Case History Report
Water Treatment
"Non‑Chemical Device"

                                                        CHRNCD 507

 Device Evaluated

     This is our second case history report, Dolphin II, on "The Dolphin HYTRONIC Series 1000" pulsed power water treatment device (Dolphin) manufactured by Clearwater Systems LLC, 145 Dennison Rd., P.O. Box 463, Essex, CT 06426, ph: 860‑767‑0850 FAX 860‑767‑8972 WEB www.clearwater‑dolphin.com

 System Data

     Clearwater representatives designed a water treatment program, based on Dolphin non‑chemical devices (NCD), for treatment of a new, large cooling tower/chiller system at a Pennsylvania convention center. At the time of our site review, the system had been in operation approximately 1 1/2 years and the operators were planning to convert to a standard chemical water management program within a month.

 Cooling Towers

     Four (4) galvanized steel construction, 1500 ton capacity, BAC 3000 series cross flow cooling towers, installed in banks of two (East and West), are used to provide cooling for the condensers of four freon cycle chillers. Typical load is two units base, two units in reserve. System metallurgy is black iron piping, copper tubes, and some brass valves. Dolphin units are installed on each chiller condenser return line (4 units) and the makeup water line (1 unit) to the cooling towers at a reported equipment cost of $120,000.

     A conductivity based blowdown control was installed for control of concentration cycles while a Lakos hydrocyclone was installed on the cooling tower hot water return line for control of suspended solids. Makeup is normally obtained from an on-site well with city water as a backup source.

 Claims Made

     Dolphin sales literature and WEB site information claim that the NCD "improves system efficiency ‑ eliminates bio‑film ‑ reduces encrustation & fouling ‑ controls bacteria to very low levels ‑ inhibits corrosion" in cooling towers.

     Dolphin WEB site data, 01/03, claims that Dolphin devices "impart pulsed, high frequency electromagnetic energy into flowing water".                                              

     No USEPA registration pesticide number has been seen in theDolphin literature reviewed. Given the claim for control of bacteria and elimination of bio-film, we believe such a registration is required under FIFRA.

History

     The Dolphin units were installed concurrent with construction of the convention center with start‑up in April, 2002.   Operation was continued through September 15, 2003, date of our review, using only the installed NCD systems as treatment with no pretreatment of the makeup well water. We have since confirmed that the convention center converted to a chemical water management program about one month after our review.

Review

     PCT personnel visited the site on September 15, 2003, to walk the system and examine the cooling towers. The site visit was at the request of operating personnel as they had determined, based on their experience with the NCD systems, to return to a chemical treatment program in the near future. During the visit, plant personnel reported substantial corrosion, scaling, deposition, and algae growth problems. The cooling towers were reported to require frequent manual cleanup to remove algae and slime growth from the decks and fill, while the tube sheets and water boxes of the chiller condensers had been wire brushed to remove rust and deposition. The tubes had been brushed once to remove fouling.

      Color pictures were supplied of cooling tower algae growth; chiller tube and water box corrosion and deposition; and cooling tower corrosion and deposition. Please note the attached pictures numbered 1 through 4.

     A report by Cyrus Rice Water Consultants (CRC), an independent water consultant, on a cooling water system water audit they had undertaken in July, 2003, was also provided to us by the operating personnel. Analytical data from this report is summarized as follows:

 

Parameter                 

Well Makeup

East CT

West CT

pH                           

8.0

8.1

8.2

Total Alkalinity mg/l as CaCO3

140

150

162

Conductivity mmhos          

544

1418

1525

Calcium mg/l as Ca                

84

102

110

Chloride mg/l as Cl               

96

273

297

Silicon mg/l as Si                

7.4

18.1

15.1

Copper mg/l as Cu                 

<0.1

0.54

0.51

Iron mg/l as Fe                   

0.70

0.82

0.85

Saturation Index            

+0.84

+0.95

+1.2

 

Microbiological samples were also taken by CRC with the following results reported:

 

Parameter                      

East CT

West CT

Planktonic Plate Count cfu/ml  

1100

1380

Sessile Swab Sample cfu/ml     

TNTC

TNTC

TNTC = to numerous to count

 

     Our own inspection of the cooling towers showed algae growth in the basins and scale on the cooling tower fill. A sample of the scale removed from the cooling tower was analyzed at Analytical Services, Inc., a state certified laboratory, with the following results reported.

 

Parameter

Results as % Dry Wt.

