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3. ENERGY PERFORMANCE ASSESSMENT OF
COGENERATION, TURBINES (GAS AND STEAM)
3.1 Introduction
Cogeneration systems involve different types of configurations with respect to mode of
power generation and ways of steam use such as extraction, back pressure or heat
recovery steam etc. Depending on power and steam load variations in the plant the entire
system is dynamic. A performance assessment would yield valuable insights into turbine
performance and need for further optimizing the system.
3.2 Purpose of the Performance Test
The purpose of the cogeneration plant performance test is to determine the power output
and plant heat rate. In certain cases, the efficiency of individual components like steam
turbine is addressed specifically where performance deterioration is suspected. In general,
the plant performance will be compared with the base line values arrived at for the plant
operating condition rather than the design values. The other purpose of the performance
test is to show the maintenance accomplishment after a major overhaul. In some cases the
purpose of evaluation could even be for a total plant revamp.
3.3 Performance Terms and Definitions
Turbine cylinder efficiency.= Actual enthalpy drop across the turbine
Isentropic (theoretical) enthalpy drop across the turbine
Turbine heat rate = Enthalpy drop across the turbine
Power output
Overall plant heat rate = Fuel consumption in kg/hr or kcal/hr
Power output
3.4 Reference standards
Modern power station practices by British electricity International (Pergamon Press)
ASME PTC 22 – Gas turbine performance test.
3.5 Field Testing Procedure
The test procedure for each co-generation plant will be developed individually taking into
consideration the plant configuration, instrumentation and plant operating conditions.
A method is outlined in the following section for the measurement of heat rate and
efficiency of a co-generation plant. This part provides performance-testing procedure for
a coal fired steam based co-generation plant, which is common in Indian industries.
52
3.5.1 Test Duration
The test duration is site specific and in a continuous process industry, 8 hour test data
should give reasonably reliable data. In case of an industry with fluctuating
electrical/steam load profile a set 24 hour data sampling for three days is suggested.
3.5.2 Measurement and Data Collection
The suggested instrumentation for the performance measurement is as under :
Steam flow measurement : Orifice flow meters
Air flow / Flue gas flow : Venturi / Orifice flow meter / Pilot tubes
Flue gas Analysis : Zirconium Probe Oxygen analysis
Unburnt Analysis : Gravimetric Analysis
Temperature : Thermocouple
Cooling water flow : Orifice flow meter / wier /channel flow
Measurements
Pressure : Bourden Pressure Gauges
Power : Trivector meter
Condensate : Orifice flow meter
It is essential to ensure that the data is collected during steady plant running conditions.
Among others the following are essential details to be collected for cogeneration plant
performance evaluation.
I. Thermal Energy :
Flow Pressure Temperature
1. Steam inlet to turbine   
2. Coal input Boiler  - -
3. Extraction steam to process   
4. Back Pressure Steam to Process   
5. Condensing steam   
6. Condensate from turbine  - 
7. Turbine by pass steam   -
II. Electrical Energy :
1. Total power generation for the trial period
2. Hourly power generation
3. Quantity of power import from utility
4. Quantity of power generation from Diesel sets
5. Auxiliaries power consumption
53
3.5.3 Calculations
The process flow diagram for cogeneration plan is shown in figure 3.1. The following
calculation procedures have been provided in this section.
 Turbine cylinder efficiency.
 Overall station heat rate
Figure 3.1 Process Flow Diagram for cogeneration plant
S
1st Extraction
Extraction cum
condensing
Turbine
Boiler
h1
Power output
100kW
Boiler
2st Extraction
Condenser
h2
h3 h4
Step 1 :
Calculate the actual heat extraction in turbine at each stage,
Steam Enthalpy at turbine inlet : h1 Kcal / kg
“ Enthalpy at 1st extraction : h2 Kcal / kg
“ Enthalpy at 2nd extraction : h3 Kcal / kg
Heat extraction from inlet : h1 – h2 Kcal / kg
to stage –1 extraction (h5)
Heat extraction from : h2-h3 Kcal / kg
1st –2nd extraction (h6)
Heat extraction from 2nd : h3-h4 Kcal / kg
Extraction – condenser (h7)
54
Step 2 :
From Mollier diagram (H- Diagram) estimate the theoretical heat extraction for the
conditions mentioned in Step 1. Towards this :
a) Plot the inlet condition point in the mollier chart – corresponding to pressure
and temperature.
b) Since expansion in turbine is an adiabatic process / the entropy is constant.
