在固定床加氢微反装置上,采用硫化态Ni Mo W/Al2O3催化剂,以廊乡林业局轻质木焦油(<300℃馏分)为原料考察反应条件对加氢脱氧性能的影响。结果表明,适当降低反应空速、提高反应压力、提高反应温度均有利于提高催化剂加氢脱氧反应活性...在固定床加氢微反装置上,采用硫化态Ni Mo W/Al2O3催化剂,以廊乡林业局轻质木焦油(<300℃馏分)为原料考察反应条件对加氢脱氧性能的影响。结果表明,适当降低反应空速、提高反应压力、提高反应温度均有利于提高催化剂加氢脱氧反应活性,提高加氢产物的热值。在反应温度380℃、反应压力8.0MPa、体积空速0.8h-1、氢/油体积比800∶1的条件下,加氢生成油的氧含量明显降低,热值显著提高。轻质馏分油可作为化工轻油原料进行下游加工,中质馏分油主要技术指标均符合船用馏分燃料油(GB/T17411-1998)标准要求,可直接作为船用燃料油调和组分使用。展开更多
The pyrolysis of different waste polymers （polyethylene, polypropylene and polystyrene） was investigated in a tube reactor at 550 ℃ in the absence of oxygen. Additionally the energetic utilization of products have ...The pyrolysis of different waste polymers （polyethylene, polypropylene and polystyrene） was investigated in a tube reactor at 550 ℃ in the absence of oxygen. Additionally the energetic utilization of products have also been followed both in refining and petrochemical industry. Pyrolysis products were separated into fractions of gases, naphtha, middle distillates and heavy oil. Raw materials have been collected both from industrial and household sources： polyethylene from agriculture, polyethylene from packaging and polystyrene from packaging and electronic equipments. Yields and properties of volatile products have changed by the raw materials. Products have been analyzed by gas chromatography. Fourier transformed infrared spectroscopy, size exclusion chromatography and other standardized methods. Naphtha had high octane numbers （80 〈 RON）, while high cetane numbers （〉 75） in case of middle distillates. Moreover fractions contained approximately half of unsaturated hydrocarbons, mainly α-olefins, but the percentage was depending on the raw materials. These properties are advantageous for fuel-like applications.展开更多
Using novel catalyst the pyrolysis of mixed plastics has been considered as an effective way to convert waste plastics into environmental friendly and industrially useful hydrocarbon gas and liquid products. Catalytic...Using novel catalyst the pyrolysis of mixed plastics has been considered as an effective way to convert waste plastics into environmental friendly and industrially useful hydrocarbon gas and liquid products. Catalytic cracking is a promising alternative for plastic wastes recycling. More than 99% of a polymer mixed converted into combustible hydrocarbon in a catalytic converting reaction. The products are mainly middle distillates. In this work equally weighted mixed HDPE （high density polyethylene）, LDPE （low density polyethylene） and Polypropylene were degraded. The reaction occurred in a semi batch reactor at several temperatures and catalyst/polymer ratios in search for an optimum operating condition. The products are liquid and gaseous hydrocarbons with minor of residue. The liquid and gas products were in the range of middle distillate cuts of gasoline, kerosene and gas oil. Finally, with a metallic base, yielded 99.5% of given mixed to valuable middle distillate products that include 86% liquid hydrocarbon and 13.5% gas, ranging between C1 and C5 with less percent of residue. The optimum condition for this yield reports at a temperature of 450 ℃ and 10% of catalyst w/w at atmosphere pressure.展开更多
文摘在固定床加氢微反装置上,采用硫化态Ni Mo W/Al2O3催化剂,以廊乡林业局轻质木焦油(<300℃馏分)为原料考察反应条件对加氢脱氧性能的影响。结果表明,适当降低反应空速、提高反应压力、提高反应温度均有利于提高催化剂加氢脱氧反应活性,提高加氢产物的热值。在反应温度380℃、反应压力8.0MPa、体积空速0.8h-1、氢/油体积比800∶1的条件下,加氢生成油的氧含量明显降低,热值显著提高。轻质馏分油可作为化工轻油原料进行下游加工,中质馏分油主要技术指标均符合船用馏分燃料油(GB/T17411-1998)标准要求,可直接作为船用燃料油调和组分使用。
文摘The pyrolysis of different waste polymers （polyethylene, polypropylene and polystyrene） was investigated in a tube reactor at 550 ℃ in the absence of oxygen. Additionally the energetic utilization of products have also been followed both in refining and petrochemical industry. Pyrolysis products were separated into fractions of gases, naphtha, middle distillates and heavy oil. Raw materials have been collected both from industrial and household sources： polyethylene from agriculture, polyethylene from packaging and polystyrene from packaging and electronic equipments. Yields and properties of volatile products have changed by the raw materials. Products have been analyzed by gas chromatography. Fourier transformed infrared spectroscopy, size exclusion chromatography and other standardized methods. Naphtha had high octane numbers （80 〈 RON）, while high cetane numbers （〉 75） in case of middle distillates. Moreover fractions contained approximately half of unsaturated hydrocarbons, mainly α-olefins, but the percentage was depending on the raw materials. These properties are advantageous for fuel-like applications.
文摘Using novel catalyst the pyrolysis of mixed plastics has been considered as an effective way to convert waste plastics into environmental friendly and industrially useful hydrocarbon gas and liquid products. Catalytic cracking is a promising alternative for plastic wastes recycling. More than 99% of a polymer mixed converted into combustible hydrocarbon in a catalytic converting reaction. The products are mainly middle distillates. In this work equally weighted mixed HDPE （high density polyethylene）, LDPE （low density polyethylene） and Polypropylene were degraded. The reaction occurred in a semi batch reactor at several temperatures and catalyst/polymer ratios in search for an optimum operating condition. The products are liquid and gaseous hydrocarbons with minor of residue. The liquid and gas products were in the range of middle distillate cuts of gasoline, kerosene and gas oil. Finally, with a metallic base, yielded 99.5% of given mixed to valuable middle distillate products that include 86% liquid hydrocarbon and 13.5% gas, ranging between C1 and C5 with less percent of residue. The optimum condition for this yield reports at a temperature of 450 ℃ and 10% of catalyst w/w at atmosphere pressure.
