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Publication numberUS3003347 A
Publication typeGrant
Publication dateOct 10, 1961
Filing dateSep 13, 1957
Priority dateSep 13, 1957
Publication numberUS 3003347 A, US 3003347A, US-A-3003347, US3003347 A, US3003347A
InventorsMoore James W, Morris Harold H, Stone Samuel E
Original AssigneeWhirlpool Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Laundry machine with hydraulic separator
US 3003347 A
Abstract  available in
Previous page
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Claims  available in
Description  (OCR text may contain errors)

1961 H. H. MORRIS ETAL 3,003,


15o q I36 f I. \Q 134 4 NJ 52 152 1 I54 INVENTORS 154 HAROLD H. MORRIS JAMES W. MOORE BYSAMUEL E. STONE Oct. 10, 1961 H. H. MORRIS ETAL 3, 3,3

LAUNDRY MACHINE WITH HYDRAULIC SEPARATQR Filed Sept. 13, 1957 3 Sheets-Sheet 2 GOOD DUDE] Magma ATTORN EYS Oct. 10, 1961 Filed Sept. 13, 1957 H. HJMORRIS ETAL LAUNDRY MACHINE WITH HYDRAULIC SEPARATOR 5 Sheets-Sheet 3 INVENTORS HAROLD H. MORRIS JAMES w. MOORE BY SAMUEL E. STONE ATT RNEYS United States Patent 3,003,347 LAUNDRY MACHINE WITH HYDRAULIC SEPARATOR Harold H. Morris, St. Joseph, James W. Moore, Benton Harbor, and Samuel E. Stone, Berrien Springs, MiclL, assignors to Whirlpool Corporation, St. Joseph, Mich., a corporation of Delaware Filed Sept. 13, 1957, Ser. No. 683,882 5 Claims. (CI. 68-42) The present invention relates to improvements in laundering machines, and more particularly to a laundering apparatus and method employing a fluid system which clears the laundering fluid and removes foreign material of a wide range in size and density, thereby being capable of successfully separating lint, soils and other foreign materials from wash water used in home laundry machines.

In a laundry machine, such as the automatic home laundry type, effective laundering of the clothes is improved with the use of clean Water. Further, if the water can be cleared of foreign, material, soils and lint during washing, these will not remain in the clothing. Clearing the water is of importance in suds saving systems where the sudsy wash water is stored between successive washing operations and reused, thus saving fuel for heating the water and saving soap and detergent. A machine which can reuse the wash Water is of especial value in areas which sufier water shortages.

The use of ordinary filters and strainers have had limitations in the effectiveness of the cleaning ability to remove particles of'all sizes, capacity, and usually have required manual attention for cleaning.

Laundry liquid as referred to herein is either a washing solution or a rinsing solution, for example, water with a liquid miscible detergent or other soluble agent therein. Soiled laundry liquid is that which is contaminated with such liquid immiscible components as are desirably removed during the washing cycle. Such immiscible components may include heavy particles or objects which do not 'go into suspension and lighter particles which are admixed with the laundry liquid in a washing zone to form a suspension. The suspended immiscible components, in turn, may include lint particles and the like which have a low density and soil particles having a heavier density. In other words, the immiscible components are of two phases, a heavy density phase and a light density phase.

The present invention also contemplates providing an improved fluid flow system for a domestic type automatic laundry and an improved fluid purifying or clearing system, which in the preferred form util zes a separator means which whirls a stream of the fluid in the form of ayvortex.' Impurities and foreign materials of all densities and Weights are removed from the fluid system at various points of the vortex and clarified fluid is continuously returned back to the washing zone. The fluid clearing system of the present invention also automatically operates to deliver the impurities and other materials removed from the fluid to a drain and is especially well suited for operation in combination with an automatic home laundry machine continuously purifying the wash water. i

A feature of the invention is the provision of apparatus which will remove foreign materials which are lightweight and of a density less than water such as lint, threads and the like, which are found in wash water, either directing them to a drain or recirculating them through the fluid clearing system until a predetermined time in the cycle when they are discharged to drain.

