DE1291436B - Wasser-in-OEl-Emulsion fuer Schmierzwecke - Google Patents
Wasser-in-OEl-Emulsion fuer SchmierzweckeInfo
- Publication number
- DE1291436B DE1291436B DEL47797A DEL0047797A DE1291436B DE 1291436 B DE1291436 B DE 1291436B DE L47797 A DEL47797 A DE L47797A DE L0047797 A DEL0047797 A DE L0047797A DE 1291436 B DE1291436 B DE 1291436B
- Authority
- DE
- Germany
- Prior art keywords
- parts
- water
- oil
- oil emulsion
- mixture
- 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.)
- Pending
Links
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- C10M173/00—Lubricating compositions containing more than 10% water
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- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
- C07C51/353—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by isomerisation; by change of size of the carbon skeleton
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- C07C55/02—Dicarboxylic acids
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- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
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Description
1 2
Gegenstand der Patentanmeldung P 14 44 857.8 können. Teile beziehen sich auf das Gewicht, wenn
(deutsche Auslegeschrift 1 270 723) ist eine Wasser-in- nichts anderes angegeben ist.
Öl-Emulsion, bestehend aus 1 bis 80 Teilen Wasser, A. Ein Polyisobutenylbernsteinsäureanhydrid wird
20 bis 99 Teilen Mineralöl und 0,2 bis 10 Teilen durch Umsetzen eines chlorierten Polyisobutene mit
entweder 5 Maleinsäureanhydrid bei 200° C hergestellt. Das
a) eines Alkali- oder Erdalkalimetallsalzes oder chlorierte Polyisobuten wurde erhalten durch Beeines
Salzes mit Ammoniak, einem Hydroxy- handeln eines Polyisobutylene mit einem mittleren
alkylamin, Alkylenamin oder einem technischen Molekulargewicht von 1000 mit Chlor bei 104 bis
Gemisch von Alkylenaminen einer Alkyl- oder 110°C, bis der Chlorgehalt 4,3% erreicht. Das Alkenyl-Alkenylbernsteinsäure
mit mindestens 50 Kohlen- io bernsteinsäureanhydrid hat ein Äquivalentgewicht
Stoffatomen im Alkyl- bzw. Alkenylrest bzw. von 518.
deren Chlorsulfonierungsprodukt oder 518 Teile (1 Äquivalent) dieses Polyisobutenyl-
b) eines Esters der Alkyl- oder Alkenylbernstein- bernsteinsäureanhydrids werden mit 200 Teilen (lÄquisäure
mit einem Hydroxyalkylamin oder einem valent) Polyäthylenglykol, 7,2 Teilen p-Toluolsulfonteilweise
acylierten mehrwertigen Alkohol oder 15 säuremonohydrat und 400 Teilen Xylol versetzt. Das
c) dem Amid, Imid oder Amidin der Alkyl- oder Gemisch wird 10 Stunden auf 140 bis 150° C erhitzt
Alkenylbernsteinsäure. und das Reaktionswasser entfernt. Dann werden
Gegenstand der vorliegenden Erfindung ist eine die flüchtigen Bestandteile bei 105° C/4 Torr ab-Wasser-in-Öl-Emulsion
in Abänderung gemäß der destilliert. Der Rückstand wird mit 471 Teilen Mineral-Patentanmeldung
P 14 44 857.8 (deutsche Auslege- ao öl verdünnt und filtriert. Das Filtrat hat eine Verschrift
1 270 723), die gekennzeichnet ist durch einen seifungszahl von 50.
Gehalt eines Esters der Alkyl- bzw. Alkenylbernstein- B. Zu 300 Teilen (0,545 Äquivalente) Polyiso-
säure mit einem mehrwertigen Alkohol oder Poly- butenylbernsteinsäureanhydrid, hergestellt gemäß A,
alkylenglykoläther. gibt man 279 Teile (0,545 Äquivalente) Polypropylen-
Die Wasser-in-Öl-Emulsion der Erfindung besteht 25 glykol, 382 Teile Mineralöl und 28,5 Teile einer säureebenfalls
aus 1 bis 80 Teilen Wasser, 20 bis 99 Teilen aktivierten Bleicherde. Das Gemisch wird auf 150°C
Mineralöl und 0,2 bis 10 Teilen des Alkyl- bzw. erhitzt und bei dieser Temperatur 20 Stunden mit
Alkenylbernsteinsäureesters. Stickstoff geblasen. Das Gemisch wird noch heiß
Die Alkyl- bzw. Alkenylbernsteinsäureester der filtriert. Das Filtrat hat eine Verseifungszahl von 35.
