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Filters and Dust Control IAOM Joint District Meeting Spring Technical Conference March 7, 2014 Darin Teetes

Filters and Dust Control

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Page 1: Filters and Dust Control

Filters and Dust Control

IAOM Joint District Meeting Spring Technical Conference March 7, 2014 Darin Teetes

Page 2: Filters and Dust Control

What is “Dust”? • Dust is a fine, dry powder consisting of tiny particles that are released or

transported into the air through processing or handling of materials.

Page 3: Filters and Dust Control

Why is “Dust” a Problem? • Product degradation or loss • Health issue for workers • Safety issue for assets and facilities • Sanitation and infestation control • Maintenance

Page 4: Filters and Dust Control

Where is “Dust” a Problem?

• Anywhere in a facility – product transfer, dump pits, load-out, tunnels, head house, even in the offices.

Page 5: Filters and Dust Control
Page 6: Filters and Dust Control

Dry-Type Collectors • Cyclone Collector • Baghouse Filter

Page 7: Filters and Dust Control

Baghouse Filter • Utilizes fabric socks/media • Very efficient, up to 99.99% on particles in

airstream that are submicron size depending on media used

• Filter bags and “dust” cake on surface of media act to separate particles from incoming dirty airstream.

• Reverse air cleaning system knocks dust into the filter hopper to be discharged.

Page 8: Filters and Dust Control

Baghouse Filters

Round Square Modular “Big Round”

Page 9: Filters and Dust Control

Bag Cleaning Systems:

• High Pressure Low Volume: – 80 to 100 psig air at low volume – Cleaning air supplied by “house” compressed air

system – Oil and moisture contamination from “house”

compressed air system are common. – Uses venturi system to induce air and whip

material from the bags

Reverse-pulse (pulse-wave or pulse-jet)

Page 10: Filters and Dust Control

Bag Cleaning Systems: Reverse-pulse (pulse-wave or pulse-jet)

• Medium Pressure – 10-15 psig at moderate to high air volume – Use of positive displacement blower to supply air. – Air supply is local to inlet of PD blower; oil and moisture contamination

not typically a problem.

Page 11: Filters and Dust Control

Bag Cleaning Systems: Reverse-pulse (pulse-wave or pulse-jet)

• Low Pressure – 20-100” w.c. – Use of fan to deliver high volume of

air at low pressure. – Physically forces dust off the bags.

Page 12: Filters and Dust Control

Baghouse Filters Air Inlet Configuration

• Properly designed and applied air inlet serves many functions: – Allow airstream with particles to enter baghouse

without damage to bags. – Allow adequate area for stock to enter baghouse

without choking. – Allows for particles to drop from airstream to filter

discharge.

Page 13: Filters and Dust Control

Baghouse Filter Type of Air Inlet

• High Air Inlet(s) – for medium and light dust

loading. – Include deflectors to reduce bag

wear from incoming particles in airstream to filter.

– Used in general dust collection or handling air from air outlets of cyclone collectors.

Page 14: Filters and Dust Control

Baghouse Filter Type of Air Inlet

• Cyclonic/Material handling inlet(s) – Ideal for Heavy-Loading or material conveying. – Inlet has tangential entry into section below filter bag section. – Typical to a heavy loaded negative lift; ie. Hammermill lift or positive pressure conveying system

Page 15: Filters and Dust Control

Baghouse Filter Type of Air Inlet

• Low air inlet(s) – Airstream(s) introduced into filter below bags – Not recommended due to potential for air turbulence in filter upon dirty air entry. – Baffle to deflect airstream downward may aid

in reducing this potential.

Page 16: Filters and Dust Control

Filter Bag Media • Selection of proper media plays a major role in filter

performance. • Must consider several factors of application:

– Operating temperatures – Humidity and moisture levels – Type of particulate being handled – Resistance to abrasion, chemicals, moisture, etc. – Filter Air to Cloth Ratio (bag length)

Page 17: Filters and Dust Control

Filter Bag Media • Media for challenging applications such as where warm and moist air from

pneumatic conveying systems is handled: – Polyester bags can be glazed or coated with finishes known as Eggshell

or Defender coats – Polypropylene can be used in hi-moisture/temperature application – Consider media utilizing “surface filtration”

Page 18: Filters and Dust Control

Baghouse Filter Performance

• Measure Pressure Differential across Baghouse filter bags/media. – The difference in static pressure

upstream (dirty air side) and downstream (clean air side) of the bags = pressure drop.

• U-tube manometer or Magnehelic gauge mounted to filter, visible to operator.

Page 19: Filters and Dust Control

Air to Cloth Ratio

• Establishes design capacity of a baghouse • Term refers to ratio of air quantity (cubic feet per minute or cfm)

to the amount of media surface area within filter (square ft.)

• Air Volume (CFM) ÷ Cloth Area (SQ.FT.) = Air to Cloth Ratio • Example: 15,000 cfm ÷ 1,555 sqft = 9.65:1 Air to Cloth Ratio

Page 20: Filters and Dust Control

Air to Cloth Ratio Rule of Thumb for design A/C Ratio

• 9-10:1 Ratio: Secondary Collector, Elevator, Cleaning House, General Suction

• 7:1 Ratio: Primary Collector, High

Humidity Air Systems,

• 5:1 Ratio: Filter / Receiver

Page 21: Filters and Dust Control

Can-Velocity of a baghouse

• Can Velocity is measured in feet per minute (fpm).

• Determined by dividing the total air flow entering the baghouse chamber by the cross sectional area of the filter housing (less bag area)

Example: 15,000 cfm ÷ (77.2 sq ft - 20.63 sq ft) = 265 fpm

Page 22: Filters and Dust Control

Can-Velocity of a baghouse

• “Rule of Thumb” for Can-velocity • Varies with application, but can generally assume a can-velocity at 300 fpm

or below to be acceptable.

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How to Size Ducting

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Minimum Duct Design Velocities Nature of Contaminant

Examples Minimum Design Velocity, fpm

Vapors, gases, smoke

All vapors, gases, smoke 1000 - 2000

Fumes Welding 2000 - 2500

Very fine light dust

Fine rubber dust, cotton dust, molding powder dust, jute lint, cotton dust, shavings (light), soap dust, leather shavings, agricultural dust

3000 - 4000

Page 25: Filters and Dust Control

How to Size to Size Ducting

• Add the CFM of both incoming lines and select the size with appropriate velocity

• Add area of both incoming lines and select the size closest Warning: Common mistake is to add diameters of the incoming lines. However, if the velocity is the identical and acceptable. You can use the following equation. D1^2+ D2^2 = SQRT(D3) As a rule of thumb.

Page 26: Filters and Dust Control

• Dust is in suspension because of correct velocities.

Good Velocity, Good Volume, Good Design

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• Dust is dropping out (in locations); • System is balanced (at end of system).

Bad Velocity, Good Volume, Bad Design

Page 28: Filters and Dust Control

• Dust is NOT in suspension because the system is not balanced. • Air taking path of least resistance.

Additions without Rebalancing

Page 29: Filters and Dust Control

• Dust is in suspension (but at higher velocity); System is not balanced.

Deductions without Rebalancing

Page 30: Filters and Dust Control

Thank you for your time Presented by: Darin Teetes