Global warming awareness criticizes further usage of fossil fuels and insists promotion of renewable energy usage. Additionally, many people in rural areas of developing countries cannot access electricity. To solve t...Global warming awareness criticizes further usage of fossil fuels and insists promotion of renewable energy usage. Additionally, many people in rural areas of developing countries cannot access electricity. To solve this sort of energy crisis including global warming, current authors developed a proto-type of a pyrolysis plant equipped with a prevacuum chamber, which can be used to produce combustible gases for an engine generator in rural areas where people cannot access electricity. The plant is simple and easily maintained in consideration of special conditions that a rural area can receive very few maintenance service, technical assistance, and supply of spare parts. However, gas yield obtained by the proto-type of plant was around 20 wt% of feedstock. One way to enhance gas yield from this proto-type of plant is to utilize reaction of secondary tar cracking. This research work aims to examine possibility of gas yield enhancement keeping a simple structure of the proto-type of plant and using a simple technique of secondary tar cracking. Two tar cracking methods are examined: one is homogeneous tar cracking and the other is heterogeneous tar cracking using catalysis. In the homogeneous tar cracking, pyrolysis gases must be heated up to 650oC to 700oC and in the heterogeneous tar cracking, wood char is used as catalysis, because wood char is byproduct of pyrolysis. It is concluded that the homogeneous tar cracking is quite unlikely in the secondary chamber, but on the other hand, heterogeneous tar cracking using wood char can produce 30 wt% of gas yield from 1 kg of feedstock.展开更多
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
文摘Global warming awareness criticizes further usage of fossil fuels and insists promotion of renewable energy usage. Additionally, many people in rural areas of developing countries cannot access electricity. To solve this sort of energy crisis including global warming, current authors developed a proto-type of a pyrolysis plant equipped with a prevacuum chamber, which can be used to produce combustible gases for an engine generator in rural areas where people cannot access electricity. The plant is simple and easily maintained in consideration of special conditions that a rural area can receive very few maintenance service, technical assistance, and supply of spare parts. However, gas yield obtained by the proto-type of plant was around 20 wt% of feedstock. One way to enhance gas yield from this proto-type of plant is to utilize reaction of secondary tar cracking. This research work aims to examine possibility of gas yield enhancement keeping a simple structure of the proto-type of plant and using a simple technique of secondary tar cracking. Two tar cracking methods are examined: one is homogeneous tar cracking and the other is heterogeneous tar cracking using catalysis. In the homogeneous tar cracking, pyrolysis gases must be heated up to 650oC to 700oC and in the heterogeneous tar cracking, wood char is used as catalysis, because wood char is byproduct of pyrolysis. It is concluded that the homogeneous tar cracking is quite unlikely in the secondary chamber, but on the other hand, heterogeneous tar cracking using wood char can produce 30 wt% of gas yield from 1 kg of feedstock.
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。
