• 专利附录
  • 专利说明
  • 权利要求
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    • 专利摘要:
    Disclosed are azeotropic compositions comprising 1,1,1,3,3-pentafluorobutane, water and hydrocarbons selected from the group consisting of n-pentane, isopentane, cyclopentane, n-hexane and isohexane The composition is environmentally preferred for use as a refrigerant, aerosol propellant, weighed amount of inhalant, blowing agent for polymer foams, heat transfer media and gaseous dielectrics.
    公开号:KR20040012884A
    申请号:KR10-2003-7015723
    申请日:2002-06-03
    公开日:2004-02-11
    发明作者:보그단메리씨.；쿡케인디.；팜항티.；크노펙게리엠.；싱라지브알.
    申请人:허니웰 인터내셔널 인코포레이티드；
    IPC主号:
    专利说明:

    Azeotrope-like Compositions of Pentafluorobutane
    [2] Fluorocarbon based fluids have been widely used in many industrial applications including refrigerants, aerosol propellants, blowing agents, heat transfer media and gaseous dielectrics. Due to the suspicious environmental issues associated with the use of some of these fluids, the use of fluids with low or no ozone depletion potential, such as hydrofluorocarbons ("HFC's"), are required.
    [3] Therefore, it is preferred to use fluids that do not contain chlorofluorocarbons ("CFC's") or hydrochlorofluorocarbons ("HCFCs"). Moreover, it is known to use single component fluids or azeotropic mixtures that do not fractionate upon boiling or evaporation. However, the preparation of new, environmentally safe, non-fractionating mixtures is difficult because the formation of azeotropes is not easily predicted.
    [4] There is a need in the art to replace CFC's and HCFCs and to develop new fluorocarbon based mixtures that are more environmentally safer. Of particular interest are combinations or mixtures comprising fluorocarbons and non-fluorocarbons with low or no ozone depletion potential. Such mixtures are the subject of the present invention. The term fluorocarbon, as used herein, includes CFCs and HCFCs.
    [1] The present invention relates to novel compositions comprising fluorocarbons, hydrocarbons and water.
    [5] 1 is a graph showing a boiling point curve for a ternary mixture comprising HFC-365mfc, isohexane and water.
    [6] We have developed several compositions that are useful as replacements for CFCs and HCFCs. In one embodiment, the present invention provides an azeotropic composition comprising pentafluorobutane, water and a hydrocarbon selected from the group consisting of n-pentane, isopentane, cyclopentane, n-hexane and isohexane.
    [7] Preferred compositions of the present invention provide alternatives with zero environmentally desirable ozone depletion potential for CFC's and HCFC's currently used. Moreover, the composition of the present invention makes the composition a better CFC and HCFC replacement than any of the materials of HFC-365mfc, n-pentane, isopentane, cyclopentane, n-hexane, isohexane or water alone.
    [8] Composition
    [9] The composition of the present invention is an azeotropic composition. As used herein, the term "azeotrope-like" is understood in a strict sense to a broad sense including both azeotropic compositions and compositions that behave like azeotropic mixtures.
    [10] In basic principle, the thermodynamic state of a fluid is defined by pressure, temperature, liquid composition and gas composition. An azeotrope is a system of two or more components having the same liquid composition and gas composition at a given pressure and temperature. In practice, this means that the components of the azeotrope have a constant boiling point or do not separate during phase change.
    [11] Azeotropic compositions have a constant boiling point or essentially a constant boiling point. That is, in the azeotropic composition, the composition of the vapor formed during boiling or evaporation is the same as or substantially the same as the original liquid composition. Thus, when boiling or evaporating, the liquid composition, even if it changes, is minimal or negligible. This is in contrast to non-azeotropic compositions where the liquid composition changes to a significant extent during boiling or evaporation. All azeotropic compositions of the invention within a specific composition range within and above the ranges described above are azeotropic.
    [12] The azeotropic composition of the present invention may include additional components that do not form a new azeotropic or azeotropic system or additional components not included in the first distillation cut. The first distillation cut is the first dose (cut) taken after the distillation column is stable under total reflux conditions. One method of determining whether the addition of components intended to deviate from the scope of the present invention forms a new azeotropic or azeotropic system is a composition having said components under conditions where the non-azeotropic mixture is expected to separate into their respective components. Is to distill the sample. If the mixture comprising the additional ingredients is non-azeotropic or non-azeotropic, the additional ingredients will be fractionated from the azeotropic or azeotropic-like ingredients. If the mixture is azeotropic, a small amount of the first distillation cut will be obtained which contains all the mixture components having a constant boiling point or behaving like a single substance.
