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Dalip S Soni

from Houston, TX
Age ~80
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Also known as:
Singh Dalip Soni, Dalip Soni Singh, Dolip S Soni, Dalip S Sonio, Dalipsingh Soni, Onior S Dalip
Phone and address:
13615 Springcross Ct, Houston, TX 77077
(281) 859-8271
Related to:
Harminder Singh, 63Joginder S Soni, 77Karan SoniJoginder S Soni, 70Manjit K Soni, 73Manjit K Soni, 72Karanvir S Soni, 37Amrita S Soni, 40Vikram S Soni, 42
Connected to:
Aakanksha Soni, 37Abu S Soni, 42Ajay K Soni, 71Ameet Soni, 43Amitkumar J Soni, 62Amrita Soni, 44Anand Soni, 51Ankoor B Soni, 43Anupam Soni, 48Apoorva Soni, 36

Dalip Soni Phones & Addresses

  • 13615 Springcross Ct, Houston, TX 77077 (281) 859-8271
  • 7707 Knolls Lodge Ct, Houston, TX 77095 (281) 859-8271
  • 1015 Country Place Dr #93, Houston, TX 77079 (281) 859-8271
  • Austin, TX
  • 4517 N Hedgerow Dr, Allentown, PA 18103 (281) 859-8271
  • Miami, FL
  • Lindenwold, NJ
  • 13615 Springcross Ct, Houston, TX 77077 (281) 501-0239

Work

Position: Professional/Technical

Education

Degree: Associate degree or higher

Emails

v***[email protected]

Resumes

Resumes

Dalip Soni Photo 1

Dalip Soni

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Location:
Houston, TX
Industry:
Oil & Energy
Work:
Cb&I May 1994 - Apr 2014
Director, Fcc Technology
Stone & Webster Aug 1988 - May 1994
Principle Process Engineer
Education:
Oklahoma State University 1975 - 1977
Master of Science, Masters, Chemical Engineering Panjab University,Chandigarh 1970 - 1974
Bachelors, Bachelor of Science, Chemical Engineering
Skills:
Iron
Fcc
Bridge
Stone
Refining
Dalip Soni Photo 2

Dalip Soni

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Location:
Houston, TX
Industry:
Oil & Energy
Work:
Cb&I May 1994 - Apr 2014
Director, Fcc Technology
Stone and Webster Jul 1988 - May 1994
Principal Process Engineer
Hri, Inc. Mar 1980 - May 1988
Senior Process Engineer
Education:
Oklahoma State University 1975 - 1977
Masters, Chemical Engineering Panjab University,Chandigarh 1970 - 1974
Bachelors, Bachelor of Science, Chemical Engineering
Skills:
Engineering

Business Records

Name / Title
Company / Classification
Phones & Addresses
Dalip Soni
Secretary, Principal, Director, President
PERFECT LINE INC
Nonclassifiable Establishments
13615 Springcross Ct, Houston, TX 77077
7707 Knl Ldg Ct, Houston, TX 77095
Dalip Soni
Director, President, Secretary
NISON CONSULTANTS INC
13615 Springcross Ct, Houston, TX 77077
7707 Knl Ldg Ct, Houston, TX 77095
13615 Spg Cross Ct, Houston, TX 77077

Publications

Us Patents

Apparatus For Countercurrent Contacting Of Gas And Solids

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US Patent:
7179427, Feb 20, 2007
Filed:
Nov 25, 2002
Appl. No.:
10/303452
Inventors:
Paul E. Marchant - Houston TX, US
Dalip S. Soni - Houston TX, US
Leonce Castagnos - Montgomery TX, US
Assignee:
ABB Lummus Global Inc. - Bloomfield NJ
International Classification:
B32B 5/02
B32B 27/12
B32B 27/04
US Classification:
422144, 422145, 422147
Abstract:
An apparatus for the countercurrent contacting of a gas and downflowing solid particles includes a housing and a plurality of baffles positioned within the housing. The baffles are arranged in at least first and second vertically spaced levels in successively lower position, each of the first and second levels including a row of at least two baffles oriented parallel to one another and inclined from horizontal so as to facilitate movement of the solid particles and provide the maximum area for flow. Baffles are oriented so as to laterally shift the direction of downflowing particles transversely as the particles move from one level to the next lower level and avoid channeling of the phases. The number of baffles, length and spacing is optimized to provide maximum interfacial area for interaction between the phases.

