Copyright & Fair-use Agreement
UNLV Special Collections provides copies of materials to facilitate private study, scholarship, or research. Material not in the public domain may be used according to fair use of copyrighted materials as defined by copyright law. Please cite us.
Please note that UNLV may not own the copyright to these materials and cannot provide permission to publish or distribute materials when UNLV is not the copyright holder. The user is solely responsible for determining the copyright status of materials and obtaining permission to use material from the copyright holder and for determining whether any permissions relating to any other rights are necessary for the intended use, and for obtaining all required permissions beyond that allowed by fair use.
Read more about our reproduction and use policy.
I agree.Information
Digital ID
Permalink
Details
Member of
More Info
Rights
Digital Provenance
Publisher
Transcription
6 - Shift Operators 13 •- BCehleimiesft Operators 1 - Superintendent The chemicals used for treatment are as follows: SCualusftaitce oSfo dAal umina Sodium Hexametaphos ph&te Aotlvated Carbon - (occa sionally) pCuarupstoisce osfod cao insv emritxiengd wtihte hc atlhec iiunmc oamnidn mga wganteesri utmo betehe r broena&ctteiso nt ot aankns ifnosorl utahbe le isst atper,o dtuhcuesd poenr mtihtist ipnrgo jietsc tr eatm ovtahle bchyl osreidniem epnltaan tio na.n d Tphuem peoadu sttoi ct hes owdaat eursed ptoruenadtsm enotf pftlaaOnHt ist hrreoquugihr 1e3d# 1f0o0r ltihnee atlr efaetemte nto f o2f ionnec hm piilplei olni ngea.l loAnbs ouotf w1a0t0e0r . Ho addition of soda ash is made. For coagulation# sulfate of alumina is added to the water ahead of the re&otio tsatnikrsr.i ngF ldoeevi cies. buTihlte uipn cionmi ntghe rlaoww weart pearr tis ofd istthrei btuantkesd bayt ath mee cbhoatntiocma lof stlohwe ttahnikc kaennded r eosnt st hvee frltiocoarl loyf tthher otuagnhk sa falnode sbwleapntk etto. a Tshleu dpgree cpiopcikteatt needa rs lutdhege is tcheen tbeort ftroom ma wnhdi cthh iet w aist epru mspeerfda ctoe wiass tleo caont etdh ea dleasregret .r ecAebiovuetr mtiod wwahyi cbhe ttwheeen excess sludge overflows. The sludge pumps operating on program switch co ntrol pump sludge from these receivers periodically. Frraopmi dt hsea nrde aficlttieorns .t ankBse fothree weantteerr ipnags stehse fdiilrteecrtsl yi tt oI st hdeo bsaetdt weiryt ho fs odeiiugmht hexamet&phosphate at the rate of about five pounds par million gallons. bTohinsa tdet ssacgaeli nisg otfo tshtea bifliilztee r tshaen dw.a teBra tseu foffi cfilenotwl yc onttor porlelveresn tr ecgaullcaituem ctaherflow of water from the filters to the stabilized water dear well in propaonrdt biaocnk wtoa shtihen gd aomfa nt.h e Aflillt egrast esa rae nhdy dvarlavuelsi ccaolnlyne cotpeedra wtietd hb yt hpei loopte rsawtiitocnh es wfartoemr thcel eaorpe wrealtli ngb y ttabwloe s1.2 * 5F0i-lHtPe,r s koaoroe bG.aPc.kM-,w ascheentdr firfougma lt hpeu msptsa#b ialti ztehde rate of 15 gallons per square foot per minute. Baokw&sh water is reclai med and retreated. At this point the total hardness of the water has undergone Palbaonutt# andr eidnutcot itohne# fairned pirto tise cdtiisotnr isbysutteemd. for general use at the Magnesium Afo puorr tZeioolni toef stohef tweantienrg lbeeadsv.i ngT hteh e cofinlttreorlsl eriss a&rdem iatctteuda ttherdo ufrgohm c ofnltoraotlsl eorns thtoe water surface of the Zeolite treated water clear well# and admit enough water through the beds to always satisfy the demand. The synthetic Zeolites are nheysdriouums frsiolmi ctahtee sw atofe rs aondidu rme laenads ael uamni neuqmu.a l Tahmoeuyn ta bosfo rsbo tdhiuem ,c alkc'ihuemn atnhed mcaagpacrietgye nofe ratthee d Zweiotlhit sea ltto abbrsinoer bt oc arlecsituomr ea ndth mea gsnoedsiiuumm a nIsd cexahnayu sotfefd tthhee baebdsso rabreed calcium and magnesium. Salt brine for regeneration is pumped through a 3 inch pipe line a distance of 13#100 feet from the Chlorine Plant, At the Water Treatment Plant the brine is passed through a pressure filter and 10