The invention relates to a low-temperature storage device for storing a plurality of objects. The invention also relates to a method for operating such a low-temperature storage device.
Storage devices of this type are e.g. used to store a large number of biological samples at low temperatures. Such samples are e.g. stored in tubes, which in turn are arranged in tube holders. Such tube holders can e.g. be held in storage cassettes.
EP 2998669 describes a low-temperature storage device for storing a plurality of objects. It has a storage chamber with a top and a bottom section. A cassette handler arranged in the top section is able to access storage cassettes in the bottom section and to transport them to a transfer location in a wall of the storage chamber.
A refrigerator device is provided for cooling the storage chamber to low temperature, typically to −80° C. or less.
Systems where the objects are to be stored at cryogenic temperatures below −80° C., in particular below −110° C., such as at −150° C.+/−20° C. (i.e. at a temperature sufficiently low for water to stably form amorphous ice), are typically cooled using liquid nitrogen. Liquid nitrogen has, at ambient pressure, a temperature of −196° C. at its boiling point, which makes it easy to maintain the desired storage temperatures. However, the present systems based on liquid nitrogen cooling are energy inefficient.
The problem to be solved by the present invention is to provide a storage device of this type for storing a plurality of objects that has high energy efficiency.
This problem is solved, in a first aspect of the invention, by the storage device of claim 1. Accordingly, the storage device comprises:
Further, the bottom section comprises at least a first and a second storage zone. The second storage zone horizontally surrounds the first storage zone from at least partially, in particular from all sides.
The storage device further comprises a first insulating wall vertically separating the first and said second storage zones.
The refrigerator device is adapted and structured to cool the first storage zone to a first temperature T1 and the second storage zone to a second temperature T2. The first temperature is at least 10° C. below the second temperature. The wording that the second storage zone “surrounds” the first storage zone “at least partially, in particular from all sides” is to be understood as follows: The second storage zone is arranged at least along a first side of the first storage zone. Advantageously, it is arranged along a first and a second side of the first storage zone, with the first and second side being adjacent to each other and extending transversally, in particular perpendicularly, to each other. Even more advantageously, it is also arranged along a third side of the first storage zone, with the third side also being adjacent to the first side and extending transversally, in particular perpendicularly, to the first side.
In a most advantageous embodiment, the second storage zone horizontally surrounds the first storage zone from all sides. In other words, there is a more or less concentric or layer-like design of storage zones in storage chamber, with the colder first storage zone being horizontally completely surrounded by the warmer second storage zone.
The claimed design greatly reduces the flow of heat into the first storage zone, thereby increasing the energy efficiency of the storage device and improving the temperature homogeneity within at least part of the zones.
Advantageously, the first insulating wall is, when seen from above, arranged in a regular polygon or a circle, in particular in a square. This class of shapes reduces the ratio between vertical surface and volume of the first zone.
The storage device can further comprise an automated cassette handler arranged in the top section, with the cassettes being accessible by the cassette handler. This allows to automatically access individual cassettes in the bottom section.
In particular, each storage cassette can comprise a plurality of storage locations above each other. Each such storage location may e.g. comprise one or more shelf members for vertically supporting one of the objects to be stored.
In that case, the storage device advantageously comprises a transfer station in a wall of the storage chamber. The transfer station comprises a transfer opening for transferring laboratory objects between the interior and the exterior of the storage chamber. In order to minimize energy loss and gas transfer through the transfer opening, the transfer opening has a height of less than three times the height of one of the storage locations, in particular of less than twice the height of one of the storage locations. Such a small-sized transfer opening also reduces the risk of erroneously accessing a wrong storage location.
For automated access, the cassette handler can adapted to vertically displace a storage cassette in the transfer station. In this way, it can position each of its storage locations next to the transfer opening.
In a second aspect, the invention relates to a low-temperature storage device for storing a plurality of objects, for example but not necessarily as described above, said device comprising:
Further, the refrigerator device comprises a refrigerant circuit conveying a non-inflammable cryo-liquid through the first storage-cooling heat exchanger. In this context, a “refrigerant circuit” is a closed circuit formed by ducts where, in operation, the cryo-liquid is in its liquid, sub-critical state over at least part of the circuit.
The term “cryo-liquid” refers to a non-inflammable liquid that is in its liquid state along at least part of the refrigerant circuit.
