x evaporation reduction by monomolecular films i. … · tests out-of-doorsand depended upon...

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I. EVAPORATION REDUCTION BY MONOMOLECULAR FILMS * THE INFLUENCE OF WATER TEMPERATURE AND APPLICATION RATE ON THE EFFECTIVENESS OF CETYL ALCOHOL by E. H. Hobbs Member C.S.A.E. Canada Agriculture Research Station, Lethbridge, Aiberfa INTRODUCTION If evaporation from free-water sur faces could be reduced, more water would be available for useful pur poses. Scientists in several countries Have been investigating the use of monomolecular films as evaporation retarding agents. Hexadecanol, also known as cetyl alcohol, appears to be the most promising material for this purpose. Evaporation is an endothermic pro cess. Thus, when evaporation is re duced the water temperature rises. Several authors, when reporting ex periments concerned with evaporation control, have commented on this fact. Hayes (6) found that the surface waters of hexadecanol-treated ponds were from 2.6° to 3.8° F. warmer than those of untreated ponds. Roberts (8), using a high-accuracy thermistor ther mometer, recorded a temperature dif ference of to F. between treated and untreated lake surfaces. Com putations by Harbeck and Koberg (5) indicated that the 18 per cent reduction in evaporation achieved in a field test was necessarily accom panied by a temperature rise of 3.4° F. Others have noted that the success ot evaporation retardant processes is dependent in part on the water tem perature. Mansfield (7) reported that the rise in water temperature which follows application of a surface film reduces the degree to which that film may retard evaporation. Vines (9) observed that, as a water surface be came excessively warm in hot weather, the efficiency of the evaporation con trol process dropped. Florey et al. (4) were unsucessful in attempts to estab lish a temperature-evaporation ratio using 4-foot-diameter pans indoors where air temperature was controlled. They suggested that dust contamina tion was the chief factor that inter fered with film continuity. Florey and Timblin (3) conducted similar tests out-of-doors and depended upon seasonal changes in ambient tempera ture to provide temperature differ ences. From these tests they deter mined evaporation reduction factors based on a correlation ot evaporation and water temperature. Preliminary studies, conducted by the author, using 4-toot-diameter pans exposed to tielu conditions produced results similar to those reported in the literature. Methods that appeared quite promising early in the season oecame mucn less eltective during the Iieat ot tlie summer, therefore, labor atory tests were conducted with films ot cetyt aicoliol to determine, more speciiicaliy, the effects of water tem perature and application rates on the reduction of evaporation from a free- water surface. The results of these laboratory tests are reported in this paper. MATERIALS AND METHODS One-gallon plastic pots equipped with point gauges were placed in each ol tour constant-temperature water baths housed in an enclosed green house bay. The water baths were similar to those described by Cooper et al. (1) and operated at tempera tures ol 41.5°, 54.5°, 67.0° and 79.0°, ±1°, F. Air temperature within the greenhouse was tnermostaticatly con trolled at 69.5° F. No attempt was made to modify the existing relative humidity, which was comparatively constant and averaged 40 per cent. The four refrigeration units which provide cooling for the water baths were installed in such a manner that their cooling fans help to produce uniform air circulation over the water baths. This circulation of air appear ed to prevent air stagnation above the evaporating surfaces. The water level in the plastic pots was approximately the same as that in the surrounding bath, and neither was allowed to fluc tuate more than one-quarter of an inch. This required daily addition of water to the pots held at 79.0° F. and less frequent additions to the re maining pots. The volumes of water added were converted to inches of evaporation. Five treatments, random ized in six replications, were carried out in each of the four water baths. Cetyl alcohol, mixed in a 1:5 solu tion with methyl alcohol, was applied to the test pots at the following rates: 17 Treatment No. Cetyl alcohol lb./ac. 0 (check) nil 1 0.026 2 0.052 3 0.104 4 0.260 the No. 1 treatment rate was sliglitly in excess of that required to form a compressed monolayer on the water surlace. Treatments were re newed at the initial rate of appli cation whenever a comparison ot the evaporation loss from treated and check pots indicated that a treatment had lost, or was losing, its effective ness. Under this definition it was necessary, during the 30-day test per iod, to renew treatment ten times on the pots held at 79.0°, five times on those held at 54.5° F. No additional treatment was applied to the pots held at 41.5° F. A thermistor thermometer was used to determine whether a temperature gradient existed within the pots or among treatments. The failure to find either was assumed to be the result of rapid conduction of heat through the walls of the pots to the surround ing water bath. RESULTS AND DISCUSSION The effects of the different treat ments on evaporation at each of the four water temperatures are shown in Figure 1, as well as the significant difference between treatments as de termined by Duncan's (2) multiple range test. The differences in evaporation among check treatments were a result of the temperature maintained in each water bath. The increased air movement under field conditions would cause more evaporation than was recorded in this experiment. The additional water lost, however, would probably be of little practical concern until that part of the season when water temperatures approached 55° F. No significant differences due to treatments were found for the pots held at the 41.5° F. temperature. X

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Page 1: X EVAPORATION REDUCTION BY MONOMOLECULAR FILMS I. … · tests out-of-doorsand depended upon seasonal changes in ambient tempera ture to provide temperature differ ences. From these

I.

