Flow Controller

Linearization and Calibration

Abstract

Experiments run in fall 2007 have indicated that the float valve can hold back head of at least 8m with less than 0.5cm 5 cm of change occurring in the flow controller water level in the first 2m 2 m of pressure. In field tests in Honduras the flow controllers have not been dosing as expected, which current lab work is aiming to correct. Data gathered in the laboratory on outflow rate has followed a linear model in the laminar flow range, but attempts to model the turbulent transition range have produced varying results. It is considered a high priority to develop a reliable model for dosing at higher flow rates, which will be used in the near future at the larger plant in Marcala, currently under constructionplants.

Keywords: Flow Controller, laminar flow, height of outflow, influent pressure, float valve

Introduction and Objectives

Constructing reliable and cost-effective solutions for water treatment in Honduras is challenging due to the lack of infrastructure. Electricity is unreliable, which has rendered modern computer-automated water treatment plants unusable, moreover the mountainous terrain sometimes makes access to materials needed for construction or repairs difficult. While it does isolate villages and their utilities, the rough topography has created an opportunity for the use of gravity-powered treatment plants. There has been success with the implementation of AguaClara researched and designed flocculators that are mixed by gravitationally-derived kinetic energy, but chemical dosing in these plants without the use of electric pumps is still inconsistent.

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Plastic bottle flow controllers have been used in Honduras for alum and chlorine dosing for several months now, and a few problems have arisen. They have been clogging and the head loss to alum dosing relationship does not appear linear. Further testing this during the fall of 2007 has been done with more precise equipment and an extra connector was removed from the flow controller to make it resemble the set up used in Honduras. The outflow to head loss relationship once again appears relatively linear in the laminar range, and it is possible that a different type of experiment should be designed to address the non-linear data from Honduras.

Other aspects of flow controller performance have also been tested this fall, including maximum inlet head allowable, water level variation in the flow controller, and corrosion resistance of the manufactured float valves. There have also been updates made to the materials used in the flow controller design.

Methods and Results from Specific Experiments

Float valve corrosion test methods

• A simple test where float valve parts were left in alum and chlorine for extended periods of time to determine corrosion effects

Flow controller body design and selection

• Includes notes on the brainstorming that went into FCM parts selection and design

Flow versus head loss data collection in the turbulent range methods

• Experiments were conducted to establish a model for the relationship between FCM outflow and headloss associated with outflow tube position

Determining the maximum inlet shut-off pressure

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Conclusions and Areas for Further Research

Through this semester the Flow Control Module testing apparatus has evolved to allow more precise testing to take place. The next upgrade to our testing equipment is an automated position control, which will be capable of changing the head loss in the system automatically. This will increase the precision and quantity of data collected in the future.

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