1 L/s Plant Testing – Fall 2016

Yang Pei, Erica Marroquin, Alicia Barrientos, Manuel Queijeiro

Abstract:

The 1 liter per second AguaClara water treatment plant was created in the summer of 2016 for small villages where it was not cost-effective to build full-sized plants. It was the culmination of 10 years of progress in AguaClara and featured new technology, including a crimped pipe flocculator and a free-standing sedimentation tank constructed from corrugated sewer pipe. The Fall 2016 team began the semester with performance checks; the team tested for leakages, dosing apparatus precision, floc blanket formation, and turbidity removal. After the team reached the conclusion of a good performance and shipped it satisfactorily to Honduras, where the work will be continued. The flocculator was re-designed to improve the existing one and test were performed to check that it gave the expected head loss. Finally, it was built.

Screen Shot 2021-05-03 at 10.14.57 PM.png

Floc Hopper Probe, Fall 2015

Miguel Castellanos, John Lopez

Abstract

The floc hopper probe team aims to create a fully functional floc hopper probe design for future visits to Honduras and elsewhere. Currently, very little information is know about the location or condition of the floc blanket in the floc hopper. This year’s research should lead to a better understanding of the events preceding sedimentation as well as more details on the location of the floc blanket inside the hopper. An experimental setup was created to test different floc hopper probe designs and observe which one gave accurate readings. This year’s team contributions include: a final design of the floc hopper probe and an assembling manual for the current probe design. The team has tackled the problem in the lab and now field testing is required for further improvement of design.

image22.PNG

Flocculator Efficiency, Fall 2015

Mallika Bariya, Tanvi Naidu, Chae Young (Flora) Eun

Abstract

The Fall 2015 Flocculator Efficiency subteam worked on designing, developing, and testing a flocculator model that optimizes the vertical­flow flocculator used in AguaClara water treatment plants. The team addressed the accumulation of low­shear regions of water above the top of the lower flocculator baffles, a phenomenon that creates a “dead” region in which collision potential for the creation of flocs is very low. Dead zone formation occurs due to a decrease in fluid velocity as water transitions from the bottom of the flocculator to the top and as it flows over the lower baffles. The team hypothesized that compressing the water flow would increase the fluid velocity and, as a result, allow the water to flow at a higher trajectory over the lower baffles and reduce the formation of dead spaces. Furthermore, the addition of an extra contraction and expansion would create more turbulence in the region above the lower baffle and increase collision potential. This issue was addressed by installing obstacles in the form of slit pipes at the tops of the lower baffles. Test results with these features showed that the obstacles were able to compress the flow and consequently increase the fluid velocity and turbulence in the ‘dead zone’ region. The team measured and observed the results of this design feature by testing the model through flow visualizations using a red dye tracer. Among the variables tested, the best desired effect was observed with a restriction of 78% of channel width, for both laminar flow and potentially turbulent flow (Re= 3000). With a 60% restriction, the formation of a circulating region was observed, although this eventually cleared up. There is a need for further research on how the geometry of the obstacle might be impacting this phenomenon.

image21.PNG

Floc Hopper Probe, Spring 2015

Steve Love and Garret Jancich

Abstract

The Fabrication Team’s purpose is to address current issues or areas of improvement in AguaClara plants. This semester, the team’s tasks included designing and fabricating a probe for monitoring sludge accumulation in the floc hopper. The floc hopper probe team created an operational tool for peering into the floc hopper in order to know when to drain it. The team also began work for developing the research capabilities of the probe. This would be achieved by taking image data via borescope snake camera and translating it into meaningful turbidity/DOM readings.

image20.PNG

Large Capacity Float Valve, Spring 2015

Kwabena Nimo

Abstract

The goal of this team is to develop a large capacity float valve to regulate flow from a storage tank to the entrance tank. This system will be put in place for smaller plants, so that they may still be operated at design flow rate during droughts. This subteam aims to create a plant that is easier to operate, troubleshoot, and build.

