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Modeling and performance analysis of subcritical and supercritical coal-fired power plants with biomass co-firing and CO2 capture

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Abstract

Coal-fired power plants are the largest source of carbon dioxide (CO2) emissions into the atmosphere, and these emissions can be effectively reduced by improving the efficiency of the plants, co-firing sustainably grown biomass and applying carbon capture and storage technologies. In this study, the energy and environmental performances of both subcritical (SubC) and supercritical (SC) pulverized coal-fired power plants with biomass co-firing and integrated with an advanced amine-based postcombustion CO2 capture system were evaluated and compared. The impact of biomass (hybrid poplar) addition was investigated at different co-firing ratios varying up to 30% on a heat input basis. All plant configurations were modeled and simulated with Aspen Plus process simulation software. The results show that the use of a SC steam cycle has a positive impact on the energy and environmental performance of the investigated plants, improving the efficiency by 2.4% points and reducing the total fuel consumption and CO2 emissions by 6% in comparison to those of the SubC cases. Biomass co-firing has a negative impact on the energy performance of plants while significantly reducing fossil-based carbon emissions. The reduction of net CO2 emissions is almost proportional to the biomass percentage in the feed. At 30% biomass co-firing, the net plant efficiency is reduced by approx. 1% point, while the net CO2 emissions are 28% lower than those in coal-fired only plants. The introduction of CO2 capture has a major impact both on the emissions generated and on the energy efficiency. Depending on the plant type and co-firing ratio used, the net plant efficiencies are 8.7–9.3% points lower than those of non-capture cases. The net CO2 emissions achieve negative values when carbon is captured from the biomass co-firing plants.

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Abbreviations

W :

Power (MW)

\(\dot{m}\) :

Mass flow rate (kg/s)

η :

Efficiency (%)

APH:

Air preheater

BA/FA/TA:

Bottom/fly/total ash

BFP:

Boiler feed pump

BFPT:

Boiler feed pump turbine

BH:

Baghouse

BOP:

Balance of plant

CP:

Condensate pump

CW:

Cooling water

DEA:

Deaerator

FD:

Forced draft

FG:

Flue gas

FGD:

Flue gas desulfurization

FW:

Feedwater

FWH:

Feedwater heater

GHG:

Greenhouse gas

HHV/LHV:

Higher/lower heating value (MJ/kg)

HP/IP/LP:

High/intermediate/low-pressure

ID:

Induced draft

LNB:

Low-NOx burner

MEA:

Monoethanolamine

OFA:

Over-fire air

PA:

Primary air

PC:

Pulverized coal

SA:

Spray attemperator

SC:

Supercritical

SCR:

Selective catalytic reduction

ST:

Steam turbine

SubC:

Subcritical

USC:

Ultra-supercritical

ar:

As-received

db:

Dry basis

th:

Thermal

e:

Electrical

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The authors are grateful to anonymous reviewers for their valuable comments and suggestions.

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Cebrucean, D., Cebrucean, V. & Ionel, I. Modeling and performance analysis of subcritical and supercritical coal-fired power plants with biomass co-firing and CO2 capture. Clean Techn Environ Policy 22, 153–169 (2020). https://doi.org/10.1007/s10098-019-01774-1

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