mecos - egcsa
TRANSCRIPT
Content
1 About Mikrotech
2 Sox legislation
3 Alternatives to reducing SOx
4 EGCs
5 Scrubber
6 ROI analysis
7 Global network
PUMYI Company History
The total work amount of DeSox project & DeNox project reached 57000MW.
Dawootech was established
Mikrotech was established by the core R&D team of Dawootech.
1MW Scrubber test platform was completed and we got LR certificate
Strategic cooperation with Nanyang Star and Zhongtian Heavy Industry
Received three orders of newbuilding
1. About Mikrotech
2. Sox Legislation
IMO has confirmed clearly to ship owners, fuel companies and technology providers: The upper limit of sulfur content of 0.5%m/m fuel in the global sea will be enforced in January 1, 2020.The original four emission control zones (North America, the Caribbean Sea, the Baltic Sea and the North Sea emission control zones still implement the fuel sulfur content standard of 0.1% m/m).
Change to Low Sulphur Fuel
Convenient
Relatively small investment cost
Higher operating cost
Future availability of low sulphur fuel
Increased engine wear
Advantage : Disadvantage :
3. Alternatives to reducing SOx
Convert to LNG
Higher operating cost
Very high cost of reconstruction
Global refueling facilities are imperfect
Solution which also reduce NOx and Particulates.
Advantage : Disadvantage :
3. Alternatives to reducing SOx
Allows use of HFOLow lifecycle cost
No need to reconstruction engine and fuel oil supply system
Advantage : Disadvantage :
High cost of one-time input
ROI is subject to the price differentbetween compliant fuel and HFO
Install EGCs
3. Alternatives to reducing SOx
Exhaust In
Exhaust Out
Sea Chest
Seawater pump
Scrubber
SO2 / CO2
CEMS
To overboard
MECOS TM Open-Loop
Wash WaterMonitoring Module
pH / PAH / Turb / T
Circulation pump
Sea WaterMonitoring Module
pH / PAH / Turb / T
4. EGCs
Use sea water
Slightly higher power demand than Closed Loop Mode
Does not need Caustic Soda
Engine Exhaust Chemistry:
S + O2 → SO2 (~95%)
SO2 + 1/2 O2 → SO3 (~5%)
Scrubber Chemistry:
SO2 + H2O → H2SO3
SO3 + H2O → H2SO4
Seawater Reactions:
CaCO3 + H2SO3 → CaSO3 + H2O + CO2
2CaSO3 + O2 → 2CaSO4
Open Loop Mode
4. EGCs
To overboard
Wash WaterMonitoring Module
pH / PAH / Turb / T
Exhaust In
Exhaust Out
SO2 / CO2
CEMS
Scrubber
Sea water
Make-up water
Alkaline additive
Sludge tank
Heat exchaner
WTS
Circulation tank
Circulation pump
Cooling pump
4. EGCs
MECOS TM Close-Loop
Independent on seawater alkalinity
Zero discharge whenever required
Low power demand
Needs Caustic Soda as a reagent
Closed Loop Mode
Engine Exhaust Chemistry:
S + O2 → SO2 (~95%)
SO2 + 1/2 O2 → SO3 (~5%)
Scrubber Chemistry:
SO2 + H2O → H2SO3
SO3 + H2O → H2SO4
Freshwater Reactions:
2NaOH + H2SO3 → Na2SO3 +2H2O
4. EGCs
To overboard
Scrubber WaterMonitoring Module
pH / PAH / Turb / T
Wash WaterMonitoring Module
pH / PAH / Turb / T
Exhaust In
Exhaust OutSO2 / CO2
CEMS
Scrubber
Sea waterAlkaline additive
Sludge tank
Circulation tank
WTS
Cooling pump
Circulation pump
Heat exchaner
Make-up water
4. EGCs
MECOS TM Hybrid-Loop
Exhaust Gas Cleaning installation
Tests run continuously
Test station at Langxi Factory
Training on Exhaust Gas Cleaning Systems
Demonstration for potential customers
Mikrotech Test Facility
4. EGCs
Performance & Parameter
- 98%+ of SO2 eliminated - 50%+ of PM eliminated( by mass )- Alkali consumption 5 - 6 L x MWh x S %- Make-up water consumption 50 L/h x MWh x S %- Sludge formation 2.5kg/h x MWh- Bleed off rate ~0.2 m3/h- Back pressure 100 mmWc ( 1000 Pa )
All values depending on the ambient conditions, water quality and installation specific issues
