US3505005A - Dry cleaning method - Google Patents

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US3505005A
US3505005A US431206A US3505005DA US3505005A US 3505005 A US3505005 A US 3505005A US 431206 A US431206 A US 431206A US 3505005D A US3505005D A US 3505005DA US 3505005 A US3505005 A US 3505005A
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solvent
dry cleaning
solvent system
polyvalent metal
metal ions
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Herman Spencer Gilbert
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Dow Chemical Co
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L1/00Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods
    • D06L1/02Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods using organic solvents
    • D06L1/10Regeneration of used chemical baths

Definitions

  • solvent system comprising essentially an organic dry cleaning solvent
  • chlorinated hydrocarbons such as perchloroethylene, trichloroethylene and the like, or volatile hydrocarbons such as benzene, naphtha and the like
  • solvent system is used herein to designate these comonly used solvents and formulated solvents.
  • the polyvalent metal ion content of the dry cleaning solvent system is reduced by contacting the solvent system with a material capable of tying up or precipitating polyvalent metal ions in a form suitable for removal from the solvent system by filtration.
  • a material capable of tying up or precipitating polyvalent metal ions in a form suitable for removal from the solvent system by filtration include cation exchange resins, which tie up polyvalent metal ions through ion exchange, and compounds or compositions which react with polyvalent metal ions to form precipitates in the solvent system.
  • the concentration of polyvalent metal ions in dry cleaning solvents may be quite low initially, there is a rapid build-up of these metal ions, together with other impurities, during repeated cleaning operations which remove these impurities from the fibrous materials cleaned.
  • the dry cleaning solvent is continually or periodically filtered in order to remove the various suspended or dispersed impurities, such as soil particles and the like, which accumulate in the solvent during cleaning operations.
  • the interfering polyvalent ions are not removed by this filtration.
  • the undesirable metal ions are established in a form removable by such a filtration step.
  • the desired removal of polyvalent metal ions, which have been precipitated from the solvent system is accomplished by separate filtration of the solvent system prior to re-use in further cleaning operations.
  • the contaminated dry cleaning solvet system is brought into intimate contact with a cation exchange resin to effect ion exchange removal of the polyvalent metal ions.
  • EXAMPLE 2 This experiment illustrates the correlation between reflectance loss and the presence of polyvalent metals in a dry cleaning solvent system used to clean swatches of material.
  • Solvent 1 is perchloroethylene
  • Solvent 2 is a chlorinated hydrocarbon dry cleaning solvent, containing a petroleum sulfonate base detergent, widely used in commercial, coin-operated, dry cleaning machines
  • Solvent 3 is a formulated perchloroethylene solvent containing a phosphate base detergent additive.
  • one procedure for reducing the polyvalent metal ion content of the solvent system involves contacting the solvent system with compounds or compositions which react with these metal ions to form precipitates which are removed from the solvent system as, for example, by filtration.
  • the compounds or compositions employed for this purpose are those which possess the property of forming chelates or complexes with polyvalent metal ions.
  • any of the wide variety of known polyvalent metal ion chelating compounds may be employed for this purpose, such as, for example, the tetrasodium salt of ethylenediaminetetraacetic acid, the pentasodium salt of diethylenetriamine pentaacetic acid, the trisodium salt of N-hydroxyethylenediaminetriacetic acid and the sodium salt of N,N-di(2-hydroxyethyl)glycine. Since these well known chelating agents are insoluble in the dry cleaning solvent system, except for very small amounts which would tend to dissolve in moisture present, it is necessary that only suflicient agitation or mixing of the insoluble compound and solvent system occur to bring the compound into reactive contact with the polyvalent metal ions present.
  • polymers of cyclic amides such as polyvinylpyrrolidone, polyvinylmorpholinone, oly-5- methyl-3-vinyl-2-oxazolidinone and mixtures thereof, are added to the solvent system, with agitation, to form polyvalent metal ion-polymer complexes which are insoluble in the solvent system and which form precipitates removable by filtration.
  • the solvent system may be agitated with a cation exchange resin, or passed through an ion exchange column of such a resin to reduce the polyvalent metal ion concentration by ion exchange.
