WO2001006051A1 - System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning - Google Patents
System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning Download PDFInfo
- Publication number
- WO2001006051A1 WO2001006051A1 PCT/US2000/019206 US0019206W WO0106051A1 WO 2001006051 A1 WO2001006051 A1 WO 2001006051A1 US 0019206 W US0019206 W US 0019206W WO 0106051 A1 WO0106051 A1 WO 0106051A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- system recited
- solvent
- articles
- dry cleaning
- Prior art date
Links
Classifications
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/007—Dry cleaning methods
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F34/00—Details of control systems for washing machines, washer-dryers or laundry dryers
- D06F34/14—Arrangements for detecting or measuring specific parameters
- D06F34/22—Condition of the washing liquid, e.g. turbidity
- D06F34/24—Liquid temperature
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/08—Associated apparatus for handling and recovering the solvents
- D06F43/081—Reclaiming or recovering the solvent from a mixture of solvent and contaminants, e.g. by distilling
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/08—Associated apparatus for handling and recovering the solvents
- D06F43/081—Reclaiming or recovering the solvent from a mixture of solvent and contaminants, e.g. by distilling
- D06F43/083—Condensing arrangements
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/08—Associated apparatus for handling and recovering the solvents
- D06F43/081—Reclaiming or recovering the solvent from a mixture of solvent and contaminants, e.g. by distilling
- D06F43/085—Filtering arrangements; Filter cleaning; Filter-aid powder dispensers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B40/00—Technologies aiming at improving the efficiency of home appliances, e.g. induction cooking or efficient technologies for refrigerators, freezers or dish washers
Definitions
- VOC's volatile organic compounds
- the grease and fatty acids which build up in the solvent are removed by filtration and by distillation of the solvent.
- the dirty solvent is boiled and all vapors are condensed through a condensation coil back to a liquid.
- the remaining NVR (non volatile residue) is later removed and disposed of according to regulations.
- the liquid recovered is comprised of both solvent and water and the liquid is then passed through a separator in order to separate the two non-miscible liquids.
- the water may originate from the natural humidity of the ambient air exposed to the textiles prior to cleaning. Another source of moisture may be materials used during pre-spotting.
- the washer Before textiles are removed from the machine, the washer becomes a dryer. Hot air is blown through the compartment but, instead of being vented outside, the air stream goes through a condenser that condenses the vapors to liquid. The water must then be separated from the solvent and the solvent returned for reuse.
- the water will carry over into an associated storage tank and due to its density will settle on the bottom of the tank. If the level of water is sufficient it will be picked up by the pump system and may be pumped onto the articles being cleaned, which would result in damaging the articles.
- the hydrocarbon solvent is a feedstock for bacteria and may quickly contributed to the growth of bacteria.
- the silicone-based solvent is not a feedstock for bacteria but the interface level between the lighter density solvent and the more dense water causes an interface level between the water and solvent.
- the polar solvent soluble contaminants in this interface level may include fatty acids, food, perspiration, and general body odor. The extended settling can quickly result in the growth of bacteria and the end result of odor.
- organic solvents vary in their degree of hygroscopic.
- Organic solvents in general which are not water-soluble, have the ability to adsorb moisture from their environment; hence they are hygroscopic.
- the cyclic and linear silicone solvents In the case of the cyclic and linear silicone solvents, they exhibit the property of adsorbing water (their saturation points are around 200 parts per million). The rate at which they adsorb water is increased when the solvents are heated in the presence of moisture.
- any remaining solvent in the garments is removed through a tumbling and heating process. The heat causes the solvent and any moisture to evaporate.
- the solvent/moisture combination is transported to a cooling coil condenser at which point the resulting liquid solvent/moisture combination may be of a milky white appearance which is known as a colloidal emulsion or lyophobic colloid.
- van der Waals forces Any two molecules attract each other and the force between them, in general terms, is called van der Waals forces. They arise from electrostatic forces between various charges in these two molecules (i.e., the constituent electrons and nuclear charges).
- the process of stripping water from hygroscopic solvents can be greatly affected by the chemical nature and design of the micro-cellular stripping filter.
- the process of stripping water from hygroscopic solvents can be greatly affected by the chemical nature and design of the micro-cellular porous structure. This is true because as the water/solvent liquid mixture is forced through the tiny orifices of the porous structure, the forces which cause the water molecules to adhere to the solvent molecules are reduced, thereby allowing the molecules to separate.
