fig1 shows a fabric tumbling device , such as a conventional or industrial washer or dryer , including a housing 10 which is relatively liquid impermeable . housing 10 is typically provided with a front end 11 having an access door 12 for loading and unloading of garments . access door 12 can be provided with a hinge 13 , or other conventional structure , to facilitate opening and closing . a door fastener 14 is also typically provided to prevent accidential opening of the door while the washer or dryer is in operation . positive locking of access door 12 is particularly preferred for large fabric tumbling devices , such as large capacity industrial washers and dryers , for safety reasons . housing 10 can be supported by a support stand 25 . a motor drive 26 can be provided to conventionally rotate inner drum 32 ( as shown in fig2 ), which is attached to shaft 27 . this can be done , for example , and as shown in fig1 conventionally by means of pulleys 28 and 29 which connect shaft 27 to the output shaft of motor drive 26 . many other alternative arrangements are possible for mounting the motor drive 26 to rotate inner drum 32 , including , for example , mounting the inner drum directly to the motor output shaft . an atomizing spray nozzle 15 can be mounted through the access door 12 to provide a mist or fog of textile treatment agent inside the housing 10 . nozzle 15 is preferably a high velocity , low pressure ( hvlp ) type atomizing nozzle assembly , such as that manufactured by , for example , spraying systems co . and sold as their model # 1 / 2 &# 34 ; jbc - ss back connect nozzle . attachments can be added to vary the shape of the fog pattern produced by the nozzle . for example , spraying systems , inc . provides screw - on attachments in its spray setup numbers su70 , sue75 or su380c which provide a round , flat , and circular pattern respectively . nozzle 15 can be constructed from any suitable material , such as , for example , stainless steel , and is typically constructed to receive feed lines having 1 / 8 inch to 3 / 4 inch or larger diameters . the most preferred line size , for use with the present invention in a high capacity industrial finishing machine , is 1 / 2 inch diameter . gas conduit 16 provides pressurized air to spray nozzle 15 . air pressure is regulated conventionally by a control valve 17 to a pre - selected value which is measured at pressure gauge 18 . aqueous solutions or dispersions of treatment agent are placed in a reservoir ( not shown ) outside the washer or dryer . this reservoir is preferably located below and aligned with the spray head . it is preferred to provide a means for heating the treatment agent in the reservoir , to enable the user , when desired , to offset the adiabatic cooling of the textile treatment agent caused by the action of the atomizing nozzle . the treatment agent reservoir is also preferably pressurized using conventional means , such as a pump , to between about 1 psi to about 50 psi . the flow of treatment agent through feed line 19 to the nozzle 15 is controlled by control valve 20 and measured by gauge 35 . air and treatment agent is thus provided to the nozzle 15 under pressure , and mixed in the nozzle 15 , to provide a substantially completely atomized spray which , under normal processing conditions , leaves substantially no residual liquid in the bottom of housing 10 . the flow rate from the reservoir is directly related to pressure : liquid flow to the nozzle 15 will increase as fluid pressure increases . thus , higher fluid pressure will require higher air pressure to the nozzle 15 to obtain proper mixing to create a fog . for example , when the spraying systems co . model jbc - ss back connect nozzle ( adapted to receive 1 / 2 inch feed line ) is used with the spraying systems co . sue - 75 spray attachment , and the liquid pressure is set to 30 psi liquid pressure , a fog will be created when the air pressure is set to 80 psi of air pressure . under these conditions , the calculated median volumetric diameter of the droplets produced is 137μ . in the preferred embodiment , gases are vented from the housing 10 through a conventional conduit , or through a conduit 21 which can be provided with a valve 22 for opening or closing conduit 21 . this allows the operator to either exhaust the gases or to recycle the gas used for entraining the textile treatment agent in a substantially closed system . a conventional washer is typically provided with a drain 23 which is controlled by a drain valve 24 , for allowing the drum to fill with cleaning liquids ( when the valve 24 is closed ) and for allowing cleaning liquids to drain ( when the valve 24 is opened ) during conventional , immersion washing or rinsing . it should be apparent that these components are not necessary for the practice of this invention , but may be convenient and useful if it is desirable to wash the garments immediately after processing according to this invention . in that