modelling of an entrained flow cal carbonator for co2
TRANSCRIPT
Modelling of an Entrained Flow CaL Carbonator for CO2 Capture in Cement Kilns
Maurizio Spinelli PhDIsabel Martinez PhDEdoardo De Lenaprof. Matteo Romanoprof. Stefano Campanariprof. Stefano Consonni
7th High Temperature Solid Looping Cycles Network MeetingLuleΓ₯, Sweden, 4-5th September 2017
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 2/20
Outline
Overview of CaL technology in cement plant:
Tail end
Integrated with EF carbonator
1D model of EF carbonator:
Results of first sensitivity analysis
Conclusion
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 3/20
Cement plant and related model
Clinker out
Raw meal* in
Gas out
Air in
Petcoke
65%
35%
CO2 80%
20%
Reference plant GS (POLIMI code)Cement plant is characterized by:
high fuel consumptions: ~ 3.2 MJLHV/kgck high CO2 emissions (~850gCO2/kgCK) from
fuel combustion and CaCO3 decomposition.
CaCO3 CaO+CO2
Calciner
* Mostly CaCO3 + additives like Fe2O3, Al2O3, SiO2, MgCO3
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 4/20
Tail-end CaL configuration
carbonatorcalciner
CaCO3 + correctives
decarbonated flue gasCO2 to
storage
heat for steam generation/raw meal preheating
heat for steam generation/raw meal preheating
High purity O2
fuel
filter
carbonator heat steam generation
CONVENTIONAL CEMENT KILN clinker
CO2-rich gas from the suspension preheater
limestone
CaO-rich CaL purge
ASU
CO2 compression and purification
unit
β’ Carbonator removes CO2 from cement plant flue gas highly suitable for retrofitβ’ CaO-rich purge from CaL calciner used as feed for the cement kilnβ’ CFB CaL reactors: d50=100-250 ΞΌm
Particle size for clinker production d50=10-20 ΞΌm CaL purge milled in the raw mill at low temperature
1) Spinelli et al., βIntegration of Ca-Looping systems for CO2 capture in cement plantsβGHGT13 conference paper, Energy Procedia 114 ( 2017 ) 6206 β 62142) De Lena et al., βProcess integration study of tail-end Ca-Looping process for CO2 capture in cement plants β Submitted to International Journal of Greenhouse Gas Control
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 5/20
Integrated CaL configuration
carbonator
calciner
CO2-rich gas from the kiln
hot clinker
fuel
decarbonated flue gas
heat recovery for steam generation
High purity O2
fuel
filter
clinker coolercooled clinker
cooling air
cooler exhaust airsecondary
airrotary kiln
carbonator heat steam generation
Raw meal preheater 1
Raw meal 1
Raw meal 2
Raw meal preheater 2heat recovery for
steam generation
CaCO3-rich material
precalcined raw meal
ASU
CO2 to storage
CO2 compression and purification
unit
CaLβ’ carbonator highly integrated within the preheating tower, on rotary kiln gasCaLβ’ calciner coincides with the cement kiln pre-calcinerCalcined raw meal as COβ’ 2 sorbent in the carbonatorSorbent has small particle size (dβ’ 50=10-20 ΞΌm) entrained flow reactors
Spinelli et al., βIntegration of Ca-Looping systems for CO2 capture in cement plantsβGHGT13, Energy Procedia 114 ( 2017 ) 6206 β 6214
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 6/20
Fresh raw meal
Raw meal preheater
CO2-poor flue gas
Fuel
O2
Carb
