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Low Cost Design of  Arsenic Removal from Groundwater in Bangladesh Kevin Banahan  |  Jeremy Kozub  |  Jesse Amsel Wentworth Institute of Technology Environmental Engineering Capstone Spring 2005
Overview of Arsenic problem ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Arsenic Pollution Mechanisms ,[object Object],[object Object],[object Object],(8FeOOH + CH 3 COO- + 15H 2 CO 3 ->  8Fe 2+  +17HCO 3 - + 12H 2 O)
Theory of Arsenic Removal
Chemistry of arsenic removal from groundwater by sorption ,[object Object],[object Object],[object Object],[object Object]
Our Design Considerations ,[object Object],[object Object],[object Object],[object Object],[object Object]
Client Statement ,[object Object],Final Design ,[object Object],[object Object],[object Object],Design Communication 5 Stage Model To develop a low-cost treatment system for the removal of Arsenic from groundwater in Bangladesh ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Conceptual Design
Sorbent Kinetics
Breakthrough Curve
Detailed Design
Effect of Particle Size on Sorption Arsenic Mass Partitioning Parts per Billion of Ingestible Arsenic (Initial Concentration = 400 ppb) Aqueous Suspended Solids Settled Solids 70 185 Rinsed Sorbent 40 400 Sorbent w/ fines settled mixed  
Column Experiments ,[object Object],[object Object]
Sorption Material Balance to Determine Sorptive Capacity mg/g 0.009 mass/mass sorptive capacity g 38 Mass Sorbent mg 0.344 Mass Sorbed L 2 Volume Treated mg/L 0.128 Final Conc mg/L 0.3 Initial Conc
Column Breakthrough Sorption Curve for Raw Sorbent
Bangladeshi Technology Transfer
Recommendations for further work ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Acknowledgments ,[object Object],[object Object],[object Object]
Thank you

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Low Cost Design of Arsenic Removal from Groundwater in Bangladesh

Notas do Editor

  1. -Before gaining independence the people of Bangladesh used surface water for all of their needs. -Water was contaminated with microbes that caused everything from diarrhea and Colera - Department of Public Health (DPH) and United Children’s Fund (UNICEF) -in the 80’s the goal of providing 80 % population well water was surpassed - 8-12 million wells were drilled to provide microbial safe drinking water -90% of the Bangladesh population of 130 million prefer to drink well water -Mid 1990’s was when the Arsenic Problem first hit the Radar Painted wells Safe and unsafe wells -The max allowable concentrations of 50 ug/L was lowered to 10 ug/L in 1993 - In New Jersey the allowable concentration will be lowered to 5 ug/L in 2006
  2. -There are Different opinions -1.) Arsenic is released by oxidation of pyrite in the sediments as the aquifer drawdown permits atmospheric oxygen to invade the aquifer ( Pyrite is a sink for not a source for Arsenic ) When the wells are pumped the oxygen from the air oxidized the pyrite and the arsenic is released… -2.) Arsenic sorbed to aquifer minerals are displaced into solution by exchange of phosphates from over application of fertilizer to surface soils -3.) anoxic conditions permit reduction of iron oxyhydroxides (FeOOH) and release sorbed arsenic to solution FeOOH - Ferric Oxide CH 3 COO - Acetate H 2 CO 3 – Carbonic acid HCO 3 – Bicarbonate H 2 O - Water
  3. Groundwater composition 1 L synthetic groundwater = 0.132 mL As(III) +0.188 g CaCl 2 + 0.255 g MgCl 2 + 0.012 g KCl Model of groundwater samples taken from wells in Bangladesh Very important to have chlorine ion’s present because it coverts arsenite to arsenate in the presence of atmospheric oxygen Arsenite (AsIII) = H 3 AsO 3 Arsenate (AsV) = H 3 AsO 4 Arsenic as As(V) is easier to remove Arsenate reacts with iron oxide (in crushed sorbent material) and sorbs to the surface of the crushed sorbent material leaving only clean water to filter through
  4. JESSE Low cost Simple to make Easy to use Constructed of local materials Takes advantage of native labor
  5. Client Statement – to develop a low-cost treatment system for the removal of Arsenic from groundwater in Bangladesh Problem Definition – Clarify Objectives - <50 ppb Establish User Requirements – family scale, easy to use Identify Constraints – transport of the water Establish Functions – adsorption system Conceptual Design – Establish Design Specifications – isotherms, retention time Generate Alternatives – tea bag, loose sorbent, column Preliminary Design – Model or analyze design Validation of analytical method - HACH kit Refining synthetic groundwater creation Saturation experiments – write up’s Regeneration experiments – write up’s Detailed Design – Choose a design to experiment with Refine and optimize design Construct scaled design Test and evaluate design Design Communication – Documentation – analytical method, groundwater creation, lab activities, experiments Final Design – Final report Interpretation of data Specifications for suggested design
  6. 10 g of sorbent with 75 ml increments of 132 ppb arsenic groundwater
  7. Sorbent Material has 2 dominant sizes. 50 sieve size particles Retained Fines Fines have much higher surface area to mass ratio which may greatly influence the sorptive capacity.
  8. The use of Plastic hosing, stands, beakers, metal screen was for lavatory accuracy.. The column may be modified using these materials Safi Cloth- used from a filter, it can be folded so the fabric fibers cross and create a very fine screen Clay pots could be used (maybe a Spick-it) to feed the water into the top and catch the water at the bottom of the column.
  9. EVERYONE