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7/14/2009 5:02:31 PM
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5/20/2009 2:48:50 PM
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UCREFRP
UCREFRP Catalog Number
7784
Author
Snyder, D. E.
Title
Impacts of Electrofishing on Fish.
USFW Year
1992.
USFW - Doc Type
\
Copyright Material
NO
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<br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br /> <br />Impacts of Electrofishing on Fish <br /> <br />relationship of these units). Siemens is the term <br />approved for the Intemational System of Units and <br />used in the remainder of this report. <br />Conductivity in natural waters ranges from as <br />low as 5 J.LS/cm in pure mountain streams (Gatz et <br />al. 1986; Zalewski and Cowx 1990) to 53,000 J.LS/crn <br />in seawater (Omega Engineering Inc. 1990). The <br />upper limit for potable water is about 1,500 J.LS/cm <br />(Wydoski 1980). Conductivity in a particular body <br />of water, although generally more-or-less uniform on <br />the same day, can vary considerably from one <br />location to another depending on substrate <br />composition and especially the inflow of tributaries <br />or effluents of highly different conductivities. <br />Conductivity will also vary directly with water <br />temperature. As temperature rises, water viscosity <br />decreases and ionic mobility and solubility of most <br />salts increase. Rates of change in conductivity <br />depend on ionic content and vary from about 5.2% <br />per oC for ultra pure waters to 1.5% per oC for acids, <br />alkalis, and concentrated salt solutions (Omega <br />Engineering Inc. 1990). For natural waters between <br />10 and 250C, the coefficient is approximately 2 to <br />2.3% per oC. To approximate water conductivities <br />at various temperatures within this range, Reynolds <br />et al. (1988) used the equation c2 = c/(1.0it1.t2~ <br />and Stemin et al. (1972, 1976) c2 = e/(I + <br />0.023(tl-~)) where" e" is conductivity and "t" is <br />temperature. Conductivity measures are often <br />normalized to 250C; it is important to note whether <br />reported conductivities are for the temperatures <br />actually encountered (as is often, but sometimes <br />incorrectly, assumed) or normalized data. <br />In addition to the transfer of electrons, the <br />process of electrolysis at the electrodes results in the <br />generation of gases and, more importantly, the loss <br />of metal ions from the anode to the water, deposition <br />of metal ions from the water onto the cathode, and <br />formation of metallic compounds such as oxides on <br />the cathode (Sharber pers. commun.). Riddle (1984) <br />suggested that it was not wise to buy aluminum <br />punts (boats) second-hand from electro-fishermen <br />because the gauge of the metal might be substantially <br />reduced. According to Sharber (pers. commun.), this <br />is not a problem when a metal boat is used as the <br />cathode. But when a metal boat is situated in an <br />electric field and not used as an electrode, it has an <br />intermediate electric charge, negative with respect to <br />the anode and positive with respect to cathode. In <br /> <br />Review I Electric Fields in Water 9 <br /> <br />this case, electrolytic reactions result in both the <br />formation of non-conductive metallic compounds on <br />the boat's surface and the loss of structural metal. <br />Over time, the latter reaction can reduce the <br />structural integrity of the boat. When a boat is used <br />as a cathode, no metal is lost but the non-conductive <br />metallic compounds that form on the boat's surface <br />can decrease its electrical efficiency. This coating <br />can be periodically scraped or sanded away to <br />recover cathodic efficiency, but in doing so, some <br />structural metal may be inadvertently lost. Some <br />researchers switch electrodes periodically to reverse <br />the buildup of metallic oxides (Sharber and Carothers <br />1988). The effectiveness of this procedure has not <br />been reported. <br /> <br />Field Strength <br /> <br />The responses of fish to . electric fields are <br />dependent on the field's strength or intensity (some <br />responses in PDC and AC are also frequency and <br />waveform dependent). Field strength can be <br />described by any of three interrelated and <br />conductivity-dependent terms: voltage gradient (E, <br />yolts per unit distance, usually V/cm), current density <br />(J, ~peres per unit area of an isopotential surface, <br />usually J.LA.Icm2), or power density (P, watts per unit <br />volume between isopotential surfaces, usually <br />J.LW/cm3). [An isopotential surface lies perpendicular <br />to the field or current lines and is defined by a set of <br />points having the same voltage differential when <br />measured from the surface of the electrode; if the <br />water is of uniform conductivity and unbounded, the <br />electrode is spherical, and other electrodes are <br />sufficiently distant, each isopotential surface will <br />form a shell the points of which are a uniform <br />distance from the surface of the electrode.] Of these <br />quantities, only voltage gradient can be measured <br />directly. The other descriptors of field strength are <br />functions of conductivity (c) and voltage gradient (J <br />= eE and P = eE = JE ; Kolz, A. L., 1989). Figures <br />5 and 6 illustrate the relationship between these <br />descriptors of field strength and conductivity. Note <br />that in the middle graph of Figure 5, the curve for <br />voltage gradient becomes asymptotic with the y-axis <br />as conductivity approaches zero and with the x-axis <br />as conductivity approaches infinity, whereas the <br />reverse is true for current density. As a result, the <br />curve for voltage gradient at a fixed power density is <br />
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