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HomeMy WebLinkAbout11/05/1991, 3 - ENVIRONMENTAL IMPACT REPORT (EIR) FOR STENNER CANYON WATER TREATMENT PLAN UPGRADE MEETING DATE m��i I�IIIII��Pn � U city of San LUIS OBISPO - COUNCIL AGENDA REPORT ITEM NUMBER b ' FROM: Arnold B. Jonas, Community Development Director PREPARED BY: Glen Matteson, Associate Planner SUBJECT: Environmental Impact Report (EIR) for Stenner Canyon Water Treatment Plan Upgrade CAO RECOMMENDATION Adopt a resolution to certify the. final EIR. DISCUSSION Before approving a project which may significantly affect the environment, the Council must complete environmental review. An initial study on this project, to improve effectiveness and expand capacity at the City's primary water treatment plant in Stenner Canyon, found that energy consumption could be significant, especially in combination with other approved and proposed City utility projects. In May 1991, Council approved consultant services to prepare an EIR focused on energy consumption. The draft EIR was published in July, and the public review period ended September 16. No comments were received from the general public or from 'State agencies. Comments were received from the County Air Pollution Control District and from the City's Public Works Director. None of the comments concerned energy usage or significant, new environmental issues. Responses to comments have been prepared. The EIR concludes that the upgraded plant will use additional energy (mainly electricity) , to treat the same amount of water as the current plant, equivalent to the usage of about 400 households. Staff is recommending that Council determine that this increased energy usage will not be significant, considering overall energy consumption in the City (which contains about 17 , 000 households and many other energy users) . The EIR recommends mitigation measures which will make existing and proposed treatment plant features as efficient as any new water treatment plant in the State producing an equivalent water quality. Separately, cost-effective energy efficiency improvements recommended in the 1989 Newcomb-Anderson audit of other City facilities are being pursued by the energy conservation coordinator in the Public Works Department. While these other measures will help contain City energy usage, they are not considered mitigation for the proposed project since they would be undertaken anyway. Water conservation is perhaps the most effective energy conservation measure for both water treatment and wastewater treatment activities. 3-1 ��� �1111111�P ��d�N crty of san ' s oaispo i COUNCIL AGENDA REPORT FISCAL IMPACTS An energy audit of the existing water treatment plant, conducted to help prepare the EIR, identified 40 conservation measures with modest initial costs, which would save about $28, 500 annually. Any features that would reduce operating costs, but which would substantially increase the construction cost of the upgrade, will be evaluated when Council is asked to approve plans and specifications. None are anticipated. ALTERNATIVES The Council may make findings or require mitigation measures other than those identified in the draft resolution. The Council may continue action'. RECOMMENDATION Adopt a resolution certifying the draft EIR, comments, and responses as adequate for a final EIR. ATTACHMENTS Draft resolution certifying EIR Comments and responses ENCLOSED Draft EIR gmD: STNREIR.WP 3-� RESOLUTION NO. (1991 SERIES) A RESOLUTION OF THE SAN LUIS OBISPO CITY COUNCIL CERTIFYING THE ENVIRONMENTAL IMPACT REPORT FOR THE WATER TREATMENT PLANT UPGRAD4 (ER 34-90) The Council of the City of San Luis Obispo resolves as follows: Findings , 1. The City has published and made available for public review a Draft Environmental Impact Report (EIR) for the proposed upgrade of its water treatment plant, in accordance with the California Environmental Quality Act and the City's Environmental Impact Procedures and Guidelines. 2 . On November 12 , 1991, the City Council conducted a public hearing on the EIR. Actions 1. The Council certifies that the EIR is adequate, provided that it includes the comments, responses, and additional information concerning mitigation and monitoring fully contained in the attached Exhibit A. A Final EIR incorporating Exhibit A is to be published within 60 days, and will be made available to any responsible agency. 2 . The Council determines that there will .be no significant, adverse impacts, since increased energy consumption will be mitigated to an insignificant level. • On motion of seconded by , and on the following roll call vote: AYES: NOES: ABSENT: the foregoing resolution was passed and adopted this day of , 1991. Mayor ATTEST: City Clerk 3-3 Resolution No. (1991 Series) Water treatment EIR .Page 2 APPROVED: City A inistrative Officer r t tt,c �(n�e Community De pment Director gmD: eir-res.wp • Exhibit A STENNER CANYON WATER TREATMENT PLANT EIR COMMENTS AND RESPONSES Following are summaries of comments received, and responses. Numbers. key to topics in the following correspondence. San Luis Obispo County Air Pollution Control District (APCD) 1. More information and an APCD permit will be required for a diesel-powered peaking generator. Response: Use of an on-site diesel-powered generator to replace utility- provided electricity could reduce the City's electricity bills, but not energy consumption. It is not recommended mitigation, though the city may decide to pursue it. If the City pursues this option, additional environmental review will occur and APCD permitting procedures will be followed. A diesel generator will be provided for emergency power only. It will be able to supply chemical feed systems (other than ozone generation), but not full plant operation. Except for tests to assure its readiness, it would be run only when utility power fails.. 2. Air pollution from construction equipment, particularly grading, should be addressed through conditions on building permits for this project. • Response: There will be no expansion or recontouring of the site, which was graded for the original treatment plant construction. However, there will be excavation and minor fill for building foundations: Ozone generator building - cut 700 cubic yards, fill 30 cubic yards; Ozone contact basins - cut 950 cubic yards, fill 70 cubic yards. Construction equipment likely to be used includes skip loaders, dump trucks, back hoes, concrete-mix trucks and concrete pumpers, and compressors for various pneumatic equipment. When the duration of use of this equipment is known, that information will be provided to the APCD for any required review prior to construction. 3. If population growth enabled by the increase in treatment capacity exceeds the projections in the Clean Air Plan, air quality impacts of additional induced growth should be evaluated. 3-5 Water Treatment EIR - Response to Comments 2 Response: The adopted general plan's build-out capacity is about 53,000 people. The nine percent additional capacity enabled by the treatment plant expansion would lead to a total service capacity of about 57,800 people. This capacity would be reached sometime between 2015 and 2020, if water supply and other. resources are adequate. The Clean Air Plan (June 1991 draft) contains two population projection series for San Luis Obispo. The lower series shows a population of 57,465 in the year 2015 and 60,657 in 2020. Therefore, the general plan and water treatment capacities are within the Clean Air Plan growth projections, and no further analysis of air quality impacts due to population growth is required for this project. 4. Address the fate of the ozone not vented to the destruction unit. Response: The ozone contact basin will have several features to contain the ozone gas and to minimize the amount of dissolved ozone in water leaving the contact basin. A. The contact basin will be fully covered. It will be maintained at a negative pressure, so any leak would result in atmospheric air flowing into the basin, rather ozone-rich air flowing out. B. After ozone has been introduced to the water, it will flow slowly through enclosed cells where there is no further ozonation, to allow the ozone (which is unstable in water) to decompose. C. Before the water leaves the contact-basin system, it will flow over a weir to remove most of any remaining ozone. According to Black & Veatch, the engineering firm designing the plant upgrade, "Our experience indicates that facilities designed with these features will operate with very low ozone residuals in the water exiting the basin and [concentrations will] comply with air quality regulations." David F. Romero. Public Works Director 5. The executive summary should clearly state that the plant's capacity is 11-5 mgd, following the 1977 upgrade. Response: Noted. 3-tC2 Water Treatment EIR - Response to Comments 5 Other energy conservation and water conservation measures which the City is pursuing will mitigate energy usage, though they are not listed as mitigation for this project. Monitoring Implementation of the mitigation measures will be monitored by the City's Energy Conservation Coordinator, assisted by the City's Water Division Manager, as construction drawings and specifications for the project are prepared and presented for City Council approval. 3 . 9 Yec\3 AIR POLLUTICuJ CONTROL DISTRICiL COUNTY OF SAN LUIS OBISPO 2156 SIEBBA WAY,SUITE B—SAN LUIS OBISPO,CAI.immu 93401 —(805) 549-5912 5 September 1991 SEP 2 31991 Mr. Glenn Matteson, Associate Planner C"y a,San Vu's oms•- Community Development Department City of San Luis Obispo P.O. Box 8100 San Luis Obispo, CA 93403-8100 SUBJECT: Draft Environmental Impact Report (EIR) for the Stenner Canyon Water Treatment Plan Upgrade Dear Mr. urtogos on; The District has reviewed the information contained in the Draft EIR for the above-mentioned project. The City of San Luis Obispo is proposing to upgrade the Stenner Canyon Water Treatment Plant to provide an ozone-based process in place of the traditional chlorine-based process in order to meet present and future water quality regulations for a capacity of 16 million gallons per day (16 mgd) . In general, the Focused EIR provides a good discussion of the impacts of the increased energy use resulting from the Stenner Canyon Water Treatment Plant and its upgrade. The following comments pertain to sections which the District feels should be expanded further: 1. Section D - Mitigation Measures, Potential Measures in Design and Operation (Page 18) : The section discussing identification of potential energy conservation measures includes the recommendation to study the option of having a diesel-generator operate as a peak-shaving generator. In evaluating the air quality impacts associated with the use of a diesel generator, it is necessary to determine the size of the generator needed (horsepower rating) , and extent of use (hours/day) . In addition, this generator (and other equipment installed at this facility) may be subject to District permitting requirements . The City should contact the APCD Engineering Department for further information regarding the permitting process. 