mehrwertigen Alkohole werden in üblicher Weise 30 C. Ein Gemisch aus 3318 Teilen (3 Mol) eines
durch Veresterung der Bernsteinsäure bzw. ihres Polyisobutenylbernsteinsäureanhydrids, hergestellt geAnhydrids
mit dem entsprechenden Alkohol her- maß A, mit einer Verseifungszahl von 101, 408 Teilen
gestellt. Man kann auch einen Bernsteinsäureester (3 Mol) Pentaerythrit und 2445 Teilen Mineralöl
eines relativ flüchtigen Alkohols oder Phenols mit wird 5 Stunden auf 15O0C und 5 Stunden auf 200
dem mehrwertigen Alkohol umestern. 35 bis 210°C erhitzt und anschließend filtriert. Das
Die mehrwertigen Alkohole enthalten vorzugsweise Filtrat hat eine Verseifungszahl von 50,-zwei
bis sechs alkoholische Hydroxylgruppen, von D. Ein Gemisch aus 544 Teilen (0,5 Mol) eines
denen zumindest eine Hydroxylgruppe nicht substi- Polyisobutenylbernsteinsäureanhydrids, hergestellt getuiert
ist. Beispiele für unsubstituierte mehrwertige maß A, und mit einer Verseifungszahl von 103,
Alkohole sind Äthylenglykol, 1,2-Propylenglykol, 40 90,6 Teilen (0,5 Mol) Sorbit und 417 Teilen Mineralöl
1,3-Propylenglykol, Glycerin, Erythrit, Pentaerythrit, wird auf 2000C erhitzt. Das Gemisch wird mit Stick-Arabit,
Adonit, Xylit, Mannit, Sorbit, Neopentyl- stoff in einer Menge von 56,61 je Stunde geblasen
glykol und Pentaerythrit. Mehrwertige Alkohole und 3V2 Stunden auf 200 bis 210° C erhitzt. Das
höheren Molekulargewichts sind ebenfalls brauch- Gemisch wird heiß filtriert. Das Filtrat hat eine Verbar.
Beispiele für diese Alkohole sind die ver- 45 seifungszahl von 55.
schiedenen Polyäthylenglykole und Polypropylen- E. Ein Gemisch aus 1156 Teilen (2 Äquivalente)
glykole. eines Polyisobutenylbernsteinsäureanhydrids, herge-
Die Veresterung der Alkyl- bzw. Alkenylbernstein- stellt gemäß A, 61 Teilen (2 Äquivalente) Glycerin
säure mit den vorgenannten mehrwertigen Alkoholen und 800 Teilen Xylol wird 16 Stunden auf 14O0C
bzw. Polyalkylenglykoläthern wird im allgemeinen 50 erhitzt und Reaktionswasser entfernt. Das Xylol
bei einer Temperatur von mindestens 100°C, Vorzugs- wird bei 150° C/20 Torr abdestilliert. Das Produkt
weise oberhalb 130° C, durchgeführt. Die Verwendung hat eine Verseifungszahl von 93.
eines Lösungsmittels, wie Benzol, Toluol, Naphtha, - F. Ein Gemisch aus 555 Teilen (1 Äquivalent)
Mineralöl, Xylol oder η-Hexan, ist zweckmäßig, eines Polyisobutenylbernsteinsäureanhydrids, hergeum
die Reaktionstemperatur leichter steuern zu 55 stellt gemäß Ä, und 45 Teilen (1 Äquivalent) 1,4-Butankönnen.
diol wird 11 Stunden auf 135 bis 190° C erhitzt und
Das Mengenverhältnis von Bernsteinsäure zu dem das Reaktionswasser entfernt. Danach werden 50 Teile
mehrwertigen Alkohol wird in der Regel so bemessen, eines Fütrierhilfsmittels und 250 Teile Mineralöl zudaß
mindestens etwa ein Zehntel und vorzugsweise gegeben, und es wird filtriert. Das Filtrat hat eine
die Hälfte der stöchiometrisch äquivalenten Menge 60 Verseifungszahl von 68.
der Alkoholkomponente je Äquivalent Bernsteinsäure G. Ein Gemisch aus 544 Teilen (1 Äquivalent)
verwendet wird. eines Polyisobutenylbernsteinsäureanhydrids, herge-
Die Alkyl- bzw. Alkenylbernsteinsäureester können stellt gemäß A, 90,6 Teilen (3 Äquivalente) Mannit
auch aus den entsprechenden Bernsteinhalogeniden und 417 Teilen Mineralöl wird 31I2 Stunden auf
erhalten werden. 65 200 bis 210° C erhitzt und mit Stickstoff geblasen.