  • EXAMPLE 3 In this experiment various compounds and compositions within the scope of the invention were employed as additives to a dirty, i.e. mature, solvent system. A quantity of 11.4 grams of the additive was added to a 12 liter sample of mature dry cleaning solvent system which had previously been used to dry clean clothing. In each case, a quantity of 21 grams of diatomaceous earth was also introduced to serve as a filter medium. After thorough mixing of the mature solvent system and additive, the mixture was filtered and the residue remaining from evaporation of a ml. portion of the filtrate was analyzed for metal content by emission spectroscopy. Table III, below, indicates the additive employed and the metal content analysis.
  • control sample run was identical to the test sample runs with the exception that no a Polymer of 5-methyl-3-vinyl-2 oxazolidinone.
  • b 50-50 mixture (by weight) of polyvinylpyrrolidone and polyvinylmorphollnone.
  • EXAMPLE 4 A 55 ml. quantity of a mature solvent obtained from a commercial dry cleaning establishment was agitated for 16 hours with 10 grams of a sulfonated styrene-divinylbenzene cation exchange resin (H+ form) sold under the trademark Dowex 50 resin (a product of The Dow Chemical Company, Midland, Mich.). The liquid phase was filtered oil and analyzed for metals by emission spectroscopy. Table IV, below, shows the percent of various metal ions removed by this treatment based on the amounts of metal ions originally present. Original metal ion content was determined by an analysis of a control sample before treatment with the ion exchange resin.
  • H+ form sulfonated styrene-divinylbenzene cation exchange resin
  • the improvement which comprises the step of reducing the polyvalent metal ion content of said solvent system prior to said re-use by contacting the solvent before reuse and filtering with either a sulfonated styrene divinyl benzene acid form cation exchange resin or an organic metal chelating agent in an amount from about 180 grams to about 0.95 gram per liter of solvent to remove at least a part of the dissolved metal ions from the solvent prior to reuse by exchange from solution with said cation exchange resin or the formation of a solid complex with said chelating agent.
  • the improvement which consists essentially of the step of reducing the polyvalent metal ion content of the solvent system by contacting the solvent before reuse as a cleaning agent with a cation exchange resin which is insoluble in said system, in an amount from about grams to about 0.95 gram per liter of solvent to remove at least some of the dissolved metal ions from the solvent, and returning the so treated solvent for reuse in said dry cleaning system, which cation exchange resin is a sulfonated styrene-divinyl benzene cation exchange resin hydrogen ion form.
  • the improvement of reducing the polyvalent metal ion content of the solvent system by treatment of said solvent system with an organic metal chelating agent to form a solid complex with said polyvalent metal ions and removing the so-formed solid complex from the solvent system and returning the so treated solvent for reuse in said dry cleaning system said chelating agents are employed in amounts of from about 180 grams to about 0.95 gram per liter of solvent and are selected from the group consisting of tetrasodium salt of ethylenediamine tetraacetic acid, trisodium salt of N-hydroxyethylenediaminetriacetic acid, sodium salt of N,N-di(2-hydroxyethyl)glycine, and the polyvinylpyrrolidone, polyvinylmorpholinone, poly- 5-methyl-3-vinyl-2-oxazolidinone, and mixtures of the polymers.

Description

United States Patent f 3,505,005 DRY CLEANING METHOD Herman Spencer Gilbert, Angleton, Tex., assignor to The Dow Chemical Company, Midland, Mich., a corporation of Delaware No Drawing. Filed Feb. 8, 1965, Ser. No. 431,206 Int. Cl. D061 1/04; Clld 7/50 US. Cl. 8-142 Claims ABSTRACT OF THE DISCLOSURE The present invention concerns the method of contacting a dry cleaning solvent formulation after use to the action of a cation exchange resin or a chelating agent to remove or chemically bind the metal ions in said solvent formulation in a form such that they are removed from the solvent formulation before the formulation is reused.
It has now been discovered that the presence of polyvalent metal cations in dry cleaning solvent systems is detrimental to the effectiveness and efficiency of dry cleaning operations. This surprising and unexpected discovery resulted from observations that the reflectance readings of cloth samples were influenced by the polyvalent metal ion content of the dry cleaning solvent system in which the samples had been cleaned.
