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Review of Brine Disposal System Review of Brine Disposal System

Review of Brine Disposal System - PowerPoint Presentation

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Review of Brine Disposal System - PPT Presentation

DEIR Monterey Desal Project DRAFT Presentation to Monterey Peninsula Regional Water Authority 23 June 2015 Outline Brine Disposal System Overview Critical Issues Near Field Approach SemiEmpirical Analysis ID: 779986

analysis field dilution brine field analysis brine dilution plume diffuser potential disposal system ports jets appendix conservative approach additional

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Slide1

Review of Brine Disposal System

DEIR, Monterey

Desal

Project

DRAFT

Presentation to Monterey Peninsula Regional Water Authority

23 June 2015

Slide2

Outline

Brine Disposal System Overview

Critical Issues

Near Field Approach

Semi-Empirical Analysis

Conservative assumptions

Potential weaknesses

Far Field Approach

Conservative assumptions

Potential weaknesses

Results and Mitigation

Conclusions

Recommendations

Slide3

Brine Disposal System

3

Monterey Regional

Water Pollution

Control Agency’s (MRWPCA) ocean outfall and

diffuser (existing)Diffuser1,100 ft long90 – 110 ft deep172 ports total130 ports open8 ft port spacingAlternating sidesHorizontal discharge3.5 to 4 ft above sea floor

Source: Appendix D2

16

ft

Slide4

Brine Disposal System

4

Buoyancy

Wastewater floats

High dilution

Brine sinksLower dilutionBlend can do either

wastewater

brine

Source: modified from Appendix D2

Slide5

Discharge Composition

5

Source: Modified from Appendix D4

Slide6

Terminology

6

Source:

Abessi

& Roberts (2014)

Near Field Far

Field

Source: Jenkins

and Wasyl (2009).Dominated by jets

Short time and length scales

Seconds to minutes

Feet to tens of feet

Dominated by ocean processes

Long time and length scales

Hours to days

Hundreds of feet to miles

Slide7

Critical Issues

Near Field (mixing due to jet/plume velocity/buoyancy)

Achieving targets at edge of “brine mixing zone” (defined as the lesser of the zone of initial dilution (ZID) and 100 m)

Change in salinity < 2.0

ppt

(SWRCB March 2015 recommendation)Concentrations for numerous constituents as per 2012 California Ocean PlanEdge of ZID governs (ZID within 100 m)Critical case is when plume sinks7

Slide8

Critical Issues

Far Field (mixing due to ambient ocean currents)

Hypoxic: low dissolved oxygen concentration

Density currents

Pooling due to bathymetry

8May 5, 2015 Draft Final Desalination Amendment to the Ocean Plan

Slide9

Near Field Approach

Rising

positively-buoyant

plume

When volume of blended wastewater is large enough plume will rise

Analyzed using Visual Plumes (VP)Well accepted for rising (buoyant) plumesUsed appropriate ambient salinity and temperature conditionsAssumed zero ambient cross-flow (conservative assumption)Large dilution (≥ 68) at edge of ZID is achievedSalinity and Ocean Plan objectives easily met9

Slide10

Near Field Approach

Sinking negatively-buoyant plume

Considered two approaches:

Visual Plumes (VP)

VP is well-validated for rising plumes

Less validation for sinking plumes (especially for horizontal discharge)Compelling evidence that dilution from VP is substantially under-estimated for negatively-buoyant discharges (Palomar et al., 2012)CORMIX, CORJET, and JetLag also substantially underestimateDilution results from VP were not usedSemi-empirical analysisBased on analysis by Kikkert et al., (2007) and Fischer et al., (1979)Approach is reasonable … 10

Slide11

Semi-Empirical Analysis (Near Field)

Plume trajectory based

on

analysis

by

Kikkert et al. (2007)Well validated by experimentsDilution based upon analysisfor non-buoyant jet (Fischer etal., 1979) using plume lengthcalculated along trajectoryFischer approach is reasonable due to flat trajectory [vertical distance (3.5 feet) << horizontal distance (~12 feet)] i.e., jet behavior dominates in this region

11

~12

ft3.5

ft

Slide12

Semi-Empirical Analysis (Near

Field)

