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KDF-SIO2AgLabortesztek
A KDF-szilikagél tartalmú vízszűrő M. A. H. Food Controll Kft. mikrobiológiai vizsgáló laboratórium 2010. szeptemberben elvégzett szűrő vizsgálata


KDF55 labortesztje angolul. Forrás a KDF töltet szállítójának honlapja, kdfft.com

KDF 55 Process Media Tested in Lab Show a 90% Removal of Chlorine in Water Filter Cartridges

Lab Test Results from Clack Corporation
 
KDF Fluid Treatment, Inc.
Attn: Mr. Don Heskett
PO Box 277
Constantine, MI 49042
 
Dear Don:
You may be interested in some of the results we have obtained using your KDF® 55D media in our water filter cartridges. The cartridges normally contain 45 cu in (740 cu cms) of granular activated carbon. In testing we maintain a flow rate of 1 gpm (3.8 L/min.) and a free chlorine feed of 2 mg/L.
Cartridges with standard grade carbon have a capacity of about 4,000 gallons to 90% removal and 8,000 gallons to 75% removal. If premium carbon is used, typical capacities are 12,000 gallons to 90% and 20,000 gallons to 75%.
When 1-1/2 lb (0.68 Kg) of KDF-55D was combined with Premium carbon, capacities increased to 30,000 gallons at 90% and 54,540 gallons at 75%. When an entire cartridge was filled with KDF, the test was carried out to 82,640 gallons (313,000L) before the test was terminated because of pressure loss. The KDF was still removing 94% of the chlorine!
I have included a graph with typical tests plotted.
Sincerely,
Mel Hemp
Research & Development
Clack Corporation, Windsor, Wisconsin




Lab Test Results Show How KDF Process Media Work in Water Treatment Processing for Bacteria Removal
KDF Lab Test Results from
Biological Research Solutions
 
Laboratory Service Performed: Analysis of the mode of action of KDF water treatment processing versus Pseudomonas fluorescens.
 
Objectives: Determine the effect of KDF on bacteria in water. If there is biocidal action of KDF, determine if the mode of action is by direct contact or by the release of soluble toxic compounds.
Experimental
Plan: The general experimental design was to compare bacterial survival in water that had been eluted through KDF to bacterial survival following direct contact with KDF 
Testing
Protocol: A number of preliminary experiments were done to develop a testing protocol. The following conclusions were derived from these preliminary experiments in resulted in the testing protocol described in Table 1:
1.Pseudomonas aeruginosa was first used for testing, but survival in deionized water or synthetic hard water was poor even in the absence of KDF treatment. Therefore a more hardy water bacteria, Pseudomonas Fluorescens, was used for all further experiments.
2.Initial testing was done in glass columns containing KDF 55-D, but the maximum flow rate that could be achieved by gravity feed was only 600 ml per hour (0.003 gpm). It was also difficult to flush the columns with sufficient volumes of water to approximate realistic use conditions. Therefore, a model water test system was constructed using 3/4 inch cpvc pipe.
3.The results of initial testing of the water system suggested several necessary modifications and the design of the test system used for the experiments reported here is shown in Figure 1.
4.Several tests of various combinations of water chemistry showed that the tap water could not be used and deionization was necessary. In order to minimize the aggressiveness of this water, AOAC synthetic hard water was injected through Injector #3 to achieve a final concentration of 100 ppm with a pH of approximately 7.
5.Since there were variable concentrations of endogenous bacteria in the system and in the pump feed lines, the system was flushed with 0.5 to 1ppm sodium hypo chlorite between each experiment.
6.Three gallons of water (1gpm) were run through the system for each sampling condition prior to sampling. Other experiments had shown (for example, the chlorine removal experiment describe below) that this volume of water was sufficient to rinse the system and reach equilibrium.
7.The carbon and bacterial filters were not effective or necessary and were not used after initial testing. When the testing protocol required bacterial injection, a fresh suspension of Ps. fluorescens in a glass reservoir was injected through Injection #1.
 
Results and Discussion: A: Effect of KDF on Ps. Fluorescens:
The results of four tests using Ps. Fluorescens and the testing protocol described in Table 1 are shown in Table 2. The bacterial in Samples 1 and 3 (Controls) survived well during the three hour incubation and indicated that there was nothing toxic in the system.
 
