(19) |
 |
|
(11) |
EP 0 354 037 A3 |
(12) |
EUROPEAN PATENT APPLICATION |
(88) |
Date of publication A3: |
|
27.02.1991 Bulletin 1991/09 |
(43) |
Date of publication A2: |
|
07.02.1990 Bulletin 1990/06 |
(22) |
Date of filing: 03.08.1989 |
|
|
(84) |
Designated Contracting States: |
|
AT BE CH DE ES FR GB GR IT LI LU NL SE |
(30) |
Priority: |
04.08.1988 US 229038
|
(71) |
Applicant: SUPER S.E.E.R. SYSTEMS INC. |
|
Burlington
Ontario L7R 3X4 (CA) |
|
(72) |
Inventor: |
|
- Gregory, Charles
Burlington, Ontario L7M 1G6 (CA)
|
(74) |
Representative: Horner, Martin Grenville et al |
|
Cruikshank & Fairweather
19 Royal Exchange Square Glasgow G1 3AE
Scotland Glasgow G1 3AE
Scotland (GB) |
|
|
|
(54) |
Apparatus for the sensing of refrigerant temperature for the control of an evaporator
valve |
(57) A new method and apparatus are provided for sensing refrigerant temperatures in refrigerator
systems, and for the control of refrigerant loading in a plurality of refrigerator
evaporator circuit coils (34a,34b) connected in parallel. Such evaporator coils are
supplied with refrigerant through a thermostatically controlled flow control valve
(30), which is controlled by a sensor (50) to restrict the flow of the liquid refrigerant
and ensure a predetermined amount of superheat. The usual minimum superheat is about
5.5°C (10°F) and it is often found that the evaporator coil clearly is underloaded,
and in the case of a multi circuit coil evaporator, that many of the circuit coils
are underloaded. To avoid this the refrigerant is rendered thoroughly turbulent and
mixed, and in the multi-coil evaporator the flows issuing from all of the circuit
coils are similarly thoroughly turbulated and mixed, by a turbulating and/or mixing
device (48) that intercepts the entire refrigerant flow just before the sensing of
the superheat, thus ensuring that the temperature is accurately measured. In the multi-circuit
coil system the device averages the temperatures of all the flows, any liquid from
circuits with lower heat transfer being broken, mixed with and evaporated by superheated
vapour from circuits with higher heat transfer. Different turbulator/mixer devices
are described and two or more such devices may be used in flow series. The amount
of superheat can now safely be reduced to about 2°C (4°F), the efficiency of the entire
system is increased, and close matching between valve size and coil loading is no
longer required.
