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HomeMy WebLinkAboutPackets - Council Packets (1321) AGENDA ORO VALLEY TOWN COUNCIL SPECIAL STUDY SESSION JANUARY 18, 2002 TWIN PEAKS PUMPING STATION 10900 W. TWIN PEAKS ROAD MARANA, ARIZONA STUDY SESSION - AT OR AFTER 9:30 AM CALL TO ORDER ROLL CALL 1. SITE TOUR OF THE CAP CANAL TWIN PEAKS PUMPING STATION LOCATED AT 10900 W. TWIN PEAKS ROAD. (The Town Council will meet at Town Hall located at 11,000 N. La Canada Drive at 8:45 a.m. to drive to the Twin Peaks Pumping Station.) ADJOURNMENT The Town of Oro Valley complies with the Americans with Disabilities Act (ADA). If any person with a disability needs any type of accommodation, please notify the Oro Valley Town Clerk, at 229-4700. POSTED: 01/15/02 4:30 p.m. ,P„ , 0 Av ra Vally {:. �Rd MI t i/1/ \ Tarin Fabs f '17'414%47\0.p■ r enure R,o cT r,1 f .� r __.� 111.` DIRECTIONS TO TWIN PEAKS PUMPING PLANT 10900 W. Twin Peaks Road Tucson 85743 From Tucson From the Freeway, west on Cortaro Farms Road to Silverbell Road(about 1 mile) North on Silverbell (about 3 miles) then west on Twin Peaks Road(over the pass). Past the conveyor belt (about 1.8 miles) to Twin Peaks (another 1.7 miles) can be seen on the right (north) side of the road. Just past the pumping plant turn right into the CAWCD office complex, take right road down into the plant. If you reach Sandario Road, you've gone too far. From Phoenix South(left) on I-17 to I-10 East on I-10 to Exit 242A, Avra Valley Road Proceed West on Avra Valley Road for 5 miles to intersection of Avra Valley Road and Sandario Road. Turn South(left) onto Sandario Road and proceed 2 miles to the intersection of Sandario Road and Twin Peaks Road. Turn East(left) onto Twin Peaks Road and proceed 1 mile to the entrance road of Twin Peaks Pumping Plant. Contacts: Eric Holler 520-670-4825 Bruce Garrett 520-721-7281 cell 520-403-7102 Bob Bradford 623-869-2618 (at Twin Peaks PP) Greg Hahn 520-616-0224 .� '� til l i � 1 k" -'4,..,,4; P .:'''41,,,,,,,,„„„„„„:„,,„. 1,7411N ia • .M Av ra\kII y R,d , ,,,,,/ i r--_..1_ ,:i.i. „-----, i __:_, k,i ,_......._.......--_—,, i ,, . ,, , ,,, , , ,,, 3/ 1 __IL / 1_id, ____+_ _ '— Tarin mks P I , __i_i___, // \., 1 ,,,,,,,,---7, --_-:_i_H.,......, „,„„„,„,„,,,„„„„„„„„,.„,„„„,„„,„„„,,„„,„„„„,„„„,„„„„„„„„„„„„„,„„„,„„,„„„„„„„„„„„„„,:„,,,,,,„„:„„.., r� ��� s _ „__.,. ,,,,,,,,,,„„:„„„„„,,,,,,„,„„„i„,::,,,,,„,,,,„,„,„,,:„„,,,,,„,:,,„,„„:„„.,,,„„.„„,.„:„,„:,,.„,:„„:,,,.,,:,,,,,„„,„„,,,,,,,,„.:„.,,,,H,.. ......, _,_TrEiw ..... „„„„,„„„„„„„„„„„,„„„„„„„„„„„„„„„„„„„„,„,„„„„,„„„„„„,„,,,,,,,,,,,,,,,:::::::::::::::::::::„.:.................. 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L.. ... 1.- .... 0 14 'lime W •(0) NE 0 113 en al E = = aul 75 E° *NE 0 — 0 0 0 e) islie a .—r4 •-- 0 m O oli LI •am Lii E � (1) U) 0 OO tn %0 am-- to- Omi4in 0 o 2 C -1, ...I • (,) in m itsmi 0 C O Nom m m IM CI %Al a 16 now > > C: e) /0 0 S I 04 • IM W 0 ;°0 C ° 1 I 11 gg Emo 0 Di ii, t, 0 LLI t) I D v ig tg 1 2 1 1 y umiu'imam 1_ y V cn � V w Cost t forTreatment Methods 1.60 - - - - - - .. - - - - - - . - w . s . w w a .. - w s - w s .. r s -'- s 1.40 .towo _ w .e • .. _ .. . . - sw . wswr • sa. . a. ., _ w .1sr, 1.20 - - - - • - - - - - • - - - to - w - s - - s - - • • th 0 1.00 - - - 0 0 0.80 0 0 0 0.40 - - - - - .e - = - - - 0.20 - • - a - s e - w - 0.00 1 1 CT SSF MF/UF CT-RO SSF-RO MF/UF-RO Water Treatment & Distribution System Total Cost CT SSF MF/UF CT-R01 SSF- MF/UF- R01 R01 $ per 1.76 to 1.31 to 1.76 to 2.25 to 1.93 to 2.20 to 1,000 2.04 1.60 2.04 3.08 2.75 3.02 gallons $ per acre- 572 to 427 to 572 to 733 to 629 to 717 to foot 666 521 666 1,004 896 984 ' includes the range of disposal alternatives delineated in appendix E. SLOWSAND FILTRATION WITH REVERSE OSMOSIS PILOT STUDY The Southern Arizona Regional Water Management Study(SARWMS) final report (August 2000) provided information on the cost of several prospective water treatment methods. Slowsand(SSF) treatment turned out to have the lowest cost- less than one-fourth the cost of conventional treatment. Because information on the effectiveness of conventional treatment, microfiltration and ultrafiltration is available from other tests, the pilot test in this Study focuses on the effectiveness of slowsand filtration. The pilot test will address the effectiveness with respect to the following questions: 1. How effective is slowsand filtration as a pretreatment to RO? Specifically, does a slowsand system provide adequate removal of particulates that foul RO membranes and reduce RO productivity? 2. Because TOC levels affect levels of disinfection byproducts produced during chlorination or chloramination and because TOC levels may affect biological fouling of RO membranes, what is the TOC removal of slowsand filtration? The SARWMS Report recommended pilot testing on Colorado River water (CAP water) to verify that the cost evaluation was accurate. ow The SARWMS SSF pilot provides an independent (and unbiased) evaluation using the detailed analysis found in the August 2000 final report, Appendix E. Ba' For the SARWMS SSF Pilot, we completed extensive quality control measures in specifying and placing the sand in the filter. gar The SARWMS SSF Pilot continues the successful participation by SARWMS members in seeking Regional approaches for water resource planning by focusing on one of several unanswered issues. vs' The SSF Pilot allows the water providers to develop on staff expertise in the assembly and operation of technically advanced water treatment systems. ow' By participating in this effort, the SARWMS partners have effectively been able to leverage up to $340,000 of Federal dollars provided by the Bureau of Reclamation. ...I tri . .1: . -414 W iit, tri ie >H C [..,,,, w I> ...Ius ka E. liel 0 > ili D -I twit i Ar 'ImmillPIIIIIV- n-- > or. ...S. ....a MS 0 Z .•IIIIIII --I ° < ›, 0 111.. Lt., Cr AMY Clii 11,1 Z.0 0 4111 •- • 0 " IL al „AM 0 1;2 Mt rte: es : _y - siii •go R z i : .. 0" •-- . , 11 ;1 NG1 co es. '-.I PI• 111113 1-, C Li. Ci ex 0 Z V) 'CI eid - s" . 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Iiii a .NC Slowsand filter design/Pilot Comparison (see SARWMS, Table E-2) Design criteria Full scale Pilot Period of operation 24 hours/day 24 hours/day Product flow 40.14 MGD 22 gal/minute or 31,680 gallons/day Hydraulic loading rate 0.112 gpm/ft2 0.112 gpm/ft2 Total filter area 330,450 ft2 or 200 ft2 7.6 acres (16-foot diameter) Number of filters 1 with 4 cells at one 13.38 MGD each Initial height of filter sand bed 3.0 ft 3.0 ft Minimum height of filter sand bed 1.5 ft 1.5 ft Sand effective size, d10 0.27 to 0.33 mm 0.27 to 0.31 mm Sand uniformity coefficient, d60/d101 Less than 2.5 0.67 Height of underdrains, including 1.5 ft 1.5 ft gravel layer Height of supernatant water 5 ft 4.5 ft