TW219950B - - Google Patents
Download PDFInfo
- Publication number
- TW219950B TW219950B TW81108598A TW81108598A TW219950B TW 219950 B TW219950 B TW 219950B TW 81108598 A TW81108598 A TW 81108598A TW 81108598 A TW81108598 A TW 81108598A TW 219950 B TW219950 B TW 219950B
- Authority
- TW
- Taiwan
- Prior art keywords
- compound
- propane
- weight
- sister
- difluoromethane
- Prior art date
Links
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 50
- RWRIWBAIICGTTQ-UHFFFAOYSA-N difluoromethane Chemical compound FCF RWRIWBAIICGTTQ-UHFFFAOYSA-N 0.000 claims description 44
- 150000001875 compounds Chemical class 0.000 claims description 41
- 239000000203 mixture Substances 0.000 claims description 31
- 238000009835 boiling Methods 0.000 claims description 30
- 239000001294 propane Substances 0.000 claims description 24
- 238000001704 evaporation Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims 3
- 230000008020 evaporation Effects 0.000 claims 1
- 238000007710 freezing Methods 0.000 description 9
- 230000008014 freezing Effects 0.000 description 9
- 150000001335 aliphatic alkanes Chemical class 0.000 description 7
- 238000000926 separation method Methods 0.000 description 6
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 5
- 230000002079 cooperative effect Effects 0.000 description 5
- 239000004615 ingredient Substances 0.000 description 5
- GTLACDSXYULKMZ-UHFFFAOYSA-N pentafluoroethane Chemical compound FC(F)C(F)(F)F GTLACDSXYULKMZ-UHFFFAOYSA-N 0.000 description 5
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 229910052731 fluorine Inorganic materials 0.000 description 4
- 239000011737 fluorine Substances 0.000 description 4
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000003507 refrigerant Substances 0.000 description 4
- -1 1, 1, 1_trifluoroethane Alkane Chemical class 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 239000003380 propellant Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- UJPMYEOUBPIPHQ-UHFFFAOYSA-N 1,1,1-trifluoroethane Chemical compound CC(F)(F)F UJPMYEOUBPIPHQ-UHFFFAOYSA-N 0.000 description 2
- NPNPZTNLOVBDOC-UHFFFAOYSA-N 1,1-difluoroethane Chemical compound CC(F)F NPNPZTNLOVBDOC-UHFFFAOYSA-N 0.000 description 2
- XPDWGBQVDMORPB-UHFFFAOYSA-N Fluoroform Chemical compound FC(F)F XPDWGBQVDMORPB-UHFFFAOYSA-N 0.000 description 2
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 230000000875 corresponding effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- UHCBBWUQDAVSMS-UHFFFAOYSA-N fluoroethane Chemical compound CCF UHCBBWUQDAVSMS-UHFFFAOYSA-N 0.000 description 2
- UKACHOXRXFQJFN-UHFFFAOYSA-N heptafluoropropane Chemical compound FC(F)C(F)(F)C(F)(F)F UKACHOXRXFQJFN-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 239000005437 stratosphere Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- YFMFNYKEUDLDTL-UHFFFAOYSA-N 1,1,1,2,3,3,3-heptafluoropropane Chemical compound FC(F)(F)C(F)C(F)(F)F YFMFNYKEUDLDTL-UHFFFAOYSA-N 0.000 description 1
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 1
- WXGNWUVNYMJENI-UHFFFAOYSA-N 1,1,2,2-tetrafluoroethane Chemical compound FC(F)C(F)F WXGNWUVNYMJENI-UHFFFAOYSA-N 0.000 description 1
- BOUGCJDAQLKBQH-UHFFFAOYSA-N 1-chloro-1,2,2,2-tetrafluoroethane Chemical compound FC(Cl)C(F)(F)F BOUGCJDAQLKBQH-UHFFFAOYSA-N 0.000 description 1
- 241000237519 Bivalvia Species 0.000 description 1
- SXSOIAXBHLPLOI-UHFFFAOYSA-N CCC.FC(F)C(F)(F)F Chemical compound CCC.FC(F)C(F)(F)F SXSOIAXBHLPLOI-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 208000001613 Gambling Diseases 0.000 description 1
- 240000007839 Kleinhovia hospita Species 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- SGVQWMHGPNLWSW-UHFFFAOYSA-N chloro(difluoro)methane;1-chloro-1,1,2,2,2-pentafluoroethane Chemical compound FC(F)Cl.FC(F)(F)C(F)(F)Cl SGVQWMHGPNLWSW-UHFFFAOYSA-N 0.000 description 1
