Pergamon
Microelectron. Reliab., Vol. 36, No. 4, pp. 477-480, 1996
Copyright © 1996Elsevier ScienceLtd
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BEHAVIOURAL ANALYSIS OF A SHELL GASIFICATION AND
CARBON RECOVERY PROCESS IN A UREA FERTILIZER PLANT
S. KUMAR
Mechanical Engineering Department, Regional Engineering College, Hamirpur, (H.P.), India
D. KUMAR and N. P. MEHTA
Mechanical Engineering Department, Regional Engineering College, Kurukshetra 132119, India
(Received for publication 20 April 1995)
Abstract--The paper discusses the behavioural analysis for a shell gasificationand carbon recovery process
in a urea fertilizerplant. The system consists of three subsystems D, E and F arranged in series, with three
possible states--good, reduced and failed. The subsystem D has three parallel operating units with two
units in cold standby. Failure and repair rates for each subsystem are taken as constant. Formulation of
the problem is carried out using simple probability consideration. An expressionfor steady-state availability
is derived. Taking data from a medium sized plant, the effect of each working unit on the system availability
is tabulated. The results are supplied to the plant personnel for improvement in designing the system and
planning the process for minimum failure.
INTRODUCTION
A probabilistic analysis of the system under given
operative conditions is helpful in the design modifica-
tion for minimum failure of the system and thus to
optimize the system workings [1]. A urea fertilizer
plant consists of a large number of sub-systems
interconnected in series/parallel or both. These
sub-systems are subjected to random failure and
can be brought back into service after repairs/
replacement. The failures of sub-systems and their
components depend upon the operating conditions
and repair policy used which are difficult to predict
precisely. Behavioural analysis is a tool to economize
operational parameters in order to ensure the maxi-
mum possible level of system availability 12].
The ammonia production process comprises various
sub-systems namely air separation, shell gasification
and carbon recovery, desulphurization, CO shift
conversion, decarbonation, nitrogen washing and
ammonia synthesis processes including refrigeration
process [3]. One of the most important functional
parts of the ammonia plant is the shell gasification
and carbon recovery process which is the subject of
our present discussion. It consists of three sub-systems:
the high pressure feed pump (D) (having five units--
three working and two in standby), (E) gasifier, waste
heat boiler, gasification economizer, quench pipe and
carbon separator and carbon scrubber (F).
The system model for the plant has been developed
on the basis of an actual study conducted in a medium
sized urea fertilizer plant located near Kurukshetra.
The failure time/repair time data in the plant were
studied. Based on the model, behavioural analysis of
the system is carried out. The findings of the paper
have been discussed with the management of the
plants with a view to appraise them of the potential
benefits that would accrue through the implementa-
tion of the analytical results.
MODELLING
The system comprises of three sub-systems in series:
(i) Sub system (D~, i= I-5) having three working
units in parallel and two in standby, used to raise
the pressure of heavy oil from 4 to 189 kg cm- 2
Failure of any one unit forces one to run the
system with standby units. The complete failure
of the system occurs only when three pumps are
in a failed state.
(ii) Sub-system (Ej, j = 1-5), having five units in
series each unit comprising three parallel working
units. Failure of any one unit reduces the capacity
of producing ammonia. Complete failure occurs
only when two units fail simultaneously.
(iii) Sub-system (F), used to remove carbon through
washing and cooling process. Its failure causes
complete failure of the system.
ASSUMPTIONS
• Failure and repair rates are constant and statistically
independent;
• a repaired unit is as good as new;
• repairmen are always available;
• each sub-system has a separate repair facility and
there is no waiting time for repair in the sub-systems;
• service includes repair and/or replacement of the units;
• the standby units are of the same nature and capacity as
the active units;
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