The current study is primarily concerned with compare between the effects of using natural gas and methanol as an alternative fuel in a dual-fuel engine on the container ship. Firstly, the emission rates (SOx, NOx, and CO2) per trip were evaluated to assess the environmental performance of using methanol and natural gas. The emissions rates are compared based on IMO limitation. Secondly, energy efficiency design index EEDI and energy efficiency operational indicator EEOI are calculated to evaluate the CO2 emission and compare with IMO requirements at different phases. Finally, the impact of using natural gas and methanol on cost-effectiveness is measured.
4.1 Emission assessment
To begin, the reduction effect of using natural gas and methanol as a dual fuel on emissions factors such as SOx, NOx, CO2, PM, CO, and HC was measured. Figure 5 illustrates the emission rates of using 95% dual fuel at (g/kwh). CO2 emission is reduced from 688.7 g/kwh to 555.23 g/kwh when using (95% NG and 5% MDO), and to 295.69 g/kwh when using (95% ME and 5% MDO). The methanol dual fuel decreased NOx emissions from 17 to 3.19 g/kwh, however, there was a slight increase compared to 2.902 for natural gas dual fuel. Both SOx and PM achieved maximum reduction for using dual fuel with ratios of 95% and 97.36%, respectively. HC emissions increased by using dual fuel from 0.6 g/kwh to 1.36 g/kwh and 0.9044 g/kwh for natural gas and methanol, in the order.
NOx emissions are assessed by comparing them with the IMO limitation. According to IMO 2016 limitations, the NOx emission rate is based on engine speed and equals 3.5549 g/kwh. Figure 6 describes the reduction effect of using methanol and natural gas as a dual fuel compared with diesel fuel on NOx emissions. Using diesel fuel is not matching with IMO 2016 regulation, and with increase the ratio of methanol dual fuel and natural gas dual fuel, the NOx emission reduced to 2.6153 g/kwh and 2.3084 g/kwh, respectively. According to Fig.6, using natural gas dual fuel with ratio above 91% NG or Methanol with ratio above 93% ME will be compliant with the new IMO requirements. For Sox emissions, IMO 2020 imposed new requirements for fuel oil used on board ships should not exceed 0.5% sulfur that equals 0.0857 ton/hr. There was a similarity for using dual fuel by natural gas or methanol, which reduced the SOx rate to 0.0001738 ton/hr with (99% NG and 99% ME), as shown in Fig.7. It is now necessary to calculate the total emission per trip and the annual emission for each emission factor. For this, a dual fuel engine with 98% natural gas and 98% methanol was used to evaluate the emission factor, as shown in Table 5. The load factor during maneuvering and standby mode was taken into consideration. It can be noticed the difference between emission factors during operation, maneuvering, and standby modes. Methanol dual fuel engine emits less SOx, CO2, and PM emissions better than natural gas; however, there is a slight increase in NOx emission. According to United Arab Shipping Company data, the Al Riffa container ship makes 6 trips per year at a rate of 49 days per trip. This equates to 295 days per year. By using Eq. (1), the total emission per trip and annual emission were calculated to assess the environmental effect from using a dual fuel engine. Table 6 illustrates the total reduction in emissions achieved by using a dual fuel engine. Using 98% natural gas dual fuel reduced the annual NOx, CO2, SOx, PM, and CO pollution by 85.55%, 20%, 98%, 98%, and 33.60%, respectively, while, using 98% methanol dual fuel recorded a reduction ratio by 83.76%, 58.87%, 98%, 98%, and 60.20%in the order. However, HC pollution increased for each dual fuel.
|
type of emission
|
emission factor (g/kwh)
|
emission rate during operation (kg/hr.)
|
emission rate during maneuvering (kg/hr.)
|
emission rate during standby (kg/hr.)
