Page 1

Practical Cryogenics

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

An Introduction to Laboratory Cryogenics

By N H Balshaw

Published by Oxford Instruments Superconductivity Limited

Old Station Way, Eynsham,

Witney, Oxon, OX29 4TL, England,

Telephone: (01865) 882855

Fax: (01865) 881567

Telex: 83413

 

 

Contents

1

2

2.1

2.2

3

3.1

3.2

3.3

3.4

3.5

3.6

3.7

3.8

4

4.1

4.2

4.3

4.4

4.5

4.6

4.7

4.8

4.9

5

5.1

3

5.2

3

He/

4

5.3

5.4

6

6.1

6.2

6.3

6.4

6.5

6.6

6.7

6.8

6.9

6.11

Interfacing superconducting magnets to dilution refrigerator

7

7.1

7.2

7.3

7.4

7.5

8

8.1

8.2

8.3

8.4

8.5

9

9.1

9.2

10

11

12

 Oxford Instruments Superconductivity Limited, 1996-2001. All rights strictly reserved.

ISBN 0 9527594 0 3

This document is intended to be used only as background information, and not

as an instruction manual. No liability will be accepted for any damages

incurred because of the information contained in, or implied by, the contents.

First edition published 1996.

This imprint 2001.

5

1

Foreword

This booklet has been written to help you to learn more about the basic principles of

cryogenics, so that you can design your experiments to make the best possible use of your

system. A little training often makes the difference between success and failure for a low

temperature experiment.

The booklet is a collection of practical notes to introduce beginners to the fundamentals

of good practice. It contains a 'glossary of terms' to explain some of the jargon commonly

used in cryogenics. The descriptions are intended to translate these terms into plain

English so that beginners can understand them.

The other sections give general advice on a range of relevant topics. A strong emphasis is

placed on practical information rather than theoretical details. Previous editions of this

booklet (then called Elementary Practical Cryogenics) contained some of this information.

Several small errors have been corrected and more information has been added.

The subject of 'safety' has deliberately been omitted. All cryogens are potentially

hazardous. Before you try to use a cryogenic or high magnetic field system you should

receive training from a competent person who knows your laboratory and the laws in your

country. You may then like to use the booklet Safety Matters (available from Oxford

Instruments) to remind you about this training when you are using a system.

N H Balshaw

7

2

Vacuum equipment

Vacuum systems are used most commonly in laboratory scale cryostats and superconducting magnet systems for the following purposes:

•

To pump out the high vacuum insulation spaces in the cryostat and transfer tube

•

To pump out an exchange gas

•

To set up a pressure gradient along a pumping line so that the flow of cryogen

through the cryostat can be controlled

•

To reduce the vapour pressure over liquid helium surfaces where temperatures below

4.2 K are required

•

To pump out the nitrogen gas from a pre-cooled helium vessel, after the liquid has

been blown out

All gases, except helium, hydrogen and neon, will condense on surfaces cooled to below

about 60 K. Therefore, once liquid helium at 4.2 K is introduced into a vacuum vessel, all

the residual gases that are normally present will condense (or cryopump), reducing the

pressure in the vacuum space by one or two orders of magnitude. Therefore, the function

of a vacuum system is to reduce the pressure in the vacuum space to a point where the

thermal insulation is sufficiently good to allow liquid helium to be held in the vessel. In a

typical laboratory scale system the pressure then drops to 10

-5

mbar or less.

In cryostats that contain only liquid nitrogen, the coldest surface is at 77 K, which is above

the temperature for effective cryopumping by a metal surface. If the cryostat is not

pumped continuously by an external pumping system, a sorption pump is mounted on the

liquid nitrogen reservoir to maintain the integrity of the vacuum. Occasionally it has to be

cleaned by warming it to a temperature around 100

o

C and pumping the vacuum space. It

pumps air to a very low pressure when cooled with liquid nitrogen.

A booklet is available from Leybold to describe how to do most common vacuum

calculations. (See section 12).

2.1

Vacuum pumps

2.1.1

Single stage rotary pumps

Rotary pumps are used as roughing pumps (to reduce the pressure to a rough vacuum) or

as backing pumps (with a diffusion pump or turbomolecular pump). If the rotary pump's

sole function is to back a small oil diffusion pump or a turbomolecular pump then a single

stage rotary pump with a base pressure of about 10

-2

mbar and a displacement of about

5 m

3

/hour is adequate. However, some laboratories prefer to use a two stage rotary pump

with a diffusion pump because of the risk of stalling the diffusion pump if the backing

pressure exceeds a critical value (about 10

-1

mbar). If the diffusion pump stalls oil back-

streams into the vacuum system and can permanently affect the performance of the

cryostat.

If the rotary pump is also to be used as a roughing pump or to reduce the vapour pressure

over a liquid surface it may be necessary to choose a higher displacement pump to suit the

requirement. Most vacuum equipment manufacturers supply the information needed to

calculate the pump size in their sales brochures.

 

 

 

 

 

 

8

In most cases, it is best to use a pump fitted with a 'gas ballast' facility. This helps the

pump to remove condensable vapours from the vacuum space of a cryostat. It is common

for water to accumulate in the vacuum spaces of cryostats if the cold surfaces are ever

exposed to air or if the cryostat is left unused for some time. Most surfaces release

absorbed water vapour when the pressure is reduced.

Practical base pressure:

10

-2

to 10

-3

mbar

Max. working pressure:

1 bar (for a limited period), few hundred mbar

continuously

Ideal for:

Rough pumping, backing high vacuum pumps, lambda

point refrigerators, variable temperature inserts, 1 K pots

Figure 1 Rotary pump system

2.1.2

Two stage rotary pumps

In some cases, it is possible to replace a rotary / diffusion pump combination with a two

stage rotary pump. A base pressure of 10

-4

mbar can be achieved in ideal conditions and

using a cold trap, but in practice the pressure in the cryostat will probably only be 10

-1

to

10

-2

mbar.

This type of pumping system is very simple but it cannot reach a low enough base pressure

to give good thermal isolation . A large amount of liquid helium would be required to

cryopump the residual gas and the static boil off of the system would be slightly increased.

In addition, if the cryostat is used above 60 K and there is no sorption pump in the vacuum

space, condensation or frosting may be seen on the outside of the cryostat.

2.1.3

Diffusion pumps

A 50 to 75 mm diameter oil diffusion pump is sufficient for pumping laboratory scale

cryostats. An air-cooled pump with an air pumping speed of about 50 litres/second and an

ideal ultimate pressure of about 10

-7

mbar is commonly used.

