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INSTRUMENT
I
NSTRUMENT FOR OPERAT
I
ON
What are the four parameter ?
Pressure
Level
Flow
Temperature
pressure
What is pressure?
šŸ ¶ T
he force acting unit area.
šŸ ¶ How calculate the pressure?
š¹
šŸ ¶ P=
š“
š‘
=
= = Pa
š‘€2
šŸ ¶ Example : if the f=50n & A=2.5š‘š2 find the p=?
pressure
šŸ ¶ Units of pressure
šŸ ¶ Kpa
šŸ ¶ KG/CM2
šŸ ¶ BAR
šŸ ¶ PSI ( pound per square inch)
šŸ ¶ mmH2O
šŸ ¶ mmHg
šŸ ¶ inH2O
šŸ ¶ inHg
šŸ ¶ Use the convert table
pressure
Units kPa Pa Bar
Std.
Atm.
psi Kg/cmĀ² mmH2O mmHg inHg inH20
kPa =1= 1000 0.01 0.0098692 0.145 0.0101972 101.9716 7.50062 0.2953 4.0146
Pa 0.001 =1= 0.00001 0.0000098 0.000145
0.0000101
97
0.1019716 0.007501 0.0002953 0.0040146
Bar 100 100,000 =1= 0.98692 14.5 1,019716 10,197.16 750.062 29.53 401.46
Std.
Atm
.
101.325 101,325 1.01325 =1= 14.696 1.033228 10,332.28 760 29.92 406.78
psi 6.89476 6,894.76 0.06895 0.068046 =1= 0.070307 703.072 51.715 2.036 27.68
Kg/cmĀ² 98.0665 98,066.5 0.980665 0.967841 14.22 =1= 10,000 735.559 28.96 393.70
mmH20 0.0098067 9.80665 0.0000981 0.0000967 0.001422 0.0001 =1= 0.0735559 0.002896 0.03937
mmHg 0.1333224 133.3224 0.0013332 0.0013158 0.0193 0.0013595 13.5951 =1= 0.03937 0.53524
inHg 3.3864 3,3864 0.033864 0.03342 0.491 0.03453 345.3155 25.4 =1= 13.5951
inH2O 0.24909 249.09 0.002491 0.00246 0.0361 0.00254 25.4 1.8683 0.0735559 =1=
pressure
šŸ ¶ Type of pressure
šŸ ¶ Atmospheric pressure
šŸ ¶ Absolute pressure
šŸ ¶ Vacuum pressure
šŸ ¶ Pressure Gauge
šŸ ¶ Differential pressure
pressure
šŸ ¶ To calculate absolute pressure
šŸ ¶ Abs =Atm +Pg when Pg < 14.7 psi
šŸ ¶ Abs =Atm - Pg when Pg > 14.7 psi
pressure
šŸ ¶ Sensor & Device
šŸ ¶ Manometer
šŸ ¶ Pressure gauge
šŸ ¶ Differential pressuretransmitter
pressure
šŸ ¶ Manometer
pressure
šŸ ¶ Digital Pressure gauge
pressure
šŸ ¶ Pressure gauge
Pressure
šŸ ¶ Differential pressure transmitter
FLOW
šŸ ¶ What is flow?
šŸ ¶ T
he amount of liquid passes through a system
šŸ ¶ How calculate the flow?
šŸ ¶ Q= V *A
šŸ ¶ Where flow rate (Q) =flow velocity (V) Ɨpipe area (A)
šŸ ¶ Q=K* ā„Ž
FLOW
šŸ ¶ Units of flow
šŸ ¶ Liter/min
šŸ ¶ m3/hr
šŸ ¶ cut/sec
šŸ ¶ Kg/sec
šŸ ¶ tans/hr
šŸ ¶ gallon/min
FLOW
šŸ ¶ FlowMeasurement
šŸ ¶ a- Primary element
šŸ ¶ b- Secondary
FLOW
šŸ ¶ a- Primary element
šŸ ¶ Venturi
šŸ ¶ Orifice
šŸ ¶ Flownozzle
FLOW
šŸ ¶ Venturi:
šŸ ¶ The Venture tube has particular advantages:
šŸ ¶ Efficiency ā€“they have very low pressurelosses
šŸ ¶ High accuracy
šŸ ¶ Suitability for fluids with suspended solids
šŸ ¶ The disadvantages of the Venture tube are:
šŸ ¶ Cost
šŸ ¶ S
ize ( length )
šŸ ¶ Difficulty of installation
FLOW
šŸ ¶ Orifice: The most common element used to create a differential pressure is the
orifice plate
šŸ ¶ The Orifice Plate has particularadvantages:
šŸ ¶ Low cost
šŸ ¶ Small size
šŸ ¶ Essay of installation
šŸ ¶ The disadvantages of the Orifice Plate are:
šŸ ¶ Low pressure
FLOW
šŸ ¶ Flow nozzle: The flow nozzle ismore rigid than an orifice plate and will not deform
at high temperatures and flow rates.
