Transport of bacteria and colloids in intermittent sand filters Maria Auset, Arturo A. Keller, Francois Brissaud and Valentina Lazarova 229 th ACS San.

Slides:



Advertisements
Similar presentations
Pore Scale.
Advertisements

Chemistries and Physics of Water Purification
Water Management in a Petroleum Refinery
Biological waste water treatment
The Drain Field Function What goes into the drain field? How the drain field functions? What causes the drain field to fail?
An-Najah National University Civil Engineering Department
Advanced Pretreatment: Proprietary Configurations, Operational Issues and O&M.
Membrane Processes For Waste Water Treatment By: Rohit Chaurasia 3 rd B. Tech. Civil Engineering 71/08.
CE 370 Filtration.
Wastewater Treatment. Municipal WW Management Systems Sources of Wastewater Processing at the Source Wastewater Collection Transmission and Pumping Treatment.
WASTEWATER ENGINEERING
Transport of bacteria and colloids in intermittent sand filters Maria Auset 1, Arturo A. Keller 1, François Brissaud 2, Valentina Lazarova 3 1 Bren School.
Lecture 6: Water & Wastewater Treatment
Chapter 3: Bioreactor Design
Experimental investigation of the role of interfacial area in two-phase flow models using glass etched micro-models N.K. Karadimitriou, S.M. Hassanizadeh.
Dr. Martin T. Auer MTU Department of Civil & Environmental Engineering Water Treatment.
Dr. Martin T. Auer MTU Department of Civil & Environmental Engineering Water Treatment.
1 Colloid acceleration and dispersion in saturated micromodels Donald Bren School of Environmental Science & Management University of California, Santa.
Biology: November 5th, 2008 Objectives: Things to do: Due Dates:
Sterilization of air: Methods Most industrial fermentations are operated under vigorous aeration and the air supplied to the fermenter must be sterilized.
Wastewater Treatment. Collection Sewers Collect wastewater and bring it to the wastewater treatment plant – Combined sewer overflows: Take untreated sewage.
Vadose-zone Monitoring System
OZONE DRINKING WATER SYSTEM. CONTENTS Properties of Ozone Production of Ozone Water Treatment Plant – 25 m 3 /hr Ozone Generation System.
Dynamic Soil Properties and Dynamic Land Uses: The Need for Dynamic Soil Interpretations Randall J. Miles University of Missouri National Cooperative Soil.
Secondary Treatment Processes
© 2011 Pearson Education, Inc. AP Environmental Science Mr. Grant Lesson 74 Wastewater and Its Treatment.
Sewage Treatment.
Environmental Engineering Lecture 6. Sources of Drinking Water  Rivers: upland and lowland  Lakes and reservoirs  Groundwater aquifers  Sea water.
DIVISION OF APPLIED TECHNOLOGIES NCSR “DEMOKRITOS” Innovative hybrid desalination unit for potable water production with simultaneous removal of harmful.
Unit 01 : Advanced Hydrogeology Review of Groundwater Flow Malcolm Reeves Civil and Geological Engineering.
Water Purification Chemistry.
Colloid Transport Project Project Advisors: Timothy R. Ginn, Professor, Department of Civil and Environmental Engineering, University of California Davis,
Module 1, Part 3: Process validation Slide 1 of 22 © WHO – EDM – 12/2001 Validation Part 3: Process validation Supplementary Training Modules on Good Manufacturing.
In The Name of Allah Microbial Enhanced Oil Recovery By: M.S. Karambeigi Supervisor: Dr. M. Ranjbar Dr. M. Schaffie June 2007 Shahid Bahonar University.
Waste Water Treatment Plant. HOW DO TREATMENT PLANTS PROTECT OUR WATER? Wastewater treatment plants: Remove solids, everything from rags and plastics.
Sanitary Engineering Lecture 14
Rural, Community & Onsite Wastewater & Waste Management Role of Soil in Biological Treatment.
Lecture 6: Water & Wastewater Treatment Objectives: Objectives: Define primary, secondary, and tertiary treatment Define primary, secondary, and tertiary.
Unit 8: Waste Management Section 2: Wastewater Treatment.
Sewage Treatment.
Variably Saturated Flow and Transport: Sorbing Solute.
1 Graduate School of Science and Engineering, Saitama University, JAPAN 2 Department of Biotechnology, Chemistry and Environmental.
Colloidal Transport: Modeling the “Irreversible” attachment of colloids to porous media Summer School in Geophysical Porous Media, Purdue University July.
Presented by Tanzina Rahman July 25, 2013 SiViRT Student Meeting Department of Civil and Environmental Engineering University of Texas at San Antonio Modeling.
Last Question of the Day- For first semester! 1. How do you get the waste out of wastewater o For Friday, please gather all Questions of the day to turn.
FLOTATION. INTRODUCTION Flotation is an operation that removes not only oil and grease but also suspended solids from wastewaters. Flotation is an operation.
Environmental Science Lab “Groundwater Pollution” Recall from last day: – POROSITY refers to the amount of space between particles of soil – Fluid stored.
1.Submit your Creek Survey if you haven’t already done so. 2.Which part of the water cycle is MOST responsible for polluting surface water? 3.Municipalities.
© 2011 Pearson Education, Inc. AP Environmental Science Mr. Grant Lesson 74 Wastewater and Its Treatment.
Objective In this lesson we will answer the following questions: How does filtration fit into the water treatment process? How does filtration clean water?
Chapter 6 Reverse Osmosis and Nanofiltration
Membrane Processes Introduction Membrane processes represent an important subset of filtration processes as there are very few pollutants found in water.
CHAPTER 2 MASS BALANCE and APPLICATION
WATER MANAGEMENT.
Filtration Processes Introduction
How Reverse Osmosis Water Purification Systems Work.
WASTE WATER TREATMENT.
Water Treatment. Water Sources and Water Treatment Drinking water should be essentially free of disease-causing microbes, but often this is not the case.
Sources of solid waste. Waste water. gas emissions
CHAP. 2.2 – WATER TO DRINK.
FORTH/ICE-HT & U. PATRAS
Introduction to Filtration
Wastewater Treatment Dr.Gulve R.M..
Warm Up p65 Which part of the water cycle is MOST responsible for polluting surface water? Municipalities (towns) get drinking water from which two sources?
FLOTATION.
Three choices: Surface water Groundwater
A low-pressure dosing system requires a pump tank and a network of small-diameter pipes (1 to 2 inches) placed in trenches. The pump tank stores the effluent,
Enhancing Rapid Sand Filtration by Backwashing with Alum
Wastewater Treatment: Characteristics and Systems
Kendra I. Brown, Dorthe Wildenschild, and Mark L. Porter H41F-0935
Presentation transcript:

