# US 5,347,018 A · Process for producing sulfolane compounds

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- Number: US 5,347,018 A
- Document ID: US5347018A
- Status: Granted
- Kind: A
- Application number: 08/127,615
- Filed: 1993-09-28
- Granted: 1994-09-13
- Earliest claimed: 1993-09-28
- Assignees: Phillips Petroleum Company
- Inventors: Earl Clark, Jr.; Howard F. Efner; Jimmie J. Straw
- Web page: https://patentgrep.com/patent/US5347018A

## CPC

- C07D 333/48: by oxygen atoms
- C07D: HETEROCYCLIC COMPOUNDS (macromolecular compounds C08)

## Abstract

A process for producing sulfolane compounds is provided which comprises: (1) contacting a conjugated diene with sulfur dioxide under conditions sufficient to synthesize a sulfolene compound whereby a mixture of the sulfolene compound and impurities comprising unreacted sulfur dioxide is produced; (2) transferring the mixture to an impurities removal vessel containing a freezing point depressant which comprises an aromatic compound; (3) removing the impurities; (4) transferring the impurities-reduced sulfolene compound to a hydrogenation reactor; (5) contacting the impurities-reduced sulfolene compound with hydrogen, in the presence of a hydrogenation catalyst, under conditions sufficient to produce a sulfolane compound; and (6) optionally recovering the sulfolane compound.

## Claims

### Claim 1

A process comprising: (1) contacting a conjugated diene with sulfur dioxide under conditions sufficient to synthesize a mixture of a sulfolene compound and impurities; (2) transferring said mixture to an impurities removal vessel; (3) contacting said mixture of sulfolene compound and impurities with a freezing point depressant; (4) substantially removing said impurities to produce an impurities-reduced sulfolene compound; and (5) hydrogenating said impurities-reduced sulfolene compound under conditions sufficient to produce a sulfolane compound; wherein said impurities comprise unreacted sulfur dioxide; said freezing point depressant comprises an aromatic compound selected from the group consisting of naphthalenes, methylnaphthalenes, biphenyl, a derivative of benzene, and combinations of two or more thereof; said derivative of benzene is selected from the group consisting of alkyl, alkenyl, amino, halo, alkaryl, and alkaryl-aromatic compounds and is liquid at about 20.degree.-30.degree. C.; and said freezing point depressant is present in an amount sufficient to keep said sulfolene compound in liquid state.

### Claim 2 (depends on 1)

A process according to claim 1 wherein said conjugated diene has the formula of R--C(R).dbd.C(R)--C(R).dbd.C(R)--R; wherein each R can be the same or different and is independently selected from the group consisting of hydrogen, hydroxyl radical, a hydrocarbyl radical, and mixtures -thereof; wherein said hydrocarbyl radical is selected from the group consisting of akyl, alkenyl, aryl, cycloalkyl, cycloalkenyl, aralkyl, alkaryl, alkylcycloalkyl, and combinations of two or more thereof.

### Claim 3 (depends on 2)

A process according to claim 2 wherein said conjugated diene is selected from the group consisting of 1,3-butadiene, 2-methyl-1,3-butadiene, 2,3-dimethyl-1,3-butadiene, 2,3-diethyl-1,3-butadiene, 3,4-dimethyl- 2,4-hexadiene, 2,4-dodecadiene, 2-methyl-1,3-hexadiene, 4-ethyl-1,3-hexadiene, 1-cyclopentyl-1,3-pentadiene, 1-(1-cyclohexene-1-yl)-1,3-butadiene, 2-phenyl-1,3-butadiene, 3-benzyl-1,3-pentadiene, 3-p-tolyl-1,3-pentadiene and combinations of two or more thereof.

### Claim 4 (depends on 3)

A process according to claim 3 wherein said conjugated diene is 1,3-butadiene.

### Claim 5 (depends on 1)

A process according to claim 1 wherein said freezing point depressant is selected from the group consisting of toluene, xylenes, naphthalenes, methylnaphthalenes, biphenyl, derivatives thereof, and combinations of two or more thereof.

### Claim 6 (depends on 5)

A process according to claim 5 wherein said freezing point depressant is toluene.

