|
Clinton Street CSO Abatement Project Facility Plan (Nov 2005)
by Environmental Engineering Associates, LLP for Onondaga County Department of Water Environment Protection
5. Detailed evaluation of most viable CSO abatement approaches
This section presents a detailed evaluation of the
four most viable Clinton Street CSO abatement
approaches selected for further evaluation. This
evaluation includes preliminary basis of design
development for the abatement approaches, preliminary
cost estimates for the abatement approaches, and
identification of the recommended/proposed CSO
abatement approach for the Clinton Street CSO service
area.
As discussed previously, sewer separation as a CSO
abatement approach entails the separation of existing
combined sewers into separate sanitary sewer and storm
sewer systems. Separation normally requires the
construction of a new sanitary sewer system parallel
to the existing combined sewer system. The combined
sewer system is then left in place to serve as a storm
sewer and all sanitary connections are switched over
to the new sanitary sewer line. However, under some
circumstances it may be determined to be more
cost-effective or otherwise preferable to convert the
combined sewer to a sanitary sewer and to construct a
new storm sewer.
In addition to being defined previously as a viable
CSO abatement approach for the Clinton Street CSO
service area, the County, pursuant to the ACJ, is
required to conduct sewer separation evaluations to
identify where sewer separation may be a more
cost-effective alternative to consolidation of CSO
flows for treatment at a Clinton Street RTF.
Specifically, the ACJ states:
A cost evaluation of sewer separation projects
proposed by the city, or by any party to this
agreement and order, shall be implemented by the
county. When doing this evaluation, the cost of
separation shall be compared with the savings realized
from the sum total of: a.) reduced CSO abatement
project costs; b.) reduced operating costs at the
Metro sewage treatment plant; and any other savings as
applicable; and achieves comparable water quality
benefits. The County is obligated to construct only
those sewer separation projects for which the
anticipated savings exceed expected costs." [emphasis
added]
To achieve compliance with the ACJ requirements,
separation of the entire and/or portions of the
Clinton Street CSO service area were evaluated as
follows:
A.
Sewer separation of the entire Clinton Street CSO
service area;
B.
Sewer separation of CSO drainage basins west of
Onondaga Creek (excluding 036)028, 031, 032, 033,
and 035with conveyance and storage or treatment of
remaining service area CSOs (027, 029, 030, 034, and
036) at a facility to be located at a final selected
preferred site; and
C.
Sewer separation of CSO drainage basins west of
Onondaga Creek and north of Tully Street (excluding
036)028, 031, and 032with conveyance and
storage or treatment of the remaining service area
CSOs (027, 029, 030, 033, 034, 035, and 036) at a
facility to be located at a final selected preferred
site.
In addition to the above sewer separation evaluations,
the County met with City of Syracuse representatives
to identify any additional areas within the Clinton
Street CSO service area where sewer separation may be
considered to be beneficial.
Appendix F includes a copy of the meeting minutes from
the meeting with City of Syracuse representatives to
discuss other potential sewer separation opportunities
in the City. Based on these discussions, the City of
Syracuse did not identify any additional areas within
the Clinton Street CSO service area where sewer
separation may be warranted and/or beneficial. For
this reason, the three sewer separation evaluations
identified above were determined to exceed the
requirements of the ACJ relative to supplemental sewer
separation evaluations.
Click here for Appendix F. Meeting minutes, meeting with City of Syracuse representatives concerning sewer separation.
As noted earlier, sewer separation entails separating
the existing combined sewers into separate sanitary
and storm sewer systems. In highly urbanized areas,
like the Clinton Street CSO service area, sewer
separation is highly disruptive to both vehicular and
pedestrian traffic. This is due to the fact that most
existing combined sewers are located below urban
streets. The construction of a new sanitary sewer
system parallel to the existing combined sewer system
below urban streets is further complicated by the
multitude of other utilities that are also generally
located beneath these streets. Another factor that
must be considered when undertaking sewer separation
in highly urbanized and concentrated commercial areas
is the potential requirement for internal plumbing
separation in large buildings including retail,
office, industrial, multi-story apartments and
institutional (e.g., churches, schools, government).
The cost of this activity will be highly variable
depending upon the specific location, building age,
structure type, modernization, presence of asbestos,
willingness of the building owner, etc. Sewer
separation involving concentrated commercial areas
should include interior inspections to determine the
need for separation of the interior plumbing. Once a
determination has been made to separate portions of
the interior plumbing of the building, provisions then
need to be made to conduct detailed investigations and
prepare detailed plans and specifications for each
location. The added cost for engineering and for
construction for interior building plumbing
modification would need to be evaluated on a case by
case basis.
Sewer separation in the Clinton Street CSO service
area is further complicated by the fact that the
Downtown Central Business District, the Armory Square
Historic District, the Syracuse University Hill Area,
and the industrial/residential areas of the City's
near westside are included within the service area.
Sewer separation within these important business
districts of downtown Syracuse would result in
negative economic impacts associated with such a
widespread and disruptive project. These conditions
would also further increase the unit cost per linear
foot to accomplish sewer separation within these
areas. In addition, the County has agreed to assume
responsibility for internal plumbing modifications for
commercial structures impacted by sewer separation
within the service area.
Sewer separation provides the ability to treat the
sanitary wastewater from the separated areas at the
Metro plant while storm water continues to discharge to
Onondaga Creek. As such, sewer separation provides a
high degree of pollutant removal as it relates to the
sanitary component of the CSO discharge. Operation and
maintenance requirements associated with the sewer
separation CSO abatement approach are generally low
when compared to conveyance and treatment facilities.
Sewer separation does not, however, eliminate the
contamination that is inherently associated with
separate storm water discharges, namely:
- Suspended solids
- Oil and grease
- Antifreeze
- Trash/floatables
- Pathogens
- Heavy metals
- Nutrients
- Organics
- Pesticides
- Fertilizers.
In addition, it is anticipated that forthcoming
federal requirements may require the implementation of
some form of treatment for storm water discharges that
are believed to be impacting the ability to satisfy
the water quality standards established for a
particular watercourse. If sewer separation were to
be implemented, the City of Syracuse would be
responsible for providing the required storm water
treatment.
Table 5-1 presents a summary overview of the
advantages and disadvantages of the sewer separation
CSO abatement approach for the Clinton Street CSO
Service Area.