Transport of bacteria and colloids in intermittent sand filters Maria Auset, Arturo A. Keller, Francois Brissaud and Valentina Lazarova 229 th ACS San Diego National Meeting Bren School of Environmental Science and Management, University of California, Santa Barbara University of Montpellier II, France

SaturatedZone VadoseZone Sewer line or Septic tank Contaminated Water Supply ? Contaminants -Viruses - Bacteria Water Air Sand grain Cycles of household water use → Transient unsaturated flow

Solid Water SuspendedAir Attached Attached Inactivated Inactivated Inactivated Suspended Attached V Fate and Transport of Colloids

Objective Investigate the effects of cyclic infiltration and draining events (transient unsaturated flow) on microorganism transport, in order to help predict removal of pathogenic bacteria in sand filters and natural porous media.

Pore scale PDMS hydrophilic micromodels of realistic pattern of pore network. Pore diameters from 20 to 100 μm. Pore depth = 12 μm. Column scale 1.5 m sand (d 60 /d 10 =2.72) sequentially dosed with secondary effluent percolating in a single pass through the unsaturated porous medium. Experimental setup 200 μm 1.5 m

Unsteady flow: Sequential applications of wastewater Cycles: Micromodel:2 min injection/8 hr drainage Column:5 min infiltration/4 hr drainage One unique application of tracers: - Soluble salt, NaI. - Escherichia coli, - 5 μm latex particles, followed by tracer-free applications. Monitoring output tracer concentrations for 4 days. 0 Time Input Flow Flushes Experimental conditions 0 Time Input Flow Tracer-free flushes Traced flush

Experimental Setup

Water Content: 41% Direction of flow Air Water Solid

First Flush 12 sec after flush

Water Content: 76% 26 sec after flush

Water Content: 78% 38 sec after flush

Water Content:78% 51 sec after flush

Water Content: 79% 1 min 04 sec after flush

Water Content: 80% 1min 12 sec after flush

Water Content: 82% 1min 28 sec after flush

Water Content: 83% 1min 39 sec after flush

Water Content: 83% 1min 55 sec after flush

Water Content: 84% 10 min 09 sec after flush

Water Content: 68% 2 h 59 min after flush

Water Content: 58% 3 h 49 min after flush

Water Content: 55% 4 h 08 min after flush

Water Content: 47% 4 h 51 min after flush

Water Content: 43% 5 h 04 min after flush

Second Flush 11 sec after flush

13 sec after second flush

Water Content: 77% 23 sec after flush

Water Content: 79% 1 min after flush

Water Content: 80% 1 min 18 sec after flush

Water Content: 82% 1 min 35 sec after flush

Water Content: 83% 2 min after flush

Water Content: 85% 2 min 28 sec after flush

Water Content: 87% 5 min 49 sec after flush

Key Findings Sorption onto AWI and SWI is “irreversible”. Colloids trapped in thin water films. Colloids sorbed onto AWI can be transported –Along with the moving air bubble –As colloidal clusters –As water is remobilized

Unsaturated column setup Bacteria suspension Wastewater solution Flowmeter Epi-fluorescent microscopy Pressure transducer Pump Data Acquisition System 0 Time Input Flow Tracer-free flushes Traced flush

Results

Column results

Key findings Transport of bacteria and tracer is influenced by variations in water velocity and moisture content. Advancement of the wetting front remobilizes bacteria either attached to the AWI or entrapped in stagnant pore water between gas bubbles leading to successive concentration peaks of bacteria in the effluent. Microbial retention rate was high, %. Retention is due to reversible bacteria entrapment in stagnant regions and sorption onto the AWI and irreversible attachment onto SWI.