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EDS6-122A Datasheet(PDF) 3 Page - Fuji Electric

Part # EDS6-122A
Description  VORTEX FLOWMETER (DELTA FLOWPET)
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Manufacturer  FUJI [Fuji Electric]
Direct Link  http://www.fujielectric.co.jp/eng/fdt/scd
Logo FUJI - Fuji Electric

EDS6-122A Datasheet(HTML) 3 Page - Fuji Electric

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Minimum flow rate
Nominal
diameter mm
0.5
0.6
0.7
0.8
0.9
1.0
1.1
1.2
10
0.3
0.3
0.3
0.2
0.2
0.2
0.2
0.2
2.2
15
0.4
0.4
0.4
0.4
0.3
0.3
0.3
0.3
4.7
25
1.0
0.9
0.9
0.8
0.8
0.7
0.7
0.7
16
40
1.7
1.5
1.4
1.3
1.3
1.2
1.2
1.1
31
50
2.7
2.5
2.3
2.2
2.1
2.0
1.9
1.8
53
80
6.0
5.5
5.1
4.7
4.6
4.6
4.6
4.6
118
100
11
11
11
11
11
11
11
11
205
Specific
gravity
unit: m3/h
Max.
flow
rate
Minimum flow rate (m3/h)
1235
10
15
20253040
10
0.3
0.4
0.6
1.1
15
0.4
1.2
1.8
2.9
25
1.8
5.9
40
2.8
6.5
14
50
3.6
7.1
15
24
80
11
16
26
38
100
14
21
28
45
55
Viscosity unit: mm2/s
Unmeasurable
Nominal
diameter mm
Kinem
atic
viscosity
For hatched area, retain Table A (according to specific gravity).
¡Gas
The flow rate range is indicated in actual base.
If the flow rate was given at standard status, be sure to convert it to actual flow rate and then, according to this table,
determine the flow rate range or nominal diameter.
Minimum flow rate (m3/h)
Maximum
flow rate (m3/h)
0.38
0.7
1.2
2.0
3.6
6
11
19
34
(60)
10
4.5
3.3
2.6
2.2
1.8
1.5
1.3
1.1
0.9
0.7
8.5
15
9.4
6.9
5.4
4.6
3.8
3.2
2.6
2.2
1.8
1.5
18
25
23
17
13
12
10
8
7
6
5
4
60
40
39
29
23
19
16
13
11
9
8
6
119
50
63
46
37
31
26
22
18
15
12
10
199
80
140
101
80
67
56
47
38
32
26
22
741
100
240
174
140
115
95
80
66
55
45
37
1280
Gas kind
Density kg/Nm3
Gas pressure MPa (gauge), temperature 20
°C
Reference: Gas viscosity
Argon
1.785
0.02
0.12
0.26
0.55
1.05
2
3.6
0.007 (mPa·s)
Air
1.293
0
0.07
0.20
0.4
0.85
1.5
2.7
0.017
Oxygen
1.429
0
0.05
0.17
0.35
0.75
1.35
2.5
4.4
0.0192
Carbon dioxide
1.977
0.01
0.1
0.23
0.5
0.95
1.7
3.3
0.0138
Nitrogen
1.251
0.07
0.21
0.42
0.85
1.55
2.8
0.0166
Nominal
diameter mm
Density
kg/m3
™Determination of minimum flow rate
In Table D, find a value that is nearest to and lower than
the pressure of gas desired, trace it upward in the same
column, and retain the value at the intersection with the
desired nominal diameter in Table C as minimum flow rate.
If it is necessary to exactly determine a minimum flow rate,
proceed to a calculation in the following manner.
Example 1
Suppose the fluid is air, the temperature 20
°C, the pres-
sure 0.5 MPa (gauge), and the nominal piping diameter
80 mm. How can the minimum flow rate nominal diam-
eter be found?
The minimum flow rate at nominal diameter of 80 mm at
air of 0.4 and 0.85 MPa in Table D is, according to Table
C, 47 and 38 m3/h, respectively. At a pressure of 0.5
MPa, therefore, the minimum flow rate is, according to
interpolation,
Or the minimum flow rate can be obtained upon calcu-
lating an actual density.
Actual density
ρ of air at 20°C and 0.5 MPa is:
From Table C, the minimum flow rate at density of 6 and
nominal diameter of 80 mm is 47 m3/h and, likewise, at
density of 11, is 38 m3/h. At density of 7.04, therefore,
the minimum flow rate is, according to interpolation,
Example 2
Suppose the fluid is carbon dioxide, the temperature 5
to 30
°C, the pressure 0.8 to 1.5 MPa, and the maximum
flow rate 800 m3/h (normal). How can the minimum flow
rate and the applicable nominal diameter be found? First
obtain the actual maximum flow rate, and then deter-
mine the nominal diameter. For calculating the maxi-
mum flow rate when the temperature and pressure have
ranges, retain the higher temperature and lower pres-
sure. Therefore, the actual maximum flow rate is:
Therefore, the nominal diameter is 40 mm. For obtain-
ing the minimum flow rate, retain the lower tempera-
ture and higher pressure.
From Tables C and D, the minimum flow rate at nominal
diameter of 40 mm and pressure of 0.95 MPa is 9 m3/h
or, at pressure of 1.7 MPa, is 8 m3/h. Therefore, accord-
ing to interpolation,
Note: If the calculated result has a value below decimal point, truncate it
for maximum flow rate, or round it up for minimum flow rate.
Table A (according to specific gravity)
Table B (according to viscosity)
0.85-0.5
Qmin = 38+
× (47-38)
45m3/h
0.85-0.4
273.15
0.1013+0.5
ρ = 1.293 ××
7.04kg/m3
273.15+20
0.1013
Qmin = 38+
× (47-38)
45m3/h
11-7.04
11-6
QMax. = 800
×
×
99m3/h
273.15
273.15+30
0.1013
0.1013+0.8
1.7-1.5
Qmin = 8+
× (9-8) 8.3m3/h
1.7-0.95
FLOW RATE RANGE [Table1]
¡Liquid
Retain the minimum flow rate in Tables A (according to specific gravity) and B (according to viscosity), whichever is the
greater.


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