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Publication numberUS3492230 A
Publication typeGrant
Publication dateJan 27, 1970
Filing dateMay 27, 1966
Priority dateMay 27, 1966
Also published asDE1643073B1
Publication numberUS 3492230 A, US 3492230A, US-A-3492230, US3492230 A, US3492230A
InventorsEugene E Richardson, Albert R Sabol, Roger W Watson
Original AssigneeStandard Oil Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of preparing alkaline earth sulfonates of high alkalinity
US 3492230 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

United States Patent US. Cl. 252-33 5 Claims ABSTRACT OF THE DISCLOSURE Preparation of oil-soluble alkaline earth sulfonates of high alkalinity is improved by using an amine promoter during the carbonation of a mixture comprising neutral alkaline earth sulfonate, excess basic alkaline earth compound, a lower alkanol, and Water.

This invention relates to improvements in preparing alkaline earth sulfonates, in particular to an improved method of preparing highly basic alkaline earth sulfonates, and more particularly highly basic magnesium sulfonates.

It has become increasingly important, in order to suit the requirements of the operation of internal combustion engines, of both the spark-ignition and diesel types, to increase the alkalinity of the detergent-type additives used in such engines. Highly basic alkaline earth sulfonates are particularly effective lubricating oil additives. It has also been found that such sulfonates are well suited as diesel fuel additives to decrease excessive smoking of diesel engine exhaust.

Increasing the alkalinity of alkaline earth sulfonates to provide an alkaline reserve is commonly referred to as over-basing or super-basing. Many methods have been proposed for obtaining compounds possessing an alkaline reserve. In general, such prior art methods make preparation by controlled carbonation of the alkaline earth oxide or hydroxide in the presence of the neutral sulfonic acid soap. The preparation of over based magnesium sulfonates is particularly different because of long reaction time, poor metal utilization and difiicult filtration.

It is an object of the present invention to provide an improved method of preparing over-based alkaline earth sulfonates. Another object of the invention is to provide an improved method of preparing over-based sulfonates which provides improved metal utilization, shorter reaction times, increased total base numbers and better filterability. Still another object of the invention is to provide an improved method of preparing over based preferentially oil-soluble magnesium sulfonates. These and other objects and advantages of the present invention will become apparent as the description thereof proceeds.

In accordance With the present invention, the above objects ate attained by preparing over-based alkaline earth sulfonates, particularly over-based magnesium sulfonates, in the presence of an amine promoter. The amine promoter, used in concentrations of from about 0.05% to about 18% of the weight of the basic alkaline earth compound, may be introduced prior to or during the overbasing stage of the process, and may be retained in the final product or removed therefrom by suitable means.

Broadly stated, the process of the present invention comprises neutralizing at a temperature of from about 80 F. to about 212 F., a preferentially oil-soluble sulfonid acid, preferably in solution in a hydrocarbon solvent, which may be aromatic, e.g. xylenes or aliphatic, e.g. hexanes, with a basic alkaline earth compound, such as an alkaline earth oxide or hydroxide, adding to the neutral sulfonate an excess of the basic alkaline earth compound, the amine, a lower alkanol, e.g. methanol, ethanol or propanol, and a small amount of water, and then blowing sufiicient carbon dioxide through the mixture to convert the alkaline earth bases to carbonates at a temperature of from about 40 F. to about F. The carbon dioxide-treated product may be heated to reflux for about 10 minutes to about 60 minutes. To the alcoholfree product, water is added and the mixture may be blown with carbon dioxide for about 15 to minutes at about 70 F. to about 212 F. The mixture is then heated to remove water and solvent, and filtered. If desired, only the water may be removed prior to filtration, and the solvent removed after filtration. Although it is preferred to add the amine after the formation of the neutral alkaline earth sulfonate, the amine can be added during the formation of the neutral sulfonate.

Sulfonic acids suitably used in accordance with this invention are preferentially oil-soluble sulfonic acids.

