the present invention includes improved compositions , methods and systems for cooling and / or refrigeration . the compositions and methods may be used in stationary or mobile systems for producing cooling . for example , the compositions and methods may be used in air conditioning systems for commercial , industrial or residential buildings . the compositions and methods may also be used in refrigerators or freezers ( stationary and mobile ), whether commercial , industrial or residential . the present inventions find their preferred application in vehicle air conditioning systems and other portable cooling systems . the invention includes circulating a composition that includes at least one refrigerant and at least one lubricant through a refrigeration device . the refrigeration device may include a compressor , a condenser and an evaporator , with a liquid refrigerant line containing an expansion device such as a capillary tube , orifice or thermal expansion valve between the condenser and evaporator . in operation , the compressor compresses the refrigerant vapors , which then condense to the liquid state in the condenser and pass through the liquid line and expansion device into the evaporator . the refrigerant vaporizes in the evaporator , thereby absorbing its latent heat of evaporation from the surrounding environment , which provides the cooling . the refrigerant may be one or more hydrofluorocarbons , such as ch 3 chf 2 , c 2 hf 5 , ch 2 f 2 , c 2 h 3 f 3 , chf 3 and c 2 h 2 f 4 which are commonly known as r - 152a , r - 125 , r - 32 , r - 143a , r - 23 and r - 134a , respectively . the preferred refrigerant consists essentially of r - 152a , for example as a substantially pure refrigerant of r - 152a . however , r - 152a may be combined with other refrigerants to modify the refrigerant &# 39 ; s overall properties , such as maintaining the boiling point or vapor pressure within a desired range . hydrocarbons , such as propane and butane , may be used as secondary refrigerants that are used in combination with hydrofluorocarbon refrigerants . the lubricant may be one or more polar , oxygenated compounds including polyalkylene oxides also known as polyalkylene glycols ( pags ), and polyol esters ( poes ). preferred pag lubricants include alkyl ether capped compounds and monols that have at least a single hydroxyl group . diols and triols may also be suitable . furthermore , homopolymers and random copolymers of pags are preferred . preferred homopolymers are polymers of propylene oxide ( po ) prepared from propylene oxide initiated with mono and polyhydric alcohols , with preferred alcohol initiators including methanol , butanol and glycerine . preferred homopolymers have the following formula : z -[(— ch 2 — ch ( ch 3 )— o —) n — r ] p , where z is the residue of a compound having 1 - 8 active hydrogens , n is a number having an average value which will give the pag with a number average molecular weight range from about 1000 to about 4000 , r is h or an alkyl group of 1 to 6 carbon atoms , and p is an integer having a value equal to the number of active hydrogens of z . preferred random copolymers comprise polymers of ethylene oxide ( eo ) and po in a ratio of eo to eo + po of between about 0 . 01 to about 0 . 75 initiated with mono and polyhydric alcohols such as methanol , butanol and glycerin . more preferred ratios include ratios incremented by about 0 . 05 between about 0 . 1 and 0 . 7 , with most preferred ration including those incremented by about 0 . 1 between about 0 . 1 and about 0 . 7 ( e . g . 0 . 1 , 0 . 2 , 0 . 3 , 0 . 4 , 0 . 5 , 0 . 6 and 0 . 7 ). stated alternatively , the pags preferably contain from about 5 % to about 95 % eo and correspondingly about 95 % to about 5 % po . more preferably , the pags contain about 25 % to about 75 % eo and , correspondingly , about 75 % to about 25 % po . the more preferred weight percents of eo and po in the random pag are from about 40 to about 60 % eo to about 60 to about 40 % po ; and the most preferred ratio is about 50 : 50 . suitable alkyls useful for capping the pags include those comprising 1 to 4 carbons to produce methyl ether capped pags , ethyl ether capped pags , propyl ether capped pags and / or butyl ether capped pags , where the pags are single or double end capped . the poe lubricants are esters of fatty acids with polyhydric alcohols , e . g . diols , triols , and polyols , and / or polyhydric polyethers . examples include dihydric alcohols , trihydric alcohols , and tetrahydric alcohols having 4 to 18 carbons such as glycerin , ethylene glycol , propylene glycol pentaerythritol , dipentaerythritol , tripentaerythritol , trimethylolpropane , trimethylolbutane , and trimethylolethane . other suitable polyhydric alcohols include those based on sugars such as sorbitol . the fatty acids include straight and branched fatty acids having from 2 - 20 carbon atoms and also polyacidic ( e . g . diacid ) fatty acids having from 4 to 36 carbon atoms . other examples include alkanoic acids of 4 to 18 carbon atoms . the polyol ester lubricants may be derived by esterifying , with one or more fatty acids , a polyhydric alcohol or a polyhydric polyether . exemplary esters include ethylene glycol distearate , propylene glycol dipelargonate , glycerine trioleate , trimethylolpropane triheptonate and pentaerythritol tetraheptonate . preferred polyolesters include those based on pentaerythritol isononanoic acid . as the viscosity of the lubricant increases , it is believed that a larger fatty acid and / or an increase in the number of active hydrogens on the polyhydric alcohol will be useful to achieve the desired result . preferred poe include those that contain substantially a single poe , where substantially a single poe means that more than about 90 % ( preferably more than about 95 %) of the poe is derived from a single fatty acid . this