Catalytic Hot Gas Cleaning with Monoliths in Biomass Gasification in Fluidized Beds. 4. Performance of an Advanced, Second-Generation, Two-Layers-Based Monolithic Reactor

2006 ◽  
Vol 45 (4) ◽  
pp. 1389-1396 ◽  
Author(s):  
José M. Toledo ◽  
José Corella ◽  
Gregorio Molina
Keyword(s):  
Fluidized Beds ◽  
Second Generation ◽  
Biomass Gasification ◽  
Gas Cleaning ◽  
Hot Gas ◽  
Hot Gas Cleaning

An advanced biomass gasification technology with integrated catalytic hot gas cleaning

Fuel ◽  
2013 ◽  
Vol 108 ◽  
pp. 409-416 ◽  
Author(s):  
Li Dong ◽  
Mohammad Asadullah ◽  
Shu Zhang ◽  
Xiao-Shan Wang ◽  
Hongwei Wu ◽  
...  
Keyword(s):  
Biomass Gasification ◽  
Gas Cleaning ◽  
Hot Gas ◽  
Hot Gas Cleaning ◽  
Gasification Technology

A Review of Hot Gas Cleaning Techniques for Hydrogen Chloride Removal from Biomass-Derived Syngas

Energies ◽  
2021 ◽  
Vol 14 (20) ◽  
pp. 6519
Author(s):  
Vera Marcantonio ◽  
Michael Müller ◽  
Enrico Bocci
Keyword(s):  
Climate Change ◽  
Hydrogen Chloride ◽  
Thermal Efficiency ◽  
Biomass Gasification ◽  
Gas Cleaning ◽  
Promising Technology ◽  
Hot Gas ◽  
Chloride Removal ◽  
Hot Gas Cleaning ◽  
Secondary Methods

Considering the pressing challenges of supply security and climate change, advanced processes to produce electricity and biofuels from biomass have to be developed. Biomass gasification is a very promising technology, but there is a lack of comprehensive reviews, specifically on the technologies for hydrogen chloride hot gas cleanup, which are necessary in order to work at the same temperature and respect the limits of advanced downstream components. In this review, the Cl content of the main biomasses in Europe is given, and data on syngas content and the tolerance of downstream equipment are highlighted. Hot gas cleaning technologies, which have the advantage of improved thermal efficiency are reviewed, analyzing the thermodynamic and primary and secondary methods. This review identifies NaAlO2 and Na2CO3 within 450–550 °C as the most effective sorbents, which are able to reduce the concentration of HCl below 1 ppm. Nevertheless, H2S cannot be simultaneously removed and has to be removed first, because it reduces the HCl adsorption sorbent capacity.

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