analyzing the behavior of an industrial system using fuzzy confidence interval based methodology
TRANSCRIPT
RESEARCH ARTICLE
Analyzing the Behavior of an Industrial System Using FuzzyConfidence Interval Based Methodology
Harish Garg
Received: 16 April 2013 / Revised: 14 August 2013 / Accepted: 24 October 2013 / Published online: 19 July 2014
� The National Academy of Sciences, India 2014
Abstract This paper presented a methodology, named as
confidence interval based lambda-tau, for analyzing the
behavior of complex repairable industrial systems by uti-
lizing vague, uncertain and imprecise data. In this, uncer-
tainties in the data related to each component of the system
are estimated with the help of fuzzy and statistical meth-
odology. Triangular fuzzy numbers are used for this pur-
pose as it allows expert opinions, operating conditions,
uncertainty and imprecision in reliability information.
Various reliability parameters are addressed for analyzing
the behavior of the system and their correspondingly
obtained results of the proposed approach are compared
with the existing fuzzy lambda-tau technique results. The
sensitivity as well as performance analysis has also been
performed to explore the effect of failure/repair rates of the
components on system availability. The approach has been
illustrated with an example of synthesis unit of a urea
fertilizer plant situated in Northern part of India. The
obtained results may be helpful for the plant personnel for
analyzing the systems’ behavior and to improve their per-
formance by adopting suitable maintenance strategies.
Keywords Uncertain system � Fuzzy reliability �Lambda-tau methodology � Fertilizer plant �Confidence interval
Introduction
Reliability and maintainability analysis is one of the
important engineering tasks in optimal design to study,
characterize and analyze the failure and repair of systems
in order to improve their operational use by increasing
their design life, eliminating or reducing the likelihood of
failures and safety risks, and reducing downtime, thereby
increasing available operating time. As a result, the job of
the reliability/ system analyst(s) has become more chal-
lenging as any unfortunate consequences of unreliable
behavior of systems or equipments have led to the desire
for reliability analysis [1, 2]. The conventional reliability
of a system is fully characterized in the context of
probability measures and is defined as the probability that
the system perform its function during a pre-defined
period under the defined conditions. Conventional meth-
ods assume that all the design information of the system
is precisely known which are based on the probabilistic
binary state model. But this precision is rarely true in the
real system because it is difficult to obtain a large
quantity of data from the system due to rare events of
components, human error and economic restraints. Even
if data is available, it is often inaccurate and thus exists
some uncertainty in the value of the survivor probabili-
ties. In such situations where sufficient information is not
available for defining a probability distribution, fuzzy set
theory can be used to represent the available data in an
analytical form [3]. Thus, the concept of fuzzy reliability
has been introduced and formulated either in the context
of the possibility measures or as a transition from fuzzy
success state to fuzzy failure state [4–6]. The main con-
tribution related to determine the component or system
reliability by using fuzzy set theory and fuzzy arithmetic
can be found in literature [7–11]. Yao et al. [12] applied a
H. Garg (&)
School of Mathematics and Computer Applications, Thapar
University Patiala, Patiala 147004, India
e-mail: [email protected]
URL: https://sites.google.com/site/harishg58iitr/
123
Natl. Acad. Sci. Lett. (July–August 2014) 37(4):359–370
DOI 10.1007/s40009-014-0239-2
statistical methodology in the fuzzy system reliability
analysis and got a fuzzy estimation of reliability. Jam-
khaneh et al. [13, 14] considered the fuzzy reliability of
both serial and parallel systems using fuzzy confidence
interval.
All the above-examined systems are non-repairable
ones and data used for their behavior analysis were col-
lected from historical records/logbooks/expert opinions
and taken as crisp data. Also, the traditional analytical
techniques need large amounts of data, which are difficult
to obtain because of various practical constraints such as
rare events of components, human errors, and economic
considerations for the estimation of failure/repair charac-
teristics of the system. In such circumstances, it is usually
not easy to analyze the behavior and performance of these
systems up to desired degree of accuracy by utilizing
available resources, data, and information. Furthermore, if
an analysis has been done by using some suitable tech-
niques listed above, then any reliability index alone is
inadequate to give a deeper idea about such type of sys-
tems’ behavior because a lot of factors exist which overall
influence the systems’ performance and consequently their
behavior. Thus, to analyze more closely the system’s
behavior, other reliability criteria should be included in the
traditional analysis and involved uncertainties must be
quantified. From the literature it is found that there are few
studies in which, using fuzzy set theory to account for
uncertainty in the analysis, system behavior in terms of
various reliability indices are analyzed [15–19]. In these
studies more emphasis is given to the evaluation of dif-
ferent reliability indices, reflecting system behavior, in the
form of fuzzy membership functions. Triangular fuzzy
numbers (TFNs) are used by using fuzzy possibility theory
for handling the uncertainty in the available/collected data.
