Patents by Inventor Hussam A. Bahlouli
Hussam A. Bahlouli has filed for patents to protect the following inventions. This listing includes patent applications that are pending as well as patents that have already been granted by the United States Patent and Trademark Office (USPTO).
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Patent number: 11780788Abstract: Methods for cracking a hydrocarbon feed stream include contacting a hydrocarbon feed stream with a catalyst system in a catalytic cracking unit having a flowing gas stream to obtain a cracking product containing light olefins. The catalyst system includes at least a base catalyst. The base catalyst includes a pentasil zeolite. The pentasil zeolite includes from 0.01% to 5% by mass lithium atoms, as calculated on an oxide basis, based on the total mass of the pentasil zeolite. The flowing gas stream comprises hydrogen and, optionally, at least one additional carrier gas.Type: GrantFiled: September 13, 2021Date of Patent: October 10, 2023Assignee: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Patent number: 11623207Abstract: A catalyst for dehydrogenation of hydrocarbons includes a support including zirconium oxide and Linde type L zeolite (L-zeolite). A concentration of the zirconium oxide in the catalyst is in a range of from 0.1 weight percent (wt. %) to 20 wt. %. The catalyst includes from 5 wt. % to 15 wt. % of an alkali metal or alkaline earth metal. The catalyst includes from 0.1 wt. % to 10 wt. % of tin. The catalyst includes from 0.1 wt. % to 8 wt. % of a platinum group metal. The alkali metal or alkaline earth metal, tin, and platinum group metal are disposed on the support.Type: GrantFiled: February 25, 2021Date of Patent: April 11, 2023Assignee: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Publication number: 20230084430Abstract: Methods for cracking a hydrocarbon feed stream include contacting a hydrocarbon feed stream with a catalyst system in a catalytic cracking unit having a flowing gas stream to obtain a cracking product containing light olefins. The catalyst system includes at least a base catalyst. The base catalyst includes a pentasil zeolite. The pentasil zeolite includes from 0.01% to 5% by mass lithium atoms, as calculated on an oxide basis, based on the total mass of the pentasil zeolite. The flowing gas stream comprises hydrogen and, optionally, at least one additional carrier gas.Type: ApplicationFiled: September 13, 2021Publication date: March 16, 2023Applicant: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Patent number: 11371329Abstract: Systems and methods of enhancing oil recovery with an electrochemical apparatus include introducing the electrochemical apparatus into an injection well bore. The electrochemical apparatus includes an anode, a cathode and an interior wall, the interior wall defining an interior that contains both the anode and the cathode. The electrochemical apparatus is operated such that injection water of the injection well bore is introduced into the interior of the electrochemical apparatus. Electrical power is introduced to the electrochemical apparatus such that a portion of the injection water is converted into a product gas, the product gas including hydrogen gas and oxygen gas. The electrochemical apparatus is operated such that the product gas forms product gas bubbles and the product gas bubbles travel into a formation, where the product gas bubbles react with a reservoir hydrocarbon of the formation to form a production fluid that is produced through a production well bore.Type: GrantFiled: March 11, 2021Date of Patent: June 28, 2022Assignee: SAUDI ARABIAN OIL COMPANYInventors: Abdulrahman Abdulaziz Al-Mulhem, Mohammed A. Al-Daous, Hussam A. Bahlouli
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Patent number: 11338269Abstract: A catalyst for dehydrogenation of hydrocarbons includes a support including zirconium oxide and alumina. A concentration of the zirconium oxide in the catalyst is in a range of from 1 weight percent (wt. %) to 20 wt. %. The catalyst includes from 0.01 wt. % to 2 wt. % of an alkali metal or alkaline earth metal. The catalyst includes from 1 wt. % to 2 wt. % of tin. The catalyst includes from 0.1 wt. % to 2 wt. % of a platinum group metal. The alkali metal or alkaline earth metal, tin, and platinum group metal are disposed on the support.Type: GrantFiled: September 10, 2019Date of Patent: May 24, 2022Assignee: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Patent number: 11292755Abstract: Olefins may be produced from C4-C6 saturated hydrocarbons by systems and methods comprising passing a feed comprising C4-C6 saturated hydrocarbons and hydrogen into a dehydrogenation unit to produce a dehydrogenation effluent, passing at least a portion of the dehydrogenation effluent into a hydrogenation unit to produce a hydrogenation effluent, and passing at least a portion of the hydrogenation effluent into a cracking unit to produce a cracking effluent comprising olefins. The dehydrogenation unit includes a dehydrogenation catalyst, the hydrogenation unit includes a hydrogenation catalyst, and the cracking unit includes a cracking catalyst.Type: GrantFiled: June 15, 2020Date of Patent: April 5, 2022Assignee: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Publication number: 20210387930Abstract: Olefins may be produced from C4-C6 saturated hydrocarbons by systems and methods comprising passing a feed comprising C4-C6 saturated hydrocarbons and hydrogen into a dehydrogenation unit to produce a dehydrogenation effluent, passing at least a portion of the dehydrogenation effluent into a hydrogenation unit to produce a hydrogenation effluent, and passing at least a portion of the hydrogenation effluent into a cracking unit to produce a cracking effluent comprising olefins. The dehydrogenation unit includes a dehydrogenation catalyst, the hydrogenation unit includes a hydrogenation catalyst, and the cracking unit includes a cracking catalyst.Type: ApplicationFiled: June 15, 2020Publication date: December 16, 2021Applicant: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Patent number: 11097257Abstract: A catalyst for dehydrogenation of hydrocarbons includes a support including zirconium oxide and Linde type L zeolite (L-zeolite). A concentration of the zirconium oxide in the catalyst is in a range of from 0.1 weight percent (wt. %) to 20 wt. %. The catalyst