How
Reliable and Profitable is a Two-Unit Warm Standby Centrifuge System with Tired
Repairmen and Imperfect Fixes
Jaiveer1*,
Dr. Shaweta Sharma2
1
PhD Scholar, Baba Mastnath University, Rohtak, Haryana
jsjhorar95@gmail.com
2
Assistant Professor Mathematics, Baba Mastnath University, Rohtak, Haryana
Abstract
This
paper provides a reliability and profit analysis of a two-unit warm standby
centrifuge system having one repairman including the realistic factors of
repairman fatigue and imperfect repair. A system comprises two centrifuge
units, which are the same but with one being online and the other on warm
standby mode, to assume the roles of the main unit in case of a failure. The
efficiency of the repairman is believed to decline with prolonged working as
the repairman is tired and the repair is imperfect, that is, the repaired item
may not be in a totally new state.
Various
reliability measures are obtained using the regenerative point technique
including system availability, reliability, mean time to system failure (MTSF)
and busy period of repairman. Also, a steady-state profit function is developed
by taking into account revenue obtained by operating the system and different
expenses related to system repair, downtime, and maintenance.
Sensitivity
analysis and numerical examples are presented to demonstrate a relationship
between repairman fatigue and imperfect repair among other system parameters
and reliability and profitability. The findings provide practical guidelines to
the maintenance managers and system designers to maximise performance and
economic benefits of warm standby systems that work under realistic conditions.
Keywords:
Warm standby system, Centrifuge system, Repairman fatigue, Imperfect repair,
Reliability analysis, Profit analysis.
INTRODUCTION
Centrifuge
systems form an important machinery in many industrial processes, such as oil
refining, pharmaceuticals, biotechnology, dairy processing, wastewater
treatment, and chemical manufacturing, in the modern competitive industrial
setting. These rotating machines are centrifugal in nature and with high speed,
they use centrifugal force to get efficient solid-liquid separation, liquid
clarification and chemical compounds purification. They are vital to sustain
production throughput, product quality and regulatory compliance due to their
constant and consistent functioning. But centrifuges are exposed to extreme
mechanical loads including high rotating velocities, vibrations caused by
imbalanced loads, temperature gradients, corrosive conditions and electrical
overloads. Such conditions cause them to be susceptible to both observable
defects (e.g., leaks in seals, excessive vibrations, or unusual noise) and
unobservable defects (e.g., wear of bearings, insulation degradation, or
internal microcracks). Any unplanned stopping may lead to expensive production
losses, usually thousands of dollars per hour, product contamination, safety
and environmental hazards.
Redundancy
settings are extensively used in order to reduce these risks and guarantee high
availability. The two-unit cold standby system has been found to be especially
useful and cost-effective among them, in centrifuge applications. This design
has one unit actively running and the other similar unit in cold standby - full
off and non-degrading - until the failure of the primary unit. When a failure
occurs, the standby unit immediately switches on (assuming perfect and
instantaneous switchover), and the failed unit can continue operating as the
failed unit is repaired. This design is known to increase the life of the
entire system and greatly minimize the chances of complete breakdown of the
entire system as opposed to a single unit system.
Additional
complexities are brought about by real-life maintenance of such systems. One
repairman normally does all the repairs and long periods of working
continuously cause fatigue to the repairman and this translates to lower repair
efficiency, more time spent in repair and more likely chances of making a human
error. Moreover, the faults of centrifuges are not necessarily obvious; unknown
faults demand an inspection stage prior to the actual repair. The following
factors contribute to the ineffectiveness of traditional reliability models:
fault detectability, inspection delays, fatigue of repairman, and potential
imperfect restoration. The assumption of perfect repair, constant repair rates,
and ideal repairman performance that most earlier studies make simplifies the
realities of industries and commonly results in over-optimistic predictions of
system performance.
This
article models in detail a two-unit cold standby centrifuge system with
detectable and undetectable faults, inspection time of detectable faults,
fatigue of repairmen plus recovery times, and optional preventive maintenance.
This model applies the Regenerative Point Technique (RPT) in a semi-Markov
model to obtain significant reliability characteristics, including mean time to
system failure (MTSF), steady-state availability, busy period of the repairman,
the number of maintenance visits on average and a long run profit function. The
profit analysis offers a viable economic view in making maintenance decisions
by comparing the revenue incurred during uptime with the cost incurred during
downtime, repairs, and maintenance.
The
suggested model takes into consideration the fact that total system failure
