Detergent compositions and washing liquors for use in textile laundering processes.

TECHNICAL FIELD

The present invention has relation to detergent compositions and wash liquors for laundering of textiles using small amounts of water and energy without substantial soil redeposition. This results in a superior level of detergency performance. A process for laundering textiles using small amounts of water and energy and apparatus for carrying out the process are disclosed in copending European Application No. 82305942.3-2304 Publication No. 0079234.

BACKGROUND INFORMATION

The conventional method of washing textiles in an automatic home-type washing machine in the United States is carried out in either a top loading or front loading machine. The difference between the two machines is that in a top loader the wash basket is rotatable around a substantially vertical axis and in a front loader the wash basket is rotatable around a substantially hori­zontal axis. Home-type top loading machines are, by far, the most popular, comprising 90% of the United States' automatic washing machine market.

The process for washing textiles in a home-type top loader begins by placing the textiles in the wash basket. In a normal capacity home-type top loader the wash basket can hold up to 7 kilograms of textiles. Detergent composition is then added to the wash basket. Finally, water, which is typically heated, is added to the wash basket to form a water and deter­gent solution known as the wash liquor. Thus, formation of the wash liquor is carried out in the wash basket in the presence of the textiles to be washed. The washing step is then completed by applying mechanical agitation to the system in order to loosen and remove the soil from the textiles.

The temperature and level of water and level of detergent composition used in the wash step can vary. 60% of the wash steps use warm water (typically around 35°C), with the balance being evenly split between hot water (typically around 50°C) and cold water (typically around 15°C). The level of water and detergent composition used in this step typically ranges from 40 liters to 90 liters and from 20 grams to 145 grams, respectively, depending upon the wash basket size and load size. The resulting detergent composition concen­tration in the wash liquor is from 210 parts per million (ppm) to 3,600 ppm.

The wash liquor is then removed and the textiles are rinsed. The rinse step normally comprises adding clear water to the wash basket. Mechanical agitation is normally applied during the rinse step to remove the detergent composition from the textiles. Finally, the water is drained and the textiles are spun to mech­anically remove as much water as possible. A cold water rinse is used in 60% of the rinse steps, with the balance being warm water rinses. The amount of water used in this step is typically the same as that used in the wash step. The rinse step is generally repeated one or more times.

The wash cycle of the home-type front loader is very similar to that of the home-type top loader. The temperature of the water and detergent composition concentration used in the wash­ing step are very similar to a home-type top loader. The basic difference is that the amount of water used in each of the wash and rinse steps typically ranges from 25 liters to 35 liters and, thus, the level of detergent composition is from 10 grams to 70 grams.

The complete conventional automatic wash process in a home-­type top loader typically uses from 130 liters to 265 liters of water. By way of contrast, a home-type front loader, though more efficient, typically uses 95 liters of water. This too is a considerable water expenditure for one wash cycle. Also, if the water is heated, there is a considerable energy expenditure. Both water and energy are costly to the consumer.

A known drawback normally exhibited by conventional auto­matic wash processes of the foregoing type is that soil redeposi­tion occurs in both the wash and rinse steps. Soil redeposition is soil that is detached from the textiles and goes into the wash or rinse liquor and is then redeposited onto the textiles. Thus, soil redeposition substantially limits the "net" cleaning per­formance.

Another known drawback normally exhibited by conventional automatic wash processes of the foregoing type is that dye trans­fer can occur when dealing with loads of differently colored textiles. Dye transfer is the detachment of dye from a textile into the wash liquor and its subsequent deposition onto another textile. To avoid dye transfer the consumer has found it neces­sary to perform the additional step of presorting the textiles, not only by textile type but also by color type.

U.S. Patent 4,344,198 issued to Arendt et al on August 17, 1982 claims a process for the washing of clothes through a wash and rinse cycle in a washing machine with a horizontal, perfor­ated, driven tub arranged inside a housing wherein the tub has at its rotating periphery a tangential area, in which during the washing and rinsing cycle as the tub rotates, the clothes are repeatedly lifted up and then fall in a trajectory path onto the lower portion of the tub and are then distributed without unbal­ance to the tub, as the tub velocity is gradually increased. The clothes are then centrifuged as the velocity is increased further. According to Arendt, his improvement comprises the steps of wetting the clothes with an amount of suds that gives a "doughy" consistency to the clothes by filling the tub with suds until the level of suds does not significantly rise above the tangential area of the tub by maintaining in the tub during washing an aqueous medium level of at least 5% of the tub's diameter, whereby the dry clothes are loaded individually into the tub which rotates at a speed at which the centrifugal velocity at the tub case is 0.3-0.8 g. The tub speed is then increased to 1 g. then gradually changed to a spin speed and after the spinning, reduced to a velocity in keeping with the loading speed. The process is thereafter followed with a rinse cycle which is similar to the washing cycle. According to Arendt, the exchange between "engaged" and "free" medium is achieved not so much by leaching but by the mechanical action of the tub. Finally, Arendt teaches that water is saved for the most part not by using smaller ratios of total media, but by reducing the number of wash and rinse cycles.

U.S. Patent 4,118,189 issued to Reinwald et al on October 3, 1978 discloses a wash process which consists of transforming a concentrated wash liquor, by the introduction of compressed air, into a foam which is thereafter applied to the soiled textiles. The textiles are mechanically agitated in the foam for at least thirty seconds, then the foam is destroyed and removed from the tex­tiles by spinning the textiles in a rotary perforated drum. This cycle is repeated at least five times, followed by conventional rinsing. Reinwald suggests that the dirt detached from the textile material and dispersed in a relatively high concentrated detergent solution is partially deposited again on the textile fiber during the subsequent rinsing due to a dilution of the wash liquor.

Still another attempt at using more concentrated wash liquor without encountering redeposition problems of the type discussed in the aforementioned patent issued to Reinwald is disclosed in U.S. Patent 3,650,673 issued to Ehner on March 21, 1972. Ehner discloses method and apparatus for washing textiles utilizing an amount of water corresponding to 50% to 150% of the dry weight of the textiles. The process consists of placing such quantities of water, the textiles to be laundered and a transfer agent, e.g., polyethylene foam having a large surface area per unit mass, in a rotatable enclosure similar to those employed in a front loader type washing machine and tumbling these materials together for a period of time. Soils removed from the textiles by the tumbling action are distributed over the combined exposed surface areas of the textiles and the transfer agent, which is subsequently separated from the textiles. Thus, the textiles are cleansed of the soils distributed onto the transfer agent. Ehner admits that a quantity of soil will be left on the textiles, but teaches that it will be substantially reduced from the original quantity and will be distributed so as to leave no objectionable areas of soil concentration. Following separation of the soil carrying transfer agent from the textiles, the textiles are sub­sequently dried in the same rotatable enclosure in which they are "washed" by tumbling them while circulating warm dry air there­through.

U.S. Patent 3,647,354 issued to Loeb on March 7, 1972 suggests that a wash process such as that disclosed in the afore­mentioned Ehner patent be followed by a rinse process employing a quantity of water sufficient only to bring the textiles to a condition of dampness. According to Loeb, the textiles are tumbled in a rotating drum with a clean transfer agent which functions in a manner similar to the transfer agent used in the wash process to separate detergent and loosened soils from the textiles.

Despite the advantages allegedly provided by wash processes of the foregoing type, they have not met with widespread com­mercial acceptance, particularly in the home laundry market.

Accordingly, an object of the present invention is to provide detergent compositions and wash liquor compositions for use in a process for laundering textiles using a small amount of water, yet minimizing soil redeposition and dye transfer, even without presorting of the textiles to be laundered.

