Performance evaluation and optimization for urea crystallization system in a fertilizer plant using genetic algorithm technique.
Kumar, Sanjeev ; Tewari, P.C. ; Kumar, Sunand 等
Introduction
Over the years as engineering systems have become more complex and
sophisticated, the performance evaluation and optimization of
engineering systems is becoming increasingly important because of
factors such as cost, risk of hazard, competition, public demand, usage
of new technology. High reliability level is desirable to reduce overall
costs of production and risk of hazards for larger, more complex and
sophisticated systems such as fertilizer plant. During the last three
decades reliability technology has been developed for use in various
technological fields. The technology is mainly used in the development
of electrical and electronics equipments. The technology has also been
used in a number of industrial and transportation problems.
A fertilizer plant is a complex engineering system comprising of
various systems: urea synthesis, urea crystallization, urea
decomposition and urea prilling etc. [3, 4]. The optimization of each
system in relation to one another is imperative to make the plant
profitable and viable for operation. Effectiveness of fertilizer plant
is mainly influenced by the availability, reliability and
maintainability of the plant, and its capability to perform as expected.
Reliability analysis techniques have been gradually accepted as standard
tools for the planning and operation of automatic and complex fertilizer
plants.
The maintenance of repairable systems has been widely studied by
many authors, considering different focus of interest, such as the
repair/replacement policy, periodic inspections, degrading, optimization
problems, among other topics. Reliability analysis is one of the main
tools to ensure agreed delivery deadlines which in turn maintain certain
intangible factors such as customer goodwill and company reputation [1].
Downtime often leads to both tangible and intangible losses. These
losses may be due to some unreliable subsystems/components, thus an
effective strategy for maintenance, replacement and design changes
related to those subsystems and component needs to be framed out [2,4].
The equipment that fails very frequently can be said to have very
low reliability and the equipment that takes very long time to be
replaced or repaired, can be said to have very low maintainability. Both
are critical and result in low availability. Availability predictive
modeling can provide insight in these cases by identifying exactly those
equipments that are critical for availability. With a predictive model
experiments can be made with different maintenance strategies and their
influence on reliability and maintainability [5]. From an economic point
of view, high reliability is desirable to reduce the maintenance costs
of systems [6]. Since failure cannot be prevented entirely, it is
important to minimize both its probability of occurrence and the impact
of failures when they do occur. To maintain the designed reliability,
availability and maintainability characteristics and to achieve expected
performance, an effective maintenance program is a must and the
effective maintenance is characterized by low maintenance cost [7]. The
type of component failure and its frequency has a direct effect on the
system's reliability. Thus it becomes very important to locate the
critical components and analyze their reliability. Furthermore, in many
situations it is easier and less expensive to test components/subsystems
rather than entire system [8]. Availability and reliability are good
evaluations of a system's performance [9].
For the prediction of availability or performance of systems,
several mathematical models have been discussed in literature, which
handle wide degree of complexities [10]. Most of these models [11, 12,
13] are based on the Markovian approach, wherein the failure and the
repair rates are assumed to be constant. In other words, the times to
failure and the times to repair follow exponential distribution. The
behaviour of complex systems can be studied in terms of their
reliability, availability and maintainability (RAM). For example, Kurien
[14] developed a predictive model for analyzing the reliability and
availability of an aircraft training facility. The model was useful for
evaluating various maintenance alternatives.
Factors that affect RAM of a repairable system include machinery
operating conditions, maintenance and infra-structural facilities.
Reliability analysis has helped in identifying the critical and
sensitive subsystems in the electricity production system, which has a
major effect on system failure. Therefore, a focus on reliability is
critical for the improvement of equipment performance and ensuring that
equipment is available for production as per production schedules [15].
Nowadays, reliability analysis has become an integral part of
system design. This is especially true for systems performing critical
applications. System designers rely on commercially available
dependability tools in order to assess the reliability of their systems.
The usage of such tools becomes therefore crucial. Systems being built
are increasingly complex and large; their components are exhibiting
behaviors and interactions that are becoming more and more difficult to
model and analyze using existing conventional tools. Markov Chains (MCs)
and their extensions have proven to be a versatile tool for modeling
complex dynamic component behavior. They have been extensively used for
dependability analysis of dynamic systems and many tools have adopted,
directly or indirectly, MCs as their formalism [16]. During the past
decade a lot of study [17, 18, 19] has been done by on analysis tools
for reliability, availability, performance modeling.