- Urea- formaldehyde foam with a cell structure under 10 microns is the preferred material for construction of the porous structure.
- the solvent and the water are immediately separated in part due to the difference in their densities and also due to the reduction of the adso ⁇ tion forces (i.e., van der Waals forces).
- Other factors that also play part in the separation include capillarity, surface tensions, and even the difference of attractive forces between water molecules and foam molecules verses silicone molecules and foam molecules. These factors along with flow rate determine the rate of separation.
- porous structure will have differing degrees of hydrophilicity (ability to attract water). If the micro-cellular structure has a
- the hydrated silicone solvent, or colloids, also classified as lyophilic colloid are produced when immiscible liquids are cooled together during the condensation of vapors both during drying and during the distillation process.
- the proper separation of water from solvent is influenced by the proper selection of and implementation of a coalescing or stripping medium.
- the medium selected acts primarily as a coalesce of tiny water droplets. Coalescence is an indication of destabilization of the colloidal emulsion.
- the "porus structure” media can also be causing soalescence by removing ions from a double layer and/or removing a solvated film.
- Various extended-surface media (as identified later, but not limited to) have a significant valence or other attractive forces left over at their extreme surfaces that can attract other materials, a phenomenon which is called adso ⁇ tion.
- the adso ⁇ tion of ions and surfactants by the "porus structure” media are reasonable methods by which the media can function and thereby bring about coalescence.
- the selection of the "porous structure" to be used as the coalesces or stripping medium is based upon its ability to in the end separate the siloxane solvent from the water.
- the present invention includes a system and method for separating water from a silicone-based solvent in a dry cleaning application.
- an inlet is capable of receiving a mixture of silicone-based dry cleaning fluid and water from a condenser of a dry cleaning apparatus.
- a chamber is coupled to the inlet for receiving the mixture from the inlet.
- a porous structure is positioned in the chamber for separating the dry cleaning fluid and the water. The dry cleaning fluid passes through pores in the porous structure.
- An outlet is coupled to the chamber to remove the dry cleaning fluid from the chamber in the substantial absence of the water.
- the cell size of the porous structure is under 10 microns.
- the porous structure can be constructed of urea- formaldehyde foam.
- the cell size of the urea-formaldehyde foam is under 5 microns.
- the porous structure can be constructed of a polyurethane foam, ideally with a cell size of under 5 microns but may exceed 10 microns.
- the porous structure is hydrophilic.
- the porous structure can be constructed of a phenyl formaldehyde polymer foam, ideally with a sell size of under 10 microns.
- fractional distillation may allow for the illumination of water from solvent based on density and re-circulation.
- Low-end boilers such as water can be distilled prior to the distillation of silicone solvent.
- the ideal distillation of silicone solvent is by producing temperatures of between 235 F and 250 F with a vacuum of from 27 inches to 29 inches. By producing temperatures above the boiling point of water 212 F and creating a slight vacuum ⁇ 20 inches the process is able to vapor off the low-end boilers and urge the condensed vapors to a separate vessel. Some azetrophic will occur and thus a water sensor on this vessel will cause the free water present to leave the system. The remaining hydrated solvent will return to the still for re-distillation.
- the full vacuum (27 to 29 inches) is established with the full temperature (235 F to 250 F) also established resulting in distillation of dehydrated silicone solvent.
- the condensed vapors are urged to a separate vessel that may have a water sensor, for safety, allowing the water if present to leave the system.
- the solvent is returned to the tanks on the dry cleaning machine for reuse.
- the second source of hydrated solvent is from the drying recovery head, this solvent is normally very hydrated and is collected in a separate vessel that may contain a water sensor so as to eliminate free water.
- the most prevalent solvent used as previously stated is PERC whose temperature is ideally maintained at a range of 78 to 82 degrees Fahrenheit. This is also a common range for all other solvents currently being used in the field of dry cleaning. If the temperature should increase, the result is a much more aggressive solvent resulting in damage to textiles being processed. The increase in the KB (kari butyl) value most often results in causing dyes to be solubilize from articles being cleaned, resulting in the transfer of these dyes to other articles being cleaned.