 

9

It is advisable to use a cold trap with a diffusion pump (although some people do not

consider it to be essential). You should never pump the vacuum space of a cold cryostat

without a cold trap between the pump and cryostat. This trap helps to remove water

vapour from the vacuum space and prevents back streaming of oil vapour from the pump.

Two types of trap are commonly used, liquid nitrogen filled traps and thermo-electric

(Peltier effect) cooled baffles. The latter require less attention and are better for very

long-term unattended operation.

Practical base pressure:

10

-7

mbar

Max. working pressure:

10

-2

to 10

-1

mbar

Ideal for:

Pumping insulating high vacuum spaces in cryostats (e.g.

OVCs)

Figure 2 Diffusion pump system

2.1.4

Turbomolecular pumps

These high vacuum mechanical pumps can be used instead of diffusion pumps. They are

especially useful if a very clean high vacuum is needed because the compression ratio is

strongly dependent on the mass of the molecules. The large hydrocarbon molecules are

pumped so well that there is virtually no backstreaming of oil. Many of the modern

pumps incorporate a molecular drag stage within the pump and can tolerate a backing

pressure of 10 mbar or higher. An oil free diaphragm pump can then be used as the

backing pump for some applications.

10

Practical base pressure:

10

-8

mbar

Max. working pressure:

A few mbar (for conventional turbomolecular pumps).

About 30 mbar (for some pumps with a molecular drag

stage).

Ideal for:

Pumping clean high vacuum spaces (with or without cold

trap).

Figure 3 Turbomolecular pump system

The pumping speed for helium is about 20% higher than that for nitrogen, but the

compression ratio is much lower. Therefore if the pump is to be used to pump helium

from a vacuum space it is best to use a two stage rotary pump, so that the backing

pressure is as low as possible. A diffusion pump is still better at pumping helium!

Turbomolecular pumps should only be vented (from the high vacuum side) while they are

still spinning slowly. This helps to prevent contamination backstreaming from the high

pressure side of the pump. Most pumps can be fitted with an automatic venting device

which is activated by the pump controller. The gas can be drawn through a drier cartridge

to prevent contamination with water.

11

2.1.5

Roots pumps

Roots pumps (or roots blowers) are mechanical booster pumps, used (in conjunction with a

backing pump) to reach the medium to high vacuum range with very high gas

throughputs. Two (or more) pumps can be used in series with some advantage. For

example, if you need a pumping speed of 1000 m

3

/h it may be best to use a 1000 m

3

/h

roots pump backed by a 250 m

3

/h roots pump, which in turn is backed by a 65 m

3

/h rotary

pump. Vacuum companies often recommend a 1000 m

3

/h roots pump backed by a

250 m

3

/h rotary pump, but this option is usually more expensive.

Practical base pressure:

10

-4

mbar

Max. working pressure:

Few hundred mbar

Ideal for:

High volume flow rates in the pressure range 10

-4

to 50 mbar

(for example, in dilution refrigerator systems)

Figure 4 Roots pump system

2.1.6

Sorption pumps (or sorbs)

Sorption pumps are often used in vacuum spaces because they are cheap and reliable, and

they require little maintenance. The adsorbent material (usually activated charcoal or a

molecular sieve) has a very large surface area, and the gas molecules are trapped onto the

surfaces when the sorb is cold.

Liquid nitrogen cryostats usually have a sorb fitted to the outside of the nitrogen vessel to

maintain a good insulating vacuum. If a sorb is not used the vacuum slowly deteriorates

as the warm surfaces outgas. A 77 K sorb will not trap helium gas, but if it is cooled to

4.2 K helium gas may be pumped to below 10

-5

mbar. Liquid helium vessels are cold

enough to freeze any gas except helium onto the metal surfaces, so a sorb is not usually

fitted because it may hinder leak detecting operations.

12

These pumps are single shot devices. They eventually become saturated and have to be

warmed (and sometimes evacuated with a suitable high vacuum pumping system) to

regenerate the absorbent material. The amount of gas that can be pumped before the

sorb is saturated depends on the type of gas and the temperature of the pump, but in a

high vacuum environment, they may be expected to last for a period of months or years

before they need to be regenerated.

2.1.7

Cryopumps

A cryopump usually consists of a large number of metal plates cooled to a temperature

close to 4.2 K, (either by liquid helium or by a closed cycle cooler). Like sorption pumps,

these are single shot pumps and they have to be regenerated when a layer of ice has

collected on the metal surfaces. The pump relies on the fact that the vapour pressure of

most materials at a temperature below 10 K is negligible. This type of pump is essentially

clean and it is suitable for use in ultra high vacuum systems.

2.2

Vacuum accessories

2.2.1

Oil mist filter

An oil mist filter is used to remove the fine mist of oil from the exhaust gas of a rotary

pump. It is desirable to remove this mist for the following reasons.

•

The vapour represents a health hazard if inhaled

•

It may contaminate any flow meters or other fittings behind the pump, changing their

calibration

•

It is desirable to avoid contaminating the helium recovery system with pump oil.

Several different types of filter are available. The following are the most common:

a) Coalescing filters, which only need to be replaced if they are dirty. The oil normally

runs back into the pump continuously.

b) Centrifugal filters or 'catch pots', which usually have a transparent bowl to collect the

oil, and have to be emptied occasionally.

2.2.2

Vacuum gauges

High vacuum is normally measured using a combination of Pirani and Penning type

gauges. Typically, the Pirani gauge operates in the range 10 mbar to 10

-3

mbar, and the

Penning in the range 10

-2

mbar to 10

-7

mbar. The calibration of these gauges (and some

others) depends on the type of gas in the system.

Vacuum in the range from 1 to 1000 mbar is normally measured with reasonable accuracy

using a simple capsule or dial gauge. Other types of gauge are available, for example,

Piezoelectric gauges and Baratron gauges, which allow accurate remote measurement.

2.2.3

Pumping lines

The pumping lines may have as large an effect on the efficiency of the vacuum system as

the pumps themselves. Check the following points:

a) The lines must be leak tight. Plastic or rubber materials are sometimes used as

pumping lines but they may be permeable to helium gas.

13

b) The throughput of the lines must be at least as high as that of the pumps. Otherwise

their impedance limits the flow of gas and may affect the base pressure at the cryostat

end of the line. It will certainly affect the amount of time required to pump down to

the required pressure.

c) The lines should be clean inside. If there is any moisture in the lines it will limit the

pressure that can be reached. If the lines are heavily contaminated with helium gas it

will be difficult to perform the normal leak tests.