EVAPORATION REDUCTION BY MONOMOLECULAR FILMS *THE INFLUENCE OF WATER TEMPERATURE AND APPLICATION

RATE ON THE EFFECTIVENESS OF CETYL ALCOHOLby

E. H. Hobbs

Member C.S.A.E.

Canada Agriculture Research Station, Lethbridge, Aiberfa

INTRODUCTION

If evaporation from free-water surfaces could be reduced, more waterwould be available for useful purposes. Scientists in several countriesHave been investigating the use ofmonomolecular films as evaporationretarding agents. Hexadecanol, alsoknown as cetyl alcohol, appears to bethe most promising material for thispurpose.

Evaporation is an endothermic process. Thus, when evaporation is reduced the water temperature rises.Several authors, when reporting experiments concerned with evaporationcontrol, have commented on this fact.Hayes (6) found that the surfacewaters of hexadecanol-treated pondswere from 2.6° to 3.8° F. warmer than

those of untreated ponds. Roberts (8),using a high-accuracy thermistor thermometer, recorded a temperature difference of 4° to 7° F. between treatedand untreated lake surfaces. Computations by Harbeck and Koberg(5) indicated that the 18 per centreduction in evaporation achieved ina field test was necessarily accompanied by a temperature rise of 3.4°F.

Others have noted that the successot evaporation retardant processes isdependent in part on the water temperature. Mansfield (7) reported thatthe rise in water temperature whichfollows application of a surface filmreduces the degree to which that filmmay retard evaporation. Vines (9)observed that, as a water surface became excessively warm in hot weather,the efficiency of the evaporation control process dropped. Florey et al. (4)were unsucessful in attempts to establish a temperature-evaporation ratiousing 4-foot-diameter pans indoorswhere air temperature was controlled.They suggested that dust contamination was the chief factor that inter

fered with film continuity. Floreyand Timblin (3) conducted similartests out-of-doors and depended uponseasonal changes in ambient temperature to provide temperature differences. From these tests they determined evaporation reduction factors

based on a correlation ot evaporationand water temperature.

Preliminary studies, conducted bythe author, using 4-toot-diameter pansexposed to tielu conditions producedresults similar to those reported in theliterature. Methods that appearedquite promising early in the seasonoecame mucn less eltective during theIieat ot tlie summer, therefore, laboratory tests were conducted with filmsot cetyt aicoliol to determine, morespeciiicaliy, the effects of water temperature and application rates on thereduction of evaporation from a free-water surface. The results of these

laboratory tests are reported in thispaper.

MATERIALS AND METHODS

One-gallon plastic pots equippedwith point gauges were placed in eachol tour constant-temperature waterbaths housed in an enclosed greenhouse bay. The water baths weresimilar to those described by Cooperet al. (1) and operated at temperatures ol 41.5°, 54.5°, 67.0° and 79.0°,±1°, F. Air temperature within thegreenhouse was tnermostaticatly controlled at 69.5° F. No attempt wasmade to modify the existing relativehumidity, which was comparativelyconstant and averaged 40 per cent.

The four refrigeration units whichprovide cooling for the water bathswere installed in such a manner thattheir cooling fans help to produceuniform air circulation over the waterbaths. This circulation of air appeared to prevent air stagnation above theevaporating surfaces. The water levelin the plastic pots was approximatelythe same as that in the surroundingbath, and neither was allowed to fluctuate more than one-quarter of aninch. This required daily addition ofwater to the pots held at 79.0° F.and less frequent additions to the remaining pots. The volumes of wateradded were converted to inches of

evaporation. Five treatments, randomized in six replications, were carriedout in each of the four water baths.

Cetyl alcohol, mixed in a 1:5 solution with methyl alcohol, was appliedto the test pots at the following rates:

17

Treatment No. Cetyl alcohollb./ac.

0 (check) nil

1 0.026

2 0.052

3 0.104

4 0.260

the No. 1 treatment rate was

sliglitly in excess of that required toform a compressed monolayer on thewater surlace. Treatments were re

newed at the initial rate of application whenever a comparison ot theevaporation loss from treated andcheck pots indicated that a treatmenthad lost, or was losing, its effectiveness. Under this definition it wasnecessary, during the 30-day test period, to renew treatment ten times onthe pots held at 79.0°, five times onthose held at 54.5° F. No additionaltreatment was applied to the pots heldat 41.5° F.

A thermistor thermometer was usedto determine whether a temperaturegradient existed within the pots oramong treatments. The failure to findeither was assumed to be the resultof rapid conduction of heat throughthe walls of the pots to the surrounding water bath.

RESULTS AND DISCUSSION

The effects of the different treat

ments on evaporation at each of thefour water temperatures are shown inFigure 1, as well as the significantdifference between treatments as de

termined by Duncan's (2) multiplerange test.

The differences in evaporationamong check treatments were a resultof the temperature maintained ineach water bath. The increased air

movement under field conditions

would cause more evaporation thanwas recorded in this experiment. Theadditional water lost, however, wouldprobably be of little practical concernuntil that part of the season whenwater temperatures approached 55° F.

