Page 428 - Advanced Mine Ventilation
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Gas and Dust Explosions                                           397

           smaller loading of the dust. In heavy loading, the total weight on a plank is about
           8e9 lbs per square feet of the airway cross section. The lightly loaded barriers may
           contain only half as much. The typical length of the barriers is 100e200 ft. The volu-
                                                                        3
           metric stone dust concentration to quench a gas/dust explosion is 7e12 kg/m . This is
           150e200 times the lower explosion concentration limit for coal dust. A typical set of
           stone dust barriers may have a total stone dust load of 5e7 tons.
              The fineness of the dust is the same as that of the rock dust used to inert the coal
           dust. In the United States, 100% of the dust must be smaller than 850 microns, 70%
           finer than 75 microns with less than 5% combustibles and less than 4% silica. Most
           rock dusts tested by the author were finer than 37 microns (400 mesh) and had no silica
           in it. Finer the dust, the better is its ability to disperse in air and higher its residence
           time in air. Some chemicals, such as stearic acid, are mixed with dust to prevent
           caking.
              Stone dust barriers appear to work better in test galleries but do not do as well in
           actual mines. It would be, therefore, prudent to (1) degas the coal seam, (2) use
           only permissible equipment in the working face, and (3) inert the coal dust with
           noncombustible dust. US coal mine regulations do not require stone dust barriers.

           Problems


           The following gas analysis was received after a mine fire. Calculate the composition
           point and determine if the atmosphere is explosive.


                          Gas          Concentration (by Volume)
                          CO           2.5
                          CO 2         0.2
                          CH 4         2.3
                          H 2          2.0
                          O 2          10
                          N 2          (100 for all other gases)





           References

            [1] Byrer C, et al. Coalbed methane: a miner’s curse and a valuable resource. In: Thakur P,
               et al., editors. Coalbed methane from prospect to pipeline. Elsevier Publishing; 2014.
               p. 1e6.
            [2] Bodurtha FT. Industrial explosions prevention and protection. McGraw-Hill Book Com-
               pany; 1980. p. 157.
            [3] Coward HF, Jones GW. Limits of flammability of gases and vapors. USBM Bulletin #503.
               1952.
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