Page 220 - Fundamentals of Magnetic Thermonuclear Reactor Design
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202     Fundamentals of Magnetic Thermonuclear Reactor Design



              TABLE 6.5 Average Characteristics of Surface-Action Pumps
                                            Pumping
                                 Operating   specific    Max sorption  Max heat
                         Gas     temperature  speed   capacity    load
                                                             2
                                                                      2
                                                        3
                                              3
                                                   2
              Pump type  removed  (K)       (m /(s·m )) (m ·Pa/m )  (W/m )
              Condensate  D–T    2–4        70–100    4 × 10 4    10 3
              Cryosorption  D–T  15–30      70–100    4 × 10 4    10 4
              (microporous
              adsorbents)
              Cryosorption  D–T  10–30      40–70     4 × 10 4    10 4
              (condensed
              gases)
              Sorption    D–T    300–700    5–100     (7–13) × 10 3  –
              (non-
              dispersible
              getters)
              Cryosorption  He   4          15–40     5000        10 3
              (microporous       20         1.0–1.5   4–6         10 4
              adsorbents)





               Hydrogen cryosorption pumping can be performed at 10–30 K using micro-
            porous adsorbents, such as coals and zeolites, or gas condensate  layers as
            cryosorbents.
               Cryosorption pumps outperform condensate pumps in terms of resistivity to
            heat flows and sensitivity to temperature changes, but have weaknesses, such as
            structural and operating complexity and a less stable performance when dealing
            with large flows.
               Non-dispersible metal getters prove effective for removing hydrogen. Their
            key strength is the relatively high operating temperature. They may be placed
            close to potentially high-temperature components of the vacuum pumping duct.
            The getters are a little sensitive to radiant energy and particle flows [16].
               He condensation is undesirable due to the high energy consumption. The
            only way to remove it is through cryosorption pumping. For example, a cryo-
                                                                      2
                                                                 3
            sorption pump using charcoal removes He at a rate of up to 40 m /(s·m ), and
                                               2
                                       4
                                          3
            has a sorption capacity of up to 10  m  Pa/m . The sorbent regeneration requires
            a heating at 35 K. A cryosorption pumping of a D–T–He mixture (zeolite; 4 K)
                                                  −3
            is only possible at pressures lower than 7 × 10  Pa. At a higher pressure, the
            cryopanel system gets blocked by H isotopes, and He removal stops. It is there-
            fore necessary to use separate He absorbing panels in reactor-scale cryopumps
            to absorb He and H isotopes. A stable He pumping is possible at up to 0.1 Pa;
                                                                3
            whereas a He flow removed from a fusion reactor is close to 1 m  Pa/s.
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