HomeMy WebLinkAbout2011-0314 Study Session PACKET
CITY OF
ASHLAND
CITY COUNCIL STUDY SESSION
AGENDA
Monday, March 14, 2010 at 5:30 p.m.
Siskiyou Room, 51 Winburn Way
5:30 p.m. Study Session
1 . Look Ahead Review
2. Does Council have questions or feedback on the proposed effluent water
temperature solution alternatives? [60 Minutes]
In compliance with the Americans with Disabilities Act, if you need special assistance to participate in this
meeting, please contact the City Administrator's office at (541) 488-6002 (TTY phone number 1-800-735-
2900). Notification 72 hours prior to the meeting will enable the City to make reasonable arrangements to
ensure accessibility to the meeting (28 CFR 35. 102-35.104 ADA Title I).
COUNCIL "IEETINCiS ARE BRO,\DC\ST LIVE ON CJI;\NNEJ. 9
VISIT TilE CITY OF !\SHIANJ)'S WEll SiTE !\T WWW!\SliL\ND.OR.US
CITY OF
ASHLAND
Council Communication
Meeting Date:
Department:
Secondary Dept.:
Approval:
Wastewater Master Plan Update Study Session
March ]4,20]] Primary Staff Contact: Michael R. Faught
Public Works . E-Mail: faughtm@ashland.or.us
Administration Secondary Contact: Scott A. Fleury
Martha Bennet Estimated Time: 60 Minutes
Question:
Does the Council have questions or feedback on the proposed effluent water temperature solution
alternatives?
Staff Recommendation:
Staff recommends that Council review the attached documentation and provide input regarding
implementation of the next steps.
Background:
At the June] 5,20] 0 council meeting, the council awarded the $303,400 wastewater master plan
update to Keller and Associates. While the consultant has accomplished many of the scope of work
items (evaluation of regulatory compliance, existing and future treatment plant flow and load
projections, updated the collection system sewer model, wastewater treatment plan existing conditions
evaluation) the most timely and critical work has been focused on developing options that bring
Ashland effluent temperature into compliance with the new 2007 Bear Creek Temperature standards.
The reason staff required the consultant to work on the effluent temperature compliance issue as the
highest priority is that the City's National Pollutant Discharge Elimination System (NPDES) Permit
(which are on a five year cycle) is up for renewal and the new NPDES permit has to include a plan for
the City to meet the new Bear Creek TMDL standards. To that end the consultant has been working
closely with both Ashland and DEQ staff to develop a list of six potential effluent temperature
compliance alternatives (Reuse on Imperatrice property or partial reuse on Imperatrice property,
discharge into the TID system, cooling towers, trading/shading, blending/flow augmentation, and
hyporheic or shallow groundwater discharge).
The consultant has evaluated the pros and cons and costs of each of the proposed options and the
results of that work are demonstrated in the following table:
Pa~e I of3
~~,
CITY OF
ASHLAND
Table I:
Description I Capital Aonual
Prf.'jed Cost Cn~t
Option ---- - ...1:1(mCIlI!i m ~ - UenetiB____J)I'UwbuckL _______ - ~ ______~I~~ _tomU1ent~
--- -
Maximum Irrigate 433 Beneficial use of High Cost. $10.8 M $(58,000) $JO.IM Savings
Reuse on acres with water. lower stream flows. assume thai
lmperatice treated effluent. Existing water right membranes
Property Pipeline to site, could be used to arena!
138-166 MG augment potable waler used.
storage. supply.
Shoulder season Potential for
storage required membrane and
I winter chemical savings.
discharge. Mitigate concerns of
"future" more stringent
rCQulalions.
Partial Reuse Lower cost does Similar to Option I A. High Cost. $5.3- $35,000 $5.8- For lower
on Impertatice includes Improvement could be Introduces complexities 8.9M 9.4M cost range,
Property -- minimum completed later if in monitoring and need to add
424 ac.fiIyr storage. Option 3 or 4 is wastewater management. cost of
Higher cost pursued. Higher O&M costs than Option 3 or
assumes more ' Option 1 A. 4, to address
storage, and Reduced stream flows cooling
periods of no available for aquatic requirement
discharue. habitat.
Discharge to Pipeline to Mitigate "near field" Not a standalone solution Not Not Not
TID Talent Canal. concerns. u still need to offset Evaluated Evaluated Evaluated
Reduction in chemical excess thennalloads.
costs. High op)X)sition from
downstream users
anticipated.
District concerns about
chemicals.
Storage for shoulder
seasons likely required.
Schedule and approval
outside ofCitvcontrol.
Cooling Tower ' Mechanical Addresses temperature Chillers required for $6.1 - $200,000 $8.6- Cost range
cooling tower. concerns. hottest periods. 8.1M 11.6M reflects use
Storage Allows continued Upstream / downstream of ponds
facilities. discharge. storage also required for versus
Maximum control in night.time operation concrete
terms of compliance storage
schedule. , reservoirs
Trading 8 miles of Lowest cost Some uncertainty u $3,400,000 spread out $2.7M
(Shading) shading. alternative. participating property over 20+ years
Channel to Bear Allows continued owners to be identified;
Creek. discharge. migration blockage
Constructed Improved fish habitat evaluation to be
wetland pond. and other completed. Potential
environmental minor additional local
benefits. coolinp rf"nuired.
Blending / Blend additional Additional stream Cannot meet temperature Not Not Not Nota
Flow water discharges flow. targets by itself. Evaluated Evaluated Evaluated viable
Augmentation from Ashland Uses water that could be alternative.
Creek or TID. used for potable water
usage.
Additional water quality
testing may show
additional water quality
concerns.
Hyporheic Subsurface Low operations costs. Difficulty in locating site Not Not Not
(shallow dis)X)salof Simple technology. with suitable soils. Evaluated Evaluated Evaluated
groundwater) treated Significant additional
wastewater to effort required to
shallow ground determine feasibility.
water. Potential large land
reauirement.
Page 2 of3
~~,
CITY Of
ASHLAND
It is important to note that with the exception of the temperature trading or shading, most of these
options are not new effluent temperature compliance concepts to Ashland. The shading concept looks
at the benefits allowing communities the option of shading along the stream channels within the
watershed as a system-wide solution to 'stream temperature reduction rather than trying to solve
effluent temperature compliance at wastewater treatment plant outfall. This concept has either the City
or a third party securing easements along the waterway at critical areas where shading is needed, and
then provides long-term funding to plant and maintain the shading materials for 25 years. The
resulting temperature reduction is then calculated and the city receives the temperature reduction credit
at the wastewater treatment plant outfall.
While this concept had some initial compliance challenges that have been worked out with DEQ, the
consultant and staff will be recommending trading/shading as the preferred alternative to meet the new
Bear Creek temperature standards.
Because the trading/shading as an option to meet temperature compliance is new to our community,
the DEQ Director has agreed to attend the Council study session to provide additional insight as to
DEQ's view of trading/shading as a solution to temperature issues.
Next Steps
. Finalize effluent temperature compliance option recommendation for NPDES permit
development
. Technical Review Committee meeting March 15.2011
. Consultant will continue to develop master plan scope items
. Public Outreach: Public Works would like recommendations on the extent of public outreach
required to inform citizens on a course of action for implementation of the preferred disposa]
option.
Related City Policies:
City of Ashland NPDES DEQ Permit
Council Options:
The Councils comments and directions regarding the next steps to be taken are encouraged and
appreciated.
Potential Motions:
No motions are presented at this study session.
Attachments:
1. TRC Meeting Agenda 2-23-201 I
2. TRC Meeting Minutes 2-23-2011
3. Wastewater Master Plan Draft Chapter 10
4. DEQ Memorandum - City of Ashland excess thermal loads limits
Pagd on
r~'
CITY OF
ASHLAND
Wastewater Technical Review Committee
AGENDA
WASTEWATER TREAMENT PLANT 1195 OAK ST.
February 23.20111:00 PM
ATTENDEES I INTRODUCTIONS:
AI Large Member (Chamber of Commerce), Meiwen Richards
At L'<lrge Member, Jeff Heglie
. AI Large Member, Joe Graf
. Council Member, Russ Silbiger
. Ashland Public Works Director -Mike Faught
Ashland Engineering Technician -Scott Fleury
Ashland Engineering (overseeing Water Study) - Pieter Smeenk
Ashland Public Works Superintendent -Terry Ellis
Ashland WastewaterlReuse Supervisor -David Gies
Ashland Wastewater Coilections-Jerry Conley
Ashland Wastewater Treatment Plant Supervisor-Ken Moser
. Ashland Water Quality Conservation Analyst-Robbin Pearce
. Medford Regional Water Reclamation Facility Superintendent, Dennis Baker
. Environmental, Lesley Adams Rogue Riverkeeper Klamath-Siskiyou Wildlands Center
Department of Environmental Quality - Jon Gasik & Ranei Nomura
Department of fish and Wildlife - Dan Vandyke
. Keiler Associates (Consulting Engineer) - James Bledsoe & Larry Rupp
. Rogue Vailey COG - Craig Harper (Rogue Valley COG)
. Fresh Water Trust - David Primozich
OVERVIEW OF MASTER PLAN:
. Collection system
. Wastewater treatment and disposal eva1uations to meet TMDL / Permit requirements
. Key deliverables of planning efforts:
o Report that documents existing and future needs
o Capital improvement plan
o Master plan with prioritization and phasing of improvements
o Financial plan with user rate and system development charge implications
REVIEW OF WORK PREVIOUSLY COMPLETED:
. Population and land use
o Provided by the City
o Study area coincides with UGB
C:\Documents and Settings\shipletd\Local Setlings\Temporary Internet Files\Content.Outlook\63KU614S\Attach 1 TRC Agenda.doc
. Design flows - developed using DEQ methodology; consider 5-year wet weather event and
10-year dry weather event
. Treatment evaluation focuses on 20-year projections; collection system evaluation
considers "build-out" projections
. Collection system evaluation - just beginning now that flow monitoring is complete
WASTEWATER TREATMENT FACILITY EVALUATION:
. Draft write-up completed
. Summary of existing deficiencies
o RAS pumps capacity
o Membranes Replacement
o UV capacity to meet peak flows
o The outfall pipeline is also a potential bottleneck, for peak flows, but this may be
resolved as part of the Temperature option.
. Improvement alternatives being considered
REGULATORY REQUIREMENTS:
. NPDES Permit (Clean Water Act) Issues
o 1992 Total Maximum Daily Loads (TMDLs)
. Phosphorus, ammonia, chlorine
o 2007 TMDLs
. Temperature
. Future? New ammonia standards, pharmaceuticals
o Other regulatory concerns
. Water rights
. Temperature concerns - DEQ Draft Tech Memo completed
o Near field - local impacts to fish caused by a thermal plume
. DEQ has internal guidelines for evaluating
. Continued discharge to Ashland C~eek -- spawning impairments, thermal shock,
and migration blockage
. Relocating to Bear Creek - minor migration blockage in September
o Far field - general watershed impacts addressed in TMDL
ALTERNATIVES TO ADDRESS TEMPERATURE CONCERNS:
o Draft Chapter 10 completed
. Refer to summary table attached
o Option 1: Reuse
. Most expensive initial cost
. Existing water rights available for potable water system
. Flow is removed from creek - ODFW would want replaced (negates water right
benefit?)
. Options involving continued WWTP discharge during low stream flow periods
would trigger additional improvements (i.e. Option 3 or 4)
o Option 2: Discharge to TID - does not appear to be viable at this time
o Option 3: Cooling Tower
. Chillers and storage required
C:\Documents and Setlings\shiph!td\Local Sellings\Temporary Internet Files\Content.Outlook\63KU614S\Attach 1 TRC Agenda.doc
. Ongoing energy costs
o Option 4: Trading (shading)
. Lowest cost option
. Other environmental benefits
. Near field impacts mitigated by relocating outfall to Bear Creek, wetlands shading
I shallow ground water interaction - potential that more than existing wetlands will
be required _
. Keller Associates would recommended extended compliance period to address
near field issues (i.e. 10 years) recognizing that 1) hyporheic action and shading
in the channel and wetlands, 2) other shading activities upstream of the outfall, 3)
additional flow and temperature data, 4) possible future changes in regulations, 5)
possible reduction in discharge if reuse is pursued, and 6) possible other future
activities may show that additional improvements are not necessary
o Option 5: Blending - does not appear to be viable
o Option 6: Hyporheic
. not enough information to fully evaluate at this time
. preliminary indicators suggest that this option could be land intensive, with
potential difficulties in finding land near Bear Creek with suitable soils
NEXT STEPS:
. Define public outreach approach
. March 14'h Council study session with DEU, 15th Meeting with City Council
. Identified preferred treatment alternatives
. NPDE5 Permit processing
C:\Documents and Settings\shipletd\Local Settings\Temporary Internet Files\Content.Outlook\63KU614S\Attach 1 TRC Agenda.doc
Table 10.2 - Ashland WW Disposal Option Comparison Chart
Descriptfon I Capital Annual
Proj~&%u:", 1 Cost Cost
~OP!!Qn_E!<l_~!!l!nel!\L~Or.wback._____N~V_Co!!l!ne.!!!L
1A Maximum Irrigate 433 Beneficial use of High Cost. $14.1 M $(58,000 $13.4M Savings
Reuse on acres with water. Lower stream flows. ) assume
Imperatice treated effluent. Existing water right that
Property Pipeline to sile, could be used to membranes
138-186 MG augment potable are not
storage_ water supply. used.