In general dry cleaning practice a solvent system comprising essentially an organic dry cleaning solvent is employed, e.g. chlorinated hydrocarbons such as perchloroethylene, trichloroethylene and the like, or volatile hydrocarbons such as benzene, naphtha and the like, and is frequently formulated to contain detergents or soaps and other additives. The term solvent system is used herein to designate these comonly used solvents and formulated solvents.
In the present invention the polyvalent metal ion content of the dry cleaning solvent system is reduced by contacting the solvent system with a material capable of tying up or precipitating polyvalent metal ions in a form suitable for removal from the solvent system by filtration. Examples of materials found suitable for establishing the ions in a form for removal, as for example by filtration, include cation exchange resins, which tie up polyvalent metal ions through ion exchange, and compounds or compositions which react with polyvalent metal ions to form precipitates in the solvent system.
Although the concentration of polyvalent metal ions in dry cleaning solvents may be quite low initially, there is a rapid build-up of these metal ions, together with other impurities, during repeated cleaning operations which remove these impurities from the fibrous materials cleaned. In usual practice, the dry cleaning solvent is continually or periodically filtered in order to remove the various suspended or dispersed impurities, such as soil particles and the like, which accumulate in the solvent during cleaning operations. The interfering polyvalent ions are not removed by this filtration. However, in practice of the method of the present invention the undesirable metal ions are established in a form removable by such a filtration step. Similarly, the desired removal of polyvalent metal ions, which have been precipitated from the solvent system, is accomplished by separate filtration of the solvent system prior to re-use in further cleaning operations. In an alternative method of the present invention thecontaminated dry cleaning solvet system is brought into intimate contact with a cation exchange resin to effect ion exchange removal of the polyvalent metal ions.
"ice
The following examples illustrate the detrimental effect on the brightness of materials caused by deposition of polyvalent metal ions onto the material. The tendency of polyvalent metal ions to deposit on materials from title cojntacting dry cleaning solvent system is also demons rate EXAMPLE 1 After the discovery that polyvalent metal ions tend to be deposited from dry cleaning solvent systems onto materials cleaned therein and that such deposits adversely alfect the brightness of the cleaned materials, experiments were conducted to determine quantitative effects of this unexpected phenomenon. Investigation revealed that the polyvalent metal ion deposit is, in most nstances, especially marked where moisture is present in the material. Moisture, of course, is normally present in materials being cleaned and additional moisture is generally present in the formulated dry cleaning solvent initially introduced into the dry cleaning system.
A series of forty loads of clothes, averaging about elght pounds per load, were cleaned in a regular commercial dry cleaning machine employing a standard perchloroethylene dry cleaning solvent system used in the cleaning industry. A number of new, 4" by 11" swatches of cotton, wool, viscose taffeta and spun acetate materials were cleaned together with this series of 40 loads of clothes and the deposit of polyvalent metal ions thereon was determined by emission spectroscopy. A portion of each of the swatches was moistened with a few drops of deionized water prior to each cleaning cycle to demonstrate the effect of moisture, present in the material being cleaned, on the tendency of the metal ions to deposit on the cloth. The original metal content of these new swatches provides a standard for determination of the amounts of metal deposited during cleaning. The results are shown in Table I, below, where metal content is reported as parts per million (ppm), weight of cloth basis.
TABLE I Metal Content (p.p.m.)
Swatch and Description Ca Mg Fe Cu Ti Zn Pb Cd Cotton:
New 47 15 14 1 5 2O 10 23 27 25 35 10 65 30 24 Dry area 160 21 22 33 13 42 30 20 47 15 340 65 Spun acetate:
New 48 2 1 20 10 2 Wet area..- 150 34 2 1 20 10 16 Dry area 230 70 30 1 20 1O 10 The largest increase in metal content was at the wetdry interface and this area also showed the greatest loss of reflectance as compared with the new sample. This may possibly explain the difficulty encountered in removing the border line portion of water spots; a frequent problem in dry cleaning of materials. This high metal content at the wet-dry interface is believed due primarily to wet area deposition with subsequent capillary action (similar to paper partition chromatography) depositing a large portion of the wet area metal species in the ring forming the wet-dry interface.