Freeboard 2ft 0.5ft Total filter basin depth 9.45ft 10ft 1 The ratio of the sieve size through which 60 percent of the sand will pass to the size through which 10 percent will pass. Economic Ba ne t � so Using � Savings frompurchasing, install'i ng, & operating bottled water or home water filtrationst sy ems ® Savings 'ofwater lost with softeners & RO units ® Savings by providing lowNsalinitywater to ALLPP household appliances (fewer repair & replacement costs) 4* Uses less idetergentsoaps and other ® . Car radiator life is extended City of MWD of Item Tucson S . California ReducingGalvanized 0.7 6 1 .1 7 pipes salinity W ater heaters 0.8 1 0 .9 1 Garbage 0 .02 0 .19 from disposals C lothes 0.1 4 0 .84 700 m /�1 washers ,x/1Evaporative 0.1 8 - to 200 m coolers C a r radiators 3 .3 6 - Toilet 0.01 - m echanism s D ishw ashers 0.23 0 .68 Faucets 0.2 8 0 .5 7 Pool 0.1 9 - equip m ent Clothes 0 .38 S �m l thperpzn'� re laceent ,� Detergents 0 .3 6 0 .1 3 i !e-fuu L a w n w ate ring 0.0 8 residence Bottled water 3 .4 6 - H om e filtration 3 .98 0 .08 o t Bottled w ater W ater - 1 .4 0 softeners Total 14.24 5 .98 • ... , • . _ • ,c . .• ' * .asainki • -• U . i,„. •raw. 1:. " • : : • . . , . • :-. I ....,,... : ... . .' . • L.L., . .• .. i '•••:::111 ' .1': . . 1 It ., t.: A. -)... ..) .• a ... ,,, . i:s.,..t. .: v_•. .: . . . .... 1--( . 0.:. • . !.;,... ...a. :. ,........., . • 4:13... VII c).-. .z.. i -t• ..,. ,.,, ...4--1 r. .: • .66 • .--1 . 0. ':. -*lir, • ..g .-• . .4:. 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C y L.U ' m 0 I 44 m 3 cx w 0 ,11-0 c 0 . 1 I gx t"'"1 a Di um u 1 D 0 ° IL ix 1W n 1 u. 1 , I ii,. u: -c� imis in 2 1 Cost Treatment Methods 1.60 1.40 - - - - - _ - .. o - _ _ _ _ _ _ _ _ _ _ _ _ - _ - m _ - _ - _ _ . 1.20 1.11 . - a - - - m c C 0 1.00 a 0) ._ O 0.80 - _- O S060 ;.. ,. ill 0.40 - • - — 0.20 - - - - - - - _ _ - - .r 1.1 0.00 a 1 CT SSF MF/UF CT-RO SSF-RO MF/UF-RO Water Treatment & Distribution System Total Cost CT SSF MF/UF CT-RO' SSF- MF/UF- R01 R01 $ per 1.76 to 1.31 to 1.76 to 2.25 to 1.93 to 2.20 to 1,000 2.04 1.60 2.04 3.08 2.75 3.02 gallons $ per acre- 572 to 427 to 572 to 733 to 629 to 717 to foot 666 521 666 1,004 896 984 1 Includes the range of disposal alternatives delineated in appendix E. SLOWSAND FILTRATION WITH REVERSE OSMOSIS PILOT STUDY The Southern Arizona Regional Water Management Study(SARWMS) final report (August 2000) provided information on the cost of several prospective water treatment methods. Slowsand(S SF) treatment turned out to have the lowest cost- less than one-fourth the cost of conventional treatment. Because information on the effectiveness of conventional treatment, microfiltration and ultrafiltration is available from other tests, the pilot test in this Study focuses on the effectiveness of slowsand filtration. The pilot test will address the effectiveness with respect to the following questions: 1. How effective is slowsand filtration as a pretreatment to RO? Specifically, does a slowsand system provide adequate removal of particulates that foul RO membranes and reduce RO productivity? 