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M a t h e m a t i c a
B a l k a n i c a
—————————
New Series Vol. 26, 2012, Fasc. 3–4
Lambert W Function in Hydraulic Problems∗
Dejan Brkić
Presented at MASSEE International Conference on Mathematics MICOM-2009
Darcy’s flow friction factor is expressed in implicit form in some of the relations such
as Colebrook’s and have to be solved by iteration procedure because the unknown friction
factor appears on both sides of the equation. Lambert W function is implicitly elementary
but is not, itself, an elementary function. Implicit form of the Lambert W function allows us
to transform other implicit functions in explicit form without any kind of approximations or
simplifications involved. But unfortunately, the Lambert W function itself cannot be solved
easily without approximation. Two original transformations in explicit form of Colebrook’s
relation using Lambert W function will also be shown. Here will be shown efficient procedure
for approximate solutions of the transformed relations.
MSC 2010: 76F65
Key Words: Lambert W function, Colebrook’s equation
1. Introduction
Flow friction factor can be expressed in implicit form in some of the rela-
tions such as Colebrook’s and hence has to be solved using iteration procedure
because the unknown friction factor appears on both sides of such equation [1,2].
Many, more or less accurate, explicit approximations of the implicit Colebrook’s
equations for the flow friction were developed [3]. These equations are valuable
for hydraulically ’smooth’ pipe region of partial turbulence and even for fully
turbulent regime [4]. The Lambert W function proposed by J.H. Lambert [5] in
1758 and refined by L. Euler can be used for explicit and exact transformation
of the Colebrook’s equation. Lambert W function is implicitly elementary but
is not, itself, an elementary function [6]. Note that name ”W” for Lambert
∗
Partially supported by Grants No 45/2006 and 451-03-01078/2009-02 from the Ministry
of Science and Technological Development of Republic of Serbia
286 D. Brkić
function is not as old as the related function. The modern history of Lambert
W began in the 1980s, when a version of the function was built into the Maple
computer-algebra system and given the name W [7]. Implicit form of the Lam-
bert W function allows us to transform other implicit functions in explicit form
without any kind of approximations or simplifications involved. But unfortu-
nately, the Lambert W function itself cannot be solved without approximation
[8,9]. How well Colebrook’s equation, itself, fits the experimental data is be-
yond the scope of this article. Some original transformations in explicit form
of Colebrook’s relation using Lambert W function will also be shown. These
reformulated Colebrook’s equations are now explicit in friction factor but with
Lambert W function involved. Hence, these are not approximations, but the
procedure for exact mathematical solution for the solution of the Lambert W
function has not been developed yet and even more, probably will not be.
2. On the Colebrook’s equation for flow friction factor
For the partial turbulence regime where the friction coefficient diverges
to different straight lines for different constant relative roughness, Colebrook
proposed adding Prandtl’s (2.1) and von Karman’s (2.2) equations for smooth,
smoothing the contact between these two lines. How well the Colebrook equa-
tion’s smoothing contact among the von Karman’s and Prandtl’s (NPK) relation
can be best seen in graphical interpretation (Figure 1).
1
√
λ
= −2 · lg

2.51
Re ·
√
λ

= 2 · lg

Re ·
√
λ

− 0.8 (2.1)
1
√
λ
= −2 · lg


3.71 · D

= 1.14 − 2 · lg


D

= 1.74 − 2 · lg

2 · 
D

(2.2)
From strictly mathematical point of view, what Colebrook had done [2] is
incorrect, i.e. log(A+B) is not log(A)+log(B), but physically this relation gives
good results (smoothing the contact between two lines). So, finally Colebrook’s
relation can be noted as (2.3):
1
√
λ
= −2 · lg

2.51
Re ·
√
λ
+

3.71 · D

(2.3)
Problem can be treated as inverse; according to logarithm’s rules it is
equally incorrect to split the Colebrook’s relation into two pieces. Colebrook
equation belong to so called log-law relationship. Other approach, not shown in
this paper is so called power-law [10]. For example, Blasius form or power-law
relationships is more suitable for flow regimes typical for plastic (polyethylene,
Lambert W Function in Hydraulic Problems 287
Figure 1: Implicit Colebrook relation and related approximations smoothed
contact among relations for smooth and rough relations
PVC) pipes, while the Colebrook’s relation (logarithmic law) with related ap-
proximations is better for flow regimes in steel pipes [11].
3. On the Lambert W-function
Lambert W-function can be noted as (3.1):
W(x) · eW(x)
= x (3.1)
For real values of the argument, x, the W-function has two branches,
W0 (the principal branch) and W-1 (the negative branch). W0 is referred to as
principal branch of the Lambert W function. Upper branch (noted as + in
Figure 2) is valid for solution of our problem.
Formal solution of the Lambert W function can be defined as (3.2):
W ≈ ln
x
ln
















x
ln






x
ln
...
!






















