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Control Theory and Informatics                                                                  www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012


 Neural Network Precept Diagnosis on Petrochemical Pipelines
                                  for Quality Maintenance
                              S.Bhuvaneswari1* R.Hemachandran2 R.Vignashwaran3
    1.   Reader, Department of Computer Science, Pondicherry University, Karaikal Campus, Karaikal
    2.   Faculty, N.I.T, Puducherry
    3.   Scholar, Department of Computer Science, Amrita University, Coimbatore
    * E-mail of the corresponding author: booni_67@yahoo.co.in
Abstract
Pipeline tubes are part of vital mechanical systems largely used in petrochemical industries. They serve to
transport natural gases or liquids. They are cylindrical tubes and are submitted to the risks of corrosion due
to high PH concentrations of the transported liquids in addition to fatigue cracks. Due to the nature of their
function, they are subject to the alternation of pressure-depression along the time, initiating therefore in the
tubes’ body micro-cracks that can propagate abruptly to lead to failure by fatigue. On to the diagnostic
study for the issue the development of this prognostic process employing neural network for such systems
bounds to the scope of quality maintenance.

Keywords: Percept, Simulated results, Fluid Mechanics


1. Introduction

  The pipelines tubes are manufactured as cylindrical tubes of radius R and thickness e. The failure by
fatigue is caused by the fluctuation of pressure-depression along the time t ( 0 ≤ P ≤ P0). These pipelines are
unfortunately usually designed for ultimate limits states (resistance).To be more realistic, a prognostic
model is proposed here based on analytic laws of degradation by fatigue (Paris’ law) in addition to the
cumulative law of damage (Miner’s law).This prognostic model is crucial in petrochemical industries for
the reason of favorable economic and availability consequences on the exploitation cost .




Fig. 1: Internal pressure diagram.


2. Paris Law
  The Paris’ law allows determining the propagation speed of the cracks da/ dN at the time of their



                                                       5
Control Theory and Informatics                                                                  www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012

               da
  detection:      = C.(∆K ) m where a is the crack length, N is the number of cycles, C and m are the Paris
               dN
constants, and ∆K is the stress intensity factor.
We can distinguish:
    -    The long cracks that obey to Paris law
    -    The short cracks that serve to decrease the speed of propagation
    -    The short physical cracks that serve to increase the speed of propagation

                                           da 
   The law can be written also as :
                                       log     = log C + m log(∆K )
                                           dN 


         da 
     log    
         dN 
                  Phase I
                                                    Phase II                                   Final fracture
                  Low speed of
                                                    Stable                                     Kc
                  propagation
                                                    propagation



                                                                                       Phase III
                                                                                     High speed of
                                                                                     propagation
                                                       da 
                                                            = C (∆K )
                                                                       m
                                                      
                                                       dN 



                                                                                         log (∆K )
                        Threshold
                     ∆Kth
Fig. 2: The three phases of cracks growth, Paris’ law.
3. Pipelines under Pressure


  A tube is considered thin when its thickness is of the order of one tenth of its radius: e ≤R/10




                                                         6
Control Theory and Informatics                                                                  www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012




 Fig. 3: Cylindrical pipelines




Fig. 4: Stress type distribution


4. State of Stresses
Te tubes are cylindrical shells of revolution. when thin tubes of radius r and of thickness e are under
internal pressure p, the state of stresses is membrane-like under bending loads. the membrane stresses are
circumferential (hoop stress) σθ and longitudinal stresses (axial stress) σL




Fig. 5: Axial stresses and Hoop stresses in cylindrical pipelines
                                         PR
                                   σ θ = e
                                   
                                         PR
These stresses are given by:       σ L =
                                   
                                         2e

  The critical cracks are those which are perpendicular to maximal stressesσθ, that means longitudinal
  cracks which are parallel to the axis of the tube. A crack is of depth a or of length a, if we measure in the
  direction of the tube thickness e.   Normally the ratio a/e is within the following range: 0.1 ≤ a/e ≤0.99


                                                       7
Control Theory and Informatics                                                                    www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012




Fig. 6: Crack length in radial view




Fig. 7: Cracked pipeline section


  The stress intensity factor KI represents the effect of stress concentration in the presence of a flat crack.




