Abstract

The influence of different catalyst cobalt loadings on the C1–C3 hydrocarbon product yields and energy consumption in plasma-catalytic Fischer-Tropsch synthesis (FTS) was investigated from the standpoint of various reactor operating conditions: pressure (0.5 to 10 MPa), current (250 to 450 mA) and inter-electrode gap (0.5 to 2 mm). This was accomplished by introducing a mullite substrate, coated with 2 wt%-Co/5 wt%-Al2O3, 6 wt%-Co/5 wt%-Al2O3 or 0 wt%-Co/5 wt%-Al2O3 (blank catalyst), into a recently developed high pressure arc discharge reactor. The blank catalyst was ineffective in synthesizing hydrocarbons. Between the blank catalyst, 2 wt%, and the 6 wt% Co catalyst, the 6 wt% improved C1–C3 hydrocarbon production at all conditions, with higher yields and relatively lower energy consumption at (i) 10 MPa at 10 s, and 2 MPa at 60 s, for the pressure variation study; (ii) 250 mA for the current variation study; and (iii) 2 mm for the inter-electrode gap variation study. The inter-electrode gap of 2 mm, using the 6 wt% Co catalyst, led to the overall highest methane, ethane, ethylene, propane and propylene yields of 22 424, 517, 101, 79 and 19 ppm, respectively, compared to 40 ppm of methane and <1 ppm of C1–C3 hydrocarbons for the blank catalyst, while consuming 660 times less energy for the production of a mole of methane. Furthermore, the 6 wt% Co catalyst produced carbon nanotubes (CNTs), detected via transmission electron microscopy (TEM). In addition, scanning electron microscopy (SEM), energy dispersive x-ray spectroscopy (EDX) and x-ray diffraction (XRD) showed that the cobalt catalyst was modified by plasma treatment.

Highlights

  • Non-thermal plasma (NTP) has typically been restricted to ignition at low current (I < 1 A) and atmospheric pressure (P ~ 1 MPa) by electric discharges, such as the dielectric barrier discharge (DBD) and corona discharge

  • The study compares a blank, 2 wt% Co catalyst and 6 wt% Co catalysts in order to determine the contribution of different cobalt loadings to the plasma-catalytic synergistic effect

  • Trace quantities of C1 –C3 gaseous hydrocarbons were produced in the arc discharge reactor for both the blank, 2 wt%, and 6 wt% Co catalyst systems

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Summary

Introduction

Non-thermal plasma (NTP) has typically been restricted to ignition at low current (I < 1 A) and atmospheric pressure (P ~ 1 MPa) by electric discharges, such as the dielectric barrier discharge (DBD) and corona discharge. There is an increase in investment in FTS technology especially in the area of gas-to-liquid (GTL) and biomass-to-liquid (BTL) production This is an indication that FTS technology is poised to play a significant role in the global energy mix in the upcoming decades. The cost associated with a large volume reaction vessel and the high temperature required for the process has led researchers to investigate the design of a micro-channel reactor as an alternative method. This new approach is considered to potentially reduce the limitations associated with mass and heat transfer within the reactor

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