Study for Catalytical Degradation of Pyrolytic Oil from Municipal Plastic Waste

2012 ◽  
Vol 518-523 ◽  
pp. 3488-3495
Author(s):  
Jian Yang ◽  
Qian Wu ◽  
Zhi Rong Zhu

HY zeolite showed better catalytic activities than FCC in the catalytical degradation of pyrolytic oil. This conclusion can be got through the evaluation experiment. HY zeolite catalysts were chosen to study the influence of operating conditions in the degradation of pyrolytic oil with different raw material concentration, reaction temperature and the amount of catalyst. Through the orthogonal test, the optimal conditions were got as follow: the reaction temperature was 450°C, the pyrolytic oil concentration was 30wt.%, and the amount of catalysts was 3g.

2013 ◽  
Vol 634-638 ◽  
pp. 1513-1517
Author(s):  
Ping Lan ◽  
Yu Xian Feng ◽  
A Ming Chen ◽  
Lei Lei Qiao ◽  
Li Hong Lan ◽  
...  

Magnetic cassava starch microspheres have been prepared by means of the method of precipitation magnetization, cassava starch as raw material adsorbing or embedding Fe3O4, many influence factors on magnetic cassava starch iron rate such as pH, reaction time, stirring speed, ratio of Fe+3 to Fe+2, reaction temperature also investigated in this paper. On the base above research, we preliminary got the optimal conditions on the synthesis of magnetic cassava starch microspheres.


Energies ◽  
2020 ◽  
Vol 13 (5) ◽  
pp. 1284 ◽  
Author(s):  
Mohammed Al-asadi ◽  
Norbert Miskolczi

This work is dedicated to the high temperature pyrolysis of municipal plastic waste using Me/Ni/ZSM-5 catalysts. Catalysts were synthetized by wet impregnation. In addition to nickel, synthetic zeolite catalysts contain calcium, ceria, lanthanum, magnesia or manganese. Catalysts were prepared and tested using 0.1, 0.5 and 2.0 Me/Ni ratios. Catalyst morphology was investigated by SEM and surface analysis. Higher concentrations of second metals can block catalyst pore channels due to the more coke formation, which leads to smaller surface area. Furthermore, the chemicals used for the impregnation were among the catalyst grains, especially in case of 2.0 Me/Ni ratios. For pyrolysis, a horizontal tubular furnace reactor was used at 700 °C. The highest hydrogen and syngas yields were observed using ceria- and lanthanum-covered catalysts. The maximum production of syngas and hydrogen (69.8 and 49.2 mmol/g raw material) was found in the presence of Ce/Ni/ZSM-5 catalyst with a 0.5 Me/Ni ratio.


2013 ◽  
Vol 544 ◽  
pp. 13-16
Author(s):  
Jing Xu

The homogeneous precipitation pathway was explored to synthesize ultrafine powders of Al(OH)3. In the experiment, the scrap aluminum were used as raw material . The effects of reaction time, reaction temperature, stirring speed, concentration of sulphuric acid and dispersant on the preparation process were investigated. The results showed that ultrafine Al(OH)3 powders can be yielded and well-controlled under the following optimal conditions: the concentration of sulphuric acid 3.0 mol•L-1, reaction temperature 0-4 °C, stirring speed 900 r.min-1 and reaction time 15 min. The diameter less than 100nm of sphericity Al(OH)3 particles with the narrow distribution were successfully obtained. The Al(OH)3 powders was analyzed with scanning electron microscopy , infrared spectrometer. The Al(OH)3 powders have good dispersancy and purity is more than 90%. The operation of the experiment was very simple, and the particles were separated easily.


2021 ◽  
Vol 10 (1) ◽  
pp. 874-881
Author(s):  
Xin Zhou ◽  
Ge Gao ◽  
Guangxiang He ◽  
Xiaoyan Guo ◽  
Haibo Jin ◽  
...  