Such sulfonic acids include preferentially oil-solublepetroleum sulfonic acids, commonly referred to as mahogany acids, alkyl sulfonic acids, aryl sulfonic acids, and alkaryl sulfonic acids. Illustrative of suitable sulfonic acids are the preferentially oil-soluble petroleum sulfonic acids, e.g. mahogany acids of about 350 to 750 molecular Weight, dilauryl aryl sulfonic acid, laurylcetyl aryl sulfonic acid, paraflin wax-substituted benzene sulfonic acids, didodecyl benzene sulfonic acids, polyolefin alkylated benzene sulfonic acids, such as polybutylene alkylated benzene sulfonic acids, in which the polybutylene substituents have molecular weights of at least about 200, and preferably within the range of from about 300 to about 2500; polypropylene alkylated benzene sulfonic acids in which the polypropylene substituents have a molecular weight of at least about 250, and preferably Within the range of from about 290 to about 1500; naphthalene sulfonic acids; alkyl-substituted naph thalene sulfonic acids; and the like.

The preparation of the sulfonic acid is well known to those skilled in the art. Such sulfonic acids can be prepared by reacting the material to be sulfonated with a suitable sulfonating agent, such as concentrated sulfuric acid, fuming sulfuric acid, chlorosulfonic acid or sulfur trioxide for a period of time suflicient to effect sulfonation, and thereafter separating insoluble acid sludge from the oil-soluble sulfonic acid.

The amine promoter used in accordance with the present invention can be an aliphatic amine, an aromatic amine, or heterocyclic amine.

Illustrative of specific suitable amines are methylamine, N-methyloctylamine, dibutylamine, cyclohexylamine, dodecylamine, octadecylamine, methylene amines, ethylene amines, butylene amines, propylene amines, hexylene amines, ethylene diamine, triethylene tetramine, propylene diamine, octylmethylene diamine, tetraethylene pentamine, dipropylene triamine, 1,3-diamino propanes such as compounds of the general formula RNHCH CH CH NH in which R is the alkyl radical derived from tallow fatty acids and from cocoa fatty acids; such products are commercially marketed as Duomeen T and Duomeen C, respectively.

The following specific examples illustrate the process of the present invention.

EXAMPLE I Part 1 Benzene alkylated with a polypropylene of about 730- 800 molecular weight was sulfonated to obtain a polypropylene alkylated benzene sulfonic acid of 880 molecular weight containing about 2.3 weight percent sulfuric acid. To 700 grams of a 50% xylene solution of the polypropylene alkylated benzene sulfonic acid were added 15 grams 3 of calcium oxide (1.5 moles per mole H 50 and the mixture stirred and heated at 150 F. for one hour under reflux conditions to convert the free sulfuric acid to water-insoluble calcium sulfate which is precipitated and removed from the xylene solution of the sulfonic acid.

Part 2 To the sulfonic acid solution of Part 1, free of sulfuric acid, were added 460 grams of a solvent extracted SAE petroleum oil, 450 grams of xylene, 16 grams of magnesium oxide and 200 cc. methanol, and the mixture stirred and heated at reflux temperature of about 160 F.

for one hour to neutralize the sulfonic acid.

Part 3 To the neutral magnesium sulfonate were added 25 grams ethylene diamine, 160 grams magnesium oxide and 72 grams water (1 mole water per mole of magnesium oxide) and the mixture blown with 1.6 cubic feet per hour (CFH) CO gas for 2.5 hours.

Part 4 The product of Part 3 was heated to 190 F. to remove the methanol, then 50 grams of water added and the mixture heated to 270 F. The mixture was then cooled to 190 F., 100 grams of water added and the mixture blown with CO at 1.6 c.f.h. for one hour at 180 F.

Part 5 The product of Part 4 was heated to 320 F. to remove the water and xylene and then filtered through diatomaceous earth.