Table 5-1. Sewer separation advantages/disadvantages
Advantages
Separates sanitary wastewater from combined sewage for separate treatment at Metro
Provides high degree of pollutant removal, including nutrients, contained in sanitary sewage
Low operation and maintenance requirements in comparison to other CSO abatement approaches
Disadvantages
Requires disconnection of existing building sewers from combined sewer to new sanitary sewer (highly disruptive construction in urban areas)
May require building replumbing to separate sanitary piping from roof drain piping
Does not eliminate contamination associated with urban stormwater runoff
Suspended solids
Oil and grease
Antifreeze
Trash, floatables
Pathogens
Heavy metals
Nutrients
Organics
Larger separate stormwater discharges will likely require separate treatment to comply with forthcoming Federal Standards
High initial capital cost in comparison to RTF CSO abatement approaches
Extended implementation period when compared to RTF implementation period; results in delayed water quality benefits
Th general basis of design for the sewer separation
CSO abatement approach would be consistent with other
County sewer separation projects recently completed or
currently under design. A new sanitary sewer system
(with ownership and maintenance responsibility assumed
by the City of Syracuse), sized to accommodate the
service area sanitary wastewater flows, would be
installed beneath city streets parallel to the
existing combined sewer system. Building service
laterals would be disconnected from the existing
combined sewer and connected to the new sanitary sewer
system. Internal plumbing modifications would be
implemented, as necessary, to disconnect non-sanitary
building flows from the service laterals. Disturbed
water services would be replaced from the water main
to the curb water valve. Streets and sidewalks
disturbed by the installation of the new sanitary
sewer system would be reconstructed to pre-existing or
improved conditions. Graphic representations
depicting the conversion of a typical combined sewer
system to a separate sanitary sewer and storm sewer
system are presented on
Figures 2-1 and 2-2.
To develop appropriate cost estimates with the three
alternative sewer separation approaches described
above, a land use analysis of the service area was
conducted. Costs to implement sewer separation in
residential areas are generally less than in
non-residential (concentrated commercial) areas due to
the additional utility conflicts, urban congestion,
more complex internal plumbing systems, etc.,
associated with non-residential (concentrated
commercial) areas.
To establish the approximate land use areas associated
with each individual Clinton Street CSO drainage
basin, the drainage basin boundaries were overlayed on
a map provided by the Syracuse-Onondaga County
Planning Agency entitled "Existing Land Uses," dated
March 2000. Using the detailed "mile-square" maps of
the City of Syracuse combined/sanitary/storm sewer
systems, as prepared by the City of Syracuse,
Department of Planning, dated 1965, the estimated
length of combined sewer that would require sewer
separation, by residential and non-residential
(commercial) land use area, was developed. Table 5-2
presents a summary of these data. These data will be
used to calculate estimated costs for the three sewer
separation CSO abatement approaches described in
Section 5.2.
| Table 5-2. Residential/non-residential (commercial) estimated sewer lengths for individual CSO drainage basins |
| |
Length of new sanitary sewer |
|
CSO drainage basin
|
Residential* (LF)
|
Non-residential* (LF)
|
|
027
|
2,695
|
28,520
|
|
028
|
1,513
|
3,216
|
|
029
|
0
|
1,635
|
|
030
|
15,362
|
35,499
|
|
031
|
1,066
|
1,492
|
|
032
|
1,664
|
1,942
|
|
033
|
1,434
|
1,948
|
|
034
|
6,813
|
27,563
|
|
035
|
1,069
|
2,352
|
|
036
|
15,897
|
13,222
|
|
TOTAL
|
47,513
|
117,389
|
*Based on length of existing sewer shown on sewer maps prepared by City of Syracuse, Department of City Planning, 1965. LF = Linear Feet
|
Regional storage with no disinfection may be
appropriate for use with three of the four most viable
CSO abatement approaches. These are as follows:
A.
A full service area storage
facility to provide storage for all CSOs (027, 028,
029, 030, 031, 032, 033, 034,
035, and 036) in the Clinton Street CSO service area;
B.
A partial service area storage
facility to provide storage for CSOs 027, 029, 030,
034, and 036, with
sewer separation for the remaining portions of the
service area; and
C.
A partial service area storage
facility to provide storage for CSOs 027, 029, 030,
033, 034, 035, and
036, with sewer separation for the remaining portions
of the service area.
Each of the storage facilities described above would
be sized to achieve full compliance with the Clinton
Street ACJ CSO bacterial requirements. In addition,
as described in
Section 2.2,
the storage facilities will provide both floatables
removal and CSO volume capture.
In order to determine the design storage volumes for
the three different sized regional storage facilities
described above, EEA coordinated with modeling
consultant Brown and Caldwell to execute the Annual
Simulation Fecal Coliform Model for Onondaga Lake
(bacteria model) assuming a storage facility with no
disinfection in lieu of a regional treatment facility
including in-line storage with disinfection (RTF) for
the Clinton Street CSO service area. The results of
these bacteria model runs are presented as Scenarios
3, 4, and 5 in the Brown and Caldwell memorandum
included as Appendix A.
Click here for Appendix A. Bacterial model update for Onondaga Lake.
The three regional storage conditions were also
analyzed at the two most preferential sites for CSO
abatement facilities (i.e., Clinton Station and
Dickerson Street) as determined in
Section 3.4.
These design storage volumes are summarized below:
|
Regional storage description
|
Design Storage Volume
|
|
Clinton Station
|
|
|
Full service area storage facility
|
21 MG
|
|
Storage facility at site with sewer separation west of Onondaga Creek (excluding 036)
|
18 MG
|
|
Storage facility at site with sewer separation west of Onondaga Creek and north of Tully Street (excluding 036)
|
19 MG
|
|
Dickerson Street
|
|
|
Full service area storage facility
|
21 MG
|
|
Storage facility at site with sewer separation west of Onondaga Creek (excluding 036)
|
18 MG
|
|
Storage facility at site with sewer separation west of Onondaga Creek and north of Tully Street (excluding 036)
|
19 MG
|
Regardless of the final selected site for the regional
storage facility, it is expected that influent flow
for the facility will be accomplished by gravity
discharge. Following the storm event, pumping
facilities would be provided to discharge the stored
flow to the MIS for subsequent treatment at Metro.
