Friday 10 April 2015

Comparison of Valve Actuator Features



Spring and diaphragm
Advantages:-
  • Lowest cost
  • Ability to throttle without positioner Simplicity
  • Inherent failure-mode action
  • Low supply-pressure requirement
  • Adjustability to varying conditions
  • Ease of maintenance
Disadvantages:-
  • Limited output capability
  • Large size and weight


High-pressure spring and diaphragm
Advantages:-
  • Compact, light weight 
  • No spring adjustment needed 
  • Costly cast components not needed 
  • Inherent fall-safe action
  • No dynamic stem seals or traditional stem connector block needed
  • Design can include integral accessories
Disadvantages:-
  • Requires high supply pressure 40 psig (2.8 bars) or higher
  • Positioner required for throtting

Pneumatic piston
Advantages:-


  • High force or torque capability 
  • Compact, light weight
  • Adaptable to high ambient temperatures 
  • Fast stroking speed 
  • Relatively high actuator stiffness
Disadvantages:-
  • Fall-safe requires accessories or addition of a spring
  • Positioner required for throttling
  • Higher cost
  • High supply-pressure requirement

Electric motor
Advantages:-

  • Compact 
  • Very high stiffness 
  • High output capability 
  • Supply pressure piping not required 
Disadvantages:-
  • High cost
  • Lack of fail-safe action
  • Limited duty cycle
  • Slow stroking speed

Electrohydraulic
Advantages:-
  • High output capability 
  • High actuator stiffness 
  • Excellent throtting ability 
  • Fast stroking speed 
Disadvantages:-
  • High cost
  • Complexity and maintenance difficulty
  • Fail-safe action only with accessories

Thursday 2 April 2015

Vortex flow meter



·         Vortex flow meter operates on the physical principle of the Karman vortex street. When a fluid flows pass a bluff body, vortices are alternately forced on the side of that body and then detached or shed by the flow.
·         The frequency of vortex shedding is proportional to the mean flow velocity and therefore the volumetric flow (with Reynolds > 4000) St = Fd/V
·         Vortex frequency = St.v/d
                 St = strouhal number (dimensionless)
                 v = velocity fluid (m/s)
                 d = width of bluff body (m)
·         Alternating pressure change caused by the vortex are transmitted via lateral port (sensor) into the bluff body.
·         The sensor detects the pressure pulses and converts these into electrical signals.
·         They are typically available in flange size from ½ inch to 12 inches.
·         In gas services frequencies are about 10 times higher than in liquid applications.
·         The proportionally between object width (d) and vortex street wavelength {(l) – (lambda)} is called the “strouhal number” (S), approximately equal to 0.17

 ls = d             l» d/0.17


Type of vortex flow meter sensor  

        i.Thermal sensing
      ii.Mechanical sensor
    iii.Capacitive sensor
    iv.Piezoelectric sensor
      v.Strain gauge sensor
    vi.Ultrasonic sensor


 Thermal sensor
·         Thermostats are using (negative temperature co-effective)

Mechanical sensor
·         Also called shuffle ball sensor
·         A magnetic ball or disc moves from side to side due to vortices.
·         This movement is detected by a magnetic pick up.
·         The main problem of stream the movement of the ball or disc can be slowed by condensation.

Capacitive sensor
·         A stain less steel diaphragms are welded onto the side of bluff body and the assembled filled with oil and sealed.
·         Purring vortex shedding diaphragm deflects and transfers through the internal port from one side to the other.
·         When diaphragm deflects there is a change in the capacitance between the diaphragm and electrodes.
·         Capacitance is inversely proportional to the distance between the electrodes and directly proportional to the plate area.
·         Modern capacitive sensors use with superheated steam for temperature upto 427° C.

Piezoelectric sensor
·         Piezo element produces voltage output that is proportional to applied pressure.
·         Whilst piezo ceramic material produces a high output it’s hawing limited operating temperature range (about 250° C).
·         Lithium niobate (linbo3) piezoelectric material offers only medium output but operating temperature range is above 300° C.
·         These type sensors are unsuitable for temp. below -40° C
·         This sensor same like capacitive sensor.

Strain gauge sensor.
·         The vortex created by bluff body causes the body itself to be displaced by small amount of the order of 10µm.
·         This elastic movement can be detected using strain gauges attached directly or indirectly to the bluff body.
·         Movement of the body produces a change in resistance of the strain gauge.
·         Main drawback is upper temperature limitation of strain gauge (about 120° C).

Ultrasonic sensing
·         Ultrasonic transmitter and receiver placed behind the bluff body.
·         The vortex modulates the ultrasonic beam and the resultant output is the vortex signal.
·         This sensor system has a good turn down ratio.
·         The main problem associated with this technique is that extraneous sound sources can affect measurement.


            The majority of vortex meter use piezoelectric or capacitance type sensor. to detect the pressure oscillation around  the bluff body. 
The strouhal number and bluff body width and the cross sectional area of the flow meter are all constants (which is defined as “K”) the equation becomes
                  Q = F/K
“K” factor can be defined as pulses per unit volume such as pulses per gallons, pulses per liter, pulses per cubic feet, therefore one can determine flow rate by counting the pulses per unit time.
Vortex frequencies range from one to thousands of pluses per second depending upon the flow viscosity the character of the process fluid and the size of meter.

Hints of vortex flow meter:
·         The pipe Reynolds number should be above 30,000 minimum. This means vortex meters can only be used on low viscosity liquids. High viscous fluids (>3 pa.s (30cp)) and slurries are not recommended applications. (higher viscous having head loss)
·         The vortex shedding meter provides a linear digital output signal without the use of separate transmitter or converters.
·         There is no drift because this is a frequency system
·         The calibration of the meter is virtually independent of the operating conditions (viscosity, density, pressure, temperature and so on) whether the meter is being used on gas or liquid.
·         Low pressure (low density) gases do not produce a strong enough pressure pulse, especially if fluid velocity are low (if use the meter will be poor and low flows will not be measurable.
·         Vortex meter accuracy is based on the known value of the meter factor (K- factor).