Sample 2 contained water that had been eluted through the KDF column prior to inoculation and there is substantial die-off of the bacteria compared to the control water. This die-off is very likely die to small amounts of copper and zinc ions that are eluted (less than 0.025 ppm copper and less than 1ppm zinc). This result is not unexpected since it is well documented that copper is toxic to bacteria.
 
Sample 4 contain bacteria that have passed through the KDF column. In the time required to collect the water sample and plate "Time 0" (not a true time 0, since 2 to 3 minutes elapse before plating) there has been substantial kill of the injected bacterial inoculums. This result has been reproducible in all experiments and the only reasonable interpretation of this result is that contact with the KDF column is toxic to Ps. fluorescens. This toxicity is substantially more that can be explains by soluble toxic compounds (comparison of Samples 2 and 4).
 
B: The Effect of Voltage Applied to the KDF Column:
 
Brass screws were inserted in the top and bottom of the KDF column. A voltage of 0.02 to 0.05 volts is produced by the column, depending on the water that is in the column. It was thought that the voltage generated by the column might be responsible for the observed direct-contact bacterial kill.
 
If this were true, the application of additional voltage should increase the toxicity of the column. The experiment summarized in Figure 3 shows that there is a slight effect on bacterial survival if 11.7 bolts are applied to the column as the injected bacteria are passing through. Most of the effect, however, is during the three hour incubation rather than during the initial direct contact. It seems very unlikely that the voltage generated by the column can be responsible for the reduction in bacterial numbers that is observed.
 
C: Effect of KDF on Legionella Pneumophila:
 
The effect of KDF on Legionella pneumophila (Philadelphia 1 strain) was measured using the standard testing protocol described in Table 1. The results of this test are shown in Figure 4 and the effect of contact with KDF appears to be very similar to the results for Ps. fluorescens.
 
This preliminary experiment offers some promise that KDF may have applications for the control of L. pneumophila, especially in recirculating water systems such as cooling towers and domestic hot water where repeated contact would occur.
 
D: Oxidation -Reduction Potential of KDF:
 
since voltage does not appear to explain the phenomenon of KDF, the oxidation-reduction (redox) potential was measured. The redox potential of deionized water containing 100 ppm synthetic hardness was measured at +340 millivolts with an Orion Redox electrode. The redox potential of this water with KDF added was -160 millivolts. After the KDF was removed by filtration the redox potential returned to +180 millivolts.
 
The observed decrease in redox potential of 500 millivolts is very likely to be the mechanism by which KDF exhibits bacterial toxicity by direct contact. A rapid shift from an oxidizing to a reducing environment should cause severe stress to the bacteria.
 
E: Removal of chlorine by KDF:
 
In order to measure if a 3 gallon water flow between sampling conditions was sufficient to reach a stable equilibrium, a 1000 ppm solution of sodium hypo chlorite was injected through Injector #3. The calculated concentration of free chlorine in the system at the maximum pump rate (120 pulses per min) was 21 ppm.
 
The measured free chlorine (Hellige DPD method) with and without passage through the KDF column is shown in Table 3. The KDF column removes chlorine and the response of the water system is linear.
 
F: Production of chlorine from chloride:
 
Another possibility for the mode of action of KDF had been previously suggested. If the column oxidized chloride to chlorine by contact with the column, this could explain the observed phenomena. Various concentrations of chloride ion (as sodium chloride) were passed through the KDF column and free chlorine was measured in the eluted water. Even at 6800 ppm chloride no free chlorine could be detected. The eluted water was checked for interference with the detection and there was no interference.
 
The KDF column could produce low levels of chlorine that are immediately removed, but this possibility seems unlikely based upon the results reported above (D:).
 
Conclusions: These studies have shown that KDF possesses inherent toxicity to Ps. fluorescens that requires direct contact for maximum efficacy. The mode of action is likely to be via a rapid reduction in redox potential as water-borne bacteria contact the column.
There seems to be great potential for this material to serve as an effective water treatment device to reduce or remove water pathogens such as Legionella pneumophila without the need for introduction of pesticides into the water.
 