- the concern for controlling temperature has caused manufactures of dry cleaning machines to install water cooling coils placed in the base tanks, and in-line water cooling jackets on the plumbing lines for heat transfer.
- an aggressiveness in cleaning is afforded, without the result of pulling or stripping dyes.
- This may be best accomplished by circulating water in a closed loop fashion between a hot water tank and through a circulating pump and through the coils (previously used for cooling) and back to the hot water tank.
- the circulating pump is controlled by a temperature probe that can be placed in the solvent. The result is precisely controlled solvent temperature which influences the aggressiveness of the solvent without causing damage to the articles being cleaned. This is optional and is not necessary to achieve good cleaning.
- Figure 1 is a schematic that represents a dry cleaning machine that is used with solvent that has a boiling point that if distilled requires vacuum distillation;
- Figure 2 is a flow diagram indicating the flow of liquid in a dry cleaning apparatus as described in Figure 1 ;
- Figure 3 is a flow diagram indicating the flow of vapor in a dry cleaning apparatus as described in Figure 1 ;
- Figure 4 is a flow diagram indicating the functional steps of the method of separating water from the solvent using a separate apparatus.
- Figure 5 is a flow diagram indicating the functional steps of separating water from solvent using an apparatus as a part (OEM) of the dry cleaning machine;
- Figure 6 is a flow diagram and schematic of a separator with functional steps of the separation of water from solvent.
- Figure 7 is a flow diagram indicating the functional steps of condensing liquid in a transfer drier and moving the liquid to a separator.
- Figure 8 is a schematic that represents a transfer drier that is used with solvent that has a boiling point that requires vacuum distillation.
- the present invention includes an apparatus and method used in conjunction for the dry cleaning of fabrics, textiles, leathers and the like.
- a dry cleaning apparatus is shown schematically in Figure 1, although it is recognized that alternative cleaning configurations can be used. It should be noted that the cleaning configuration of Figure 1 may be used for processing with a Class 3-A (solvent having a flash point between 140 F and 200 F) type solvent.
- Class 3-A solvent having a flash point between 140 F and 200 F
- the dry cleaning of articles or other items begins by placing them in a horizontal rotating cleaning basket 10.
- the wash cycle is initiated with a dry cleaning fluid including an organo silicone-based siloxane solvent being pumped using a pump 12.
- the solvent is pumped from either a working tank 14, or a new solvent tank 16, and then to the cleaning basket 10 with the articles.
- the course of the pumped solvent can either be through a filter 18, or directly to the cleaning basket 10.
- the solvent is then circulated through the button trap 20 to the pump 12. After agitation for a predetermined amount of time, the solvent is drained and pumped to either of the three tanks 14, 16, and 22 shown in Figure 1. The cleaning basket 10 is then centrifuged in order to extract the remaining solvent to any of the tanks or to the still.
- the types of filtration systems compatible with the particular solvent of the present invention are: a spin disc of a 20 and 60 micron type and may use diatomaceous earth being capable of optional use with the larger micron spin disc type; a tubular filtration (flex, rigid, or bump) also being capable of optional use with diatomaceous earth; a cartridge (carbon core, all carbon of the standard size, jumbo or split size); and Kleen Rite cartridge system which may result in no need for a still. Filters may also be used with a dimension between 10 to 100 microns to filter condensed vapors prior to separation.
- the solvent may be filtered so as to eliminate the particulate soil that is released from the articles
- the solvent being used for cleaning may be distilled at a rate of 10 to 20 gallons per hundred pounds cleaned, unless the aforementioned Kleen Rite cartridge system is being used.
- a still 24 may be used to receive solvent from the filter 18, or from the dirty tank 22, or the wheel 10.
- the solvent in the dirty tank 22 can be introduced to the still through suction since the still is under a vacuum that maybe controlled by a float ball valve (not shown).
- Any recovered or condensed vapors originating from the still may be condensed by water-cooled coils of a still vapor condenser 26. Thereafter, gravity urges the condensed solvent into a primary separator 28 or holding vessel.
- the rate of flow depending on the still, may range between .75 and 2.50 GPM, and the separator is engineered accordingly.
- Vacuum may be created by a liquid-head pump 30 or an evacuation process created by a venturi.
- the articles are tumbled in 10 with air being forced by a fan 32 over heating coils 34, which results in the incoming air flow to be between 120 and 180 degrees Fahrenheit.