In this aspect, the invention also relates to a method for operating such a low-temperature storage device comprising the step of circulating the non-inflammable cryo-liquid through at least part of the liquid refrigerant circuit, advantageously with the cryo-liquid being liquid at least in the coldest part of the refrigerant circuit.
This second aspect of the invention is based on the understanding that using a non-inflammable cryo-liquid for transferring heat between the storage zone and the rest of the refrigerator device provides for improved safety because the storage zone is poorly aired.
Advantageously, the cryo-liquid is argon or nitrogen. These materials are not only non-inflammable, but non-toxic, too. In their liquid state, they can transfer a large amount of energy per volume in an efficient manner.
Further, the use of the refrigerant circuit obviates the need for cooling by directly filling liquid nitrogen delivered in vessels into the storage zone. Hence, the technique is based on generating the cooling where it is needed and not at a remote liquid nitrogen generation plant. No transport of liquid nitrogen vessels between sites is needed. Further, since the cooling is to the desired cooling temperature only, e.g. to −150° C.+/−20° C., refrigeration can operate more efficiently as compared to liquefying nitrogen, which requires temperatures below −196° C. at normal pressure.
Also, one kilogram of liquid nitrogen has no more than 56 Wh of cooling energy. Hence, substantial amounts of liquid nitrogen are required for largescale storage, and the cold parts of the storage must be highly insulated.
Using heat-pump-based cooling units as an on-site refrigerator device comes with the disadvantage that suitable pump liquids at cryogenic temperatures are typically flammable and/or toxic, and, for safety reasons, they are therefore poorly suited to cool a closed, well-insulated storage zone. However, combining them with the refrigerant circuit of the present invention allows to keep the heat pump liquid away from the storage zone.
Hence, in one embodiment, the refrigerator device comprises a heat pump having an evaporator, wherein the refrigerant circuit is thermally coupled to the evaporator.
An on-site refrigerator device may also comprise an air cycle machine, which is defined as a cooling device with an, advantageously closed, air cycle. In this cycle, air is first compressed in a compression turbine, then it is cooled in at least one hot-side heat exchanger, whereupon it is expanded in an expansion turbine. Finally, it is fed through at least one cold-side heat exchanger and fed back to the compression turbine. During the whole cycle, the air remains in its gaseous state.
This type of refrigeration device requires a large volume flow of air. Hence, they it is poorly suited for cooling storage devices where samples should be held in a tranquil, clean environment. This problem can be solved by coupling the cold-side heat exchanger to the refrigerant circuit mentioned above.
Hence, in a second embodiment, the refrigerator device comprises an air cycle machine having a closed air circuit with a compression turbine, a hot-side heat exchanger, an expansion turbine, and a cold-side heat exchanger. The refrigerant circuit is thermally coupled to the second heat exchanger. In operation, air is cycled (in that order) through the compression turbine, the hot side exchanger(s), the expansion turbine, and the cold-side heat exchanger(s). Thus, the cold-side heat exchanger can extract heat from the refrigerant circuit.
The storage device of both aspects of the invention is advantageously used for storing laboratory samples, such as biological or chemical samples.
Other advantageous embodiments are listed in the dependent claims as well as in the description below.
The invention will be better understood and objects other than those set forth above will become apparent from the following detailed description thereof. Such description makes reference to the annexed drawings, wherein:
A “low-temperature storage device” is a storage device adapted to store objects at temperatures below 0° C., in particular below −20° C., advantageously below −60° C.
A “heat pump” moves thermal energy in the opposite direction of spontaneous heat transfer by absorbing heat from a cold space and releasing it to a warmer one. Advantageously, a heat pump is a device having a condenser, an expansion valve, an evaporator and a compressor, with the compressor pumping a fluid to the condenser (which is heated), through the expansion valve, through the evaporator (which is cooled), and back to the compressor.
In the present context, heat pumps are used for cooling purposes.
Overview:
An embodiment of a storage device is shown in
The storage device comprises a storage chamber 1 enclosed by vertical insulating side walls 2a, an insulating ceiling 2b and an insulating floor 2d.
A transfer chamber 3 (
A door 6 provides user access to transfer chamber 3. In the embodiment of
A refrigerator device 10 is provided to cool storage chamber 1 to a storage temperature below 0° C., in particular below −20° C., and in the second aspect of the device below −80° C. Details of the temperatures within storage chamber 1 follow below.