2.2.4

Mass spectrometer leak detectors

Although these machines are expensive, it is very useful to have access to one. The leak

detector need not be dedicated to one system; it can be shared by the lab or the

department. In general, the more complicated the system is, the more useful the leak

detector will be. For example, a complex dilution refrigerator system may have 500 to

2000 joints that must be leak tight. Many of these are subject to thermal cycling, and a

leak from almost any of them could cause a system failure. It is clearly important that any

leaks can be traced and cured as quickly and easily as possible. A sensitivity of 10

-8

mbar l/s

(or standard cm

3

/s) is sufficient for most purposes, but 10

-10

mbar l/s is preferred when

looking for very fine leaks or superleaks.

If you have little or no experience of using these leak detectors , refer to section 3.

2.2.5

Foreline traps

A foreline trap is sometimes used on the inlet of a rotary pump to reduce the amount of

oil backstreaming up the pumping line. The active material in the foreline trap must be

changed regularly so that it remains effective.

2.2.6

Choosing an appropriate 'O' ring material

Silicone rubber is often used for 'O' rings in electrical equipment, but it is not generally

suitable for cryogenic equipment because the material is porous to helium gas. However,

it is probably suitable for dynamic seals at temperatures down to -60°C, or static seals

down to -100°C. It can also be used up to 250°C.

Butyl rubber was an old favourite material for vacuum applications, and it was often used

because of its low gas permeability. Suitable for temperatures down to -60°C.

Nitrile rubber (or Buna N) is probably the best material for most common vacuum

applications. It is cheap, easily available in a range of sizes, and appropriate for

temperatures slightly below room temperature. It is also resistant to silicon grease (for

example, vacuum grease). Its working temperature range is from -40°C to +120°C.

Fluoroelastomer (for example, 'Viton') is also suitable for vacuum. It is better than nitrile

rubber for high temperature applications, but it is more expensive and tends to be

deformed permanently after being compressed for a length of time. Its working

temperature range is from -20°C to +200°C. Beware: if it is subjected to temperatures

much higher than 200

o

C, the black sticky residue contains hydrofluoric acid!

Teflon (or PTFE) can also be used to make vacuum seals. However, the joint has to be

designed to prevent the Teflon 'creeping' when it is compressed.

14

3

Detecting vacuum leaks

3.1

Introduction

These notes describe how to locate leaks in complex vacuum systems using a helium

sensitive mass spectrometer leak detector. They do not describe how to use the leak

detector in detail, because so many different models are available. Consult the instruction

booklet for this information (and good luck!). Better still, ask someone to show you how

to use the leak detector.

Warning:

Before you attempt to carry out a leak test, it is important to check that it is safe

to evacuate a vessel, and that there is no risk of it collapsing because of the

external pressure of the atmosphere. This is especially important for vessels

which have thin walled tubes (for thermal reasons) and for large vessels. If you

collapse a vacuum vessel you might be badly injured by the shock wave or by

flying fragments.

Helium sensitive leak detectors are used because:

•

Helium atoms are small and mobile, so they can pass through small holes easily

•

Helium gas is inert and safe to use

•

There is very little helium in the air allowing the leak to be located precisely

Vacuum leaks are most commonly associated with:

Welds

Leaks caused by imperfect welds, cracked welds, or corrosion around the weld.

Soldered joints

Leaks caused by imperfect joints, or corrosion.

'O' ring seals

Dry, damaged or broken 'O' rings, or scratches or hairs lying across the seal are the most

common sources of problems. (As a rough guide, a hair lying across an 'O' ring may cause

a leak in the range 10

-6

to 10

-3

mbar ls

-1

, depending on many factors.)

Indium seals

Insufficient compression of the indium wire, dirt on the metal faces or scratches across the

seal may cause leaks. Problems after thermal cycling might point to poor flange design.

Glued joints

Leaks may be caused by bad joint design, bad surface preparation, inappropriate choice of

glue, or rapid thermal cycling.

Porosity of metals

Gas sometimes leaks along the grain of a metal (especially in some grades of brass). Small

flanges are commonly made of plate rather than bar for this reason.

Diffusion

Many plastics and composites are porous to helium gas at room temperature but not

when cooled down. Materials must be chosen appropriately for the working environment

and temperature range.

Thermal cycling

Leaks may be undetectable at room temperature but only open when the component is

cooled to liquid nitrogen temperature. Sometimes the leak will still be detectable when it

is warmed up again. If not, repeated thermal cycling may help to open the leak path and

make detection easier.

15

Superfluid leaks

Components that are leak tight at room temperature and even in liquid helium may leak

when subjected to superfluid helium (which has zero viscosity). This is the most difficult

type of leak to find!

3.1.1

Getting started

Vacuum leak detection is an art, but a scientific approach helps. When you start to learn

how to use the leak detector you will almost certainly find yourself looking for leaks that

do not exist, and you could waste hours if you are not careful. These notes should help

you to avoid most of the common problems.

Most leak detectors have an audible signal and a visual display. Both of these are useful.

The visual display is used to quantify a leak and detect a slow change in the signal, so it is

especially useful to help you locate small leaks. The audible signal is much easier to use

for general leak testing, because you do not have to look at the leak detector. You can

then concentrate on looking at the equipment that you are testing and if you hear the

signal rise you can go back over the same area again more slowly, and try to pin point the

position of the leak.

From time to time the sensitivity of the leak detector should be checked and reset using a

'standard leak', since the sensitivity peak may drift.

3.2

Leak testing a simple vessel

3.2.1

Preparations

Consider first how to test a simple vessel for leaks: for example, a flexible pumping line.

The principles learnt here can then be extended to more complex systems.

Evacuate the line to a rough vacuum using a suitable rotary pump, and then pump it to a

sufficiently high vacuum for the mass spectrometer to be used (typically 10

-5

mbar). Many

leak detectors will evacuate the vessel and switch on the mass spectrometer for you

automatically.

Select a suitable sensitivity range so that a small leak can be detected. For most cryogenic

systems the 10

-8

mbar l/s range (or 10

-8

standard cm

3

/s) is best. If you use a more sensitive

range than this the background helium signal in the vacuum space may exceed full scale

on the leak detector. If you use a less sensitive range you may not notice the leak.

