Examples of 'liquid propylene' in a sentence

Meaning of "liquid propylene"

Liquid propylene is a form of propylene that is in a liquid state at a specific temperature and pressure. Propylene is a chemical compound commonly used in various industrial processes, such as plastics manufacturing, fuel production, and chemical synthesis

How to use "liquid propylene" in a sentence

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liquid propylene
Preferably the polymerization medium is liquid propylene.
Liquid propylene can be employed as a solvent.
Again the polymerizations were completed in liquid propylene.
Liter of liquid propylene.
An exemplary refrigerant used is liquid propylene.
The liquid propylene was practically completely transformed into solid polypropylene.
Polymerizations in liquid propylene.
I of liquid propylene.
In a bulk process the polymerization is carried out in liquid propylene as reactor medium.
One liter of liquid propylene was introduced into a Buechi reactor at room temperature.
Polymerisation in liquid propylene.
Two liters of liquid propylene were introduced into a 4 liter bench reactor at room temperature.
Composite uniformity at such levels is not obtained when operating in liquid propylene.
The distillation vessel separates the liquid propylene from polymerization by-products, such as atactic polypropylene.
The feed to the reactor was a dispersion of the prepolymerised catalyst in liquid propylene.

See also

Suitably, the adsorbent is dispersed in the liquid propylene oxide yielding a slurry.
The examples relate to the preparation of ethylene / propylene copolymers in liquid propylene.
The catalysts prepared were polymerised in liquid propylene as described for Examples 7 to 9.
Polymerization The solid catalyst component was used to polymerize liquid propylene.
Liquid propylene is obtained by condensing unconverted and make-up propylene in an external condenser ( 7 ).
The catalyst is distributed within the continuous bore by circulating liquid propylene monomer.
Meanwhile the liquid propylene glycol was blended with a 10 % active solution of the photobleach.
The polymerization can for example be carried out in liquid propylene as reaction medium.
For example, when a liquid propylene phase is used, polymerization pressure is usually about 30 bars.
Typically for the polymerization of propylene the reactor contained liquid propylene as the reaction diluent.
Grams of liquid propylene are charged into a perfectly anhydrous 3.3 dm ³ autoclave equipped with a propeller stirrer.
Using these catalysts, propylene was polymerized in a slurry-phase process in liquid propylene.
Grams of liquid propylene were charged into a perfectly anhydrous 2.8 dm ³ autoclave equipped with a propeller stirrer.
The catalysts were employed to polymerize propylene in a slurry-phase process in liquid propylene as diluent.
Liquid propylene was introduced to the reactor at a temperature of 30°C.
When used, hydrogen was charged in the reactor at room temperature, before charging liquid propylene.
A matrix was produced in liquid propylene at 60°C in the first stage.
Transferred to a loop-reactor and the polymerisation is then carried out in a surplus of liquid propylene.
The content of the reactors is liquid propylene and polypropylene ( PP ) polymer.
When slurry polymerization is employed, the liquid phase for polymerization is preferably liquid propylene.
PP is made by polymerizing liquid propylene ( bulk polymerization ) or propylene gas gas-phase polymerization.
The reactor was closed and filled the 750 milliliters of liquid propylene.
PP is made by polymerizing liquid propylene ( bulk polymerization ) or propylene gas gas-phase poly merization.
The reactor was closed and filled with approximately 800 ml liquid propylene.
EXAMPLE 1 l of liquid propylene was added into a dried 1,5 l glass reactor equipped with inclined stirrer.
At room temperature was charged 80 g liquid propylene with nitrogen.
Adding liquid propylene to said carrier stream of ( b ) ;.
The reactor was sealed and charged under pressure with 500 mL of liquid propylene.
After this 300g of liquid propylene was conducted to the reactor.
Process according to Claim 13, in which the process is carried out in liquid propylene.
In succession, 150 ml of prepurified liquid propylene was added under stirring.
Copolymerizations were carried out in a 10 l reactor charged with 3.5 kg of liquid propylene.
The autoclave was then charged with 1.4 liters of liquid propylene and 16 mmoles of gaseous hydrogen.
Ideally, the polymerisation takes place in bulk, i.e. in a medium of liquid propylene.
Liquid propylene was fed and a pre-polymerization was carried out at 20 °C for 6 min.

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