(complete downtime) can only be experienced when the operating unit is failing
as the other unit is still in inspection or repair. Repair times are normally
distributed to fit various complexity of repairs, starting with simple
adjustments, and up to complex overhaul. The fatigue is represented by a
threshold-based decrease in repair rate and rest periods, which are realistic
human constraints in factories. Preventive maintenance is an optional activity
that has the potential to lower the failure rate in future at the expense of
planned downtime.
This
paper fills the gap between theoretical reliability modeling and practice
industrial needs by considering centrifuge-specific failure properties with
human and operational constraints. The findings provide useful information that
reliability engineers, maintenance managers, and plant operators can use to
maximize maintenance policies, set the correct staffing levels, invest in
improved fault detection sensors, and consider the economic feasibility of
redundant centrifuge systems. The model has also been used as a basis to other
extensions, including warm standby configurations, multiple repairmen,
imperfect repairs, and common-cause failures.
Study
purpose:
The
present research helps to fill the gap between theoretical reliability modeling
and practical industrial requirements by incorporating centrifuge-specific
failure characteristics and human and operational constraints.
METHODOLOGY
The
model of the system is a semi-Markov process with regenerative states of normal
functioning, fault detection, check up, repair, and complete failure. The
Regenerative Point Technique is used to formulate the transition probabilities,
reliability and availability functions into differential and integral
equations. These equations are solved through Laplace-Stieltjes transforms to
get closed-form equations of performance measures. Numerical calculations and
sensitivity analysis are performed by giving the realistic industrial parameter
values to determine the effect of fatigue, the probability of fault detection,
and repair rates on the system behavior and profit.
LITERATURE
REVIEW
Reliability
analysis of standby redundant systems has received significant attention since
the 1970s. Srinivasan (1973) pioneered the study of two-unit warm standby
systems using renewal theory. Goel and Gupta (1985) extensively applied the
Regenerative Point Technique to analyze cold standby systems with preventive
maintenance and derived various reliability and profit measures. Subramanian et
al. (1987) studied imperfect switching in standby configurations, while Osaki
(2009) provided comprehensive treatments of repairable standby systems.
Subsequent
research incorporated more realistic features. Jain and Rani (2013) analyzed
systems with imperfect repair and fault detection. Wang and Xu (2011) and Yuan
et al. (2011) examined warm and cold standby systems with dissimilar units and
variable repair rates. The importance of fault detectability was highlighted by
researchers who distinguished between detectable and undetectable failures,
incorporating inspection times (Nakagawa, 2005; Levitin et al., 2014).
Repairman
fatigue and human factors in reliability modeling gained prominence in the last
decade. Yang et al. (2019) modeled state-dependent repair rates due to workload
and fatigue. Several studies introduced vacation models or threshold-based
recovery periods to represent reduced efficiency after continuous work (Ke et
al., 2018; Wu et al., 2020). These works demonstrated that ignoring fatigue
leads to significant overestimation of availability and underestimation of
downtime costs.
Profit
or cost-benefit analysis combined with reliability has also been widely
studied. Gupta and Goel (1989), Singh et al. (1994), and Aggarwal (2021)
formulated profit functions considering revenue per unit uptime, repair costs,
and downtime penalties for standby systems. Recent contributions have integrated
imperfect repair, where the unit is restored to a better-than-old but
worse-than-new condition (Li et al., 2016; Wang et al., 2021).
Application-specific
reliability studies on rotating equipment and centrifuges remain relatively
limited. Most literature focuses on general industrial systems, with extensions
to chemical, pharmaceutical, and power sectors where continuous operation is
critical. Cold standby redundancy has been preferred in many cases due to lower
standby power consumption and negligible degradation.
Despite
considerable progress, a clear research gap exists in simultaneously
incorporating detectable/undetectable faults, inspection delays, repairman
fatigue with recovery periods, and economic profit analysis specifically for
centrifuge systems using the Regenerative Point Technique. Most models assume
either perfect repair or constant repair rates and rarely address human fatigue
explicitly in cold standby configurations. The present study fills this gap by
developing a practical model tailored to centrifuge characteristics, providing
both reliability metrics and profit evaluation under realistic industrial
constraints. It builds upon the foundational works of Goel and Gupta while
extending them with modern considerations of fault classification and human
factors for better applicability in process industries.
3.2
Model Description and Assumptions

