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Lin Luo, 29Houston, TX

Related to:
Wei Wang 52 James Luo 80 Bangqian Luo 60

Lin Luo Phones & Addresses

Houston, TX   

Austin, TX   

6 Twin Valley Dr, Sugar Land, TX 77479    832-5123591   

2828 Hayes Rd, Houston, TX 77082    713-7520823   

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Lin Luo

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Work

Position: Personal Care and Service Occupations

Education

School / High School: University of Virginia School of Law

Ranks

Licence: New York - Currently registered Date: 2004

Industries

Restaurants
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Career records & work history

Lawyers & Attorneys

Lin Luo Photo 1

Lin Luo - Lawyer

Address:
Zhonglun W&D Law Firm
339-1739581 (Office)
Licenses:
New York - Currently registered 2004
Education:
University of Virginia School of Law

Lin Luo resumes & CV records

Resumes

Lin Luo Photo 31

Manger At Chinois

Location:
Houston, Texas Area
Industry:
Restaurants

Publications & IP owners

Us Patents

Fluid Catalytic Cracking Additive

US Patent:
2008028, Nov 20, 2008
Filed:
Mar 8, 2006
Appl. No.:
11/908084
Inventors:
Julie Ann Francis - Houston TX, US
Lin Luo - Lake Jackson TX, US
Darrell Ray Rainer - Houston TX, US
International Classification:
B01J 21/04
B01D 53/56
B01D 53/62
B01J 23/50
B01J 23/72
B01J 23/44
B01J 21/16
US Classification:
502 63, 4232391, 423247, 502 74
Abstract:
The present invention relates to a catalyst composition comprising rhodium supported on an anionic clay. This catalyst composition is suitable as CO combustion additive in fluid catalytic cracking units. Compared to prior art CO combustion additives, the formation of NOis minimized.

Low Nox Co Oxidation Promoters

US Patent:
2009005, Feb 26, 2009
Filed:
Jun 9, 2008
Appl. No.:
12/135461
Inventors:
Darrell Ray Rainer - Houston TX, US
Julie Ann Francis - Houston TX, US
Jorge Alberto Gonzalez - Houston TX, US
Lin Luo - Lake Jackson TX, US
Assignee:
ALBEMARLE NETHERLANDS B.V. - AMERSFOORT
International Classification:
C10G 11/00
B02C 23/00
B01J 29/04
B01J 21/16
US Classification:
20812005, 20812015, 2081203, 20812035, 241 3, 502 61, 502 73, 502 74, 502 84, 502 63
Abstract:
Particulate compositions for promoting CO oxidation in FCC processes are provided, the compositions comprising an anionic clay support having at least one dopant, wherein at least one compound comprising iridium, rhodium, palladium, copper, or silver is deposited on the anionic clay support, and the composition is substantially free of platinum.

Process To Prepare Olefins From Aliphatic Alcohols

US Patent:
2012010, Apr 26, 2012
Filed:
Jun 28, 2010
Appl. No.:
13/320931
Inventors:
Mark William Stewart - Pearland TX, US
Howard W. Clark - Lake Jackson TX, US
Duncan Paul Coffey - Lake Jackson TX, US
Lin Luo - Sugar Land TX, US
International Classification:
C07C 1/24
US Classification:
585324
Abstract:
A process to prepare an olefin from its corresponding alcohol is improved by reacting, under reaction conditions including a first temperature, an aliphatic alcohol and, optionally, diluent water, to form a reaction product including at least a dialkyl ether. The product is then reacted again, under higher temperature to complete the dehydration of the dialkyl ether to the desired olefin. This process is particularly suitable to prepare ethene from ethyl alcohol. The stepped temperature scheme serves to reduce the formation of byproduct aldehydes, which in turn reduces coke formation, fouling, and the need to handle large amounts of water, thereby lowering energy and capital costs.

Non-Oxidative Dehydrogenative Process

US Patent:
2013017, Jul 11, 2013
Filed:
Aug 24, 2011
Appl. No.:
13/814583
Inventors:
Lin Luo - Sugar Land TX, US
Devon C. Rosenfeld - Houston TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
C07C 5/333
US Classification:
585660
Abstract:
Use a supported catalyst that includes a catalyst support and a combination of nickel, gallium, and, optionally, one or more of an alkali metal, an alkaline earth metal and a lanthanide to effect non-oxidative dehydrogenation of an oxygen-free gaseous stream that comprises an alkane such as ethane, propane or butane to a product stream that comprises a corresponding alkene such as propylene where the alkane is propane.