Fig. 8: Non-uniform distribution of stresses near the crack


The stress intensity factor is given [6] by:

K I = y (a ) × πa σ θ

⇒ K I = 0.6 × g (a )× πa × P.
                                  R
                                    ≤ K IC
                                  e




             with Y (a ) = 0.6 × g (a ) : is the geometric factor ;
                           a
                      1 + 2 
             g (a ) =      e                                                                J IC ⋅ E
                              3                                                   K IC =
                       a 2                                                                 1 − (ν ) 2
                      1 −                             8
                          e
Control Theory and Informatics                                                                      www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012




K IC : is the tenacity of material (critical stress intensity factor) and is given by:

                                                                                                   J IC ⋅ E
Note that the factor KI must not exceed the value of KIC .                               K IC =
                                                                                                  1 − (ν ) 2
5. Proposed Percept Model


  Consider a pipeline of radius R = 240 mm and of thickness e = 8 mm transporting natural gases, the
parameters related to materials and to the environment are taken as being equal to
  : [5] m= 3 et C = ε = 5.2.10 −13
                                                                                                    e    e
The length of the crack is denoted by a with an initial value a 0 = 0.2 mm a0 ≤ a ≤ a N =             ⇒    =8
                                                                                                    8   aN
We have to respect the following ratio:


         a                e
0 .1 ≤     ≤ 0.99 ⇒ 1.01 ≤ ≤ 10
         e                a

Take a similar form to
                          da
                                as    a = εφ 1 ( a ) φ 2 ( p )
                                      &
                          dN


with: ε = C ;                     (
                     φ1 (a) = Y (a ) π a           )   m
                                                           ;    p = ∆σ and


φ 2 ( p) = p m = (∆σ)m
The initial damage is:   a(0) = a0
A recurrent form of crack length gives:

a i = εφ1 ( a i −1 ) φ 2 ( p i ) + a i −1
And the corresponding degradation is given by:

 Di = Di −1 + ηφ1 ( Di −1 )φ 2 ( pi )
for m = 3 ⇒ φ 2 ( p i ) = p i3 = (∆ σ θ i )3

                         ε
Morevor η =
                     a N − a0


                                                           9
Control Theory and Informatics                                                                    www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012

                                                            da j
                                             dj =
We define the damage fraction by:
                                                         aN − a0
Therefore, we get the cumulated total damage:

                                               i

        i           i      da j
                                             ∑ da j                ai
                                              j =1
Di = ∑ d j = ∑                         =                    =
       j =1         j =1 a N   − a0          a N − a0           a N − a0

                                                     N
                                DN = ∑ d j = 1
We can easily prove that:
                                                     j =1



                                                                     D
                                                                                    Failure
                                                                1
                                                                         Reliable




                                                                                          ni/Ni
                                                                0

Fig. 9: Miner’s law of damage

     where :
     0 ≤ n ≤ N , a0 ≤ a ≤ a N ;
                                      N
     D0 ≤ D ≤ 1 = D N ; D N = ∑ d j = 1
                                      j =1

                 a0          D a
     D0 =              ⇒ a0 = 0 N
              a N − a0       1 + D0




                                                                    10
Control Theory and Informatics                                                             www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012


            The other sequences are :
                    a0
            D0 =
                 a N − a0
                      a1
            D1 =
                   a N − a0
                      a2
            D2 =
                   a N − a0
            M
                      an
            Dn =
                   a N − a0
6. Percept simulation of levels




Fig. 10: Triangular simulation of internal pressure




                       Table :1 Statistical Characteristics of Each Pressure Mode

                                       Mean of p i
   Pressure mode                                                    C.o.v. of     p i in   %           Law
                                      ( p i in       MPa)


   High (mode 1)                                 8                              10 %                 Triangular


  Middle (mode 2)                                5                              10%                  Triangular


   Low (mode 3)                                  3                              10%                  Triangular



                                                            11
Control Theory and Informatics                                                                  www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012




     We study three levels of maximal pressures in pipelines which are: 3 MPa, 5 MPa, and 8 MPa that are
repeated within a specific interval of time T=8 hours. At each level, we deduce the degradation trajectory D
in terms of time or in terms of the number of cycles N.
The failure by fatigue is obtained for a certain critical number of cycles: pressure-depression or for a certain
time period. Therefore, the lifetime of the pipeline for each level of maximal pressure is deduced at D=1.