The major drawback of the above techniques is that none
of them found the estimation of reliability index in the
fuzzy sense. Furthermore, they neither use fuzzy data nor
the robust and comprehensive fuzzy confidence interval. In
the evaluation of the reliability indices, data uncertainty is
one of the major challenges in the real world. The statis-
tical failure data (in the form of failure rates and repair
times) of systems are still sparse, which introduces
imprecision in the estimation of reliability parameters of
the system’s components. Moreover, due to uncertainties
in statistical data, it is necessary to estimate a range of a
reliable parameter rather than a single value. Thus current
failure data (crisp) are not sufficient to account the
involved uncertainties. Since, the population of reliability
parameters of the subsystem is unknown, therefore using
sampling, it is desirable to use the statistical confidence
interval for estimation of reliability parameters. To tackle
this problem, a new method for reliability evaluation of the
repairable industrial system by using both fuzzy data and
comprehensive fuzzy confidence interval has been pre-
sented here.
Thus, the main objective of the present paper is to
quantify the uncertainties of reliability data with the help of
both fuzzy numbers and fuzzy confidence intervals and to
develop a methodology named as confidence interval based
lambda-tau (CIBLT) for analyzing the behavior of the
complex repairable industrial systems by utilizing vague,
imprecise and uncertain data. The proposed methodology
involves qualitative modeling using PN and quantitative
analysis using lambda-tau method of solution with basic
events represented by fuzzy numbers of triangular mem-
bership functions through statistical estimation technique
and data records. To strengthen the analysis various reli-
ability indices such as system’s failure rate, repair time,
MTBF etc. are computed in the form of fuzzy membership
functions. Results obtained from CIBLT technique are
compared with the fuzzy lambda-tau (FLT) results. The
obtained results will help the management for reallocating
the resources to achieve the targeted goals of higher profit.
The synthesis unit of the urea fertilizer plant, situated in the
Northern part of India, producing approximately
1,500–2,000 metric tons of urea per day has been taken to
demonstrate the approach.
Basic Concepts of Fuzzy Set Theory
Zadeh [3] first introduced the fuzzy set theory and gener-
alize the mathematical concepts of the set to the fuzzy set.
He then theorized that if the available information is such
that the uncertain value can be located inside a closed
interval, which he called interval of confidence, then a
membership function that maps each element of the
interval of confidence to a value in the interval [0,1] can be
defined. In classical set theory, an element x in a universe
U is either a member of some crisp set A or not. This binary
issue of membership can be represented mathematically by
the characteristic function
vAðxÞ ¼1 if x 2 A
0 if x 62 A
�ð1Þ
Zadeh [3] extended the notion of binary membership to
accommodate various degrees of membership on the real
continuous interval [0,1]. The fuzzy set eA in the universe of
discourse U can be defined as a set of ordered pairs and is
given by,
eA ¼ fðx; leAðxÞÞ : x 2 Ug ð2Þ
where leAðxÞ is the degree of membership of element x in
fuzzy set eA and its value is given as leA 2 ½0; 1�.A fuzzy set eA in universe U is convex if and only if
membership functions of leAðxÞ of eA is fuzzy-convex i.e.
360 H. Garg
123
leAðkx1 þ ð1� kÞx2Þ� minðleAðx1Þ; leAðx2ÞÞ8x1; x2 2 U; 0� k� 1
ð3Þ
and is said to be normal if there exist at least one points
x 2 U such that leAðxÞ ¼ 1. A fuzzy subset eA ¼fðx; leAðxÞÞ j x 2 Rg of the real line R is called fuzzy
number if eA is convex, normal and bounded.
a-Cut
An a-cut of a fuzzy set eA is a crisp set which consists of
elements of eA having at least degree a. It is denoted by AðaÞ
and is defined mathematically as
AðaÞ ¼ fx 2 U : leAðxÞ� ag ð4Þ
where a is the parameter in the range 0� a� 1. The
concept of a-cut offers a method for resolving any fuzzy
sets in terms of constituent crisp sets. Every a-cut of a
fuzzy number is a closed interval and a family of such
intervals describes completely a fuzzy number under study.
Hence we have AðaÞ ¼ ½AðaÞL ;AðaÞU � where
AðaÞL ðaÞ ¼ inffx 2 R j leAðxÞ > ag
AðaÞU ðaÞ ¼ supfx 2 R j leAðxÞ > ag
Membership Functions and Interval Arithmetic
Membership function defines the fuzziness in a fuzzy set
irrespective of the elements in the set, which are discrete or
continuous. For a fuzzy set eA a membership function,
denoted by leAð�Þ maps U to the subset of the non-negative
real numbers [0, 1] i.e. leA : U ! ½0; 1�. Many membership
functions such as normal, triangular, trapezoidal can be
used to represent fuzzy numbers. However, triangular
membership functions (TMF) are widely used for calcu-
lating and interpreting reliability data because of their
simplicity and understandability [20, 16, 21].
