Uop Lcc

Daniel James Pintar

Gavin Paul Towler

Xin X Zhu

Richard K Hoehn

Vasant P Thakkar

Ping Sun

Grant H Yokomizo

James P Glavin

John J Jeanneret

Dorothy M Richmond

Jeffrey M Bray

Pamela Roxas

A method of reducing catalyst agglomeration in a slurry hydrocracking zone containing at least two reactors is described. A hydrocarbon feed and a slurry hydrocracking catalyst are contacted in a first reactor to form a first effluent containing slurry hydrocracking reaction products, unreacted hydrocarbon feed, and the slurry hydrocracking catalyst, wherein the slurry hydrocracking catalyst agglomerates. The first effluent and an unsupported hydrogenation catalyst are contacted in a second reactor to form a second effluent containing the slurry hydrocracking reaction products, unreacted hydrocarbon feed, the slurry hydrocracking catalyst, and asphaltene reaction products.

Staged introduction of additives in slurry hydrocracking process

Disclosed are methods and systems for manufacturing lubrication oils. In one embodiment, a method for manufacturing a lubrication oil includes the steps of receiving into an activated carbon guard bed unit an unconverted oil (UCO) feedstock, the UCO feedstock comprising polynuclear aromatic (PNA) compounds and contacting the UCO feedstock with activated carbon within the activated carbon guard bed unit to remove at least a portion of the PNA compounds, thereby forming a treated UCO feedstock.

Methods and systems for manufacturing lubrication oils

Methods of maximizing diesel production are describes. The methods include providing a stream of heavy heavy naphtha; and blending the stream of heavy heavy naphtha with a diesel stream from the crude distillation zone to increase diesel production while maintaining the blended diesel stream within a specification for diesel. Various apparatus for maximizing diesel production are also described.

Process for maximizing diesel production using a heavy heavy naphtha stream

A process for filtering a liquid stream from a fixed bed reaction zone in order to remove catalyst fines contained in the stream. The effluent stream is passed to a filtering section which may contain at least two filtering vessels. Each filtering vessel includes at least two differently filtering sections, each section designed to collect differently sized particles. If a pressure drop occurs in one of the filtering vessels, it may be taken offline to remove the filtering sections and recover the metal in the particles collected on the filtering sections. The other filtering vessel can remain online to allow the filtering process to be continuous. Metal on the catalyst fines may be recovered.

Process for removing catalyst fines from a liquid stream from a fixed bed reactor

An integrated slurry hydrocracking process and apparatus are described. The process includes introducing heavy residual hydrocarbon oil and a hydrogen stream into a slurry hydrocracking zone. The hydrocarbon feed is cracked to form a slurry hydrocracking effluent. At least a portion of the shiny hydrocracking effluent is introduced to a distillate hydrotreater along with make-up hydrogen. The slurry hydrocracking effluent is hydrotreated to form a hydrotreated effluent. The hydrotreated effluent is separated into a liquid stream and a gas stream containing hydrogen. The gas stream containing the hydrogen is recycled to the slurry hydrocracking zone forming the hydrogen stream introduced into the slurry hydrocracking zone.

Growing community of inventors

Hoffman Estates, IL, United States of America

Daniel James Pintar