Teledyne hfc-302 ユーザーズマニュアル

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Manual: 151-082010 300-302 Series
  
Page 12 of 31 
 
The first method requires that the two controllers use the same signal range (0 to 5 VDC or 4 to 20 mA) 
and that they be sized and calibrated to provide the correct ratio of gasses. Then, by routing the 
actual flow Output signal from the primary meter/controller through the secondary controller’s 
External Input pin (See Tables 2.1 & 2.2), the ratio of flows can be maintained over the entire range of 
gas flows. 
EXAMPLE:  Flow controller A has 0-100 slpm range with a 5.00 volt output at full scale.  Flow 
controller B has 0-10 slpm range with a 5.00 volt output at full scale.  If flow controller A is set at 80 
slpm, its output voltage would be 4.00 volts (80 slpm/100 slpm x 5.00 volts = 4.00 volts).  If the output 
signal from flow controller A is connected to the command Set Point
 
of flow controller B, then flow 
controller B becomes a slave to the flow signal of controller A. The resultant flow of controller B will 
be the same proportion as the ratio of the flow ranges of the two flow controllers. 
If the set point of flow controller A is set at 50% of full scale, and the reference voltage from flow 
controller A is 2.50, then the command signal going to flow controller B would be 2.50 volts .  The flow 
of gas through flow controller B is then controlled at 5 slpm (2.50 volts/5.00 volts x 10 slpm = 5 slpm). 
The ratio of the two gases is 10:1 (50 slpm/5slpm).  The % mixture of gas A is 90.9090 (50slpm/55 slpm 
and the % mixture of gas B is 0.09091% (5 slpm/55 slpm).   
Should the flow of flow controller A drop to 78 slpm, flow controller B would drop to 3.9 slpm, hence 
maintaining the same ratio of the mixture.  (78 slpm/100slpm x 5v = 3.90v x 50% = 1.95v; 1.95v/5.00v 
x 10 slpm = 3.9 slpm; 78 slpm: 3.9 slpm = 20:1) 
In the blending of two gases, it is possible to maintain a fixed ratio of one gas to another.  In this case, 
the output of one flow controller is used as the reference voltage for the set point potentiometer of a 
second flow controller.  The set point potentiometer then provides a control signal that is proportional 
to the output signal of the first flow controller, and hence controls the flow rate of the second gas as a 
percentage of the flow rate of the first gas. 
2.7. Output  Filter 
The output signal may have noise superimposed on the mean 
voltage levels.  This noise may be due to high turbulence in 
the flow stream that the fast sensor is measuring or it could 
be electrical noise when the flow meter has a high internal 
gain.  i.e. 5 sccm full scale meter.  Varying levels of radio 
frequency noise or varying airflow over the electronics cover 
can also induce noise. 
Noise can be most pronounced when measuring the flow 
output with a sampling analog/digital (A/D) converter.  
When possible, program the system to take multiple samples 
and average the readings to determine the flow rate.   
If less overall system noise is desired, a jumper may be 
installed over the pins of JP-1 on the flow measurement 
card. See Figure 2.6. Covering the pins closest to the “D” 
connector will activate a resistor-capacitor (RC) filter that 
has a time constant of one second. This will increase the 
settling time of the indicated flow rate to approximately 4 seconds. Covering the other two pins will 
lower the response time to approx. 1 second. This adjustment will not affect the calibration of the 
flow meter circuit or the actual flow response to change in command signal (flow controllers).  This 
will only slow down the indicated response (output voltage/current). 
2.8. Controlling Other Process Variables 
Normally, a flow controller is setup to control the mass flow.  The control loop will open and close the 
valve as necessary to make the output from the flow measurement match the input on the command 
line.  Occasionally, gas is being added or removed from a system to control some other process 
variable.  This could be the system pressure, oxygen concentration, vacuum level or any other 
parameter which is important to the process.  If this process variable has a sensor that can supply an 
analog output signal proportional to its value then the flow controller may be able to control this 
JP-1 
Fig. 2.6