A further feature of the invention is the provision of 'a fluid clearing system .for an automatic washing machine which will operate continuously during the operation of the washer and will automatically flush itself to discharge foreign materials to drain at a predetermined period in the cycle of operation.

An object of the present invention is to provide an improved fluid clearing system for an automatic home laundry machine or the like, which will separate impurities from the washing fluid in a continuous operation and is capable of removing impurities, soils and foreign materials of all sizes and of all densities.

Another object of the invention is to provide an improved apparatus and method for the separation of lightweight particles of a density less than water from a fluid such as wash water used in a laundry machine.

Another object of theinvention is to provide a completely automatic fluid clearing system for use in a home laundry machine which is capable of continuous operation without having need of any manual attention which will automatically completely flush and clean all elements of the clearing system, thereby obviating the need for manual cleaning.

Another object of the invention is to provide an improved clearing system using a hydraulic cyclone separation chamber of an improved design for separation of impurities from a fluid without the loss of a significant amount of fluid during separation operation.

A further object of the invention is to provide an improved separation system for removing particles from a fluid wherein certain particles are retained in the system during operation, but are flushed to a drain at a predetermined time in the complete operational cycle.

Another object of the invention is to provide a fluid separation apparatus for removing particles both of a density heavier than water and of a density lighter than water with an improved fluid flow control means for allowing the escape of a predetermined minimum amount of fluid during operation and for periodically dumping and flushing the separated particles to a drain.

Another object of the invention is to provide an improved fluid recirculation system for a home laundry machine wherein large heavy foreign objects are removed from the fluid during recirculation ahead of a separation unit which operates to separate other foreign particles of densities both heavier and lighter than water, and wherein the cleared water is delivered back to the laundry machine.

Other objects and advantages will become more apparent with the teaching of the principles of the present invention in connection with the disclosure of the preferred embodiments in the specification, claims and drawings, in which: 7

FIGURE 1 is a front elevational view shown partially in schematic form, of a laundry machine combined with a fluid clearing system in accordance with the principles of the present invention;

FIGURES 2a and 2b are detailed schematic showings of the fluid control valve illustrating the operation of the flush and dump valve;

FIGURE 3 is' a schematic showing of a portion of the fluid clearing system illustrating an alternative structure for removing the lightweight materials from the FIGURE 4 is a schematic showing of a portion of the fluid clearing system illustrating another form for removing the lightweight materials from the system; 7

FIGURE 5 is a vertical sectional view showing the details of the hydraulic separator;

FIGURE 6 is a plan view of a portion of the separator for removing the heavy phase particles from the fluid; and, t

FIGURE 7 is a sectional view taken along VII of FIGURE 5, and illustrating the separator from the Whilethe features of the invention are shown in the i preferred arrangement, it will be understood that eleintents of the invention may be utilized in other environrhents "taking advantage of their inherent features and functions; As illustrated in the drawings, withfreference jto FIGURE 1, the invention is shown embodied in an "automatic home laundry mechanism. The laundry machine employs a fluid recirculation arrangement wherein a'stream of laundry liquid is driven through a hydraulic circuit, and the soils, foreign particles, lint and the like are removed atone point in the circuit in order that clarified liquidmay be returned to a treatment or washing zone in which foreign particles washed out of clothes are admixed with the fluid at another point in the circuit. The laundry machineis shown as including a cabinet 10 which'houses the operating mechanism. It'will be understood that the fluid separation system is shown in enlarged form in order that the details may be better observed and described. However, in'normal size relationship, the fluid separating mechanism would be much smaller in proportion to the cabinet and other elements of; the laundry machine than shown in the drawings, and the separation system would be housed completely within the cabinet 'tomake an attractive appearing unit. Theover-all system includes the elements of a tub 1 2, which contains the laundering fluid, a recirculating conduit. means 14 which leads from the tub to withdraw fluid therefrom and returns it back to the tub, apump means 16in the recirculation conduit means, a trap 18 ahead of the pump, and a separation apparatus 20 for the heavy fihhseand light phase material suspended in the washing d.