A triangular fuzzy number (TFN) is defined by the
ordered triplet eA ¼ ða; b; cÞ representing, respectively, the
lower value, the modal value, and the upper value of a
triangular fuzzy membership function. Its membership
function l ~A : R �! ½0; 1�; is defined as:
leAðxÞ ¼x�ab�a
; a� x� b
1; x ¼ bc�xc�b
; b� x� c
0; otherwise
8>>><>>>:
ð5Þ
and their corresponding a-cut is defined as
AðaÞ ¼ ½aðaÞ; cðaÞ� ¼ ½ðb� aÞaþ a; c� aðc� bÞ� ð6Þ
The two-sided 100(1� c)% confidence interval for the a-
cut of the fuzzy set ~A is
AðaÞ ¼�
aþ aðb� aÞ � rffiffiffikp tk�1
c2
� �;
c� aðc� bÞ þ rffiffiffikp tk�1
c2
� �� ð7Þ
where r be estimation of the population standard deviation
of b. Let T be a t distributed random variable with k � 1
degree of freedom then tk�1ðc2Þ satisfies
P T � tk�1
c2
� �� �¼ c
2ð8Þ
The basic arithmetic operations, i.e., addition, subtraction,
multiplication and division, of fuzzy numbers depends
upon the arithmetic of the interval of confidence. The four
main arithmetic operation on two triangular fuzzy sets eA ¼\ða1; b1; c1Þ[ and eB ¼\ða2; b2; c2Þ[ described by
the a-cuts are given below for the following intervals:
AðaÞ ¼ ½AðaÞ1 ;AðaÞ3 � and BðaÞ ¼ ½BðaÞ1 ;B
ðaÞ3 �; a 2 ½0; 1�
(i) Addition : ~Aþ ~B ¼ ½AðaÞ1 þ BðaÞ1 ;A
ðaÞ3 þ B
ðaÞ3 �
(ii) Subtraction : ~A� ~B ¼ ½AðaÞ1 � BðaÞ3 ;A
ðaÞ3 � B
ðaÞ1 �
(iii) Multiplication : ~A � ~B ¼ ½PðaÞ;QðaÞ�where PðaÞ ¼ minðAðaÞ1 � B
ðaÞ1 ;A
ðaÞ1 � B
ðaÞ3 ;A
ðaÞ3 � B
ðaÞ1 ;
AðaÞ3 � B
ðaÞ3 Þ
and QðaÞ ¼ maxðAðaÞ1 � BðaÞ1 ;A
ðaÞ1 � B
ðaÞ3 ;A
ðaÞ3 � B
ðaÞ1 ;
AðaÞ3 � B
ðaÞ3 Þ
(iv) Division : ~A� ~B ¼ ~A � 1~B
if 0 62 ~B
It is clear that the multiplication and division of two TFNs
is not again a TFN with linear sides but it is a new fuzzy
number with parabolic sides.
Confidence Interval Based Lambda-Tau Methodology
Lambda-tau methodology is a traditional method in which
fault tree is used to model the system. The constant failure
rate model is adopted in this method and the basic
expressions used to evaluate the system’s failure rate ðkÞand repair time (s) associated with the logical AND-gates
and OR-gates are summarized in Table 1.
Knezevic and Odoom [18] and Garg [22] extended this
idea by coupling it with PN and fuzzy and vague set theory
respectively. But they did not find the estimation of reli-
ability of the system using statistical confidence interval.
Keeping this in mind, Jamkhaneh et al. [14] has analyzed
the fuzzy system reliability, for non-repairable system,
using the statistical confidence interval for estimation of
reliability. But any reliability index alone is inadequate to
give a deeper idea about such type of systems’ behavior
because a lot of factors exist which overall influence the
systems’ performance and consequently their behavior. To
overcome this, the present paper presented a methodology,
named as confidence interval based lambda-tau (CIBLT)
for analyzing the behavior of a repairable system. The
Analyzing the Behavior of an Industrial System 361
123
constant failure rate model is adopted in this technique
because most of the technical systems exhibit constant
failure and repair rates (i.e. exponentially distributed) after
initial burn-in-period in bathtub curve.
The basic assumptions used in this methodology are:
– Component failures and repair rates are statistically
independent, constant, very small and obey exponential
distribution function;
– After repairs, the repaired component is considered as
good as new;
– There are no simultaneous failures among the
subsystems.
– Separate maintenance facility is available for each com-
ponent. The repair process begins soon after a unit fails.
The details of the methodology are given as below:
The technique starts from the information extraction
phase in which data related to various components of the
systems are collected from the various resources in the
form of their failure rate (ki) and repair time (si). As mostly
the collected data are imprecise in nature due to various
constraints and hence fuzzy set theory has been used for
handling the uncertainties in the data. For more specfically,
triangular fuzzy numbers with equal spread, say �15 %, in
both the directions (left and right to the middle) are used
for converting the crisp data into fuzzy numbers and are
shown in Fig. 1 where, ~ki is a fuzzy failure rate and ~si is a
fuzzy repair time of ith component in the form of triangular
fuzzy numbers.