Abstract The side-chain alkylation of cumene and ethylene over a solid superbase catalyst K/KOH/γ-Al2O3 is investigated. The effects of the reaction temperature, pressure, and time on the conversion of cumene and selectivity of tert-amylbenzene (TAB) are discussed. The experimental results show that the conversion of cumene to tert-pentylbenzene increases with the increase in reaction temperature and ethylene pressure. The catalytic reaction has certain operational flexibility in terms of the reaction temperature, pressure, and time. In addition, the catalytic reaction can achieve directional conversion. The optimum operating conditions are obtained using a single factor test. The conversion of cumene is 99.8% and the selectivity toward TAB is 97.9% under catalyst concentration of 4 wt%, reaction temperature of 55°C, reaction pressure of 0.45 MPa, and reaction time of 30 min. The deactivation of catalyst is mainly caused by oxygen and water in the raw material.


Holzforschung ◽  
2018 ◽  
Vol 73 (1) ◽  
pp. 3-13 ◽  
Author(s):  
Juan C. Solarte-Toro ◽  
Juan M. Romero-García ◽  
Ana Susmozas ◽  
Encarnación Ruiz ◽  
Eulogio Castro ◽  
...  

Abstract The aim of this work was to evaluate the economic feasibility of the bioethanol production (BEP) based on olive tree pruning (OTP) as a biomass feedstock with optimization of the dilute acid pretreatment in focus. For this, the BEP was simulated taking into account the influence of the operating conditions of the pretreatment stage. Then, the techno-economic results were analyzed by means of the response surface methodology (RSM). The results show that lowest price of BE was 1.94 USD l−1 with a yield of 174.12 l t−1 OTP under optimal conditions. As a conclusion, the raw material cost has a strong influence in the economic feasibility of the BEP from OTP. The inclusion of other processing lines into the process would improve the process economy.


2013 ◽  
Vol 320 ◽  
pp. 429-434
Author(s):  
Jun Jia ◽  
Yu Chao Qu ◽  
Yue Gao ◽  
Yong Peng Yuan ◽  
Kai Kai Wang ◽  
...  

By the method of high boiling solvent (HBS), HBS-lignin has been separated from pine-nut hull with 1,4-butanediol solution as solvent, and characterized by GPC, IR, 1HNMR and TG. The optimal conditions are described as: the ratio of solid raw material to solvent (g:mL) in 1:12, the amount of catalyst in 6%, the reaction time for 2 hrs, reaction temperature at 200°C, and 90% of 1,4-butanediol as the solvent, and the yield of lignin up to 70%. The hydroxyl value of obtained HBS-lignin is about 197.2mgKOH/g. Furthermore, the HBS-lignin replaces the partial PEG400 to employ the synthesis of lignin-PEG-PAPI. The experimental results indicate that mechanical properties and solvent resistance of lignin-PEG-PAPI are apparently improved with comparison to the PEG-PAPI.


Author(s):  
Yotwadee Hawangchu ◽  
Duangduen Atong ◽  
Viboon Sricharoenchaikul

Glycerol waste from biodiesel production can be converted to syngas (CO+H2) via a thermochemical conversion process. In this study, microwave was used to initiate a glycerol conversion reaction in a specially fabricated quartz tube reactor with a silicon carbide bed as the microwave absorber. A nickel-based catalyst and steam were added to the reacting bed to enhance production of hydrogen. By adjusting the microwave power level from 110 to 880 watt (W), the reaction temperature of 500°C to more than 1400°C could be rapidly achieved within a few minutes, which is much faster than heating by conventional furnaces. The gasification reaction commenced by feeding raw material continuously through the hot silicon carbide bed at a rate of 1 g/min with the O2 to fuel ratio varying from 0-0.25. The overall time for each trial was 20-30 minutes including preheating of the bed material. In contrast to typical biomass gasification, char and tar yields were small in most runs. In general, glycerol waste yielded higher syngas when compared with pure glycerol conversion. Complete conversion to gas product may be achieved at a power level of 440W. The maximum syngas production from glycerol waste without a catalyst was more than 23.98 L over 20 min run at 660 W with 0.25 O2 to fuel ratio. Overall content of other hydrocarbon gases was around 3-28 vol.% depending on operating conditions and raw material. Lower heating values (LHV) of product gas for glycerol waste were much higher for runs at 1.0 L/min carrier gas flow, ranging from 3.75-17.64 MJ/m3 while relatively stable LHV of 1.96-5.88 were obtained from 2.0 L/min flow. The addition of a catalyst significantly increased gas production at lower wattage runs where overall conversions were comparable to those of higher wattage experiments without catalysts. The maximum total conversion and LHV were obtained from 1%Ni/SiC catalyst at a reaction temperature of 600°C (330W) and no external O2 with a gas product heating value of 9.18 MJ/m3 and 1.32 H2 to CO ratio. From these results, the novel microwave-induced heating technique can be considered as an efficient option for conversion of glycerol waste via the gasification process to acceptable quality syngas.