Shoulder season Potential for
storage required membrane and
I winter chemical savings.
discharge. Mitigate concems of
"future" more
strinaent rP.CIulations.
18 Partial Similar to Option 1 A. High Cost. $11.7 - $53.000 $12.4 - Additional
Reuse on Introduces complexities in 12.4M 13.0M costs for
Impertatice monitoring and wastewater cooling
Property - management. would be
Periods of Higher O&M costs than required for
No Option 1A. discharge
Discharge Reduced stream flows during each
available for fish. month.
2 Discharge to Pipeline to Mitigate -near field- Not a standalone solution - Not Not Not
TtD Talent Canal. concerns. - still need to offset excess Evaluate Evaluate Evaluate
Reduction in chemical thermal loads. d d d
costs. High opposition from
downstream users
anticipated.
District concerns about
chemicals.
Storage for shoulder
seasons likely required.
Schedule and approval
outside of Citv control.
3 Cooling Mechanical Addresses Chillers required for hottest $6.1 - $200,000 $8.6 - Cost range
Tower cooling tower. temperature periods. 8.1M 11.6M reflects use
Storage facilities. concerns. Upstream I downstream of ponds
Allows continued storage also required for versus
discharge. night-time operation concrete
Maximum control in storage
terms of compliance reservoirs
schedule.
4 Trading 8 miles of lowest cost Some uncertainty - $3,400,000 spread $2.7M
(Shading) shading. alternative. participating property out over 20+ years
Channel to Bear Allows continued owners to be identified;
Creek. discharge. migration blockage
Constructed Improved fish habitat evaluation to be
wetland pond. and other completed. Potential minor
environmental additional local cooling
benefits. r<:>nuired.
5 Blending I Blend additional Additional stream Cannot meet temperature Not Not Not Not a viable
Flow water discharges flow. targets by itself. Evaluate Evaluate Evaluate alternative.
Augmentatio from Ashland Uses water that could be d d d
n Creek or 110. used for potable water
usage.
Additional water quality
testing may show
additional water quality
concems.
6 Hyporheic Subsurface low operations costs. Difficulty in locating site Not Not Not
(shallow disposal of Simple technology. with suitable soils. Evaluate Evaluate Evaluate
groundwater) treated Significant additional effort d d d
wastewater to required to determine
shallow ground feasibility.
water. Potential large land
r<:>nuirement.
NEXT MEETING DATE: March 15'h, 2011 1 :00 PM
C:\Documents and Settings\shipletd\local Settings\Temporary Internet Files\Content.Outlook\63KU614S\Attach 1 TRC Agenda.doc
Call Scott al 552-24 I 6 if vou will be unable 10 attend!
In compliance with the Americans with Disabilities Act, if you need special assistance
to participate in this meeting, please contact the City Administrator's office at (541)
488-13002 (TTY phone number 1-800-735-2900). Notification 48 hours prior to the
meeting will enable the City to make reasonable arrangements to ensure accessibility
to the meeting (28 CFR 35. 102-35.104 ADA Title I).
C:\Documents and Settings\shipletd\Local SeUings\Temporary Internet Files\Conlent.Outlook\63KU614S\Attach 1 TRC Agenda.doc
~:.,
,
W ASTEW A TER TECHNICAL REVIEW COMMITTEE (TRC)
February 23RD, 2011
MINUTES
MEMBERS PRESENT: JOSEPH GRAF, LESLEY ADAMS, MEWIEN RJCHARDSON, DENNIS
BAKER
STAFF: SCOTT FLEURY, TERRY ELLIS, DAVID GIES, JERRY CONLEY, KEN MOSER
CONSULTANTS: JAMES BLEDSOE, LARRY RUPP
MEMBERS ABSENT: JEFF HELGlE, RUSS SILBIGER, ROBBIN PEARCE, MIKE FAUGHT
Visitors: Jon Gasik (DEQ), Ranei Nomura (DEQ), David Primozich (Freshwater Trust), Alan Horton
(Freshwater Trust), David Laurance (Freshwater Trust), Dan Vandyke (ODFW)
I. CALL.TOORDER: I :00 PM
2. APPROVAL OF MINUTES: No previous minutes to approve.
Additional Items: None
3. Public Forum: No comments
4. OLD BUSINESS: None
5. NEW BUSINESS:
A. Round Table Introduction: All members of the committee introduce themselves and
provide a basic background. Bledsoe asks if anyone has any questions before critical items
are discussed.
B. Master Planning Overview: Bledsoe provides a general overview of the master planning
process to committee members. The master plan is a snapshot in time of the current
collection and facilities system along with a road map of where the system is headed over an
extended planning period.
C. Previously Completed Work: Bledsoe reviews the work completed by Keller to this point
in the process. Keller Associates has been working on master plan scope items for
approximately 6 months now and have completed some tasks with a focus towards effluent
disposal options. Keller has also evaluated the treatment plant and provided the City with
draft chapter 9, "Treatment Plant Existing Conditions" and chapter 10 "Effluent Disposal
Alternatives". Committee members will be provided a copy of draft chapter 10 with minutes
from TRC meeting, with the hope that comments from the TRC members may be received by
March 7, 2011. Keller Associates will try to have a draft chapter 9 that incorporates City and
DEQ comments prior to the next scheduled meeting.
D. Regulatory Requirement: Jon Gasik from DEQ gives brief overview of the Clean Water
Act and how it relates to the National Pollution Discharge Elimination System (NDPES)
permit process. The Clean Water Act established water quality standards for municipalities to
follow with regards to discharges into watersheds. DEQ performed tests on waters to
determine if waters met the established standards. If they did not, then DEQ created Total
Maximum Daily Level (TMDL) permits for point source discharges. In 1992, a TMDL was
developed for the Bear Creek Watershed. AsWand has a point source discharge that is part of
C:\Documents and Settings\shipleld\Local SeWngs\Temporary Internet Files\Content.Oullook\63KU614S\Attach 2 TRC Minutes.doc
the Bear Creek Watershed and thus must follow a DEQ developed NPDES permit. The
TMDL permits developed by DEQ for point source discharges are good for five years. At the
end of each five year permit iteration a renewal process begins and new permits include
updated standards that have been developed. The 1992 Bear Creek TMDL developed
included phosphorus, ammonia and chlorine load allocation requirements. These
requirements where addressed as part of the 1998 wastewater treatment plant upgrade. The
2007 Bear Creek TMDL develops load allocations for temperature, bacteria, and sediment.
Out of these new standards for load allocations the primary focus for Ashland is the
temperature requirements for effluent. Through the NDPES permit the City must address "far
field" impacts and "near field" impacts with regards to temperature. DEQ has provided an
analysis to Keller Associates and the City that the current effluent discharge into Ashland
Creek creates near field temperature impacts that include fish migration blockage, thermal
shock, and spawning effects during particular months of the year. In order to meet the new
NDPES permit requirements the City must address these near field issues with a compliance
schedule developed with the approval of DEQ. With respect to the far field impacts, over the
past couple of years new protocols and procedures have been developed that make
temperature trading a more viable option to address the far field TMDL concerns for the City
of Ashland. Temperature trading is a kind of creekside riparian restoration that involves
planting trees and vegetation to block the solar impact to waters. The City will need to meet
both near field thermal requirements and far field heat load reduction as part of a new
NDPES permit. Not only with temperature trading assist the City in meeting far field heat
load allocations, but it provides a proven ecological benefit via riparian restoration.
E. Disposal Options: Bledsoe reviews the 6 disposal options attached as part of the Agenda.
E.I: Reuse (or Recyle): This option involves taking treated effluent and irrigating a
portion of the City owned Impertrice property. This option was previously considered
as an alternative to address phosphorous removal in the 1990s, but was reportedly not
pursued at that time because of concern about removing water from receiving waters.
The reuse could eliminate both near field and far field concerns by eliminating
discharges during most of the year. Eliminating discharges during critical time
periods would require a large volume of effluent storage. This is the most expensive
cost option to address temperature concerns. One advantage of reuse, is that the
existing 424 Ac*ft of water rights on the Impertrice property could be made available
for potable water system. Based on water master planning efforts, a variation of this
alternative could be one of the lower cost options to address anticipated future
shortfalls in the City's potable water supply. A drawback ofreuse is that flow is
removed from Ashland Creek - and ODFW would want some of the flow replaced,
especially during critical low flow periods. This would negate some of the water right
benefit. Options involving continued WWTP discharge between April and November
would trigger additional improvements to address both near field and far field impacts
of adding warm effluent to receiving waters (i.e. Items E.3 or EA below).
E.2: Dishcharge to T.I,D: After meetings with the T.1.D Board of Directors by
Keller Associates and city staff, too many concernslobstacles where developed to
proceed with this option within the required time frame for permit renewal.
E.3: Cooling Towers: Mechanical cooling towers could be constructed that would
allow the city to meet the temperature requirements for effluent discharge. These
cooling towers would also require chillers and storage for the hottest periods of the
C:\Documents and Settings\shipletd\Local Settings\Temporary Internet Files\Content.Outlook\63KU614S\Attach 2 TRC Minutes.doc 2
year. The cooling towers would meet both the near field and far field impacts for the
temperature requirements. This option is not viewed as a green alternative because of
the ongoing energy costs.
E.4: Temperature Trading: David Primozich reviews temperature trading with the
committee. The Freshwater Trust developed a model of Bear Creek that shows
riparian sections that can be shaded with trees and vegetation to reduce solar impacts.
This alternative addresses the far field concerns by offsetting excess thennalloads
from the treatment plant by shading approximately 8 miles of Bear Creek. Near field
concerns would be addressed by relocating the existing outfall to Bear Creek and
constructing some wetlands. Trading is considered the lowest cost option. Trading
provides environmental benefits by the restoration of fish habitat. Keller Associates
would recommend an extended compliance period to address near field issues (i.e. 10
years) recognizing that I) hyporheic action and shading in the channel and wetlands,
2) other shading activities upstream of the outfall, 3) additional flow and temperature
data, 4) possible future changes in regulations, 5) possible reduction in discharge if
reuse is pursued, and 6) possible other future activities may show that additional
improvements are not necessary. Pursuing this alternative would not preclude the City
from pursuing other alternatives including cooling and recycling water in the future.
As part of relocating the outfall to Bear Creek, other concerns expressed by ODFW
can be addressed. These include, preventing fish from swimming into the effluent
line of the treatment plant, possibly removing the influent pipeline to the existing
pond/wetlands, and modifying the outfall from the existing pond/wetlands.
E.5: Blending: Two concerns were discussed with blending. First, temperature data
gathered suggests that the likely source of water for blending (TID) has temperatures
that exceed the target levels. This effectively makes it impossible to meet the TMDL
requirements during certain periods of the year. Second, some concerns were
expressed about the water quality of the TID sources.
E.6: Hyporheic: Hyporheic is the subsurface disposal of effluent through shallow
groundwater. This alternative was previously recommended as the preferred
alternative. After additional investigation by Keller Associates, preliminary indicators
suggest that this option could be land intensive, with potential difficulties in finding
large amounts of land near Bear Creek with suitable soils.
6, FINAL COMMENTS:
The City and Keller Associates would like the committee members to review disposal options and
provide comments back. The City and Keller plan to have a study session with the City Council in
March to discuss effluent disposal options. The City will provide minutes and the draft chapters to
the committee as soon as possible. In addition, the City would like to discuss the extents of its public
outreach program with committee members with regards to disposal options and the master planning
process in general.
7. NEXT MEETING DATE: March 15'\ 1:00pm at the Wastewater Treatment Plant
ADJOURN: Meeting adjourned at 3:10
I
C:\Documents and Settings\shipletd\Local Settings\Temporary Internet Files\Content.Outlook\63KU614S\Attach 2 TRC Minutes.doc 3
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN . ~~.~
10,0 EFFLUENT DISPOSAL ALTERNATIVES
10.1 BACKGROUND
During certain periods of the year, the wastewater effluent from the City's treatment plant
accounts for a significant portion of the flow in Ashland Creek and Bear Creek. Higher
effluent temperatures can raise the temperature of the creek and negatively impact aquatic
habitat. DEQ will include new standards for excess thermal load limits when the NPDES
permit for the City of Ashland's wastewater treatment plant (WWTP) is renewed to address
the waste load allocation in the TMDL. DEQ may also include a temperature limit to address
local impacts to aquatic habitat.
Current effluent temperatures have the potential to exceed allowable levels for the May
through October period. Keller Associates reviewed the previous five years of temperature
and flow data, and determined that there is an existing excess thermal load of approximately
44 million kcal/day (critical month is October). This is anticipated to increase to
approximately 53 million kcal/day by 2030. Similar calculations by DEQ correspond to Keller
Associates' calculation results [1].
Reducing the excess thermal load from the Ashland WWTP is important in meeting target
downstream temperatures in Bear Creek. An evaluation of wastewater disposal options
completed in 2009 [2] looked for strategies or alternatives to address the excess thermal
loads. This master plan builds upon the work previously completed. Additionally, since the
completion of 2009 evaluation, guidelines for evaluating the local (near field) impacts and
temperature trading programs have been more fully developed by the State.
