Honeywell SMV 3000 사용자 설명서
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SMV 3000 Transmitter User’s Manual
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Appendix B– Configuration Record Sheet,
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2. Flow - PV4 - Configuration Section
(If using SMV 3000 for PV1, PV2 and PV3 measurement only, do not complete flow section.)
(If using SMV 3000 for PV1, PV2 and PV3 measurement only, do not complete flow section.)
2a. Dynamic Flow Compensation Section
(If you are using a primary element that is not listed, use the Standard Flow Equation Section below.)
(If you are using a primary element that is not listed, use the Standard Flow Equation Section below.)
Flow Element Type:
Orifice - Flange Taps (ASME-ISO) D >/= 2.3 inches
Orifice - Flange Taps (ASME-ISO) D >/= 2.3 inches
_____
Orifice - Flange Taps (ASME-ISO) 2 </= D </= 2.3
_____
Orifice - Corner Taps (ASME-ISO)
_____
Orifice - D and D/2 Taps (ASME-ISO)
_____
Orifice - 2.5D and 8D Taps (ASME-ISO)
_____ (Liquids only)
Venturi - Machined Inlet (ASME-ISO)
_____ (Liquids only)
Venturi - Rough Cast Inlet (ASME-ISO)
_____ (Liquids only)
Venturi - Rough W elded Sheet-Iron Inlet (ASME-ISO) _____ (Liquids only)
Nozzle (ASME Long Radius)
Nozzle (ASME Long Radius)
_____ (Liquids only)
Venturi nozzle (ISA Inlet)
_____ (Liquids only)
Leopold venturi
_____ (Liquids only)
Gerand venturi
_____ (Liquids only)
Universal Venturi Tube
_____ (Liquids only)
Lo-Loss Venturi Tube
_____ (Liquids only)
Preso Ellipse Ave. Pitot Tube
_____ (Specify 7/8”, 1.25” or 2.25” Probe diameter)
Material ____________
Bore Diameter (inches at 68 deg. F) ___________ (not required for Pitot Tube)
Design Temperature ______________ (not required for Pitot Tube)
Bore Diameter (inches at 68 deg. F) ___________ (not required for Pitot Tube)
Design Temperature ______________ (not required for Pitot Tube)
Fluid State:
Gas _____
Liquid _____
Steam _____
Fluid Name:
________________________________________________
Pipe Properties:
Material __________
Pipe Schedule ______
Pipe Diameter _________
Isentropic Exponent:
_____________ (not required for Liquid applications or Pitot Tube)
2b. Standard Flow Compensation Section
(Standard equation should be used for any primary element not listed in Dynamic Flow Section above.)
(Standard equation should be used for any primary element not listed in Dynamic Flow Section above.)
Fluid State:
Gas _____
Liquid _____
Steam _____
Fluid Name:
________________________________________________
Flow Data: (obtained from Primary Element Sizing Sheet)
Normal Flowrate __________________
Normal Flowrate __________________
Design Pressure
_____________(Gas applications only)
Normal Diff. Pressure_________________ Design Temperature ________________ (Gas applications only)
Design Density ___________________ (required only for Steam and Liquid applications)
Standard Density __________________ (required only for Standard Volume equations)
Design Density ___________________ (required only for Steam and Liquid applications)
Standard Density __________________ (required only for Standard Volume equations)
Flow Compensation:
None ___
Full ___
Pressure Only ___
Temperature Only___
Flow Data: (obtained from Primary Element Sizing Sheet)
Design Pressure __________________ (required only for Gas applications)
Design Temperature ________________ (required only for Gas applications)
Design Density ___________________ (required only for Steam applications)
Standard Density __________________ (required only for Standard Volume equations)
Design Pressure __________________ (required only for Gas applications)
Design Temperature ________________ (required only for Gas applications)
Design Density ___________________ (required only for Steam applications)
Standard Density __________________ (required only for Standard Volume equations)
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