[1]曾宏,林少杰,方柏山.生物柴油酸催化甲醇法生产工艺全流程模拟与经济分析[J].华侨大学学报(自然科学版),2014,35(1):67-71.[doi:10.11830/ISSN.1000-5013.2014.01.0067]
　ZENG Hong,LIN Shao-jie,FANG Bai-shan.Process Simulation Analysis on Acid Catalysis Method for Biodiesel Production[J].Journal of Huaqiao University(Natural Science),2014,35(1):67-71.[doi:10.11830/ISSN.1000-5013.2014.01.0067]
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生物柴油酸催化甲醇法生产工艺全流程模拟与经济分析()
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《华侨大学学报（自然科学版）》[ISSN:1000-5013/CN:35-1079/N]

卷:
第35卷
期数:
2014年第1期
页码:
67-71
栏目:
出版日期:
2014-01-20

文章信息/Info

Title:
Process Simulation Analysis on Acid Catalysis Method for Biodiesel Production
文章编号:
1000-5013(2014)01-0067-05
作者:
曾宏1; 2;  林少杰2;  方柏山3; 4
1. 华侨大学 化工学院, 福建 厦门 361021;2. 泉州师范学院 化学与生命科学学院, 福建 泉州 362000;3. 厦门大学 化学化工学院, 福建 厦门 361005;4. 厦门大学 醇醚酯化工清洁生产国家工程实验室, 福建 厦门 361005
Author(s):
ZENG Hong1; 2;  LIN Shao-jie2;  FANG Bai-shan3; 4
1. College of Chemical Engineering, Huaqiao University, Xiamen 361021, China; 2. College of Chemistry and Life Sciences, Quanzhou Normal University, Quanzhou 362000, China; 3. College of Chemistry and Chemical Engineering, Xiamen University, Xiamen 361005
关键词:
生物柴油;  甘油三油酸酯;  酸催化甲醇法;  过程仿真;  经济分析
Keywords:
biodiesel;  glycerol trioleate;  acid catalyzed methanol method;  process simulation;  economic analysis
分类号:
TQ018;TQ9
DOI:
10.11830/ISSN.1000-5013.2014.01.0067
文献标志码:
A
摘要:
应用SuperPro Designer流程模拟软件,对生物柴油酸催化甲醇法工艺进行全过程仿真模拟与计算,并技术经济分析.模拟结果表明:主要过程数据符合实验结果,生物柴油产品脂肪酸甲酯(FAME)质量分数大于97%,满足欧盟生物柴油标准,工艺流程设计合理.经济分析表明:年产8 000 t生物柴油的酸催化甲醇法工艺,其直接固定成本约2 078 万元,其中主要设备购置成本为363 万元,原料成本占操作成本71%以上;项目总投资约2 572 万元,税后净利润可达962 万元·a-1,投资收益
Abstract:
The Superpro Designer emluator was used to design and simulate the whole process of acid catalyzed methanol method technology for biodiesel production, by coupling with costing and economic evaluation of flowsheeting. Simulation results indicated that the process design was reasonable with main process data in agreement with experimental results. The mass fraction of fatty acid methyl ester(FAME)in biodiesel products was more than 97%, which met the EU biodiesel standards. The economic analysis showed that the direct fixed capital cost(DFC)was about 20.78 million CNY for acid catalyzed methanol technology of a 8 000 ton per year. The main equipment purchase cost was about 3.63 million CNY, and the cost of raw materials accounted for over 71% of the operating costs. The expected return on investment(ROI)was to reach 37.39% of approximately 25.72 million CNY project total investments, as the after-tax profits about 9.62 million CNY per year.

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备注/Memo

备注/Memo:
收稿日期: 2013-03-29
通信作者: 曾宏(1977-),男,副教授,博士,主要从事生物化工工艺的研究.E-mail:hongzeng@126.com.
基金项目: 福建省高校产学合作科技重大项目(2010H6023); 福建省教育厅A类科技项目(JA11219); 福建省泉州市技术研究与开发项目(2010G6)
更新日期/Last Update: 2014-01-20