Representatives from DEQ, the City of Ashland, Keller Associates, Oregon Department of
Fish and Wildlife (ODFW), and other stakeholders met on several occasions to better define
the impacts of Ashland's wastewater discharge. DEQ completed a thermal plume analysis
for continued discharge to Ashland Creek as well as discharge to Bear Creek. Because of
concems with near field spawning impairments, thermal shock, and migration blockage, it is
unlikely that continued discharge into Ashland Creek would be permitted without first
significanUy cooling the effluent [1]. Relocating the outfall to Bear Creek would eliminate
concerns of thermal shock and greaUy mitigate other near field impacts. Based on 3D
modeling completed by DEQ, a side bank discharge would allow discharge to Bear Creek
without impairing spawning. However, based on historical data, there still remains a potential
for migration blockage during the month of September [1].
Keller Associates' scope of work for this study was to update the evaluation for the three
most promising disposal alternatives. However, because of continued interest on the part of
the City and new developments, six alternatives were evaluated in more detail. The findings
of this evaluation follow.
10,2 REUSE OPTIONS
Reuse options include those options that recycle treated wastewater. Land application of
wastewater effluent during the growing season could reduce or eliminate the discharge of
thermal loads to Ashland and Bear Creek during critical periods. Another benefit of reuse is
that the treatment process is likely to be less affected by future changes in regulations
requiring increasingly more stringent levels of treatment for discharge. For example, had the
City of Ashland chosen to land apply their effluent rather than remove phosphorous via
nRAIT
CITY OF ASHLAND
Page I
February 2011
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
eaoci.ta8
membrane filtration 10 years ago, they would not now be faced with addressing temperature
concems. As discussed in Chapter 2, two items on the horizon that may affect future
discharge requirements for the plant include 1) stricter ammonia limits, and 2) Oregon Senate
Bill 737, which addresses pharmaceuticals. In addition to regulatory benefits, recycling water
has the potential to offset potable water demands and make better use of available water
resources.
Maintaining stream flows has been a priority to the City in the past. One of the drawbacks
with any reuse altemative that involves removing the existing discharge flow from Ashland
Creek is that the recycled water would not be available for use for potential downstream
users or to create higher flow conditions for aquatic habitat.
From a water rights standpoint, the City of Ashland is not required to keep their effluent
discharge in the creek. However, according to ORS 537.132, the following would occur if the
City were to move forward with removing their flow for reuse purposes:
. The Department of Water Resources (DWR) would notify affected users if discharge
from Ashland WWTP to Ashland Creek were to cease (this because Ashland has
discharged for more than 5 years and the WWTP discharge may at times make up
50% or more of the flow).
. An affected downstream water right holder would need to demonstrate to DWR that
the "cessation of discharge by the municipality substantially impairs the ability to
satisfy a water right. . .. and if this person is successful, they would get preferential
use of the reuse water.
. The City is not required to incur additional expenses (beyond a more favorable
altemative) to deliver water to the affected penson desiring the reuse water.
10.2.1 Recycling Water (Reuse) on Imperatrice Ranch Property
The City has property north of 1.5 (Imperatrice Ranch) that could be used for crop irrigation
using effluent. A conveyance pipeline crossing Ashland Creek was constructed when the
City was considering a project in 1997 for biosolids application, effluent storage and irrigation
on the pro~rty.
Due to steep terrain and other limiting features (Talent Irrigation District canal, wetland
swale), portions of the Imperatrice site are not useable for irrigation. Limiting irrigation to
slopes less 20% and providing necessary buffer zones for the canal, swale and property lines
provides a usable irrigation area of 412 acres for Class C effluent, or 433 acres for Class B
effluent (smaller buffer to property lines) (3).
One of the primary benefits the City would realize with recycling water on the Imperatrice
Ranch property is that the water rights currently used there could be transferred and used as
additional water supply for the potable water system.
Two recycling options are summarized for the Imperatrice Property - Option 1A includes
maximizing the total amount of water recycled on the property, and Option 1B includes
recycling only the amount necessary to offset the existing water rights. Regardless of the
disposal option selected by the City, Keller Associates recommends that the City work with
DEQ so that future NPDES permits allow for recycling of treated effluent.
nRA~
CITY OF ASHLAND
Page 2
February 2011
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
..aoDi.cae
10.2.1.1 Option 1A: Maximum Reuse on Imperatrice Property
The potential for thermal shock and migration blockage in Ashland Creek would be averted
by eliminating discharge from June through October, and potential salmonid spawning
impairment from thermal discharges would be prevented by reducing/eliminating discharge
during November and March through May. Storage volumes for this option were determined
based on irrigating as much land as possible without supplemental water, and discharging
excess to the creek only to the extent that impairment of salmonid spawning is avoided. This
results in limited discharge during March, April and November, and discharge of stored
excess during January and February when creek temperatures are low enough to easily
accommodate the thermal load.
Alfalfa, pasture grass, and grass seed are potential crops; pasture grass and grass seed use
more water than alfalfa and thus have lower storage requirements. Based on average net
irrigation requirements and 70% irrigation efficiency, the acreage available on the Imperatrice
property is sufficient to use 442 MG or 492 MG if planted to grass seed or pasture grass,
respectively. Since the amount applied to crops is less than influent flows to the WWTP, the
remainder would be discharged. At year 2030 flows (average 2.59 mgd), storage would be
needed to provide sufficient volume during June, July and August. Additional storage volume
would allow excess flows to be stored for discharge in the winter.
An irrigated area of 433 acres of pasture grass would handle (without supplemental water) up
to 2.77 mgd, with a storage volume of 138 MG (water balance in Appendix). A total of 512
MG would be discharged to the creek from November through April. The same acreage in
grass seed would handle year 2030 flows with a storage volume of 139 MG and 496 MG
discharged (November through April).
The estimated project cost for Option 1A is approximately $10.8 million. Eliminating the need
for phosphorus removal required for surface discharge would result in annual savings of
$71,000 a year for alum. An estimated additional $100,000 potential annual savings could
be realized in energy and chemical (sodium hypochlorite and citric acid) with elimination of
the membrane operation. However, it is understood that the public perception may require
the continued use of the membranes. If membrane operation were eliminated as part of the
reuse option, the combined savings ($171,000) would more than offset the estimated
$113,000 annual costs of pumping to storage on the site and from storage to irrigation.
Though effluent quality would still need to be monitored with reuse, testing requirements (and
related costs) are expected to decrease with the elimination of discharge.
10.2.1.2 Option 1B: Partial Reuse on Imperatice Property
Keller Associates also evaluated an alternative that would recycle just enough effluent to
offset the existing 424 ac-ft of irrigation rights on the Imperatrice property, and maintain the
remaining flow in the stream. This scenario would allow the water right to be transferred to
the City's potable water system and would also allow continued discharge to the creek.
However, under this scenario, the temperature requirements of the TMDL would have to be
met by employing other improvement alternatives.
To offset the 424 ac-ft water right, enough water would need to be supplied to irrigate
approximately 136 acres of land. The amount of storage required would depend on how
much is discharged during specific periods of time. If minimum storage were provided, then
close to half of the existing discharge during July and August would be used for irrigation,
while the balance would be discharged to the creek. With additional storage, discharges
nRAFT
CITY OF ASHLAND
Page 3
February 2011
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
alNlOCi.~
could be eliminated during specific periods and restricted during others to eliminate the need
for additional treatment to reduce thermal and phosphorus loads for discharge. (Existing
alum and membrane treatment would still be required.) This approach would require close
monitoring to consistently meet the discharge limits.
If the City's primary objective is to maximize the discharge available during critical periods for
aquatic habitat while offsetting the water right, this alternative could be adjusted to include
increased storage during high stream flow periods and continued effluent discharge during
low flow and spawning periods.
The estimated project Cost for Option 1 B, not including a cooling component, is
approximately $5.3-8.9 million (includes 6.5-168 MG storage). Since discharge to the creek
would continue, all the costs for phosphorus removal discussed above would be included in
the annual operation and maintenance cost of this option. In addition, there would be the
added costs (estimated $35,OOOlyear) of pumping to storage on the site and from storage to
irrigation.
10.2.2 Option 2: City.wide Reuse
City-wide reuse (on parks, golf courses and other public spaces) was evaluated as part of the
water master plan as an alternative to reduce potable water use [4]. From an implementation
standpoint, Keller Associates would envision this being phased in over many years. Reuse
on City property could be phased with agricultural reuse on the Imperatrice property. Since
the distribution system for city-wide reuse may be extensive, the cost for implementation will
exceed that of the option to apply all effluent to the Imperatrice property.
In addition, storage during shoulder seasons would still be required for temperature TMDL
compliance (storage location could be at Imperatrice property).
10.3 RELOCATED DISCHARGE OPTIONS
10.3.1 Option 3: Discharge to Talent Irrigation District (TID)
This altemative would involve discharging the City's effluent into the TID irrigation system.
The likely discharge location would be Talent Canal, which has a capacity of 35 to 45 cfs.
According to the District, the Talent Canal services approximately 3500-4000 acres. One of
the benefits of this alternative would be the reduced chemical requirements needed to
remove phosphorous, because most of the water would be reused or land applied
downstream. This alternative would mitigate concerns about near field impacts to aquatic
habitat, and would reduce the thermal load requirements to the extent that the effluent is
reused downstream.
On October 5, 2010, representatives from Keller Associates and the City met with TID board
members to further discuss this altemative. The following concems would need to be
addressed before approval could be obtained for this option:
. Real and Perceived Concems of Receiving Effluent - The TID currently does not
receive any treated effluent. The district has a number of patrons who have already
expressed deep concems about receiving Ashland's effluent.
nRAFT
CITY OF ASHLAND
Page 4
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN .. ~~L.~
. Not Wanting Any Additional Chemicals - downstream farmers have already fought
with the district to eliminate other chemical additives for moss control in the district's
canals. This concern is heightened by the number of organic farmers.
. Approval of Patrons - Because of the controversial nature of this alternative, the
board indicated that they would want their patrons to weigh in on the matter, possibly
even having a vote of the patrons. Educating the public, addressing their concerns,
and obtaining approval at this time would require a great deal of effort with an
uncertain outcome. This would also require many months to do.
. Removal of flow from Ashland Creek. ODFW has expressed a desire to keep as
much flow in Ashland and Bear Creek as possible. There may also be other
downstream water right impacts that would need to be addressed by removing
discharge.
. Other Potential Additional Regulatory Requirements
. Additional Maintenance Requirements:
o The district's water chemistry is very sensitive to temperature. Even a small
increase in temperature or phosphorous is believed to increase the potential for
moss growth in their system.
o Receiving water during the shoulder seasons - particularly October and
November - would adversely affect district operational practices. The City would
need to plan on being able to store their effluent during these periods.
o Additional fish screening may be required by DEQ. If these screens are required
at outfalls, this could result in more maintenance to the district.
In addition to needing to address the above concerns, this option would also require that
Ashland quantify and then mitigate excess thermal loads corresponding to the portion of flow
that is not reused downstream. Given the number of issues and potential road blocks, Keller
Associates recommends that this altemative not be pursued at this time. However, it may be
that in the future as public perception changes and if drought conditions make the water
resources more valuable, it may be beneficial to reevaluate this alternative.
10.4 OPTIONS FOR CONTINUED DISCHARGE TO ASHLAND/BEAR CREEK
10.4.1 Option 4: Cooling Tower I Heat Exchanger I Chiller
Background
.
A cooling tower could be used to reduce the temperature of the effluent through evaporation
to reduce the effluent temperature. The primary benefit of the cooling tower alternative is it
addresses the temperature requirements without concern for off-site improvements, water
rights, potential reduced flows in the stream, or potential compliance schedules. However,
this alternative would be an energy-consuming option because the effluent would have to be
pumped to the top of the cooling tower and a large fan would be operated continuously. This
option was determined to be a viable alternative by Carollo in an evaluation of disposal
alternatives completed in 2009 [2]. However, as noted in the Carollo report, a cooling tower
nRAIT
CITY OF ASHLAND
Poge 5
February 20] 1
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
eaaoai.C88
could not meet the limits all the time and a chiller would have to be added to reduce the
temperature of the effluent to meet the limits during some days.
In a cooling tower, air is simultaneously drawn up through the tower in the opposite direction
from the water flow. A small portion of the water is evaporated, which removes the heat from
the rest of the water. Warm, moist air is discharged to the atmosphere and cooled plant
effluent is discharged to the creek.
There are two types of cooling towers that would be considered for Ashland: open loop and
closed loop, both using plastic media. In the open loop design, the plant effluent would be
pumped to the water distribution system at the top of the cooling tower for distribution evenly
across the top of the media. In the closed loop design, the plant water is kept separate from
the cooling water. The advantage to the closed loop system is that the cooling water is
separate from the wastewater, and anti-scaling chemicals could be added to prevent scaling
in the tower without affecting the effluent water quality. .
There are two types of closed loop designs. In one, the plant effluent would be pumped
through coiled tubes from the top of the cooling tower to the bottom of the cooling tower.
Cooling water would be pumped to the water distribution system at the top of the cooling
tower for distribution evenly across the top of the media. In the second design, the layout is
the same as the first except that the cooling water is put through a plate heat exchanger to
further cool the cooling water. For larger systems, like that needed for Ashland, this closed
loop option is less expensive.
The cooling tower would not have to be operated year-round. Its months of operation would
be spring to fall. Effluent temperature limits are a daily maximum of 13 oC from October 15 to
May 15, and a daily maximum of 18 oC from May 16 to October 14.