The general design basis for the regional storage
facility would be as follows:
-
CSO conveyance pipelines to collect and transport
captured CSO, up to 1-year design storm event, to the
regional storage facility;
-
influent stilling well/grit sump;
-
mechanically cleaned coarse screening;
-
below ground storage tank with segmented
compartments to optimize flow storage utilization
during smaller storm events;
-
pumping facilities to dewater and convey the maximum
storage tank volume to the MIS within a maximum 48
hour period following storm event;
-
flushing system to clean dewatered storage tank
following storm event; and
-
odor control facilities.
The storage capacity associated with the regional
storage facility requires that this CSO abatement
approach use more land area than with a vortex
separator treatment system or an ORF treatment system.
Based on a preliminary conceptual layout of the
conveyance pipelines for the Clinton Street CSO
service area and the associated pipeline invert and
available land area at the two most preferential
sites, the preliminary conceptual depth of a regional
storage facility would be approximately 45 feet.
Based on this depth, a regional storage facility will
require approximately 35% more land area than a vortex
separator treatment system and approximately 6% more
land area than an ORF treatment system.
A summary of the principal advantages and
disadvantages of the regional storage (with no
disinfection) CSO abatement/treatment approach is
presented in Table 5-3.
| Table 5-3. Regional storage (with no disinfection) advantages / disadvantages |
|
Advantages
|
Disadvantages
|
|
Captures higher volume storms for post-storm treatment at Metro
|
Land area requirement (2-3 acres) results in limited siting alternatives within an urban area
|
|
High degree of settleable solids, TSS, BOD, TKN, P and floatables removal
|
Larger consolidation pipelines required for regional storage facilities will require deeper and wider excavation areas in comparison to sewer separation
|
|
Provides capture and treatment of storm water pollutants as well as sanitary wastewater pollutants
|
|
|
Disruption due to construction is confined to a smaller area in comparison to sewer separation
|
Does not provide back-to-back storm protection for non-disinfected bacteria laden discharges.
|
|
Existing sanitary connections and storm leaders within buildings in the urban area are undisturbed
|
Requires additional land area requirements in comparison to vortex separator facility and ORF
|
|
Smaller above grade facilities mean less visual impact in comparison to vortex and overflow retention facility (ORF)
|
Requires larger capacity pumps to dewater the facility in the same amount of time as the vortex separator facility and ORF
|
|
Conveys larger volume of CSO to Metro for treatment in comparison to vortex and ORF
|
May not allow permanent closure of CSOs
|
|
|
For Clinton Street CSO service area, MIS available capacity limits total storage allowable storage volume, requiring additional, more costly sewer separation
|
It should be noted that a flow capacity evaluation of
the County MIS was performed by modeling consultant
Brown and Caldwell to assess the capability of the MIS
to accept the pump back of captured CSO from a full
storage facility over a 48-hour period (maximum pump
back period established by NYSDEC) for the Clinton
Street CSO service area. A copy of the MIS flow
capacity evaluation memorandum prepared by Brown and
Caldwell is included as Appendix G.
Click here for Appendix G. Memorandum: MIS flow capacity evaluation.
As noted in the
MIS flow capacity evaluation memorandum, at the
Clinton Street location, the available capacity (Qa)
of the MIS is estimated to be 14.3 million gallons per
day (mgd). The proposed design for the Midland Avenue
CSO in-line storage/RTF, which will be located
upstream of the Clinton CSO service area, includes a
total storage volume of 8.45 mgd. Assuming that
dewatering (pump back) of a fully stored Midland
Avenue CSO in-line storage/RTF facility will occur
coincident with dewatering (pump back) of a full
Clinton CSO service area storage facility, the
available capacity (Qa) of the MIS at the Clinton
Street location will be reduced by 4.23 mgd (8.45 mgd
ö 2 days) to approximately 10.1 mgd (14.3 mgd - 4.23
mgd). Assuming the same maximum 48-hour (2 day) pump
back period for a Clinton Street CSO regional storage
facility, the maximum storage volume that can be
implemented for the Clinton Street CSO service area is
20.2 MG (10.1 mgd x 2 days). As indicated by the
required storage volume data previously presented, a
full service area storage facility at 21 MG exceeds
the ability of the existing MIS to accept the pump
back of the stored CSO for this facility over a
48-hour period. Therefore, additional facilities
would need to be provided to convey the excess volume
of stored CSO i.e., 0.8 MG (21 MG - 20.2 MG), to Metro
for treatment. Alternatively, additional sewer
separation would need to be implemented to reduce the
full service area storage facility volume to 20.2 MG.
Both approaches would require that these additional
costs be added to the base storage facility cost.
In-line storage/vortex separation with high-rate
disinfection, as an RTF, may be appropriate for use
with three of the four most viable CSO abatement
approaches. These are as follows:
A.
A full service area vortex separator to treat all
CSOs (027, 028, 029, 030, 031, 032, 033, 034, 035, and
036) in the Clinton Street CSO service area;
B.
A partial service area vortex separator to treat
CSOs 027, 029, 030, 034, and 036, with sewer
separation provided for the remaining portions of the
service area; and
C.
A partial service area vortex separator to treat
CSOs 027, 029, 030, 033, 034, 035, and 036, with sewer
separation provided for the remaining portions of the
service area.
Pursuant to the requirements of the ACJ, the CSO
Abatement Program is required to provide high-rate
treatment, including floatables removal, settleable
solids removal, and disinfection of CSOs up to the
1-year design storm event. As described in
Section 2.2,
vortex separation with high-rate disinfection,
designed for the 1-year design storm event, will
achieve these objectives.
In order to determine the design flow rates for the
three different-sized vortex separators described
above, EEA coordinated with modeling consultant Brown
and Caldwell to execute the Clinton Street CSO service
area sewer system model for these three vortex
separator conditions.
The results of these model runs are presented in Table 1 in the Brown and Caldwell summary letter included as Appendix H.
Appendix H. Correspondence: Design flow rate & flow volume info for CSO abatement alternatives: Email Susan Miller, Project Deputy Director or phone 315-435-2260 for copy.
