Systems and methods for separating hydrocarbons on an internal combustion powered vehicle via one or more metal organic frameworks are disclosed. Systems and methods can further include utilizing separated hydrocarbons and exhaust to generate hydrogen gas for use as fuel.

Systems and methods for separating hydrocarbons on an internal combustion powered vehicle via one or more metal organic frameworks are disclosed. Systems and methods can further include utilizing separated hydrocarbons and exhaust to generate hydrogen gas for use as fuel.

Processes to selectively crack alkyne compounds from a hydrocarbon stream including olefinic and di-olefinic compounds are described. The process includes contacting the hydrocarbon stream with a supported CuO catalyst under conditions sufficient to crack the alkynes to form a product stream that included cracked compounds and further separating the cracked organic compounds from the hydrocarbon stream.

Processes to selectively crack alkyne compounds from a hydrocarbon stream including olefinic and di-olefinic compounds are described. The process includes contacting the hydrocarbon stream with a supported CuO catalyst under conditions sufficient to crack the alkynes to form a product stream that included cracked compounds and further separating the cracked organic compounds from the hydrocarbon stream.

Processes incorporating a common organic chloride decomposition reactor and chloride treater to be used by both the C.sub.4 and C.sub.5-6 isomerization reaction zones are described. A portion of the C.sub.4 isomerization reaction zone off gas is routed to the C.sub.4 HCl absorber, which provides about 85% of the HCl requirement for the C.sub.4 isomerization reaction zone. A small amount of the C.sub.5-6 isomerization reaction zone off gas is mixed with the C.sub.4 isomerization reaction zone off gas portion going to the C.sub.4 HCl absorber.

Processes incorporating a common organic chloride decomposition reactor and chloride treater to be used by both the C.sub.4 and C.sub.5-6 isomerization reaction zones are described. A portion of the C.sub.4 isomerization reaction zone off gas is routed to the C.sub.4 HCl absorber, which provides about 85% of the HCl requirement for the C.sub.4 isomerization reaction zone. A small amount of the C.sub.5-6 isomerization reaction zone off gas is mixed with the C.sub.4 isomerization reaction zone off gas portion going to the C.sub.4 HCl absorber.

This invention is directed to transition metal-based-halloysite nanocomposites and methods of making and using the same.

This invention is directed to transition metal-based-halloysite nanocomposites and methods of making and using the same.

Disclosed herein are processes for producing neopentane. The processes generally relate to demethylating isooctane to produce neopentane. The isooctane may be provided by the alkylation of isobutane with butylenes.

Disclosed herein are processes for producing neopentane. The processes generally relate to demethylating isooctane to produce neopentane. The isooctane may be provided by the alkylation of isobutane with butylenes.