View source for 18055059. Process to Hydrothermally Produce Gases From Residue Streams Using a Series of Reactors simplified abstract (Saudi Arabian Oil Company)

=Process to Hydrothermally Produce Gases From Residue Streams Using a Series of Reactors=


==Organization Name==

[[:Category:Saudi Arabian Oil Company|Saudi Arabian Oil Company]]


[[Category:Saudi Arabian Oil Company]]

==Inventor(s)==

[[:Category:Faisal Almulla of Dhahran (SA)|Faisal Almulla of Dhahran (SA)]][[Category:Faisal Almulla of Dhahran (SA)]]

[[:Category:Mazin Fathi of Dhahran (SA)|Mazin Fathi of Dhahran (SA)]][[Category:Mazin Fathi of Dhahran (SA)]]

[[:Category:Mohammed Dossary of Dhahran (SA)|Mohammed Dossary of Dhahran (SA)]][[Category:Mohammed Dossary of Dhahran (SA)]]

==Process to Hydrothermally Produce Gases From Residue Streams Using a Series of Reactors - A simplified explanation of the abstract==


This abstract first appeared for US patent application 18055059 titled 'Process to Hydrothermally Produce Gases From Residue Streams Using a Series of Reactors

==Simplified Explanation==

The process described in the abstract is a method for hydrogen production involving the mixing of hot water and hot oil, upgrading the reactor feed in both non-catalytic and catalytic reactors, and separating the gases to produce a gas product and a light hydrocarbon stream.

* Mixing hot water and hot oil to produce a mixed stream
* Increasing the temperature of the mixed stream to produce a reactor feed
* Upgrading the reactor feed in a non-catalytic reactor to produce a non-catalytic effluent
* Upgrading the catalytic feed in a catalytic reactor to produce a reactor effluent
* Separating the reactor effluent in a high-pressure separator to produce a gas stream
* Separating the gas stream in a gas separator to produce a gas product and a light hydrocarbon stream

== Potential Applications ==
This technology could be applied in industries requiring hydrogen production, such as fuel cells, ammonia production, and refineries.

== Problems Solved ==
This technology provides a more efficient and cost-effective method for hydrogen production compared to traditional methods.

== Benefits ==
The process offers higher yields of hydrogen, reduced energy consumption, and lower production costs.

== Potential Commercial Applications ==
The technology could be utilized in hydrogen production plants, refineries, and chemical manufacturing facilities.

== Possible Prior Art ==
One possible prior art could be the use of steam methane reforming for hydrogen production, which is a common method but may have limitations in terms of efficiency and cost-effectiveness.

=== Unanswered Questions ===

=== How does this process compare to other hydrogen production methods in terms of efficiency and cost-effectiveness? ===
The article does not provide a direct comparison with other hydrogen production methods, so it is unclear how this process stacks up against existing technologies in terms of efficiency and cost.

=== What are the environmental impacts of this hydrogen production process? ===
The article does not address the environmental impacts of the process, such as emissions or waste generation, leaving a gap in understanding the sustainability of this technology.


==Original Abstract Submitted==

A process for hydrogen production, the process comprising the steps of mixing hot water and hot oil to produce a mixed stream; increasing a temperature of the mixed stream to produce a reactor feed; upgrading the reactor feed in the non-catalytic reactor to produce a non-catalytic effluent, wherein a temperature in non-catalytic reactor is between 375° C. and 500° C., wherein the non-catalytic reactor is in the absence of catalyst; upgrading the catalytic feed in the catalytic reactor to produce a reactor effluent, wherein a temperature in catalytic reactor is between 550° C. and 700° C., wherein the catalyst is selected from the group consisting of transition metal oxides, lanthanide oxides, and combinations of the same, separating the reactor effluent in the high pressure separator to produce a gases stream; and separating the gases stream in the gases separator to produce a gas product and a light hydrocarbon stream.



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