Date post: | 04-Dec-2014 |
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2013
1.NO NEGATIVE MARKS
2.ANSWER LEGIBLY & CLEARLY
3.No Mobile Phones, No books…..
4. Its not just your knowledge which is being tested,
but common sense, speed, different thinking, and
discipline.
5.ENJOY THE QUIZ !
1. HEAT TRANSFER2. FLUID MECHANICS3. MASS TRANSFER4. IDENTIFY THE MISTAKE5. TROUBLE SHOOTING6. RAPID FIRE
HEAT TRANSFER
What is the use of baffles in a heat exchanger?
1
In a Furnace, tubes in the convection section are usually provided with studs / fins. Why?
2
What is the main purpose of floating head type tubes in Shell and Tube heat exchanger and where are they typically used?
3
4
What is the name given to a heater if there is an Induced Draft fan as well as a forced draft fan to function the heater?
5
What is the main purpose and principle behind Steam jet ejectors?
6
What do you mean by fouling factor in Shell and Tube Heat Exchanger?
7
How does a thermosyphon reboiler functions?
FLUID MECHANICS
What do you mean by pump affinity laws?
1
What is a centrifugal pump curve?
2
What are the two NPSH’s for a pump and how are they related?
3
4
Define in simple terms what is Bernoulli’s Principle?
5
Role of Inter stage coolers in multistage compressors?
6
How can you vary the discharge flow of a centrifugal pump without
controlling it through a control valve in its discharge line?
7
Define in simple terms what is Hagen – Poiseuille Equation?
MASS TRANSFER
What is the principle behind “OPEN STEAM” in distillation
columns?
1
Name two mass transfer operations happening in your
kitchen.
2
What is HETP?
3
4
FENSKE Equation in distillation column design?
5
VLE for uniform Vap-liq equilibrium mixture VLE for ?
6
What is being measured if you measure actual air temperature +
Humidity?
7
In Mc Cabe – Thiele method of calculating the number of
theoretical plates, how can you identify that the column is
operating under TOTAL REFLUX?
IDENTIFY THE
MISTAKE
Kettle type ReboilerDistillation Column bottoms
Liquid outlet
Distillation Column bottoms
To Flare
Design Conditions:
Pressure (T/B) – 5.0 / 5.4 kg/cm2gTemp (T/B) – 110 / 160oC
Operating Conditions
Pressure (T/B) – 2.0 / 2.4 kg/cm2gTemp (T/B) – 75 / 120oC
Set Pressure: 8.5kg/cm2g
Feed
Cooler
Lighter Gas
Bottom product
Top Reflux
Reboiler
1” diaCarbon steel
DIESEL IN
62oC
DIESEL OUT31oC
Cooling Water
32oC
40oC
Steam main header
Condensate return
Steam main header
Condensate return
Bottoms product
P1
Tank-1
P2
5 kg/cm2g
5 kg/cm2g
Case-1Disc Pr = 25 kg/cm2gQ = 150 m3/hr
N2 3 kg/cm2g
Tank-1
P1
P2
P1 H = 10 kg/cm2gQ = 100 m3/hr
P2 H = 10 kg/cm2gQ = 50 m3/hr
5 kg/cm2g
Case-2Disc Pr = 15 kg/cm2gQ = 100 m3/hr
N2 3 kg/cm2g
P1
Tank-1
P2
5 kg/cm2g
5 kg/cm2g
Case-1Disc Pr = 15 kg/cm2gQ = 150 m3/hr
N2 3 kg/cm2g
Tank-1
P1
P2
P1 H = 10 kg/cm2gQ = 100 m3/hr
P2 H = 10 kg/cm2gQ = 50 m3/hr
5 kg/cm2g
Case-2Disc Pr = 25 kg/cm2gQ = 50 m3/hr
N2 3 kg/cm2g
Rx-1Rx-2 Rx-3
Product Stripper
Feed100 TPH
Steam5 TPH
P – 30 kgT – 350 C
P – 27.2 kgT – 360 C
P – 28.5 kgT – 320 C P – 24 kg
T – 340 C
P – 28.2 kgT – 325 C
H2 Quench@ 100 deg C
20 TPH
Light Distillates
Heavy Distillates
Rx-1Rx-2 Rx-3
Product Stripper
Feed100 TPH
Steam5 TPH
P – 30 kgT – 350 C
P – 27.2 kgT – 360 C
P – 28.5 kgT – 320 C P – 24 kg
T – 340 C
P – 28.2 kgT – 325 C
H2 Quench@ 100 deg C
20 TPH
Light Distillates
Heavy Distillates
Trouble Shooting
A distillation column separating BENZENE & TOLUENE
06:00hrs sample result Toluene content in Benzene was 10ppm
08:00 hrs Toluene content became 100ppm and then at
10:00hrs reported 1.0%
And the maximum allowable toluene in Benzene is 50ppm
Boiling Pt of Benzene 81.5oCBoiling Pt of Toluene
REASONS and SOLUTION.