The effluent temperature regulations allow for exceedence of the effluent limits when the
daily maximum temperature exceeds the 90th percentile of the last ten years of the maximum
daily temperature 7 -day average. Based on the last 10 years of temperature data from the
Medford Airport (closest weather station to Ashland), the 90th percentile maximum daily
temperature is 93.3 OF.
When the cooling tower cannot meet the effluent limit, a chiller would also need to be used to
reduce the temperature of the effluent lower than can be done by evaporation alone. A
chiller uses condensers and electrical energy to obtain the additional cooling required similar
to a refrigerator.
The Oregon Administrative Rules (OAR) provide some relief for meeting the temperature
limits with an air temperature exclusion (34041-0028(12)(c)) and a low receiving stream flow
exclusion (340-41-0028(12)(d)). The air temperature exclusion provides that effluent
temperatures that exceed the limit are not considered violations when "the daily maximum air
temperature exceeds the 90th percentile value of annual maximum seven-day average
maximum air temperatures calculated using at least 10 years of air temperature data.'
Analysis
Continuous Discharae. A cooling tower can continuously cool the effluent wastewater to
approximately 50F above the atmospheric wet bulb temperature. During each day the wet
bulb temperature increases and decreases with the air temperature. The historical climate
data for the Medford airport provided daily minimum, maximum, and average wet bulb
nRAFT
CITY OF ASHLAND
Poge 6
February 201 1
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
___Bee.
temperature. Using this historical climate data from January 1, 1999 to August 30, 2010, the
plant effluent temperatures can be calculated for the minimum, maximum, and mean wet bulb
temperatures. Plots showing the estimated cooled WWTP effluent temperature at the mean,
minimum and maximum wet bulb temperatures, respectively, are shown in Charts 10.1, 10.2,
and 10.3.
The mean wet bulb temperature graph is based on the average effluent temperature, while
the maximum wet bulb temperature graph shows the maximum daily effluent temperature,
and the minimum wet bulb temperature graph shows the lowest daily effluent temperature
achievable using a cooling tower. These charts show that, using only a cooling tower and
continuous discharge, there would have been a significant number of temperature violations
over the last 11 years. When the temperature exclusion discussed above is considered,
there still would have been more the 40 violations over the last 11 years.
Chart 10.1 - Calculated WWTP Effluent Temperature at the Mean Wet Bulb
5.00
Melin Wet Bulb Tmnpclllturo
25.00
20.00
o
'15.00
110.00
i
0.00
3/11/1997 7/2411998 121811999 ....1912001 91112002 1114J2004 512812005 101101200 2/22/2008 71612009 11/181201 41112012
. 0
~
Temperature
nRAn
CITYOFASHLAND
Page 7
February 2011
~ - ~- -" - <
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
8AOCi.~
Chart 10.2 - Calculated WWTP Effluent Temperature at the Minimum Wet Bulb
Temperature
25.00
20.00
15.00
} 1000
i
i
5.00
0.00
3111 1997 7124/1
-5.00
-10.00
-Minimum Wet Bulb Temperature
Emuent limn
-15.00
-20.00
""'"
Chart 10.3 - Calculated WWTP Effluent Temperature at the Maximum Wet Bulb
Temperature
30.00
25.00
20.00
I ".00
I
i
10.00
5.00
0.00
3111 997 7124/1998 12J611999 411912001 9/112002
11/181201 4/1 012
o
-5.00
-10.00
-15.00
- Max Wet Bulb Temperah.n&
- -- Effluent Limit
-20.00
""'"
nRAFT
Page 8
CITY OF ASHLAND
February 20 I ]
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
..88Om.tea
Storaae. In order to meet the effluent temperature limits with a cooling tower, Keller
Associates looked at using storage to cool plant effluent only during the night when the air
temperatures are lower. A discharge period of 12-hour period was assumed. The storage
would be sized for half the peak flow between April and October, as some of the potential
violations for continuous treatment are in the shoulder periods. The estimated peak daily
flow during this period'is 5.5 mgd, and thus the storage tank would be sized at approximately
3.0 million gallons.
The Oregon Department of Fish and Wildlife (ODFW) has indicated that they would want the
City. to continue to provide continuous discharge to maintain a more uniform flows in the
creeks. This would require the City to store the cooling tower effluent and discharge
continuously from this tank. For planning purposes the effluent tank was also assumed to be
3.0 million gallons.
Since the cooling tower effluent would be stored, the final effluent temperature would be
between the effluent at the mean and minimum wet bulb temperatures shown in Charts 10-1
and 10-2. Thus, there would still be several violations of the effluent temperature limit. The
cooling tower may not meet the DEQ effluent temperature requirements all the time without
additional treatment utilizing chillers to lower the effluent temperature during hot nighttime
weather periods.
Chiller. In order to prevent any discharge temperature violations, a chiller would be needed
to reduce the effluent water temperature further. A chiller would use condensers and
electrical energy to obtain. the cooling required. Based on the climate data analysis, the
chiller may be required to reduce the effluent a further 3 DC at times. To reduce the size of
the chiller, it would be installed in the effluent line from the final storage tank and thus be
sized for 5.5 mgd or 3800 gpm. The preliminary sizing of the chiller is 1,500 tons. The chiller
would also need to be installed in a building.
Cooling Tower and Chiller Alternative
A cooling towerlchiller alternative that would allow the City to meet the effluent temperature
limits at all times would consist of the following components:
. Cooling tower inlet storage, sized to hold 12 hours of plant effluent flow from 10 AM to
10 PM during the period April 1 to October 30. The tank would hold 3.0 million
gallons (50% of the peak dry weather day in 2030). For budgeting purposes, Keller
Associates assumed the storage would be a concrete tank (high range) or a lined
pond (low range).
. Pumps, sized to pump the daily flow from the storage tank to the cooling tower
(assumes permeate pumps or filter pumps can feed the tower).
. Cooling tower, closed loop type, sized for the twice the peak dry weather day flow
(7,600 gpm) in order to pump the peak day during the 12 coolest hours of the day.
For budgeting purposes, Keller Associates assumed that the cooling tower would
include a plate heat exchanger for the cooling water and non-<:hemical water
treatment system for the cooling water to prevent scaling.
. Cooling tower effluent storage, sized at 3.0 million gallons; assume continuous gravity
discharge at the plant influent flow rate via a motor-contro,"ed valve. For budgeting
nRAI'T
CITY OF ASHLAND
Page 9
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN
t.1l:l. KELLER
~ eaaoai.cea
purposes, Keller Associates assumed the storage would be a concrete tank (high
range) or a lagoon (low range).
. A 1,500 ton chiller, sized to cool 3,800 gpm 3 DC, in a building (approx. 32 feet by 22
feet and 16 feet high).
The estimated capital cost for this option is $ 6,100,000 to $8,100,000, depending on the
type of storage. The estimated annual O&M costs for the cooling system are approximately
$200,000 (for either storage option).
The O&M challenges are:
. Scale control in tower and chiller.
. Tuming cooling tower system on as temperature limit is approached and off as tower
is not needed.
. Controlling the pump rates to the tower and chiller and outlet rate from the final
effluent equalization tank.
. Operating chiller when needed.
10.4.3 Option 5: Trading (Shading)
Temperature trading allows for excess thermal loads to be offset by shading (from riparian
vegetation) and other approaches that reduce heat loading such. as constructed wetlands,
flood plain restoration, and restoration of cold water refugia. In recent years, the temperature
. trading program has been developed more fully in the State of Oregon. With project
protocols, verifications, and reporting procedures in place and accepted by DEQ, trading is
now a viable solution for cities facing new thermal load limits like Ashland. DEQ allows for
offsets in the TMDL area to apply both upstream and downstream of the point discharge.
While there are few opportunities for trading in Ashland Creek, there are many opportunities
to trade along Bear Creek and within the Bear Creek watershed.
In evaluating this altemative, a non-profrt organization, The Freshwater Trust, assisted in the
analysis. To complete the analysis, The Freshwater Trust coordinated with and received
and field verified data from DEQ's Heat Source models for Bear Creek to determine the
extent of opportunities for riparian revegetation with native species to create shade and
minimize solar loading in the TMDL area. In addition to using DEQ data for the analysis, The
Freshwater Trust worked closely with DEQ technical staff to confirm its analysis procedures.
The heat source data for Bear Creek was divided into three equal interval classes: LOW, MID
and HIGH, based on the difference between existing shade cover and potential shade cover.
Areas with the highest potential for improvements and shade credits are designated as
HIGH. The lengths and potential solar load reductions for these reaches are summarized in
Table 10.1. The location of LOW, MID, and HIGH Bear Creek river stretches is further
illustrated in Chart 10A.
nRA>T
CITY OF ASHLAND
Page 10
February 2011
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
eaaoalBtae
Table 10.1 Bear Creek Heat Source Analysis Results'
Average of 25%
Potential per mile
kcaVda
3 257 325
6616843
10141,007
, 6,795,376
TOTALS wei hied aye e 27.15
'Information provided by The Fresh Water Trust
# Miles by
Potential
Cat 0
5.16
16.65
5.34
% Miles by
Potential
Cat
19%
61%
20%
100%
164 494 510
Chart 10.4 Bear Creek - Potential Solar Load Reduction by River Mile
PoI.ntJalSo~r load Rlduction
.
I ..;- ,
2 -h
4, I
~
6
,
<::"
I ... I
I
10.
-
w 12
~" t..
-, ,
7::14
.. ..- j..
~, .
~ 16. T
-
1_-
11.
,
2J ,
:
22
24 I_~
26 -.::; I
,
5.0 10.Q, 15.0 20.0
IMIion,s of Kca~milelday
ste-mTotal5
,/l(rfl'lio
~ OwneD
~ Pat~ Points
'i low Poteontiilll Tolls! lmillian ICcal)
Md Potentlat-Tctill million "cal
; Total 5 swm Potentl.1 _
The Heat Source analysis showed that revegetation projects on Bear Creek will produce
between 3,257,325 and 10,141,007 kcaVday per mile with a weighted average of
approximately 6,800,000 kcalslday per mile. Using this weighted average, to meet the
projected 2030 excess heat load of 53,000,000 kcaVday, an estimated 7.8 miles of riparian
revegetation will be needed. The actual length of shading requirements will depend on the
existing conditions for the reaches targeted.
nRA~
CITY OF ASHLAND
Page J 1
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN . !,<~.~
With over 27 miles of riparian area, over 80% of which are in the mid to high-potential range,
the data show there are sufficient revegetation opportunities along Bear Creek to meet
reduction targets. For the purpose of this analysis, two conservative assumptions were
made: first, the Solar Load Change actually projected is reduced by half to account for
planting along only one side of the stream bank; and second, DEQ requires that the load be
reduced by half again to cover risk factors of temporal loss and uncertainty.
Under this alternative, the temperature of the effluent is not cooled prior to discharge. This
creates the potential for near field (local) impacts to aquatic habitat that must be accounted
for. To address these concerns, Keller Associates has worked closed with regulatory
agencies, the City, and other stakeholders to develop a plan that will work. This includes the
following improvements intended to address near field concerns:
. Relocating the outfall from Ashland Creek to Bear Creek. Keller Associates proposes
that this be completed via an open channel arrangement that would convey treated
wastewater to Bear Creek via a side bank discharge. Based on modeling completed
by DEQ, this single improvement would alleviate all near field concerns with the
exception of potential migration concerns in September (there have been a few days
in the last fIVe years that would require the effluent temperature to be lowered from
23.5C to 22.3C in September). Using an open channel conveyance could further cool
the effluent via shading and interaction with shallow ground water.
. Modifying the existing wetland pond. While this improvement may not be required to
meet DEQ thermal load improvements, the wetlands could further serve to cool the
effluent and improve aquatic habitat. The existing pond is too deep to encourage
growth of vegetation and additional shallow groundwater interaction that would further
cool the water. Creating a shallower wetland could support growth of wetland
vegetation that would further cool the effluent. Additionally, ODFW has expressed a
desire for off channel habitat which could be provided through properly designed
wetlands. The final size of the wetlands may need to be expanded depending on a
number of issues yet to be determined such as hyporheic action, shading in the
channel and wetlands, and other shading activities along Bear Creek upstream of the
outfall, and additional flow and temperature data.
. Other improvements that could be added into this alternative to improve conditions for
fish include: 1) removing the current outfall structure which allows fish to enter the
effluent pipeline of the WWTP (and possibly be trapped), 2) constructing a fish barrier
(i.e. waterfall) in the new discharge channel from the WWTP..3) modifying the existing
pond by replacing/removing inlet and outlet structures.
The Oregon DEQ has expressed support for temperature shading as a means for meeting
thermal compliance at WWTPs. Other benefits of this alternative include:
. Low capital and O&M costs. On-going power costs associated with other alternatives
. such as cooling towers can be avoided. Costs are also spread out over the duration
of the project.
. Flows remain in the stream for improved conditions for aquatic habitat during low flow
periods.
. Shading along the creek also improves aquatic habitat.
. Other aesthetic and environmental benefits associated with trees.
nRAn-
CITY OF ASHLAND
Page 12
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN
I2l. KELLER
W eaaocda&a8
An estimated cost for this alternative was prepared with input from The Freshwater Trust, and
has an estimated net present value of approximately $2.7 million. Actual costs could vary
depending on the final sections of river that are targeted for shading and the final scope of
improvements targeted for the outlet relocation and wetlands work near the treatment plant.