    [13] From this, another feature of the azeotropic composition is that there is a composition range containing the same components in different proportions such that the azeotropic or boiling point is the same. All such compositions are included in the terms "azeotrope-like" and "constant boiling". For example, upon pressure change, the composition of a given azeotrope will change at least slightly as the boiling point of the composition changes. Thus, the azeotrope of A and B shows a unique type of relationship, but the composition changes with temperature and / or pressure. This indicates that in the azeotropic composition, there is a composition range that includes the same components in different proportions that are azeotropic. All such compositions are intended to be included in the term azeotropes used in the present invention.
    [14] Pentafluorobutane / n-pentane / water
    [15] In one embodiment of the present invention, an azeotropic composition comprising HFC-365mfc, n-pentane and water is provided. Preferably, the new azeotropic composition of the present invention comprises an effective amount of HFC-365mfc, n-pentane and water. As used herein, the term "effective amounts" refers to the amount of each component that forms the azeotropic composition of the invention when combined with other ingredients or components.
    [16] In these embodiments, an azeotropic composition is provided which comprises and preferably consists essentially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of n-pentane and about 1-80 parts by weight of water. . Such compositions are characterized by a boiling point of about 36 ° C. ± 4 ° C., preferably ± 2 ° C., more preferably ± 1 ° C. at about 760 mmHg.
    [17] Preferred, more preferred and most preferred compositions according to the invention are shown in Table 1. The numerical ranges in Table 1 are understood to include the term "about."
    [18] TABLE 1
    [19] ingredient Preferred range (% by weight) More preferred range (% by weight) Most preferred range (% by weight) HFC-365mfc 10-98 40-98 60-98 n-pentane 80-1 40-1 30-1 water 80-1 40-1 30-1
    [20] Pentafluorobutane / isopentane / water
    [21] In one embodiment of the present invention, an azeotropic composition comprising HFC-365mfc, isopentane and water is provided. Preferably, the new azeotropic composition of the present invention comprises an effective amount of HFC-365mfc, isopentane and water.
    [22] In these embodiments, an azeotropic composition is provided which comprises and preferably consists essentially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of isopentane and about 1-80 parts by weight of water. Such compositions are characterized by a boiling point of about 36 ° C. ± 4 ° C., preferably ± 2 ° C., more preferably ± 1 ° C. at about 760 mmHg.
    [23] Preferred, more preferred and most preferred compositions according to the invention are shown in Table 2. The numerical ranges in Table 2 are understood to include the term "about."
    [24] TABLE 2
    [25] ingredient Preferred range (% by weight) More preferred range (% by weight) Most preferred range (% by weight) HFC-365mfc 10-98 40-98 60-98 Isopentane 80-1 40-1 30-1 water 80-1 40-1 30-1
    [26] Pentafluorobutane / cyclopentane / water
    [27] In one embodiment of the present invention, an azeotropic composition comprising HFC-365mfc, cyclopentane and water is provided. Preferably, the new azeotropic composition of the present invention comprises an effective amount of HFC-365mfc, cyclopentane and water.
    [28] In these embodiments, an azeotropic composition is provided which comprises and preferably consists essentially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of cyclopentane and about 1-80 parts by weight of water. Such compositions are characterized by a boiling point of about 36 ° C. ± 4 ° C., preferably ± 2 ° C., more preferably ± 1 ° C. at about 760 mmHg.
    [29] Preferred, more preferred and most preferred compositions according to the invention are shown in Table 3. The numerical ranges in Table 3 are understood to include the term "about."
    [30] TABLE 3
    [31] ingredient Preferred range (% by weight) More preferred range (% by weight) Most preferred range (% by weight) HFC-365mfc 10-98 40-98 60-98 Cyclopentane 80-1 40-1 30-1 water 80-1 40-1 30-1
    [32] Pentafluorobutane / n-hexane / water
    [33] In one embodiment of the present invention, an azeotropic composition comprising HFC-365mfc, n-hexane and water is provided. Preferably, the new azeotropic composition of the present invention comprises an effective amount of HFC-365mfc, n-hexane and water.
