Oxy-fuel Combustion
eBook - ePub

Oxy-fuel Combustion

Fundamentals, Theory and Practice

  1. 384 pages
  2. English
  3. ePUB (mobile friendly)
  4. Available on iOS & Android
eBook - ePub

Oxy-fuel Combustion

Fundamentals, Theory and Practice

About this book

Oxy-fuel Combustion: Fundamentals, Theory and Practice provides a comprehensive review of various aspects of oxy-fuel combustion technology, including its concept, fundamental theory, pilot practice, large-scale feasibility studies and related practical issues, such as the commissioning and operation of an oxy-fuel combustion plant. Oxy-fuel combustion, as the most practical large-scale carbon capture power generation technology, has attracted significant attention in the past two decades. As significant progress has been achieved in worldwide demonstration and the oxy-combustion concept confirmed by Schwartze Pump, CUIDEN, Callide, Ponferrada and Yingcheng projects in the past five years, this book provides a timely addition for discussion and study.- Covers oxy-fuel combustion technology- Includes concepts, fundamentals, pilots and large-scale feasibility studies- Considers related practical issues, such as the commissioning and operation of an oxy-fuel combustion plant- Focuses on theories and methods closely related to engineering practice

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Yes, you can access Oxy-fuel Combustion by Chuguang Zheng,Zhaohui Liu in PDF and/or ePUB format, as well as other popular books in Physical Sciences & Industrial & Technical Chemistry. We have over one million books available in our catalogue for you to explore.
Chapter 1

Opportunities and Challenges of Oxy-fuel Combustion

Xiaohong Huang; Junjun Guo; Zhaohui Liu; Chuguang Zheng Huazhong University of Science and Technology, Wuhan, China

Abstract

This chapter briefly reviews the background, concept, components, R&D history, and opportunities related to the use of oxy-fuel combustion and then discusses the theoretical and practical challenges of oxy-fuel combustion. An outline for subsequent chapters is also provided.

Keywords

Oxy-fuel combustion; Opportunities; Challenges

1.1 Climate Change and Carbon Capture Storage

1.1.1 Carbon Emission and Climate Change

Greenhouse gases actually guarantee life by preventing heat from escaping the Earths atmosphere. Without this greenhouse effect, the Earth would be very cold. On the other hand, too big an increase in the greenhouse effect causes too much heat to be captured and may result in the Earth being unsuitable for human, plant, and animal life.
CO2 is the most significant component of greenhouse gases. In addition to the carbon released naturally into the Earths ecosystem, humans emit a significant amount of carbon through activities such as burning fossil fuels, wood, and other biofuels. Moreover, human activities release carbon more effectively and rapidly into the atmosphere than natural sources do, thus increasing the atmospheric CO2 concentration. In fact, the atmospheric CO2 concentration is higher now than at any time during the past 500,000 years or longer.
Fig. 1.1 shows the atmospheric CO2 levels at 400,000 years [1]. This data was based on the comparison of atmospheric samples contained in ice cores from Greenland and Antarctica and more recent direct measurements. It is significant that the atmospheric CO2 level fluctuated regularly over the past 400,000 years but that the amount of CO2 dramatically increased to >300 ppm in just the past few decades. This figure provides evidence-based proof that the Industrial Revolution led to a dramatic increase in atmospheric CO2 levels.
Fig. 1.1

Fig. 1.1 The atmospheric CO2 levels for 400,000 years.
Fig. 1.2 presents the global CO2 emissions in the past 250 years [2,3] and shows that global CO2 emissions significantly increased during the past 100 years. The increasing trend almost looks like an exponential curve. To facilitate assessments of long-term trends of atmospheric global temperature, climatologists from NASA's Goddard Institute of Space Studies (GISS) compared the mean for a base period with the annual mean [4]. The temperature anomaly was used to indicate the change in global temperatures, which is defined as the difference between the baseline mean and the annual mean.
Fig. 1.2

Fig. 1.2 The global carbon emissions in the 1751 to 2015 period.
Fig. 1.3 shows the global temperature anomalies between 1880 and 2015 from the Land Meteorological station [5]. In this figure, the period from 1951 to 1980 is used for the baseline period. It is shown that the temperature anomalies were consistently negative during the 1880–1935 period. In contrast, the anomalies have been consistently positive since 1980. The global temperature has increased continuously. Within the past 120 years, the most recent years show the highest anomalies of +0.8°C.
Fig. 1.3

Fig. 1.3 The global annual temperature anomalies in the 1880–2015 period.
The climate of the Earth has varied throughout its history, sometimes considerably. Although the warming before 1950 was natural, it has shown that the processes of human-inspired industrialization are the main reasons for recent significant climate warming.