10.4.4 Option 6: Blending / Flow Augmentation
The concept of blending or flow augmentation involves releasing cold water upstream of the
Ashland WWTP. The source of this water would be either flow from TID (ideally from lower
depths of the Emigrant Dam) or from Ashland Creek. The City of Ashland is currently in the
process of permanently securing an additional 600 ac-ft of additional water rights formerly
belonging to the City of Talent. The purpose of this right would be to augment existing flows
in Ashland Creek and/or provide additional potable water supply. One of the benefits of this
alternative is that increased stream flows could improve stream conditions in Ashland and
Bear Creeks.
For flow augmentation to work, the water quality and temperature conditions of the
supplemental water need to be considered. This study does not include a comprehensive
evaluation of these parameters. However, the City did install a temperature monitoring
device in the TID system for about a week in August of 2010. Based on this temperature
data, flow in the TID system already exceeded the target temperature thermal limits (180C)
and therefore would not be able to cool Ashland's effluent to levels that met the TMDL
standard. Additionally, it should be noted that if flow augmentation were used, that DEQ has
indicated that they want to see information on presence of parameters in the source water for
which Ashland and Bear Creeks are water quality limited (see 1992 and 2007 TMDLs) and
additional parameters may be needed depending on origin of source water.
Given the need for additional potable water rights and the preference of the City to use
Ashland Creek water over TID supplied water, it is unlikely that if additional Ashland Creek
water rights could be s'upplied, that these rights would be used for flow augmentation during
critical low flow conditions when they would be needed the most for flow augmentation.
While flow augmentation may help mitigate thermal impacts during certain times of the year,
Keller Associates does not recommend this as a sole solution to address excess thermal
loads.
10.4.5 Option 7: Hyporheic (shallow groundwater mixing)
The hyporheic zone is the region where shallow ground water interacts with the surface water
in a stream or river. Depending on numerous conditions (e.g., channel geometry, soil
characteristics, diurnal variations, season, etc.), the hyporheic exchange can act as a buffer
for river temperatures and/or as a mechanism to coollwarm river temperatures. Using a
hyporheic discharge was previously recommended for future study as a disposal option for
temperature control.
Implementing this process can take several forms, which can be divided into either a direct or
indirect injection into the water table. Each application must satisfy the following
requirements [5]:
1. Definition and maintenance of a Waste-Management Area (WMA), which defines the
confines of the infiltrate influence (Chart 10.5). The WMA must be situated so that the
infiltrate remains within the confines of the property and does not affect existing wellS.
nRA~
CITY OF ASHLAND
Page 13
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN
.!,<~.~
Also, it needs to be shown that the infiltration will not contaminate the
groundwater/aquifer.
2. Site/soil suitability, primarily that the hydrology of the site would permit the injection of
the proposed quantity of effluent.
3. Public acceptance of the practice.
Chart 10.5 - Waste-Management Area [5]
y=
Limit
Groundwakr/Smface
Wattf Interbtt
"DiIIbs..-"
F'ig1In 1
Piau \'Iow Scbomatic
IDdlrKt D1"'bargo Modol
To SnrfDU \Vatf'r
Shop< md dowu st=m limit
ofll1o Mixing:zo..IO 1><
_ by tile Mixing
Modrl md st=m dl'o=.:$.
Notes:
I. At L. provick grouncIwattt \"OImDt. \~lot:dy and C'OOttIltratioa ottcy wattr quality pa:nmtttrs for mixing zone
modd. These typically will 1>< _ bas<d ..._... modeIiDg.
2. L fimctions as a.snrbce wattf d:if't'bser.
3. EtOumt ~ in the Wask-~ Aro. em. br in gronwtwa1rf. hypolbric wakr. or both.
4. IimiIs ofWasro-Mzug..".", A=... d.~ by_~ of tile _ in grooo<Iw>....
hypodlric ...... en both. .
Symbols:
E}j Verification monitoring \\-eD locatioD (i.e.. dmtcttan monito1'lng \\'t:U)
ex COI1Ceotr.Ition of try ".ok:w.ta dDumt ............tus..
Cy Concmtmion of try efIbxnt ~ in grouncIwattt Of hyporll:ric wattr at trmsitioo. to surface W2tft"
for mixing zom: analysis. t_g. (uw.~.tioD COt di1fusn- at L.
L l.atgthofW..~^,"."'=ri\-ingwmrbody.
While the effluent temperature could conceivably be reduced through dispersion and
conduction with ground water, this relationship cannot be adequately desc~bed without
sufficient site data. A rough, preliminary design can be completed using semi-conservative
values, which can be used as a basis to formulate site parameter investigations.
nRAFT
CITY OF ASHLAND
Page J 4
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN . ~~.~
A planning level evaluation of this alternative was completed for Ashland. This section
includes summary information. For more detail refer to Appendix XX. A preliminary
evaluation of the Imperatrice property was considered. However, due to the low permeability
of the Imperatice property's soil, potentially shallow soil depth, significant slope, and
incOmplete WMA control, the site would likely not be well suited for effluent infiltration and
hyporheic exchange.
The hyporheic option could be implemented at other sites in close proximity, assuming
property acquisition was a possibility. Soil maps from the National Wetland Inventory
indicate substantial soil type differences in the valley, namely the presence of sandy
characteristics in some areas. Sandy soils typically have a higher permeability rate, with
typical values ranging from 0.13 to 12.96 in hr" for clayey sand. Over this range of values,
the foot print for each MGD of effluent would be between 780 and 8 acres (assuming 15 ft of
head and 300 m spacing between the river and the infiltration basin). These areas only
include that needed for the WMA; due to plot dimensions, considerable additional property
would likely be purchased as well.
If this option were pursued, the following phased approach should be completed in stages,
obtaining more and more detailed estimates of the site characteristics, while minimizing
potentially unwarranted expenditures. Initial sample planning should be based on the
aforementioned design, first assessing if the City owns property that could be isolated
enough to satisfy the groundwater protection requirements while providing an adequate
footprint for the above design. Behind each stage is a progressively more accurate model of .
the groundlhyporheic water flow and the river mixing, which determines the viability of the
design and directs subsequent investigations. We would recommend the following approach,
each phase of which could be conducted in stages:
Phase. 1 - Initial Site Assessment and Monitoring Well Installations
A preliminary assessment of the sites suitability for this approach can be completed by
installing ground water monitoring wells throughout the site, as directed by the preliminary
design. Placing the wells near the creek's edge as well as toward the site's boundaries will
allow the wells to be used in the future for compliance testing, assuming the site is suitable.
Recording soil properties and water levels in the drilling processes of the wells should
provide a rough approximation of the site's geology and groundlhyporheic water state.
These parameters could be used to estimate the site's infiltration capacity and subsurface
conductivity. With these estimates, a rough design of the infiltration basins could be
completed, balancing the need to minimize the waste-management area while maximizing
the distance between the infiltration basin and the creek.
Phase 2 - Single and Multiple Well Aquifer Tests, Mixing Model Precursors
Assuming that the preliminary design completed using the estimated site parameters were
viable, a more refined estimate of the site hydrology should be completed. To accomplish
this task, wells should be drilled according to the predicted design, with locations in the
infiltration area(s). Single well aquifer tests should then be performed to obtain actual
conductivity information for the site, using the previously installed monitoring wells to observe
the site's response. Using the results from these tests, the actual distribution of site
conductivities can be more accurately estimated. These values can then be used to refine
the previously developed model to reassess the site's viability. Tracer studies could also be
used to determine ground water flow and dispersion.
nRAFT
CITY OF ASHLAND
Page 15
_ COMPREHENSIVE SANITARY SEWER MASTER PLAN .. ~~.~
The Oregon DEQ requires a mixing model analysis to be performed to determine the impact
of the hyporheic exchange on the creek temperature profile, to estimate the mixing effects.
To approximate these effects, the creek profile should be approximated over the range of
available property, determining cross section profiles, depth, and velocity. An estimate of the
hyporheic mixing capacity would also be of help. As indicated by the research of Lancaster
et al.[6], if properly distanced from the creek, the injected heat should not substantially impact
the creek temperature.
Phase 3 -Long Term Monitoring
Provided that the refined design was still viable, the behavior of the groundwater should be
observed to determine seasonal variation and response to rainfall and creek flows. These
observations would provide additional insight into the actual response of the site to real
infiltration, allowing further calibration of the model and verification of the groundwater flow
direction and velocity.
Phase 4 - Scaled Infiltration Test
Using a full scale design based on the estimated infiltration capacity and ground water
response as a guide, a large scale infiltration test would provide a final model verification
prior to full construction.
Using this approach, the capital investment required for an accurate model (which is
expected for permitting [5] could be expended in stages, each of which would. allow for the
overall evaluation of the process, to determine if further investment is warranted.
Other Hyporehic Considerations
It should be noted that hyporehic activity can also occur through leaky wetlands. Thus some
hyporehic activity could occur if the City's existing effluent outfall were relocated from
Ashland Creek to Bear Creek via a channel and possible downstream wetlands.
10.5 SUMMARY AND RECOMMENDATIONS
Table 10.2 on the following page summarizes the disposal alternatives, benefits, drawbacks,
and costs. Based on the available information, Keller Associates recommends that the City
proceed with Option 4, Trading (Shading). Concurrent to pursuing Option 4, Keller
Associates recommends that the City pursue recycling as needed to address future potable
water supply needs.
nRAI'T
CITY OF ASHLAND
Page 16
February 2011
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
euoai.C88
Table 10.2 - Ashland WW Disposal Opflon Comparison Chart
Not
DescriptIon I Capital Annual Present
- Option _ PrSlJect Ek.!"ents B~~lts - Drawbacks - - Cost Cost V,!II,l~mments
lA Maximum Irrigate 433 acres Beneficial use of water. High Cost. $10.8 M $(58,000) $13.4M Savings
Reuse on with treated Existing water right could lower stream flows. assume that
Imperatrice effluent. be used to augment membranes
Property Pipeline to site. potable water supply. are not used.
138-166 MG Potential for membrane
storage. and chemical savinp.
Shoulder season Mitigate concerns of
storage required .future- more stringent
I winter regulations.
dischare:e.
18 Partial Reuse lower cost does Similar to Option 1A. High Cost. $5.3- $35,000 $5.8- For lower
on includes Improvement could be Introduces complexities in 8.9M 9.4M cost range,
Imperatrice minimum completed later if Option monitoring and wastewater need to add
Property - storage. 3 or 4 is pursued. management. cost of
424 ac*ft/yr Higher cost Higher o&M costs than Option 3 or 4
assumes more Option lA. to address
storage, and Reduced stream flows rooting
periods of no available for aquatic habitat. requirement
discharge.
2 Discharge to Pipeline to Mitigate "near field" Not a standalone solution Not Not Not
liD Talent Canal. concerns. still need to offset excess Evaluated Evaluated Evaluated
Reduction in chemical thermal loads.
costs. High opposition from
downstream users
antidpated.
District concerns about
chemicals.
Storage for shoulder seasons
likely required.
Schedule and approval
outside of Cltv ~ntrol.
3 Cooling Tower Mechanical Addresses temperature Olillers required for hottest $6.1- $200,000 $8.6- Cost range
cooling tower. concerns. periods. 8.1M 11.6M reflects use
Storage facilities. Allows continued Upstream I downstream of ponds
discharge. storage also required for versus
Maximum control In night~time operation concrete
terms of compliance storage
schedule. reservoirs
4 Trading B miles of lowest cost alternative. Some uncertainty- $3,400,000 spread out $2.7M
(Shading) shading. Allows continued participating property over 20+ years
Channel to Bear discharge. owners to be identified;
Creek. Improved aquatic habitat migration blockage
Constructed and other environmental evaluation to be completed.
wetland pond. benefits. Potential minor additional
local coolinll reouired.
5 Blending I Blend additional Additional stream flow. Cannot meet temperature Not Not Not Not a viable
Flow water discharges targets by itself. Evaluated Evaluated Evaluated alternative.
Augmentation from Ashland Uses water that could be
Creek or TlD. used for potable water usage.
Additional water quality
testing may show additional
water quality concerns.
6 Hyporheic Subsurface Low operations costs. Difficulty in locating site with Not Not Not
(shallow disPosal of Simple technology. suitable soils. Evaluated Evaluated Evaluated
groundwater) treated Significant additional effort
wastewater to required to determine
shallow ground feasibility.
water. Potential large land
requirement.
nRAH
CITY OF ASHLAND
Page 17
February 2011
COMPREHENSIVE SANITARY SEWER MASTER PLAN
KELLER
.1I8OCd.~
References
1. John Gasik: City of Ashland Excess Thermal Load Umits, WQ File No. 3780, ODEQ
Memorandum, February 16, 2011.
2. Carollo Engineens: City of Ashland Updafe to WWTP Facilities Plan and Permitting
Evaluation, Temperature Management and Wafer Recycling, November 2009.
3. Carollo Engineens: City of Ashland Wastewater Treatment Plant Upgrade Project,
Project B - Offsite Facilities Predesign Report, November 1997.
4. Carollo Engineens: City of Ashland Water Conservation & Reuse stuc:/y (WCRS) &
Comprehensive Water Master Plan (CWMP), Technical Memorandum No. 7 -
Recycled Water Regulations, September 2010.
5. Oregon DEQ (2007). Disposal of Municipal Wastewater Treatment Plant Effluent by
Indirect Discharge to Surface Water via Groundwater or Hyporl1eic Water. Internal
Management Directive.state of Oregon Department of Environmental
QualityPortJand. 2007.
