US1759155A - Cleaning fluid and method of producing the same - Google Patents
Cleaning fluid and method of producing the same Download PDFInfo
- Publication number
- US1759155A US1759155A US34227A US3422725A US1759155A US 1759155 A US1759155 A US 1759155A US 34227 A US34227 A US 34227A US 3422725 A US3422725 A US 3422725A US 1759155 A US1759155 A US 1759155A
- Authority
- US
- United States
- Prior art keywords
- cleaning fluid
- distillate
- carbon tetrachloride
- same
- producing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06L—DRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
- D06L1/00—Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods
- D06L1/02—Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods using organic solvents
Definitions
- This invention relates to a cleaning fluid.
- cleaning fluids have een produced through admixing with petroleum distillates a certain percentage of carbon tetrachloride, the carbon tetrachloride being added to form a cleanin fluid which will not take fire or explode.
- T e percentage of carbon tetrachloride required to render the admixture fireproof depends upon the boiling points and flash of the distillate employed.
- the lighter boiling point distillates which are desirable to employ in cleaning fluids have generally such low flash points that they require the addition of an excessive amount of carbon tetrachloride to render them non-explosive or fire roof at the temperatures at which these flui s are on dinarily employed.
- the preferred cleaning fluid and method of manufacturing the same comprises the 1 employment or fractionation of a light petroleum distillate'until a product is obtained having a boiling point range between 220 to 375 F., preferably the fractionation being continued until the boiling point range is from 260 to 360 F.
- Such prepared petroleum distillate is then admixed with carbon tetrachloride sufficient to raise the flash point of a distillate to above 110 F. producing the desired cleaning fluid.
- carbon tetrachloride sufficient to raise the flash point of a distillate to above 110 F. producing the desired cleaning fluid.
- the ordinary petroleum distillate havingra boiling point range of from 100 to 400 tetrachloride is required to roduce a clean-' ing fluid of the desired flas point whereas by the employment of the fractionated disof carbon;
- the special distillate is preferably treated with acid and washed to form a purified, water-white, sweet smelling product, as is customary in the manufacture of such cleaning fluids.
- a cleaning fluid of the class described capable of evaporatingwith suificient readicleaned therewith
- E cleaning fluid of the class described consisting of a petroleum distillate with a boiling point range of between 220 and 375 F. admixed with suflicient carbon tetrachloride to raise the flash point to above F.
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Detergent Compositions (AREA)
Description
lf'atented May 20, 1930 UNITED STATES PATENT OFFICE I BRUCE B. FABRINGTON, OF BERKELEY, CALIFORNIA, ASSIGNOR, BY MLESNE ASSIGN- MENTS, TO STANDARD OIL COMPANY OF CALHORNIA, OF SAN FRANCISCO, CALI- PORN IA, A CORPORATION OF DELAWARE CLEANING FLUID AND METHOD OF PRODUCING THE SAME I70 Drawing.
This invention relates to a cleaning fluid.
and the method of producing or manufacturin the same. Hitherto, cleaning fluids have een produced through admixing with petroleum distillates a certain percentage of carbon tetrachloride, the carbon tetrachloride being added to form a cleanin fluid which will not take fire or explode. T e percentage of carbon tetrachloride required to render the admixture fireproof depends upon the boiling points and flash of the distillate employed. The lighter boiling point distillates which are desirable to employ in cleaning fluids have generally such low flash points that they require the addition of an excessive amount of carbon tetrachloride to render them non-explosive or fire roof at the temperatures at which these flui s are on dinarily employed. It is necessary for the production of a satisfactory cleaning fluid that the petroleum distillate employed should have a relatively low mean boiling point in order that the cleaning fluid will have a quick dryin time. Thus, for instance, mixtures of carbon tetrachloride and petroleum which have heretofore been employed as cleaning fluids, have been made from petroleum dis tillates with a boiling point range of from 100 to 400 F. or thereabouts.
It is an object of the present invention to provide a cleaning fluid comprising an ad mixture of carbon tetrachloride anda petroleum distillate in which the percentage of the carbon tetrachloride em' loyed is materially reduced while still providing a relatively low boilin point cleaning fluid which is nonexplosive at ordinary temperatures or the temperatures at which a cleaning fluid'is generally employed.