    7. Results and Discussion on Simulation
  The Monte Carlo one level percept simulations for 1000 times for the pipeline system and under the 3
modes of internal pressure (high, middle and low) gives the degradation trajectory which are represented in
the following 3 figures.




                                 Fig. 11:   Degradation evolution for mode 1




                                                      12
Control Theory and Informatics                                           www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012




                           Fig. 12:   Degradation evolution for mode 2




                           Fig. 13:   Degradation evolution for mode 3




                                                 13
Control Theory and Informatics                                                                www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012




                               Fig. 14:   Degradation evolution for All three modes



We deduce from the percept interrogation that the pipeline lifetime is nearly 115 hours for mode 1 (high
pressure), nearly 160 hours for mode 2 (middle pressure), and nearly 240 hours for mode 3 (low pressure).
From these curves, we can see that our prognostic model, using analytic laws, gives the remaining lifetime
of pipelines at any instant.


8. Conclusion and Scope for Future Work


     The percept neural network sustains in predicting the life time effectiveness on field efficiency for the
radial pipelines by which the user is able to read the rear and bear happenings on fluid mechanics in
industries. The study also helps in predicting the sustainability feature of turbines in heavy alloy plants
which could be scope for the work in future.
References
     G. Vachtsevanos, F. Lewis, M. Roemer, A. Hess, B. Wu, Intelligent Fault Diagnosis and Prognosis
     for Engineering Systems, John Wiley & Sons, Inc., 2006, ch. 5,6 and 7.
     J. Lemaitre and J. Chaboche, Mechanics of Solid Materials. New York: Cambridge University Press,
     1990.
     M. Langon, Introduction a la Fatigue et Mécanique de la Rupture, Centre d’essais aéronautique de
     Toulouse, ENSICA April,1999
     K. El-Tawil, S. Kadry, Fatigue Stochastique des Systèmes Mécaniques Basée sur la Technique de
     Transformation Probabiliste, internal report, Lebanese University, grant research program, 2010
     J. Lemaitre, R. Desmorat, Engineering Damage Mechanics, New York: Springer-Verlag, 2005, ch. 6.


                                                        14
Control Theory and Informatics                                                        www.iiste.org
ISSN 2224-5774 (print) ISSN 2225-0492 (online)
Vol 2, No.2, 2012

    K. El-Tawil, A. Abou Jaoude and S. Kadry, “Life time estimation under probabilistic fatigue of
    cracked plates for multiple limit states”, ICNAAM, 2009.
    K. El-Tawil, Mécanique Aléatoire et Fiabilité, cours de master2r mécanique, Ecole doctorale des
    sciences et technologies EDST Université libanaise, Beyrouth 2004
    A. Abou Jaoude, K. El-Tawil, S. Kadry, H. Noura and M. Ouladsine, ”Analytic prognostic model for
    a dynamic system”, European Conference of Control, 2010, submitted for publication.




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11.[5 15]neural network precept diagnosis on petrochemical pipelines for quality maintenance

