[0001] The invention relates to cooling apparatus, for example for use in cooling electrical
conductors to a temperature at which they superconduct. The invention is particularly
suited for cooling electromagnets to their superconducting condition for use in NMR
(nuclear magnetic resonance) and ICR (ion cyclotron resonance) experiments.
[0002] High field NMR magnets are often "sub-cooled" to a temperature a few Kelvin below
the atmospheric boiling point of liquid
4He (4.2K) to improve the critical current capacity of the superconductor and allow
a higher magnetic field to be generated. This is commonly achieved using a bath of
liquid
4He in which the magnet is submerged. The magnet bath or vessel is commonly cooled
to ~2.2K, which is just above the superfluid transition temperature, or λ point, of
4He (T
λ = 2.17K).
[0003] 2.2K is the preferred operating temperature for two reasons. The specific heat capacity
of
4He peaks at the λ point (Fig. 2), so it is desirable to operate as near the lambda
point as possible to improve the temperature stability of the system. However, it
is generally considered undesirable to operate below the λ point. This is because
a proportion of the liquid becomes superfluid, with zero viscosity, and it will flow,
even against gravity, through the smallest cracks and orifices towards areas of the
cryostat at higher temperature, thus causing a large heat leak and increasing boil-off
(the so-called "superleak" phenomenon).
[0004] In early sub-cooled systems the magnet containing vessel which contained liquid He
was simply pumped to a lower pressure, hence gradually evaporating the liquid bath
and sub-cooling the magnet. With this simple design it is necessary to warm up the
system, and hence de-energise the magnet, when the bath needs re-filling. To avoid
this major cost and inconvenience, the lambda point refrigerator was invented by Roubeau
and others ("The operation of superconducting magnets at temperatures below 4.2K",
Cryogenics, Feb 1972, p.44-47, Biltcliffe, Hanley, McKinnon, Roubeau).
[0005] More recently, as shown in Figure 1, a "lambda point refrigerator" has been used.
Referring to Fig. 1 a magnet 2 is submerged in liquid He in a first coolant containing
vessel 1 at atmospheric pressure. A second coolant containing vessel 3, which is open
to atmosphere, holds a reservoir of liquid He boiling at 4.2K; this reservoir 3 may
be refilled at any time. It is connected to the vessel 1 via a quench valve 14. Liquid
He is conveyed from the second vessel 3 to a heat exchanger 5 in the first vessel
1 via an (optional) second heat exchanger 6 and an expansion valve 4. The heat exchanger
5 is typically a coiled loop tube immersed in the top of the liquid helium bath of
the first vessel 1. The pressure in the loop 5, on the downstream side of the valve
4, is reduced by pumping using an external pump 13, typically to 20-50mbar. Helium
liquid passing through the valve 4 is partially vaporized and cooled by a few Kelvin
due to the pressure drop across the valve. The reduced vapour pressure in the loop
lowers the boiling temperature of the remaining liquid, which consequently evaporates,
absorbing heat from the magnet bath and cooling it via heat exchange through 5. The
vapour leaving the heat exchanger 5 is passed through the optional second heat exchanger
6, which pre-cools the liquid entering the valve with the aim of reducing the fraction
vaporized in the valve, and hence reducing the mass flow rate required for a given
cooling power.
[0006] The cooling power of the lambda point refrigerator constituted by components 4,5,6
is given by:

where dm/dt is the total mass flow rate, H is enthalpy and λ is the fraction of
liquid flashed to vapour in the valve.
[0007] The components described so far are located within a cryostat 20 comprising a number
of shields to be described below.
[0008] The cold vapour leaving the second heat exchanger 6 passes up the cryostat 20 though
another heat exchanger 10, absorbing heat from a gas cooled shield 7, which sits at
a temperature at about 40K, and then through a final heat exchanger 11, absorbing
heat from the second shield 8. The shields 7,8 of the cryostat 20 reduce the radiation
heat load on the helium vessels 1 & 3, reducing total boil-off. Because the outer
shield 8 sees the largest radiation load, it is common for it to have supplementary
cooling from nitrogen boiling at atmospheric pressure (77K) in a vessel 8a thermally
connected to the shield 8. The entire vessel assembly is enclosed in an evacuated
vessel 9 to reduce conduction and convection loss. The magnet 2 and inner vessels
are typically suspended using a web of fibreglass rods (not shown) to reduce conduction
heat load. A bore tube (not shown) at room temperature and pressure passes through
the assembly and through the magnet bore 22 to allow samples to be placed inside the
magnet 2.