' The tub 12 of the laundry machine contains a launderingfluid and may be provided with a basket 22 therein :which is supported for rotation about'a vertical axis. :rhe basket. may be of varying design, and is shown as perforated by openings 24 for the escape of fluid when the basket is spun at high speeds to centrifugally extract ,the fluid from clothes therein. However, other designs of laundering machine elements may be employed, and, for example, imperforate tapered baskets may be used.

The machine could also be of the horizontal drum type or could comprise a so-called combo or, combination washer dryer.

The basket contains laundering means for performing the washing operation, such as an agitator, and'the laundering means including the agitator, the basket drive, and the drive pump, are operated by power'means'such as -anelectric motor 24. The motor connects to a gear re- -'duction system (not shown) to drive a shaft 26 for operating the agitator and to drive the basket. The motor isshown connected to a pulley 28 over which passes a belt 30 that drives a pulley 32 connected to a drive shaft f the pump 16. The pump 16 may be continuously driven throughout the operation of the laundry machine 'solthatwhenever fluid is available in the tub 12, it will .be recirculated through the clearing system, thus clearing the rinse water as well as the wash Water.

' The cycle of operations of the laundry machine is controlled JiChIOllgh a pre-settable sequential control means suchas atime cycle device 34, which may be provided with the usual time1- motor and cam operated. time series of washing, rinsing and drying operations or cycles. The time elapsed and operational phase of the machine .may be indicated on a dial 36provided with a knob 38 'for manually setting the operation of the machine. The .timecycle control device 34, of course, startsthe machine stops it at the end of operations. In the present arrangement, the time cycle means is used to control a dumpingand flushing valve apparatus 40, which will .be

laterindetail. I r

switches to. sequentially operate the machine through a discharge through the fluid outlet.

The construction and operation of the fluid clearing apparatus may be best understood by following the flow of fluid through the conduit 14. In other words, a hydraulic circuit is provided through which a stream of laundry liquid is driven. At one point in the circuit, namely the washing zone foreign liquid immiscible components are admixed with the stream including settleable solids, and particles of varying density which form with the stream a suspension all of which is withdrawn from the tub 12 through an outlet conduit 42 connected to the tub 12 by a fitting 44. The outlet conduit 42 leadsinto the top of the trap 18 positioned directly beneath the tub 12 so that settleable solids which will not remain in suspension in the fluid, such as nails, hairpins, buttons, and the like, will settle or drop and deposit themselves in the bottom 46 of the trap 18. The trap has a removable base 48 for effecting periodic cleaning at infrequent intervals. 7

The fluid continues its flow in the recirculation conduit -means14 by leaving the trap 18 through the trap outlet conduit 50, which leads to a 'T-fitting 52 and up into. the pump 16 through a pump inlet line 54, The other branch ofthe T is connected to a conduit 56, which carries the light phase materials that have been separated in the cyclone chamber 58 wherein the stream of fluid is vortically whirled to form aliquid vortex.

The pump 16 is a positive displacement pump or-the like which forces or drives the fluid stream through the hydraulic circuit. The fluid leaves the pump 16 through the pump discharge line 60 flowing through the conduit 62 andenters the cyclone chamber 58 through the separator inlet 64. V

The separator 20 operates to remove both light phase and heavy phase materials and in its preferred form employsa conical chamber which is substantially conical in shape, and is provided at or near its widest part with a tangential inlet for the fluid to be supplied under pressure and to circulate therein with a vortical flow. As a result of the shape of the chamber and the tangential inlet, the liquid body in the cyclone chamber is compelled to rapidly rotate around the axis of the chamber. The chamber is providedwith a central aperture in its large end for discharging the liquid rotating therein while the separated materials gather at the apex of the chamber. 1

The rotational movement of the'fluid or suspension in the cyclone chamber consists of two generally concentrical vortices of the same rotation but of opposite axial directions with the outer one rotating toward the apex of the chamber, and the inner one rotating toward the large end. The major part of the liquid, that which is purified, rotates in the outer vortex to flow toward the axis of the chamber and passes into the innervortex and discharges through the outlet.