6. Lancaster, S., Haggerty, R., Gregory, S., Farthing, K.T., and Biorn-Hansen, S.
Investigation of the Temperature Impact of Hyporl1eic Flow: Using Groundwater and
Heat Flow Modeling and GIS Analyses to Evaluate Temperature Mitigation Strategies
on the Willamelte River, Oregon. Final Report to Oregon Dept. Environmental
Quality.Oregon State Univensity, Corvallis. 2005.
nRAFT
CITY OF ASHLAND
Page 18
~
r4
m:m
State of Oregon
Department of
Environmental
Quality
OREGON DEPARTMENT OF ENVIRONMENTAL QUALITY
Memorandum
WESTERN REGION - MEDFORD
To:
Ashland STP File
Date: February 16,2011
From:
Jonathan Gasik, MS, PE, Senior Engineer
Western Region Medford Office
Subject:
City of Ashland Excess Thermal Load Limits
WQ File No. 3780
BACKGROUND
The Ashland WWTF discharges into Ashland Creek .approximat~ly 1600 ft (490'1JI) fr9m its
confluence with Bear Creek. Although Ashland Cieek'isnot currently on the 2004/2006 303(d)
list for temperature, a review of temperature logger datilJrom Ashland Creek abov'e the WWTF
discharge point indicates that the stream should be listed yeir,cround for an exceedance of the
applicable temperature criteria (Table] 6),,11) July 2007, DEQ.finalized the Bear Creek
Watershed TMDL. The Bear Creek TMDLailocates the Ashland WWTF a O,IOC increase
(HUA) above the applicable criterion in A~hiaild <;:ieek as well a~'at the point of maximum
impact. The TMDL also states that "As part of the NPDES' permit renewal process, the city of
Ashland may wish to compute daily or monthly,theritlal wa~te load allocations based on the
applicable standard, actual rece'iyjng water flows,: imd actual WWTF discharges,"
, . l ..
In April 2008, DEQ i~s!Jed the Te!Jiperature Stanaard Implementation Internal Management
Directive (IMD). This memo will 'use the methods'described in the IMD to calculate Excess
, ,. ~, , ,
Thermal Loads based on the 2008 Bear. Creek TMDL, and evaluate whether the Ashland WWTF
can immediately comply with the' ne~ Exf~~~,Th~rmal Load Limits. I
.. ". . , . '. ~
EXCESS THERMAL LOAD LIMits
For point' squrces, TMDL wasieload ailocations (WLAs) are implemented through effluent limits
in NPDES p'ermits. Thermal WLAs are expressed in permits as thermal load limits, Because the
TMDL is based on aHuman.lJse Allowance above the applicable criterion, the thermal load
limit is known as an' excess tllermalload(ETL), As mentioned above, the TMDL allows for the
thermal limits to be based'on various river flows. Therefore, DEQ may calculate ETL limits
based on critical case low-flows or actual measured flows,
As described in the IMD and the TMDL, the thermal WLA can be converted directly to ETLs
using the following equation:
Thermal WLA = HUA · (Qps + Qr) · c
Where,
HUA = Human Use Allowance
Qps = Point Source Effluent Flow (cfs)
Qr = upstream river flow (cfs)
C = conversion factor (2,446,665 kcal's/ oCft3'day)
City of Ashland Excess Thermal Load Limits
February ]6,2011
Page 2 of 13
Criticallow-Ilow based limit: A conservative approach would be to use a critical low river
flows (Qr) to calculate the WLA and apply this WLA directly as an ETL limit for each water
quality limited season; summer (May 16 - Oct 14) and spawning (Oct 15 - May 15), The critical
low flow is the lowest seven day average that has a 10 year recurrence (7Q 1 0). This approach
has the advantages of simplicity and that no additional information in needed, However, it may
be overly conservative and may result in an unnecessarily restrictive ETL limit. For Ashland
Creek, the critical low-flow based ETL limits are as follows:
Month Applicable Dry Receiving Hnman WLA Effluent
Criterion Weather Water Use 2 Temp
(MW)
0 Design 7QlO Allowance Limit
C HWLA
Flows I 0 0
CFS Q CHUA CT
CFS Qps R WLA
May 16- 18C 3.65 I ~ O,IC :.055 18.13
Oct 14 . .
Oct 15~ 13C 3.65 3: : O.IC .079 13.18
May 15 "
-
, .
The TMDL WLAs are in megawatts, but the Temperature]MD directs staff to calculate the ETL
limits in kilocalories. Therefore, the critical low-flow based ETL limits are 788 Kcal and 1132
Kcal, for the summer and spawning season,s respec~ively. ':, .
Actual Stream Flow-based Limit: The ETL'limit may.also be based on the actual stream flow.
,.. ".,'
In this case, Ashland would need to collect and report stream' flow data. The ETL limit would be
calculated by direct conv,ersion .oft,he WLA usin'g'the equations above:
Excess Thennal Load (ETLj,
(Year Roun(!) _ ,
Limitations
Shall not exceed a rolling seven-day average based on the
. - .
.equation: -!O:n: =: (Qps + Qr) * 0.245 million kcalosf oCoft3oday
Parameter
" .
Where,
Qps = Effluent Flow (cfs)
r= u stream river flow cfs
EXCESS THERMAL LOAD'(ETL)
The ETL calculated using th7: following equation:
Thermal Load ":': 9Ps* t> Pc
Where, Qps = point source effluent flow
t>T = difference between the effiuent temperature and the applicable criterion (Te-
T criterion)
C = unit conversion factor (2,446,665 kcal'sl oCft3.day)
As discussed above, the applicable criterion is either the biologically-based numeric criteria or
the natural thermal potential (NTP), whichever is higher. Ashland Creek was not Heat Source
modeled by DEQ as part of the temperature TMDL. In the absence of modeling the temperature
criteria that applies to Ashland Creek is 13.0oC (55.40F) October] 5 through May 15; 18.0oC
City of Ashland Excess Thermal Load Limits
February ]6,20] I '
Page 3 of]3
(64.40F) May 16 through October ]4 (Biologically Based Numeric Criteria OAR 340-0041-
0028).
The ETL is calculated as a weekly average by using the seven day average of the effluent flow
and the seven day average of the daily maximum effluent temperatures.
The City of Ashland collects daily effluent flows, effluent temperatures, and receiving stream
(Ashland Creek) flows. The following table shows a comparison of the maximum ETLs with the
critical case based ETL limits:
Month Critical Low flow ETL Maxim.um ETL
Limit
May]6-0ct 788 Kcal 46,000,000.kcal
]4
Oct 15 - May I ] 32 Kcal 45,000,000 kca] .
15 , .
As mentioned above, the TMDL allows for the thermal limits to be based on various river flows,
The following charts use data from Ashland WWTP's discharge monitoring repol1s. from 2009 to
show the flow-based ETL limit and the ETL. .
Summer Thermal Limits
50
45
40
~ 35
."
~ 30
~ 25
c:
~ 20
:E 15
10
5
o
-Ell
--------
- - Ell limit
~ m m m m m m m m m m m m m m m m m m
~ 0 0 0 0 0 0 0 0 000 0 0 0 0 0 0 0
c ~ ~ 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2 2
......................---------..............----
~ N ~ 0 m ~ ~ w q ~ N ~ m 00 ~ w ~ ~
N_~NN_~N_~NM_rlN-rlN
_~___~__ro___m__o__
~ ~ ~ w ~ ~ 00 00 00 m m rl 0 0
~ ~
City of Ashland Excess Thermal Load Limits
February 16,2011
Page 4 of 13
Spawning Season Thermal Limits
SO
40
> 30
'"
." 20
.....
..
u 10
...
"
~ 0
~ -10
-20
-30
-Ell
- - Ell limit
vmmmmmmmmmmmmmmmmmmm
~ooaoaoooooooooooooo
00000000000000000000
NNNNNNNNNNNNNNNNNNN
........................--.......................-----------
~NNM~~rommo~N~~Nm~~~
MN_.-iN_.-iN_N_.-iN_.-iN_.-iN
__N__~__~_~__~__N__
.-1M NN mm q UlO.-i..............NN
.... .-i..... .........
,., .
As can be seen by the charts above, the current ETL exceeds the ETL limit during both the
summer and spawning seasons. '-; '. _ . -::': .
Existing Facilities and Strategies for Temperature Managem'ent::,.:,
Recognizing that significant thermal reductio~~ w~~ldbe re9,!ired ~y'the Bear Creek TMDL, the
City began exploring options i~ ?006 with the' formation Of aiJ'ad hoc committee. The
committee's goal was to explor~ options to meei!he proposed thermal limitations with an
emphasis on water recyCling. Th'e.€ity continued-to work on options and in November 2009
completed a report whicp il]c1uded'4:strategies, cost e.stimates, non-economic evaluation, and a
recommendation. The follo~in.g t~ble i~ a ;mmmartofthe report:
-
Strateg Strategy Description Capital Present Non-Economic Evaluation
y Cost Worth
Cost
No'. I - Effluent Cooling in ; . $2,500,00 $2,540,00 Proven technology. May need
mechanical cooling 0 0 storage ponds for critical
towers' : . periods,
No.2 No discharge with $1,600,00 $1,630,00 Poor local public perception
effluent reuse via 0 0 regarding reuse, TID's
discharge to Talent irrigation season does extend
Irrigation District Canal into Fall.
(TID)
No.3 No discharge with $11,700,0 $1 ],750,0 Supplements City water supply.
effluent reuse in City 00 00 Poor local public perception
identified properly regarding reuse.
No.4 Discharge to hyporheic $2,600,00 $2,600,00 Maintains stream flows.
water 0 0 Opportunities to improve
riparian zone. New strategy,
unproven,
City of Ashland Excess Thermal Load Limits
February 16, 20 I I
Page 5 of 13
The report recommended pilot study to further evaluate Strategy No.4 (hyporheic discharge). If
this study shows that hyporheic discharge has limited potential to address temperature issues in
Ashland Creek, the recommendation is to construct a cooling tower. Regardless, the report
recommends that the City continue to work with the TID to identifY opportunities for taking
recycled water into the TlD system and using stored water to offset flow impacts of effluent
withdrawal.
Tbermal Plume Analvsis
In addition to the temperature criteria, the mlxmg zone rule contains limitations regarding
thermal plumes. In accordance with OAR 340-041-0053(2)(d), temperature mixing zones and
thermal effluent limits will be established as necessary to prevent or minimize the following
adverse effects on salmon ids: . . .
A) Impairment of an active salmonid spawning area where spawiling redds are located or
likely to be located.
B) Acute impairment or instantaneous lethality: .
C) Thermal shock caused by sudden incre~se in water temperature. ,.
D) Migration blockage caused by temperature .differential between the"pliJme and the
receiving stream. ,- ., .
The following chart shows the minimum"maximum, and average effluent temperatures reported
on Ashland's Discharge Monitoring Report~' fi'om ' . :
- .
.,'
Ashland STP Effluent Temperature
25
20
u
~
"
"
tic 15
"
o
- -
10
5
Jan
Feb
Mar
Apr May Jun
Jul
Aug
5ep
Oct
Nov
Dee
The City of Ashland collected stream temperature data from July 2004 to August 2005. The
reported stream temperature exceeded 300C on several days. However, due to the sudden jump in
the temperature, these appear to be periods when the temperature sensor was exposed to air, and
not the actual water temperature, Excluding these periods from the dataset, the Ashland Creek
temperatures are as follows:
City of Ashland Excess Thennal Load Limits
February] 6, 20] 1
Page 6 of ] 3
Ashland Creek Temperature (7 day average)
25.00
... .....................................................................1.........1......:.........................................
20.00 - --I'
--- ......
, ,
,
~ 15.00 ,,'"
..
..
~
..
..
o
10.00
5.00
0.00
.,~ .,~
~.:;j ~v
"\'b <<.~
is
.,'
~
~~
~<i
~.,,,-
,,'"
\V
.s"-
~
~ rz}
~ ~'O
'I:?-';:; ~e;
<,"'''1
~
if'
C'
o
e" rz}
.-? ~'O
,.:::."'" (..e
~o ()e
In previous studies, DEQ estimated the 7Q 10 /low in Ashland Creek at ] cfs. Since that time, the
City has collected almost ] 0 years of /low. data. The following table shows the lowest seven day
average stream /low, the average STP /low, the average stream temperature, the average STP
temperature, and the calculated stream temperature aft.er mixing by 1110nth:
Month Lowest seven Average STP . .Average. ' Average STP Stream
, ...
day averag~<; .,/low (mgd) . UpStream.' Temperature Temperature
stream /low . . Temperature after complete
(cf;{. . ,
. . mixing
Januarv 1.36 , . 2.49 ',' 4.86 ]3.39 ]1.16
February 1.66 . . " .2.35 . . 5.22 ]3.47 10.88
March : :..... ',0.98 . , 2.27' 7.01 ]5.70 ]3.80
. .
April ',1.67 " 2.19 8.64 ]7.0] 14.25
May'. '0:87, ',2.22 ] ].02 ]9.99 18.]7
June -: , 0.87, 2.08 14.83 22.06 20.52
July '. , 1.77- 2.04 18.83 25.40 23.04
August , ].22, , 2.0] 20.5] 25.40 24.02
. . ~
. .
September ',. . ~ ].66, 2,02 17.06 23.50 21.27
., .
