chapter.5 and chapter.11
DESCRIPTION
Chapter.5 and Chapter.11. 마찰력 ( 전단력 ) = 압력에 의한 힘 = 수두손실 ( 압력손실 ) 위의 식을 정리하면 다음과 같다. < 관로 내부에서의 유속 , 압력 , 전단응력 >. < 관류의 전단응력 및 유속 분포 >. 뉴턴의 제 1 점성법칙은 다음과 같다 . 위의 식을 에 대입하면 다음과 같다 . 위의 유속에 대한 식을 관의 내경에 대하여 적분하면 다음과 같다 . 위의 식의 적분상수 C 는 다음과 같이 구할 수 있다. - PowerPoint PPT PresentationTRANSCRIPT
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Chapter.5 and Chapter.11
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() = = () .
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1 .
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C .
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r=0 , .
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1/2. : - - - -
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. = /
() .
Poiseulli .
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, , , . , . 1. : : 20 * 0.5// = 10/ Q 2. P, L . 3. V, D .
* , .
, , : Re < 2000 : Re > 4000 : 2000
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5.2 Derive the equations of the head loss for the problem 5.1 such as Darcy-Weisbach equation. : Darcy-Weisbach Darcy-Weisbach . , . Darcy-Weisbach . .
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. () = = ()
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. 1 .
, .
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Osborne Reynolds Reynolds . : . .
Figure 3.4
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Re < 2000 Laminar Flow 2000 < Re < 4000 Transition Region Re > 4000 Turbulent Flow Poiseuille . -> -> -> : - -> : / -> , ,
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5.3 Derive the equations of the velocity from the head loss equation for the problem 5.2 such as Manning's, Chezy's, and Hagen-William's formula. 1) Manning's for turbulent regions of rough pipes, or for canals.
R = = / = perimeter/area n = = roughness coefficient : hydraulic radius ( for a circular pipe)
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2) Chezy's , .
(5.6.1)
. () .
. () (secondary flow) () .
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5.15 ()
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5.15 , . f2 . . . . () () .
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(3.10.1) .
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(5.6.2)
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, (3.11.2) . P () ()(wetted perimeter). ( ) . L sin = z1 - z2 (5.6.3) . (5.6.2), (5.6.3) (5.6.1) (5.6.4)
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. R (hydraulic radius) . R . . (5.6.4) m N/N ft lb/lb ()(head loss due to friction) . () S (5.6.5) , V (5.6.6)
. C . Chezy . Chezy C () () . C .
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3) Hagen-William's Hazen-Williams .
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5.4 Explain the concept of Reynold's number and hydraulic radius. Reynolds . Reynolds (), , .
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Reynolds Mach .
, .
. , () .
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(transverse interchange of momentum) . , , Reynolds .
() () . 1. (). () . 2. () (). () .
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2 () , Reynolds () () . , , , Reynolds .
, , . Reynolds R . (5.1.1)
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Reynolds 5.1 . , . () , () () () () .Reynolds , . .
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. Reynolds .
. . () .
. Reynolds .
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5.1 Reynolds
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Reynolds , .
() Reynolds(Reynolds upper critical number) . Reynolds Reynolds .
Reynolds Reynolds R 2,000 .
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() Reynolds(Reynolds lower critical number) , . Reynolds 2,000~4,000 . . , 1.7~2.0 .
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Reynolds () Reynolds . , () . () , () .
Reynolds . .
, () , , .
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(inertial force), . () . Reynolds . Reynolds . () (fine scale) () () , (large scale) . , . , () . () .
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. Reynolds . . .
() ()( 1 2 ) . Reynolds () .
hydraulic radius: , . (hydraulic radius) . . .
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5.5 Explain the computational algorithm of the pipe network using the concept as shown in the section of 4.3-4.5 in the Brebbia's textbook. , . I D, C, L .
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, k, j , i . i k, j , . Poiseuille ( ).
, . .
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Hazen-Williams ( ). :
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( ) .
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, .
, +, - ( ). .
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, , , .
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. , .
, , .
