Synfuels International, Inc.

Other

The Dow Chemical Company

Peterson, Edward R.

Rolfe, Thomas Agnew

Nitti, Michael Christopher

Edward R Peterson

Sean C Gattis

Marvin M Johnson

Joel G Cantrell

Duane Morrow

David A Babb

Gerald M Lancaster

Katherine S Clement

W Frank Richey

Donald J Perettie

Zdravko P Jezic

Larry D Bratton

Alvin P Kennedy

Thomas Agnew Rolfe

Michael Christopher Nitti

Eckel Lan

Antimicrobial compositions and films are provided comprising a polymer and antimicrobial nanoparticles evenly dispersed in the polymer. The antimicrobial nanoparticles comprises an ionic antimicrobial agent and a support agent that localizes the ionic antimicrobial agent to surfaces of the support agent, and wherein the support agent releases the ionic antimicrobial agent through chemical exchange. In this manner, the antimicrobial nanoparticles act as a stored source of antimicrobial agents. The polymer configured to allow the ionic antimicrobial agent released by the support agent to permeate or migrate through the polymer and to the surface of the composition or film, thereby maintaining antimicrobial properties on the surface of the composition for film over an extended time.

Antimicrobial transparent plastic in the form of film or extruded shape

A method and system of storing and transporting gases comprising mixing the gases with liquid natural gas to form a mixture. The mixture is a liquid-liquid mixture or slurry, and is stored in vessel configured for maintaining the mixture at a first location. The mixture is transported to a second location for storage in vessel for maintaining the mixture. The mixture is removed from the second location storage vessel for separation and use in additional processes.

Method of storing and transporting light gases

A method of screening catalysts for liquid-phase selective hydrogenation by preparing a test catalyst by adding a promoter to a reference catalyst; preparing a liquid reactant stream comprising CHdissolved in n-methyl-2-pyrrolidone; testing the test and reference catalysts by contacting the reactant stream and gas mixture comprising hydrogen and carbon monoxide in continuous flow with the test catalyst and reference catalyst, respectively, at selective hydrogenation reaction conditions to produce a product stream, condensing substantially all of the n-methyl-2-pyrrolidone from the product stream; measuring the concentrations of products comprising CH, CH, and CHin the product stream at steady state; determining performance parameters for the test catalyst and the reference catalyst comprising the respective CHconversion Sand CHselectivity relative to CHS; and comparing the test catalyst performance parameters to those for the reference catalyst.

Catalyst formulation for hydrogenation

A process for converting natural gas from which contaminants have been sufficiently removed to acetylene includes heating the purified gas through a selected range of temperature for adequate time or combustion of the purified gas at adequate temperature within a suitable environment during an adequate reaction time to convert a fraction of the gas stream to acetylene, wherein the acetylene is directed for other processes, reactions, and uses. A process for converting natural gas to liquid hydrocarbons by combusting externally derived hydrogen for heating natural gas to a selected range of temperature. A process for converting natural gas to liquid hydrocarbons by reacting conversion products with externally derived hydrogen to form olefins comprising ethylene, and catalytically forming liquid hydrocarbons from the olefins comprising ethylene.

Process for the conversion of natural gas to acetylene and liquid fuels with externally derived hydrogen

In this disclosure, a reactor system is described. The reaction system comprises (a) a reaction vessel having an inner wall, wherein said reaction vessel is configured to receive reactants and export products and byproducts; (b) a primary quench device (PQD) configured to receive a coolant and disperse said coolant into said reaction vessel; and (c) a secondary quench device (SQD) configured to receive a coolant and disperse said coolant into said reaction vessel; wherein said PQD comprises an array of spray nozzles fixed on the inner wall of said reaction vessel at a first axial position; and wherein said SQD comprises (1) an axially movable pipe having a coolant entry end and a nozzle end, wherein said pipe is configured to be removably fixed inside said reaction vessel; and (2) a spray nozzle that is fluidly connected to said pipe at its nozzle end via a fluid tight seal connection.

Secondary reaction quench device and method of use

A process and catalyst for the liquid phase selective hydrogenation of alkynes to alkenes with high selectivity to alkenes relative to alkanes, high alkyne conversion, and sustained catalytic activity comprising a reactant comprising an alkyne and a non-hydrocarbon solvent/absorbent, contacting the reactant stream with a hydrogen-containing stream in the presence of a supported, promoted, Group VIII catalyst, removing the solvent/absorbent, and recovering the alkene product.

Process for liquid phase hydrogenation

A composition and method for preparation of a catalyst for the liquid phase selective hydrogenation of alkynes to alkenes with high selectivity to alkenes relative to alkanes, high alkyne conversion, and sustained catalytic activity comprising a Group VIII metal and a Group IB, Group IIB, Group IIIA, and/or Group VIIB promoter on a particulate support.

A method for the absorption of alkynes and diolefins from an ethylene or propylene containing stream with conversion to alkenes by catalytic hydrogenation in a solvent over a fixed bed comprising a supported catalyst.

Absorption and conversion of acetylenic compounds

A process for converting natural gas to liquid hydrocarbons comprising heating the gas through a selected range of temperature for sufficient time and/or combustion of the gas at a sufficient temperature and under suitable conditions for a reaction time sufficient to convert a portion of the gas stream to reactive hydrocarbon products, primarily ethylene or acetylene. The gas containing acetylene may be separated such that acetylene is converted to ethylene. The ethylene product(s) may be reacted in the presence of an acidic catalyst to produce a liquid, a portion of which will be predominantly naphtha or gasoline. A portion of the incoming natural gas or hydrogen produced in the process may be used to heat the remainder of the natural gas to the selected range of temperature. Reactive gas components are used in a catalytic liquefaction step and/or for alternate chemical processing.

Growing community of inventors

Pearland, TX, United States of America

Edward R Peterson