Energy Conservation Through the Removal of Bio-film

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Presentation transcript:

Energy Conservation Through the Removal of Bio-film The intent of this study is to demonstrate the impact of biofilm on water cooled condenser heat transfer surfaces in an electric driven chiller plant and the associated increase in electrical usage.

Significance of Bio-Film to Energy Loss Old thinking: Bio-film was a concern. Current understanding: New data and studies indicate that Bio-film is the single biggest contributor to energy loss. 1 mm of bio-film increases energy demand by 10% Bio-film also acts as the glue for scale to adhere to heat transfer surfaces

Power of Bio-Film Bio-film is almost 5 times more insulating that scale. Thermal Conductivity Calcium Carbonate 2.6 Calcium Phosphate 2.6 Calcium Sulfate 2.3 Iron Oxide 2.9 Bio-film 0.6

Porous Mixture of Organic and Inorganic Material

Ozone Bio-film’s Worst Enemy Biofilm Prevention and Removal Ozone Bio-film’s Worst Enemy

What is Ozone? 03 - an unstable form of oxygen with three atoms Powerful oxidizing biocide 500% more effective than chlorine Short life in evaporative cooling water (around 20 minutes) Environmentally Safe- breaks down to oxygen

Biofilm Prevention and Removal Keep system clean Mechanically- physical removal Chemically- micro-biocides, dispersants Reduce Food Filtration Oxidation Location of Equipment Process Leaks

Biological Control and Standards Chemically – must use dual biocide program to prevent development of immunity Standard – maintain growth below 10,000 CFU (Colony Forming Units per ml) Ozone – uses clod combustion to destroy cell wall and oxidize waste – impossible for bacteria to develop immunity Standard – maintain growth below 100 CFU

Data Collection Fouling Factor Bio-film Data collected prior to changeover to Ozone Data collected after changeover to Ozone Bio-film Readings collected with the use of a coupon and results from a 15 minute reaction – all readings in BMR, or Bio-Mass Reading Range – from <0.2 indicating no problem to >4.0 indicating severe Bio-fouling Average readings prior to changeover to Ozone Average readings after changeover to Ozone

BioMass Readings - Biofilm Testing Washington & Lee University Chiller Plant Lexington, VA Before Ozone Treatment After Ozone Treatment Date BMR Coupon Location 12/27/2011   1.03 1 1/10/2012 0.71 2 1/24/2012 0.31 2/14/2012 2.27 3/8/2012 0.88 3/15/2012 0.47 4/18/2012 2.11 5/8/2012 2.08 6/4/2012 1.72 6/15/2012 1.36 7/13/2012 0.49 * * Acid over feed on day of sample - pH at 5.0. Removing this reading results in an average BMR of 1.38 7/25/2012 0.72 8/21/2012 1.26 9/12/2012 10/3/2012 *** *** Turned on Ozone system 10/13/2 10/22/2012 0.26 11/28/2012 0.19 12/11/2012 0.16 1/16/2013 0.17 3/12/2013 0.67 4/15/2013 0.28 5/1/2013 0.79 5/16/2013 1.31 5/29/2013 1.33 6/18/2013 4.02 ** **Allowed Bromine to run out 7/1/2013 7/16/2013 0.55 8/1/2013 0.85 8/13/2013 *** Turned on Ozone system 8/13/13 9/5/2013 9/17/2013 0.33 10/3/2013 0.41 10/23/2013 11/20/2013 1.16 Average Biofilm Reading Before Ozone 0.29 Average Biofilm Reading After Ozone 1.29 Average Biofilm Reading During Chemical Re-evaluation Average Biofilm Reading After Ozone Re-start

Program Results Electrical Savings of 3.58% Fouling Factor Improvement of 17% Over Chemical Program Significantly Higher Savings When Chiller Load Above 840 Tons (on a 1200 Ton Chiller) Bio-film Readings Significantly Reduced Corrosion Rates Maintained in the Excellent Range Eddy Current Test Results Identify No Impact Results of Test Backed by Excellent Copper Corrosion Results