SUMMARY OF THE INVENTION

According to the present invention there is provided a laundry detergent composition comprising surfactant, detergency builder and also one or more detergent auxiliary ingredients selected from; <ul id="ul0001" list-style="none"><li>i) activated bleach comprising a mixture of organic bleach activator with an oxygen bleach selected from sodium perborate, sodium carbonate peroxyhydrate, sodium pyrophosphate peroxyhydrate, urea peroxyhydrate and sodium peroxide and mixtures thereof;</li><li>ii) chlorine bleach;</li><li>iii) a mixture of one or more amylolytic and/or proteolytic enzymes with an oxygen bleach as recited in i) or with an activated bleach as defined in i);</li></ul> said auxiliary ingredient or ingredients being present at levels in said composition that would provide no consumer noticeable benefit for said auxiliary ingredient or ingredients when said detergent composition is used at the normal usage level in a conventional automatic wash process, wherein any activated bleach, comprising a mixture of bleach activator and oxygen bleach as hereinbefore defined, is present in an amount to provide from 0.03% to 0.3% by weight of the composition of available oxygen that can potentially be generated by peracid, any oxygen bleach is present in an amount to provide from 0.01% to 0.5% of available oxygen by weight of the composition, any chlorine bleach is present in an amount to provide 0.03% to 1.2% of available chlorine by weight of the composition, any proteolytic enzymes in combination with said oxygen bleach or mixture of bleach activator and oxygen bleach are present in an amount of from 0.01 to 0.27 Anson Units (A.U.) per 100g of the composition and any amylolytic enzymes in combination with said oxygen bleach or mixture of bleach activator and oxygen bleach are present in an amount of from 150 to 24,000 Amylase units per 100g of the composition.

A preferred detergent composition incorporates one or more of the above recited peroxygen bleaching compounds in combination with a bleach activator that can react with the bleaching compound to generate a peracid. Another highly preferred detergent composition incorporates a mixture of the bleaching compound and bleach activator together with a protease or an amylase or a mixture thereof.

In the wash liquor aspect of the invention the detergent composition is preferably present at a level of from 5000 ppm to 150,000 ppm, more preferably at a level of from 13,000 ppm to 50,000 ppm.

BRIEF DESCRIPTION OF THE DRAWINGS

While the Specification concludes with claims particularly pointing out and distinctly claiming the present invention, it is believed the present invention will be better understood from the following description in which: <ul id="ul0002" list-style="none"><li>Figure 1 is a schematic perspective illustration of parti­cularly preferred apparatus for carrying out the present launder­ing process;</li><li>Figure 2 is a cross-sectional illustration of the embodiment disclosed in Figure 1 taken along section line 2-2 of Figure 1;</li><li>Figure 2A is an inset of the drive pulley system shown in Figure 2 with the pulley-actuating clutch assembly in its alter­native position;</li><li>Figure 3 is a cross-sectional segment of the apparatus illus­trated in Figure 1 taken in a plane which passes through the center of the wash liquor applicator nozzle and the axis of rota­tion of the movable drum disclosed in Figure 1;</li><li>Figure 4 is a simplified cross-sectional illustration of a particularly preferred wash liquor applicator nozzle; and</li><li>Figure 5 is an end view of the wash liquor applicator nozzle shown in Figure 4.</li></ul>

DETAILED DESCRIPTION OF THE INVENTION

A. PREFERRED APPARATUS

Disclosed in Figure 1 is a schematic illustration of parti­cularly preferred apparatus for carrying out a laundering process using detergent compositions and liquors in accordance with the present invention. Figure 1 discloses a preferred embodiment of a washing machine 10 useful in the present invention. The apparatus in Figure 1 is particularly preferred when the quantity of wash liquor utilized is, at most, 2½ times the dry weight of the textiles to be laundered. Such maximum quantity of wash liquor approaches the maximum absorp­tion capacity of an average wash load. For purposes of clarity, none of the details of the cabinet nor the access door is shown in Figure 1.

In the embodiment of Figure 1, the washing machine 10 comprises a stationary drum 15 of generally cylindrical construc­tion and having a horizontal access opening 20. The centerline of the cylindrical stationary drum 15 coincides with the axis of rotation 300 of a movable drum 40 (sometimes referred to in the prior art as a wash basket) mounted within stationary drum 15.

As is more clearly illustrated in the cross-sectional views of Figures 2 and 3, stationary drum 15 comprises a peripheral wall 16, a back wall 17 secured to one edge of the peripheral wall, a front wall 18 secured to the opposite edge of the peripheral wall, said front wall having a tubular-shaped extension 19 having an access opening 20 used to load and unload laundry from the washing machine 10. Access opening 20 forms a seal with pliable sealing gasket 210 which is secured about its outermost periphery to the front wall 200 of the washing machine cabinet. When the washing machine 10 is in operation, the washing machine's access door 220 is in the closed position shown in Figure 2 and forms a watertight seal against the outermost portion of pliable sealing gasket 210. These latter elements are illustrated only in the cross-section of Figure 2 to ensure maximum clarity in the remaining drawing figures. The lowermost portion of stationary drum 15 is provided with a drain connection 21 located in peri­pheral wall 16. The drain connection 21 is connected by means of a flexible connecting line 142 to the suction side of a rinse liquor discharge pump 140 which is secured by means of support 141 to the base of the washing machine cabinet (not shown). Connect­ing line 143 conveys rinse liquor discharged from the pump 140 to a sewer drain (not shown).

As can also be seen in Figures 1 and 2, stationary drum 15 is supported by means of four suspension springs 66 which are connected at one end to anchor means 65 secured to the upper­most portion of the stationary drum 15 and at their other end to fixed anchor means 67 which are secured to the washing machine cabinet (not shown).

Extending from the lowermost portion of peripheral wall 16 are four support members 70, the lowermost ends of which are secured to motion limiting damper pads 71. A vertical guide plate 72 passes between the two sets of motion limiting damper pads 71. Sufficient clearance is provided between the motion limiting damper pads 71 and the guide plate 72, which is secured to the base of the washing machine cabinet (not shown), so that the stationary drum 15 may undergo limited up-and-down and side-to-­side movement while access opening 20 and tubular extension 19 remain in sealed engagement with pliable sealing gasket 210. The resilient mounting of stationary drum 15 minimizes the transmis­sion of vibration which occurs during moments of imbalanced loading to the washing machine cabinet (not shown).

Located inside stationary drum 15 is a movable drum 40 comprising a perforated peripheral wall 41, a substantially imper­forate back wall 42 secured to one edge of said peripheral wall and a substantially imperforate front wall 43 secured to the opposite edge thereof. Extending from the front wall 43 of the movable drum 40 is a tubular-shaped extension 44 which termi­nates in an access opening 45 which is concentrically aligned with the access opening 20 in stationary drum 15. Equally spaced on the inner circumference of peripheral wall 41 are three lifting vanes 47 of substantially triangular cross-section. The innermost edge of the side walls 48 of the triangular-shaped vanes 47 preferably terminate to form an innermost land area 49. In a particularly preferred embodiment, each of the vanes is symmetrically-shaped about a radially extending line originating at the axis of rotation 300 of movable drum 40 and passing through its altitude. This permits rotation of movable drum 40 in opposite directions with equal lifting effect on the articles being laun­dered.

In an exemplary embodiment of a washing machine 10 useful in the present invention, the movable drum 40 measured approximately 21½" (54.6 cm.) in diameter by approximately 12" (30.5 cm.) in depth, while the triangular-shaped lifting vanes 47 exhibited a base of approximately 2" (5.1 cm.) in width by 9" (22.9 cm.) in depth, an overall altitude of approximately 3" (7.6 cm.) and a land area 49 measuring approximately 1" (2.5 cm.) in width by 7" (17.8 cm.) in depth. The inner movable drum 40 exhibited approximately 750 uniformly spaced peforations 46, each perfora­tion having a diameter of approximately 1/4" (0.635 cm.). The stationary drum 15 enclosing the aforementioned movable drum 40 measured approximately 24" (61 cm.) in diameter.

As will be apparent from an inspection of Figure 2, movable drum 40 is rotatably secured to stationary drum 15 by means of driveshaft 29. The innermost end of driveshaft 29 incorporates an integral flange 30 which is secured by means of companion flange 31 and a multiplicity of fasteners, such as rivets 32, to the back wall 42 of movable drum 40. The shaft portion of driveshaft 29 passes through a clearance hole 51 in the back wall 42 of movable drum 40 and is supported by means of a pair of bearings 25 secured to the back wall 17 of stationary drum 15. Bearings 25 are secured in position by means of bearing retainers 22 which are joined to one another and to the back wall 17 by a multiplicity of conventional fasteners, such as rivets 33. The shaft portion of driveshaft 29 passes through a clearance hole 26 in back wall 17 of stationary drum 15.