(3.2)
288 D. Brkić
Figure 2: Real branches of the Lambert W function
But after Boyd [8], it is more convenient to define a new function and a
new parameter such that both the domain and range are the nonnegative real
axis as (3.3):
ω = W + 1 ⇔ W = ω − 1 (3.3)
With also ’shifted’ argument of the function y (3.4) [8]:
y = 1 + x · e1
≈ 1 + 2.71 · x ⇔ x =
y − 1
e1
≈
y − 1
2.71
≈ 0.367 · (y − 1) (3.4)
Then, the Lambert-W function can be transformed in shifted function
(3.5) [8]:
(ω − 1) · eω
≈ y − 1 (3.5)
Approximate solution of shifted function can be expressed as (3.6) [8]:
ω0 ≈ (ln(y + 10) − ln(ln(y + 10))) · tanh
√
2 · y
ln(10) − ln(ln(10))
!
(3.6)
Lambert W Function in Hydraulic Problems 289
Improved solution after Boyd is also available (3.7) [8]:
ω0 ≈ ω0 · (1 +

ln(y) − 7
5

· e− 3
40
·(ln(y)−7
5 )
2
10
) (3.7)
This solution can be used as the first guess for Newton’s iteration scheme
to reduce the relative error (3.8) [8]:
ωi+1 ≈ ωi −
(ωi − 1) − e(−ωi)·(y−1)
ωi
(3.8)
Barry et al [9] give different way for calculation of approximate solution
of the Lambert W function (3.9):
W+
0 (x) ≈ ln




6 · x
5 · ln

5
12 ·

x
ln(1+12·x
5 )




 (3.9)
This solution (3.9) is used in this paper to develop approximation of
Colebrook’s equation based on the Lambert-W function.
4. Transformations of Colebrook’s equation based on Lambert-
W function
Transformation of Colebrook’s equation based on Lambert-W function
already exist in scientific literature (4.1) [12]:
λ =

O1 · W


e
O1
O2·O3
O2 · O3

 −
O1
O2


−2
(4.1)
where:
O1 =

3.71 · D
O2 =
2.51
Re
O3 =
2
ln(10)
≈ 0.868589
Note that previous equation (4.1) cannot be used for high values of
Reynolds number and relative roughness, because numbers become too big even
for capabilities of today available computers [13,14]. Papers of Goudar and
290 D. Brkić
Sonnad [13-17], Nandakumar [18] and Clamond [19] deal with the Lambert W
function in hydraulic in a very successful way.
According to the original idea of Colebrook and White to unite the
Prandtl’s (NPK) and von Karman’s equations in a one coherent model, their
equation can be reformulated using the Lambert W-function in a manner pre-
sented as (4.2):
1
√
λ
= −2 · lg

10
−1
ln(10)
·W
Re·ln(10)
5.02

+

3.71 · D

(4.2)
Or equivalent equation can be given in similar form (4.3):
1
√
λ
= −2 · lg


5.02 · W

Re·ln(10)
5.02

Re · ln(10)
+

3.71 · D

 (4.3)
Note that previous two equations are not approximations of Colebrook’s
relation (2.3). They are exact mathematical transformed, but unfortunately
they contain Lambert W-function which cannot be solved without approxima-
tions.
5. Approximation of Colebrook’s equation based on Lambert-
W function
Using equation (4.2) and approximate solution after Boyd (3.9), approx-
imate formula for calculation of Darcy’s friction factor after Colebrook can be
written as (5.1):
1
√
λ
≈ −2 · lg

10−0.4343·S
+

3.71 · D

≈ 2 · lg

2.18 · S
Re
+

3.71 · D

(5.1)
where:
S = ln
Re
1.816 · ln

1.1·Re
ln(1+1.1·Re)

