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INDUSTRY, LABOR A HUMAN RELATIONS 43 <br /> Ind g <br /> The foregoing formula is Eased on Q=21,000 A 0.82 where <br /> Q=the amount of heat transferred. <br /> (f) [2-2.5.6] The total emergency relief venting capacity for any <br /> specific stable liquid can be determined by the following formula: <br /> Cubic feet of free air per hour= V = 1,337 <br /> V=cubic feet of free air per hour from Table 8.19-8. <br /> L = latent heat ul vaporization ,:f specific liquid in Btu per lb. <br /> M= molecular«e , ht of specific liquids. <br /> (g) [2-2.5.7.] For t.:nks containing stable liquids,the required air-flow <br /> rate of par. (d) or (f, may be mule, lied by the appropriate factor listed <br /> in the following schecule when protection is provided as indicated.Only <br /> one factor can be used for any one tank: <br /> .5 For drainage in accordance with sub. (4) (b) for tanks over <br /> 200 square feet of wetted area;or <br /> .3 For water spray in accordance with standards approved by <br /> the department, and drainage in accordance with sub. (4) <br /> (b);or <br /> .3 For insulation in accordance with subd. 1.;or <br /> .15 For water spray with insulation in accordance with subd. 1. <br /> and drainage in accordance with sub. (4) (b). <br /> 1.Insulation systems for which credit is taken shall meet the following <br /> performance criteria: <br /> a. Remain in place under fire exposure conditions, <br /> b. Withstand dislodgment when subjected to hose stream impinge- <br /> ment during fire exposure except that this requirement may be waived <br /> where use of solid hose streams is not contemplated or would not be <br /> practical,and <br /> c. Maintain a maximum conductance value of 4.0 Btu's per hour per <br /> square foot per degree F. (Btu/hr/sq ft/°F.) when the outer insulation <br /> jacket or cover is at a temperature of 1,660°F.and when the mean tem- <br /> perature of the insulation is 1,000°F. <br /> (h) [2-2.5.8] The outlet of all vents and vent drains on tanks <br /> equipped with emergency venting to permit pressures exceeding 2.5 psig <br /> shall be arranged to discharge in such a way as to prevent localized over- <br /> heating of or flame impingement on any part of the tank, in the event <br /> vapors from such vents are ignited. <br /> (i) [2-2.5.9] Each co tank venting device shall have stamped <br /> on it the opening pressure,the pressure at which the valve reaches the <br /> full open position and the flow capacity at the latter pressure.If the start <br /> to open pressure is less than 2.5 psig and the pressure at full open posi- <br /> tion is greater than 2.5 psig, the flow capacity at 2.5 psig shall also be <br /> stamped on the venting device.The flow capacity shall be expressed in <br /> cubic feet per hour of air at 60° F. and 14.7 psia. <br /> Register,March,1962,No.315 <br />