As soon as TFNs corresponding to each of the compo-
nents are known, the corresponding fuzzy value for the top
place (system fails) can be obtained using the extension
principle coupled with a-cut and interval arithmetic oper-
ations on triangular fuzzy numbers. The interval expression
for the triangular fuzzy number, for the failure rate ~k and
repair time ~s, for AND/OR-transitions are as follows:
Expressions for AND-Transitions
kðaÞ ¼Yn
i¼1
ðki2 � ki1Þaþ ki1 �riffiffiffi
kp tk�1
c2
� �� ��
"
Xn
j¼1
Yi¼1i6¼j
n
ðsi2 � si1Þaþ si1 �riffiffiffi
kp tk�1
c2
� �� �2664
3775;
Yn
i¼1
�ðki3 � ki2Þaþ ki3 þriffiffiffi
kp tk�1
c2
� �� ��
Xn
j¼1
Yi¼1i6¼j
n
�ðsi3 � si2Þaþ si3 þriffiffiffi
kp tk�1
c2
� �� �2664
37753775 ð9Þ
sðaÞ ¼
Qni¼1
ðsi2 � si1Þaþ si1 � riffiffikp tk�1
c2
n o
Pnj¼1
Qi¼1i 6¼j
n
�ðsi3 � si2Þaþ si3 þ riffiffikp tk�1
c2
n o264
375;
2666666664
Qni¼1
�ðsi3 � si2Þaþ si3 þ riffiffikp tk�1
c2
n o
Pnj¼1
Qi¼1i 6¼j
n
ðsi2 � si1Þaþ si1 � riffiffikp tk�1
c2
n o264
375
3777777775
ð10Þ
1 1
(a) Triangular Membership functions of (b) Triangular Membership functions of
Fig. 1 Input triangular fuzzy
number for the ith component of
the system
Table 1 Basic expressions of lambda tau methodology
Gate kAND sAND kOR sOR
Expression
Qnj¼1
kj
Pni¼1
Qj¼1
i 6¼j
n
sj
2664
3775
Qni¼1
si
Pn
j¼1
Qi¼1i 6¼j
n
si
24
35
Pni¼1
ki
Pn
i¼1
kisi
Pn
i¼1
ki
362 H. Garg
123
Expressions for OR-Transitions
kðaÞ ¼Xn
i¼1
ki1 þ aðki2 � ki1Þ �riffiffiffi
kp tk�1
c2
� �� �;
"
Xn
i¼1
ki3 � aðki3 � ki2Þ þriffiffiffi
kp tk�1
c2
� �� �# ð11Þ
By using these systems expression (9)–(12), the reli-
ability parameters are analyzed, with left and right spreads,
at various degrees of membership functions with the
increment of 0.1 confidence level a. The expression of
these reliability parameters is summarized in Table 2. As
the obtained results are fuzzy in nature but the decision
maker or system analyst always wants a crisp or binary
nature value for implementing it into their system. In this
center of gravity [23] has been used for defuzzification due
to the property of their equivalent to the mean of the data.
Mathematically centroid or center of gravity (COG)
method is represented as an Eq (13)
�x ¼R
xx � l ~BðxÞdxRxl ~BðxÞdx
ð13Þ
where eB is the output fuzzy set, and l ~B is the membership
function.
Illustrative Example
To illustrate, a fertilizer plant situated in the northern
part of India and producing approximately 1,500–2,000
metric tons per day has been considered as a main sys-
tem [24]. The fertilizer plant is large, complex and
repairable engineering unit which is a combination of
two dependent systems namely ammonia production
system and the urea production system. The urea plant is
composed of synthesis, decomposition, crystallization and
prilling system, arranged in predetermined configuration.
Among these, urea synthesis is one of the most important
and vital functional processes which is the subject of our
discussion. The process of the system is briefly described
below.
System Description
In this process, an ammonia production plant releases
carbon dioxide gas (CO2) as a by-product which is pumped
through a CO2 booster compressor and a CO2 high-pres-
sure compressor to the synthesis reactor after getting it
passed through a methanol absorber. Liquid ammonia from
the first tank (raised to 250 atm pressure by two liquid
ammonia feed pumps arranged in parallel) is passed
through two ammonia preheaters (arranged in series) to
raise its temperature to 82:3 C then it is fed into the urea
synthesis reactor, maintained at 190 C and 250 atm. In
addition to this about 40 %, ammonium carbonate (con-
sisting of a CO2; NH3; CO2, Biuret mixture) recovered
from the recovery section is fed into the urea synthesis
reactor through a multistage centrifugal pump. This allows
CO2 and ammonia to react at 190 C and 250 atm in the
synthesis reactor to form urea. Naturally the failure of any
intermediate equipment in this process will stop the for-
mulation of the urea. So the behavior analysis of each part
of the equipment is necessary for the design modification
for the system.