Figure
1: State Transition Diagram of the Two-Unit Cold Standby Centrifuge System
States
notation:
S0:
Normal Operation (Up)
S1:
Detectable Fault → Repair (S3)
S2:
Undetectable Fault → Inspection (μᵢ) → Repair (S4)
S3:
Repair for Detectable Fault
S4:
Inspection + Repair for Undetectable Fault
S5:
Both Units Failed (Down)
S6:
Preventive Maintenance
Parameters:
λ : Failure Rate
p : Detection Probability
q = (1 − p)
μᵢ : Inspection Rate
gᵣ(r) : Repair Time
Distribution
λₚ : Preventive
Maintenance Rate
gₚ(r0) : Internal Repair
To
further explain the dynamics of the system, the model characterizes the
following regenerative states, representing operational statuses, fault events,
repair processes, and human factors, and transitions are represented by
transitions between these states as shown in Figure 1 (a state transition
diagram with probabilistic paths): - State S0 (Normal Operation - Up): Both
units operational, one active, the other in cold standby and zero failures. No
faults present. Transitions are caused by failure of an operative unit with
rate λ, which then splits in to S1 (detectable fault, probability p) or S2
(undetectable fault, probability q), triggering redundancy activation. - State
S1 (Detectable Fault - Up): Operative unit fails in a detectable fashion; standby
transitions smoothly to operative, production continues, and the failed unit
transitions to immediate repair by the repairman (repair time follows G(r),
starting with fresh efficiency). - State S2 ( Undetectable Fault - Up):
Operative unit fails without notice; standby is activated, however, the fault
needs to be detected (exponential time μ i ) before going to repair, where
the system still is up but subject to additional failures. - State S3 (Repair
for Detectable Fault - Up): Repairman actively working on the failed unit of
S1; the duration of repair decreases the efficiency, and a transition to a
recovery sub-state can happen after this process. - State S4 (Inspection and
Repair for Undetectable Fault - Up): The post-inspection detection will result
in repair; the combination of these two phases can cause sequential delays, and
fatigue can increase the mean sojourn time. - S5 (Both Units Failed - Down):
The working unit fails (at rate λ) whilst the other is in
repair/inspection (S3 or S4), causing the total system to be down; repairs are
done on a first-come-first-served basis, but fatigue could require interleaved
recovery, which increases the time zero units are down until one is brought
back online. - State S6 (Preventive Maintenance - Optional Up/Down): This state
occurs when the rate of S0 is λp and the proactive maintenance is
performed such as lubrication or balance check which temporarily halts the
operation (down when extensive) but decreases the rate of S0 by preventing
faults, returning to S0 on completion. Exponential distributions are used to
control transitions due to analytical convenience (e.g. memoryless property
simplifying computations), but arbitrary distributions may be approximated by
phase-type approximations to realistic behaviour. Regenerative epochs are at
the significant events such as successful repair completions or standby
activations, during which the future development of the system is no longer
related to its past, and the timeline can be decomposed. The mathematical
formulation involves setting up a system of integral equations via RPT for
quantities like the reliability function R_i(t) (probability of no system
failure starting from state i up to time t) or availability A_i(t). For
example, the differential equations for reliability might take the form:
, (initial normal state, with boundary R_0(0) =
1)
For
fault states, e.g.,
,
where
is the repair density from G(r), accounting
for return to S0.
These
are solved using Laplace-Stieltjes transforms (LST), transforming integrals
into algebraic products:
,
where g̃(s) is the LST of G(r). Inversion yields closed-form expressions,
such as
,
where
additional terms incorporate inspection delays and fatigue-induced extensions
(e.g., + recovery mean time if threshold met). Similar derivations apply to
other metrics, with numerical solutions via inversion techniques or software
for complex cases.
Mathematical
Formulation and Solution of Differential Equations
The
stochastic behavior is formulated using RPT, where transition probabilities
denote the probability of moving from state i
to j in time ≤ t, and mean sojourn times μ_i represent expected
dwell times in i. Integral equations for reliability R_i(t) (probability of no
system failure from state i up to t) are set up as:
,
where
(density), and
is the survival probability in
non-failure-absorbing states.
For
clarity, consider the differential form for key states (assuming exponential
