ammonia as an efficient cox-free hydrogen carrier ......fundamentals and applications. 1. hydrogen...
TRANSCRIPT
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Young Suk JoKorea Institute of Science and Technology
AIChE, 2018.10.31
Ammonia as an Efficient COX-free Hydrogen Carrier:
Fundamentals and Applications
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1. Hydrogen Energy
2. Ammonia as an Efficient COX Hydrogen Carrier
3. Technical Applications
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Hydrogen Energy
H2
2013 2014 2015
NEXO
2018
609 km of Driving range
“Korean government expects 5000 H2 stations by 2030”
Congress R&D Meeting(’18.03.30)
Clarity
MIRAI
Tucsan
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Elements on Earth
Oxygen
47%
Silicon
28%
Al 8%
Fe 5%
Others
12%
Nitrogen
78%
Oxygen
21%
Ar 0.9%
Trace 0.1%
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Energy Density of Hydrogen
U.S. Department of Energy
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Research Motivation
Production
Storage
Utilization
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Hydrogen Society - Final Goal
Excess renewable E
BatteryESS
for < MWh
Wind
Electrolyzer Power Transportation
H2
Solar
E-Chemicals/Chemicals(e.g., eH2,
eNH3, eMeOH)
H2O, N2/H2O
CO2/H2O
Fuel Cells
Fossil FuelsReforming
P2L
H2
P2G
(e.g., CH4)
e-
Transportation
CCS
ConventionalRenewable
House
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Ammonia as a H2 Carrier
ReleaseStoreHydrogenation
NH3
N2
➲ Well-developed NH3 synthesis process ( Haber-Bosch )
➲ Easy storage (0.8 MPa, 20 ℃, liquid) & transportation
➲ High hydrogen contents ( 17.7 wt%, 108 gH2/ L(l) )
No further emission of CO2)
Dehydrogenation
Electrolysis PEMFC
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Ammonia to Hydrogen
N2NH3
H2NH3
NH3Decomposition
H2Purification
NH3Removal
• On-site power generation• Hydrogen station
High-purityHydrogen
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COX-free Power-pack fueled by NH3
Chem E (NH3) Fuel CellReformer
Chem E (C4H10) Combustor
Heat E (Heat)
Cham E (H2)
Applications
Electrical E
Jo. Y., et al., Applied Energy 224:194-204, 2018
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Catalyst Development
Jo. Y., et al., Applied Energy 224:194-204, 2018
Surface area
(m2/g)
Pore size
(cm3/g)
Pore
diameter
(Å)
Al2O3 155.3 0.52 129.5
La(10)-Al2O3
145.8 0.60 160.5
La(20)-Al2O3
95.62 0.46 188.8
La(30)-Al2O3
59.47 0.28 184.5
La(40)-Al2O3
47.30 0.22 176.9
La(50)-Al2O3
35.76 0.17 189.3
La doped Al2O3 LaAlO3 (perovskite phase)
La mol (↑) Surface area, Pore size (↓)
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Catalyst Evaluation
Jo. Y., et al., Applied Energy 224:194-204, 2018
➲ 10 or 20 mol% of La promoted Al2O3 showed activities
➲ La(10)-Al2O3 density 0.55 g/mL , La(20)-Al2O3 density 0.78 g/mL
➲ Select Ru2 wt%/La(20)-Al2O3
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Reactor Development
Jo. Y., et al., Applied Energy 224:194-204, 2018
> 99.7% Conversion
Amount of H2 produced>800 L (2.6 kWh)
➲ Stable operation for about 60 min at 550 ℃(currently ~ 7 months durability tested)
➲ Energy efficiency 70%
Adsorbent MaterialsCapacity
(mmol NH3/g)
13X zeolite 3.08
HY zeolite 1.31
HZSM-5 zeolite 0.23
10 wt% Mg-Al2O3 0.46
10 wt% Ca-Al2O3 0.38
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System Process Design
Jo. Y., et al., Applied Energy 224:194-204, 2018
1 kW PEMFC
13X Zelolite
Ru/La-Al2O3
Reactor
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System Integration
Jo. Y., et al., Applied Energy 224:194-204, 2018
0 20 40 60 80 100 120
0
200
400
600
800
1000
1200
Fu
el C
ell P
ow
er
Ou
tpu
t (W
)
Time (min)
Butane + Hydrogen
> 2.3kWh
NH3 9L/min [ 32A, 32.7V ]
Power Generation Demonstration
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Efficiency Analysis
Jo. Y., et al., Applied Energy 224:194-204, 2018
Reformer: ~ 63 %System: ~ 31%
2 3 4 5 6 7 8
35
40
45
50
55
60
Reformer Efficiency
System Efficiency
NH3 Feed rate (L min
-1)
Re
form
er
Eff
icie
nc
y (
%)
18
20
22
24
26
28
30
32
34
Sy
ste
m E
ffic
ien
cy
(%
)
➲ Reformer ηNH3 feed rate, heat source/transfer
➲ System η Waste H2 recovery
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NH3 to H2 to Electricity - Best Efficiency Reported
Jo. Y., et al., Applied Energy 224:194-204, 2018
6 10 14 18 22
20
25
30
35
40
45
50
Sy
ste
m E
ffic
ien
cy
(%
)
Current Loaded (A)
Hydrogen
Butane + Hydrogen
Butane
(b)
OriginalReformer Efficiency: ~ 63 %System Efficiency: ~ 31%
Improved~ 84 %~ 49 %
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Electricity from Ammonia
Jo. Y., et al., Applied Energy 224:194-204, 2018
0 50 100 150 200 250 3000
1
2
3
4
5
6
7
8
System weight (kg)
Gra
vim
etr
ic h
yd
rog
en
cap
acit
y (
gH
2/g
syste
m)
0
10
20
30
40
50
60
Vo
lum
etr
ic h
yd
rog
en
cap
acit
y (
gH
2/L
syste
m)
ReactorCatalyst
Ammonia Tank
Power Pack Packaging
PEMFCUS DOE target
(onboard automotive H2 storage)
➲ 3.4 wt% system based (with heavy NH3 tank)
➲ 4.9 wt% expected (with light NH3 tank)
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Jo. Y., et al., Applied Energy 224:194-204, 2018
Tethered Drone Application
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First Flight Test
Duration Test
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Ammonia Energy Scenarios
Renewable Hydrogen
2018.07.13“Liquid sunshine: Ammonia made from sun, air, and water could turn Australia into a renewable energy superpower,”
2018.05.03
2018.08.08
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NH3 to H2 using Membrane Reactor
Membrane
Catalyst
MR(Simultaneous reforming + purification)
MemCatalyst
Reforming Purification
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Novel NH3 MR Concept
Jo. Y., et al., Journal of Power Sources 400:518-526, 2018
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Membrane and Membrane Reactor
Jo. Y., et al., Journal of Power Sources 400:518-526, 2018 Jo. Y., et al., Seperation and Purification Technology 200:221-229 (2018)
Jo. Y., et al., Applied Energy 224:194-204, 2018
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Performance Improvements
Jo. Y., et al., Journal of Power Sources 400:518-526, 2018
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Comparisons
Jo. Y., et al., Journal of Power Sources 400:518-526, 2018
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암모니아 분리막 반응기
Jo. Y., et al., Journal of Power Sources 400:518-526, 2018
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Ammonia: What needs to be done?
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Novel Strategy: H2 as a Heat Source
Jo. Y., et al., Applied Energy 224:194-204, 2018
𝑆𝐿 ~ 180 𝑐𝑚/𝑠
𝑆𝐿 ~ 35 𝑐𝑚/𝑠