2. Section F - Unavoidable Adverse Impacts (Page 21) : Short-term unavoidable impacts occur as a result of construction traffic and activities; however, it is believed that these potential impacts are minor. 3"/0 reevnetl oaoer G. Matteson . DEIR for Stenner Canyon Water Treatment Plant Page 2 The District has been designated a nonattainment area for the state ozone standard and is required to reduce emissions of nonattainment pollutants (or their precursors) by at least 58 per year until the standards are achieved. State law requires that emissions of nonattainment pollutants countywide will have to be decreased by at least 408 from the 1987 levels in order to meet clean air standards. Pursuant to state law, the District has developed guidelines for air quality impacts from project construction (see attached) . In O accordance with those guidelines, it will be necessary for the City to provide a construction and grading plan identifying the proposed amount of cut and fill required for the project, proposed grading equipment to be used and duration of use. That information should be provided to the District when it becomes available so that APCD construction mitigations may be included as conditions on the building permits. 3. Section I - Growth Inducing Impacts (Page 24) : 'The existing water treatment facility was designed to treat a maximum of 8 mgd. Due to modifications, it has been able to treat up to 11.5 mgd at a lower quality of treatment. The upgraded facility will have the capacity to treat 16 mgd at a relatively high quality of treatment. This increase will not automatically lead to additional growth. The added capacity will raise one of the thresholds which could constrain growth. The correction sheet to the initial study (dated 7-26-91) indicates that the proposed project would establish a treatment capacity level approximately 98 higher than is needed for build-out of the City's adopted General Plan. If the population projections in the General Plan are consistent with those presented in the District's O 1991 Clean Air Plan (CAP) , then the air quality considerations are adequately addressed. However, if treatment capacity and the resultant growth projections exceed that presented in the CAP, the potential air quality impacts associated with growth inducement should be evaluated further. 4. Additional Information: In the letter from David Dixon dated January 8, 1991 a concern was raised regarding the proposed system's ability Oto release greater than 0.09 ppm ozone to the atmosphere. A �- suggestion to redesign the system in order to vent less ozone to the atmosphere was also made. Please address the fate of the ozone not vented to the destruction unit. 3-ll G. Matteson DEIR for Stenner Canyon Water Treatment Plant Page 3 We appreciate the opportunity to provide input into this project. Please contact the District at (805) 549-5912 if you have any questions concerning these comments. Respectfully, LARRY R. ALLEN Senior Air Qu ity Specialist DIANA GOULD Air Quality Specialist, Planning cc: D. Dixon, APCD eir/dsg91/90228c.doc enc. (1) 3-/Z AIR POLLUTI N CONTROL DISTRICT C0UNW OF SAN LUIS OBISPO _. 2156 SmexA WAY,SUrn B -SAN LUIS OBISPO.CALIFORNIA 93401 -(805) 549-5912 MITIGATION GUIDELINES FOR AIR QUALITY IMPACTS FROM CONSTRUCTION Heavy construction generates dust and combustion emissions that may have substantial temporary impacts on local air quality. Building and road construction are the prevalent construction categories with the highest emissions potential. Emissions during the construction of buildings and roads are associated with land clearing, blasting, ground excavation, cut and fill operations, and the construction of the particular facility itself. Emissions vary substantially from day to day depending on the level of activity, the specific type of operation and, for dust, t$e prevailing weather conditions. A large portion of fugitive dust emissions result from equipment traffic over temporary roads at the construction site. Calculation of emissions from construction activities should include peak hour, daily and total construction phase emissions of nitrogen oxides (NOx) , reactive organic gases (ROG) , sulfur dioxide (SO2) , carbon monoxide (CO) and fine particulate matter (PM10) . Sources of emissions primarily include heavy-duty mobile construction equipment, non-vehicular equipment such as compressors and portable generators, and fugitive dust. The appropriate emission factors for off-highway mobile construction equipment (such as bulldozers, scrapers, etc.) and non-vehicular equipment (such as generators) are contained in the federal Environmental Protection Agency publication, Compilation of Air Pollutant Emission Factors. AP-42 (latest edition) . Tables II-7.1 and II-7.2 in volume II of that document list the AP-42 emission factors for construction vehicles. Those tables are provided at the end of this document for your convenience. In calculating emissions from construction equipment, it is important to use the most accurate equipment scenarios possible, including estimates of the number and type of equipment that may be operating simultaneously. If that information is not available , however, it is possible to estimate emissions wirholit knowing the specific cquipment that will used. Although each project will vary, an average of 0. 27 gallons of diesel fuel are burned for each cubic yard of earth moved. Based on that estimate, the following emissions rates would apply: TABLE 1 DIESEL CONSTRUCTION EQUIPMENT EMISSION RATES (Grams Per Cubic Yard of Material Moved) Pollutant G/Cu, Yd. Particulate 2,6 CO 11.2 ROG 5.6 NOx 42.9 Sox 4,9 PM10 1.2 tons/acre of construction activity per month -1- 3-/3 � (SOURCE: Bay Area AQMD: Guidelines for Assessing Impacts of Projects and Plans - November 1985. ) MITIGATION THRESHOLDS Mitigation of construction activities is required when the following emission thresholds are equalled or exceeded: 1. ROG or NOx - Greater than 185 lbs/day requires BACT. - 2.5 - 6.0 tons/quarter requires BACT. - Over 6.0 tons/quarter requires BACT plus further mitigations, including emission offsets. 2. PM10 - 2.5 tons/quarter requires mitigation Using emission estimates from Table 1 and the mitigation thresholds identified above, the following table shows the approximate level of construction activity that would require mitigation for each pollutant of concern: TABLE 2 ROG EMISSIONS AMT. MATERIAL MOVED TONS/OTR. LBS DAY CU. YDS. /OTR, CU, YDS. /DAY 2.5 185 405,080 15,000 6.0 972,776 NOx EMISSIONS AMT. MATERIAL MOVED TONS/OTR, LBS/DAY CU. YDS. /OTR. CU. YDS./DAY 2.5 185 52,884 1950 6.0 126,984 PM10 EMISSIONS Any project with a grading area greater than 2.0 acres will generate 2. 5 tons of PM10 per quarter and will thus require PM10 mitigation measures (All calculations assume working conditions of 8 hours per day, 5 days per week, for a total of 65 days per quarter. ) NOx emissions will Ve the controlling factor in determining the application of control strategies for combustion-related emissions. In the absence of project-specific emission calculations, any project requiring grading of>1950 cubic yards/day or ;iP50,000 cubic yards within a three-month period will need to apply BACT combustion controls. Projects requiring X125,000 cubic yards of grading in a three month period will need to apply BACT plus offsets and/or other mitigation. Applicable mitigation measures are defined- below. 23-�� NOx AND ROG MITIGATION MEASURES The following measures are considered Best Available Control Technology (SACT) for construction equipment: 1. Use of Caterpillar prechamber diesel engines (or equivalent) together with proper maintenance and operation to reduce emissions of oxides of nitrogen (NOx) . 2. Electrify equipment where feasible. 3. Maintain equipment in tune per manufacturer's specifications, except as required in condition 5. 4. Install catalytic converters on gasoline-powered equipment. 5. Implement engine timing retard (four degrees) for diesel-powered equipment. 6. Substitute gasoline-powered for diesel-powered equipment, where feasible. PM-10 MITIGATION MEASURES 1. Reduce the amount of the disturbed area. 2. Use of water trucks or sprinkler systems in sufficient quantities to prevent airborne dust from leaving the site. Increased watering frequency would be required whenever wind speeds exceed 15 mph. 3. All dirt stock-pile areas should be sprayed daily as needed. 4. Permanent dust control measures identified in the approved project revegetation and landscape plans should be implemented as soon as possible following completion of any soil disturbing activities. 5. Exposed ground areas that are planned to be reworked at dates greater than one month after initial grading should be sora with a fast-germinating native grass seed and watered until vegetation is established. 6 . All disturbed soil areas not subject to revegetation should be stabilized using approved chemical soil binders, jute netting, or other methods approved in advance by the APCD. 7. All roadways, driveways, sidewalks, etc. to be paved should be completed as soon as possible. In addition, building pads should be laid as soon as possible after grading unless seeding or soil binders are used. 8. Vehicle speed for all construction vehicles shall not exceed 25 mph on any unpaved surface at the construction site.. -3- 3-15 ACTIVITY MANAGEMENT TL_rfNIOUES 1. Development of a comprehensive construction activity management plan designed to minimize the amount of large construction equipment operating during any given time period. 2. Scheduling of construction truck trips during non-peak hours to reduce peak hour emissions. 3. Limiting the length of the construction work-day period, if necessary. 4. Phasing of construction activities , if appropriate. ®eir®dsg®cetsum dsg®lra 1-4-91 -4- 3-1� Table 11 -7 . 3 r-miss:on Factors Cor Heavy-Duty . Diesel -Powered Construction Equipment° it Emission Factor Rating: C Track-type wheeled wheeled Motor roloutant tractor tractor dozer° Scraperrq ader CARBON MONOXIDE o/hr 157.01 1622 . 77 568. 19 68 .46 lb/hr 0.346 3. 59 1. 257 0. 151 9/kWh 2.88 9.84 3 . 28 2 .06 g/hphr - _2. 15 7 . 34 2 .45 1.54 kg/103 liter 9.4 32 . 19 10. 16 6.55 lb/103 qal 78.5 268.5 1. 84. 6 54.65 EXHAUST HYDROCARBONS g/hr 55.06 85.26 128. 15 18.07 lb/hr 0. 121 0. 188 0. 282 0.040 g/kWh 1.01 2.36 0. 74 0.48 g/hphr 0.75 1.76 0. 55 0. 36 k.g/103 liter 3.31 7 .74 2. 28 1.53 lb/103 qal 27.6 64.6 19.0 12.73 NITROGEN OXIDES (NO, as N01 ) g/hr 570.70 575.84 1740.74 324 .43 lbihr 1. 26 1.269 . 3 . 840 0.713 9/kWh 10.47 15.96 10.00 9. 57 g/hphr 7.81 11.91 7 .46 7 . 14 kg%ld liter 34.16 52.35 30.99 30.41 lb/103 qal 28A .92 436.67 258. 6 253.84 ALDEHYDES (RCHO as HCHO) g/hr 12 .4 13. 5 29.5 65. 5. 54 lb/hr 0.027 0.030 0.065 0. 143 0.012 g/kWh 0.228 0. 378 0.215 0. 375 0. 162 g/hphr 0. 170 0. 282 0. 160 0. 280 0. 121 kg/103 liter 0.745 1. 23 0.690 1 . 16 0. 517 1b%103 aal 6 . 22_ 10. 3 5.76 9. 69 4 . 31 SULFUR OXIDES (SC. as SO, (;/'r,. 62 . 3 30. 9 158. 210 . 39 .0 1b/`.; 0. 137 0.090 0. 348 0.463 0.056 g 'vWh 1 . 1; 1. 14 l. It. 1 . 21 1 . 17 a/".;hr 0.851 0. 351 0.817 0. 901 0. 874 lir.c- 3 .'3 3 . 73 3 . 7; 3 . 74 3 . 73 31 :.1 31 . 1 31 . 2 31. 2 31. 1 _ - ----- 50.7 131 . 5 75. 184 . 27 . 7 0. 112 0. 136 0. 165 0.406 0.061 0. 928 1 . 70 0 . 551 1 . 06 0 . 83E y,...:.nhr 0 . ;;2 1 . 