Ramp Loading; Capacity Override; High Discharge Temperature Control; Oil Cooler - Carrier 19XRV Start-Up, Operation And Maintenance Instructions Manual

Hermetic centrifugal liquid chillers with pic iii controls 50/60 hz hfc-134a
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Ramp Loading
-- Tile rmnp loading
control slows down
tile rate at which the compressor
loads up. This control can pre-
vent the compressor
fiom loading up during the short period of
time when tile chiller is started and tile chilled water loop has to
be brought
down to CONTROL
POINT.
This helps reduce
electlical demand charges by slowly bringing the chilled water
to CONTROL
POINT. The total power draw during this period
remains ahnost unchanged.
There are several methods of romp loading with the PIC III.
Ramp loading can be based on LEAVING
CHILLED
WATER,
ENTERING
CHILLED
WATER, PERCENT
LINE CURENT or
PERCENT
MOTOR
KILOWATFS.
PULLDOWN
RAMP
TYPE is selected fiom tile RAMP
DEM screen.
1. Temperature
ramp loading (TEMP
PULLDOWN
DE(;/
MIN) limits the degrees
per minute
rote at which either
LEA VING CHILLED
WATER or ENTERING
CHILLED
WATER temperature
decreases. This rate is configured by
the operator on the TEMP_CTL
screen.
NOTE:
If chiller
control power has been off for 3 hours or
more, file next startup (only)
will follow temperature
ramp
loading using the minimum rate regardless
of the rmnp loading
method and rate which m:e configured
in the screens. This is
used to maximize
oil reclaim during stmtup.
2. Motor load ramp
loading (AMPS
OR KW RAMP
%/
MINI limits the rate at which tile compressor
motor cur-
rent or complessor
motor load increases.
The AMPS OR
KW RAMP
%/MIN
rate is configured
by the operator
on the RAMP_DEM
screen
in line current
or motor
kilowatts.
If kilowatts is selected for the DEMAND
LIMIT SOURCE,
the MOTOR
RATED LOAD KILOWATTS
must be entered
in
the VFD_CONF
screen.
The TEMP
PULLDOWN
DEG/MIN
may be viewed
or
modified
on the TEMP_CTL
screen which is accessed
from
the EQUIPMENT
SERVICE
screen.
PULLDOWN
RAMP
TYPE, DEMAND
LIMIT SO URCE, and AMPS OR KW RAMP
_/MIN
may be viewed
or modified
on the RAMP_DEM
screen.
Capacity
Override
(Table 7) -- Capacity overrides can
prevent some safety shutdowns
caused by exceeding
the motor
amperage
limit, low evaporator
temperature
safety limit, high
motor temperature
safety limit, and high condenser
pressure
limit. In all cases there are two stages of compressor
capacity
control applied by guide vane operation.
1. When
the value of interest
crosses
the First Stage Set
point
into the Override
Region,
the guide
vanes
are
prevented
from opening furthel: and the status line on the
ICVC
indicates
the reason
for the override.
Normal
capacity
control
operation
is restoled
when the value
crosses back over the First Stage Set point, leaving the
Override Region. (Refer to Table 7.)
2. When the value of interest is in the Override
Region and
further crosses
the Second
Stage Set point, the guide
vanes
me closed
until the value
meets
the Ovenide
Termination
Condition.
The
PIC
III controls
resume
norm_d capacity
control
operation
after the override
termination
condition
has been satisfied.
(In the case of
high dischmge supeflleat, there is an intermediate
stage).
Whenever
the
motor
current
demand
limit
set point
(ACTIVE DEMAND
LIMIT) is reached, it activates a capacity
ovenide,
again, with a 2-step process. Exceeding
110% of the
rated load amps for more than 30 seconds will initiate a safety
shutdown.
The high compressor
lift (surge prevention)
set point will
cause a capacity ovenide
as well. When the surge prevention
set point is reached, the controller
normally will only prevent
the guide vanes from opening.
If so equipped,
the hot gas
bypass valve will open instead of holding the vanes. The hot
gas bypass will only open if the compressor
is at 100% speed.
See the Surge Prevention
Algorithm
section, page 42.
High Discharge Temperature
Control -- If the
COMP DISCltARGE
TEMP increases
above 160 F (71.1 C),
the guide vanes _ue proportionally
opened to increase gas flow
through the compressol:
If the LEAVING
CHILLED
WATER
temperature
decreases 5 ° F (2.8 ° C) below the control set point
temperature,
as a result of opening the guide vanes, the PIC III
will bring the chiller into the recycle mode.
Oil
Sump
Temperature
and
Pump
Con-
trol
--
The oil sump telnperature is regulated by the PIC III,
with the oil heater relay when the chiller is shut down.
As part of the pre-start checks executed by the controls, the
oil sump temperature
(OIL SUMP
TEMP)
is compared
to
the cooler refrigerant
temperature
(EVAPORATOR
REFRIG
TEMP) if the OIL SUMP TEMP is less than 150 F (65.6). If
the diffelence
between these 2 temperatures
is 50 F (27.8 C) or
less, the start-up will be delayed until either of these conditions
is no longer true. Once this temperature
criteria is satisfied, the
start-up continues.
The oil heater relay is energized
whenever
the chiller com-
pressor is off and the oil sump temperature
is less than 140 F
(60.0 C) or the OIL SUMP
TEMP
is less than the EVAP
REFRIG
TEMP plus 53 ° F (29.4 ° C). The oil heater is turned
off when the OIL SUMP TEMP is either:
morethan
152 F (66.7 C), or
more
than
142 F (61.1
C) and more
than the EVAP
REFRIG
TEMP plus 55 ° F (30.6 ° C).
The oil heater
is always
off during start-up
or when the
compressor
is running.
The oil pump is also energized
dnring the time the oil is be-
ing heated (for 30 seconds at the end of every 30 minutes).
The oil pump will not operate if the EVAPORATOR
PRES-
SURE is less than -5 psig (-34.5 kPa).
Oil Cooler
--
The oil must be cooled when the compres-
sor is running. This is accomplished
through a small, plate-type
heat exchanger
(also called the oil cooler) located behind the
oil pump. The heat exchanger
uses liquid condenser
refrigerant
as the cooling
liquid.
Refrigerant
thermostatic
expansion
valves (TXVs) regulate refrigerant
flow to control the oil tem-
perature
entering
the bearings.
The bulbs for the expansion
valves
are strapped
to the oil supply
line leaving
the heat
exchangel: and the valves are set to maintain
110 F (43 C).
NOTE: The TXVs me not adjustable. The oil sump tempemtme
may be at a lower temperature
during compressor
operation.
39

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