Optimisation of circulating fluidised-bed gasification for biomass/straw (OCIFF)

Various combinations of wood, straw and additives, catalysts and bed materials have been evaluated and a number of tests have been made.

Project description

Additives and bed materials will be tested with the aim of finding components and mixtures that can improve the circulating fluid bed gasification of biomass. The focus will be on sintering, agglomeration and reactivity. Calculation models, lab. experiments, small-scale fluid bed and possibly pilot scale fluid bed experiments will be used to optimise ash and additive behaviour in gasification of biomass. The project consists of a theoretical, a fundamental experimental and an experimental part. Experiments will be performed using the thermogravimetric equipment at the laboratories of ReaTech and at The Department of Energy Engineering, DTU. Experiments will be planned at VTT's 'Process Development Unit' (PDU). The residual products will be examined with the aim of improving their value. With the aim of predicting sintering, agglomeration and fuel reactivity in biomass gasification, equilibrium calculations will be performed using the equilibrium programs FACT ('Facility for the Analysis of Chemical Thermodynamics') and HSC (from Outokumpu, Finland), both programs used by ReaTech. The program 'Gaussian' (Ålborg Univ. Esbjerg) will be used to predict thermodynamic 'parameters that are relevant for catalytic effects in gasification of biomass. The physical structure and its dependence of the char conversion and the pre-treatment of the raw straw is tested by ReaTech and The University of Roskilde. In case of positive results, plans for future pilot scale experiments will be made

Results

A comprehensive literature (Stoltze) search and quantum mechanical calculations suggest that alkali is bound as oxygen-alkali salt with a significant heat of bonding. This is in accordance with experiments made by Moilanen. The results suggest that chars from straws with a high alkali-salt to silicon ratio causes a steadily increasing catalyst/carbon ratio and thus increasing reactivity as a function of conversion. Furthermore, the internal area evolution as measured by the BET technique does not support a steeply increasing reactivity as a function of conversion caused by internal area evolution only. According to a simplified formulation the reactivity is proportional to the amount of independent water-soluble catalyst compounds weighed by coefficients characteristic for the individual compounds. Therefore when catalysts are catalysts with low catalytic coefficients, e.g., K_3PO_4 or reacted into non-soluble compounds like potassium calcium silicates or potassium aluminum silicates the reactivity is decreased as observed earlier. Experiments made in a H_20 and C0_2 atmosphere with very little H_2 and CO available suggests that two significantly different types of CO desorption step are important, one fast and one slow reaction pathway (Barrio). In accordance to Global Equilibrium Analysis (GEA) the strongest ash sintering was experimentally observed for wheat straws rich in silicon and with a low reactivity, while highly reactive straw rich in potassium but poor in silicon caused much less sintering, little slag formation but significant salt formation. In order to reduce the sintering tendency of fuels rich in potassium the use of kaolin and magnesium oxide additives had a great preventive effect on bed agglomeration and freeboard deposit formation in the VTT bench-scale bubbling fluidised-bed gasification tests carried out with straw. Calcium added in the form of ions in the form of calcium acetate to straw or a calcium hydroxide/calcium saccharate solution into straw pellets and calculations indicated that the major role of reactive calcium is to bind silicon. High-temperature diffraction measurements suggests that the reaction takes place rapidly after that the carbonaceous material (molasses/saccharate) is converted, i.e. at high degrees of conversion. A dissolved or activated calcium and phosphate additive mixture, 'CAP', apparently effectively binds corrosive potassium and sodium elements into very stable, less sintering and less-corroding compounds. Atmospheric fluidised bed gasification tests were made, where the addition of the CAP additive greatly reduced sintering and agglomeration. Additionally two tons of the pelletised additive-impregnated Wheat 2000+ straw could be gasified during a four days test-run in a two-stage gasifier with a dry straw conversion of 98 wt.%. During the test there were no signs of agglomeration or sintering in the char bed

Key figures

Period:
2000 - 2002
Funding year:
2000
Own financial contribution:
2.19 mio. DKK
Grant:
1.71 mio. DKK
Funding rate:
44 %
Project budget:
3.90 mio. DKK

Category

Oprindelig title
Optimering af cirkulerende fluid-bed forgasningsprocesser til biomasse/halm (OCIFF)
Programme
EFP
Technology
Bio and waste
Project type
Udvikling
Case no.
1373/00-0032

Contact

Kontakperson
Holst Sørensen, Lasse
Comtact information
ReaTech
P.O. Box 30
DK-4000 Roskilde, Denmark
Holst Sørensen, Lasse , 46775932, LHS-ReaTech@Catscience.dk
Øvr. Partnere: Elkraft; Danmarks Tekniske Universitet. Energiteknik; Danmarks og Grønlands Geologiske Undersøgelse (GEUS); Aalborg Universitet Esbjerg. Kemiteknik; Roskilde Universitetscenter. IMFUFA; Oslo Universitet. Kjemisk Institut (NO); VTT Energy (FI)

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