27 0 . 411 0. 789 0. o25 ,.) • : i'.?: 3 .03 5. 57 1 . 77 3 . 27 2 . 66 25. 3 b... 5. _...14 .8 27 . 3 22 _2 . -.efe: h YC/CO,4O. emissions , and eCe en: 1 arc _' Cc: SSiOnS. -he - !.,-lied in the nff II-7-4 ��/ Table II-7. 1 ( C'd) Emission Factors for He -Duty Diesel-Powered Construction Equipmenta Emission Factor Rating: C Off- Wheeled Tracktype Highway Miscel- Pollutant loader loader truck° Roller laneous CARBON MONOXIDE g/hr 259.58. 91. 15 816.81 137.97 306.37 lb/hr 0.572 0.201 1.794 0. 304 0:675 9/kWh 3.63 3.03 4.70 _8.08 6. 16 g/hphr 1 2.711 2.26 --- 2.28- - 6.034.60_ kg/10 liter 14.73 22.64 18.41 lb/103 gal 98_66 82.85 123.46 188.37 153. 51 EXHAUST HYDROCARBONS 9/hr 113.17 44.55 86.84 30.58 69. 35 lb/hr 0.25 0.098 0.192 0.067 0. 152 9/kWh _ 1.59 1.49 0.50 1.30 1.35 gAphr 0.97 1.11 0..37_- _ 0..97 1.01_ g-71-003 (ite 5.17 4.85 1.58 3.60 4.04 lb/103 qal 43.16 40. 55 13.16 30.09 33.70 NITROGEN OXIDES (N0: as NOz) g/hr 858.19 375. 22 1889.16 392.90 767. 30 lb/hr 1.89 0. 827 4.166 0.862 1.691 g/kWh 11.81 12.46_ 10_92-_17.49 9/hphr - - - 8.81 _ 9. 30 8.15_____ 13_05 11.0.1 . kq/10� liter 38.5 40.78 34.29 48.49 44. 10 lb/10' qal 321.23 339. 82 286.10 404 . 51 368.01 ALDEHYDES (RCHO as HCHO) g/hr 18.8 4.00 51.0 7.43 13.9 lb/hr 0.041 0.009 0. 112 0.016 0.031 9/kWh 0.264 0. 134 0:295 0. 263 0. 272 9/hphr 0.197 0. 100 0.220 0. 196 0. 203 kg/103 liter 0.859 0.439 0.928 0.731 0.813 lb/10' qal 7.17 3.66 7 .74 6. 10 6.78 SULFUR OXIDES (SO. as SOz) g/hr 82.5 34.4 206. 30.5 64 .7 lb/hr 0.182 0.076 0.454 0.067 0. 143 g/kWh 1...1,5 1. 14 1.19 _ ._ _ 1. 34 1. 2r. q/h hr_ 0.857 __ . 0.,853 0.887. .. .__._1_0.0...-.....-.0..9.32- kg 0 liter 3.74 3.74 3.74 3.73 3 .73 lb/10' cal 31.2 31. 2 31.2 31. 1 31 . 1 PARTICULATE 9/hr 77.9 26.4 116. 22 .7 63 . 2 lb/hr 0.172 0. 058 0.256 0.050 0. 139 9/kWh _--. 1.08 0. 878 0.673 1.04 1 . 21 /hphr 0.805 0. 6550.502 0. 778 0.902 _ -- - - - kg/10' liter 3.51 2. 88 2. 12 2.90 •3 .61 lb/10'ga1 29. 3 24 . 0 17.7 24. 2 30. 1 a References 3 and 4 for the HC/CO/NO, emissions and references 1 and 2 for other emissions. The off-highway truck category incudes HC/CO/NO„ emissions fron,-the wheeled dozer. 11-7-5 3-/S Table II -7 . . fission Factors for Heavy-Dut; gasoline-Powered Construction Equipment° Emission Factor Rating: C Wheeled Motor Wheeled Miscel- Pollutant tractorrq ader loader Roller laneous CARBON MONOXIDE 9/hr 4320. 5490. 7060. 6080. 7720. lb/hr 9.52 12 . 1 15.6 13 .4 17 .0 g/kWh 190. 251. 219. 271 . 2.66. g/hphr 142. 187 . 163. 202 198. kq/10' liter 389. 469. 435. 460. 475. lb/10' gal 3250. 3910. 3630. 3840. 3960. EXHAUST HYDROCARBONS g/hr 164. 186. 241. 277 . 254. lb/hr 0.362 0.410 0.531 0.611 0. 560 q/kWh 7.16 8.48 7.46 12 .40 8.70 g/hphr 5.34 6. 32 5.56 9. 25 6.49 kg/10' liter 14.6 15.8 14. 9 21. 1 15. 6 lb/10' gal 122. 132. 124. 176. 130. EVAPORATIVE HYDROCARBONS° 9/hr 30.9 30.0 29.7 28.2 25.4 lb/hr 0.0681 0. 0661 0.0655 0.0622 0.0560 CRANKCASE HYDROCARBONS° g/hr 32.6 37 . 1 48.2 55.5 50.7 lb/hr 0.0719 0.0818 0.106 0. 122 0. 112 NITROGEN OXIDES (NO. as NO2 ) g/hr 195. 145. 235. 164 . 187 . lb/hr 0.430 0. 320 0.518 0. 362 0.412 g/kWh 8. 54 6. 57 7 .27 7.08 6.48 g/hphr 6.37 4 . 90 5.42 5. 28 4 .79 kg/10' liter 17 .5 12 . 2 14 . 5 12.0 11 . 5 lb/10' qal 146. 102__ 121._ 100. 95. 8 ALDEHYDES (RCHO as HCHO) g/hr 7 .97 8 . 80 9.65 7 . 57 9.00 lb/hr 0.0176 0.0194 0.0213 O.C167 0.0198 0.0198 g/kAh 0. 341 0 . 386 0. 298 0. 34"s• 0. 298 g/hphr 0. 254 0. 288 0. 222 0. 256 0. 222 kg/10' liter 0.697 0.721 0.593 0. 582 0. 532 lb/10' gal 5. 82 6. 02 4 .95 _ 4 . 86 4 .44 SULFUR OXIDES (sox as SO2 ) g/hr 7 .03 7 . 59 10.6 8. 38 10. 6 lb/hr 0.0155 0.0167 0.0234 0.0185 0. 0234 g/kWh 0. 304 0 . 341 0. 319 0. 373 0. 354 g/hphr 0. 227 0. 25; 0. 239 0.. 278 0. 264 kg/10' liter 0.623 0. 636 O. 536 0. 633 0 . 633 lb/101 gal 5.20 _5 . 31 5. 31 5. 28 _ 5. 28 11_7_6 3_�9 ����������►�iifl��illllllllillllli@11°""°►i III city osAn tuis oBispo Noffimm 955 Morro Street • San Luis Obispo, CA 93401 August 5, 1991 MEMORANDUM TO: Glen Matteson, Community Development Department FROM: David F. Romero, Public Works Director SUBJECT: Stenner Canyon EIR Although I have no involvement in the proposed modification and expansion of the Water Treatment Plant, I am quite familiar with the history. I submit the following suggestions for changes in the EIR. Executive Summary, first paragraph I believe it should be made clear in the executive summary that Othe 1977 upgrade to the plant provided a treatment capacity of 11. 5 MGD. This was made clear in the body of the report but not corrected in the executive summary. In the initial study of environmental impact, there was a two paragraph correction made to a discussion regarding population growth. I question a couple of statements within both the initial study and the correction. I do not believe that water treatment is really a bonafide "threshold which now constrains growth" . Our current process treats something in the magnitude of 8 MGD, with an 11.5 MGD treatment capacity for emergency or peak periods. Under current operations, this does not constrain growth in any way. In addition, it is relatively easy to increase the capacity should this be seen as a constraint on growth. The second paragraph of both the initial study and the correction imply that as of the year 2015 the City will be built out and growth will cease. Can anyone really believe that 2015 is a Omagic year when growth would or could be stopped? I believe that 7 year is just a planning year to give us direction for upgrading City facilities. In actuality the proposed expansion of the Water Treatment facilities will probably be in operation in 1993 , thus giving only a 22 year increment for this improvement. This is a relatively short service period for a major plant upgrade. ' c: Bill Hetland growth/dfrr#31 3-zO STATE OF CALIFORNIA PETE WILSON, Governor GOVERNOR'S OFFICE OF PLANNING AND RESEARCH 1400 TENTH STREET ' "'CRAMENTO,CA 95814 Sep 16, 1991 $EQ 1 9199► o1 San Lu+s OVE-" GLEN MATTESON - CITY OF SAN LUIS OBISPO 990 PALM STREET (BOX 8100) SAN LUIS OBISPO, CA 93403-8100 . Subject: STENNER CANYON WATER TREATMENT PLANT UPGRADE SCH # 91081011 Dear GLEN MATTESON: The State Clearinghouse submitted the above named environmental document to selected state agencies for review. The review period is closed and none of the state agencies have comments. This letter acknowledges that you have complied with the State Clearinghouse review requirements for draft environmental documents, pursuant to. the California Environmental Quality Act. Please call Tom Loftus at (916) 445-0613 if you have any questions regarding the environmental review process: When contacting the Clearinghouse in this matter, please use the eight-digit State Clearinghouse number so that we may respond promptly. Sincerely, David C. Nunenkamp Deputy Director, Permit Assistance Notice of Completion Appendix F}fadto:SlaneClwnaghouse•1400TcooSueaL memo•C4 95814 916/445-0613ProJeetTltlos 5ternzr Can on Water fitment Plant Upgrade SCH:03:� Lead AleocY: City of San Luis Obispo Cont�Pe. , Glen t4atteson Seen Addrar 990 Palm Street (PO lox 8100) Phone 805 549-7165 Gtr: San i 'e n�icgo 93403-8100 Zip: County- ----------------------------------------- ounty. can � iiie Obispo PrejeotLoeadps --— ------------------------------ County. -San I'li c Q i Dc Cuy/Nso Commmtity San Luis Obispo Cross steeera: Hi Chway 1 and Stenner Canyon Road .averse's Patcel No. Tout Ate: n.a. Section: 10 Top, 30S Range 12E Base:MOSM Widbm'.M,ls Sum Hwy S.- 1 Waoesaye Stenner Creek Ate¢ ^-a- SPTCO Rdr Schools: a O y NOp CEO&- ❑❑8017 Cons ❑s ay, NEPA: ❑NOI OtherC]EDl(Prior SCH Nos ❑Joint Doamenn aDDs�Dec ❑ O Drat EM O oNvFinal DR+mtnu ❑FONSi ----------------------------------------- - -- Local Actloerype - —_— �---------- ❑Gena)Roo Updaa ❑Slow,&Plat r�-General Plum ❑M r2 C esel Plan E3, 0M. Plan Q � ❑ Anneauum L Ceao®min Plan 13De planned Unit rebpmen, ❑use Penns ❑ Redevelopment [3 Sim Plancontai permit ❑Land Diviemt(Subdivlsba Otho3,,e1l�r. Panod Map.Trap Map.sea) -'Foe Davellopeated Types ❑ ReethessuL Univ Acaa _ ❑ OQics: S94L=AonW+na Fadi u : Type Yh vn t.-}v a•..m&MGD f 6 ❑ COmmeeak s9/►• Acer ❑Trattsporut� Type Ml,d,neiaL S9ft- Aac F vbveQ ❑ MiRM& Mind Educ conal E-111,1eyea ❑ Pover. r ve.77: Retreacmw ❑Wasm Truanent T;P, wen:� Cl Hazardous Wute:Type —rl w. Projoat[sues olacussood in Doeumeed ------- ---- C] A=MwNlsud C]Flood Pldtt/Floodbtg 13 SclsooWU,tivenitia •�sr'I W ❑Foaest LandrFuv Hamed ❑Septic Spaces 11 WNW Quaa9' ❑ [3Gaob•:'1e_:m - ❑Sawa�1' ❑Ware SWNYremmdraos 12 coa"_Arclsociopol ❑ Afmmsts ❑ Wildlife poiot ❑ �RdAbsoepoes ❑popdau Baloee ❑Solid Waste NO= 0 sadB ❑ WildH[a g . Eooeomie/loba ❑ ❑ oaicMazodom a Grawth ❑ Aacal ❑ BrR�obn/Parb ❑❑ Veoeuoonottculauon ❑eumWauve Effeeu *(Other =•/20'•ek V ------ .7 Peraesst Lard llse/ZoMegfGeeerd Plea Use ----------- Public facility Project Dsoeripwon ---_--- --- -T-77 �.: Upgrade treatment process with ozonation and expand cm m 11.° to 16 million gallons per day, for capacity fro the city's main rater treatment plant. I !�I,�t'y �•a t .EARINC•HOUSE OONTACT: Ruse colllau t (916) 445-0617 ' 8 „ . air sir otT atrr ATE REVIEW DLGANt Resources Stets/Conaumer Svcs ' s :PT REV TO ACEMM �. ENCY REV TO SCH : 12Bd �conwr�etlon-&Fish came CA Yuts Hgmt Bd _ i X COMPLIANCE t _� GS R I cO — y _ t--Vtr Rights YD/APCDI (Resources,_/ ) _ -&DyR �Re6• VQCB f n• Wcalrsnt /�� Roar Co® State Lands Comm t• Sen •a• sent b /��n MEETING AGENDA DATE w�Z-6-11 ITEM # , Draft Environmental Impact Report on Stenner Canyon Water Treatment Plant Upgrade for City of San Luis Obispo P.O. Box 8100 San Luis Obispo, California 93403 by Technical Analysis Corporation 282 Second Street, Third Floor San Francisco, California 94105 July 25, 1991 List of Acronyms and Abbreviations B&V . . . . . . . . . . Black and Veatch BLCC . . . . . . . . . Building Life Cycle Cost CEQA . . . . . . . . . California Environmental Quality Act EIR . . . . . . . . . . Environmental Impact Report ft2 . . . . . . . . . . . square feet gpm . . . . . . . . . . gallons per minute kW . . . . . . . . . . . kilowatt kWh . . . . . . . . . . kilowatt -hour 1 . . . . . . . . . . . . liter lb . . . . . . . . . . pound LCC . . . . . . . . . . Life Cycle Cost mg . . . . . . . . . . . milligram Mgal . . . . . . . . . . Mega gallons, million gallons mgd . . . . . . . . . . million gallons per day MW . . . . . . . . . . Megawatt PG&E . . . . . . . . . Pacific Gas & Electric SLO . . . . . . . . . . The City of San Luis Obispo TAC . . . . . . . . . . Technical Analysis Corporation Table of Contents Executive Summary Introduction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1 Environmental Procedures and Intended Use of the EIR . . . . . . . . . . . . . 1 Initial Study and Focused EIR . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1 A. Project Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2 1. Upgrades in Equipment and Processes . . . . . . . . . . . . . . . . . . . . . . . 7 2. Fuel Type and End Use . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8 3. Energy Conservation Equipment and Design . . . . . . . . . . . . . . . . . . . 8 4. Initial and Life Cycle Costs . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 9 B. Environmental Setting . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 10 C. Environmental Impacts . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11 1. Energy Requirements and Efficiencies . . . . . . . . . . . . . . . . . . . . . . 11 2. Local and Regional Effects . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12 3. Peak and Base Loads . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12 4. Comparison to Existing Standards . . . . . . . . . . . . . . . . . . . . . . . . 15 5. Effects on Energy Resources . . . . . . . . . . . . . . . . . . . . . . . . . . . . 15 6. Transportation Energy . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16 D. Mitigation Measures . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 17 1. Potential Measures in Design and Operation . . . . . . . . . . . . . . . . . . 17 2. Potential Measures of Siting, Orientation . . . . . . . . . . . . . . . . . . . . 19 3. Potential for Reducing Peak Demand . . . . . . . . . . . . . . . . . . . . . . . 19 4. Alternate Fuels . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 5. Recycling . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 E. Alternatives . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 20 F. Unavoidable Adverse Effects . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 21 G. Irreversible Commitment of Resources . . . . . . . . . . . . . . . . . . . . . . . 22 H. Short-term Gains vs. Long-Term Impacts . . . . . . . . . . . . . . . . . . . . . 23 I. Growth Inducing Effects . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 24 List of Figures Figure 1 Regional Setting . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3 Figure 2 Plant Vicinity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4 Figure 3 Plant Layout and Proposed Changes . . . . . . . . . . . . . . . . . . . . . . . . . . 5 Figure 4 Schematic Flow Diagram . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6 Figure 5 Monthly Water Demand for the City of San Luis Obispo . . . . . . . . . . . . 13 Figure 6 Monthly Energy Usage of the Stenner Canyon Facility . . . . . . . . . . . . . 14 Figure 7 Monthly Energy Cost for the Stenner Canyon Facility . . . . . . . . . . . . . . 14 List of Thbles Table . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11 List of Attachments Attachment 1. Initial SWdy of Environmental Im=tt(City of San Luis Obispo, December 1990, Updated January 15, 1991). Attachment 2. Letter from Ronald E. Henderson, Black & Veatch, to David Dietrich, Technical Analysis Corporation, dated June 25, 1991, one attachment. Attachment 3. Life Cycle Cost Program BLCC 3.0 Summary. Attachment 4. Nomogram for Converting mgd to Acre-Feet per year. Executive Summar The City of San Luis Obispo provides water service to businesses, agencies, Cal Poly, and about 42,000 residents. The existing water treatment plant in Stenner Canyon was built in 1963 and was designed to treat about eight million gallons per day (8 mgd, equivalent to about 9,000 acre-ftlyr). At times of peak demand, the plant has treated water at the rate of up to 11.5 mgd, The City of San Luis Obispo has proposed to upgrade the facility to provide an ozone-based process in place of the traditional chlorine-based process in order to meet present and future water quality regulations for a capacity of sixteen million gallons per day (16 mgd, or about 18,000 acre-ftlyr). An Initial Study of Environmental Impact on the proposed upgrade to the Stenner Canyon Water Treatment Plant reviewed sixteen potential impacts of the proposed upgrade and determined that the only impact to warrant an Environmental Impact Report was the increased energy use resulting from the upgrade. Technical Analysis Corporation (TAC) was contracted by the City of San Luis Obispo to prepare a Focused Environmental Impact Report on the energy use of the water treatment plant and its proposed upgrade. Because the energy efficiency of the plant is dependent on the volume of water treated per day, we have evaluated the energy use of both the existing and the upgraded plant at a specific rate of water treatment. Although the future supply and demand of water are largely indeterminate, a volume rate of treatment of 8 mgd was chosen as a comparison point because it is very close to the level of pre-drought water treatment at Stenner Canyon. At a water treatment rate of 8 mgd, the existing plant consumes approximately 1.2 million kilowatt hours (kWh) of electricity per year. At that same rate of water treatment, the upgraded plant is expected to use approximately 3.7 million kWh per year. This is approximately a 210% increase in energy use. An average single family residential customer in San Luis Obispo uses about 6,300 kWh of electricity per year. The increased energy use of the upgraded plant is therefore equivalent to the electrical usage of about 400 households. The overall energy use of the upgraded plant will be equivalent to that of about 590 single-family dwellings. Under contract to San Luis Obispo, Technical Analysis Corporation carried out an energy audit of the pre-upgrade and post-upgrade facility, and presented recommendations to the City in a formal report. These recommendations would reduce the energy costs of the existing plant by about$28,500 per year and would reduce those of the upgraded plant by a larger amount. Introduction Envirommental Procedures and Intended Use of the EIR The California Environmental Quality Act (CEQA) requires the city to prepare an environmental impact report (EIR) when it considers an action that could significantly affect the environment. The purpose of an EIR is to help the parties understand the consequences of the action, to consider possible alternatives, and to include features that will nuinhimize harmful effects. Actions of the City of San Luis Obispo that are subject to this environmental review requirement include approving public projects such as the Stenner Canyon-water treatment plant upgrade. Initial Study and Focused EIR The Initial Study of Environments Impar (City of San Luis Obispo, December 1990, Updated January .15, 1991, Attachment 1) reviewed sixteen potential impacts. The conclusions of the Initial Study were that, with the exception of energy/resource use, none of the issues resulted in significant impacts requiring further evaluation in an EIR. The initial study described increased energy use as an apparently "significant impact for which no mitigation is available". To ensure that all practical mitigation measures were evaluated, the City of San Luis Obispo contracted with Technical Analysis Corporation for a technical energy audit. The purpose of this audit was to provide mitigation in the form of energy conservation both at the existing plant and in the design of the upgraded plant. The City of San Luis Obispo also contracted with TAC to prepare a focused EIR. This document was written in strict accordance with the content and format requirements of the California Environmental Quality Act (CEQA Law and Guidelines, January 1984, Appendix F). It addresses only that item identified in the Initial Study as requiring further evaluation, namely, energy/resource use. The report that follows is the Draft EIR which is open to public comment. Following the t;ompletion of the comment period, TAC will take all comments into account before revising this report It will then be published as the Final Environmental Impact Report for the proposed upgrade to the Stenner Canyon Water Treatment Plant. 1 A. Project Description - The City of San Luis Obispo proposes to modify treatment processes and capacity at its existing water treatment plant in Stenner Canyon north of the city. Figure 1 shows the regional setting and Figure 2 shows the plant vicinity. Figure 3 shows the plant layout and proposed changes. Figure 4 shows a schematic flow diagram. The changes are intended to meet anticipated stricter requirements for drinking water quality. The plant treats water from Salinas Dam (Santa Margarita Reservoir) and Whale Rock Reservoir. Salinas Dam can store about 23,300 acre-feet of waterl and provides a safe annual yield of 4,800 acre-feet. Whale Rock Reservoir can store about 40,660 acre-feet of water and has a safe annual yield of about 4,400 acre-feet (4 mgd), of which the City is entitled to 2,057 acre-feet(1.8 mgd). These two sources combined can provide enough water to supply the needs of 20 to 27 thousand single-family homes. The quality of the water from the two sources differs, and seasonal variations are also usual. Groundwater from wells is treated at smaller package units close to the wells and not at the main plant. The monthly aggregate demand for water is illustrated in Figure 5 (see section C.3). 1 An acre-foot of water would cover one acre to a depth of one foot(about 326,000 gallons). One acre-foot of water will supply the needs of three to four single-family homes for one year. 2 �o u v, u 0.' H 0 ' c is 0 a O . H 0 o Ju .. V e7 a C U 3 e7 A m s e n G c ■ U C u F 011 A .. � > n 1 o u m o A U 0 0 "q DID cp m a m a s r v 3 m � u N bll -A Gy 3 Figure .2 . 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P+� _ � �h: '�1r �i •�,..N ^wTL•^r���. .i 41 a . y r.'4• 'J' ..W'.l 1 i b .a,_ f ice. ,Y . : :• O i..i:_ � •pr ^ � '�4".f,�"�' .a'R - 171 O _ ' ,�..�.�,r•� •yam ':;m,�.t.t�. ,y .Eta - _ - t�-..,, ted.�ri� ,•^��.'. 7•.:v�, ..'. pp r. y�+";"cae+ �rvYa' a ' b1 Wit- - -�by Ev JS�� •� .E.:+-•j .w { ��V r+� �r .„a�2. r�� �1 Ll � " �: .^E a r -..�}., pc ya..n „S-+�'1"ze 1 . jYl•+�. r �r, , [r .,,+� :wee: .,.• .f,' ° `"�t',s'�y a�'r$�i�.oi ria .'rn � s:i v .+s ,'P'?�. L'. a'��•:t'� '+ 7 �~ ,r'C.°f�,.�.�fv `tea- 'xr 1J 4`T. S �Tegf'a: �'tii'r t.,n;.; .{ "ail 04. . • �. '.'{` i, l;�i�'F..�J+7-�5.�1"{'-i � l .� f� f vr•�. O V O O 0 O �i W o N2 o � 30000 W 8 w ON ro a 3 P4 ro e ti � ti z x b G4 6�L 2 N ti 0 vi 3 fRQAI SACIIWLS fXOAI Wl'14Lf fnOCX 6 1. Upgrades in Equipment and Processes Some proposed changes were evaluated in the Environmental Impact Reoort for the Water Management Element and Water Management Plan (City of San Luis Obispo, February 1987). That EIR concluded that the previously proposed changes would have no impacts and could be considered "categorically exempt," since they would be changes to an existing facility with no substantial expansion of capacity. Additional changes are now proposed. These are: a. Use ozone rather than chlorine as the primary disinfectant. Equipment includes ozone generators and an ozone contact basin. (Improve water quality.) b. Provide a two-story, 7,000-fr building to house the ozone generators, new chemical feed systems, control room, and additional office space. Eliminate a smaller existing building. c. Replace the initial flash mixing facilities with a larger, two-stage facility. (Improve introduction of chemicals to raw water.) d. Replace the flocculation equipment in the existing basin. (Improve particle aggregation and settling.) e. Replace filter media and repair drains and outflow pipe. (Improve effective- ness of filters and filter backwashing.) L Add a tank and pumps. (Reduce the time between backwashing cycles.) g. Modify equipment and flow path for recycling filter backwash water. (Improve accessibility, improve water quality.) h. Use liquid sodium hypochlorite (bleach) rather than chlorine gas for residual disinfection. (Improves safety on-site and water quality.) i. Provide standby metering pumps for each of several chemical feed systems. (Improve reliability.) j. . Upgrade electrical systems, replacing 208-Volt service with 120- and 480- . Volt services. (Improve safety, reliability.) k. Provide new controls for new and existing equipment. (Improve process control.) 