[0009] After passing through a pump 13 located outside the cryostat 20 the helium gas is
either vented to atmosphere and lost, or collected for later re-use (after reliquefaction
in a separate plant).
[0010] In the event of a magnet quench (a failure of superconducting state and release of
stored magnetic energy as heat), the spring-closed pop-off valve 14 allows the boiling
helium in the first vessel 1 to escape to the second vessel 3, and hence to atmosphere,
before a dangerous over-pressure condition develops.
[0011] Whilst the system described above solves the refilling problem, it consumes a large
quantity of helium. The global supply of helium is limited and prices are expected
to rise significantly in the next decade. It is therefore desirable to reduce the
quantity of helium used in a sub-cooled cryostat.
[0012] In accordance with the present invention, cooling apparatus comprises a cooling system
defining a closed path around which a coolant flows, the system including a pump for
causing coolant flow, a supply line extending from the pump to a cold location, positioned
in a cryostat, in order to cool that location, and a return line extending from the
cold location to the pump, the pump being located externally of the cryostat; a first
heat exchanger positioned within the cryostat and linking the supply and return lines
to allow heat exchange therebetween such that coolant flowing in the supply line is
cooled by coolant flowing in the return line; and a refrigerator having a cooling
stage within the cryostat and coupled to the supply line downstream of the first heat
exchanger such that coolant reaching the first cooling stage has been precooled by
the first heat exchanger.
[0013] We have developed a solution to the problem mentioned above by providing a cooling
system defining a closed path around which the coolant, such as He, flows. This avoids
the need to refill the cooling system and has the additional advantage that only small
changes are required to be made to existing cooling systems in order to implement
the invention. The solution involves utilizing a refrigerator having at least one
cooling stage and assisting that cooling stage by including the first heat exchanger
so as to precool the coolant before it reaches the first cooling stage. This reduces
the power requirement of the first cooling stage to such an extent that conventional
refrigerators such as pulse tube refrigerators, can be used. Typically, the cooling
system includes a lambda point refrigerator located at the cold location while the
cold location may be located within an auxiliary coolant containing vessel. Alternatively,
an item to be cooled could be connected directly to the closed path of the cooling
system.
[0014] Although in some cases a single, first heat exchanger is sufficient, particularly
when cooling to higher temperatures, preferably the apparatus further comprises a
second heat exchanger, located within the cryostat, and linking the supply and return
lines such that coolant flowing in the supply line is cooled by coolant flowing in
the return line, the second heat exchanger being upstream of the first heat exchanger
with respect to coolant flow direction along the supply line.
[0015] The use of the second heat exchanger enables additional precooling to be achieved
thus further producing the power requirements on the refrigerator. Of course, further
heat exchangers could be provided if required.
[0016] In some cases, a single stage refrigerator can be used but in the preferred examples,
the refrigerator has an additional cooling stage, warmer than the one coolant stage,
the additional cooling stage being located within the cryostat and being coupled to
the supply line to cool the supply line at a location upstream of the first heat exchanger.
[0017] In addition, or alternatively, the refrigerator has an additional cooling stage,
warmer than the one cooling stage, the additional cooling stage being located within
the cryostat and being coupled to a shield of the cryostat so as to cool the shield.
[0018] In the most preferred embodiment, the additional cooling stage cools both coolant
in the supply line and the shield.
[0019] Where a second heat exchanger is provided, this is preferably located upstream of
the one cooling stage of the refrigerator with respect to the direction of flow of
coolant along the supply line.
[0020] Typically, the coolant which flows in the closed path of the cooling system comprises
He although other coolants could be used depending upon the temperature required at
the cold location. An alternative, for example is nitrogen.