- the airflow exits the cleaning basket 10 and passes over cooling coils of a drying vapor condenser 36 where the vapors condense back to a liquid. Gravity urges such liquid to the primary separator 28 or holding vessel via a conduit 37.
- the vapor laden air that leaves the cleaning basket 10 ranges in temperature between 120 and 160 degrees Fahrenheit. This temperature is important in that it can also be an advantage to regulate the temperature at or below 140 degrees such that the temperature is 30 degrees
- the rate of flow of the condensed liquid may be limited to 0.75 GPM, and the separator may thus be engineered for the combined flow rate of condensed liquid from the still and drying vapor condensers 26 and 36.
- Figure 2, 3 & 4 illustrates an order in which the various components of the present invention may be employed for clarification pu ⁇ oses. Having followed the foregoing process of dry cleaning, there are no less than one but as many as two or more sources of solvent to the
- a method of water and solvent separation is provided, as shown in Figure 4, 5, & 6.
- a mixture of the silicone-based dry cleaning fluid and any water from the articles is received from one or both sources of condensed solvent being; drying and or distillation of the dry cleaning process.
- the mixture may either enter a holding vessel or be urged directly through a porous structure that separates the dry cleaning fluid and the water.
- the dry cleaning fluid is removed in the substantial absence of water and is recycled into the dry cleaning system.
- Figure 6 is a schematic of the separators of one embodiment of the present invention, which is capable of performing the method of Figure 4 & 5.
- the mixture may be filtered 54 to prevent lint and particulate soil from entering the separator Figure 6 which may in turn restrict a coalescent filter that is downstream.
- coalescent media 54 may be draped at the initial termination of an inlet tube 52.
- the various media of the present invention may include nylon or any other coalescing media.
- the plumbing connection from the vapor condensers 26 and 36 of the dry cleaning of Figure 1 & 8 may be plumbed to terminate at inlet 52
- the hydrated solvent enters the separator Figure 4, 5 & 6 where gravity feeds it down the inlet tube 52, which terminates several inches above an interface level between the water and the dry cleaning fluid.
- the silicone-based solvent is insoluble in water, yet water, in small cellular size does suspends itself in the hydrated solvent until they form globules. Due to the combined weight, the globules settle to the bottom of the main chamber 48.
- a float level switch 58 is tripped which in turn activates a pump 60.
- the liquid is then pumped by the pump 60 through either 1 or 2 filters 62 that are rated as high as 20 to 50 microns and as low as 5 microns for filtering Figure 4, 5 &
- the hydrated solvent is then forced or pulled through a porous structure 64 which may be positioned within the filter housing 62 or placed in-line post filter 62 and which acts as a "coalescening medium".
- this structure is between 1/2 and 15 inches in length with a cross-section between 1/4 and 4 inches and has a cell size of under 20 microns.
- the pump 60 may be electrical or pneumatic in form.
- the use of any flow method such as the pump 60 or, in the alternative, a vacuum results in sufficient separation.
- the flow methodology chosen should affect a flow of 0.5 to 3.5 GPM. If the inflow of hydrated solvent is greater than the porous structure 64 will allow, the re-positioning of the float level switch 58, which activates the flow controller, can be lowered to allow for a larger buffer for the hydrated solvent.
- the flow rate can be modified by raising or lowering the air pressure or using a throttling valve.
- the hydrated solvent is moved from the primary vessel 48 through the suction line 59, through the filter or filters 62.
- the hydrated solvent is exposed to the striping media 64 and then out into the final vessel 68 having passed through a diffuser 65 and into the dry cleaning machines clear tank 16, Figure 1.
- a safety overflow 70 which carries the solvent back to the primary vessel 48.
- the middle height line 66 carries the solvent to the clear tank 16 and the lower line 67 carries the possibly hydrated solvent to the primary vessel 48 and creates a closed-loop process to protect the clear tank 16 from hydrated solvent.
- the principals are the same but the vessels may change.
- the source of the condensed liquid 26 and 36 are the same with the hydrated solvent routed to the first vessel 48 which if equipped with a water sensor 71 will actuate a valve so as to drain the water off and close again once the water has been removed.
