Examples of 'polymerization zone' in a sentence

Meaning of "polymerization zone"

polymerization zone: This phrase refers to a specific area or region where the process of polymerization occurs, which is the chemical reaction in which small molecules (monomers) are combined to form larger molecules (polymers)

How to use "polymerization zone" in a sentence

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polymerization zone
An inert gas may also be present in the polymerization zone.
The first polymerization zone is typically a continuous stirred tank reactor.
The fourth reaction zone is preferably a gas phase polymerization zone.
The polymerization zone will typically be a polymerization reactor or a series of polymerization reactors.
All of the soap is charged into the first polymerization zone.
The polymerization in the first polymerization zone is conducted in slurry in a loop reactor.
Continuously withdrawing unreacted monomers and gases from the polymerization zone.
In slurry polymerization zone more than one reactor can be used in series.
The elastomeric copolymer as synthesized is continuously withdrawn from the polymerization zone.
The second polymerization zone can be a reactor or a series of two or more reactors.
The pressure is measured in the vapor phase above the polymerization zone.
The pressure in the polymerization zone changes over the bed height.
At least one primary feed source is connected to the polymerization zone or reactor.
The first polymerization zone will normally be a reactor or series of two or more reactors.
The polymerization solution in the second polymerization zone was in the plug flow.

See also

Any polymerization zone known in the art to produce ethylene polymers can be utilized.
The catalyst is introduced into the polymerization zone using a nitrogen carrier gas.
The first polymerization zone can thus be advantageously cooled with external cooling means.
The first reaction zone may be a slurry polymerization zone or a gas phase polymerization zone.
Liquefiable monomers may also be introduced by injecting them under pressure in the polymerization zone.
All of the soap is charged into the first polymerization zone in practicing this invention.
The monomers may be continuously or intermittently introduced simultaneously or separately into the polymerization zone.
The precursor is introduced into the polymerization zone using both isopentane and nitrogen as a carrier.
Additional styrene monomer and butadiene monomer are charged into the second polymerization zone.
Slurry The polymerization in the first polymerization zone may be conducted in slurry.
The fog flows substantially with the fluidizing gases and is recirculated to the polymerization zone.
In any case, the second polymerization zone is subsequent to the first polymerization zone.
Preferably the rectified meta-xylylene diamine is fed back to the polymerization zone.
The effluent from said second catalytic polymerization zone is fractionated in a second fractionation zone ;.
A solution of the styrene-butadiene polymer is continuously removed from the second polymerization zone.
Thus, any polymerization zone known in the art to produce olefin-containing polymers can be utilized.
Styrene and divinyl benzene ( DVB ) will also be continuously fed into the second polymerization zone.
The precursor is introduced into the polymerization zone using both n-hexane and nitrogen as a carrier.
From the separation zone 4, the polymer enters the second polymerization zone 2.
Thus, any polymerization zone known in the art to produce ethylene-containing polymers can be utilized.
The monomer conversion attained in the polymerization zone will normally be at least about 85 %.
However, they can also be fed at any point of said second polymerization zone 2.
The effluent from the finishing polymerization zone is conveyed through line 9 to the fractionation zone 10.
Another intermediate conveyor 14 transfers the coated articles to tunnel 15 corresponding to the polymerization zone.
Furthermore, a polymer content in a polymerization zone was low, i.e., productivity for the polymer was low.
The slurry velocity in the post polymerization zone is preferably between 1m/s and 20m/s.

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