度顯著降低, 可知與此等聯動且吐出壓力及熱交換器出口之冷凍劑温度 會顯著降低。如此,可最大限度的發揮丁烷—R2 3系冷凍劑 之冷凍能力γ此情形亦與上述情形同樣由填充量得知回復 ^凍劑之冷卻忐力上大致在一定的適當範圍,即使增加該 fe圍以上的冷凍劑填充量亦未提高冷凍能力。 在上述例子,於市售的冷凍機内填充二成分系之混合 東劑並藉由實際機器運轉雖可確認其作用效果,惟此等 卢::3在非::沸^"合冷媒之組合或此等冷凍劑之種類的 方:姑糸共同的’又其組合的冷凍劑之種類數量亦 在2個以上的數目,餘旅細 的。 I揮同樣的作用、功效係顯而可知 亦 之沸點 溫度降 利用液 為可能 冷凍能 點’或 能者, 持溫度 界壓力 又 吁,不 曲線可 低,液 相之沸 ,同時 力。又 向蒸氣 此等的 或冷象 之關係 ’基本 見,隨著非 相之組成會 點會降低者 亦可使所需 ’此等的功 壓之冷媒為 冷凍劑之種 機壓縮機等 予以選定並 上冷凍系統 係如混 共彿糸 移行至 ,欲使 的壓縮 效係以 混合冷 類或數 的能力 可適當 之構成 合冷束劑 混合冷束 低沸點成 冷凍溫度 壓力降低 在室溫未 凍劑而使 量係因應 ,由沸點 的組合。 亦依據上 之氣液平 劑之冷凝 分侧,又 較降低一 且可顯著 能液化的 容易處理 目的冷朿 、臨界溫 衡曲線 過程的 由而亦 事即成 的提高 低沸 成為可 機之、維 度•臨 述實施例,對較In the refrigerating system of the present invention, it can be seen from the above Table 4 that as the refrigerant filling amount increases, the temperature of the returning refrigerant in the heat exchanger decreases significantly. It can be seen that the refrigerant that is linked to these and discharges pressure and the heat exchanger outlet is The temperature will decrease significantly. In this way, the freezing capacity of the butane-R2 3 series refrigerant can be maximized. This situation is also the same as the above situation. It can be learned from the filling amount that the cooling power of the refrigerant is approximately within a certain appropriate range, even if it is increased. The amount of refrigerant filled above fe does not increase the freezing capacity. In the above example, a commercially available freezer is filled with a two-component mixed agent and the actual effect can be confirmed by running the actual machine, but these Lu :: 3 in non :: boiling ^ " combination of refrigerant Or the type of these refrigerants: the number of types of refrigerants that are common, and the combination of refrigerants is also more than two, and Yu Lu is fine. I have the same effect and effectiveness. It is also known that the boiling point is also the temperature drop. It is possible to use the liquid to freeze the energy point, or to hold the temperature and pressure, but the curve can be low, the liquid phase can boil at the same time. In addition, it is basically based on the relationship between the steam and the cold image. If the non-phase composition will be reduced, the required refrigerant can be selected as the seed compressor of the refrigerant. The combination refrigeration system is such as the mixed Buddha shrine. The desired compression effect is the ability to mix cold types or numbers. It can be appropriately composed of the cold bundle agent. The mixed cold bundle has a low boiling point and the freezing temperature is reduced. The pressure is not frozen at room temperature. The amount of the agent depends on the combination of the boiling points. It is also based on the condensing side of the gas-liquid leveling agent, which is relatively lower and can be liquefied easily. The cold heading and critical temperature equilibrium curve process of the easy-to-handle process can be improved by improving the low boiling point. Dimensions • Describe the examples, compare

500902 五、發明說明(13) 低溫用方面,為促進在熱交換器中的低溫度沸點冷凍劑之 冷凝過程,為作成容量較大的熱交換器構造,又作成緊密 的構成,亦可採用螺旋管或層合構造者以取代雙層管。500902 V. Description of the invention (13) In the aspect of low temperature, in order to promote the condensation process of the low-temperature boiling point refrigerant in the heat exchanger, in order to make a heat exchanger with a large capacity and a compact structure, a spiral can also be used. Tube or laminated construction to replace the double tube.