EXAMPLE 2 This experiment illustrates the correlation between reflectance loss and the presence of polyvalent metals in a dry cleaning solvent system used to clean swatches of material.
A series of cloth swatches was agitated for extended time periods in quantities of three different commercially available dry cleaning solvent systems. In each case the reflectance readings of swatches agitated in samples of the new, uncontaminated dry cleaning solvent system were compared with reflectance readings of swatches agitated in portions of the same dry cleaning solvent system which had been saturated with Zn, Cu, Fe, and Mg ions. These saturated portions were prepared by extended stirring of water soluble salts of these metal species with the dry cleaning solvent employed. The reflectance readings, taken on a standard reflectometer, are tabulaed in Table II, below, as taken initiall and at the end of one, two and three days of agitation in the solvent. In the following table, Solvent 1 is perchloroethylene; Solvent 2 is a chlorinated hydrocarbon dry cleaning solvent, containing a petroleum sulfonate base detergent, widely used in commercial, coin-operated, dry cleaning machines; Solvent 3 is a formulated perchloroethylene solvent containing a phosphate base detergent additive.
TABLE II.REFLECTANCE READINGS 1 day 2 day 3 day Spun acetate swatches: 1
Solvent 1:
Metals absent 84. 5 84. 5 84. 5 Metals present 84. 82.5 81. Solvent 2:
Metals absent 84. 5 84. 0 84. 0 Metals present 83. 0 80. 5 78. 5 Solvent 3:
Metals absent- 83. 5 83. 0 83. 0 Metals present 82. 0 78. 5 78. 5 Worsted gabardine wool swatches: 2
Solvent 1:
Metals absent 73. 0 73. 0 73. 0 Metals present 70.0 68. 0 67. 5 Solvent 2:
Metals absent 73. 0 72. 5 73. 0 Metals present 71. 5 67. 5 65. 0 Solvent 3:
Metals absent 72. 5 72. 5 72. 5 Metals present 71. 0 69. 5 69. 5
1 Initial reflectance reading-85 units. 1 Initial reflectance reading-73.5.
As shown by the comparative reflectance readings in Table II, above, the presence of the polyvalent metal ions (which were the only contaminants present in the test samples of solvent) cause a significant loss of whiteness in the swatches.
As previously noted, one procedure for reducing the polyvalent metal ion content of the solvent system involves contacting the solvent system with compounds or compositions which react with these metal ions to form precipitates which are removed from the solvent system as, for example, by filtration. The compounds or compositions employed for this purpose are those which possess the property of forming chelates or complexes with polyvalent metal ions. Any of the wide variety of known polyvalent metal ion chelating compounds may be employed for this purpose, such as, for example, the tetrasodium salt of ethylenediaminetetraacetic acid, the pentasodium salt of diethylenetriamine pentaacetic acid, the trisodium salt of N-hydroxyethylenediaminetriacetic acid and the sodium salt of N,N-di(2-hydroxyethyl)glycine. Since these well known chelating agents are insoluble in the dry cleaning solvent system, except for very small amounts which would tend to dissolve in moisture present, it is necessary that only suflicient agitation or mixing of the insoluble compound and solvent system occur to bring the compound into reactive contact with the polyvalent metal ions present.
In another procedure, polymers of cyclic amides, such as polyvinylpyrrolidone, polyvinylmorpholinone, oly-5- methyl-3-vinyl-2-oxazolidinone and mixtures thereof, are added to the solvent system, with agitation, to form polyvalent metal ion-polymer complexes which are insoluble in the solvent system and which form precipitates removable by filtration.
In an alternative procedure the solvent system may be agitated with a cation exchange resin, or passed through an ion exchange column of such a resin to reduce the polyvalent metal ion concentration by ion exchange.
The following examples describe completely representative specific embodiments of procedures for accomplishing the method of the present invention, i.e. reducing polyvalent metal ion content in a dry cleaning solvent system. These examples, however, are not to be interpreted as limiting the invention other than as defined in the claims.
