Method for producing low-odor n-butane
View Patent ↗The invention relates to a method for producing low-odor n-butane by catalytic hydrogenation of a feed mixture. The aim of the invention is to provide such a method, wherein the feed material, in addition to n-butane, n-butene and up to 1 mass % formic acid and/or up to 1 mass % pentanals and/or up to 0.5 mass % pentanols, also comprises carbon monoxide. The aim is achieved by treating the feed mixture in the temperature range of 15 to 120° C. with an aqueous solution of an alkali metal or alkaline earth metal hydroxide in the concentration range of 0.5 to 30 mass % and subsequently subjecting the feed mixture to the catalytic hydrogenation.
1. A process for preparing low-odor n-butane, the process comprising:
mixing a n-butane feedstock with an aqueous solution comprising an alkali metal hydroxide or an alkaline earth metal hydroxide to obtain a biphasic mixture; allowing the biphasic mixture to separate into an aqueous phase comprising a formate salt of the alkali metal or alkaline earth metal and an n-butane phase consisting essentially of n-butane, n-butenes and water;
separating the aqueous phase from the n-butane phase;
removing the water from the n-butane phase to obtain an anhydrous mixture of n-butane and n-butenes; and
catalytically hydrogenating the anhydrous mixture to obtain the low odor n-butane;
wherein
a temperature of the biphasic mixture is from 15 to 120° C., and
wherein
the n-butane feedstock comprises n-butene, carbon monoxide, and formic acid in a content of from 0.001 to 1% by mass, and
a content of the alkali metal hydroxide or alkaline earth metal hydroxide in the aqueous solution is from 0.5 to 30% by mass.
2. The process of claim 1 ,
wherein the aqueous solution comprises sodium hydroxide in a concentration of from 0.5 to 2.5% by mass.
3. The process of claim 1 ,
wherein a pressure of the mixing and separation is from 0.5 to 5 MPa.
4. The process of claim 1 ,
wherein a proportion of carbon monoxide in the n-butane feedstock is from 1 to 10% by mass.
5. The process of claim 1 ,
wherein the n-butane feedstock further comprises hydrogen.
6. The process of claim 1 ,
wherein the mixing and separation comprises extracting in a mixer-settler unit.
7. The process of claim 6 ,
wherein the mixer-settler unit is a static mixer.
8. The process of claim 6 ,
wherein the mixer-settler unit is a pump.
9. The process of claim 1 ,
wherein the mixing and separation comprises extracting in an extraction column.
10. The process of claim 1 ,
wherein the extracted mixture is entirely or partly liquid.
11. The process of claim 1 ,
wherein catalytically hydrogenating the anhydrous mixture comprises hydrogenating in a liquid phase over a palladium catalyst at a temperature of from 20 to 140° C. and at a pressure of from 0.6 to 3 MPa.
12. The process of claim 1 , wherein removing the water comprises distillation.
13. The process of claim 1 ,
further comprising dewatering the low odor n-butane by distillation, to obtain a dewatered output.
14. The process of claim 1 ,
further comprising removing C 5 hydrocarbons from the n-butane phase or the low-odor n-butane by distillation.
15. The process of claim 1 ,
wherein the n-butane feedstock is a stream from a C 4 hydroformylation.
16. The process of claim 4 , wherein the proportion of carbon monoxide in the n-butane feedstock is from 2 to 7% by mass.
17. The process of claim 8 , wherein the mixer-settler unit is a centrifugal pump.
18. The process of claim 1 , wherein a content of linear butane in the n-butane feedstock is below 30% by mass.
19. The process of claim 1 , wherein the aqueous solution is a sodium hydroxide solution, a potassium hydroxide solution, or both.
20. The process of claim 13 , further comprising removing C 5 hydrocarbons from the low-odor n-butane or the dewatered output by distillation.