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<br />84 <br /> <br />, <br />4031. <br />RUEDI DAM AND RESERVOIR, COLO. <br /> <br />i <br />I <br />1 <br /> <br />type than were tne development to OCCllr .jn fl mo-:e populated. area. <br />Very little supporting in.dustr)' of .the km.d reqUIred Il?''''' eXlsts.,_ <br />To summnrlze shale OIl productIOn durmg phase 1\' from In,o <br />to If)75 will inc;ease to about ll/:! million barrels per day. This is <br />less than 8 percent of anticipated U.S. pet,rolemn demand in 1975. <br />The product, priucipally hydrogenated shaJe 011, free of con- <br />t,ft1l1innllt.s a.nd equivn.le.nt to the hlghe.st qun-lIty crude petroleum, <br />will be transported by large-cnpncity pipelines t,o markets on ,the <br />Pacitic Coast and in t.he .Middle '\Test.. The gasolme- find other fuel <br />requirements of tlte lOCH 1 community also will be served from fL <br />complete shale oill'efinerv in the. aren. <br />In addition to shale i~)il f;lcilities cost.ing nn estimated $:') hillion, <br />a moderate supporting industry will begin during .this period, Ex- <br />plosive:;. sulfuric acid, lime, and cement, are 1l10:->t likely to be mflnl1- <br />factl1I'E'(l. Numerolls manufact.uring and service faeilities of lesser <br />magnitude :l1so ,,'ill be started. <br />Ii. is unlikely t,hat. oil shale by products will be utilized locally <br />except for explosives, sl1lflll'ic acid, and possibly cement ma.nufacture. <br />A population of nearly ;)00,000 in addition to the phase III de- <br />,'e.lopme-nt. is foreseen mn.king- t.he tota.l population for sha.le and re- <br />lated industries about. :340,000. Rio Bl'll1cO County and llintall <br />Connty, Utah, will share this population growth. <br /> <br />WAT!':R REQUIREMENTS FOR ,sH...".'E OIL PRODUCTION <br /> <br />The product-ion of the crude shnle oil requires very little water. <br />Consumption of water for mining- chiefly is fOI" drilling- hlastholes <br />and ns a dust pallintiye. Retorting uscs only bearing-coolant. water <br />(l,nd a. sma,ll amount of steam for heat.ing alld clefl-lling purpose-so <br />Processes have been developed which do llot require water for cool- <br />ing and condensnt.ioll of the oil. (Certain European processes con- <br />sume steam directly in the retort, but. this t.ype process is not. now <br />lIllder considerat.ion for Colorado shale.) Pel'sollnel, of course, re- <br />quire drinking and sanitary water. Oyernll water reqllirement~ for <br />cTw.1e oll pl'Odntt.loHI both mlning f\nd l'e.tort.\ng. are less t.han HI <br />gallons pel' barrel of oil, of whicll- a smn.1I amount. can be, reused 01' <br />ret.urned to t.he stream. <br />Shale oil refining requires relat.i\rely lnr.rre quantities of water both <br />as a. procp.ss coolnJJt and for the fl'enera6on of steallJ. Since steam <br />is consumed in the manufact.ure ofllydrog-e-n, where t.he re-fining proc- <br />esses ~lse hydrogen as a. reagent, this ]Jart,icHlnr requirement. is lnrg-er <br />than III cOllyentional refineries, Ste.nlll alsu is lIsed to dri\'e pumps <br />and rompressor:-i, <br />Coo~illg water requirements for refining are large eyen when ex- <br />cllllllgtng heat bet.ween hot outgoinO" and cool incoming process <br />strenms, In the refining process sorne~ of the, oil fract.ions fire heated <br />to elevated temperatures se\'eral t.imes and the products must be con- <br />densed and/or cooled Let-\veen process steps as well as when re.fining- <br />has heen c-ompletf'd. 'Yater usually is the most economicnl coolant for <br />this purpose. <br />Cooling wMer may be user1 once or recirculated. On a once.throu,lrh <br />Imsi:-;. most of the water would be ret.urned to the stream e,sse-ntially <br />without. loss, but at a higher tempemt.ure. A recirculation system uses <br />