event , using a washer as the tumbling device would be most preferred . fig2 shows a cross - sectional view of a preferred embodiment of the present invention as shown in fig1 omitting ( for clarity ) the motor drive 26 . the preferred embodiment includes an inner drum 30 mounted for rotation inside the housing 10 . inner drum 30 is preferably cylindrical in shape , and the sides of inner drum 30 can include perforations 31 . a shaft 27 is preferably provided centered on the back end 32 of inner drum 30 for rotating the drum 30 . bearings 33 , which form a rotary union , allow shaft 27 to rotate freely through back end 34 of housing 10 . bearings 33 preferably provide a substantially water impermeable seal , and are preferably substantially aligned with the horizontal axis of rotation of inner drum 30 . access to the interior of inner drum 30 is obtained by releasing door fastener 14 and opening access door 12 . in the embodiment shown in fig2 one or more stationary atomizing spray heads 15 can be mounted through access door 12 to create an atomized mist or fog for garment processing inside the inner drum 30 . in this embodiment , access door 12 , and the attached spray head 15 , remain stationary during operation while the inner drum 30 rotates . another embodiment of the present invention , using one or more spray heads 128 , 138 mounted inside a rotating inner drum is illustrated in fig3 . in this embodiment , a substantially liquid impermeable housing 101 is provided with a front end door 102 closed by fastener 103 . housing 101 is supported by base 104 . a rotating inner drum 112 , which may be provided with perforations 117 , is mounted for rotation on hollow shaft 113 which passes through an opening in the rear 116 of housing 101 . bearings 124 , which form a rotary union , allow shaft 113 to rotate in stationary housing 101 . bearings 124 permit free rotation of shaft 113 and seal the opening in the rear wall 116 of housing 101 through which shaft 113 passes . bearings 124 are preferably substantially aligned with the horizontal axis of rotation of inner drum 112 . rotation of shaft 113 can be accomplished , for example , through pulley 115 which can be connected by a belt or a shaft drive ( not shown ) to a motor ( not shown ) in an arrangement similar to that depicted in fig1 . as shown in fig3 rotating inner drum 112 can be provided with a door 139 which is mounted on hinges 134 to permit the door 139 to be selectively opened and closed to load and unload garments for processing . a lock ( not shown ) can be provided for securing door 139 in a closed position during operation . air conduit 105 and liquid conduit 106 can be securely mounted in opening 142 of door 102 using fittings 107 , 108 . a bearing 135 substantially aligned with the horizontal axis of rotation of the inner drum can be provided through inner door 133 to permit the inner drum to rotate about the stationary conduits 105 , 106 . stationary conduits 105 , 106 terminate in a stationary nozzle 138 which can be mounted along the axis of rotation , or , alternatively , may be mounted offset as shown in fig3 and described in more detail below . likewise , air conduit 129 and liquid conduit 130 pass through hollow shaft 113 which preferably extends through and is mounted to an opening 143 in rear wall 114 . a bearing 126 substantially aligned with the axis of rotation of inner drum 112 can be provided in rear wall 114 ( or in a second door mounted in the rear of the drum ) to permit the inner drum 112 to rotate about the stationary conduits 129 , 130 . stationary conduits 129 , 130 terminate in a stationary nozzle 128 which can be mounted along the axis of rotation or , alternatively , may be mounted offset as shown in fig3 and described in more detail below . the conduits 16 , 19 , 105 , 106 , 129 and 130 can be selected from any suitable conduit material capable of withstanding the pressures described herein . preferably , the conduits are formed from polyethylene tubing having an inside diameter ranging from about 1 / 8 inch to about 1 / 2 inch . most preferably , conduits 19 , 105 and 130 are transparent to provide a visual indication of the presence of textile treatment agent in these conduits . flow of pressurized air through air conduits 106 , 129 can be regulated by regulating valves 109 , 132 to a pre - selected value which is measured at air pressure gauges 110 , 133 respectively . flow of liquid treatment agent through conduits 105 , 130 is regulated by valves 111 , 131 to a preselected value which is measured at gauges 118 , 119 respectively . gases are preferably vented from housing 101 through a conventional venting arrangement depicted schematically as conduit 120 and valve 121 . alternatively , a closed system can be obtained by recycling the propellant air used to create the treatment fog . if a conventional washing machine is selected as the tumbling mechanism , and is used conventionally to wash the garments after processing , washing liquids can be removed through conduit 122 and valve 123 as described above . one or more atomizing spray nozzles can be provided adjacent to the rear wall 114 of the inner drum 112 . most preferably , the nozzles 128 , 138 are mounted along , and centered substantially on , the center of the axis of rotation of inner drum 112 . alternatively , however , nozzles 128 , 138 could be mounted off - center from the axis of rotation of the inner drum as shown in fig3 . because this means the conduits 105 , 106 and 130 , 129 will be inside the rotating inner drum , a structure should be provided to prevent the conduits from ensnaring tumbling garments and thus preventing the even treatment of the ensnared garments by the treatment mist . for example , a bracket 125 , 136 can be provided along the conduits 105 , 106 and 130 , 129 . as shown in fig3 brackets 125 , 136 pass through the openings formed in the front 102 and rear 116 of housing 101 . bearing 126 is substantially aligned with the horizontal axis of rotation of inner drum 112 , and is mounted in back end 114 of inner drum 112 . bearing 126 rotates with the inner drum , thus enabling bracket 125 to remain stationary when inner drum 112 rotates . likewise , a bearing 135 substantially aligned with the horizontal axis of rotation of the inner drum can be provided through inner door 133 . thus , when bracket 136 is mounted through bearing 135 , bracket 136 will remain stationary when the inner drum rotates . the bracket 125 , 136 can also be used to provide a structure to which a stationary panel 127 , 137 can be mounted inside rotatable inner drum 112 . in the embodiment shown in fig3 a panel 127 , 137 is mounted on bracket 125 , 136 so as to be substantially parallel and in close proximity to each end of inner drum 112 to prevent tumbling garments from coming into contact with the liquid and gas conduits feeding the spray heads 128 , 138 . the outer edge of each panel 127 , 137 follows the contours of the cylindrical wall of inner drum 112 without contacting the wall . the atomizing spray nozzles 128 , 138 can be mounted on the panels 127 , 137 , for example , as shown in fig3 . the space inside bearings 126 , 135 through which the brackets 125 , 136 and conduits 105 , 106 , 129 and 130 pass , preferably provide a substantially liquid impermeable seal . as will immediately be understood by one having skill in the art , brackets 125 , 136 must be very strong and stable to withstand the motion of the inner drum and the tumbling action of the garments during processing . the preferred embodiments described above illustrate a two drum arrangement , with a rotating inner drum and a stationary outer drum , since this is the typical configuration of most conventional , industrial washers or dryers which are possessed and used by most garment manufacturers . however , a single drum washer or dryer , such as that disclosed in u . s . pat . no . 4 , 941 , 333 , could easily be modified by one skilled in the art using the disclosure in this application to produce an apparatus of the present invention . likewise , a chamber could be constructed that either ( 1 ) rotates itself , or ( 2 ) has a rotating perforated drum or basket within it , for tumbling garments in the presence of a fog or mist of treatment agents created within the chamber . dry or damp garments are preferably processed in a device of the present invention as depicted in fig1 - 3 . &# 34 ; damp &# 34 ; means the garments have absorbed during other processing steps moisture of no more than about 125 % of dry weight . garments can be processed using the method of this invention in the following way : a textile treatment agent reservoir is filled with a solution or dispersion of the desired textile treatment agent to be applied to the garments . these typically include fabric softeners , anti - ozonate compounds , permanent - press type fabric finishes , bleach , potassium permanganate solution , dyes , or other chemical agents . if the temperature of the textile treatment agent is important , it should be heated . this can be done , for example , by heating the solution or dispersion of textile finishing agent to the desired temperature and placing it in the reservoir just prior to beginning the finishing process , or by heating the solution or dispersion of textile finishing agent in the reservoir using a heating element . because adiabatic cooling will reduce the temperature of the solution fog when it contacts the garments ( depending on the pressure drop of the liquid as it exits the nozzle ), the temperature of the solution or dispersion in the reservoir should be somewhat higher than that desired at the point of contact with the garments . the reservoir is also preferably pressurized to a pressure which can range from about 1 psi to about 50 psi . a pre - determined quantity of dry or damp garments is placed inside inner drum 32 / 112 , the door is then closed and fastener 14 / 103 is engaged . motor