Übersetzung für "Vorlagegefäß" in Englisch

Air is blown into the feed vessel at a rate of 100 l/h.

Prior to the coating, the components are mixed and stirred in the specified container in the dark.

Subsequently, the mixture is stirred for 30 minutes and transferred to a reservoir vessel.

The suspension was drained from the reactor and transferred to a storage vessel.

The clear solution was transferred into the receiving vessel over a period of 30 minutes under intensive stirring.

130 g of n-butyl acetate and 50 g of hexamethylene diisocyanate are weighed into a preliminary vessel and premixed.

By means of a gear pump, the cell suspension is pumped from a stirred vessel into a microwave oven.

The second tank can be emptied in a continuous and controlled manner via a base outlet into a receiver vessel.

As an alternative, in the case of high-viscosity additives, a pump with a heated feed line and with a heated receiver was used.

In the case of high-viscosity additives a pump with heatable supply line and heatable feed vessel was used if required.

The central compartment is visited by the recirculating alkali metal sulfate solution via a reservoir vessel which can be replenished with sodium sulfate.

The density of the solution of 1.023 g/ml at 22° C. This solution is sterile filtered under aseptic conditions into a sterile vessel through a membrane filter having a pore size of 0.2 ?m and filled in sterile dropper bottles of 10 ml each.

In a feed vessel, 4 l of a sulfuric acid solution at pH 4 is saturated with air (0.0205% by volume of O2 in water at 15° C.) by introducing an air stream at 100 l/h.

After about 20 minutes the pH in the feed vessel has risen to 8 and no longer differs from the pH in the reaction vessel.

After about 17 minutes the pH in the feed vessel has risen to 8 and is no longer different from the pH in the reaction vessel.

The reaction mixture then passes through a tubular afterreaction space (?=15 mm, 1=3000 mm) having a cooling water cooling jacket and is then passed into a stirred receiver vessel (100 1 kettle made of steel/enamel).

In a feed vessel, 4 l of sulfuric acid solution of pH 3 is prepared.

In the case of water-miscible diols (for example 1,6-hexanediol), one can promote saving the heat of melting the solution of diol in water simply from the receiving vessel in the vaporizer and superheater.

1,6-Hexanediol was melted in a heated reactor vessel, and then analogously to Example 1 was fed with a constant volume stream of 1.5 ml/minute through a feed pump over vaporizer and superheater to the reactor.

A prepared solution of the precursors or precursor compounds 5 of the catalytically active components is injected from receiver container 4 with one or several capillary tubes 6 (inside diameter approximately 1 mm) under the surface into dispersion 2.

Thereafter, a dilute ammonia solution can be injected from another receiver container (not shown here) in an entirely analogous manner into the now-present mixture of dispersion and solution of the precursors in order to precipitate the catalytically active components on the support material by raising the pH of the mixture.

In the case of larger particles the separation can also readily be effected by the particles being is allowed to trickle out from the decomposition apparatus and being collected in a receiver.

From storage vessel 4, a ready-made, common solution of precursor compounds 5 for the stabilizers and optionally for cerium is injected below the surface into dispersion 2 using one or more capillary tubes 6 (internal diameter about 1 mm).