- 235000020639 clam Nutrition 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000003989 dielectric material Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 235000012907 honey Nutrition 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- CUONGYYJJVDODC-UHFFFAOYSA-N malononitrile Chemical compound N#CCC#N CUONGYYJJVDODC-UHFFFAOYSA-N 0.000 description 1
- QYSGYZVSCZSLHT-UHFFFAOYSA-N octafluoropropane Chemical compound FC(F)(F)C(F)(F)C(F)(F)F QYSGYZVSCZSLHT-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229960004065 perflutren Drugs 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Landscapes
- Detergent Compositions (AREA)
Description
經濟部中央標準局R工消費合作社印製 A6 _B6_ 五、發明説明(1 ) 發明背景 一 本發明和氟化碳氫化合物與脂肪族碳氫化合物的混合物 有關,更明確地說是和實質上恆定沸點之二氰甲烷與丙烷 姐合物有闞。 關切某些鹵化族的臭氧消耗潛力已烴導致研究具有較低 的臭氧消耗潛力之替代性化合物,最近碳氟氯的長期_境 效應已纆在實質科學仔细研討之内,因為曾假定這些材料 會在同溫層分解,它在紫外媒辐射的影響下會放出氯原子 。氛原子在理論上會在同溫曆進行化學反應,這樣能夠消 耗同溫靥的臭氧層,而且同溫層奥氧的實質減少對地球的 生活品質有嚴重不良的衝擊。 對氟化碳氫化合物的數量有一個限制,這種物質可能是 對環境不會產生危害的材料,然而,如果要求的棍合性質 可在給與的混合物中發現,則可能使用已知材料的混合。 不過,簡易混合物在冷凍的設計和操作Μ及其它的設備中 產生問題,因為成份要在蒸汽和液相中進行。為了避免過 多成份分離問題,特別需要發現沒有成份分離問題的恆定 沸點混合物。不幸的是預测共沸混合物或是像共沸混合物 姐成的處方是不可能的,因此使得擁有所要的混合性霣之 组成研究變得很複雜。 作用和單一化合物相似,而且在煮沸時會造成微不足道 的混合物分離之賁質上恆定沸點组合,現在有很迫切的需 要。 (請先閱讀背面之注意事項再塡寫本·頁) 本紙張又度通用中园国家橒準(CNS)甲4規格(210 X 297公笼) 81.9.25,000 219950 Λβ Βί; 經濟部中央標準局S工消费合作社印« 五、發明説明(2 ) 發明摘要 t 本發明是針對實質上恆定沸點姐合物•它包括⑶二氟甲 烷和收丙烷,其中上述的姐合物包含大約67到9〇重量百分 比·較佳的是大約到75重量百分比的二氟甲烷 (HFC-32) ·這是和<b)的重量德和為基礎•差額大約是 10到33重量百分比為丙烷(HC-290),較佳的是25到的重 量百分比。尤其在較佳的共沸混合物姐合物中,包括大約 70重量百分比的二氟甲烷和3Q重量百分比的丙烷,其中的 重量百分比是基於二氟甲烷和丙烷的重最缌和來計算的。 本發明的姐成比它的兩種成份有較高的蒸汽壓。如使用 在本發明的實質上恆定沸點姐合物意味著在最混合物的一 半已被允許蒸發之後,它在251C的最初蒸汽壓不會變化 10¾ Μ上。因此,描述在此能抵抗成份分離的姐成會嚴重 地減少它們在預期應用中的效用。這些實質上恆定沸點包 含著碳氟化合物的姐成在做為動力循環適用流體時特別有 效,例如冷凍_、熱傳媒介、氣溶膠推進劑、氣體電介質 、滅火萷和聚合物膨脹劑,舉例來說有聚烯烴和聚氨基甲 酸酯。 較佳的具雅例證之詳细描述 使用在本發明的姐合物之氟化碳氫化合物成份是二氣甲 烷,在鹵化碳工業中稱之為H FC-32;在姐合物中所使用的 第二種成份是飽和脂肪族碳氫丙烷。 ---------;-------~ --------裝 II----.玎----I 嫁 、清'1:^--!苛*之;1*事項冉«'寫本頁) 本紙張又度遇用中囷因家標準(CNS〉甲4规格(210 X 297公釐) 81.9.20,000 219&50A6 _B6_ printed by R Industry and Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy V. Description of the invention (1) Background of the invention The present invention relates to a mixture of fluorinated hydrocarbons and aliphatic hydrocarbons, more specifically and essentially constant The boiling point of dicyanomethane and propane sister compound is unkind. Concerned that the ozone depletion potential of certain halogenated groups has led to the study of alternative compounds with lower ozone depletion potential. The long-term environmental effects of fluorocarbons have recently been carefully studied in substantive science because it was assumed that these materials would Decomposition in the stratosphere, it will release chlorine atoms under the influence of ultraviolet medium radiation. Atmospheric atoms theoretically undergo chemical reactions at the same temperature, which can consume the ozone layer of the same temperature, and the substantial reduction of the oxygen in the stratosphere has a serious adverse impact on the quality of life of the earth. There is a limit to the amount of fluorinated hydrocarbons. This substance may be a material that does not harm the environment. However, if the required sticking properties can be found in the given mixture, it may be possible to use known materials. mixing. However, simple mixtures pose problems in the design and operation of refrigeration and other equipment because the ingredients are carried out in steam and liquid phase. In order to avoid excessive component separation problems, it is especially necessary to find a constant boiling point mixture without component separation problems. Unfortunately, it is not possible to predict azeotropic mixtures or prescriptions like azeotropic mixtures, which complicates the study of the composition with the desired mixing properties. The action is similar to that of a single compound, and when boiling, it will cause insignificant mixture separation and the constant boiling point combination on the substrate is now urgently needed. (Please read the precautions on