image19.PNG

Laminar Tube Flocculator - Summer 2014

Shreya Jain, Tanya Peifer, Nadia Shebaro, and Luke Zhu

Abstract:

Over the summer of 2014, the laminar tube flocculation team has worked to test AguaClara's new residual turbidity monitoring system, SWaT, as compared with prior teams that used FReTA. The group has also implemented PID control for the laminar tube flocculator to regulate the amount of clay added to the system. In order to achieve these goals, the laminar tubing system was simplified and reconfigured to eliminate the feedback loop with the turbidimeter. The team plans to continue optimizing the system and confirming the self regulating controls were working before starting experiments using varying dosages of coagulant.

2014 Spring Laminar Tube Flocculator.png

Laminar Tube Flocculator - Spring 2014

Victoria Chou and Yining Dai

Abstract:

Flocculators are an integral part of the water treatment process. The􏱕focculation process turns the colloidal matter within water into flocs that will eventually be removed through the sedimentation process. The creation and eventual settling of flocs formed in the flocculator results in cleaner, clearer water. According to Swetland et al.'s hypothesis, flocs that reach a certain size are no longer effective in removing colloids be- cause the shear on the surface of the flocs becomes too high for the colloids to attach. Thus, by breaking large flocs, they may regrow and scavenge additional small colloids that were not able to settle out from the suspension. The purpose of this series of experiments is to continue testing the Floc Breakup Theory and, if valid, to determine the most effective way to break up flocs in order to have the highest removal rate of colloidal particles. The settled water turbidity analyzer (SWaT), a new turbidity measurement system, was designed and implemented for the Spring 2014 research, in which the effluent water first travels through an angled tube settler with continuous 􏱕ow before being analyzed by the effluent turbidimeter. A base case test was run to serve as a control showing residual turbidity with the new turbidity measurement system. Adjustments to the new setup were made to accommodate for issues that arose from the new turbidity measurement system.

2014 Spring Laminar Tube Flocculator.png

Foam Filtration - Spring 2014

Kristin Chu, Skyler Erickson, Melissa Shinbein, Jeffrey Suen, Kadambari Suri

Abstract:

The Spring 2014 foam filtration team will focus on improving the water treatment system designed in Fall 2013 and incorporating the knowledge learned on the trip to Honduras in January, 2014. This includes: redesign- ing the cleaning techniques to improve efficiency in removing dirty water off of the top of the foam, investigating foam re-expansion in a drum with vertical sides, designing the LFOM, and implementing a coagulant doser. The goal for this semester is to design, build, and test a compact system that can be easily transported and eventually implemented in small communities. In order to achieve this long-term goal, the Foam Filtration team will need to investigate multiple design options and create an operational system in the AguaClara lab. The foam filter will then be tested in Honduras.

2014 Spring Foam Filtration.png

Foam Filtration - Summer 2014

Abby Brown, Ethan Keller, Skyler Erickson, Ji Young Kim

Abstract:

The Summer 2014 Foam Filtration team will continue to improve the water treatment system, aiming to send a complete filter design to Honduras in July 2014. The goal of the summer is to verify the safety of the foam filter itself and to improve the design of the filtration system for better performance, easy fabrication and transportation. The foam filter will be additionally tested in Honduras.

2014 Summer Foam Filtration.png

Sed Tank Temperature Gradients, Spring 2014

Dhaval Mehta, Hui Zhi, Surya Kumar

Abstract

AguaClara is an engineering program based at Cornell University that develops sustainable  water treatment technology with current applications in developing countries. In Honduras,  one  of  the  countries  with  AguaClara  technologies,  the  treatment  plant  at  San  Nicolas  experiences raw water with a temperature gradient of around 1°C/hr during warming and  cooling  portions  of a  day. These gradients  are  primarily  caused  due  to  the  approximately  15km of piping that brings raw water to the plant, much of which is exposed to the sun.  Agua  Clara  plants  use  sedimentation  tanks  with  floc  blankets  and  plate  settlers.  The  temperature gradient  during warming  periods  causes a  circulation  current  to  form in  the  vertical Gflow sedimentation  tank, due  to  the effect of continually warmer water displacing  colder water. This current in the tank at San Nicolas causes flocs to aggregate on one side of  the  tank and rise up  to  the  top with  the hotter, less dense water; hence  the effluent water  leaving the tank is not sufficiently clean. Our experiment is motivated by this problem, with  the  goal  of  studying  the  problem’s  origins  and  providing  initial  research  towards  its  solution