### Claim 7 (depends on 1)

A process according to claim 1 wherein said freezing point depressant further comprises a sulfone compound selected from the group consisting of sulfolane, 3-methylsulfolane, 2,4-dimethylsulfolane, 3-ethylsulfolane, and combinations of two or more thereof.

### Claim 8 (depends on 1)

A process according to claim 1 wherein the weight ratio of said freezing point depressant to said sulfolene compound is in the range of from about 1:0.001 to about 1:100.

### Claim 9 (depends on 8)

A process according to claim 8 wherein said range is from about 1:0.05 to about 1:50.

### Claim 10 (depends on 9)

A process according to claim 9 wherein said range is from 0.1 to 1:20.

### Claim 11 (depends on 1)

A process according to claim 1 wherein said sulfolene compound is contacted with said freezing point depressant at a temperature in the range of from about 25.degree. C. to about 100.degree. C.

### Claim 12 (depends on 11)

A process according to claim 11 wherein said range is from about 35.degree. C. to about 80.degree. C.

### Claim 13 (depends on 12)

A process according to claim 12 wherein said range is from 45.degree. C. to 70.degree. C.

### Claim 14 (depends on 1)

A process according to claim 1 wherein said sulfolene compound is contacted with said freezing point depressant under a pressure in the range of from about 0.001 to about 35 atmospheres.

### Claim 15 (depends on 14)

A process according to claim 14 wherein said range is from about 0.01 to about 20 atmospheres.

### Claim 16 (depends on 15)

A process according to claim 15 wherein said range is from 0.1 to 7 atmospheres.

### Claim 17

A process for preparing a sulfolane compound comprising: (1) reacting a conjugated diene with sulfur dioxide at a temperature in the range of from about 60.degree. C. to about 120.degree. C. under a pressure in the range of from about 20 psig to about 300 psig for about 2 hours to about 24 hours whereby a mixture of sulfolene compound and impurities comprising unreacted sulfur dioxide is produced; wherein said conjugated diene is selected from the group consisting of 1,3-butadiene, 2-methyl- 1,3-butadiene, 2,3-dimethyl- 1,3-butadiene, 2,3-diethyl- 1,3-butadiene, 3,4-dimethyl-2,4-hexadiene, 2,4-dodecadiene, 2-methyl-1,3-hexadiene, 4-ethyl- 1,3-hexadiene, 1-cyclopentyl-1,3-pentadiene, 1-(1-cyclohexene-1-yl)-1,3-butadiene, 2-phenyl-1,3- butadiene, 3-benzyl-1,3-pentadiene, 3-p-tolyl-1,3-pentadiene, and their homologues and analogues, and mixtures thereof; (2) transferring said mixture at a temperature in the range of from about 25.degree. C. to about 100.degree. C. to an impurities removal vessel wherein said vessel contains a freezing point depressant selected from the group consisting of benzene, toluene, xylenes, sulfolane, 3-methylsulfolane, 2,4-dimethylsulfolane, 3-ethylsulfolane, naphthalenes, methylnaphthalenes, biphenyl, derivatives thereof, and combinations of two or more thereof; (3) removing said impurities to produce an impurities-reduced sulfolene compound; (4) transferring said impurities-reduced sulfolene compound to a hydrogenation reactor; (5) contacting said impurities-reduced sulfolene compound with hydrogen, in the presence of a hydrogenation catalyst under hydrogenation conditions sufficient to produce said sulfolane compound.

### Claim 18

A process for producing sulfolane comprising: (1) contacting 1,3-butadiene with sulfur dioxide at 65.degree. C. to 80.degree. C. under 30 psig to l.20 psig to produce a mixture of sulfolene and impurities comprising unreacted sulfur dioxide; (2) transferring at said mixture to an impurities removal reactor which contains toluene; (3) removing said impurities to produce an impurities-reduced sulfolene; (4) transferring said impurities-reduced sulfolene to a hydrogenation reactor; (5) contacting said impurities-reduced sulfolene compound with hydrogen, in the presence of a hydrogenation catalyst.

### Claim 19 (depends on 7)

A process according to claim 7 wherein said sulfone compound is sulfolane.