the back before writing this page.) This paper is also used in the Central Park National Standard (CNS) A 4 specifications (210 X 297 male cage) 81.9.25,000 219950 Λβ Βί; Central Bureau of Standards S of the Ministry of Economic Affairs Industrial and consumer cooperatives printed «V. Description of the invention (2) Summary of the invention t The present invention is directed to a substantially constant boiling point compound • It includes (3) difluoromethane and propane, wherein the above compound contains about 67 to 90 weight Percentage · Preferably it is about 75% by weight of difluoromethane (HFC-32) · This is based on the weight and sum of < b). The difference is about 10 to 33% by weight for propane (HC-290) , Preferably 25 to weight percent. In particular, the preferred azeotropic mixture includes about 70% by weight of difluoromethane and 3Q by weight of propane, wherein the weight percentage is calculated based on the weight of the difluoromethane and propane. The sister component of the present invention has a higher vapor pressure than its two components. If used in the present invention, a substantially constant boiling point compound means that after half of the most mixture has been allowed to evaporate, its initial vapor pressure at 251C will not change by 10¾ M. Therefore, it is described here that resistance to component separation will seriously reduce their utility in the intended application. These substantially constant boiling point fluorocarbon-containing sisters are particularly effective as fluids suitable for power cycling, such as freezing, heat transfer media, aerosol propellants, gas dielectrics, fire extinguishing agents, and polymer expansion agents. Said there are polyolefins and polyurethanes. Detailed description of the preferred elegant example The fluorinated hydrocarbon component used in the sister compound of the present invention is methane gas, which is called H FC-32 in the halogenated carbon industry; used in the sister compound The second component is saturated aliphatic hydrocarbon propane. ---------; ------- ~ -------- outfit II ----. 玎 ---- I marry, clear '1: ^-! Harsh * Of; 1 * matters Ran «'write this page) This paper once again meets the Chinese family standard (CNS> A 4 specifications (210 X 297 mm) 81.9.20,000 219 & 50
At; Βι:. 經濟部中央標準居員工消费合作社印5衣 五、發明説明(5 ) 二氟甲烷和丙烷的各種混合物之相位研究中,姐合麥化 包括大不相同的二氟甲烷和丙烷數量表示在恆溫下,共沸 混合物在研究的溫度範圍中形成了。本發明的實質上垣定 沸點姐合的更進一步研究包括廣大範臞的二氟甲烷和丙院 之比例,它們能抵抗混合物的成份分皤,使得姐合在恆溫 下保持一個實霣上恆定的沸點。在揭露的数量中利用氟 甲烷和丙烷成份很意外地描述在25υ恆溫中姐合物的蒸汽 懕麥化,即使在最初姐合物旳50¾已獲得許可蒸發的赛化 不超過10XM上。在恆溫下蒸汽懕的微小變化描述遇量的 成份分離和損失將實質地改變混合物的沸點者並不會發生 ,這使得姐合物特別適合預期用途,例如冷凍蜊、氣溶膠 推進劑、發泡劑等。 此外,研究已指出本發明新奇的實質上恆定沸點組合物 以微小壓力差展現霣點和氣泡點。做為埴棰技藝中聞名的 方法,在相同溫度的露點和氣泡壓力之間的差異是一種混 合物的恆沸點或是共沸混合物狀行為之指檷,當和那些為 人所知的共沸姐成比較之下•本發明的實質上恆定沸點姐 合物所-展現之壓力差是很小的。 本發明的姐合物更進一步K這種方式來表現特徴。在恆 溫下,混合物的對應於氣泡點之壓力和對應於露點之壓力 間的差異不得大於約10 psia(10磅/平方吋)。 做為這種技術領域中被良好認可的方法,有一個姐合範 圍包括和真實的共沸混合物相同的成份,它非但展現和真 買的共沸混合物幾乎完全相當的性質來做為冷凍或是其它 -----------------------裝- -----.玎----~ ·Μ. (--^-背而之注-事^冉場寫本頁) . 本紙張又度適用中國國家標準(CNS>甲4規格(210 X 297公笼) 81.9.20,000 _ _ ~ /·*·. ff" rf~·. 經濟部中央標準局KK工消費合作社印製At; Βι :. Printed by the Ministry of Economic Affairs of the Central Standards Residents ’Consumer Cooperatives. 5. Description of the invention (5) In the phase study of various mixtures of difluoromethane and propane, Simeima Chemicals included greatly different difluoromethane and propane. The quantity indicates that at constant temperature, the azeotrope is formed in the temperature range studied. The essence of the present invention is to further determine the boiling point of the further research including the ratio of the majority of Fan Di ’s difluoromethane and propionate, which can resist the composition of the mixture, so that the sister at a constant temperature to maintain a constant boiling point . The use of fluoromethane and propane components in the quantities disclosed unexpectedly described the steaming of the sister