Nachstehend werden Vorschriften zur Herstellung Das Gemisch wird noch heiß filtriert. Das Filtrat
der Bernsteinsäureester angegeben, die für die Wasser- hat eine Verseifungszahl von 56.
in-Öl-Emulsion der Erfindung verwendet werden Für die Wasser-in-Öl-Emulsion der Erfindung
kann als Öl ein Kohlenwasserstofföl mit einer Viskosität
von 50 SUS bei 380C bis 200 SUS bei 99°C verwendet
werden. Mineralöle mit Schmierviskositäten sind zur Verwendung in den Emulsionen besonders
vorteilhaft. Auch ein Gemisch von Ölen aus verschiedenen Quellen ist brauchbar. Ein derartiges
Gemisch kann z. B. aus Mineralölen, pflanzlichen Ölen, tierischen Ölen, synthetischen Ölen des Silicontyps,
synthetischen Ölen des Polyolefintyps und synthetischen Ölen des Polyestertyps hergestellt
werden.
Die Wasser-in-Öl-Emulsionen mit den günstigsten Eigenschaften enthalten 30 bis 50 Teile Wasser und
50 bis 70 Teile Öl. Die Wasser-in-Öl-Emulsionen, die als nicht brennbare Hydraulikflüssigkeiten vorgesehen
sind, müssen mindestens etwa 30% Wasser enthalten. Die Konzentration des Bernsteinsäureesters
in den Emulsionen beträgt vorzugsweise 1 bis 5 Teile je 100 Teile der Wasser-in-Öl-Emulsion. Die Hauptfunktion
des Bernsteinsäureesters ist die eines Emulgators, obwohl er der Emulsion auch reinigende
Eigenschaften verleiht.
Die Emulsionen können einfach dadurch hergestellt werden, daß man in einem Homogenisator oder einer
anderen wirksamen Mischvorrichtung Wasser, Öl, den Bernsteinsäureester und andere gewünschte Bestandteile
miteinander mischt. Ein Erhitzen der Emulsion während oder nach ihrer Herstellung ist
nicht erforderlich. Die Reihenfolge des Mischens der Bestandteile ist ohne Bedeutung. Es ist jedoch
zweckmäßig, zunächst ein Ölkonzentrat mit etwa 50 bis 95 Teilen der öllöslichen Bestandteile und etwa
5 bis 50 Teilen Öl herzustellen und dann das Konzentrat mit Wasser in den entsprechenden Mengen zu emulgieren.
Dies kann vom Verbraucher vorgenommen werden.
Die Wasser-in-Öl-Emulsion der Erfindung enthält vorzugsweise noch einen oder mehrere der in der
Hauptpatentanmeldung genannten Zusätze.
Die Beispiele erläutern die Konzentrate und Wasserin-Öl-Emulsionen
der Erfindung.
