US1484167A - Cleaning solvent - Google Patents
Cleaning solvent Download PDFInfo
- Publication number
- US1484167A US1484167A US530453A US53045322A US1484167A US 1484167 A US1484167 A US 1484167A US 530453 A US530453 A US 530453A US 53045322 A US53045322 A US 53045322A US 1484167 A US1484167 A US 1484167A
- Authority
- US
- United States
- Prior art keywords
- gasoline
- carbon
- centrifugal
- cleaning
- solvents
- 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
Links
- 239000002904 solvent Substances 0.000 title description 12
- 238000004140 cleaning Methods 0.000 title description 8
- 239000003502 gasoline Substances 0.000 description 27
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 26
- 229910052799 carbon Inorganic materials 0.000 description 14
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 10
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 5
- 229960003563 calcium carbonate Drugs 0.000 description 5
- 229910000019 calcium carbonate Inorganic materials 0.000 description 5
- 235000010216 calcium carbonate Nutrition 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 239000000084 colloidal system Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000000344 soap Substances 0.000 description 2
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical group ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011280 coal tar Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000005108 dry cleaning Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000021588 free fatty acids Nutrition 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- D06L1/10—Regeneration of used chemical baths
Definitions
- I solved matters andit takes out but little of the colloidal. matter. Distillation is sometimes employed by cleaners in recovering soline,-but where the gasoline contains ree fatty acids (from dissociated soaps), after a few distillations the distillate is apt to become what is known as sour gasoline, which is not deemed desirable for cleaning his invention relates to cleaning solvents; and must be discarded.
- While ugal action in the presence of activated other kinds of activated carbon may be carbon, advantageously that of the Mumused, I find the type described and claimed ford Patent No. 1,286,187 all'asmore fully in various patents to one Mumford (see No. 1,286,187) best adapted.
- the activated carbon adds several other functions of importance to its ordinary decolorizing function. One of these added functions is removal (to a greater or less extent) of dissolved greases and resins, and another is collection of colloid suspensions and emulsions and their conversion into a form amenable to centrifugal separation.
- the solvents used by the cleaners are gasoline and benzol (coal tar benzene); although used carbontetrathe chlorethylene; and particularly is a desideratum. le to any of these state, but I shall chlorid, chloroform,
- non-inflammabilit My invention is applica solvents in an impure applied to the treatment of gasoline which may be regarded as typical of the cleaners solvents.
- "Dry cleaners gasoline is a special grade of petroleum distillate or of gaslow end boiling point. rimary object in using gas oline in dry (ileaning is to dissolve and re-. move grease, gasoline being an excellent solventfor fatty and greasy substances, yet, as a matter of fact, it removes and carries with it dirt of all kinds. After a certain gasoline used in cleaning becomes too much contaminated or dirty and must be purified.
- solvents carrying colloidal matter of the wing carbon, together with dissolved and WlllCll comprises agitating such a solvent suspended impurities of the gasolene.
- the process 30 thereby removing the residue of the decolortype of dry' cleaners gasoline, the process I stead of using a centrifugal, a filter press calcium carbonate to collect such colloid may be employed; but the centrifugal I rematter and neutralize acidity and separating gard as. better.
- the eflluent gasoline is the carbon and collected matter by centrifuready for re-use but, if desired, it may be gal action.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
v Patented'feb. 19, 1924.
- hereinafter set forth-and as claimed.
' hereinafter more particularly describe it as or pseudo-solutions of finely l lo Drawing.
citizen of the United-States, residing at wherein such generally Ioccasionally. there are oline having a length of time,
partly because of stances present.
v I 1,484,161 uurrao' STATES PATENT OFFICE.
inc'ron s., ALL1EN, or WiLMINGTdN, DELAWARE, ASSIGNOR T0 mmoo oo'aroaa'rron, or WILMINGTON, DELAWARE, A CORPORATION or DELAWARE.
CLEANING, so'nvnnrl Application filed January 19, 1922. Serial No. 530,453.