Hence draw a vertical line from inlet point (parallel to y-axis) upto the
condensing conditions.
c) Read the enthalpy at points where the extraction and condensing pressure
lines meet the vertical line drawn.
d) Compute the theoretical heat drop for different stages of expansion.
Theoretical Enthalpy after 1st extraction : H1
“ “ “ 2nd extraction : H2
“ “ at condenser conditions : H3
Theoretical heat extraction from inlet to : h1 – H1
stage 1 extraction h8
Theoretical heat extraction from : H1-H2
1st – 2nd extraction h9
Theoretical heat extraction from : H2-H3
2nd extraction – condensation h10
Step 3 :
Compute turbine cylinder efficiency
Efficiency of 1st stage : h5
-------
h8
Efficiency of 2nd stage : h6
------
h9
55
Step 4 :
Calculate station heat rate
M (h1 – h11)
Heat rate = ------------------------------ x 100 Kcal / Kwh
P
M – Mass flow of steam h1 - Enthalpy of inlet steam
P - Power generated Kwh h11 - Enthalpy of feed water
3.6 Example
3.6.1 Small Cogeneration Plant
A distillery plant having an average production of 40 KL of ethanol is having a
cogeneration system with a back pressure turbine. The plant steam and electrical demand
are 5.1 TPH and 100 kW. The process flow diagram is shown in figure 3.2.
Figure 3.2 Process Flow Diagram for small cogeneration plant
S
Process Steam
Back
Pressure
Turbine
Boiler
Coal
1500 kg/hr
Q – 5100 kg/hr
P – 15 kg/cm2g
T – 250oC
Q – 5100 kg/hr
P – 2 kg/cm2g
T – 130oC
Power output
100kW
56
Calculations :
Step 1 :
Total heat of steam at turbine inlet conditions - Kcal / kg
15lg / cm2 and 250oC h1
Step 2 :
Total heat of steam at turbine outlet conditions - 648 Kcal / kg
2 kg/cm2 and 130oC
Step 3 :
Heat energy input turbine / kg of inlet steam - (698-648) = 50 Kcal / kg
Step 4 :
Total steam flow rate Q1 - 5100 kg/hr
Power generation - 100 KW
&
Equivalent thermal energy - 100 x 860 = 8,60,000 KW
Step 5 :
Energy input to the turbine - 5100 x 50 = 2,55,000 Kcal/Hr.
Step 6 :
Energy output
Power generation efficiency of the turbo alternator = ---------------------
Energy Input
8,60,000
------------------ = 34%
2,55,000
Step 7 :
Efficiency of Alternator - 92 %
Efficiency of gear transmission - 98 %
Turbine efficiency - 34 %
Overall efficiency - 0.92 x 0.98 x 34 = 30.6 %
57
Step 8 :
Quantity of steam bypassing the turbine - Nil
Step 9 :
Coal consumption of the boiler - 1550 kg/Hr.
Step 10 :
Overall plant heat rate including boiler - 1550/100
= 15.5 kg coal / kw
Analysis of Results:
The efficiency of the turbine generator set is as per manufacturer design specification.
There is no steam by pass indicating that the power generation potential of process steam
is fully utilized. At present the power generation from the process steam completely
meets the process electrical demand or in other words, the system is balanced.
Consideration can be given for high efficiency turbine (efficient 48%) when plant
electrical demand alone increases by 50 KW with an ETP installation of ETP.