Gewichtsteile
Produkt von A 9,0
Sojabohnenlecithin 1,8
tert.-Cn~i4-Alkyl-prim.-amm,
Molekulargewicht 191 0,6
Zinksalz der Di-isooctyldithiophos-
phorsäure 3,0
Mineralschmieröl SAE 40 285,6
Antischaummittel 0,0075
Wasser 200
45
Gewichtsteile
Produkt von C 9,0
Sojabohnenlecithin 1,8
Primäres Amin von Beispiel 1 0,6
Zinksalz der Di-(heptylphenyl)-dithio-
phosphorsäure 3,7
Mineralschmieröl SAE 40 284,9
Antischaummittel 0,0045
Wasser 200
Gewichtsteile
Produkt von B 18,0
Sojabohnenlecithin 3,6
Salpetrigsaures Salz des primären
Amins von Beispiel 1 1,2
Sulfuriertes Spermöl mit einem
Schwefelgehalt von 10 % 18,0
4-Methyl-2,6-di-tert.-butylphenol 3,0
Mineralschmieröl SAE 5 536,2
Antischaummittel 0,015
Wasser 400,0
Die Schmiereigenschaften, insbesondere die verschleißmindernden Eigenschaften der Wasser-in-Öl-Emulsionen,
zeigen sich aus den Ergebnissen einer ASTM-Verschleißprüfung. Bei diesem Test wird die
Emulsion in einer hydraulischen Pumpe (einer Vickers Flügelradpumpe 104E) verwendet, die unter den
folgenden Bedingungen arbeitet: Motordrehzahl U/min; ungefähre Durchflußmenge 30,31 je
Minute; Druck 70,3 kg/cm2; Sumpf temperatur 66° C. Zum Vergleich wurde auch eine im Handel erhältliche
wasserhaltige Emulsion für Hydraulikflüssigkeiten geprüft. Unter den Versuchsbedingungen
zeigten die Wasser-in-Öl-Emulsionen der Erfindung bessere schmierende und verschleißmindernde Eigenschaften.
Claims (1)
- Patentanspruch:Wasser-in-Öl-Emulsion in Abänderung gemäß der Patentanmeldung P14 44 857.8 (deutsche Auslegeschrift 1270 723), gekennzeichnetdurch einen Gehalt eines Esters der Alkyl- bzw. Alkenylbernsteinsäure mit einem mehrwertigen Alkohol oder Polyalkylenglykoläther.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13486061A | 1961-08-30 | 1961-08-30 | |
US18894762A | 1962-04-20 | 1962-04-20 | |
US280453A US3255108A (en) | 1961-08-30 | 1963-05-14 | Water-in-oil emulsions containing succinic esters |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1291436B true DE1291436B (de) | 1969-03-27 |
Family
ID=27384639
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEP1270A Pending DE1270723B (de) | 1961-08-30 | 1962-08-30 | Wasser-in-OEl-Emulsion fuer Schmierzwecke |
DEL47797A Pending DE1291436B (de) | 1961-08-30 | 1964-05-12 | Wasser-in-OEl-Emulsion fuer Schmierzwecke |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEP1270A Pending DE1270723B (de) | 1961-08-30 | 1962-08-30 | Wasser-in-OEl-Emulsion fuer Schmierzwecke |
Country Status (3)
Country | Link |
---|---|
US (1) | US3255108A (de) |
DE (2) | DE1270723B (de) |
GB (2) | GB1009197A (de) |
Families Citing this family (84)
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DE1271877B (de) * | 1963-04-23 | 1968-07-04 | Lubrizol Corp | Schmieroel |
US3381022A (en) * | 1963-04-23 | 1968-04-30 | Lubrizol Corp | Polymerized olefin substituted succinic acid esters |
GB1054276A (de) * | 1963-05-17 | |||
US3346354A (en) * | 1963-07-02 | 1967-10-10 | Chvron Res Company | Long-chain alkenyl succinic acids, esters, and anhydrides as fuel detergents |
US3459663A (en) * | 1967-04-06 | 1969-08-05 | Sun Oil Co | Aluminum rolling oil |
US3507792A (en) * | 1967-11-30 | 1970-04-21 | Sinclair Research Inc | Biodegradable,water-dispersible lubricant compositions |
US3859318A (en) * | 1969-05-19 | 1975-01-07 | Lubrizol Corp | Products produced by post-treating oil-soluble esters of mono- or polycarboxylic acids and polyhydric alcohols with epoxides |
US3639242A (en) * | 1969-12-29 | 1972-02-01 | Lubrizol Corp | Lubricating oil or fuel containing sludge-dispersing additive |
US3708522A (en) * | 1969-12-29 | 1973-01-02 | Lubrizol Corp | Reaction products of high molecular weight carboxylic acid esters and certain carboxylic acid acylating reactants |
