Low Temperature Methods (1K-300K) By Charulata Y. Barge, Graduate student, Prof. Zumbühl Group Department of Physics Date:- 3-11-2006 Outline Cryogenics Liquid Gases Liquid Helium Helium-4 refrigeration techniques Cryogenics Processes at low temperatures, defined arbitrarily as below 150 K. liquefaction and solidification of ambient gases loss of ductility and embrittlement of some structural materials such as carbon steel increase in the thermal conductivity to a maximum value decrease in the heat capacity of solids decrease in thermal noise and disorder of matter appearance of quantum effects such as superconductivity and superfluidity LT environments are maintained with cryogens (liquefied gases) or with cryogenic refrigerators. The temperature afforded by a cryogen ranges from its triple point to slightly below its critical point Commonly used cryogens are liquid helium-4 (down to 1 K), liquid hydrogen, and liquid nitrogen Less commonly used because of their expense are liquid helium-3 (down to 0.3 K) and neon Down to about 1.5 K, refrigeration cycles involve compression and expansion of appropriately chosen gases Latent heat of vaporization and the sensible heat of the gas (heat content of the gas) is removed to liquefy a gas Liquid Gases Cyogenic liquids Liquefied gases that are kept in their liquid state at very low temperatures Liquid gases are extremely cold have boiling points below -150°C(- 238°F) In gaseous state at normal temperatures and pressures. Gases cooled below room temperature, an increase in pressure can liquefy them Different cryogens become liquids under different conditions of temperature and pressure All have two properties in common • • they are extremely cold small amounts of liquid can expand into very large volumes of gas. Different types of cryogenic liquids Each cryogenic liquid has its own specific properties Inert Gases: Do not react chemically Do not burn or support combustion. Examples:- nitrogen, helium, neon, argon and krypton Flammable Gases: can burn in air. Examples:- hydrogen, methane and liquefied natural gas Oxygen: Materials considered as non-combustible can burn in the presence of liquid oxygen. Organic materials can react explosively with liquid oxygen. How are cryogenic liquids contained? used in thermally insulated containers cryogenic liquid containers are specifically designed to withstand rapid temperature changes and extreme differences in temperature Liquid Dewar Flasks Laboratory Liquid Dewar Flasks non-pressurized, vacuum-jacketed vessels low- boiling liquids have an outer vessel of liquid nitrogen for insulation. wide-mouthed openings and do not have lids or covers. primarily used in laboratories for temporary storage. Liquid Cylinders pressurized containers specifically designed for cryogenic liquids. valves for filling and dispensing the cryogenic liquid, pressure-control valve with a bursting disk as backup protection. There are three major types of liquid cylinders which are designed for dispensing: a) liquid or gas b) only gas c) only liquid Liquid Nitrogen(N2) inert, colorless, odorless, non-corrosive, nonflammable, and extremely cold. Makes up the major portion of the atmosphere (78.03% by volume, 75.5% by weight). Does not support combustion; however, it is not life supporting. Inert except when heated to very high temperatures where it combines with some of the more active metals, Health Effects nontoxic and inert, Inhalation of nitrogen in excessive amounts can cause dizziness, nausea, vomiting, loss of consciousness, and death. Atomic Number:7 Atomic Mass Average:- 14.00674 Boiling Point: 77.5K -195.65°C -320.17°F Density: 1.2506g/L @ 273K & 1atm Heat of vaporization: 2.7928kJ/mol Melting point: 63.29K -209.86°C -345.75°F Molar Volume: 17.3 cm3/mole Optical Refractive Index: 1.000298 (gas) 1.197 (liquid) Physical State (at 20°C & 1atm): Gas Specific Heat: 1.04J/gK Handling and Storage Store and use :- with adequate ventilation Do not store in a confined space Do not plug, remove, or tamper with any pressure relief device Never allow any unprotected part of the body to come in contact with uninsulated pipes or equipment that contains cryogenic product The extremely cold metal will cause the flesh to stick fast and tear when one attempts to withdraw from it. Use a suitable hand truck for container movement Containers should be handled and stored in an upright position Use piping and equipment designed to withstand the pressures to be encountered On gas withdrawal systems, use a check valve or other protective apparatus in any line or piping from the container to prevent reverse flow Liquid Helium(He) inert, colorless, odorless, non-corrosive, extremely cold, and nonflammable non react with other elements or compounds under ordinary conditions non-corrosive Health Effects Being odorless, colorless, tasteless, and nonirritating, helium has no warning properties Humans possess no senses that can detect the presence of helium a simple asphyxiant by displacing the oxygen in air to levels below that required to support life Inhalation of helium in excessive amounts can cause dizziness, nausea, vomiting, loss of consciousness and death Atomic Number: 2 Boiling point: 4.365KK Density:- 0.1785g/L @ 273K & 1 atm Enthalpy of Vaporization: 