Trouble – 1
A distillation column separating LPG and Naphtha.
Trouble – 2
Time Top temperatureoC
Top PressureKg/cm2g
Top refluxTPH
Bottom temperatureoC
O/H vent gas flowKg/hr
06:00 75 9 45 150 100
06:03 78 9.8 47 152 110
06:06 80 10.7 52 155 200
06:08 85 12.2 60 162 450
06:10 100 14.5 NIL 175 1000
06:00hrs…all was fine…but in 10 mins….
What probably might have went wrong between 06:00 and 06:03?What is the reason for ‘NIL’ top reflux at 06:10hrs?
A distillation column separating Light Naphtha and Heavy Naphtha.Typical boiling range of Light Nap 60 – 90 and that of Heavy Nap is 90 – 140The unit was steady and results were OK, then got an instruction at 10:00hrs to reduce the FBP of Lt Nap to 80oC.
Trouble – 3
Time Top temperatureoC
Top refluxTPH
Bottom temperatureoC
Light Naphtha boiling rangeLab result
06:00 92 40 150 62 – 91
10:00 92 40 150 62 – 92
14:00 85 48 147 62 – 105
What probably might have went wrong? Operator did the right thing, he reduced the top temperature to reduce FBP of Light Naphtha or was he wrong?
The operator reduced the top temperature of the distillation column by increasing the top reflux, as usual . Then….
Trouble – 4
1st January 2012 DATA OF FIRED HEATERFired heat duty 50 MMKCal
Absorbed heat duty 45 MMKcal
Stack temperature 230oC
Heater stack oxygen content 3.5 %
Fired heat duty 50 MMKCal
Absorbed heat duty 40 MMKcal
Stack temperature 253oC
Heater stack oxygen content 5.5 %
1st January 2013 DATA OF FIRED HEATER
Analyze the data given above and tell us what is the problem, if any?
Trouble – 5
A pump was used to transfer treated water from tank-01 to Effluent Treatment plant. Pump details are
NPSHR – 5kg/cm2gNPSHA – 6 kg/cm2gFlow – 100 m3 / hr
Tank-01 was decommissioned by July 2012 and the pump was redundant. Later during Dec 2012, the company set up a small unit for treating impure Naphtha and the company decided to use this pump as part of cost reduction measures. New conditions are
Please advice the operating conditions of the treater to ensure that the pump can be effectively used in the new service.
Height of the naphtha treater 15 metersNaphtha density 700kg/cm3 @40 C Pumping temperature 40 deg C
Trouble – 6The unit was shut down due to power failure at 09:15 am today.
• Operators and other officials are working hard to start the unit and bring it back on line.
• The heater had cooled down and reached a furnace outlet temperature of 200oC.
• As part of their start up activities, operators ignited the fired heater at 09:38 am and started to increase the furnace outlet temperature to the required temperature of 400oC @ 40oC / hour.
