A dual-reactor, assembled with the on-line syngas conditioning and methanol synthesis, was successfully applied for high efficient conversion of rich CO2 bio-oil derived syngas to bio-methanol. In the forepart catalys...A dual-reactor, assembled with the on-line syngas conditioning and methanol synthesis, was successfully applied for high efficient conversion of rich CO2 bio-oil derived syngas to bio-methanol. In the forepart catalyst bed reactor, the catalytic conversion can effectively adjust the rich-CO2 crude bio-syngas into the CO-containing bio-syngas using the CuZnA1Zr catalyst. After the on-line syngas conditioning at 450℃, the CO2/CO ratio in the blo- syngas significantly decreased from 6.3 to 1.2. In the rearward catalyst bed reactor, the conversion of the conditioned bio-syngas to bio-methanol shows the maximum yield about 1.21 kg/（kgcatarh） MeOH with a methanol selectivity of 97.9% at 260 ~C and 5.05 MPa using conventional CuZnA1 catalyst, which is close to the level typically obtained in the conventional methanol synthesis process using natural gas. The influences of temperature, pressure and space velocity on the bio-methanol synthesis were also investigated in detail.展开更多
This study explores the synthesis of bio-methanol from biogas,focusing on the optimization of carbon dioxide(CO_(2))separation via alternating pressure adsorption and subsequent methanol production using varying metha...This study explores the synthesis of bio-methanol from biogas,focusing on the optimization of carbon dioxide(CO_(2))separation via alternating pressure adsorption and subsequent methanol production using varying methane(CH_(4))ratios.Methanol synthesis was conducted under CH_(4)/CO_(2)ratios of 30/70,50/50,and 70/30,utilizing both pure water and methanol solutions at concentrations of 10%,20%,30%,and 40%.The results demonstrated that increasing the CH_(4)ratio led to enhanced CO_(2)conversion,with maximum values of 42.59%and methanol production reaching 3,850 g/day.The study further investigated the refining process of crude methanol,achieving a purity exceeding 99%through a three-column distillation approach.Notably,the recycling of waste methanol significantly improved both methanol yield and CO_(2)consumption,indicating a promising pathway for sustainable bio-methanol production.Overall,this research highlights the potential of integrating biogas utilization with efficient methanol synthesis and refining processes.展开更多
利用自制的酶柱反应器,通过改变反应液流量、溶剂的种类、反应时间以及水含量等参数,考察了大豆油和甲醇在固定化脂肪酶(Cand ida sp.99-125)催化下进行酯交换反应制备生物柴油的工艺条件,并用气相色谱对产物进行了分析。实验结果表明,...利用自制的酶柱反应器,通过改变反应液流量、溶剂的种类、反应时间以及水含量等参数,考察了大豆油和甲醇在固定化脂肪酶(Cand ida sp.99-125)催化下进行酯交换反应制备生物柴油的工艺条件,并用气相色谱对产物进行了分析。实验结果表明,反应液流量和水含量对转化率影响比较大,转化率随反应液流量的增加出现先增后减的趋势,采用正己烷为溶剂要优于其它溶剂。当以固定化的脂肪酶为催化剂、正己烷为溶剂、n(大豆油)∶n(甲醇)=1∶3、m(大豆油)∶m(水)=5∶1、反应时间为24h、反应液流量1.2mL/m in时,产物中主要脂肪酸甲酯的质量分数可以达到91.87%。展开更多
基金This work was supported by the National High Tech Research and Development Program （No.2009AA05Z435）, the National Basic Research Program of Ministry of Science and Technology of China （No.2007CB210206）, and the National Natural Science Foundation of China （No.50772107）.
文摘A dual-reactor, assembled with the on-line syngas conditioning and methanol synthesis, was successfully applied for high efficient conversion of rich CO2 bio-oil derived syngas to bio-methanol. In the forepart catalyst bed reactor, the catalytic conversion can effectively adjust the rich-CO2 crude bio-syngas into the CO-containing bio-syngas using the CuZnA1Zr catalyst. After the on-line syngas conditioning at 450℃, the CO2/CO ratio in the blo- syngas significantly decreased from 6.3 to 1.2. In the rearward catalyst bed reactor, the conversion of the conditioned bio-syngas to bio-methanol shows the maximum yield about 1.21 kg/（kgcatarh） MeOH with a methanol selectivity of 97.9% at 260 ~C and 5.05 MPa using conventional CuZnA1 catalyst, which is close to the level typically obtained in the conventional methanol synthesis process using natural gas. The influences of temperature, pressure and space velocity on the bio-methanol synthesis were also investigated in detail.
基金funding from the National Science,Research and Innovation Fund(NSRF)via the Program Management Unit for Human Resources&Institutional Development,Research and Innovation[grant number B40G660043].
文摘This study explores the synthesis of bio-methanol from biogas,focusing on the optimization of carbon dioxide(CO_(2))separation via alternating pressure adsorption and subsequent methanol production using varying methane(CH_(4))ratios.Methanol synthesis was conducted under CH_(4)/CO_(2)ratios of 30/70,50/50,and 70/30,utilizing both pure water and methanol solutions at concentrations of 10%,20%,30%,and 40%.The results demonstrated that increasing the CH_(4)ratio led to enhanced CO_(2)conversion,with maximum values of 42.59%and methanol production reaching 3,850 g/day.The study further investigated the refining process of crude methanol,achieving a purity exceeding 99%through a three-column distillation approach.Notably,the recycling of waste methanol significantly improved both methanol yield and CO_(2)consumption,indicating a promising pathway for sustainable bio-methanol production.Overall,this research highlights the potential of integrating biogas utilization with efficient methanol synthesis and refining processes.
文摘利用自制的酶柱反应器,通过改变反应液流量、溶剂的种类、反应时间以及水含量等参数,考察了大豆油和甲醇在固定化脂肪酶(Cand ida sp.99-125)催化下进行酯交换反应制备生物柴油的工艺条件,并用气相色谱对产物进行了分析。实验结果表明,反应液流量和水含量对转化率影响比较大,转化率随反应液流量的增加出现先增后减的趋势,采用正己烷为溶剂要优于其它溶剂。当以固定化的脂肪酶为催化剂、正己烷为溶剂、n(大豆油)∶n(甲醇)=1∶3、m(大豆油)∶m(水)=5∶1、反应时间为24h、反应液流量1.2mL/m in时,产物中主要脂肪酸甲酯的质量分数可以达到91.87%。
