Allothermal Methane Reforming with Physical Energy Recovery
Simple SummaryContent extracted from patent full text and abstract with AI.
The patent describes a process for allothermal methane reforming, where methane is converted to synthesis gas (a mix of carbon monoxide and hydrogen) using carbon dioxide as a reactant. The process takes place in a packed bed reactor containing electrically conductive and catalytic particles, which are electrically heated to high temperatures. Additionally, a gas expansion turbine is used downstream of the reactor to recover physical energy from the high-temperature synthesis gas.
Use CasesContent extracted from patent full text and abstract with AI.
- Hydrogen production for industrial applications or as a clean fuel
- Synthesis gas (syngas) production for chemical manufacturing (e.g., ammonia, methanol)
- Carbon dioxide utilization and conversion into valuable fuels and chemicals
- Integration into renewable energy systems (e.g., coupling with renewable electricity sources for heating)
- Efficient energy recovery systems in chemical process plants
BenefitsContent extracted from patent full text and abstract with AI.
- Improved energy efficiency through physical energy recovery via a gas expansion turbine
- Utilizes carbon dioxide as a reactant, contributing to CO2 utilization and reduction
- Allows precise temperature control via electrical heating of reactor bed
- Potential for integration with renewable electricity, supporting decarbonized chemical production
- Produces high-purity synthesis gas suitable for various downstream processes
Technical Classifications (CPCs)
Main Classifications
Chemistry & Materials Science
Sub Classifications
Inorganic Chemistry
CPC Codes
Inventors & Applicants
Applicants
Tech Universität Bergakademie Freiberg
Patent Abstract
Die Erfindung betrifft ein Verfahren zur allotherme Methan-Reformierung mit physikalischer Energierückgewinnung, wobei Methan mittels Kohlenstoffdioxid zu Synthesegas, bestehend aus Kohlenstoffmonoxid und Wasserstoff, reformiert wird. Dabei werden die Ausgangsgase CH4 und CO2 in einen Festbettreaktor bestehend aus elektrisch leitfähigen und katalytischen Partikeln geleitet, die elektrisch auf Temperaturen von ca. 1000 K erhitzt ist. Im Festbett erfolgen die Umsetzung der Edukt-Gase sowie die Erhitzung des erzeugten Synthesegases. In der erfindungsgemäßen Vorrichtung ist dem Reformergehäuse eine Gasentspannungsturbine zur Energierückgewinnung nachgeordnet.
Key Information
Publication No.
DE102013226126A1
Family ID
53192393
Publication Date
2015-06-18
Application No.
DE102013226126A
Application Date
2013-12-16
Priority Date
2013-12-16
Granted
No
Possible Cooperation
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