EXAMPLE 3 In this experiment various compounds and compositions within the scope of the invention were employed as additives to a dirty, i.e. mature, solvent system. A quantity of 11.4 grams of the additive was added to a 12 liter sample of mature dry cleaning solvent system which had previously been used to dry clean clothing. In each case, a quantity of 21 grams of diatomaceous earth was also introduced to serve as a filter medium. After thorough mixing of the mature solvent system and additive, the mixture was filtered and the residue remaining from evaporation of a ml. portion of the filtrate was analyzed for metal content by emission spectroscopy. Table III, below, indicates the additive employed and the metal content analysis. The control sample run was identical to the test sample runs with the exception that no a Polymer of 5-methyl-3-vinyl-2 oxazolidinone. b 50-50 mixture (by weight) of polyvinylpyrrolidone and polyvinylmorphollnone.
EXAMPLE 4 A 55 ml. quantity of a mature solvent obtained from a commercial dry cleaning establishment was agitated for 16 hours with 10 grams of a sulfonated styrene-divinylbenzene cation exchange resin (H+ form) sold under the trademark Dowex 50 resin (a product of The Dow Chemical Company, Midland, Mich.). The liquid phase was filtered oil and analyzed for metals by emission spectroscopy. Table IV, below, shows the percent of various metal ions removed by this treatment based on the amounts of metal ions originally present. Original metal ion content was determined by an analysis of a control sample before treatment with the ion exchange resin.
TABLE IV Percent removal of metal ions organic dry cleaning solvent system in which an organic dry cleaning solvent is contacted with said textile, removed from said textile and the solvent reused, the improvement which consists essentially of the step of reducing the polyvalent metal ion content of the solvent system by contacting the solvent before reuse as a cleaning agent with a sulfonated styrene-divinyl benzene acid form of a cation exchange resin which is insoluble in said system, said resin being employed in an amount from about 180 grams to about 0.95 gram per liter of solvent to remove at least some of the dissolved metal ions from the solvent, while in contact with said solvent, and returning the so treated solvent for reuse in said dry cleaning system.
2. In the method of cleaning fibrous materials in an organic dry cleaning solvent system in which an organic dry cleaning solvent is contacted with said textile, removed from said textile and the solvent reused, the improvement of reducing the polyvalent metal ion content of the solvent system by treatment of said solvent before reuse with an organic chelating agent to form an insoluble complex with said polyvalent metal ions dissolved in said solvent and removing by filtration the so-formed complex from the solvent system, said agent being employed in an amount from about 180 grams to about 0.95 gram per liter of solvent to remove at least a part of said dissolved metal ions, and returning the so treated solvent for reuse in said dry cleaning system.
3. In the method of dry cleaning fibrous materials in a dry cleaning solvent system which comprises the successive steps of introducing the fibrous material into the solvent system, circulating the solvent through the fibrous material and filtering the solvent for subsequent re-use in cleaning additional fibrous materials, the improvement which comprises the step of reducing the polyvalent metal ion content of said solvent system prior to said re-use by contacting the solvent before reuse and filtering with either a sulfonated styrene divinyl benzene acid form cation exchange resin or an organic metal chelating agent in an amount from about 180 grams to about 0.95 gram per liter of solvent to remove at least a part of the dissolved metal ions from the solvent prior to reuse by exchange from solution with said cation exchange resin or the formation of a solid complex with said chelating agent.
4. In the method of cleaning textile materials in an organic dry cleaning solvent system in which an organic dry cleaning solvent is contacted With said textile, removed from said textile and the solvent reused, the improvement which consists essentially of the step of reducing the polyvalent metal ion content of the solvent system by contacting the solvent before reuse as a cleaning agent with a cation exchange resin which is insoluble in said system, in an amount from about grams to about 0.95 gram per liter of solvent to remove at least some of the dissolved metal ions from the solvent, and returning the so treated solvent for reuse in said dry cleaning system, which cation exchange resin is a sulfonated styrene-divinyl benzene cation exchange resin hydrogen ion form.
