2 resultados para Batch-wise process

em AMS Tesi di Laurea - Alm@DL - Università di Bologna


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Supported by the increasing sustainable awareness, glycerol carbonate has gained much interest over the last 20 years because of its versatile reactivity and as a way to valorize waste glycerol. Numerous synthesis pathways for this molecule were identified, some of them very promising and on the verge of being applied at an industrial scale. Here, we report a study aimed at valorizing glycerol carbonate as chemical intermediate, in order to synthesize 2-hydroxymethyl-1,4-benzodioxane (HMB). This molecule finds important applications as key intermediate for the synthesis of a broad class of pharmaceuticals and therapeutic agents. Concerning the presence of a stereogenic center on the hydroxymethyl group, due to the pharmaceutical importance to obtain and isolate one single enantiomer, , nowadays HMB is obtained through batch scale process, using a multi-reaction approach and starting from reagents of the chiral pool. We carried out the reaction from a solution of glycerol carbonate and catechol 2:1. In the presence of a simple basic catalyst, at high temperatures, it was possible obtain total reactants conversion and high yield to HMB in few hours reaction time. Also, in the aim of developing a process which might adhere the principles of Green Chemistry, we avoided the use of solvents. Similar results were obtained using a 1:1 feed ratio of reactants, even if selectivity to HMB decrease, due to the presence of side reactions. A complete study of the reaction mechanism is proposed in this thesis.

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The first part of this essay aims at investigating the already available and promising technologies for the biogas and bio-hydrogen production from anaerobic digestion of different organic substrates. One strives to show all the peculiarities of this complicate process, such as continuity, number of stages, moisture, biomass preservation and rate of feeding. The main outcome of this part is the awareness of the huge amount of reactor configurations, each of which suitable for a few types of substrate and circumstance. Among the most remarkable results, one may consider first of all the wet continuous stirred tank reactors (CSTR), right to face the high waste production rate in urbanised and industrialised areas. Then, there is the up-flow anaerobic sludge blanket reactor (UASB), aimed at the biomass preservation in case of highly heterogeneous feedstock, which can also be treated in a wise co-digestion scheme. On the other hand, smaller and scattered rural realities can be served by either wet low-rate digesters for homogeneous agricultural by-products (e.g. fixed-dome) or the cheap dry batch reactors for lignocellulose waste and energy crops (e.g. hybrid batch-UASB). The biological and technical aspects raised during the first chapters are later supported with bibliographic research on the important and multifarious large-scale applications the products of the anaerobic digestion may have. After the upgrading techniques, particular care was devoted to their importance as biofuels, highlighting a further and more flexible solution consisting in the reforming to syngas. Then, one shows the electricity generation and the associated heat conversion, stressing on the high potential of fuel cells (FC) as electricity converters. Last but not least, both the use as vehicle fuel and the injection into the gas pipes are considered as promising applications. The consideration of the still important issues of the bio-hydrogen management (e.g. storage and delivery) may lead to the conclusion that it would be far more challenging to implement than bio-methane, which can potentially “inherit” the assets of the similar fossil natural gas. Thanks to the gathered knowledge, one devotes a chapter to the energetic and financial study of a hybrid power system supplied by biogas and made of different pieces of equipment (natural gas thermocatalitic unit, molten carbonate fuel cell and combined-cycle gas turbine structure). A parallel analysis on a bio-methane-fed CCGT system is carried out in order to compare the two solutions. Both studies show that the apparent inconvenience of the hybrid system actually emphasises the importance of extending the computations to a broader reality, i.e. the upstream processes for the biofuel production and the environmental/social drawbacks due to fossil-derived emissions. Thanks to this “boundary widening”, one can realise the hidden benefits of the hybrid over the CCGT system.