QUESTIONS
1. What is meant by turbine heat rate? What is its significance?
2. What is meant by turbine cylinder efficiency? How is it different from turbo-
generator efficiency
3. What parameters should be monitored for evaluating the efficiency of the turbine?
4. What is the need for performance assessment of a cogeneration plant?
5. The parameters for steam turbine cogeneration plant is given below
Inlet Steam: P =16 kg/cm2
, T = 310o
C , Q = 9000kg/hr
Outlet Steam: P = 5.0 kg/cm2
, T = 235o
C , Q = 9000kg/hr
Find out the turbine cylinder efficiency
REFERENCES
1. NPC report on’ Assessing cogeneration potential in Indian Industries’
2. Energy Cogeneration Handbook, George Polimeros, Industrial Press Inc.

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Cogeneration systems

  • 1. 51 3. ENERGY PERFORMANCE ASSESSMENT OF COGENERATION, TURBINES (GAS AND STEAM) 3.1 Introduction Cogeneration systems involve different types of configurations with respect to mode of power generation and ways of steam use such as extraction, back pressure or heat recovery steam etc. Depending on power and steam load variations in the plant the entire system is dynamic. A performance assessment would yield valuable insights into turbine performance and need for further optimizing the system. 3.2 Purpose of the Performance Test The purpose of the cogeneration plant performance test is to determine the power output and plant heat rate. In certain cases, the efficiency of individual components like steam turbine is addressed specifically where performance deterioration is suspected. In general, the plant performance will be compared with the base line values arrived at for the plant operating condition rather than the design values. The other purpose of the performance test is to show the maintenance accomplishment after a major overhaul. In some cases the purpose of evaluation could even be for a total plant revamp. 3.3 Performance Terms and Definitions Turbine cylinder efficiency.= Actual enthalpy drop across the turbine Isentropic (theoretical) enthalpy drop across the turbine Turbine heat rate = Enthalpy drop across the turbine Power output Overall plant heat rate = Fuel consumption in kg/hr or kcal/hr Power output 3.4 Reference standards Modern power station practices by British electricity International (Pergamon Press) ASME PTC 22 – Gas turbine performance test. 3.5 Field Testing Procedure The test procedure for each co-generation plant will be developed individually taking into consideration the plant configuration, instrumentation and plant operating conditions. A method is outlined in the following section for the measurement of heat rate and efficiency of a co-generation plant. This part provides performance-testing procedure for a coal fired steam based co-generation plant, which is common in Indian industries.
  • 2. 52 3.5.1 Test Duration The test duration is site specific and in a continuous process industry, 8 hour test data should give reasonably reliable data. In case of an industry with fluctuating electrical/steam load profile a set 24 hour data sampling for three days is suggested. 3.5.2 Measurement and Data Collection The suggested instrumentation for the performance measurement is as under : Steam flow measurement : Orifice flow meters Air flow / Flue gas flow : Venturi / Orifice flow meter / Pilot tubes Flue gas Analysis : Zirconium Probe Oxygen analysis Unburnt Analysis : Gravimetric Analysis Temperature : Thermocouple Cooling water flow : Orifice flow meter / wier /channel flow Measurements Pressure : Bourden Pressure Gauges Power : Trivector meter Condensate : Orifice flow meter It is essential to ensure that the data is collected during steady plant running conditions. Among others the following are essential details to be collected for cogeneration plant performance evaluation. I. Thermal Energy : Flow Pressure Temperature 1. Steam inlet to turbine    2. Coal input Boiler  - - 3. Extraction steam to process    4. Back Pressure Steam to Process    5. Condensing steam    6. Condensate from turbine  -  7. Turbine by pass steam   - II. Electrical Energy : 1. Total power generation for the trial period 2. Hourly power generation 3. Quantity of power import from utility 4. Quantity of power generation from Diesel sets 5. Auxiliaries power consumption
