<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 />
|