The recovered product had the following properties:

Percent sulfonate 30 Total base number 300 Viscosity at 80 F. Fluid Filterability Excellent EXAMPLE II Part 1 sulfonate.

Part 2 To the product of Part 1 were added 500 grams xylene, 110 grams magnesium oxide powder, 400 grams methanol, 50 cubic centimeters water and 20 grams ethylene diamine and the mixture stirred and cooled to a temperature of 76 F. Carbon dioxide was then passed into the mixture at the rate of 1.6 cubic feet per hour for 1.5 hours. The temperature of the mixture rose to 114 F after 55 minutes, and then fell to 104 F. at the end of 1.5 hours.

Part 3 The product of Part 2 was then heated to 210 F. to remove the methanol, then 50 cc. of water added, and the mixture heated, without the reflux condenser, to 240 F. to distill 01f most of the water.

Part 4 The product of Part 3 was then filtered at 240 F. through diatomaceous earth and the filtrate heated to 320 F. under reduced pressure to remove the xylene solvent.

EXAMPLE III The product of this example was prepared substantially as in Example II, except that the ethylene diamine was omit d n P t 2, i

4 The products of Examples II and III had the following properties.

Example II Example III Percent Sulfonate 30 34 Q Total Base Number 350 105 MgO Utilization, percent 95+ 33 Viscosity at F Fluid Fluid Filterability Excellent Fair EXAMPLE IV Part 1 A mixture of 820 grams of a hexane solution of a polypropylene alkylated benzene sulfonic acid (540 grams 80% active sulfonic acid of 865 molecular weight), 640 grams of a solvent extracted SA-E 5 petroleum oil, 10 grams of magnesium oxide powder and 5 cubic centimeters of water was heated to 240 F. to neutralize the free sulfonic acid and form the neutral magnesium sulfonate. The hexane was then removed by distillation.

Part 2 The product of Part 2 was heated to 210 F. and 50 cubic centimeters of water added. The reflux condenser was removed and the mixture heated to 240 F. until substantially all of the water was distilled off.

Part 4 The product of Part 3 was filtered through diatomaceous earth and the filtrate heated to 320 F. under reduced pressure to remove the xylenes.

EXAMPLE V Polypropylene alkylated benzene sulfonic acid was treated with magnesium oxide substantially as in Example IV, except that the ethylene diamine was omitted in Part 2.

The products of Examples IV and V had the following properties:

Example IV Example V Percent Sulfonate 30 34 Total Base Number 250 97 MgO Utilization. percent 38 Viscosity at 80 F Fluid Fluid Filterability Excellent Good The data presented by the foregoing examples demonstrate that the use of amine promoters in the preparation of over-based alkaline earth sulfonates in accordance with the herein-described invention results in improved metal utilization, improved filterability, shorter reaction time and increase total base number of the sulfonates. While in the examples given we have employed magnesium oxide as the basic alkaline earth compound, similar results are attainable with the hydroxides, carbonates and oxides of the other members of the alkaline earth group, such as, for example, calcium and barium.

Percentages given herein are weight percentages unless otherwise stated.

While particular embodiments of the invention have been described, it is to be understood that the invention is not limited thereto, but covers such modifications and variations as come Within the spirit and scope of the apt pended claims,

We claim:

1. The method of preparing an over-based oil-soluble magnesium sulfonate comprising the steps of:

(a) forming in a petroleum oil vehicle a reaction mixture of (i) neutral oil-soluble magnesium sulfonate, (ii) magnesium oxide, (iii) a lower alkanol, (iv) about 0.9-1 mol of water per mol of magnesium oxide, and (v) ethylene diamine in an amount of about 0.05-18% of the weight of the magnesium oxide; (b) treating said reaction mixture at a temperature of about 40-175 F. with an amount of carbon dioxide sufiicient to convert said magnesium oxide to magnesium carbonate; (0) heating the carbonated product mixture to remove said alkanol; ((1) adding about 0.9 1 mol of water per mol of magnesium oxide to the alkanol-free mixture; and (e) thereafter heating the aqueous mixture to remove water therefrom, and filtering the water-free product mixture. 2. The method of claim 1 wherein said sulfonate is an alkaryl sulfonate; and the lower alkanol is methanol.

