HELICAL FLOW PATTERN IN AERATED GRIT …...2018/03/03  · h : head,ft Q : flow,cfs e,m : empirical...

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HELICAL FLOW PATTERN IN AERATED GRIT CHAMBERS 1

Transcript of HELICAL FLOW PATTERN IN AERATED GRIT …...2018/03/03  · h : head,ft Q : flow,cfs e,m : empirical...

Page 1: HELICAL FLOW PATTERN IN AERATED GRIT …...2018/03/03  · h : head,ft Q : flow,cfs e,m : empirical constants dependent on the throat width FREE FLOW & SUBMERGED FLUMES 14 The upstream

HELICAL FLOW PATTERN IN AERATED

GRIT CHAMBERS

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AERATED GRIT CHAMBERS WITH AIR LIFT PUMPS

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AERATED GRIT CHAMBERS WITH GRIT PUMPS

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AERATED GRIT CHAMBER WITH HOPPER

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TYPICAL DESIGN PARAMETERS FOR AERATED GRIT CHAMBERS

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EXAMPLE GRIT CHAMBER DESIGN

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Grit

Chambers

Design

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ROTATING BLADES GRIT REMOVAL

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ROTATING BLADES GRIT REMOVAL WITH OIL

REMOVAL

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SIZING FOR ROTATING BLADES GRIT TANKS

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FLUMES

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• Known geometry gives a predictable head discharge relationship, measured upstream of the flume, usually via ultrasonics.

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FLUME PARTS

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• A flume has three basic parts

– Entry transition - this is where the channel

width is reduced

to the flume throat width via curved sections.

The throat should be central to the channel.

– Throat- this is where the flow passes through

the critical depth. The throat length must be at

least twice the depth upstream. The throat is

usually around half the channel width.

– Exit transitions - this is where the flume throat

is widened out to the downstream channel

width. This is done using straight tapers.

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DIMENSIONS & FLOW RANGES

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PARSHAL FLUME HEAD EQUATION

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e

m

Qh

1

Where:

h : head,ft

Q : flow,cfs

e,m : empirical constants dependent

on the throat width

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FREE FLOW & SUBMERGED FLUMES

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The upstream head must be at least 1.25 times the downstream head. If it is not then the flume is drowned out. This means that the head discharge relationship will no longer be true. The flume will be over recording, I.e. it will indicate that a greater flow has passed than has actually passed.

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PRIMARY SEDIMENTATION TANKS(PST)

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Functions of the primary clarifiers include:

• Remove floating material, thereby minimizing

operational issues such as the buildup of scum in the

secondary treatment process.

• Concentrate primary sludge before pumping to gravity

thickeners, and

• Reduce suspended solids and biochemical oxygen

demand (BOD) loading to the downstream treatment

processes

A tank in which suspended solids are allowed to settle out of

a liquid under the influence of gravity.

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PST COMPONENTS

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FLOW PATTERN & ZONES IN PSTs

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EFFLUENT LAUNDER

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Trough which collects the wastewater flowing out of the

sedimentation tank and directs it to the effluent pipe. One or

both sides of a launder typically have weirs attached. Weirs are

walls preventing wastewater from flowing uncontrolled into the

launder

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TYPICAL DESIGN PARAMETERS FOR

PRIMARY SEDIMENTATION TANKS

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Average %TSS removal = 60%

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SURFACE LOADING RATE

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AreaSurfaceTank

RateFlowSLR

__

_

SLR

RateFlowAreaSurfaceTank

___

The surface loading rate is the quantity of wastewater passing over

1 m2 of tank per day

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WEIR OVERFLOW RATE

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LengthWeirTank

RateFlowWOR

__

_

RateFlow

VolumeEffectiveTimeDetention

_

__

The weir overflow rate is the amount of wastewater leaving the settling

tank per linear meter of weir

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HYDRAULIC DETENTION TIME

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RateFlow

VolumeEffectiveTimeDetention

_

__

Sufficient time for contact between solid particles is

necessary for flocculation and sedimentation.

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DESIGN EXAMPLE FOR PST

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PST

Sizing

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PERCENTAGE POLLUTANTS REMOVAL IN PST

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PST

Removal

Rates

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This Project is funded by the European Union

SWIM and Horizon 2020 Support Mechanism Working for a Sustainable Mediterranean, Caring for our Future

Thank you for your attention.