compound at a constant temperature of 25 °, even though the initial sister compound 5050 had obtained permission to evaporate at a temperature not exceeding 10XM. The small changes in steam at constant temperature describe the separation and loss of the amount of ingredients that will substantially change the boiling point of the mixture and will not occur, which makes the compound particularly suitable for the intended use, such as frozen clams, aerosol propellants, foaming Agent. In addition, studies have pointed out that the novel substantially constant boiling point composition of the present invention exhibits a low point and a bubble point with a small pressure difference. As a well-known method in the craftsmanship, the difference between the dew point and the bubble pressure at the same temperature is the constant boiling point of a mixture or the azeotropic mixture-like behavior, and should be known to those azeotropic sisters. In comparison • The pressure difference exhibited by the substantially constant boiling point compound of the present invention is very small. The sister compound of the present invention further expresses characteristics in this way. At constant temperature, the difference between the pressure corresponding to the bubble point and the pressure corresponding to the dew point of the mixture must not be greater than about 10 psia (10 psi). As a well-recognized method in this technical field, there is a sister range that includes the same ingredients as the real azeotrope. It not only exhibits properties that are almost exactly equivalent to the real azeotrope to be used for freezing or Others ----------------------- installed- -----. 玎 ---- ~ · M. (-^-Contrary note -事 ^ Ranchang wrote this page). This paper is again applicable to the Chinese National Standard (CNS> A4 specifications (210 X 297 male cage) 81.9.20,000 _ _ ~ / · * ·. Ff " rf ~ ·. Ministry of Economic Affairs Printed by KK Industrial and Consumer Cooperative of Central Bureau of Standards
Afi __ B<; 五、發明説明(4 ) 應用,但是它也將在其它的溫度和壓力下以固定沸點不在 沸嫌時去分雄成分豳之特性和傾向來展現和真實的共沸混 合物幾乎完全相當的性質。 其它的氟碳氫化合物也能被加到HFC-32和丙烷的恆定沸 點混合物中而不用改變姐合物的幾乎完全像共沸混合物之 性質。代表性的氟碳氫化合物能被添加到本發明的恆萣沸 黏溻合物中,包括氯二氟甲烷 (HCFC-22)、五氟乙烷 < H F C - 1 2 5 )、過氟丙烷(F 0*2 1 8 ) 、1 ,1 ,2,2 —四 氟乙烷 (HCF-134)、1一氛一 1 . 1 ,2,2 —四氟乙烷 (HCFC-124) 、1,1,1,2,3,3·3 —七氟丙烷 (HFC-227ea)、 1,1,1,2,2,3, 3—七氟丙烷 (HFC-227ca)、 1 , 1 , 1 _三氟乙烷(HFC-143a)、三 氟乙烷 (HFC-23) 、 1 , 1 -二氟乙烷 (HFC-152a)以及 氟乙烷(HFC-161)。 本發明的氟碳姐合物中常常加入添加劑,包括潤滑劑、 腐牲抑制劑、安定劑和染料。 除了冷凍應用之外,本發明的新奇恆定沸點姐合物做為 氣溶膠推進劑、熱傳媒介、氣體電介質、滅火劑、聚合物 膨脹劑也很有效用,例如做為聚烯烴和聚氨基甲酸酯之用 ,Μ及用做動力循環適用流賭。 在此所描述的姐合能夠藉著凝縮恆定沸點姐合物並在随 後蒸發這種組合物來提供冷凍•例如凝縮被冷卻體鄰近的 部份。此外,這些姐合物能被用來提供熱悬,舉例而這, 在熱泵中•藉著蒸發被加熱體鄰近的組合並在随後凝縮恆 -------------------------裝——----.玎----1 0 (^t:K,._T背面之注念事項再填寫本頁) . 本紙張又度適用中國國家標準(CNS)甲4峴格(210 X 297公釐) 81.9.20,000 210950 A 6 B(; 五、發明説明(5 ) f飧"'"•:'-,!背面之注*事項再塡寫本1) 定沸點姐合物。 、 本發明的實質上恆定沸點姐合物之應用淌除了糸統操作 中成份分豳的問題,因為這些姐合物實質上作用的像一個 單一物質。 和具有臭氧消耗潛力0.25的冷凍劑502互相比較之下, 本發明的組合物具有臭氧消耗潛力零。 、 實例1 * 對二氟甲烷和丙烷的混合物做了相位研免,其中姐合物 改變了,並且在恆溫-15.310測量蒸汽壓力。獲得一種共 沸化合物姐合物,正如觀察得來的最大蒸汽®所證明的, 並經證實如下: 二氟甲烷=大約70重量百分比 丙烷=大約30重量百分比 蒸汽壓=在-15.3Ό時約為4832托 在其它溫度所做的相位研究表示共沸化合物的改變如下 經濟部中央標準局員工消費合作社印製 (a) 二氟甲烷=大約72重最百分比 丙烷=大約28重量百分比 蒸汽壓=在251C時約為15997托 (b) 二氟甲烷=大約74重量百分比 7 本紙張又度適用中國國家標準(CNS)甲4规格(210 X 297公釐) 81.9.20,000 2199o〇 Λ 6 __BG _ 五、發明説明(6 ) 丙烷=大約2S重量百分比 蒸汽壓=在5 0 時約為 2 8 9 5 4托 (α二氟甲烷=大約S8重量百分比 丙烷=大約32重量百分比 蒸汽壓=在-5〇υ時約為1216托 實例2 在二氟甲烷和丙烷的恆定沸點姐合物做了 一個相位研究 來證明在251C蒸汽損失期間最低的分器ΙΜ及蒸汽壓和姐成 之變化。最初液鸦(IQ)、最後液體(FQ)、最初蒸汽 (0)、最後蒸汽(I)、蒸汽壓Μ及蒸汽壓從最初蒸汽壓的 變化都要加Μ研究以便決定在姐合物和蒸汽壓的蒸汽漏損 效懕,如同下列表1所示 --------------1---------裝------1Τ---ί 丨線 f^tlr-""面 >/;i"f;fi’ 冉塡寫本頁) 經濟部中央標準屬員工消費合作社印製 81.9.20,000 本紙張又度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 2i9Do〇 Λ 6 m 五、發明説明(7 ) 樣品 混合物 的椹牛 姐 合 重量百 二氱田榇 物 分比 丙烷 蒸汽壓 i D 55 i a ) 蒸汽壓變化 (d s丨a百分蜜) IQ 0 70.0 3 0' 0 310.0 0 0 0 72.2 27.8 310.0 0 1 50 71.9 28.1 309.9 0 . 03 FQ 50 67.9 32 . 1 309.9 0 . 03 IQ 0 80.0 20.0 309.3 0 0 0 74.3 25.7 309.3 0 1 50 76.0 24.0 307.0 0 . 