    [34] In these embodiments, an azeotropic composition is provided which comprises and preferably consists essentially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of n-hexane and about 1-80 parts by weight of water. . Such compositions are characterized by a boiling point of about 36 ° C. ± 4 ° C., preferably ± 2 ° C., more preferably ± 1 ° C. at about 760 mmHg.
    [35] Preferred, more preferred and most preferred compositions according to the invention are shown in Table 4. The numerical ranges in Table 4 are understood to include the term "about".
    [36] TABLE 4
    [37] ingredient Preferred range (% by weight) More preferred range (% by weight) Most preferred range (% by weight) HFC-365mfc 10-98 40-98 60-98 n-hexane 80-1 40-1 30-1 water 80-1 40-1 30-1
    [38] Pentafluorobutane / isohexane / water
    [39] In one embodiment of the invention, there is provided an azeotropic composition comprising HFC-365mfc, isohexane and water. Preferably, the new azeotropic composition of the present invention comprises an effective amount of HFC-365mfc, isohexane and water.
    [40] In these embodiments, an azeotropic composition is provided which comprises and preferably consists essentially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of isohexane and about 1-80 parts by weight of water. Such compositions are characterized by a boiling point of about 36 ° C. ± 4 ° C., preferably ± 2 ° C., more preferably ± 1 ° C. at about 760 mmHg.
    [41] Preferred, more preferred and most preferred compositions according to the invention are shown in Table 5. The numerical ranges in Table 5 are understood to include the term "about."
    [42] TABLE 5
    [43] ingredient Preferred range (% by weight) More preferred range (% by weight) Most preferred range (% by weight) HFC-365mfc 10-98 40-98 60-98 Isohexane 80-1 40-1 30-1 water 80-1 40-1 30-1
    [44] A boiling point curve for this embodiment of the invention is shown in FIG. 1. Table 6 shows the boiling point data for HFC-365mfc / isohexane / water according to a preferred embodiment of the present invention.
    [45] Use of the composition
    [46] The composition of the present invention can be widely used as a substitute for CFCs and HCFCs. For example, the compositions of the present invention are usefully used as solvents, blowing agents, refrigerants, cleaning agents and aerosols.
    [47] One embodiment of the present invention relates to a blowing agent comprising one or more azeotropic compositions of the present invention. In another embodiment, the present invention provides a foam composition, preferably to provide a polyurethane and polyisocyanurate foam composition and a method for preparing the foam. In such foams, one or more azeotropic compositions of the invention are included as foaming agents in the foaming composition, which foaming composition is preferably foamed by reaction and foaming under suitable conditions, as is well known in the art. It includes one or more additional ingredients that can form water or cellular structures. The process of the invention preferably comprises providing such a foamable composition and reacting it under conditions effective to obtain a foam and preferably a closed cell foam. The invention also relates to foams and preferably closed cell foams prepared from polymer foam formulations containing blowing agents comprising the azeotropic composition of the invention.
    [48] Any method well known in the art, as described in "Polyurethanes Chemistry and Technology," Volumes I and II, Saunders and Frisch, 1962, John Wiley and Sons, New York, NY, incorporated herein by reference. This may be used or applied to use in connection with the foam implementations of the invention. In general, such preferred methods include isocyanate, polyol or polyol mixtures, blowing agents or blowing agent mixtures comprising one or more compositions of the present invention, and other materials such as catalysts, surfactants and any flame retardant, colorant or other additives. To prepare a polyurethane or polyisocyanurate foam. In many applications it is convenient to provide the polyurethane or polyisocyanurate foam components in a pre-mixed formulation. Most typically, the foam formulation is pre-mixed in two components. The isocyanate and any particular surfactants and blowing agents comprise the first component, commonly referred to as "component A". The polyols or polyol mixtures, surfactants, catalysts, blowing agents, flame retardants and other isocyanate-reactive components form a second component, commonly referred to as "component B". Thus, polyurethane or polyisocyanurate foams can be applied manually in small quantities and in blocks, slabs, laminates, pour-in-place panels and other items, and spray applications. In order to form the foams, foams, and the like, it is easily prepared by blending the A and B subcomponents with each other preferably by a mechanical mixing method. Optionally, other ingredients such as flame retardants, colorants, auxiliary blowing agents and even other polyols may be added to the mixing head or reaction site in a third stream. However, most conveniently, they are all incorporated into one B-component as described above.