In this apparatus the denser andgreater particles in the suspension are thrown outwardly toward the circumference of the cyclone chamber when the fluid enters tangentially. The larger or heavier particles which have a density greater than the fluid and which are referred to as the heavy phase particles are thus thrown outwardly along with the liquid into the center of the rotating liquid body and move in an opposite axial direction for By selectively varying the size of the solids outlet at the apex of the cone variations in the character of the fluid and the waste particles to be removed can be accommodated.

As maybe viewed in the drawings of FIGURES, 5,

' 6 and 7, which show the details-of the separator unit 20, the cyclone: inlet 64 enters tangentially at the large end of the cyclonechamber 58. The hydraulic cyclone providing the interior comically shaped cyclone chamher 58 therein. The chamber 58 has a cap 68 bolted to the large upper end by studs 71 threaded into the flanged upper circular end 73 of the cyclone shell 66.

The fluid enters tangentially through the inlet 64 and whirls around within the cyclone chamber 58 in a circular outer vortex path, as indicated by the arrows 70. The centrifugal force carries the heavy phase particles against the wall of the shell 66 whereby they pass downwardly to the discharge opening 72. Simultaneously, a counterflowing vortex is formed moving upwardly within the cyclone chamber 58 and carrying at its center the light phase particles or those which have a density less than the fluid which is, in this case, wash water. These light phase particles will include heavier hollow particles, elongated thin particles, and particularly particles such as lint and the like which are removed from the clothes in the basket during washing. This lint is particularly objectionable in that it will cling to the clothes within the tub and it will be forced against the surface of the clothes during the spin-dry operation. It is, therefore, an important feature of the invention that the separating system is'capable of removing these particles of lint from the washing fluid and returning the lint-freei'cleared fluid back to the machine.

The lint-laden vortex will pass into the vortex-finder tube 74 which projects coaxially down into the center of the cyclone chamber. This fluid will continue to circulate carrying the very light lint materials to the very center of the vortex where they are picked up by a second coaxial vortex-finder tube 76, which is positioned Withdrawn into the first larger vortex-fiinder tube 74, for the express purpose of removing the light phase material. The inner smaller vortex-finder tube 76 leads out through the outlet conduit 78 which connects to the conduit 56 leading back to the pump, as may be viewed in FIGURE 1.

Thus, as in the form shown inFIGURE 1, the light phase materials are removed in the cyclone separator and returned back to the pump 16. As may be observed, the pump again will receive thematerials and return them back to the cyclone separator through the inlet 64. During the operation of the laundering machine and during the operation of the separator mechanism, the light phase materials will continue to be recirculated and reseparated. During some predetermined time in the operation, preferably at the end of the washing cycle, these materials will be flushed down to drain in a manner which will be later described. However, it is important that theselight materials will continue to be separated and this is'accomplished without the loss of any washing fluid.

As may be viewed in FIGURES 5 and 6, the cleared fluid continues to flow out around the inner vortex-finder tube 76, and flows out through the cleared fluid outlet 80. a The outlet is connected to an outlet conduit 82, which passes through the valve assembly 40 to a 'fluidreturn conduit 84, which leads back to the tub. The fluid return conduit 84 may lead to the side wall of the tub through a connection 86 or may be directed back into the top of the tub through-a connection 88. This form of connection is not critical, and the cleared fluid may be returned to the tub in any desirable manner.