In the present article, performance of a critical urea
crystallization system in the fertilizer plant has been worked out using
a Markovian model. The need and the relevance for carrying out such a
study have been described in the script. The actual failure and repair
data on the identified urea crystallization system has been used in the
analysis.
For efficient functioning, it is essential that various systems of
the plant remain in upstate as far as possible. However, during
operation they are liable to fail in a random fashion. The failed
elements can however be inducted back into service after
repairs/replacements. The rate of failure of the components in the
system depends upon the operating conditions and repair policy used
[20].This paper discusses the performance evaluation and optimization of
urea crystallization system in a medium sized fertilizer plant.
System Description
The Urea Crystallization system comprises of four subsystems
arranged in series:
(i) Subsystem (A1) consists of two-stage ejector, barometric
condenser (used to generate the pressure of 175 mm of Hg), concentrator
(lower part) and crystallizer (upper part), all are arranged in series.
Failure of any one unit causes the complete failure of the system.
(ii) Subsystem (B) consists of five centrifugal pumps arranged in
series. Failure of any unit causes the complete failure of the system.
(iii) Subsystem (D) consists of two crystallizer pumps one in
operative and other in cold standby. Complete failure of the system will
occur only when both pumps fail at a time.
(iv) Subsystem (E) consists of two slurry feed pumps arranged in
parallel (one operative and other in cold standby). Complete failure of
the system will occur only when both pumps fail at a time.
Notations
The notations used to represent the various states of the
subsystems in the transition diagram of Urea Crystallization system
(figure 1) and system modeling, are as follows:
A, B, D, E : denotes that the subsystems are full operating state.
Ds, Es : denotes that the subsystems D and E are working on standby
unit.
A, b, c, d, e : denotes that the subsystems are in failed state.
[P.sub.0] (t) : Probability that at time t all subsystems are in
original working state (without standby unit).
[P.sub.i] (t) : Probability that at time t all subsystems are in
full load condition (standby mode) for i = 1-3.
[P.sub.j] (t) : Probability that at time t all subsystems are in
breakdown state for j = 4-15 [[alpha].sub.i], i = 1-5 : mean failure
rates in A, B, D, E.
[[beta].sub.i], i =1-5 : mean rate of repairs in A, B, D, E.
[DELTA]t : Time increment
d/dt : represents derivative w.r.t. 't'.
[circle] : System working at full load condition.
[rectangle] : System breakdown.
Assumptions
Modeling is carried out on the basis of following assumptions:
(1) Failure/repair rates are constant over time and statistically
independent.
(2) A repaired unit is good as new, performance wise for a
specified duration.
(3) Sufficient repair facilities are provided as and when required.
(4) Standby units are of the same nature as that of active units
[4, 5].
(5) System failure/repair follows exponential distribution.
(6) Service includes repair and/or replacement [9].
(7) System may work at reduced capacity.
(8) There are no simultaneous failures.
[FIGURE 1 OMITTED]
Mathematical Modeling
Mathematical modeling has been developed for the prediction of
steady state availability of the individual components as well as entire
system. The failure and repair rates of the different subsystems,
available from the maintenance sheets of the fertilizer plant, are used
as standard input information for the analysis. The state of the system
defines the condition at any instant of time and the information is
useful in analyzing the current state and in the prediction of the
failure state of the system. If the state of the system is probability
based, then the model is a Markov probability model. Markov model is
defined by a set of probabilities [P.sub.ij], where [P.sub.ij] is the
probability of transition from any state i to any state j. One of the
most important features of the Markov process is that the transition
probability [P.sub.ij] ; depends only on states i and j and is
completely independent of all past states except the last one, state i.
Let the probability of n occurrences in time t be denoted by
[P.sub.n](t), i.e.,
Probability(X = n, t) = [P.sub.n] (t) (n = 0, 1, 2 ...).
Then, [P.sub.0] (t) represent the probability of zero occurrences
in time t. The probability of zero occurrences in time (t + [DELTA]t) is
given by equation (1); i.e.
[P.sub.0] (t + [DELTA]t) = (1 - [beta]t), [P.sub.0](t) (1)
Similarly [P.sub.1] (t + [DELTA]t)) = ([alpha] + [DELTA]t).