    [49] The compositions of the invention can also be used to prepare thermoplastic foams. For example, conventional foamed polyurethane and isocyanurate blends can be prepared into rigid foams by combining with azeotropic-compositions in conventional manner.
    [50] Azeotropic mixtures comprising HFC-365mfc of the present invention are particularly suitable as foaming agents for foams in which the foams foamed with HFC-365mfc have relatively low initial and aging thermal conductivity and good dimensional stability at low temperatures. Particularly of interest are the azeotropic compositions of the present invention further comprising, for example, other hydrofluorocarbons such as difluoromethane (HFC-32); Difluoroethane (HFC-152); Trifluoroethane (HFC-143); Tetrafluoroethane (HFC-134); Pentafluoroethane (HFC-125); Pentafluoropropane (HFC-245); Hexafluoropropane (HFC-236); Heptafluoropropane (HFC-227); And other zero depleting potentials of inert gases such as air, nitrogen, carbon dioxide. Where isomers of the hydrofluorocarbons described above are present, each isomer may be used alone or in the form of a mixture.
    [51] Dispersants, cell stabilizers and surfactants may also be incorporated into the blowing agent mixture. A surfactant better known as silicone oil is added as cell stabilizer. Several representative materials are sold under the trade names DC-193, B-8404 and L-5340, which are generally U.S. Polysiloxane polyoxyalkylene block co-polymers such as those disclosed in patents 2,834,748, 2,917,480, and 2,846,458. Other optional additives to the blowing agent mixture include tri (2-chloroethyl) phosphate, tri (2-chloropropyl) phosphate, tri (2,3-dibromopropyl) -phosphate, tri (1,3-dichloropropyl Flame retardants such as phosphate, diammonium phosphate, various halogenated aromatic compounds, antimony oxide, aluminum trihydrate, polyvinyl chloride, and the like.
    [52] In other embodiments, the azeotropic compositions of the invention may be used alone or in combination with other known propellants in the sprayable composition. The injectable composition comprises, consists essentially of, and consists essentially of, and consists of, the propellant comprising the material to be sprayed and the azeotropic composition of the invention. Inert ingredients, solvents and other materials may also be present in the sprayable mixture. Preferably the sprayable composition is an aerosol. Suitable materials to be sprayed include, but are not limited to, anti-asthma, as well as cosmetic materials such as deodorants, fragrances, hair sprays, cleansers and polishing agents. Medicines such as agents and anti-halitosis agents.
    [53] In another process implementation, a method of removing water from HFC-365mfc is provided, which method is from HFC-365, water and a group consisting of n-pentane, isopentane, cyclopentane, n-hexane, and isohexane. Distilling the mixture of selected hydrofluorocarbons to separate the azeotropic composition consisting essentially of HFC-365, the hydrofluorocarbon of the azeotropic composition and water. Thus, an azeotropic mixture composed of HFC-365, hydrofluorocarbons selected from the group consisting of water and n-pentane, isopentane, cyclopentane, n-hexane, and isohexane azeotrope is HFC-365mfc manufacturing process. It can be used to remove the bulk amount of water in the furnace. In another embodiment of the invention, the hydrofluorocarbon selected from the group consisting of HFC-365, water and n-pentane, isopentane, cyclopentane, n-hexane, and isohexane before carrying out the distillation step A method of phase separation of a mixture to remove bulk water is provided. Residual amounts of water on HFC-365mfc can be distilled off due to the presence of azeotropes. Subsequent distillation and multiple distillation may be used to remove other impurities with trace amounts of water to achieve the desired purity.
    [54] The components of the composition according to the invention may be known materials that are commercially available or may be prepared by known methods. Preferably, the components should be of sufficient high purity so that no adverse effects on the cooling or heating properties, constant boiling properties or blowing agent properties of the system are introduced. For measurable inhalers, current good manufacturing processes suitable for the production of these materials can be used.
    [55] Additional components may be added as needed to adjust the properties of the azeotropic compositions of the invention. As an example, oil dissolution aids may be added when the compositions of the present invention are used as refrigerant. Stabilizers and other materials may also be added to improve the properties of the compositions according to the invention.
    [56] Hereinafter, the present invention will be described in detail through examples. However, the following Examples do not limit the present invention.
