Uop Lcc

Phuong T M Do

Alakananda A Bhattacharyya

Beckay J Mezza

Stephen C Houdek

Lance Awender Baird

Fred G Sollberger

Timothy A Brandvold

Hayim Abrevaya

Nancy E Iwamoto

Avram Michael Buchbinder

Mark Van Wees

Ping Sun

Grant H Yokomizo

A process using a dealkylated aromatic liquid improves a heavy hydrocarbon liquid used for supporting molybdenum carbonized catalyst. Dealkylated aromatic liquid can be derived from heavy hydrocarbon materials that have been subjected to cracking, such as fluid catalytic cracking or slurry hydrocracking. The heavy hydrocarbon liquid can comprise a portion of resid SHC feed and a portion of a gas oil stream from SHC effluent.

Process for making and using metal catalyst for slurry hydrocracking

A process is disclosed for using an iron oxide and alumina catalyst with no more than more than about 55 wt % of the alumina in the diaspore phase or in the alpha phase in SHC. Alpha alumina is less effective catalyst component for slurry hydrocracking in terms of TIOR conversion. Drying procedures should avoid more than about 51 wt % of the alumina change to the alpha phase. The SHC catalyst is for converting heavy hydrocarbon feed into lighter hydrocarbon products.

Process for slurry hydrocracking using catalyst with low diaspore alumina

A process and catalyst is disclosed for converting heavy hydrocarbon feed into lighter hydrocarbon products using multifunctional catalysts. Multifunctional catalysts enable use of less expensive metal by substituting expensive metals for less expensive metals with no loss or superior performance in slurry hydrocracking. Less available and expensive ISM can be replaced effectively.

Process for using iron and molybdenum catalyst for slurry hydrocracking

Process for using iron and particulate carbon catalyst for slurry hydrocracking

Process for using molybdenum and particulate carbon catalyst for slurry hydrocracking

Process for using and composition of iron, molybdenum and particulate carbon catalyst for slurry hydrocracking

A process and catalyst is disclosed for converting a heavy hydrocarbon feed stream into lighter hydrocarbon products using a two component catalyst. The catalyst comprises iron and molybdenum containing catalyst. Alumina may be a third catalyst component. The molybdenum is present in the heavy hydrocarbon feed stream at about 500 wppm or less and the weight ratio of iron to the molybdenum is less than 5. Much lower concentrations of expensive molybdenum can be used due to the addition of iron in the catalyst.

Process for making and using iron and molybdenum catalyst for slurry hydrocracking

A process of making terephthalic acid or a derivative of terephthalic acid is described. The process includes reacting a derivative of 2,5-dimethylfuran, with a dienophile containing an unsaturated 2-carbon unit, in the presence of a catalyst having Br&#xf6;nsted acidity to form a para-xylene derivative; and optionally reacting the para-xylene derivative to terephthalic acid.

Processes and catalysts for conversion of 2,5-dimethylfuran derivatives to terephthalate

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Des Plaines, IL, United States of America

Phuong T M Do