FR2087740A5 (de) * | 1970-05-29 | 1971-12-31 | Pechiney Saint Gobain | |
US4031118A (en) * | 1973-09-17 | 1977-06-21 | The Lubrizol Corporation | Ester-containing process and compositions |
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US4045363A (en) * | 1975-11-07 | 1977-08-30 | The Elco Corporation | Invert emulsions of improved extreme pressure properties |
US4094800A (en) * | 1976-07-14 | 1978-06-13 | Standard Oil Company (Indiana) | Anti-wear lubricating oil compositions |
FR2363622A1 (fr) * | 1976-09-01 | 1978-03-31 | Nat Res Lab | Composition stabilisee de fluide pour le travail des metaux et son obtention |
US4216114A (en) * | 1977-11-18 | 1980-08-05 | Imperial Chemical Industries Limited | Demulsification process |
GB2017719B (en) * | 1978-03-23 | 1982-07-21 | Ici Ltd | Surfactant compositions comprising a blend of two types of alk(en)yl succinic polyester |
US4329249A (en) * | 1978-09-27 | 1982-05-11 | The Lubrizol Corporation | Carboxylic acid derivatives of alkanol tertiary monoamines and lubricants or functional fluids containing the same |
US4666620A (en) * | 1978-09-27 | 1987-05-19 | The Lubrizol Corporation | Carboxylic solubilizer/surfactant combinations and aqueous compositions containing same |
US4368133A (en) * | 1979-04-02 | 1983-01-11 | The Lubrizol Corporation | Aqueous systems containing nitrogen-containing, phosphorous-free carboxylic solubilizer/surfactant additives |
US4466909A (en) * | 1980-09-29 | 1984-08-21 | Chevron Research Company | Oil-in-water microemulsion fluid |
US4447348A (en) * | 1981-02-25 | 1984-05-08 | The Lubrizol Corporation | Carboxylic solubilizer/surfactant combinations and aqueous compositions containing same |
US4448703A (en) * | 1981-02-25 | 1984-05-15 | The Lubrizol Corporation | Carboxylic solubilizer/surfactant combinations and aqueous compositions containing same |
US4486324A (en) * | 1981-11-06 | 1984-12-04 | Edwin Cooper, Inc. | Hydraulic fluids |
GB2123029B (en) * | 1982-07-02 | 1985-09-25 | Conoco Inc | Storage stable fire resistant hydraulic fluid and compositions therefor |
US4471091A (en) * | 1982-08-09 | 1984-09-11 | The Lubrizol Corporation | Combinations of carboxylic acylating agents substituted with olefin polymers of high and low molecular weight mono-olefins, derivatives thereof, and fuels and lubricants containing same |
US4486573A (en) * | 1982-08-09 | 1984-12-04 | The Lubrizol Corporation | Carboxylic acylating agents substituted with olefin polymers of high molecular weight mono-olefins, derivatives thereof, and fuels and lubricants containing same |
US4613342A (en) * | 1982-08-09 | 1986-09-23 | The Lubrizol Corporation | Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same |
US4575526A (en) * | 1982-08-09 | 1986-03-11 | The Lubrizol Corporation | Hydrocarbyl substituted carboxylic acylaging agent derivative containing combinations, and fuels containing same |
US4596663A (en) * | 1982-08-09 | 1986-06-24 | The Lubrizol Corporation | Carboxylic acylating agents substituted with olefin polymers of high molecular weight mono-olefins, derivatives thereof, and fuels and lubricants containing same |
US4623684A (en) | 1982-08-09 | 1986-11-18 | The Lubrizol Corporation | Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same |
US4489194A (en) * | 1982-08-09 | 1984-12-18 | The Lubrizol Corporation | Carboxylic acylating agents substituted with olefin polymers of high/low molecular weight mono-olefins, derivatives thereof, and fuels and lubricants containing same |
US4559155A (en) * | 1982-08-09 | 1985-12-17 | The Lubrizol Corporation | Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same |
