问答题 6分

Basically, these units incorporate an evaporating section beneath a condensing or distilling section...

Basically, these units incorporate an evaporating section beneath a condensing or distilling section in a
common vessel of appropriate shape. A controlled flow of filtered feed, taken preferably from a salt
circulating outlet, enters the evaporating section and ascends through a battery of vertical tubes, surrounded
by steam or hot water, vaporizing as it goes, to the condensing section through a labyrinth or screen
(generally called a demister) which ensures that no droplets of salt water enter the condenser with the vapor.
The vapor, directed by suitably placed baffles, passes over the condenser tubes and falls as water to an
outlet duct, from which it is removed by a distillate pump, via a salinometer.

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5 问答题 6分
For a certain provision cooling plant, the capacity regulator is generally controlled depending on
pressure, temperature or relative humidity. The pulse emitter is therefore either a pressostat(压力继电器),
thermostat or hygrostat. The switching difference of the control units should be rated as large as possible.
This applies in particular to control by means of the pressure, because change to the load in the
refrigeration circuit results in relatively quick pressure changes compared to temperature, which can in turn
lead to inadmissible oscillation of the regulator.

Under partial load, the suction volume and thus the gas speed can undergo marked changes depending on the
regulation stage. For this reason, the rating and routing of the suction line must be given particular attention.
In order to guarantee sufficient oil return, neither full load nor partial load operation may allow the gas speed
to fall below a minimum level: 4 m/s in horizontal pipe sections; 8 m/s in vertical pipes.

For this reason we recommend that vertical pipes bestaggered into two separate sections (as illustration).
As a result of the falling suction gas speed velocity in partial load operation, the pipe elbow B is
blocked by an accumulation of oil. This increases the gas velocity in pipe section A. In order to guarantee adequate
oil return, both cross sections must be rated so large that the velocity does not fall below the minimum level
in full and partial load operation. In plants with extensive pipe systems it is recommended at least for R22 and NH3
to install an additional oil separator. This reduces the oil circulation period and can have positive effects above
all for cold starts with relatively high oil ejection.