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Inventory and Tertiary Treatment of Effluent from Textile Industries in Bangladesh The use of a new system combining an enhanced coagulation, flocculation and filtration M.A.H. Badsha Supervisor: Prof. J.B. van Lier Mentor(s): C.M. Hooijmans H.A. Garcia Hernandez Delft, April 14, 2015
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Presentation File of M.Sc. Thesis

Apr 20, 2023

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Page 1: Presentation File of M.Sc. Thesis

Inventory and Tertiary Treatment of Effluent

from Textile Industries in BangladeshThe use of a new system combining an enhanced

coagulation, flocculation and filtration

M.A.H. BadshaSupervisor:

Prof. J.B. van Lier

Mentor(s):

C.M. Hooijmans

H.A. Garcia Hernandez Delft, April 14, 2015

Page 2: Presentation File of M.Sc. Thesis

Introduction

Effluent from textile industries is a great concern in

Bangladesh, because

• High TDS

• Chemical dyes

Major impacts:

o Causing health consequences

o Damaging agricultural lands

o Killing aquatic lives

2

Source: http://oecotextiles.wordpress.com/2009/09/01/dyes-synthetic-and-natural/

Page 3: Presentation File of M.Sc. Thesis

Problem Statement

• Efficient technology to remove color is expensive

• Limited space for up-gradation

• Unplanned expansion of textile industry in rural areas

As a result, integration of a compact, low cost and

efficient technology to remove colour from textile

effluent is desired.

3

Page 4: Presentation File of M.Sc. Thesis

Existing ETP of Masco Industries Ltd

4

Inlet Collection Tank Aeration Tank

Secondary Clarifier EC Skid DAF unit

Page 5: Presentation File of M.Sc. Thesis

5

Compact Treatment System

Figure: Schematic of the polishing unit using AFM grains (Dryden Aqua, 2014)

APF- All Poly Floc (mixer of poly aluminum chloride and poly electrolytes)

ZPM- Zeta Potential Mixer (static mixer)

Page 6: Presentation File of M.Sc. Thesis

Research Questions

What technologies are available and in operation

to treat textile waste-waters in Bangladesh?

What is the colour removal performance of a

treatment system using AFM and APF with

effluent from an existing wastewater treatment

plant at a textile industry?

6

Page 7: Presentation File of M.Sc. Thesis

Research Objectives

The specific objectives of the proposed study are:

1. Make an overview of the available technologies

2. Study the adsorption capacity of colour by AFM

3. Study the effect of different flow rates on the

performance of the AFM filter media

4. Compare the performance of APF and a conventional

coagulant

5. Study the performance of the local sand against AFM

6. Run a pilot AFM system at Masco Industries Ltd

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Page 8: Presentation File of M.Sc. Thesis

Research Methodology

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Observe the removal rate of colour by adsorption,

coagulation-flocculation and filtration

Sample collection and characterization

Results and Discussion

Conclusions

Batch studies

Inventory Study

Column studies

Pilot study at Masco Ind. Ltd

Page 9: Presentation File of M.Sc. Thesis

Inventory Study

Poor treatment facility

9

(a) No overflow in the primary clarifier (b) Paddy field surrounded

by ETP (c) No overflow in secondary clarifier (d) No flow meter

Page 10: Presentation File of M.Sc. Thesis

Inventory Study

Sludge Management

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(a) Filter press out of operation (b) Limited space for SDB (c) Dry sludge on

SDB (d) Sludge ready to dispose

Page 11: Presentation File of M.Sc. Thesis

Batch Studies

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Wastewater Sample AFM grade-1

Adsorption Test Optimum Coagulant Dosage

Page 12: Presentation File of M.Sc. Thesis

Batch Adsorption Test Result

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0%

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0 10 20 30 40 50 60 70 80 90 100 110

24 hr 48 hr 72 hr Natural Degradation

Rem

ov

al

Eff

icie

ncy

(%

)

AFM Mass (gm)

Page 13: Presentation File of M.Sc. Thesis

Optimum Dosing of Coagulant “APF”

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0%

10%

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0.00 0.10 0.20 0.30 0.40 0.50 0.60 0.70 0.80 0.90 1.00 1.10 1.20 1.30

Rem

ov

al

Eff

icie

ncy

(%

)

APF Dosage (ml/L)

Page 14: Presentation File of M.Sc. Thesis

Column StudiesSchematic of the Column Set-up

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Page 15: Presentation File of M.Sc. Thesis

Column Set-up at the Lab

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Page 16: Presentation File of M.Sc. Thesis

Results of Column Studies(only feed water without coagulation-flocculation)

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Thousands

Removal Efficiency Colour Concentration

Filtrate Volume (ml)

Rem

ov

al

Eff

icie

ncy

(%

)

Co

nce

ntr

ati

on

(Pt.

