in accordance with the invention , novel azeotrope - like compositions have been discovered comprising from about 51 to about 98 . 8 weight percent 1 , 1 - dichloro - 1 - fluoroethane ( hcfc - 141b ), from about 1 to about 40 weight percent dichlorotrifluoroethane , from about 0 . 1 to about 4 weight percent ethanol and from about 0 . 1 to about 5 weight percent cyclopentane and boil at about 31 . 5 ° c .± about 0 . 6 ° c . at 760 mm hg . dichlorotrifluoroethane exists in three isomeric forms , 1 , 1 - dichloro - 2 , 2 , 2 - trifluoroethane ( hcfc - 123 ), 1 , 2 - dichloro - 1 , 2 , 2 - trifluoroethane ( hcfc - 123a ), and 1 , 1 - dichloro - 1 , 2 , 2 - trifluoroethane ( hcfc - 123b ). for purposes of this invention , dichlorotrifluoroethane will refer only to the hcfc - 123 and hcfc - 123a isomers . each of these isomers exhibits the properties of the invention . hence , either isomer may be used as well as mixtures of the isomers in any proportion . hcfc - 123 is the preferred isomer . commercial hcfc - 123 contains from about 90 . 0 to about 95 . 0 weight percent hcfc - 123 , from about 5 . 0 to about 10 . 0 weight percent hcfc - 123a , and impurities like trichloromonofluoromethane , trichlorotrifluoroethane , and methylene chloride . however , because they are present ininsignificant amounts , these impurities have no deleterious effect on the properties of the azeotropelike compositions . hcfc - 123 is also available in an &# 34 ; ultra pure &# 34 ; form . &# 34 ; ultra pure &# 34 ; hcfc - 123 contains from about 95 . 0 to about 99 . 5 weight percent hcfc - 123 , from about 0 . 5 to about 5 . 0 weight percent hcfc - 123a , and impurities listed above . commercially available cyclopentane may be used in the present invention . commercial grade cyclopentane contains impurities such as 2 , 2 - dimethylbutane ; 2 , 3 - dimethylbutane ; 2 - methylpentane ; 3 - methylpentane ; and n - hexane . hcfc - 141b has a low ozone depletion potential . dichlorotrifluoroethane has a still lower ozone depletion potential . when these materials are combined in effective amounts with cyclopentane and ethanol , a very low ozone depleting composition results . hcfc - 141b and dichlorotrifluoroethane also suppress the flammability of the alkane component , cyclopentane , when used in effective amounts . ethanol and cyclopentane exhibit superior solvent properties . hence , when all of these materials , i . e ., hcfc - 141b , dichlorotrifluoroethane , ethanol and cyclopentane , are combined in effective amounts , a novel environmentally acceptable , nonflammable , azeotropic cleaning solvent results . the azeotrope - like compositions of the invention consist essentially of from about 51 to about 98 . 8 weight percent hcfc - 141b , from about 1 to about 40 weight percent dichlorotrifluoroethane , from about 0 . 1 to about 5 weight percent cyclopentane and from about 0 . 1 to about 4 weight percent ethanol and boil at about 31 . 5 ° c .± about 0 . 6 ° c . at 760 mm hg . in a preferred embodiment , the azeotrope - like compositions of the invention consist essentially of from about 58 to about 96 . 8 weight percent hcfc - 141b , from about 3 to about 35 weight percent dichlorotrifluoroethane , from about 0 . 1 to about 4 weight percent cyclopentane and from about 0 . 1 to about 3 weight percent ethanol . in a more preferred embodiment , the azeotrope - like compositions of the invention consist essentially of from about 65 to about 95 . 8 weight percent hcfc - 141b , from about 4 to about 30 weight percent dichlorotrifluoroethane , from about 0 . 1 to about 3 weight percent cyclopentane and from about 0 . 1 to about 2 weight percent ethanol . in the most preferred embodiment , the azeotrope - like compositions of the invention consist essentially of from about 71 to about 94 . 8 weight percent hcfc - 141b , from about 5 to about 25 weight percent dichlorotrifluoroethane , from about 0 . 1 to about 2 . 5 weight percent cyclopentane , and from about 0 . 1 to about 1 . 5 weight percent ethanol . the compositions of the invention containing a mixture of 1 , 1 - dichloro - 2 , 2 , 2 ,- trifluoroethane ( hcfc - 123 ) and 1 , 2 - dichloro - 1 , 2 , 2 - trifluoroethane ( hcfc - 123a ) behave like azeotropic compositions because the separate ternary azeotrope - like compositions with hcfc - 123 and hcfc - 123a have boiling points so close to one another that they are virtually indistinguishable . when a mixture of hcfc - 123 and 123a is used , the azeotrope - like compositions of the invention consist essentially of from about 51 to about 98 . 