7 1. Remodel the existing laboratory and office. (Improve ability to monitor performance.) 2. Fuel Type and End Use Electricity will be virtually the only source of energy during normal operations. An emergency diesel generator is included to provide for orderly shutdown of the plant in the case of a loss of off-site power, and will use fuel only during regular maintenance and testing, or in the event of a power failure. Electrical resistance heating is currently used for space heating at the plant, but is not allowed-under California code Title 24. Since natural gas is not available at the site, space heating will be provided by propane fueled furnaces. 3. Energy Conservation Equipment and Design The architect/engineering firm of Black & Veatch (B&V) has designed the plant upgrade under contract to San Luis Obispo. B&V incorporated energy conservation into the design and described these measures in a letter, Attachment 2, which is summarized here. Reduced voltage starters are specified for all motors 75 horsepower and larger. Power factor correction capacitors are specified for all motors 25 horsepower and larger. High efficiency motors are specified with all equipment in Division 11 of the specification. Variable Frequency Drives have been specified on six small motors for the purpose of process control; these will conserve a small amount of energy. Electrical interlocks are specified to prevent the simultaneous operation of two service water pumps and of two air backwash blowers. Lighting has been designed to meet or exceed Title 24. Administrative areas include a tandem wired system. The present electrical resistance heating will be replaced by two propane fueled furnaces (Reznor CRPB400 and Reznor CRPB250), one in each building. The air preparation system-provides cool, dry air to increase ozone generator efficiency. Rotary lobe compressors, a type with high efficiency, were specified 8 for the system. Multiple compressors (3 x 50% of capacity)2 were selected to increase efficiency at partial load. Ozone contact basins are deep and will have fine bubble diffusers to achieve a transfer efficiency of 95%. To destroy ozone not transferred to the water,catalytic units are provided,a more efficient type than thermal units. 4. Initial and Life Cycle Casts The initial capital cost of the upgrade, $8,685,000 is taken from the B&V Pilot Plant Study for Alternative 50B. Energy and power requirements for the plant were based on assumptions of processing eight million gallons per day, roughly the pre-drought demand of the city of San Luis Obispo. For 30 years of ozone plant and auxiliaries operation, from start of construction in 1991, startup in 1993, and operation through 2020, the life cycle cost (LCC) of the encgy used is calculated to be $3,921,804 (in 1991 dollars). Nominal amounts were included for maintenance and replacements. Non-ozone opera- tional costs would be incurred regardless of the upgrade and have been omitted from our calculations. These calculations were performed with the National Institute of Standards and Technology code BLCC 3.04,Type 5 Generic LCC without tax analysis as appropriate for state and local governments. The life cycle cost is thus about $12,463,000 (in 1991 dollars) in total, equivalent to $811,000 annually from 1991 to 2020. Any 30-year financial calculation, such as the one described above, is subject to significant assumptions. Assumptions and results are documented in the TAC workpapers, which are available from Technical Analysis Corporation upon request. 2 Telecon, W. McCullough, B&V, to D.Dietrich, TAC,July 8, 1991. 3 Black&Veatch, City of S „a T n;c Obi=Water Treatment Plant Modifications jnd Ozone Pilot Stud, Final Report,June 1990,p. 27� 4 Building Life Cycle Cost Program, Version 3.0, U.S. Dept. of Commerce, National Institute of Standards and Technology, Computing and Applied Mathematics Laboratory, Office of Applied Economics, Gaithersburg, MD,January 1991. 9 B. Environmental Setting The environmental setting in this section refers to the existing energy supplies in the San Luis Obispo region and locality. The water treatment plant gets its electricity from the PG&E electrical network which carries approximately 5000 MW of power. This network is supplied by a mixture of electrical generating stations controlled by PG&E's network dispatcher. The generating stations that supply the network generate electricity from a variety of sources including nuclear, natural gas, oil, hydroelectric and geothermal. The upgrade in the Sterner Canyon water treatment plant will result in an increase in energy use that will have an insignificant impact on PG&E's electrical network. 10 C. Environmental Impacts This section discusses the consequences of the plant design and operation in terms of energy consumption. 1. Energy Requirements and Efficiencies The following table summarizes the overall power consumption of the proposed Stenner Canyon ozone-based water treatment plant. The data were provided by Black & Veatch based on the design that B&V will use to request bids for the equipment to be purchased. Table 1 Projected Power Consumption and Relevant Information for Upgraded Plant Demand Half Full Load Type Load Load Water Treated (mgd) 8 16 continuous Ozone (lb/day) 250 500 continuous Compressors (kW) 41 82 continuous Generators (kW) 77 154 continuous Off-Gas Equipment(kW) 3 3 continuous 65 hp Svc Water Pumps 54 54 continuous 150 hp Process Blowers 124 124 intermittent Max. connected load (kW) 940 arithmetical Max. plant demand (kW) 840 intermittent Avg. plant demand (kW) 420 continuous The proposed interior lighting consists primarily of standard 4 ft. fluorescent lights. The outdoor lighting consists of high pressure sodium fixtures. Overall the currently specified lighting will draw approximately 7.8 kW. 11 - Two air conditioning units are specified in the upgrade (Payne 584ANO30040 and Payne 580BPV0480074), one for each building. Two furnaces are specified (Reznor CRPB400 and Reznor CRPB250), one for each building. These are propane fueled. Currently chlorine is shipped to the plant in loads of 10,000 pounds and used as a disinfectant. Energy is expended during its collection, compression, storage, and delivery to SLO. This hidden energy use is approximately 1.42 kWh per pound of chlorine or about 321 kWh per day(at 8 mgd treatment). The upgraded plant,by using ozone produced on site instead of importing chlorine, avoids these indirect energy expenditures. 2. Local and Regional Effects All electricity is supplied by PG&E; this increase in power demanded will not significantly affect their operation. There will therefore be no significant local or regional effects in terms of energy resources. 3. Peak and Base Loads The existing facility used 1,207,179 kWh on site during the year 1987 to process a volume of 8,400 acre-feet (about 7.5 mgd). To process that same amount, the upgraded facility would consume approximately 3,440,000 kWh over the course of one year. Estimates of average water demand for treated water by the completion of this proposed upgrade are 8 mgd, dependent on drought forecasts and continued water conservation estimates. The treatment of this throughput by the upgraded plant would consume an estimated 3,670,000 kWh yearly. Figure 5 presents the historical demand for water over the past five years. This period was selected in order to show the pre-drought demand and the subsequent effects of water conservation. Currently average demand is approximately 4 mgd with a peak demand of 4.5 mgd, as compared to the pre-drought values of 7 mgd and 9.5 mgd respectively. Note that this is total water demand, which, since July 1989, has been satisfied by filtered and chlorinated groundwater in addition to treated water from Stenner Canyon. 12 Figure 5 San Luis Obispo Water Demand u Average MGD by Month 10 9 8 A 7 .A G6 5 3 2 1 0 1 3 Ili 5 111 3 5 7 9111 3 5i9I''lIl 1 W74 it 1 3 8602 6 8 10 8702 6 8 10 8802 6 8 10 8902 6 8 10 9002 6 8 10 9102 January 1986—March 1991 (YYMM) Figure 6 (on the following page) presents historical demand for energy over the past five years. It exhibits a declining trend similar to that of Figure 5. Compare Figure 5 to Figure 6. The two curves have the same basic shape, but do differ slightly due to fixed costs such as heating and lighting. Also, the energy consumed by the transfer pumps is not directly related to the volume of water treated by the plant. The pumps are run at the discretion of the plant personnel to store treated water and their use accounts for some of the fluctuation in the historical energy use of the plant. Figure 7 (on the following page) shows the monthly energy bills of Stenner Canyon for the past five years. This figure differs from Figure 6 due to differences in seasonal rates among the various rate schedules used by PG&E. 13 _ 1 1 1 1 1 VA VW XX �Am AOAMA -OA Amm AAM :t. ' e. J �. AA 1 :i j ' : J i Munn At AA 1 1 A •,�. AIM At- :, _ J ,t .J i • .iii :YJ V: tf ti .'JI J:: _ tI tti t J V AAA itt r AAA 1J fAll A .. t J. i A. :. ! y i ., ;•. J j. ..t The preceding data lead to the conclusion that energy conservation is a direct result of water conservation, due to reduced volumes being treated. There is a privately owned hydroelectric generator at the inlet to the forebay which sells PG&E about 100 kW of power. Its direct use by Stenner Canyon as a peak load shaving measure would have no adverse environmental consequences. 4. Comparison to Existing Standards The amount of energy expended per million gallons of water treated (1,260 kWh in the case of the upgraded Stenner Canyon plant) is dependent on the treatment process, on the amount of pumping necessary to move that gallon to and from the treatment facility (which is site-specific), and on the quality of incoming, as well as outgoing water(which are both also site-specific); therefore, any direct comparisons of energy use between different facilities would be misleading. For this reason we did not compare the energy use of the Stenner Canyon Water Treatment Plant to other existing facilities. 5. Effects on Energy Resources The ozone treatment process was chosen as an upgrade for technical reasons of water quality, rather than for energy efficiency. The large organic load from the Salinas source (Santa Margarita Lake) makes ozone a choice far superior to chlorine on a public health basis. The direct energy consumption figures (at 8 mgd) are as follows; the existing facility has a ratio of energy use to water processed of 400 kWh/Mgal as compared to 1,260 kWh/Mgal for the upgraded facility. For a more accurate comparison, though, the hidden energy costs of the current plant's chemical use (as described in the following section) should be taken into account, and result in an energy consumption of 439 kWh/Mgal for the current plant. 