[P.sub.0] (t) + (1 + [beta]. [DELTA]t). [P.sub.1] (t) (2)
The equation 2 shows the probability of one occurrence in time (t +
[DELTA]t) and is composed of two parts, namely, (a) probability of zero
occurrences in time t multiplied by the probability of one occurrence in
the interval [DELTA]t and (b) the probability of one occurrence in time
t multiplied by the probability of no occurrences in the interval
[DELTA]t [21]. Then simplifying and putting [DELTA]t [right arrow] 0,
one gets
(d/dt + [alpha]) [P.sub.1](t) = [beta] [P.sub.0](t) (3)
Using the concept used in equation 3 and various probability
considerations, the following differential equations associated with the
transition diagram of urea crystallization system are formed [26, 27,
28].
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.] (4)
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.] (5)
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.] (6)
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.] (7)
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.] (8)
Where in equation (8), for,
m=1, i = 4, 6, 9, 12, j = 0,1, 2, 3. m=2, i = 5, 7, 10, 13, j =
0,1,2,3 m=3, i = 8, 14, j = 1, 3 m=4, i = 11, 15, j = 2, 3
With the initial condition [P.sub.0] (0) =1, otherwise zero, since
any urea plant is a process industry where raw material is processed
through various subsystems continuously till the final product is
obtained [29, 30]. Thus, the long run availability of the urea
crystallization system of a fertilizer plant is attained by putting
derivatives of all probability functions equal to zero as:
t [right arrow] [infinity] d/dt = 0
into differential equations, one gets,
[P.sub.4] = ([[alpha].sub.1]/[[beta].sub.1])[P.sub.0] = (9)
[P.sub.5] = ([[alpha].sub.2]/[[beta].sub.2])[P.sub.0] = (10)
[P.sub.6] = ([[alpha].sub.1]/[[beta].sub.1])[P.sub.0] = (11)
[P.sub.7] = ([[alpha].sub.2]/[[beta].sub.2])[P.sub.1] = (12)
[P.sub.8] = ([[alpha].sub.3]/[[beta].sub.3])[P.sub.1] = (13)
[P.sub.9] = ([[alpha].sub.1]/[[beta].sub.1])[P.sub.1] = (14)
[P.sub.10] = ([[alpha].sub.1]/[[beta].sub.1])[P.sub.2] = (15)
[P.sub.11] = ([[alpha].sub.4]/[[beta].sub.4])[P.sub.2] = (16)
[P.sub.12] = ([[alpha].sub.1]/[[beta].sub.1])[P.sub.2] = (17)
[P.sub.13] = ([[alpha].sub.2]/[[beta].sub.2])[P.sub.3] = (18)
[P.sub.14] = ([[alpha].sub.3]/[[beta].sub.3])[P.sub.3] = (19)
[P.sub.15] = ([[alpha].sub.4]/[[beta].sub.4])[P.sub.3] = (20)
([[alpha].sub.3] + [[alpha].sub.4])[P.sub.0] =
[[beta].sub.3][P.sub.1] + [[beta].sub.4][P.sub.2] (21)
([[alpha].sub.4] + [[beta].sub.3])[P.sub.1] =
[[beta].sub.4][P.sub.3] + [[beta].sub.3][P.sub.0] (22)
([[alpha].sub.3] + [[beta].sub.4])[P.sub.2] =
[[beta].sub.3][P.sub.3] + [[beta].sub.4][P.sub.0] (23)
([[beta].sub.4] + [[beta].sub.4])[P.sub.3] =
[[beta].sub.4][P.sub.1] + [[alpha].sub.3][P.sub.2] (24)
Mathematical task is performed to solve the set of equations
(21)-(24) simultaneously in terms of 0 P as given by:
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.]
The probability of full working capacity, namely, [P.sub.0] is
determined by using normalizing condition: (i.e. sum of the
probabilities of all working states and failed states is equal to 1)
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.]
Now, the steady state availability of Urea Crystallization system
may be obtained as summation of all working state probabilities as:
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.]
Therefore, Availability of the system (Av.) represents the
performance evaluating system of Urea Crystallization system. This
performance-evaluating model includes all possible states of nature,
that is, future events ([[alpha].sub.i]) and the identification of all
the courses of action, that is, repair priorities ([[beta].sub.i]). This
model is used to implement the maintenance policies for a Urea
Crystallization system of a fertilizer plant. The various availability
levels may be computed for different combinations of failure and repair
rates / priorities. It can be used for performance optimization of this
operating system of a fertilizer plant by using Genetic Algorithm
Technique.