In brief, the various subsystems and the components
associated with them are defined as below [24]:
– Subsystem 1 has one unit CO2 booster compressor (A),
a centrifugal type pump, which raise the pressure of
Table 2 Some reliability prarameters
Parameters Expressions
Mean time to failure MTTFs ¼ 1ks
Mean time to repair MTTRs ¼ 1ls¼ ss
ENOF Wsð0; tÞ ¼ ksls tksþls
þ k2s
ðksþlsÞ2½1� e�ðksþlsÞt�
MTBF MTBFs ¼ MTTFs þMTTRs
Reliability Rs ¼ e�ks t
Availability As ¼ ls
ksþlsþ ks
ksþlse�ðksþlsÞt
sðaÞ ¼
Pni¼1
ðki2 � ki1Þaþ ki1 � riffiffikp tk�1
c2
n o� ðsi2 � si1Þaþ si1 � riffiffi
kp tk�1
c2
n oh iPni¼1
�ðki3 � ki2Þaþ ki3 þ riffiffikp tk�1
c2
n o ;
2664
Pni¼1
�ðki3 � ki2Þaþ ki3 þ riffiffikp tk�1
c2
n o� �ðsi3 � si2Þaþ si3 þ riffiffi
kp tk�1
c2
n oh iPni¼1
ðki2 � ki1Þaþ ki1 � riffiffikp tk�1
c2
n o3775
ð12Þ
Analyzing the Behavior of an Industrial System 363
123
CO2 from 0.1 to 29.5 atm. Its failure causes complete
failure of the system.
– Subsystem 2 has one unit CO2 high-pressure compres-
sor (B), a reciprocating type pump, which raises the
pressure of CO2 from 29.5 to 250 atm. Its failure causes
complete failure of the system.
– Subsystem 3 contains the liquid ammonia feed pumps
(E) which are of reciprocating type that raise the
ammonia pressure from 16.5 to 250 atm. Two pumps
are in operation simultaneously and two remain in cold
standby. The system fails when three pumps fail.
– Subsystem 4 has two ammonia pre-heaters (D)
arranged in series. The first one raises the temperature
of gas up to 53:2 C and the second heat the gas to
82:3 C. Failure of either causes complete failure of the
system.
– Subsystem 5 has the recycle isolution feed pump (F), a
multistage centrifugal pump, to raise the pressure of
ammonia carbonate from 17 to 250 atm. It has one unit
in standby. The system fails only when both units fail.
The schematic diagram and the Petri Net model of this
system are shown in Fig. 2, where ‘‘top’’ in Fig. 2b
represents the system failure of the synthesis unit (Fig. 2).
Behavior Analysis
The procedural steps used for conducting the analysis by
using CIBLT technique are given as below.
Step 1: Under the information extraction phase, the data
related to failure rates (k’s) and repair times (s’s)
of the main components of the system are
collected from the historical/present records such
as historical records, reliability databases, system
reliability expert opinion etc and is integrated
with expertise of maintenance personnel as
presented in Table 3 [24].
Step 2: Since the extracted database on which reliability
analysis depends is either out of date or collected
under different operations and environmental
conditions and hence contains an imprecise or
uncertain data. So to handle these impreciseness
or vagueness, the obtained/collected data are
fuzzified into the triangular fuzzy numbers with
some known spread �15; �25 and �50 % as
suggested by the decision makers/system analyst
and two-sided significance level of confidence
interval is 95 %. After obtaining the fuzzified
data of the basic events of the system, the top
place event of the system is obtained by using the
extension principle coupled with the a-cuts along
with the interval expression of the system failure
rate and repair times as given in equation (9)–
(12) respectively for their membership functions.
Step 3: Based on their PN model, the top event of the
system failure events based on the basic events
are calculated by using the expressions of the
systems’ failure rate (ks) and repair time (ss)
listed in Table 1. Using these expressions of ks
and ss, various reliability parameters for the
mission time t = 10(h) with left and right spread,
for each level (a-level), ranging from 0.1 to 1,
with increments of 0.1, are obtained and shown
graphically in Fig. 3 for �15; �25 and �50 %spreads along with FLT results. From the Fig. 3,
it has been concluded that the membership