7 FQ 50 85.1 14.9 307.0 0 . 7 IQ 一 0 90.0 10.0 301.5 0 0 0 .78.7 21.3 301.5 0 1 50 89.3 10.7 273 . 9 9 . 2 FQ 50 97 . 4 2 . 6 273 . 9 9 . 2Afi __ B <; Fifth, the description of the invention (4) is applied, but it will also show the true azeotropic mixture at other temperatures and pressures with a fixed boiling point and the characteristics and tendency of the male component to be separated when it is not boiling. Completely equivalent in nature. Other fluorocarbons can also be added to the constant boiling point mixture of HFC-32 and propane without changing the sister compound's almost completely azeotropic mixture properties. Representative fluorocarbon compounds can be added to the constant boiling boiling compounds of the present invention, including chlorodifluoromethane (HCFC-22), pentafluoroethane < HFC-1 2 5), perfluoropropane (F 0 * 2 1 8), 1, 1, 2, 2-tetrafluoroethane (HCF-134), 1 atmosphere-1.1, 2, 2, 2-tetrafluoroethane (HCFC-124), 1 , 1,1,2,3,3 · 3-heptafluoropropane (HFC-227ea), 1,1,1,2,2,3,3-heptafluoropropane (HFC-227ca), 1, 1, 1, 1_trifluoroethane Alkane (HFC-143a), trifluoroethane (HFC-23), 1,1-difluoroethane (HFC-152a) and fluoroethane (HFC-161). Additives are often added to the fluorocarbon compound of the present invention, including lubricants, putrefaction inhibitors, stabilizers and dyes. In addition to freezing applications, the novel constant boiling point compound of the present invention is also very effective as an aerosol propellant, heat transfer medium, gas dielectric, fire extinguishing agent, polymer expansion agent, such as polyolefin and polyurethane For esters, Μ and used as power cycle are suitable for flow gambling. The sisters described here can provide freezing by condensing a constant boiling sister compound and subsequently evaporating this composition. For example, condensing the portion adjacent to the object to be cooled. In addition, these sister compounds can be used to provide thermal suspension, for example, and this, in the heat pump • by evaporating the adjacent combination of the heated body and then condensing constant ------------- ------------ 装 ——----. 玎 ---- 1 0 (^ t: K, ._ T Note on the back of the page and then fill out this page). This paper is again Applicable to the Chinese National Standard (CNS) A 4 Dange (210 X 297 mm) 81.9.20,000 210950 A 6 B (; 5. Description of the invention (5) f 飧 " '" •:'-,! * The matter will be written in 1) The sister compound with a fixed boiling point. The application of the substantially constant boiling point compound of the present invention eliminates the problem of component separation in the operation of the system, because these compounds essentially act like a single substance. Compared with the refrigerant 502 having an ozone depletion potential of 0.25, the composition of the present invention has zero ozone depletion potential. , Example 1 * Phase-exemption was performed on the mixture of difluoromethane and propane, where the sister compound was changed, and the steam pressure was measured at a constant temperature of 15.310. A sister compound of an azeotropic compound was obtained, as evidenced by the observed maximum steam®, and confirmed as follows: difluoromethane = approximately 70 weight percent propane = approximately 30 weight percent vapor pressure = approximately at -15.3Ό A phase study conducted at 4832 Torr at other temperatures indicated that the azeotrope changes are as follows: Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs (a) Difluoromethane = approximately 72 weight percent propane = approximately 28 weight percent vapor pressure = at 251C When the time is about 15997 torr (b) difluoromethane = about 74% by weight 7 This paper is again applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm) 81.9.20,000 2199o〇Λ 6 __BG _ V. Invention Description (6) Propane = about 2S weight percent vapor pressure = about 2 8 9 5 4 Torr at 