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PROPER CONTROL VALVE SELECTION -
AN ENGINEER’S PERSPECTIVEDOUG SHOWERS, PE
NOVEMBER 12, 2018
MADISON ASHRAE CHAPTER MEETING
LEARNING OBJECTIVES
• BETTER UNDERSTANDING OF CONTROL VALVE FUNCTION
• REVIEW OF CONTROL VALVE OPTIONS
• SELECTING THE RIGHT VALVE
• SIZING CONTROL VALVES
• WHEN TO USE PRESSURE INDEPENDENT CONTROL (PIC) VALVES
BETTER UNDERSTANDING OF CONTROL VALVE FUNCTION
• FLOW CONTROL (2-POSITION – OPEN/CLOSED)
• TEMPERATURE CONTROL (MODULATION OF FLOW TO AFFECT ENERGY TRANSFER)
• PRESSURE CONTROL (MODULATION OF FLOW TO AFFECT PRESSURE OR PRESSURE
DIFFERENTIAL AT A GIVEN POINT)
• COMBINATION TEMPERATURE/PRESSURE CONTROL
• CONTROL VALVES CAN CHANGE THE FLOW RESISTANCE OF THE SUB-CIRCUIT ONLY!
• INDIRECTLY AFFECTS FLOW IN OTHER PARTS OF THE SYSTEM.
SupplyReturn
A BCoil / Heat
Exchanger
Best location
Sub-circuit A-B
TEMPERATURE CONTROL VALVE FUNCTION
SupplyReturn
A B
Sub-circuit A-B
PRESSURE CONTROL VALVE FUNCTION
PDT
SupplyReturn
A BCoil / Heat
Exchanger
Sub-circuit A-B
TEMPERATURE/PRESSURE CONTROL VALVE
FUNCTION
PIC
Pressure
Flow
ControlValve Pressure Drop
Coil and Sub-Circuit PipingPressureDrop
Cons
tant
Pre
ssur
eTEMPERATURE CONTROL VALVE FUNCTION
VALVE CHARACTERISTICS
FROM 2016 ASHRAE SYSTEM HANDBOOKCH. 47
VALVE CHARACTERISTICS
Combined with Heating Coil PerformanceFROM 2016 ASHRAE SYSTEM HANDBOOKCH. 47
REVIEW OF CONTROL VALVE OPTIONS
• VALVE BODY STYLES AND MATERIALS
• PORT SHAPES/CHARACTERISTICS
• ACTUATOR TYPES/FAIL POSITIONS
½” TO 2” BRONZE BALL VALVES• USED FOR MODULATING OR SHUTOFF SERVICE
• BODIES:
• AVAILABLE IN 2 PORT, 3-PORT MIXING, AND 3-PORT DIVERTING CONFIGURATIONS
• NPT OR SWEAT END CONNECTIONS
• CLASS 125 TO 250 PSIG WORKING PRESSURE (FUNCTION OF FLUID TEMPERATURE)
• AVAILABLE IN STAINLESS STEEL FOR CERTAIN APPLICATIONS
• BALL/PORT CHARACTERISTICS
• NORMAL, FULL, EQUAL PERCENTAGE
• BALL MATERIALS – BRASS, CHROME-PLATED BRASS, STAINLESS STEEL
• SEALS
• EPDM, VITON
• TEMPERATURE RANGES (0OF TO 250OF)
• CLOSE OFF PRESSURE – APPROX. 200 PSI
• FAIL OPEN, FAIL CLOSED, FAIL LAST POSITION
• COMMERCIAL VALVES VS. INDUSTRIAL GRADE VALVES
• STEAM AND CRYO SERVICE OPTION MAYBE AVAILABLE FOR INDUSTRIAL VALVES
2-1/2” TO 6” IRON/STEEL BODY BALL VALVES• USED FOR MODULATING OR SHUTOFF SERVICE
• BODIES:
• AVAILABLE IN 2 PORT, 3-PORT MIXING, AND 3-PORT DIVERTING CONFIGURATIONS
• NPT OR CLASS 150/300 ASME FLANGED END CONNECTIONS
• CLASS 150 TO 275 PSIG WORKING PRESSURE (FUNCTION OF FLUID TEMPERATURE)
• AVAILABLE IN CAST IRON, CAST STEEL OR CAST STAINLESS STEEL
• BALL/PORT CHARACTERISTICS
• NORMAL, FULL, EQUAL PERCENTAGE
• BALL MATERIALS – BRASS, CHROME-PLATED BRASS, STAINLESS STEEL
• SEALS
• EPDM, VITON
• TEMPERATURE RANGES (0OF TO 250OF)