Comparison of accuracy of different approximations of implicit Cole-
brook’s equation (2.3) are available in literature [3].
6. Conclusion
It may be difficult for many to recall the time as recently as the 1970’s
when there were no personal computers or even calculators that could do much
more than add or subtract. In that environment an implicit relationship such
Lambert W Function in Hydraulic Problems 291
as Colebrook’s (2.3), which was well-known then, was impractical and some
simplification was essential. All available approximations of the Colebrook’s
equation are very accurate, but most of these explicit relations created to solve
the implicit Colebrook’s form have been made obsolete by advance in computing
technology. The average error of almost all explicit approximations of the Cole-
brook’s relation is less than 1%. Solution of this implicit equation today can be
obtained easily and quickly by Microsoft Office Excel 2007 very accurately.
References
[1] C. F C o l e b r o o k, C.M. W h i t e. Experiments with fluid friction in rough-
ened pipes. // Proc. Roy. Soc. Ser. A: Math. Phys. Sci., 161, No 906,
1937, 367–381.
[2] C. F C o l e b r o o k. Turbulent flow in pipes with particular reference to the
transition region between the smooth and rough pipe laws. //J. Inst. Civil.
Eng. (London), 11, No 4, 1939, 133–156.
[3] G. Y i l d i r i m. Computer-based analysis of explicit approximations to the
implicit Colebrook-White equation in turbulent flow friction factor calcu-
lation. // Adv. Eng. Softw., 40, No 11, 2009, 1183–1190.
[4] L. F. M o o d y. Friction factors for pipe flow. // Trans. ASME, 66, No 8,
1944, 671–684.
[5] J. J. G r a y. Johann Heinrich Lambert, mathematician and scientist, 1728–
1777. // Hist. Math., 5, No 1, 1978, 13–41.
[6] R. M. C o r l e s s, G. H. G o n n e t, D. E. G. H a r e, D. J. J e f f r e y, D. E.
K n u t h. On the Lambert W-function. // Adv. Comput. Math., 5, No 4,
1996, 329–359.
[7] B. H a y e s. Why W? // Am. Sci., 93, No 2, 2005, 104–108.
[8] J.P. B o y d. Global approximations to the principal real-valued branch of
the Lambert W-function. // Appl. Math. Lett., 11, No 6, 1998, 27–31.
[9] D. A. B a r r y, J.-Y. P a r l a n g e, L. L i, H. P r o m m e r, C. J. C u n n i n g h a m,
F. S t a g n i t t i. Analytical approximations for real values of the Lambert
W-function. // Math. Comput. Simulat., 53, No 1-2, 2000, 95–103.
[10] M. V. Z a g a r o l a, A. E. P e r r y, A. J . S m i t s. Log laws or power laws: The
scaling in the overlap region. // Phys. Fluids., 9, No 7, 1997, 2094–2100.
[11] M. G. S u k h a r e v, A. M. K a r a s e v i c h, R. V. S a m o i l o v, I. V. T v e r s k o i.
Investigation of the hydraulic resistance in polyethylene pipelines. // Jour-
nal of Engineering Physics and Thermophysics, 78, No 2, 2005, 350–359.
[12] A. A. M o r e. Analytical solutions for the Colebrook and White equation
and for pressure drop in ideal gas flow in pipesl. // Chem. Eng. Sci., 61,
No 16, 2006, 5515–5519.
292 D. Brkić
[13] J. R. S o n n a d, C. T. G o u d a r. Constraints for using Lambert W function-
based explicit Colebrook-White equation. // J. Hydraul. Eng. ASCE, 130,
No 9, 2004, 929–931.
[14] J. R. S o n n a d, C. T. G o u d a r. Explicit reformulation of the Colebrook-
White equation for turbulent flow friction factor calculation. // Ind. Eng.
Chem. Res., 46, No 8, 2007, 2593–2600.
[15] J. R. S o n n a d, C. T. G o u d a r. Turbulent flow friction factor calculation
using a mathematically exact alternative to the Colebrook-White equation.
// J. Hydraul. Eng. ASCE, 132, No 8, 2006, 863–867.
[16] C. T. G o u d a r, J. R. S o n n a d. Explicit friction factor correlation for
turbulent flow in smooth pipes. // Ind. Eng. Chem. Res., 42, No 12,
2003, 2878–2880.
[17] C. T. G o u d a r, J. R. S o n n a d. Comparison of the iterative approximations
of the Colebrook-White equation. // Hydrocarb. Process., 87, No 8, 2008,
79–83.
[18] V. N a n d a k u mva r. Analytical calculation of Fanning friction factor. //
Hydrocarb. Process., 86, No 1, 2007, 97–100.
[19] D. C l a m o n d. Efficient resolution of the Colebrook equation. // Ind. Eng.
Chem. Res., 48, No 7, 2009, 3665=-3671.
Ministry of Science and Technological Development Received 04.02.2010
and Faculty of Mining and Geology
Beograd 11000
SERBIA
E-MAIL: dejanrgf@tesla.rcub.bg.ac.rs

