|Publication number||US3619116 A|
|Publication date||Nov 9, 1971|
|Filing date||Apr 2, 1969|
|Priority date||Apr 2, 1969|
|Also published as||DE1931479A1|
|Publication number||US 3619116 A, US 3619116A, US-A-3619116, US3619116 A, US3619116A|
|Original Assignee||Thomas Burnley & Sons Ltd|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (5), Referenced by (19), Classifications (17)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent  Inventor Nell Seville Liversedge, England  Appl.No. 812,8!3  Filed Apr. 2,1969  Patented Nov. 9, 1971  Assignee Thomas Burnley & Sons Limited Cleckheaton, Yorkshire, England  METHOD FOR SCOURING WOOL 3 Claims, 5 Drawing Figs.
 US. Cl 8/l39.l, 8/139, 8/142 511 Int. Cl D0lc3/00  Field of Search 8/139, l39.l, 142
 References Cited UNITED STATES PATENTS 656,528 8/1900 Donard 8/139 l,947,522 2/l934 Fluss 8/1391 2,655,428 l0/l953 Lundgren et al... 8/139 2,7 l7,90l 9/1955 Norman 8/l39.l 2,925,639 2/1960 LaFleur 8/139 Primary Examiner-Mayer Weinblatt Atlorney-Holman & Stein PATENTEnunv 9 ml 3.6 1 9. l l 6 SHEET 1 OF 4 lcohol water to atmosphere METHOD son scoumnc WOOL This invention relates to a process of scouring raw wool, to plant for the performance of such process and a method based on the process for recovering the cleaning agent used in the scouring process and producing purified wool grease.
The invention thus consists in a process of scouring wool comprising treating wool with a dry cleaning agent, such as for instance trichloroethylene or perchlorethylene, separating the used cleaning agent from the wool and washing the cleaning agent with a mixture of water and alcohol, separating the cleaning agent, containing wool grease, from the water and alcohol, and recovering the cleaning agent in a solvent recovery low pressure and temperature distillation plant.
The invention further consists in wool scouring plant comprising at least one cleaning machine and means for passing and recycling a cleaning agent through the machine and is characterized by a solvent recovery low pressure and temperature distillation plant, which may operate in three stages and incorporate a thin film evaporator device. The use of such distillation plant materially avoids degradation of the wool grease.
During the phase separation dirt and water soluble impurities pass into the water/alcohol phase and the wool grease remains in the solvent phase.
The wool grease therefore passes into the still with the cleaning agent and is tapped off from the bottom of the still after distillation of the solvent.
The purified solvent is reused for scouring further batches of raw wool.
One particular and at present preferred form of plant, to be described only by way of nonlimitative example is diagrammatically illustrated in the accompanying drawings, in which FIG. 1 is a combined block and flow diagram illustrating the plant components and their interrelation in the operation of the process;
FIG. 2 illustrates the cooling water system;
FIG. 3 illustrates the hot water system;
FIGS. 4 and 5 are side elevation and plan views respectively of a convenient plant layout.
Referring now to these drawings, there is shown a battery of eight Permac Bt'iwe dry cleaning machines 1, each having an associated 500 gallon tank. These machines are coupled to an air cooling system including an activated carbon adsorber 3 connected to the atmosphere and an air cooler 4 connected to a water separator (not shown). The cleaning machines are also connected to a 3000 gallon buffer tank 5 for solvent/grease mixture and also to a 3,000 gallon buffer tank for spent solvent. The buffer tank 6 is in turn connected to a series of three decanters 7A, 7B, 7C each of 3,000 gallon capacity and including a mixing device. The decanters could be replaced by a centrifuge which would perform the same function. The outlets from these decanters are connected to a steam operated evaporator 8 for the recovery of alcohol/water mixture from the cleaning solvent. This evaporator may have a 450 sq.ft. exchange surface and include a stirrer. The evaporator 8 is connected to a double roller drier 9 for drying dirt and suint mixture and to a condenser and receiver 10 for condensing alcohol/water mixture.
FIGS. 4 and 5 show a solvent storage tank 11 of 3,000 gallon capacity, and there is also an alcohol storage tank not shown of 500 gallon capacity.