Co

.)

Initial Color = 282 Pt.Co.

Initial Flow Rate = 315 ml/min

Page 17: Presentation File of M.Sc. Thesis

Effect of Different Flow Rates(fed with supernatant after coagulation-flocculation with APF)

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Removal % for F1 Removal % for F2 Removal % for F3

Color Concen. (F1) Color Concen. (F2) Color Concen. (F3)

Rem

ov

al

Eff

icie

ncy

(%

)

Time (min)

Co

nce

ntr

ati

on

(P

t.C

o.)

Initial Color = 482 Pt.Co., Supernatant = 184 Pt.Co.

F1 = 120ml/min, F2 = 220ml/min and F3 = 350ml/min

Page 18: Presentation File of M.Sc. Thesis

Performance of the Column(fed with supernatant after coagulation-flocculation with APF and Aluminium)

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0 5 10 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90

Removal % (APF) Removal % (Aluminium)

Color Concen.(APF) Color Concen.(Aluminium)

Rem

ov

al

Eff

icie

ncy

(%

)

Time (min)

Co

nce

ntr

ati

on

(P

t.C

o.)

Initial Color = 572 Pt.Co., Supernatant (using Aluminium)= 382 Pt.Co.,

Supernatant (using APF) = 207 Pt.Co. and Flow Rate = 315ml/min

Page 19: Presentation File of M.Sc. Thesis

Performance of Sand and AFM (fed with supernatant after coagulation-flocculation with APF)

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0 5 10 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90

Removal % (Sand) Removal % (AFM)

Color Concen.(Sand) Color Concen.(AFM)

Time (min)

Rem

ov

al

Eff

icie

ncy

(%

)

Co

nce

ntr

ati

on

(P

t.C

o.)

Initial Color = 479 Pt.Co., Supernatant = 119 Pt.Co. and Flow Rate = 315ml/min

Page 20: Presentation File of M.Sc. Thesis

Backwash Efficiency with Fresh Water(fed with supernatant after coagulation-flocculation with APF)

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Removal % (used AFM media) Removal % (fresh AFM media)

Color Concen.(used AFM) Color Concen.(fresh AFM)

Rem

ov

al

Eff

icie

ncy

(%

)

Time (min)

Co

nce

ntr

ati

on

(P

t.C

o.)

Initial Color = 257 Pt.Co., Supernatant = 64 Pt.Co. and Flow Rate = 315ml/min

Page 21: Presentation File of M.Sc. Thesis

Pilot Study at Masco Ind. Ltd

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Filter Tank APF Dosing Pump Storage Tank

Page 22: Presentation File of M.Sc. Thesis

Result of the Pilot Study

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Removal % Color Concentration

Time (min)

Rem

ov

al

Eff

icie

ncy

( %

)

Co

nce

ntr

ati

on

(P

t.C

o.)

Initial Color = 549 Pt.Co. and Flow Rate = 1m3/h

Discharge

Standard

(In-situ coagulation-flocculation and filtration)

Page 23: Presentation File of M.Sc. Thesis

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Removal % (sludge) Color Concentration

Time (sec)

Rem

ov

al

Eff

icie

ncy

(%

)

Co

nce

ntr

ati

on

(P

t.C

o.)

Backwash Efficiency

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Flow Rate = 12m3/h

Page 24: Presentation File of M.Sc. Thesis

Proposed Treatment Scheme

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AFM System

Page 25: Presentation File of M.Sc. Thesis

Conclusions

Regarding the overview on the existing treatment technology:

o Illegal discharge of wastewater

o poorly managed and often non-operational

o coloured effluent is being discharged without any tertiary treatment

o Sludge management is important and needs immediate attention

Regarding activated filter media (AFM) and APF dosing:

o The AFM media has no significant adsorption capacity (with and without

APF dosing)

o APF is a good coagulant compared to aluminium

o Performance of local sand is better than AFM filter media

o Coagulation and flocculation followed by a clarifier could be good enough

Regarding AFM system

o Not suitable as a tertiary treatment system to remove color at a textile

industry

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Page 26: Presentation File of M.Sc. Thesis

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