8 weight percent 1 , 1 - dichloro - 1 - fluoroethane , from about 1 to about 40 weight percent of a mixture of hcfc - 123 / hcfc - 123a , from about 0 . 1 to about 5 weight percent cyclopentane , and from about 0 . 1 to about 4 weight percent ethanol and boil at about 31 . 5 ° c .± about 0 . 6 ° c . at 760 mm hg . in the most preferred embodiment utilizing a mixture of hcfc - 123 / hcfc - 123a , the azeotrope - like compositions of the invention consist essentially of from about 71 to about 94 . 8 weight percent 1 , 1 - dichloro - 1 - fluoroethane , from about 5 to about 25 weight percent of a mixture of hcfc - 123 / hcfc - 123a , from about 0 . 1 to about 2 . 5 weight percent cyclopentane , and from about 0 . 1 to about 1 . 5 weight percent ethanol it is known in the art that the use of more active solvents , such as lower alkanols in combination with certain halocarbons such as trichlorotrifluoroethane , may have the undesirable result of attacking reactive metals such as zinc and aluminum , as well as certain aluminum alloys and chromate coatings such as are commonly employed in circuit board assemblies . the art has recognized that certain stabilizers , like nitromethane , are effective in preventing metal attack by chlorofluorocarbon mixtures with such alkanols . other candidate stabilizers for this purpose , such as disclosed in the literature , are secondary and tertiary amines , olefins and cycloolefins , alkylene oxides , sulfoxides , sulfones , nitrites and nitriles , and acetylenic alcohols or ethers . it is contemplated that such stabilizers as well as other additives may be combined with the azeotrope - like compositions of this invention . the precise or true azeotrope compositions have not been determined but have been ascertained to be within the indicated ranges . regardless of where the true azeotropes lie , all compositions within the indicated ranges , as well as certain compositions outside the indicated ranges , are azeotrope - like , as defined more particularly below . it has been found that these azeotrope - like compositions are on the whole nonflammable liquids , i . e . exhibit no flash point when tested by the tag open cup test method -- astm d 1310 - 86 . from fundamental principles , the thermodynamic state of a fluid is defined by four variables : pressure , temperature , liquid composition and vapor composition , or p - t - x - y , respectively . an azeotrope is a unique characteristic of a system of two or more components where x and y are equal at the stated p and t . in practice , this means that the components of a mixture cannot be separated during distillation , and therefore in vapor phase solvent cleaning as described above . for purposes of this discussion , the term &# 34 ; azeotrope - like composition &# 34 ; is intended to mean that the composition behaves like a true azeotrope in terms of its constant - boiling characteristics or tendency not to fractionate upon boiling or evaporation . such composition may or may not be a true azeotrope . thus , in such compositions , the composition of the vapor formed during boiling or evaporation is identical or substantially identical to the original liquid composition . hence , during boiling or evaporation , the liquid composition , if it changes at all , changes only slightly . this is contrasted with non - azeotrope - like compositions in which the liquid composition changes substantially during boiling or evaporation . thus , one way to determine whether a candidate mixture is &# 34 ; azeotrope - like &# 34 ; within the meaning of this invention , is to distill a sample thereof under conditions ( i . e . resolution - number of plates ) which would be expected to separate the mixture into its components . if the mixture is non - azeotropic or non - azeotrope - like , the mixture will fractionate , with the lowest boiling component distilling off first , etc . if the mixture is azeotrope - like , some finite amount of a first distillation cut will be obtained which contains all of the mixture components and which is constant boiling or behaves as a single substance . this phenomenon cannot occur if the mixture is not azeotrope - like i . e ., it is not part of an azeotropic system . if the degree of fractionation of the candidate mixture is unduly great , then a composition closer to the true azeotrope must be selected to minimize fractionation . of course , upon distillation of an azeotrope - like composition such as in a vapor degreaser , the true azeotrope will form and tend to concentrate . it follows from the above discussion that 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 intended to be covered 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 a and b represents a unique type of relationship but with a variable composition depending on temperature and / or pressure . accordingly , another way of defining azeotrope - like within the meaning of this invention is to state that such mixtures boil within about ± 0 . 