By John W. Wireman, PhD
Dated July 31, 1990
 
Submitted by Biological Research Solutions
John W. Wireman, PhD,   Dated: February 25, 1991

KDF Fluid Products, Inc.
Lab Test Results from
Biological Research Solutions
 
Laboratory Service Performed: Evaluation of the Bacteriostatic Properties of a Water Treatment Device Containing an Alloy of Copper and Zinc (KDF® media) Introduction: Water treatment devices may be colonized by bacteria and thus promote the growth of bacteria contained in the influent water. It is important, therefore, that devices that are intended for use in potable water supplies be tested to determine if they are bacteriostatic (i.e. do not stimulate the growth of microorganisms).
Procedures: The testing protocol used is described in Table 1. This procedure provides a heavy bacterial challenge over a seven day period followed by a period of time to allow the growth of the challenge bacteria. If the treatment device provides an environment that is favorable for bacterial growth, there should be a demonstrable increase in bacterial numbers during the latter stages of the test.
In order to test the device, the model water system diagrammed in Figure 1 was used. The supply water for the model system was chlorine free deionized water that was reconstructed to approximate Detroit city water by the injection of AOAC synthetic hard water to achieve a final concentration of 100 ppm and a pH value of 7.0
 
A fresh suspension of Enterobacter aerogenes (former name Aerobacter aero genes) was prepared daily and injected into the flowing water stream to achieve a final bacterial concentration of 300 cfu/ml.
 
Results and Discussion: The results of the 19 day bacterial challenge test are shown in Table 2. For the first seven days Enterobacter was injected into the influent water stream and the survivors that passed through the test device were measured. There were endogenous bacteria (naturally occurring water bacteria other than Enterobacter) present in the model water system at the beginning of the testing, and there was a large reduction in these bacteria as a result of passage through the water treatment device. The results shown in Table 2 for the first seven days of testing show the Enterobacter survivors only. The measurements after 11 and 19 days, during which time no additional Enterobacter was injected into the system, the results in Table 2 show the percent reduction in these endogenous bacteria (no Enterobacter survivors were detected).
This testing showed that the water treatment device is bacteriostatic and does not stimulate the growth of Enterobacter nor does it provide an environment that promotes survival. In addition, the device is effective in reducing the concentration of Enterobacter or other endogenous bacteria present in the influent water (bactericidal effect) and thus may be useful in the control of potentially harmful bacteria that may inadvertently enter potable water supplies.
 
By John W. Wireman, PhD
Dated February 25, 1991

Lab Test Result Show Heavy Metal and Lead Removal in Water Filter Device with KDF Process Media
Lab Test Results from PatChem Laboratories
 
Customer: Systematix Inc.
Sample Date: 3-23-90
Report Date: 5-04-90
Sample ID: 9003-1233B Di-Tech KDC+1.5
Subject: One Systematix 9-3/4" filter cartridge was received for testing to determine its ability to remove heavy metals from water.
Method: Reagent grade lead chloride was spiked into drinking water and run through the filter per manufacture and NSF specifications. The influent and effluent water were tested per EPA Methods for Chemical Analysis of Water and Waste (EPA-600/4-79-020).

Total Flow Influent Water Effluent Water % Removal
1 Gallon 0.17 mg/L < 0.01 mg/L  99.99%
5 Gallon 0.16 mg/L < 0.01 mg/L  99.99%
10 Gallon 0.16 mg/L < 0.01 mg/L  99.99%
50 Gallon 0.17 mg/L < 0.01 mg/L  99.99%
100 Gallon 0.16 mg/L < 0.01 mg/L  99.99%
250 Gallon 0.16 mg/L < 0.01 mg/L  99.99%
500 Gallon 0.16 mg/L < 0.01 mg/L  99.99%
600 Gallon 0.17 mg/L < 0.01 mg/L  99.99%
750 Gallon 0.16 mg/L < 0.01 mg/L  99.99%
1000 Gallon 0.16 mg/L < 0.01 mg/L  99.99%
1250 Gallon 0.17 mg/L < 0.01 mg/L  99.99%
1350 Gallon 0.16 mg/L 0.03 mg/L  81.25%
1425 Gallon 0.16 mg/L 0.08 mg/L  50.00%

Initial flow: 0.4 gallon/minute at 60 psi.
Cycle: 10% on and 90% off for a maximum of 16 hours/day.
Comments: The Systematix 9-3/4" cartridge filter reduced the level of lead pumped through the unit to a non-detectable level (<0.01mg/L) to 1250 gallons.
 
Respectfully Submitted, Pat Brueckner, Chemist

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