- the hydrated solvent will be circulated either by an add on pump 60 or using an exiting dousing pump 60 that will circulate the hydrated solvent from the vessel 48 through a filter (less than 10 micron) 62 and then through the stripping medium 64 which will cause the water molecules to form globular size water structures which
- the water that is collected at the bottom of the main chamber 48 & 68 is evacuated manually or by a water float switch (not shown) which mechanically opens a hinged valve
- a water float switch (not shown) which mechanically opens a hinged valve
- two conductivity points, or probes (not shown), that make contact as the water rises in order to complete a circuit to signal either a pneumatic or electric valve which may discharge the water that is in the main chamber 48 & 68.
- the composition of the main chamber 48 & 68 can be stainless steel, or polyethylene. Constructing with the use of carbon steel is discouraged since oxidation and rusting can quickly occur.
Abstract
Description
Claims
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
MXPA02000359A MXPA02000359A (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning. |
EP00947357A EP1194628A1 (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning |
BR0012416-8A BR0012416A (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods for improving the cleaning process |
JP2001511254A JP2004512854A (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process that includes a silicone-based solvent, and a method for enhancing the cleaning process |
KR1020027000354A KR20020031386A (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning |
CA002378940A CA2378940A1 (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning |
IL14753800A IL147538A0 (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning |
AU60984/00A AU6098400A (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning |
NO20020196A NO20020196L (en) | 1999-07-14 | 2002-01-14 | System and Method for Extracting Water in a Purification Process Including a Silicone-Based Solvent and Methods for Increasing the Purification Process |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/354,387 US6059845A (en) | 1997-08-22 | 1999-07-14 | Dry cleaning apparatus and method capable of utilizing a siloxane composition as a solvent |
US09/353,212 | 1999-07-14 | ||
US09/354,387 | 1999-07-14 | ||
US09/353,212 US6086635A (en) | 1997-08-22 | 1999-07-14 | System and method for extracting water in a dry cleaning process involving a siloxane solvent |
US61660400A | 2000-07-13 | 2000-07-13 | |
US09/616,604 | 2000-07-13 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2001006051A1 true WO2001006051A1 (en) | 2001-01-25 |
WO2001006051A8 WO2001006051A8 (en) | 2002-06-20 |
Family
ID=27408101
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2000/019206 WO2001006051A1 (en) | 1999-07-14 | 2000-07-14 | System and method for extracting water in a dry cleaning process involving a silicone-based solvent and methods enhancing the process of cleaning |
Country Status (13)
Country | Link |
---|---|
EP (1) | EP1194628A1 (en) |
JP (1) | JP2004512854A (en) |
KR (1) | KR20020031386A (en) |
AU (1) | AU6098400A (en) |
BR (1) | BR0012416A (en) |
CA (1) | CA2378940A1 (en) |
HU (1) | HUP0202336A2 (en) |
IL (1) | IL147538A0 (en) |
MX (1) | MXPA02000359A (en) |
NO (1) | NO20020196L (en) |
PL (1) | PL353585A1 (en) |
RU (1) | RU2002103601A (en) |
WO (1) | WO2001006051A1 (en) |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6564591B2 (en) | 2000-07-21 | 2003-05-20 | Procter & Gamble Company | Methods and apparatus for particulate removal from fabrics |
WO2003089709A2 (en) * | 2002-04-22 | 2003-10-30 | General Electric Company | Apparatus and method for article cleaning |
US6706677B2 (en) | 2000-06-05 | 2004-03-16 | Procter & Gamble Company | Bleaching in conjunction with a lipophilic fluid cleaning regimen |
US6706076B2 (en) | 2000-06-05 | 2004-03-16 | Procter & Gamble Company | Process for separating lipophilic fluid containing emulsions with electric coalescence |
US6818021B2 (en) | 2000-06-05 | 2004-11-16 | Procter & Gamble Company | Domestic fabric article refreshment in integrated cleaning and treatment processes |