The three alternative vortex
separator facilities were also analyzed at the two
most preferential sites for CSO abatement facilities
(i.e., Clinton Station and Dickerson Street) as
determined in Section 3.4. These 1-year design storm
flow rates are summarized below:
|
Vortex separator description
|
1-yr design storm flow rate
|
|
Full service area vortex separator
|
755 cfs
|
|
Vortex separator at site with sewer separation west of Onondaga Creek (excluding 036)
|
660 cfs
|
|
Vortex separator at site with sewer separation west of Onondaga Creek and north of Tully Street (excluding 036)
|
700 cfs
|
|
Dickerson Street
|
|
|
Full service area vortex separator
|
755 cfs
|
|
Vortex separator at site with sewer separation west of Onondaga Creek (excluding 036)
|
660 cfs
|
|
Vortex separator at site with sewer separation west of Onondaga Creek and north of Tully Street (excluding 036)
|
700 cfs
|
Regardless of the final selected site for the in-line
storage/vortex separator treatment system, influent
pumping will be required to "lift" the collected CSO
flow into the vortex separator system to permit
gravity discharge of treated flows from the treatment
system into Onondaga Creek. The general design basis
for the in-line storage/vortex separator treatment
would be as follows:
-
CSO conveyance pipelines to collect and transport captured CSOs, up to the 1-year design storm event, to the vortex separator treatment system;
-
Influent stilling well/grit sump;
-
Coarse screening/manually cleaned trash racks;
-
Influent pumping;
-
Vortex solids separators to provide storage for smaller storm events, and floatables and settleable solids removal for larger storm events;
-
Vortex solids separator underflow conveyance to the MIS during a storm event;
-
High rate disinfection by chlorination/dechlorination for bacterial reduction prior to discharge to Onondaga Creek;
-
Dewatering of the vortex separator and disinfection tank stored flows to the MIS following a storm event;
-
Noise control; and
-
Odor control facilities.
For planning purposes, the vortex separator treatment
system was considered to include USEPA swirl
concentrator treatment units. Figure 2-3 depicts a
typical USEPA vortex separator (swirl concentrator).
In addition, high-rate disinfection following the
USEPA vortex solids separator treatment, previously
documented by USEPA demonstration projects to achieve
up to three log bacterial reduction with a 5-minute
detention time in conjunction with high intensity
mixing, will be used as the basis for achieving the
required bacterial reductions pursuant to the ACJ.
Dechlorination using a 1-minute detention time will
also be included to reduce potential toxicity issues
that may be associated with chlorinated discharges.
A summary of the principal advantages and
disadvantages of the in-line storage/vortex separator
(with high-rate disinfection) CSO treatment approach
is presented in Table 5-4.
| TABLE 5-4. IN-LINE STORAGE/VORTEX SEPARATOR (WITH HIGH-RATE DISINFECTION)ADVANTAGES/DISADVANTAGES |
|
Advantages
|
Disadvantages
|
|
Designed to operate under all, including extremely high, flow conditions
|
Larger consolidation pipelines required for regional treatment facilities will require deeper and wider excavation areas in comparison to sewer separation
|
|
Reduced land area requirements in comparison to ORF alternative
|
May not allow permanent closure of CSOs
|
|
High degree of settleable solids and floatables removal
|
|
|
Provides sufficient treatment for downstream disinfection
|
|
|
Provides capture and treatment of storm water pollutants as well as sanitary wastewater pollutants
|
|
|
Disruption due to construction is confined to a smaller area in comparison to sewer separation
|
|
|
Existing sanitary connections and storm leaders within buildings in the urban area are undisturbed
|
|
As discussed in
Section 4,
in-line storage/ORF with high-rate disinfection, as an
RTF, may be appropriate for use with the same three
CSO abatement approaches as evaluated for the vortex
separator, i.e.:
A.
A full service area ORF to treat all CSOs in the
Clinton Street CSO service area;
B.
A partial service area ORF to treat CSOs 027, 029,
030, 034, and 036, with sewer separation provided for
the remaining portions of the service area; and
C.
A partial service area ORF to treat CSOs 027, 029,
030, 033, 034, 035, and 036, with sewer separation
provided for the remaining portions of the service
area.
As with the vortex separator RTF, the design basis for
the ORF is to provide floatables removal, settleable
solids removal, and disinfection of CSOs up to the
1-year design storm event. The peak design flow rates
for the three different-sized ORFs described above, at
the two most preferential RTF sites, would be the same
as those defined previously for the vortex separator
RTF.
Similar to the vortex separator RTF, the following
general design basis of the ORF will be required.
-
CSO conveyance pipelines to collect and transport captured CSOs, up to the 1-year design storm event, to the ORF treatment system;
-
Influent stilling well/grit sump;
-
Manually cleaned coarse screening;
-
ORF to provide storage for smaller storm events and provide floatables and settleable solids removal for larger storm events;
-
High-rate disinfection by chlorination/dechlorination for bacterial reduction prior to discharge to Onondaga Creek;
-
Dewatering of the ORF and disinfection tank stored flows to the MIS following the storm event;
-
Flushing system to clean dewatered ORF and disinfection tank following storm event; and
-
Odor control facilities.
As described previously in
Sections 2.2 and 2.3,
ORFs, while performing as a high-rate primary
sedimentation process prior to disinfection, are
generally sized to retain a specific storm event.
Sizing the ORF to capture and treat all service area
CSOs up to the 1-year design storm event, with
adequate disinfection of excess flows prior to
discharge, will permit compliance with the County's
ACJ requirements. For this reason, the ORF design
basis was selected on the 1-year design storm volume,
with post-retention disinfection facilities provided
to achieve a 5-minute disinfection/1-minute
dechlorination contact time at the peak service area
flow rate, in the event back-to-back storms are
delivered to the ORF. For the three different-sized
ORFs previously described, the 1-year design flow
volumes for the two most preferential abatement
facilities sites are as follows:
|
ORF description
|
1-yr design storm flow volume
|
|
Clinton Station
|
|
|
Full service area ORF
|
16.0 MG
|
|
ORF at site with sewer separation west of Onondaga Creek (excluding 036)
|
14.3 MG
|
|
ORF at site with sewer separation west of Onondaga Creek and north of Tully Street (excluding 036)
|
15.1 MG
|
|
Dickerson Street
|
|
|
Full service area ORF
|
16.0 MG
|
|
ORF at site with sewer separation west of Onondaga Creek (excluding 036)
|
14.3 MG
|
|
ORF at site with sewer separation west of Onondaga Creek and north of Tully Street (excluding 036)
|
15.1 MG
|
The ORF, due to its design basis, provides more
storage capacity for small intensity/duration storm
events than the vortex separator RTF due to its
inherently larger design volume. It does, however,
provide less storage capacity than a regional storage
facility. The captured flow is then pumped back to
the MIS for treatment at Metro following the storm
event.