If the background signal is too high to allow you to use a sensitive range, pump the vessel

until the signal has been reduced sufficiently. You can sometimes reduce the signal more

quickly by 'pumping and flushing'. Pump the air out of the system until it reaches a

pressure of a few mbar, allow dry nitrogen (or air if this is not available) into the vacuum

space again (slowly to avoid damaging the vacuum vessel), and repeat the process as often

as necessary.

3.2.2

Leak testing the pumping line

Spray the pumping line with helium gas, paying special attention to any joints. If possible,

place it in a plastic bag, and fill the bag with helium, so that there is no chance of missing

a small leak in an unexpected position. However this is likely to be impractical for large

vessels.

16

If the signal on the leak detector rises at any time during the test, a leak should be

suspected, and you should methodically check to find out whether the leak is real, or an

artefact caused by the outgassing of some trapped gas within the vacuum system.

3.2.3

Work from the top

Remember that helium gas is lighter than air so it rises. Therefore you should start by

spraying gas on the highest point, and slowly work downwards. If the signal on the leak

detector rises at any time, go back over the area that you have just covered, and check

again. If you do not start at the top you can get misleading results when you are checking

an area below the position of the real leak.

When you have found the approximate location of the leak, fit a fine nozzle to the end of

the helium gas line, and reduce the flow of gas. Check the suspect areas in detail. You

can locate leaks very precisely. Usually (but not always) you can see a small hole, flaw in

the material or dullness of the surface at the leak position.

If you want to test a long weld on a large vessel you can fix a tunnel of plastic sheet to the

vessel with adhesive tape and fill the tunnel with helium gas.

3.3

Locating 'massive' leaks

Occasionally you may find a leak that is so big that you cannot reduce the pressure

sufficiently to use the mass spectrometer. How can you find the position of the leak?

3.3.1

The safe method

Connect a large displacement medium vacuum pumping system in parallel with the mass

spectrometer, as shown in Figure 5.

Figure 5 Locating a massive leak in a vacuum system

Pump the vacuum system to a rough vacuum with the rotary pump. Then slightly open

the throttle valve on the pumping port of the mass spectrometer. Make sure that the

pressure at the inlet of the leak detector is not too high for it to work properly.

17

It is sometimes possible to check for a leak by slightly pressurising the vessel with helium

gas as described in section 3.8.

3.3.2

The other way (at your own risk)

Some people use water, acetone or methanol to locate leaks on small systems. Open the

gas ballast valve on the pump to make sure that contamination does not collect in the

pump oil.

Hazard:

Acetone or methanol are flammable so you must not use them in large quantities. Take

care not to create a fire hazard - contact your safety officer first.

Pump the vessel to a rough vacuum and measure the pressure. Brush liquid onto the

outside of the vessel. The pressure rises quickly when the area of the leak is found.

These liquids may also be used to block a 'massive' leak temporarily, so that the rest of the

vessel may be tested. Apply the liquid with a brush. Initially the pressure rises, but soon

the liquid freezes and blocks the leak. You can remove the ice by gently warming the

area with a hot air blower.

3.4

Leak testing sub-assemblies

If you are building a complex system you can test the sub-assemblies before you join them

together. In this way you can locate leaks before the system is assembled. Components

that are not fitted with standard vacuum fittings can be sealed to suitable plates using a

product such as Apiezon

TM

'Q compound'. This is a malleable material that can be used to

make a temporary seal, but it is only suitable for use at room temperature.

Occasionally you may find a component that has a detectable leak in one direction but not

in the other. Therefore it is best to test components by evacuating the side that will be

under vacuum in the finished assembly. In any case you must check that it is safe to

evacuate the vessel, and that there is no danger of it collapsing.

3.5

Testing more complex systems

Most real cryogenic systems are quite complex. It may be useful to consider a liquid

nitrogen shielded liquid helium dewar, which would usually be tested at room

temperature and at liquid nitrogen temperature. If a vessel is leak tight at 77 K it is

unusual for it to develop a leak as it is filled with liquid helium at its normal boiling point.

This is probably because most materials undergo very little thermal contraction below

77 K, so thermal stresses induced by cooling to 4.2 K are smaller than those caused by the

initial pre-cooling process.

The dewar must be leak tight in the following ways:

•

Outer vacuum chamber (OVC) to air

•

Liquid helium reservoir to OVC

•

Liquid nitrogen reservoir to OVC

18

Evacuate the OVC, and set up the leak detector to monitor it. Check the outside of the

dewar as described in section 3.2. Then flush the liquid nitrogen and liquid helium vessels

with helium gas. The best way to check them thoroughly is to pump the air out of each

vessel using a small rotary pump, and then to fill each vessel in turn with helium gas.

Sometimes the signal on the leak detector rises and falls again as the pressure in one of

the reservoirs changes. This might not indicate a leak; small movements of the vessels can

release gas from the surfaces. You can check this by repeating the test using air instead of

helium gas.

If there is any doubt about the presence of a minute leak, use a chart recorder to monitor

the signal from the leak detector. You should then see a step on the chart when the

helium gas is allowed into (or pumped out of) the suspect space. This makes it easier to

distinguish between a real leak signal and noise on the signal.

When you have finished the room temperature leak tests, you can pre-cool the cryostat to

77 K. Then blow the liquid nitrogen out of each space in turn using helium gas, while you

monitor the OVC with the leak detector.

3.5.1

Pumping and flushing with helium gas

When you have removed all of the liquid, pump the vessel to a pressure of a few mbar,

and then fill it with helium gas. This ensures that small leaks are not blocked by

remaining droplets of liquid nitrogen.

3.5.2

Temperature effects

If you see a signal rise it may have been caused by a temperature change. Helium gas

(trapped on the surfaces) may be released as warm gas is allowed into the vessel.

3.5.3

Masking cold leaks

If you discover a cold leak, you might be able to determine the approximate position of

the leak by refilling the vessel with liquid nitrogen and then blowing the liquid out again

with helium gas. When you see the signal rise again stop blowing out the liquid, and

measure the level of the liquid. The leak is probably at this height in the vessel.

3.5.4

More complicated systems

You can check even more complicated systems in a similar way; for example, dewars with

variable temperature inserts or dilution refrigerator inserts in the liquid helium reservoir.

Think in advance about the best order to carry out the leak tests. In this way you can

often reduce the number of pumping operations. You may be able to test several vessels

at once. It is only necessary to check them individually if you discover a leak.

19

3.6

Leaks at 4.2 K and below

Any leak found at a temperature below 4.2 K is difficult to locate, because helium gas

tends to be absorbed onto the cold surfaces. It may take a long time for the leak detector

to respond to a small leak, so patience is essential. Do not be tempted to hurry the tests.