    [57] Example 1
    [58] An ebulliometer consisting of a vacuum jacketed tube with a condenser on top was used. About 20 g of HFC-365mfc was charged into a scaffold, and isohexane was added little by little while increasing the measured amount, and water was added little by little while increasing the measured amount. When isohexane and water were added to HFC-365mfc, the temperature dropped, indicating that azeotropes with a minimum boiling point of three components were formed. At about 0.1-30% by weight of isohexane and about 0.1-30% by weight of water, the boiling point of the composition changed below about 3 ° C. The three component mixtures shown in Table 6 were investigated and the boiling point of the composition was changed by about 3 ° C. Thus, the composition exhibits azeotropic and / or azeotropic properties in the above range. 1 is a graph showing the boiling point data of Table 6.
    [59] TABLE 6
    [60]
    [61] Example 2
    [62] A scaffold consisting of a vacuum jacketed tube with a condenser on top was used. About 20 g of HFC-365mfc was charged to the scaffold, and n-pentane was added little by little with increasing measurement amount, and water was added little by little with increasing measurement amount. When n-pentane and water were added to HFC-365mfc, the temperature dropped, indicating that an azeotrope with a minimum boiling point of three components was formed. At about 0.1-30% by weight of n-pentane and about 0.1-30% by weight of water, the boiling point of the composition changed below about 3 ° C. Thus, the composition exhibits azetrope and / or azetrope-like properties in the above range.
    [63] Example 3
    [64] A scaffold consisting of a vacuum jacketed tube with a condenser on top was used. About 20 g of HFC-365mfc was charged to a boiling system, and then cyclopentane was added little by little with increasing measurement amount, and water was added little by little with increasing measurement amount. When cyclopentane and water were added to HFC-365mfc, the temperature dropped, indicating that azeotropes with a minimum boiling point of three components were formed. At about 0.1-30 wt% cyclopentane and about 0.1-30 wt% water, the boiling point of the composition changed below about 3 ° C. Thus, the composition exhibits azeotropic and / or azeotropic properties in the above range.
    [65] Example 4
    [66] A scaffold consisting of a vacuum jacketed tube with a condenser on top was used. About 20 g of HFC-365mfc was charged to a scaffold, and n-hexane was added little by little with increasing measurement amount, and water was added little by little with increasing measurement amount. When n-hexane and water were added to HFC-365mfc, the temperature dropped, indicating that azeotropes with a minimum boiling point of three components were formed. At about 0.1-30% by weight of n-hexane and about 0.1-30% by weight of water, the boiling point of the composition changed below about 3 ° C. Thus, the composition exhibits azeotropic and / or azeotropic properties in the above range.
    [67] Example 5
    [68] A scaffold consisting of a vacuum jacketed tube with a condenser on top was used. About 20 g of HFC-365mfc was charged into a scaffold, and isopentane was added little by little while increasing the measured amount, and water was added little by little while increasing the measured amount. When isopentane and water were added to HFC-365mfc, the temperature dropped, indicating that an azeotrope with a minimum boiling point of three components was formed. At about 0.1-30% by weight of isopentane and about 0.1-30% by weight of water, the boiling point of the composition changed below about 3 ° C. Thus, the composition exhibits azeotropic and / or azeotropic properties in the above range.
    [69] Example 6
    [70] This example shows data for heat associated with foams made using the blowing agent compositions of the present invention.
    [71] The following materials were used in Example 6 and Comparative Example 1.
    [72] Polyol A: Polyester polyol having an OH number of 240. It is commercially available from Stepan.
    [73] Isopentane: 2-methylbutane available as Borger Isopentane from Phillips 66 Company.
    [74] HFC-365mfc: 1,1,1,3,3-pentafluorobutane available from Solvay.
    [75] Surfactant A: Polysiloxane polyether copolymers commercially available from Goldschmidt.
    [76] Catalyst A: Inorganic potassium based amine commercially available from Air Products.
    [77] Catalyst B: Trimerization catalyst commercially available from Air Products.
    [78] Two foams ("Job # 00-26-1" and "Job # 00-26-2") are prepared in a general manner, commonly referred to as "handmixing". For each blowing agent or pair of blowing agents, a premix of polyols, surfactants and catalysts is prepared in the same proportions as shown in Table 7. About 100 g of each formulation is combined. The premix is mixed in a 32 oz paint can and stirred at about 1500 rpm using a Conn 2 "diameter ITC mixer until a uniform mixture.
    [79] Upon completion of mixing, the cans were covered and placed in a refrigerator controlled at 50 ° F. The foam blowing agent or pre-mixed pairs of blowing agents are also stored in a 50 ° F. pressure vessel. Ingredient A is stored in a sealed container at 70 ° F.
