The effect of reactor scale on biochars and pyrolysis liquids from slow pyrolysis of coffee silverskin, grape pomace and olive mill waste, in auger reactors.

Several studies have addressed the potential biorefinery, through small-scale pyrolysis, of coffee silverskin (CSS), grape pomace (GP) and olive mill waste (OMW), which are respectively the main solid residues from coffee roasting, wine making and olive oil production processes. However, increasing the scale of reactor to bring these studies to an industrial level may affect the properties, and hence applications, of the resulting products. The aim of this study is therefore to perform pilot scale experiments to compare and verify the results of analytical study (TGA) and bench scale reactor runs, in order to understand the fundamental differences and create correlations between pyrolysis runs at different scales. To this end, pyrolysis liquids and biochars from the slow pyrolysis of CSS, GP and OMW, performed using different scale auger reactors (15 kg/h and 0.3 kg/h), have been analysed (TGA, pH, density, proximate and ultimate analyses, HHV, FTIR, GCMS) and compared. The results showed no major differences in biochars when the temperature and the solid residence time were fixed. However, regarding pyrolysis liquids, compounds from the lab reactor were more degraded than pilot plant ones, due to, in this case, the vapour residence time was longer. Regarding the properties of the pyrolysis products, GP 400 °C biochars showed the best properties for combustion; CSS biochars were especially rich in nitrogen, and 400 °C GP and OMW pyrolysis liquids showed the highest number of phenolics. Hence, this study is considered a first step towards industrial scale CSS, GP and OMW pyrolysis-based biorefinery.

Production of antioxidants and other value-added compounds from coffee silverskin via pyrolysis under a biorefinery approach.

The coffee roasting industry produces about 0.4 Mt of coffee silverskin (CSS) per year, the only residue generated from the roasting process that is mostly disposed as industrial waste. The aim of this study is to convert CSS into value-added products by intermediate pyrolysis, transforming the waste into a resource within an integrated biorefinery perspective. To this end, bio-oils and biochars from the intermediate pyrolysis of CSS at 280 °C, 400 °C and 500 °C have been studied. GC-MS analysis showed that bio-oils were composed of value-added products such as caffeine, acetic acid, pyridine and phenolics, the latter being the most interesting due to their antioxidant properties. Total phenolic content and antioxidant capacity of the samples were determined through Folin-Ciocalteu (FC) and DPPH methods, revealing an increase in phenolics in bio-oils compared to CSS extract directly from the feedstock. The bio-oil with the highest phenolic content and antioxidant properties was produced at 280 °C and contained 6.09 and 3.02 mg of gallic acid equivalents /g of bio-oil determined by FC and DPPH methods, respectively. This represents a global potential of up to 487 and 242 tones of gallic acid equivalents per year, considering the FC results and DPPH respectively. The resulting 280 °C biochar presented significant calorific values (22 MJ/kg), indicating its potential use as an energy source. Hence, CSS pyrolysis converts a waste into a by-product and a resource, increasing the environmental benefits and contributing to the circular economy and bioeconomy.