کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
7048259 | 1457126 | 2016 | 41 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Plant-wide control of coupled distillation columns with partial condensers
ترجمه فارسی عنوان
کنترل کامل ستون تقطیر شده با خازن های جزئی
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
جریان سیال و فرایندهای انتقال
چکیده انگلیسی
Common natural gas processing provides a specific example of this alternative control system. Natural gas commonly includes high concentrations of CO2 that must be removed prior to pipeline or LNG distribution. The existence of a minimum-boiling temperature azeotrope between ethane, virtually always present in natural gas, and carbon dioxide complicates the separation of CO2 from the hydrocarbons. This separation commonly employs extractive distillation with high-molecular-weight hydrocarbons. Our recent paper Ebrahimzadeh et al. (2016) discusses in detail the steady-state economic design of a new extractive distillation strategy for the CO2-ethane azeotrope separation with three columns. This strategy shows a 5% reduction in capital and 15% reduction in operating costs when compared to optimized versions of the conventional process. The new strategy also produces CO2 in a liquid rather than a vapor phase, which simplifies transport, storage, and handling. Two columns of the proposed design use partial condensers and are the focus of this investigation.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Applied Thermal Engineering - Volume 102, 5 June 2016, Pages 785-799
Journal: Applied Thermal Engineering - Volume 102, 5 June 2016, Pages 785-799
نویسندگان
Edris Ebrahimzadeh, Larry L. Baxter,