October <';',l.f4 2.00 ]2.67 21.79 19.33
November ;. 1.13 2.01 8.55 18.36 15.75
December 1.11 2.30 5.25 ]4.74 12.49
Impairment of spawning is prevented or minimized by limiting potential fish exposure to
temperatures above ]3 degrees Celsius [OAR 340-041-0053(2)(d)(A)]. The area in the
immediate vicinity of the discharge is an active spawning area for winter steel head, summer
stee]head, resident trout, and coho salmon. Figure 271 B of OAR 340 Division 4] designates
Ash]and Creek as'spawning from October 15 through May 15.
City of Ashland Excess Thennal Load Limits
February] 6, 20] ]
Page 7 of 13
Because Ash]and Creek is so small, there is currently no regulatory mixing zone or ZID assigned to
the wastewater treatment plant. The discharge is currently configured so that the discharge
transverses the entire stream almost immediately and DEQ is not able to allow any significant
dilution in the ZID. Therefore, because the effluent exceeds 130C during all of the spawning period,
the effluent has the potential to impair spawning. Additionally, the .tab]e and charts above show
that the effluent causes entire stream to exceed the 130C during March, April, May, October,
November, and December.
Active Acute impairment or instantaneous lethality is prevented or minimized by limiting
potential fish exposure to temperatures of 320C or more to less. than two seconds. Acute
impairment requirements are met because all of the City's effl,uent temperature data was
below this temperature. The highest effluent temperature recorded'is26.30 C on 7/27/2003.
.. .
Thermal shock is prevented or minimized by limiting pD,ten.tiill, fish exposure to temperatures of
250C or more to less than 5 percent of the cross section. of the water body, ,unl.ess the upstream
temperature is above 230C. Migration blockage is prevented or minimized by limiting potential
fish exposure to temperatures of 2] oC or more to.le);"s.than 25 'percent of the cross'section of the
water body, unless the upstream temperature is above'Zfoc. ,-:. "
. ",.. J.
',.' ","
The figure above shows that ,the seven day average stream~.tell)perature does not exceed 230C.
However, there are periods in July and August. that are above.21 ~.c. The table below shows the
calculated stream temperatures based on the Iciwest.7 day average stream /low, the average STP
flow, the highest 7 day average STP temperature':an<J.!he aver~g~ stream temperature after
mixing with 5 percent and 25 percent of the ;stream.'fl6w: ;P.eriods' when the stream temperature
was 21 oC or greater were 5xcluded from the 25 ,~!lrcent calc~laiion:
"
Month Stream,Temp Stream Temp
after'mixing. after mixing
"
with 5% . with.25%
January 13:24 12.69' . .
February:- 13:29 :', . : 12.62
March' ]5.58 15.13'
Abril" ;.: ]6.81 , 16.10
May 19.87 19.45
June , 21.96 21.60
July -25.22 23.38
August 25.29 23.79
September 23.33 :- 22.74
October 21.62 21.02
Nov'ember 18.18 17.54
December 14.60 14.06
1.>~'"
..>
The table above shows that the effluent has the potential to cause thennal shock during June and
July and cause a migration blockage during June, Ju]y, August, September, and October.
Therefore, effluent temperature limits are needed to mitigate potential spawning impainnents,
thennal shock, and migration blockage concerns.
City of Ashland Excess Thennal Load Limits
February 16,20]]
Page 8 of 13
Calculation of Thermal Effluent Limits Based on Thermal Plume Requirements in Ashland
Creek
SPA WNING IMPAIRMENT: Per the TMDL, the ambient temperatures in Ashland Creek are
above 130C during late October. Therefore, per the IMD, the spawning criteria and the human use
allowance of 0.1 oC, rather than a thennal plume limitation, will detennine penn it limits. These
limits would be temperature limits, in addition to load limits, to prevent spawning impainnent. The
temperature limits are as follows: '
Te = (Tc+HUA)(Qe+Qr)-Qr*Tc)/Qe
Where, HUA = O.loC
Qe = Effluent Flow in cfs
Qr = Stream Flow in cfs
Tc = applicable numeric criterion = ] 30C
THERMAL SHOCK: Pursuant to the Temperatur~. Standard Implementation IMD; .the. following
fonnal should be used to prevent the temperature of Ashland Creek from exceeding' 250C after
mixing with 5% of the 7QI 0 low flow: . : :. . .
Te = D (25-Tr) + Tr
Where, D = dilution = (Qe +0.05Qr)/Qe .
Tr = 7 day average upstream tempeniture in:oC
From the above analysis, thel1)1al shock limitations are only applicable July and August.
.
MIGRATION BARRIER: PU';suilnt to the Te!l1perature Standard Implementation IMD, the
following fonnal should be used to prevent the temperature of Ashland Creek from exceeding 2 JOC
after mixing with 25% of~e 7QI 0.10:-" /low: ..
Te =: D(2I'.Tr) + Tr
From t~e.above analysis,.~ig~ation barrier is only a concern during June through October.
SUMMARY OF THERMAL LIMITS FOR ASHLAND CREEK DISCHARGE
Montb .:' : Temperature Temperature Limit Temperature Most
'Limit (oC) based (oC) based on Limit (oC) based Limiting
"'. ,
on spa~ning tbermal shock on migration criterion
imoairment blockal!e
Januarv .13.15 na na Spawning
Februarv 13.17 na na Spawning
March 13.14 na na Spawning
April 13.18 na na Spawning
May 13.14 na na Spawning
June Na na 30.93 Migration
Ju]y Na 25.27 21.82 Migration
August Na 25.14 22.37 Migration
September Na na 22.79 Migration
October 13.16 na 29.54 Spawning
City of Ashland Excess Thennal Load Limits
February] 6, 20] ]
Page 9 of 13
November 13.16 na na Spawning
December 13.15 na na Spawning
The most limiting criterion would be used to calculate the temperature limit. Note that in addition
to the temperature limit above, the City must also meet the excess thermal load (kcal/day).
BEAR CREEK OUTFALL EVALUATION
The City has also requested an evaluation of the thennal plume effects if the outfall was moved
to Bear Creek downstream of the confluence with Ashland Creek. The eyaluation follows:
The US Geological Survey maintains a gage in Bear Creek downstream of Ashland Creek. 7Q I 0
/lows for each month at this location were derived using the progran;t pFLOW. These values are
presented in the following table: .
, .
. ,
Min of Ashland Creek Flow Bear Creek Below Ashland
Month above outfall (CFS) 7Q10 flow ICfs) ,
January 1.36 . , 13.80 . .
February 1.66 . ' "16.70
March 0.98 19.40
April 1.67 19.00
May 0.87,-: '.' '. 21.40
June 0.87," ',', ,24,10
July 1.77 . . .23.80
AUQust 1.22 , 28.90
September -, 1.66 . ' 9.22
October / . . . '.. 1.14 4.19
November' 1.13 6.50
December' , , 1.11 11.00
",. .,
. . ~"
Since August' 2004; .t:Jie. Jackson' County Water Master has collected temperature data in Bear
" , ~ ,
Creek above the conf1u'ence with. Ashland Creek (near Neil Creek). Using the same
methodology as that for ilie'discharge' into Ashland Creek, the following table shows the Bear
Creek 7Q1O .stream flow, il)e, averag~' 'STP flow, the average stream temperature, the average
STP temperahire,. and the calc~]ated stream temperature after mixing by month:
,. '<< I.
Average of
7 day
, average
, Bear Creek
,
Bear Creek Average Temps Max of Stream Stream
Below of above Effluent Temp Stream Temp
Ashland Effluent Ashland Temper after Temp after
7Q10 flow Flow Creek (Deg ature 100% after 25%
Month (cIs) (mgd) C) (DegC) mix 5% mix mix
January 13.80 2.49 5.15 13.39 6.95 12.14 .9.50
Februarv 16.70 2.35 6.53 13.47 7.77 12.17 9.76
March 19.40 2.27 8.47 15.70 9.58 14.13 11.51
April 19.00 2.19 10.49 17.01 11.48 15.59 13.21
City of Ashland Excess Thennal Load Limits
February] 6, 20 I ]
Page 10 of 13
Mav 21.40 2.22 13.71 19.99 14.58 18.49 16.16
June 24.10 2.08 17.06 22.06 17.65 20.70 18.80
Julv 23.80 2.04 16.80 25.40 17.81 23.04 19.78
Auaust 28.90 2.01 18.76 25.40 19.40 23.29 20.76
September 9.22 2.02 19.90 23.50 20.81 23.04 21.97
October 4.19 2.00 14.04 21.79 17.33 21.29 19.83
November 6.50 2.01 8.86 18.36 11.94 17 .46 15.10
December 11.00 2.30 4.96 14.74 7.36 13.44 10.48
The table above shows that moving the outfall to Bear Creek below the confluence with Ashland
Creek would eliminate thermal shock concerns, reduce that time period when there is potential
migration blockage, and provide opportunities to reconfigure . the' 'thennal plume to minimize
spawning impainnent. .;.' . ....
~ . . .
Calculation or Thennal Effluent Limits Based on Therma/'Plume Requirements in Bear Creek
SPA WNING IMPAIRMENT: Salmon and steelhe~d'spawn in t/1e receiving water' downstream of
the proposed discharge location in Bear Creek, therei~ potentiallYllctive spawning in:the proposed
thennal plume, and the effluent temperature is greater. than ,1,30C.during the spawning season
(October 15 through May 15). Additionally, the upstreanHeinperatures are above] 30C in October.
Therefore, per the IMD, the spawning criteria and the humahbse, allowance of 0.1 oC, rather than a
thennal plume limitation, will detennine' penn it limits in May' and, October. The fonnula for
temperature limits is the same as for the Ashhmd:Creek example. .;.,
Bear Creek is, however, large enough to allow for a small zone of immediate dilution (lID). Bear
Creek is approximately 30 feet wide at the proposeddiscliargt;:poirit. For streams of this size, DEQ
could propose a mixing zone. up' to 60 feet in length and a ZID that is 10% of the mixing zone.
Therefore, DEQ could allow a lID. that reaches approximately 6 feet from the point of discharge.
Using the CORMIX model and assuining that the effluent is introduced into Bear Creek through a 4
foot wide channel flush with.the bank, the dilution atthis point is approximately 1.3:], or about 30
percent of the stream flow. -:':, .::,':. . , .
THERMAt:SHOCK:. From the'aJ>ove analysis, moving the outfall to Bear Creek would eliminate
the po~e?Jial for thennal'shock. '... . .
.. .
MIGRATION BARRIER: From the above analysis, moving the outfall to Bear Creek would limit
the potentia]'for thennal shock to September only. The fonnula for temperature limits is the same as
for the Ashland Creek example:
SUMMARY OF THERMAL LIMITS FOR ASHLAND CREEK DISCHARGE
Month Tenip'erature Temperature Temperature Temperature
Limit (oC) based Limit (oC) based Limit (oC) based Limit (oC)
on TMDL "UA on spawning on migration
criteria and ZlD block3l!e
Januarv 13.46 19.53 na 19.5
February 13.56 19.90 na 19.9
March 13.65 18.81 na 18.8
April 13.66 16.27 na 16.7
May 13.72 na na 13.72
June Na na na na
City of Ashland Excess Thennal Load Limits
February 16, 2011
Page ] ] of] 3
Julv Na na na na
August Na na na na
Septem ber Na na 22.26 22.26
October 13.24 na na 13.24
November 13.31 15.01 na 15.01
December 13.41 18.77 na 18.77
Note that in addition to the temperature limit above, the City must also meet the excess thennal
load (kcal/day),
Water Ouality Tradinl! to Meet Thermal Requirements
The City is considering water quality trading to meet the thenna] requirements discussed above.
Water quality is an innovative approach to achieve water .quality gQals more efficiently than
traditional methods. The proposed trade would involve '1on:point source thennal reductions (i.e.
riparian improvements or other similar thennal improvements): The framework for evaluating
water quality trades is contained in "Water Q!laiity Traqing in NPDES. penn its Internal
Management Directive" (Trading IMD). '
... ., '
Per the Trading IMD, the City may trade their point so'urce'thennal load with non-point source
thennalload within the Bear Creek watershed to the poini'ofmaximum impact, which has been
detennined to be four miles upstream o(t~e.mouth of Bear cre~K:.However, as discussed above,
the City must also meet the thennal plume 'requirements. The Ci'tY may use trading to mitigate
thennal plume concerns, however this m;'tigat;'ort .must, be above. the discharge point. This is
because cooler upstream temperatures are rieeded.tooffset.near field thermal plume impacts.
Earlier evaluations detennined that there is insufficient non-point source reductions available in
Ashland Creek abovtHhe 'disc~afge to offset' 'the thermal load. Therefore, without effluent
cooling, continued .discharge inio: 'Ashland Creek is unacceptable because of thennal shock,
migration blockage: and' sRa:-vning ,i~pairment. '
. .
From the eva]uation'above, if the effluenHs:nioved to Bear Creek, no effluent cooling is needed
. '" .,.~ . . , ~ , -
to eliminate thermal shock concerns. Also, the effluent need only be cooled to 22.30C to
eliminate the migration' blockage concerns. Alternatively, the City may implement non-point
source' i'e~i1ctions upstrearii a~<1 trade 'fo~' it higher temperature limit.