It may take many hours for a positive result to be obtained. It is sometimes best to warm

up the system to 77 K and pump the helium gas away thoroughly before cooling to 4.2 K

again, because this removes the gas absorbed on the cold surfaces. Check each possible

source of the leak in turn, with the others under vacuum to eliminate any possibility of

confusion. At best, you will only be able to determine which space is responsible for the

leak.

If the leak is very small, it is possible for the leak detector to pump away the helium gas at

the same rate as the leak, and so the signal may not be seen to rise at all. In this case,

close off the vacuum space for a few hours, and compare the signals before and after the

test period. Make sure that the conditions for both readings are identical, so that thermal

effects on the outgassing rate can be neglected.

3.7

Superfluid leaks (or superleaks)

Superleaks will only be seen at temperatures below the lambda point (2.2 K). Superfluid

liquid

4

He (also known as helium II) has zero viscosity and can pass through very small

holes quickly. Fortunately these leaks are quite rare, because it can take days or weeks to

cure them.

Location of the precise position of the leak is extremely difficult. It may be possible to

open up the leak sufficiently to detect it at 77 K (or even room temperature) by rapid

thermal cycling, but this technique is not always successful. Failing this, the only other

course of action is to replace joints or components, starting from the easiest operations.

This would normally be done in the following order (probably with a leak test after each

step):

•

Indium seals replaced

•

Wood's metal joints re-run

•

Soft soldered joints re-run

•

Silver soldered joints re-run

1

•

Welds re-made

•

Components or sub-assemblies replaced

1

You can only re-run silver soldered joints if there is no soft solder nearby. If soft solder is heated to

the melting temperature of silver solder it can dissolve other materials into solution. It is then almost

inevitable that the joint will leak, even if a large hole has not appeared.

20

3.8

Overpressure leak detection

Overpressure helium sensitive leak detectors ('sniffers') can be used to detect helium gas in

the air. You can use these to detect very large leaks on vacuum systems but they should

not be relied upon for the routine testing of cryogenic equipment. The vessel should be

slightly pressurised with helium gas, and the sniffer is then used to detect where the gas is

escaping. It is also important to check that it is safe to over-pressurise the vessel before

trying to use this technique.

Sniffers are especially useful to detect the location of a leak in a helium recovery system,

or on the (room temperature) fittings on the helium reservoir of a cryostat.

21

4

Cryostats and coolers

Various types of cryostat are available, and each type has advantages and disadvantages

compared with the others. The following notes may help you to decide on the best type

of system for your application.

In general, if the cryostat has to be very large (for example, to contain a superconducting

magnet or conventional

3

He/

4

He dilution refrigerator) it is best to use a 'bath' cryostat.

You can fit a suitable continuous flow insert within the bath cryostat to achieve the

sample temperature range required for your experiment.

However, if the cryostat has to fit into a small space or has to be thermally cycled rapidly

and often, and the experimental equipment does not need a self contained reservoir of

cryogen, it may be better to feed liquid from a remote storage dewar through a special

transfer tube. This is called a 'continuous flow' cryostat.

The different types of cryostat that are widely available are described individually in the

following sub-sections.

4.1

Bath cryostats

Bath cryostats contain large enough supplies of cryogens for a convenient period of

operation. There is no need to refill the cryostat continuously from a storage dewar. The

'hold time' depends on a number of factors, (for example, size, experimental heat load

and cryogen consumption rate). They are typically designed to give operating periods

between 10 hours and 4 months.

Two types of bath cryostat are commonly used for laboratory scale liquid helium

temperature systems. Both types are vacuum insulated to reduce the heat load due to

conduction and convection. However, the helium reservoir is shielded from the room

temperature radiation heat load in different ways. According to Stefan's Law, the amount

of heat radiated from a warm body to a cold body varies with the difference between the

fourth power of their temperatures. Therefore a 300 K surface radiates 230 times more

heat to a 4.2 K surface than a 77 K surface would radiate onto the same 4.2 K surface.

Therefore liquid helium reservoirs are always shielded from room temperature radiation

by a cooled shield. In most cryostats, the radiation load is further reduced by the use of

'multi-layer superinsulation'. This consists of many thin layers of low emissivity material, in

the insulating vacuum space.

4.1.1

Liquid nitrogen shielded cryostats for liquid helium

In this type of cryostat, the liquid helium reservoir is surrounded either by a reservoir of

liquid nitrogen, or by a shield cooled by this reservoir. The liquid nitrogen vessel is

thermally linked to the neck of the liquid helium vessel to form a thermal barrier to heat

conducted down from room temperature. Figure 6 shows a typical small liquid nitrogen

shielded cryostat used to cool an infra-red detector to 1.5 K.

22

Figure 6 Low loss infra-red detector cryostat

The advantages and disadvantages of liquid nitrogen shielded cryostats are summarised in

Table 1 on page 23.

4.1.2

Vapour shielded cryostats for liquid helium

As an alternative to liquid nitrogen cooled shields, it is possible to link several thermal

shields to the neck of the liquid helium vessel. The cold gas that has evaporated from the

reservoir is then used to cool these shields. This type of cryostat typically has between two

and six shields (depending on the required performance) linked to different points on the

neck. The space between the shields is filled with superinsulation.

The boil off rates of the two types of cryostat are similar, providing that there are no

dimensional constraints on the system. Table 2 shows the advantages and disadvantages

of vapour shielded cryostats.

23

Advantages of liquid nitrogen

shielding

Disadvantages of liquid nitrogen

shielding

The shield forms a firm point to fix the

temperature of windows or thermal

anchors, and the temperature of the

shield is fairly constant.

The system may be warmed up quickly

by allowing gas into the vacuum space.

The small amount of superinsulation

does not become badly contaminated,

and the gas can be pumped out to an

acceptable level.

Comparatively short systems can be

made, because of the firm 77 K thermal

link in the neck of the helium vessel.

Liquid nitrogen must be filled regularly.

Boiling liquid nitrogen creates intermittent

vibration since it tends to boil in bursts. The

gas flow from the LN

2

exhaust port may be

very low for an extended period as liquid in

the cryostat stratifies. Liquid near the

bottom of the reservoir can become warmer

than the surface because of the hydrostatic

pressure of the liquid above it. When this

stratification is disturbed the evaporation

rate increases dramatically. This is sometimes

sufficient to blow liquid out of the cryostat.