onat
or
CO2-rich gas to CPU
Fuel
Calc
iner
Recarbonated sorbent + fresh preheated raw
meal to calciner
Calcined raw meal to rotary kiln
Calcined raw meal to carbonator
Rotary kiln
CO2 recycle
Integrated CaL concept: entrained flow (EF) reactors
CO2 from kiln
CO2 to storage
CO2 from calciner
O2 from ASU
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 7/20
Reference cement plant
w/o CO2 capture
Tail-end CaLconfiguration
Integrated CaL
configuration
Direct CO2 emissions [kgCO2/tclk] 863.1 143.2 71.4Indirect CO2 emissions [kgCO2/tclk] 105.2 -123.5 128.7Equivalent CO2 emissions [kgCO2/tclk] 968.3 19.7 200.1Equivalent CO2 avoided [%] -- 98.0 79.3SPECCA [MJLHV/kgCO2] -- 3.26 2.32
Integrated / Tail End CaL concepts: results
Spinelli et al., βIntegration of Ca-Looping systems for CO2 capture in cement plantsβGHGT13, Energy Procedia 114 ( 2017 ) 6206 β 6214
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 8/20
Entrained flowcarbonator model
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 9/20
CaLβ’ kineticsGasβ’ -solid drag velocitiesInterphaseβ’ heat transferExternalβ’ heat transferPressureβ’ lossesFluidβ’ -dynamic checkInternalβ’ sorbent recycle
NASAβ’ polynomials for gas /solid TDN propertiesSteadyβ’ stateIncompressibleβ’ flowHomogeneousβ’ mixturesMassβ’ transfer effect neglected (low Da numbers)
Main Assumptions
Entrained flow CaL carbonator modelingDilute reactor is the most suitable option for the cement plant CaL application, becauseof the experience with entrained flow technologies and the low particle size.A simple, finite-difference model (axial discretization) has been developed to solve mass,momentum and energy equations and evaluate the potential CO2 capture rate.
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 10/20
Mass
Carbonation kinetics
1 β πΊπΊπΊπΊπΊπΊ:πποΏ½ΜοΏ½πππ
ππππ= β
οΏ½ΜοΏ½ππ π ,ππ
π’π’π π οΏ½
ππππππππ
οΏ½ πππΆπΆπΆπΆ2 2 β ππππππππππ:πποΏ½ΜοΏ½ππ π
ππππ= β
πποΏ½ΜοΏ½πππ
ππππ
Temperature influence Xmax influenceπΆπΆπΊπΊπΆπΆ π π + πΆπΆπΆπΆ )2(ππ
ββ+πΆπΆπΊπΊπΆπΆπΆπΆ )3(π π
ππππππππ =
πππ π οΏ½ ππππ
1 β πππποΏ½ 1 β ππ οΏ½ πΆπΆπΆπΆπΆπΆ2 β πΆπΆπΆπΆπΆπΆ2,ππππ οΏ½ 1 β Ξ¨ ππππ 1 β ππ
πππ π = πππ π ,0 οΏ½ expβ20300πππ π οΏ½ π π π’π’
ππππ = ππ0 οΏ½ ππππππππ
π π πΊπΊππππππππ ππππππππ ππππππππππ π€π€ππππβ ππππππππ ππππππππππππππ
EF carbonator modeling β EquationsDilute reactor is the most suitable option for the cement plant CaL application, becauseof the experience with entrained flow technologies and the low particle size.A simple, finite-difference model (axial discretization) has been developed to solve mass,momentum and energy equations and evaluate the potential CO2 capture rate.
G. Grasa et al., βApplication of the random pore model to the carbonation cyclic reactionβ, AIChE J. 55 (2009)
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 11/20
Dilute reactor is the most suitable option for the cement plant CaL application, becauseof the experience with entrained flow technologies and the low particle size.A simple, finite-difference model (axial discretization) has been developed to solve mass,
momentum and energy equations and evaluate the potential CO2 capture rate.
Energy5 β πΊπΊπΊπΊπΊπΊ:
ππ οΏ½ΜοΏ½πππ οΏ½ βππ + 0.5 οΏ½ οΏ½ΜοΏ½πππ οΏ½ π’π’ππ2 + πΌπΌπΊπΊ οΏ½ οΏ½ΜοΏ½πππ οΏ½ ππ οΏ½ ππ
ππππ= βοΏ½ΜοΏ½π€πππ π β οΏ½ΜοΏ½πππππ β οΏ½ΜοΏ½ππππ π β οΏ½ΜοΏ½ππΆπΆπΆπΆ2,ππππππππ
6 β ππππππππππ:ππ οΏ½ΜοΏ½ππ π οΏ½ βπ π + 0.5 οΏ½ οΏ½ΜοΏ½ππ π οΏ½ π’π’π π
2 + πΌπΌπΊπΊ οΏ½ οΏ½ΜοΏ½ππ π οΏ½ ππ οΏ½ ππππππ
= οΏ½ΜοΏ½π€πππ π β οΏ½ΜοΏ½ππ π ππ + οΏ½ΜοΏ½ππππ π + οΏ½ΜοΏ½πππ,ππππππππ + οΏ½ΜοΏ½ππΆπΆπΆπΆ2,ππππππππ
3-Gas: ππ οΏ½ΜοΏ½ππποΏ½π’π’ππ
ππππ+ π΄π΄ οΏ½ ππππ
ππππ= βπΌπΌπΊπΊ οΏ½ π΄π΄ππ οΏ½ ππππ οΏ½ ππ β πΉπΉππππ β πΉπΉπππ π
4 β ππππππππππ: ππ οΏ½ΜοΏ½ππ π οΏ½π’π’π π ππππ
= βπΌπΌπΊπΊ οΏ½ π΄π΄π π οΏ½ πππ π οΏ½ ππ β πΉπΉπππ π + πΉπΉπππ π
Momentum
Mass 1 β πΊπΊπΊπΊπΊπΊ:πποΏ½ΜοΏ½πππ
ππππ= β
οΏ½ΜοΏ½ππ π ,ππ
π’π’π π οΏ½
ππππππππ
οΏ½ πππΆπΆπΆπΆ2 2 β ππππππππππ:πποΏ½ΜοΏ½ππ π
ππππ= β
πποΏ½ΜοΏ½πππ
ππππ
EF carbonator modeling β Equations
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 12/20
Complementary correlations
Dilute reactor is the most suitable option for the cement plant CaL application, becauseof the experience with entrained flow technologies and the low particle size.A simple, finite-difference model (axial discretization) has been developed to solve mass,momentum and energy equations and evaluate the potential CO2 capture rate.
Energy5 β πΊπΊπΊπΊπΊπΊ:
ππ οΏ½ΜοΏ½πππ οΏ½ βππ + 0.5 οΏ½ οΏ½ΜοΏ½πππ οΏ½ π’π’ππ2 + πΌπΌπΊπΊ οΏ½ οΏ½ΜοΏ½πππ οΏ½ ππ οΏ½ ππ
ππππ= βοΏ½ΜοΏ½π€πππ π β οΏ½ΜοΏ½πππππ β οΏ½ΜοΏ½ππππ π β οΏ½ΜοΏ½ππΆπΆπΆπΆ2,ππππππππ
6 β ππππππππππ:ππ οΏ½ΜοΏ½ππ π οΏ½ βπ π + 0.5 οΏ½ οΏ½ΜοΏ½ππ π οΏ½ π’π’π π
2 + πΌπΌπΊπΊ οΏ½ οΏ½ΜοΏ½ππ π οΏ½ ππ οΏ½ ππππππ
= οΏ½ΜοΏ½π€πππ π β οΏ½ΜοΏ½ππ π ππ + οΏ½ΜοΏ½ππππ π + οΏ½ΜοΏ½πππ,ππππππππ + οΏ½ΜοΏ½ππΆπΆπΆπΆ2,ππππππππ
4 β ππππππππππ: ππ οΏ½ΜοΏ½ππ π οΏ½π’π’π π ππππ
= βπΌπΌπΊπΊ οΏ½ π΄π΄π π οΏ½ πππ π οΏ½ ππ β πΉπΉπππ π + πΉπΉπππ π
Momentum
Mass 1 β πΊπΊπΊπΊπΊπΊ:πποΏ½ΜοΏ½πππ
ππππ= β
οΏ½ΜοΏ½ππ π ,ππ
π’π’π π οΏ½
ππππππππ
οΏ½ πππΆπΆπΆπΆ2 2 β ππππππππππ:πποΏ½ΜοΏ½ππ π
ππππ= β
πποΏ½ΜοΏ½πππ
ππππ
3-Gas: ππ οΏ½ΜοΏ½ππποΏ½π’π’ππ
ππππ+ π΄π΄ οΏ½ ππππ
ππππ= βπΌπΌπΊπΊ οΏ½ π΄π΄ππ οΏ½ ππππ οΏ½ ππ β πΉπΉππππ β πΉπΉπππ π
EF carbonator modeling β Equations
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 13/20
Methodology and scope
Simulation assumptions:Reactor length: β’ 150 mSorbent nature: calcined raw meal β(66.1% CaO, 4%CaCO3, 21% SIO2, 3.1% Al2O3, 1.1% Fe2O3, 3.6% MgO, 1.1%CaSO4)
Inlet solid/gas velocities: β 0/15 m/sInlet solid/gas temperatures: β 600/600Β°CIsothermal reactor walls.β
Sensitivity analysis on:Solid loading β ( οΏ½οΏ½ΜοΏ½πππ
οΏ½ΜοΏ½πππ = 1/3/6);Reactor wall temperature (Tβ W=260/320/500Β°C)Carbonators number (β 1/4)Sorbent maximum conversion (Xβ MAX=10/20/30%).
Definition of reactor boundary conditions and simplified design;1)Calculation of the CO2) 2 capture rate as a function of kinetic models;Identification of the most promising operating parameters.3)
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 14/20
Simulation results (i) β Effect of solid loading (οΏ½ΜοΏ½πππ/οΏ½ΜοΏ½πππ)
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0 20 40 60 80 100 120 140
CO2
capt
ure
effic
ienc
y
Reactor length [m]
XMax=20%TW=320Β°CRaw meal as sorbent
ππ Μ_ππ/ππ Μ_ππ= 3
ππ Μ_ππ/ππ Μ_ππ= 1
οΏ½ΜοΏ½πππ/οΏ½ΜοΏ½πππ= 6
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 15/20
L=150 m , v=15 m/s L=60 m , v=4 m/s
Alternative geometry: downdraft carbonator
DOWNDRAFTUPDRAFT
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 16/20
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
0 20 40 60 80 100 120 140
CO2
capt
ure
effic
ienc
y
Reactor length [m]
XMax=20%, TW=320Β°C- - - - Conventional (vGas=15 m/s)____ Downdraft (vGas=4 m/s)
ππ Μ_ππ/ππ Μ_ππ=1
Simulation results (ii) β Downdraft vs updraft
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 17/20
Simulation results (iii) : Natural raw meal as sorbent
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 18/20
Simulation results (iv) : Synthetic raw meal as sorbent
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 19/20
Conclusions
A relatively high solid loading (β ms/mg=6Γ·10) is required for obtaining high capture rates;
Sorbent capacity (β raw meal nature, calcination condition) has a significant impact on carbon capture rate;
Downdraft option allows for higher residence time and higher sorbent βloadings improves capture rates;
Further research needs :
-properties of different raw meals and calcination conditions on CaO sorbent performance
-fluid dynamics of EF reactor at high solid/gas ratio -experimental validation of the concept under realistic conditions
Entrained flow CaL reactors for CO2 capture in cement plants, 7th HTSLC, LuleΓ₯, 4/5-9-2017 20/20
Thank you for your attention!
Activities related to Cemcap project have received funding from the European Unionβs Horizon 2020 research and innovation programme under grant agreement No 641185.https://www.sintef.no/projectweb/cemcap/
http://www.leap.polimi.it/leap/http://www.gecos.polimi.it/
ACKNOWLEDGMENTS