Processing Of Different Feeds In A Fluid Catalytic Cracking Unit

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US Patent:
7682501, Mar 23, 2010
Filed:
Dec 23, 2004
Appl. No.:
11/021274
Inventors:
Dalip S Soni - Houston TX, US
Leonce F Castagnos - Montgomery TX, US
Assignee:
ABB Lummus Global, Inc. - Bloomfield NJ
International Classification:
C10G 11/00
US Classification:
208113, 208153, 208157
Abstract:
An apparatus and method for processing different feeds in a fluid catalytic cracking unit are disclosed which result in improved yields of C, Cand gasoline range hydrocarbons as compared to conventional systems. The process comprises injecting a main hydrocarbon feed into a catalyst-containing riser reactor through a plurality of main feed injectors, and injecting a light hydrocarbon feed into the riser reactor at a location upstream from the main feed injectors and downstream from a control valve such as a regenerated catalyst slide valve, the light feed being injected in a region having a high density of catalyst particles. The light feed is injected in a dispersed way such the amount of feed injected corresponds to the density of catalyst particles at that particular point, with greater amounts of feed being injected at locations having a large number of catalyst particles. Also, a heavy hydrocarbon feed or a heavy recycle stream from the same FCC unit can be injected at the same elevation as the main feed injectors but through separate injectors.

System And Method For Selective Component Cracking To Maximize Production Of Light Olefins

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US Patent:
20050161369, Jul 28, 2005
Filed:
Jan 18, 2005
Appl. No.:
11/039125
Inventors:
Dalip Soni - Houston TX, US
Leonce Castagnos - Montgomery TX, US
Assignee:
ABB Lummus Global, Inc. - Bloomfield NJ
International Classification:
C10G011/00
US Classification:
208113000
Abstract:
A process for the fluid catalytic cracking of hydrocarbons includes contacting relatively heavy hydrocarbons with a fluidized particulate catalyst in a reaction zone under catalytic cracking conditions to convert at least some of the heavy hydrocarbons to light olefins having from 3 to 4 carbon atoms, conveying a reaction mixture containing spent catalyst particles and a gaseous stream containing the light olefins and other reaction products to a cyclone separation system directly connected to the reaction zone, at least part of the cyclone separation system being positioned within an interior space enclosed by a vessel, the interior space including a stripping region and an upper region in which the cyclone separation system is positioned. The cyclone separation system includes at least one cyclone connected directly to the reaction zone and having an interior pressure at least 0.05 psig lower than the pressure in the stripping region.

Processing Of Different Feeds In A Fluid Catalytic Cracking Unit

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US Patent:
20100158766, Jun 24, 2010
Filed:
Mar 8, 2010
Appl. No.:
12/719325
Inventors:
Dalip S. Soni - Houston TX, US
Leonce F. Castagnos - Montgomery TX, US
International Classification:
B01J 8/18
US Classification:
422144
Abstract:
An apparatus and method for processing different feeds in a fluid catalytic cracking unit are disclosed which result in improved yields of C, Cand gasoline range hydrocarbons as compared to conventional systems. The process comprises injecting a main hydrocarbon feed into a catalyst-containing riser reactor through a plurality of main feed injectors, and injecting a light hydrocarbon feed into the riser reactor at a location upstream from the main feed injectors and downstream from a control valve such as a regenerated catalyst slide valve, the light feed being injected in a region having a high density of catalyst particles. The light feed is injected in a dispersed way such the amount of feed injected corresponds to the density of catalyst particles at that particular point, with greater amounts of feed being injected at locations having a large number of catalyst particles. Also, a heavy hydrocarbon feed or a heavy recycle stream from the same FCC unit can be injected at the same elevation as the main feed injectors but through separate injectors.

