کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
686956 1460094 2014 7 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Catalyst retention in continuous flow with supercritical carbon dioxide
ترجمه فارسی عنوان
احتباس کاتالیزور در جریان مداوم با دی اکسید کربن فوق بحرانی
کلمات کلیدی
دی اکسید کربن فوق بحرانی، جریان مداوم، کاتالیزور همگن، احتباس کاتالیست
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تکنولوژی و شیمی فرآیندی
چکیده انگلیسی


• This review provides an overview of catalyst retention and use of supercritical carbon dioxide in continuous flow processes.
• Discussed as methods for catalyst retention are catalyst immobilization, membrane reactors and biphasic processes.
• The added advantages of using micro- and milli-flow systems are considered.
• Future challenges are outlined for each method.

This review discusses the retention of organometallic catalysts in continuous flow processes utilizing supercritical carbon dioxide. Due to its innovative properties, supercritical carbon dioxide offers interesting possibilities for process intensification. As a result of safety and cost considerations, processes that use supercritical carbon dioxide are preferably done in continuous flow, as they require a pressure upwards of 74 bar. Many of the reactions that benefit from the application of supercritical carbon dioxide also involve the use of a homogeneous catalyst however, requiring efforts to recycle the catalyst when these are applied in continuous flow. Alternatively, the catalyst may be retained in the reactor by modifying the process or catalyst, such as by catalyst immobilization, membrane separation, or biphasic processing exploiting the properties of supercritical carbon dioxide. Each of these methods is discussed, including their advantages and drawbacks. Also discussed are milli- and micro-flow processes and their possibilities for integrated catalyst retention and handling supercritical carbon dioxide.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering and Processing: Process Intensification - Volume 83, September 2014, Pages 26–32
نویسندگان
, , , ,