Refrigerator device 10 also cools transfer chamber 3 to a transfer temperature below 0° C., in particular to approximately −20° C.
Advantageously, the air in transfer chamber 3 is cooled and dried such that it has a low dew point, in particular below −30° C.
The storage chamber 1 shown here is of cuboid shape. As best seen in
Top section 12 is located vertically above bottom section 11.
Bottom section 11 holds a cassette store 14 formed by a grid 15 located at the top of bottom section 11. Grid 15 forms an array of rectangular apertures 16. Each rectangular aperture 16 forms a cassette location for receiving a storage cassette.
An example of a storage cassette 17 is shown in
A metal plate 24 or a mechanical coupling member 24′ (shown in dotted lines) is located at the top of each storage cassette 17. It is used for gripping the storage cassettes as described in EP 2998669.
The individual cassette locations or apertures 16 in cassette store 14 have a size fitting the footprint of the storage cassettes 17 to be received. There may be differently shaped apertures 16 to receive differently shaped storage cassettes, such as cassettes having the SBS footprint of 134×86 mm and/or cassettes having a “cryobox” square footprint of 137×137 mm.
As best seen in
A first insulating wall 111 separates first storage zone 101 from second storage zone 102.
Second storage zone 102 surrounds first storage zone 101 in all horizontal directions. Insulating wall 111 is arranged vertically between them.
As explained above, the temperature T1 in first storage zone 101 is lower than the temperature T2 in second storage zone 102.
For example, the temperature T1 in first storage zone 101 is advantageously below −80° C. In particular, it is smaller than ˜110° C., in particular smaller than the glass transition temperature of water, i.e. smaller than ˜130° C.
The temperature T2 in second storage zone 101 is advantageously below −60° C., in particular between −100° C. and −60° C. Other temperature regimes are possible. However, the first temperature T1 is advantageously at least 10° C. below second temperature T2.
As described above, this design reduces the flow of heat from the environment into first storage zone 101 and therefore makes the storage device more energy efficient.
As shown in
Hence, if the top of bottom section 11 is to be at the same height over first and second zone 101, 102, longer storage cassettes 17 can be used in second zone 102 in order to fully exploit the available space.
Cassette Handler:
As best seen in
Cassette lift 26, or at least the cassette holder, is arranged on a transport mechanism 27a, 27b, which is adapted to horizontally displace the cassette holder with a raised cassette, between a position where the raised cassette is vertically above its cassette location to a transfer station 29 having a transfer opening 30 (see
In order to provide enough room for an upright storage cassette 17 as well as the overhead required by cassette handler 25, top section 12 of storage chamber 1 is advantageously somewhat higher than bottom section 11.
Transport mechanism 27a, 27b comprises a horizontal beam 27a spanning storage chamber 1 and being held at opposite ends by rails 27b. Beam 27a is located at the top of top section 12. Cassette lift 26 is suspended from beam 27a. A displacement drive is provided for horizontally displacing beam 27a along the rails 27b, and also for horizontally displacing cassette lift 26 along beam 27a.
The design of cassette lift 26 can e.g. correspond to the one shown in EP 2998669 as described in reference to
Transfer Station:
Transfer station 29 is shown in
In contrast to the design of EP 2998669, transfer opening 30 has a height H of less than three times the height h of one of the storage locations 22, in particular of less than two times the height of one of the storage locations.
In specific numbers, height H may be less than 50 cm, in particular less than 20 cm.
Further, transfer opening 30 may have a width W of less than two times the width w of the storage locations 22.
Using such a small transfer opening 30 in an otherwise closed wall 30 has the advantage of reducing heat and gas exchange when accessing the stored object. It also reduces the risk of accessing the wrong object.
Since transfer opening 30 has a height much smaller than the total height of a storage cassette 17, cassette handler 26 is programmed to vertically displace cassette 17 in transfer station 29 in order to position any desired storage location 22 next to transfer opening 30.
As is best seen in
Pit 33 is open at its top but it may be insulated against the storage zones.
Transfer opening 30 may be equipped with an automated door 34 for closing in when not used. In addition or alternatively thereto, a manually operatable door 35 may be provided.