Cooling the'~ffl.uent so that ;ilje temperature of Bear Creek is raised no more than 0,1 would
eliminate the potential for spawning impairment. However, water quality trading allows point
sources to contin~li :10 d\scharge at a higher temperature. So, even though the thennal load is
offset elsewhere in ihe: watershed, the potentia] for localized impacts to salmonid spawning
remains. On option for "establishing temperature limits for spawning protection described in the
Temperature IMD is to re-configure the discharge to disperse the plume and/or maximize
mixing. DEQ has modeled a Fall spawning scenario using the CORM IX model, assuming an
effluent temperature of ] 80C and an upstream temperature of II oC. This model shows that the
plume is buoyant and initially floats over the spawning area. The model shows that the effluent is
cooled to below 130C before it mixes to the bottom of the stream. The following figures are a 3-
D view, a plan view, and a profile view of the CORMIX output:
City of Ashland Excess Thennal Load Limits
February ]6,20]]
Page 12 of 13
~..
'i
//
/'
/
/~....
\
i
.
., ,
~'" ......... ,
,-' ,
'- "
....... ..".
'- '
'......
'"
,,/""
-..",.-..-
~/~
-<-,---
~~~
--
'.""_'.'_''''-'M',
.....,-,.......-,..."
,." ..,.--.,-.".",
='~:::.~
Figure ]. CORMIX 3-D view of side 6~k~ischarge into Bea.r Creek during early spawning
season. _
.
-~~-
~~;(~
"..u.z"'.................'"
.....""....t;..".".,.....,
~:..~::::,t';1,_,.
::::"<='''''''''
Figure 2. CORMIX plan view of side bank discharge into Bear Creek during early spawning
season.
City of Ashland Excess Thennal Load Limits
February ]6,201]
Page 13 of 13
....-...
.--~l_.___ __ ___._...___________~_
.
----~,
-.,....--=---
.~ m.....r
-
---
,._~"....,,",""','''';.,'"'
..........,.."""""";.'..r;
~." ;~ '. " ' ." -,'0 "."~ .
::'i:.-::.:::;.,.
Figure 3. CORMIX profile view of side ba~k discharge into 'B,ellr. Creek during early spawning
season. ., , ;, ~
Therefore, because the effluent is buoyant and because s';me,c!loli~g occurs prior to downward
mixing, a higher temperature limit is allowable for a surface discharge.
- . ' ~ ' " ' . . "
'.
, .
~ ~
~ ~
g'~g
:E~~
'" ,,,. "
~",-'"
=:;rUl
ffi tit 0"
UI a ~
~~~
-'!l1 III
~~~
'" ;0 =>
00<0
g:gm
~;::=>
;:: 2l ~
-. III
"2..3
~ &
~
go
=r
III
=>
"
'"
in'
'"
..
<0
iil
'"
3
'"
=>
or
-c....
:iE....
~
!!!.
."
m
'"
(1)
Q,
~
z z
m m
:;; :;;
Ie
;;
.,
':1
~
~ ~~~I~~~~ ~ ~~Q)~C) ~
-c)> ml:::O "'tJ c;CO--l;::C>Q
l::::J (D CD Q. Ul"'C(ii'm.i!IlCJ
g~ Sl g fJ" Q.g-g~oZo
Om i=i' a 2-.m~..;:J.S:-1
::z:: ~ (I) CD 'T1=, 0 _ _. COlli <:
<D~ 5"'-1' . :Joo :::l!i~
Q) Il::! _ c..... CD l:II :::l Q. n '" -
::!o oa;:- .-c.....m-.o
:J;:J. --1<.30. () CDcn~-a:()O
fOO (D'S 0 CD_. CDN03
ill:J 0 '(DIS' 3 ~ ffi ii'9 ~ :J CD
- ::::T1Il-.tJ:J [D cn(1)::'-n
iilQ)::tI Ul!i'ci3'''I~UlUl~(J)mCD
en ~ ~ () ~_. m ~'" 5 ~a: Q) r- OLctI~ 5i n :J
o,~o. - . :::::J-' ,-<; -
CIlUl5.'~~g'.~~.!.=-&l~ .C!:::O~
CD Q) Q) CD '''''1 .,.........,.,.. :::l ~ ..... 0-
::t :::J ,~, -:::I Q) ::I: ....'1 CD' ....'1 (II CD ..... ~ G>
s'o.OC;;::::lI 0<0 <DO _-)>
f.Cco~.,g:::03~3 o~ 5 b
<n~co=r3~3 -'(1) s:
~ 0 g :::J '~~~-'13~-' ~ ~ ~
Q.::::::::: C1Q)'~<D'm"O::3 F-
eto:!!: ~-:::J a=
coo CD CD)>3:'l-3:' <1i)
< men" _ a. CDl "'t ""
CD ~ =to 03:CD :CD ;:::;j
;l,....,;! m:r'" '" 0",
"'"'I~~' 'cl,:::l ::::lI (II ~
mro::, a:r.n !!.S::
CIl g.~ i'~
'i: a~ CD ~
~ I ~
liP
I I I
I I I
I: III
III ~
I Igl
Ii Igl
~
-c
Q.
f,j
I,
I
~,
"'ji
:::0" g UI
mJ:Z(;)
CJ)
"'0")>---,"'011
:iE:iE~~:iE~
-. =>
=> g
z z z
m m m
:;;:;; :;;
~ ~;c ,,::tI-c ~
"T1:!! ~J:m:I: rD
zz
;0
'"
'"
o
~
o'
=>
'"
~
5'
<0
C'
"
'"
5'
'"
'"
'"
:;;:: ~c:;;~ ~ ~ 0 (O(XI--.JCJ) Ul ,J:o. wl\J~'I--f!ll
(0 ~ ~,: ~
~ ~1~~~~gQ~~~~~~?~~ , ~I
~ ~ oao~c~~~Na~~~mo 0"
5" ~ ~~~~~gg~~~a<~a<o~ ~
I - -~0~=cI-O- 0 -3'~ CD
ro ~ 2?j g 8' a ~ 9: ~ CD CD ;::0 ~ ~ 5" ~ ~ 2t"\ cr
~ mCb(D:J~roo~o(ij3o-accr;. ::J
5" 0~~croCo::J5~~m~~-m::J ~ 0
~ ~~m0..&ga~o~~o~roQ>o~~ ::Jmj
o m~I~~>a.m::Jroo::Jm~S'>~::J~ o~
::J (limen -o01::Jcn::Jm~ O'Cil:r>;me>oc::a:
~~mUl~~cnI ::J O~~::J 'cn~~~85~
(ij~&~~CO cn~om~~~ m3~g~lcrr~1
@ ~ ;;? ~f2. @ ~ 5 ~ ~ (it ~ ~ ~ (1) m 0 5. G; en
5f = X- '~I ii: 03 ~ 3 G)~5 ;a g ca gLIB ~I ~~. 0 gJ5'
~o"'=>" t'D_ ro , ~ en CD::J~~O-~o~_
~2 ~ ~~ ~1Il~;~6 Glt'D g@~~l&:-
c - - ... CI'l IW :::: '" y '< = CD C en < :;_
cn::J, ~ men o~ ~o ... z-~::J~Q~
~ ~ oS -c ffi "S. ~ !P.I~ ~ ~ 0 l- 2. mLZf~'
~~ I~ -c~ o"O=c - ~ (D=bl~~
,..~ _ a_ ::J~ ~~ ' ~ -.~_m~
$' ~. :: Q3 () ~o'~ ~ ~ ~ ~ ~ ~~ ~~~ ~1
en 0 =003 - V' _ o' ~~~~
Q. ~: m i~' ~::J eJ:J ,;:0
!~ I'il I I I I I' 1m
en ;~~
I, iI
II ff 88rr8 j 88~lfl~.
I ~I~I
I ~ ~ ~ ~ ~ ~ ~ ~ ~ H ~I
f,j
=>
'"
CD
iil'
'"
'"
?
'"
~
."
5'
..
=>
"
'"
"'I
" "
"'~
o
"
'?
~
. .
..
.
.
.
.
.
.
-10
:r -.
-.:<
.l/l
-0
l/l...
)>~
C:>,
~[
"TIc,
-10
)>0
ZC
C=
l/lg,
Cs:
ID..
'-..
m..
o :i'
-Ice
-Ir-
00
O~
:r)>
)>:>'
Z..
C)Dl
mc'
.
.
.
.
.
"
.
.
.
.
.
.
-g~
"'z
~~
~U
00
..JI-
"'I-
.5 U
-w
"'-,
"'Ill
:!!::l
'u VI
cO
=z
oce
UI-
'tiLL
j~
.cO
.::!ce
o~
~!!2
ui!=
.
.
.
.
.
'" '"
~~
..'"
;00
'"
.
..
.
.
Is
:;;
I~
I~ ~ ~
:s i 0
" " -
:;; :;; g:
" " "
~ ~ "
'E E .!!
E E il
o ~ 0 c
o.~o Q)o"
-2:--
,! " !!> ~ c c
'.;:; 0> .c X.2 _ oW
::) ::::J .! en ::0 12),
CQa.m- U') Q)~'
- Q) Q) -c f!1.=
U ~I~ al~
~ !:)"'O -=6:
~ ~ ~~;:;:
,2 ;. ~\"
:0 ~ ~
d: ii: ~.
:! en N 0 ~ .....!~
aoNIOt">li)M'jj5
~ '"
lO ~
-I
i
I~'I
~{
1;,'
'i~
\il~
~~.
'J.;
11;.
:~~.
-.,
.t..
ri
t""l
~"
.~
r~[,~:,
,
"
~.
'c
iij
o
'"
'"
'"
o
t::: :co en
<0 o..a:; W
o '"
"''''
UJUJ
"''''
!!!'"
,,'"
~
;0
o
u
III III 1l 1l
c c: c: c:
ro ttl m to
c: C c c:
u:u:u:u:
jjj
'"
"
x
J!l
g
"
"
"
:;;
u
c
"
o
o
~
..
~
"
lk:
" >-
co ~
I", 11 I-
E" B E
g u.. ~ 1m g
D::1E c ~ Q) D::
::I ...;: Idlm ::s
I p .5 t: 'E III Q) l!!l
I." 0 ~ 0 ",,.J "I.~
~ c: co :JI- Q).lI:
.! ~=o C Gl,-J.!!
0.-"'0) ~~IIlU)
cu..C:c <DQ)cC
I:.: c & :c ~ ~ gp=
cQ)om -'-roc
.~~.!a::_Q) ~$'~.2
- ....!p~
=g=.~ --
(I)-~u.. .E~s:!~
I~ i;j lk: -g =~ ~I~
:It:: ro ~~.s.a
.. m 0> ... '"
(I)~ c oo=ai
Q) 'C _ _ en
c ttl C c: c
Q) Q) 000
0:: I :;::~-.;::;
c u_..2.2.=!
ro = -:: 000
..c ..c:HU)(I)(I)
:5 ~...J~~tl.
,..
;0
o
~ IO to N
<"l C') C") 'iC
~ ~ ~
~
~
i!
'"
'" '"
w ~
'"
NO
co t!j
o
~
'"
1l
C
OJ
C
ii:
1l
C
..
C
ii:
I~
o
""
go!!
1..- <I.l cu-
~:HI'!~'g~
.5.,...J.5"01!J cu
_1- ... all ~ 0
Q) ell Q) "C 11)1 :.
Q) Q) CI) Q)"I ~
:E~::EQ.l.Ec
-I;' - c: . ;:;
'u1? 'Cj ~ "0 t:
S~3~~::E
OOOC:&:
O~o41Egg
:; 0 'ii - m :s
'5ffi'o~(,)o
=CI!!'6CO
~'-IIOI<(O'"
a:: "ECI)_iij.!!
!2 ~ illl~
I~ -g,,,,&!
I,S alii,
" ~"
m ;::tii
lk: w..
~ ~
u:: u::
C'\l r- re IX).:! It)
co M (0 M..... r::::
"'",
;::'"
'"
;::
o
u
1,,-
1- ~
E'"
Ote
o 0
lk:1 ~ C
=0::;::;
19.!!l al
I.::' tI) :e
-:1.2: _
- <<1'-
"'CO
C <( c
1'=li 6
c;;(,)
o.a ~
iij'ii).!!
= m ;:
Cl)ll..i
~!!,lk:
"t::
Ci)m
3
"
C
"
lk:
C
'"
-e
:J
'" m m
r::::Mr::::
m
,..
~
ia
Ie
o
o
lk:
"
o
I.~
...
..
iii
c
1=
c
o
'iij
'"
"
I~
"
"
-
'"
C
OJ
ii:
m
C
ii:
>-
Id
i~
" "
:;;w..
_ll.
'u to:
c_
" OJ
o ;.
0"
~ iji
.!!O::',
= C
iii OJ
lk:-e
:J
~
C
o
~
'EO
~:::::
.t~
ia
'"
ia
;:
UJ
Z
o
u
'li
.,
'li
"
u
'"
.
>-
;;
z
. =>
~ ~~
o "'..
I- ~!
j~::J~
~S5~
~.Iii -5
o ~'3
-5~g
'3 ! '~ :a
gg~o.::
'2j]j ~ ,2
~~3_
~~~~
~ ~ .Iii U)
ii.iU5~1-
o
..
o
~
'"
'"
o
'"
.
'"
.
Q.
:;<
"
;
'u
C
"
o
o
..
'0
S
CD
..
~
..
.c
l!
..
:;;
~
~
o
..
...
..
l!!
III
'"
'~I
'"
'"