4. EGCs
Exhaust gas discharge
Correspondence between fuel oil sulfur limits and SO2/CO2 ratios
SO2(ppm)/ CO2 (%v/v)Fuel oil sulfur limits
(%m/m)Remarks
195.0 4.50 MARPOL Annex VI Reg.14.1.1
151.7 3.50 MARPOL Annex VI Reg.14.1.2
65.0 1.50 MARPOL Annex VI Reg.14.4.1
43.3 1.00 MARPOL Annex VI Reg.14.4.2
21.7 0.50 MARPOL Annex VI Reg.14.1.3
4.3 0.10 MARPOL Annex VI Reg.14.4.3
4. EGCs
Wash water discharge
pH > 6.5(4m from discharge point)Turbitidy < Inlet + 25FNUPAH:
Scrubber Water Volume(t/MWh) PAH(ug/L)
0-1 2250
2.5 900
5 450
11.25 200
22.5 100
45 50
90 25
4. EGCs
Procedure for retrofitting
4. EGCs
Onboardsurvey&
3D scanning(2~3days)
Onboard survey & 3D scanning
Feasibility study report
Detailed design for class approval
Production design
Installation in shipyard
Commissioning
Sea trial
Scrubber
U-type or I-type design
All metallic construction
designed with long service life
5. Scrubber
5. Scrubber
Material selection guideNO Part of EGC scrubber Operation condition Material
1 Jet spary
Dry and wet zoneTemperature: ~65℃
PH: >5.5CL-: ~20000ppm
254 SMo1.4529
2 Bottom of jet spary
Wet zoneTemperature: ~65℃
PH: >5.5CL-: ~20000ppm
Super duplex 2507
3Bottom of absorber(including inernal)
Wet zoneTemperature: <50℃
PH: >4CL-: <20000ppm
Super duplex 2507
4Middle of absorber(including inernal)
Wet zoneTemperature: <45℃
PH: >6CL-: <20000ppm
Duplex 2205
5Top of absorber
(including inernal)
Wet zoneTemperature: <45℃
PH: >7CL-: <20000ppm
Duplex 2205
Utilization of proven high efficiency all metallic internals, including low pressure nozzles and non-clogging droplet separators,reducing pressure drop while also reducing weight.Very low maintenance cost
Very high reliability
Excellent efficiency
Meeting IMO, SECA and EPA compliance requirements even when using cheaper high sulfur fuels
Scrubber internal
5. Scrubber
6. ROI analysis(Take 62000BC for example)
62000BC Sox Scrubber calculatorEngine data of ME Scrubber date
SFOC g/kWh 161 scrubber type Open loopFuel consumption Tonnes/day 23.8 Newbuilding or retrofit retrofit
Engine power SMCR KW 8200 Uncertainty in scrubber CAPEX and OPEX % 10
operation load % 75 Scrubber CAPEX Mill.USD 0.65Annual days of operation days/year 200 Retrofit costs Mill.USD 0.4Engine operating power KW 6150 Design costs Mill.USD 0.15
Total CAPEX Mill.USD 1.32Engine data of GE Additional fuel(efficiency) USD/Y 41550
SFOC g/kWh 196Difference in fuel consumption(energy
content)USD/Y 138500
Fuel consumption Tonnes/day 10.8 Maintance cost USD/Y 15000Engine power SMCR KW 900 Total actual OPEX Mill.USD/Y 0.195
operation load % 85Annual days of operation days/year 200 Fuel oil priceEngine operating power KW 765 HFO USD/T ~400
0.5% S min % above HFO % 300.5% S max % above HFO % 80
Actual cost HFO Mill.USD/Y 2.77Actual cost 0.5%Smin Mill.USD/Y 3.6
Payback Actual cost 0.5%Smax Mill.USD/Y 4.98payback after min years 0.6payback after max years 1.8Actual savings min Mill.USD/Y 0.73Actual savings max Mill.USD/Y 2.08
7. Global network
NAVSTAR (HK) TECHNOLOGIES
T: +852-3580-0852 | M: +852-9036-5301
Christine Wong
DAWOO TECH
507ho,Songnae Leaderstel 447 B/D, Sang-dong, Wonmi-
gu, Puchon, Kyounggi-do, South Korea
T: +82-32-327-1080 | F: +82-32-327-1084
GLORYOCEAN
10-103, Xiang Feng Yuan, Chang Zhi, Zhoushan City.
M: +86 188 0580 1539, +86 138 6012 8291
T: +86 580 2180335 | E: [email protected]
AIMSS
Thoornseweg 92 | 4854 EH Bavel |
The Netherlands
T: +31 6 27 28 90 98 |
E: [email protected] | W: aimss.nl
.
MIKROTECH
Jianzhu West Road No. 599, Wuxi City,
Jiangsu Province
T: +86-137-7362-9267 |
E: [email protected] | W: mikrotech.cn