Naphtha cracking through a pulsed DBD plasma reactor: Effect of applied voltage, pulse repetition frequency and electrode material

► Plasma cracking of naphtha is investigated through pulsed DBD plasma reactor. ► Effect of applied voltage, pulse frequency and inner electrode material is examined. ► Product is hydrogen-rich gas which is free of carbon monoxide. ► A little amount of coke is produced during experiments. ► Continuo...

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Published in:Chemical engineering journal (Lausanne, Switzerland : 1996) Vol. 191; pp. 416 - 425
Main Authors: Jahanmiri, A., Rahimpour, M.R., Mohamadzadeh Shirazi, M., Hooshmand, N., Taghvaei, H.
Format: Journal Article
Language:English
Published: Oxford Elsevier B.V 15-05-2012
Elsevier
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Summary:► Plasma cracking of naphtha is investigated through pulsed DBD plasma reactor. ► Effect of applied voltage, pulse frequency and inner electrode material is examined. ► Product is hydrogen-rich gas which is free of carbon monoxide. ► A little amount of coke is produced during experiments. ► Continuous plasma cracking operation is done due to little coke deposition. In this study, a nano second pulsed dielectric barrier discharge plasma reactor has been investigated for conversion of heavy naphtha. Continuous liquid hydrocarbons cracking and instant production of hydrogen and light gaseous hydrocarbons in the range of C1–C3 have been studied at room temperature and atmospheric pressure by using argon as a carrier gas. The effect of applied voltage, pulse frequency and inner electrode material has been examined on the quantity and quality of products. Aluminum, copper, stainless steel, iron and brass have been selected to investigate the effect of electrode material. Results show that applied voltage, pulse repetition frequency and inner electrode material, affect the energy efficiency of the plasma cracking process. Stainless steel has been selected due to its high performance among all tested materials. The highest process efficiency has been obtained at 7kV and 18kHz which was 79.38lkWh−1 for 1mlmin−1 of feed injection and 24.70W input power. In this condition, the generation rate of hydrocarbon is 22.50mlmin−1. Results indicate that the hydrocarbon product distribution during the process is ethylene≫C2>C1≫C3.
Bibliography:http://dx.doi.org/10.1016/j.cej.2012.02.031
ObjectType-Article-1
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ISSN:1385-8947
1873-3212
DOI:10.1016/j.cej.2012.02.031