I solved matters andit takes out but little of the colloidal. matter. Distillation is sometimes employed by cleaners in recovering soline,-but where the gasoline contains ree fatty acids (from dissociated soaps), after a few distillations the distillate is apt to become what is known as sour gasoline, which is not deemed desirable for cleaning his invention relates to cleaning solvents; and must be discarded. I Y and it comprises a method of purifying In the present invention I -modify the solvents (gasoline, benzol, etc.) used in dry purification process by incorporating alittle cleaning garments, and for similar purposes, decolorizing carbon into the used gasoline solvent is exposed to centrifprior to the centrifugal separation. While ugal action in the presence of activated other kinds of activated carbon may be carbon, advantageously that of the Mumused, I find the type described and claimed ford Patent No. 1,286,187 all'asmore fully in various patents to one Mumford (see No. 1,286,187) best adapted. In treating dirty gasoline, the activated carbon adds several other functions of importance to its ordinary decolorizing function. One of these added functions is removal (to a greater or less extent) of dissolved greases and resins, and another is collection of colloid suspensions and emulsions and their conversion into a form amenable to centrifugal separation. By the simple expedient of adding a little activated carbon to gasoline and agitating the two together for a time, the carbon collects very fine matters in suspension or pseudo-suspension. On then centrifugaling the two are thrown out together. In so doing, a light-colored clean gasoline is obtained suitable for direct use in dryicleaning. If the gasoline treated is acid, that is, contains free fatty acids or resin acids, it is-advantageous to use a little calcium carbonate, or lime with the carbon, v say, one per cent or so, of calciumcarbonate on the weight of the carbon. The calcium salts of these fatty and resin acids are insoluble and are collected by the carbon. The gasoline thus neutralized can be dis tilled withoutproduction of fsour gasoline.
In a specific embodimentyof the [present invention, used asolinefis allowed to stand 100 in a storage tan or is-filtered in anysuitable way to free it of coarse dirt..' To this gasoline is then added a small proportion of one of the commercial-activated carbons. In the case of the Mum-ford ma terial, about 35 parts by weight to' 100gallons-of used. gasoline are advantageous. th gasoline is particularlydirty, somewhat be employed, while 'ifit is fairly e b somewhat re- To all whom it may concern Be 1t known that I, VICTOR S. ALLIEN, a
Wilmington, in the county of New Castle and State ofDelaware, have invented certain new and ,useful Improvements 1n Cleaning Solvents, of which the following is a specification. I
In dry cleaning garments, the solvents used by the cleaners are gasoline and benzol (coal tar benzene); although used carbontetrathe chlorethylene; and particularly is a desideratum. le to any of these state, but I shall chlorid, chloroform,
ethylene chlorid, etc., where non-inflammabilit My invention is applica solvents in an impure applied to the treatment of gasoline which may be regarded as typical of the cleaners solvents. "Dry cleaners gasoline is a special grade of petroleum distillate or of gaslow end boiling point. rimary object in using gas oline in dry (ileaning is to dissolve and re-. move grease, gasoline being an excellent solventfor fatty and greasy substances, yet, as a matter of fact, it removes and carries with it dirt of all kinds. After a certain gasoline used in cleaning becomes too much contaminated or dirty and must be purified. This purificationofi'ers considerable difliculty, this being the wide variety of sub- In addition to the coarse and easily removed dirt and greases, resins, etc., in so ution, there are colloid suspensions divided liquid and solid matters. In cleaning establishments the dirty, used gasoline is ordinaril put in storage 'tanksto settle'out as much dirt as possible and is then frequent y run through a centrifugal to separate a further quantity. This, however, is not very efi'ect-' ual and does not give a clean product. A more -ma, I centrifugal does not, of course, remove disclean, the proportion may While the Q I insane? duced. With other activated carbons or- What I claim is dinarily considerably more is required. a The Y 1. In the purification of used and impure carbon and the gasoline are well a 'tated solvents carrying colloidal matter of the for a period of 10 to 30 minutes and to settle. Much of the carbon deposits, carvwhich comprises agitating such a solvent rying impurities removed from the gasoline with activated carbon to collect such 001- with it. Without waiting for a complete loid matter and separating the carbon and separation in this manner, the gasoline is collected matter by centrifugal action.
