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潘偉平 Wei-Ping Pan
Taipei, Taiwan
October 23-26, 2016
CLEAN COAL TECHNOLOGY FOR
THE POWER INDUSTRY
26th Modern Engineering & Technology Seminar 2016
主要內容
Contents
• Coal may be challenged, but Coal is not
dead!
• Solution for Cleaning Coal Power
Legislation & Regulation
Implementation
Using & Optimization (Performance Improvement:
efficiency, reliability, availability)
Monitoring Continuously
美國煤炭現狀
Current Coal Status in the U.S.
51% 38%
9%
2%
2012年
美國煤炭探明儲量2372億噸
煙煤 bituminous
次煙煤
subbituminous coal
褐煤 lignite
無煙煤 anthracite
燃煤发电
钢铁
建材
生活
化学产品
美國煤炭消費中
有約94%都用於發電
燃煤發電
Coal-fired Power
Generation
鋼鐵
Iron and Steel
建材
Building materials
化學產品
Chemicals
生活
Life
% Share of Power Source Coal Deposited in USA
Source: U.S Energy Information Administration, http://www.eia.gov/coal/data.php#consumption
美國燃煤、燃油電廠分佈
Location of Coal and Oil Power Plants in USA
能源價格對美國電力行業的影響 Impact of Energy Prices on the U.S Power Industry
2005-2015年美國能源價格
Do
llar
per
to
n
Do
llar
per
Mcf
D
oll
ar p
er b
arre
l
Source: 1.U.S Energy Information Administration. COAL DATA BROWSER. Market average price, annual.
2.U.S Energy Information Administration. U.S. Natural Gas Wellhead Price. https://www.eia.gov/dnav/ng/hist/n9190us3a.htm
3.U.S Energy Information Administration .U.S. Crude Oil First Purchase Price.
https://www.eia.gov/dnav/pet/hist/LeafHandler.ashx?n=PET&s=F000000__3&f=A
美國發電量及其能源結構分佈 U.S. Energy Generation and Distribution Structure
美國電力產業
U.S. Electrical Power Industry
33.77%
32.91%
19.14%
5.93%
4.38%
1.02%
2.84%
煤
coal
天然氣
natural gas
核能
nuclear
水電
hydropower
風能
wind energy
太陽能
solar
其它
other
38.33%
27.86% 19.48% 6.40%
4.41%
1.02% 2.84%
44.70%
23.93% 19.56%
6.38% 0.00%
2.82%
2015 2014 2010
Source: U.S Energy Information Administration, Electric Power Monthly. Net Generation for all sectors monthly,
http://www.eia.gov/electricity/data/browser/.
2015 電力來源百分比份額 2015 Percentage share of power source
美國,中國以及台灣電力產業
U.S., China and Taiwan Electrical Power Industry
Source: 1. U.S Energy Information Administration, Electric Power Monthly. Net Generation for all sectors monthly, http://www.eia.gov/electricity/data/browser/.
2. 《2016-2022年中国电力行业运行态势及投资战略研究报告》
3. Provided by Prof. Hsu Heng-Wen, Natural Resources Technology Division, Green Energy and Environment Research Lab, Industrial Technology Research Institute
世界電力行業能源結構預測
Prediction of Energy Structure in the World
World net electricity generation by fuel (trillion kilowatthours)
Source: 1. U.S Energy Information Administration, International Energy Outlook 2013.
1. U.S Energy Information Administration, International Energy Outlook 2016.
40%
36%
22%
24%
Prediction in 2013 Prediction in 2016
29%
28%
40%
22%
美國電力控制污染排放環保政策的制定 U.S. Power Plants to Develop Pollution Control Environmental Policy
Sources of Mercury Emissions in the U.S.