The additional storage capacity associated with the
ORF requires that the ORF treatment system use more
land area than the vortex separator treatment system,
however, it would require less land area than a
regional storage facility. Based on a preliminary
conceptual layout of the conveyance pipelines for the
Clinton Street CSO service area and the associated
pipeline inverts, the preliminary conceptual depth of
an ORF treatment system would be approximately 40
feet. Based on this depth, for the 1-year design
storm flows/volumes being used for the Clinton Street
CSO service area, an ORF treatment system will require
approximately 25% more land area than a vortex
separator treatment system.
Because the ORF treatment system captures and stores
more smaller intensity rainfall events, there would be
slightly higher operation and maintenance requirements
for this ORF treatment system when compared to the
vortex separator treatment system. The ORF will,
however, capture more flow for treatment at Metro than
the vortex separator treatment system. The ORF
treatment system also does not have the high degree of
flexibility to provide effective pretreatment prior to
disinfection under extremely high flow conditions, in
excess of the 1-year design storm event, that the
vortex separator treatment system provides. Under
extremely high flow conditions, the ORF treatment
system is susceptible to solids washout from the ORF
into the post-treatment disinfection system, and
disinfection effectiveness may be impacted.
A typical ORF is presented on Figure 2-10. Table 5-5
presents a summary of the principal advantages and
disadvantages of the in-line storage/ORF (with
high-rate disinfection) CSO treatment approach.
| TABLE 5-5. IN-LINE STORAGE/ORF (WITH HIGH-RATE DISINFECTION)ADVANTAGES/DISADVANTAGES |
|
Advantages
|
Disadvantages
|
|
High degree of settleable solids and floatables removal
|
Land area requirement (2-3 acres) results in limited siting alternatives within an urban area
|
Provides sufficient treatment for downstream disinfection Provides capture and treatment of storm water and sanitary wastewater
|
Larger consolidation pipelines will require deeper and wider excavation areas than sewer separation
|
|
Disruption due to construction is confined to a smaller area in comparison to sewer separation
|
Less efficient during high flow rates in comparison to vortex separator facility
|
|
Existing sanitary connections and storm leaders within buildings in the urban area are undisturbed
|
Requires additional land area requirements in comparison to vortex separator facility
|
|
Smaller above grade facilities will result in less visual impact in comparison to vortex separator facility
|
Requires larger capacity pumps to dewater the facility in the same amount of time as the vortex separator facility
|
|
Conveys a larger volume of CSO to Metro for treatment in comparison to a vortex separator facility
|
May not allow permanent closure of CSOs Above grade facilities will have more visual impact in comparison to regional storage facility
|
A summary listing the most feasible CSO abatement
approaches and preferential storage/RTF sites is
presented in Table 5-6. A total of 19 alternative
options have been identified for further cost
evaluation.
| TABLE 5-6. MOST FEASIBLE CSO ABATEMENT APPROACHES AND PREFERENTIAL SITES |
|
Abatement approach
|
|
1. Storage/RTF at Clinton Station Site
|
|
a. Storage - no sewer separation
|
|
b. Storage (separate CSO 028, 031, 032, 033, 035)
|
|
c. Storage (separate CSO 028, 031, 032)
|
|
d. RTF (vortex separator) - no sewer Separation
|
|
e. RTF (separate CSO 028, 031, 032, 033, 035)
|
|
f. RTF (separate CSO 028, 031, 032)
|
|
g. RTF (orf) - no sewer separation
|
|
h. RTF (separate CSO 028, 031, 032, 033, 035)
|
|
i. RTF (separate CSO 028, 031, 032)
|
|
2. Storage/rtf at dickerson street site
|
|
a. Storage - no sewer separation
|
|
b. Storage (separate CSO 028, 031, 032, 033, 035)
|
|
c. Storage (separate CSO 028, 031, 032)
|
|
d. RTF (vortex separator) - no sewer separation
|
|
e. RTF (separate CSO 028, 031, 032, 033, 035)
|
|
f. RTF (separate CSO 028, 031, 032)
|
|
g. RTF (orf) - no sewer separation
|
|
h. RTF (separate CSO 028, 031, 032, 033, 035)
|
|
i. RTF (separate CSO 028, 031, 032)
|
|
3. Complete sewer separation
|
Preliminary construction cost estimates were developed
for the 19 alternative options to preliminarily screen
these options.
To establish appropriate sewer separation costs for
the Clinton Street CSO abatement project, the County's
Program Management consultant, CDM/C&S, a Joint
Venture, coordinated a detailed review of sewer
separation costs in the Syracuse metropolitan area
based upon recently completed and ongoing County
projects. The results of this analysis are included
in a memorandum from CDM/C&S to the County, a copy of
which is included as Appendix I.
Appendix H. Correspondence: Design flow rate & flow volume info for CSO abatement alternatives: Email Susan Miller, Project Deputy Director or phone 315-435-2260 for copy.
Based on the CDM/C&S memorandum, the following unit
costs (updated to February 2005 costs, ENRCCI = 7298)
were determined to be applicable and reflective of the
cost to implement sewer separation within the Syracuse
metropolitan area. These unit costs for sewer
separation include disconnection and re-plumbing of
internal building storm water plumbing systems for
non-residential buildings; replacement of the sanitary
lateral service lines to the curb or to the building
where modifications to private plumbing is required;
replacement of disturbed water services from the main
to the curb water valve; and restoration of sidewalks,
curbing, and pavement.
Sewer separation unit costs
(per linear foot of new sanitary sewer to be installed):
A. Residential Areas - $823/linear foot
B. Non-Residential (Commercial) Areas - $819/linear foot
(Note: the above per linear foot costs include a 10% contingency factor as suggested in the CDM/C&S memorandum; the above per linear foot costs are based on a February 2005 ENRCCI of 7298.)