15 6. Transportation Energy The energy consumed processing and transporting the various inputs necessary to effec- tively run the water treatment plant does not affect the plant's direct energy consumption (as measured by PG&E), but does in fact affect overall (global) energy consumption; it therefore warrants closer scrutiny. Propane must be delivered to the upgraded facility to fuel the two furnaces which replace the existing electric resistance heating. The furnaces will increase transportation energy use by necessitating propane deliveries; but, due to their increased efficiency over electric resistance heating, the furnaces will result in a net energy savings. Currently chlorine is shipped to the existing plant in loads of 10,000 pounds and used as a disinfectant. The upgraded plant, by using ozone produced on-site instead of importing chlorine, avoids about eight deliveries of chlorine per year. In its current state the plant must have a variety of chemicals(excluding chlorine)delivered to it; the upgraded facility will need chemicals of a different variety to be delivered, but in approximately the same quantity. These changes will not significantly affect the energy expended during the transportation of chemicals. 16 D. Mitigation Measures 1. Potential Measures in Design and Operation Potential mitigation measures were identified in an energy audit of the existing Stenner Canyon plant. These are not technically within the scope of the EIR, since they deal with existing facilities, but are discussed here for the sake of completeness. Thirteen general and 24 lighting energy conservation measures were recommended for the existing plant. These include: • Run transfer pumps in preferred order using most efficient first. • Run only one transfer pump at a time, especially on peak. • Maintain finished water level as high as possible to minimize pumping costs. • Install high efficiency motors immediately on three transfer pumps. (Planned during upgrade.) • Reduce size of pump and motor at reservoir #1. • Reduce size of pump and motor at reservoir #2. • Specify numerical minimum efficiencies for existing motors to be replaced during the upgrade. • Eliminate electrical resistance heating of office areas. (Planned during upgrade.) • Optimize rate schedules. • Replace T12 fluorescent lighting with T8 lamps and ballasts in 11 locations. 17 • Install electronic ballasts on existing eight-foot fluorescent lamps in two loca- tions. • Replace mercury vapor and incandescent lighting with high pressure sodium in nine locations. • Replace incandescent flood lights with halogen floods lamps in two locations. Potential energy conservation measures have been included in the upgraded design by Black& Veatch. These were discussed in Section A.3. above and are described in detail by B&V in Attachment 2. Potential energy conservation measures were also identified by TAC in its energy audit for the plant upgrade. Because the design is not completed, these measures are necessarily less detailed. Most of the recommendations take the form of advising the city to consider the measures in detail when more information becomes available. The recommendations are: Select an operating schedule that gives adequate consideration to on-peak and off-peak energy and demand charges. If possible, avoid the peak charge periods from 12:00 noon to 6:00 p.m. on weekdays from May through October. Consider variable frequency drives on 65-horsepower plant service water pumps used for ozone process cooling. Peak demand for water has been reduced from about nine mgd to about 4.5 mgd during the current drought. Consider some appropriate long-term measures for water conservation. Consider operation of diesel-generator as peak-shaving generator. (There are unknown factors including .availability of natural gas as fuel and air quality 'considerations. The recommendation is to study the concept.) Operate the existing hydroelectric generator as a peak shaving device. (Unknown factors include legal status and ownership of the generator, but this would be an attractive option with no environmental impacts.) Install T8 fluorescent lamps and electronic ballasts in place of planned T12s in 18 14 applications. Install PL type fluorescent lamps instead of incandescent lamps in two applica- tions. 2. Potential Measures of Siting, Orientation The existing site at Stenner Canyon limits the option of choosing an alternative site. The existing plant orientation takes advantage of gravity to move water through the treatment process, and the upgrade maintains this advantage. No other potential measures were considered. 3. Potential for Reducing Peak Demand Peak load shaving measures were identified for both the existing plant and for the upgrade to the plant. These measures are detailed in Section 1 above. 4. Alternate bels The ozone process requires electricity and there is no alternative. B&V have specified Number 2 diesel fuel as being necessary for the emergency diesel generator. Propane will be supplied to furnaces, thus eliminating electrical resistance heating. S. Recycling The major opportunity for recycling at the Stenner Canyon site lies with the water used .for filter backwashing. This water is recovered and treated with the raw water supply rather than being discharged. 19 E. Alternatives The decision to change from chlorination to ozonation as the primary disinfection method for the treatment of water was made for public health reasons. We believe that no acceptable alternatives to ozone treatment meet the objectives of compliance with the disinfection requirements of the Safe Drinldng Water Act and the need to reduce the total amount of Trihalomethanes created by treating the water with chlorine. No alternatives were considered for purposes of this impact assessment. 20 R Unavoidable Adverse Effects The upgraded facility, including the use of ozone for water treatment, requires approxi- mately 210% more electricity than the existing water treatment plant to treat the same volume of water (8 mgd). By using additional electricity, the project will add to demand for generation, and may therefore increase air pollution to the extent that fossil fuels are used by the serving utility, Pacific Gas and Electric. The relationship between this added demand for electricity and plans for San Luis Obispo's or other air basins cannot be determined at this time. There will be minor, short-term impacts to the access routes and to the site itself due to the construction traffic and activities. These impacts are believed to be short-term and localized to the immediate access and site areas. The potential impacts are believed to be minor. 21 G. Irreversible Commitment of Resources Use of fuel for project construction and use of electricity and chemicals to operate the upgraded plant will be irreversible. The amounts consumed are believed to be small in comparison with demands and supplies for such items throughout the state and region. 22 H. Short-term Gains vs. Long-Term Impacts The primary gains from converting to the ozone treatment of water are reducing potential public health risks. The long-term impacts of changing to the ozone treatment process are the potential impacts on air and water quality due to the increase in long-term energy use for the purpose of ozone generation. These impacts are discussed in detail in this EER and are not believed to be significant. There will be a minor short-term impact on the site and the access road to it due to the construction activities. These impacts are minor when compared to the long-term gains to the public health from the change to ozone treatment process. 23 I. Growth Inducing Effects The existing water treatment facility was designed to but a maximum of 8 mgd. Due to modifications it has been able to treat up to 11.5 mgd at a lower quality of treatment. The uprgaded facility will have the capacity to treat 16 mgd at a relatively high quality of treatment.5 This increase will not automatically lead to additional growth. The added capacity will raise one of the thresholds that could constrain growth. Other constraints include water availability from reservoirs and ground water, waste water treatment capacity, air quality, road capacity, and residents' desires for the size and pace of change within the community, reflected in the general plan and growth management regulations. 5 The 500 lb/day of ozone generation is sufficient for treating 15 mgd at the maximum dose of 4 mg ozone/liter of water(mg/1). If a lower concentration is required, more water could be treated. Average is expected to be 3 mg/l and minimum 1.5 mg/l. 24 c Attachment 1. Initial Study of EnvironmenW Imnact (City of San Luis Obispo, Decem- ber 1990, Updated January 15, 1991) MY O� San LUIS OBISp0 �����►I►lillliliil���l������I��I a INITIAL STUDY OF ENVIRONMENTAL IMPACT 8 SITE LOCATION Stenner Canyon, north of San Lu i s Obispo APPLICATION NO. ER 34-90 PROJECT DESCRIPTION Upgrade the city's water treatment plant and expend tr +mo + capacity. APPLICANT City of San Lulc Obispo (Gary Henderson, Itiliti s Fnnineer) STAFF RECOMMENDATION: NEGATIVE DECLARATION _MITIGATION INCLUDED EXPANDED INITIAL STUDY REQUIRED _X ENVIRONMENTAL IMPACT REPORT REQUIRED PREPARED BY DATE '17-13-Qn COMMUNITY DEVELOPMENT DIRECTOR'S ACTION: DATE 17 30 FhV%jt ML Is p SUMMARY OF INITIAL STUDY FINDINGS s.DESCRIPTION OF PROJECT AND ENVIRONMENTAL SETTING 11.POTENTIAL IMPACT REVIEW POSSIBLE ADVERSE EFFECTS A. COMMUNITY PLANS AND GOALS ............. YES* B. POPULATION DISTRIBUTION AND GROWTH.......................................... YES* C. LAND USE ..................................... D. TRANSPORTATION AND CIRCULATION .............................................._- YFS* E. PUBLIC SERVICES ................................................................. nln* F. UTILITIES............................ ................. G. NOISE LEVELS ..................................... yr-¢* ................ H. GEOLOGIC&SEISMIC HAZARDS&TOPOGRAPHIC MODIFICATIONS .................... nip I. AIR QUAUTY AND WIND CONDITIONS................................................ yES* J. SURFACE WATER FLOW AND QUALITY ................................................ NO K. PLANTLIFE L. ANIMAL LIFE...................................... M. ARCHAEOLOGICAL/HISTORICAL ................................................... NO N. AESTHETIC ............................ .......................................... YES* 1. ENERGY/RESOURCEUSE ................. YQS* ................ 1'. OT111"I1 ,••I�I II I I I, '..I f n I Y.. ..I.f!�!.I•r•.'., . ... . .. .. . .. .. .................. ........ .. ... . . .... rlul III.STAFF RECOMMENDATION 'SEE ATTACHED REPORT seas Correction to Initial Study Page 3 - discussion of population growth Change first two paragraphs to read: The existing plant was designed to treat about 8 million gallons per day (mgd). An upgrade completed several years ago increased the rated treatment capacity to 11.5 mgd, which has been approached at times of peak demand. The proposed project would increase the treatment capacity to 16 mgd. The project would increase one threshold which now constrains growth. Other growth-limiting resource thresholds are the amount of water supply (the reason for the current moratorium on projects which increase water use), wastewater treatment capacity, and air quality. The project would have -no effect on the amount of water available for treatment: the safe yield of the existing reservoirs, or possible new sources of water. Considering peak demand experienced with existing population, and assuming that peak treatment demands would increase approximately in proportion to city population, the increased capacity could serve a city population of about 58,000. City population, consistent with the general plan, is projected to increase from about 42,000 in 1991 to about 53,000 by the year 2015, assuming other resource thresholds are increased. Thus, the proposed project would establish a treatment capacity level about nine percent higher than needed for build-out of the adopted general plan. (Additional long-term water conservation would allow additional development within this limit.) The excess capacity created by the project is considered a reasonable margin of safety for potential differences in the future composition of the community under the adopted plan, and is not seen as inducing substantial growth beyond that allowed by the general plan. gm 7-26-91 INITIAL ENVIRONMENTAL STUDY 34-90 Water Treatment Plant Upgrade DESCRIPTION OF PROJECT & SETTING The City of San Luis Obispo proposes to modify treatment processes at its existing water treatment plant in Stenner Canyon. The changes are intended to make the treatment process safer for employees and the public, and to help meet anticipated, stricter requirements for drinking water quality. The changes will also double the. designed treatment capacity, from about eight million gallons per day (mgd) to 16 mgd. All the new facilities would be built within the existing treatment plant site. The plant treats water from Salinas Reservoir and from Whale Rock Reservoir. The quality of raw water arriving from the two reservoirs varies substantially throughout the year, and differs between the two sources. The plant does not treat water from the city's wells, which is treated in smaller "package plants" close to the wells. The treatment plant is set into a gradually sloping hillside above Stenner Creek, and is bordered by the Southern Pacific Railroad and grazing land. The nearest development; . other than utility structures, is a dwelling about one-third mile to the northwest Some proposed changes were evaluated in the Environmental Impact Report for the Water Management Element and Water Management Plan (City of San Luis Obispo, February 1987). That EIR concluded that the .previously proposed changes would have no impacts; in fact, they could be considered "categorically exempt," since they would be changes to an existing facility with no substantial expansion of capacity. Additional changes are now proposed. They are: 1. Replace the initial ('flash") mixing facilities with a larger, two-stage facility. This facility introduces chemicals to the incoming, raw water so that contaminating particles will group together rather than repel each other. The city does not propose changing the types of chemicals used in this stage. 2. Replace the flocculation equipment, in the existing basin. This step gently mixes the water, encouraging larger clumps of particle to form so they will settle out 3. Replace filter media and rehabilitate drains and outflow pipes, to improve the effectiveness of filtering and filter washing. 4. Add a tank and pumps to reduce the time between cycles of filter washing. 5. Make more accessible and modify the equipment which recycles water used to wash the filters back to earlier treatment steps, to make removal of solids more ^ effective. The changes will help meet state standards for water treatment plants. Water Treatment Plant Environmental Review 2 6. Use liquid sodium hypochlorite (bleach) rather than chlorine gas for residual disinfection. Adding chlorine in an active form is the final step before treated water is sent to storage tanks and distribution pipes throughout the city. The chlorine inhibits growth of viruses and bacteria which survive the treatment process or which enter the water system (a concern primarily in dead-end water mains where water may stay for a long time before being used). The liquid chemical is safer to store and handle, and far easier to contain if it leaks, than the pressurized gas. 7. Provide a stand-by metering pump for each of several systems which feed chemicals into the stream of water undergoing treatment. 8. Upgrade the electrical system, replacing the 208-volt service with 480- and 120- volt services. 9. Provide new control equipment, which will be compatible with existing equipment to be retained. 10. Remodel the existing laboratory and office to better provide for monitoring requirements. 11. Use ozone rather than chlorine as the primary disinfectant, which will require an ozone generator and a new ozone contact basin at the beginning of the treatment process. 12. Provide a new building to house the ozone generator, new chemical feed systems, control room, and additional office space. This building will be two stories, with about 7,000 square feet of floor space. POTENTIAL IMPACT REVIEW A. Community lans andgols Overall, the project is consistent with community goals. With the exception of policies concerning energy use, discussed under item "O" below, the project is consistent with the general plan Water and Wastewater Management Element. The project raises no issues of consistency with other general plan elements. B. Population distribution and growth The project will raise one threshold which now constrains city growth, but this project alone will not induce growth. Water Treatment Plant Environmental Review 3 The existing plant was designed to treat about 8 million gallons per day (mgd). At times of peak demand during summer and fall, it has treated at a rate of about 11 mgd for short periods, though the'level of treatment was barely adequate. The proposed project would increase the designed treatment capacity to 16 mgd. The project would increase one threshold which now constrains growth. Other growth-limiting resource thresholds are the amount of water supply (reason for the current moratorium on projects which increase water use), wastewater treatment capacity, and air quality. The project would have no effect on the amount of water available for treatment: the safe yield of the existing reservoirs, or possible new sources of water. Considering peak demand experienced with existing population, and assuming that peak treatment demands would increase approximately in proportion to city population, the increased capacity could serve a city population of about 59,000. City population, consistent with the general plan, is projected to increase from about 42,000 to about 53,000 by the year 2015, assuming other resource thresholds are increased. Constructing and installing the new facilities will increase construction employment in the area by.roughly 50 people at a time, for up to one year. Probably, there will be several specialized contractors working in sequence,.with insignificant impact on migration to the area. There are now eight permanent workers for the plant, with one to four on duty per shift. With completion of the project, there would be nine or ten workers. The number of additional workers which may be needed when the plant is running at full capacity sometime in the future, if any, is not known at this time. D. Transportation and circulation The project will not significantly affect traffic in the vicinity. Stenner Canyon Road is a paved county road, which is wide enough to accommodate one vehicle travelling in each direction, though lanes are not marked. It connects the site with Highway 1, about one mile to the south, at a "I" intersection with no signal. (The Highland Drive entry to the Cal Poly campus provides an alternate connection to Highway 1 at an intersection with signals and turn lanes.) Stenner Canyon Road also serves a few dwellings in the area, and is a minor entrance to the north end of the Cal Poly campus. It is lightly travelled. Traffic from permanent employees at the plant will not change significantly. There may be slightly less truck traffic for chemical supply, with use of ozone. Construction traffic, both workers and material trucks, will be a substantialincrease over existing traffic levels on Stenner Canyon Road, but will not significantly affect Highway 1. Water Treatment Plant Environmental Review 4 E. Ppblic services The project will not directly impact other public services. The estimated total capital cost of about 8.7 million dollars is expected to be funded by water rates and connection fees, and therefore will not affect the level of funding for other public services. G. Noise levels Noise impacts will not be significant. Construction activity will temporarily increase noise at the plant and along the access route. Operation of the ozone generator and blowers will cause more noise than current plant operations, but the increase is not expected to be noticeable along Stenner Canyon Road, and will not be detected from existing dwellings in the vicinity. 1. Air quality The project will not significantly impact air quality. Construction traffic will cause a minor increase in emissions for a few months. The ozonation process raises air quality issues. Ozone is a highly chemically active form of oxygen, which lasts about 20 to 30 minutes in the atmosphere before forming other compounds. In the lower atmosphere, it is a major component of smog, causing irritation of eyes and lungs, and damage to plants and some synthetic materials. County air quality is in violation of state ozone standards, which have been exceeded several times per year in recent years. The draft County Air Quality Attainment and Maintenance Plan aims for a 40 percent reduction in ozone production from current levels. The ozone generation system would have a firm capacity of about 500 pounds per day. The system would produce air that is about two percent ozone, by weight, which is far higher than occurs even in smoggy air. This ozone-rich air would be brought into contact with the water. The ozone generation equipment and pipes would be air tight, and the chamber where water receives the ozone would be sealed. About 90 percent of the ozone brought into contact with the water would be transferred to it. The ozone that is not transferred would be held in an air space at the top of the chamber. The pressure in the contact chamber would be kept below atmospheric pressure, to prevent leaks. Air vented from the vacuum blower which provides the lower pressure would pass through a catalytic converter, where nonhazardous manganese dioxide would convert the ozone to elemental oxygen If ozone is detected at 0.01 parts per million (ppm) or more in the ozone generation building, indicating a leak, the generation system will shut down and the building Water Treatment Plant Environmental Review 5 ventilation will stop, to contain leaks. A vent gas ozone analyzer will be provided to assure that discharges stay below 0.10 ppm under all operating conditions. The San Luis Obispo County Air Pollution Control District staff has conducted a preliminary review of the proposed ozone system, and has concluded