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  • 1. M a t h e m a t i c a B a l k a n i c a ————————— New Series Vol. 26, 2012, Fasc. 3–4 Lambert W Function in Hydraulic Problems∗ Dejan Brkić Presented at MASSEE International Conference on Mathematics MICOM-2009 Darcy’s flow friction factor is expressed in implicit form in some of the relations such as Colebrook’s and have to be solved by iteration procedure because the unknown friction factor appears on both sides of the equation. Lambert W function is implicitly elementary but is not, itself, an elementary function. Implicit form of the Lambert W function allows us to transform other implicit functions in explicit form without any kind of approximations or simplifications involved. But unfortunately, the Lambert W function itself cannot be solved easily without approximation. Two original transformations in explicit form of Colebrook’s relation using Lambert W function will also be shown. Here will be shown efficient procedure for approximate solutions of the transformed relations. MSC 2010: 76F65 Key Words: Lambert W function, Colebrook’s equation 1. Introduction Flow friction factor can be expressed in implicit form in some of the rela- tions such as Colebrook’s and hence has to be solved using iteration procedure because the unknown friction factor appears on both sides of such equation [1,2]. Many, more or less accurate, explicit approximations of the implicit Colebrook’s equations for the flow friction were developed [3]. These equations are valuable for hydraulically ’smooth’ pipe region of partial turbulence and even for fully turbulent regime [4]. The Lambert W function proposed by J.H. Lambert [5] in 1758 and refined by L. Euler can be used for explicit and exact transformation of the Colebrook’s equation. Lambert W function is implicitly elementary but is not, itself, an elementary function [6]. Note that name ”W” for Lambert ∗ Partially supported by Grants No 45/2006 and 451-03-01078/2009-02 from the Ministry of Science and Technological Development of Republic of Serbia
  • 2. 286 D. Brkić function is not as old as the related function. The modern history of Lambert W began in the 1980s, when a version of the function was built into the Maple computer-algebra system and given the name W [7]. Implicit form of the Lam- bert W function allows us to transform other implicit functions in explicit form without any kind of approximations or simplifications involved. But unfortu- nately, the Lambert W function itself cannot be solved without approximation [8,9]. How well Colebrook’s equation, itself, fits the experimental data is be- yond the scope of this article. Some original transformations in explicit form of Colebrook’s relation using Lambert W function will also be shown. These reformulated Colebrook’s equations are now explicit in friction factor but with Lambert W function involved. Hence, these are not approximations, but the procedure for exact mathematical solution for the solution of the Lambert W function has not been developed yet and even more, probably will not be. 2. On the Colebrook’s equation for flow friction factor For the partial turbulence regime where the friction coefficient diverges to different straight lines for different constant relative roughness, Colebrook proposed adding Prandtl’s (2.1) and von Karman’s (2.2) equations for smooth, smoothing the contact between these two lines. How well the Colebrook equa- tion’s smoothing contact among the von Karman’s and Prandtl’s (NPK) relation can be best seen in graphical interpretation (Figure 1). 1 √ λ = −2 · lg 2.51 Re · √ λ = 2 · lg Re · √ λ − 0.8 (2.1) 1 √ λ = −2 · lg 3.71 · D = 1.14 − 2 · lg D = 1.74 − 2 · lg 2 · D (2.2) From strictly mathematical point of view, what Colebrook had done [2] is incorrect, i.e. log(A+B) is not log(A)+log(B), but physically this relation gives good results (smoothing the contact between two lines). So, finally Colebrook’s relation can be noted as (2.3): 1 √ λ = −2 · lg 2.51 Re · √ λ + 3.71 · D (2.3) Problem can be treated as inverse; according to logarithm’s rules it is equally incorrect to split the Colebrook’s relation into two pieces. Colebrook equation belong to so called log-law relationship. Other approach, not shown in this paper is so called power-law [10]. For example, Blasius form or power-law relationships is more suitable for flow regimes typical for plastic (polyethylene,
