Production of clean combustible gas with pressurised thermal gasification of wet biomass

Catalytic experiments with organic solutions have shown, that it is possible to convert the organic matter into a hydrogen-rich gas at temperatures belov 450 deg. C and residence times less than 1 hour.

Project description

Goal of the project is: 1) to convert wet biomass in one step into clean combustible gas aimed for heat and power production. 2) to identify and collect data relating to the reaction mechanism of the process. 3) to optimise the process thermodynamically and maximise the regain of energy. 4) to investigate intermediates and side products of the process. 5) to calculate the process economy. Research in geochemical laboratories has shown that it is possible to convert organic matter by pressurised thermal treatment into a clean gas with hydrocarbons. The conversion is taking place at a pressure between 100 and 200 bar and a temperature between 350 deg. C and 600 deg. C. Late experiments have shown that an effective utilisation of biomass is taking place when the organic matter first is dissolved before conversion in a supercritical fluid like steam or carbon dioxide. The solute is then reacted thermal/catalytic into a combustible gas containing hydrogen, carbon monoxide and hydrocarbobs. If the biomass is heated to fast or the steam pressure is too low, considerable amount of carbon is formed. The pressure is favouring a high heating value as a pressurised absorption process easily separates the formed carbon dioxide. The work programme is covering model experiments in micro reators with different fluid fraction of biomass in order to identify the reaction pathways, intermediates for the conversion into the conbustible gases: Hydrogen, carbon monoxide and methane. Experiments are carried out with the following solutions: 1) Cellulose monomer: Glucose. 2) Hemicellulose monomer: Xylose. 3) Lignin compound: Cutin. 4) Tar water with phenol. 5) Organic sludge. Inert and catalytic material is tested at 200-600 deg. C and 10-200 bars. The space-time is varied between 0.25-24 hours

Results

Experiments have been conducted with the constitutents of biomass: Glucose representing the cellulose fraction; Xylose representing the hemicellulose fraction; Phenol representing the lignin fraction. Phenol turned out to be the least reactive component, for which reason the investigations have been concentrated on this component. The rate of reaction is correlated to a first order reaction with respect to the phenol concentration. Rate = K*C. The rate constant has the unit [h-"1]. The Rate constant K is a second order function to the total pressure. The rate constant is calculated from the conversion (X) of the involved components by using the integrated equation. K=LHSV*-LN(1-X). The activation energy is 32 KJ/mole. The composition of the gas by decompostion of alcohols like methanol is much like the gas composition of phenol. The rate constant stabilises at a constant level after approximately 30 hours on stream, when the pressure is higher than 10 Mpa. The experiments show that it is possibel to produce hydrogen by catalytic conversion of organic matter in steam at temperatures around 400 deg. C and at pressure of 10 Mpa or higher. The catalyst is stable at the reaction conditions. The same sample of catalyst has been operating for 10 month at various conditions in the test unit for with more than 2000 hours on stream

Key figures

Period:
1999 - 2000
Funding year:
1999
Own financial contribution:
0.10 mio. DKK
Grant:
1.00 mio. DKK
Funding rate:
91 %
Project budget:
1.10 mio. DKK

Category

Oprindelig title
Fremstilling af rene brændbare gasser med tryksat termisk forgasning af våd biomasse
Programme
EFP
Technology
Bio and waste
Project type
Forskning
Case no.
1383/99-0005

Participants

Teknologisk Institut (Main Responsible)
Partners and economy
Partner Subsidy Auto financing
Aarhus Universitet
Universitetet i Bergen (NO)
Newcastle University (UK)
Statoil A/S

Contact

Kontakperson
Pedersen, Karsten
Comtact information

Øvr. Partnere: