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Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Thermoneutral Point Analysis of Lignite Coal DryGasification
Chaitanya Gupta1 Varsha Choudhary1 Dr. Ganesh R Kale2
1Department of Chemical EngineeringIIT Bombay
2Chemical Engineering and Process Development divisionNational Chemical Laboratory
International Conference on Advances in Energy Research, 2013
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Outline
1 IntroductionDefinitionMotivationObjective
2 Schematic
3 Key Parameters
4 Data Simulation
5 Observations and FiguresFeed ConditionSyngas variationTNP AnalysisEnergy Optimization
6 Conclusion
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Definition
Definitions
Coal gasification → Process in which coal reacts with anoxidizer at high temperature to produce a fuel-rich product.
1 Oxidizers can be → H2O, CO2 and air.
2 CO2 involvment in oxidizer → Dry gasification
3 O2 involvement in oxidizer → Autothermal gasification
Thermonutral Point → Temperature at which reactionenthalpy becomes zero.
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Motivation
Why are we doing this process ?
CO2 emission → A major reason for climate change.
Utilizing CO2 in dry gasification of lignite coal to make fuelrich product
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Objective
Problem Formulation
Find optimum operating conditions of lignite coal drygasification with respect to
1 Change in pressure
2 Temperature
3 Feed compositions
Solution approach→ Thermodynamic analysis of the process
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Process Flow Diagram
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Key Parameters
Fuel → Lignite coal (C 73%, O 20%, H 5%, S 1%, N 1%)
Operating temperature range → 500− 1200 ◦C
Pressures → 1, 15, 30 bar
CCCR (Feed CO2 to carbon in coal ratio) → 1, 2, 3
OCCR (Feed O2 to carbon in coal ratio) → 0, 0.1, 0.2, 0.3
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Data Simulation
HSC Chemistry Package (Version 5.1)
1 Used for thermodynamic equilibrium study
2 Uses Gibbs free energy minimization algorithm to find theequilibrium compositions of species in a chemical reaction.
Input species → Coal composition, CO2(g), air(g)
Output species → H2(g), CH4(g), CO2(g), CO(g), NH3(g),H2S(g), H2O(g), H2O(l), C(s), S(s)
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Feed Condition
Feed Condition
S.no. Notation Composition
1. A1 OCCR=0, CCCR=1
2. A2 OCCR=0, CCCR=2
3. A3 OCCR=0, CCCR=3
4. B1 OCCR=0.1, CCCR=1
5. B2 OCCR=0.1, CCCR=2
6. B3 OCCR=0.1, CCCR=3
7. C1 OCCR=0.2, CCCR=1
8. C2 OCCR=0.2, CCCR=2
9. C3 OCCR=0.2, CCCR=3
10. D1 OCCR=0.3, CCCR=1
11. D2 OCCR=0.3, CCCR=2
12. D3 OCCR=0.3, CCCR=3
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Syngas variation
Syngas variation with Temperature, Pressure andComposition
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Syngas variation
Syngas variation with Temperature at Pressure = 1 bar
0.00
0.50
1.00
1.50
2.00
2.50
500 600 700 800 900 1000 1100 1200
Syng
as (m
oles
)
Temperature (0C)
A1
A2
A3
B1
B2
B3
C1
C2
C3
D1
D2
D3
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
TNP Analysis
TNP Calculation
-200
-150
-100
-50
0
50
100
150
500 600 700 800 900 1000
Reac
tion
Ent
halp
y
Temperature (0C)
A1
A2
A3
B1
B2
B3
C1
C2
C3
D1
D2
D3
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
TNP Analysis
TNP variation with Pressure
500.00
600.00
700.00
800.00
900.00
1000.00
0.00 5.00 10.00 15.00 20.00 25.00 30.00
TNPs
Pressure(bar)
A1
A2
A3
B1
B2
B3
C1
C2
C3
C1
C2
A1
C3
B3 A2
A3
B2
B1
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
TNP Analysis
Syngas moles variation at TNP
0.60
0.80
1.00
1.20
1.40
1.60
1.80
2.00
550.00 600.00 650.00 700.00 750.00 800.00 850.00 900.00 950.00
Mo
les
of
Syn
gas
pro
du
ced
at
TN
P
Temperature (0C)
P=1
P=15
P=30
A1
A2
A3
B1
B2
B3
C1
C2
C3
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
TNP Analysis
Syngas ratio variation at TNP
0.00
0.05
0.10
0.15
0.20
0.25
0.30
0.35
0.40
0.45
550.00 600.00 650.00 700.00 750.00 800.00 850.00 900.00 950.00
Syn
gas
rati
o a
t T
NP
Temperature(0C)
P=1
P=15
P=30
A1
A2
A3
B1
B2
B3
C1
C2
C3
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
TNP Analysis
Product compositions at TNP for Pressure = 1 bar
A1
A2
A3 B1 B2 B3 C1 C2 C3
TNP (0C)
640
595
568 677 628 602 703 652 625
CO(g)
0.5758
0.6084
0.6088 0.9958 1.0278 1.0523 1.4617 1.4709 1.5016
CO2(g)
0.7404
1.6977
2.6824 0.6505 1.6065 2.5789 0.5336 1.4987 2.4673
N2(g)
0.0061
0.0061
0.0059 0.3821 0.3819 0.3820 0.7583 0.7583 0.7583
C
0.6748
0.6872
0.7035 0.3479 0.3607 0.3646 0.0000 0.0265 0.0276
H2(g)
0.2389
0.1909
0.1636 0.2856 0.2314 0.2022 0.3198 0.2610 0.2299
H2O(g)
0.1488
0.2016
0.2318 0.1086 0.1645 0.1952 0.0766 0.1371 0.1691
CH4(g)
0.009
0.0067
0.0053 0.0058 0.0050 0.0042 0.0047 0.0039 0.0034
H2S(g)
0.0051
0.0051
0.0051 0.0051 0.0051 0.0051 0.0051 0.0051 0.0051
Syngas 0.8147 0.7994 0.7724 1.2814 1.2592 1.2545 1.7815 1.7319 1.7315
Syngas ratio 0.4149 0.3138 0.2687 0.2868 0.2251 0.1922 0.2188 0.1774 0.1531
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
TNP Analysis
H2O/CO Vs Temperature
0.00
0.50
1.00
1.50
2.00
2.50
3.00
3.50
4.00
500 600 700 800 900 1000 1100 1200
H2O/CO
Temperature
A1
A2
A3
B1
B2
B3
C1
C2
C3
D1
D2
D3
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Energy Optimization
Energy Optimization
Composition
Enthalpy of
Preheating
(KJ)
Extra steam
amount
(Moles)
Enthalpy for
extra steam
(KJ)
Total enthalpy of
Preheating (KJ)
Total enthalpy /
mole of syngas
(KJ/mole)
B1 61.2561 0.9868 66.9054 128.1615 100.0168
B2 84.1462 0.9661 63.3385 147.4848 117.1258
B3 106.7602 0.9623 62.3394 169.0995 134.7944
C1 74.0139 1.5313 105.4509 179.4648 100.7381
C2 97.1531 1.4809 98.9095 196.0626 113.2067
C3 120.359 1.4827 97.2947 217.6537 125.7024
Introduction Schematic Key Parameters Data Simulation Observations and Figures Conclusion
Results
Syngas yield decreases with increase in pressure.
C1 (OCCR 0.2, CCCR 1) is optimum composition for coalgasification from every aspect.
Applicability
1 Low syngas ratio can be used for petrochemicals manufacture.
2 High syngas yield can be used in SOFC.
Thank you