  • 1. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 Neural Network Precept Diagnosis on Petrochemical Pipelines for Quality Maintenance S.Bhuvaneswari1* R.Hemachandran2 R.Vignashwaran3 1. Reader, Department of Computer Science, Pondicherry University, Karaikal Campus, Karaikal 2. Faculty, N.I.T, Puducherry 3. Scholar, Department of Computer Science, Amrita University, Coimbatore * E-mail of the corresponding author: booni_67@yahoo.co.in Abstract Pipeline tubes are part of vital mechanical systems largely used in petrochemical industries. They serve to transport natural gases or liquids. They are cylindrical tubes and are submitted to the risks of corrosion due to high PH concentrations of the transported liquids in addition to fatigue cracks. Due to the nature of their function, they are subject to the alternation of pressure-depression along the time, initiating therefore in the tubes’ body micro-cracks that can propagate abruptly to lead to failure by fatigue. On to the diagnostic study for the issue the development of this prognostic process employing neural network for such systems bounds to the scope of quality maintenance. Keywords: Percept, Simulated results, Fluid Mechanics 1. Introduction The pipelines tubes are manufactured as cylindrical tubes of radius R and thickness e. The failure by fatigue is caused by the fluctuation of pressure-depression along the time t ( 0 ≤ P ≤ P0). These pipelines are unfortunately usually designed for ultimate limits states (resistance).To be more realistic, a prognostic model is proposed here based on analytic laws of degradation by fatigue (Paris’ law) in addition to the cumulative law of damage (Miner’s law).This prognostic model is crucial in petrochemical industries for the reason of favorable economic and availability consequences on the exploitation cost . Fig. 1: Internal pressure diagram. 2. Paris Law The Paris’ law allows determining the propagation speed of the cracks da/ dN at the time of their 5
  • 2. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 da detection: = C.(∆K ) m where a is the crack length, N is the number of cycles, C and m are the Paris dN constants, and ∆K is the stress intensity factor. We can distinguish: - The long cracks that obey to Paris law - The short cracks that serve to decrease the speed of propagation - The short physical cracks that serve to increase the speed of propagation  da  The law can be written also as : log  = log C + m log(∆K )  dN   da  log   dN  Phase I Phase II Final fracture Low speed of Stable Kc propagation propagation Phase III High speed of propagation  da   = C (∆K ) m   dN  log (∆K ) Threshold ∆Kth Fig. 2: The three phases of cracks growth, Paris’ law. 3. Pipelines under Pressure A tube is considered thin when its thickness is of the order of one tenth of its radius: e ≤R/10 6
  • 3. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 Fig. 3: Cylindrical pipelines Fig. 4: Stress type distribution 4. State of Stresses Te tubes are cylindrical shells of revolution. when thin tubes of radius r and of thickness e are under internal pressure p, the state of stresses is membrane-like under bending loads. the membrane stresses are circumferential (hoop stress) σθ and longitudinal stresses (axial stress) σL Fig. 5: Axial stresses and Hoop stresses in cylindrical pipelines  PR σ θ = e   PR These stresses are given by: σ L =   2e The critical cracks are those which are perpendicular to maximal stressesσθ, that means longitudinal cracks which are parallel to the axis of the tube. A crack is of depth a or of length a, if we measure in the direction of the tube thickness e. Normally the ratio a/e is within the following range: 0.1 ≤ a/e ≤0.99 7
  • 4. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 Fig. 6: Crack length in radial view Fig. 7: Cracked pipeline section The stress intensity factor KI represents the effect of stress concentration in the presence of a flat crack. Fig. 8: Non-uniform distribution of stresses near the crack The stress intensity factor is given [6] by: K I = y (a ) × πa σ θ ⇒ K I = 0.6 × g (a )× πa × P. R ≤ K IC e with Y (a ) = 0.6 × g (a ) : is the geometric factor ; a 1 + 2  g (a ) = e J IC ⋅ E 3 K IC =  a 2 1 − (ν ) 2 1 −  8  e