|
Table 5
the emission factor during, operation, maneuvering, and standby by using natural gas or methanol dual fuel
98% Natural gas (NG) dual fuel
|
NOx
|
2.4568
|
132.8313
|
31.25443
|
7.813607
|
Sox
|
0.0072
|
0.389281
|
0.091596
|
0.022899
|
CO2
|
551.0118
|
29791.44
|
7009.752
|
1752.438
|
PM
|
0.0038
|
0.205454
|
0.048342
|
0.012086
|
CO
|
0.9296
|
50.2605
|
11.826
|
2.9565
|
HC
|
1.384
|
74.82845
|
17.60669
|
4.401674
|
98% Methanol (ME) dual fuel
|
NOx
|
2.7606
|
149.2568
|
35.11925
|
8.779812
|
Sox
|
0.0072
|
0.389281
|
0.091596
|
0.022899
|
CO2
|
283.2758
|
15315.82
|
3603.721
|
900.9304
|
PM
|
0.0038
|
0.20545384
|
0.04834208
|
0.01208552
|
CO
|
0.5572
|
30.12602
|
7.088476
|
1.772119
|
HC
|
0.91409
|
49.42192
|
11.62869
|
2.907172
|
emission
|
Fuel type
|
Emission ton /trip
|
Emission ton /year
|
Reduction ton/year
|
% Of reduction / year
|
Table 6
Environmental analysis of the Al Riffa container ship.
NOx
|
Diesel fuel
|
1408.680
|
8429.770
|
|
|
NG dual fuel
|
203.145
|
1218.251
|
7211.519
|
85.55%
|
ME dual fuel
|
228.266
|
1368.896
|
7060.874
|
83.76%
|
Sox
|
Diesel fuel
|
29.767
|
178.510
|
|
|
NG dual fuel
|
0.595
|
3.570
|
174.940
|
98.00%
|
ME dual fuel
|
0.595
|
3.570
|
174.940
|
98.00%
|
CO2
|
Diesel fuel
|
56954.000
|
341549.500
|
|
|
NG dual fuel
|
45561.529
|
273229.607
|
68319.893
|
20.00%
|
ME dual fuel
|
23423.234
|
140467.655
|
201081.845
|
58.87%
|
PM
|
Diesel fuel
|
15.710
|
94.215
|
|
|
NG dual fuel
|
0.314
|
1.884
|
92.331
|
98.00%
|
ME dual fuel
|
0.314
|
1.884
|
92.331
|
98.00%
|
CO
|
Diesel fuel
|
115.762
|
694.216
|
|
|
NG dual fuel
|
76.866
|
460.960
|
233.256
|
33.60%
|
ME dual fuel
|
46.073
|
276.298
|
417.918
|
60.20%
|
HC
|
Diesel fuel
|
49.612
|
297.521
|
|
|
NG dual fuel
|
114.439
|
686.283
|
-388.762
|
-130.67%
|
ME dual fuel
|
75.583
|
453.269
|
-155.748
|
-52.35%
|
4.2 Energy efficiency assessment
Based on IMO requirements, evaluated, the EEDI is the most effective way to assess the energy efficiency of a ship. As mentioned, there are two values of EEDI, required values that can be calculated by Eq. (7), where X is the reduction percentage and increased from 10% in 2015 to 30% in 2025, as shown in Fig. 8. The required EEDI for the Al-Riffa ship, which was built in 2012, is 15.971 gCO2/ton-nm at the DWT 145528 ton. According to IMO, this value should be reduced to 20% at phase 2 and equal 12.777 gCO2/ton-nm. Another value is the attained EEDI, which is calculated using Eq. 8, and then compare this value with required EEDI in phase 2. Based on IMO regulations, the service speed (23 kn) can be used as a reference velocity (Vref), and 70% DWT is considered as a ship capacity. The actual EEDI is 14.83 gCO2/ton-NM; this value reduced from required EEDI with ratio 7.14%, which is lower than the required EEDI, but will be incompatible with phase 2 from 2020 to 2025, as shown in Fig. 9. The reduction effects from using natural gas and methanol as a dual fuel engine were evaluated for variable ratios (70%, 80%, 90%, and 95%) to find the best percentage of dual fuel that achieves the required EEDI. Fig. 10, illustrates the reduction values from using natural gas and methanol as a dual fuel. The actual EEDI reduced from 11.27 g.CO2/ton. NM at 70% NG dual fuel to 10.827 g.CO2/ton. NM at 95% NG dual fuel, while methanol dropped to 8.362 g.CO2/ton. NM at 95% ME dual fuel. Both of dual fuels complicated with IMO regulation.
Energy Efficiency Operational Indicator (EEOI) is another method adopted by IMO to measure the energy efficiency of the ships and carbon emissions during operations. According to Eq. (14), the EEOI is calculated based on the distance traveled, the transported TEU cargo, and the amount of fuel consumed per trip. For A13 class container ship, theTEU cargoes transported are 13500, over distance 20600 nautical miles. Figure 11 shows that the EEOI during operation is reduced from 0.00017 to CO2/TEU-NM when use MDO to 0.000146 tonCO2/TEU-NM and 0.000077 tonCO2/TEU-NM when use 95% NG and 95% ME, respectively. The calculations for maneuvering and standby were carried out based on 20% and 5% fuel consumption, in order.
4.3 Economic assessment
The economic impact of converting the diesel engine into a dual fuel engine was examined in this section, and the cost-effectiveness of reducing ship NOx, CO2, and CO emissions by using natural gas and methanol was assessed. In terms of capital cost, to calculate the annual fuel cost, it is important to evaluate the total fuel consumption in the case of using diesel fuel and dual fuel, as shown in Table 7. Because marine diesel fuel and alternative dual fuels are so similar, using natural gas or methanol requires only minor changes to diesel fuel infrastructure. As a result, the cost of bunkering facilities for diesel fuel and dual fuel is assumed to be the same in this study. The calculations are based on diesel, natural gas, and methanol fuel costs of 1320.8 $/m3, 684.2 $/m3, and 528.34 $/m3, in addition to 8.0 $/m3 for the bunkering prices (Afdc 2022). Table 8 illustrates the annual fuel cost for diesel fuel and dual fuel (natural gas or methanol)
Table 7
Al Riffa container ship main engine fuel consumptions.
Fuel consumption (m3)
|
diesel engine
|
Dual fuel engine with 90% Natural gas
|
Dual fuel engine with 90% Methanol
|
|
MDO
|
Natural gas
|
MDO
|
Methanol
|
MDO
|
per trip
|
17,280
|
20,753
|
1,900
|
30,226
|
1,900
|
per year
|
103,632
|
124,941
|
11,400
|
181,267
|
11,400
|
Table 8
Fuel consumption annual cost for diesel and dual-fuel engine
cost item
|
Prices in (millions US$/year)
|
|
diesel engine
|
NG-dual fuel engine
|
ME-dual fuel engine
|
Diesel fuel
|
136.877
|
15.057
|
15.057
|
Diesel bunkering
|
0.829
|
0.0912
|
0.0912
|
Natural gas
|
0
|
85.485
|
0
|
Natural gas bunkering
|
0
|
1
|
0
|
Methanol
|
0
|
0
|
95.771
|
Methanol bunkering
|
0
|
0
|
1.45
|
total fuel cost
|
137.706
|
101.6332
|
112.3692
|
For conversion cost from the main engine to a dual fuel engine, it is expected to be 10.72 million dollars with 285 $/kW conversation rate (Andersson and Salazar 2015; Stefenson 2014). For operation and maintenance costs, according to data collected, the total operation and maintenance cost is 714749 $/years (Banawan et al., 2010). Now, the total cost-effectiveness calculated for each emission type based on the added annual cost of the conversion process as discussed by using Eq. (15). Fig. 12, shows the annual cost-effectiveness of the proposed dual-fuel engine in reducing ship emissions for the container ship.