- Referring to FIGURES 1 through 5, the heavy particles which flow downwardly through the cyclone discharge outlet 72. pass into a primary outlet chamber 90, as shown in FIGURES 5 and 6, the primary outlet chamber has an internally threaded boss 92 receiving the fitting 94 of the cyclone shell 66. The primary outlet chamber has a closure cap 96 which is threaded into the top and is provided with a gasket seal 98 for a fluid tight connection to close the'chamber 90. r r I a The heavy phase particles flow from the cyclone chamber 58 through the discharge outlet 72 and into the primary chamber 90. They then flow downwardly through the opening 100, which leads to the collection vessel 102. A chamber tube 104 projects downwardly into, the collection vessel and has a flared end 106 which functions to distribute fluid outwardly when the collection vessel 102 is flushed with a rapid passage of fluid through the opening 100.

In the larger collection vessel 102, the heavy part1- cles settle from the fluid and the controlled flow of fluid escapes through the riser tube 108, which connects to the fluid escape conduit 110. This conduit as may be viewed in FIGURE 1, also connects to the flushing and dumping valve 40.

The solid particles settle in the vase 112 of the collection vessel, which tapers downwardly and has an outlet opening connecting to a flushing conduit 114. This conduit is also connected to the flushing and dumping valve 40, shown schematically in FIGURE 5.

As discussed in connection with FIGURES 1 and 5, the light density materials, which are removed through the inner vortex-finder tube 76, are delivered through conduit 56 to the inlet of the pump 16 to be contlnually recirculated during operation. It will be understood that this recirculation could also be achieved by connecting the conduit 56 at the other locations ahead of the pump in order to form a flow loop which provides for continued recirculation of the light phase materials.

Instead of directing the light phase material, which leaves through the outlet 78 of the hydraulic cyclone separator in a flow loop, the light phase material may be directed to a collection chamber '116, which is shown in FIGURE 3. The collection chamber presents a form of settling container and an inlet tube 78a projects down into a base 118 of the collection chamber and is connected to the outlet 78. The fluid leaves the inlet tube 78a and passes up past the lower baflfle 120 over the upper surface of the lower baflle and out past the outer edge of an upper baflle 122. The upper and lower baffles 122 and 120 are conically shaped and project downwardly. The upper baifle 122 is suspended on the tube 78a and is of a diameter less than the inside of the collection chamber whereby it forms a flow gap 124 at its outer edge for the fluid to pass upwardly into the discharge line 82a. The lower baflie 120 is secured at its outer edge to the collection chamber and its inner edge is short of the central inlet tube 78a to form a flow passageway 126. A substantial portion of the fine material will settle at the base 118 and the cleared carrier liquid will flow through the discharge line 82a which is connected to the conduit 82, as shown in FIGURE 1, whereby the fluid is returned to thetub, Discharge line 82a could also be connected to the inlet 54 of the pump whereby the cleared fluid could be again recirculated through the cyclone chamber 58. A flow regulating valve 126 may be placed in the line 82a to limit the escape of canier fluid.

A solids outlet line from the base of the light phase collection chamber 116 may be connected to the flushing conduit 114 by line 114a.

A control valve '128 may be provided in this line for flushing the chamber 116 when valve 40 is periodically used to flush the system.

Another manner of getting rid of the light phase materials which are suspended in the fluid that leaves through the inner vortex tube 76 of the cyclone chamber 58, is to direct it to a drain. A number of connections may be adopted for this purpose such as connecting the outlet 78 to the controlled overflow line 110, FIG- DRE 1.

Another manner of directing the fluid to drain is shown in FIGURE 4. In this instance, the outlet 78 is connected to line 78b, which leads in through the top of the primary outlet chamber a, which corresponds to the primary outlet chamber 90 of FIGURE 1. Tube 78b extends down into the primary outlet chamber past the cyclone discharge outlet 72a. The fine material will thus pass downwardly into the collection vessel 102g and materials will settle therein with the fluid flowing through the controlled overflow riser 108a. V v

accordance with the present invention, the heavy phase and light phase materials are periodically dumped and the cyclone=chamber is periodically flushed. H Asniay be illustrated in connection with the constructional examples shown, the operation of the flushing and dumping valve 40 is illustrated in FIGURES 2a and 2 b.

