The present invention generally relates to freezers and, more particularly, to freezers that use liquid cryogen as a refrigerant.
Freezers for storing biological specimens, samples, materials, products and the like often use cryogenic liquids as a refrigerant. Such freezers typically feature a reservoir of a liquid cryogen, such as liquid nitrogen, in the bottom of the freezer storage chamber with the product stored above the reservoir or partly submerged with in the cryogenic liquid. The freezers typically also feature a double-walled, vacuum insulated construction so that the storage chamber is well insulated. Such freezers provide storage temperatures ranging from approximately −90° C. to −195° C.
A disadvantage of prior art liquid cryogen freezers is that the temperature cannot be directly controlled. The temperature is controlled by maintaining the amount of cryogenic liquid in the reservoir. The temperature of the freezer storage compartment thus varies dependent upon the amount of liquid cryogen in the freezer.
A further disadvantage of prior art liquid cryogen freezers is that there is some concern that submerging biological specimens in the cryogenic liquid presents a risk of cross-contamination between specimen containers. Even when the stored specimen containers are placed in the cold vapor above the cryogenic liquid reservoir, there is still the potential for the specimen containers to come into contact with, or be submerged within, the cryogenic liquid if the freezer is overfilled with the cryogenic liquid.
Also available are freezers that use mechanical refrigeration systems in place of a liquid cryogen reservoir. The mechanical refrigeration systems typically include a compressor, an evaporator, a condenser and a fan. Air is circulated through the storage chamber and across a cooling coil to maintain the desired temperature in the freezer storage chamber. The freezers normally do not feature vacuum insulation and employ materials such as foam and/or fiberglass insulation to insulate the storage chamber. Such freezers typically provide storage temperatures in the −40° C. to −80° C. range.
A disadvantage of the mechanical freezer is that the mechanical refrigeration system requires a significant amount of electrical power to maintain the desired temperature within the freezer storage chamber. Furthermore, mechanical refrigeration systems remove heat from the storage chamber and reject it to the environment around the freezer. This adds significant heat to the room within which the freezer is stored so that additional air conditioning capacity is required for the room. This adds additional electrical power requirements to the facility. In addition, in the event of a power failure, the storage chamber will warm rapidly, which could result in the loss of the stored biological materials.
An embodiment of the freezer with liquid cryogen refrigerant of the invention is indicated in general at 10 in
An insulated plug or lid 20 is removably positioned within an offset access opening 22 of the freezer which permits access to the storage chamber 14. The lid 20 is preferably mounted to the remaining portion of the freezer by hinged bracket 24. A rotating tray 26 is positioned within the storage chamber 14 and holds the items being stored while also providing access through offset access opening 22 when the lid 20 is open.
The storage chamber 14 of the freezer, and thus the items stored therein, are cooled by a heat exchanger positioned within a top portion of the storage chamber. The heat exchanger preferably takes the form of a cooling coil 28, but alternative heat exchanger components or structures could be used instead.
A storage container 29 containing a supply of liquid cryogen refrigerant is in communication with the inlet 30 of feed line 32. Feed line 32 communicates with the inlet of cooling coil 28. While liquid nitrogen is discussed below as the liquid cryogen refrigerant, it should be understood that alternative cryogenic liquids could be substituted for the liquid nitrogen. The liquid nitrogen is pressurized for transfer to the inlet 30 of the feed line 32 such as by a pump 33. Alternatively, the liquid nitrogen could be stored under pressure in storage container 29 so that no pump is needed. Other alternatives for supplying cryogenic liquid under pressure are known in the art and may be used as well.
With regard to operation of the freezer of
There will initially be gas in the transfer line connecting the inlet 30 of the feed line with the source of pressurized liquid nitrogen. This gas normally will be warmer than the storage chamber of the freezer. To prevent this gas from entering the heat exchanger, a bypass line 38 having an outlet 40 also communicates with a portion of the feed line 32 positioned between the inlet of the cooling coil 28 and the inlet 30 of the feed line. When the controller opens bypass valve 42, the warm gas that enters through inlet 30 is vented through the bypass line 38 and outlet 40.
The temperature of the gas entering the feed line 32 is monitored by feed temperature sensor 44, which also communicates with controller 34. When the temperature of the incoming gas (indicated as TG in decision block 45 of
As a result, liquid nitrogen refrigerant flows through the cooling coil 28. The liquid nitrogen flowing through the cooling coil is colder than the gas inside of storage chamber 14 so that it absorbs heat from inside of the chamber. As the liquid nitrogen absorbs the heat, it is vaporized and exits the heat exchanger taking the absorbed heat with it.
As illustrated by arrows 51a and 51b in
As illustrated in
In addition, ice formation on the exterior surface of the cooling coil 28 can insulate it from the storage chamber of the freezer and reduce the coil's cooling effectiveness. The nitrogen purge gas exiting the purge outlets 62 above the cooling coil 28 is a dry gas. This dry nitrogen purge gas displaces ambient air (which could contain water) from the space around the exterior surface of the cooling coil to reduce the possibility of ice forming on the coil. Furthermore, when the process of
To prevent purge gas that is substantially colder than the desired storage chamber temperature of the freezer from discharging into the chamber 14, the controller 34 monitors the temperature of the purge gas via a purge gas temperature sensor 64. When the temperature of the purge gas (indicated as TP in decision block 66 of
When the purge gas valve 46 is closed, the cooling gas exhaust valve 56 is opened by the controller 34, as indicated at 73 in
The controller 34 monitors the exhaust gas temperature via an exhaust gas temperature sensor 82. When the temperature of the nitrogen exhaust gas flowing through exit line 52 and exhaust line 74 (indicated as TE in decision block 78 of
The exhaust gas temperature sensor 82 is positioned external to the freezer. As a result, it is warmed by ambient external air while there is no flow through the cooling coil 28. Once the exhaust gas temperature sensor detects that the gas within line 52 has warmed above the maximum desired storage chamber temperature (indicated as TDmax in decision block 86 of
As indicated by decision block 90 of
As indicated by decision block 96, when the storage chamber temperature of the storage chamber again warms to the maximum desired temperature, as measured by the chamber temperature sensor 92, the bypass valve 42 is again opened by the controller and the process of
The freezer of
The freezer of
The freezer of
Furthermore, in the event of a power failure, the freezer of
While the preferred embodiments of the invention have been shown and described, it will be apparent to those skilled in the art that changes and modifications may be made therein without departing from the spirit of the invention, the scope of which is defined by the appended claims.