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Hence, increased reactor temperature was suggested to allow faster foam drainage and breakdown which was reflected in the lower pressure drop levels as well as in the faster collapse in pressure drop when the flow was switched from gas to liquid feed.
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The size of the primary particle exhibited a minimum with increasing reactor temperature.
The methane conversion increased with increasing reactor temperature, oxygen input flow rate and steam methane ratio and decreased with increasing reactor pressure as expected.
Experimental results show that the Pt Sn/Al2O3 coated microchannel combustor was active enough to initiate hydrogen combustion at room temperature and able to increase reactor temperature up to 800 °C by hydrogen combustion uniformly.
The results show that an increased reactor exit temperature leads to a more controllable optimal design while a high activation energy results in a less controllable one.
A typical example is the hydrotreating process in petroleum refineries where the operators increase reactor temperature to compensate for catalyst deactivation.
An increased reactor coolant outlet temperature directly drives an increase of the nuclear fuel temperature.
The results indicated that the rate of CaO carbonation considerably increased with reactor temperature increasing from 500 °C to 595 °C.
There was a temperature difference of 5°C between the two reactors, 185°C at Case 1 and Case 2, and 190°C for Case 3 and Case 4, because of the limitation of steam supply with the increased reactor size.
Increasing the feed temperature in the steam reforming of methane increases the reactor temperature, causing the formation of coke filaments when the water concentration is not high enough.
It should be noted that increasing the reactor temperature has, as a consequence, two opposite effects: firstly, it increases the rate of reactions; secondly, it shifts WGS reaction to reactants.
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