• CLOSE OFF PRESSURE – APPROX. 200 PSI
• NORMALLY FAIL IN LAST POSITION UNLESS SPRING LOADED OR BATTERY OPERATED ACTUATOR IS USED
• COMMERCIAL VALVES VS. INDUSTRIAL GRADE VALVES
½” TO 2” BRONZE GLOBE VALVES• USED FOR MODULATING OR SHUTOFF SERVICE
• BODIES:
• AVAILABLE IN 2 PORT, 3-PORT MIXING, AND 3-PORT DIVERTING CONFIGURATIONS
• NPT OR SWEAT END CONNECTIONS
• CLASS 125 TO 250 PSIG WORKING PRESSURE (FUNCTION OF FLUID TEMP)
• AVAILABLE IN CAST STEEL OR CAST STAINLESS STEEL FOR INDUSTRIAL VAVLES
• PORT CHARACTERISTICS
• EQUAL PERCENTAGE, LINEAR, QUICK OPENING
• CAGE-GUIDED VALVES
• SEALS
• EPDM, VITON
• TEMPERATURE RANGES (0OF TO 250OF)
• CLOSE OFF PRESSURE – APPROX. 4 TO 365 PSI (FUNCTION OF VALVE SIZE AND ACTUATOR TYPE)
• COMMERCIAL VALVES VS. INDUSTRIAL GRADE VALVES
• STEAM AND CRYO SERVICE OPTION MAYBE AVAILABLE FOR INDUSTRIAL VALVES
2-1/2” TO 6” IRON/STEEL BODY GLOBE VALVES• USED FOR MODULATING OR SHUTOFF SERVICE
• BODIES:
• AVAILABLE IN 2 PORT, 3-PORT MIXING, AND 3-PORT DIVERTING CONFIGURATIONS
• CLASS 125 ASME FLANGED END CONNECTIONS
• CLASS 125 TO 250 PSI WORKING PRESSURE FOR CAST IRON (FUNCTION OF FLUID TEMPERATURE)
• CLASS 150 TO 275 PSI WORKING PRESSURE FOR CAST STEEL (FUNCTION OF FLUID TEMPERATURE)
• PORT CHARACTERISTICS
• EQUAL PERCENTAGE, LINEAR, QUICK OPENING
• CAGE-GUIDED VALVES
• SEALS
• EPDM, VITON
• TEMPERATURE RANGES (0OF TO 250OF NORMAL, UP TO 400OF WITH SEAL SEATS AND TRIM)
• CLOSE OFF PRESSURE – APPROX. 20 TO 80 PSI (FUNCTION OF VALVE SIZE AND ACTUATOR TYPE)
• COMMERCIAL VALVES VS. INDUSTRIAL GRADE VALVES
• STEAM AND CRYO SERVICE OPTION MAYBE AVAILABLE FOR INDUSTRIAL VALVES
GENERAL PURPOSE BUTTERFLY VALVES (2” TO 60”)• USED FOR SHUTOFF SERVICE (NOT RECOMMENDED FOR MODULATING SERVICE)
• BODIES:
• CAST IRON, DUCTILE IRON, CAST STEEL, ALUMINUM
• AVAILABLE IN 2 PORT AND 3-PORT (2-VALVES LINKED TOGETHER) CONFIGURATIONS
• CLASS 125 OR 250 ASME FLANGED END CONNECTIONS FOR CAST IRON
• CLASS 150 OR 300 ASME FLANGED END CONNECTIONS FOR CAST STEEL
• PORT CHARACTERISTICS
• QUASI-EQUAL PERCENTAGE, QUICK OPENING
• SEALS
• EPDM, VITON
• TEMPERATURE RANGES (0OF TO 250OF)
• CLOSE OFF PRESSURE – UP TO 175 PSI (FUNCTION OF VALVE SIZE AND ACTUATOR TYPE)
• COMMERCIAL VALVES VS. INDUSTRIAL GRADE VALVES
• STEAM AND CRYO SERVICE OPTION MAYBE AVAILABLE FOR INDUSTRIAL VALVES
HIGH PERFORMANCE BUTTERFLY VALVES (2” – 54”)
• USED FOR MODULATING OR SHUTOFF SERVICE
• RELATIVELY HIGH CV VALUES
• BODIES:
• AVAILABLE IN 2 PORT AND 3-PORT (2-VALVES LINKED TOGETHER) CONFIGURATIONS
• CLASS 150 OR HIGHER ASME FLANGED END CONNECTIONS (FUNCTION OF FLUID TEMPERATURE)
• AVAILABLE HIGHER PRESSURE CLASSES USING CAST STEEL OR CAST STAINLESS STEEL FOR INDUSTRIAL VAVLES
• PORT CHARACTERISTICS
• QUASI-EQUAL PERCENTAGE, QUICK OPENING
• SEALS