US6914040B2 (en) | 2001-05-04 | 2005-07-05 | Procter & Gamble Company | Process for treating a lipophilic fluid in the form of a siloxane emulsion |
US6955761B2 (en) | 2001-09-10 | 2005-10-18 | Procter & Gamble Company | Multifunctional filter |
US7084099B2 (en) | 2001-09-10 | 2006-08-01 | Procter & Gamble Company | Method for processing a contaminant-containing lipophilic fluid |
US7258797B2 (en) | 2001-09-10 | 2007-08-21 | The Procter & Gamble Company | Filter for removing water and/or surfactants from a lipophilic fluid |
US7276162B2 (en) | 2001-09-10 | 2007-10-02 | The Procter & Gamble Co. | Removal of contaminants from a lipophilic fluid |
US7297277B2 (en) | 2003-06-27 | 2007-11-20 | The Procter & Gamble Company | Method for purifying a dry cleaning solvent |
US7300593B2 (en) | 2003-06-27 | 2007-11-27 | The Procter & Gamble Company | Process for purifying a lipophilic fluid |
US7300594B2 (en) | 2003-06-27 | 2007-11-27 | The Procter & Gamble Company | Process for purifying a lipophilic fluid by modifying the contaminants |
US7704937B2 (en) | 2000-06-05 | 2010-04-27 | The Procter & Gamble Company | Composition comprising an organosilicone/diol lipophilic fluid for treating or cleaning fabrics |
CN102230488A (en) * | 2011-05-06 | 2011-11-02 | 三一重工股份有限公司 | Sewage discharge device for hydraulic system |
US9771497B2 (en) | 2011-09-19 | 2017-09-26 | Baker Hughes, A Ge Company, Llc | Methods of forming earth-boring tools |
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WO2000004221A1 (en) * | 1998-07-14 | 2000-01-27 | Greenearth Cleaning, Llc | Dry cleaning method and solvent |
US6086635A (en) * | 1997-08-22 | 2000-07-11 | Greenearth Cleaning, Llc | System and method for extracting water in a dry cleaning process involving a siloxane solvent |
-
2000
- 2000-07-14 HU HU0202336A patent/HUP0202336A2/en unknown
- 2000-07-14 JP JP2001511254A patent/JP2004512854A/en active Pending
- 2000-07-14 KR KR1020027000354A patent/KR20020031386A/en not_active Application Discontinuation
- 2000-07-14 BR BR0012416-8A patent/BR0012416A/en active Pending
- 2000-07-14 CA CA002378940A patent/CA2378940A1/en not_active Abandoned
- 2000-07-14 WO PCT/US2000/019206 patent/WO2001006051A1/en active Search and Examination
- 2000-07-14 IL IL14753800A patent/IL147538A0/en unknown
- 2000-07-14 RU RU2002103601/12A patent/RU2002103601A/en not_active Application Discontinuation
- 2000-07-14 PL PL00353585A patent/PL353585A1/en unknown
- 2000-07-14 MX MXPA02000359A patent/MXPA02000359A/en not_active Application Discontinuation
- 2000-07-14 AU AU60984/00A patent/AU6098400A/en not_active Abandoned
- 2000-07-14 EP EP00947357A patent/EP1194628A1/en not_active Withdrawn
-
2002
- 2002-01-14 NO NO20020196A patent/NO20020196L/en not_active Application Discontinuation
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US7258797B2 (en) | 2001-09-10 | 2007-08-21 | The Procter & Gamble Company | Filter for removing water and/or surfactants from a lipophilic fluid |
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US7297277B2 (en) | 2003-06-27 | 2007-11-20 | The Procter & Gamble Company | Method for purifying a dry cleaning solvent |
US7300593B2 (en) | 2003-06-27 | 2007-11-27 | The Procter & Gamble Company | Process for purifying a lipophilic fluid |
US7300594B2 (en) | 2003-06-27 | 2007-11-27 | The Procter & Gamble Company | Process for purifying a lipophilic fluid by modifying the contaminants |
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Also Published As
Publication number | Publication date |
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WO2001006051A8 (en) | 2002-06-20 |
KR20020031386A (en) | 2002-05-01 |
AU6098400A (en) | 2001-02-05 |
PL353585A1 (en) | 2003-12-01 |
JP2004512854A (en) | 2004-04-30 |
NO20020196D0 (en) | 2002-01-14 |
NO20020196L (en) | 2002-03-14 |
IL147538A0 (en) | 2002-08-14 |
BR0012416A (en) | 2002-06-04 |
RU2002103601A (en) | 2003-08-20 |
CA2378940A1 (en) | 2001-01-25 |
EP1194628A1 (en) | 2002-04-10 |
HUP0202336A2 (en) | 2002-11-28 |
MXPA02000359A (en) | 2002-07-02 |
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