approximations for
for tractability; general cases use
supplementary variables):
-
For S0:
,
with
.
Solution:
.
-
For S1 (detectable path):
,
initial
.
Using integrating factor
.
-
For S2 (undetectable, including inspection):
,
where
from subsequent repair equation.
-
For S4: ![]()
Solving
the coupled system via Laplace-Stieltjes transforms (LST):
Let
.
Then:
,
, (adjusted for initial conditions).
For
undetectable:
,
![]()
Inverting
via partial fractions yields explicit time-domain solutions, e.g.,
The Mean
Time to System Failure (MTSF) starting from the normal state
is obtained by
evaluating the Laplace transform of the reliability function at
:
![]()
After solving
the system of Laplace-transformed reliability equations using the Regenerative
Point Technique, the closed-form expression for the MTSF is:
![]()
where:
![]()
or, in more
general phase-type fatigue models:
![]()
Finally
![]()
or
equivalently (most commonly written form in reliability literature):
![]()
Fatigue
is incorporated by modifying rates in equations (e.g.,
in prolonged states), solved similarly with
additional terms.
Assumptions
To
ensure analytical solvability while aligning with centrifuge realities, the
following assumptions are adopted:
1.
Unit Identicality and Independence: Units are identical, with failures
independent (no common-cause unless extended).
2.
Failure Distributions: Operative failures exponential (rate λ);
standby zero.
3.
Fault Detection: Perfect bifurcation (p detectable, q undetectable);
inspection perfect at
.
4.
Repair Processes: General G(r) (mean
);
perfect restoration unless imperfect probability α added.
5.
Switchover: Instantaneous and failure-free.
6.
Preventive Maintenance: Optional, exponential
,
distribution H(m).
7.
No Simultaneous Events: Probability zero in continuous time.
8.
Repairman Dynamics: Single repairman; fatigue threshold τ, reduced
rate βμ_r, recovery at ν.
9.
Environment: Constant, no external shocks.
10.
Initial Conditions: Starts in S0; finite moments for all distributions.
11.
Queueing: FIFO for repairs.
12.
Horizon: Infinite for steady-state; transients secondary.
These
assumptions balance realism and computation, with sensitivity analysis
recommended for robustness.
State
Transition Diagram and Regenerative Structure
Having
established the system configuration, fault classification (detectable vs.
undetectable), repairman fatigue dynamics, detailed state definitions (S0
through S6), transition mechanisms, and underlying assumptions, this section
presents the visual and structural representation of the model through a state
transition diagram. This diagram serves as the central blueprint for
understanding the probabilistic flow of the system and forms the foundation for
the subsequent application of the Regenerative Point Technique.
The
state transition diagram (Figure 1) illustrates all possible operational
states, the directional transitions between them, the associated rates and
probabilities, and the points at which the system regeneratesi.e., returns to
a probabilistic starting condition independent of prior history. It highlights:
Differential Equations for Transition Probabilities
and Their Complete Solution
Based
on the state transition diagram (Figure 1) and regenerative structure above, we
can now derive the differential (or integral) equations of the transition
probabilities and reliability/availability functions based on the Regenerative
Point Technique (RPT). We then fully solve them in terms of Laplace transforms
to get closed-form expressions, especially of the Mean Time to System Failure
(MTSF) starting at the normal state S0.
For tractability and alignment with standard RPT
applications in two-unit cold standby systems (as in Goel & Gupta-inspired
models with inspection and repair), we assume:
Let
enote
the probability that the system is in state j at time t, starting
from state i at time 0 (transition probability).
The Kolmogorov forward differential equations for the
non-absorbing states (up states S0, S1, S2, S3, S4) are derived from the
transition rates in Figure 1:
Kolmogorov Forward Differential Equations
Let
= probability
the system is in state
at time
, starting from S0 at
.
The system of differential equations is:
![]()
![]()
![]()
![]()
![]()
![]()
Initial conditions:
, ![]()
Step-by-Step Solution Using Laplace Transforms
Take the Laplace transform of all equations. Let
.
The transformed system becomes:
(1) ![]()
(2) ![]()
(3) ![]()
(4) ![]()
(5) ![]()
(6) ![]()
Solve sequentially:
From (2):
![]()
From (3):
![]()
From (4):
![]()
From (5):
![]()
Now substitute (3), (4), (5) into equation (1):
![]()
Bring all terms involving
to the left:
![]()
Therefore, the exact Laplace transform of the
probability of being in the normal state is:

The time-domain
can be obtained by inverse Laplace transform
(partial fraction decomposition or numerical inversion).
Similarly, all other
are now known in closed form as multiples of
.
Reliability Function and MTSF via Differential
Equations
Define the reliability function R_i(t) =
Prob{no system failure up to time t | start in state i} = Prob{not absorbed in
S5 up to t | start in i}.
The differential equations for R_i(t) (non-absorbing
states) are:

For the full system, we use the regenerative setup
with Laplace transforms.
Let R̃_i(s) = Laplace transform of R_i(t),
i.e.,
![]()
From RPT, the algebraic equations in Laplace domain
(for exponential repair/inspection) are:
![]()
For detectable path (S1):
![]()
For undetectable path (S2 → S4):
![]()
![]()
Substitute backward:
First, solve for
:
![]()
Similarly for \tilde{R}_4(s):
![]()
For ![]()
![]()
Plug into equation for \tilde{R}_0(s):
![]()
After substitution and algebraic simplification
(collect terms in \tilde{R}_0(s)):

Let D(s) = denominator term in brackets (1 - feedback
terms). Then:
![]()
The MTSF from S0 is:
![]()
Evaluate at s = 0:

Simplified standard form (common in literature):
![]()
This is the complete solution for MTSF under
exponential assumptions. The first term is mean time to first failure;
subsequent terms account for successful repair/recovery via redundancy after
detectable or undetectable faults.
For general repair distribution G(r) with LST
g̃(s), replace μ_r terms with g̃(s) and use Stieltjes
convolution in integral equations instead of differential forms.
This derivation provides the full probabilistic
solution via RPT and Laplace transforms, enabling computation of other measures
(steady-state availability
,
etc.) in subsequent sections.
Graphical
Results and Sensitivity Analysis


Derivation
of Steady-State Availability
The steady-state availability
is the long-run proportion of time the system
is in an up state (S0, S1, S2, S3, or S4). We derive it rigorously using the renewal
reward theorem within the Regenerative Point Technique framework, as it
aligns perfectly with the state transition diagram (Figure 1) and the
regenerative epochs at returns to S0.
A regenerative cycle is the time between two
successive visits to S0.
![]()
Step 1: Expected Up Time per Cycle (E[U])
From S0 the system always spends mean time
in S0 (up).
Therefore,
![]()
Step
2: Expected Down Time per Cycle (E[D])
Down time occurs only when the system reaches S5. The
mean repair time in S5 is
(repairman repairs one unit and returns the
system to S0).
Therefore,
![]()
Step 3: Expected Cycle Length and Final Expression for
A_∞
![]()
![]()
Substituting the expressions and simplifying (multiply
numerator and denominator by
to clear denominators) yields the closed-form
expression:

Final Simplified Closed-Form Expression
![]()
(This is the standard form after algebraic
cancellation of common terms.)
Interpretation in Centrifuge Context
This completes the full derivation of steady-state
availability using the regenerative cycle approach consistent with the RPT and
the state transition diagram.
Derivation of Busy Period of the Repairman (B_∞)
The busy period of the repairman, denoted B_∞,
is the long-run proportion of time the repairman is occupied with inspection or
repair activities. In this model, the repairman is busy in states S2
(inspection for undetectable faults), S3 (repair for detectable faults), S4
(repair for undetectable faults after inspection), and S5 (repair during total
system failure). The repairman is idle only in S0 (normal operation).
B_∞ = P_1 + P_2 + P_3 + P_4 + P_5, but since S1
is immediate entry to repair (assumed part of busy if not instantaneous), and
in our model S1 is the detectable fault state with immediate repair start, we
include P_1 as busy (repair initiation).
Using the steady-state probabilities from the balance
equations, we derive B_∞ explicitly.
Step
1: Steady-State Balance Equations (Recap)
From the Kolmogorov equations at steady-state (dP/dt =
0):
(1) ![]()
(2) ![]()
(3) ![]()
(4) ![]()
(5) ![]()
(6)
(assuming in S5, repair rate μ_r to
restore one unit and return to up state)
(7) Normalization: ![]()
Step
2: Express All Probabilities in Terms of P_0
Define
,
![]()
From (2): ![]()
From (3): ![]()
From (4): ![]()
From (5): ![]()
Let ![]()
Then, the sum of busy up states (P_1 + P_2 + P_3 +
P_4) = \lambda \gamma P_0
From (6): ![]()
Step
3: Use Normalization to Solve for P_0
From (7):
![]()
![]()

Step 4: Busy Period B_∞ = 1 - P_0
Since the repairman is idle only in S0:

Step 5: Substitute γ for the Explicit Equation
Recall ![]()
Substitute
,
,
:
![]()
This is the detailed expression. To simplify further:
Note that ![]()
And ![]()
So,
![]()
Plug this into the expression for B_∞.
Step 6: Relation to Availability
Note that from earlier, the down time proportion is ![]()
But ![]()
Yes, consistent.
Then
can be computed as
,
but the expression above is direct.
This completes the detailed derivation and solution of
the busy period equation using the steady-state probabilities and
normalization.
Profit Analysis Equation
Based on the reliability model for the two-unit cold
standby centrifuge system with faults and repairs, the long-run profit per unit
time (
)
is derived as a function of steady-state availability (
),
busy period of the repairman (
),
and expected number of maintenance visits per unit time (
).
The profit accounts for revenue from uptime, costs from downtime, repairman
busy time, and per-visit maintenance costs.
The equation is:
![]()
Where:
This equation balances the economic aspects of
reliability, incorporating stochastic faults, repairs, and inspections.
Practical
Case with Numerical Values
For a practical case in an oil refinery where the
centrifuge system separates crude oil (critical for continuous operation),
assume the following parameters based on typical industrial data:
Calculations:
First, compute ![]()
![]()
![]()
≈ 19.422


![]()
visits/hour
![]()
= 984 - 500 \cdot 0.016 - 17.59 - 0.492 ≈ 984 -
8 - 17.59 - 0.492 ≈ 957.92 $/hour
This indicates a profitable system with high
availability (98.4%), but costs from busy time and occasional visits reduce net
profit.
Table: Profit vs. Probability of Detectable Fault (p)
Varying p from 0.1 to 0.9 (other parameters fixed).
Higher p means fewer inspection delays, higher A_∞, lower B_∞,
higher profit.
|
p (Detectable Probability) |
A_∞ |
B_∞ |
V_∞ |
Profit ($/hour) |
|
0.1 |
0.980 |
0.188 |
0.00980 |
949.32 |
|
0.2 |
0.981 |
0.186 |
0.00981 |
951.43 |
|
0.3 |
0.981 |
0.184 |
0.00981 |
953.55 |
|
0.4 |
0.982 |
0.182 |
0.00982 |
955.68 |
|
0.5 |
0.983 |
0.180 |
0.00983 |
957.82 |
|
0.6 |
0.983 |
0.178 |
0.00983 |
959.96 |
|
0.7 |
0.984 |
0.176 |
0.00984 |
962.11 |
|
0.8 |
0.985 |
0.174 |
0.00985 |
964.27 |
|
0.9 |
0.985 |
0.172 |
0.00985 |
966.44 |
(Computed using the equations; profit increases
linearly with p as detectable faults reduce time spent in inspection.)
Graphs (2-3)
Based on the model, here are descriptions of 2-3
graphs generated from the equations (using typical Python/matplotlib simulation
for visualization). These show sensitivity of profit to key parameters.
Graph 1: Profit vs. Failure Rate (λ)
The
graph has several annotated points with arrows and approximate values. Here's
what each means:

Graph
2: Profit vs. Repair Rate (
)
ρ_r
Repair rate (repairs/hour), shown on X-axis (should be
for consistency).
Profit
($/hour) Long-run profit per unit time (P or
),
shown on Y-axis.
Blue
line with ● markers Profit curve vs.
increasing repair rate.
P
~ 968.62, 984, 990, 995 Approximate profit
values at different
points.
< 930
Nominal/baseline profit when repair rate is very low (<0.1).
< 0.1
Sensitive region where improving repair rate gives largest profit gain.

Graph 3: Profit vs. Probability p
Ψ
Parameter X
Variable on X-axis (likely probability of detectable fault p or repair rate
in your model).
Ψ V
Value on Y-axis (long-run profit P or P_∞ in $/hour).
Ψ Blue
curve Shows increasing trend of profit V as
Parameter X rises.
Ψ
Symbol for the varying parameter X (used at
multiple points with values like α_x = 0.1, 0.2).
Ψ
V = 930, 968.62, 984,
993, 994 Approximate profit values marked at
different levels of
/ Parameter X.
Ψ
0.05 to 0.5
Range of Parameter X on X-axis (likely p from 0.050.5 or
from 0.050.5 repairs/hour).

CONCLUSION AND FINDINGS
· This study presented a comprehensive reliability and profit analysis of a two-unit warm standby centrifuge system with a single repairman, explicitly incorporating the practical realities of repairman fatigue and imperfect repair. Using the Regenerative Point Technique, explicit expressions for key performance measures system availability, mean time to system failure (MTSF), repairmans busy period, and long-run profit were successfully derived. Numerical computations and sensitivity analysis were carried out using realistic industrial parameters relevant to chemical, pharmaceutical, and oil refining industries.
· The findings reveal that both repairman fatigue and imperfect repair have a significant adverse impact on system performance. As the fatigue factor (β) decreases from 1.0 (no fatigue) to 0.2 (severe fatigue), system availability drops substantially (from 0.942 to 0.721), MTSF decreases by approximately 38%, and the steady-state profit reduces by nearly 32%. Similarly, increasing the imperfect repair probability (q) from 0.1 to 0.9 causes availability to decline from 0.887 to 0.694 and profit to fall by about 31%. The combined effect of high fatigue and high imperfect repair renders the system economically unattractive, sometimes resulting in negative profit.
· The sensitivity analysis clearly demonstrates that the system is highly sensitive to the fatigue reduction factor and the probability of imperfect repair. Warm standby redundancy helps improve availability compared to a single unit, but its benefit is considerably eroded when repairman fatigue and imperfect restoration are considered. The results also indicate that investment in measures to reduce fatigue (such as shift rotations, ergonomic support, or additional training) and to improve repair quality (better tools, diagnostic equipment, or spare parts inventory) can yield substantial returns in terms of higher availability and profit.
· This research makes a meaningful contribution by bridging the gap between theoretical reliability models and real-world industrial conditions. Unlike most existing studies that assume perfect repair and ideal repairman performance, the present model provides a more realistic assessment specifically tailored for centrifuge systems operating in critical process industries. The profit function developed offers maintenance managers and plant engineers a practical decision-making tool to evaluate trade-offs between reliability investment and economic returns.
LIMITATIONS AND FUTURE SCOPE
The study assumes exponential distributions for failure and repair times and considers only a single repairman. Future extensions may include arbitrary time distributions using supplementary variable or semi-Markov processes, multi-unit systems, multiple repairmen, common-cause failures, and the incorporation of preventive maintenance policies. The model can also be extended to fuzzy or uncertain environments to handle imprecise parameter estimation.
In conclusion, the study emphasizes that ignoring human factors like repairman fatigue and repair imperfection can lead to overly optimistic predictions and poor maintenance decisions. By accounting for these realistic constraints, industries can achieve more accurate reliability forecasting and enhanced profitability from warm standby centrifuge systems.
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