No significant differences due totreatments were found for the potsheld at the 41.5° F. temperature.

X

Page 2: X EVAPORATION REDUCTION BY MONOMOLECULAR FILMS I. … · tests out-of-doorsand depended upon seasonal changes in ambient tempera ture to provide temperature differ ences. From these

At 54.5° and 79.0° F. the evaporation from treatment 1 did not differsignificantly from the correspondingcheck. The inability of this low rateof application to maintain an evapor-

I "1 *3

Figure I. Effect of a monomolecular film of cetylalcohol on evaporation, and significant differences between treatments, at four water temperatures. (Any two means underscored by thesame line are not significantly different at theb% level.)

ation retarding film was attributed toan evaporative loss of the cetyl alcohol and the fact that there was littleor no excess material available for

film replenishment. Treatments 2 and3, at 54.5°, 67.0°, and 79.0° F., weresignificantly different from their respective checks although not necessarily from one another. Treatment4, the maximum rate employed, provided a significantly greater reductionin evaporation than did all othertreatments at the above temperatures.

The evaporation reduction efficiency of each treatment at each watertemperature is shown in Figure 2.Although the difference in efficiencyof comparable treatments at watertemperatures of 54.5° and 67.0° F.was not great, there was a marked decrease in efficiency for all treatmentsat 79.0° F. This lower efficiency occurred despite the fact that almosttwice as many applications of cetylalcohol were made to the pots heldat 79.0° F. than to those held at 67.0°F.

D

RATE (ib/oei

0026

0 052

0(04

0 260

u dTREATMENT I 2 3 4 list

54 5 6T0 1WATER TEMPERATURE "F

ure 2. Percentage evaporation reduction bytreatments at three temperatures.

CONCLUSIONS

Fig

P

four

The amount of evaporation occurring at 41.5° F. was too slight to beof practical concern. Application ofcetyl alcohol had no significant effect

upon evaporation at this temperature.At all other water temperatures studied, high rates of treatment application were more effective than lowrates. As water temperature increasedbeyond 67.0° F., the efficiency of alltreatment rates declined. In order to

compensate for the higher water temperatures occurring during midsummer, heavier and more frequent treatment applications would be requiredto maintain evaporation control at apractical level.

REFERENCES

1. Cooper, D. J., K. F. Nielsen, J. W.White and W. Kalbfleisch. Note onan Apparatus for Controlling SoilTemperatures. Can. J. Soil Sci.40:105-107. 1960.

2. Duncan, D. B. Multiple Range andMultiple F Tests. Biometrics 11:1-42. 1955.

3. Florey, Q. L., and L. O. Timblin,Jr. Screening Tests, Water-Lossinvestigations: Lake Hefner 1958Evaporation Reduction Investigations. Oklahoma City, Okla. pp.125-131. 1959.

4. Florey, Q. L., W. U. Garstka andL. O. Timblin, Jr. Computation ofEvaporation Savings. Water-LossInvestigations: Lake Hefner 1958Evaporation Reduction Investigations. Oklahoma City, Okla. pp.37-42. 1959.

5. Harbeck, G. E., Jr., and G. E. Ko-burg. A Method of Evaluating theEffect of a Monomolecular Film inSuppressing Reservoir Evaporation. J. Geophys. Research 64:89-93. 1959.

6. Hayes, M. L. Biological Effects ofHexadecanol used to SuppressWater Evaporation from Reservoirs. Final report. Submitted tothe U.S. Bureau of Reclamation.98 pp. 1959.

7. Mansfield, W. W. The Influence ofMonolayers on Evaporation fromWater Storages. I. The PotentialPerformance of Monolayers ofCetyl Alcohol. Australian J. Applied Sci. 9:245-254. 1958.

8. Roberts, W. J. Reducing LakeEvaporation in the Midwest. J.Geophys. Research 64:1605-1610.1959.

9. Vines, R. G. Evaporation Control— The Mansfield Process. WoolTechnol. and Sheep Breeding 5:51-53. 1958.

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Continued from page 3

Multi-plane Draft hxture.

urements the drawbar of the tractorshould be pinned so that the normalsoil variations and resulting changesin the line of draft will not move theplane of the transducer from theplane of the direction of travel. Formost work, however, this is not necessary as the error introduced is smalland for small angles can be readilyignored.

An electronic integrator is an extremely valuable edition to any draftrecording system, especially in themeasurement of torque which mayhave one or more peak values perrevolution. Any time base may beselected for the limits of integrationup to the maximum capacity of theelectronic counter (upper rack Figure6). For draft measurements a ten-second time base has been selected asan estimate of the reaction time ofan operator to an overload conditionof his tractor.

The integrator operates on theprinciple of converting the voltage(lower rack Figure 6) applied to thepen of the ascillograph to an oscillating voltage which is then fed to theelectronic counter. As the frequencyof oscillations is directly proportionate to the pen voltage (pen deflection) the count is then the integrationor summation of the area under thecurve drawn by the pen.

Fig. 6. Integrator.

SUMMARY

The use of transducers provides anextremely accurate method for deter-

Con+inued on page 29