Power to rotate movable drum 40 is transmitted to the exter­nal portion of driveshaft 29 either by means of an eccentrically mounted driven pulley 28 or by means of a concentrically mounted driven pulley 34 which are both secured in fixed relation to driveshaft 29. As will be explained in greater detail hereinafter, the eccentrically mounted driven pulley 28 is used to vary the speed of rotation of the movable drum 40 throughout each revolu­tion of the drum, while the concentrically mounted driven pulley 34 is used to drive the movable drum 40 at a constant speed of rotation throughout each revolution.

The drive system for the movable drum 40 preferably com­prises a variable speed drive motor 60 secured by means of support 61 to the peripheral wall 16 of stationary drum 15. Because the drive motor 60 is secured to the stationary drum 15, any movement of the stationary drum 15 does not affect the speed of rotation of movable drum 40. The output shaft 62 of drive motor 60 has secured thereto a concentrically mounted drive pulley 38 and a concentrically mounted drive pulley 36. A two-­position, pulley-actuating clutch assembly 37 is positioned inter­mediate pulleys 36 and 38. Drive pulleys 36 and 38 are both of two-piece construction so as to permit engagement or disengage­ment of their respective drive belts by pulley-actuating clutch assembly 37. The housing of clutch assembly 37 through which drive motor shaft 62 freely passes is preferably secured to the housing of drive motor 60 by means of a laterally extending support 63, as generally shown in Figures 1 and 2.

Concentrically mounted drive pulley 38 is connected to eccentrically mounted driven pulley 28 by means of a conventional drive belt 27. Likewise, concentrically mounted drive pulley 36 is connected to concentrically mounted drive pulley 34 by means of a conventional drive belt 35. When clutch assembly 37 is in its first position, the distance between the opposing faces of drive pulley 36 is sufficiently great that drive belt 35 is allowed to freely slip therebetween when driveshaft 29 revolves. When clutch assemby 37 is actuated into its second position, the opposing faces of drive pulley 36 are brought sufficiently close together that drive belt 35 is driven by pulley 36. Simultane­ously, the distance between the opposing faces of drive pulley 38 is increased to a distance which is sufficiently great that drive belt 27 is allowed to freely slip therebetween when driveshaft 29 revolves. Figure 2 depicts drive pulley 36 in the engaged posi­tion, while the inset of Figure 2A depicts drive pulley 38 in the engaged position.

In a particularly preferred apparatus for use in the present inven­tion, drive motor 60 is not only variable speed, but is also reversible so that movable drum 40 may be rotated first in one direction and then in the opposite direction throughout the vari­ous portions of the laundering cycle. It is believed that revers­ing the direction of drum rotation several times during the laundering cycle will provide more uniform application of the wash liquor, more uniform agitation and more uniform heat transfer to the textiles being laundered, and hence more effective cleansing.

In the exemplary washing machine described earlier herein, the eccentrically mounted driven pulley 28 was used to provide rotation of the movable drum 40 at a speed which varied from 48 to 58 revolutions per minute during each complete revolution of the drum, while the concentrically mounted pulley system comprising pulleys 36 and 34 was used to provide rotation of the movable drum at a constant speed of about 544 revolutions per minute.

Referring again to the particularly preferred apparatus of Figure 1, there is shown an air circulating blower 160, preferably of the centrifugal variety, secured by means of a support 162 to an upper portion of peripheral wall 16 of the stationary drum 15. The air circulating blower 160 is preferably powered by variable speed drive motor 161. A connecting duct 163 conveys air from the blower discharge to a heater 164. The heater 164 includes a heating element 165 over which the air must pass prior to enter­ing connecting duct 166 which conveys heated air from the heater 164 to an inlet opening 180 located in the peripheral wall 16 of the stationary drum 15. In the apparatus disclosed in Figures 1-3, heated air is introduced intermediate the peripheral wall 16 of stationary drum 15 and the peripheral wall 41 of movable drum 40. The bulk of the heated air introduced in this area is forced to enter movable drum 40 via perforations 46 located in peripheral wall 41. As pointed out earlier herein, the movable drum 40 is caused to rotate at varying speed during the laundering portion of the cycle via the eccentrically mounted pulley 28. Since the articles being laundered are normally located at or adjacent the innermost surface of peripheral wall 41 of movable drum 40 during the laundering cycle, the heated air introduced between the stationary and movable drums is caused to penetrate the textiles being laundered on its way to return opening 190 located in tubular extension 19 of stationary drum 15.

Return opening 190 is connected to a diverter valve 168 by means of connecting duct 167. Diverter valve 168 has two posi­tions. In its first position, connecting ducts 170 and 171 are blocked off and all of the humid air withdrawn from stationary drum 15 is returned to the suction side of air circulating blower 160 via connecting duct 172. As will be explained in greater detail in the ensuing preferred process description, diverter valve 168 remains in its first position during the laundering portion of the cycle described herein. The temperature of the returning air is sensed in connecting duct 167 by means of a sensing element 173 mounted in the duct. The sensing element 173, which is preferably of the thermistor type, sends a signal to temperature controller 175 via signal transmission line 174. The temperature controller 175, which is preferably adjustable, trans­mits a signal via signal transmission line 176 to the heating element 165 in heater 164 to either raise, lower or maintain the temperature of the air being introduced into connecting duct 166. Thus, the heated air employed during the laundering portion of the cycle is continually recirculated by means of the aforemen­tioned closed loop system, and its temperature is continuously monitored and maintained at a predetermined level.

In a particularly preferred apparatus for use in the present inven­tion, the washing machine 10 may also be employed as a clothes dryer. This is accomplished by manipulation of diverter valve 168. Advancing control lever 169 from the aforementioned first position of the diverter valve to a second position connects air duct 171 with return air duct 172 and air duct 170 with return air duct 167. Since air ducts 170 and 171 are both vented to atmosphere, the effect of advancing the diverter valve 168 to its second position is to convert the closed loop recirculation system described earlier herein in conjunction with the laundering cycle to a non-recirculating vented system. In the vented mode of operation, fresh air is drawn into duct 171 and routed through the heater as before to provide warm dry air for drying the laundered textiles contained within movable drum 40. Similarly, the moist air withdrawn from stationary drum 15 is discharged to the atmosphere via connecting duct 170 rather than being recir­culated to the suction side of the air circulating blower 160. During the drying portion of the cycle, movable drum 40 is rotated, as during the laundering cycle, by drive motor 60 oper­ating through the eccentrically mounted pulley and drive belt system described earlier herein. Temperature of the air used during the drying cycle is also monitored and controlled by sensing element 173 and temperature controller 175. However, the temperature selected during the drying cycle may differ from that employed during the laundering cycle. Accordingly, the temperature controller 175 preferably has two independently adjustable set points which may be preadjusted to different tem­perature levels for the laundering and drying cycles.

As will be readily apparent to those skilled in the art, diverter valve control lever 169 may be automatically actuated rather than manually actuated, as disclosed in the present illus­trations. This may be accomplished utilizing solenoids or similar control apparatus well known in the art and therefore not shown.

In the exemplary washing machine described earlier herein, the air circulating blower 160 utilized to recir­culate the humid air during the laundering portion of the cycle had a rated capacity of 460 cubic feet (13.03 cubic meters) of air per minute at a pressure of 0.25" (0.635 cm.) of water, and the connecting ducts used to construct the recirculation loop were sized to permit recirculation of the air at rated flow. The heater 164 employed on the exemplary machine contained a heating ele­ment 165 comprising a 240 volt AC, 5200 watt, spiral wound, nichrome coil. The temperature sensing element 173 comprised a thermistor inserted into return air duct 167. Temperature con­troller 175 comprised a 0-200°F (-17.8 - 93.3°C) adjustable unit having a set point accuracy of 3% of range and a set point stability of 2% of span from the nominal setting. A high limit snap disc-type thermostat (not shown) having a range of 400-450°F (204.4 - 232.2°C) was also utilized to protect the system.