w "The valve'40 has a body 130 with inlets 1-32, 134 and 136 and the outlets 138 and 140. Flow through thevalve is controlled 'by spool valve member 142 which slidably projects intothe valve body 130. The spool valve is controlled by asolenoid 144 which connects to the movable spool valve by alink 146. The solenoid'144 is energized through electrical leads 148, which are shown leadingto the time control mechanism 34. During normal operation, thevalve spool is 'in the position shown in FIGURE 2a; and duringthe flushing and dumping operation, the valve spool moves to the position of FIGURE 2b. V The valve spool 142 has a reduced portion or an annular groove 150 which permits the fluid to flow from the inlet 132 ,to the outlet 138. The inlet 132 is connected :to the clear fluid outlet'80 of the cyclone throughconduit 82. Outlet 138 is connected to the fluid return conduit '84 so that the cleared fluid'flow's back to the tub. 7 V

The valve spool also has a tapered end 152 which provides fora limited controlled flow between the valve inlet 134 and the valve drain outlet 140. The outlet dischargesto a drain 154. The inlet 134 receives fluid from 'the controlled overflow conduit 110 leading from the collection vessel 102. Thus, the valve plunger 142 inits normal-position permits the tapered face 152 to justclear inlet 134 and permits a controlled leakage of fluid from the. collection vessel. This is merely a suflicient flow to 'aid in carrying the heavy suspended materials through the cyclone passageway 72 and down intothe collection vessel for settling, but which is not sufliciently large to permit a substantial loss of washing fluid. Thus, heavy particles settle'at the base 112 'of the collection vessel.- A controlledescape of fluid'is permitted through the riser tube 108;'and? down through the controlled overflow conduit -110=and the fluid flows past the inclined face 152 of the end of the spool valve 142 and down to the drain 154. When the valve'spool 142 is moved to open position by-energization ofthe solenoid 144, as shownin FIG- URE 2b; a-rush of fluid is permitted through thefvalve toithe' drain 154 to dump the'separated foreign particles and-flush the; separation system. The valve spool 142 raises to a location where all of the inlets 132, 134, and 136=are connectedto the'drain outlet 140. The tapered end-1520f the valve blocks the fluid return conduit 133 back to the washer to prevent any of the flushing fluid from accidentally flowing back to the tub. V a In flushingiand dumping position 'of the valve spool .1'42,1the fluid from cyclone outlet conduit 82 is permitted to flow directly to drain 154. A free flow is also permitedzfrom thetcontrolled overflow conduit 110 leading items-the collection vessel.

The base of the collection vessel through the-flushingiconduit 114 is also opened to-flush the settled-sedimenu down to" the drain "154.- This inereasefiin flow through-the-large discharge opening 72at the base of cyclone chamber 58 greatlyincreases the flow through the base of -the-cyclone chamber and thereby enlarges the central vortex, within the chamber. The light phase materials which have been continually recirculating through tlre. cyclone light phase separation system, will in part,.be flushed out through the :heavyphase separation system. discharging throughrthe passageway 72 at the 2 base; v."Howev er, since much'of the fluid escapes through passageway 7 2, the circulation'tliroughj theflight' phase '8 fi d r lub 1 h y .wi l th n flont engh t e clear O t e on i 42 p s d wn h q h rain. The ea d. wihr u ig h cyclonecfhamber. will a s fl h h inn r Wa l h rthea h mbe ,i se1 ,;.thusremoving the settling which may have, accumulated there. The flared end 105 of the tube 104 in the collectionyessel will tend to discharge fluid against the walls. ofsthe collection vessel to flush itclean.

-. i u p n dfl shi g p a o eat d .byiopening the spool valve 40, can be done intermittentlyduring any cycle of operation andflis 'preferably performed at the end of the washing operation.- At time,. the,,lojss of washing water by .gflushing willinot matter substantially and a complete and thorough flushing ofgthe cleaning system is automatically accomplished without requiring manual attention. The flushing may be. done, however, without the loss of a large quantity of water. and .the remainderof the water may be directed to aisuds, saver system through a valving arrangement, notshown.