    [80] The pre-cooled blowing agent is added in the required amount to the premix. Stir the contents for 2 minutes with a Conn 2 "ITC mixing blade rotating at 1000 rpm. Then re-weigh the mixing vessel and contents. If weight loss exists, add blowing agent or mixture to solution to compensate for any weight loss. Then cover the cans and place in the refrigerator.
    [81] After the contents have cooled back to 50 ° F., remove the mixing vessel from the refrigerator for about 10 minutes and take it to the mixing site. Quickly add the pre-weighed portion of the A-component, isocyanurate to the B-component, mix the components at 3000 rpm for 10 seconds using a Conn 2 "diameter ITC mixing blade and 8" x8 "x4" cardboard cake Pour into the box and let it rise. Cream, initiation, gel and time without viscosity is recorded for each polyurethane foam sample.
    [82] Allow the foam to cure in a box at room temperature for at least 24 hours. After curing, the blocks are trimmed to a uniform size and the density is measured.
    [83] The k-factor of the foam is tested according to ASTM C518 with an average temperature of 36.5 ° C. The k-value results are shown in Table 7 below.
    [84] TABLE 7
    [85] Job #00-26-100-26-2 Ingredient (pbw) Polyol100100 Surfactants22 Catalyst A0.50.63 Catalyst B3.85.6 water1.72.8 HFC-365mfc12.810.3 Isopentane6.25 index250250 density2.052.05 Process temperature (iso / polyol) (℉)70/5070/50 k-value 36.5 ℉0.1470.172
    [86] Comparative Example 1
    [87] Three foams ("Job # 00-25-1", "Job # 00-25-2" and "Job # 00-25-3") were used with HFC-365 and water, and isopentane as blowing agent. Prepared without use, the resulting k-value is measured according to Example 6. For each blowing agent and blowing agent pair, a premix of polyol, surfactant and catalyst is prepared in the same proportions as shown in Table 8.
    [88] TABLE 8
    [89] Job #00-25-100-25-200-25-3 Ingredient (pbw) Polyol100100100 Surfactants222 Catalyst A0.250.50.63 Catalyst B2.83.85.6 water01.72.8 HFC-365mfc3825.520.5 Isopentane000 index250250250 density1.982.052.04 Process temperature (iso / polyol) (℉)70/5070/5070/50 k-value 36.5 ℉0.160.150.227
    [90] As shown in the table above, the k-values of the HFC-365mfc and blister foamed foams exhibit a lower (high) k-value compared to the k-values of the foams foamed with the corresponding HFC-365 / isopentane / water blowing agents. .
    [91] The azeotropic composition consisting of 1,1,1,3,3-pentafluorobutane, water and a hydrocarbon selected from the group consisting of n-pentane, isopentane, cyclopentane, n-hexane and isohexane is a refrigerant Environmentally suitable for use as aerosol propellants, weighed portions of inhalants, blowing agents for polymer foams, heat transfer media and gaseous dielectrics.
    权利要求:
    Claims (25)
    [1" claim-type="Currently amended] An azeotropic composition comprising 1,1,1,3,3-pentafluorobutane, water and a hydrocarbon selected from the group consisting of n-pentane, isopentane, cyclopentane, n-hexane and isohexane.
    [2" claim-type="Currently amended] The azeotropic composition according to claim 1, wherein the constant boiling point is about 36 ° C. ± 4 ° C. at about 760 mmHg.
    [3" claim-type="Currently amended] The azeotropic composition of claim 1 consisting substantially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of n-pentane and about 1-80 parts by weight of water.
    [4" claim-type="Currently amended] The azeotropic composition of claim 3 consisting substantially of about 40-98 parts by weight of HFC-365mfc, about 1-40 parts by weight of n-pentane and about 1-40 parts by weight of water.
    [5" claim-type="Currently amended] The azeotropic composition of claim 4 consisting substantially of about 60-98 parts by weight of HFC-365mfc, about 1-30 parts by weight of n-pentane and about 1-30 parts by weight of water.
    [6" claim-type="Currently amended] The azeotropic composition of claim 1 consisting substantially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of isopentane and about 1-80 parts by weight of water.
    [7" claim-type="Currently amended] 7. The azeotropic composition of claim 6, consisting substantially of about 40-98 parts by weight of HFC-365mfc, about 1-40 parts by weight of isopentane, and about 1-40 parts by weight of water.