Referring again to Figures 1-3, preferred wash liquor and rinse liquor addition systems are disclosed. In particular, the wash liquor utilized during the laundering portion of the cycle is prepared in wash liquor reservoir 89 which is schematically illus­trated in Figure 1. In a particularly preferred form of the present invention, the cycle is initiated by introducing a predetermined amount of detergent composition, which may be in granular, paste, gel or liquid in form, into the wash liquor reservoir 89. Water from supply line 80 passes through pressure regulator 81, connecting line 101 and control valves 82, 84 and 87, which are in the open position, into the side of wash liquor reservoir 89 via connecting lines 96, 94 and 99. Control valves 85 and 88 are closed at this point in time to prevent the water from escaping via delivery lines 95 and 98. Located within wash liquor reservoir 89 is a level sensing probe 92 which is connected at its uppermost end to a level sensor 91. The level of the liquid introduced into the wash liquor reservoir rises along probe 92. When the liquid level within reservoir 89 reaches a predetermined point, level sensor 91 transmits a signal to level controller 93 via signal transmission line 105. Level controller 93 sends a signal via signal transmission line 106 to close off control valve 82. After control valve 82 has been closed, pump 86 is started to initiate recirculation, mixing and formation of a wash liquor within reservoir 89. Control valves 85 and 88 remain closed during the mixing cycle. Pump 86 withdraws liquid from the bottom of wash liquor reservoir 89 via connecting lines 99 and 97 and discharges the liquid withdrawn back into the reservoir via connecting lines 94 and 96. Recirculation of the liquid is carried out until such time as the detergent composition is substantially dissolved or dispersed in the water. The time required will of course vary, depending upon such variables as the solubility characteristics of the particular detergent composition employed, the concentration of detergent composition, the temperature of the incoming water and like. To minimize the mixing time, it is generally preferred to design the liquid recirculation loop to maximize the turbulence of flow during recirculation.

As will be explained in greater detail in conjunction with the ensuing preferred process description, the present laundering process may be carried out without the addition of heat energy via heating element 165. However, experience to date has demon­strated that it is generally preferable that wash liquor and rinse liquor temperatures be in the range of 25°C, or higher to maximize the benefits afforded by the present process. To achieve this objective when the heat energy addition option is not employed during the laundering cycle, a water preheating unit (not shown) may be utilized on the incoming water supply line to ensure that the temperature of the incoming water does not fall below 25°C, even during cold weather conditions.

As pointed out earlier herein, a relatively small amount of wash liquor is utilized during the present laundering process when compared to prior art laundering processes. Accordingly, the method of applying the wash liquor to the textiles to be laundered must be highly effective in order to provide substan­tially even and complete distribution, especially when very reduced quantities of wash liquor are utilized. One particularly preferred means of accomplishing this objective has been to apply the wash liquor by means of a high pressure spray nozzle 100 as the movable drum 40 rotates. During the wash liquor application step control valves 82 and 88 are closed and control valves 84, 85 and 87 are opened. Wash liquor 230 is withdrawn from reservoir 89 by means of pump 86 and is conveyed via flexible delivery line 95 to high pressure spray nozzle 100 which, in the illustrated embodiment, is mounted in the tubular-shaped extension 19 of stationary drum 15. A small amount of wash liquor is also per­mitted to flow through valve 84 and delivery line 96 back into reservoir 89 to provide some recirculation and mixing during the wash liquor application cycle. As can be seen from Figure 3, which is a simplified diametral cross-section taken through spray nozzle 100 and the axis of rotation 300 of movable drum 40, high pressure nozzle 100 is located at approximately the 8 o'clock position and a substantially flat, fan-shaped spray of wash liquor 230 is targeted to strike peripheral wall 41 and back wall 42 of the movable drum 40 which, in the illustrated apparatus is rotating in a counterclockwise orientation, at approximately the 2 o'clock position.

In order to distribute the textiles to be laundered substan­tially uniformly about the periphery of the movable drum 40, the textiles are initially tumbled at low speed via eccentrically mounted driven pulley 28. Movable drum 40 is thereafter acceler­ated by concentrically mounted driven pulley 36 to a speed which is sufficient to hold the substantially uniformly distributed articles against peripheral wall 41. The wash liquor application step is initiated while the articles are held against peripheral wall 41. However, after several revolutions of movable drum 40, the speed of drum rotation is reduced by transferring the input driving force from concentrically mounted driven pulley 36 back to eccentrically mounted driven pulley 38. The slower speed of rotation, which varies throughout each revolution of movable drum 40, causes the textiles within the drum to be carried by lifting vanes 47 to approximately the 1 o'clock position, at which point they tend to fall away from peripheral wall 41 and pass through the substantially flat, fan-shaped spray of wash liquor 230 on their return to the bottom of the drum.

While in the illustrated apparatus the drum rotation is oriented in a counterclockwise direction, it has also been learned that the drum may, if desired, be rotated in a clockwise direc­tion. In the latter case the textiles which fall away from the peripheral wall 41 at approximately the 11 o'clock position still pass through the fan-shaped spray of wash liquor 230 on their return to the bottom of the drum.

The wash liquor application step is carried out until all or a predetermined amount of the wash liquor contained in reservoir 89 has been applied to the textiles being laundered. The quantity of wash liquor applied for a given laundering cycle will vary, depending upon such factors as the quantity of textiles being laundered, their materials of construction, and the soil type and level of soil loading, as more fully described in the accompanying detailed process description. When the wash liquor application step has been completed, even with the smallest quantities of wash liquor within the invention, the wash liquor is substantially evenly and completely distributed onto the textiles being sub­jected to the present laundering process.

To further enhance distribution, wash liquor application may be carried out in several stages, with the movable drum 40 being momentarily stopped and restarted between each stage to allow the articles to completely redistribute themselves prior to each stage of wash liquor application. Similarly, multiple spray nozzles may be employed.

Figures 4 and 5 disclose the internal configuration of the spray nozzle 100 employed in the exemplary washing machine described earlier herein. In particular, an irregularly-shaped orifice 400 is formed by intersection of a V-shaped groove 410 having an included angle α of approximately 45° extending across the nozzle's face 430 and a cylindrical passageway 420 passing through its longitudinal axis. A cross-­sectional view of this exemplary nozzle 100 is generally disclosed in Figure 4, and an end view taken along view line 5-5 is shown in Figure 5. The maximum width W of the aforementioned groove 410 was approximately 0.075" (0.19 cm.), as measured at the face 430 of the nozzle. The diameter D₂ of the nozzle face 430 was approximately 0.40" (1.02 cm.). The diameter D₁ of passageway 420 was approximately 0.125" (0.32 cm.) along its length, con­verging at an included angle β of approximately 120° adjacent the nozzle face 430. Intersection of groove 410 and passageway 420 produced the irregularly shaped orifice 400 generally shown in Figure 5. Wash liquor was fed by means of a pump 86 having a rated capacity of 500 gallons per hour at 7 psi connected to nozzle 100 via a 1/4" (0.635 cm.) diameter flexible delivery line 95. The nozzle 100 was installed in tubular shaped extension 19 at approximately the 8 o'clock position with its spray oriented so as to strike peripheral wall 41 and back wall 42 of movable drum 40, as generally shown in Figure 3. Drum rotation was oriented clockwise when viewed from its front wall side.

While spraying has been found to be a particularly preferred method of wash liquor application, other application means, e.g., atomizers, which will produce a similar distribution of wash liquor throughout the textiles to be laundered, as described in the accompanying detailed process description, may be employed with equal success.

After the wash liquor application has been completed, pre­ferably mechanical energy is applied to the textiles by rotating movable drum 40 at relatively low speed such that the textiles being laundered are continually lifted by vanes 47 secured within the movable drum and caused to mechanically tumble back toward the bottom of the drum. As pointed out earlier herein, the tumbling action is accentuated by varying the speed of rotation of the movable drum 40 throughout each revolution of the drum. This is accomplished in the machine embodiment disclosed in Figure 1 by driving the movable drum 40 via eccentrically mounted driven pulley 28. In a particularly preferred embodiment of the invention, the direction of rotation of movable drum 40 is reversed several times throughout the laundering cycle. This provides more thorough mechanical agitation of the textiles being laundered and, hence, more uniform heat transfer throughout the textiles. In addition, it minimizes the tendency of textiles, particularly long and thin appendages on textiles, e.g., sleeves on shirts, from becoming knotted up.

Heat energy is preferably supplied to the textiles being laundered during the aforementioned mechanical agitation process. In the machine disclosed in Figure 1 this is accom­plished by recirculating moist humid air through heater 164 using air handling blower 160. Preferred air temperature ranges and cycle times are specified in the accompanying detailed process description.

