(80d) Identifying Heat Recovery Paths to Be Used in Improving the Energy Efficiency of Pre-Heat Trains

A heat recovery
path consists of a combination of heat exchangers and pipework linking a heat
source and a heat sink. The concept of transferring heat along paths in order to reduce the energy
consumption of process plants was first suggested by Dhole [1]. It was
subsequently investigated by Adiarso [2] and Van Reisen [3,4]. It forms the basis
of a technique known as ?Network Pinch? introduced by Zhu & Asante [5].

The
application of the approach to pre-heat trains has been discussed by Polley
[6]. It was shown that the presence of process operations (de-salting and
pre-flash) resulted in the need for a special feature (termed a ?bridge?) that
allowed process heat balances to be maintained as additional heat is recovered.
The presence of heat recovery ?blocks? (or local ?pinches?) had to be
identified but could be removed through the introduction of stream splits. It
was further shown that the presence of ?fixed duties?, such as those associated
with pump-around streams had to be handled with particular care. Finally, it
was claimed that whilst heat recovery paths can be quite complex and that
usually there are a number of options available, the
better options could be identified without the need for computer software.

In this
paper the authors show, by working through a large example, how the presence of
?fixed duties? aids the identification of the paths that should be exploited in
order to improve energy efficiency. The improvement in energy efficiency can
come about through the installation of additional larger heat exchangers or
through fouling mitigation. Both options involve the use of the path. So, path
identification forms the first and key part of any energy reduction study.

The problem
studied involves a pre-heat train containing both an atmospheric column and a
vacuum column. Process operations employed are de-salting and pre-flash. There
are ten heat recovery units positioned below the de-salter. These units link
with eight individual coolers. Between the de-salter and the pre-flash column
there are eleven heat recovery matches, one of which links directly with a
cooler. Finally, there are five heat recovery matches positioned between the
pre-flash column and the fired heater at the base of the atmospheric column.

Both of the
distillation columns have pump-around streams (two used on the atmospheric
column, three are used on the vacuum column).

The heat
recovery system prior to the de-salter is shown in Figure 1. Heat recovery
units associated with pump-arounds are shown in red.
Other recovery units are shown in blue and coolers are shown in green. A bridge
is provided by heat recovery matches involving the same process streams. There
are three of these across the de-salter. They involve E3 and E21, E6 and E14
and E9 and E11.

Figure 1.
Heat Recovery System Prior to De-Salter

The system
between the de-salter and the pre-flash column is shown in Figure 2.

Figure
2. Heat Recovery
System Between de-salter and Pre-flash

There are two
parallel heat recovery trains. One of these trains has two units associated
with column pump around.

Bridges across
the pre-flash column are provided by identical matches in E21 and E23, E14 and
E22, and E15 and E24.

One cooler
(cooling the hot process stream leaving E15) is positioned in the system.

Finally, the
heat recovery system positioned above the pre-flash column is shown in Figure
3.

Figure
3. Heat recovery
System at Hot End of Train

Examining the
available paths leads to the following conclusions. The best bridge across the
de-salter is that between E6 and E14 for this allows recovery to be made from a
four individual coolers. However, E6 has a downstream effect on E10 so any
reduction in inlet conditions on this unit needed to be compensated. (This
occurs for all available bridges across the de-salter).

The bridge
involving E3 and E21 is subsequently blocked by E19. If this bridge is to be
used then careful consideration has to be given to the control of the pump
around. It will only be justified if the loads on coolers C2 and C4 are large.

With regard to
bridges across the pre-flash column, that involving E15 and E24 provides
linkage to cooler C1 and should be used. The bridge involving E14 and E22
should also be used for E22 is positioned on a separate stream split to E24.

The bridge
involving E21 and E23 has a downstream effect on the pump around flowing
through E19 and the comments made for the bridge involving E3 and E21 apply.

We conclude that
the best heat recovery path through the pre-heat train is probably that
involving E6-E14 and then E14-E22. This should be supplemented by the path
involving E15-E24.

References

[1]  V.R.Dhole,
Private Communication, UMIST, 1990

[2]  Adiarso,
?Application of Problem Decomposition in Process Integration Retrofit?, M.Sc.
Dissertation, UMIST, 1993

[3] Van Reisen J.L.B., Grievink J.,
Polley G.T. & Verheijen P.J.T. ?The placement of
two-stream and multi-stream heat-exchangers in an existing network through path
analysis?, Comp.& Chem. Engng., 1995,
19,S143-S148

[4] Van Reisen J.L.B., Polley G.T. & Verheijen P.J.T. ?Structural Targeting for Heat Integration
Retrofit?, Appl. Thermal Engng. 1998, 18(5), 283-294

[5] Asante
N.D.K. & Zhu X.X. ?An automated approach for heat exchanger network
retrofit featuring minimal topology modifications?, Comp.&
Chem. Engng., 1996, 20,S7-S12

[6]
Polley G.T., Tutorial on Practical Process Integration Retrofit, Part 3. Path
Analysis, AIChE Spring Meeting, 2011