becomes possible because commercial grade fatty acids are up to about 95 % pure . the lubricants preferably have a molecular weight ( as measured by gel permeation chromatography ( gpc ) or time of flight mass spectrometry ( tof - ms between about 1000 and 4000 , more preferably between about 1500 and 3500 . lubricants with molecular weights in these ranges provide falex wear testing results that are more favorable compared to lubricants with molecular weights outside of these ranges . the lubricants are selected to have a viscosity of between about 10 and about 460 cst at 40 ° c ., preferably between about 22 and about 220 cst at 40 ° c . and most preferably between about 40 and about 150 cst at 40 ° c . the lubricant should have sufficient solubility in the refrigerant to insure that the lubricant can return to the compressor from the evaporator . furthermore , the refrigerant and lubricant composition should have a low temperature viscosity so that the lubricant is able to pass through the cold evaporator . in one preferred embodiment , the refrigerant and the lubricant are miscible over a broad range of temperatures . the portions of the refrigerant and lubricant in the composition are determined so that there is sufficient lubricant to lubricate the compressor . typically , the lubricant makes up about 1 wt % to more than about 50 wt % of the composition at the time the composition is charged into a system ; and preferably between about 3 wt % and about 30 wt %, the wt % of the lubricant will typically affect the mutual solubility of the refrigerant and lubricant and thus the available operating temperatures for the refrigeration device . in another aspect of this invention , the solubility of the lubricant in the refrigerant is temperature dependent because the temperature within the compressor is usually significantly higher than the temperature within the evaporator . preferably , in the compressor , the lubricant and the refrigerant are separate from each other and not soluble ; the lubricant is a liquid and the refrigerant is a gas being compressed . on the contrary , in the evaporator , preferably the lubricant and the refrigerant are mutually soluble . this ideal situation would lead to minimal decreases in viscosity of the lubricant in the compressor due minimal dilution by the refrigerant . this in turn leads to better lubricity and decreased lubricant discharge from the compressor . at the same time , the low temperature solubility helps insure that any lubricant that is discharged from the compressor is returned by diluting the cold lubricant and thus keeping its viscosity low . thus , in one embodiment , a lubricant that exhibits low temperature solubility and high temperature insolubility is desirable . in a preferred embodiment , the lubricant is soluble in the refrigerant at temperatures between about − 40 ° c . and about 40 ° c . and more preferably in the range of about − 40 ° c . and about 55 ° c . and most preferably in the range of about − 40 ° c . and about 100 ° c . the compositions of the present invention also include an additives package with some or all the following : an extreme pressure additive , an anti - wear additive , an antioxidant , a high - temperature stabilizer , a corrosion inhibitor , a detergent and an anti - foaming agent . extreme pressure additives improve the lubricity and load bearing characteristics of the refrigerant composition . preferred additives include those described in u . s . pat . nos . 5 , 152 , 926 ; 4 , 755 , 316 , which are hereby incorporated by reference . in particular , the preferred extreme pressure additives include mixtures of ( a ) tolyltriazole or substituted derivatives thereof , ( b ) an amine ( e . g . jeffamine m - 600 ) and ( c ) a third component which is ( i ) an ethoxylated phosphate ester ( e . g . antara lp - 700 type ), or ( ii ) a phosphate alcohol ( e . g . zelec 3337 type ), or ( iii ) a zinc dialkyldithiophosphate ( e . g . lubrizol 5139 , 5604 , 5178 , or 5186 type ), or ( iv ) a mercaptobenzothiazole , or ( v ) a 2 , 5 - dimercapto - 1 , 3 , 4 - triadiazole derivative ( e . g . curvan 826 ) or a mixture thereof . the additive package preferably includes a flame retardant that reduces or eliminates the likelihood of the lubricant being the fuel for a fire . flame retardants may increase the vapor pressure of the composition , increase the flash point of composition , or otherwise reduce the chance of fire . in one embodiment , the flame retardant is a gaseous phase flame retardant ( all though not necessarily the case ) such that the flame is gaseous when the refrigerant is also gaseous . suitable flame retardants include trifluorochloromethane , trifluoroiodomethane , phosphorus compounds such as phosphate esters and hydrocarbons , hydrofluorocarbons , or fluorocarbons that also contain iodine and / or bromine . several lubricants are investigated for suitability for use in combination with r - 152a and an additives package . unless noted otherwise , the composition contains up to about 3 wt % of the additives package as described in the last example of table xv of u . s . pat . no . 