Primary head vfs 1000 (i) – KROHNE VFM 1091 User Manual

Page 35

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Primary head VFS 1000 (I)

Versions and meter sizes

Pressure ratings see “Dimensions” Table

(Note operating limits given in DIN 2501 and ANSI B 16.5)

Sandwich design to ... DIN 19205

DN 25 to 150

ANSI

1”

to

6”

Flange connections to ...DIN 2501

DN 10S to 200

ANSI B 16.5

3/8”S TO 8”

Groove joint to...

DIN 2515

DN 25 TO 150

(Optional) ANSI

1” to 6”

Process and ambient temperature

see

Diagram

III





















1

Housing

SR.NO. DESCRIPTION MATERIAL REMARKS

GASKET, TEFLON (PTFE)

GASKET, STYLE AF-160, NON
ASBESTOS

5. Gaskets GASKET, STYLE AF-139, NON

ASBESTOS Any one as per application

M10 = 5.5 kg - m

M8 = 2 kg - m

4. Bluff body metal seal C ring Inconel Ni plated Once used metal C ring shoul

d

not be used again. Tightening

torques for new seals are

m

M6 = 1.5kg -

3.

a. upto 180 deg C(356deg.F) Viton O ring Non steam applications

Seals

b. upto 220deg C(428deg.F) Kalrez 4079 O ring Non steam applications

c. upto 240deg C(464deg.F) Parofluor O ring Steam applications

2. Vortex shedding body Unalloyed Titanium (No.3.7035) as standard

Stainless Steel, A351 CF3M (316L) Upto size DN100/4''

Stainless Steel, A351 CF8 (304) From DN150/6'' to DN200/8''

Materials

Max. allowable operating pressure (primary head) 40 bar (580 psig), optionally upto 100 bar (1450 psig)

Hazardous Duty Versions: FM, CSA, PTB approvals pending.

Error limits

Measuring error (in linear range)

± 1 % of measured value for DN 25 (1”) & above
± 2 % of measured value for DN 10S (3/8”S) to DN 20 (3/4”)

Repeatability (in measuring range)

± 0.5 % of measured value

Temperature Error

- 0.025 % of measured value per 10Kelvin (50

o

F) variation

Pressure loss

D

p

at normal conditions
for air[1.013 bar (14.7psig)/0

o

c(32

o

F) /

r

n

= 1.29 kg/m(0.081 lbs/ft)]

see Diagram I

for water [20

o

C (68

o

F) /

r

n

= 998.2 kg/m (63.32 lbs/ft)]

see Diagram II DP = Pressure loss in Pa

at operating conditions

C = A constant

for

gases

and

liquid

DP=

C

*

Q

v

2

*

r

op

(values:

see

Table)

Qv = Flow rate in m/hr

for saturated steam

DP = C * Qm2 Qm = Flow rate in kg/hr

r

op

r

op

=operating density in kg/m

35

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