US4564460A (en) * | 1982-08-09 | 1986-01-14 | The Lubrizol Corporation | Hydrocarbyl-substituted carboxylic acylating agent derivative containing combinations, and fuels containing same |
US4539125A (en) * | 1982-11-30 | 1985-09-03 | Idemitsu Kosan Company | Water-based metal-working fluid |
DE3572492D1 (en) * | 1984-02-14 | 1989-09-28 | Lubrizol Corp | Nitrogen- and phosphorus-containing compositions and aqueous systems containing same |
GB8407300D0 (en) * | 1984-03-21 | 1984-04-26 | Ici Plc | Surfactants |
GB2156799B (en) * | 1984-03-21 | 1987-12-16 | Ici Plc | Emulsion explosive |
GB8410393D0 (en) * | 1984-04-24 | 1984-05-31 | Ici Plc | Fluid compositions |
US4618450A (en) * | 1984-11-07 | 1986-10-21 | The Lubrizol Corporation | Aqueous systems containing amino sulfonic acid derivatives of carboxylic acids |
CA1265415A (en) * | 1984-12-27 | 1990-02-06 | Robert Edwin Quinn | Dispersant salts |
GB8522052D0 (en) * | 1985-09-05 | 1985-10-09 | Ici Plc | Polymerisation process |
US4911736A (en) * | 1985-09-18 | 1990-03-27 | The Standard Oil Company | Emulsifier and stabilizer for water base emulsions and dispersions of hydrocarbonaceous materials |
US4708753A (en) * | 1985-12-06 | 1987-11-24 | The Lubrizol Corporation | Water-in-oil emulsions |
ZW23786A1 (en) * | 1985-12-06 | 1987-04-29 | Lubrizol Corp | Water-in-oil-emulsions |
US4844756A (en) * | 1985-12-06 | 1989-07-04 | The Lubrizol Corporation | Water-in-oil emulsions |
US4770803A (en) * | 1986-07-03 | 1988-09-13 | The Lubrizol Corporation | Aqueous compositions containing carboxylic salts |
USRE36479E (en) * | 1986-07-03 | 2000-01-04 | The Lubrizol Corporation | Aqueous compositions containing nitrogen-containing salts |
US4689166A (en) * | 1986-07-17 | 1987-08-25 | Pennzoil Product Company | Succinic acid esters and hydraulic fluids thereform |
US4784784A (en) * | 1986-07-17 | 1988-11-15 | Pennzoil Products Company | Succinic acid esters and hydraulic fluids therefrom |
NL8601862A (nl) * | 1986-07-28 | 1988-02-16 | Magyar Asvanyolaj Es Foeldgaz | Ep-toevoegsels bevattende hulpstoffen voor de metaalbewerkende industrie. |
US4720555A (en) * | 1986-09-12 | 1988-01-19 | Pennzoil Products Company | Hydrocarbyl anhydrides |
US5047175A (en) | 1987-12-23 | 1991-09-10 | The Lubrizol Corporation | Salt composition and explosives using same |
US5527491A (en) | 1986-11-14 | 1996-06-18 | The Lubrizol Corporation | Emulsifiers and explosive emulsions containing same |
US4840687A (en) * | 1986-11-14 | 1989-06-20 | The Lubrizol Corporation | Explosive compositions |
US4863534A (en) * | 1987-12-23 | 1989-09-05 | The Lubrizol Corporation | Explosive compositions using a combination of emulsifying salts |
US4828633A (en) * | 1987-12-23 | 1989-05-09 | The Lubrizol Corporation | Salt compositions for explosives |
US5129972A (en) | 1987-12-23 | 1992-07-14 | The Lubrizol Corporation | Emulsifiers and explosive emulsions containing same |
US5041622A (en) * | 1988-04-22 | 1991-08-20 | The Lubrizol Corporation | Three-step process for making substituted carboxylic acids and derivatives thereof |
EP0360394A3 (de) * | 1988-09-21 | 1992-03-18 | Imperial Chemical Industries Plc | Emulsionssprengstoff vom Wasser-in-Öl-Typ |
CA2014700C (en) * | 1989-04-20 | 2001-02-13 | Robert E. Quinn | Method for reducing friction between railroad wheel and railway track using metal overbased colloidal disperse systems |
EP0407124A1 (de) * | 1989-07-07 | 1991-01-09 | Tonen Corporation | Schmierölzusammensetzung |
US5622649A (en) * | 1991-06-27 | 1997-04-22 | Emory University | Multiple emulsions and methods of preparation |
US5518517A (en) | 1994-11-14 | 1996-05-21 | The Lubrizol Corporation | Water-in-oil emulsion fertilizer compositions |
US5512079A (en) * | 1994-11-14 | 1996-04-30 | The Lubrizol Corporation | Water-in-oil emulsifiers for slow release fertilizers using tertiary alkanol amines |
