View source for 18554246. Method for Carrying Out a Chemical Reaction and Reactor Arrangement simplified abstract (BASF SE)

=Method for Carrying Out a Chemical Reaction and Reactor Arrangement=


==Organization Name==

[[:Category:BASF SE|BASF SE]]


[[Category:BASF SE]]

==Inventor(s)==

[[:Category:Mathieu Zellhuber of Martinsried (DE)|Mathieu Zellhuber of Martinsried (DE)]][[Category:Mathieu Zellhuber of Martinsried (DE)]]

[[:Category:Martin Hofst�tter of München (DE)|Martin Hofst�tter of München (DE)]][[Category:Martin Hofst�tter of München (DE)]]

[[:Category:Kiara Aenne Kochendoerfer of Ludwigshafen (DE)|Kiara Aenne Kochendoerfer of Ludwigshafen (DE)]][[Category:Kiara Aenne Kochendoerfer of Ludwigshafen (DE)]]

[[:Category:Andrey Shustov of Ludwigshafen am Rhein (DE)|Andrey Shustov of Ludwigshafen am Rhein (DE)]][[Category:Andrey Shustov of Ludwigshafen am Rhein (DE)]]

[[:Category:Eric Jenne of Hassloch (DE)|Eric Jenne of Hassloch (DE)]][[Category:Eric Jenne of Hassloch (DE)]]

[[:Category:Andrea Haunert of Ludwigshafen (DE)|Andrea Haunert of Ludwigshafen (DE)]][[Category:Andrea Haunert of Ludwigshafen (DE)]]

[[:Category:Scott A. Stevenson of Houston TX (US)|Scott A. Stevenson of Houston TX (US)]][[Category:Scott A. Stevenson of Houston TX (US)]]

[[:Category:Robert R. Broekhuis of Sugar Land TX (US)|Robert R. Broekhuis of Sugar Land TX (US)]][[Category:Robert R. Broekhuis of Sugar Land TX (US)]]

[[:Category:Andrew M. Ward of Yorkshire (GB)|Andrew M. Ward of Yorkshire (GB)]][[Category:Andrew M. Ward of Yorkshire (GB)]]

==Method for Carrying Out a Chemical Reaction and Reactor Arrangement - A simplified explanation of the abstract==


This abstract first appeared for US patent application 18554246 titled 'Method for Carrying Out a Chemical Reaction and Reactor Arrangement

'''Simplified Explanation:'''
The patent application describes a method for carrying out a chemical reaction using a reactor arrangement with reaction tubes heated by electric heating elements in a gas atmosphere with a defined oxygen volume fraction.

* Key Features and Innovation:
    - Reactor arrangement with reaction tubes heated by electric heating elements
    - Reaction tube temperature level between 400°C and 1,500°C
    - Gas atmosphere with defined oxygen volume fraction during the reaction period

* Potential Applications:
    - Chemical synthesis processes
    - Material processing industries
    - Research and development laboratories

* Problems Solved:
    - Efficient heating of reaction tubes
    - Control of oxygen volume fraction in the gas atmosphere
    - Enhanced reaction kinetics

* Benefits:
    - Improved reaction efficiency
    - Precise control over reaction conditions
    - Increased productivity in chemical processes

* Commercial Applications:
    - High-temperature chemical reactions
    - Production of advanced materials
    - Industrial scale chemical processing

* Prior Art:
    - Researchers can explore prior patents related to high-temperature chemical reactions, reactor arrangements, and gas atmosphere control.

* Frequently Updated Research:
    - Researchers may find updated studies on high-temperature reactions, reactor design, and gas atmosphere effects on chemical processes.

'''Questions about the Technology:'''
1. How does the method described in the patent application improve the efficiency of chemical reactions?
2. What are the potential challenges in implementing this reactor arrangement in industrial settings?


==Original Abstract Submitted==

A method for carrying out a chemical reaction includes using a reactor arrangement in which reaction tubes arranged in a reactor vessel are heated to a reaction tube temperature level between 400° C. and 1,500° C. during a reaction period using radiant heat provided by means of one or more electric heating elements arranged in the reactor vessel. In at least a part of the reactor vessel in which the heating elements are provided, a gas atmosphere is provided during the reaction period, which gas atmosphere has a defined volume fraction of oxygen.



[[Category:B01J19/24]]
[[Category:B01J3/00]]
[[Category:CPC_B01J19/243]]