šŸ ¶ The advantages are:
šŸ ¶ Inexpensive
šŸ ¶ Easily manufactured
šŸ ¶ S
imple to install or change because they
fit between flanges
šŸ ¶ The disadvantages are:
šŸ ¶ Unsuitable for flows with suspended solids
šŸ ¶ Not as accurate as Venturi tubes
šŸ ¶ Have higher pressurelossesthan Venturi tubes
FLOW
šŸ ¶ b- Secondary
šŸ ¶ U-tube monometer
šŸ ¶ Differential pressure
FLOW
šŸ ¶ Flow devices:
šŸ ¶ Rota mater
FLOW
šŸ ¶ Flow devices:
šŸ ¶ Ultrasonic flowmete
FLOW
šŸ ¶ Flow devices:
šŸ ¶ Turbine flowmeter
FLOW
šŸ ¶ Flowdevices:
šŸ ¶ magnetic flow meter
LEVEL
šŸ ¶ What is the level?
šŸ ¶ Height of the liquid is called level
šŸ ¶ How calculate the level?
šŸ ¶ h =
āˆ†š‘·
š†š’ˆ
h=high of liquid & āˆ†š‘·=pressure & š† =Densityof liquid
g =Gravity
LEVEL
šŸ ¶ Units of level
šŸ ¶ mm
šŸ ¶ Cm
šŸ ¶ Feet
šŸ ¶ meter
LEVEL
šŸ ¶ Level types:
šŸ ¶ Liquid
šŸ ¶ Solid
šŸ ¶ Level measurement:
šŸ ¶ 1-Direct method
šŸ ¶ 2-indirect method
LEVEL
šŸ ¶ 1-Direct method
A-Dip stick
LEVEL
šŸ ¶ B-Gauge glasses
šŸ ¶Type 1-Tubular glass.
šŸ ¶Usingin the low pressure
šŸ ¶Easy maintenance
šŸ ¶Easy to broken
šŸ ¶Open tank
šŸ ¶Closed tank
šŸ ¶No severeoperation
LEVEL
šŸ ¶ Type 2-Reflex gauge glass.
šŸ ¶ Usingin the high pressure
šŸ ¶ Usuallyattached with light
šŸ ¶ Closedtank
šŸ ¶ Severe operation
LEVEL
šŸ ¶ C-Floats
LEVEL
šŸ ¶ 2-indirect method
A-Displacer type
LEVEL
šŸ ¶ B- Ultra sonic
LEVEL
šŸ ¶ C-Bubble system
LEVEL
šŸ ¶ D-DifferentialPressure
TEMPERATURE
šŸ ¶ What is the Temperature?
šŸ ¶ Itis measurement of hotness or coldness
šŸ ¶ Unit of Temperature:
šŸ ¶ 1-Celsius scale
Ex:F=63.5 C=?
šŸ ¶ 2-Kelvin scale
Ex:C=32 K=?
šŸ ¶ 3-The Fahrenheit scale
Ex:C=17.5 F=?
šŸ ¶ 4-Rankine
Ex:F=120 R=?
(C={F-32}/1.8)
C=(63.5-32 )/1.8 =17.5 C
(K=C+273)
K=32+273=305K
(F=1.8*
C {
+
32})
F=(1.8*
17.5)+32=63.5F
(R=F+460)
R=120+460=580R
TEMPERATURE
šŸ ¶ TEMPERATURE Device:
šŸ ¶ 1-Glass thermometers
TEMPERATURE
šŸ ¶ 2-Bimetallic thermometers
TEMPERATURE
šŸ ¶ 3-Filled system thermometer
TEMPERATURE
šŸ ¶ 4-Thermocouple Thermometer
šŸ ¶ Type:
šŸ ¶ A-Copper-Constantan
šŸ ¶ B-Iron- Constantan
šŸ ¶ C-Nickel-Nickel chromium
šŸ ¶ D-Chrome- Aluminum
šŸ ¶ E-Platinum- Platinum Rhodium
type T
type J
type E
type K
types R-S
TEMPERATURE
šŸ ¶ 5-Electrical resistance thermometer
Thank you

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