Air Products and Chemicals, Inc.

Other

Glatt Systemtechnik Gmbh

Roger Dean Whitley

Matthew James Labuda

Timothy Christopher Golden

Shubhra Jyoti Bhadra

Glenn Paul Wagner

Robert Ling Chiang

William Jack Casteel, Jr

Erin Marie Sorensen

Garret Chi-Ho Lau

David Lester Rarig

Craig E Steigerwalt

Edward Landis Weist, Jr

David Ross Graham

Douglas Paul Dee

James Michael Occhialini

Qiao Zhao

Charles G Coe

Mohammad Ali Kalbassi

Robert Quinn

Charles F Watson

Paul Anthony Wright

Stuart Alexander Kerr

Daniel Louis Vassilaros

Geoffrey John Ochs

Marissa Ann Bonanno

Pascal Lisbet

Magdalena M Lozinska

Jane Elizabeth Ostroski

Christopher Robert Bongo

William Jack Casteel

Paul A Wright

Rakesh Agrawal

David R Schiff

Ravi Kumar

Madhukar Bhaskara Rao

Donn Michael Herron

Steven R Auvil

Chun Christine Dong

Jeffrey Raymond Hufton

Peter D Byar

Dingjun Wu

Andrew Weiman

Fred William Taylor

Thomas Stephen Farris

Annemarie Ott Weist

Stephen Clyde Tentarelli

Seth McCue GaleWyrick

Jin Cao

Bo Jin

Kevin Alan Lievre

Jason Michael Ploeger

Erdem Arslan

George Matthew Harriott

Wolfgang Hungerbach

Cory E Sanderson

Xue Mei Liu

Edwin John Miller

Yong Cao

Jinzhong Liu

Constant Johan Van Lookeren

Christopher Michael O'Neill

Michael Jamie McKerrow

Michael L Meyer

Seth Galewyrick

Junxiao Wu

Almuth Gerds

Norman Reger-Wagner

Elizabeth M Seibel

Elliott L Bruce

Michael S Yankovoy

Dingiun Wu

Luigi Depari

Garrett Chi-Ho Lau

Gregory John Gondecki

Charles Gardner Coe

Andrew M Weiman

Christopher Michael O'neill

Edward Landis Weist

Pascal Lisbit

Charles Franklin Watson

Michael Jamie Mckerrow

Paula A Wright

William Jack Casteel Jr

Norman Reger

Steven Ray Auvil

Seth Gale Wyrick

Process and apparatus for producing helium, neon, or argon product gas using an adsorption separation unit having minimal dead end volumes. A purification unit receives a stream enriched in helium, neon, or argon, and a stream is recycled from the purification unit back to the adsorption separation unit in a controlled manner to maintain the concentration of the helium, neon, or argon in the feed to the separation unit within a targeted range.

Separation process and apparatus for light noble gas

Disclosed herein are rapid cycle pressure swing adsorption (PSA) process for separating Ofrom Nand/or Ar. The processes use a carbon molecular sieve (CMS) adsorbent having an O/Nand/or O/Ar kinetic selectivity of at least 5 and an Oadsorption rate (1/s) of at least 0.2000 as determined by linear driving force model at 1 atma and 86&#xb0; F.

Carbon molecular sieve adsorbent

Disclosed herein are multi-bed rapid cycle pressure swing adsorption (RCPSA) processes for separating Ofrom Nand/or Ar, wherein the process utilizes at least five adsorption beds each comprising a kinetically selective adsorbent for Ohaving an Oadsorption rate (1/s) of at least 0.20 as determined by linear driving force model at 1 atma and 86&#xb0; F.

Multi-bed rapid cycle kinetic PSA

Disclosed herein is a stator plate for a rotary bed PSA apparatus that has an exhaust slot that has first and second sections for receiving blowdown and purge exhaust gas streams, the sections being separated by a flow restriction that restricts but does not full prevent gas flow between the sections, or that has separate exhaust slots for separately receiving the blowdown and purge exhaust gas streams. Also disclosed is pressure swing adsorption (PSA) apparatus including such a stator plate, and a rotary bed PSA process using such an apparatus.

Port separation for rotary bed PSA

Disclosed are novel, as-crystallized RHO zeolite compositions with improved uniformity in morphology. These RHO compositions are useful for preparing cation-exchanged RHO zeolites that can be used as adsorbents for oxygen and/or nitrogen with improved properties. The adsorbents can be used in pressure swing adsorption processes for selectively adsorbing oxygen and/or nitrogen from feed streams such as an air stream or crude argon stream. Also disclosed are novel methods of preparing RHO zeolites with improved morphology control.