Following the mechanical and/or heat energy application phase of the laundering process, the textiles contained within the movable drum 40 are rinsed with an aqueous rinse liquor 240, which in a particularly preferred embodiment com­prises water. This is supplied from water supply line 80 via control valve 83 which is opened to permit delivery of rinse water to movable drum 40 via flexible delivery line 110 and applicator nozzle 120. Applicator nozzle 120 is also preferably mounted in the tubular shaped extension 19 of stationary drum 15. Appli­cator nozzle 120 need not, however, be a high pressure spray nozzle such as that utilized to apply wash liquor. Because free standing liquor is employed in movable drum 40 during the rinse portion of the present laundering cycle, it is believed that the particular manner of applying the rinse liquor to the laundered textiles is much less critical than the manner of applying the wash liquor. Accordingly, the rinse liquor may be added by any of several means well known in the art, e.g., directly into stationary drum 15 via an orifice in peripheral wall 16.

The textiles being laundered are preferably subjected to mechanical agitation during both the rinse liquor addition and the rinse cycles. This is preferably done by rotating movable drum 40 at relatively low speed via eccentrically mounted driven pulley 28. As with the mechanical energy and heat energy application phase of the laundering cycle, the direction of rotation of movable drum 40 is preferably changed several times during the rinse cycle to ensure more uniform rinsing.

In a particularly preferred mode of operation, several relatively short rinse cycles are employed to remove the loosened soil and detergent from the textiles being laundered.

It is believed preferable to remove the rinse water from movable drum 40 during the initial rinse cycles without resorting to high speed centrifugation, i.e., high speed rotation of movable drum 40. While not wishing to be bound, it is believed that avoidance of centrifugation during the early rinse cycles minimizes the chance of redepositing suspended soils onto the textiles being laundered, since the rinse liquor is not forced through the tex­tiles being laundered on its way to the perforations 46 in peri­pheral wall 41 of movable drum 40. Accordingly, centrifugation to remove as much moisture as possible from the laundered and rinsed textiles is preferably deferred until the last rinse cycle. As will be clear from an inspection of Figures 1 and 2, rinse water which is removed from movable drum 40 either by gravity or by centrifugation is ultimately removed from stationary drum 15 through drain connection 21 by means of discharge pump 140 from whence it is preferably conveyed to the sewer.

If desired, laundry additives of various types, e.g., fabric softeners, may be employed in conjunction with the laundering process described herein. If desired, such additives may be applied to the articles being laundered by conventional gravity addition (not shown) or via pressure spray nozzle 100. In the latter instance, one or more secondary reservoirs 90 may be employed. The discharge of these secondary reservoirs may be connected, as by delivery line 98 and control valve 88, to the wash liquor mixing system.

Depending upon the nature of the additive, it may be desir­able to flush the wash liquor reservoir 89 with water prior to introducing the additive into the reservoir. This may be done by refilling the reservoir with water and recirculating the solution via pump 86 prior to discharging it into one of the rinse cycles. After wash liquor reservoir 89 has been flushed, control valve 88 may be opened to permit delivery of an additive from reservoir 90 to the wash liquor reservoir via pump 86. When a predetermined quantity of the additive has been transferred to wash liquor reservoir 89, a water dilution cycle may, if desired, by carried out in a manner similar to that employed for mixing the wash liquor, i.e., water from the supply line is added to reservoir 89, control valves 82, 85 and 88 are closed, and the additive solution is recirculated via pump 86 to the wash liquor reservoir 89 until such time as the additive is ready for application to the articles being laundered. Application of the mixed additive solution may thereafter be carried out during one or more of the rinse cycles employed in the present process in a manner generally similar to that employed for the application of the wash liquor.

Following centrifugation by high speed rotation of movable drum 40 to mechanically remove as much rinse liquor as is feasible, the washing machine 10 may be operated as a conven­tional clothes drying apparatus by actuating diverter valve 168 from its first position to its second position. In its second position, diverter valve 168 permits fresh air to be drawn into connecting duct 171 via suction from blower 160, heated to a predetermined temperature by heater 164, circulated through the laundered and rinsed textiles contained in rotating drum 40 and vented from stationary drum 15 to the atmosphere via connecting duct 170. As will be appreciated by those skilled in the art, movable drum 40 is preferably operated at low speed via eccentri­cally mounted driven pulley 28 throughout the drying cycle to provide more uniform air flow and heat transfer through the laundered and rinsed textiles contained therein.

PREFERRED PROCESS

The detergent compositions and wash liquors of the present invention are adapted for use in a process for laundering textiles, hereinafter referred to as the "concentrated laundering process". The process utilizes quantities of an aqueous liquid wash liquor in the wash step ranging from, at least, just enough to be substantially evenly and completely distributed onto all portions of the textiles to, at most, 5 times the dry weight of the textiles to be laundered. The quantities of wash liquor are applied to the textiles during the wash step. It is essential that the wash liquor be substantially evenly and completely distributed onto the textiles. In the final step or steps of the process the textiles are rinsed with water to remove both the soil and detergent composition.

The quantities of wash liquor that can be used in the wash step range from, at least, just enough to be substantially evenly and completely distributed onto all portions of the textiles to, at most, 5 times the dry weight of the textiles to be laundered. The quantities of wash liquor in the range of the lower limit approach what is equivalent to directly applying a conventional level of a typical commercially available heavy duty liquid detergent composition to the textiles. Surprisingly, the addition of more wash liquor, i.e., adding both water and deter­gent composition to the wash liquor such that the wash liquor concentration remains constant, so that the upper limit is exceeded results in essentially no additional soil removal and no less soil redeposition. It should be noted that depending on the nature of the textiles, soil types, soil levels, detergent compo­sition levels and detergent composition formulations that the upper limit can vary slightly. When quantities of wash liquor exceeding the absorption capacity of the textiles are utilized, only limited amounts of mechanical energy should be applied to the textiles during the wash step in order to prevent oversudsing. But, surprisingly, a good level of cleaning performance is achieved nonetheless. Also, with quantities of wash liquor exceeding the absorption capacity of the textiles, though possible, it is not essential that the preferred apparatus be utilized.

MORE PREFERRED QUANTITIES OF WASH LIQUOR

Therefore, in a more preferred mode of operation the quantity of wash liquor that can be used in the wash step ranges from about just enough to be substantially evenly and completely distributed onto all portions of the textiles to, at most, none or minimal amounts of wash liquor in excess of the absorption capacity of the textiles. With such quantities there is at most minimal amounts of "free" wash liquor. Thus, essentially all of the wash liquor and, therefore, essentially all of the detergent composition contained in the wash liquor, will be in intimate contact with the textiles throughout the wash step. This permits the application of a substantial amount of mechanical agitation to the textiles during the wash step, as discussed below, without any oversudsing.

Surprisingly, numerous other benefits are obtained when the quantities of wash liquor of this more preferred mode of operation are utilized. For example, since essentially all of the detergent composition is in intimate contact with the textiles, the detergent composition is being utilized extremely efficiently. Also, there is lower limit approach what is equivalent to directly applying a conventional level of a typical commercially available heavy duty liquid detergent composition to the textiles. Surprisingly, the addition of more wash liquor, i.e., adding both water and deter­gent composition to the wash liquor such that the wash liquor concentration remains constant, so that the upper limit is exceeded results in essentially no additional soil removal and no less soil redeposition. It should be noted that depending on the nature of the textiles, soil types, soil levels, detergent compo­sition levels and detergent composition formulations that the upper limit can vary slightly. When quantities of wash liquor exceeding the absorption capacity of the textiles are utilized, only limited amounts of mechanical energy should be applied to the textiles during the wash step in order to prevent oversudsing. But, surprisingly, a good level of cleaning performance is achieved nonetheless. Also, with quantities of wash liquor exceeding the absorption capacity of the textiles, though possible, it is not essential that the preferred apparatus be utilized.

MORE PREFERRED QUANTITIES OF WASH LIQUOR

Therefore, in a more preferred mode of operation the quantity of wash liquor that can be used in the wash step ranges from about just enough to be substantially evenly and completely distributed onto all portions of the textiles to, at most, none or minimal amounts of wash liquor in excess of the absorption capacity of the textiles. With such quantities there is at most minimal amounts of "free" wash liquor. Thus, essentially all of the wash liquor and, therefore, essentially all of the detergent composition contained in the wash liquor, will be in intimate contact with the textiles throughout the wash step. This permits the application of a substantial amount of mechanical agitation to the textiles during the wash step, as discussed below, without any oversudsing.

