Friday, March 30, 2012
Thursday, March 22, 2012
REFERIGERATION & AIR-CONDITIONING
REFRIGERATION
Science of providing and maintaining temperatures below that of surroundings.
· Deals with the chilling or freezing of a substance by removing some of its heat.
· Transfer of this heat to another system at high temperature.
· For this mechanical work must be performed to satisfy the second law of thermodynamics.
AIR CONDITIONING refers to simultaneous control of temperature, humidity, cleanliness and air motion within a confined region.
Tuesday, March 13, 2012
measuring quality of steam
Measurement of Quality of Steam
For pure substances –in-dependant properties such as pressure and temperature are needed (if pressure is known, temperature can be found)
We need specific volume, enthalpy or quality of mixture(liquid & vapour)
For measuring specific volume of mixture (quality) calorimeters are used.
a) Separating Calorimeter
b) Throttling Calorimeter
c) Separating & Throttling Calorimeter
d) Barrel Calorimeter
e) Electric Calorimeter
a) Separating Calorimeter:
Fig
X = M/ (M+m)
M=Mass of dry steam read from gauge of condenser
M=Mass of water separated in specified time interval
x= Dryness fraction or quality of steam
b) Throttling Calorimeter
Fig
x1= (h-hf1)/ hfg1
Let P1 = Initial Pressure
x1 = Dryness Fraction
hf1 = Enthalpy of water at P1
hfg1 = Enthalpy of vaporization
Cps = Sp heat of superheated steam after throttling..kJ/ kg
Tsat = Saturation temp at P2
During throttling process, the enthalpy remains constant.
Enthalpy of steam at P1 before throttling= Enthalpy of steam at P2 after throttling
hf1 + x1 hfg1 = hg2 + Cp (T2-Tsat)
x1 hfg1= hg2 + Cp (T2-Tsat) - hf1
x1= hg2 + Cp (T2-Tsat) - hf1/ hfg1
= h- hf1/ hfg1
h = sp enthalpy at state 2 from superheat read from table
MEASUREMENT OF QUALITY OF STEAM
Measurement of Quality of Steam
For pure substances –in-dependant properties such as pressure and temperature are needed (if pressure is known, temperature can be found)
We need specific volume, enthalpy or quality of mixture(liquid & vapour)
For measuring specific volume of mixture (quality) calorimeters are used.
a) Separating Calorimeter
b) Throttling Calorimeter
c) Separating & Throttling Calorimeter
d) Barrel Calorimeter
e) Electric Calorimeter
a) Separating Calorimeter:
Fig
X = M/ (M+m)
M=Mass of dry steam read from gauge of condenser
M=Mass of water separated in specified time interval
x= Dryness fraction or quality of steam
b) Throttling Calorimeter
Fig
x1= (h-hf1)/ hfg1
Let P1 = Initial Pressure
x1 = Dryness Fraction
hf1 = Enthalpy of water at P1
hfg1 = Enthalpy of vaporization
Cps = Sp heat of superheated steam after throttling..kJ/ kg
Tsat = Saturation temp at P2
During throttling process, the enthalpy remains constant.
Enthalpy of steam at P1 before throttling= Enthalpy of steam at P2 after throttling
hf1 + x1 hfg1 = hg2 + Cp (T2-Tsat)
x1 hfg1= hg2 + Cp (T2-Tsat) - hf1
x1= hg2 + Cp (T2-Tsat) - hf1/ hfg1
= h- hf1/ hfg1
h = sp enthalpy at state 2 from superheat read from table
CLAUSIUS STATEMENT OF SECOND LAW
▀Clausius Statement of second law:
It is impossible to construct a device that operates in a cycle and produces no effect other than the transfer of heat from a system at low temperature to another system at high temperature.
Clausius statement points-out the essence of work input required in Refrigerators & Heat pumps
Fig
Heat can’t flow from low temperature to high temperature systems.
COP=Q/W=Q/0=∞.............(impossible)
It is impossible to construct a refrigerator, which operates without an input of work.
Fig
CLAUSIUS STATEMENT
▀Clausius Statement of second law:
It is impossible to construct a device that operates in a cycle and produces no effect other than the transfer of heat from a system at low temperature to another system at high temperature.
Clausius statement points-out the essence of work input required in Refrigerators & Heat pumps
Fig
Heat can’t flow from low temperature to high temperature systems.
COP=Q/W=Q/0=∞.............(impossible)
It is impossible to construct a refrigerator, which operates without an input of work.
Fig