2021 ◽  
Vol 14 (1) ◽  
Author(s):  
Alberto Palma ◽  
Javier Mauricio Loaiza ◽  
Manuel J. Díaz ◽  
Juan Carlos García ◽  
Inmaculada Giráldez ◽  
...  

Abstract Background Burning fast-growing trees for energy production can be an effective alternative to coal combustion. Thus, lignocellulosic material, which can be used to obtain chemicals with a high added value, is highly abundant, easily renewed and usually inexpensive. In this work, hemicellulose extraction by acid hydrolysis of plant biomass from three different crops (Chamaecytisus proliferus, Leucaena diversifolia and Paulownia trihybrid) was modelled and the resulting solid residues were used for energy production. Results The influence of the nature of the lignocellulosic raw material and the operating conditions used to extract the hemicellulose fraction on the heat capacity and activation energy of the subsequent combustion process was examined. The heat power and the activation energy of the combustion process were found to depend markedly on the hemicellulose content of the raw material. Thus, a low content in hemicelluloses resulted in a lower increased energy yield after acid hydrolysis stage. The process was also influenced by the operating conditions of the acid hydrolysis treatment, which increased the gross calorific value (GCV) of the solid residue by 0.6–9.7% relative to the starting material. In addition, the activation energy of combustion of the acid hydrolysis residues from Chamaecytisus proliferus (Tagasaste) and Paulownia trihybrid (Paulownia) was considerably lower than that for the starting materials, the difference increasing with increasing degree of conversion as well as with increasing temperature and acid concentration in the acid hydrolysis. The activation energy of combustion of the solid residues from acid hydrolysis of tagasaste and paulownia decreased markedly with increasing degree of conversion, and also with increasing temperature and acid concentration in the acid hydrolysis treatment. No similar trend was observed in Leucaena diversifolia (Leucaena) owing to its low content in hemicelluloses. Conclusions Acid hydrolysis of tagasaste, leucaena and paulownia provided a valorizable liquor containing a large amount of hemicelluloses and a solid residue with an increased heat power amenable to efficient valorization by combustion. There are many potential applications of the hemicelluloses-rich and lignin-rich fraction, for example as multi-components of bio-based feedstocks for 3D printing, for energy and other value-added chemicals.


2015 ◽  
Vol 713-715 ◽  
pp. 2909-2912
Author(s):  
Bin Zhao ◽  
Li Ke Zou ◽  
Guo Yong Li

Cuprous oxide catalyst was prepared and applied as photocatalist to treat chromium (VI) in wastewater, and the photocatalytic activity of the cuprous oxide was studied. The optimal conditions for the treatment was as follows: the pH of wastewater was 3, the amount of catalysts was 0.3 g/L, the reaction temperature was 60°C. Under the optimal conditions, the removal rate of chromium (IV) in wastewater reached 50% in the presence of cuprous oxide catalyst.


2012 ◽  
Vol 550-553 ◽  
pp. 1866-1870
Author(s):  
Xiao Dan Tang ◽  
Hai Yang Hang ◽  
Shao Yan Wang ◽  
Jing Xiang Cong

Gypenosides III is a major bioactive component which is rich in Gynostemma pentaphyllum. For better utilization of the native resource, response surface methodology was used to optimize the extraction conditions of gypenosides III from G. pentaphyllum. The effects of three independent variables on the extraction yield of gypenosides III were investigated and the optimal conditions were evaluated by means of Box-Behnken design. The optimal conditions are as follows: ratio of ethanol to raw material 25, extraction temperature 58°C and ultrasonic time 25min. Under these conditions, the yield of gypenoside III is 1.216±0.05%, which is agreed closely with the predicted yield value.


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