Surprisingly, numerous other benefits are obtained when the quantities of wash liquor of this more preferred mode of operation are utilized. For example, since essentially all of the detergent composition is in intimate contact with the textiles, the detergent composition is being utilized extremely efficiently. Also, there is essentially no wash liquor for the dye of the textiles to be released into and subsequently deposited onto another textile. Thus, dye transfer during the wash step is minimized and, therefore, it is generally not necessary for the consumer to presort the textiles. This is particularly significant if the laundry load contains the type of textile commonly known as a dye bleeder, i.e., one that contains excessive amounts of highly soluble dyes. Another benefit is that the addition of more wash liquor, i.e., adding both water and detergent composition to the wash liquor such that the wash liquor concentration remains constant, to approach the upper limit of 5 times the dry weight of the textiles to be laundered provides minimal additional soil removal in view of the cost of the additional detergent com­position utilized.

In a more preferred embodiment, the quantity of wash liquor that can be used in the wash step is from just enough to be substantially evenly and completely distributed onto the tex­tiles to 2½ times the dry weight of the textiles and preferably from 3/4 to 1½ times the dry weight of the textiles. These ranges provide the most efficient use of a deter­gent composition. That is to say, in these ranges, for a given quantity of detergent composition, there is the most soil removal and least soil redeposition. Surprisingly, the addition of more water to the wash liquor, i.e., diluting the wash liquor, so as to exceed this upper limit, results in less soil removal from the textiles and more soil redeposition. Also, with this preferred limit, contact dyeing is minimized. Contact dyeing is the transfer of dye from the surface of one textile directly to that of another. These preferred ranges can also vary depending on the nature of the textiles, soil types, soil levels, detergent composition levels and detergent composition formulations.

THE WASH LIQUOR

The wash liquor contains from 40% to 99.9%, preferably from 85% to 99.5% and most preferably from 95% to 98.7% of water and from 1,000 ppm to 600,000 ppm, preferably from 5,000 ppm to 150,000 ppm and most preferably from 13,000 ppm to 50,000 ppm of a detergent composition. Wash liquor concentra­tions of detergent composition below 1,000 ppm result in substantially less soil removal from the textiles and above 600,000 ppm do not provide sufficient additional benefit to justify the addition of more detergent composition. However, in absolute terms, the wash liquor should contain from about five grams of detergent composition to 200 grams per kilogram of wash load. As utilized herein the wash load refers to the dry weight of the textiles, unless otherwise specified. Preferably, the absolute amount of detergent composition in the wash liquor is from 10 grams to 60 grams per kilogram of wash load. However, the most preferable detergent composition levels are heavily dependent on the detergent composition formulation. It should be noted that the wash liquor of the present invention is much more concentrated than the wash liquor utilized in the conventional automatic home-type top loader washing machines, although similar quantities of detergent composition are used.

The detergent composition can contain all of the standard ingredients of detergent compositions, i.e., detergent surfactants and detergency builders. Suitable ingredients include those set forth in U.S. Patents 3,936,537, Baskerville et al, February 3, 1976; 3,664,961, Norris, May 23, 1972; 3,919,678, Laughlin et al, December 30, 1975; 4,222,905, Cockrell, September 16, 1980; and 4,239,659, Murphy, December 16, 1980.

The wash liquor should preferably contain from 400 ppm to 150,000 ppm, more preferably from 1,500 ppm to 10,000 ppm of detergent surfactant and, in absolute terms, preferably from 1 gram to 45 grams per kilogram of wash load. The wash liquor should also contain preferably from 0 ppm to 100,000 ppm, more preferably from 1,000 ppm to 50,000 ppm of a detergency builder and, in absolute terms, preferably from 10 grams to 50 grams per kilogram of washload. It should be noted that another benefit of the concentrated laundering process is that, due to the small quantities of water utilized, water hardness control is not as critical as in a conventional wash process. Suitable detergent surfactants and detergency builders for use herein are disclosed in the U.S. patents cited immediately hereinbefore. The wash liquor can also contain inorganic salts other than detergency builders, enzymes and bleaches. The level of inorganic salts in the wash liquor is from 0 ppm to 150,000 ppm and preferably from 1,500 ppm to 50,000 ppm. The preferred enzymes for use herein are selected from proteases, amylases and mixtures thereof. The level of enzymes present in the wash liquor is from 0 ppm to 3,000 ppm, preferably from 0 ppm to 1,500 ppm. The level of proteases present in the wash liquor is from 0 Anson Units per liter (A.U./L/) to 1.0 A.U./L. and preferably from 0.03 A.U./L. to 0.7 A.U./L. The level of amylases present in the wash liquor is from 0 Amylase Units/liter of wash liquor to 26,000 Amylase Units/liter of wash liquor and preferably from 200 Amylase Units/liter of wash liquor to 13,000 Amylase Units/liter of wash liquor wherein Amylase Units are as defined in U.K. Patent 1,275,301 Desforges (Published May 24, 1972). Bleach levels in the wash liquor are from 0 ppm to 6,000 ppm and preferably from 500 ppm to 2,000 ppm. Also, bleach levels in the wash liquor are from 0 ppm to 2,000 ppm, preferably from 20 ppm to 1,000 ppm and most preferably from 50 ppm to 750 ppm of available chlorine when a chlorine bleach is utilized and from 0 ppm to 1,500 ppm, preferably from 50 ppm to 750 ppm and most preferably from 100 ppm to 500 ppm when an oxygen bleach is utilized.

Other parameters of the wash liquor are pH, viscosity, oil/water interfacial tension and particle size. The pH range for the wash liquor is from 5 to 12, preferably from 7 to 10.5 and most preferably from 9 to 10.5. It has been generally observed that superior cleaning can be achieved in the concentrated laundering process without the use of highly alkaline detergent compositions. The viscosity of the wash liquor can range preferably from about the viscosity of water to 250 centipoise and more preferably from the viscosity of water to 50 centipoise. Also, it is preferred that the oil/water interfacial tension is no greater than 10 dynes and more preferably no greater than 5 dynes and preferably that no solid ingredient is larger than 50 microns and more preferably no larger than 10 microns. Typically, the quantity of wash liquor utilized in the concentrated laundering process when utilized for home-type laundry loads will range from 1 liter to 20 liters and preferably from 2 liters to 5 liters.

The detergent compositions utilized in the concentrated laundering process can be in any form, such as granules, pastes, gels or liquids. However, based upon ease of preparation of the wash liquor, liquid detergent compositions and rapidly dissolving granular detergent compositions are desirable.

The conditions and detergent compositions for the present concentrated laundering process can be mild and safe for the most delicate fabrics cleaned by the least experienced consumer without unduly sacrificing cleaning.

WASH LIQUOR APPLICATION STEP

The wash liquor for the present process can be prepared by mixing the detergent composition and water. In the case of granular detergent compositions, the granules must be dissolved and/or dispersed before the resulting wash liquor can be applied to the textiles. In the illustrated apparatus such predissolu­tion and/or predispersion occurs by placing a predetermined quantity of granules in wash liquor reservoir 89 which is then filled from the water supply line 80 via control valve 82 and delivery line 96. If a highly concentrated liquid detergent com­position is used, then a flow-through mixing cell, e.g., a static mixer, can be used as an alternative to the wash liquor reservoir to mix the detergent composition and water. However, in ranges of the minimal quantity of water, an appropriate concentrated aqueous liquid detergent composition can be applied "as is" with­out further dilution.

The wash liquor is applied as an aqueous liquid directly onto the textiles. Preferably, the textiles are dry when the wash liquor is applied. It is also desirable that the application of the wash liquor, especially when there is no free wash liquor, is such that it is substantially completely and evenly distributed onto the textiles. That is to say, that if the wash liquor is not evenly distributed over substantially all of the textiles, then the untreated portions will not be cleaned as well and/or those por­tions of the textiles which are treated with more than their pro­portionate share of the wash liquor may appear as "clean" spots after the concentrated laundering process has been carried out. It should be noted that with the larger quantities of wash liquor within the invention it is easier to make such a distribution. This is especially true with quantities of wash liquor exceeding the absorption capacity of the textiles.

The foregoing detailed description of a preferred machine to accomplish such an application where there is no free wash liquor will be used in the following discussion.