1.1.2 Status of CCS

Like efficiency improvements and low-carbon fuels, carbon capture and storage (CCS) is considered as a potential technology for achieving large-scale reduction of CO2 emissions from fossil fuel-fired power generation. CCS comprises three stages: CO2 capture, CO2 transport, and CO2 storage.
The aim of CO2 capture technology is to provide high-concentration, high-pressure CO2 sources from large point sources such as power plants. Captured CO2 must be compressed and transported to suitable storage sites. Using pipelines to pump CO2 is the cheapest transport method, and it is already a well-known and reliable technology. The purpose of CO2 storage is to store the captured CO2 and prevent it from entering the atmosphere. There are three options for geological CO2 storage: saline formations, oil and gas reservoirs, and deep unmineable coal seams [6].
The technologies for each stage of the full CCS chain have different degrees of maturity, each CCS stage is technically available and has been used for many years.
CO2 capture technologies have long been used in industry to remove CO2 from gas streams where its not desired or to separate it as a product gas. Some of the earliest CCS projects were in natural gas processing, such as the Sleipner CO2 storage project in Norway, which captures approximately one million tons of CO2 per year.
CO2 transport technology has been used safely for the past 30 years. Thousands of miles of CO2 pipelines that transport CO2 deal with naturally occurring CO2 for enhanced oil recovery (EOR) in the United States. However, challenges exist in the systems that transport CO2 from industrial power plants, because the amount of impurities in the CO2 stream captured from the plants will influence the calculations for the hydraulic design of these pipelines.
Geologic CO2 storage has been carried out for >10 years. Early projects injected CO2 into different geologic formations, including saline formations and oil and gas reservoirs. Monitoring data has shown that the CO2 performed as expected after storage. However, more investigation is needed to improve the predictions of CO2 behavior and to evaluate possible storage sites, because each site will have unique circumstances. The deep saline formations are expected to provide long-term CO2 storage solutions.
Currently, there are five commercial-scale CCS projects worldwide. The CO2 streams of the Sleipner, Snøhvit (Norway), and In Salah (Algeria) projects all come from extracted natural gas, which contains a high concentration of CO2. The CO2 is separated, captured, and stored in underground geological formations. The Rangely project in North America uses CO2 from natural gas processing for EOR and storage at the Rangely field in Colorado. At Weyburn-Midale, the CO2 is captured from a coal-based synfuel plant in North Dakota and piped to an oil field in Canada. In total, five projects store over 5 Mt. of CO2 per year.
In addition to using CO2 for EOR, other CCS paths are not financially feasible. CCS reduces efficiency and adds cost. Thus commercial power plants and industrial facilities will not invest in CCS in the current regulatory and fiscal environment. Only when the costs are reduced will CCS be seen as viable in coal combustion [7]. Meanwhile, the driving force behind CCS research and development is mainly government funding.
Validation of the full CCS process is very expensive. However, the only way to solve the problem of integration and scale-up is to build and operate commercial-scale CCS facilities. In the past year, governmental and demonstration activities increased dramatically. Most of the major economies have already invested in large-scale CCS demonstration projects. For example:
Australia committed AUD 100 million per year for 3 years for the formation of the Global CCS Institute (GCCSI) to foster international collaboration and announced AUD 2 billion for large-scale demonstration.
Canada announced financial support of CAD 3.3 billion for research and development, mapping, and large-scale CCS project demonstration.
The European Union (EU) allocated EUR 1.05 billion from an economic recovery energy program for the support of seven CCS demonstrations.
Norway continues to play a leading role in the development of the Mongstad and Karstø projects.
The United Arab Emirates is developing three large-scale CCS projects, building on the EOR area.
The United Kingdom annou...

Table of contents

  1. Cover image
  2. Title page
  3. Table of Contents
  4. Copyright
  5. Contributors
  6. Preface
  7. Chapter 1: Opportunities and Challenges of Oxy-fuel Combustion
  8. Chapter 2: Fundamentals of Oxy-fuel Combustion
  9. Chapter 3: Coal Ignition in Oxy-fuel Combustion Environment
  10. Chapter 4: Pulverized Coal Combustion Characteristics in Oxy-fuel Atmospheres
  11. Chapter 5: Nitrogen and Sulfur Behavior During Oxy-fuel Combustion and Its Retention
  12. Chapter 6: Mineral Behavior During Oxy-fuel Combustion
  13. Chapter 7: Mercury Behavior and Retention in Oxy-fuel Combustion
  14. Chapter 8: Flame Characteristics of Oxy-fuel Combustion and Burner Design
  15. Chapter 9: Heat Transfer During Oxy-fuel Combustion and Boiler Design
  16. Chapter 10: Pilot and Industrial Demonstration of Oxy-fuel Combustion
  17. Chapter 11: System Integration and Optimization for Large Scale Oxy-fuel Combustion Systems
  18. Chapter 12: Control Concepts, Dynamic Behavior and Mode Transition Strategy for Oxy-fuel Combustion Systems
  19. Chapter 13: Oxygen Production for Oxy-fuel Combustion
  20. Chapter 14: MILD Oxy-fuel Combustion
  21. Chapter 15: Oxy-Steam Combustion
  22. Chapter 16: Chemical Looping Combustion
  23. Index