, () ( , ), ( ) .
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, , .
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, j .
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. .
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5 . 5 .
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, 5 , . 3 . 5 .
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, ., . .
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(ii) . (iii) .
(iv) .
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.( . , .)
i k, j . - (k,k) (j,j) . - (k,j) (j,k) .
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Fortran .
c c... initialize global matrix ... c npmax : total number of nodes = 6 c glob : global matrix after assembling c do i=1,npmax do j=1,npmax glob(i,j) = 0 enddo enddo c c... assemble each element matrix for overall element ... c nelmax : total nuber of elements : 9 c do nel=1, nelmax c c... read information about element connectivity ... c nodemax : total number of node in each elment : 2 c element1st node2nd node112213c read(nodeele(nel,ie), ie=1, nodemax) c... c... compute each element of element matrix at each node ... c ig : global nodal number of ieth node in element nel c jg : global nodal number of jeth node in element nel c do ie=1, nodemax do je=1, nodemax ig=nodeele(nel,ie) jg=nodeele(nel,je) c c... compute each element in k matrix ... c ek= rk(nel)*(-1)**(ie+je) c c... assemble each element in k matrix ... c glob(ig,jg) = glob(ig,jg)+ek c enddo enddo enddo
. , , , .
element1st node2nd node112213
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5.6 Determine the discharge through the system as shown below by using the concept of the equivalent pipe where, =0.5, =300m, =600mm, = 2mm, =240 m, =1m, =0.3mm, , and H=6m.
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5.21 , 5.21 .
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5.7 Determine flow through each pipe and the pressure at B as shown below for a total flow of 12 cfs. Where, =3000ft, =1ft, =0.00 ft; =2000ft, =8in, =0.0001ft; =4000ft, =16in, =0.0008ft; =2.00 slugs/ , =0.00003 /s, =8psi, =100ft, =80ft.
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, 2 (parallel-pipe) .
, .
, .
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11.9 (11.5.1)
. , , .
. (1) . (2) , , .
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, . .
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. 1. 1 . 2. . 3. . 4. 3 , . 5. .
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. , 1 (11.5.2) . .
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5.8 Find the discharges for water at 20C with the following pipe data and reservoir elevations as shown below. Where
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. . , . Darcy-Weisbach . J . .
. .
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, . , . ,
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0.029m3/s . .
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5.9 Explain the algorithm of the Hardy Cross Method for the pipe network analysis. . .
, . .
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1. 0 . () 2. . () 3. Darcy-Weisbach . , . ( : =, )
: : :
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, 11.15 A G AG AFEDG .
. 11.15
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. Hardy Cross (3) . , .
. , r (11.1.1) . r (Darcy-Weisbach ), -(loop-balancing) .
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. , (11.7.1) . . . . , .
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. (11.7.2) (11.7.1) . , . .
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1. , . 2. . . (11.7.2) , . 3. 2 . . 4. (he) 2 3 . . r . . .
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5.10 The distribution of flow through the network as shown below is desired for the inflows and outflows as given. For simplicity n has been given the value 2.0. Implement the Hardy Cross Method for this problem.
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11.16(a) . 1 . . 2 . 15 + 11.06 = 26.06 , 35 + (-21.17) + (-11.06) = 2.77. 11.16(b) 11.16(c) 4 .
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11.16 , 15 100 . , , Hardy Cross - .
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11.16
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[4-7] , Hardy Cross, (node balancing) .
Newton-Raphson .
[5,6] .
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5.11 The program in Fig. 11.18 in the text book is used to solve the network problem displayed as below. The pump data are as follows: Implement the pipe network modeling for this problem by using thesuggested program of Hardy Cross Method.
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. . .
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, (pseudo elements) . . , . 3 ( 11.17) .
(11.8.1)
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1 4 . , . (11.8. (11.7.2) . Newton( B) . . 8 - 3 . . 4
(11.8.2)
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5 8 . (11.8.2) Newton . , - 0 . 11.18 BASIC . Hardy-Cross - , Hazen-Williams Darcy-Weisbach . , , . USC Sl .