TRANSPORTATION OF DRY FLYASH: ISSUES FOR CONSIDERATION

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TRANSPORTATION OF DRY FLYASH: ISSUES FOR CONSIDERATION By V.K.Agarwal Indian Institute of Technology, Delhi

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TRANSPORTATION OF DRY FLYASH: ISSUES FOR CONSIDERATION. By V.K.Agarwal Indian Institute of Technology, Delhi. Figure 9 Sketch of Particulate Flow in Dilute Phase Conveying. Mode of Conveying. Dilute Phase - Suspension Flow: Requirements No ne - PowerPoint PPT Presentation

Transcript of TRANSPORTATION OF DRY FLYASH: ISSUES FOR CONSIDERATION

Page 1: TRANSPORTATION OF DRY FLYASH: ISSUES FOR CONSIDERATION

TRANSPORTATION OF DRY FLYASH: ISSUES FOR

CONSIDERATION

By

V.K.Agarwal

 Indian Institute of Technology, Delhi

 

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Figure 9 Sketch of Particulate Flow in Dilute Phase Conveying

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Mode of Conveying

Dilute Phase - Suspension Flow:

Requirements None

Pick-Up Velocity 12 m/s fine powders (minimum)

16 m/s fine granules

for horizontal conveying

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Figure 11 Sketch of Particulate Flow in Moving Bed Flow

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Mode of ConveyingDilute Phase - Suspension Flow

Requirements NonePick-Up Velocity 12 m/s fine powders (minimum) 16 m/s fine granules

Dense Phase - Non-Suspension FlowSliding Bed Flow:

Requirements Good Air Retention

Pick-Up Velocity 3 m/s (minimum)

 

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Figure 14 Sketch of Particulate Flow in Plug Type Flow

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Mode of ConveyingDilute Phase - Suspension Flow

Requirements NonePick-Up Velocity 12 m/s fine powders (minimum) 16 m/s fine granules

Dense Phase - Non-Suspension FlowSliding Bed Flow:

Requirements Good Air Retention

Pick-Up Velocity 3 m/s (minimum)

  Plug Flow: 

Requirements Good PermeabilityPick-Up Velocity 3 m/s

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Solids Loading Ratio

a

p

m

m

63

where ϕ = solids loading ratio

= mass flow rate of material - tonne/h

and = mass flow rate of air used - kg/s

pm

am

(dimensionless) - - (3)

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Diagram to Illustrate the Wide Range of Conveying Systems Available for Conventional Systems Operating With a Single Air Source

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Sketch of Typical Negative Pressure Conveying System

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Ash Accumulation Points and Typical Ash Distribution of a Dry Bottom Furnace

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Typical Arrangement of Electrostatic Precipitator Ash Collection Hoppers

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Pneumatic Ash Removal Systems with Conveying Parameters Indicated

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Typical Dry Fly Ash Handling Arrangement at a Power Station

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CONVEYING CAPABILITY

In Terms of• Material Flow Rate• Conveying Distance• Minimum Conveying Air Velocity• Power Requirements

Depends Upon:• Pipeline Bore

• Pipeline Length

• Pressure Drop Available

• Material Properties

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Parameters Relating Compressor Rating with Material Flow Rate

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Influence of Solids Loading Ratio on Conveying Air Velocity for Fine and

Coarse Grades of Flyash

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Sketch of Test Facility Pipeline at the IIT

Pipeline Details:

Bore - 63 mm Length - 133 m

Bends - 10

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Conveying Characteristics for Fine Grade of Fly Ash with Conveying Line Inlet Air Velocity Data

Superimposed

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Conveying Characteristics for Coarse Grade of Fly Ash with Conveying Line Inlet Air Velocity Data

Superimposed

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Air Mass Flow Rate - kg/s

Fly

Ash

Flo

w R

a te

- t o

nne/

h

24

20

16

12

8

4

0

Conveying line pressure

drop - bar

Solids loading ratio

Conveying limit

0 0·04 0·08 0·12 0·16

Conveying line inlet air

velocity - m/s

152·0

14161820

0·40·8

1·2

1·6 10

5

NO

GO

AREA

Air Mass Flow Rate - kg/s

24

20

16

12

8

4

0

Conveying line pressure drop

- bar

Solids loading ratio

Conveying limit

0 0·04 0·08 0·12

Conveying line inlet air velocity - m/s

NO

GO

AREA

20

10

30

40

506080

160 120 4 6 8 10

12

1∙4

0·40·8

1·2

1·6

2·0

100

Fly

Ash

Flo

w R

a te

- t o

nne/

h

a) Coarse fly ash b) Fine fly ash

Figure 5 Comparison of Conveying Characteristics for Fine and Coarse Grades of Fly Ash in IIT Pipeline

1·8

14

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Conveying Parameters for Design Cases Considered in Relation to 63 mm Bore Line

 

 

 

Reference Point

Pressure Drop(bar)

Air Flow Rate (kg/s)

Inlet Air

Velocity (m/s)

Solids Loading Ratio

Fly Ash Flow Rate (tonne/h)

Test Loop

Plant Test Loop

Plant

1 1.8 0.038 3.7 150 103 20.5 14.1

2 1.3 0.060 7.2 55 40 11.8 8.64

3 1.0 0.090 12.3 20 16 6.6 5.22

4 0.8 0.087 13.2 14 11 4.5 3.59

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Fly Ashy Flow Rate in Plant Pipeline of Various Bores for Range of Conveying Line

Pressure Drops Considered

Pipeline Bore(mm)

Fly Ash Flow Rate – (tonne/h)

Conveying Line Pressure Drop – (bar)

1.8 1.3 1.0 0.8

150 80 51 33 23

200 144 91 60 41

250 226 144 95 65

300 325 209 138 94

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Sketch of a Typical Vacuum Conveying System Incorporating a Stepped Pipeline for

Conveying Different Grades of Fly Ash

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Conveying air Velocity Profiles for the Conveying of both Coarse and Fine Ash in a

Common Negative Pressure Conveying System

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RECOMMENDED OPTIONS FOR COAL ASH HANDLING AND SAFE DISPOSAL