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Tofik K Khanmamedov

from Alpharetta, GA
Age ~79
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Also known as:
Tofik Dr Khanmamedov, Tofik M Khanmamedov, Tofik R, Tofik V, Tofik O
Related to:
Yingxia Xie, 37T KhanmamedovLin Khanmamedov, 49Drtofik K KhanmamedovAlla K Khanmamedova, 77Lin KhanmamedovQicheng Gao, 72Jianmi Gao, 79Xu U Gao, 44Djavad T Khanmamedov, 51
Connected to:
Pirouz Khanmalek, 73Mansoor M Khanmohamed, 46Abhay Khanna, 39Akhil Khanna, 48Ankur Khanna, 46Anubha Khanna, 54Anuj Khanna, 39Anuradha Khanna, 60Apeksha Khanna, 41Chander M Khanna, 77

Tofik Khanmamedov Phones & Addresses

  • Alpharetta, GA
  • 2006 Summerfield Pl, Sugar Land, TX 77478
  • 4504 Burnhill Dr, Plano, TX 75024
  • 2934 Belt Line Rd, Garland, TX 75044
  • Richardson, TX
  • Houston, TX
  • Dallas, TX
  • 403 Fox Briar Ln, Sugar Land, TX 77478

Resumes

Resumes

Tofik Khanmamedov Photo 1

Owner

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Location:
Houston, TX
Industry:
Oil & Energy
Work:
Tkk Technology Company Dba Tkk Company Feb 2003 - 2011
President and Chief Executive Officer
Tkk Company Feb 2003 - 2011
Owner
Education:
Gubkin Russian State University of Oil and Gas (National Research University)
Doctorates, Doctor of Science, Chemical Engineering
Skills:
Chemical Engineering
R&D
Environmental
Science
Engineering
Simulation
Research
Interests:
Music
Tofik Khanmamedov Photo 2

President And Chief Executive Officer

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Location:
403 Fox Briar Ln, Sugar Land, TX 77478
Industry:
Oil & Energy
Work:
Tkk Company
President and Chief Executive Officer
Tofik Khanmamedov Photo 3

President And Chief Executive Officer

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Work:
Tkk Company
President and Chief Executive Officer

Business Records

Name / Title
Company / Classification
Phones & Addresses
Tofik Khanmamedov
President
TOFAL LLC
2006 Summerfield Pl, Sugar Land, TX 77478
3120 SW Fwy, Houston, TX 77098
Tofik Khanmamedov
Managing M, President, Director
TKK TECHNOLOGY COMPANY LLC
14090 SW Fwy #300-196, Sugar Land, TX 77478
2006 Summerfield Pl, Sugar Land, TX 77478
403 Fox Briar Ln, Sugar Land, TX 77478

Publications

Us Patents

Process For Removal Of Contaminants From A Gas Stream

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US Patent:
6506349, Jan 14, 2003
Filed:
Jul 2, 1997
Appl. No.:
08/887149
Inventors:
Tofik K. Khanmamedov - Garland TX, 75044
International Classification:
B01D 5348
US Classification:
423210, 423220, 423228, 4232421, 4235731, 423DIG 5
Abstract:
A selected contaminant is removed from a gas stream containing an unselected component that is also absorbed by the solvent, although to a lesser degree than the selected contaminant. In a typical application, hydrogen sulfide is removed from a natural gas stream that contains carbon dioxide as an unselected component. The process employs a solvent absorption/regeneration sequence, carried out in an absorber and regenerator, to remove the selected contaminant (hydrogen sulfide, for example) from the gas stream. The overhead gas from the regenerator has a higher concentration of the selected contaminant than the original gas stream. This contaminant rich overhead gas stream is partially employed as a recycle stream that is combined with the original gas stream, with the resulting combined gas stream being fed to the absorber. The increased partial pressure of the selected contaminant in the absorber shifts the operating point, resulting in increased absorption of the selected contaminant relative to the unselected component. The regenerator overhead gas has a relatively high concentration of the selected contaminant.

Method And Apparatus For Controlling The Hydrogen Sulfide Concentration In The Acid Gas Feedstock Of A Sulfur Recovery Unit

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US Patent:
55566065, Sep 17, 1996
Filed:
Oct 7, 1994
Appl. No.:
8/319746
Inventors:
Tofik K. Khanmamedov - Dallas TX
International Classification:
C01B 1716
C01B 1700
US Classification:
423228
Abstract:
An apparatus for controlling the hydrogen sulfide concentration in an acid gas stream and the hydraulic loading of a sulfur recovery unit of the type having an absorber for contacting a sour gas stream with an absorbent, a regenerator for regenerating the absorbent to form an acid gas stream and a recycle system. Embodiments using multiple absorbers and/or multiple regenerators are disclosed.

Apparatus For Controlling The Hydrogen Sulfide Concentration In The Acid Gas Feedstock Of A Sulfur Recovery Unit

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US Patent:
57188726, Feb 17, 1998
Filed:
Jun 21, 1996
Appl. No.:
8/668404
Inventors:
Tofik K. Khanmamedov - Garland TX
International Classification:
B01D 5000
US Classification:
422168
Abstract:
An apparatus for controlling the hydrogen sulfide concentration in an acid gas stream and the hydraulic loading of a sulfur recovery unit of the type having an absorber for contacting a sour gas stream with an absorbent, a regenerator for regenerating the absorbent to form an acid gas stream and a recycle system. Embodiments using multiple absorbers and/or multiple regenerators are disclosed.

Apparatus For Removal Of Contaminates From A Gas Stream

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US Patent:
57165874, Feb 10, 1998
Filed:
Jun 21, 1996
Appl. No.:
8/670796
Inventors:
Tofik Khanmamedov - Garland TX
International Classification:
B01D 5000
US Classification:
422168
Abstract:
An apparatus is disclosed for removal of contaminate(s) from a gas stream in an oil or gas refinery using an absorber-regenerator process wherein a portion of the contaminate rich overhead gas from the regenerator is utilized to increase the partial pressure of the contaminate at the absorber so as to enhance selective absorption of the contaminate(s).

Process For Recovery Of Sulfur From An Acid Gas Stream

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US Patent:
59651008, Oct 12, 1999
Filed:
Sep 6, 1996
Appl. No.:
8/709107
Inventors:
Tofik K. Khanmamedov - Garland TX
International Classification:
C01B 1720
US Classification:
4235768
Abstract:
A gas stream containing hydrogen sulfide is combusted in a furnace to form a gas having a hydrogen sulfide to sulfur dioxide ratio of at least three to one. The gas is contacted with a conventional Claus catalyst to form elemental sulfur, which is separated and removed. The remaining gas is combined with an oxidizing gas stream and contacted with a special catalyst. The special catalyst has an active ingredient comprising a mixture of metal oxides or a mixed metal oxide, where metal is defined as at least two of the transition metals occurring in the first transition group of the periodic table. The special catalyst preferably has a spinel structure. As an option, a portion of the acid gas feed can be bypassed a point before the final reactor to ensure that the gas going to the final reactor promotes the desired catalytic action. The special catalyst oxidizes both COS and CS. sub. 2 to CO. sub. 2 and SO. sub. 2, and converts H. sub.
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Tofik K Khanmamedov from Alpharetta, GA, age ~79 Get Report