“…The synergistic effects of carbon-containing functional groups and different types of proton are shown in Figures 2 and 3, respectively. The contents of aromatic carbon (16.60%, 11.19%, 8.4%) were greater than the theoretical values (16.17%, 10.98%, 7.86%), which may be due to the Diels-Alder reaction between the olefins derived from PP and the furans derived from CS [33][34][35][36][37][38], promoting the formation of aromatic compounds. Due to the addition of PP, the effective hydrogen-carbon ratio (H/Ceff ratio) of the system was increased, which reduced generation of polycyclic aromatic hydrocarbons (PAHs), so the content of H-PAH was far less than the theoretical value.…”
The pyrolysis behavior of corn stover and polypropylene during co-pyrolysis was studied using a tube furnace reactor. The effects of mixing ratio of corn stover and polypropylene, pyrolysis temperature, addition amount of catalyst (HZSM-5) and reaction atmosphere (N2 and CO2) on the properties of pyrolysis products were studied. The results showed that co-pyrolysis of corn stover and polypropylene can increase the yield of pyrolysis oil. When corn stover:polypropylene = 1:3, the yield of pyrolysis oil was as high as 52.1%, which was 4.5% higher than the theoretical value. With the increase of pyrolysis temperature, the yield of pyrolysis oil increased first and then decreased, and reached the optimal yield at 550 °C. The addition of catalyst (HZSM-5) reduced the proportion of oxygenates and promoted the generation of aromatic hydrocarbons. CO2 has a certain oxidation effect on the components of pyrolysis oil, which promoted the increase of oxygen-containing aromatics and the reduction of deoxy-aromatic hydrocarbons. This study identified the theoretical basis for the comprehensive utilization of plastic and biomass energy.
“…The synergistic effects of carbon-containing functional groups and different types of proton are shown in Figures 2 and 3, respectively. The contents of aromatic carbon (16.60%, 11.19%, 8.4%) were greater than the theoretical values (16.17%, 10.98%, 7.86%), which may be due to the Diels-Alder reaction between the olefins derived from PP and the furans derived from CS [33][34][35][36][37][38], promoting the formation of aromatic compounds. Due to the addition of PP, the effective hydrogen-carbon ratio (H/Ceff ratio) of the system was increased, which reduced generation of polycyclic aromatic hydrocarbons (PAHs), so the content of H-PAH was far less than the theoretical value.…”
The pyrolysis behavior of corn stover and polypropylene during co-pyrolysis was studied using a tube furnace reactor. The effects of mixing ratio of corn stover and polypropylene, pyrolysis temperature, addition amount of catalyst (HZSM-5) and reaction atmosphere (N2 and CO2) on the properties of pyrolysis products were studied. The results showed that co-pyrolysis of corn stover and polypropylene can increase the yield of pyrolysis oil. When corn stover:polypropylene = 1:3, the yield of pyrolysis oil was as high as 52.1%, which was 4.5% higher than the theoretical value. With the increase of pyrolysis temperature, the yield of pyrolysis oil increased first and then decreased, and reached the optimal yield at 550 °C. The addition of catalyst (HZSM-5) reduced the proportion of oxygenates and promoted the generation of aromatic hydrocarbons. CO2 has a certain oxidation effect on the components of pyrolysis oil, which promoted the increase of oxygen-containing aromatics and the reduction of deoxy-aromatic hydrocarbons. This study identified the theoretical basis for the comprehensive utilization of plastic and biomass energy.
“…29 The coke reduced from 2.27% to 1.18%. According to the report of Duan et al, 30 higher catalytic temperatures promote the decomposition of the long chain hydrocarbons and phenolic compounds, thus the number of the large molecules decreased and the light compound formed. In addition, the yield of char uctuated but remained relatively stable.…”
Section: Analysis Of Pyrolysis Product Yieldmentioning
confidence: 97%
“…32 By further observation, the bio-oil yield reduced (from 74.79% to 61.15%) and the gas yield increased (from 19.44% to 32.208%) with the increasing of the catalyst ratio, this phenomenon occurred because more catalyst aided the bio-oil cracking into gaseous compounds thus caused variation trend. 30 During the ex situ pyrolysis process, a small amount of the coke (3.51-0.96%) was obtained. With the decreasing of the catalyst to feedstock ratio, formation of the coke was hindered, because higher catalyst to feedstock ratio provided more locations for pyrolysis vapors to deposit on the catalyst.…”
Section: Analysis Of Pyrolysis Product Yieldmentioning
“…With the catalytic temperature increasing, the proportion of cycloalkenes and oxygenates of all the soapstocks initially decreased and then increased, reaching the minimum at 300°C. Duan et al [39] had explained the cause of oxygenates change. When the vapor generated from pyrolysis passed through HZSM-5, deoxidation and cracking reactions occurred.…”
Section: Effect Of Catalytic Temperature On Bio-oil Compositionmentioning
In this study, the effects of catalytic temperature and the type of soapstock on products from microwave-assisted pyrolysis were investigated. HZSM-5 was used as the catalyst to study the pyrolysis of six different soapstocks at 200°C, 300°C, and 400°C catalytic temperature. Results showed that the bio-oil yields initially increased and then decreased with the increase in catalytic temperature. When the catalytic temperature was 300°C, the bio-oil reached up to the maximum value (65.8 wt.%). Findings indicated that the composition of bio-oil was related to the degree of unsaturation of fatty acids sodium in the soapstocks. In the case of saturated fatty acid sodium, a series of alkanes was formed, whereas the pyrolysis of monounsaturated fatty acid sodium resulted mainly in cycloalkanes, the cycloalkenes obtained from bio-oil was produced by polyunsaturated fatty acid sodium.
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