Although the operation of theoverallsystem will have become apparent from the description of the individual elements, the summary of operation may be helpful in understanding certain of the advantages of. theinvention.

' Washing fluid is contained in the tub 12 and during the washing operation is continually. recirculated. through a fluid recirculation means r14. Very heavy particlesv incapable of being suspended in the fluid are caughtin the trap 18 as the fluid leaves through the outlet conduit 42. The fluid cleared of these heavy particles passes safely through the positive displacement pump 16 andis delivered to the fluid inlet 64 of the cyclone chamber 58. Upon entering tangentially into the cyclonevchamber, the fluid flows downwardly in the vortex path and the heavy phase par ticles pass through the discharge passageway 72 into the primary outlet chamber 90., They then flow downwardly to the tube 104 into the collection vessel 102 wh're the particles settle at the base 112. 1

The fluid circulates in the cyclone chamber 58 and passes into thevortex-finder tube 74,- which coaxially projects' into"thechamber.v The light phase particles col- 7 lectin the coaxialsm'aller inner vortex finder tube 76 and endiof the cyclone will be slowed. The vortex in the cyclone wilh'enlzrrg'e and the particles will not coiicjen trate as closely at' the small light phase yortexdinder tube 76; andinstead pass-out through the large vortexflow back to the pump 16 in a flow loop and are continually recirculated during operation. Thecleared fluid flows through the outlet 80, the cleared fluid conduit 82, and through the valve through the fluid return conduit 84 backinto the tub a2. g V h t The system is automatically flushed, preferably at the end ofthe washingop'eration by raising'th spool valve 142by eh e rgizatio'n Oh the solenoid-144; opens the flushing conduit 144 to flush theheavy particles but-of the base Ofthfi collection vessel and permits ali increased new throiigh' the Controlled 'overflew 11 10 tofdrainl 'Ihe'incrased 'flow the cyclone chamber fiuslies'the side walls of the chamber and increases the size ofjtlie' inner vortex whefeby the light,l?hase particles 'will'flo'w through the clear'fluidjoii tle't' flo' andtlie clear fluid outletconduittlZ Also a portion of the light phase particles-will pass through the'dis'char'ge'passageway 7 2 anmuihs the light phase particles'will and be "dumped Y J M smeanarrate V d'the y t is e n afi rea sa' -an flier a ator; ms i winv aired. the w ihai 's iq d fl clean'ng' system 'fori 'i a we -teen er? man a: or the] like which meets the jobject-ives; and advantages h re ett g The se a appear n h me used t rd v r m ve p t s Q 'aW variation dnl i i o. obta er i e fu th r t i is accomplished without a significant loss of fluid and because-of the 'widevariationof foreign part'icles'fremoved and the insignificant loss of fluid, the system "is exeeeding'ly well ada'ptedto ass witha laundry machine for clearing laundry fluid. r V

Theme'ch fn'ism 's c'mp letely" automatic and can be dry machine'fwithout' aaeauen or used: in a home laun cleared during operation, it is well adapted to use in areas where water is at premium and the fluid can be used for succeeding washing operations without necessitating the provision of replacement washing water, thus efiecting a saving of water, and of fuel to heat replacement water and in soap or detergent required to provide additional suds.

We have, in the drawings and specification, presented a detailed disclosure of the preferred embodiments of our invention, but it is to be understood that we do not intend to limit the invention to the specific forms disclosed, but intend to cover all modifications, changes and alternative constructions and methods falling within the scope of the principles taught by our invention.