Genetic Algorithm Technique (G.A.T)
Genetic Algorithms (G.A.) are computerized search and optimization
algorithms based on the mechanics of natural genetics and natural
selection [32]. G. A.'s have become important because they are
found to be potential search and optimization techniques for complex
engineering optimization problems. The action of G.A.T. for parameter
optimization in the present problem can be stated as follows:
(1) Initialize the parameters of the G.A.T.
(2) Randomly generate the initial population and prepare the coded
strings.
(3) Compute the fitness of each individual in the old population.
(4) Form the mating pool from the old population.
(5) Divide the population repeatedly into random tournaments,
consisting of four population members per tournament.
(6) Copy the most fit population member in each tournament to the
mating pool.
(7) The process is repeated until the mating pool has the same size
as the population.
(8) Determine the new generation pool.
(9) Select two parents from the mating pool randomly.
(10) Perform the crossover of the parents to produce to produce two
off springs.
(11) Mutate, if required.
(12) Place the child strings to new population.
(13) Compute the fitness of each individual in new population.
(14) Replace the old population with the new population.
(15) Repeat the steps 3 to 8 until the best individuals in new
population represent the optimum value of the performance function
(system availability).
Performance Optimization using G.A.T.
The performance behavior of Urea Crystallization system is highly
influenced by the failure and repair parameters of each subsystem. These
parameters ensure high performance of the Urea Crystallization system.
G.A.T. is hereby proposed to coordinate the failure and repair
parameters of each subsystem for stable system performance i.e. high
availability. Here, number of parameters is eight (four failure
parameters and four repair parameters). The design procedure is
described as follows [32]:
To use G.A.T. for solving the given problem, the chromosomes are to
be coded in real structures. Here, concatenated, multi-parameter,
mapped, fixed point coding is used. Unlike, unsigned fixed point integer
coding parameters are mapped to a specified interval [[X.sub.min],
[X.sub.max]], where [X.sub.min] and [X.sub.max] are the maximum and
minimum values of system parameters. The maximum value of the
availability function corresponds to optimum values of system
parameters. These parameters are optimized according to the performance
index i.e. desired availability level. To test the proposed method,
failure and repair rates are determined simultaneously for optimal value
of system availability. Effects of population size and number of
generations on the availability of Urea Crystallization system are shown
in Table 1 and 2. To specify the computed simulation more precisely,
trial sets are also chosen for G.A. and system parameters. The
performance [availability] of Urea Crystallization system is determined
by using the designed values of the system parameters [32].
Failure and repair rate parameter constraints
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII.]
Here, real-coded structures are used.
Maximum number of Population size is varied from 20 to 160.
Number of Generations--100
Crossover probability--0.8
Mutation Probability--0.2
Total number of run--01
The effect of population size on availability of Urea
Crystallization system is shown in figure 2. The optimum value of
system's performance is 98.43 %, for which the best possible
combination of failure and repair rates is [[alpha].sub.1] = 0.0103,
[[beta].sub.1] = 0.9912, [[alpha].sub.2] = 0.0041, [[beta].sub.2] =
0.8811, [[alpha].sub.3] = 0.0206, [[beta].sub.3] = 0.6711,
[[alpha].sub.4] = 0.0013, [[beta].sub.4] = 0.3972, at population size
140, as given in table 1.
Maximum number of Generations is varied from 50 to 300.
Population size--100
Crossover probability--0.8
Mutation Probability--0.2
Total number of run--01
The effect of number of generations on availability of the Urea
Crystallization system is shown in figure 3. The optimum value of
system's performance is 98.45 %, for which the best possible
combination of failure and repair rates is [[alpha].sub.1] = 0.0103,
[[beta].sub.1] = 0.9983, [[alpha].sub.2] = 0.0040, [[beta].sub.2] =
0.8998, [[alpha].sub.3] = 0.0215, [[beta].sub.3] = 0.6858,
[[alpha].sub.4] = 0.0010, [[beta].sub.4] = 0.3709 at generation size
200, as given in table 2.