Refrigerator Device:
In the shown embodiment, refrigerator device 10 advantageously comprises several heat pumps 40a, 40b, 40c arranged in series, with the condenser 41a of the first heat pump 40a being cooled e.g. by means of environmental air or cooling water, and its evaporator 41b cooling the condenser 42a of the next heat pump 40b etc., thus generating a series of temperature levels T1 (coldest) through Tn (with n >1 being the number of heat pumps and n=3 in
The evaporator 43b of the last heat pump may be used to cool the first storage zone 101, while the evaporator 42b of the second last heat pump may be used to cool the second storage zone 102, etc.
In the embodiment of
The storage-cooling heat exchangers 44, 45a, 45b can e.g. be designed as liquid-air exchangers or radiators cooling the air in the various parts of the storage device. In addition, they can be used for drying the air, in particular in transfer chamber 3.
The heat transfer device 46 coupling refrigerator device 10 to storage-cooling heat exchanger 44 in first zone is advantageously a refrigerant circuit, i.e. a circuit where a cryo-liquid, in particular argon or nitrogen, is circulated, at least in part in its liquid, sub-critical phase.
More details about heat transfer devices based on the refrigerant circuit are provided below.
Alternatively, liquid gas, in particular liquid nitrogen, may be used to cool one or more of the storage zones 101, 102.
As mentioned, the invention is also directed to a storage device having a refrigerant circuit for cooling the first storage zone. This second aspect can be applied to the storage device shown above but also to other types of storage devices, e.g. also to storage devices having non-concentric storage zones or only a single storage zone.
Some further embodiments of the second aspect are described in the following.
Storage chamber 1 has an outer region 50 (forming e.g. top section 12 and/or transfer chamber 3 in the embodiments above). Further, it comprises an inner region 52 (forming e.g. bottom section 11 in the embodiments above).
Outer region 50 reduces the transfer of humidity into inner region 52, and it is e.g. maintained at a temperature of −10° C. to −40° C.
Inner region 52 comprises a first storage zone 101 for storing objects at a temperature T1 below −80° C., in particular below −110° C., in particular below −130° C., e.g. at −150° C.+/−20° C.
Inner region 52 may also comprise a second storage zone 102 for storing objects at a higher temperature T2. Second zone 102 may horizontally surround first zone 101, as in the first embodiment, but this is not strictly required in the second aspect of the present technique.
Refrigerator device 10 of the present embodiment comprises several heat pumps 40a, 40c arranged in series.
Same as in the embodiment of
The evaporator 43b of the last (i.e. the coldest) heat pump 40c is thermally coupled to a refrigerant circuit 46 by means of a heat exchanger 54.
Refrigerant circuit 46 at least comprises a duct section 55 in heat exchanger 56, which is thermally coupled to evaporator 43b, and the storage-cooling heat exchanger 44.
In operation, the cryo-liquid is circulated in refrigerant circuit 46 to transfer heat from storage-cooling heat exchanger 44 to heat exchanger 54, thereby cooling storage zone 101.
In the shown embodiment, refrigerant circuit 46 is designed as a heat pump with a compressor 58 and an expansion valve 60. Storage-cooling heat exchanger 44 forms an evaporator, and duct 55 in heat exchanger 56 forms a condenser for the cryo-liquid. The cryo-liquid is in its sub-critical, liquid state at least on its path from heat exchanger 56 to expander or throttle 60.
Advantageously, an expansion vessel 61 is provided in refrigerant circuit 46. It is designed to receive cryo-liquid in case the temperature in the refrigerant circuit is high, e.g. when the storage device is not in operation.
In operation, first heat pump 40a may e.g. have a temperature between −10° C. and −40° C. at its cold side, i.e. at its evaporator 41b.
Heat exchanger T1 is coupled to a cooling device 45b by means of a heat transfer device 47b. Heat transfer device 47b may e.g. be a liquid circuit with a suitable pump.
Heat exchanger T1 is also coupled to evaporator 43a of heat pump 40c, which can e.g. use methane (R50), which evaporates at a temperature below −160° C. Methane is advantageous not only because of its low boiling point but also because it can be used as a heat pump fluid over a large temperature difference.
Heat pump 40c may e.g. also use ethane or another liquid. Suitable liquids are typically flammable.
Methane and ethane are environmentally friendly. However, flammable liquids should not be used in closed, poorly aired spaces, such as in first storage zone 101. However, refrigerant circuit 46 allows to design the cooling system without ethane or methane entering the storage zone.