  • 3. Lambert W Function in Hydraulic Problems 287 Figure 1: Implicit Colebrook relation and related approximations smoothed contact among relations for smooth and rough relations PVC) pipes, while the Colebrook’s relation (logarithmic law) with related ap- proximations is better for flow regimes in steel pipes [11]. 3. On the Lambert W-function Lambert W-function can be noted as (3.1): W(x) · eW(x) = x (3.1) For real values of the argument, x, the W-function has two branches, W0 (the principal branch) and W-1 (the negative branch). W0 is referred to as principal branch of the Lambert W function. Upper branch (noted as + in Figure 2) is valid for solution of our problem. Formal solution of the Lambert W function can be defined as (3.2): W ≈ ln x ln                 x ln       x ln ... !                       (3.2)
  • 4. 288 D. Brkić Figure 2: Real branches of the Lambert W function But after Boyd [8], it is more convenient to define a new function and a new parameter such that both the domain and range are the nonnegative real axis as (3.3): ω = W + 1 ⇔ W = ω − 1 (3.3) With also ’shifted’ argument of the function y (3.4) [8]: y = 1 + x · e1 ≈ 1 + 2.71 · x ⇔ x = y − 1 e1 ≈ y − 1 2.71 ≈ 0.367 · (y − 1) (3.4) Then, the Lambert-W function can be transformed in shifted function (3.5) [8]: (ω − 1) · eω ≈ y − 1 (3.5) Approximate solution of shifted function can be expressed as (3.6) [8]: ω0 ≈ (ln(y + 10) − ln(ln(y + 10))) · tanh √ 2 · y ln(10) − ln(ln(10)) ! (3.6)
  • 5. Lambert W Function in Hydraulic Problems 289 Improved solution after Boyd is also available (3.7) [8]: ω0 ≈ ω0 · (1 + ln(y) − 7 5 · e− 3 40 ·(ln(y)−7 5 ) 2 10 ) (3.7) This solution can be used as the first guess for Newton’s iteration scheme to reduce the relative error (3.8) [8]: ωi+1 ≈ ωi − (ωi − 1) − e(−ωi)·(y−1) ωi (3.8) Barry et al [9] give different way for calculation of approximate solution of the Lambert W function (3.9): W+ 0 (x) ≈ ln     6 · x 5 · ln 5 12 · x ln(1+12·x 5 )     (3.9) This solution (3.9) is used in this paper to develop approximation of Colebrook’s equation based on the Lambert-W function. 4. Transformations of Colebrook’s equation based on Lambert- W function Transformation of Colebrook’s equation based on Lambert-W function already exist in scientific literature (4.1) [12]: λ =  O1 · W   e O1 O2·O3 O2 · O3   − O1 O2   −2 (4.1) where: O1 = 3.71 · D O2 = 2.51 Re O3 = 2 ln(10) ≈ 0.868589 Note that previous equation (4.1) cannot be used for high values of Reynolds number and relative roughness, because numbers become too big even for capabilities of today available computers [13,14]. Papers of Goudar and
  • 6. 290 D. Brkić Sonnad [13-17], Nandakumar [18] and Clamond [19] deal with the Lambert W function in hydraulic in a very successful way. According to the original idea of Colebrook and White to unite the Prandtl’s (NPK) and von Karman’s equations in a one coherent model, their equation can be reformulated using the Lambert W-function in a manner pre- sented as (4.2): 1 √ λ = −2 · lg 10 −1 ln(10) ·W Re·ln(10) 5.02 + 3.71 · D (4.2) Or equivalent equation can be given in similar form (4.3): 1 √ λ = −2 · lg   5.02 · W Re·ln(10) 5.02 Re · ln(10) + 3.71 · D   (4.3) Note that previous two equations are not approximations of Colebrook’s relation (2.3). They are exact mathematical transformed, but unfortunately they contain Lambert W-function which cannot be solved without approxima- tions. 5. Approximation of Colebrook’s equation based on Lambert- W function Using equation (4.2) and approximate solution after Boyd (3.9), approx- imate formula for calculation of Darcy’s friction factor after Colebrook can be written as (5.1): 1 √ λ ≈ −2 · lg 10−0.4343·S + 3.71 · D ≈ 2 · lg 2.18 · S Re + 3.71 · D (5.1) where: S = ln Re 1.816 · ln 1.1·Re ln(1+1.1·Re) Comparison of accuracy of different approximations of implicit Cole- brook’s equation (2.3) are available in literature [3]. 6. Conclusion It may be difficult for many to recall the time as recently as the 1970’s when there were no personal computers or even calculators that could do much more than add or subtract. In that environment an implicit relationship such