values, of the various reliability indices, obtained
by using the traditional (crisp) methodology are
CO2 BoosterCompressor
A
MethanolAbsorber
CO2Compressor
B
deefnoitulosIpump
F
LiquidAmmonia Feed
pumpsE
1 2
CO2fromtank
Mixture (urea + NH 3 + CO2 H+ 2 +teriuB+OCH3 )HO to Decomposer
Required AmmoniaCarbonate
NH3fromtank
Preheaters (D)
Secondary process
Main Process
A B
SS3
SS1
SS2
SS4 SS
5
F1
F2
Top
E2
E1
E3
E4
D1
D2
Fig. 2 a Systematic diagram and b Petri net model of the synthesis unit
364 H. Garg
123
Table 3 Data for failure rate and repair time
Subsystems (SS) ! A B E D F
Failure rate (ki 10�3)(h�1) 3.8730 5.3950 2.7590 4.4750 6.6910
ri (10�4) 4.7539 6.9386 3.1886 4.9943 7.7710
Repair time (si)(h) 4.5640 2.8380 4.7360 3.7270 4.3840
ri 0.4888 0.3469 0.5109 0.3869 0.4936
0.016 0.018 0.02 0.0220
0.2
0.4
0.6
0.8
1
Failure rate (hrs−1)
Deg
ree
of m
embe
rshi
pFuzzy failure rate
CIBLTFLTCrisp
(a)
1.5 2.2 2.9 3.6 4.3 5 5.7 6.40
0.2
0.4
0.6
0.8
1
Repair time (hrs)
Deg
ree
of m
embe
rshi
p
Fuzzy repair time
CIBLTFLTCrisp
(b)
43 48 53 58 63 68 730
0.2
0.4
0.6
0.8
1
MTBF (hrs)
Deg
ree
of m
embe
rshi
p
Fuzzy Mean Time Between Failures
CIBLTFLTCrisp
(c)
0.14 0.16 0.18 0.2 0.220
0.2
0.4
0.6
0.8
1
ENOF
Deg
ree
of m
embe
rshi
pFuzzy Expected Number of Failures
CIBLTFLTCrisp
(d)
0.8 0.81 0.82 0.83 0.84 0.85 0.860
0.2
0.4
0.6
0.8
1
Reliability
Deg
ree
of m
embe
rshi
p
Fuzzy Reliability
CIBLTFLTCrisp
(e)
0.9 0.92 0.94 0.960
0.2
0.4
0.6
0.8
1
Availability
Deg
ree
of m
embe
rshi
p
Fuzzy Availability
CIBLTFLTCrisp
(f)
Fig. 3 Various reliability plots
of the system at �15 % spread
along with FLT results
Analyzing the Behavior of an Industrial System 365
123
constant at all values of a. It means that they do
not consider the uncertainties in the data. Thus
the method is suitable only for a system whose
data are precise. On the other hand, results
proposed by the proposed technique have
reduced region and smaller spread than the FLT
results. This suggests that DM have smaller and
more sensitive region to make more sound and
effective decision in lesser time. Based on the
results shown in Fig. 3, decrease in the spread
from FLT to CIBLT results have been computed
and tabulated in Table 4. It shows that the largest
and the smallest decrease in spread occurs
corresponding to MTBF and ENOF, respectively
which means that the prediction range of reli-
ability indices decreased. The maintenance engi-
neer/expert may use this information to get
higher system reliability and/or availability to
achieve the goals of maximum profit.
Step 4: In order to take a decision related to these plots, it
is essential that resultant output should be in crisp
form. Thus defuzzification is essential for the
system analyst and hence the center of gravity
method [23] is used because it has the advantage
of being taken the whole membership function
into account for this transformation. From Fig. 3,
it is clear that sides of membership functions of
reliability parameters are parabolic, not linear as
were taken initially. The crisp and defuzzified
values for various reliability parameters at
�15; �25 and �50 % spreads are calculated
and depicted in Table 5, which reflects that the
crisp values do not change irrespective of the
spread chosen. However, defuzzified values of
various reliability parameters change with change
of spreads. From these results it has been clearly
shown that the results given by the proposed
technique acts as a bridge between the FLT and
Markovian (crisp) results. Also it has been
observed from Table 5 that when uncertainty
levels in the form of spread increases, defuzzified
values of reliability indices have almost the same
trend (increase or decrease) as shown by lambda-
tau. This suggests that values obtained through
proposed approach are conservative in nature,
which may be beneficial for plant personnel and
have some idea about the behavior of the system.