5 , 152 , 926 ( e . g . antara lp - 700 . jeffamine m - 600 and tolyltriazole ). the lubricant tests are summarized in table 1 and include several pag and poe lubricants as well as a mineral oil lubricant for comparison . the viscosity of the lubricant is also noted at 40 ° c . and at 100 ° c . for each of the pag lubricants , four compositions with r - 152a are made , while two compositions each are made with the poe lubricant and the comparison mineral oil lubricant . each of the compositions varies in the wt % of the lubricant in the composition . the compositions are then tested at various temperatures or over a range of temperatures . the compositions are visually inspected to determine if , and at what temperature , the composition separates into its component parts . other visual characteristics are also noted as appropriate . from the results of the testing , it can be seen that both the pag and the poe lubricants exhibit excellent solubility in r - 152a over a wide range of temperatures and weight percentages , whereas the mineral oil is never soluble in the refrigerant , regardless of the temperature or weight percentage . also , rl - 488 exhibits an advantageous temperature dependent solubility profile i . e . low temperature solubility and high temperature insolubility . likewise , the solubility of three pag lubricants is tested for r - 134a using the same procedure as described above substituting r - 134a for r - 152a . as mentioned above , four compositions with r - 134a are made for each of the three tested pag lubricants . each of the compositions varies in the wt % of the lubricant . the compositions are then tested over a range of temperatures . the compositions are visually inspected to determine if , and at what temperature , the composition separates into its component parts . other visual characteristics are also noted as appropriate . testing the solubility of the lubricants in both r - 152a and r - 134a differs in that the upper temperature limit for r - 134a is lower that for r - 152a . the insolubility of r - 134a at higher temperatures would create a composition that is not a single phase and this may interfere with the ability of the composition to be carried along through the condenser of a refrigeration system . a single phase composition in the condenser may be desirable for some systems . next , the long term stability of the refrigerant and lubricant compositions is studied . mixtures of 50 wt % lubricant and 50 wt % r - 152a are sealed in high pressure glass tubes along with steel , aluminum and copper containing metals . the tubes are then heated in an oven at 175 ° c . for 2 weeks . the compositions are visually inspected for the number of phases and cloudiness . further , the metals are also visually inspected . the results are shown in table 4 . as can be seen , the refrigerant and lubricant remain soluble and stable over an extended period of time in the presence of metals likely to be found refrigeration systems . next , the lubricity of r - 152a / lubricant additives package compositions and r - 134a / lubricant compositions were tested according to astm d3233 modified procedure a . the test procedure includes the use of a pin and v - block apparatus to incrementally increase the force of the v - block on the pin . for this test , samples of lubricant ( 95 ml ) are saturated with either r - 134a or r - 152a . the lubricity , measured as load failure ( lb . ), is tested at about 24 ° c . as seen above , r - 152a / lubricant / additives package compositions possess desirable temperature solubility profiles and the compositions are stable . however , because of its cost and mild flammability , r - 152a has not previously been a suitable substitute for r - 134a , because r - 134a cannot meet the stringent environmental regulations related to global warming potential , r - 152a / lubricant compositions , in spite of their drawbacks , are now suitable substitutes for r - 134a / lubricant compositions especially with the use of a flame retardant . further , r - 152a / lubricant / additives package compositions are more desirable than using co 2 because r - 152a may be used as a ‘ drop - in ’ replacement for r - 134a , whereas co 2 cannot thus , the r - 152a / lubricant / additives package compositions may be used to retrofit or recondition existing systems merely by replacing the existing refrigerant with the new composition . furthermore , the cost of monitoring or controlling the mild flammability of r - 152a is small in comparison to the cost of designing , manufacturing and using high pressure co 2 systems . it will be further appreciated that functions or structures of a plurality of components or steps may be combined into a single component or step , or the functions or structures of one - step or component may be split among plural steps or components . the present invention contemplates all of these combinations . unless stated otherwise , dimensions and geometries of the various structures depicted herein are not intended to be restrictive of the invention , and other dimensions or geometries are possible . plural structural components or steps can be provided by a single integrated structure or step . alternatively , a single integrated structure or step might be divided into separate plural components or steps . in addition , while a feature of the present invention may have been described in the context of only one of the illustrated embodiments , such feature may be combined with one or more other features of other embodiments , for any given application . it will also be appreciated from the above that the fabrication of the unique structures herein and the operation thereof also constitute methods in accordance with the present invention . the explanations and illustrations presented herein are intended to acquaint others skilled in the art with the invention , its principles , and its practical application . those skilled in the art may adapt and apply the invention in its numerous forms , as may be best suited to the requirements of a particular use . accordingly , the specific embodiments of the present invention as set forth are not intended as being exhaustive or limiting of the invention . the scope of the invention should , therefore , be determined not with reference to the above description , but should instead be determined with reference to the appended claims , along with the full scope of equivalents to which such claims are entitled . the disclosures of all articles and references , including patent applications and publications , are incorporated by reference for all purposes .