“…Several approaches have been developed to utilize food waste to produce heat, power, biogas, biochar, bio-oil, and other important products using incineration [ 9 ], gasification [ 10 , 11 ], hydrothermal liquefaction [ 12 , 13 ], and pyrolysis [ 14 , 15 ]. However, incineration creates unpleasant gases and ash; gasification requires a lot of energy and has a high operating cost; and hydrothermal liquefaction has a high capital cost (expensive autoclaves), insufficient protection, and an unobservable reaction process [ 16 ].…”
“…Several approaches have been developed to utilize food waste to produce heat, power, biogas, biochar, bio-oil, and other important products using incineration [ 9 ], gasification [ 10 , 11 ], hydrothermal liquefaction [ 12 , 13 ], and pyrolysis [ 14 , 15 ]. However, incineration creates unpleasant gases and ash; gasification requires a lot of energy and has a high operating cost; and hydrothermal liquefaction has a high capital cost (expensive autoclaves), insufficient protection, and an unobservable reaction process [ 16 ].…”
“…The material decomposes into gas, bio-oil, and solid hydrocarbons during the pyrolysis process, which thermally decomposes organic molecules in an inert environment while anaerobically modifying their structure at a comfortable temperature (300-800 °C) Compared to paper waste and other biomass, plastic waste has a lower water content since it does not absorb water. Additionally, plastic has a calorific value comparable to fossil fuels like gasoline and diesel [2]. Plastic polymers can be divided into three primary categories: polypropylene, polyethylene, and polystyrene.…”
Section: Introductionmentioning
confidence: 99%
“…The quality of bio-oil can be improved by various processes, one of which is upgrading with a vacuum distillation process. The use of catalysts in the process of upgrading the quality of bio-oil has been widely carried out by previous researchers [2], [6][7][8] , but the improvement of the quality of bio-oil through the vacuum distillation process has not been widely carried out.…”
Since plastic and food waste are both types of non-lignocellulosic biomass, these must be handled and managed correctly to avoid pollution problems and damage to the environment. Bio-oil, made from recycled materials, including plastic and food waste, is one focus of these attempts. The co-pyrolysis method is being investigated in this study as a technique of recycling plastic waste and food waste to produce biofuels with reduced environmental impact. In terms of energy efficiency, bio-oil is unequal to other fuels like coal or natural gas because of its high acidity, high oxygen content, and low thermal stability. Therefore, a vacuum distillation process is required to improve bio-oil quality by adjusting the distillation temperature from 300 to 350 OC and the percentage of plastic waste used from 30 to 50%. The bio-oil was analyzed using a Gas Chromatography-Mass Spectrometer (GC-MS). The general compound showed that acids (60%) and alcohols (20%) were the most prevalent chemical compounds, followed by phenol (4%), aldehyde (14%), aliphatic (5%), Furan (14%), and ketones (11%) at maximum temperature (350 oC) for 30-50% plastic waste. Meanwhile, the final product is affected by temperature and plastic waste (PET) ratio factors. At 350 °C and a plastic waste addition of 50%, the highest bio-oil yield is 45%.
“…The current pilot-scale reactor was developed based on a literature review and the University of Illinois Urbana–Champaign (UIUC) team’s own experience on HTL of biomass waste, from batch to continuous and from lab scale to pilot scale. HTL of biowaste aims at not only producing biocrude oil but also mitigating the negative environmental effects of conventional biowaste disposal, such as greenhouse gas emissions and leachate during degradation in landfills . In 2000, He et al − reported conversion of swine manure into biocrude oil with a lab-scale batch reactor.…”
Section: Introductionmentioning
confidence: 99%
“…HTL of biowaste aims at not only producing biocrude oil but also mitigating the negative environmental effects of conventional biowaste disposal, such as greenhouse gas emissions and leachate during degradation in landfills. 23 In 2000, He et al 24−27 reported conversion of swine manure into biocrude oil with a lab-scale batch reactor. Based on the batch test, Ocfemia et al 28,29 developed and evaluated a continuous stirred tank reactor with a processing capacity of 2 L/h to convert swine manure into biocrude oil.…”
Pilot-scale hydrothermal liquefaction (HTL) of biowaste is a critical step toward commercialization of the HTL technology. Despite many HTL studies conducted with wet biomass, including food waste, few were performed with a pilot-scale continuous plug-flow reactor (PFR), with the biocrude yield and quality analysis based on dewatering (ASTM D2892 Annex X1). This paper describes the development and performance evaluation of a mobile pilot-scale HTL continuous PFR, with a processing capacity of 60 L/ h of wet feedstock and 6 L/h of biocrude production. The reactor system was designed for reaction conditions of up to 325 °C and 17.25 MPa. The reactor has a volume of 28.88 L with an additional counterflow heat exchanger volume of 18.07 L. Two types of food wastes, from a food processing plant and grocery store, were processed at 280 °C for 30 min, producing biocrude oil yields of 52.19 and 47.06 wt %, energy recoveries of 68.17 and 70.77%, and carbon recoveries of 66.91 and 64.78%, respectively. Due to its high feedstock capacity and reaction volume, large amounts of biocrude oil and post-HTL wastewater (PHW) were obtained from this pilot-scale reactor to allow downstream research on upgrading biocrude oil for transportation fuel as well as PHW treatment and nutrient recovery.
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