In a domestic front loading automatic washing machine of the type described hereinbefore and illustrated in Figures 1-5, the wash liquor is pumped from either the wash liquor reservoir 89 or mixing cell (not shown) through a delivery line 95 which has a high pressure spray nozzle 100 attached at the end of it. The nozzle should be situated inside of the machine in such a position so as to optimize the even and complete application of the wash liquor onto the textiles. This can be accomplished by attaching the nozzle 100 in the tubular shaped extension 19 of the stationary drum 15, as generally shown in Figure 1. As an option, more than one nozzle can be used. Such multiple nozzles may be positioned so they will effectively increase the area of the drum that would be sprayed by the nozzles and, therefore, ensure a more complete application of the wash liquor onto the textiles. As an alternative to a nozzle, an atomizer (not shown) can be used. An atomizer is believed to be particularly desirable when minimal quantities of water are used because the wash liquor must be extremely finely divided to ensure uniform distribution. It should be noted that with quantities of wash liquor exceeding the absorption capacity of the textiles, but within the invention, less sophisticated means may be utilized to ensure good distribu­tion of the wash liquor onto the textiles.

As generally described in the foregoing apparatus descrip­tion, before the wash liquor is pumped through the delivery line 95 and out the nozzle 100, the movable drum 40 is preferably rotated. The purpose of the rotation is to clear the textiles from the center of the drum so that they are not blocking the field of spray of the nozzle 100, to distribute them substantially uniformly along the peripheral wall 40, and to expose as much of their surface area to the initial spray as is feasible. This is pre­ferably accomplished by initially driving movable drum 40 via concentrically mounted driven pulley 34 at a constant speed which is sufficient to force the textiles against the peripheral wall 41 of the movable drum 40 and thereafter driving movable drum 40 via eccentrically mounted driven pulley 28 at a reduced varying speed which allows the textiles to tumble continuously through the spray.

The pressure in the delivery line 95 should be high enough to produce a substantially flat fan-shaped spray of the wash liquor 230 through the nozzle 100, said spray preferably covering the entire depth of the movable drum 40, as generally shown in Figure 3.

This particularly preferred method of wash liquor application permits the textiles to be substantially completely and evenly con­tacted by the wash liquor. This permits the very effective detergent/soil interaction of the concentrated laundering process to occur. Additionally, such a method of wash liquor application is extremely efficient because when the quantity of wash liquor utilized does not exceed the absorption capacity of the textiles essentially all of the wash liquor is on the textiles.

A benefit of the concentrated laundering process is that effective cleaning results can be obtained over a wide range of wash liquor temperatures. The temperature of the wash liquor can range from 2°C to 90°C, preferably from 15°C to 70°C and most preferably from 25°C to 50°C. Surprisingly, the cleaning performance achieved at tem­peratures from 25°C to 50°C is as good as that achieved at temperatures above 50°C. Also, such low temperatures are especially safe for dyed and/or synthetic tex­tiles. Dye transfer is minimized at such temperature, especially when there is no free wash liquor. If it is desired to perform the wash liquor application step at temperatures above ambient temperature, either the wash liquor or the incoming water from supply line 80 can be heated before the wash liquor is applied to the textiles. However, it is preferred that the temperature of the textiles not exceed 70°C, as this may result in exces­sive wrinkling and shrinkage. Furthermore, temperature-­sensitive synthetic textiles should not be heated above their manufacturer-recommended washing temperatures.

APPLICATION OF ENERGY AFTER TEXTILES HAVE BEEN CONTACTED WITH WASH LIQUOR

In a preferred embodiment, energy can be applied to the textiles after they have been contacted by the wash liquor. It may be in the form of heat energy and/or mechanical energy, albeit they are not completely interchangeable, for a period ranging from 1 to 30 minutes, preferably from 5 to 15 minutes.

The application of heat energy permits the consumer to obtain excellent bleaching performance from bleaches such as sodium perborate, sodium percarbonate and hydrogen peroxide which are generally more effective at higher temperatures. This is not economical in a conventional home-type automatic wash process due to the cost of heating such large quantities of wash liquor. Further, since small quantities of water are used in the concentrated laundering process, conventional levels of bleach will have a higher effective concentration. This too contributes to the effective and/or efficient use of bleach in the concentrated laundering process.

In a preferred embodiment, heat energy is applied by recir­culating moist air which is heated via heating element 165 to raise the temperature of the textiles to 60°C, the temperature at which hydrogen peroxide based bleaches become particularly reactive. In addition to the closed loop moist air recirculation system disclosed in Figure 1, numerous other methods may be used for the application of heat energy. Nonlimiting examples are microwaves, steam and solar energy.

As an alternative to the application of heat energy to acti­vate the bleach, inorganic peroxide salt activators or low tem­perature active bleaches such as peroxyacids can be used. Such activated bleaches are effective below 50°C. Organic peroxide salt activators are well known in the art and are described extensively in the literature. For example, see U.S. Patents 4,248,928, Spadini et al, issued February 3, 1981, and 4,220,562, Spadini et al, issued September 12, 1980. Active bleaches such as organic peroxyacids and water soluble salts thereof are well known in the art. For a more detailed description of such bleaches see U.S. Patents 4,126,573, Johnston, issued November 21, 1978 and 4,100,095, Hutchins et al, issued June 11, 1978.

Other benefits of the application of heat energy are the assistance in the distribution of wash liquor onto the textiles and lipid/oily soil removal. If during the wash liquor application step the wash liquor was not substantially evenly and completely distributed onto the textiles, then the application of heat energy does provide some additional distribution. Also, experimental evidence indicates that heat energy does assist somewhat in the removal of lipid/oily soil. Some other potential benefits of the application of heat energy are the effective use of enzymes and the creation of desirable detergent surfactant phases. Different enzymes are most effective at different temperatures. Therefore, the textiles could be heated through certain temperature ranges to maximize enzyme effectiveness. However, as discussed herein­before, heat energy does not provide a major performance bene­fit, except as discussed hereinbefore with respect to bleaches, to the concentrated laundering process. It is preferred that heat energy be applied such that the temperature of the textiles is preferably from 15°C to 70°C and more preferably from 25°C to 50°C.

The application of mechanical energy provides numerous benefits. Mechanical energy helps to distribute the wash liquor so that it is more evenly and completely distributed onto the textiles. Thus, if during the wash liquor application step the wash liquor was not substantially evenly and completely distri­buted onto the textiles, then the input of mechanical energy will enhance such distribution. Mechanical energy also minimizes the period of time that the same textiles will remain in intimate con­tact with each other. Consequently, contact dyeing is minimized. Also, it is believed that mechanical energy contributes to improved cleaning efficacy. However, with quantities of wash liquor exceeding the absorption capacity of the textiles, only a limited amount of mechanical energy should be applied in order to prevent oversudsing. But, this is dependent on the concentra­tion and nature of the detergent composition in the wash liquor.

In the apparatus illustrated in Figures 1-5, mechanical energy can be applied by continuing rotation of the movable drum 40 at the last speed at which the wash liquor was applied. This creates a tumbling action by the textiles in movable drum 40 and results in the textiles being mechanically agitated.

THE RINSE

After the foregoing steps have been completed, the textiles are rinsed in a rinse liquor which preferably comprises clear water. Unlike a conventional automatic wash process wherein the goal of the rinse is to remove primarily the residual detergent composition, the goal of the present rinse is to remove the entire detergent composition and the soil. Thus, the present rinse step simultaneously performs the soil and detergent composition trans­port functions normally performed sequentially in conventional washing and conventional rinsing steps. Surprisingly, it has been observed that, during the rinse step, soil redeposition and dye transfer are minimal. Also, it has been observed that the rinse liquor contains stable emulsion particles whereas the rinse liquor in a conventional automatic wash process does not contain such emulsion particles.

