Numerical modeling of heat transfer characteristics in a two-pass oxygen transport reactor for fire tube boilers under oxy-fuel combustion
- 1. Mechanical Engineering Department, College of Engineering, Prince Sattam bin Abdulaziz University, AlKharj 16273 (Saudi Arabia)
- 2. KACST TIC on CCS and Mechanical Engineering Department, King Fahd University of Petroleum & Minerals, Dhahran 31261 (Saudi Arabia)
- 3. Researcher at K.A.CARE Energy Research & Innovation Center at Dhahran (Saudi Arabia)
Description
Highlights: • Increase in boiler thermal load decreases the heat transferred by 2% at 50 bar. • Combustion heat transferred decreases significantly by about 16% at 50 bar. • Total heat transferred to the load slightly decreases as pipe emissivity increases. • The optimum thermal conductivity of the inner pipe was found to be 0.1 W/m-K. Among the available mitigation options for CO2 emissions, oxy-fuel combustion technology has been gaining significant attention as a promising technology for curtailing the CO2 emission. Currently the technology is at the demonstration phase on existing coal and gas power plants and some new pilot plants are being tested. In spite of the prospect, to integrate oxy-combustion to fire-tube boilers, heat transfer challenges need to be addressed due to fragility of the membrane at the hostile operating conditions. In the current study, numerical modeling of a two-pass oxygen transport reactor for fire-tube boiler was conducted to investigate the heat transfer characteristics to the saturated water and steam at various operating pressures, emissivities and thermal conductivities. The results indicate that the effect of varying the boiler thermal load resulted in slight decrease in heat transferred by only about 2% at 50 bar, at fixed fuel firing rate. Despite this insignificant increase in the total heat transferred, the combustion component of the total heat transferred decreases significantly by about 16% at 50 bar. The combustion efficiency was also found to decrease by only about 0.03%, which is considered as insignificant. The total heat transferred to the load slightly decreases as the emissivity of pipes increases up to the emissivity of 0.95 beyond which the heat transferred decreased drastically at emissivity of 1 due to the flame quenching. The optimum thermal conductivity of the inner pipe to deliver highest heat to the load by ensuring flame availability, maximum combustion efficiency of 98.58% as well as optimum heat transfer is found to be 0.1 W/m-K. There were no significant variations in heat transferred and combustion efficiency when the emissivity of the membrane was varied between 0.5 and 1.
Availability note (English)
Available from http://dx.doi.org/10.1016/j.applthermaleng.2021.117248Additional details
Identifiers
- DOI
- 10.1016/j.applthermaleng.2021.117248;
- PII
- S1359431121006852;
Publishing Information
- Journal Title
- Applied Thermal Engineering
- Journal Volume
- 195
- Journal Page Range
- vp.
- ISSN
- 1359-4311
- CODEN
- ATENFT
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 53107278
- Subject category
- S20: FOSSIL-FUELED POWER PLANTS; S42: ENGINEERING;
- Descriptors DEI
- CARBON DIOXIDE; COAL; COMBUSTION; COMBUSTION HEAT; COMPUTERIZED SIMULATION; EFFICIENCY; EMISSIVITY; FLAMES; FOSSIL-FUEL POWER PLANTS; HEAT TRANSFER; MEMBRANES; OXYGEN; PILOT PLANTS; PIPES; THERMAL CONDUCTIVITY
- Descriptors DEC
- CARBON COMPOUNDS; CARBON OXIDES; CARBONACEOUS MATERIALS; CHALCOGENIDES; CHEMICAL REACTIONS; COMBUSTION PROPERTIES; ELEMENTS; ENERGY; ENERGY SOURCES; ENERGY TRANSFER; ENTHALPY; FOSSIL FUELS; FUELS; FUNCTIONAL MODELS; HEAT; MATERIALS; NONMETALS; OPTICAL PROPERTIES; OXIDATION; OXIDES; OXYGEN COMPOUNDS; PHYSICAL PROPERTIES; POWER PLANTS; REACTION HEAT; SIMULATION; SURFACE PROPERTIES; THERMAL POWER PLANTS; THERMOCHEMICAL PROCESSES; THERMODYNAMIC PROPERTIES; TUBES
Optional Information
- Copyright
- Copyright (c) 2021 Elsevier Ltd. All rights reserved.