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 Encyclopedia of Physical Science and Technology  EN004D-156  June 8, 2001  15:28







              Cryogenic Process Engineering                                                                31

              TABLE III Characteristics of Selected Insulation  evacuated space as the pressure is reduced, free molec-
                                                                ular conduction is encountered. The gaseous heat conduc-
                                      Apparent thermal
                                        conductivity            tion under free molecular conditions for most cryogenic
                                       (k a , J/sec · m · K)  Bulk  applications is given by:
                                       (between 77 and  density
                                                          3
                  Type of insulation      300 K)      (k/gm )          Q gc  γ + 1     R    1/2
                                                                          =                  αp(T 2 − T 1 )  (8)
              Pure gas at 0.1 MPa, 180 K                               A 1   γ − 1 8π MT
               H 2                      34.07 × 10 −2  0.080    where α, the overall accommodation coefficient, is defined
               N 2                       5.67 × 10 −2  1.21     by:
              Pure vacuum, 0.13 mPa or less  1.70 × 10 −2  Nil
                                                                                       α 1 α 2
              Straight insulation                                          α =                             (9)
               Polystyrene foam          8.52 × 10 −2  32–48                   α 2 + α 1 (1 − α 2 )(A 1 /A 2 )
               Polyurethane foam        10.79 × 10 −2  80–128   and γ is the ratio of the heat capacities, R the molar gas
               Glass foam               11.36 × 10 −2  144      constant, M the molecular weight of the gas, and T the
              Evacuated powder                                  temperature of the gas at the point where the pressure p is
               Perlite (133 mPa)      0.34–0.68 × 10 −2  144–64
                                                                measured. The subscripted A 1 and A 2 , T 1 and T 2 , and α 1
               Silica (133 mPa)       0.57–0.68 × 10 −2  64–96  and α 2 are the areas, temperatures, and accommodation
              Combination insulation                            coefficients of the cold and warm surfaces, respectively.
               Aluminum foil and fiberglass                      The accommodation coefficient depends on the specific
                 (12–28 layers/cm, 1.33 mPa)  1.14–2.27 × 10 −4  64–112  gas–surface combination and the surface temperature.
                 (30–60 layers/cm, 1.33 mPa)  0.57 × 10 −4  120   Heat transport across an evacuated space by radiation
               Aluminum foil and nylon net                      can be reduced significantly by inserting one or more
                 (32 layers/cm, 1.33 mPa)  5.68 × 10 −4  89     low-emissivityfloatingshieldswithintheevacuatedspace.
                                                                Such shields provide a reduction in the emissivity factor.
                                                                The only limitation on the number of floating shields used
              general categories are by no means distinct. However, the
                                                                is one of complexity and cost.
              classification scheme does offer a framework by which the
              widely varying types of insulation can be discussed.
                Since heat transfer through these insulations can oc-  2. Multilayer Insulation
              cur by several different mechanisms, the apparent ther-
                                                                Multilayer insulation provides the most effective thermal
              mal conductivity k a of an insulation that incorporates all
                                                                protection available for cryogenic storage and transfer
              of these heat-transfer possibilities offers the best means
                                                                systems. It consists of alternating layers of highly reflect-
              of comparing these difference types. Table III provides a
                                                                ing material, such as aluminum foil or aluminized Mylar,
              listing of some accepted k a values for popular insulations
                                                                and a low-conductivity spacer material or insulator, such
              used in cryogenic storage and transfer systems.
                                                                as fiberglass mat or paper, glass fabric, or nylon net, all un-
                                                                der high vacuum. When properly applied at the optimum
                1. Vacuum Insulation
                                                                density, this type of insulation can have an apparent ther-
              The mechanism of heat transfer prevailing across an evac-  mal conductivity as low as 10 to 50 µW/m · K between 20
              uated space (0.13 mPa or less) is by radiation and conduc-  and 300 K. The very low thermal conductivity of multi-
              tion through the residual gas. Radiation is generally the  layer insulations can be attributed to the fact that all modes
              more predominant mechanism and can be approximated  of heat transfer are reduced to a bare minimum.
              by:                                                 Theapparentthermalconductivityofahighlyevacuated
                                                                (pressures on the order of 0.13 mPa or less) multilayer
                                                    −1



                   Q r       4   4   1  A 1  1                  insulation can be determined from:
                      = σ T − T 1     +        − 1       (7)
                           2
                   A l             ε 1  A 2 ε 2                            	        3
                                                                                              2
                                                                        1        σeT 2     T 1      T 1
              where Q r /A 1 is the radiant heat flux, σ the Stefan–  k a =  N/	x  h s +  2 − e  1 +  T 2  1 +  T 2  (10)
              Boltzmann constant, and ε the emissivity of the surface.
              The subscripts 1 and 2 refer to the cold and warm surfaces,  where N/	x is the number of complete layers (reflect-
              respectively. The bracketed term on the right is generally  ing shield plus spacer) of insulation per unit thickness,
              referred to as the emissivity factor.             h s the solid conductance for the spacer material, σ the
                When the mean free path of gas molecules becomes  Stefan–Boltzmann constant. e the effective emissivity of
              large relative to the distance between the walls of the  the reflecting shield, and T 2 and T 1 the temperatures of
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