FIGS. 1, 4 and 5 also show a first stage evaporator 13 including a falling film evaporator. In FIG. 1 there is also shown a first stage steam ejector 14, a first stage condenser 15, a second stage evaporator 16 of the wiped thin film type, a second stage tubular condenser 17, a third stage wiped thin film evaporator 18 and a thermocompressor 19 including intermediate condenser 19 and steam ejector.
FIG. 2 shows a cooling system including two packaged water chillers 20 and a packaged cooling tower 21.
FIG. 3 shows a hot water system 22 to provide process water at 60f-65PC.
The mode of use of the plant as above described is as follows:
The scouring of the wool takes place in the dry cleaning machines 1; the cycle time for each load (208 pounds of dirty wool) is 20 minutes including loading, two washes, drying, cooling and unloading. It is found to be most economical to lose one gallon of solvent (e.g. perchlorethylene) per 600 lbs. of clean wool as the excessive steam consumption for further drying would counterbalance the additional gain in solvent. The loss of solvent carried along with the cooling air is however cut to a minimum by using the chilled water cooler and the activated carbon adsorption plant. The spent solvent from the first wash containing the suint, dirt and grease is pumped into the buffer tank 6, whereas the solvent from the second wash is pumped into the tanks 2 which are associated with the washing machines to be used for the first wash of the next load.
From the buffer tank 6 the spent solvent is continuously mixed with a water/isopropyl alcohol mixture which dissolves the suint and dirt, forming a suspension which is separated from the solvent/grease mixture in the decanters 7A, 7B, 7C.
The water/alcohol mixture containing suint and dirt is led to the evaporator 8 which recovers the alcohol and water by distillation. The bottom stream from the evaporator 8 is fed on to the double roller drier 9 which recovers the remainder of the alcohol and water and discharges the suint and dirt as a dry powder. This dry powder may be usefully employed in agriculature.
The solvent containing the grease is fed from the last decanter 7C into the other buffer tank 5 where it is mixed with grease-free solvent returning from the solvent recovery part of the plant. To minimize the size of the recovery section the concentration of grease in this tank should be kept as high as possible. A grease content of about 3 percent to about 7 percent and preferably of 5 percent by weight has been found acceptable to the scouring process.
The bufier tank 5 is bled continuously to the solvent recovery section which is in three stages. In the first stage the bulk of the solvent is recovered in the tubular evaporator 13 under a pressure of about 25 mm. Hg Abs. and the preconcentrated grease is led to the second stage which is the agitated thin film evaporator 16. Here the preconcentrated grease flows over a heated wall in a thin film which is being agitated by' a rotor under a pressure of about 12 mm. Hg Abs. Further concentration takes place, while the solvent is condensed and recovered in the tubular condenser 17. The third stage is similar to the second stage but operates at even lower pressure e.g. about 2 mm. Hg Abs. and includes steam stripping which ensures the removal of the last traces of solvent and some lower boiling impurities of the grease. Wool grease of high quality is discharged from the third stage ready to be packed and sold. In order to condense the solvent and the stripping steam from the third stage the thermocompressor 19 is used. The resulting solvent/ water mixture is consequently separated in a decanter before the solvent is passed back to the buffer tank 5. In order to avoid degradation of the wool grease during the solvent recovery stage hot water is used as the heating medium throughout the process.
Each cleaning machine has a button trap. and an optionally associated filter unit through which the cleaning solvent is pumped before it is returned to the wool in the drum of the machine. Each filter unit is of the diatomaceous earth type and filters down to 4 microns. It is essential periodically to clean the filter units and this is done by pumping clean grease laden solvent from the buffer tank 5 in reverse direction, thus causing dirt and filter powder to be washed away and carried to the buffer tank 6. No additives are normally required.
The drums of the cleaning machines are preferably lined with perforated fabric.
By use of the plant as specifically described, 5,000 pounds of dirty wool (e.g. 53 percent wool, 15 percent grease, 20 percent suint and dirt and 12 percent moisture) can be treated per hour with about 3,000 gallons of perchlorethylene to yield 750 pounds per hour of highly purified grease.
The invention is applicable to most chlorinated hydrocarben dry cleaning agents with or without addition of alcohols, e.g. 5 percent isobutyl alcohol or cyclohexane.
perchlorethylene under cooled conditions, separating the used cleaning agent from the wool and continuously washing it with a mixture of water and a lower alkyl monohydric alcohol, recovering the alcohol and water by distillation and recovering the cleaning agent by multistage low pressure and temperature distillation.
