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Hazem N Haddad

from Houston, TX
Age ~60
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Also known as:
Hazem H Haddad, Hazem M Judeh, Haddad Hazem
Phone and address:
2147 Paso Rello Dr, Houston, TX 77077
(281) 589-2154
Related to:
Abraham HaninJulie Nelson, 60Hanadi JudehFerras J Zereik, 31E Abraham
Connected to:
Abla A Haddad, 67Amber J Haddad, 37Ana M Haddad, 62Andres Haddad, 65Angel Haddad, 47Anton A Haddad, 46Antonio S Haddad, 68Assaad M Haddad, 70Azizeh M Haddad, 94Bachar Haddad, 57

Hazem Haddad Phones & Addresses

  • 2147 Paso Rello Dr, Houston, TX 77077 (281) 589-2154
  • 11710 Briar Forest Dr, Houston, TX 77077
  • Livingston, TX
  • Rolla, MO
  • Katy, TX
  • Alhambra, CA

Resumes

Resumes

Hazem Haddad Photo 1

Hazem Haddad

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Location:
2147 Paso Rello Dr, Houston, TX 77077
Industry:
Oil & Energy
Work:
Linde Engineering North America Inc. Oct 2016 - May 2020
Principle Process Engineer
Middough Inc. May 2012 - Mar 2015
Discipline Manager - Process
Urs Corporation/Washington Division Feb 2008 - Feb 2009
Senior Consulting Engineer Iv
Sabic/United Jul 2006 - Sep 2007
Senior Process Staff Engineer and Plant Area Engineer
Urs Corporation Jan 2006 - Jan 2006
Consultant and Principal Olefins Technologist
Education:
Missouri University of Science and Technology 1993 - 1998
Doctorates, Doctor of Philosophy, Chemical Engineering Missouri University of Science and Technology 1982 - 1986
Master of Science, Masters, Bachelors, Bachelor of Science, Chemical Engineering
Skills:
Process Simulation
Distillation
Energy
Aspen Hysys
Process Engineering
Commissioning
Process Optimization
Natural Gas
Project Engineering
Chemical Engineering
Gas
Aspen Plus
Feed
Ethylene
Visual Studio .Net
Refining
P&Id
Refinery
Gas Processing
Petrochemical
Heat Exchangers
Hysys
Pro/Ii
Factory
Process Design
Languages:
Arabic
English
Hazem Haddad Photo 2

Mortgage Loan Officer

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Location:
Houston, TX
Work:
Quicken Loans
Mortgage Loan Officer
Education:
Wayne State University 2008 - 2012
Bachelors, Bachelor of Business Administration
Hazem Haddad Photo 3

Owner, Heat

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Location:
Houston, TX
Industry:
Entertainment
Work:

Owner, Heat

Business Records

Name / Title
Company / Classification
Phones & Addresses
Hazem H. Haddad
President
HOME & BODY COMPANY
Mfg Polish/Sanitation Gd Mfg Soap/Other Detergent Mfg Toilet Preparations Mfg Chemical Preparation · Mfg Polish/Sanitation Goods
18352 Enterprises Ln, Huntington Beach, CA 92648
18352 Enterprise Ln, Huntington Beach, CA 92648
(714) 842-8000

Publications

Us Patents

Cryogenic Process Utilizing High Pressure Absorber Column

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US Patent:
6712880, Mar 30, 2004
Filed:
Oct 22, 2001
Appl. No.:
10/003388
Inventors:
Jorge H. Foglietta - Missouri City TX
Hazem Haddad - Houston TX
Earle Ross Mowrey - Houston TX
Sanjiv N. Patel - Sugarland TX
Ajit Sangave - Houston TX
Assignee:
ABB Lummus Global, Inc. - Houston TX
International Classification:
B01D 5314
US Classification:
95184, 95204, 95227, 95228, 95237, 62618, 62625
Abstract:
A cryogenic process and apparatus for separating multi-component gaseous hydrocarbon streams to recover both gaseous and liquid compounds. More particularly, the cryogenic processes and apparatus of this invention utilize a high pressure absorber to improve the energy efficiency of processing natural gas for pipeline gas sales and recovering natural gas liquids (NGL) gas from gaseous hydrocarbon streams.

Optimized Heating Value In Natural Gas Liquids Recovery Scheme

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US Patent:
6964181, Nov 15, 2005
Filed:
Aug 28, 2003
Appl. No.:
10/651178
Inventors:
Paul Barton Milios - Katy TX, US
Hazem Haddad - Houston TX, US
David C. Vogel - Houston TX, US
Sanjiv N. Patel - Sugar Land TX, US
Jorge H. Foglietta - Missouri City TX, US
Assignee:
ABB Lummus Global Inc. - Houston TX
International Classification:
F25J003/00
F25J001/00
US Classification:
62620, 62613
Abstract:
A process and apparatus for controlling or reducing the heating value or BTU content of NGL recovered from LNG streams. LNG pipelines have a maximum allowable heating value that LNG must be within prior to entering the pipeline. If the LNG heating value is too high, the components contributing to the high heating value must be removed prior to being introduced in the pipeline. The process controls the heating value of the residue LNG gas stream by splitting a feed stream and warming at least a portion of the feed stream. Substantial differences in enthalpy content and temperature between the two portions of the feed stream exist prior to being sent to a fractionation tower.

Mixed Refrigerants In Ethylene Recovery

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US Patent:
56260342, May 6, 1997
Filed:
Nov 17, 1995
Appl. No.:
8/560469
Inventors:
David Manley - Rolla MO
Hazem Haddad - Rolla MO
International Classification:
F25J 100
US Classification:
62623
Abstract:
The present invention is a process of high efficiency rectification zone separation of cracked or other ethylene-containing gas chilled primarily by two closed mixed refrigerant loops and at least part of the dephlegmated overhead gas. The composition of the mixed refrigerants is optimally chosen to obtain an extremely close approach between the process condensation temperatures in the high efficiency rectification zone and the temperature of the chilling streams. An approach of about 3. degree. F. to 8. degree. F. can be achieved for the full condensation curve in the high efficiency rectification zone operating with either ethane or naphtha derived cracked gas. Highly reliable and stable operation is obtained by closed refrigeration loops in the present invention, in addition to reducing high efficiency rectification zone design cost.

Low Cost Thermal Coupling In Ethylene Recovery

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US Patent:
56750544, Oct 7, 1997
Filed:
Jul 17, 1995
Appl. No.:
8/503486
Inventors:
David Manley - Rolla MO
Hazem Haddad - Rolla MO
International Classification:
C07C 700
C10G 4922
B01D 300
US Classification:
585809
Abstract:
The invention is a process for reducing capital and energy costs in ethylene recovery. Moderate pressure processing and thermally coupled fractionation steps are achieved through the use of integrator columns. Ethylene separation from cracked gas originating from ethane through gas oil feeds can now be done with thermodynamically efficient fractionation at capital cost competitive with low efficiency designs. Acetylene hydrogenation may be done before demethanization where desired, and dephlegmation is preferred to accomplish high-efficiency rectification of hydrogen and methane from ethylene. Open loop heat pumps can optionally be incorporated into the ethane/ethylene splitter fractionation step, whose desirability is controlled by optimization of capital and energy costs.
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Hazem N Haddad from Houston, TX, age ~60 Get Report