Industrial
Category
1990
Emissions
tons per year
(tpy)
2005
Emissions
(tpy)
Percent
Reduction
Power Plants 59 53 10%
Municipal Waste
Combustors 57 2 96%
Medical Waste
Incinerators 51 1 98%
臭氧
Ozone
細顆粒物
PM2.5
'08 '09 '10 '11 '12 '13 '14 '15 '16 '17
Beginning
CAIR Phase I
Seasonal
NOx Cap
HAPs MACT
proposed
rule
Beginning
CAIR Phase
II Seasonal
NOx Cap
Revised
Ozone
NAAQS
Begin
CAIR
Phase I
Annual
SO2 Cap
Beginning CAIR
Phase II Annual
SO2 & NOx Caps
Next PM-
2.5
NAAQS
Revision
Next Ozone
NAAQS Revision
SO2 Primary
NAAQS
SO2/NO2
Secondary
NAAQS
NO2
Primary
NAAQS
二氧化硫/
氮氧化物
SO2/NO2
New PM-2.5 NAAQS
Designations
CAMR &
Delisting
Rule vacated
汞/有害空氣污染物
Hg/HAPS
Final EPA
Nonattainment
Designations
PM-2.5
SIPs due
(‘06)
Proposed CAIR
Replacement
Rule Expected
HAPS MACT
final rule
expected
CAIR
Vacated
HAPS MACT
Compliance 3 yrs
after final rule
CAIR
Remanded
空氣
Air
Begin
CAIR
Phase I
Annual
NOx Cap
PM-2.5
SIPs due
(‘97)
316(b) proposed
rule expected
316(b) final rule
expected
316(b) Compliance
3-4 yrs after final rule Effluent
Guidelines
proposed rule
expected
水Water
Effluent Guidelines
Final rule expected Effluent Guidelines
Compliance 3-5 yrs
after final rule
Begin Compliance
Requirements under
Final CCB Rule
(ground water
monitoring, double
monitors, closure,
dry ash conversion)
灰Ash
Proposed
Rule for CCBs
Management
Final
Rule for
CCBs
Mgmt
Final CAIR
Replacement
Rule Expected
Compliance with
CAIR
Replacement Rule
二氧化碳
CO2
CO2
Regulation
Reconsidered
Ozone
NAAQS
美國電力控制污染排放環保政策的制定 U.S. Power Plants to Develop Pollution Control Environmental Policy
(Legislation & Regulation)
污染物排放控制政策及規定 Emission Policies and Regulations for Pollutants Control
Regulation/Policy
Emission limits
(mg/Nm3)
SO2 NOx PM Mercury (Hg)
United States EPA 2013 113 181 10 MACT
(90% removed)
China
GB13223-2011 50 100 20 0.03
Plan for energy-
saving and
emission-
reduction in coal-
fired power plants
(2014-2020)
35 50 10 —
Near Zero
Emission 2014 35 50 5 —
Taiwan Existing 172 144 20 0.005
New-built 86 62 10 0.002
CO2
Capture
Low-NOx
Burner
OFA
Urea
Injection Stack
CO2
Compressed for transport and storage SO2 & Hg
Scruber
ESP/ FF
PM & Hg
Capture
Activated
Carbon
or
Fly ash
SCR
DeNOx
BOILER
(~90%)
(~??.?%)
(~95%)
燃煤電廠清潔燃燒的解決途徑 Solutions and Opportunities for Cleaning Coal Power
WESP
Low Temperature Economizer
蒸汽循環技術發展 Technology Development of Steam Cycles
(Performance Improvement)
煤電機組效率提高方法
Improving Coal-Burning Unit Efficiency
T h e t h e o r e t i c a l b a s i s o f
thermodynamic cycle in coal-
burning unit——Rankine cycle
The improving method of coal-
burning unit efficiency:
• Capacity expansion reforming
• Main steam / reheat steam temperature improving retrofit
• Subcritical unit upgraded to supercritical/Ultra-supercritical unit
鍋爐 Boiler
• Conventional flow path retrofit
• Main steam / reheat steam temperature improving retrofit
• Subcritical unit upgraded to supercritical/Ultra-supercritical unit
汽輪機Turbine
發電機相關技術改造
Generator related reformation
輔助系統相關技術改造
Auxiliary System related reformation
Reheating cycle Regenerative cycle
𝜼 =𝑾𝒏𝒆𝒕
𝒒𝟏≈𝒉𝟏 − 𝒉𝟐𝒉𝟏 − 𝒉𝟑
= 𝟏 −𝒉𝟐 − 𝒉𝟑𝒉𝟏 − 𝒉𝟑
中國煤電機組平均供電煤耗
The Average Coal Consumption Rate of Power Supply in China
The average coal consumption rate of power supply in China: 315g/kWh (2015)
Unit: g/kWh
1000MWe
Ultra-
supercritical
660MWe
Ultra-
supercritical
600MWe
Supercritical
350MWe
Supercritical
600MWe
Subcritical
300MWe
Subcritical
Water
cooling unit 282 289 300 310 312 324
Air cooling
unit 305 307 320 323 330 340
0
5
10
15
20
25
Quantity of Ultra-supercritical unit in China
1000MWe 660MWe
Source: Jianxiong Mao, Development of Utra-supercritical Technology for Power Generation, Paper presented at the Chinese Society
of Power Engineering Annual Conference on Ultra-Supercritical Technology 2015, January 13-15, 2016, Nanjing, Jiangsu, China.