[FIGURE 2 OMITTED]
[FIGURE 3 OMITTED]
Conclusions
The performance optimization of the Urea Crystallization system of
a fertilizer plant is discussed in this paper. Genetic Algorithm
Technique (G.A.T) is hereby proposed to select the various feasible
values of the system failure and repair parameters. Then, G.A.T is
successfully applied to coordinate simultaneously all these parameters
for an optimum level of system performance. Besides, the effect of G.A.
parameters such as population size and number of generations on system
performance i.e. availability has also been discussed. The findings of
this paper are discussed with the concerned fertilizer plant management.
Such results are found highly beneficial for the purpose of performance
optimization of the Urea Crystallization system of a fertilizer plant
concerned.
Acknowledgement
The author is grateful to Sh. Sudesh Chohan, National Fertilizer
Limited Panipat (India), for providing every possible help during the
work.
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(a) Sanjeev Kumar, (b) P.C. Tewari, (c) Sunand Kumar and (d) Meenu
(a) Department of Mechanical Engineering, AKG Engineering College,
Ghaziabad--201009 (Uttar Pradesh),INDIA, E-mail :
[email protected]
(b,d) Department of Mechanical Engineering, National Institute of
Technology, Kurukshetra--136119 (Haryana) INDIA, E-mail:
[email protected],
[email protected]
(c) Department of Mechanical Engineering, National Institute of
Technology, Hamirpur--177005 (Himachal Pradesh) INDIA, E-mail:
[email protected]
Declaration
The research material in the paper title "Performance
Evaluation and Optimization for Urea Crystallization System in a
Fertilizer Plant using Genetic Algorithm Technique" submitted to
the International Journal of Applied Engineering and Research (IJAER)
has neither been published elsewhere nor is being considered elsewhere
for publication.
Sanjeev Kumar
Assistant Professor,
Department of Mechanical Engineering
AKG Engineering College,
Ghaziabad--201009 (Uttar Pradesh)
INDIA
Email:
[email protected]
Table 1: Effect of Population Size on Availability of Urea
Crystallization System.
Pop. [[alpha]. [[alpha]. [[alpha]. [[alpha].
Size Av. sub.1] sub.2] sub.3] sub.4]
20 0.9775 0.0154 0.0041 0.0234 0.0013
40 0.9824 0.0108 0.0045 0.0261 0.0012
60 0.9830 0.0110 0.0042 0.0227 0.0012
80 0.9837 0.0103 0.0043 0.0200 0.0010
100 0.9835 0.0110 0.0041 0.0216 0.0010
120 0.9838 0.0101 0.0043 0.0244 0.0014
140 0.9843 0.0103 0.0041 0.0206 0.0013
160 0.9843 0.0101 0.0040 0.0201 0.0011
Pop. [[beta]. [[beta]. [[beta]. [[beta].
Size sub.1] sub.2] sub.3] sub.4]
20 0.9250 0.7772 0.6879 0.1915
40 0.9670 0.8518 0.6727 0.3839
60 0.9690 0.8773 0.6766 0.3580
80 0.9974 0.7824 0.6908 0.3941
100 0.9715 0.8889 0.6915 0.3932
120 0.9682 0.7920 0.6986 0.3992
140 0.9912 0.8811 0.6711 0.3972
160 0.9457 0.8915 0.6914 0.3951
Table 2: Effect of Number of Generations on Availability of Urea
Crystallization System.
Gen. [[alpha]. [[alpha]. [[alpha]. [[alpha].
Size Av. sub.1] sub.2] sub.3] sub.4]
50 0.9819 0.0126 0.0042 0.0213 0.0012
100 0.9835 0.0110 0.0041 0.0216 0.0010
150 0.9844 0.0103 0.0040 0.0206 0.0011
200 0.9845 0.0103 0.0040 0.0215 0.0010
250 0.9834 0.0111 0.0041 0.0222 0.0011
300 0.9836 0.0109 0.0040 0.0242 0.0010
Gen. [[beta]. [[beta]. [[beta]. [[beta].
Size sub.1] sub.2] sub.3] sub.4]
50 0.9821 0.8999 0.6994 0.3948
100 0.9715 0.8889 0.6915 0.3932
150 0.9946 0.8722 0.6730 0.3891
200 0.9933 0.8998 0.6858 0.3709
250 0.9984 0.8670 0.6768 0.3893
300 0.9966 0.8929 0.6872 0.3955