Cleaning compositions for solid surfaces – auxiliary compositions – Cleaning compositions or processes of preparing – Liquid composition
Reexamination Certificate
2003-05-06
2004-07-06
Gupta, Yogendra N. (Department: 1751)
Cleaning compositions for solid surfaces, auxiliary compositions
Cleaning compositions or processes of preparing
Liquid composition
C510S411000, C510S412000, C510S415000, C570S101000, C570S123000, C570S170000, C570S178000
Reexamination Certificate
active
06759381
ABSTRACT:
BACKGROUND OF THE INVENTION
The present invention relates to azeotropic and azeotrope-like compositions of 1-chloro-1,3,3,3-tetrafluoropropane and 1,2-dichloro-3,3,3-trifluoropropene, or more particularly to such azeotropic and azeotrope-like compositions useful as intermediates in the production of 1,1,1,3,3-pentafluoropropane, and as refrigerants, blowing agents and solvents.
Traditionally, chlorofluorocarbons (CFCs) like trichlorofluoromethane and dichlorodifluoromethane have been used as refrigerants, blowing agents and diluents for gaseous sterilization. However, these materials are undesirable because they contribute to the depletion of the ozone layer. Therefore, stratospherically safer alternatives to these materials are desirable.
In recent years there has been universal concern that completely halogenated chlorofluorocarbons might be detrimental to the Earth's ozone layer. Consequently, there is a worldwide effort to use fluorine-substituted hydrocarbons which contain fewer or no chlorine substituents. Accordingly, the production of HFC's, or compounds containing only carbon, hydrogen and fluorine, has been the subject of interest to provide environmentally desirable products for use as solvents, blowing agents, refrigerants, cleaning agents, aerosol propellants, heat transfer media, dielectrics, fire extinguishing compositions and power cycle working fluids. In this regard, 1,1,1,3,3-pentafluoropropane (HFC-245fa), a hydrofluorocarbon (HFC) having zero ozone depletion potential, is considered as a replacement for chlorofluorocarbons such as dichlorodifluoromethane in refrigeration systems and trichlorofluoromethane as a blowing agent. It is known in the art to produce HFC's by reacting hydrogen fluoride with various hydrochlorocarbon compounds. For example, HFC-245fa is well known in the art and is described in U.S. Pat. Nos. 5,496,866 and 5,574,192, which are herein incorporated by reference.
An important intermediate in the production of HFC-245fa is the partially substituted intermediate 1-chloro-1,3,3,3-tetrafluoropropane (HCFC-244fa). It has now been found that purification of this intermediate is complicated by the presence of an azeotrope or azeotrope-like mixture of 1-chloro-1,3,3,3-tetrafluoropropane and 1,2-dichloro-3,3,3-trifluoropropene (HCFC-1223xd). This is despite the rather wide disparity of the normal boiling points of these two compounds (HCFC-244fa boils at about 43° C., while HCFC-1223xd boils at about 53° C.). This composition, once formed, may thereafter be separated into its component parts by extraction techniques or reaction techniques.
DESCRIPTION OF THE INVENTION
The invention provides an azeotropic or azeotropic-like composition comprising 1-chloro-1,3,3,3-tetrafluoropropane and 1,2-dichloro-3,3,3-trifluoropropene.
The invention also provides a process for forming an azeotropic or azeotropic-like composition of 1,2-dichloro-3,3,3-trifluoropropene (HCFC-1223xd) and 1-chloro-1,3,3,3-tetrafluoropropane (HCFC-244fa) comprising the steps of:
(a) reacting hydrogen fluoride with 1,1,1,3,3-pentachloropropane (HCC-240fa) thereby producing an intermediate composition; and thereafter
(b) separating an azeotropic or azeotropic-like composition of 1,2-dichloro-3,3,3-trifluoropropene (HCFC-1223xd) and 1-chloro-1,3,3,3-tetrafluoropropane(HCFC-244fa) from the intermediate composition.