C

onservative assumptions

Dilution calculation assumed

round jet, whereas jet is oval shapedOval shape has higher area to volume ratio and will achieve more dilution than circular shapeAssumed minimum height above sea-floor of 3.5 feet (only 19 ports have height of 3.5 feet, most ports have height nearer to 4 feet)Larger height will allow for longer travel distance and more dilution12

Slide13

Semi-Empirical Analysis (Near

Field)

C

onservative assumptions

The dilution at the impact point was used in the analysis. However, the near-field continues beyond the impact point (the flow and mixing are still dominated by jet processes) and additional dilution will occur within the near field (i.e., the ZID is larger than assumed)

“the increase in dilutionfrom the impact point tothe end of the near fieldis approximately 60% for nonmerged jets” (inclined jets, Abessi & Roberts, 2014)13

Slide14

Semi-Empirical Analysis (Near

Field)

Potential Weaknesses

Analysis used in DEIR to assess merging of jets is ad-hoc

Volume of water entrained in 10 seconds was compared to volume of water available per port

Merging of jets will reduce dilutionRecommend replacing analysis in EIR with improved Port Spacing Analysis by Geosyntec (provided on Slide 16)Coanda effect is not addressed in DEIRCoanda effect is the tendency for a jet to deviate towards and attach to near surfaces (in this case the sea-floor)Coanda attachment would reduce dilutionRecommend including new Coanda Analysis by Geosyntec in EIR (provided on Slide

17)

14

Slide15

Semi-Empirical Analysis (Near

Field)

Potential Weaknesses

Existing ports are horizontal which is not optimal for negatively-buoyant discharges

Consider retrofit with inclined ports if additional dilution is required

15

Slide16

Port Spacing Analysis

Based on experiments

Abessi

& Roberts (2014) recommend the following to avoid merging of jets;

s >~2.d.F

where s = spacing, d = port diameter, and F = densimetric Froude numberd = 1.86 inches (Appendix D2, Table 3)F ≈ 26 (Appendix D1, Table 5)→ s > ~ 8 ftPort spacing on diffuser is 16 ft (alternating sides)Jets will not mergeSame conclusion as in DEIR, but this analysis is more robust16

Slide17

Coanda

Analysis

Based on experiments Shao & Law (2011) recommend the following minimum clearance above the sea-floor to prevent

Coanda

attachment;

z0 > 0.12 (π/4)0.25 d.F = 0.11 d.Fwhere, d = port diameter, and F = densimetric Froude numberd = 1.86 inches (Appendix D2, Table 3)F ≈ 26 (Appendix D1, Table 5)→ z0 > ~ 0.5 ft

Ports are 3.5 ft above sea-floor

Coanda attachment will not occurInclude this analysis in EIR

17

Slide18

Far Field Approach

Uses regional ocean model (ROM) to extract time-series of horizontal velocities (u and v) at diffuser location

Examines different seasonal patterns

Oceanic, Davidson, Upwelling

Assumes the velocity field (

u,v) is spatially homogeneousGenerally conservative assumptionNeglects local variations in bathymetryBathymetry in vicinity of brine plume is generally flat (no depressions or ridges) and sloping to seaBrine plume does not extend to Monterey CanyonDiffuser structure may act as a ridge to trap brine locallySolves 2-D advection-diffusion18

Slide19

Far Field Approach

Conservative assumptions

Neglects vertical mixing

Mixing and dilution underestimated away from the diffuser

Stability was examined via computing Richardson number

Uses low-end lateral diffusion coefficient1.37 m2/s (versus 2 m2/s measured by Ledwell et al., (1998))Neglects wave actionWaves provide additional mixingNeglects gravity currentGravity current would tend to move brine away from diffuser more quickly (down-slope)19

Slide20

Far Field Potential Weaknesses

Present analysis is “dated”

Modern approach would use full 3D model including density effects and spatially varying velocity field

However, present analysis is generally conservative

3D model will likely result in additional dilution

Neglects gravity currentsUnlikely to affect conclusions, since bathymetry is generally flat in vicinity of diffuserBrine plume does not reach Monterey Canyon20

Appendix D1, page 8

Slide21

Far Field Potential Weaknesses

Brine particles are only tracked for 48 hours

Simulation period is 90 days

What happens to particle after 48 hours?

If particle simply disappears then will the extent of the plume be underestimated?