To raise the flash point of a petroleum distillate sufiicient to render the same non-explosive, or to.above say 110 F., there is required 60% of carbon tetrachloride when a distillate with a boiling point range of. 100 to 400 F. or thereabouts is em loyed. If the desired flash point is obtained by employing a higher boiling point distillate, the drying time will be too long and there will be a lasting odor on the fabric cleaned by the fluid.-
This invention comprehends that theflash Application flled June 1, 1925. Serial No. 34,227.
point can be raised and the drying time thus kept the same if a distillate is employed-for the admixture, which distillate has been fractionated to narrow down the boiling point range of the distillate.
Thus the preferred cleaning fluid and method of manufacturing the same comprises the 1 employment or fractionation of a light petroleum distillate'until a product is obtained having a boiling point range between 220 to 375 F., preferably the fractionation being continued until the boiling point range is from 260 to 360 F. Such prepared petroleum distillate is then admixed with carbon tetrachloride sufficient to raise the flash point of a distillate to above 110 F. producing the desired cleaning fluid. With the ordinary petroleum distillate havingra boiling point range of from 100 to 400 tetrachloride is required to roduce a clean-' ing fluid of the desired flas point whereas by the employment of the fractionated disof carbon;
tillate there is required only 30% of the carbon tetrachloride to obtain the same flash point; Thus a cleaning fluid is provided of equal properties to those now in use at a reduced cost.
It is understood that before adding the carbon tetrachloride the special distillate is preferably treated with acid and washed to form a purified, water-white, sweet smelling product, as is customary in the manufacture of such cleaning fluids.
It is to be understood that this invention is not limited to the specific method-of manufacture described to illustrate the invention,
but includes all such modifications as come within the scope of the appended claims.
I claim s v 1. A cleaning fluid capable of evaporating with suflicient readiness so as not to leave a ring in material cleaned therewith, and consisting of a petroleum distillate having a boiling point range between 220 degrees F: and 400 degrees F., admixed with suflicient car-v bon tetrachloride to raise the flash point above 100 degrees F., but containin less than fifty per cent carbon tetrachlori e.
2. A cleaning fluid of the class described capable of evaporatingwith suificient readicleaned therewith,
leave a ring in material and having a flash oint above degrees F., comprising a petro eum distillate having a boiling point range of between 220 degrees F. and 400 degrees F., and having a flash point of over 10 degrees F., admixed with suflicient carbon tetrachloride to produce a mixture having a flash pointabove 100 degrees F., but containing less than fifty er cent carbon tetrachloride.
3. E cleaning fluid of the class described, consisting of a petroleum distillate with a boiling point range of between 220 and 375 F. admixed with suflicient carbon tetrachloride to raise the flash point to above F.
Signed at Richmond, Calif. this 15th day of May, 1925.
BRUCE B. FARRINGTON.
ness so as not to
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US34227A US1759155A (en) | 1925-06-01 | 1925-06-01 | Cleaning fluid and method of producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US34227A US1759155A (en) | 1925-06-01 | 1925-06-01 | Cleaning fluid and method of producing the same |
Publications (1)
Publication Number | Publication Date |
---|---|
US1759155A true US1759155A (en) | 1930-05-20 |
Family
ID=21875085
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US34227A Expired - Lifetime US1759155A (en) | 1925-06-01 | 1925-06-01 | Cleaning fluid and method of producing the same |
Country Status (1)
Country | Link |
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US (1) | US1759155A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2541703A (en) * | 1951-02-13 | Liquid composition | ||
US3080724A (en) * | 1958-09-19 | 1963-03-12 | Little Inc A | Reduction of explosion hazards in the separation of gaseous mixtures |
-
1925
- 1925-06-01 US US34227A patent/US1759155A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2541703A (en) * | 1951-02-13 | Liquid composition | ||
US3080724A (en) * | 1958-09-19 | 1963-03-12 | Little Inc A | Reduction of explosion hazards in the separation of gaseous mixtures |
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