Howard L Fang, Age 77518 Glen Ridge Dr, Bridgewater, NJ 08807

Howard Fang Phones & Addresses

518 Glen Ridge Dr, Bridgewater, NJ 08807 (908) 725-0937 (908) 725-5265 (812) 342-7498

Basking Ridge, NJ

665 Greystone Ct, Columbus, IN 47201 (812) 342-7498

Highland Heights, OH

Katy, TX

518 Glen Ridge Dr S, Bridgewater, NJ 08807 (812) 290-4740

Work

Position: Professional/Technical

Education

Degree: Graduate or professional degree

Emails

Mentions for Howard L Fang

Publications & IP owners

Us Patents

Fuel Composition

US Patent:
8569554, Oct 29, 2013
Filed:
Jul 12, 2012
Appl. No.:
13/547826
Inventors:
Howard L. Fang - Bridgewater NJ, US
Meifang Qin - Princton NJ, US
Moshe Ben-Reuven - Princeton NJ, US
Assignee:
Primus Green Energy Inc - Hillsborough NJ
International Classification:
C10L 1/16
US Classification:
585 14, 585 1, 208 17
Abstract:
This invention relates to fuel compositions for use in combustion engines, such as for motor vehicle and aircraft usage. The fuel composition contains at least 99. 5% of aromatic hydrocarbons and paraffinic hydrocarbons. The composition also preferably contains no lead, no multi-ring compound (only single ring compounds are present), less than about 15 ppm sulfur, and/or less than about 5 ppm nitrogen species. The resulting fuel is a drop-in fuel that provides clean burning with little to no engine deposit, high lubricity, high stability, and low corrosion.

Exhaust Aftertreatment Emission Control Regeneration

US Patent:
2004011, Jun 17, 2004
Filed:
Feb 12, 2002
Appl. No.:
10/075036
Inventors:
Aleksey Yezerets - Columbus IN, US
Neal Currier - Columbus IN, US
Matthew DeWitt - Beavercreek OH, US
Sriram Popuri - Greenwood IN, US
George Muntean - Richland WA, US
Michael Cunningham - Greenwood IN, US
Barry Verdegan - Stoughton WI, US
Robert Miller - Indianapolis IN, US
Jer-Sheng Chen - Columbus IN, US
Howard Fang - Columbus IN, US
Herbert Dacosta - Columbus IN, US
Cary Bremigan - Madison WI, US
William Haberkamp - Cookeville TN, US
International Classification:
B01J038/04
US Classification:
502/034000
Abstract:
An exhaust emission control regeneration system regenerates a particulate filter by combusting trapped particulate and producing a combustion product from such combustion, and uses the combustion product to assist regeneration of a downstream catalyst, such as CO assisting regeneration of a downstream NOadsorber, located in sufficiently close proximity to a diesel particulate filter.

Single Loop Multistage Fuel Production

US Patent:
2012011, May 10, 2012
Filed:
Nov 9, 2010
Appl. No.:
12/942680
Inventors:
Howard L. Fang - Bridgewater NJ, US
Moshe BEN-REUVEN - Princeton NJ, US
Richard E. BOYLE - Philadelphia PA, US
Robert M. KOROS - Westfield NJ, US
Assignee:
PRIMUS GREEN ENERGY INC. - HILLSBOROUGH NJ
International Classification:
C07C 1/02
B01J 8/00
US Classification:
585317, 585310, 422187, 585322
Abstract:
Synthetic fuels are produced from synthesis gas in a four-stage reactor system with a single recycle loop providing the requisite thermal capacity to moderate the high heat release of the reactions and to provide the reactants and reaction environments for the efficient operation of the process. The first stage converts a portion of the synthesis gas to methanol, the second stage converts the methanol to dimethylether, the third stage converts the methanol and dimethylether to fuel and the fourth stage converts the high melting point component, durene, and other low volatility aromatic components such as tri- andtetra-methylbenzenes to high octane branched paraffins. The four-stage catalyst used for hydrotreating is resistant to CO poisoning. The reactions i produce water as a side product that is carried through to a high pressure separator after the fourth stage. The streams from the separator are a liquid fuel stream, a water stream and a gaseous stream that contains light hydrocarbon gases and the unreacted synthesis gas. The larger part of this gas stream is recycled to the inlet of the first stage and mixed with the fresh synthesis gas stream. Alternatively, the fresh synthetic gas stream is mixed with the product of the second stage. The smaller part of the gas stream from the separator is sent to hydrocarbon recovery and to fuel gas used for providing preheat of various streams. The liquid fuel is sent for blending into fuel products, such as gasoline, jet fuel, or diesel, and the water stream can be sent, for example, to the synthesis gas producing plant for steam generation.