3. The method of claim 2 wherein the aqueous mixture in step (d) is treated with additional carbon dioxide prior to removal of water therefrom.

6 4. The method of claim 2 wherein said alkaryl sulfonate is a polypropylene-alkylated benzene sulfonate in which the polypropylene substituent has a molecular weight of about 290-1500.

5. The method of claim 2 wherein the reaction mixture contains about 2.75-4 mols of magnesium oxide.

References Cited UNITED STATES PATENTS 2,779,784 1/1957 Sharrah 25233 XR 2,856,359 10/1958 Schlicht 25233 2,856,360 10/1958 Schlicht 25233 2,856,361 10/1958 Schlicht 25233 2,881,206 4/1 959 Kjonaas et al. 25233 XR 2,888,279 6/ 1959 Carlyle et al. 25233 XR 3,027,325 3/1962 McMillen et al 25233 PATRICK P. GARVIN, Primary Examiner I. VAUGHN, Assistant Examiner US. Cl. X.R. 25218

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2779784 *May 13, 1954Jan 29, 1957Continental Oil CoBasic alkaline earth metal sulfonates and method of making same
US2856359 *Jul 20, 1956Oct 14, 1958Texas CoSuperbasic alkaline earth metal sulfonates
US2856360 *Jul 20, 1956Oct 14, 1958Texas CoSuperbasic alkaline earth metal sulfonates
US2856361 *Jul 20, 1956Oct 14, 1958Texas CoSuperbasic alkaline earth metal sulfonates
US2881206 *Apr 8, 1957Apr 7, 1959Sinclair Refining CoProcess for preparing stable high detergency barium sulfonates
US2888279 *Aug 23, 1955May 26, 1959Super Oil Seal Mfg Co LtdRailway journal box seal
US3027325 *Nov 7, 1955Mar 27, 1962Lubrizol CorpOil-soluble calcium carbonate dispersions and method of preparation
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4086170 *Feb 1, 1977Apr 25, 1978Labofina S. A.Process for preparing overbased calcium sulfonates
US4179385 *May 3, 1978Dec 18, 1979Tenneco Chemicals, Inc.Process for the production of overbased manganese salts of organic acids
US4225446 *Apr 3, 1978Sep 30, 1980Calumet Industries, Inc.Process for preparing highly basic magnesium sulfonates
US4248718 *Dec 26, 1978Feb 3, 1981Chevron Research CompanyOverbased lubricating oil additive
US4822502 *Apr 1, 1987Apr 18, 1989Nec CorporationImidazoline promoter overbased calcium sulfonates
DE2745202A1 *Oct 7, 1977Apr 13, 1978Labofina SaVerfahren zur herstellung von ueberbasischen calciumsulfonaten
EP0240327A2Mar 31, 1987Oct 7, 1987Exxon Chemical Patents Inc.Cyclic phosphate additives and their use in oleaginous compositions
EP0834544A2 *Sep 26, 1997Apr 8, 1998Chevron Chemical CompanyHigh overbased metal sulfurized alkylphenates
EP2507208A2 *Nov 24, 2010Oct 10, 2012Chevron Oronite Company LLCHighly overbased magnesium alkyltoluene sulfonates
Classifications
U.S. Classification508/396
International ClassificationC07C309/01, C10N30/04, C10M159/24, C07C309/37, C10N40/25, C07C301/00, C10N10/04, C10L1/30, C07C303/32, C07C67/00, C10L1/24
Cooperative ClassificationC10M159/24, C10L10/02, C10M2219/046, C10L1/2437
European ClassificationC10L10/02, C10L1/24C1, C10M159/24