Production of stilbene and styrene

Claim 2

A process for producing stilbene and stilbene derivatives free of polar impurities from toluene and toluene derivatives as the starting hydrocarbon which comprises: a. effecting dehydrocoupling of toluene and toluene derivatives in the vapor phase in the presence of a solid metal oxide selected from the group consisting of the oxides of lead, cadmium and bismuth and mixtures thereof at a temperature in the range of from about 500°C to about 650°C, b. separating the dehydrocoupling effluent by distillation to provide a stilbene fraction, c. treating said stilbene fraction to remove polar impurities by either (1) passing it through a bed of an absorbent material capable of adsorbing polar impurities at a temperature in the range of from 75° to 200°C and at such a rate to provide a contact time of the stilbene and absorbent material of from 0.1 second to 15 minutes, or (2) intimately contacting it with a chemical treating agent selected from the group consisting of alkali metals, alkyl aluminums, aluminum alkoxides, Grignard reagents, metal hydrides, phenyllithium and disodium stilbene, or (3) distilling it to remove all compounds boiling below 128°C, and cooling the distillation residue to effect crystallization; and d. recovering said stilbene fraction substantially free of polar impurities.

Claim 3

The process of claim 1 wherein the metal oxide is PbO.

Claim 4

The process of claim 2 wherein said stilbene fraction is trans-stilbene which is treated by passing it through a bed of activated alumina at a temperature in the range from 125° to 150°C.

Claim 5

The process of claim 2 wherein said stilbene fraction is treated by intimately contacting it with a chemical treating agent and said chemical treating agent is aliminum isopropoxide.

Claim 6

The process of claim 1 wherein said metal oxide is supported on a solid carrier selected from the group consisting of silica, alumina, silica-alumina and metal silicates.

Claim 7

The process of claim 5 wherein the solid carrier is MgAl 2 O 4 spinel.

Claim 8

The process of claim 5 wherein said metal oxide is PbO.

Claim 9

The process of claim 6 wherein the metal oxide is PbO.

Claim 10

The process of claim 6 wherein the MgAl 2 O 4 spinel has a surface area of from 0.01 to 10 m 2 /gram.

Claim 11

The process of claim 1 wherein the dehydrocoupling effluent is separated to produce at least three fractions, an unreacted toluene fraction, a cis-stilbene and bibenzyl fraction and a trans-stilbene fraction.

Claim 12

The process of claim 10 wherein the unreacted toluene and cis-stilbene and bibenzyl fractions are recycled to the dehydrocoupling reaction.

Claim 13

The process of producing styrene from toluene as the starting hydrocarbon which comprises: a. effecting dehydrocoupling of toluene in the vapor phase in the presence of PbO at a temperature in the range of 500° to 650°C, b. separating the dehydrocoupling effluent by distillation to provide a liquid stilbene fraction, c. treating said stilbene fraction to remove polar impurities therefrom by either (1) passing it through a bed of an adsorbent material capable of adsorbing polar impurities at a temperature in the range of from 75° to 200°C and at such a rate to provide a contact time of the stilbene and adsorbent material of from 0.1 second to 15 minutes, or (2) intimately contacting it with a chemical treating agent selected from the group consisting of alkali metals, alkyl aluminums, aluminum alkoxides, Grignard reagents, metal hydrides, phenyllithium and disodium stilbene, or (3) distilling it to remove all compounds boiling below 128°C, and cooling the distillation residue to effect crystallization; d. recovering said stilbene fraction substantially free of polar impurities, e. effecting reaction of said recovered stilbene fraction in the vapor phase with ethylene in the presence of a disproportionation catalyst at a temperature in the range from 350° to 500°C, and f. separating and recovering styrene from the catalytic reaction.

Claim 14

The process of producing styrene from toluene as the starting hydrocarbon which comprises: a. effecting dehydrocoupling of toluene in the vapor phase in the presence of PbO at a temperature in the range of 500° to 650°C, b. separating the dehydrocoupling effluent by distillation to provide a liquid stilbene fraction, c. treating said stilbene fraction to remove polar impurities therefrom by either (1) passing it through a bed of an adsorbent material capable of adsorbing polar impurities at a temperature in the range of from 75° to 200°C and at such a rate to provide a contact time of the stilbene and adsorbent material of from 0.1 second to 15 minutes, or (2) intimately contacting it with a chemical treating agent selected from the group consisting of alkali metals, alkyl aluminums, aluminum alkoxides, Grignard reagents, metal hydrides, phenyllithium and disodium stilbene, or (3) distilling it to remove all compounds boiling below 128°C, and cooling the distillation residue to effect crystallization; d. recovering said stilbene fraction substantially free of polar impurities, e. effecting reaction of said recovered stilbene fraction in the vapor phase with ethylene in the presence of a disproportionation catalyst at a temperature in the range from 350° to 500°C, and f. separating and recovering styrene from the catalytic reaction.

Claim 15

The process of claim 12 wherein said stilbene fraction is trans-stilbene which is treated by passing it through a bed of activated alumina at a temperature in the range from 125° to 150°C.

Claim 16

The process of claim 12 wherein said stilbene fraction is treated by intimately contacting it with a chemical treating agent and said chemical treating agent is aluminum isopropoxide.

Claim 17

The process of claim 12 wherein said stilbene fraction is treated by contacting it with a chemical treating agent and said chemical treating agent is disodium stilbene dissolved in tetrahydrofuran.

Claim 18

The process of claim 12 wherein said disproportionation catalyst is WO 3 on SiO 2 .

Claim 19

The process of claim 12 wherein the PbO is supported on a solid carrier selected from the group consisting of silica, alumina, silica-alumina and metal silicates.

Claim 20

The process of claim 17 wherein the solid carrier is MgAl 2 O 4 spinel.

Claim 21

The process of claim 18 wherein the spinel has a surface area of from 0.01 to 10 m 2 /gram.

Claim 22

The process of claim 12 wherein the dehydrocoupling effluent is separated by distillation to produce at least three fractions, a benzene fraction, an unreacted toluene -cis-stilbene - bibenzyl containing fraction, and a trans-stilbene fraction.

Claim 23

The process of claim 18 wherein the unreacted toluene and cis-stilbene and bibenzyl are recycled to the dehydrocoupling step.

Claim 24

The process of claim 21 wherein the cis-stilbene fraction is isomerized to trans-stilbene and is then passed through the absorbent bed.

Claim 25

The process of claim 2 wherein said stilbene fraction is treated by intimately contacting it with a chemical treating agent and said chemical treating agent is disodium stilbene dissolved in tetrahydrofuran.