Table 1 Liquid nitrogen shielded cryostats for liquid helium

Advantages of vapour shielded

cryostats.

Disadvantages of vapour shielded

cryostats.

Liquid nitrogen does not need to be re-

filled.

Vibration levels may be reduced, since

there is no vibration from the

intermittent boiling of liquid nitrogen.

Warming up the system may take longer

than it would take if the vacuum space could

be 'softened' with gas.

Very short systems may have a higher boil off

than a corresponding liquid nitrogen

shielded system.

The temperature of the shields varies with

the liquid helium level.

Table 2 Vapour shielded cryostats for liquid helium

4.1.3

Bath cryostats for liquid nitrogen

In some ways it is more difficult to make a reliable bath cryostat for liquid nitrogen than

for liquid helium. Unlike liquid helium, liquid nitrogen is not cold enough to freeze (or

cryopump) all the contaminating gases in the surrounding vacuum space onto a cold metal

surface. The quality of the vacuum is critical for operation of the cryostat, so a sorption

pump (containing charcoal or molecular sieve) is normally fitted to the outside of the

liquid nitrogen reservoir to maintain the vacuum. The vessel is usually superinsulated, but

other insulation techniques are occasionally used; for example, filling the vacuum space

with a low conductivity material such as a suitable mineral powder.

24

4.2

Lambda point refrigerators

Superconducting magnets are usually operated in liquid helium at 4.2 K. Their

performance can often be enhanced by cooling the magnet to lower temperatures as

described in section 6.3 on page 41. The simplest way to achieve temperatures below

4.2 K is to pump the whole liquid helium reservoir with a rotary pump, to reduce the

vapour pressure above the liquid. If the bath is cooled to 2.2 K in this way, about 35% of

the helium is evaporated to cool the remaining liquid. Temperatures below 2.2 K can be

achieved, but if the bath is cooled below the lambda point, the liquid helium consumption

increases significantly (both to reach the low temperature and to maintain it).

This simple approach has several disadvantages. A large amount of liquid is used to cool

the magnet down, and since the reservoir is then below atmospheric pressure, access to

the reservoir is difficult and all the fittings on the top plate have to be reliably leak tight.

The liquid helium can only be re-filled by de-energising the magnet to its 4.2 K field and

filling the reservoir to atmospheric pressure with helium gas, which interrupts the

experiment.

Lambda point refrigerators (also known as 'lambda plates' or 'pumped plates') are used

to cool superconducting magnets to about 2.2 K and maintain this temperature

continuously. See Figure 7. They consist of a needle valve (to control the flow of liquid

helium into the refrigerator) and a tube or chamber with a pumping line. They are

normally built into the 'magnet support system'. The refrigerator is in good thermal

contact with the liquid helium just above the magnet.

Liquid is continuously fed into the refrigerator and pumped to a low pressure so that it

cools. The cooling power is determined by the liquid flow rate and the size of the pump,

and it can be adjusted using the needle valve. High flow rates are typically used at high

temperatures to cool the system quickly or to obtain high cooling power, but when base

temperature is reached, the flow can be reduced to make operation as economical as

possible.

The density of liquid helium changes rapidly with temperature, so strong convection

currents are set up, around the magnet. The cold liquid from the refrigerator sinks to the

bottom of the reservoir, cooling the magnet and keeping it at about 2.2 K. Meanwhile

the warmer liquid above the refrigerator is affected very little. The thermal conductivity

of the liquid is so low that the region immediately above the plate has a steep

temperature gradient, and the liquid surface remains at 4.2 K and at atmospheric pressure.

It is important to make sure that this thermal gradient is maintained, and not short

circuited by high conductivity components.

25

Figure 7 Lambda point refrigerator

Lambda point refrigerators have several advantages. In particular:

a) Since only a small proportion of the liquid in the reservoir is cooled by the lambda

plate less liquid has to be used, and this reduces the cost of operation.

b) Operation can be automated (using a Teslatron Lambda controller).

c) The reservoir can be refilled without stopping operation of the system, as long as the

transfer tube does not stir the liquid and upset the temperature gradient above the

lambda plate.

The performance of these systems is dominated by the amount of liquid helium that has

to be cooled. Although the mass of the magnet is much larger than that of the liquid, its

heat capacity is very much lower. It is possible to calculate the amount of heat that has to

be removed if the magnet and liquid are cooled from 4.2 K to 2.2 K. In a typical system,

containing a 50 kg magnet, there may be about 3 litres (0.5 kg) of liquid below the

lambda plate. Only 5 J has to be removed from the magnet, but about 3 kJ has to be

removed from the liquid. Therefore it is important to minimise the amount of liquid

around the magnet so that it will cool quickly and cheaply.

In most systems the magnet can only be cooled to 2.2 K in this way, because liquid helium

has a phase change (the lambda point) at this temperature. Below the lambda point, the

liquid becomes 'superfluid' and has a very high thermal conductivity, so the phase

transition can only occur if the whole reservoir is cooled to the lambda point.

26

The heat from any warmer region in the reservoir would be rapidly conducted to the

colder region, keeping its temperature above the critical level. However, in a few

specialised applications, the refrigerator is built into the top of a separate chamber around

the magnet. The refrigerator is fed from a 4.2 K liquid reservoir, but thermally isolated

from it. The lambda plate then cools the whole of this chamber, and temperatures below

the lambda point can be reached and maintained continuously, while the liquid is at

atmospheric pressure. The optimum temperature is about 1.8 K, as the superfluid is then

able to carry heat away from the magnet most effectively.

4.3

Continuous flow cryostats

A wide range of continuous flow cryostats is available. Some of these are supplied with

cryogens from a storage vessel; others are mounted in a bath cryostat which supplies

liquid. In most of these systems the cooling power available from a flow of cryogen (LN

2

or LHe) is balanced by power supplied electrically to a heater near the sample (usually by a

temperature controller).

4.3.1

Variable temperature inserts (VTI)

Variable temperature inserts are used in bath cryostats to adjust the temperature of a

sample without affecting the helium reservoir. 'Dynamic' and 'static' types of VTI are

available, and the advantages and disadvantages of each type are described in section 4.4.

The inner parts of the insert are vacuum insulated from the liquid helium. There may also

be a radiation shield between the sample space and the liquid reservoir to reduce the

radiated heat load on the reservoir when the sample is at a high temperature. This shield

is usually cooled by the exhaust gas or the boil off from the main bath.