image34.PNG

Small Scale Plant Model, Fall 2014

Serena Takada and Nick Cassab-Gheta

Abstract

During the fall semester of 2014, the Small Scale Plant Model Team worked on repairing the current small scale plant model and began using AutoCAD to 3D print a small scale model of AguaClara plants. The purpose of using AutoCAD to print models of AguaClara plants, rather than using Rhinoceros 5, is to automate as much of the printing process as possible. The team evaluated multiple methods of converting a solid in AutoCAD to a meshed solid. In addition, the team looked into alternative printers that would be more compatible to printing using AutoCAD. Eventually, the team hopes to develop a system where anyone can request an STL file containing the design of the most up to date design of an AguaClara plant at any flow rate. Upon request, this STL file should be sent to any 3D print shop to be printed.

image33.PNG

StaRS Backwash, Fall 2014

Vicki Chou, Nick Farino, Chenhao Qi, Rui Zhang

Abstract

The goal of StaRS Backwash is to determine the sand grain sizes and distribution for the most efficient and effective backwash in the stacked rapid sand filters. The proper fluidization velocity for efficient backwash must first be determined. An expansion ratio of 1.3 is the current standard for the sand bed during fluidization. A sand size ratio below 1.5 is suggested for minimal segregation during backwash. The team ran experiments with sands sized by sieve combinations of 20­40 and 30­40 at different backwash velocities to test for segregation. Through the experiments, the team found that the 20­40 sized grains always segregated at all backwash velocities, but the 30­40 sand, which is under the 1.5 sand size ratio, did not segregate below backwash velocities of 15 mm/s. Current AguaClara plants use a backwash velocity of 11 mm/s, so using 30­40 sand would be a good option because it should not segregate according to the data collected.

image32.PNG

Pipeline Cooling, Spring 2014

Alexandra Cheng, Apoorv Gupta

Abstract

The AguaClara water treatment plant in San Nicolas was inaugurated on April 5, 2014, and has successfully started operation. However, a major problem that has become apparent is the heating of raw water during the day from the source to the plant entrance tank. Raw water travels 4.5 km through a steel pipeline exposed to sunlight which has been identified as the likely cause for the temperature increase. Since the plant is hydraulic and gravity-powered, the temperature of the influent water affects its properties and behavior in the various stages of the AguaClara treatment system, particularly in the sedimentation tank. While the stacked rapid sand liter has been able to keep effluent turbidities low enough to be deemed acceptable, the resulting required amount of backwash places excess stress on the system; therefore, it is imperative to seek a method to maintain a relatively low raw water influent temperature to ensure plant success in producing potable water.

image31.PNG

Floc Probe, Spring 2014

Alexandra Green, Tiago Viegas, Paul Vieselmeyer

Abstract

The visualization of the floc blanket in Aguaclara plants has been difficult and limited, so our team has tried to simulate it and create a new apparatus to solve or at least to reduce the problem. We found reports and materials from the turbidimeter team that could help in our task. Research was done on commercial sensors that could help monitor the floc blanket level, but none of the results were feasible. An experimental set up was also created in order to simulate the floc blanket and clear water interface with no success. Finally, a sludge judge apparatus was created to hopefully help with the observation of the floc blanket in San Nicolas.

