نتایج جستجو برای: fixed bed reactors

تعداد نتایج: 254658  

2001
JUN SEOK KIM Y. Y. LEE ROBERT W. TORGET

The kinetics of cellulose hydrolysis under extremely low acid (ELA) conditions (0.07 wt%) and at temperatures >200°C was investigated using batch reactors and bed-shrinking flow-through (BSFT) reactors. The maximum yield of glucose obtained from batch reactor experiments was about 60% for α-cellulose, which occurred at 205 and 220°C. The maximum glucose yields from yellow poplar feedstocks were...

Mohammad Faramarzian, Mohammad Hassan Ehrampoush, Mohammad Taghi Ghaneian, Zahra Derakhshan,

Introduction: The modeling aims to simulate or optimize a process in physical, chemical or biological environments and the derived model will provide a considerable assistance to generate data and predict unknown condition, in case of sufficient suitability. Unsuitable disposal and elimination of waste tires have polluted the environment and human life areas, it also have caused removal of a hu...

2008
Tobias Pröll Philipp Kolbitsch

A fluidized bed system combining two circulating fluidized bed reactors is proposed and investigated for chemical looping combustion using metal oxides as oxygen carriers. The global solids loop starts in one of the two reactors (primary reactor) where solids are entrained, separated from the gas in a cyclone and sent to the other reactor (secondary reactor) via a fluidized loop seal. From the ...

1999
A. Renken

The catalytic properties of Pd and Pt supported on woven glass fabrics were explored for liquid-phase hydrogenation of benzaldehyde as a model for three-phase catalytic reaction. The catalysts demonstrated high activity and are suitable materials to be used in reactors with structured catalytic bed. The main characteristics of catalytic bed are discussed. ( 1999 Elsevier Science Ltd. All rights...

Journal: :journal of chemical and petroleum engineering 2012
arezoo sadat emrani mohammad saber fatola farhadi

in this paper, modeling and optimization of fischer-tropsch synthesis is considered in a fixed-bed catalytic reactor using an industrial fe-cu-k catalyst. a one dimensional pseudo-homogenous plug flow model without axial dispersion is developed for converting syngas to heavy hydrocarbons. the effects of temperature, pressure, h2 to co ratio in feed stream, and co molar flow on the mass flow rat...

پایان نامه :وزارت علوم، تحقیقات و فناوری - دانشگاه شیراز - دانشکده عمران و محیط زیست 1394

تکنولوژی رشد چسبنده به صورت غوطه ور به منظور تصفیه فاضلاب، بیش از 60 سال است که مورد استفاده قرار می گیرد. اقدامات ابتدایی در این زمینه فرآیندهای استفاده شده در سال های 1930 تا 1940، شامل "هوادهی تماسی" بوده است. در دهه اخیر استفاده و به کارگیری سیستم رشد چسبنده به صورت غوطه ور، شکل بین المللی به خود گرفته است. اندازه کوچک و کاربری آسان سیستم رشد چسبنده به صورت غوطه ور، اولین عواملی هستند که مو...

2012
F. M. Hady

The natural convection flow over a surface embedded in saturated porous media is encountered in many engineering problems such as the design of pebble-bed nuclear reactors, ceramic processing, crude oil drilling, geothermal energy conversion, use of fibrous material in the thermal insulation of buildings, catalytic reactors and compact heat exchangers, heat transfer from storage of agricultural...

Journal: :International Journal of Chemical Engineering 2021

To overcome the weak point of gas type heating (failure in uniformly and persistently), liquid molten salt as a concentration solar energy was considered heat source for dry reforming. This high-temperature flowing through center tubular reactor supplies necessary heat. The dependence on number hydrogen production investigated under assumption fixed volume catalyst bed. By changing these number...

Journal: :Journal of the Environmental Engineering Division 1982

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