50 (α difluoromethane = about S8 weight percent propane = about 32 weight percent vapor pressure = at -5〇υ Approximately 1216 Torr Example 2 A phase study was conducted on the constant boiling point compound of difluoromethane and propane to prove the lowest splitter IM and the change in vapor pressure and sister temperature during the 251C steam loss. Initial liquid crow (IQ) , The post-liquid (FQ), initial steam (0), final steam (I), steam pressure M and the change of steam pressure from the initial steam pressure should be studied by M in order to determine the steam leakage effect in the sister compound and steam pressure , As shown in Table 1 below -------------- 1 --------- installed ------ 1Τ --- ί 丨 line f ^ tlr- " " 面 >/; i "f; fi 'Ran Cheng wrote this page) Printed by the Ministry of Economy Central Standards Staff Consumer Cooperative 81.9.20,000. 297 mm) 2i9Do〇Λ 6 m V. Description of the invention (7) The total weight of the sample mixture is 200% of the total weight of the fermented material. The vapor pressure of propane i D 55 ia) Variation of vapor pressure (ds 丨 a 100% honey ) IQ 0 70.0 3 0 '0 310.0 0 0 0 72.2 27.8 310.0 0 1 50 71.9 28.1 309.9 0. 03 FQ 50 67.9 32. 1 309.9 0. 03 IQ 0 80.0 20.0 309.3 0 0 0 74.3 25.7 309.3 0 1 50 76.0 24.0 307.0 0. 7 FQ 50 85.1 14.9 307.0 0. 7 IQ 1 0 90.0 10.0 301.5 0 0 0 .78.7 21.3 301.5 0 1 50 89.3 10.7 273. 9 9. 2 FQ 50 97. 4 2. 6 273. 9 9. 2
J---------裝------訂---1 I ^ f^t"··?#面之:;i"事項再塡寫本莨W 經濟部中央標準局S工消費合作社印製 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 81.9.20,000 219950 五、發明説明(8) 上表的數據表示二氟甲烷和丙烷的混合物(它代表本發 明之姐合物的極值)只Μ蒸發的最初混合物之5〇π而有 9.2Χ的最大蒸汽懕變化者是賁霣上恆定沸點。如果在25 υ 恆溫下混合物漏損50¾之後,其蒸汽壓的變少於105Κ,則 這種混合物可被視為賁質上恆定沸點。 * 霣例3 本發明的實質上恆定沸黏姐合物對單一化合物HCFC - 22 ,冷凍劑-502M及五氟乙烷(HFC-125)的冷凍性質評估 列示在表2中。 (^'"^"背面之注念事項'再壜寫本頁) —裝, -έ . •線- 經濟部中央標準局員工消費合作社印s 衣紙張又度適用中國囷家標準(CMS)甲4规格(210 X 2町公釐) 10 - 81.9.20,000 219950J --------- installed ------ ordered --- 1 I ^ f ^ t " ··? #Face:; i " The matter is written again W Central Ministry of Economic Affairs S The paper scale printed by the Industrial and Consumer Cooperatives is applicable to the Chinese National Standard (CNS) A4 specifications (210 X 297 mm) 81.9.20,000 219950 V. Description of the invention (8) The data in the table above indicates the mixture of difluoromethane and propane (it Represents the extreme value of the sister compound of the present invention) Only 50 π of the initial mixture evaporated and the maximum vapor change of 9.2X is the constant boiling point on the beast. If the mixture's vapor pressure changes less than 105K after the leakage of 50¾ at a constant temperature of 25 υ, this mixture can be regarded as a constant boiling point on the substrate. * Example 3 The freezing properties of the substantially constant boiling viscosity compound of the present invention for a single compound HCFC-22, refrigerant -502M and pentafluoroethane (HFC-125) are listed in Table 2. (^ '" ^ " Notes on the back' will be written on this page again) — Installed,-έ. • Thread-The Ministry of Economic Affairs, Central Standards Bureau, Employee Consumer Cooperatives prints clothes and paper again applicable to the Chinese standard (CMS) ) A 4 specifications (210 X 2 mm) 10-81.9.20,000 219950
Afi Bfi 五、發明説明(9) _2 洽凍鏞牧的hh » 丙烷 經濟部中央標準局®:工消費合作社印*'1衣 32/Propane 五氟乙烷(重營百分fch 成 份 Η C F Γ - ?. ? R - 5 0 2 H F Γ. - 1 2 5 8 0/20 7 0/20 蒸發 器 溫度 Τ -30 -30 -30 -30 -30 蒸發 器 壓力 (PS i a) 19.6 24.0 26.7 34.7 45.8 冷凝 器 溫度 °F 115 115 115 115 115 冷凝 器 壓力 (P s 1 at 258 282 327 420 389 懕縮 機 .. ‘ 釋放 溫度 T 303 239 223 337 273 績效 係數 1 . 97 1.89 1.69 1.83 2.06 冷凍 能力 (B t u /分鐘) 76.6 80.0 79.4 124 151 - 11 - 本紙張尺度適用t國國家標準(CNS)甲4規格(210 X 297公釐) 81.9.20,000 ---------------^ --------裝------#----^ I線 (--^--^面之注-革項再塡寫本頁) ^50 五、 發明_説明(10)Afi Bfi V. Description of the invention (9) _2 Hah, Qiao Yongyongmu »Propane Ministry of Economic Affairs Central Standards Bureau ®: Industrial and Consumer Cooperatives printed * '1 Yi 32 / Propane pentafluoroethane (percentage fch ingredients H CF Γ -?.? R-5 0 2 HF Γ.