Sensitivity Analysis
To analyze the impact of change in values of reliability
indices on the system’s behavior, behavioral plots have
been plotted for different combination of reliability,
availability and failure rate and the effects on MTBF are
Table 5 Defuzzified values of reliability parameters at different spreads
Spread (%) Method Reliability parameters at different spreads
Failure rate Repair time MTBF ENOF Reliability Availability
�0 Crisp 0.01889894 3.59212763 56.50513321 0.180809689 0.827795237 0.939680436
FLT 0.01892200 3.78455030 57.33118301 0.180763669 0.827796316 0.936292670
�15 CIBLT 0.01893238 3.68203939 56.76929755 0.180994924 0.827593279 0.938108116
FLT 0.01896301 4.15293800 58.88753679 0.180684419 0.827799104 0.929824443
�25 CIBLT 0.01899705 4.02558685 57.87044233 0.181148284 0.827316521 0.932413998
FLT 0.01915550 6.51000963 68.17447552 0.180483438 0.827827024 0.892024500
�50 CIBLT 0.01941744 12.3448105 69.89778872 0.180140644 0.825407465 0.859895864
Table 4 Data related to spread of reliability indices
Failure rate Repair time MTBF ENOF Reliability Availability
Spread related to reliability parameters
I 0.00608284 3.53943475 20.93593113 0.06773362 0.05033814 0.06726437
II 0.00368437 2.13131996 12.50205931 0.04103464 0.03048880 0.04056775
Decrease in spread from I to II
39.43010172 39.78360640 40.28419738 39.41761860 39.43200921 39.68909543
I: FLT II: CIBLT
366 H. Garg
123
computed and are shown in Fig. 4. Throughout the nine
combinations, ranges of repair time and ENOF are fixed
and computed by their membership functions (Fig. 3b, d)
at cut levels a ¼ 0 i.e. repair time are varied from 2.207237
to 5.746671 and 2.672436 to 4.803756 for FLT and CIBLT
techniques respectively. Similarly the computed range of
ENOF varies from 0.146851 to 0.214585 and 0.160455 to
0.201489 for respective techniques. The computed range of
MTBF for all combinations as well as of both techniques
are tabulated in Table 6. For instance, for the first
combination of Table 6, the selected value of reliability
and availability are 0.7854 and 0.9189 respectively while
the failure rate are changes from 1:4561 10�2 to
1:8898 10�2 and further to 2:5489 10�2. In this com-
bination, the computed range of MTBF is
78.144635–116.142677 and 83.410683–105.819301 for
FLT and CIBLT respectively. It may be observed that for
this combination the predicted range of MTBF is reduced
almost by 41.027 % from fuzzy lambda-tau when CIBLT
technique is applied. This observation infers that if system
2.2
3.6
50.16
0.19
0.2280
95
110
Repair time
Reliability = 0.7854, Failure rate = 0.014561,
Availability = 0.9189
ENOF
MT
BF
(a)
2.2
3.6
50.16
0.19
0.2260
72.5
85
Repair time
Reliability = 0.7854, Failure rate = 0.018898,
Availability = 0.9189
ENOF
MT
BF
(b)
2.2
3.6
50.16
0.19
0.2245
54
63
Repair time
Reliability = 0.7854, Failure rate = 0.025489,
Availability = 0.9189
ENOF
MT
BF
(c)
2.2
3.6
50.16
0.19
0.2265
75
85
Repair time
Reliability = 0.8276, Failure rate = 0.014561,
Availability = 0.9396
ENOF
MT
BF
(d)
2.2
3.6
50.16
0.19
0.2250
57.5
65
Repair time
Reliability = 0.8276, Failure rate = 0.018898,
Availability = 0.9396
ENOF
MT
BF
(e)
2.2
3.6
50.16
0.19
0.2235
42.5
50
Repair time
Reliability = 0.8276, Failure rate = 0.025489,
Availability = 0.9396
ENOF
MT
BF
(f)
2.2
3.6
50.16
0.19
0.2245
55
65
Repair time
Reliability = 0.865, Failure rate = 0.014561,
Availability = 0.9585
ENOF
MT
BF
(g)
2.2
3.6
50.16
0.19
0.2235
42.5
50
Repair time
Reliability = 0.865, Failure rate = 0.018898,
Availability = 0.9585
ENOF
MT
BF
(h)
2.2
3.6
50.16
0.19
0.2226
32
38
Repair time
Reliability = 0.865, Failure rate = 0.025489,
Availability = 0.9585
ENOF
MT
BF
(i)
Fig. 4 Behavior of MTBF for different combinations of reliability parameters
Analyzing the Behavior of an Industrial System 367
123
analysts use CIBLT results, then they may have less range
of prediction which finally leads to more sound decisions.
Similar kind of reductions have been notified for other
combinations too. Thus, based on the behavioral and sen-
sitivity analysis plots and corresponding tables, the system
manager can analyze the critical behavior of the system
and plan for suitable maintenance.
Performance Analysis
As the performance of the system directly depends on each
of the constituent components. So to increase the perfor-
mance of the system, more attention should be given to
their corresponding subsystem for the effectiveness of the
maintenance program. In order to find the most critical
component, as per preferential order, of the system, an
investigation has been done on system availability by
varying their failure rate and repair time simultaneously
and fixing the failure rate and repair time of other com-
ponents’ at the same time. The results thus obtained are
shown graphically in Fig. 5 which contains five subplots
corresponding to five main components of the system.
It has been observed from Fig. 5a that the variation in
the failure rate and repair time of the booster compressor
component shows the significant impact on the availability
of the system i.e. an increase in their failure rate from
2:90475 10�3 to 4:84125 10�3 and repair time from
3.4230 to 5.7050 reduce the system availability up to 3.465
percent. The variation in the failure rate (5:01825 10�3
to 8:36375 10�3) and repair time (3.288–5.480) of the
isolution feed pump component have a large effect on
system availability (up to 7.616 %) as shown in Fig. 5e.
Similar effect on the system availability by the variation of
the other component failure rates and repair times are
analyzed from the Fig. 5. The magnitude of the effect of
variation in failure rates and repair times of various sub-
systems of the system on its performance is summarized in
Table 7. From the results, it can be analyzed that for
improving the performance of the system, more attention
should be given to the components as per the preferential
order; isolution feed pump, booster compressor, pre-heat-
ers, high-pressure compressor and feed pumps.