next treated in an eflicient separating ma- '2. In the purification of used and impure chine of the centrifugal separator type, solvents carrying colloidal matter of the wing carbon, together with dissolved and WlllCll comprises agitating such a solvent suspended impurities of the gasolene. Inwith activated carbon in the presence of lowed type of dry cleaners gasoline, the process 30 thereby removing the residue of the decolortype of dry' cleaners gasoline, the process I stead of using a centrifugal, a filter press calcium carbonate to collect such colloid may be employed; but the centrifugal I rematter and neutralize acidity and separating gard as. better. The eflluent gasoline is the carbon and collected matter by centrifuready for re-use but, if desired, it may be gal action.
distilled. As the carbon takes out the'mois- 3. The process of recovering ,dry cleaners ture (of soap emulsions and :the like), the gasoline, which comprises settling said gasgasoline coming fro the centrifugal is suboline to remove coarse impurities, adding stantially dry. Where the used oline is activated carbon and calcium carbonate, ag1-' acid in its nature, it is, as statei useful tating and separating by centrifugal action; expedient to add a little calcium carbonate In. testimony whereof, I have hereunto at the time of adding the carbon. Or the 'aflixed my signature. carbon may be treated with a little lime water prior to use. v VICTOR S. ALLIEN.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US530453A US1484167A (en) | 1922-01-19 | 1922-01-19 | Cleaning solvent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US530453A US1484167A (en) | 1922-01-19 | 1922-01-19 | Cleaning solvent |
Publications (1)
Publication Number | Publication Date |
---|---|
US1484167A true US1484167A (en) | 1924-02-19 |
Family
ID=24113688
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US530453A Expired - Lifetime US1484167A (en) | 1922-01-19 | 1922-01-19 | Cleaning solvent |
Country Status (1)
Country | Link |
---|---|
US (1) | US1484167A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2613181A (en) * | 1947-09-13 | 1952-10-07 | Infilco Inc | Treatment of oily waste water |
US3242097A (en) * | 1961-04-27 | 1966-03-22 | Phillips Petroleum Co | Separation of liquid phases |
US4033860A (en) * | 1975-09-10 | 1977-07-05 | Uop Inc. | Mercaptan conversion process |
-
1922
- 1922-01-19 US US530453A patent/US1484167A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2613181A (en) * | 1947-09-13 | 1952-10-07 | Infilco Inc | Treatment of oily waste water |
US3242097A (en) * | 1961-04-27 | 1966-03-22 | Phillips Petroleum Co | Separation of liquid phases |
US4033860A (en) * | 1975-09-10 | 1977-07-05 | Uop Inc. | Mercaptan conversion process |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3553099A (en) | Process for extracting tar from tar sand | |
US2301240A (en) | Purification of acetylene prepared by thermal or electrical methods | |
US2774716A (en) | Process for removing finely divided solids from raw low temperature carbonization coal tars | |
CH515345A (en) | Method of cleaning wool | |
US2437649A (en) | Separation of phenols from hydrocarbon distillates by steam distillation | |
US1484167A (en) | Cleaning solvent | |
CN106943775B (en) | Device and method for continuously separating solid phase from liquid phase in caprolactam distillation heavy residual liquid | |
US2123554A (en) | Purification of crude phosphorus | |
US2320106A (en) | Purification of oil | |
US1827165A (en) | Separation of oil from bleaching clay | |
US1693417A (en) | Filtering process | |
US2928882A (en) | Purification of aqueous liquors containing phenol | |
US1619869A (en) | Method of treating hydrocarbon oils | |
US1633941A (en) | Process for removing suspended matters from oils and organic solvents | |
US1873900A (en) | Removal of phenols from waste and other liquors | |
US1975171A (en) | Process of purifying tetra alkyl lead | |
US1919644A (en) | Process for purifying dry cleaners' solvents | |
US2139629A (en) | Dry cleaning process | |
US2063940A (en) | Process for concentrating aqueous aliphatic acids recovered from cellulose esterification processes | |
US1571986A (en) | Process for the purification of crude ammoniacal liquors | |
US1716632A (en) | Process of refining mineral lubricating oils | |
US2607786A (en) | Process for recovering oil from the solvent cleaning or scouring of raw wool or woolfabric | |
RU2127297C1 (en) | Method of purifying oil lube fractions | |
DE1036454B (en) | Purification of fission gases | |
US2027770A (en) | Process of treating lubricating oil stock |