Examples of 'column reactor' in a sentence
Meaning of "column reactor"
column reactor - This phrase seems to refer to a specific type of reactor known as a 'column reactor.' In the context of chemistry or chemical engineering, a column reactor generally denotes a vertical vessel or chamber used for carrying out various chemical reactions. These reactors often involve the use of columns or trays for efficient mixing, separating, or catalytic processes
How to use "column reactor" in a sentence
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column reactor
The bubble column reactor was connected to feed vessels.
A three inch diameter distillation column reactor was used.
The column reactor has a plurality of esterification trays.
Concurrently in said distillation column reactor.
The countercurrent column reactor was heated with a clamshell heater.
These units are then disposed in a distillation column reactor.
The immobilized yeast column reactor can be pressurized as discussed above.
These systems were well suited for a column reactor approach.
The bubble column reactor typically consists of vertically arranged cylindrical columns.
These units are then disposed in the distillation column reactor.
In a second embodiment the first distillation column reactor is a dehexanizer rather than a depentanizer.
Process for the conditioning of a catalyst contained in a bubble column reactor.
This solution is hydrogenated continuously in a column reactor with an irrigated catalytic bed.
Another embodiment of the present invention concerns a bubble column reactor.
Referring to the drawing the distillation column reactor is divided into three sections.
See also
The sulfonic acid resin catalyst was present in a packed column reactor.
The success of the evaporation column reactor system may be attributed to several factors.
As in any distillation there is a temperature gradient within the distillation column reactor.
The bubble column reactor of the instant invention outperforms other forms of stripping.
Returning a portion of said condensed overheads to said distillation column reactor as reflux.
The column reactor was lagged and wound with external electrical heating tapes.
Isobutene and isobutane are withdrawn from the distillation column reactor as overheads.
At start up the column reactor was charged with resin and with methyl laurate.
Different solid esterification catalysts may be used on different trays of the column reactor.
The object may be used in a packed column reactor vessel to polymerize monomer feeds.
The oxidation can be conducted in a continuous stirred tank reactor or in a bubble column reactor.
In the column reactor the esterification trays each hold a charge of a solid esterification catalyst.
In such an esterification process a vaporous mixture exits the column reactor as an overhead product.
Here the column reactor will be described in terms of a column reactor including a packed column.
The deep tank reactor may be a liquid mixed reactor or preferably a bubble column reactor.
The bubble column reactor includes an external reaction vessel and an internal reaction vessel.
The process is realized in a horizontal sectionalized bubble column reactor with one or many sections.
The bubble column reactor may be preferred for Cytomim reaction conditions.
Withdrawing an overheads stream from said distillation column reactor containing isobutene and isobutane.
The catalyst packing is preferably arranged in the middle portion of the distillation column reactor.
Withdrawing unreacted materials from the distillation column reactor at a point above said reaction zone.
Said olefin is separated from the dealkylation product and withdrawn from said distillation column reactor.
Withdrawing sulfide products from said distillation column reactor at a point below said distillation reaction zone.
Preferably, the reaction is conducted in a bubble column reactor.
Withdrawing the ether from the distillation column reactor at a point below the feed zone and.
Bubble column reactor for gas-liquid exchange reactions.
Concurrently in the distillation column reactor system,.
The column reactor was washed with water, ethanol and dried with diethyl ether.
The residence time in the column reactor is 3 hours.
According to preferred embodiments, the reactor is a tubular reactor or a column reactor.
Feeding hydrogen to said distillation column reactor at a point below said bed ;.
It is preferred to use a tubular reactor, a vessel reactor or a distillation column reactor.
Fractionating within the distillation column reactor the products of said contacting ;.
Fig . 5 is schematic cross section of a structure positioned in a distillation column reactor.
The activated mixture is added to the column reactor under nitrogen to react for 2h.
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