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Questions and Answers
What is the primary purpose of the water-gas shift reaction in oxy-fuel technologies?
What is the primary purpose of the water-gas shift reaction in oxy-fuel technologies?
Which process is common to Integrated Gasification Combined Cycle (IGCC) power plants?
Which process is common to Integrated Gasification Combined Cycle (IGCC) power plants?
What is the main feedstock for oxy-fuel technologies?
What is the main feedstock for oxy-fuel technologies?
In the steam reforming process, what is the chemical equation for the conversion of CH4 to CO and H2?
In the steam reforming process, what is the chemical equation for the conversion of CH4 to CO and H2?
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What is the method used for the separation of H2 from the H2/CO2 mixture after the water-gas shift reaction?
What is the method used for the separation of H2 from the H2/CO2 mixture after the water-gas shift reaction?
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What is the primary product of the water-gas shift reaction?
What is the primary product of the water-gas shift reaction?
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What is the purpose of the air separation unit in an Integrated Gasification Combined Cycle (IGCC) power plant?
What is the purpose of the air separation unit in an Integrated Gasification Combined Cycle (IGCC) power plant?
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What is the primary purpose of carbon capture in power generation?
What is the primary purpose of carbon capture in power generation?
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What is the main purpose of the steam reforming process in natural gas recovery?
What is the main purpose of the steam reforming process in natural gas recovery?
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What is the end goal of the carbon capture process in the context of power generation?
What is the end goal of the carbon capture process in the context of power generation?
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What is the overall stoichiometry after the water-gas shift reaction when pure carbon is the component gasified?
What is the overall stoichiometry after the water-gas shift reaction when pure carbon is the component gasified?
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What is the composition of CO2 in the situation where pure carbon is gasified?
What is the composition of CO2 in the situation where pure carbon is gasified?
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What is the current capital cost difference between gasification of coal and conventional coal-fired generation?
What is the current capital cost difference between gasification of coal and conventional coal-fired generation?
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How many large scale plants worldwide are currently using gasification of coal?
How many large scale plants worldwide are currently using gasification of coal?
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What is the maximum efficiency of fuel cells when employing Hydrogen from IGCC?
What is the maximum efficiency of fuel cells when employing Hydrogen from IGCC?
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What are the advantages of gasification?
What are the advantages of gasification?
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What does the capture cost comparison indicate between absorption capture in post-combustion capture and precombustion capture involving IGCC?
What does the capture cost comparison indicate between absorption capture in post-combustion capture and precombustion capture involving IGCC?
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What primarily involves H2 recovery in carbon capture?
What primarily involves H2 recovery in carbon capture?
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What additional power demand arises in the reformer operation?
What additional power demand arises in the reformer operation?
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What is the equation for the minimum power in the given context?
What is the equation for the minimum power in the given context?
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What are the advantages of fluidized bed gasification units compared to fixed or slow moving bed units?
What are the advantages of fluidized bed gasification units compared to fixed or slow moving bed units?
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What is the minimum gas velocity for fluidization obtained from?
What is the minimum gas velocity for fluidization obtained from?
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What is the typical range for gasification temperature to ensure thermodynamic equilibrium and fast kinetics?
What is the typical range for gasification temperature to ensure thermodynamic equilibrium and fast kinetics?
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What are the two types of solid gasification units mentioned in the text?
What are the two types of solid gasification units mentioned in the text?
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What are the common disadvantages of fluidized bed gasification units mentioned in the text?
What are the common disadvantages of fluidized bed gasification units mentioned in the text?
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What determines the average conversion of the carbon-based feedstock in designing a solid phase gasification unit?
What determines the average conversion of the carbon-based feedstock in designing a solid phase gasification unit?
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What are the new designs being developed to overcome traditional fluidized bed design drawbacks?
What are the new designs being developed to overcome traditional fluidized bed design drawbacks?
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What describes the behavior of reacting particles in the gasification process?
What describes the behavior of reacting particles in the gasification process?
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What type of gasification units are suitable for gasification of low-grade and higher grade solid fuels, as well as fuels forming highly corrosive ash?
What type of gasification units are suitable for gasification of low-grade and higher grade solid fuels, as well as fuels forming highly corrosive ash?
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What is the fluidization velocity?
What is the fluidization velocity?
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Study Notes
Types of Solid Gasification Units
- Two types of solid gasification units are co-current moving bed and counter-current moving bed.
- Co-current moving bed units operate at low throughput and produce high-temperature gas with low tar levels.
- Counter-current moving bed units have low throughput, moderate temperature gas output, and high tar levels.
- Fluidized bed gasification units have advantages such as rapid heat transfer, temperature control, and higher throughput than fixed or slow moving beds.
- Fluidized bed units are suitable for gasification of low-grade and higher grade solid fuels, as well as fuels forming highly corrosive ash.
- Common disadvantages of fluidized bed gasification units include low conversion efficiency and influence by back-mixing process.
- New designs like Entrained Flow Gasifiers and Transport Gasifiers are being developed to overcome traditional fluidized bed design drawbacks.
- Fluidization velocity is the velocity at which particles in the packed bed become "fluidized."
- The minimum gas velocity for fluidization is obtained from the Ergun equation.
- Two models describe the behavior of reacting particles: partially reacted particle and flaking ash or gaseous products causing shrinkage.
- The gasification temperature is typically maintained in the range of 1200-1400K to ensure thermodynamic equilibrium and fast kinetics.
- Designing a solid phase gasification unit requires considering the average conversion of the carbon-based feedstock, largely determined by residence time distribution (RTD).
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Description
Test your knowledge of solid gasification units with this quiz! Learn about co-current and counter-current moving bed units, fluidized bed gasification, new designs like Entrained Flow Gasifiers and Transport Gasifiers, gasification temperature, and more.