  • 7. Lambert W Function in Hydraulic Problems 291 as Colebrook’s (2.3), which was well-known then, was impractical and some simplification was essential. All available approximations of the Colebrook’s equation are very accurate, but most of these explicit relations created to solve the implicit Colebrook’s form have been made obsolete by advance in computing technology. The average error of almost all explicit approximations of the Cole- brook’s relation is less than 1%. Solution of this implicit equation today can be obtained easily and quickly by Microsoft Office Excel 2007 very accurately. References [1] C. F C o l e b r o o k, C.M. W h i t e. Experiments with fluid friction in rough- ened pipes. // Proc. Roy. Soc. Ser. A: Math. Phys. Sci., 161, No 906, 1937, 367–381. [2] C. F C o l e b r o o k. Turbulent flow in pipes with particular reference to the transition region between the smooth and rough pipe laws. //J. Inst. Civil. Eng. (London), 11, No 4, 1939, 133–156. [3] G. Y i l d i r i m. Computer-based analysis of explicit approximations to the implicit Colebrook-White equation in turbulent flow friction factor calcu- lation. // Adv. Eng. Softw., 40, No 11, 2009, 1183–1190. [4] L. F. M o o d y. Friction factors for pipe flow. // Trans. ASME, 66, No 8, 1944, 671–684. [5] J. J. G r a y. Johann Heinrich Lambert, mathematician and scientist, 1728– 1777. // Hist. Math., 5, No 1, 1978, 13–41. [6] R. M. C o r l e s s, G. H. G o n n e t, D. E. G. H a r e, D. J. J e f f r e y, D. E. K n u t h. On the Lambert W-function. // Adv. Comput. Math., 5, No 4, 1996, 329–359. [7] B. H a y e s. Why W? // Am. Sci., 93, No 2, 2005, 104–108. [8] J.P. B o y d. Global approximations to the principal real-valued branch of the Lambert W-function. // Appl. Math. Lett., 11, No 6, 1998, 27–31. [9] D. A. B a r r y, J.-Y. P a r l a n g e, L. L i, H. P r o m m e r, C. J. C u n n i n g h a m, F. S t a g n i t t i. Analytical approximations for real values of the Lambert W-function. // Math. Comput. Simulat., 53, No 1-2, 2000, 95–103. [10] M. V. Z a g a r o l a, A. E. P e r r y, A. J . S m i t s. Log laws or power laws: The scaling in the overlap region. // Phys. Fluids., 9, No 7, 1997, 2094–2100. [11] M. G. S u k h a r e v, A. M. K a r a s e v i c h, R. V. S a m o i l o v, I. V. T v e r s k o i. Investigation of the hydraulic resistance in polyethylene pipelines. // Jour- nal of Engineering Physics and Thermophysics, 78, No 2, 2005, 350–359. [12] A. A. M o r e. Analytical solutions for the Colebrook and White equation and for pressure drop in ideal gas flow in pipesl. // Chem. Eng. Sci., 61, No 16, 2006, 5515–5519.
  • 8. 292 D. Brkić [13] J. R. S o n n a d, C. T. G o u d a r. Constraints for using Lambert W function- based explicit Colebrook-White equation. // J. Hydraul. Eng. ASCE, 130, No 9, 2004, 929–931. [14] J. R. S o n n a d, C. T. G o u d a r. Explicit reformulation of the Colebrook- White equation for turbulent flow friction factor calculation. // Ind. Eng. Chem. Res., 46, No 8, 2007, 2593–2600. [15] J. R. S o n n a d, C. T. G o u d a r. Turbulent flow friction factor calculation using a mathematically exact alternative to the Colebrook-White equation. // J. Hydraul. Eng. ASCE, 132, No 8, 2006, 863–867. [16] C. T. G o u d a r, J. R. S o n n a d. Explicit friction factor correlation for turbulent flow in smooth pipes. // Ind. Eng. Chem. Res., 42, No 12, 2003, 2878–2880. [17] C. T. G o u d a r, J. R. S o n n a d. Comparison of the iterative approximations of the Colebrook-White equation. // Hydrocarb. Process., 87, No 8, 2008, 79–83. [18] V. N a n d a k u mva r. Analytical calculation of Fanning friction factor. // Hydrocarb. Process., 86, No 1, 2007, 97–100. [19] D. C l a m o n d. Efficient resolution of the Colebrook equation. // Ind. Eng. Chem. Res., 48, No 7, 2009, 3665=-3671. Ministry of Science and Technological Development Received 04.02.2010 and Faculty of Mining and Geology Beograd 11000 SERBIA E-MAIL: dejanrgf@tesla.rcub.bg.ac.rs