US6020061A (en) * | 1997-04-15 | 2000-02-01 | S. C. Johnson Commercial Markets, Inc. | Emulsion polymerization using polymeric surfactants |
US5936194A (en) * | 1998-02-18 | 1999-08-10 | The Lubrizol Corporation | Thickened emulsion compositions for use as propellants and explosives |
US6054493A (en) * | 1998-12-30 | 2000-04-25 | The Lubrizol Corporation | Emulsion compositions |
US6176893B1 (en) | 1998-12-30 | 2001-01-23 | The Lubrizol Corporation | Controlled release emulsion fertilizer compositions |
US6200398B1 (en) | 1998-12-30 | 2001-03-13 | The Lubrizol Corporation | Emulsion explosive compositions |
US20040111957A1 (en) * | 2002-12-13 | 2004-06-17 | Filippini Brian B. | Water blended fuel composition |
GB2408748B (en) * | 2004-02-05 | 2006-12-13 | Niche Products Ltd | Hydraulic fluids containing Lecithin |
US20070054968A1 (en) * | 2005-08-23 | 2007-03-08 | Bj Services Company | Environmentally friendly defoamer |
GB0622947D0 (en) * | 2006-11-17 | 2006-12-27 | Croda Int Plc | Surfactant compounds |
CN101985577B (zh) * | 2010-11-01 | 2012-10-10 | 彭美东 | 线切割乳化油 |
US20120178824A1 (en) * | 2011-01-11 | 2012-07-12 | Henkel Ag & Co. Kgaa | Hydrogels based on esters of polyisobutenesuccinic acid |
CN102676134A (zh) * | 2012-05-02 | 2012-09-19 | 陆明富 | 一种植物油防卡润滑剂的制备方法 |
US10336954B2 (en) | 2013-02-07 | 2019-07-02 | Bl Technologies, Inc. | Compositions and methods for inhibiting fouling in hydrocarbons or petrochemicals |
US10012066B2 (en) | 2015-05-19 | 2018-07-03 | The Mosaic Company | Reverse emulsions for cavity control |
EP3257920A1 (de) * | 2016-06-17 | 2017-12-20 | Total Marketing Services | Schmiermittelpolymere |
RU2652714C1 (ru) * | 2017-07-17 | 2018-04-28 | Общество с ограниченной ответственностью "РудХим" | Универсальный эмульгатор обратных эмульсий |
CN109352100A (zh) * | 2018-12-07 | 2019-02-19 | 辽宁泰克诺美科技有限公司 | 一种低烟雾加工效率高的电火花加工液 |
Family Cites Families (7)
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US2221162A (en) * | 1938-08-06 | 1940-11-12 | Texas Co | Lubricating oil |
US3057890A (en) * | 1958-04-17 | 1962-10-09 | Petrolite Corp | Certain polyoxyalkylene glycol esters |
US3070546A (en) * | 1959-01-16 | 1962-12-25 | Lubrizol Corp | Nitrogen-, phosphorus- and sulfurcontaining lubricants |
US3062612A (en) * | 1959-04-25 | 1962-11-06 | Inst Francais Du Petrole | Method of protecting metals against electrochemical corrosion of the acidic type |
FR1265086A (fr) * | 1959-08-24 | 1961-06-23 | California Research Corp | Compositions d'huiles lubrifiantes renfermant des alkényl succinimides de la tétraéthylène pentamine |
FR1265085A (fr) * | 1959-08-24 | 1961-06-23 | California Research Corp | Compositions d'huiles lubrifiantes renfermant des n-dialkylaminoalkyl alkényl succinimides |
FR1283719A (fr) * | 1960-03-15 | 1962-02-02 | California Research Corp | Compositions d'huiles lubrifiantes contenant des mélanges de dithiophosphates métalliques et de n-dialkylaminoalcényl succinimides |
-
1962
- 1962-08-30 GB GB33400/62A patent/GB1009197A/en not_active Expired
- 1962-08-30 DE DEP1270A patent/DE1270723B/de active Pending
-
1963
- 1963-05-14 US US280453A patent/US3255108A/en not_active Expired - Lifetime
-
1964
- 1964-05-12 DE DEL47797A patent/DE1291436B/de active Pending
- 1964-05-14 GB GB20156/56A patent/GB1059847A/en not_active Expired
Non-Patent Citations (1)
Title |
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None * |
Also Published As
Publication number | Publication date |
---|---|
US3255108A (en) | 1966-06-07 |
GB1059847A (en) | 1967-02-22 |
GB1009197A (en) | 1965-11-10 |
DE1270723B (de) | 1968-06-20 |
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