In the preferred laundering apparatus illustrated in Figures 1-5, rinse liquor is introduced to the interior of movable drum 40 from water supply line 80 via control valve 83, delivery line 110 and applicator nozzle 120. Movable drum 40 is preferably rotated at varying speed via eccentrically mounted driven pulley 28 so that the textiles being rinsed are caused to tumble in a manner similar to the wash liquor application step. For more complete agitation of the articles being rinsed movable drum 40 may be stopped and its direction of rotation reversed several times throughout the rinse cycle. After the initial rinse has been completed, the rinse liquor is preferably removed from movable drum 40 by pumping it out via pump 140 without accelerating the rotation of the movable drum. This procedure can be repeated several times until the detergent composition and soil are removed. However, the textiles need not be spun out by high speed rotation of movable drum 40 between rinses. This mini­mizes the potential for wrinkling if the textiles are warm and also minimizes the potential for soil redeposition due to the rinse water being "filtered" through the textiles. If desired, adjuvants such as optical brighteners, fabric softeners and perfumes can be added to the rinse or applied, via the applicator nozzle 120, after the last rinse and distributed by tumbling. Bodying agents, such as starch, can also be added by spraying after the last rinse. Following the last rinse the textiles can be spun out by high speed rotation of movable drum 40.

An effective rinse can thus be accomplished with reduced water consumption and, there­fore, if heated water is used, reduced energy consumption. The amount of rinse liquor per kilogram of wash load is from 4 liters to 32 liters, preferably from 5 liters to 10 liters per rinse cycle. Rinse liquor levels below this amount would not produce enough free water on the surface of the tex­tiles to adequately suspend the soil and detergent composition. Generally more than one rinse cycle is necessary to remove all of the soil and detergent composition from the textiles. The use of such small quantities of rinse liquor permits the consumer to perform an entire laundering cycle with 25 liters or less of water per kilogram of wash load. The rinse liquor temperature is from 15°C to 55°C and preferably from 25°C to 45°C.

In a particularly preferred laundering process carried out in the apparatus of Figures 1-5, the complete rinse comprises two or three cycles which can be carried out in either cold or warm clear water. Each cycle can be from 1 to 10 minutes with each cycle not necessarily being the same length of time.

In a particularly preferred laundering process the weight of the dry wash load is determined by an auto­matic weight sensor (not shown) and the quantities of wash liquor, detergent composition, and rinse liquor are automatically regulated thereafter by control means known in the art and therefore not shown.

After the final rinsing step the laundered textiles can, if desired, be dried in the apparatus illustrated in Figures 1-5. This is done by positioning diverter valve 168 so that atmospheric air is drawn into connecting duct 171 by blower 160, heated by heating element 165, circulated through the tumbling textiles contained in the moving drum 40, withdrawn from drum 40 in a humid condition via connecting duct 167 and vented to atmosphere via connecting duct 170. Exercising this option enables the consumer to perform the entire laundering and drying process in a single apparatus and in continuous fashion.

The present concentrated laundering process can be employed to clean up even the dingiest of textiles and especially synthetic textiles in a number of laundering cycles. When an effective bleach is employed, the number of laundering cycles required for such purposes is reduced. This is believed to be due to the combination of excellent soil removal and substantial avoidance of excessive dye transfer and soil redeposition. Also, it has been observed that the present concentrated laundering process extends the useful "life" of textiles. This is believed to be due to the wash liquor lubricating the textile fibers.

The present invention contemplates a granular paste, gel or liquid detergent composition packaged in association with instructions for use in the concentrated laundering process. When such detergent composition is combined with water it pro­duces from just enough wash liquor to be substantially evenly and completely distributed onto a wash load of textiles to 5 kilo­grams of a wash liquor per kilogram of wash load of textiles, said wash liquor containing from 10 grams to 60 grams of the detergent composition per kilogram of wash load of textiles.

The process in which the compositions of this invention are used is primarily directed to house­hold laundry which consists of wash loads essentially made up of textiles, i.e., the process is a small batch process, that typically cleans less than 10 kilograms of soiled textiles which are a mixture of textile types and/or colors. While the concen­trated laundry process has been described in detail in conjunction with a preferred home laundering apparatus, it will be appre­ciated by those skilled in the art that the process can also be carried out on an industrial scale if provision is made for proper distribution of the wash liquor over the textiles and avoidance of appreciable amounts of free wash liquor in contact with the tex­tiles.

Various modifications can be made to the invention.

For example, the wash liquor can be applied to the textiles by a brush, rollers, a wash liquor permeable structure mounted on the inner surface of the movable drum to allow contact of the textiles with the wash liquor that passes through the permeable structure, a gravity feed system which allows the wash liquor to drop onto the moving textiles, or any other means which applies the required amount of wash liquor evenly and completely to the textiles; other detergent compositions can be substituted for the specific detergent com­positions described herein, etc.

Another aspect of this invention is that the concentrated laundering process permits the effective use of detergent composi­tions comprising bleaches and enzymes at levels in such detergent compositions that would provide essentially no benefit when such detergent compositions are utilized at normal usage levels in conventional automatic wash processes. "Normal usage levels in conventional automatic processes" are defined as the use of 146 grams of detergent composition in 20 liters of water at 75°C for Europe.

The bleaches that can be utilized in the detergent composi­tions are peroxygen bleaching compounds capable of yielding hydrogen peroxide in an aqueous solution. These compounds are well known in the art and include hydrogen peroxide and the alkali metal peroxides, organic peroxide bleaching compounds such as urea peroxide, and inorganic persalt bleaching compounds, such as the alkali metal perborates, percarbonates, perphos­phates, and the like. Mixtures of two or more such bleaching compounds can also be used, if desired. Preferred peroxygen bleaching compounds include sodium perborate, commercially available in the form of mono- and tetrahydrates, sodium carbon­ate peroxyhydrate, sodium pyrophosphate peroxyhydrate, urea peroxyhydrate, and sodium peroxide. The level of such bleaches in the detergent compositions is from 0.01% to 0.5% and preferably from 0.1% to 0.5% of available oxygen.

Other bleaches than can be utilized are activated bleaches such as peracids or peroxygen bleaching compounds capable of yielding hydrogen peroxide in an aqueous solution plus a bleach activator that can react to generate a peracid. Such peracids and bleach activators are well known in the art. For example, see U.S. Patents 4,126,573, Johnston (November 21, 1978) and 4,100,095, Hutchins et al (June 11, 1978) which deal with per­acids and U.S. Patents 4,248,928, Spadini et al (February 3, 1981) and 4,220,562, Spadini et al (September 12, 1980), which deal with bleach activators.

The preferred peracid is magnesium monoperoxy phthalate hexahydrate as disclosed in European Patent Application 0,027,693. The detergent compositions can contain from 0.03% to 0.3% and preferably from 0.1% to 0.25% of available oxygen that can potentially be generated by peracid.

As another alternative, the detergent compositions can contain a chlorine bleach. Chlorine bleaches are well known in the art. The preferred chlorine bleach is sodium dichlorocyanur­ate dihydrate. Other suitable chlorine bleaches are sodium and potassium dichlorocyanurates, dichlorocyanuric acid; 1,3-dichloro-­5,5-dimethyl hydantoin; N,Nʹ-dichlorobenzoylene urea; paratoluene sulfondichloroamide; trichloromelamine; N-chloroammeline; N-chlorosuccinimide; N,Nʹ-dichloroazodicarbonamide; N-chloro­acetyl urea; N,Nʹ-dichlorobiuret; chlorinated dicyandiamide; sodium hypochlorite; calcium hypochlorite; and lithium hypo­chlorite. The detergent compositions contain from 0.03% to 1.2% and preferably from 0.1% to 0.6% of avail­able chlorine.

The enzymes that can be utilized in the detergent composi­tions are protease, amylases and mixtures thereof. The level of proteases present in the detergent composition is from 0.01 Anson Units (A.U.) per 100 grams to 0.27 A.U. per 100 grams and preferably from 0.06 A.U. per 100 grams to 0.25 A.U. per 100 grams. The level of amylase present in the detergent composition is from 150 Amylase Units per 100 grams of detergent composition to 24,000 Amylase Units per 100 grams of detergent composition and preferably from 1200 Anylase Units per 100 grams of detergent composition to 6000 Amylase Units per 100 grams of detergent composition. Amylase Units are defined in U.K. Patent 1,275,301 Desforges (published May 24, 1972).

These ingredients are used at levels in a deter­gent composition that provide no consumer noticeable benefit when the detergent composition is used in conventional automatic home-­type washing machine processes at normal usage levels.

A "consumer noticeable benefit" is based upon a representa­tive number of consumers, the benefit being such that it can be recognized by a majority of the consumers at the 95% confidence level. More preferably these ingredients are used at less than 3/4 of the level at which a consumer benefit is seen, most pref­erably at less than 1/2 of said level.