User Guide
Figure 4 shows the same internally equalized valve on a
system having the same evaporator pressure at the sens-
ing bulb location. The evaporator coil, however, now has a
pressure drop of 6 psi. Since an internally equalized valve
senses evaporator pressure at the valve outlet, the total
pressure in the closing direction becomes 58 psig plus the 12
psi spring pressure, or 70 psig. A bulb pressure of 70 psig is
now required for proper valve regulation, which translates
to a 41°F bulb temperature. The superheat becomes 13°F, or
4°F higher than the superheat calculated in Figure 3. This
rise in superheat is due to the pressure drop in the evapora-
tor. Consequently, pressure drop between the valve outlet
and the sensing bulb location causes an internally equalized
TEV to operate at a higher than desired superheat.
Page 6 / BULLETIN 10-9
Figure 5 shows the same system as in Figure 4, but with
an externally equalized TEV installed. Since an externally
equalized TEV senses evaporator pressure at the evapora-
tor outlet, it is not influenced by pressure drop through the
evaporator. As a result, the TEV senses the correct pressure,
and controls at the desired superheat.
These diagrams can be used to show the influence evapo-
rator pressure drop has on internally equalized TEVs as
evaporating temperatures fall. Table 1 provides general
recommendations for maximum pressure drops that can be
safely tolerated by internally equalized valves. These recom-
mendations are suitable for most field installed systems.
Use externally equalized TEVs when pressure drops exceed
values shown in Table 1, or when pressure drops cannot be
determined. An externally equalized TEV should be
used whenever a refrigerant distributor is used with
the evaporator.
Refer to Bulletin 10-11, TEV Installation, Field Service and
Assembly, regarding recommendations for the location of
the sensing bulb and external equalizer connection to the
suction line.
Thermostatic Charges
As previously mentioned, the TEV’s sensing bulb transmits
pressure to the top of the diaphragm by a length of capillary
tubing. The thermostatic charge is the substance in the
TEV’s sensing bulb which responds to suction line tempera-
ture to create the bulb pressure, and it is designed to allow
the TEV to operate at a satisfactory level of superheat over
a specific range of evaporating temperatures. The subject of
thermostatic charges is best approached by describing the
categories into which charges are classified. These catego-
ries are the following:
1. Liquid Charge
2. Gas Charge
3. Liquid-Cross Charge
4. Gas-Cross Charge
5. Adsorption Charge
The conventional liquid charge consists of the same refriger-
ant in the thermostatic element that is used in the refrig-
eration system, while the liquid-cross charge consists of a
refrigerant mixture. The term cross charge arises from
the fact that the pressure-temperature characteristic of the
refrigerant mixture used within the sensing bulb will cross
the saturation curve of the system refrigerant at some point.
Both the liquid and liquid-cross charges contain sufficient
liquid such that the bulb, capillary tubing, and diaphragm
chamber will contain some liquid under all temperature condi-
tions. This characteristic prevents charge migration of the
thermostatic charge away from the sensing bulb if the sensing
bulb temperature becomes warmer than other parts of the
thermostatic element. Charge migration will result in loss of
valve control. An additional characteristic of these charges is
their lack of a maximum operating pressure (MOP) fea-
ture. A thermostatic charge with an MOP feature causes the
TEV to modulate in the closed direction above a predetermined
evaporator pressure, thereby restricting flow to the evaporator
and limiting the maximum evaporator pressure at which the
system can operate.
Similarly, the gas charge consists of the same refrigerant in
the thermostatic element that is used in the refrigeration
system, while the gas-cross charge consists of a refrigerant
mixture. Unlike the liquid type charges, both gas charges are
distinguished by having a vapor charge in the thermostatic
element which condenses to a minute quantity of liquid when
41°
52
58
58
Bulb Pressure
70 psig
Evaporator
Inlet Pressure
58 psig
Evaporator
Outlet Pressure
52 psig
Diaphragm
Spring Pressure
12 psi
Closing Pressure............................................................................= 58 + 12 = 70 psig
(Evaporator Inlet Pressure Plus Spring Pressure)
Bulb Pressure Necessary to Open Valve.........................................................70 psig
Bulb Temperature Equivalent to 70 psig................................................................41°F
Saturated Temperature Equivalent to Evaporator Outlet Pressure..........................28°F
SUPERHEAT....................................................................................................13°F
Bulb Temperature Minus Saturated Evaporator Temperature
12
70
Converted to Temperature = 41°F
37°
52
58
Bulb Pressure
64 psig
Evaporator
Inlet Pressure
58 psig
Evaporator
Outlet Pressure
52 psig
Diaphragm
Spring Pressure
12 psi
Closing Pressure.............................................................................= 52 + 12 = 64 psig
(Suction Pressure at Bulb Plus Spring Pressure)
Bulb Pressure Necessary to Open Valve..........................................................64 psig
Bulb Temperature Equivalent to 64 psig.................................................................37°F
Saturated Temperature Equivalent to Evaporator Outlet Pressure...........................28°F
SUPERHEAT............. ......................................................................................... 9°F
Bulb Temperature Minus Saturated Evaporator Temperature
52
Suction Pressure
at Bulb 52 psig
12
64
Converted to Temperature = 37°F
Figure 5
Figure 4