Novel technologies to improve the performance of biomass pyrolsis systems

Shi-Shen Liaw

doi:10.7273/000005571

Biomass pyrolysis is a thermochemical conversion process to convert lignocellosic materials into bio-oil, gas, and char. The bio-oil can be further refined to produce transportation fuels, high-value chemicals and heat. Although fast pyrolysis is a very promising technology for high bio-oil production yield, the reactors used have several technological problems that limit their future techno-economic viability. Current fast pyrolysis reactors use large quantities of carrier gas that reduce their thermal efficiency. The use of sand to accelerate heating rates results in serious attrition problems responsible for sand contamination of the bio-char produced. Most of the fast pyrolysis reactors currently used need to process very small particles which consume large quantities of energy in grinding. The bio-oil produced is also highly acidic and corrosive mainly due to the presence of acetic acid. The lack of a viable technology to use the acetic acid contained in these oils is a major challenge for the development of viable bio-oil refineries. The objective of this dissertation is to evaluate several technologies to improve the techno-economic viability of biomass pyrolysis systems. The main hypotheses of this dissertation are: (1) high yields of bio-oils could also be obtained by using auger pyrolysis reactors using very low volumes of carried gas and no sand as a heat carrier if the system is fed with very small particles (2) The grinding energy can be reduced if the biomass is torrefied. There are torrefaction conditions that will not affect the overall yield of pyrolysis products (3) Acetic acid produced during pyrolysis can be removed with the use of a fractional condensation system (4) The acids produced during the torrefaction and pyrolysis with the use of the fractional condensation system can be anaerobically digested to produce methane. In this dissertation, it was proved through Py-GC/MS studies that yield of most of the pyrolytic products can be explained by grouping them in five groups or families. The C1 family is formed by products of cellulose fragmentation reactions (glycoaldehyde, acetol, 1,2-ethanediol, monoacetate, butanedial). The products grouped in the C2 family (levoglucosan, levoglucosenone, 1,4:3,6-dianhydro-alpha-D-glucopyranose) are derived from cellulose depolymerization reactions. The molecules derived from hemicellulose (Acetic acid, furfural, 2-furanmethanol) were grouped in the H family. The products derived from lignin were grouped in two families L1 (derived from p-hydroxyl phenol (H) and guaiacyl (G) structures) and L2 (derived from syringyl (S) structures). The yield and properties of bio-oil obtained from an auger pyrolysis reactor is comparable with other existing fluidized bed reactors in the similar pyrolysis condition. The system proposed required much lower volumes of carrier gas and result in the production of a sand-free bio-char. It was also found that the reactions leadings to the formation of bio-char products and the yield of bio-oil are not affected if the pretreatment (torrefaction) temperature is maintained below 290 C. Torrefaction at higher temperatures results in a dramatic reduction of the bio-oil yield and an increase in the bio-char yield. A condensation system coupled with the auger pyrolysis reactor was constructed and studied for the separation of crude bio-oil produced from Douglas Fir wood. As the first condenser temperature increases up to 80 C, the content of light oxygenated organic compounds (chiefly the acetic acid and water) in the first condenser decreased significantly. For the first time, this dissertation reports the anaerobic digestion of the aqueous phase obtained in the thermal pretreatment (torrefaction) step and in the second condenser during biomass pyrolysis to produce bio-methane. Acid washing was studied to minimize the inhibitors (hydroxyaceta

Novel technologies to improve the performance of biomass pyrolsis systems

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