Catalytical Gasifier Configuration For Biomass Pyrolysis

US Patent:
2013027, Oct 17, 2013
Filed:
Jul 17, 2012
Appl. No.:
13/551146
Inventors:
Moshe BEN-REUVEN - Princeton NJ, US
Howard L. Fang - Bridgewater NJ, US
Meifang Qin - Princton NJ, US
Robert M. Koros - Westfield NJ, US
Arie Toren - Kendall Park NJ, US
Assignee:
Primus Green Energy Inc. - Hillsborough NJ
International Classification:
C01B 3/02
C01B 3/38
US Classification:
252373, 422600, 422139, 422620, 422608
Abstract:
The invention relates to systems and methods for producing synthesis gas. In particular, the systems of the present invention include two catalytic reactors in series, a wet reformer/gasifier followed by a dry reformer. The systems produce synthesis gas with very little to no methane.

Polymers Having Dihydroxy Moieties

US Patent:
5712231, Jan 27, 1998
Filed:
Jun 4, 1996
Appl. No.:
8/659129
Inventors:
Manuel Anthony Francisco - Washington NJ
Ken Lewtas - Wantage, GB
Howard Lih Fang - Bridgewater NJ
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C10M14500
C07C 3714
US Classification:
508587
Abstract:
The present invention provides novel polymers comprising a plurality of dihydroxy aromatic moieties and at least one polyalkyl moiety. In one embodiment of the present invention, the polymer is formed from about 2 to about 50 interconnected dihydroxy aromatic moieties each having an attached polyalkyl moiety. In another embodiment of the present invention, the polymer is represented by the formula A. sub. x P. sub. y where A is an aromatic dihydroxy moiety and P is a polyalkyl moiety. The polymers of the invention are useful as lubricating oil additives.

Method For Reducing Viscosity Increase In Sooted Diesel Oils

US Patent:
5837657, Nov 17, 1998
Filed:
Dec 2, 1997
Appl. No.:
8/982681
Inventors:
Howard L. Fang - Bridgewater NJ
Jonathan M. McConnachie - Flemington NJ
Edward Ira Stiefel - Bridgewater NJ
International Classification:
C10M13500
C10M13900
US Classification:
508363
Abstract:
The present invention is directed to a method for improving the performance of a sooted diesel oil and controlling soot induced viscosity increase by adding to a major amount of a diesel oil a minor amount of a composition comprising at least one compound having the formula Mo. sub. 3 S. sub. k L. sub. n Q. sub. z and mixtures thereof wherein the L are independently selected ligands having organo groups with a sufficient number of carbon atoms to render the compound soluble or dispersible in the oil, n is from 1 to 4, k varies from 4 through 10, Q is selected from the group of neutral electron donating compounds such as water, amines, alcohols, phosphines, and ethers, and z ranges from 0 to 5 and includes nonstoichiometric values.

Single-Loop Octane Enrichment

US Patent:
2020001, Jan 9, 2020
Filed:
Sep 17, 2019
Appl. No.:
16/572980
Inventors:
- Hillsborough NJ, US
Howard L. FANG - Bridgewater NJ, US
Zhong HE - Harrison NJ, US
Ricardo ORENCH - Langhorne PA, US
Zhiyi WU - Hillsborough NJ, US
Arie TOREN - Kendall Park NJ, US
International Classification:
C10G 3/00
C10G 35/095
C07C 29/152
C10L 1/06
C07C 41/09
Abstract:
The present invention provides apparatuses and processes for producing high octane fuel from synthesis gas. The process combines transalkylation and zeolite-forming/aromatization in conjunction with a single recycle loop configuration in order to effectively promote the fuel quality, particularly octane rating. The process involves adding a step for enriching octane of the fuel coming from the single recycle loop process. Preferably, the enrichment step takes place in an octane enrichment reactor containing two different catalysts, a zeolite-forming/aromatization catalyst followed by a transalkylation catalyst. The final fuel product preferably has an octane of about 92 to about 112.

Single-Loop Octane Enrichment

US Patent:
2017022, Aug 10, 2017
Filed:
Feb 9, 2017
Appl. No.:
15/428956
Inventors:
- Hillsborough NJ, US
Howard L. FANG - Bridgewater NJ, US
Zhong HE - Harrison NJ, US
Ricardo ORENCH - Langhorne PA, US
Zhiyi WU - Hillsborough NJ, US
Arie TOREN - Kendall Park NJ, US
International Classification:
C10G 3/00
C07C 41/09
C07C 29/152
C10G 35/095
C10L 1/06
Abstract:
The present invention provides apparatuses and processes for producing high octane fuel from synthesis gas. The process combines transalkylation and zeolite-forming/aromatization in conjunction with a single recycle loop configuration in order to effectively promote the fuel quality, particularly octane rating. The process involves adding a step for enriching octane of the fuel coming from the single recycle loop process. Preferably, the enrichment step takes place in an octane enrichment reactor containing two different catalysts, a zeolite-forming/aromatization catalyst followed by a transalkylation catalyst. The final fuel product preferably has an octane of about 92 to about 112.

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