John Anthony Petri, 57Tomah, WI

6709640, Mar 23, 2004

Nov 28, 2000

09/724232

Jacques J. L. Romatier - Riverwoods IL
John A. Petri - Palatine IL

UOP LLC - Des Plaines IL

F28F 300

422200, 422198, 165166, 165173, 165DIG 355, 165DIG 356

A process and apparatus for indirectly exchanging heat with narrow channel in a heat exchange type reaction zone uses manifold space to interconnect the common ends of channels and to provide controlled distribution of additional reactants. The invention simplifies the operation and construction of the heat exchanging type reaction zone by directly communicating reaction channels and/or heating channels with a manifold located at the end of the channels. The manifold can provides the extra function of mixing additional reactants. The invention promotes simplified intermediate injection of reactants over tube and shell heat transfer arrangements that have been used for similar purposes. Improved process control has particular benefits for exothermic reactions. The narrow channels are preferably defined by corrugated plates. The reaction channels will contain a catalyst for the promotion of the primary reaction.

7511181, Mar 31, 2009

Feb 25, 2008

12/036553

John A. Petri - Palatine IL, US
Terry L. Marker - Palos Heights IL, US

UOP LLC - Des Plaines IL

C07C 1/20

585240, 585241

A process has been developed for producing a hydrocarbon component useful as diesel fuel from biorenewable feedstocks such as plant oils and greases. The process involves hydrogenating and deoxygenating, i. e. decarboxylating and/or hydrodeoxygenating the feedstock to provide a hydrocarbon fraction useful as a diesel fuel. An optional pretreatment step to remove contaminants such as alkali metals from the feedstock can also be carried out. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties.

7578927, Aug 25, 2009

Aug 31, 2006

11/468813

Terry L. Marker - Des Plaines IL, US
John A. Petri - Des Plaines IL, US

UOP LLC - Des Plaines IL

C10G 1/00

208 67, 585242

A process for the conversion of biomass to a liquid fuel is presented. The process includes the production of diesel and naphtha boiling point range fuels by hydrocracking of pyrolysis lignin extracted from biomass.

7799209, Sep 21, 2010

Jun 29, 2007

11/771136

John A. Petri - Palatine IL, US

UOP LLC - Des Plaines IL

C10G 11/20

208113

Disclosed is a process for recovery power from an FCC product. Gaseous hydrocarbon product from an FCC reactor is heat exchanged with a heat exchange media which is delivered to an expander to generate power. Cycle oil from product fractionation may be added to the gaseous FCC product to wash away coke precursors.

7799288, Sep 21, 2010

Jun 29, 2007

11/771224

John A. Petri - Des Plaines IL, US

UOP LLC - Des Plaines IL

F27B 15/14

422146, 422147, 60721

An apparatus for recovery power from an FCC product is described. Gaseous hydrocarbon product from an FCC reactor is heat exchanged with a heat exchange media which is delivered to an expander to generate power. Cycle oil from product fractionation may be added to the gaseous FCC product to wash away coke precursors.

8008534, Aug 30, 2011

Jun 30, 2008

12/165444

John Anthony Petri - Palatine IL, US
Peter Kokayeff - Naperville IL, US

UOP LLC - Des Plaines IL

C10G 51/02

585263, 208 46, 208 49

A method of hydroprocessing hydrocarbons is provided using a substantially liquid-phase reactor having first and second catalyst beds with a heat transfer section positioned therebetween. The first and second catalyst beds and the heat transfer section are combined within the same reactor vessel. Each catalyst bed having an inlet temperature and an exit temperature and having a hydroprocessing catalyst therein with a maximum operating temperature range. The method hydroprocesses the hydrocarbons and removes sufficient heat from the hydrocarbons using the heat transfer section so that the exit temperature of the hydrocarbons existing the first catalyst bed is substantially maintained below the maximum operating temperature range of the hydroprocessing catalysts in the first bed and, at the same time, also providing the hydrocarbons to the second catalyst bed at the inlet temperature so that the exit temperature of the hydrocarbons at the exit of the second catalyst bed also does not exceed the maximum operating temperature range of the hydroprocessing catalyst in the second bed.

8110092, Feb 7, 2012

Aug 23, 2010

12/860959

John A. Petri - Palatine IL, US

UOP LLC - Des Plaines IL

C10G 11/20

208113, 208114, 208115, 208116, 208117, 208118, 208119, 208121, 208122, 208123, 208124

Disclosed is a process for recovery power from an FCC product. Gaseous hydrocarbon product from an FCC reactor is heat exchanged with a heat exchange media which is delivered to an expander to generate power. Cycle oil from product fractionation may be added to the gaseous FCC product to wash away coke precursors.

8221706, Jul 17, 2012

Jun 30, 2009

12/495601

John A. Petri - Palatine IL, US
Vedula K. Murty - Willowbrook IL, US
Peter Kokayeff - Naperville IL, US

UOP LLC - Des Plaines IL

B01J 8/00
C07C 5/00

422600, 585250, 585251, 585265, 585310, 585314, 585315

Apparatuses for processing a hydrocarbonaceous feedstock flows are provided. In one aspect, the method includes providing two or more hydroprocessing stages disposed in sequence, each hydroprocessing stage having a hydroprocessing reaction zone with a hydrogen requirement and each stage in fluid communication with the preceding stage. A hydrogen source is provided substantially free of hydrogen from a hydrogen recycle compressor. The hydrocarbonaceous feedstock flow is separated into an portions of fresh feed for each hydroprocessing stage, and the first portion of fresh feed to the first hydroprocessing stage is heated. The heated first portion of fresh feed is supplied with hydrogen from the hydrogen source in an amount satisfying substantially all of the hydrogen requirements of the hydroprocessing stages to a first hydroprocessing zone. The unheated second portion of fresh feed is admixed with effluent from previous stage to quench the hot reactor effluent before entering a second stage.