The temperature range of a VTI is typically from 1.5 to 300 K, but in certain circumstances

this range may be extended. The sample temperature can be controlled continuously at

any point in this range. Lower temperatures can often be achieved in single shot mode:

the sample space is filled with liquid and the needle valve is closed to allow the pump to

reduce the vapour pressure above the liquid to the lowest possible level.

4.3.2

Independent continuous flow cryostats (CF)

The operating principles of CF cryostats are generally the same as those of VTIs. Dynamic

and static versions are available as described in section 4.4. However, they normally have

their own independent thermal shielding, and they are supplied with coolant from an

independent storage vessel through a 'low loss' or 'gas flow shielded' (GFS) transfer tube.

These cryostats are sometimes used with a superconducting magnet if it has a room

temperature bore. They are also used with resistive magnets.

27

Figure 8 Optistat - an optical continuous flow cryostat

The transfer tubes are always vacuum insulated. In order to reduce the losses in the tube,

GFS type transfer tubes use the enthalpy in the exhaust gas from the CF cryostat to cool a

radiation shield in the tube.

28

The temperature range of CF cryostats is typically < 4 to 300 K in continuous mode, with

lower temperatures available for limited periods in 'single shot mode'. However the

range may be extended to give higher or lower temperatures if necessary. In general it is

difficult to achieve temperatures as low as those available in VTIs because of the thermal

losses in the transfer tubes, but some cryostats are designed to reach 1.6 K continuously.

Figure 8 shows one of them schematically.

4.4

Static and dynamic continuous flow systems

Although all continuous flow cryostats work on the principle of balancing the cooling

power of a flow of cryogen with electrical power from the temperature controller, there

are several distinct types of cryostat: the most important are referred to as 'dynamic' and

'static'.

4.4.1

Dynamic systems

In a dynamic continuous flow cryostat, the sample is mounted in a flowing gas or in liquid,

and its temperature is strongly influenced by the fluid. The temperature of the fluid is

controlled by passing it through a heat exchanger (usually placed at the bottom of the

sample space). The heat exchanger temperature is set by simultaneously controlling the

cryogen flow rate and the heater on the heat exchanger. A temperature controller is

usually used to do this automatically. Providing that the flow of cryogen through the heat

exchanger is not too high the temperature of the flowing fluid can be controlled quite

accurately. The fluid flows past the sample and out of the exhaust port of the insert to

the pump.

This type of insert is easy to operate and it responds very quickly if the set temperature is

changed to a new value. However, the temperature stability is not as high as that of a

static insert. It is also possible to block the small capillary that feeds the cryogen to the

heat exchanger with frozen water or air during the sample changing operation if care is

not taken.

4.4.2

Static systems

Static systems are also fitted with heat exchangers, and the temperature of the heat

exchanger is controlled in a similar way. However, the exhaust gas does not flow over the

sample, but it passes out of the cryostat to the pump through a separate pumping line.

The heat exchanger usually forms an annulus around the sample space, and thermal

contact is made to the sample through exchange gas. The exchange gas pressure can be

adjusted to suit the conditions. The sample temperature follows the temperature of the

heat exchanger, but rapid temperature fluctuations tend to be filtered out, and the

temperature stability of the sample can be improved considerably. In some cases, a heater

is fitted to the sample block for fine control of the temperature or to warm the sample

quickly.

29

Static inserts are as easy to operate as the dynamic type, and have the advantage that it is

not possible to block the heat exchanger during the sample changing process. Indeed,

quite large amounts of air may be frozen into the sample space without affecting the

operating procedure. However, the increased sample temperature stability has to be

traded off against the increased time taken to change the sample temperature to a new

value. In particular, it is not possible to cool the sample as quickly, and static systems are

generally used for small sample spaces.

Figure 9 Flow system for a continuous flow cryostat

4.5

Storage/transport dewars

Storage (or transport) dewars are generally only suitable for supplying cryogens to the

cryostat, (whether it is of the bath or continuous flow type). They are designed to be

robust and to have a low evaporation rate. They usually have very narrow necks and a

large amount of superinsulation. A few liquid helium storage dewars are fitted with

liquid nitrogen jackets (especially older dewars).

However, some small variable temperature inserts are available to fit into storage dewars,

providing that the diameter of the neck is sufficiently large, (50 mm). In particular, Oxford

Instruments can supply a variable temperature inserts (the Compact VTI), a

3

He refrigerator

(Heliox 2VL) or a

3

He/

4

He dilution refrigerator insert (Kelvinox15) to fit into a storage

dewar. These inserts give temperature ranges from 0.03 to 300 K.

30

4.6

Closed cycle coolers

Modern closed cycle coolers offer a highly reliable method of achieving low temperatures.

They may either be used alone, to cool a sample and a radiation shield, or with a bath

cryostat to cool one or two radiation shields and thus reduce the evaporation rate of the

cryostat. This can considerably extend the hold time of a low loss cryostat, but it is not

usually appropriate if the equipment inside the cryostat has a high consumption rate

which has a dominant effect on the hold time. It is now possible to build cryogen free

systems containing superconducting magnets.

However, this type of cooler has a high initial cost and the pay back time (in terms of

reduced cryogen costs) may be very long. They also need to be serviced regularly (typically

every 5,000 hours). There is also the possibility of introducing unwanted vibration into the

experiment if it is not mounted very carefully.

4.7

'Stinger' systems

Some closed cycle cooler systems are used to re-condense helium gas into a bath cryostat

continuously. They take the form of a cold finger that fits into the helium reservoir. They

need quite high cooling powers both at the 4.2 K stage and at higher temperatures

because they have to provide enough cooling to replace the enthalpy of the boil off gas,

which usually helps to cool the neck of the reservoir. The helium reservoir is normally

pressurised slightly so that the gas recondenses effectively, and so the liquid helium is held

at a temperature close to 4.5 K.

4.8

Peltier effect coolers

Peltier effect coolers work by the thermoelectric effect; they are a thermodynamically

reversible low impedance devices, operating at a high current from a d.c. power supply. A

single stage cooler can typically achieve a temperature of -40°C, and lower temperatures

can be achieved using several stages. A six stage device may achieve -100°C and give a

cooling power of around 1 mW at -80°C. They do not introduce vibration into the

cryostat. Although they have a small temperature range and limited cooling power, they

offer a cheap solution for some requirements, (for example, Peltier effect cooled baffles,

see section 2.1.3).

4.9

Making indium seals

Oxford Instruments uses two main types of indium seal, as illustrated in Figure 21 on page

80. They both use 1mm diameter wire, retained

•

Either in a groove by a flat surface

•

Or in a corner between two flanges

In both cases, the indium wire is overlapped by bending one end of the wire sharply

outwards and laying the other end across the corner of the bend. The wire is so soft that

the joint will be compressed into a cold weld.

