Übersetzung für "Heat number" in Deutsch

Heat transfer number and exchange path increase correspondingly.

Thermal processing of organic waste materials can produce heat or a number of liquid or gaseous fuels.

Without considering the dampening value of the air layer, a heat throughput number k=2.6 kcal/m2 h°C. is stated as the empirical measuring value.

The delta wings assist in preventing a film of steam on the underside of the plate through which the heat transfer number, which is decisive for heat transfer from the heated plate to the cooling water flow, would be undesirably reduced.

The determined average temperature value depends in such cases on the temperature drop between the electromagnetic coils and the sensor, the time elapsed for the heat transport, the number of the electromagnetic coils controlled.

The by-pass stream varies for the reheater heating surface in the fluidized-bed cooler the inner heat transfer number on the one hand and the logarithmic temperature difference on the other hand.

Briefly, the invention provides a building with at least one room with a floor and an outside wall including a window and an opaque wall part wherein the heat transfer figure (the overall k-value) of the entire window and the heat transfer number of the opaque wall parts each have a value of at most one W/m2. K and that the air supply, distributed over at least one of the walls of the room, takes place in the vicinity of the floor, with the incoming velocity of the supply air into the room not exceeding a maximum value which corresponds to the comfort velocity in the zone occupied by persons.

So it'll be the specific heat times the number of grams we're warming up of ice times the change in temperature that we're trying to get.

The heat transfer number k indicates how much energy is lost, indicated in watts per square meter of glass surface and degree of temperature difference in Kelvin (W/m 2 K).

It was finally found that, surprisingly, the heat conductivity number of polymers C obtained using the combination of polyols A1a, A1b and A1c which is provided according to the present invention is further improved on producing said polymers C by the variable output method of the present invention.

Because power supply lines to a superconducting magnet arrangement provide an undesirable heat input, the number of supply lines should be minimized.

In this manner, one can heat twice the number of preforms 5 with the same diameter of the heating wheel 2 in a surface saving manner.

Since a PA without coloring impurities is required for most use purposes, particular importance is attached to characterization by the so-called color numbers—particularly the melt color number and the heat color number.

With the process according to the invention, a melt color number of the PA of less than 10 APHA and a heat color number of less than 20 APHA is achieved.

Stage housing 7 ? of second rotor disk 2 ?, which is also used for compressing a cold gas, is thermally separated from the machine housing in a corresponding manner, by means of a partition 11 ? that is made of an insulation material having a very low heat conductivity number.

So that the reinforced cooling according to the invention can be utilized on regions of the vane wheel with increased heat load which are particularly to be cooled, in such regions of increased heat load the number of turbulators or pockets provided per unit area should be increased, as compared with regions of lower heat load.

The supercritical substance properties lead, at a corresponding flow rate which is achievable with acceptable pressure drop owing to these substance properties, to a very high heat transfer number, which permits the input of the reaction energy required via the relatively small tube wall surface area.

Because a phthalic anhydride without discoloring impurities is required for most intended uses, characterization by the color numbers—primarily the melt color number and the heat color number—is particularly important.

This apparatus produces a forced cooling water guide means whose configuration corresponds to the outer circumference of a roll, wherein the uniform distance relative to the roll produces an intermediate space between the cooling water guide means and the roll through which the cooling water is conveyed under pressure, which is supposed to achieve an average heat transfer number which is about four times the value of the conventional heat transfer number.