Examples of 'ethylene pressure' in a sentence
Meaning of "ethylene pressure"
ethylene pressure - This likely refers to a specific type of pressure measurement or condition related to ethylene gas.
How to use "ethylene pressure" in a sentence
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ethylene pressure
At this time the ethylene pressure was eased down.
The reaction is carried out under ethylene pressure.
The ethylene pressure must be greater than atmospheric pressure.
The reactor is cooled and the ethylene pressure is vented.
The ethylene pressure was then maintained at a nearly constant pressure.
Introduction of ethylene is regulated to maintain an ethylene pressure in the range indicated above.
Ethylene pressure was then vented.
The solution was then introduced into the autoclave by means of excess ethylene pressure.
The ethylene pressure was kept constant at the set pressure.
The reaction temperature and ethylene pressure were maintained for 1 hour.
The ethylene pressure and the temperature are adjusted to the desired values.
The polymerization time is of 3 hours, during which time ethylene pressure is kept constant.
The temperature and the ethylene pressure are kept constant throughout the polymerization.
The mixture was continuously stirred for 1 hour with maintaining the constant ethylene pressure.
The temperature and the ethylene pressure were kept constant for the duration of the polymerization.
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The polymerization time was 2 hours, during which time the ethylene pressure was kept constant.
The temperature and the ethylene pressure were maintained constant for the duration of the polymerization.
Polymerization was effected for 1 hour, keeping the temperature and the ethylene pressure constant.
The ethylene pressure was held constant and a mass flow meter measured the uptake of ethylene.
When the monomer is ethylene, the reaction pressure can be the monomer ethylene pressure.
The ethylene pressure was adjusted to 5 psig.
Polymerization was carried out for 1 hour, keeping the temperature and the ethylene pressure constant.
An ethylene pressure of 1 bar was applied for five minutes.
The reactor was then, with stirring, heated to the desired temperature under a desired ethylene pressure.
The ethylene pressure during the polymerisation was estimated to be approximately 8 bar.
The polymerization run lasted 3 hours, during which time the ethylene pressure was kept constant.
After ethylene pressure had been applied, a metered addition of isobutylene was initiated.
Example 1 was repeated except that the ethylene pressure was 2 MPa.
While the ethylene pressure was maintained, the mixture was continuously stirred.
The monomer delay, surfactant delay, and ethylene pressure were completed at the 5 hour mark.
The ethylene pressure was raised to 15 bar and it was continuously fed into the reactor.
The polymerisation was carried out at a temperature of 80°C and at an ethylene pressure of 8 bars.
Decreasing the ethylene pressure ( and therefore the ethylene concentration in the medium ).
During the reaction, ethylene was fed so as to maintain the ethylene pressure at 2.6 kg / cm.
While the ethylene pressure was maintained, the mixture was stirred continuously for 1 hour.
The stirring at 500 rpm was continued under constant ethylene pressure for at least 2 h.
The ethylene pressure in the polymerization reactor is generally chosen between atmospheric pressure and 5 MPa.
The monomer delay, surfactant delay, and ethylene pressure were completed at the 360 minute mark.
The ethylene pressure was maintained at 30 atm.
The vinyl acetate delay, surfactant delay, and ethylene pressure were stopped at the 300 minute mark.
The ethylene pressure was set to 10 bar to check any leaks.
The temperature was raised to 30 ° C. and the ethylene pressure was kept at 1 MPa.
The ethylene pressure was kept constant at 20 bars during the polymerisation.
The autoclave was pressurized to 8 bar ethylene pressure and heated to 50°C.
The ethylene pressure was increased to a total reactor pressure of 550 psig.
The reactor conditions were maintained at 80°C and 4 bar ethylene pressure.
After the mixture was cooled, ethylene pressure was applied and maintained at a constant level.
Ethylene pressure was adjusted to maintain a constant ethylene concentration in the liquid phase, typically 6 wt - %.
The reactor temperature and ethylene pressure were allowed to equilibrate for 15 - 20 minutes.
The charge was cooled to -15°C and placed under constant ethylene pressure.
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