US2005150059A1PendingUtilityA1
Non-aqueous washing apparatus and method
Priority: Oct 31, 2003Filed: Dec 7, 2004Published: Jul 14, 2005
Est. expiryOct 31, 2023(expired)· nominal 20-yr term from priority
D06F 43/00D06F 43/007D06F 43/08D06F 43/085
49
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Claims
Abstract
The invention relates to a non-aqueous washing machine, methods of using the machine, methods of washing, and recycling.
Claims
exact text as granted — not AI-modified1 . A method of cleaning fabrics, including the steps of:
disposing a fabric load in a wash container; delivering a wash liquor to said wash chamber, said wash liquor comprising a substantially non-reactive, non-aqueous, non-oleophilic, apolar working fluid and at least one washing adjuvant; removing said wash liquor from said fabric load; delivering a liquid extraction solvent to said fabric load; removing said liquid extraction solvent from said fabric load; and recovering the liquid extraction solvent and working fluid for reuse.
2 . The method of claim 1 wherein the liquid extraction solvent has at least one of the following properties:
a KB Value less than 30, a solubility in water of less than 10%, or a flash point greater than 145 C.
3 . The method of claim 2 wherein the liquid extraction solvent is selected from the group consisting of: perfluorocarbons, hydrofluoroethers, fluorinated hydrocarbons, fluoroinerts and carbon dioxide.
4 . The method of claim 3 wherein the liquid extraction solvent is further selected from the group consisting of methoxynonafluorobutane, ethoxynonafluorobutane and mixtures thereof.
5 . The method of claim 1 wherein said non-reactive, non-aqueous, non-oleophilic, apolar working fluid under standard conditions is further characterized by:
a KB value less than 30; a surface tension less than approximately 35 dynes/cm 2 ; and a solubility in water of less than 10%.
6 . The method of claim 1 wherein the working fluid is selected from the group consisting of hydrofluoroethers, highly fluorinated hydrocarbons, volatile methyl siloxanes or mixtures thereof.
7 . The method of claim 6 wherein the working fluid is further selected from decamethylcyclopentasiloxane, dodecamethylpentasiloxane, decamethyltetrasiloxane, octylmethylcyclotetrasiloxane, hexamethyldisiloxane, octamethyltrisiloxane, tetradecamethylhexasiloxane, hexadecamethylheptasiloxane, methyltris(trimethylsiloxane) silane or mixtures thereof.
8 . The method of claim 1 wherein recovering the liquid extraction solvent and working fluid further comprises recovering the liquid extraction solvent before dissolved contaminants are removed from the working fluid.
9 . The method of claim 8 , wherein the liquid extraction solvent is subjected to a treatment selected from the group consisting of: gravity separation, filtration, centrifugation, fractional distillation, freeze distillation, temperature reduction, adsorption, absorption, inducing electrical fields, vaporization, pressure reduction or mixtures thereof.
10 . The method of claim 1 wherein the temperature of the working fluid never exceeds 30° F. below its flash point.
11 . The method of claim 8 wherein the working fluid is further recovered from a wash liquor by sequentially performing the following treatments: treating the wash liquor either with carbon dioxide under pressure, performing temperature reduction, contacting it with a flocculating agent, adjusting its pH or contacting it with an ion exchange resin; and treating the effluent from the above step by means of one of the following materials: a dissolver, an emulsifier, an adsorption agent, an absorption agent, a soap, a pH shifter, a flocculating agent, a filtration material, a cake/drying material agent, by gravimetric means, by vortex separation, by distillation, by freeze distillation; treating the effluent from the above step with one of the following a coalescence agent, an absorption agent, an adsorption agent, a pH adjustment agent, an ion exchange resin; and treating the effluent from the above step by means of one of the following carbon dioxide under pressure, a flocculating agent, a pH adjuster, performing temperature reduction, an adsorption agent, an absorption agent, an ion exchange resin.
12 . The method of claim 8 wherein the working fluid is further recovered from a wash liquor by sequentially performing the following treatments: treating the wash liquor either with carbon dioxide under pressure, performing temperature reduction, contacting it with a flocculating agent, adjusting its pH or contacting it with an ion exchange resin; treating the effluent from the above step with one of the following: a coalescence agent, an absorption agent, an adsorption agent, a pH adjustment agent, an ion exchange resin; then treating the effluent from the above step by means of one of the following materials: a dissolver, an emulsifier, an adsorption agent, an absorption agent, a soap, a pH shifter, a flocculating agent, a filtration material, a cake/drying material agent, by gravimetric means, by vortex separation, by distillation, by freeze distillation; and then treating the effluent by means of one of the following carbon dioxide under pressure, a flocculating agent, a pH adjuster, temperature reduction, an adsorption agent, an absorption agent, an ion exchange resin.
13 . The method of claim 1 wherein after recovering the liquid extraction solvent and working fluid, they are stored separately for reuse.
14 . The method of claim 8 wherein after recovering the liquid extraction solvent, the liquid extraction solvent contains less than 25% working fluid.
15 . The method of claim 1 wherein the liquid extraction solvent and wash liquor undergo a treatment step to reduce the amount of dissolved contaminants.
16 . The method of claim 15 wherein the treatment step is further characterized by a temperature reduction step.
17 . The method of claim 16 wherein the temperature reduction step reduces the temperature to the freezing point of at least one of the solvents in the mixture.
18 . The method of claim 16 wherein the treatment step is further characterized by passing the liquid extraction solvent and wash liquor through a filtration means.Join the waitlist — get patent alerts
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