5. In the method of cleaning fibrous materials in an organic dry cleaning solvent system in which an organic dry cleaning solvent is contacted with said textile, removed from said textile and the solvent reused, the improvement of reducing the polyvalent metal ion content of the solvent system by treatment of said solvent system with an organic metal chelating agent to form a solid complex with said polyvalent metal ions and removing the so-formed solid complex from the solvent system and returning the so treated solvent for reuse in said dry cleaning system, said chelating agents are employed in amounts of from about 180 grams to about 0.95 gram per liter of solvent and are selected from the group consisting of tetrasodium salt of ethylenediamine tetraacetic acid, trisodium salt of N-hydroxyethylenediaminetriacetic acid, sodium salt of N,N-di(2-hydroxyethyl)glycine, and the polyvinylpyrrolidone, polyvinylmorpholinone, poly- 5-methyl-3-vinyl-2-oxazolidinone, and mixtures of the polymers.
References Cited UNITED STATES PATENTS 3,057,676 10/1962 Wedell et al.
3,238,011 3/1966 Lawrence et al. 252153 3,173,862 3/1965 Clements et al 210-138 2,723,222 11/1955 Stark 252-89 2,874,124 2/1959 Vitalis 252-89 3,000,830 9/1961 Pong et al 252-89 3,317,424 5/ 1967 Schmidt 210 24 OTHER REFERENCES .RoseThe Condensed Chem. Dictionary (6) 1961, Reinhold Publ. 00., p. 1013.
LEON D. ROSDOL, Primary Examiner W. SCHULZ, Assistant Examiner US. Cl. X.R.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4098697A (en) * 1972-04-10 1978-07-04 Sobin Chlor-Alkali, Inc. Apparatus for removing mercury from waste water
EP0878454A1 (en) * 1997-05-15 1998-11-18 Elf Atochem S.A. Process for purifying quasi-anhydrous organic liquids
US6059857A (en) * 1996-08-14 2000-05-09 Bend Research, Inc. Ultrapurification of organic solvents

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2723222A (en) * 1954-12-06 1955-11-08 Phillips Petroleum Co Use of chelating agents to improve color and color stability of petroleum distillate
US2874124A (en) * 1955-06-10 1959-02-17 American Cyanamid Co Anti-soil redeposition agents
US3000830A (en) * 1952-12-05 1961-09-19 Fong Willie Use of polyvinylpyrrolidone as a soil-suspending agent
US3057676A (en) * 1957-04-27 1962-10-09 Bohme Fettchemie Gmbh Dry-cleaning composition and process
US3173862A (en) * 1960-12-14 1965-03-16 Celanese Corp Process for treating liquids
US3238011A (en) * 1960-11-29 1966-03-01 Du Pont Drycleaning process and compositions
US3317424A (en) * 1963-03-01 1967-05-02 Nalco Chemical Co Demineralization of polar liquids, especially water

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3000830A (en) * 1952-12-05 1961-09-19 Fong Willie Use of polyvinylpyrrolidone as a soil-suspending agent
US2723222A (en) * 1954-12-06 1955-11-08 Phillips Petroleum Co Use of chelating agents to improve color and color stability of petroleum distillate
US2874124A (en) * 1955-06-10 1959-02-17 American Cyanamid Co Anti-soil redeposition agents
US3057676A (en) * 1957-04-27 1962-10-09 Bohme Fettchemie Gmbh Dry-cleaning composition and process
US3238011A (en) * 1960-11-29 1966-03-01 Du Pont Drycleaning process and compositions
US3173862A (en) * 1960-12-14 1965-03-16 Celanese Corp Process for treating liquids
US3317424A (en) * 1963-03-01 1967-05-02 Nalco Chemical Co Demineralization of polar liquids, especially water

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4098697A (en) * 1972-04-10 1978-07-04 Sobin Chlor-Alkali, Inc. Apparatus for removing mercury from waste water
US6059857A (en) * 1996-08-14 2000-05-09 Bend Research, Inc. Ultrapurification of organic solvents
EP0878454A1 (en) * 1997-05-15 1998-11-18 Elf Atochem S.A. Process for purifying quasi-anhydrous organic liquids
FR2763330A1 (en) * 1997-05-15 1998-11-20 Atochem Elf Sa PROCESS FOR THE PURIFICATION OF QUASI ANHYDROUS ORGANIC LIQUIDS
US6123850A (en) * 1997-05-15 2000-09-26 Elf Atochem Process for the purification of virtually anhydrous organic liquids

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