that impacts will not be significant. However, the volume of air to be vented from the containment area is not known at this time. A complete review of the discharge will occur when the design is further refined. At that point, the district may require the city to obtain an "authority to construct" and a "permit to operate," which would specify any additional ozone control measures. N. Aesthetic The appearance of the plant will not change substantially. The plant is visible from several hundred feet along the Southern Pacific Railroad (Amtrak) line on the hillside above, on both approaches to the "horseshoe" curve. A relatively small part of the plant is visible from Stenner Canyon Road near the plant access road. The existing multistory building at the plant is visible from 100 to 200 feet on the northbound lanes of Highway 1, near the Stenner Canyon Road intersection. It is not visible from the southbound lanes unless one looks back (to the left rear) at that short segment Most of the proposed changes will be below ground or in existing structures. The new building will be in the same area and about the same size as the existing building. No specific design is proposed at this time. O. Energy use The cumulative impact of increasing energy use in city utility projects is significant. The water treatment plant now uses about 1.6 million kilowatt hours (kwh) per year. The ozone process will substantially increase electricity usage. Aber the upgrade, the plant would use about 4.5 million kilowatt hours per year. This additional energy use is an unavoidable consequence of the ozone process. While there will be a small, but unknown, reduction in the amount of energy used to produce and transport chlorine, the reduction would not nearly offset the increase due to ozone production. The general plan Water and Wastewater Management Element says, "Water operations will minimize energy use and will incorporate all cost-effective energy production facilities" (Policy 53). The Energy Conservation Element says, "The city will set an example for energy conservation and the use of renewable sources in its own facilities and operations." * 1-15-91 update: the project will be designed to limit vent gas ozone concentration to 0.09 ppm or less, in compliance with State ambient standa0d. gm Water Treatment Plant Environmental Review 6 The engineers who recommend the proposed project concluded, after evaluating six alternative treatment processes, including pilot plant evaluations, that ozone treatment was the most desirable due to treatment effectiveness and safety (Water Treatment Plant Modifications and Ozone•Pilot Study,. Final Report; Black and Veatch, June 1990). Four of the six alternatives involved ozone at some stage of treatment, while two did not. The cumulative impact of increasing energy use in city utility systems is significant. In addition to this proposed project, the recently approved upgrade of the city's wastewater treatment plant will increase energy use, from about 1.75 million to about 5 million kwh per year (Final EIR for Wastewater Treatment Plant Upgrade and Sewer Line Replacement, City of San Luis Obispo, March 1990). That increase was determined to be significant, adverse, and unavoidable, but justified by the overriding concern of meeting water quality standards.' Further, the city proposes a seawater desalination plant at Morro Bay which would use between 19.5 million and 32.6 million kilowatt hours per year (EIR 45-90, forthcoming). Energy use in the area would be further increased if the proposed wastewater treatment plant is built in Los Osos (not a city Project), and if additional water transmission lines are built in connection with the State Water Project Coastal Branch or other regional water projects. An average single-family residential customer in San Luis Obispo uses about 6,300 kwh per year of electricity. The increased electricity usage due to the proposed project is therefore equivalent to the usage of about 460 households. The combined additional electricity usage of the three utility projects, 38.7. million kwh per.year, would equal the usage of about 6,100 households in the San Luis Obispo area. California Energy Commission policy favors accommodating added electricity demands of new customers or new uses by increased efficiency in energy use (conservation) of existing customers. Assuming that the average residential customer can still reduce electricity usage by 25 percent through more efficient lighting and motors on appliances, the added usage by the water treatment upgrade would cancel out the savings of about 1,800 households, while the increased usage of all three city utility projects would cancel out the savings of about 25,000 households. The secondary effects of increased energy use are major environmental concerns. Pacific Gas & Electric Company, the utility serving this area, generates electricity from oil-fired and natural-gas fired plants, hydropower, nuclear, wind, and geothermal (to be eliminated) sources at many stations throughout central and northern California. At times, California power demand is met by purchases from out-of-state sources, including coal-fired plants. The impacts of increased electricity production, depending on power sources, include: air pollution (including acid-rain and acid-fog contributors); greenhouse gases; radioactive waste; water pollution from petroleum spills; land disturbance from mining; inundation of free-flowing streams, forests, and farmland; noise,.appearance, and bird mortality due to wind generators; and soil or water pollution from geothermal brine. Water Treatment Plant Environmental Review 7 The increased energy usage of the proposed project would represent about 0.1 percent of the 1987 output of Pacific Gas & Electric Company's fossil-fueled Morro Bay power plant, which was about 3.5 billion kwh (primarily to meet peak demands in other parts of the state); the three projects' usage combined would be about one percent of that year's output. P.P. Public safM There will be no adverse impacts; hazards will be reduced by the proposed project. Chlorination has been the conventional means of disinfecting public drinking water, including San Luis Obispo's. Chlorine (the active component of household bleach) kills microorganisms. However, it does not remove all tastes and odors from the water. In fact, in relatively high concentrations, it adds its own taste and odor (as found in swimming pools, which have. far higher chlorine concentrations than drinking water). Also, chlorine reacts with some natural or synthetic organic compounds often found in water to produce trihalomethanes (THMs), a group of compounds which have been shown to cause cancer. While the city's treated water has met current standards for THMs on average, there have been occasional, short-term exceedances. Further, the chlorine treatment methods will not be able to consistently meet new federal standards, which will allow about one-half the THM concentration which has been allowed, or potential federal standards which would again reduce by one-half the allowed concentration. The ozone system will use an electrical current to produce a stream of air rich in this chemically active form of oxygen, which will be brought in contact with the water. Ozonation will remove tastes and odors, as well as avoiding formation of THMs. Further, it will eliminate the need for pretreatment using both powdered activated carbon and potassium permanganate, which is a potentially explosive combination. STAFF RECOMMENDATION To comply with CEOA, an EIR should be prepared even though it would address only one issue: energy consumption. The city has already determined that an increase in electricity usage about the same as that caused by the proposed project is individually significant. The cumulative energy impact of the three currently proposed major water and wastewater projects also would be significant. Increased energy use appears to be a significant impact for which no mitigation is available. 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Wath• �! 1�•_.•-..`� 1�D'_._. .. � ' n // �a�,1�\`. Attachment 2. Letter from Ronald E. Henderson, Black & Veatch, to David Dietrich, Technical Analysis Corp., dated June 25, 1991, one attachment. BLACK & V EATCH ENGINEERS-ARCHITECTS 2300 CLAYTON ROAD.SUITE 1200 CONCORD.CALIFORNIA 94520-2100 TEL (415) 246-8000 FAX: 14151 674.9458 San Luis Obispo, California B&V Project 17432.200 Mater Treatment Plant Modifications June 25, 1991 Mr. David Dietrich, P.E. Associate Technical Analysis Corporation 282 Second Street, Third Floor San Francisco, CA 94105 Dear Mr. Dietrich: Enclosed for your use, as requested, is a list of energy conservation measures that are incorporated into our design. we are pleased to help expedite the EIR process. If you have any additional questions or comments, do not hesitate to contact us. Very truly yours, BLACK & VEATCH rRnald E. Henderson, P.E. Project Engineer Mit Enclosure cc: K. Earing, SLI G. Henderson, SLO W. Hetland, SLO Mal Black & Veatch SAN LUIS OBISPO, CALIFORNIA ENERGY CONSERVATION DESIGN MEASURES I . Specifications will require high-efficiency motors be supplied for Division 11 equipment. 2. Electrical interlocks have been provided to prevent the simultaneous operation of the two service water pumps. 3. Electrical interlocks have been provided to prevent the simultaneous operation of the two air backwash blowers. 4. Reduced-voltage starters have been provided for all motors 75 horsepower and larger. 5. Adjustable frequency drives have been provided for all variable speed applications. 6. Power factor correction capacitors have been provided for all motors 25 horsepower and larger that operate continuously. 7. Lighting design in the administrative areas of the ozone building utilizes a "master/slave" tandem-wired system. 8. Lighting design in the ozone building meets or exceeds the requirements of California Title 24. 9. Rotary lobe compressors were selected for the ozone generation air preparation system. The rotary lobe is a very high efficiency unit. 10. Multiple compressors were used in the air preparation system to increase efficiency during turndown (reduced capacity). 11 . Deep (>20 foot) ozone contact basins with fine bubble diffusers. This will provide an ozone transfer efficiency of greater than 95 percent. 12. The design incorporates catalytic type ozone destruct .units in lieu of thermal types. Catalytic units require less power. 13. Ozone air preparation system is designed to provide cool , dry air which will increase ozone generator efficiency. L1Oa2 Attachment 3. Life Cycle Cost Program BLCC 3.0 Summary. BLOC SUMMARY FOR SLO Run 03 ---------------------------------------------------------------- PRESENT VALUE ANNUAL VALUE INITIAL COST (AT OCCUPANCY) $8,273 , 989 $538 , 235 ANNUALLY RECURRING O&M COSTS $135, 130 $8,790 NON-AN. RECURRING O&M COSTS $10,595 $689 ENERGY COSTS $31921,804 $255, 119 REPLACEMENT COSTS $121,205 $7, 885 LESS: REMAINING VALUE ( $0) ( $0) --------------------------------------------------------- ------- TOTAL LCC $12,462,723 $810,718 [\BLCC San Luis \SLORUN03 .SUM] Attachment 4. Nomogram for converting mgd to Acre-Feet per year. r . n e � a 1000 I