Economic Optimization and Evaluation Assumptions

Table 2: economic assumptions for the 50 MW gas / solar hybrid plant

Investment costs:

Specific Powerblock Investment 6

671 €/kWel, net

Gas burner

Burner Invest = 80 €/kWth x 120 MWth x 1’000 kW/MW x (P/120 MWth)07

^ 75 €/kWth (150 MWth) — 169 €/kWth (10 MWth)

Annual costs:

Operation&Maintenance Power Block

5.5% of Power Block Investment

O&M_Gas Boiler

5.2% of Gas Boiler Investment

Natural Gas (fuel cost)

1.4 ct/kWh

Gas Boiler Efficiency

95%

If not otherwise defined the assumptions of table 1 apply.

Results

In figure 10 the levelised electricity costs are plotted as a function of solar field and burner size.

Levelised

Electricity

Costs

[ct/kWh]

Solar Field Size [m2]

Figure 10: Levelised electricity costs dependent on boiler [MWth] and solar field size [m2]

For all observed burner sizes an optimal solar field size exists resulting in a minimal LEC (convex shape of the surface).

It was taken into account that the gas fraction of the produced thermal energy should not exceed a certain amount for legal, respectively ecological reasons. The Californian SEGS plants are allowed to use 25% gas. In Spain it is being discussed at present to allow small amounts of co-firing but probably only in combination with a thermal storage.

without boiler

Table 3: Optimal plant configurations for Solar Only, 15% and 25% gas co-firing

Optimal configurations

Solar Only

15%

25%

gas share

gas share

Plant Design

Solar field [m2]

490’000

450’000

450’000

Boiler size [MW]

0

30

70

economic results

LEC [ct/kWh]

13.2

12.1

11.3

cost red. due to gas hybrid

8%

14%

Investment [Mio. €]

97

96

99

Full load hours

2’019

2’325

2’716

O&M [ct/kWhel]

3.2

2.9

2.6

O&M [% of total invest]

3.4

3.5

3.6

The results for the examined plant configurations are given in the next table.

Due to more full load hours and comparably low gas prices the levelised electricity costs can be reduced by 8% respectively 14% with increasing gas share in comparison with the Solar Only plant. A further and important advantage of hybrid mode is more reliable operation. The investment costs of all three variants are approximately the same (around 100 M€ for 50 MWel).

Conservative assumptions for O&M-costs have been taken into account and vary between 2.6 and 3.2 ct/kWh (depending on the solar field size). These values are slightly higher than the values of the trough plants in California (2.5 ct/kWh) [6].

An important issue is how efficiently precious natural gas is used in such a hybrid steam plant compared to a high efficiency combined cycle (CC) plant. To answer the question corresponding efficiencies have to be defined:

Table 4: Efficiencies of converting gas into electricity, plant configurations see table 3.

Gas-co-firing:

15% 25%

n1 = Eel, total / Egas

212% 126%

n 2 = (Eel, hybrid — Eel, SolarOnly) / Egas

28% 32%

Пі gives the ratio of plant electricity output and fuel input. r|2 is defined as the ratio of the supplementary electricity yield due to hybrid operation (in excess of a Solar Only plant) divided by the gas input. For p2 it was assumed that the plants are designed optimally according to the LEC (see plant variants in table 3). That means that the hybrid plants have smaller solar fields than the Solar Only plant. In case the optimally designed Solar Only plant was equipped with a gas burner providing for 15 resp. 25% co-firing, the gas converting efficiency would be higher for both variants. For further interpretation of the efficiencies see summary and outlook.