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甲醇甲烷联产工艺技术研究

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采用沉淀法制备了甲醇合成催化剂、甲烷合成催化剂,并将其应用于甲醇甲烷联产工艺流程中.针对甲醇甲烷联产工艺,考察了反应温度、反应压力、空速、进料组成、补碳等因素对甲醇、甲烷合成反应以及串联工艺的影响,反应温度、反应压力、空速、进料组成、补碳对甲醇、甲烷合成反应均有不同程度的影响;在空速为 8 000 h-1,反应压力为5.0 MPa,甲醇合成反应温度为230℃,甲烷合成反应温度为 320℃,原料气采用焦炉气补碳后组成(φ)为CO 7.9%、CO2 10.2%、H2 58.2%、CH4 23.7%的条件下进行了累计 500 h的稳定性试验.结果表明,CO总转化率高于 99.8%,CO2 总转化率高于 90.0%,产品中粗甲醇含量(w)大于 90.0%,CH4 含量(φ)大于 91.0%,甲醇合成反应段CO转化率高于60.0%,甲烷合成反应段CO转化率高于99.5%.
Study on the technology of methanol methane co-production
Methanol synthesis catalyst and methane synthesis catalyst are prepared by precipitation method and applied in the methanol methane co-production process.Regarding the methanol methane co-production process,the effects of reaction temperature,reaction pressure,space velocity,feed composition,carbon supplementation,and other factors on the methanol and methane synthesis reactions and the series process are investigated.Reaction temperature,reaction pressure,space velocity,feed composition,and carbon supplementation all have varying degrees of impact on the methanol and methane synthesis reactions.The stability test is conducted for a total of 500 hours under the conditions of space velocity of 8 000 h-1,reaction pressure of 5.0 MPa,methanol synthesis reaction temperature of 230℃,methane synthesis reaction temperature of 320℃,and feed gas composed(φ)of CO 7.9%,CO2 10.2%,H2 58.2%,and CH4 23.7%after carbon supplementation using coke oven gas.The results show that the total conversion rate of CO is higher than 99.8%,the total conversion rate of CO2 is higher than 90.0%,the crude methanol content(w)in the product is greater than 90.0%,the CH4 content(φ)is greater than 91.0%,the CO conversion rate in the methanol synthesis reaction section is higher than 60.0%,and the CO conversion rate in the methane synthesis reaction section is higher than 99.5%.

methanolmethaneco-productioncoke oven gascarbon supplementation

张杰

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中石化南京化工研究院有限公司,江苏南京 210048

甲醇 甲烷 联产 焦炉气 补碳

2024

能源化工
中国石化集团南京化学工业有限公司技术中心

能源化工

CSTPCD
影响因子:0.419
ISSN:2095-9834
年,卷(期):2024.45(3)