Loss on ignition

18.8

Acid insoluble

0.5

Aluminum as Al2O3

0.03

Calcium as CaO

47.2

Copper as CuO

0.36

Iron as Fe2O3

1.93

Magnesium as MgO

0.72

Manganese as MnO2

1.80

Silicon as SiO2

0.63

Sodium as Na2O

0.08

Phosphate as PO4

0.03

Sulfate as SO4

0.29

Zinc as ZnO

0.57

 

     A Dolphin unit control box was opened and found to contain a small transformer. The transformer output, passing through  an inductor coil, fed into the actual Dolphin unit. The Dolphin unit was also inspected and appeared to be nothing more than an insulated coil of wire wound around a pipe spool. Typical power input was listed on the literature as 110 to 390 va.

Discussion  

     The data in the CRC report clearly shows that the cooling tower system had a substantial loss of calcium and alkalinity while operating with NCD treatment. True cycles of concentration, based on chlorides, was 2.8 to 3.1 cycles, east and west cooling towers respectively, while the alkalinity cycles were only 1.1 and 1.2, and calcium cycles were 1.2 and 1.3. Picture 1, which clearly shows calcium scale slough off and some scale still on the cooling tower fill, shows where the calcium and alkalinity went. The analysis of the scale obtained from the cooling tower fill agrees with the water analysis data in that the majority of the scale was calcium carbonate. Picture 3 also shows what appears to be calcium scale on the inside surface of the condenser tubes.

     We also note that the iron present in the makeup water, 0.7 mg/l, has also failed to cycle in the cooling water, levels of 0.82 and 0.85 being reported in the cooling waters. Given aeration of the cooling waters and the alkaline pH, iron would be expected to precipitate. Looking at pictures 1, 2, and 3; the red coloration of the scale and deposits is likely due to iron. Further, the scale analysis confirms the presence of iron at 1.93 % 

     Again referencing picture 3, it appears that the tube sheet is suffering from rather extensive corrosion as indicated by the presence of rusty areas. This was further confirmed by operating personnel reporting pits in the tube sheet when it was cleaned of deposits.

     Looking at the water analysis data, we also see that the level of copper in both cooling towers is substantially elevated over what would be expected based upon cycling of the makeup water. This is a good indication that corrosion of the copper tubes in the condenser was a problem.

     The low microorganism planktonic plate count found was not a surprise. Given the obvious calcium precipitation within the system, removal of microorganisms from the cooling water by simple flocculation could be expected. Flocculation is the chemical process commonly used in many potable water treatment plants and has nothing to do with "operation" of the NCD, being simply a precipitation of calcium carbonate when the concentration present in the water exceeds its solubility limit.

     The high sessile microorganism level reported is visually confirmed by picture 4, showing substantial algae growth, and our own observations. The high level of sessile microorganisms found is of great concern due to both under deposit corrosion and the effects when these organisms slough off. Such organism masses are an ideal place for legionella bacteria to multiply and they would become dispersed throughout the water during sloughing events, and thus able to enter the cooling tower windage stream.                                  

Conclusions

     Based on the analytical data and observed corrosion, it is evident that the Dolphin NCD does not control corrosion in a cooling water environment.

     The analytical data and scale observed prove that the Dolphin NCD does not provide an acceptable level of scale control when a moderate hardness water is used as makeup. Substantial scale formation within the cooling tower fill was observed and picture 3 shows scale formation within the condenser tubes.   

     While the CRC report noted that planktonic microorganisms were at low numbers, the very high levels of sessile microorganisms found is completely unacceptable for operation of a cooling water system. Based on the high levels of sessile microorganisms reported and observed, it is clearly evident that the Dolphin NCD has no effect on biofilms. We are also of the opinion that the low level of planktonic microorganisms is due solely to flocculation, with subsequent removal in the hydrocyclone, resultant from calcium precipitation within the cooling water.  

Literature

     Review of the supplied literature and Clearwater WEB site shows no theory of operation for the Dolphin NCD which is consistent with accepted scientific principals.

     For instance, reference is made to Faraday's Law of Magnetic Induction (1) to "explain" how the Dolphin unit "effects” surface charge and precipitation". This law concerns induction of an electrical voltage via movement of a magnetic field relative to a conductor. At no place in the equation for this law, EMF = ‑lamba X (dif magnetic flux/dif time), can one find an addition, or removal, of an electron to a particle, which would be required to effect surface charge.

     Dolphin literature further states operation is via "The electric field effects the surface charge and precipitation behavior of charged particles‑‑".  It is a commonly accepted chemical principal that the constituents responsible for scale formation exist in water as separate, hydrated ions, not as "charged particles". Since there are no particles in the water to be "effected" by an electric field, there will be no action by the NCD.

