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<br />. <br /> <br />. <br /> <br /> <br />In order to a'cquaint you with the United States-~1exico l'later Treaty of <br />bE'L <br />1944 and the relationship of Minute No. 242 to the Treaty, Mr. ~ McNealy, <br /> <br />, <br />'f <br /> <br /> <br />~ <br />l-" <br />rv <br />W <br /> <br />International Boundary and Vlater Conmission, E1 Paso; Texas, is prepared <br /> <br />, <br /> <br />to give you a brief ,outline of the history of the International Agreement, <br />......Mr. tkNea1y..... <br /> <br />~ f <br /> <br />,,' <br /> <br />The large maps displayed in the room sho~ the project features. The <br />ori gi na 1 draft envi ronrr.enta 1 statement was prepared in support of H. R. 12834 <br />and S. 3094 and did not include the Protective and Regulatory Ground Water <br /> <br /> <br />Pumping feature. Subsequently, a supplement to the draft environmental <br />statement was prepared in response to the bill that was enacted into law <br /> <br />on June 24, 1974. The final bill added the protective well fields in the <br />Title I portion of the Act. Accordingly, this hearing is concerned with <br />the environmental impacts of ALL of the features included in Title I of <br />Public Law 93-320. To better acquaint you with these features, I will <br /> <br />A desalting plant is proposed to be located adjacent to the Wellton-Mohawk <br /> <br />t~ain Outlet Drain Extension and the Yuma Varley levee, about 4 miles west <br /> <br /> <br />~ <br /> ,,', <br /> hi'" <br /> :: <br /> , <br /> ';'0 <br /> :;;; <br /> /,. <br /> , <br /> Y' <br /> ? <br /> '~~ <br /> y, <br /> , <br /> .", <br /> , <br /> :'lv <br /> t" <br /> , <br /> ~' <br /> , <br /> ., <br /> ;r- <br /> -' ;W <br /> "": <br /> 'e' <br />r :.:~ <br />, .;;; <br />< .,. <br /> ,";: <br /> <br />give you a brief description of the individual components of the project. <br />Mr. Lopez will point out these features on the maps as they are discussed. <br /> <br />of Yuma, Arizona, and about 2 miles north of Morelos Dam. The plant will <br /> <br />treat a portion of Wellton-Mohawk drainage flows which presently have an <br /> <br />average salinity of about 3,700 p/m. The dissolved salts will be removed <br /> <br />by means of a membrane process, either reverse osmosis, electrodialysis, <br /> <br />or both. The desalting plant win J1iwe a capacHy of approximately 100 MC\al/d <br /> <br />2 <br /> <br />'f -,' <br /> <br />c <br /> <br />"" <br /> <br />;j{ g,".,o,_ <br /> <br />. j; <br /> <br />, ~- <br /> <br />,.~.-.;i:& u>,;' J-1 ...._L_,~~ _~.L': <br /> <br />, 4 ,~", <br />. W <br />:: ,,' '- " - -" - - - - ~ -;~ ~ -~;;--: <br />_~__,~~~~;l_i~~:; k:)' : '! <br />