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K Gimouhopoulos, D Doulia, A Vlyssides and D Georgiou
Department of Chemical Engineering, National Technical University of Athens, Zografou Campus, Athens 157 80, Greece
Department of Chemical Engineering & Applied Chemistry, University of Toronto, 200 College Str., Toronto, Ont. M5S 3E5, Canada
Abstract
The disposal of municipal solid waste (MSW) is currently one of the main environmental concerns especially in the industrialized regions. Converting the organic fraction of MSW into useful products, e.g. gas and liquid fuels, seems to be an option of a great interest both environmentally and economically. This paper examines the results of coliquefaction of low-grade coal, e.g. lignite, with post-consumer plastics. Special catalysts were prepared for this purpose and tested along with different types of organic solvents. The presence of these solvents during the coliquefaction process almost doubled total solids conversion into gas and liquid products. Decane and toluene were found to be the best organic solvents for coliquefaction of lignite with high density polyethylene (HDPE) and polystyrene, respectively. Total solids conversion reached almost 90% when a two-stage process was employed.
K. Gimouhopoulos, D. Doulia, A. Vlyssides and D. Georgiou
Department of Chemical Engineering, National Technical University of Athens, Zografou Campus, Athens 157 80, Greece
Department of Chemical Engineering & Applied Chemistry, University of Toronto, 200 College Str., Toronto, ON MSS 3E5, Canada
Abstract
This paper presents a detailed study of post-consumer polymers coliquefaction with lignite assessing the feasibility of the new processes. The results of four series coprocessing experiments undertaken with and without catalysts on a suite of four heavy organic solvents are summarized initially. Taking into consideration the prescribed findings two newer series of experiments were also designed and carried out aiming at the optimization of this complex transformation using this time lignite oxidatively pretreated. The conversion of reacting solids into gaseous and liquid products and in particular into hexane and tetrahydrofuran (THF) soluble material was determined. It was found that the mentioned hydroliquefaction is a promising way of hydrocarbon synthesis and that oxidatively pretreated lignite proved more effective than the raw material since it promoted coliquefaction product yields sufficiently. It was also found that interactions and synergy of the catalysts employed was changing as a function of the solvents nature, influencing thus the efficacy of the conversions achieved."
As in other reputable research we've cited, the conversion of solids into liquid hydrocarbons was in the range of 90% when some specific waste plastics were combined with coal in a liquefaction process, even in the case of lower-rank, higher ash, lower-Btu coal such as Canadian lignite.
And, yet again, the word "synergy" is applied to describe the effect of adding what otherwise might become an environmental contaminant, or landfill occupant, to coal to enhance the productivity of coal-to-liquid conversion.
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Ronald W. Thring, Sai P. R. Katikaneni and Narendra N. Bakhshi
Department of Chemical Engineering, University of New Brunswick, P.O. Box 4400, Fredericton, New Brunswick, Canada E3B 5A3
Department of Chemical Engineering, University of Saskatchewan, Saskatoon, Saskatchewan, Canada S7N 5C4
The conversion of a solvolysis lignin to useful chemicals and fuels was investigated using HZSM-5 catalyst. The study was carried out in a fixed bed reactor operating at atmospheric pressure, over a temperature range of 500°C–650°C, and weight hourly space velocities of 2.5 to 7.5 h−1. The major objective was to investigate the use of HZSM-5 catalyst in the production of both liquid and gaseous hydrocarbon products directly from the lignin. Conversion was high and ranged between 50% and 85% for the reaction conditions used. Using a WHSV of 5 h−1, the liquid product (LP) yield was 39 wt.% at 500°C but decreased to 34 wt.% at 600°C and then to 11 wt.% at 650°C. The highest yield of liquid product (43 wt.%) was obtained at 550°C with a WHSV of 5 h−1. In all the experiments, the liquid product mainly consisted of aromatic hydrocarbons (mostly benzene, toluene and xylene — with toluene dominating). The yield of toluene increased from 31 wt.% of the liquid product at 600°C (WHSV=2.5 h−1) to 44 wt.% at 650°C (WHSV=5 h−1). The total gas yield increased dramatically with increasing temperature but only moderately with increasing WHSV. The yields of the major components in the gas stream (propane, ethylene, propylene, carbon dioxide and carbon monoxide) were greatly affected by temperature."
We've no idea what a "weight hourly space velocity (WHSV)" might be, but:
"HZSM-5 catalyst" is a zeolite, in all likelihood very similar to, or exactly the same as, the one specified by Exxon-Mobil in their "MTG", methanol-to-gasoline, Process; wherein the methanol is posited to be made from coal.
Since both lignin and, as we've earlier documented, cellulose, can both be converted into gasoline precursor hydrocarbons, 80% of a tree's weight can be converted into liquid transportation fuels, and most of that weight will be carbon recycled from atmospheric Carbon Dioxide.
Moreover, "benzene, toluene and xylene" are all useful as raw materials for synthesizing plastics, among other things, in addition to their use as building blocks for gasoline. Any of those compounds directed into plastics manufacturing would be, for all intents and purposes, along with their Carbon content, permanently "sequestered". Moreover, they, and their Carbon, would be sequestered for a profit, and not for a huge loss as would be incurred by pumping CO2 through miles of pipelines, and then stuffing it deep underground at high pressure, all to help Big Oil squeeze more of the stuff he extorts the rest of us with out of his drying-up reservoirs.
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