Thermal Processes Flashcards

1
Q

Up draught combustor

A

Design: Simple, natural draught.
Fuel: Batch above bed, secondary air above.
Combustion: Through most of bed.
Suitable for: Wood logs or large biomass.
Issue: Excessive smoke.
Variation: Can use natural or forced draught.

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2
Q

Down draught combustor

A

Requirement: Combustion or flue gas fan.
Fuel Combustion: Partial at base, completed in afterburner.
Control: Microprocessor-controlled for emissions.
Cost: Expensive

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3
Q

Large scale combustion technology

A
  • Fixed bed: combustion on a grate
  • Fluidised bed: combustion in inert suspended particles.
  • Pulverised fuel combustion.
  • Fife: bubbling/circulating fluidised bed.
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4
Q

Emissions in combustion boilers?
How are they reduced?

A

CO, NOx, HC and particulates (dioxins and furans in wood combustion)
Using secondary air

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5
Q

What is gasification?

A

Conversion of solid carbonaceous fuels into a flammable mixture of gas.

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6
Q

How is heat supplied for gasification?

A

Externally or by using a small amount of air for partial oxidation.

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7
Q

Process of gasification

A

1.) Pyrolysis (high T favours gases):
C6H10O5  5CO + 5H2 + C
2.) Partial oxidation (direct, less than stoichometric):
C6H10O5  5CO + 5CO2 + 5H2
3.) Reforming (gasification in the presence of steam, or steam-air:
C6H10O5 + H2O  6CO + 6H2

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8
Q

Applications of biomass gasification

A

IC engines gas turbine, fuel cells

H production, chemical feedstocks

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9
Q

What are the gas/solid reactions in gasification?

A

C + H2O  CO + H2
CO2 + C  2CO
Heat provided by:
C + 0.5O2  CO

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10
Q

Gas phase reactions in gasification:

A

WGS:
* CO + H2O  CO2 +H2
Methanation:
* CO + 3H2 CH4 + H2O

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11
Q

What other reactions occur in gasification?

A

Hydrogenation of biomass and char (exo)
pyrolysis, cracking, rearrangement of polymers and tars.

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12
Q

Effect of increasing T and P on the syngas composition?

A

P - favours CH4 and CO2
T - Favours CO and H2

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13
Q

Updraft gasifier

A

Operation: Fuel added from above, sub-stoichiometric air from below.
Zones: Combustion at bottom, gasification in middle, drying at top.
Tar Production: Yields large quantities of tar.

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14
Q

Downdraft gasifier

A

Direction: Fuel and gas flow in the same direction.
Design: Modern designs include air nozzles for hot char bed.
Tar Production: Yields small amount of tar, requires low ash, low moisture fuel.
Issue: Ash slagging in combustion zone can be problematic

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15
Q

Fluidised bed gasifier

A

Operation: Gas stream passes through bed of inert particles.
Mixture: Turbulent mixture, fuel is small fraction of solid.
Temperature Control: Uniform temperature and concentration, simultaneous gasification.
Advantages: Easily scalable, wide fuel variety usable.

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16
Q

Entrained flow gasifier

A

Conversion: High char conversion, low tar.
Suitability: Ideal for coal, less so for biomass without co-gasification.
Challenges: Expensive for biomass due to fine particle production, low energy density, high sintering.

17
Q

What gasifier is used commercially, what’s the problem

A

Fluidised bed - ammonia removal

18
Q

What are pyrolysis products used for?

A

Char: solid fuel or gasify
Liquid: liquid fuel, chemicals, refinery feedstock.
Gas: Fuel

19
Q

What is pyrolysis oil and problems associated

A

Bio-oil is a low viscosity dark-brown fluid with a high water content, but generally does not phase separate. Highly oxygenated and highly unstable.

20
Q

What is fast pyrolysis of biomass

A
  • Short heat up and reaction times.
  • Rapid removal and quenching of organic volatiles minimises carbonisation or further cracking. Short residence time.
  • Reactor configuration acheives yields of liquid up to 70-80% based on dry biomass
21
Q

What compounds are water soluble/insoluble in pyrolysis oil? How to remove

A
  • Water soluble: low MW acids
  • Water insoluble: Aromatics (lignin, BTX, phenols)

Addition of equal volume water precipitates lignin

22
Q

Uses of pyrolysis bio oil

A
  • Direct substitute for heating oil.
  • Possible fuel for combustion turbines or modified diesel engines.
  • Possible recovery of high value chemicals
  • Interest in blending and upgrading of pyrolysis oil.
23
Q

State of technology for pyrolysis

A
  • Close to commercial for biomass
  • Waste biomass (negative fuel costs) – Compact power Bristol.
  • Problems of acidic and unstable bio-oil must be solved.
  • Options include combustion, transport fuels, extraction of chemicals.
  • Market required for char
  • Poor economics compared to fossil fuels.
24
Q

What do holoecullose degrade to in pyrolysis

A

holo - ugars,
levoglucosan, acids, furfural, lactones, hydroxyacetaldehyde

lignin - phenols, methoxyphenols and dimethoxyphenols

25
Q

compare pyrolysis oil to solid biomass.

A

Energy content is similar on mass, much higher on volume