91057-DR-P001.ptd 第16頁 500902 圖式簡單說明 圖式之簡單說明 第1圖為本發明之冷凍機系統構成圖。 第2圖為不適用本發明之比較例。 第3圖為習用的超低溫用多元系(三元系)冷凍機系 統。 圖號之說明 1壓縮機 2 冷凝器 3乾燥器 4 節流閥(毛細管) 5蒸發器 6第一氣液分離機 7第一熱交換器 8 第二氣液分離機 9第二氣液分離機 1 0熱交換器 5 0 冷束庫91057-DR-P001.ptd Page 16 500902 Brief description of the drawings Brief description of the drawings Fig. 1 is a structural diagram of a refrigerator system of the present invention. Fig. 2 is a comparative example to which the present invention is not applied. Figure 3 is a conventional multi-temperature (three-element) freezer system for ultra-low temperature. Explanation of drawings 1 compressor 2 condenser 3 dryer 4 throttle (capillary) 5 evaporator 6 first gas-liquid separator 7 first heat exchanger 8 second gas-liquid separator 9 second gas-liquid separator 1 0 heat exchanger 5 0 cold beam warehouse

91057-DR-P001.ptd 第17頁91057-DR-P001.ptd Page 17

Claims (1)

500902 六、申請專利範圍 1 /種冷康系統,其特徵在於採用含有一個以上的冷凍劑 成分之#共沸系混合冷凍劑之冷凍系統,藉由經過壓縮 機、冷凝器、節流閥、蒸發器而反饋至壓縮機之循環路徑 内的由蒸發器反饋至壓縮機之低溫動作流体,冷卻由冷凝 器i節流闕間之動作流体以促進低沸點成分之液化。 2 ·如申請專利範圍第 發器至節流閥間之動 沸點成分之不同使成 1項之冷凍系統,其中冷卻由上述蒎 φ\%\ 作流体的低溫動作流体係依液狀的高 為濕潤狀態。 3 ·如申請專利範圍 發器反饋至壓縮機 閥之間的動作流体 力降低。 第1項之冷凍系統, 之低溫動作流体, 可使來自壓縮機 、其中籍由由上述蒸 2由冷凝器至節流 作流体的吐出壓 4·如申請專利範圍第1 it ;弗系混人、人土… Z或3項之冷來系么 共沸系此合冷凍劑之至少果系统,其中上述 溫 以下。 成界邋度係在約略室500902 VI. Application for patent scope 1 / Kind of cold health system, which is characterized by the use of a # azeotrope-based mixed refrigerant refrigeration system containing more than one refrigerant component, by passing through a compressor, condenser, throttle valve, evaporation The low-temperature working fluid fed back from the evaporator to the compressor in the circulation path of the compressor is cooled by the condenser i to throttle the working fluid between the thighs to promote the liquefaction of low-boiling components. 2 · If the difference in the dynamic boiling point components between the sender and the throttle valve is applied in the scope of the patent application, a refrigeration system of item 1 is used, in which the low-temperature operating flow system cooling the above 蒎 φ \% \ as the fluid depends on the liquid height as Wet state. 3 · If the scope of the patent application, the force of the working fluid between the transmitter and the compressor valve is reduced. The refrigerating system of item 1, the low-temperature operating fluid, can make the discharge pressure from the compressor, which is from the above steaming 2 to the condenser to the throttling fluid 4. As the scope of the patent application 1 it; , Human soil ... Z or 3 is cold at least the azeotropic system of the refrigerant system, where the above temperature is below. Cheng Jie Duo is in the approximate room
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111076479A (en) * 2019-12-05 2020-04-28 合肥晶弘电器有限公司 Household refrigeration equipment for realizing ultralow-temperature storage by using non-azeotropic mixed refrigerant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111076479A (en) * 2019-12-05 2020-04-28 合肥晶弘电器有限公司 Household refrigeration equipment for realizing ultralow-temperature storage by using non-azeotropic mixed refrigerant

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