In a method of preparing HFC-245fa, 1,1,1,3,3-pentachloropropane (HCC-240fa), is fluorinated with hydrogen fluoride (HF). The intermediate reaction products of this reaction include HFC-245fa, unreacted HF, hydrochloric acid, 1-chloro-1,3,3,3-tetrafluoropropane (HCFC-244fa), and 1,2-dichloro-3,3,3-trifluoropropene (HCFC-1223xd), and other intermediates and by-products. Upon removal of the by-products, including the removal of HFC-245fa, an azeotrope or azeotrope-like composition of HCFC-244fa and HCFC-1223xd is formed. This azeotrope or azeotrope-like composition is then available for separation into its component parts. The azeotropic or azeotrope-like composition may also be recycled to a fluorination reactor.
In particular, from about 5 moles to about 50 moles of hydrogen fluoride, more preferably from about 6 moles to about 30 moles of HF, and most preferably from about 7 moles to about 20 moles of HF, is reacted with about 1 mole of 1,1,1,3,3-pentachloropropane (HCC-240fa). The reaction is conducted at a temperature of from about 30° C. to about 200° C., more preferably from about 50° C. to about 180° C., and most preferably from about 70° C. to about 170° C. at a pressure of from about 15 psia to about 465 psia, more preferably from about 25 psia to about 265 psia and most preferably from about 30 psia to about 215 psia.
The result is an intermediate composition comprising 1,1,1,3,3-pentafluoropropane (HFC-245fa), unreacted hydrogen fluoride and hydrochloric acid (HCl), 1,2-dichloro-3,3,3-trifluoropropene (HCFC-1223xd) and 1-chloro-1,3,3,3-tetrafluoropropane(HCFC-244fa). Residual hydrogen fluoride, hydrochloric acid, and at least part of said 1,1,1,3,3-pentafluoropropane and other by-products are removed from the intermediate composition by purification methods, such as distillation, thereby leaving a remainder. The remainder is then distilled to remove any remaining 1,1,1,3,3-pentafluoropropane leaving an azeotropic or azeotrope-like composition of HCFC-244fa, and HCFC-1223xd. The distilling steps may be conducted at a pressure of from about 1 psia to about 250 psia, more preferably from about 15 psia to about 150 psia, and most preferably from about 20 psia to about 80 psia. The distilling steps may be conducted at a temperature of from about 30° C. to about 160° C., more preferably from about 35° C. to about 120° C. and most preferably from about 41° C. to about 97° C.
The thermodynamic state of a fluid is defined by its pressure, temperature, liquid composition and vapor composition. For a true azeotrope-like composition, the liquid composition and vapor phase are essentially equal at a given temperature and pressure range. In practical terms this means that the components cannot be separated during a phase change. For the purpose of this invention, an azeotrope-like composition means that the composition behaves like a true azeotrope in terms of its constant boiling characteristics and tendency not to fractionate upon boiling or evaporation. During boiling or evaporation, the liquid composition changes only slightly, if at all. This is in contrast with non-azeotrope-like compositions in which the liquid and vapor compositions change substantially during evaporation or condensation. One way to determine whether a candidate mixture is azeotrope-like within the meaning of this invention, is to distill a sample of it under conditions which would be expected to separate the mixture into its separate components. If the mixture is a non-azeotrope or non-azeotrope-like, the mixture will fractionate, i.e. separate into its various components with the lowest boiling component distilling off first, and so on. If the mixture is azeotrope-like, some finite amount of the first distillation cut will be obtained which contains all of the mixture components and which is constant boiling or behaves like a single substance. Another characteristic of azeotrope-like compositions is that there is a range of compositions containing the same components in varying proportions which are azeotrope-like. All such compositions are included by the term azeotrope-like as used herein. As an example, it is well known that at different pressures the composition of a given azeotrope will vary at least slightly as does the boiling point of the composition. Thus an azeotrope of two components represents a unique type of relationship but with a variable composition depending on the temperature and/or pressure. As is well known in the art, the boiling point of an azeotrope will vary with pressure.
As used herein, an azeotrope is a liquid mixture that exhibits a maximum or minimum boiling point relative to the boiling points of surrounding mixture compositions. An azeotrope or an azeotr
Johnson Robert C.
Merkel Daniel C.
Tung Hsuehsung
Elhilo Eisa
Gupta Yogendra N.
Honeywell International , Inc.
Szuch Colleen D.
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