3. A process of scouring wool as set forth in claim 1 wherein the cleaning agent is recovered in three stages under progressively lower pressures, the second of said stages involving thin film evaporation and the third stage including steam stripping.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US656528 *||May 27, 1898||Aug 21, 1900||Eugene Donard||Process of removing solvent vapors from wool.|
|US1947522 *||Nov 30, 1932||Feb 20, 1934||Viktor Fluss||Process of removing fatty and pitchy matters from animal fibres and for making them more readily feltable|
|US2655428 *||Mar 27, 1950||Oct 13, 1953||Lundgren Harold P||Method of wool scouring with composition containing suint, alcohols, ketones, and inorganic electrolytes|
|US2717901 *||Jan 31, 1951||Sep 13, 1955||Pacific Mills||Process for degreasing wool and the recovery of wool grease|
|US2925639 *||Nov 30, 1953||Feb 23, 1960||Deering Milliken Res Corp||Method of fulling and scouring wool|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4207072 *||Feb 21, 1975||Jun 10, 1980||Bruckner Apparatebau Gmbh||Processes for removing impurities from textile materials|
|US4343619 *||Mar 24, 1981||Aug 10, 1982||Asahi-Dow Limited||Method of preparing a scoured animal hair material|
|US4558574 *||Jul 19, 1983||Dec 17, 1985||O.T.H. Beier & Company (Proprietary) Limited||Wool washing and recovery of wool wax and water therefrom|
|US5486211 *||Sep 26, 1994||Jan 23, 1996||Glidden, Sr.; John L.||Wool purification|
|US6537326 *||Sep 25, 1998||Mar 25, 2003||Wool Research Organisation Of New Zealand, Inc.||Method for significantly enhancing the quality of scoured wool and machinery for achieving those enhancements|
|US7316781||Jun 24, 2004||Jan 8, 2008||The Procter & Gamble Company||Pseudo-distillation method for purifying a dry cleaning solvent|
|US7465321||Aug 30, 2002||Dec 16, 2008||Keratec Limited||Production of biopolymer film, fibre, foam and adhesive materials from soluble S-sulfonated keratin derivatives|
|US7579317||Mar 8, 2006||Aug 25, 2009||Keratec, Ltd.||Nutraceutical composition comprising soluble keratin or derivative thereof|
|US7732574||Dec 16, 2004||Jun 8, 2010||Keraplast Technologies, Ltd.||Wound care products containing keratin|
|US7767756||Sep 13, 2004||Aug 3, 2010||Keraplast Technologies, Ltd.||Composite materials containing keratin|
|US7892572||Oct 9, 2007||Feb 22, 2011||Keraplast Technologies, Ltd.||Orthopaedic materials derived from keratin|
|US8124735||Dec 11, 2007||Feb 28, 2012||Keraplast Technologies, Ltd.||Porous keratin construct and method of making the same|
|US8138362||Feb 27, 2008||Mar 20, 2012||Centro Technologico Gaiker||Method for extracting internal lipids from wool using supercritical fluids|
|US8142807||Dec 6, 2007||Mar 27, 2012||Keraplast Technologies, Ltd.||Bone void fillers and methods of making the same|
|US20040262570 *||Jun 24, 2004||Dec 30, 2004||The Procter & Gamble Company||Pseudo-distillation method for purifying a dry cleaning solvent|
|WO1996010113A1 *||Sep 22, 1995||Apr 4, 1996||John L Glidden Sr||Wool purification|
|WO2001004244A1 *||Jun 27, 2000||Jan 18, 2001||Coderch Negra Ma Luisa||Compositions of internal lipid extract of wool and use thereof in the preparation of products for skin care and treatment|
|WO2005003443A1 *||Jun 6, 2004||Jan 13, 2005||Victor Manuel Arredondo||Pseudo-distillation method for purifying a dry cleaning solvent|
|WO2008104630A1||Feb 27, 2008||Sep 4, 2008||Alcega Jorge Alvarez||Method for extracting internal lipids from wool using supercritical fluids|
|U.S. Classification||8/139.1, 8/142, 8/139|
|International Classification||D01B3/04, D06L1/10, D01C3/00, D01B3/00, C11B11/00, D06L1/00|
|Cooperative Classification||D06L1/10, C11B11/005, D01B3/04, D01C3/00|
|European Classification||D01C3/00, C11B11/00B, D06L1/10, D01B3/04|