PHE General
Flow principle and parts
The Gasketed Plate Heat
Exchanger
– The PHE –
• The function of the plate pack – Single pass:
1
PHE General
The Gasketed Plate Heat
Exchanger
– The PHE –
• The function of the plate pack – Multi pass:
The Gasketed Plate Heat
Exchanger
– The PHE –
• The plate corrugation has two
functions:
Mechanical
Flow dynamic
2
PHE General
The Gasketed Plate Heat
Exchanger
– The PHE –
• Two plate corrugations L and H:
L: Low theta
H: High theta
The Gasketed Plate Heat
Exchanger
– The PHE –
• Two plate corrugations may form three
different interplate channels:
L + L = L channels
H + H = H channels
L + H = M channels
3
PHE General
PHE groupings influence on
performance
Example
•
•
•
•
Product: 5 000 kg/h raw milk, inlet temp 20º C
Service: 15 000 kg/h water, inlet temp 1º C
PHE:
Clip-6RM with 17 plates = 2,75m²
Channels:
Low, high and mixed theta
Parallell grouping
Example 1 * 8
1*8
4
PHE General
PHE groupings influence on
performance
• Low pressure drop
• Low heat transfer
Grouping
Temp
program, ºC
Pressure k-value, Heat
drop, kPa W/m², ºC transfer, kW
1 * 8 L
1 * 8 L
20 ! 9.0
4.4 1
3
21
1860
60
1 * 8 H
1 * 8 H
20 ! 6.0
5.4 1
12
105
2980
76
1 * 8 MH 20 ! 7.7
1 * 8 ML 4.8 1
5
45
2280
67
Series grouping
Example 8 * 1
8*1
5
PHE General
PHE groupings influence on
performance
•High pressure drop
•High heat transfer
Grouping
Temp
program, ºC
Pressure
drop, kPa
k-value,
W/m², ºC
Heat
transfer, kW
8 * 1 L
8 * 1 L
20 ! 2.5
6.5 1
1090
9450
6180
96
8 * 1 H
8 * 1 H
20 ! 1.6
6.7 1
5750
49500
8690
101
8 * 1 MH
8 * 1 ML
20 ! 1.9
6.6 1
2400
19700
7370
99
Combined grouping (symmetric)
Example 4 * 2
4*2
6
PHE General
PHE groupings influence on
performance
Grouping
Temp
program, ºC
Pressure
drop, kPa
k-value,
W/m², ºC
Heat
transfer, kW
4 * 2 L
4 * 2 L
20 ! 4.0
6.0 1
140
1210
4260
87
4 * 2 H
4 * 2 H
20 ! 2.4
6.5 1
740
6350
6300
96
4 * 2 MH
4 * 2 ML
20 ! 3.2
6.2 1
315
2580
5150
92
Combined grouping (asymmetric)
Example 4 * 2
2*4
7
PHE General
PHE groupings influence on
performance
Grouping
Temp
program, ºC
Pressure
drop, kPa
k-value,
W/m², ºC
Heat
transfer, kW
4 * 2 L
2 * 4 L
20 ! 4.8
5.7 1
140
160
3670
83
4 * 2 H
2 * 4 H
20 ! 3.1
6.3 1
740
815
5280
93
4 * 2 MH
2 * 4 ML
20 ! 3.9
6.0 1
315
340
4390
88
8
PHE General
Milk pasteurization
Parameters
•
•
•
•
•
•
•
•
•
Capacity
Temp programme; in, out, past
Running costs
Running times
Separation, temperature, skimming
Homogenisation, temperature, pressure
Deaeration, temperature, temperature drop
Heating media, cooling media
Drainability
Milk pasteurization
Heat Recovery
•
•
•
•
•
•
•
Capacity
Running hours
Cleaning intervals
Media costs
Product costs
Maintenance
Capital cost
+
+
+
+
-
9
PHE General
Heat Recovery
Product
inlet
Pasteurisation
temperature
IW
A
Cooler
B
C
Regenerative
D
HW
C
B-A
C-A
Heat recovery =
Example:
Heater
A = 4°C
B = 67°C
C = 74°C
x 100 (%)
67 - 4
74 - 4
x 100 =
63 x 100 = 90 %
70
Heat Recovery
Milk Pasteurizer
80000
70000
60000
EUR
50000
Series1
40000
Series2
30000
20000
10000
0
75
80
85
90
95
100
Regenerative
10