2. Because TOC levels affect levels of disinfection byproducts produced during chlorination or chloramination and because TOC levels may affect biological fouling of R0 membranes, what is the TOC removal of slowsand filtration? The SARWMS Report recommended pilot testing on Colorado River water (CAP water) to verify that the cost evaluation was accurate. rtzr The SARWMS SSF pilot provides an independent (and unbiased) evaluation using the detailed analysis found in the August 2000 final report, Appendix E. ow For the SARWMS SSF Pilot, we completed extensive quality control measures in specifying and placing the sand in the filter. IQ' The SARWMS SSF Pilot continues the successful participation by SARWMS members in seeking Regional approaches for water resource planning by focusing on one of several unanswered issues. Fa' The SSF Pilot allows the water providers to develop on staff expertise in the assembly and operation of technically advanced water treatment systems. we By participating in this effort, the SARWMS partners have effectively been able to leverage up to $340,000 of Federal dollars provided by the Bureau of Reclamation. n y ...e . 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Slowsand filter design/Pilot Comparison (see SARWMS, Table E-2) Design criteria Full scale Pilot Period of operation 24 hours/day 24 hours/day Product flow 40.14 MGD 22 gal/minute or 31,680 gallons/day Hydraulic loadingrate 0.112 gpm/ft2 0.112 gpm/ft2 Y Total filter area 330,450 ft2 or 200 ft2 7.6 acres (16-foot diameter) Number of filters 1 with 4 cells at one 13.38 MGD each Initial height of filter sand bed 3.0 ft 3.0 ft Minimum height of filter sand bed 1.5 ft 1.5 ft Sand effective size, d10 0.27 to 0.33 mm 0.27 to 0.31 mm Sand uniformity coefficient, d60/d101 Less than 2.5 0.67 Height of underdrains, including 1.5 ft 1.5 ft gravel layer Height of supernatant water 5 ft 4.5 ft Free board 2 ft 0.5 ft Total filter basin depth 9.45 ft 10 ft 1 The ratio of the sieve size through which 60 percent of the sand will pass to the size through which 10 percent will pass. Economic Benefits of sing Low-Salinity Wa Si Savings frompurchasing, installing, & 9 o eratin bottled water or home operating water filtration systems ® Savings of water lost with softeners & RO units ® Savings by providinlow-salinitywater to ALL household appliances (fewer repair & replacement costs) • Uses less laundrydetergent and other soaps • Car radiator life is extended City of MWD of Item Tucson S . C alifornia ReducingGalvanized 0.7 6 1 .17 • pipes salinity W Ater heaters 0.8 1 0 .9 1 Garbage 0 .02 0 .19 from disposals C lothes 0.1 4 0 .84 700 m /L w ashers Evaporative 0.1 8 - to 200 m coolers C a r radiators 3 .3 6 - Toilet 0.01 - m echanism s D ishw ashers 0.23 0 .68 Faucets 0.28 0 .57 P ool 0.19 - equip m ent C lothes 0.3 8 - :;-,/month per replacement ; � ss D etergents 0 .3 6 0 .13 sin ale-famish. Lawn watering 0.0 8 residence - B ottled water 3 .46 H o rn e filtration 3 .9 8 0 .0 8 of Bottled w ater W ater - 1 .40 softeners Total 14.24 5 .98 ' • . • 0, U • :..: •e+ *ii.-.4%..... ..."-,...iviaiumw......voio- ...!..nsomp,....0 — ..._. ,..- •I I..- : . t.. . , 0: . k::H---------'"l 1 i V-.1 - .. ,. N....z... . . 1......,a, •...1:....i,•,!... 11 . :: A • w. .. . 61 . J , 7; lir 4),.2:4 iw ...0 :.) i) 4,:s ,.::w 1,1:....1.:.:. . gag..• VI • in i *".:,./ I' $ $. i t: I. 0 • H ,..C. . .. E $. 1 1 1...: g 43 t .a ..: •• c 4.-.;:;:. " olk Mr: w .4.,. . HArl 1 ' • 1.1 ....—,,. \ • e . . 0. . • . r, • .. nm :§,0; ....; . . • • o Ill .. i.,..8. ' 40.:•.::00 '. 13' ' D i ..., .:.. , > g • . :„; .„...,,, . . kr. 41Vi la> :T1'.• *is: • l ,- .17) •.i7.1. 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