Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
214 words
A process for making an extreme pressure lubricant additive comprising the steps of: (a) reacting sulfur monochloride with from about 1 to 2 moles of isobutylene per mole of sulfur monochloride at a temperature of from about 20° C. to about 80° C.; (b) reacting the product produced in step (a) with an alkali metal monosulfide and free sulfur in a ratio of moles of alkali metal monosulfide to gram-atoms of free sulfur from about 1.8 to about 2.2:1; (c) reacting the product produced in step (b) with an aqueous solution containing from about 5 to about 20 percent of an alkali metal hydroxide for a time sufficient to reduce the chlorine content below about 0.5 percent; and (d) reacting the sulfurized isobutylene produced in step (c) with a mild oxidizing agent in a mole ratio of oxidizing agent to sulfurized isobutylene of between about 0.5 and about 2.5 moles of equivalent oxygen to 1 mole of sulfurized isobutylene at a reaction temperature between about 20° C. and about 95° C. under conditions sufficient to effect the appearance of new infrared frequency bands at 1300 cm -1 and 1030 cm -1 indicative of the formation of sulfoxides and sulfones and recovering a liquid oxidized sulfurized isobutylene product which is soluble in a lubricating composition.
Claim 2
Dependent Claim
214 words
A process for making an extreme pressure lubricant additive comprising the steps of: (a) reacting sulfur monochloride with from about 1 to 2 moles of isobutylene per mole of sulfur monochloride at a temperature of from about 20° C. to about 80° C.; (b) reacting the product produced in step (a) with an alkali metal monosulfide and free sulfur in a ratio of moles of alkali metal monosulfide to gram-atoms of free sulfur from about 1.8 to about 2.2:1; (c) reacting the product produced in step (b) with an aqueous solution containing from about 5 to about 20 percent of an alkali metal hydroxide for a time sufficient to reduce the chlorine content below about 0.5 percent; and (d) reacting the sulfurized isobutylene produced in step (c) with a mild oxidizing agent in a mole ratio of oxidizing agent to sulfurized isobutylene of between about 0.5 and about 2.5 moles of equivalent oxygen to 1 mole of sulfurized isobutylene at a reaction temperature between about 20° C. and about 95° C. under conditions sufficient to effect the appearance of new infrared frequency bands at 1300 cm -1 and 1030 cm -1 indicative of the formation of sulfoxides and sulfones and recovering a liquid oxidized sulfurized isobutylene product which is soluble in a lubricating composition.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein the mole ratio of isobutylene to sulfur monochloride is from about 1.25 to about 1.8:1.
Claim 4
Dependent Claim
22 words
The process of claim 1 wherein the sulfurized isobutylene produced in step (c) contains from about 4 to about 60 percent sulfur.
Claim 5
Dependent Claim
22 words
The process of claim 3 wherein the sulfurized isobutylene produced in step (c) contains from about 46 to about 50 percent sulfur.
Claim 6
Dependent Claim
53 words
The process of claim 1 wherein the sulfurized isobutylene is produced by reacting sulfur monochloride with from about 1.25 to about 1.8:1 moles of isobutylene per mole of sulfur monochloride, reacting the product of that reaction with an alkali metal monosulfide and 0.5 gram-atoms of free sulfur per mole of alkali metal monosulfide.
Claim 7
Dependent Claim
34 words
The process of claim 5 wherein the sulfurized isobutylene is dissolved in a carrier liquid selected from the group consisting of benzene, toluene, xylenes and others which do not react with the oxidizing agent.
Claim 8
Dependent Claim
29 words
The process of claim 6 wherein the oxidizing agent is an aqueous solution of a per acid selected from the group consisting of perchloric, permanganic, permonosulfuric and persulfuric acid.
Claim 9
Dependent Claim
13 words
The process of claim 1 wherein the alkali metal monosulfide is sodium hydroxide.
Claim 10
Dependent Claim
13 words
The process of claim 1 wherein the alkali metal monosulfide is sodium sulfide.
Claim 11
Dependent Claim
27 words
The process of claim 1 wherein the mole ratio of alkali metal monosulfide to the product produced in step (a) is from about 0.8 to about 1.0:2.
Claim 12
Dependent Claim
28 words
The process of claim 1 wherein the alkali metal monosulfide and sulfur are reacted with the product produced in step (a) in the presence of a water-soluble alcohol.
Claim 13
Dependent Claim
34 words
The process of claim 1 wherein the sulfurized isobutylene is dissolved in a carrier liquid selected from the group consisting of benzene, toluene, xylenes and others which do not react with the oxidizing agent.
Claim 14
Dependent Claim
16 words
The process of claim 1 wherein the oxidizing agent is an aqueous solution of hydrogen peroxide.
Claim 15
Dependent Claim
21 words
The process of claim 12 wherein the aqueous solution of hydrogen peroxide is acidified before being reacted with the sulfurized isobutylene.
Claim 16
Dependent Claim
16 words
The process of claim 1 wherein the recovered reaction product is purified by washing With water.
Claim 17
Dependent Claim
18 words
The process of claim 1 wherein the oxidizing agent is an aqueous solution of potassium or sodium permanganate.
Claim 18
Dependent Claim
18 words
The process of claim 1 wherein the oxidizing agent is an aqueous solution of potassium or sodium dichromate.
Claim 19
Dependent Claim
18 words
The process of claim 1 wherein the oxidizing agent is an aqueous solution of potassium or sodium iodate.
Claim 20
Dependent Claim
18 words
The process of claim 1 wherein the oxidizing agent is an aqueous solution of potassium or sodium perborate.
Claim 21
Dependent Claim
29 words
The process of claim 1 wherein the oxidizing agent is an aqueous solution of a per acid selected from the group consisting of perchloric, permanganic, permonosulfuric and persulfuric acid.