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07_Chap_Wang.qxd  05/05/2004  4:19 pm  Page 334
                    334                                                    Lawrence K. Wang et al.

                    2.4. Steam Requirements
                       Steam requirements for steam-assisted flare operation depend on the composition of
                    the flare gas and the flare tip design. Typical design values range from 0.15 to 0.50 lb
                    steam/lb flare gas. In this handbook, the amount of steam required for 98% destruction
                    efficiency is assumed as 0.4 lb steam/lb flare gas. The following equation is used to
                    determine steam requirements (5):
                                              Q = 1.03 × l0 −3  × Q  × MW                      (4)
                                               s              flg     flg
                    where Q is the steam requirement (lb/min), MW  is the molecular weight of the flare
                            s                                   flg
                    gas (lb/lb-mole)
                                           MW   = [(Q )(16.7) + (Q )(MW )]/Q                   (5)
                                              flg    f         e     e   flg
                       MW is the molecular weight of the emission stream (lb/lb-mole).
                           e
                    3. ENGINEERING DESIGN
                    3.1. Design of the Flame Angle
                       The flare tip diameter, D , should be rounded up to the next largest commercially
                                             tip
                    available size (14–16). The minimum diameter is 1 in. with larger diameters available
                    in 2-in. increments between 2 and 24 in., and 6-in. increments between 24 and 60 in.
                       The flame angle, θ, is calculated using
                                                   −1
                                                                      1/2
                                             θ = tan [1.47V /(550(∆P/55) ]                    (6a)
                                                          w
                    where θ is the flame angle (deg), V is the wind velocity (assumed to equal 60 mph),
                                                    w
                                                                     2
                    and ∆P is the pressure drop (in. H O) = 55 (U /550) , where U  is obtained from
                                                    2          flg             flg
                    Section 2.3. This reduces to
                                                  θ = tan −1  (88.2/U )                       (6b)
                                                                flg
                    3.2. Design of Flare Height
                       The flare height is calculated using
                                                                   −3
                                 H = (0.012185)(Q  × h ) 1/2  − (6.05 × 10 )(D )(U )(cos θ)    (7)
                                                flg  flg                tip  flg
                    where H is the flare height (ft), Q  is the flare gas flow rate (scfm), h  is the flare gas
                                                  flg                             flg
                    heat content (Btu/scf), D  is the flare tip diameter (in.), and U  is the exit velocity of
                                          tip                               flg
                    flare gas (ft/s).
                    3.3. Power Requirements of a Fan
                       The electricity cost results mainly from a fan needed to move the gas through the
                    flare. Equation (8) can be used to estimate the power requirements for a fan. This
                    equation assumes a fan-motor efficiency of 65% and a fluid specific gravity of 1.0:

                                             F = 1.81 × 10 −4  (Q  )(P)(HRS)                   (8)
                                              p              flg,a
                    where F is the power requirement for the fan (kWh/h), Q  is the actual flare gas flow
                           p                                          flg,a
                    rate (scfm), P is the system pressure drop (in. H O [typically 16 in. of H O]), and HRS
                                                              2                     2
                    is the annual operating hours (h/yr).
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