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Energy distribution unit pressurized

Figure 6.22 Schematic assembly of a pressurized enclosure for a large-volume Group I energy distribution unit [31],... Figure 6.22 Schematic assembly of a pressurized enclosure for a large-volume Group I energy distribution unit [31],...
Figure 6.23 Pressurized Group I energy distribution unit at the manufacturer s site. Type of protection EEx p I Doors of the control and monitoring unit (left side) and airlock (right side) in closed position. Figure 6.23 Pressurized Group I energy distribution unit at the manufacturer s site. Type of protection EEx p I Doors of the control and monitoring unit (left side) and airlock (right side) in closed position.
Vapor pressure. Individual molecules in the liquid have different amounts of kinetic energy, distributed roughly along a normal curve. Some molecules will have energy exceeding the inter-molecular forces of attraction. These molecules will vaporize. The number of molecules, per unit time and unit area, that vaporize dictates the vapor pressure of the substance. Since kinetic energy is directly proportional to temperature, vapor pressure is dependent solely on temperature. [Pg.58]

With hot water units, time clock control can operate satisfactorily as automatic bypass valves built into the distribution system will help the heater to achieve its working temperature quickly. With steam boilers, it is important that the boiler reaches a reasonable working pressure before steam is allowed into the distribution system. For example, if boilers are left open to a system for an extended length of time while not firing they will quickly lose their pressure. This is not only wasteful of energy but eventually creates a problem on start-up. To... [Pg.364]

In all of the above equations, is assumed to be constant and uniform throughout the flow field. In most items of bioprocess equipment, however, there is a spatial distribution of energy dissipation. The definition of an average or a maximum energy dissipation rate is notoriously difficult in the case of bioprocess equipment such as high pressure homogenisers, centrifuges, pumps and microfiltration units which all have complex flow fields. [Pg.99]

The molecular weight distribution in the process is controlled by the choice of catalyst. The density (between 0.915 and 0.97 g/crr ) is controlled by the amount of comonomer added. This versatile process avoids using hydrocarbon dilutants or solvents. In comparison to conventional high pressure LDPE units, Union Carbide has reported significant savings in plant investment and energy costs with this gas-phase technology. [Pg.474]


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