We claim as our invention:

1. A laundry machine comprising,

an automatic washer having presettable sequential control means for operating the machine through a cycle including a series of laundering periods, said machine comprising a tub adapted to receive laundry liquid therein,

washing means in said tub for admixing immiscible solids including fight phase particles and heavy phase particles washed from materials contained therein with the laundry liquid,

pumping means having an inlet connected with the tub for driving the laundry liquid and the admixed solids drawn from the tub in the form of a stream,

a separator for purifying the stream of laundry liquid during selected periods of the laundry machine cycle, p g,

a cyclone chamber in said separator,

having a tangential inlet orifice receiving the stream discharged by said pumping means and vertically whirling the stream to produce a fluid vertex in said cyclone chamber,

inner and outer concentrically disposed vortex finding tubes extending into said cyclone chamber at the large end of the fluid vortex and forming an annulus between said inner and outer tubes for receiving clarified eflluent, said inner finding tube receiving light phase particle-rich fluid for removal thereof from the separator, eflluent conduit means connected to said annulus and to said tub for returning the clarified eflluent to said tub,

means connected to said cyclone chamber at the small end of the fluid vortex having an outlet for receiving the heavy phase particles including a collection vessel communicating with said outlet to provide a quiescent pool in which the separated solids gravitationally settle, a drain conduit connected to the bottom of said collection vessel,

an overflow conduit arranged to receive overflow fluid 10 from near the top of the collection vessel, and a dumping and flushing valve having inlet portions connected to said drain conduit and said overflow conduit and having an outlet portion leading to drain, said dumping and flushing valve having a separate inlet and outlet portion in said efiluent conduit means, said dumping and flushing valve having actuator means including a valve spool regulated by said presettable sequential control means and having a first position wherein clarified efiluent is directed through said eflluent conduit means to said tub and a limited controlled flow of fluid from said overflow conduit is directed to said outlet portion, saidvalve having a second position wherein said drain conduit, said overflow conduit and said eflluent con duit means are communicated with said outlet portion, thereby to flush the separator, while blocking flow through the eflluent conduit means to said tub.

2. A laundry machine as defined in claim 1, and

a conduit connected to said inner finding tube and to said inlet of said pumping means, thereby to recirculate the light phase particle-rich fluid.

3. A laundry machine as defined in claim 1, and

a conduit connected to said inner finding tube,

a settling container connected to said conduit for separating out the light phase particles, and

means to direct particle free fluid from said settling container to said eflluent conduit means for return of the particle free fluid to the tub.

4. A laundry machine as defined in claim 1, and

a conduit connected to said inner finding tube and discharging into said collection vessel, whereupon said light phase particles will settle in said collection vessel.

5. A laundry machine as defined in claim 1,

said washing means in said tub comprising a perforated vertical axis basket to confine the materials being laundered and agitating means in said basket to mechanically flex the materials.

References Cited in the file of this patent UNITED STATES PATENTS 1,866,519 Rataiczah July 5, 1932 2,346,005 Bryson Apr. 4, 1944 2,724,503 Fontein Nov. 22, 1955 2,756,878 Herkenbofi July 31, 1956 2,823,534 Loehle Feb. 18, 1958

Patent Citations
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US1866519 *Jun 20, 1929Jul 5, 1932Rataiczak Thomas FWashing machine
US2346005 *Aug 15, 1940Apr 4, 1944Bryson Tandy AVortex separator
US2724503 *Dec 30, 1952Nov 22, 1955StamicarbonHydrocyclone apparatus
US2756878 *Jun 10, 1952Jul 31, 1956Erie Mining CoThree product wet cyclone
US2823534 *Oct 7, 1955Feb 18, 1958Gen ElectricClothes washing machine
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3134734 *Aug 26, 1960May 26, 1964Equipment Engineers IncSeparating apparatus
US3234995 *Mar 27, 1962Feb 15, 1966StamicarbonProcess for separating an amorphous polymer from a solution thereof
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U.S. Classification68/12.8, 137/546, 209/731, 8/158, 68/208, 55/459.1, 134/109, 68/18.00R, 8/159
International ClassificationD06F39/10, D06F39/00
Cooperative ClassificationD06F39/10
European ClassificationD06F39/10
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Oct 10, 2006ASAssignment
Effective date: 20060930