To determine the estimated construction costs for the
various sewer separation approaches identified as
being appropriate to further evaluate, the total
linear footage of residential and non-residential
(commercial) new sanitary sewer to be installed under
the alternative approaches was defined. Table 5-7
presents the residential and non-residential linear
footage of new sanitary sewer to be installed for each
of the three most viable sewer separation alternatives
for the Clinton Street CSO service area determined
previously.
| TABLE 5-7. RESIDENTIAL/NON-RESIDENTIAL SEWER SEPARATION LINEAR FOOTAGE* |
|
Sewer separation alternative
|
Residential
|
Non-residential [Commercial]
|
|
Separate 028, 031, 032
|
4,243
|
6,650
|
|
Separate 028, 031, 032, 033, 035
|
6,746
|
10,950
|
|
Complete service area sewer separation
|
47,513
|
117,389
|
|
Note: *Linear feet of new separate sanitary sewer to be installed.
|
Table 5-8 presents the estimated
construction cost for these same three sewer
separation alternatives.
| TABLE 5-8. RESIDENTIAL/NON-RESIDENTIAL SEWER SEPARATION ESTIMATED CONSTRUCTION COSTS* |
|
Sewer separation alternative
|
Residential
|
Non-residential [commercial]
|
Total
|
|
Separate 028, 031, 032
|
$3,492,000
|
$5,446,000
|
$8,938,000
|
|
Separate 028, 031, 032, 033, 035
|
5,552,000
|
8,968,000
|
14,520,000
|
|
Complete service area sewer separation
|
39,103,000
|
96,142,000
|
135,245,000
|
*Note: Does not include costs for rehabilitation of existing combined sewer lines. Costs based on Feb 2005 dollar (ENRCCI=7298)
|
To determine the estimated construction costs for the
CSO abatement approaches that would utilize a regional
storage or in-line storage/treatment facility (either
vortex separator or ORF), preliminary conceptual
planning layouts were developed for each of the two
preferential sites.
Figures 5-1, 5-2, and 5-3 depict
the preliminary planning layout of an RTF (vortex
separator shown) and potential CSO conveyance
pipelines for the Clinton Station site, and Dickerson
Street site (east and west options), respectively.
The preliminary planning layout for storage facilities
or ORF RTFs would be similar to those presented on
Figures 5-1, 5-2, and 5-3, with the exception that the
storage facilities area would be approximately 35%
greater than that shown for the vortex separator RTF
and the ORF facilities area would be approximately 25%
greater than that shown for the vortex separator.
Fig 5-1: preliminary planning layout: RTF and potential CSO conveyances, Clinton Station
Figure 5-2: Dickerson Street site (east option)
Figure 5-3: Dickerson Street site (west option)
Preliminary construction cost estimates were developed
for the RTFs and conveyance pipelines based upon the
preliminary planning layouts depicted on Figures 5-1
and 5-3 (Note: Estimated construction costs were
developed for the Dickerson Street west option only
for preliminary screening purposes, as the Dickerson
Street east option estimated construction costs are
expected to be generally consistent with the west
option). Due to the fact that, at this facilities
planning level, there are more project unknowns
associated with the storage facility and RTF (vortex
separator and ORF) construction implementation than
are associated with the sewer separation CSO abatement
approach, a 25% construction contingency was included
in the estimated construction costs. Table 5-9
presents a summary of the estimated construction costs
for the 19 CSO abatement options for the Clinton
Street CSO service area.
| TABLE 5-9. CSO ABATEMENT ALTERNATIVES ESTIMATED CONSTRUCTION COSTS ($000,000) |
|
Abatement approach
|
Convey- ances
|
Storage/ RTF
|
Sewer sep
|
Total
|
|
1. Storage/RTF at Clinton Station Site
|
|
|
|
|
|
a. Storage - No Sewer Separation
|
$19.0
|
$60.7
|
$0
|
$79.7
|
|
b. Storage (Separate CSO 028, 031, 032, 033, 035)
|
14.3
|
52.0
|
14.5
|
80.8
|
|
c. Storage (Separate CSO 028, 031, 032)
|
14.8
|
54.9
|
8.9
|
78.6
|
|
d. RTF (Vortex Separator) - No Sewer Separation
|
19.0
|
33.0
|
0
|
52.0
|
|
e. RTF (Separate CSO 028, 031, 032, 033, 035)
|
14.3
|
28.9
|
14.5
|
57.7
|
|
f. RTF (Separate CSO 028, 031, 032)
|
14.8
|
30.6
|
8.9
|
54.3
|
|
g. RTF (ORF) - No Sewer Separation
|
19.0
|
57.3
|
0
|
76.3
|
|
h. RTF (Separate CSO 028, 031, 032, 033, 035)
|
14.3
|
51.2
|
14.5
|
80.0
|
|
i. RTF (Separate CSO 028, 031, 032)
|
14.8
|
54.1
|
8.9
|
77.8
|
|
2 Storage/RTF at Dickerson Street Site (West Option)
|
|
|
|
|
|
a. Storage - No Sewer Separation
|
22.5
|
66.7
|
0
|
89.2
|
|
b. Storage (Separate CSO 028, 031, 032, 033, 035)
|
18.4
|
57.2
|
14.5
|
90.1
|
|
c. Storage (Separate CSO 028, 031, 032)
|
18.4
|
60.4
|
8.9
|
87.7
|
|
d. RTF (Vortex Separator) - No Sewer Separation
|
22.5
|
33.0
|
0
|
55.5
|
|
e. RTF (Separate CSO 028, 031, 032, 033, 035)
|
18.4
|
28.9
|
14.5
|
61.8
|
|
f. RTF (Separate CSO 028, 031, 032)
|
18.4
|
30.6
|
8.9
|
57.9
|
|
g. RTF (ORF) - No Sewer Separation
|
22.5
|
63.1
|
0
|
85.6
|
|
h. RTF (Separate CSO 028, 031, 032, 033, 035)
|
18.4
|
56.4
|
14.5
|
89.3
|
|
i. RTF (Separate CSO 028, 031, 032)
|
18.4
|
59.5
|
8.9
|
86.8
|
|
3 Complete Sewer Separation
|
0
|
0
|
135.2
|
135.2
|
Notes: (1) Costs have been rounded to the nearest $100,000. (2) Costs based on November 2005 dollars (ENRCCI = 7298)
|
In addition to construction cost, O&M costs will
impact the overall cost-effectiveness of a particular
option. To assess this impact, estimated annual O&M
costs were developed for the most feasible CSO
treatment technologies/approaches at a single site, in
addition to full sewer separation of Clinton Street
CSO service area. Due to the fact that all of the CSO
treatment technologies/approaches at the Clinton
Station site were determined to have lower estimated
construction costs than if implemented at the
Dickerson Street site (see Table 5-9) O&M costs were
developed for these CSO technologies/approaches for a
total present worth cost comparison. Table 5-10
presents the estimated annual O&M costs for the CSO
treatment technologies/approaches at the Clinton
Street site plus full sewer separation for the Clinton
Street CSO service area.