drive 26 is engaged to rotate the inner drum , at a speed ranging from about 10 revolutions per minute ( rpm ) to about 35 rpm , and more preferably from about 20 rpm to about 30 rpm . inner drum rotation at this speed causes the garments to tumble inside inner drum 32 / 112 . preferably , the garments are tumbled for a short period of time before fog generation begins . if a modified dryer is being used to carry out the procedure , the pretumble can be used to bring the equipment and garments to a uniform temperature before the generation of treatment fog begins . this temperature can be any temperature within the operating capabilities of the equipment . such temperature equilibration can also help offset the adiabatic cooling of the treatment agent during atomization . to generate the treatment agent fog , valves 17 / 109 , 20 / 111 , 131 and 132 are opened and adjusted to provide air or other entraining gas to the spray nozzle at a preselected pressure . air pressure is measured at pressure gauge 18 / 110 and 133 . a preferred range of air pressure is about 40 psi to about 80 psi , but can range up to about 100 psi . the flow of pressurized liquid to the nozzle is regulated by adjusting liquid control valve 20 / 111 , 131 , and measured by gauge 35 / 118 , 119 to a range of about 10 psi to about 40 psi . preferred liquid flow rates are about 1 - 3 gallons per minute . however , the process will work at flow rates as low as about 0 . 05 gallons per minute to as high as about 10 gallons per minute . the entrainment of the textile treatment agent in the gas stream by the nozzle creates a mist or fog of treatment agent inside the inner drum . as garments are tumbled in the inner drum , they are uniformly exposed to the treatment agent . valve 22 / 121 can be opened during mist spraying to vent the air introduced through the spray nozzle . a predetermined quantity of treatment agent is applied to the garments by tumbling them in the mist for a period of time . mist can be generated either continuously or at intervals while the garments are tumbled . for example , using an interval method , the garments could be tumbled for 30 seconds during mist production , tumbled for 60 seconds without mist production , followed by 30 seconds of mist production and so on . if only the desired amount of textile treatment agent is placed in the reservoir , and if a transparent conduit is used for the conduits 19 / 105 , 130 the end of the treatment will be signalled by the absence of liquid in these conduits . when the desired quantity of treatment agent has been added , the valves 17 / 109 and 132 are closed to stop the flow of air and liquid to the nozzles 15 / 138 and 128 . following the generation of mist , the garments are tumbled for a period ranging from about one minute to about ten minutes to evenly distribute to the tumbling garments the chemical agent fog remaining in the housing , and to evenly distribute the moisture absorbed by the garments between the garments . garments treated according to this process typically absorb textile treatment agents in an amount ranging from about 5 % up to about 100 % of their dry weight , and very likely could absorb up to about 150 % of their dry weight in textile treatment agents , depending upon the cloth used in producing the garment or garment work piece and the desired finish . the garments may then be subjected to other processes or may be dried . the quantity of treatment agent applied to , and absorbed by , the garments is controlled by the flow rates and time of treatment . the quantity of treatment agent required to achieve a particular result can be easily determined by simple experimentation , and depends upon the concentration of the liquid agent used , its ability to affect fabrics , the type of fabric used to construct the garments , the starting color and &# 34 ; hand &# 34 ; of the garments , and the final finish desired . the following examples are provided to illustrate the process described above . it is not intended , in any way , to limit the present invention : a milnor model 450 washing machine was fitted with a spraying systems co . model no . 1 / 2jbc - ss back connect nozzle modified for open and flat spray using a spraying systems co . sue75 adapter , mounted to be substantially aligned with the axis of rotation of the washer drum . 200 pounds of cotton , canvas trousers were loaded in the drum . 