供電凈效率與材料成本
Net Power Supply Efficiency and Material Cost
Ultra-Supercritical unit (28-31MPa/600℃/600℃)
Ultra-Supercritical unit (28-31MPa/600℃/620℃)
High Ultra-Supercritical unit (33-35MPa/640℃/650℃)
High Ultra-Supercritical unit (40MPa/700℃/700℃) Further improve efficiency:
600℃→700℃
Approximation to the Carnot cycle
Net
po
wer
su
pp
ly e
ffic
ien
cy, %
Steam temperature, ℃
Improve
thermodyn
amic design
of power
plant Development of high-temperature
material technology
700℃ double-reheat USC (after 2025)
600℃ double-reheat USC (2015)
600℃ single-reheat USC (2006 - present)
影響燃煤電廠能效水平的主要因素 Principal Factors Influencing the Energy Efficiency of Power Plant
Influencing Factors
Impact on the coal
consumption amount
(g/kWh)
1 Poor Performance of Turbine 5-12
2 Operation in Low Load 3-7
3 Poor Performance of Cold End(low vacuum) 0.5-5
4 Low Efficiency of Boiler 1-3
5 Large Quantity of Desuperheater Spray of Boiler 0.5-2
6 Valve Internal Leakage of Thermodynamic System 0.5-3
7 Frequently Starting and Stopping of Unit 0.5-1.5
8 Main/Reheat Steam Temperature & Pressure <1
9 Poor Heat-Retaining Capacity <0.2
10 Poor Performance of Boiler Feed Pump Turbine 0.5-1
煤質調節:酵素技術及其收益 Coal Conditioning : Enzyme Technology and Benefits
Enzyme
Dilution
Spray
Coal Preparation
Stilling Combustion
optimization
超低排放改造技術路線 Technology Route for Ultra-Low Emission Retrofitting
Low NOx Burner
Boiler -- 353oC ---- 350oC ----- 117oC ------- 90oC ---------- 89oC --------- 50oC ---------------------- >80oC
Flue Gas Temperature
ESP,FGD,WESP細顆粒物質量分佈 Fine PM Mass Distribution in ESP, FGD and WESP
吸附劑注射汞捕集方法起源 Genesis of Sorbent Injection for Mercury Capture
Hg0 Hg2+ Hgp
Contact Conversion Capture
Particles Surface Pores
• Major issues with
measurement of Hg
at these low levels in
actual flue gas.
(OHM)
• Development of Hg
control technologies
in laboratory and
pilot scale.
1990s
• Hg measurement
improvements and
options expanded.
(OHM, CEM &30B)
• Field studies with
halogen-treated
sorbents (AC and
non-carbon
sorbents)
2000s
• Measurement still
challenging and high
maintenance.
• Specific application
challenges (SO3, concrete,
compatibility &
corrosion)
• compliance at 1.2 lb/Tbtu,
using ACI considered as
maximum achievable
control technology and
best available control
technology
2016
飛灰基汞控制系統
Fly Ash-base Mercury Control System
07:3
0:0
0
08:3
0:0
0
09:3
0:0
0
10:3
0:0
0
11:3
0:0
0
12:3
0:0
0
13:3
0:0
0
14:3
0:0
0
15:3
0:0
0
16:3
0:0
0
1
2
3
4
5
6
7
experiment 3experiment 2
Me
rcu
ry c
on
ce
ntr
atio
n(
ug
/m3) baseline experiment 1
SCR
ESP
FGD
燃煤電廠產生的煙氣中,二氧化碳所佔比例僅15%左右,所以碳捕集過程中最大的花費是如何提高二氧化碳的濃度。
CO2 separation:
~ $50-100 / ton carbon
& energy intensive
CO2 disposal:
~ $4-8 / ton carbon
CO2 separation:
~ $100-200 / ton carbon
& energy intensive
碳捕集的技術:挑戰 CO2 Sequestration Technologies – Technical Obstacles
燃燒后 捕集
IGCC燃燒前 捕集
富氧燃燒
CO2 separation:
~ $35 / ton carbon
& energy intensive
Chemical
MEA
Caustic
Ammonia
Others
Adsorber beds
MOF
Zeolite
Active carbon
Tire char
Chicken waste
Others
Regeneration
method
(Vacuum) Pressure swing
Temperature swing
Washing
Open system
Close system
Gas separation
Polyphenyleneoxide
Polydimethylsiloxane
Gas absorption
Polypropelene
Ceramic based
systems
Oxygen Carriers
Cu based
Ni based
Fe based
碳分離和捕集的技術:解決方法 CO2 Separation and Capture
Absorption
Cryogenics
Microbial/
Algal
Systems
Membranes Oxy-
Combustion
Chemical
Looping
Combustion
Adsorption
碳酸氫銨CO2捕集技術中試實驗 Pilot-scale of CO2 Capture by Ammonium Bicarbonate Technology
碳酸氫銨CO2捕集技術中試實驗 Pilot-scale of CO2 Capture by Ammonium Bicarbonate Technology
Steam
from
turbine
Condensate
return
SaskPower Clean Coal Project:
Cansolv Amine-base SO2&CO2 Integrated System
Flue gas
Steam
from
turbine Condensate
return
Lean
SO2
Amine
Rich
SO2
Amine
Lean
CO2
Amine
Rich
CO2
Amine
10% CO2 Storage
90% CO2 Enhanced Oil Recovery
SO2
converted
to Sulfuric
Acid
傳統CCS技術的花費 Current Costs for Conventional CCS options
Post Combustion Capture $65/t CO2 or another $65/MWh added to a new Supercritical PC unit + WFGD + SCR
Oxy-combustion $54/t CO2 or another $54/MWh added to a new Sub-Critical PC unit + WFGD + SCR
Pre-Combustion Capture with IGCC $41/t CO2 or another $41/MWh added to a new IGCC
Chemical Looping Combustion Potential $19/t CO2 to $35/t CO2 or another $19/MWh to $35/MWh added to a new Circulating
Fluidized Bed Combustor
Only if the coat for capturing CO2 can be reduced to a cost less than the
CO2 can be sold for beneficial uses like Enhanced Oil Recovery (EOR)
-- i.e. < $35/t CO2
Only if processes can be developed to convert the CO2 into high value
liquid fuels and chemicals while paying for the CO2 at >$35t/ CO2
不依靠碳捕集&儲存技術,未來電廠能否符合CO2排放標準? Can Future Coal Plants Meet CO2 Emission Standards Without Carbon Capture & Storage?
US EPA “New source performance standard” (August 3, 2015, court pending) :
new coal power plant : 636kg/MWh of CO2 emission Current state-of-art coal-fired power plant with USC steam conditions above 593℃ , emit
approximately 800kg/ MWh.
IGCC plant: 700kg/MWh
Advanced USC with 12.5% Steam utilization (high efficiency combined heat-and-power
applications): 636kg/MWh
IGCC plant with high quality coal: 627kg/MWh
Development of gasifiers integrated with solid oxide fuel cells, with combined cycle plants
having firing temperatures for the combustion turbine approaching 1700℃ : ~ 500kg/MWh
為何煤電?
Why Coal Power ?
If not Coal then what ?
Wind & Solar Ok - availability
Hydro Ok - location
Gas & Oil Ok - cost
Nuclear Ok – waste / base
Coal – Clean Coal ??
Clean Coal is not a silver bullet, however, we
will almost surely have to burn more coal
for a few decades.
“If your only tool is a hammer – then your solution is very likely to be a nail”
電廠潔淨煤技術 Clean Coal Technology for the Power Industry
The USA, China and Taiwan will continue to rely on coal for about 30% of their power
generation needs. This is because of the lower cost and abundance of the resource.
由於費用低廉和資源豐富,美國、中國、臺灣30%以上的電力依然將依賴於燃煤。
However, the challenge is to reduce the amount of pollution and green gas emitted
during coal combustion. The increase in power efficiency through Ultra supercritical
unit (such as Subcritical unit upgraded to Supercritical /Ultra-supercritical
unit)with ultra-low emission technologies (the combined application of lower
temperature economizer, retrofitted SCR, ESP, FGD and WESP) is the most effective
way to continue to use coal.
由於燃煤過程中產生污染物和溫室氣體,超臨界(例如亞臨界升級為超臨界/超超臨界)和超低排放技術(例如採用低溫省煤器、濕式電除塵,對SCR、ESP、FGD改造升級)是燃煤發電持續發展最有效的措施。
Ultimately, cost and emissions are issues for thermal energy, space is an issue for wind energy
and safety is an issue for nuclear energy.
根本上,費用和排放是燃煤發電的關鍵,空間限制是風電的關鍵,安全性是核電的關鍵。
The most important criteria for establishing energy policy will have to be based on each
countries energy resources, economic security and energy security.
能源政策的建立要依賴于能源資源、經濟性和安全性。