• Initially the operators encountered no trouble with the furnace. • But by around 12:30 pm when they were trying to increase the
temperature by increasing the fuel flow, a sudden back fire occurred from the furnace, injuring two operators who were below the furnace.
What all may be the reason for the incident and how it can be avoided?
Trouble – 7
A pump was used to feed an old Crude Oil to the distillation Unit. Details of the pump are
Minimum / Normal / Maximum Flow 600/700/750 m3 / hrPumping temperature 40 deg CPumping Density 800 kg/m3
The company decided to cut down the charge rate of the CDU from 560 TPH to 300 TPH as the unit efficiency was very low. Company wanted to use the same charge pump for the reconditioned unit also.
Can the company use the same charge pump?Do they require any modification in the pump?If so, what cost effective modifications are possible so that the same pump can be used for a revised charge rate?
Rapid fire
TRUE / FALSE
IDENTIFY THE VALVE TYPE
DATE OF SIGNIFICANCE
DIMENTIONLESS NUMBER
EXPAND
GLOSSARY
ENERGY / ENVIRONMENT
STEAM
LOGO OF AN OIL COMPANY
UNIT
March 22
Number used to characterize the different flow regimes
Unit of CALORIFIC VALUE
Permanent hardness of water is due to the presence of sulphates and chlorides of Ca&Mg , T / F
1
Amount of extra metal thickness provided to a pipe / vessel wall
Expand -- IRR
Indirect steam heating makes use of ____ heat
_____ is the only form of energy which derives directly from the relative motion of the Earth – Moon system
APRIL – 22nd
Ratio of convective to conductive HT Coeff..
W/m2K is the unit of _______
THORIUM deposits are largely found in the coastal region of Kerala – T/F
2
A method to remove heat from a section of distillation column
Expand -- NPV
Steam trap that operates based on the difference in temperature between steam and condensate is _____________ trap
Which is the Nodal agency for
coordinating the energy conservation
activities under the EC act of India?
September – 16
Ratio of viscosity to Mass Diffusivity
SI unit of Kinematic Viscosity
LINDE’s and CLAUDE’S process are used to produce HYDROGEN, T / F
3
Exterior temperature of a tube in a furnace or a heater so measured are called
Expand – PBT
Economic and Energy efficient type of insulation material used in steam lines
Who is the Union Minister for new
and renewable Energy?
National Energy Conservation Day
Ratio of convective MT coefficient to mass diffusivity
Pascal second is the SI unit of _________
Boiling removes temporary hardness of water T / F
4
Vapour at its dew point is called______
Expand -- FIFO
Proper sizing of steam pipelines helps to minimize _________
The only Green House Gas produced without any interference from human beings
JUNE 5th
Ratio of kinematic viscosity to thermal diffusivity
CLAUS process is used for the production of Sulphur, T/F
5
Unit of VACUUM
Filling the casing of the pumps with the liquid is called _______
Expand – P & ID
Water that has been softened / deaerated for use in boilers
Started in Mexico in 1943 by famous environmentalist Norman Borlaug which changed the face of the world.
Engineers Day
Ratio of buoyancy to viscous forces acting on a fluid
Raw material for CAPROLACTUM (raw material for NYLON-6) is Benzene, T / F
6
Unit of Specific Gravity
Equipment where heat of Waste process gas is used to generate steam
Vapour Pressure X mole Fraction =
2013 is the UN International year of ______
Expand – ROI
Rajiv Gandhi National Renewable Energy Day
Grasshof no X Prandtl no =
Calcium Carbide is the raw material for the production of Acetylene T/F
7
Unit of Gas Constant ‘R’
Chart relating to Enthalpy, Entropy, temperature and Pressure of steam is called _______
Ratio of Discharge Pressure to Suction Pressure of a compressor is called _____
Expand – ROR
In the High Courts of Kerala, Kolkatta, MP & Punjab and Haryana, special benches function to take care of environmental related cases.
That’s all friends…..