A demand = 1000 n/min (N)VBA2, (N)VBA4 C H A R G E C H A R A C T E R I S T I C S NVBA1 C H A R G E C H A R A C T E R I S T I C S Charging time for 10l t(s) Charging time for 10l t(s) Pressure increase ratio (P2/P1) Pressure increase ratio (P2/P1) These graphs illustrate the time required to inrease pressure in a closed tank e.g.
How to Find the Flow Rate (at air temperature of 20C) Subsonic flow when P1 + 0.1013 < 1.89 (P2 + 0.1013) Q = 226S P(P2 + 0.1013) Sonic flow when P1 + 0.1013 1.89 (P2 + 0.1013) Q = 113S (P1 + 0.1013) Q: Air flow rate [l/min (ANR)] S: Effective area (mm) P: Differential pressure (P1-P2) [MPa] P1: Upstream pressure [MPa] P2: Downstream pressure [MPa] Correction for different air temperatures
Copper/Fluorine/Silicone free + Low particle generation 21 Prefix the asterisk to the part no. of the solenoid valve, etc.
Copper/Fluorine/Silicone free + Low particle generation 21 Prefix the asterisk to the part no. of the solenoid valve, etc.
analog Nil 21 22 23 24 P kPa Applicable to plug connector.
When the work piece comes close to the detection nozzle, the back pressure P2 increases until it is larger than P1 (P2 P1). Then the switch output turns on to notify that the pressure is below the detection gap.
L dimension 135.5 9 123 8 160.5 11 148 10 185.5 13 173 12 210.5 15 198 14 235.5 17 223 16 19 248 18 20 260.5 285.5 21 273 No.
Example: The figure below is based on the condition of set values as P1 = 40[kPa] and P2 = 20[kPa].
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 60
How to Find the Flow Rate (at air temperature of 20C) Subsonic flow when P1 + 0.1013 < 1.89 (P2 + 0.1013) Q = 226S P(P2 + 0.1013) Sonic flow when P1 +0.1013 1.89 (P2 + 0.1013) Q = 113S (P1 + 0.1013) Q: Air flow rate [l/min(ANR)] S: Effective area (mm) P: Pressure drop (P1-P2) [MPa] P1: Upstream pressure [MPa] P2: Downstream pressure [MPa] Maintenance Correction for different air temperatures
VE How to Order Flow Characteristics VY1 12 AF 00 8 127 R Pressure drop (MPa) G P1 = 0.3 MPa P1 = 0.3 MPa Option P1 = 0.5 MPa P1 = 0.7 MPa P1 1 = 0.5 MP = 0.5 MPa P1 = 0.7 MP = 0.7 MPa P1 = 0.1 MPa P1 1 = 0.1 MPa Air filter PPA Drain cock thread piping {Rc 1/4} Drain guide D Body size 4 J R 8 9 1 2 1 2 AL Flow direction: From Right Left Auto-drain specifications Option Flow rate (/min (ANR
A port: n-Rc 1/8 Note for P1 Confirm internal pilot or common external pilot by checking whether P1 has a M5 screw or not. Internal pilot P1 has no M5 screw. Common external pilotP1 has an M5 screw.
)No LinkNo Activity BUS IN (P1) LinkNo Activity BUS IN (P1) Link Activity L/A2 BUS OUT (P2)No LinkNo Activity BUS OUT (P2) LinkNo Activity BUS OUT (P2) Link Activity 7.2 LED LED LED PWR ALM MS NS EtherNet/IP EEPROM : LED EEPROM (PWR()) * () -30- 8 8.1 No.
A Graph 1 Graph 2 120 60 110 B 100 50 C P1 63 63 90 80 40 70 Regulator Circuit C Load weight (kg) Load weight (kg) P2 60 30 50 50 A 50 Regulator valve 40 20 40 40 30 B 32 32 20 10 C P1 10 0 0 0.4 0.3 0.3 0.5 0.6 0.7 Operating pressure (MPa) 0.4 0.5 0.6 0.7 Operating pressure (MPa) Selection example Confirmation of allowable kinetic energy Selection conditions: Transfer direction: Vertical
OUT2 P2(n2) P1(n1) Supply pressure verification Leak test CH P2(n1) > P1(n2) 10.0 to 101.0 kPa Increases the set value 1 2 3 4 PRESSURE For normally closed P2(n2) P1(n1) P2(n1) > P1(n2) 0.1 to 1000.0 MPa Decreases the set value SET P3(n3) and P4(n4) are the same as P1(n1) and P2(n2).
Type (mm) 1in = 25.4mm PA3000 115 68 85 105 4-7 7.5 FLUID OUT 3/8 5.5 AIR SUP (P1) 1/4 FLUID OUT PROCESS PUMP P1 2 90 74.5 FLUID I N P2 44.5 3 AIR SUP (P2) 32 1/4 100 130 FLUID IN 3/8 PA5000 179 4-9 90 90 FLUID OUT 1/2, 3/4 AIR SUP (P1) 1/4 112 56 165 56 RESET PROCESS PUMP FLUID OUT 167 P1 132.5 FLUID I N 125.5 103.5 P2 58.5 48.5 202 114 3.5 3 AIR SUP (P2) FLUID IN 1/2, 3/4 1/4 10 Series
Type PA3000 115 68 85 105 4-7 7.5 FLUID OUT Rc 3/8 5.5 AIR SUP (P1) Rc 1/4 FLUID OUT PROCESS PUMP P1 2 90 74.5 FLUID I N P2 44.5 3 AIR SUP (P2) 32 Rc 1/4 100 130 FLUID IN Rc 3/8 PA5000 179 4-9 90 90 FLUID OUT Rc 1/2, 3/4 AIR SUP (P1) Rc 1/4 112 56 165 56 RESET PROCESS PUMP FLUID OUT 167 P1 132.5 FLUID I N 125.5 103.5 P2 58.5 48.5 202 114 3.5 3 AIR SUP (P2) FLUID IN Rc 1/2, 3/4 Rc 1/4 10
Type PA3000 115 68 85 105 4-7 7.5 FLUID OUT Rc 3/8 5.5 AIR SUP (P1) Rc 1/4 FLUID OUT PROCESS PUMP P1 2 90 74.5 FLUID I N P2 44.5 3 AIR SUP (P2) 32 Rc 1/4 100 130 FLUID IN Rc 3/8 PA5000 179 4-9 90 90 FLUID OUT Rc 1/2, 3/4 AIR SUP (P1) Rc 1/4 112 56 165 56 RESET PROCESS PUMP FLUID OUT 167 P1 132.5 FLUID I N 125.5 103.5 P2 58.5 48.5 202 114 3.5 3 AIR SUP (P2) FLUID IN Rc 1/2, 3/4 Rc 1/4 10
Type) Dimensions: Air Operated Type PA3000 115 68 85 VC VDW 105 4-7 7.5 VQ FLUID OUT Rc 3/8 5.5 VX2 AIR SUP(P1) Rc 1/4 VX Courtesy of Steven Engineering, Inc.-230 Ryan Way, South San Francisco, CA 94080-6370-Main Office: (650) 588-9200-Outside Local Area: (800) 258-9200-www.stevenengineering.com FLUID OUT PROCESS PUMP VX3 P1 2 VXA 90 74.5 FLUID I N VN P2 44.5 3 32 Rc 1/4 AIR SUP(P2) LVC
Pmax Vacuum pressure P1 Qmax Q1 How to Read the Time to Reach Vacuum Suction flow rate The graph indicates the time required to reach a vacuum pressure determined by adsorption conditions for workpieces, etc., starting from atmospheric pressure in a 1 L sealed tank.