200 pounds of an aqueous solution containing cross - linking , easy care ( e . g ., permanent press type ) fabric finish was prepared and loaded into a chemical reservoir . tumbling began , with tumbling speed at 30 rpm . air pressure was set to 80 psi . liquid flow rate at ambient pressure was set to 25 pounds per minute . after 6 minutes , atomizing was discontinued and tumbling continued for a total of 10 minutes . at this point , the door was opened and the garments checked for moisture distribution . of the 160 pounds of solution used , 150 - 154 pounds was absorbed by the garments ( about 75 - 77 % of the garments &# 39 ; dry weight ). there was no residual liquid in the bottom of the washer drum . following treatment , the garments were transferred to a dryer and dried at 180 degrees to remove all but 10 - 12 % of the moisture , followed by a 10 minute cool down . the treated garments were then pressed followed by curing at 320 degrees for at least 6 minutes to react the fabric finish . uniform coverage was obtained , with a result equivalent to that which we previously obtained using a prior , conventional immersion process used for applying the same easy care fabric finish . use of the prior , conventional immersion process typically required the preparation and use of 1600 pounds of the same liquid fabric finish solution . a unimac washer model no . uy230 having a sample port was modified by placing a metal bracket into the washing machine drum through the sample port . a spraying systems co . model 1 / 4 &# 34 ; jbc - ss back connect nozzle was fitted to an air line and a liquid line using swagelok precision instrument fittings ( 1 / 4 &# 34 ; npt to 1 / 4 &# 34 ; tube stainless steel male connector ). the air line and liquid line were formed from polyethylene tubing rated for up to 90 psi and having an inside diameter of 0 . 295 &# 34 ; and an outside diameter of 0 . 375 &# 34 ; the liquid and air lines were attached to a binks pressure spraying reservoir with a 2 gallon capacity . the reservoir includes two air gauges : one measures the pressure of the air entering the vessel , and the other measures the pressure being induced to the liquid . these gauges are controlled by regulating valves , with the incoming air valve being a ball valve to enable even introduction of air into the vessel . 4 kg of an aqueous solution containing 200 grams of a cationic , polyethylene softener was placed in the reservoir . the incoming air regulating valve was adjusted to provide 80 psi of incoming air and the outgoing regulating valve was adjusted to provide 20 psi of liquid pressure . incoming air was provided from a standard compressor which can furnish air at 120 psi . 5 kg of 100 % cotton denim garments was loaded into the washer , and rotation of the inner drum was commenced at 30 rpm . atomization was commenced by opening control valves leading to the nozzle , and was continued until there was no more liquid flowing through the liquid feed line . the control valves were closed , and the process was completed by tumbling for 2 minutes . the garments actually gained about 77 % of their dry weight during the process . the garments were removed and completely dried in a conventional dryer . the final product was examined visually and by feel , and found to match or exceed current production standards using immersion techniques . 800 grams of 100 % cotton natural denim ( no indigo or dyes ) was placed in a unimac model no . uy18 washer . these were conventionally pre - washed and extracted to about 60 % moisture . a 0 . 5 % solution of dye was prepared by mixing 2 liters of water with 4 grams of remazol navy rgb and 10 grams of 50 % naoh . the ph of the solution was measured at 11 . 6 . the dye solution was heated to a temperature of 180 degrees fahrenheit . two liters of the heated dye solution was loaded into the reservoir . the garments were tumbled at 30 rpm , and air and liquid pressure was set at 50 and 20 psi respectively . mist generation began after a few minutes of pretumbling , and was continued until the dye solution was exhausted . tumbling continued for two minutes after the air and liquid valves were turned off . the washer was opened and distribution of the dye mist was checked . conventional washing was then employed to complete the dyeing process . by using the method and apparatus of this invention , a wide variety of fabric finishes can be advantageously applied to provide a permanent - press type easy care finish , or a uniform worn / soft look without the use of abrasive particles , or to apply a dye or other fabric finish . the method and apparatus of the present invention allows significant savings of water and processing chemicals . further , the method and apparatus of the present invention , particularly when used with bleaches or dyes , should provide unique &# 34 ; looks &# 34 ; not hitherto producable by conventional means . the present invention achieves these results by creating a mist or fog of textile treatment agent and tumbling dry or damp garments or fabric work pieces through the treatment fog . one skilled in the art will recognize that it would be possible to construct the elements of the present invention from a variety of materials and to modify the process in a variety of ways . while the preferred embodiments have been described in detail and shown in the accompanying drawings , it will be evident that various further modifications are possible without departing from the scope of the invention as set forth in the following claims .