| TABLE 5-10. ESTIMATED ANNUAL OPERATION AND MAINTENANCE COSTS |
|
Abatement approach
|
Est annual O&M cost
|
|
1. Storage/RTF at Clinton Station Site
|
|
|
a. Storage - No Sewer Separation
|
$656,000
|
|
b. Storage (separate CSO 028, 031, 032, 033, 035)
|
584,000
|
|
c. Storage (separate CSO 028, 031, 032)
|
617,000
|
|
d. RTF (vortex separator) - No Sewer Separation
|
1,026,000
|
|
e. RTF (separate CSO 028, 031, 032, 033, 035)
|
901,000
|
|
f. RTF (separate CSO 028, 031, 032)
|
957,000
|
|
g. RTF (ORF) - no sewer separation
|
659,000
|
|
h. RTF (separate CSO 028, 031, 032, 033, 035)
|
586,000
|
|
i. RTF (separate CSO 028, 031, 032)
|
617,000
|
|
3. Complete sewer separation
|
46,000
|
|
Costs based on Feb 2005 dollars (ENRCCI=7298)
|
Table 5-11 presents the total estimated project costs
for the CSO abatement technologies/approaches at the
Clinton Station site plus full sewer separation for
the Clinton Street CSO service area.
| TABLE 5-11. ESTIMATED PROJECT COSTS ($000,000) |
|
Abatement approach
|
Construc- tion (1)
|
Site mitigation (2)
|
Subtotal
|
Project-related (3)
|
Total
|
|
1. Storage/RTF at Clinton Station site
|
|
|
|
|
|
|
a. Storage - No Sewer Separation
|
$79.7
|
$6.3
|
$86.0
|
$19.9
|
$105.9
|
|
b. Storage (separate CSO 028, 031, 032, 033, 035)
|
80.8
|
6.3
|
87.1
|
20.2
|
107.3
|
|
c. Storage (separate CSO 028, 031, 032)
|
78.6
|
6.3
|
84.9
|
19.7
|
104.6
|
|
d. RTF (vortex separator) - no sewer separation
|
52.0
|
6.3
|
58.3
|
13.0
|
71.3
|
|
e. RTF (separate CSO 028, 031, 032, 033, 035)
|
57.7
|
6.3
|
64.0
|
14.4
|
78.4
|
|
f. RTF (separate CSO 028, 031, 032)
|
54.3
|
6.3
|
60.6
|
13.6
|
74.2
|
|
g. RTF (ORF) - No Sewer Separation
|
76.3
|
6.3
|
82.6
|
19.1
|
101.7
|
|
h. RTF (separate CSO 028, 031, 032, 033, 035)
|
80.0
|
6.3
|
86.3
|
20.0
|
106.3
|
|
i. RTF (separate CSO 028, 031, 032)
|
77.8
|
6.3
|
84.1
|
19.5
|
103.6
|
|
3. Complete sewer separation
|
135.2
|
0
|
135.2
|
33.8
|
169.0
|
Notes: (1) Based on Feb 05 dollars (ENRCCI = 7298) rounded.
(2) Site mitigation costs include temporary and permanent replacement parking, site enhancements, residential relocations, business relocations, and demolition costs, as warranted. Special Costs Associated
with Site includes property acquisition, architectural enhancements, contaminated soil disposal and construction access bridge, as warranted.
(3) Project related costs include engineering, legal and administrative costs estimated to equal 25% of the Estimated Construction Cost.
Using the O&M cost data presented in Table 5-10, a
25-year present worth cost comparison was developed
for each of the most viable CSO abatement
technologies/approaches described above. The 25-year
period for the present worth analysis was selected as
this generally represents the standard useful life for
installed CSO abatement facilities, including
mechanical equipment, pumps, instrumentation, etc.
Table 5-12 presents the results of the present worth
analysis.
| TABLE 5-12. PRESENT WORTH ANALYSIS ($000,000) |
|
Abatement approach
|
Est proj cost (1)
|
Est annual O&M
|
Present worth (2)
|
|
1. Storage/RTF at Clinton Station site
|
|
|
|
|
a. Storage - no sewer separation
|
$105.9
|
$0.656
|
$115.3
|
|
b. Storage (separate CSO 028, 031, 032, 033, 035)
|
107.3
|
0.584
|
115.6
|
|
c. Storage (separate CSO 028, 031, 032)
|
104.6
|
0.617
|
113.4
|
|
d. RTF (vortex separator) - No Sewer Separation
|
71.3
|
1.026
|
85.9
|
|
e. RTF (separate CSO 028, 031, 032, 033, 035)
|
78.4
|
0.901
|
91.3
|
|
f. RTF (separate CSO 028, 031, 032)
|
74.2
|
0.957
|
87.9
|
|
g. RTF (ORF) - No Sewer Separation
|
101.7
|
0.659
|
111.1
|
|
h. RTF (separate CSO 028, 031, 032, 033, 035)
|
106.3
|
0.586
|
114.7
|
|
i. RTF (separate CSO 028, 031, 032)
|
103.6
|
0.617
|
112.4
|
|
3. Complete sewer separation
|
169.0
|
0.046
|
169.7
|
Notes: (1) Based on Feb 05 dollars (ENRCCI = 7298), rounded. (2) Present Worth Cost Based on a 25-year useful life and a discount rate equal to 5.0%
|
A summary of the most viable CSO abatement technologies/approaches is presented in Table 5-13.
Based on the present worth analysis presented in Table
5-12, it is concluded that an in-line storage/vortex
separator RTF at a final selected preferred site
(Approach 1d, Table 5-13)
will be the most cost effective approach for abating CSOs
in the Clinton Street CSO service area.
A schematic of this CSO abatement technology/approach is depicted on Figure 5-4.
To further evaluate the cost-effectiveness of
implementing an in-line storage/vortex separator RTF
at the two preferential site locations, an assessment
of the various anticipated mitigation measures that
would be required at each of these sites was
undertaken. A discussion of these anticipated
mitigation measures is presented below.