[0021] The refrigerator is typically an electrically powered mechanical refrigerator such
as a pulse tube refrigerator since this has minimum vibration problems. However, it
will be appreciated that any cooler providing a low temperature cold stage and where
coolant (such as
4He) is consumed, could be used. Therefore, alternatives to pulse tube refrigerators
include Stirling, Gifford-McMahon, Joule-Thomson refrigerators, dilution refrigerators
and so on.
[0022] As explained above, the cooling apparatus can be utilized to cool a variety of objects
but it is particularly suited to the cooling of electrical conductors to their superconducting
condition as required, for example, in NMR, MRI and ICR where superconducting magnets
are required. In these cases, the magnets will define a bore, typically at room temperature
and the surrounding vessels will be shaped to allow remote access to the bore.
[0023] An example of cooling apparatus according to the invention will now be described
with reference to the accompanying drawings, in which:-
Figure 1 is a schematic cross-section through a known cooling apparatus;
Figure 2 illustrates the heat capacity of 4He near the lambda point; and,
Figure 3 is a view similar to Figure 1 but of an example of the invention.
[0024] In the following description, those components of the apparatus shown in Figure 3
which are the same as those shown in Figure 1 have been given the same reference numerals
and will not be described again in detail.
[0025] In the Figure 3 example, a closed cooling system is provided defined by a supply
line 26 extending from the pump 13 via a pump filter 13a into the cryostat 20 to the
lambda refrigerator 4-6 and a return line 28 extending from the lambda refrigerator
back to the pump 13. The supply line 26 opens into the second vessel 3 and is coupled
to a second stage 16 of a two stage pulse tube refrigerator (PTR) 24. This second
stage 16 recondenses helium vapour which boils in the vessel 3 and also condenses
helium supplied along the supply line 26. It absorbs typically a few 10s to 100s mW
of power.
[0026] Prior to reaching the second stage 16 of the PTR 24, the supply line extends through
a "first" heat exchanger 17 which links the supply line 26 with the return line 28.
This heat exchanger 17 allows the cold returning helium in the return line 28 to cool
helium being supplied along the supply line 26 prior to reaching the first cooling
stage 15. This reduces the cooling power required at the first cooling stage 15. This
first heat exchanger 17 is particularly important because it keeps the cooling power
requirement of the second stage 16 of the PTR 24 below about 1W (the limit of current
PTR technology at 4.2K).
[0027] A "second" heat exchanger 19 is provided upstream of the heat exchanger 17 with respect
to the supply line. The heat exchanger 19 allows further heat exchange between the
supply and return lines 26,28 so as to further precool the helium in the supply line.
[0028] A "third" heat exchanger 18 is provided coupled between the supply line 26 and the
shield 8. The shield 8 is connected to a first stage 15 of the PTR 24 which is used
to cool the outer shield 8 to about 40K, requiring about 30W for a typical large NMR
magnet system. In view of these connections, the first stage 15 of the PTR 24 cools
both the shield 8 and helium in the supply line 26.
[0029] The heat exchangers 17 and 19 utilise the enthalpy of the cold gas leaving the lambda
point refrigerator that, in the prior-art system, was used to cool the shields 7 and
8. The heat exchanger 18 adds a small heat load (a few watts) to the first stage 15
of the PTR 24.
[0030] Current PTR technology is limited to a cooling power in the second stage 16 of about
1W at 4.2K. Without the heat exchanger 17 it would not be possible to re-condense
all the helium boil-off from the lambda fridge in a typical state-of-the-art high-field
NMR magnet cryostat. By exchanging the enthalpy of the warm gas with the fridge exhaust
in exchanger 17 (and preferably also 19) the problem is solved.
[0031] It will be seen therefore that the invention provides a zero boil-off (ZBO) system
consuming no helium in normal operation and thus providing significant advantages
of no disruptive and costly refilling being required.
[0032] The effect of the "first" heat exchanger 17 can also be seen from the following analysis.