• METAL, BUTYL, EPDM, VITON
• TEMPERATURE RANGES (0OF TO 500OF)
• CLOSE OFF PRESSURE – UP TO 1480 PSI (FUNCTION OF VALVE SIZE, PRESSURE CLASS AND ACTUATOR TYPE)
• STEAM AND CRYO SERVICE OPTION MAYBE AVAILABLE FOR CERTAIN VALVES
PRESSURE INDEPENDENT CONTROL (PIC) VALVES(1/2” – 16”)
• USED FOR MODULATING
• BODIES:
• SAME AS BALL OR GLOVE VALVE OPTIONS
• CAN BE TWO VALVES IN SERIES WITH PRESSURE CONTROL VALVE/DEVICE UPSTREAM OF CONTROL VALVE
• PORT CHARACTERISTICS
• EQUAL PERCENTAGE
• SEALS
• EPDM
• TEMPERATURE RANGES (0OF TO 250OF)
• PRESSURE CONTROL DEVICE
• SPRING LOADED PRESSURE DIAPHRAGM
• ACTIVE CONTROL VALVE
• CLOSE OFF PRESSURE – APPROX. 200 PSI (FUNCTION OF VALVE SIZE AND ACTUATOR TYPE)
ACTUATORS• MOVEMENT TYPE (LINEAR VS ROTARY)
• LINKAGES TO ACHIEVE MOVEMENT OF EITHER TYPE
• ENERGY SOURCE
• COMPRESSED AIR (15 TO 100 PSIG)
• LOW VOLTAGE (24 VAC)
• FLOATING POINT VS ANALOG
• WITH OR WITHOUT FEEDBACK
• LINE VOLTAGE (120 OR 240 VAC)
• MOVEMENT ACTION – 2-POSITION OR MODULATING
• FAIL POSITION
• SPEED OF ACTUATORS
• TIME DELAYS
• FEEDBACK OPTIONS
• OPEN/CLOSED POSITION SWITCHES FOR 2-POSITION VALVES
• ANALOG FOR MODULATING VALVES
SELECTING THE RIGHT VALVE
• SERVICE – MODULATING, SHUTOFF
• DESIRED PORT CHARACTERISTICS
• EQUAL PERCENTAGE
• LINEAR
• QUICK OPENING
• PRESSURE/TEMPERATURE CLASS
• SHUTOFF PRESSURE
• DIFFERENTIAL VS DEAD-END
ASME/ANSI PRESSURE CLASS
SELECTING THE RIGHT VALVE
• CHARACTERIZED BALL VALVE
• ROTARY VALVE (90 DEGREE ROTATION)
• MORE FLOW THAN A GLOBE VALVE AT THE SAME SIZE
• LARGER CV
• BETTER SHUTOFF
• LARGE GLOBE VALVE = POOR SHUTOFF
• RECOMMEND USING MULTIPLE SMALLER CHARACTERIZED BALL VALVES INSTEAD
SELECTING THE RIGHT VALVE
SELECTING THE RIGHT VALVE
• COMMERCIAL VALVES
• SOME OPTIONS
• TRIM TYPE, MATERIAL
• SPRING RETURN, VOLTAGE, SIGNAL TYPE, FEEDBACK
• INDUSTRIAL VALVES
• MANY OPTIONS
• DIFFERENT TRIM TYPES TO REDUCE NOISE OR HANDLE CAVITATION, VALVE MATERIALS
• SELECTION SOFTWARE AVAILABLE FOR USE
• SMART VALVE POSITIONERS
• HART COMMUNICATION, DIAGNOSTICS
SELECTING THE RIGHT VALVE
VALVE TYPE RECOMMENDED FLUIDS SIZE RANGE CV RANGE
SHUTOFF
PRESSURE
RELATIVE
COST
BRONZE BALL VALVE WATER <200oF, LPS 1/2" - 2" 1.2 - 77 200 LOW
CI/CS BALL VALVE WATER <200oF, LPS 2" - 12" 16 - 4200 200 MED-HIGH
BRONZE GLOBE VALVE WATER <200oF, LPS 1/2" - 2" 0.7 - 46 4 - 80 LOW
CI/CS GLOBE VALVE WATER <250oF, LPS, HPS 2 - 6" 51 - 347 4 - 100 MED-HIGH
PIC VALVE WATER <200oF 1/2" - 16" 3.4 - 2460 200 MED-HIGH
GP BUTTERFLY VALVE WATER <200oF, LPS 2-1/2" - 60" 300 - 190,000 175 LOW
HP BUTTERFLY VALVE WATER <400oF, LPS, HPS 2" - 60" 160 - 160,000 600 HIGH
NOTE - ALL VALUES VARY BY MANUFACTURER
VALVE COMPARISON TABLE
SIZING CONTROL VALVES
• VALVE AUTHORITY
• SIZE FOR 25-50% VALVE AUTHORITY