Unlikely to affect conclusions, since exceedances are governed by near field21

Slide22

Far Field Potential Weaknesses

Local trapping of brine by diffuser structure was not fully addressed

Trapping is minimized by aligning diffuser structure with slope (perpendicular to shore)

Recommend adding discussion of this issue considering current directions (from ROM) with respect to diffuser alignment and tidal reversals

Potential for hypoxia was not addressed

Recommend including Hypoxia Analysis by Geosyntec in EIR (provided on Slides 23-25)22

Slide23

Hypoxia Analysis

Potential for hypoxia can be addressed using simple mass balance approach;

Estimate oxygen demand from sediments

Estimate oxygen supplied by brine plume (including entrained flow)

23

Sediment oxygen demand

Entrainment of dissolved oxygen

Slide24

Hypoxia Analysis

Sediment oxygen demand (SOD) in Monterey Bay

5.0 to 13.5

mmol

/m

2/day (Berelson et al., 2003)0.16 to 0.43 g/m2/dayAreal extent of plume~3,000 ft x 1,500 ft = 4,500,000 ft2~420,000 m2Mass flux consumed;70 to 180 kg/day24

Figure 4.3-5

Slide25

Hypoxia Analysis

Brine flow rate = 13.98 MGD

Dilution > 15

Entrained flow > 15 x 13.98 = 210 MGD = 9.2 m

3

/sAmbient dissolved oxygen concentration > 7 mg/Llower limit of Ocean PlanMass flux supplied;> 5,600 kg/dayOxygen supplied by entrained flow > 30 times greater than oxygen consumed by sedimentsHypoxia unlikely25

Slide26

Results and Monitoring

Results of analyses indicate some exceedances of Ocean Plan criteria at edge of ZID are possible for certain constituents;

Copper,

Ammonia

, Chlordane, DDT,

PCBs, TCDD Equivalents, ToxapheneDepends upon Project versus Variant and on flow blendsMonitoring program may indicate no exceedancesMany conservative assumptions in analysisDrawing source water through sand/sediments will likely remove some PCBsWill this cause a build up of PCBs in sediments?26

Slide27

Mitigation Measures

Proposed Mitigation Measure 4.3-4

Additional pre-treatment of source water

Treatment of discharge

Temporary storage and release of brine

3 million gallon brine storage basinStore 5 to 8 hours of flowCan pulsing achieve necessary dilutions?Recommend conducting additional near-field analysis to demonstrate (if necessary)Consider retrofit of diffuser to add inclined ports60o – 65o is optimal for negatively-buoyantNeed to also consider buoyant cases (trade-off)27

Slide28

Brine Disposal System - Conclusions

Brine disposal governed by near field

C

oncentrations at ZID

DEIR used two methodologies for near field

Visual Plumes for rising dischargesSemi-empirical analyses for sinking dischargesTrajectory for sinking plume from Kikkert et al., (2007)Dilution for sinking plume estimated using method for non-buoyant jet (Fischer et al., 1979)28

Slide29

Brine Disposal System - Conclusions

Near

field analyses

make

reasonable and conservative

assumptionsRound jets (instead of oval)Minimum height of port above sea-floor of 3.5 feetZID defined as jet impact point and not end of near field29

Slide30

Brine Disposal System - Conclusions

Near

field analysis of merging jets was

ad-hoc

New analysis by

Geosyntec indicates jets will not mergeNear field analysis of Coanda attachment was not includedAnalysis by Geosyntec indicates Coanda attachment will not occurNear field analysis was not performed to demonstrate extent of increased dilution due to pulsingMitigation measure 4.3-430

Slide31

Brine Disposal System - Conclusions

F

ar field analyses makes conservative assumptions

No vertical mixing of brine

Low-end estimate for horizontal diffusivity

Neglects wave actionNo density current*Far field method is “dated”3D simulations including density currents could be used3D simulations would likely result in more dilutionFlat bathymetry in the vicinity of the diffuser and conservative assumptions31

Slide32

Brine Disposal System - Conclusions

Potential for hypoxia not discussed

Analysis by

Geosyntec

indicates

hypoxia is unlikelyBrine trapping by diffuser structure not analyzedMinimized by aligning diffuser structure with slope (perpendicular to shore)Brine particles are only tracked for 48 hoursWhat happens to particle after 48 hours?32