0.083 kJ/mole Heat of vaporization: 0.0845kJ/mol Melting point: 1.1K -272.05°C -458°F Molar Volume: 31.8 cm3/mole Optical Refractive Index: 1.000035 (gas) 1.028 (liquid) Specific heat: 5.193J/gK Handling and storage Equipment:- liquid containers, vacuum jacketed transfer lines, process equipment, and accessories needed to safely handle and use the product. never tip, slide or roll liquid containers on their side. Liquid helium container valves should never be left open to atmosphere for extended periods. Keep the fill/withdrawal vent outlets closed to prevent contamination. Check the system regularly for frost accumulation. Provide a safety relief valve on any part of the system where liquid can be trapped between closed valves in lines or vessels. Transfer liquid from containers by using the product vapor pressure or external gaseous product pressure. Provide protection for liquid helium containers against extremes of weather, where outside storage areas are used. carbon steel must be avoided in cryogenic service. Liquid Helium He is the only element that remains liquid at T=0. The reasons (a) large zero-point oscillations of light atoms, and (b) the binding forces between the atoms are very weak. Small atomic mass, large zero point energy The zero-point energy larger than the latent heat of evaporation the zero-point vibration amplitude is ~1/3 of the mean separation of atoms in the liquid state No static dipole moment:- closed electronic s shell for any processes that bring a system at T = 0 from one equilibrium state to another, ΔS = 0 Liquid Helium (He) Two Isotopes Helium 4 :- Common isotope boils at a substantially lower temperature, 4.2 K below 2.172 K the liquid exhibits the extraordinary properties of superfluidity Helium 3 :- rare isotope normal boiling point of 3.2 K superfluid transition at a very much lower temperature near 0.001 K Both forms of helium remain in a liquid state at absolute zero. Some Properties of Liquid Helium Properties of Liquid Helium Helium-4 Helium 3 Critical Temperature 5.2 K 3.3 K Boiling Point at 1 atm 4.2 K 3.2 K Minimum melting pressure 25 atm 29 atm at 0.3 K Superfluid transition temperature at saturated vapor pressure 2.17 K 1 mK in zero magnetic field Type Boson Fermion Outline Cryogenics Liquid Gases Helium-4 refrigeration techniques Helium-4 the most abundant of the two naturally-occurring isotopes of helium A boson The appearance in superfluid state is related to the Bose- Einstein Condensation Phase diagrame of Helium 4 The critical point Tc = 5.20 K Pc = 2.264 atm Typical phase diagram Helium I and Helium II states Helium I : Normal colourless liquid state a very low viscosity and density Normal fluid characteristics Helium II: high thermal conductivity Absense of bubbling heat input causes evaporation Superfluid:- No measurable viscocity liquid helium below the lambda point is viewed as containing a proportion of helium atoms in a ground state, which are superfluid and flow with exactly zero viscosity, and a proportion of helium atoms in an excited state, which behave more like an ordinary fluid Creeping Effect When a surface extends past the level of helium II, the helium II moves along the surface, seemingly against the force of gravity will escape from a vessel that is not sealed by creeping along the sides until it reaches a warmer region where it evaporates moves in a 30 nm thick film Rollin film regardless of surface material. leaks rapidly through tiny openings Helium 4 Cryostats small latent heat i.e. Boils off easily LHe cryostats has to be thermaly decoupled Separating He vessel from outer world by a vacuum container is made up from material with poor thermal conductivity environment is shilded by surrounding LHe vessel with LN Wraping the dewar in ‚super insulating‘ foil Cryostats are equipped with superconducting magnet Magnets are cooled below Tc by LHe Nb alloys :- very large critical magnetic fields Helium 4 bath cryostat Sample is immersed in LHe Sample cooled by pumping away He vapor LHe evaporates,cools liquid Pumping speed and incoming heat flux determines the lowest possible temperature Helium 4 Gas flow cryostat The sample sits in flow of cold helium gas LHe enters via needle valve additional vacuum chamber to thermaly decouple Sample chamber Contunous variation of temperature between 1.2K and room temperature Working mechanism Claussius Clapeyron equation ⎛ dP⎞ Sgas−Sliq L = ⎜ ⎟ = ⎝dT⎠vap Vgas−Vliq TΔV For the liquid-gas phase transition, we can make the following reasonable assumptions: the molar volume of the liquid is much smaller than the molar volume of the gas the molar volume of gas is given by the ideal gas law V = RT/P the latent heat is almost T-independent L LP ⎛ dP ⎞ = ⎜ ⎟ ≈ 2 ⎝ dT ⎠ vap TVgas RT dP L dT = P R T2 ⎛ L ⎞ Pvap ∝ exp⎜ − ⎟ RT ⎝ ⎠ Working mechanism Cooling power (P):- latent heat taken from from liquid per evaporated atom x no. of atoms evaporated per time P= (dn/dt)*L dn/dt determined by pumping speed (dV/dt) dn/dt =1/mHe (dM/dt) = 1/mHe *ρ (dV/dt) =P(T)/kBT (dV/dt) Cooling power drops exponentially as T decreases Steady state:- P=heat load of LHe With 10m3/h, T reached 1.2K For lower temperature, powerful pumps or Helium 3 Thank you for your attention
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