    [8" claim-type="Currently amended] The azeotropic composition of claim 7 consisting substantially of about 60-98 parts by weight of HFC-365mfc, about 1-30 parts by weight of isopentane and about 1-30 parts by weight of water.
    [9" claim-type="Currently amended] The azeotropic composition of claim 1 consisting substantially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of cyclopentane and about 1-80 parts by weight of water.
    [10" claim-type="Currently amended] The azeotropic composition of claim 9 consisting substantially of about 40-98 parts by weight of HFC-365mfc, about 1-40 parts by weight of cyclopentane and about 1-40 parts by weight of water.
    [11" claim-type="Currently amended] The azeotropic composition of claim 10 consisting substantially of about 60-98 parts by weight of HFC-365mfc, about 1-30 parts by weight of cyclopentane and about 1-30 parts by weight of water.
    [12" claim-type="Currently amended] The azeotropic composition of claim 1 consisting substantially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of n-hexane and about 1-80 parts by weight of water.
    [13" claim-type="Currently amended] The azeotropic composition of claim 12 consisting substantially of about 40-98 parts by weight of HFC-365mfc, about 1-40 parts by weight of n-hexane and about 1-40 parts by weight of water.
    [14" claim-type="Currently amended] The azeotropic composition of claim 13 consisting substantially of about 60-98 parts by weight of HFC-365mfc, about 1-30 parts by weight of n-hexane and about 1-30 parts by weight of water.
    [15" claim-type="Currently amended] The azeotropic composition of claim 1 consisting substantially of about 10-98 parts by weight of HFC-365mfc, about 1-80 parts by weight of isohexane, and about 1-80 parts by weight of water.
    [16" claim-type="Currently amended] The azeotropic composition of claim 15 consisting substantially of about 40-98 parts by weight of HFC-365mfc, about 1-40 parts by weight of isohexane, and about 1-40 parts by weight of water.
    [17" claim-type="Currently amended] The azeotropic composition of claim 16 consisting substantially of about 60-98 parts by weight of HFC-365mfc, about 1-30 parts by weight of isohexane, and about 1-30 parts by weight of water.
    [18" claim-type="Currently amended] Method for producing a foam comprising the composition comprising the azeotropic composition of claim 1.
    [19" claim-type="Currently amended] A premix of blowing agent comprising a polyol and the composition of claim 1.
    [20" claim-type="Currently amended] Closed cell foaming composition prepared by foaming a foamable composition comprising the azeotropic composition of claim 1.
    [21" claim-type="Currently amended] A blowing agent comprising the azeotropic composition of claim 1.
    [22" claim-type="Currently amended] A sprayable composition comprising a propellant comprising the substance to be sprayed and the azeotropic composition of claim 1.
    [23" claim-type="Currently amended] 23. The injectable composition of claim 22 wherein the injectable composition is an aerosol.
    [24" claim-type="Currently amended] The sprayable composition of claim 23, wherein the sprayable composition is a cosmetic material.
    [25" claim-type="Currently amended] The injectable composition of claim 23, wherein the substance to be sprayed is a medicine.
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    同族专利:
    公开号 | 公开日
    CN1246063C|2006-03-22|
    CN1529625A|2004-09-15|
    EP1425075A4|2010-07-14|
    AU2002310252B2|2005-12-01|
    US6686326B2|2004-02-03|
    US20030022802A1|2003-01-30|
    JP2005504133A|2005-02-10|
    JP4443921B2|2010-03-31|
    EP1425075A1|2004-06-09|
    WO2002098528A1|2002-12-12|
    KR100898520B1|2009-05-20|
    TW588080B|2004-05-21|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    法律状态:
    2001-06-01|Priority to US29505301P
    2001-06-01|Priority to US60/295,053
    2002-06-03|Application filed by 허니웰 인터내셔널 인코포레이티드
    2002-06-03|Priority to PCT/US2002/017245
    2004-02-11|Publication of KR20040012884A
    2009-05-20|Application granted
    2009-05-20|Publication of KR100898520B1
    优先权:
    申请号 | 申请日 | 专利标题
    US29505301P| true| 2001-06-01|2001-06-01|
    US60/295,053|2001-06-01|
    PCT/US2002/017245|WO2002098528A1|2001-06-01|2002-06-03|Azeotrope-like compositions of pentafluorobutane|
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