31

4.9.1

Preparations

Before you make the seal ensure that the groove and the mating surfaces are clean.

Thoroughly remove any old indium wire from the seal faces. If necessary a solvent can be

used for cleaning. Some people like to grease the metal surfaces with silicone vacuum

grease to make it easier to remove the wire later, but this is not necessary.

4.9.2

Making the seal

Lay a new piece of indium wire in the groove or round the male spigot on one of the

flanges and overlap it as shown on the diagram. There are usually alignment marks on

the flanges to indicate the correct orientation. Carefully bring the two flanges together

and hold them loosely in place with two bolts while you put the other bolts into the

flanges and tighten them by finger only. Slowly and evenly tighten all of the bolts with a

small spanner (wrench) or Allen key. Do not tighten them too much. There is no need to

use an extension on the tool to give extra leverage. On large seals (typically > 50mm

diameter) it is then best to leave them for about an hour. The indium flows slightly

during this period so it is often possible to tighten the bolts slightly more.

4.9.3

Separating indium seal flanges

It is often difficult to separate indium seal flanges because the indium metal seems to glue

them together. Most large indium seals made by Oxford Instruments have two or more

threaded holes in one of the flanges for 'jacking screws'.

Remove the bolts that hold the indium seal together (leaving two of the bolts loosely in

place so that the flanges do not fall apart when they separate). Use another two of these

bolts to jack the flanges apart by screwing them evenly into the jacking screw holes from

the same side of the flange. This will push the flanges apart.

If there are no jacking screw holes (as often happens on small diameter indium seals), the

flanges can be separated by inserting a sharp blade between the flanges. Make sure that

the blade does not slip and cut you as the flanges separate.

32

5

Ultra low temperatures

Refrigerators working at temperatures below 1 K are used for a surprisingly diverse range

of applications in research establishments. A range of specialised techniques is used to

achieve these temperatures. Most of the systems described in the previous chapters use

liquid helium and liquid nitrogen to reach and maintain low temperatures, but it is

difficult to achieve temperatures significantly below 1 K using these cryogens alone.

However, most ultra-low temperature systems are immersed in liquid helium (

4

He) at 4.2 K,

so that the heat load from the surroundings is minimised.

It is possible to reach temperatures slightly below 1 K by pumping liquid

4

He to a low

pressure but very large pumps are required and it is not usually economically viable.

4

He

may also be used to give very low cooling powers at temperatures down to 0.7 K in 'vortex

refrigerators' which rely on the special properties of superfluid

4

He.

However, the valuable lighter isotope of helium,

3

He, is usually used in refrigerators

working below 1 K. Evaporating

3

He is used in some systems, and temperatures slightly

below 0.3 K can be achieved by reducing its vapour pressure. Temperatures below 0.3 K

are usually reached by continuously diluting a flow of

3

He in liquid

4

He using a

3

He/

4

He

dilution refrigerator.

5.1

3

He Refrigerators

3

He refrigerators are usually designed for routine operation in the temperature range

from 0.3 to 1.2 K, and they use evaporating

3

He as the refrigerant. Their operating range

can often be extended to 100 K or higher. Some of these systems can run continuously,

returning the liquid

3

He to the system to replace the evaporated liquid. Others work in

'single shot' mode, by pumping on a small charge of liquid

3

He condensed into the system.

In an efficient cryostat a 20 cm

3

charge of liquid

3

He may last for longer than 50 hours.

Small laboratory refrigerators may give a cooling power of a few milli-watts at 0.5 K, but

very large and high powered machines can give cooling powers of several watts at this

temperature.

5.1.1

Sorption pumped

3

He systems

Sorption pumped

3

He systems are usually single shot refrigerators, capable of high

performance operation for a limited time. Several types of system are available to suit the

majority of laboratory requirements. Most of them can be used with high field

superconducting magnets if required. The top loading systems allow the sample to be

mounted on a probe which is loaded directly into liquid

3

He. They may also be designed

to operate in rapidly sweeping magnetic fields, and a wide range of special services may

be fitted to make connections to the sample. The maximum temperature limit is typically

100 K.

33

The Heliox 2VL insert is a low cost miniature

3

He system designed to allow inexperienced

users to cool samples to 0.3 K. It is designed for operation in a liquid helium storage

dewar, or with a superconducting magnet system. The sample is mounted in vacuum, and

wiring can be connected easily. The whole insert is removed from the cryostat to change

the sample, but since it is small, the time scale for sample changing is similar to that on the

top loading systems. The Heliox system can be run up to about 200 K if it is used with a

superconducting magnet, but higher temperatures (up to 300 K) can be reached if the

insert is pulled up into the neck of the cryostat.

Figure 10 Principle of operation of a typical sorption pumped

3

He system

(top loading type)

Figure 10 shows the working parts of a typical system. Although a top loading insert is

shown, the principle of operation is similar for all Oxford Instruments' sorption pumped

inserts. The insert has an inner vacuum chamber, (IVC), to provide thermal isolation from

the main liquid helium bath.

The sorption pump, (or sorb), will absorb gas when cooled below 40 K, and the amount of

gas that can be absorbed depends on its temperature. It is cooled by drawing some liquid

helium from the main bath through a heat exchanger. The flow of

4

He through the heat

exchanger is promoted by a small diaphragm pump and the rate of flow is controlled by a

valve in the pumping line. A heater is fitted to the sorb so that its temperature can be

controlled.

The 1 K pot is used to condense the

3

He gas and then to reduce the amount of heat

conducted to the sample space. It is fed from the main liquid helium bath through a

needle valve, and it can be filled continuously.

34

During condensation, the sorb is warmed above 40 K. When it is at this temperature it will

not absorb any

3

He (see Figure 10).

 The

3

3

the

3

3

3

3

3

3

3

3

3

3

3

3

3

3

3

3

3

3

3

35

5.2

3

He/

4

3

He

4

3

3

3

3

He/

4

3

3

4

He

3

4

3

36

37

3

He/

4

3

3

3

3

3

3

4

3

He

3

3

3

3

-3

3

38

5.3

3

He/

4

3

3

He/

4

5.4

5

39

6

6.1

3

3

C

3

40

6.2

-8

-14

41

6.3

LI

=

1

2

2

L

dI

dt

'

L

R

=

42

6.4

3

5

7

2