-1 2 5 8 0/20 7 0/20 Evaporator temperature T -30 -30 -30 -30 -30 Evaporator pressure (PS ia) 19.6 24.0 26.7 34.7 45.8 Condenser temperature ° F 115 115 115 115 115 Condenser pressure (P s 1 at 258 282 327 420 389 Compressor: 'Release temperature T 303 239 223 337 273 Coefficient of performance 1. 97 1.89 1.69 1.83 2.06 Freezing capacity (B tu / min) 76.6 80.0 79.4 124 151-11-This paper scale is applicable to the national standard (CNS) A 4 specifications (210 X 297 mm) of the country t 81.9.20,000 -------------- -^ -------- 装 ------ # ---- ^ I line (-^-^ face note-leather item and then write this page) ^ 50 V. Invention_ Description (10)
Af; 續效係數(C · ’它是測量冷凍 能力意味著在 是在蒸發器中每 於一涸固定的壓 對於蒸發器和 型化的冷凍遇期 烷(HFC-125)的 的共沸混合物比 高。HFC-32和丙 是HFC較高的容 對於蒸發器和 表的冷凍週期, 0 . P .) 能量效 蒸發器 次由冷 縮櫬排 冷凝器 ,列於 是淨冷凍效應對壓縮櫬作用的比率 率的—種方法。 中冷凍劑的焓之變化,換言之,就 凍劑所除去的熱量。冷凍能力是基 量。 而言*由顯示於表2的狀況加以典 實例弋的C · 0 . P .值比五氟乙 C · Ο * P ·值高,此外·· HFC-32和丙烷 R-502 和HCFC-22 的C · 0 . P .值來得 烷的共沸混合物有比HCFC-22 ,R-502或 量。 冷凝器而言,由顯示於表2的狀況加以代 能力是一個最重要的考慮變數。 實例4 本發明的賁質恆定沸點姐合之列示壓差是由每次製造時 在251的充點壓力與25T:的氣泡點懕力之差值來決定,為· 了能夠加以比較,成份範圃之外的混合物之必要懕力差要 給與。 ---------------一--------裝——----訂 (-也:,4-'背面之:;1念务項冉塡寫本頁) 經濟部中失標準局ιβ工消费合作社印製 本纸張尺度適用中國國家標準(CNS) Ψ 4規格(210 X 297公釐) 81.9.20,000 經濟部中央標準局員工消費合作社印製 219950 ΛΓ丨F.r, 五、發明説明(11 ) ^_3 - 冷凍劑姐成 露點 氣泡點 差異 (重畺百分 Hi ) ( ρ a i a ) ( p a i a ) ( p a i a ) 院40烷35烷30 甲· + 甲 + 甲 + 氟60氟60氟70 /IV iv /fv二 二 二 烷28烷20烷10烷10烷5)烷1) 甲 + 甲 + 甲 V 甲 + 甲 + 甲 + 氟72氟80氟85氟90鎮95氟99 /IV /IV /IV . /IV /IV二 二 二 二 二 二 丙 烷 丙 烷 丙 烷 丙 烷 丙 烷 丙 烷 丙 烷 丙 烷 丙 269 290 . 307.7 38 309.5 19 307.2 310. 307.4 309.2 307.8 309. 309 310. 306 . 277 307.0 301.5 287,6 19 259.2 18 - 13 - 本纸張尺度適用中國國家標準(CNS)甲4規格(2i0 X 297公釐) 81.9.20,000 ---------------^ --------裝——----'玎----1 -_ 「-“0^二斤面之:;1--事項再塡寫本頁) 1 219950Af; The coefficient of continuity (C · 'It is a measure of the freezing capacity means that it is an azeotropic mixture for the evaporator and the type of frozen encounter alkanes (HFC-125) at a fixed pressure in the evaporator The ratio is higher. HFC-32 and C are the higher capacity of HFC. For the refrigeration cycle of the evaporator and the table, 0. P.) The energy-efficient evaporator is divided by the cold-shrinking condenser and the net freezing effect is listed on the compression. The ratio of the rate-a method. The change in the enthalpy of the medium refrigerant, in other words, the heat removed by the refrigerant. The freezing capacity is the basis. In terms of *, the C · 0. P. Values exemplified by the conditions shown in Table 2 are higher than pentafluoroethane C · Ο * P · values, in addition · HFC-32 and propane R-502 and HCFC-22 The C · 0. P. Value to obtain the azeotrope of alkane has an amount higher than that of HCFC-22, R-502. For condensers, the ability to be replaced by the conditions shown in Table 2 is the most important consideration variable. Example 4 The pressure difference of the present constant boiling point of the present invention is determined by the difference between the charging point pressure of 251 and the bubble point force of 25T: every time it is manufactured, in order to be able to be compared, the ingredients The necessary force difference of the mixture outside the Fan Pu must be given. --------------- One -------- installed -------- ordered (-also:, 4- 'on the back :; 1 read the item Ran 塡This page is printed by the Standards and Loss Bureau of the Ministry of Economic Affairs. This paper is printed in accordance with the Chinese National Standard (CNS) Ψ 4 specifications (210 X 297 mm). 81.9.20,000 Printed by the Staff Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 219950 ΛΓ 丨 Fr, Fifth, the description of the invention (11) ^ _3-The difference in the bubble point of the refrigerant dew point (percentage of weight) (ρ aia) (paia) (paia) Hospital 40 alkyl 35 alkyl 30 A + A + A + fluorine 60 fluorine 60 fluorine 70 / IV iv / fv didioxane 28 alkane 20 alkane 10 alkane 10 alkane 5) alkane 1) A + A + A + A V + A + A + A + F 72 F 80 F 85 F 90 Town 95 Fluorine 99 / IV / IV / IV. / IV / IV 222 212 Propane Propane Propane Propane Propane Propane Propane Propane Propane 269 290. 