includes from 5 wt. % to 15 wt. % of an alkali metal or alkaline earth metal. The catalyst includes from 0.1 wt. % to 10 wt. % of tin. The catalyst includes from 0.1 wt. % to 8 wt. % of a platinum group metal. The alkali metal or alkaline earth metal, tin, and platinum group metal are disposed on the support.Type: GrantFiled: September 10, 2019Date of Patent: August 24, 2021Assignee: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Publication number: 20210198991Abstract: Systems and methods of enhancing oil recovery with an electrochemical apparatus include introducing the electrochemical apparatus into an injection well bore. The electrochemical apparatus includes an anode, a cathode and an interior wall, the interior wall defining an interior that contains both the anode and the cathode. The electrochemical apparatus is operated such that injection water of the injection well bore is introduced into the interior of the electrochemical apparatus. Electrical power is introduced to the electrochemical apparatus such that a portion of the injection water is converted into a product gas, the product gas including hydrogen gas and oxygen gas. The electrochemical apparatus is operated such that the product gas forms product gas bubbles and the product gas bubbles travel into a formation, where the product gas bubbles react with a reservoir hydrocarbon of the formation to form a production fluid that is produced through a production well bore.Type: ApplicationFiled: March 11, 2021Publication date: July 1, 2021Applicant: Saudi Arabian Oil CompanyInventors: Abdulrahman Abdulaziz Al-Mulhem, Mohammed A. Al-Daous, Hussam A. Bahlouli
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Publication number: 20210178369Abstract: A catalyst for dehydrogenation of hydrocarbons includes a support including zirconium oxide and Linde type L zeolite (L-zeolite). A concentration of the zirconium oxide in the catalyst is in a range of from 0.1 weight percent (wt. %) to 20 wt. %. The catalyst includes from 5 wt. % to 15 wt. % of an alkali metal or alkaline earth metal. The catalyst includes from 0.1 wt. % to 10 wt. % of tin. The catalyst includes from 0.1 wt. % to 8 wt. % of a platinum group metal. The alkali metal or alkaline earth metal, tin, and platinum group metal are disposed on the support.Type: ApplicationFiled: February 25, 2021Publication date: June 17, 2021Applicant: Saudi Arabian Oil CompanyInventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Patent number: 10982517Abstract: Systems and methods of enhancing oil recovery with an electrochemical apparatus include introducing the electrochemical apparatus into an injection well bore. The electrochemical apparatus includes an anode, a cathode and an interior wall, the interior wall defining an interior that contains both the anode and the cathode. The electrochemical apparatus is operated such that injection water of the injection well bore is introduced into the interior of the electrochemical apparatus. Electrical power is introduced to the electrochemical apparatus such that a portion of the injection water is converted into a product gas, the product gas including hydrogen gas and oxygen gas. The electrochemical apparatus is operated such that the product gas forms product gas bubbles and the product gas bubbles travel into a formation, where the product gas bubbles react with a reservoir hydrocarbon of the formation to form a production fluid that is produced through a production well bore.Type: GrantFiled: December 1, 2017Date of Patent: April 20, 2021Assignee: SAUDI ARABIAN OIL COMPANYInventors: Abdulrahman Abdulaziz Al-Mulhem, Mohammed A. Al-Daous, Hussam A. Bahlouli
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Publication number: 20210069677Abstract: A catalyst for dehydrogenation of hydrocarbons includes a support including zirconium oxide and alumina. A concentration of the zirconium oxide in the catalyst is in a range of from 1 weight percent (wt. %) to 20 wt. %. The catalyst includes from 0.01 wt. % to 2 wt. % of an alkali metal or alkaline earth metal. The catalyst includes from 1 wt. % to 2 wt. % of tin. The catalyst includes from 0.1 wt. % to 2 wt. % of a platinum group metal. The alkali metal or alkaline earth metal, tin, and platinum group metal are disposed on the support.Type: ApplicationFiled: September 10, 2019Publication date: March 11, 2021Inventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Publication number: 20210069683Abstract: A catalyst for dehydrogenation of hydrocarbons includes a support including zirconium oxide and Linde type L zeolite (L-zeolite). A concentration of the zirconium oxide in the catalyst is in a range of from 0.1 weight percent (wt. %) to 20 wt. %. The catalyst includes from 5 wt. % to 15 wt. % of an alkali metal or alkaline earth metal. The catalyst includes from 0.1 wt. % to 10 wt. % of tin. The catalyst includes from 0.1 wt. % to 8 wt. % of a platinum group metal. The alkali metal or alkaline earth metal, tin, and platinum group metal are disposed on the support.Type: ApplicationFiled: September 10, 2019Publication date: March 11, 2021Inventors: Mohammed Abdulmajeed Al-Daous, Hussam A. Bahlouli
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Publication number: 20190169969Abstract: Systems and methods of enhancing oil recovery with an electrochemical apparatus include introducing the electrochemical apparatus into an injection well bore. The electrochemical apparatus includes an anode, a cathode and an interior wall, the interior wall defining an interior that contains both the anode and the cathode. The electrochemical apparatus is operated such that injection water of the injection well bore is introduced into the interior of the electrochemical apparatus. Electrical power is introduced to the electrochemical apparatus such that a portion of the injection water is converted into a product gas, the product gas including hydrogen gas and oxygen gas. The electrochemical apparatus is operated such that the product gas forms product gas bubbles and the product gas bubbles travel into a formation, where the product gas bubbles react with a reservoir hydrocarbon of the formation to form a production fluid that is produced through a production well bore.Type: ApplicationFiled: December 1, 2017Publication date: June 6, 2019Inventors: Abdulrahman Abdulaziz Al-Mulhem, Mohammed A. Al-Daous, Hussam A. Bahlouli