[0033] Assuming that the first stage 15 cools the vaporized helium to about 45K, then in
the absence of the heat exchanger 17, the cooling power required by the second stage
16 must be:

[0034] Where
- L =
- 83 J/Mol - helium latent heat,
- n' =
- flow rate of helium,
- HT =
- Helium enthalpy
[0035] However, since the cooling power of the outgoing helium flow does not need to be
utilized for cooling any radiation shields (unlike in the prior art) since the first
stage 15 achieves this cooling, this cooling power can be used to pre-cool the incoming
helium flow. The circulation of outgoing and return or incoming flows is the same
and so pre-cooling of the return flow from 45K down to about 5K can be achieved using
the heat exchanger 17. As a result, the heating power required at the second stage
16 can be reduced to about 0.3-0.45W. Such powers are readily available from commercially
available pulse tube refrigerators.
[0036] As explained earlier, the system shown in the drawings can be used to cool a variety
of items but particularly superconducting magnets which may be used in any conventional
configuration such as MRI, NMR, and ICR.
1. Cooling apparatus comprising a cooling system defining a closed path around which
a coolant flows, the system including a pump for causing coolant flow, a supply line
extending from the pump to a cold location, positioned in a cryostat, in order to
cool that location, and a return line extending from the cold location to the pump,
the pump being located externally of the cryostat; a first heat exchanger positioned
within the cryostat and linking the supply and return lines to allow heat exchange
therebetween such that coolant flowing in the supply line is cooled by coolant flowing
in the return line; and a refrigerator having a cooling stage within the cryostat
and coupled to the supply line downstream of the first heat exchanger such that coolant
reaching the first cooling stage has been precooled by the first heat exchanger.
2. Apparatus according to claim 1, wherein the cooling system includes a coolant containing
vessel forming part of the supply line, the cooling stage of the refrigerator being
located in the coolant containing vessel.
3. Apparatus according to claim 2, wherein the coolant containing vessel is also connected
to an auxiliary coolant containing vessel at the cold location whereby a portion of
the coolant can flow from the coolant containing vessel to the auxiliary coolant containing
vessel.
4. Apparatus according to any of the preceding claims, wherein the cooling system includes
a helium lambda-point refrigerator positioned at the cold location.
5. Apparatus according to any of the preceding claims, further comprising a second heat
exchanger, located within the cryostat, and linking the supply and return lines such
that coolant flowing in the supply line is cooled by coolant flowing in the return
line, the second heat exchanger being upstream of the first heat exchanger with respect
to coolant flow direction along the supply line.
6. Apparatus according to any of the preceding claims, wherein the refrigerator has an
additional cooling stage, warmer than the one coolant stage, the additional cooling
stage being located within the cryostat and being coupled to the supply line to cool
the supply line at a location upstream of the first heat exchanger.
7. Apparatus according to any of claims 1 to 5, wherein the refrigerator has an additional
cooling stage, warmer than the one cooling stage, the additional cooling stage being
located within the cryostat and being coupled to a shield of the cryostat so as to
cool the shield.
8. Apparatus according to claim 6 and claim 7, wherein the shield is coupled via a third
heat exchanger to the supply line so that the additional cooling stage of the refrigerator
cools both the shield and coolant in the supply line.
9. Apparatus according to claim 8, wherein the second heat exchanger is located outside
the shield.
10. Apparatus according to any of claims 7 to 9, wherein the shield is also cooled by
a second coolant contained within a second, coolant containing vessel attached to
the shield.
11. Apparatus according to any of the preceding claims, wherein the coolant in the cooling
system comprises helium.
12. Apparatus according to any of the preceding claims, wherein the refrigerator comprises
a pulse tube cryocooler.
13. Apparatus according to any of claims 1 to 11, wherein the refrigerator comprises a
Stirling, Gifford-McMahon, Joule-Thomson or dilution refrigerator.
14. Apparatus according to any of the preceding claims, wherein the one cooling stage
of the refrigerator provides a temperature of about 4K.
15. Apparatus according to at least claim 6, wherein the additional cooling stage of the
refrigerator provides a temperature in the range 40-50K.
16. Apparatus according to any of the preceding claims, further comprising a superconducting
magnet located at the cold location.
17. Apparatus according to claim 16, wherein the superconducting magnet defines a room
temperature bore adapted to receive a sample.
18. NMR or ICR apparatus including cooling apparatus according to claim 17; and a probe
for insertion into the bore, the probe having means to support a sample.