  • 5. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 K IC : is the tenacity of material (critical stress intensity factor) and is given by: J IC ⋅ E Note that the factor KI must not exceed the value of KIC . K IC = 1 − (ν ) 2 5. Proposed Percept Model Consider a pipeline of radius R = 240 mm and of thickness e = 8 mm transporting natural gases, the parameters related to materials and to the environment are taken as being equal to : [5] m= 3 et C = ε = 5.2.10 −13 e e The length of the crack is denoted by a with an initial value a 0 = 0.2 mm a0 ≤ a ≤ a N = ⇒ =8 8 aN We have to respect the following ratio: a e 0 .1 ≤ ≤ 0.99 ⇒ 1.01 ≤ ≤ 10 e a Take a similar form to da as a = εφ 1 ( a ) φ 2 ( p ) & dN with: ε = C ; ( φ1 (a) = Y (a ) π a ) m ; p = ∆σ and φ 2 ( p) = p m = (∆σ)m The initial damage is: a(0) = a0 A recurrent form of crack length gives: a i = εφ1 ( a i −1 ) φ 2 ( p i ) + a i −1 And the corresponding degradation is given by: Di = Di −1 + ηφ1 ( Di −1 )φ 2 ( pi ) for m = 3 ⇒ φ 2 ( p i ) = p i3 = (∆ σ θ i )3 ε Morevor η = a N − a0 9
  • 6. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 da j dj = We define the damage fraction by: aN − a0 Therefore, we get the cumulated total damage: i i i da j ∑ da j ai j =1 Di = ∑ d j = ∑ = = j =1 j =1 a N − a0 a N − a0 a N − a0 N DN = ∑ d j = 1 We can easily prove that: j =1 D Failure 1 Reliable ni/Ni 0 Fig. 9: Miner’s law of damage where : 0 ≤ n ≤ N , a0 ≤ a ≤ a N ; N D0 ≤ D ≤ 1 = D N ; D N = ∑ d j = 1 j =1 a0 D a D0 = ⇒ a0 = 0 N a N − a0 1 + D0 10
  • 7. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 The other sequences are : a0 D0 = a N − a0 a1 D1 = a N − a0 a2 D2 = a N − a0 M an Dn = a N − a0 6. Percept simulation of levels Fig. 10: Triangular simulation of internal pressure Table :1 Statistical Characteristics of Each Pressure Mode Mean of p i Pressure mode C.o.v. of p i in % Law ( p i in MPa) High (mode 1) 8 10 % Triangular Middle (mode 2) 5 10% Triangular Low (mode 3) 3 10% Triangular 11
  • 8. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 We study three levels of maximal pressures in pipelines which are: 3 MPa, 5 MPa, and 8 MPa that are repeated within a specific interval of time T=8 hours. At each level, we deduce the degradation trajectory D in terms of time or in terms of the number of cycles N. The failure by fatigue is obtained for a certain critical number of cycles: pressure-depression or for a certain time period. Therefore, the lifetime of the pipeline for each level of maximal pressure is deduced at D=1. 7. Results and Discussion on Simulation The Monte Carlo one level percept simulations for 1000 times for the pipeline system and under the 3 modes of internal pressure (high, middle and low) gives the degradation trajectory which are represented in the following 3 figures. Fig. 11: Degradation evolution for mode 1 12
  • 9. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 Fig. 12: Degradation evolution for mode 2 Fig. 13: Degradation evolution for mode 3 13
  • 10. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 Fig. 14: Degradation evolution for All three modes We deduce from the percept interrogation that the pipeline lifetime is nearly 115 hours for mode 1 (high pressure), nearly 160 hours for mode 2 (middle pressure), and nearly 240 hours for mode 3 (low pressure). From these curves, we can see that our prognostic model, using analytic laws, gives the remaining lifetime of pipelines at any instant. 8. Conclusion and Scope for Future Work The percept neural network sustains in predicting the life time effectiveness on field efficiency for the radial pipelines by which the user is able to read the rear and bear happenings on fluid mechanics in industries. The study also helps in predicting the sustainability feature of turbines in heavy alloy plants which could be scope for the work in future. References G. Vachtsevanos, F. Lewis, M. Roemer, A. Hess, B. Wu, Intelligent Fault Diagnosis and Prognosis for Engineering Systems, John Wiley & Sons, Inc., 2006, ch. 5,6 and 7. J. Lemaitre and J. Chaboche, Mechanics of Solid Materials. New York: Cambridge University Press, 1990. M. Langon, Introduction a la Fatigue et Mécanique de la Rupture, Centre d’essais aéronautique de Toulouse, ENSICA April,1999 K. El-Tawil, S. Kadry, Fatigue Stochastique des Systèmes Mécaniques Basée sur la Technique de Transformation Probabiliste, internal report, Lebanese University, grant research program, 2010 J. Lemaitre, R. Desmorat, Engineering Damage Mechanics, New York: Springer-Verlag, 2005, ch. 6. 14
  • 11. Control Theory and Informatics www.iiste.org ISSN 2224-5774 (print) ISSN 2225-0492 (online) Vol 2, No.2, 2012 K. El-Tawil, A. Abou Jaoude and S. Kadry, “Life time estimation under probabilistic fatigue of cracked plates for multiple limit states”, ICNAAM, 2009. K. El-Tawil, Mécanique Aléatoire et Fiabilité, cours de master2r mécanique, Ecole doctorale des sciences et technologies EDST Université libanaise, Beyrouth 2004 A. Abou Jaoude, K. El-Tawil, S. Kadry, H. Noura and M. Ouladsine, ”Analytic prognostic model for a dynamic system”, European Conference of Control, 2010, submitted for publication. 15
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