کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
210693 461721 2011 9 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Heat-integrated reactive distillation process for synthesis of fatty esters
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Heat-integrated reactive distillation process for synthesis of fatty esters
چکیده انگلیسی

Catalytic reactive distillation (RD) offers novel opportunities for manufacturing fatty acid alkyl esters involved in specialty chemicals and at a larger scale in biodiesel. The integration of reaction and separation into one RD unit, corroborated with the use of a heterogeneous catalyst, provides major benefits such as low capital investment and operating costs. This work presents a novel heat-integrated process based on reactive distillation that aims to reduce furthermore the energy requirements for biodiesel production, leading to competitive operating costs. Despite the high degree of integration, the process is well controllable using an efficient control structure proposed in this work. Rigorous simulations embedding experimental results were performed using computer aided process engineering tools, such as AspenTech Aspen Plus and Aspen Dynamics. The RD column was simulated using the rigorous RADFRAC unit with RateSep (rate-based) model, and explicitly considering three phase balances. Steady-state and dynamic simulation results are given for a plant producing 10 ktpy fatty acid methyl esters (FAME) from methanol and waste vegetable oil with high free fatty acids (FFA) content, using sulfated zirconia as green catalyst. The heat-integrated RD process eliminates all conventional catalyst related operations, efficiently uses the raw materials and the reactor volume offering complete conversion of the fatty acids and allowing significant energy savings. Remarkably, compared to previously reported RD processes, the energy requirements of this process are about 45% lower – only 108.8 kW h/ton biodiesel – while the capital investment cost remains the same as no additional equipment is required.

Research highlights
► Low capital investment and 45% less energy requirements for biodiesel production.
► Well controllable process using an efficient plantwide control structure.
► Rigorous Aspen Plus and Dynamics simulations embedding experimental results.
► Green/solid catalyst used to eliminates all conventional catalyst related operations.
► Efficient uses of the raw materials and the reactor volume allowing complete conversion.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fuel Processing Technology - Volume 92, Issue 7, July 2011, Pages 1288–1296
نویسندگان
,