RHO zeolites and method of making the same

Disclosed herein are novel RHO zeolites useful as kinetically selective adsorbents for oxygen and/or nitrogen. The adsorbents can be used in pressure swing adsorption processes for selectively adsorbing oxygen and/or nitrogen from feed streams such as an air stream or crude argon stream. Also disclosed are novel methods of preparing RHO zeolites, including in particular mixed-cation RHO zeolites.

RHO adsorbent compositions, methods of making and using them

Disclosed herein are new processes for adsorbing oxygen using adsorbent compositions comprising RHO zeolites kinetically selective for oxygen. The RHO zeolites can be used in pressure swing adsorption processes for separating oxygen from oxygen containing streams, such as for, but not limited to, purifying a crude argon feed stream or separating oxygen from an air feed stream.

Processes using improved RHO adsorbent compositions

An adsorbent having a composition comprising at least 90% chabazite where the chabazite is a single phase chabazite having an Si/Al ratio of 1.2 to 1.8, the chabazite includes a mixture of at least two types of cations, and each of the at least two types of cations are in a molar ratio relative to Al of at least 0.05.

Modified chabazite adsorbent compositions, methods of making and using them

Methods and systems for purifying argon from a crude argon stream are disclosed, employing pressure swing adsorption at cold temperatures from &#x2212;186&#xb0; C. to &#x2212;20&#xb0; C.; more preferably from &#x2212;150&#xb0; C. to &#x2212;50&#xb0; C.; and most preferably from &#x2212;130&#xb0; C. to &#x2212;80&#xb0; C. with oxygen-selective zeolite adsorbent. In some embodiments, the oxygen-selective zeolite adsorbent is a 4A zeolite, a chabazite, or a combination thereof.

Method for argon production via cold pressure swing adsorption

A method of separating oxygen from an oxygen-containing fluid stream is disclosed, the method including the step of contacting the oxygen-containing fluid stream with an oxygen-selective zeolite adsorbent comprising at least 90% chabazite, wherein the chabazite is a single phase chabazite having an Si/Al ratio of 1.2 to 1.8. The single phase chabazite may comprise a mixture of at least two types of cations.

An adsorption vessel comprising a packed bed region of adsorbent particles contiguously arranged, comprising a perforated adsorbent particles, a gas separation process using the perforated adsorbent particles, and methods for making the perforated adsorbent particles. The perforated adsorbent particles each comprise an adsorbent material where the perforated adsorbent particles each have at least 10 channels extending through the particle. The equivalent diameter of the channels may range from 0.05 mm to 1.5 mm, and the void fraction of the channels may range from 0.05 to 0.5.

Perforated adsorbent particles

Pressure swing adsorption system comprising two or more vessels, each having a feed end, a product end, and adsorbent material adapted to adsorb one or more components from a multi-component feed gas mixture; piping adapted to (1) introduce the feed gas mixture into the feed ends, withdraw a product gas from the product ends, and withdraw a waste gas from the feed ends of the vessels, and (2) place the product ends of any pair of vessels in flow communication; a feed pipe adapted to supply the feed gas mixture to the system; a product pipe adapted to withdraw the product gas from the system; and a waste gas pipe adapted to withdraw the waste gas from the system. An indexed rotatable multi-port valve is adapted to place the product end of each vessel in sequential flow communication with the product end of each of the other vessels.

Pressure swing adsorption system with indexed rotatable multi-port valves

Composite adsorbent beads have a porous and non-adsorbent core comprising at least one inorganic material and a porous and adsorbent shell comprising at least one adsorbent layer comprising a porous adsorbent material on the surface of the core. The core preferably comprises agglomerated inorganic particles having a mean particle size equal to or smaller than the mean particle size of the surrounding agglomerated adsorbent particles. The beads preferably are manufactured by calcining together a non-sintered core and the adsorbent layer. The beads can be used at the outlet end of an adsorption column to improve performance.

Composite adsorbent bead, process for its production, gas separation process and gas adsorption bed

A built in purifier for a cylinder of essentially nitrogen free gas having a low water content is provided with a molecular sieve 3A adsorbent to adsorb water from the gas, the 3A adsorbent having a particularly low adsorption capacity for nitrogen.

Method and apparatus for the supply of dry gases

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Allentown, PA, United States of America

Roger Dean Whitley