
Evaporator
Liquid refrigerant enters the evaporator and is distributed over the top of the tube bundle. As the
refrigerant droplets cover the outside surface of the tubes, the heat from the returning chilled
water passing through the tubes causes the refrigerant to flash from a liquid to a vapor. The
temperature at which this happens depends on the evaporator shell pressure which is dictated
by the absorber section of the chiller-heater. The refrigerant vapor passes through the mist
eliminators and into the absorber section of the chiller-heater. As the liquid refrigerant passes
down through the bundle of evaporator tubes, more and more of the refrigerant vaporizes. The
refrigerant remaining in a liquid state at the bottom drains into the refrigerant tank and is pumped
back up the top of the tube bundle where the process is repeated.
Absorber
Concentrated LiBr solution enters the absorber section of the chiller-heater and is sprayed over
the absorber tube bundle. Because the vapor pressure of the concentrated solution is very low,
the refrigerant, or water, vapor from the evaporator flows into the absorber and is absorbed into
the LiBr solution. This mass transfer process lowers the concentration of the LiBr solution as the
refrigerant, or water, is absorbed into the solution. This dilution process generates heat and, if
not cooled, would eventually stop as the solution temperature would rise with a corresponding
rise in vapor pressure. This would be similar to closing the vanes or slowing down a centrifugal
compressor on a centrifugal chiller where the load was constant. The water flowing inside the
absorber tube bundle comes from the cooling tower and serves to cool the LiBr solution as it
flows down over the tube bundle. This allows the absorption process to continue and the solution
becomes more diluted as it absorbs more refrigerant vapors. When the LiBr solution reaches the
bottom of the absorber section, it goes into the suction of the solution pump. The liquid is then
pumped to the generators.
The following section describes the unique two-step evaporator-absorber design of the YHAU-CG
direct fired absorption chiller-heater.
Two-step evaporator – absorber
The evaporator and the absorber are each split into two sections. This design, similar to a series-
counter-flow chiller-heater arrangement along with the parallel flow cycle, enables lower LiBr
solution concentrations. This reduces pressure, the potential for corrosion, and the risk of
crystallization as well as improves efficiency in conjunction with other advanced components
described later in this section.
The two evaporators are in series with respect to the chilled water flow through the tubes. In other
words, the chilled water flows through the lower evaporator tubes first and then to the upper
evaporator tubes. Each evaporator operates at a slightly different temperature and pressure.
The refrigerant in the lower evaporator boils at a slightly higher temperature than in the upper
evaporator, consequently cooling the chilled water in two steps.
The two absorber sections are split as well, with the strong solution first entering the top of the
uppermost absorber and flowing down through the top absorber bundle. It then flows into the top
of the lower absorber section. The strong solution entering the upper absorber takes advantage
of its lower vapor pressure allowing the upper evaporator to operate at a lower pressure and
temperature.
When the LiBr solution enters the lower absorber section it is somewhat diluted from the
refrigerant vapor that boiled off in the upper evaporator. At this lower concentration the solution
vapor pressure would normally not be sufficient to provide an evaporator pressure low enough to
satisfy the leaving chilled water design. However, the lower evaporator is the first step of the chilled
water cooling cycle, and the dilute solution’s vapor pressure is adequate to maintain the required
temperature and pressure in the lower evaporator.
17YHAU-CGN/H Double Effect Direct Fired Absorption Chiller-Heater (Mod A)