• THIS MEANS THAT 25-50% OF THE SUBCIRCUIT PRESSURE DROP IS DUE TO THE VALVE
• OVERSIZED VALVES HAVE POOR VALVE AUTHORITY
• VALVE PRESSURE DROP △P = FUNCTION OF FLOW (Q) , SPECIFIC GRAVITY (SG), AND FLOW
COEFFICIENT CV
• CV = Q (SG/△P)0.5 OR △P = SG (Q/CV)2
• FOR WATER (SG=1), CV = FLOW (GPM) AT 1 PSI PRESSURE DROP
CONTROL VALVE AUTHORITY
• CONTROL VALVE AUTHORITY (N) = RATIO OF VALVE △P/SUBCIRCUIT △P
• IDEAL AUTHORITY IS WHEN N < 0.5
• 0.25 < N < 0.5 IS USUALLY ACCEPTABLE
• UNSTABLE CONTROL RESULTS WHEN N < 0.25
• OVERSIZED VALVES RESULT IN LOW VALVE AUTHORITY
• CAN ALSO BE DESCRIBED AS TOO MUCH GAIN IN THE VALVE
SIZING CONTROL VALVES
• RULES OF THUMB FOR TERMINAL DEVICES
• SUBCIRCUIT △P USUALLY < 10 FT. (4.3 PSI)
• SIZE MOST VALVES FOR △P BETWEEN 1.5 AND 2.2 PSI BUT NO LOWER THAN 1.1 PSI FOR GOOD
CONTROL AUTHORITY
• SOME UH/CUH COULD HAVE SUBCIRCUIT △P AS HIGH AS 25 FT (10.8 PSI)
• SIZE UH/CUH VALVES FOR △P BETWEEN 3 AND 5 PSI BUT NO LOWER THAN 2.7 PSI FOR GOOD
CONTROL AUTHORITY
SIZING CONTROL VALVES
• PRIMARY EQUIPMENT
• SUBCIRCUIT △P CAN VARY BETWEEN 10 AND 40 FT (4.3 – 17.3 PSI)
• 1-2 ROW HEATING COILS ARE AT THE LOWER RANGE
• 6-10 ROW COOLING COILS ARE AT THE HIGHER RANGE
• FOR ACCURATE SIZING, CONSIDER DETERMINING SUBCIRCUIT PRESSURE DROP AND SELECTING VALVE FOR UP TO 50% OF SUBCIRCUIT △P.
• RULE-OF-THUMB METHOD:
• SIZE HEATING VALVES FOR △P BETWEEN 3 AND 5 PSI BUT NO LOWER THAN 3 PSI FOR GOOD CONTROL AUTHORITY
• SIZE COOLING VALVES FOR △P BETWEEN 3 AND 9 PSI BUT NO LOWER THAN 3 PSI FOR GOOD CONTROL AUTHORITY
SIZING CONTROL VALVES
INSTALLATION
• RULE OF THUMB IS NO MORE THAN TWO SIZES SMALLER THAN PIPE
• IF MORE THAN 2 SIZES, NEED STRAIGHT PIPE UPSTREAM AND DOWNSTREAM VALVE TO AVOID
CAVITATION
• NO AGREEMENT ON STANDARDS OR RULES
• CONTROL VALVE TEST STANDS HAVE AS MUCH AS 20D UPSTREAM AND 10D DOWNSTREAM
• USUALLY NOT PRACTICAL IN THE REAL WORLD
• BEST PRACTICE IS TO HAVE 2/3 OF STRAIGHT RUN UPSTREAM OF VALVE
CAVITATION, FLASHING AND CHOKED FLOW
• CAVITATION AND FLASHING
• CAVITATION AND FLASHING OCCURS
WHEN PRESSURES WITHIN THE VALVE
(@ P2 LOW - BEFORE RECOVERY)
DROPS BELOW THE VAPOR PRESSURE
OF THE FLUID AT A GIVEN
TEMPERATURE
• CHOKED FLOW FOR NON-
COMPRESSIBLE LIQUIDS OCCURS AS A
RESULT OF CAVITATION OR FLASHING
• CHOKED FLOW FOR COMPRESSIBLE
GASES OCCURS WHEN VELOCITY
THROUGH THE PORT REACHES MACH 1
CAVITATION, FLASHING, AND CHOKED FLOW
WHEN TO USE PRESSURE INDEPENDENT CONTROL (PIC) VALVES
• FOR LARGE UNBALANCED SYSTEMS
• FOR SYSTEMS WHERE LOAD OR △P VARIES
• PROPERLY SIZED PRESSURE DEPENDENT VALVE CAN ACCOMPLISH THE SAME THING
• RESPONSE MAY BE SLOWER
• CONSIDER WHETHER TO USE ON ENTIRE SYSTEM OR ONLY LARGE VALVES
• NECESSARY FOR TERMINAL VALVES TO BE PRESSURE INDEPENDENT?
• COST IS MORE COMPETITIVE THAN IN THE PAST