5 ° c . ( at 760 mm hg ) of the boiling point of the most preferred compositions disclosed herein . as is readily understood by persons skilled in the art , the boiling point of the azeotrope will vary with the pressure . in the process embodiment of the invention , the azeotrope - like compositions of the invention may be used to clean solid surfaces by treating said surfaces with said compositions in any manner well known to the art such as by dipping or spraying or use of conventional degreasing apparatus . the hcfc - 14lb , dichlorotrifluoroethane , ethanol and cyclopentane components of the invention are known materials . preferably they should be used in sufficiently high purity so as to avoid the introduction of adverse influences upon the solvency properties or constant - boiling properties of the system . it should be understood that the present compositions may include additional components so as to form new azeotrope - like or constant - boiling compositions . any such compositions are considered to be within the scope of the present invention as long as the compositions are constant - boiling or essentially constant - boiling and contain all of the essential components described herein . the present invention is more fully illustrated by the following non - limiting examples . the azeotropic properties of hcfc - 141b , hcfc - 123 , ethanol , and cyclopentane are studied via the method of distillation . the examples also illustrate that these mixtures do not fractionate during distillation . a 5 - plate oldershaw distillation column with a cold water condensed automatic liquid dividing head was used in these examples . for examples 1 - 2 , the distillation column was charged with approximately 350 grams of a mixture of hcfc - 141b , hcfc - 123 , ethanol and cyclopentane . the mixture was heated under total reflux for about an hour to ensure equilibration . a reflux ratio of 3 : 1 was employed for these particular distillations . approximately 50 percent of the original charges were collected in four similar - sized overhead fractions . the compositions of these fractions were analyzed using gas chromatrography . table i shows the composition of the starting materials . the averages of the distillate fractions and the overhead temperatures are quite constant within the uncertainty associated with determining the compositions , indicating that the mixtures are azeotrope - like . table i______________________________________ eth - cyclo - example hcfc - 141b hcfc - 123 anol pentane______________________________________starting material ( wt . %) 1 91 . 77 5 . 15 1 . 02 2 . 062 71 . 78 25 . 19 1 . 02 2 . 01distillate composition ( wt . %) 1 91 . 37 5 . 83 1 . 45 1 . 352 70 . 23 27 . 27 0 . 91 1 . 59______________________________________ boiling barometric boiling pointex - point pressure corrected toample (° c .) ( mm hg ) 760 mm hg (° c . ) ______________________________________1 31 . 1 737 . 5 32 . 02 30 . 6 743 . 2 31 . 2______________________________________ mean : 31 . 5 ° c . ± 0 . 6 ° c . examples 1 - 2 illustrate that hcfc - 141b , hcfc - 123 , cyclopentane and ethanol form a constant - boiling mixture . the azeotrope - like properties of hcfc - 141b , hcfc - 123a , ethanol , and cyclopentane are studied by repeating the experiment outlined in examples 1 - 2 above . the results obtained are substantially the same as those for hcfc - 123 , i . e . hcfc - 141b , hcfc - 123a , ethanol and cyclopentane form a constant boiling mixture . the azeotrope - like properties of hcfc - 141b , a mixture of hcfc - 123 / hcfc - 123a , ethanol , and cyclopentane are studied by repeating the experiment outlined in examples 1 - 2 above . the results obtained are substantially the same as those for hcfc - 123 , i . e . hcfc - 141b , a mixture of hcfc - 123 / hcfc - 123a , ethanol and cyclopentane form a constant boiling mixture . having described the invention in detail and with reference to preferred embodiments thereof , it will be apparent that modifications and variations are possible without departing from the scope of the invention defined in the appended claims .