     The claimed "activation of colloidal nucleation sites" resulting in bulk water precipitation of calcium carbonate is easily explained by well known chemical processes, operating with, or without, the presence of the Dolphin NCD.

     A further claim is made that bacteria are controlled, by the Dolphin NCD, in cooling water by application of "pulsed power" magnetic fields. Control of bacteria has been demonstrated in fluids by application of very powerful magnetic fields, several orders of magnitude greater than any possible field generated by a Dolphin NCD based simply upon its low power input. It is thus highly unlikely that any measurable effect is produced by the low intensity magnetic field generated in the Dolphin NCD. This claim could be easily tested by running plate counts on the influent and effluent from a Dolphin NCD. To date, we have not seen any such data in the literature.

     We would also comment that even if the Dolphin NCD did demonstrate biocidal action, the effect would be restricted to the water actually passing through the device and thus provide no control of sessile microorganisms in the rest of the cooling system. As many problems in cooling tower systems are caused by sessile microorganisms, either in place or after they slough off, such an effect would not be of much utility.

Economics

     A general claim is made that programs based on Dolphin NCD are less expensive to operate than typical chemical water management programs. With the convention center spending $120,000 for the Dolphin units and noting that they have operated for the last 1 1/2 years at approximately 25 percent (1500 ton) of design load, we have calculated the following cost comparison with a typical chemical program.

Item                   

Dolphin NCD

Chemical Program evaporation

GPD        

37,332

37,332

Cycles                  

3

4.5

Blowdown GPD          

18,666

10,666

Capital                 

$120,000

$5,376

Capital Cost 5%         

$6,000

$269

Annual Chemical Cost    

0

$12,724

Sewerage at $2.00/1000 

$13,651

$7,811

Total Operating Cost    

$19,651

$20,804

Annual cost reduction for Dolphin NCD = $1,153

 

     This analysis shows that the Dolphin NCD has a lower, about 5.5%, annual operating cost than a chemical program. However, when the difference in capital costs are considered, the Dolphin NCD has a very poor return on investment as shown in the following.

Capital cost difference = $114,624

Simple return on investment = 99.4 years  

     Since most industrial projects are required to yield a maximum return on investment time of 5 years, even if the Dolphin NCD worked as claimed, it is a very poor investment based on the cost savings obtained.

     Please note that this evaluation did not consider the cost for makeup water, since the convention center uses well water, which at a typical $2.00/1000 gallons would have given the chemical program the lower operating cost by $4,687. In general, we observe that most such studies use inflated chemical program costs to make the NCD the low cost option.

 Legal

     ProChemTech, and the reporter, have received two (2) letters, dated July 24, 2003 and September 10, 2003, from an attorney representing Clearwater LLC, supplier of the Dolphin NCD. Both letters referenced our first Case History Report (CHR) on the Dolphin NCD and demanded that the CHR be removed from our WEB site, and withdrawn from distribution, on threat of litigation based on the "false and misleading statements" contained in.

     It is our opinion that legal threats, as noted above, made with the express purpose of preventing publication of findings is a good indication that the particular device, or process, investigated is, in fact, not capable of the marketing claims made. If the product functioned as advertised, there would be no adverse findings to report and thus no need of legal threats.

     The standing policy of ProChemTech International, Inc., is to investigate any "new" technology in the water treatment field to ascertain its effectiveness and report the results. We believe that open presentation of such findings advances the entire field and science of water management.  

 Reporter

Timothy Keister, FAIC, CWT

Chief Chemist

 

 (1)     Specific Faraday law noted in letter dated July 24, 2003,

           From Robinson & Cole, attorneys for Clearwater Systems, LLC.

                  

ProChemTech International, Inc.

Brockway, PA 15824

814-265-0959 www.prochemtech.com

 

 

 

 


 

 

 

 

Picture 1, Convention Center, interior of BAC Model 3000 cooling tower showing rusty scale on deck and

scale on fill.

 

 

 


 

                                   

 

 

Picture 2, Convention Center chiller condenser with head removed.

 

 

 


                                   

                       

 

Picture 3, Convention Center, close-up of chiller condenser tube sheet.

 

 

 

 

 


                                                                                                                                                                       

                        Picture 4, Convention Center, algae and slime growth in cooling tower basin and fill.

 

| Company Info | Products | Home | Technical Papers |
| Career Opportunities | Literature | Contact Us |

Problems, questions, comments?
prochem@prochemtech.com

Copyright © 2004 ProChemTech International, Inc. All rights reserved.