Page 56 - 2022年第53卷第11期
P. 56

联立求解式(1)(29)得
                                           +                                h (T - T),i = 1 ,2,3
                         s,i  w  E,i  E,i             c,i         s,i  a         s,i  g
                                                            h )(T - T) - φ g,i ba
                       (T - T)k ?h = φ cs,i φ a,i φ ab0 - (h + φ a,i ba
                      +   = 1,整理得渡槽外壁温度
              因为 φ a,i φ g,i
                                               +
                                  1         φ cs,i φ a,i φ ab0 + Tk ?h + (h + φ a,i ba  a  h T
                                                               E,i
                                                                    c,i
                                                         w E,i
                                                                          h )T+ φ g,i ba g
                     T =                                                                ,i = 1 ,2,3 (30)
                      s,i
                          (k ?h )(h + h )                h ?k + 1?(h + h )
                            E,i  E,i  c,i  ba             E,i  E,i   c,i  ba
              上式适用于渡槽架于各种地表上,包括土石地面、水面、冰面和雪面等。
                  当渡槽架于土石地面上,包括地面积冰和积雪时,为使问题简化,一般假设地表温度接近于气
              温  [17] ,即 T≈T,这时
                             a
                         g
                                 +      )(h ?k )?(h + h ) + T?(h + h ) + (h ?k )T
                            ( φ cs,i φ a,i φ ab0  E,i  E,i  c,i  ba  w  c,i  ba  E,i  E,i  a
                        T =                                                          ,i = 1,2,3       (31a)
                         s,i
                                                h ?k + 1? (h + h )
                                                    E,i
                                                 E,i
                                                                ba
                                                            c,i
              式中
                                                      { 7.57 + 3.83V, i = 1 ,2
                                                                 a
                                              h + h =                                                (31b)
                                               c,i  ba  6 .07 + 3.83V, i = 3
                                                                 a
              2.5 渡槽外壁的净热通量与气温和水温的关系 把式(31)代入式(1)得渡槽外壁净热通量
                         k
                                                                                        w)
                                                E,i
                                                      c,i
                                            E,i
                                                                   c,i
                                                               w
                                                                       ba
                                                                                 E,i
                                                                             E,i
                                                          ba
                          E,i ( φ cs,i φ a,i φ ab0
                       = h (     +       )(h ?k )?(h + h ) + T?(h + h ) + (h ?k )T   a - T ,i = 1,2,3
                   φ wa,i  E,i                  h ?k + 1?(h + h )
                                                                ba
                                                 E,i
                                                     E,i
                                                            c,i
              整理得
                                              +      )?(h + h ) + h (T- T),i = 1 ,2,3                  (32)
                                 φ wa,i = h ( φ cs,i φ a,i φ ab0  c,i  ba  wa,i  a  w
                                       wa,i
                                               h = 1? [h ?k + 1? (h + h )]                             (33)
                                                wa,i    E,i  E,i   c,i  ba
                                                   2
              式中 h 为渡槽外壁热交换系数,W?(m·℃)。
                    wa,i
                  当渡槽边墙和底板沿流动方向是均值平板时,则渡槽外壁的等效净热通量
                                          1
                                         = ( χ     + χ    + χ           + h (T- T)
                                     φ wae    1 φ wa,1  2 φ wa,2  3 φ wa,3 ) = φ wae0  wae  a  w       (34)
                                           χ
                                       1  3                                    1  3
                                     =  ∑            +      )?(h + h ),h =         χ h                 (35)
                                                                          wae ∑
                                 φ wae0     χ h ( φ cs,i φ a,i φ ab0  c,i  ba       i wa,i
                                       χ                                       χ
                                            i wa,i
                                         i =1                                   i =1
                                                                                                 2
                                                       2
                        为渡槽外壁的等效净热通量,W?m ;h 为渡槽外壁的等效热交换系数,W?(m·℃); χ =
              式中:φ wae                                     wae
              χ + χ + χ 为渡槽湿周,m; χ 和 χ 分别为两边墙的湿周,m; χ 为底板的湿周,m。
               1  2  3                  1   2                          3
              3 渡槽水温的时空变化规律
                  随着渡槽水体与周围环境的热交换,包括水面与大气的热交换与水体与渡槽边墙和底板的热交
              换,热量通过水流的运动和紊动向下游和整个过水断面传递,在一维条件下,沿流向的对流 - 热扩散
              方程是
                                                                    T w
                                     ( ρ CAT) + ( ρ CAVT) -   x (        ) = B φ sa + χ               (36)
                                                                Eρ CA
                                                                                   φ wbe
                                    t   p  w   x   p   w       x  p   x
                                                                 3
                                                                                3
              式中:t为时间,s;x为距离,m;ρ 为水的密度,kg?m ,ρ≈1000kg?m ;C为水的比热,在 0℃时
                                                                                     p
                                                             2
              C = 4217.7J?(kg·℃);A为渡槽过水断面面积,m ;V为断面平均流速,m?s;E为热扩散系数;φ sa
                                                                                         x
               p
                                   2
              为水面净热通量,W?m ;左边第一项表示过水断面热量随时间的变化;第二项表示过水断面热量随水
              体运动的变化,又称为热量的对流传递;第三项表示过水断面热量随水体热扩散的变化。
                                    采用参考文献[14]线性化热交换模型时,则水面与大气的热交换与水体与渡
                  当水面净热通量 φ sa
              槽边墙和底板的热交换可描述为
                                 + χ                                 2
                             B φ sa  φ wbe = B( φ sa0 + h(T- T) - h (T- T)) + χ ( φ wae0 + h (T- T))   (37)
                                                                                 wae
                                                                                     a
                                                                                        w
                                                sa
                                                                   a
                                                            sa2
                                                    a
                                                       w
                                                                w
                                                        =   - a - bT                                   (38)
                                                    φ sa0 φ sn  sa  sa a
                —  1 3 2 —
                     2
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