Fluid Cracking Process And Apparatus For Maximizing Light Olefins Or Middle Distillates And Light Olefins

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US Patent:
20140014555, Jan 16, 2014
Filed:
Jul 12, 2012
Appl. No.:
13/547807
Inventors:
Rama Rao Marri - Houston TX, US
Dalip Singh Soni - Houston TX, US
Pramod Kumar - Gurgaon, IN
Assignee:
LUMMUS TECHNOLOGY INC. - Bloomfield NJ
International Classification:
C10G 51/06
B01J 8/00
US Classification:
208 78, 422187
Abstract:
A fluid catalytic cracking apparatus and process is disclosed, providing for efficient conversion of heavy hydrocarbon feeds to light olefins, aromatics, and gasoline. A countercurrent flow reactor operating in bubbling or turbulent fluidization regimes is integrated with a fluid catalytic cracking riser reactor. A heavy hydrocarbon feed is catalytically cracked to naphtha and light olefins in the riser reactor, a co-current flow reactor. To enhance the yields and selectivity to light olefins, cracked hydrocarbon products from the riser reactor, such as Cand naphtha range hydrocarbons, may be recycled and processed in the countercurrent flow reactor. The integration of the countercurrent flow reactor with a conventional FCC riser reactor and catalyst regeneration system may overcome heat balance issues commonly associated with two-stage cracking processes, may substantially increase the overall conversion and light olefins yield, and/or may increases the capability to process heavier feedstocks.

Apparatus For The Return Of Particulate Solids Through A Cyclone Separator To A Vessel

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US Patent:
50376179, Aug 6, 1991
Filed:
Jan 4, 1990
Appl. No.:
7/461065
Inventors:
Dalip S. Soni - Houston TX
Assignee:
Stone & Webster Engineering Corporation - Boston MA
International Classification:
F27B 1509
B01J 826
US Classification:
422142
Abstract:
An apparatus and process for transferring and regulating the recycle of particulate solids separated from a gas-particulate solids suspension in which an auxiliary vessel and slanted pipe are provided to transfer and regulate particulate solids flow.

Process For The Return Of Recovered Particulate Solids By A Cyclone Separator To A Vessel

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US Patent:
51103230, May 5, 1992
Filed:
May 9, 1991
Appl. No.:
7/697702
Inventors:
Dalip S. Soni - Houston TX
Assignee:
Stone & Webster Engineering Corp. - Boston MA
International Classification:
B01D 2436
B01D 4512
US Classification:
55 1
Abstract:
A process for transferring and regulating the recycle of particulate solids separated from a gas-particulate solids suspension in which an auxiliary vesssel and slanted pipe are provided to transfer and regulate particulate solids flow.

Fluid Catalytic Cracking Process And Apparatus For Maximizing Light Olefins Or Middle Distillates And Light Olefins

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US Patent:
20170009150, Jan 12, 2017
Filed:
Sep 26, 2016
Appl. No.:
15/275802
Inventors:
- Bloomfield NJ, US
Dalip Singh Soni - Houston TX, US
Pramod Kumar - Gurgaon, IN
Assignee:
Lummus Technology Inc. - Bloomfield NJ
International Classification:
C10G 51/02
B01J 8/00
B01J 8/26
B01J 8/18
Abstract:
A fluid catalytic cracking apparatus and process is disclosed, providing for efficient conversion of heavy hydrocarbon feeds to light olefins, aromatics, and gasoline. A countercurrent flow reactor operating in bubbling or turbulent fluidization regimes is integrated with a fluid catalytic cracking riser reactor. A heavy hydrocarbon feed is catalytically cracked to naphtha and light olefins in the riser reactor, a co-current flow reactor. To enhance the yields and selectivity to light olefins, cracked hydrocarbon products from the riser reactor, such as Cand naphtha range hydrocarbons, may be recycled and processed in the countercurrent flow reactor. The integration of the countercurrent flow reactor with a conventional FCC riser reactor and catalyst regeneration system may overcome heat balance issues commonly associated with two-stage cracking processes, may substantially increase the overall conversion and light olefins yield, and/or may increases the capability to process heavier feedstocks.
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Dalip S Soni from Houston, TX, age ~80 Get Report