307.7 38 309.5 19 307.2 310. 307.4 309.2 307.8 309. 309 310. 306 . 277 307.0 301.5 287,6 19 259.2 18-13-This paper scale is applicable to the Chinese National Standard (CNS) A 4 specifications (2i0 X 297 mm) 81.9.20,000 ------------- -^ -------- outfit -------- '玎 ---- 1 -_ 「-“ 0 ^ Two catties :; 1-- matter again Chen wrote on this page) 1219950
An Bf; 五、發明説明(12)這種结果顯示在251C時荛點和泡沫點壓力差只有微小的 差異。這表示這個姐合物不會進行重大的份豳•而且作用 的像是具有一種質上恆定沸點的單一化合物。 {-":"二,:、-'而>/ ‘,-•.-广項冉塡寫本頁) 經濟部中央標準局員工消费合作社印*'*衣 - 14 - 本紙張又度適用中國國家標準(CNS)甲4規格(210 X 297公縈) 81.9.20,000An Bf; 5. Description of the invention (12) This result shows that there is only a slight difference in the pressure difference between the black point and the foam point at 251C. This means that this sister compound will not make a significant share • and acts like a single compound with a qualitatively constant boiling point. {-": " Second ::,-'And> /',-• .-Guangxiang Rancheng wrote this page) Printed by the Ministry of Economic Affairs Central Standards Bureau Employee Consumer Cooperative *** Clothes-14-This paper Applicable to China National Standard (CNS) A 4 specifications (210 X 297 Gongyu) 81.9.20,000
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/767,846 US5234613A (en) | 1991-09-30 | 1991-09-30 | Substantially constant boiling compositions of difluoromethane and propane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| TW219950B true TW219950B (en) | 1994-02-01 |
Family
ID=51348042
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW81108598A TW219950B (en) | 1991-09-30 | 1992-10-28 |
Country Status (1)
| Country | Link |
|---|---|
| TW (1) | TW219950B (en) |
-
1992
- 1992-10-28 TW TW81108598A patent/TW219950B/zh active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP2780873B2 (en) | Refrigerant composition containing hexafluoropropane and hydrofluorocarbon | |
| US5670079A (en) | Azeotropic and azeotrope-like compositions of a hydrofluorocarbon and a hydrocarbon | |
| JP3237850B2 (en) | Hydrofluorocarbon composition | |
| JP3369559B2 (en) | Composition of difluoromethane and tetrafluoroethane | |
| US5441659A (en) | Compositions including a fluoroamine and a second component | |
| EP0682683B1 (en) | Compositions of a hydrofluorocarbon and a hydrocarbon | |
| US5234613A (en) | Substantially constant boiling compositions of difluoromethane and propane | |
| JPH06503828A (en) | Constant boiling composition of fluorinated hydrocarbons | |
| CN101400756B (en) | Working medium for heat cycle, rankine cycle system, heat pump cycle system, and refrigeration cycle system | |
| JPH06503832A (en) | Constant boiling composition of fluorinated hydrocarbons | |
| CN102959036A (en) | Heat transfer compositions | |
| EP0883662B1 (en) | Azeotropic compositions of cyclopentane | |
| JP2000178543A (en) | Azeotropic or azeotropic composition | |
| EP0606360B1 (en) | Substantially constant boiling compositions of difluoromethane and trifluoroethane or perfluoroethane | |
| EP0592555A1 (en) | Azeotropic or azeotrope-like compositions of pentafluoroethane and propane or isobutane. | |
| TW219950B (en) | ||
| US5248433A (en) | Binary azeotropic mixtures of octafluoropropane and fluoroethane | |
| TW305874B (en) | ||
| US5447646A (en) | Compositions of 2,2-dichloro-1,1,1-trifluoroethane and pentafluoropropane | |
| WO1994004629A1 (en) | Substantially constant boiling mixtures of 1,1,1,2-tetrafluoroethane, dimethyl ether and isobutane | |
| JPH07508519A (en) | Mixture of pentafluoroethane and trifluoroethane | |
| CN105925248A (en) | Environment-friendly mixed refrigerant used for substituting dichlorofluoromethane | |
| CN102181269A (en) | Mixed working medium for heat pump system |