170.200-IOM (FEB 23)
Page 5
Remote Distributed Condensing Units (RDC)
Installation - Operation - Maintenance
precise control of condensing capacity.
The RDC unit uses an optional glycol plate-style condenser
which incorporates thermal efciency and reliability with
the potential benet of additional heat recovery capability.
Process heat recovery results in immediate and potentially
signicant cost savings that lower operating costs and
increases overall protability.
RDC glycol plate condensers are designed to ASME VIII,
Division 1 standards and use corrosion resistant 316 stain-
less steel plate material with highly engineered chevron
plate patterns for optimal heat transfer. Specialized plate
geometry provides low pressure drop and low fouling
while delivering high thermal efciency. Semi-welded
plate heat exchanger gasketed joints use EDPM and HNBR
elastomers for industrial reliability while offering easy
disassembly for maintenance and serviceability.
The highly efcient glycol plate heat exchangers are com-
pact allowing RDC units to handle large heat loads while
maintaining a small footprint and low refrigerant charge.
Liquid storage vessel
The liquid storage vessel (LSV) is designed and con-
structed in accordance with ASME Section VIII, Divison 1
and outtted with dual 300 psi rated safety relief valves.
The LSV provides a constant pressure liquid refrigerant in
order to properly feed the evaporators. Condensed refrig-
erant ashes down to an intermediate pressure and the
vapor separates from the liquid inside the LSV. Control of
the LSV pressure is accomplished by using a dual pressure
regulator. The ash gas maintains liquid pressure inside
the LSV to feed the DX evaporators and the excess vapor
ows to either the economizer port of the screw compres-
sors for increased system efciency, or to one of the main
suction lines.
The pressure setting of the back pressure regulator con-
trolling the LSV varies according to system design. Refer
to the sales order P&ID for the design pressure set-point.
The secondary standby pressure set-point of the pressure
regulator is to provide relief for rising pressure inside the
vessel before reaching the set-point of the safety relief
valves mounted on the vessel. A typical scenario would
be rising pressure inside the liquid lled vessel from direct
exposure to the sun. The standby pressure is commonly
set at 200 psig but may vary.
The LSV is equipped with a guided microwave wire-style,
liquid level transmitter as part of the liquid refrigerant level
control. A mechanical high level oat switch provides high
LSV liquid level protection for compressors.
RDC control panel
Each RDC has a factory-mounted, Nema 4 Remote I/O
control panel built to UL-508A standards. The RDC control
panels use 24 VDC control modules to provide smaller,
safer ARC Flash compliant controls. Refrigeration System
Control PLC is programmed to manage LSV refrigerant
levels in the critically charged LCCS system for the entire
facility. The RDC panels are factory-wired with most of the
necessary safety and operating devices to provide stable,
efcient, and safe operation of the entire system under
varying loads and operating conditions. The Refrigera-
tion System Control PLC and the RDC I/O panels connect
through the use of Ethernet.
Defrost operation
RDC Units are designed to accommodate either hot gas
defrost or air-cooled defrost applications. The hot gas
supply control valves and defrost condensate liquid return
oat valves are provided as part of the ship loose valve
sets for eld installation. The defrost condensate return
line is designed to return condensed liquid to the LSV dur-
ing the defrost cycle.
The FRICK control system can be programmed to initi-
ate defrost operation in a number of ways including time
elapsed since last defrost cycle, coil temperature, direct or
optical detection of frost buildup, or other methods. While
the mechanism to initiate the defrost cycle may vary, the
hot gas defrost process includes the following basic steps:
1. Pump out phase: The liquid feed valve to the evapo-
rator is closed while the suction line remains open
allowing liquid refrigerant remaining inside the coils
to vaporize and leave the evaporator. This allows heat
from the hot gas supply line to immediately begin
melting the frost build up on the coils. Removing the
liquid refrigerant rst also helps prevent damage to the
coil from pressure shocks or liquid hammer that may
occur as hot gas enters. After the liquid refrigerant is
completely vaporized the evaporator fans are turned
off and the motorized control valve in the line from the
evaporator outlet and the suction line is closed.
2. Hot Gas Phase: Each evaporator equipped with hot
gas defrost has a branch feed line tied into the hot gas
header. This same line also supplies high pressure va-
por to the local condenser. The pressure of the hot gas
must be reduced before entering the evaporators to
prevent damage to the coils. To accomplish this there
is an outlet pressure regulating valve in the evapora-
tor hot gas supply piping. The pressure drop across the
valve is determined by the design defrost temperature
setting used in the defrost cycle. Traditionally, the
defrost cycle temperature is between 40°F and 55°F.
Defrosting at a higher temperature does not gener-
ally improve the defrost efciency because most of the
melting energy is attributed to the hot gas’ latent heat
and not its sensible heat. Higher defrost temperatures
would also mean additional energy is required to cool
the coils back down after the defrost cycle is complete.
For the FRICK LCCS systems, the defrost temperature
and subsequent saturation pressure may need to be
set a little higher in order to create a pressure dif-
ferential between the defrosting coils and the LSV in
order to return condensate liquid to the vessel. Using
a defrost temperatures between 40°F and 55°F means
the discharge pressure supplying the hot gas must be
reduced to between 85 psig to 115 psig. As the hot gas
cools and then condenses it transfers heat to melt the
frost. A liquid return oat valve at the outlet of the coil
routes the condensate back to the LSV. This process
continues until either a time limit is reached or a tem-
perature sensor terminates the defrost cycle.