Examples of 'distillation column reactor' in a sentence
Meaning of "distillation column reactor"
Distillation column reactor: This is a technical term used in the field of chemical engineering, specifically in the process of distillation to separate components of a liquid mixture based on differences in boiling points
How to use "distillation column reactor" in a sentence
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distillation column reactor
A three inch diameter distillation column reactor was used.
As in any distillation there is a temperature gradient within the distillation column reactor.
In a second embodiment the first distillation column reactor is a dehexanizer rather than a depentanizer.
The catalyst packing is preferably arranged in the middle portion of the distillation column reactor.
Referring to the drawing the distillation column reactor is divided into three sections.
Said olefin is separated from the dealkylation product and withdrawn from said distillation column reactor.
Concurrently in said distillation column reactor.
By insertion of the catalyst into the distillation column, the column becomes a distillation column reactor.
Withdrawing an overheads stream from said distillation column reactor containing isobutene and isobutane.
A distillation column reactor 10 is provided having a bed 12 of hydrodesulfurization catalyst in a distillation reaction zone.
These units are then disposed in a distillation column reactor.
In the process, the distillation column reactor serves as a regeneration reactor for an alkyl nitrite.
These units are then disposed in the distillation column reactor.
The hydrogen rates to the distillation column reactor are preferably maintained at between 5 and 40 SCFH.
Returning a portion of said condensed overheads to said distillation column reactor as reflux.
See also
Fractionating within the distillation column reactor the products of said contacting ;.
It is preferred to use a tubular reactor, a vessel reactor or a distillation column reactor.
Withdrawing unreacted materials from the distillation column reactor at a point above said reaction zone.
Fig . 5 is schematic cross section of a structure positioned in a distillation column reactor.
Withdrawing sulfide products from said distillation column reactor at a point below said distillation reaction zone.
Hydrocarbon stream 10 containing nitriles may be fed to a distillation column reactor 12.
Withdrawing the ether from the distillation column reactor at a point below the feed zone and.
Hydrocarbon stream 10 containing nitrites may be fed to a distillation column reactor 12.
Feeding hydrogen to said distillation column reactor at a point below said bed ;.
An apparatus according to Claim 11 characterised in that the distillation column reactor comprises,.
Hydrogen may be fed to the distillation column reactor along with the mixed methanol/C4 feed.
In the following example a one inch diameter 30 foot tall distillation column reactor was used.
The advantages of using a distillation column reactor in place of the Green Oil Tower are,.
Feeding diolefins and a hydrocarbon stream containing mercaptans, to a distillation column reactor into a feed zone ;.
Referring to the drawing, distillation column reactor 10 is divided into two sections.
Withdrawing a C6 and lighter stream containing cyclohexane from distillation column reactor as overheads ;.
Example 1 A distillation column reactor 1 as shown in Fig . 1 was employed.
Isobutene and isobutane are withdrawn from the distillation column reactor as overheads.
Concurrently in the distillation column reactor system,.
Feeding a light reformate stream containing aryl compounds to a distillation column reactor into a feed zone ;.
Withdrawing a bottoms from said distillation column reactor containing butene-2 ; and.
Withdrawing tertiary ether product from said distillation column reactor as bottoms ;.
Feeding said bottoms and hydrogen to a distillation column reactor and concurrently therein,.
Feeding a primary alcohol and an isoalkene to a distillation column reactor in a feed zone ;.
The hydrogen may be recycled to the distillation column reactor if desired ( not shown ).
Withdrawing ether product from the distillation column reactor as bottoms ; and.
High purity methanol is withdrawn from the distillation column reactor as bottoms vía flow line 5.
Withdrawing said alkylation product from said distillation column reactor at a point below said fixed bed ;.
Withdrawing an overheads from said distillation column reactor containing said H2S ;.
The use of a catalyst as a packing material in a distillation column reactor is described in U. S.
Removing butene-2 from said distillation column reactor as bottoms.
Feeding the effluent from step ( a ) to a distillation column reactor into a feed zone ;.
Feeding a stream containing n-butanol to a distillation column reactor into a feed zone, concurrently,.
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