DANIEL MARC CHINN, MD
Radiology at East St, Concord, CA

License number
California A60944
Category
Radiology
Type
Radiation Oncology
Address
Address 2
2540 East St EAST, Concord, CA 94520
4301 Northstar Way, Modesto, CA 95356
Phone
(209) 342-2300
(209) 524-4240 (Fax)

Professional information

Daniel M Chinn Photo 1

Dr. Daniel M Chinn, Concord CA - MD (Doctor of Medicine)

Specialties:
Radiation Oncology
Address:
Bay Area Therapeutic Oncology
2540 East St, Concord 94520
(925) 674-2521 (Phone)
Conditions:
Vulvar Cancer
Certifications:
Radiation Oncology, 2000
Awards:
Healthgrades Honor Roll
Languages:
English
Hospitals:
Bay Area Therapeutic Oncology
2540 East St, Concord 94520
John Muir Medical Center - Concord
2540 East St, Concord 94520
Education:
Medical School
University Of California, San Francisco, School Of Medicine
Graduated: 1996


Daniel Marc Chinn Photo 2

Daniel Marc Chinn, Concord CA

Specialties:
Oncologist
Address:
2540 East St, Concord, CA 94520
Education:
Doctor of Medicine
Board certifications:
American Board of Radiology Certification in Radiation Oncology (Radiology)


Daniel Chinn Photo 3

Hydrogen Recovery From Hydrocarbon Synthesis Processes

US Patent:
7166643, Jan 23, 2007
Filed:
Mar 8, 2004
Appl. No.:
10/794084
Inventors:
Clifford M. Lowe - Moraga CA, US
Daniel Chinn - Concord CA, US
Assignee:
Chevron U.S.A. Inc. - San Ramon CA
International Classification:
C07C 27/00
US Classification:
518726, 518700, 518722, 518709
Abstract:
The invention relates to a process for producing a hydrogen-rich stream from a hydrogen-depleted stream. More particularly, the invention relates to a hydrocarbon synthesis process, by way of example, a Fischer Tropsch process, from which both hydrocarbons and high purity hydrogen are obtained. The process comprises contacting the hydrogen-depleted stream with a reverse-selective membrane to provide a CO-enriched permeate and a hydrogen-containing retentate. The high purity hydrogen is produced from the hydrogen-containing retentate. The high purity hydrogen thus obtained may be used in a process selected from the group consisting of upgrading hydrocarbons produced from the hydrocarbon synthesis process, hydrotreating a natural gas stream, recycling to the hydrocarbon synthesis reaction unit, high purity hydrogen production, catalyst rejuvenation, and combinations thereof.


Daniel Chinn Photo 4

Hydrogen Recovery From Hydrocarbon Synthesis Processes

US Patent:
7405243, Jul 29, 2008
Filed:
May 13, 2004
Appl. No.:
10/844378
Inventors:
Clifford M. Lowe - Moraga CA, US
Daniel Chinn - Concord CA, US
Paul Bryan - Pinole CA, US
Assignee:
Chevron U.S.A. Inc. - San Ramon CA
International Classification:
C07C 27/00
US Classification:
518700, 518709, 518722, 518726
Abstract:
The invention relates to a process for producing a hydrogen-rich stream from a hydrogen-depleted stream. More particularly, the invention relates to a hydrocarbon synthesis process, by way of example, a Fischer Tropsch process, from which both hydrocarbons and high purity hydrogen are obtained. The process comprises contacting the hydrogen-depleted stream with a first reverse-selective membrane and a second reverse-selective membrane to provide a CO-enriched permeate and a hydrogen-containing retentate. The high purity hydrogen is produced from the hydrogen-containing retentate. The high purity hydrogen thus obtained may be used in a process selected from the group consisting of upgrading hydrocarbons produced from the hydrocarbon synthesis process, hydrotreating a natural gas stream, recycling to the hydrocarbon synthesis reaction unit, high purity hydrogen production, catalyst rejuvenation, and combinations thereof.


Daniel Chinn Photo 5

Hydrogen Recovery From Hydrocarbon Synthesis Processes

US Patent:
7745502, Jun 29, 2010
Filed:
Dec 13, 2006
Appl. No.:
11/637802
Inventors:
Clifford M. Lowe - Moraga CA, US
Daniel Chinn - Concord CA, US
Assignee:
Chevron U.S.A. Inc. - San Ramon CA
International Classification:
C07C 27/06, C01B 3/12, C01B 3/16
US Classification:
518709, 423655, 423656, 518722, 518726
Abstract:
The invention relates to a process for producing a hydrogen-rich stream from a hydrogen-depleted stream. More particularly, the invention relates to a hydrocarbon synthesis process, by way of example, a Fischer Tropsch process, from which both hydrocarbons and high purity hydrogen are obtained. The process comprises contacting the hydrogen-depleted stream with a reverse-selective membrane to provide a CO-enriched permeate and a hydrogen-containing retentate. The high purity hydrogen is produced from the hydrogen-containing retentate. The high purity hydrogen thus obtained may be used in a process selected from the group consisting of upgrading hydrocarbons produced from the hydrocarbon synthesis process, hydrotreating a natural gas stream, recycling to the hydrocarbon synthesis reaction unit, high purity hydrogen production, catalyst rejuvenation, and combinations thereof.


Daniel Chinn Photo 6

Co2 Removal From Gas Using Ionic Liquid Absorbents

US Patent:
2005012, Jun 16, 2005
Filed:
Dec 16, 2003
Appl. No.:
10/737090
Inventors:
Daniel Chinn - Concord CA, US
De Vu - Richmond CA, US
Michael Driver - San Francisco CA, US
Laura Boudreau - Houston TX, US
International Classification:
B01D053/62
US Classification:
423226000
Abstract:
A process and method for separating COfrom a gaseous stream such as natural gas. An ionic liquid comprising an anion having a carboxylate function is used as an adsorbent to selectively complex the COyielding a gaseous stream with a greatly reduced COcontent. The ionic liquid can then be readily be regenerated and recycled.


Daniel Chinn Photo 7

Aqueous Separation Of Syngas Components

US Patent:
2003020, Oct 30, 2003
Filed:
Apr 29, 2002
Appl. No.:
10/133437
Inventors:
Dennis O'Rear - Petaluma CA, US
Curtis Munson - Oakland CA, US
Daniel Chinn - Concord CA, US
International Classification:
C07C027/06
US Classification:
518/728000
Abstract:
Unreacted syngas containing COfrom a Fischer-Tropsch synthesis reactor, a methanol synthesis reactor or a dual functional syngas conversion is scrubbed with an aqueous medium to adsorb at least some of the CO. At least a portion of the unreacted CO-depleted syngas is then recycled to the reactor. The aqueous medium containing absorbed COis treated to desorb CO. A CO-enriched stream and a CO-depleted stream are recovered. A portion of the CO-enriched stream may be recycled to a syngas generator while another portion is dissolved in an aqueous phase and disposed in a marine environment and/or a terrestrial formation. The CO-depleted stream preferably is used in the scrubber to absorb COfrom the unreacted syngas. The process reduces the amount of COreleased into the atmosphere while improving the over-all efficiency of the syngas conversion process.