Slide33

Brine Disposal System - Recommendations

Include the following analyses provided by

Geosyntec

Port merging

Coanda

effectHypoxiaAddress/discuss potential for build up of PCBs in sediments surrounding intakesConduct additional near field analysis to estimate additional dilution achievable by pulsing brine dischargeConsider retrofit of diffuser ports with inclined angles to achieve more dilution if necessary33

Slide34

Brine Disposal System - Recommendations

Add discussion

of

potential for diffuser structure to trap brine

Consider current

directions (from ROM) and bathymetry slope with respect to diffuser alignment and tidal reversalsConsider using 3D far field modelWill likely result in additional dilutionWill better address potential for brine trapping by diffuser structureAdd discussion of the effect of only tracking brine particles for 48 hours34

Slide35

Recommended Minor Edits

35

Issue

Description

Page

Comments / RecommendationsIncorrect interpretation of SWRCB 2012aSWRCB 2012a states that increase in salinity should be limited to < 5% of background, corresponding to 1.7 ppt in California waters. The DEIR then rounds this to 2.0 ppt

, but this is an incorrect interpretation of the 2012 document (i.e., it should be 1.7 ppt).

4.3-27The phrase, “(rounded to 2.0

ppt)” should be removed from the EIR. Note that SWRCB 2015 refers directly to 2.0 ppt (it does not refer to 5% or 1.7 ppt). That is, 2.0 ppt is the correct target per SWRCB 2015, but not per SCWRCB 2012a.

Different number of ports

The

correct number of

open ports (130) is first mentioned in Section

4.3. This is late in the report to mention the change (from 120) and surprises the reader.

4.3-72

The incorrect number of ports should be mentioned earlier in the EIR, including in the Executive Summary. It should also be re-iterated that using 130 instead of 120 provides additional dilution (as demonstrated in Addendum to Appendix D4).

Misleading statement overstates the extent of the plumeThe DEIR states, “where the plume extended from near the Monterey Submarine Canyon rim to the center of the southern half of Monterey Bay”. This statement overstates the extent of the plume, and is perhaps mistakenly based on the inset figure.4.3-88Revise wording to better indicate that the plume extent is several miles from the Monterey Submarine Canyon rim.

Slide36

Recommended Minor Edits

36

Issue

Description

Page

Comments / RecommendationsUnnecessary footnote in tableSee Comments / RecommendationsTable 4.3-11

Footnote ‘a’

should be removed and the column header changed from “Average Dilution” to “Centerline Dilution”.

Equation for centerline dilution not providedEquation (7) presented in Appendix D2 is for average dilution, whereas calculations provide centerline dilution (which is ~1.4 times lower (Fischer et al., 1979)). App D2,pages 10 and C-13

EIR should be modified to include the relation between average and centerline dilution.

Apparent discrepancy in port and duckbill size

4 inch duckbill valves are specified, but the port size is given as 2 inch.

App D2

This discrepancy should be corrected or explained.

Slide37

References

Abessi

& Roberts (

2014), Multiport Diffusers for Dense Discharges,

J. Hydraul. Eng. 04014032-1.Berelson, McManus, Coale, Johnson, Burdige, Kilgore, Colodner, Chavez,

Kuleda, Boucher (2003), A time series of benthic flux measurements from Monterey Bay, CA,

Continental Shelf Research 23 (2003) 457-481.Fischer, List,

Koh, Imberger, Brooks (1979), “Mixing in Inland and Coastal Waters”, Academic Press

Jenkins

&

Wasyl

(2009), Current Analysis for Receiving Water of the Santa

Cruz Seawater

Desalination Project, submitted to City of Santa Cruz, 49 pp + app.

Kikkert, Davidson, Nokes (2007), Inclined Negatively Buoyant Discharges, J. Hydraul. Eng. 2007.133:545-554.Ledwell, Watson, Law, Law, (1998), Mixing of a tracer in the pycnocline, Journal of Geophysical Research, 103(C10), 21499-21529.Palomar, Lara, Losada (2012), Near field brine discharge modeling part 2: Validation of commercial tools, Desalination 290 (2012) 28-42.Shao & Law (2011

), Boundary impingement and attachment of horizontal offset dense jets, Journal of Hydro-environment Research 5 (2011) 15-24.37