image30.PNG

Convection Flow in Plate Settlers, Spring 2014

Eric Grohn

Abstract

The AguaClara project team develops a simple, low-cost water purification plant for developing global communities. One part of the AguaClara plant is a sedimentation tank. During this stage of the purification, large coagulated contaminant particles (”flocs”) collect and settle out of the water, leaving it cleaner than before. Recently, one problem has been noticed with the current design of the AguaClara sedimentation tank. If the water entering the tank is warmer than the water already within, the tank doesn’t perform as well as it should. The suspected reason for this is that the warm buoyant water rises rapidly to the top of the tank, taking the flocs with it, at a velocity that is too great for the tank to function correctly. The top of the tank consists of an array of angled closely packed parallel plates called plate settlers. My project here is to determine the flow pattern for a convective flow through the plate settlers, with the hope that this will provide a clearer picture of the poor sedimentation tank performance. A 2d analytical solution is determined for the flow velocity between two angled parallel plates when the flow is convective. Further topics are discussed as they relate the sedimentation tank performance, such as turbulence between opposing flows and shear flow instabilities.

image29.PNG

Arsenic, Fall 2013

Tanapong Jiarathanakul, Imtiaz Karim, Michelle Wagner

Abstract

The AguaClara Arsenic team for the Fall 2013 semester is the first to begin testing different methods of removing arsenic from drinking water. The initial goal was to develop a reliable method for testing water treatment alternatives and be able to detect small concentrations of arsenic. The work this semester follows the literature review performed in Spring 2013 which evaluated alternative arsenic testing methods and water treatment options for arsenic removal. A key issue is the need to measure low levels of arsenic (below ten parts per billion). Over the summer a graphite furnace atomic absorption spectrophotometer (GFAAS) was repaired for use in arsenic analysis. The lamp and power source of GFAAS have been replaced to improve the arsenic detection limit and the team is learning to operate the instrument. We will be using different coagulants to see which provides the best adsorption of arsenic to remove it from water, and dierent sample processing methods to simulate larger scale treatment processes. The team has a designated area for handling the solutions and samples as arsenic is toxic and we would like to minimize the contact it has with any person or object in the lab. The issue of arsenic waste is also a concern and this is why we are performing experiments using small sample volumes in order to reduce the amount of toxic waste produced.

image44.PNG

Calcium Carbonate Scaling, Spring 2013

David Buck and Andrea Castro

Abstract

The municipality of Las Vegas, Honduras is currently experiencing a decrease in the capacity of their water distribution network due to the accumulation of scale in pipes. Our hypothesis is that this is caused by the karst topography of the region. The water source for Las Vegas is a groundwater spring. Groundwater, initially at a low temperature, flows across sediments containing calcium carbonate, CaCO3(s) . The water heats up when it reaches the surface and as it flows through shallow pipes to the end of the distribution system. As the water warms and reaches equilibrium at a new temperature, calcium carbonate precipitates, coating the pipes in a hard scale. An AguaClara plant could solve this problem by dosing acid, which would drop the pH and prevent the formation of scale by keeping calcium in aqueous form. The purpose of the present analysis is to determine how much acid in the form of aluminum sulfate, Al2 (SO4) 3 , should be added and provide further analysis giving evidence for the present solution.

Coagulant Management, Spring 2013

Madeline Haas, Rudra Koul, Jack Newman

Abstract

Coagulants are an essential part of a water filtration plant as well as a signifiant operating cost. Therefore, it is very important that they be used as effiently as possible. This semester, the Coagulant Management team has calculated and analyzed the relationship between PACl density and concentration that was ultimately used in calculations necessary for centrifugal pump parameters and for hydrometer recommendations. In addition, the team brainstormed fabrication ideas for the coagulant injection point. The centrifugal pump was partially fabricated, but because of the density vs. concentration relationship calculated, the pump, once fully fabricated, can be tested using PACl. In addition, the Coagulant Management team has recommended the testing and use of a plastic (polycarbonate) hydrometer from Krackeler Scientific Inc. with a specific gravity range between 1.000 and 1.220.

image42.PNG