Chemical Processing Utilizing Hydrogen Containing Supplemental Fuel For Catalyst Processing

US Patent:
2022034, Oct 27, 2022
Filed:
Jul 8, 2022
Appl. No.:
17/860357
Inventors:
- Midland MI, US
Mark W. Stewart - Pearland TX, US
Lin Luo - Sugarland TX, US
Hangyao Wang - Pearland TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
C07C 5/333
B01J 8/00
B01J 8/18
B01J 8/24
B01J 21/12
B01J 23/62
B01J 23/96
B01J 38/02
B01J 38/12
Abstract:
A method for processing a chemical stream includes contacting a feed stream with a catalyst in a reactor portion of a reactor system that includes a reactor portion and a catalyst processing portion. The catalyst includes platinum, gallium, or both and contacting the feed stream with the catalyst causes a reaction which forms an effluent stream. The method includes separating the effluent stream from the catalyst, passing the catalyst to the catalyst processing portion, and processing the catalyst in the catalyst processing portion. Processing the catalyst includes passing the catalyst to a combustor, combusting a supplemental fuel in the combustor to heat the catalyst, treating the heated catalyst with an oxygen-containing gas to produce a reactivated catalyst, and passing the reactivated catalyst from the catalyst processing portion to the reactor portion. The supplemental fuel may include a molar ratio of hydrogen to other combustible fuels of at least 1:1.

Methods For Operating Acetylene Hydrogenation Units During Integration Of Chemical Processing Systems For Producing Olefins

US Patent:
2022025, Aug 11, 2022
Filed:
Jun 8, 2020
Appl. No.:
17/621945
Inventors:
- Midland MI, US
Lin Luo - Sugar Land TX, US
Yu Liu - Lake Jackson TX, US
Matthew T. Pretz - Lake Jackson TX, US
Andrzej Malek - Midland MI, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
C07C 7/167
C07C 7/00
C07C 7/04
C07C 4/04
C07C 5/333
B01J 23/62
B01D 45/16
B01D 3/14
Abstract:
A method for operating an acetylene hydrogenation unit of a steam cracking system that integrates a fluidized catalytic dehydrogenation (FCDh) effluent from a fluidized catalytic dehydrogenation (FCDh) system may include separating a cracked gas from the steam cracking system into at least a hydrogenation feed comprising at least acetylene, CO, and hydrogen, introducing the FCDh effluent to the separation system, combining the FCDh effluent with the cracked gas upstream of the separation system, or both. The method may include hydrogenating acetylene in the hydrogenation feed. Elevated CO concentration in the hydrogenation feed due to the FCDh effluent may reduce a reaction rate of acetylene hydrogenation. The acetylene hydrogenation unit may operate at an elevated temperature relative to normal operating temperatures when the portion of the FCDh effluent is not integrated, such that a concentration of acetylene in the hydrogenated effluent is less than a threshold acetylene concentration.

Chemical Processes And Systems That Include The Combustion Of Supplemental Fuels

US Patent:
2021026, Aug 26, 2021
Filed:
Jun 26, 2019
Appl. No.:
17/256688
Inventors:
- Midland MI, US
Hangyao Wang - Pearland TX, US
Lin Luo - Sugarland TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
C07C 5/333
Abstract:
According to one or more embodiments presently disclosed, a method for processing a chemical stream may include contacting a feed stream with a catalyst in a reactor portion of a reactor system that includes a reactor portion and a catalyst processing portion. Contacting the feed stream with the catalyst may cause a reaction forming an effluent. The method may include separating the effluent stream from the catalyst, passing the catalyst to the catalyst processing portion, and processing the catalyst in the catalyst processing portion. Processing the catalyst may include passing the catalyst to a combustor, combusting a supplemental fuel stream in the combustor to heat the catalyst, and treating the heated catalyst with an oxygen-containing gas. The supplemental fuel stream may include at least 1 mol % of one or more hydrocarbons, and a weight ratio of catalyst to hydrocarbons in the combustor may be at least 300:1.

Chemical Processing Utilizing Hydrogen Containing Supplemental Fuel For Catalyst Processing

US Patent:
2021026, Aug 26, 2021
Filed:
Jun 26, 2019
Appl. No.:
17/256706
Inventors:
- Midland MI, US
Mark W. Stewart - Pearland TX, US
Lin Luo - Sugarland TX, US
Hangyao Wang - Pearland TX, US
Assignee:
Dow Global Technologies LLC - Midland MI
International Classification:
C07C 5/333
B01J 23/62
B01J 21/12
B01J 23/96
B01J 38/02
B01J 38/12
B01J 8/00
B01J 8/24
B01J 8/18
Abstract:
A method for processing a chemical stream includes contacting a feed stream with a catalyst in a reactor portion of a reactor system that includes a reactor portion and a catalyst processing portion. The catalyst includes platinum, gallium, or both and contacting the feed stream with the catalyst causes a reaction which forms an effluent stream. The method includes separating the effluent stream from the catalyst, passing the catalyst to the catalyst processing portion, and processing the catalyst in the catalyst processing portion. Processing the catalyst includes passing the catalyst to a combustor, combusting a supplemental fuel in the combustor to heat the catalyst, treating the heated catalyst with an oxygen-containing gas to produce a reactivated catalyst, and passing the reactivated catalyst from the catalyst processing portion to the reactor portion. The supplemental fuel may include a molar ratio of hydrogen to other combustible fuels of at least 1:1.

Possible Relatives

David S Luo  Dan Luo  Dennis E Luo  Disong X Luo  Dongqing B Luo  Eric C Luo  Feng Q Luo  Lin C Johnson  Lin Kane  Lin B Kings 

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