Uop Lcc

Cummins Inc.

David S Lafyatis

Edwin Paul Boldingh

Zhanping Xu

Robert L Mehlberg

Douglas A Nafis

Kurt A Detrick

Sean G Mueller

Eric Leeton

Eric J Baker

Gregory J Schrad

Deng-Yang Jan

Jaime G Moscoso

Bryan K Glover

Antoine Negiz

Aleksey Yezerets

Susan C Koster

Neal W Currier

James A Johnson

Mark Paul Lapinski

Gregory R Werba

Robert B Larson

Avram Michael Buchbinder

Matthew Lippmann

Sriram S Popuri

Paul James Millington

Michael G Gatter

Christian D Freet

Robert W Broach

Edward M Casey

Terrence E Deak

Michael W Penninger

William Shelbourne Epling

Gary A Marr

Processes for increasing an octane value of a gasoline component by dehydrogenating a stream comprising Chydrocarbons and methylcyclohexane in a first dehydrogenation zone to form an intermediate dehydrogenation effluent, and then dehydrogenating the intermediate dehydrogenation effluent in a second dehydrogenation zone to form a Cdehydrogenation effluent. The Cdehydrogenation effluent has an increased olefins content compared to an olefins content of the intermediate dehydrogenation effluent. The first dehydrogenation zone is operated under conditions to convert methylcyclohexane to toluene and minimize cracking reactions. The intermediate dehydrogenation effluent may be heated before being passed to the second dehydrogenation zone.

Processes for increasing an octane value of a gasoline component

Reactor systems for use with ionic liquid catalyst. The reactor systems include one or more stages, which include a reactor and a heat exchanger, and a separation zone. The reactor and the heat exchanger may have a vertical orientation. Additionally, a separation vessel may also include a vertical orientation. The heat exchanger may allow for linear flow of process fluid to control residence time.

Reactor system for use with an ionic liquid catalyst

A process for treating an ionic liquid containing waste stream is described. If there is a liquid waste stream, the liquid waste stream is introduced into a liquid treatment zone. The ionic liquid in the liquid waste stream is neutralized. The concentration of the ionic liquid in the liquid waste stream is determined, and the allowed concentration of the ionic liquid in the liquid waste stream is determined. The concentration of the ionic liquid in the neutralized liquid waste stream is reduced to the allowed concentration, and the liquid waste stream having the allowed concentration is released. If there is a vapor waste stream, the vapor waste stream is introduced into a vapor treatment zone. The vapor waste stream is treated to form a treated vapor waste stream, and the treated vapor waste stream is released to a plant vapor treatment zone.

Ionic liquid waste handling system

A method of controlling a hydrocarbon conversion process is described. The method involves introducing a reactant into a reaction zone containing an ionic liquid catalyst. The reaction zone has at least two zones. The mass transfer resistance in the second zone is greater than the mass transfer resistance in the first zone.

Selectivity of ionic liquid alkylation

The present invention is a process for transalkylating aromatic hydrocarbon compounds, the process comprising introducing an aromatic hydrocarbon feed stream into a transalkylation zone to yield high-purity benzene as a byproduct while meeting transalkylation objectives. The feed stream contacts a catalyst in the transalkylation zone under conditions adjusted to control benzene purity as well as transalkylation performance.

Process for transalkylating aromatic hydrocarbons

An OBD system that diagnoses on board the condition of NOx adsorber catalysts in diesel engines and that relies on existing mass-produced exhaust gas oxygen sensor, also known as lambda sensor, technology, and the following established phenomena. In a reducing environment, typical exhaust gas oxygen (lambda) sensors have different sensitivities to various reductants, with sensitivity decreasing in this order: H&#x3e;CO&#x3e;short-chain hydrocarbons&#x3e;long-chain hydrocarbons. In the process of regeneration of the NOx adsorber catalyst, the original reductant may evolve into a different reductant species, e.g., via reactions such as a water-gas shift (WGS), a reforming, a partial oxidation, etc. This leads to a difference in exhaust gas oxygen sensor readings between the inlet to the catalyst and outlet from the catalyst. It has been observed in diesel engine testing that the ability of the NOx adsorber catalyst to perform such a reductant evolution is correlative to the catalyst's NOx reduction capability.

Method for on-board diagnostics of diesel engine NOx adsorber catalysts

This invention embodies a catalyst and a process for transalkylation of C, C, and Caromatics to obtain a high yield of xylenes. The catalyst comprises a novel UZM-14 catalytic material comprising globular aggregates of crystallites having a MOR framework type with a mean crystallite length parallel to the direction of the 12-ring channels of about 60 nm or less and a mesopore volume of at least about 0.10 cc/gram. The UZM-14 catalyst is particularly active and stable in a transalkylation process.

Transalkylation process

The subject invention comprises an aromatics complex to improve yields from a mixed aromatics feed. Through the use of a novel catalyst having higher activity and stability in a transalkylation unit in the complex, a higher xylene yield is obtained.

Integrated process yielding xylenes from mixed aromatics

Growing community of inventors

Schaumburg, IL, United States of America

David S Lafyatis