  • 3. 53 3.5.3 Calculations The process flow diagram for cogeneration plan is shown in figure 3.1. The following calculation procedures have been provided in this section.  Turbine cylinder efficiency.  Overall station heat rate Figure 3.1 Process Flow Diagram for cogeneration plant S 1st Extraction Extraction cum condensing Turbine Boiler h1 Power output 100kW Boiler 2st Extraction Condenser h2 h3 h4 Step 1 : Calculate the actual heat extraction in turbine at each stage, Steam Enthalpy at turbine inlet : h1 Kcal / kg “ Enthalpy at 1st extraction : h2 Kcal / kg “ Enthalpy at 2nd extraction : h3 Kcal / kg Heat extraction from inlet : h1 – h2 Kcal / kg to stage –1 extraction (h5) Heat extraction from : h2-h3 Kcal / kg 1st –2nd extraction (h6) Heat extraction from 2nd : h3-h4 Kcal / kg Extraction – condenser (h7)
  • 4. 54 Step 2 : From Mollier diagram (H- Diagram) estimate the theoretical heat extraction for the conditions mentioned in Step 1. Towards this : a) Plot the inlet condition point in the mollier chart – corresponding to pressure and temperature. b) Since expansion in turbine is an adiabatic process / the entropy is constant. Hence draw a vertical line from inlet point (parallel to y-axis) upto the condensing conditions. c) Read the enthalpy at points where the extraction and condensing pressure lines meet the vertical line drawn. d) Compute the theoretical heat drop for different stages of expansion. Theoretical Enthalpy after 1st extraction : H1 “ “ “ 2nd extraction : H2 “ “ at condenser conditions : H3 Theoretical heat extraction from inlet to : h1 – H1 stage 1 extraction h8 Theoretical heat extraction from : H1-H2 1st – 2nd extraction h9 Theoretical heat extraction from : H2-H3 2nd extraction – condensation h10 Step 3 : Compute turbine cylinder efficiency Efficiency of 1st stage : h5 ------- h8 Efficiency of 2nd stage : h6 ------ h9
  • 5. 55 Step 4 : Calculate station heat rate M (h1 – h11) Heat rate = ------------------------------ x 100 Kcal / Kwh P M – Mass flow of steam h1 - Enthalpy of inlet steam P - Power generated Kwh h11 - Enthalpy of feed water 3.6 Example 3.6.1 Small Cogeneration Plant A distillery plant having an average production of 40 KL of ethanol is having a cogeneration system with a back pressure turbine. The plant steam and electrical demand are 5.1 TPH and 100 kW. The process flow diagram is shown in figure 3.2. Figure 3.2 Process Flow Diagram for small cogeneration plant S Process Steam Back Pressure Turbine Boiler Coal 1500 kg/hr Q – 5100 kg/hr P – 15 kg/cm2g T – 250oC Q – 5100 kg/hr P – 2 kg/cm2g T – 130oC Power output 100kW
  • 6. 56 Calculations : Step 1 : Total heat of steam at turbine inlet conditions - Kcal / kg 15lg / cm2 and 250oC h1 Step 2 : Total heat of steam at turbine outlet conditions - 648 Kcal / kg 2 kg/cm2 and 130oC Step 3 : Heat energy input turbine / kg of inlet steam - (698-648) = 50 Kcal / kg Step 4 : Total steam flow rate Q1 - 5100 kg/hr Power generation - 100 KW & Equivalent thermal energy - 100 x 860 = 8,60,000 KW Step 5 : Energy input to the turbine - 5100 x 50 = 2,55,000 Kcal/Hr. Step 6 : Energy output Power generation efficiency of the turbo alternator = --------------------- Energy Input 8,60,000 ------------------ = 34% 2,55,000 Step 7 : Efficiency of Alternator - 92 % Efficiency of gear transmission - 98 % Turbine efficiency - 34 % Overall efficiency - 0.92 x 0.98 x 34 = 30.6 %
  • 7. 57 Step 8 : Quantity of steam bypassing the turbine - Nil Step 9 : Coal consumption of the boiler - 1550 kg/Hr. Step 10 : Overall plant heat rate including boiler - 1550/100 = 15.5 kg coal / kw Analysis of Results: The efficiency of the turbine generator set is as per manufacturer design specification. There is no steam by pass indicating that the power generation potential of process steam is fully utilized. At present the power generation from the process steam completely meets the process electrical demand or in other words, the system is balanced. Consideration can be given for high efficiency turbine (efficient 48%) when plant electrical demand alone increases by 50 KW with an ETP installation of ETP. QUESTIONS 1. What is meant by turbine heat rate? What is its significance? 2. What is meant by turbine cylinder efficiency? How is it different from turbo- generator efficiency 3. What parameters should be monitored for evaluating the efficiency of the turbine? 4. What is the need for performance assessment of a cogeneration plant? 5. The parameters for steam turbine cogeneration plant is given below Inlet Steam: P =16 kg/cm2 , T = 310o C , Q = 9000kg/hr Outlet Steam: P = 5.0 kg/cm2 , T = 235o C , Q = 9000kg/hr Find out the turbine cylinder efficiency REFERENCES 1. NPC report on’ Assessing cogeneration potential in Indian Industries’ 2. Energy Cogeneration Handbook, George Polimeros, Industrial Press Inc.