In the embodiment of
Instead of or in addition to using a plurality of heat pumps in series, refrigerator device 10 may also comprise a heat pump using mix of several fluids having different boiling points and with liquid/gas separators in order to generate different temperature levels as known to the skilled person.
Cold-side heat exchanger 54 is again coupled to refrigerant circuit 46.
The hot-side heat exchanger(s) 72, 73 may be cooled e.g. by environmental air and/or water.
Advantageously, though, and as shown in
Heat pump 40a may comprise condenser 41a cooled e.g. by environmental air and/or water and an evaporator 41b. Evaporator 41b is coupled to second hot-side heat exchanger 73 of air cycle machine 65, which allows to reach lower temperatures at cold-side heat exchanger 54.
In other words, refrigerator device 10 advantageously comprises a first heat pump 40a having an evaporator 41b thermally coupled to a hot-side heat exchanger 73 of air cycle machine 65.
Advantageously, evaporator 41b of heat pump 40a is also coupled to at least one heat transfer device 47a, 47b for cooling a part of storage device 1 to a temperature between −5° C. and −80° C., in particular between −10° C. and −40° C.
In operation, air is compressed by compression turbine 66, cooled in the hot-side heat exchanger(s) 72, 73, and expanded in expansion turbine 68. The cooled air after expansion turbine 68 receives thermal energy in heat exchanger 54, whereupon it returns to compression turbine 66.
As described above, air cycle machine 65 can be used for reaching very low temperatures, e.g. around −150° C.+/−20° C., at heat exchanger 54.
Refrigerant circuit 46 is coupled to heat exchanger 54.
Refrigerant Circuit
As mentioned above, the refrigerant circuit 46 is used to carry heat away from storage zone 101.
As described above, refrigerant circuit 46 can be a heat pump evaporating the cryo-liquid in storage-cooling heat exchanger 44.
Alternatively, the cryo-liquid in refrigerant circuit 46 may be circulated in its subcritical, liquid state by natural convection or by means of a pump, without a phase change taking place.
Advantageously, the temperature in refrigerant circuit 46 is below −80° C., in particular below −110° C., in particular below −130° C. On the other hand, it is advantageously above −180° C.
In particular, the temperature at first storage-cooling heat exchanger 44 in storage zone 101 is at −150° C.+/−20° C.
To keep the cryo-liquid in its liquid state, the pressure in at least part of refrigerant circuit 46 (namely at the parts where the cryo-liquid should be liquid) is advantageously at least 2 bar, in particular at least 5 bar, e.g. 10-30 bar, in particular when using argon or nitrogen as a cryo-liquid. In one embodiment, it is at 15+/−3 bar when operating at a cryo-liquid temperature of −150+/−4° C. In another embodiment, it is at 25+/−3 bar when operating at an cryo-liquid temperature of −140+/−3° C.
The storage device further comprises a control unit 62 (which is shown, by way of example, in
Notes:
In some of the embodiments of the first aspect described so far, there are two storage zones 101, 102. There may, however, also be more than two storage zones, e.g. at least three storage zones, 101, 102, 103 as shown in
Refrigerator device 10 may control the third temperature T3 in third storage zone 103 to be higher than the second temperature T2 in second storage zone 102. Advantageously, second temperature T2 is at least 10° C. below third temperature T3.
In the embodiments of the first aspect as described above, second storage zone 102 horizontally surrounds first storage zone 101. Alternatively, and as mentioned, second storage zone 102 may surround first storage zone 101 only partially.
The temperatures and pressures of the refrigerant circuit given above are particularly optimized for using argon as a cryo-liquid, but they can be easily adapted to e.g. nitrogen or another inert gas by using the material's phase diagram.
The storage device can be used to store a vast range of objects, such as chemical or biological samples. The objects may e.g. be tube holders (tube racks) or microtiter-plates, with each tube rack or microtiter-plate being stored in its own storage location 22.
While there are shown and described presently preferred embodiments of the invention, it is to be distinctly understood that the invention is not limited thereto but may be otherwise variously embodied and practiced within the scope of the following claims.
Number | Date | Country | Kind |
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01375/19 | Oct 2019 | CH | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2020/078612 | 10/12/2020 | WO |