If the RTF were to be located at the Clinton Station
site, replacement parking would be required both
during construction and permanently after construction
is completed. At the present time, the Clinton
Station site provides low-cost parking for both
employment and recreational activities in the Central
Business District. Public input from the Downtown
Committee of Syracuse, the Armory Square Merchants
Association, and the City of Syracuse have confirmed
that the loss of low-cost parking in close proximity
to employees and patrons of the Armory Square Historic
District will have negative impacts to the future
prosperity for these areas. It is estimated that
permanent replacement parking will be required for
approximately 300 to 400 vehicles at the Clinton
Station site. In addition, temporary replacement
parking will need to be provided for approximately 450
vehicles during construction.
In the event an ORF or storage facility were to be
located at the Clinton Station site, its location at
the north end of the parking lot will necessitate
closing of the existing tunnel beneath the adjacent
elevated railway tracks during construction due to its
larger size in comparison to a vortex separator RTF.
This condition would alter access to and use of the
parking lot during construction. Requirements for
permanent replacement parking at the Clinton Station
site may be reduced if the ORF or storage facility is
designed to accommodate permanent replacement parking
above the underground tankage for these facilities.
In addition to parking mitigation noted above,
construction access to the Clinton Station site is
severely restricted. The main entry to the site is at
the extreme southern portion of the site. This entry
point will need to be maintained for access to parking
spaces that will not be disturbed by construction of
the RTF. In addition, there is an access tunnel that
is located under the railroad tracks on the east side
of the site. Height clearances will not allow access
of most major pieces of construction equipment. On
the west side of the site, there is an old railroad
bridge that spans Onondaga Creek and connects the site
with Fabius Street and the West Street Arterial. This
bridge is unused and in a state of disrepair.
Construction access to the Clinton Station site will
require the construction of a new access bridge.
Construction of an RTF at the Dickerson Street site
could be undertaken in several ways.
One alternative (east option) could include
demolishing the existing Ward Supply Company building
and reconstructing the existing Rescue Mission
Recreation Center at a different location on the
Rescue Mission property. This may entail raising
abandoned buildings along Seymour Street to
reconstruct the Rescue Mission Recreation Center in
this general vicinity. It may also be necessary to
provide additional improvements to other portions of
the Rescue Mission property that are in close
proximity to the Dickerson Street site.
A second alternative (west option) could include
demolishing the existing Ward Supply Company building,
relocating several active businesses on the west side
of Granger Street, and demolishing the business
buildings.
The land area available for both the Dickerson Street
east and west options would severely limit contractor
staging areas for construction for the previously
identified cost-effective in-line storage/vortex
separator CSO abatement facilities for the Clinton
Street CSO service area. (Note: as presented
previously, the vortex separator CSO treatment
technology requires less land area than both the
regional storage technology [35% less] and the ORF
technology [25% less]). Therefore, additional
property acquisitions and/or permissible use by the
nearby property owners would be required to provide
the necessary contractor staging areas to implement
these CSO abatement technologies at the Dickerson
Street (east and west options) site.
As part of this facilities planning effort, a Phase 1A
archeological literature review and assessment was
performed for each of the preferential site locations
noted above and the preliminary conveyances routing.
This information is included in the companion Clinton CSO Abatement: Environmental Information Document (Feb 2005) to
this Facilities Plan. Based upon the past record of
commercial/industrial activity identified in the Phase
1A literature review and assessment for the three
sites, site environmental remediation activities may
be required at these sites during construction.
In addition, a limited program of subsurface
exploration was performed at the Clinton Station and
Dickerson Street sites. These data indicate that
there is a greater likelihood of adjacent/nearby
building settlement due to construction activities at
the Dickerson Street site rather than at the Clinton
Station site. In addition existing site features
(Rescue Mission Recreation Center and potential
utilities located in Dickerson and Granger Streets may
preclude the use of external tie-backs for temporary
excavation bracing support at the Dickerson Street
site.
Table 5-14 presents the estimated total project cost
summary for an in-line storage/vortex separator RTF
located at either the Clinton Station site or
Dickerson Street West site. (Note: costs at the
Dickerson Street East site are expected to be higher
than the Dickerson Street West site due to the
required removal and relocation of the existing Rescue
Mission Recreation Center.)
TABLE 5-14. TOTAL ESTIMATED PROJECT COST(1), INCLUDING MITIGATION ($000,000) ALTERNATIVE RTF SITES |
|
|
Clinton Station Site
|
Dickerson Street Site (West Option)
|
|
Estimated Construction Costs
|
$52.0
|
$55.5
|
|
Estimated Site Mitigation Costs (2)
|
4.4
|
1.4
|
|
Estimated Special Costs Associated with Site (3)
|
1.9
|
2.2
|
|
Subtotal
|
58.3
|
59.1
|
|
Estimated Other Project Related Costs (4) (25% of est const cost)
|
13.0
|
13.9
|
|
Total Estimated Project Cost
|
$71.3
|
$73.0
|
Notes: (1) In-Line Storage/Vortex Separator RTF
(2) Includes temporary and permanent replacement parking, site enhancements, residential relocations, business relocation, and demolition costs, as warranted.
(3) Includes property acquisition, architectural enhancements, contaminated soil disposal, and construction access bridge, as warranted.
(4) Includes engineering (including construction phase services) legal, and administrative costs
Costs based on Feb 2005 dollars (ENRCCI=7298)
The total project cost includes the following cost
components:
Estimated construction cost
(see Table 5-9).
Estimated site mitigation costs
(includes temporary
and permanent replacement parking, site enhancements,
residential relocations, business relocations, and
demolition costs, as warranted).
Estimated special costs associated with site
(includes property acquisition, architectural
enhancements, contaminated soil disposal, and
construction access bridge, as warranted).
Estimated other costs
(includes engineering
[including construction phase services], legal, and
administrative costs; estimated at 25% of the
estimated construction cost).
As identified in Section 5.6, the most cost-effective
CSO abatement approach for the Clinton Street CSO
service area is in-line storage/vortex separator RTF
at one of the two preferential site locations. As
shown in Table 5-14, in-line storage/vortex separator
RTF at the Clinton Station site has the lowest
estimated construction cost and the lowest total
estimated project cost. Therefore, in-line
storage/vortex separator RTF at the Clinton Station
site is the recommended/preferred CSO abatement
approach for the Clinton Street CSO service area.
|