Examples of 'oxidation reactor' in a sentence
Meaning of "oxidation reactor"
Oxidation reactor: An oxidation reactor is a device used in chemical processes to facilitate oxidation reactions. It provides the necessary conditions, such as temperature, pressure, and catalysts, to promote the conversion of a substance into its oxidized form. Oxidation reactors are commonly used in industries such as petrochemicals, pharmaceuticals, and environmental engineering.
How to use "oxidation reactor" in a sentence
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Advanced
oxidation reactor
The oxidation reaction is conducted in an oxidation reactor.
The oxidation reactor is generally a fixed bed multitubular reactor.
The reduction reactor is associated with an oxidation reactor.
Many partial oxidation reactor systems include a quench chamber.
This feed was then subjected to a second oxidation reactor.
The oxidation reactor can comprise one or more reactor vessels.
Methylnapthalene is fed into an oxidation reactor.
Supercritical water oxidation reactor with wall conduits for boundary flow control.
The methylnaphthalene fraction is fed into an oxidation reactor.
Methods of feeding air into the oxidation reactor are well known in the art.
The resulting stream is introduced into an ammoxidation or oxidation reactor.
The catalyst in the catalytic partial oxidation reactor preferably contains a platinum group metal.
The metal oxide is then recycled to the oxidation reactor.
Most of the ethylbenzene leaves the oxidation reactor as solvent for the ethylbenzene hydroperoxide.
Oxidant gas is also introduced into the oxidation reactor.
See also
The liquid oxidation reactor consists of two discrete process zones partitioned by a gas containment baffle.
This technology is referred to as the liquid oxidation reactor technology.
The wet oxidation reactor comprises one or more reactor vessels 50 connected in series.
One subsidiary stream is returned directly to the oxidation reactor.
Residence time in the oxidation reactor was 4 hours.
Said unreacted ethylbenzene may be recycled to the oxidation reactor.
The process of claim 1 wherein said oxidation reactor is a bubble column reactor.
This recycle stream is introduced into the selective oxidation reactor.
The catalyst in the catalytic partial oxidation reactor is rhodium supported on MgO or MgAl2O4.
The oxidation zone comprises at least one oxidation reactor.
If a separate oxidation reactor is used, the air is passed exclusively through this reactor.
Planar ceramic membrane assembly and oxidation reactor system.
The vapor space of the liquid oxidation reactor is normally operated under non-flammable conditions.
These are dissolved in water and then recycled to the oxidation reactor.
First, the amount of oxygen entering the oxidation reactor can be reduced by other means.
Decrease the circulation rate of the metal oxides in the oxidation reactor.
Likewise, in the oxidation reactor embodiment of Fig.
The refractory may be any effective material for a partial oxidation reactor.
And the oxidation reactor comprising,.
This solvent ratid is similar to that expected in the oxidation reactor effluent.
The liquid oxidation reactor comprises,.
Increase of a production scale of a plant requires increase of production per oxidation reactor.
This allows therefore the lower pressure oxidation reactor to take the form of a tank.
The dehydrated acetic acid is then recycled at least in part to the oxidation reactor.
Although optional in the continuous oxidation reactor system shown in Fig.
The buffering compounds must be tolerated by the bacteria present in the oxidation reactor.
Figure 1 is a simplified diagram of an oxidation reactor of the present invention.
Maleic anhydride is separated from the gaseous effluenct downstream of the oxidation reactor.
Although the catalyst filter 9 in the oxidation reactor system shown in Figs.
Such burners are used to simultaneously introduce the various feedstreams into the partial oxidation reactor.
The cumene left unoxidized after passing the last oxidation reactor is separated from the CHP.
The present invention relates to a method for increasing the rated capacity of a commercial oxidation reactor.
This time, residence time in the oxidation reactor was 2 hours.
These catalyst components are recovered from the water stream and recycled to the oxidation reactor.
Preferably, the reaction medium in the oxidation reactor in step ( e ) is buffered.
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