Conclusion
The paper presents the methodology named as confidence
interval based lambda-tau (CIBLT) for analyzing the
behavior of the complex repairable industrial systems by
utilizing uncertain data. Major advantages of the proposed
technique are that it uses the fuzzy confidence interval for
estimating the uncertainties in the data by using triangular
fuzzy numbers. The technique has been demonstrated
through a case study of synthesis unit of a fertilizer plant
Table 6 Effect of various parameters on system MTBF
S. no. [Reliability, failure rate, availability] Mean time between failures
FLT CIBLT
Fig. 4a [0:7854; 1:4561 10�2; 0:9189] Min: 78.144635 83.410683
Max: 116.142677 105.819301
Fig. 4b [0:7854; 1:8898 10�2; 0:9189] Min: 60.402263 64.515192
Max: 90.216829 82.091494
Fig. 4c [0:7854; 2:5489 10�2; 0:9189] Min: 44.999026 48.110862
Max: 67.709018 61.491937
Fig. 4d [0:8276; 1:4561 10�2; 0:9396] Min: 61.181650 65.297441
Max: 90.856786 82.798839
Fig. 4e [0:8276; 1:8898 10�2; 0:9396] Min: 47.283336 50.495843
Max: 70.548028 64.211894
Fig. 4f [0:8276; 2:5489 10�2; 0:9396] Min: 35.217362 37.645673
Max: 52.916754 48.075433
Fig. 4g [0:8650; 1:4561 10�2; 0:9585] Min: 46.841453 49.981605
Max: 69.446801 63.315097
Fig. 4h [0:8650; 1:8898 10�2; 0:9585] Min: 36.189531 38.637388
Max: 53.881794 49.069721
Fig. 4i [0:8650; 2:5489 10�2; 0:9585] Min: 26.941946 28.788781
Max: 40.368863 36.702441
368 H. Garg
123
Table 7 Effect of varying failure rate and repair time on system availability
Components Range of failure rate Range of repair time System availability
(10�3 per hours) (h) Min Max
A: Booster compressor 2.90475–4.84125 3.4230–5.7050 0.93939503 0.97195047
B: High-pressure compressor 4.04625–6.74375 2.1285–3.5475 0.94157098 0.97465331
E: Feed pumps 2.06925–3.44875 3.5520–5.9200 0.95084559 0.97935308
D: Pre-heaters 3.35625–5.59375 2.7952–4.6587 0.93954719 0.97287215
F: Isolution feed pump 5.01825–8.36375 3.2880–5.4800 0.88594676 0.95341870
3
4.5
6
2.5
3.7
4.9
x 10−3
0.93
0.9525
0.975
Repair Time
Booster compressor
Failure rate
Ava
ilabi
lity
(a)
2
3
4
4
5.5
7
x 10−3
0.93
0.955
0.98
Repair Time
High−pressure compressor
Failure rate
Ava
ilabi
lity
(b)
3.4
4.7
6
2
2.75
3.5
x 10−3
0.945
0.9675
0.99
Repair Time
Feed pumps
Failure rate
Ava
ilabi
lity
(c)
2.5
3.7
4.9
3
4.3
5.6
x 10−3
0.93
0.955
0.98
Repair Time
Pre−heaters
Failure rateA
vaila
bilit
y
(d)
3.2
4.4
5.6
5
7
9
x 10−3
0.88
0.93
0.98
Repair Time
Isolution feed pump
Failure rate
Ava
ilabi
lity
(e)
Fig. 5 Effect on system
availability when failure rate
and repair time vary for a
particular component and fixing
these for remaining components
Analyzing the Behavior of an Industrial System 369
123
situated in the northern part of India, a complex repairable
industrial system. Various reliability parameters of the
system have been computed in terms of fuzzy membership
functions. The computed results are compared with the
existing FLT technique and concluded that the proposed
technique has less range of uncertainty which indicates that
they have a higher sensitivity zone and thus may be useful
for the reliability engineers/experts to make more sound
decisions. The sensitivity analysis has also been performed
to explore the effect of failure/repair rates of the units on
system performance. It is concluded that in order to
improve the availability and reliability aspects, it is nec-
essary to enhance the maintainability requirement of the
system. Thus, it will facilitate the management in reallo-
cating the resources, making maintenance decisions,
achieving long run availability of the system, and
enhancing the overall productivity of the industry. From
the results, it has been analyzed that maintenance should be
given as per the preferential order; isolution feed pump,
booster compressor, pre-heaters, high-pressure compressor
and feed pumps for improving the performance and hence
increasing the productivity of the system.
In nutshell, the important managerial implications
drawn using the discussed techniques are to:
– Predict the behavior of systems in more consistent
manner and in higher sensitivity zone;
– Analyze failure behavior of industrial systems in more
realistic manner as they often make use of imprecise
data;
– Determine reliability indices such as MTBF, MTTR
which are important for planning the maintenance need
of the systems; and
– Plan suitable maintenance strategies to improve system
performance and to reduce operation and maintenance
costs.
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