Cost model to drive biosolids planning decisions - ghd.com · Why Class A does not always make...

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Why Class A does not always make cents: Cost model to drive biosolids planning decisions Thor A. Young | Service Line Leader Sebastian E. Smoot | Engineer

Transcript of Cost model to drive biosolids planning decisions - ghd.com · Why Class A does not always make...

Why Class A does not always make cents: Cost model to drive biosolids planning decisions

Thor A. Young | Service Line Leader

Sebastian E. Smoot | Engineer

GHD @ WEFTEC 2015

Acknowledgements

Charles County Department of Public Works • Bill Shreve • Greg Boykin • Ed Gorham • Rea Schafer • Olin Straus • Sam Walter • Sam Simanovsky GHD • Kristi Perri • Brandon Gott

Context & objectives

GHD @ WEFTEC 2015

Context

Many municipal utilities considering upgrading their Class B biosolids operations to Class A Common project drivers: • Less restrictions than Class B • More outlets for distribution • “Hedging their bets” against

future Class B restrictions • Biosolids volume reduction • Increased biogas production • “Greener” process/product • Greater public acceptance Source: Scanlan et al. (2010). “Class A Digestion – What is its future in the US?” Proceedings of the Water Environment Federation. WEFTEC 2010.

GHD @ WEFTEC 2015

Solids Disposal, 37%

Labor, 21%

Energy, 18%

Misc, 11%

Maintenance, 7%

Chemicals, 6%

Typical operating costs for wastewater treatment

Source: U. Halbach (2003) Abwasserentsorgung in Brandenburg, Orientierungswerte Jahr 2003, Land Brandenburg, 2003. http://cgi.tu-harburg.de/~awwweb/wbt/emwater/documents/lesson_c2.pdf

GHD @ WEFTEC 2015

Image placeholder

Stock image of

scale balance with coins?

Cost considerations

In evaluation of future biosolids management options, utilities must consider the following for Class A alternatives vs. current operations: • Capital expenses (CAPEX) • Operation and maintenance expenses (OPEX) • Payback period • Impact on rate payers • Availability of funds for capital projects

Project background

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Mattawoman WWTP

• Located in Charles County, Maryland • Design capacity: 20 MGD • Current flow: 11 MGD (55%) • Upgraded for ENR in 2003 • Receives sludge from satellite facilities at the

headworks • A portion of plant effluent (5%) is reused

Image Source: Bing Maps

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25-yr projections of flows and solids production

2012 2017 2022 2027 2032 203702468

1012141618

Year

Flow

, mgd

; Sol

ids,

dry

tons

/day

WRF Influent Flow WRF Solids Production

GHD @ WEFTEC 2015

Primary Clarifiers

Secondary Clarifiers

Admin. Bldg

NORTH

Final Clarifiers

Aerobic Digesters

Dewatering Building

Gravity Thickeners

Septage Receiving

Reactors

Image Source: Bing Maps

Filters

GHD @ WEFTEC 2015

LEGEND Solids

Scum

Operated by Contractor

Simplified solids process flow schematic

Gravity Thickeners

Aerobic Digesters

3 & 4

Aerobic Digesters

6 - 11

Septage Receiving

Lime Stabilization

Belt Filter

Presses

Land Application

Thickening

Stabilization

Dewatering

Primary Clarifiers

Secondary Clarifiers

Final Clarifiers

Aerobic Digesters

1 & 5

GHD @ WEFTEC 2015

LEGEND Solids

Scum

Simplified solids process flow schematic

Gravity Thickeners

Aerobic Digesters

3 & 4

Aerobic Digesters

6 - 11

Septage Receiving

Thickening

Stabilization

Dewatering

Primary Clarifiers

Secondary Clarifiers

Final Clarifiers

Aerobic Digesters

1 & 5

Operated by Contractor

Mechanical Thickeners

Lime Stabilization

Belt Filter

Presses

Land Application

Thickened Combined Sludge to Stabilization and/or Dewatering

(Multiple Alternatives)

and other beneficial reuse

GHD @ WEFTEC 2015

0

10,000

20,000

30,000

40,000

50,000

60,000

70,000

0

20,000

40,000

60,000

80,000

100,000

120,000

140,000

160,000

Thickened PS(includes septage& 45% of WCS)

Thickened WAS(includes 55% of

WCS)

Total Sludge,Average

Conditions

Total Sludge,Maximum Month

Conditions

Solid

s, lb

/day

Flow

, gal

/day

Flow, gpd TSS, lb/d VSS, lb/d

Projection of solids flows at 20 MGD

19.3 Tons per day

29 Tons per day

GHD @ WEFTEC 2015

Existing Class B biosolids facility

Approach

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Technologies considered

Thermal Hydrolysis Thermal Dryer Anaerobic Digestion

Anaerobic Digestion Thermal Drying Thermal Hydrolysis

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Alternative 0 – status quo Class B lime stabilization

Thickened Primary Sludge

Thickened Secondary Sludge

Class B Biosolids

Dewatering (new centrifuges)

Lime Stabilization

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Alternative 1 – TPAD Temperature-Phased Anaerobic Digestion

Thickened Primary Sludge

Thickened Secondary Sludge

Class A Biosolids

Dewatering Mesophilic Anaerobic Digestion

(MAD)

Thermophilic Anaerobic Digestion

Cogeneration Electricity Natural Gas

GHD @ WEFTEC 2015

Alternative 2 – dryer Thermal dryer

Thickened Primary Sludge

Thickened Secondary Sludge

Class A Biosolids

Dewatering

Drum Dryer Hopper

GHD @ WEFTEC 2015

Alternative 3 – AD + dryer Mesophilic anaerobic digestion followed by thermal dryer

Thickened Primary Sludge

Thickened Secondary Sludge

Class A Biosolids

Dewatering

Drum Dryer

Boiler

MAD

Hopper

Natural Gas

GHD @ WEFTEC 2015

Alternative 4 – THP Thermal Hydrolysis Process and anaerobic digestion

Thickened Primary Sludge

Thickened Secondary Sludge

Class A Biosolids

MAD Dewatering

Thermal Hydrolysis

Process (THP)

Cogeneration

Hopper

Electricity Natural Gas

GHD @ WEFTEC 2015

Alternative 5 – THP + dryer THP and anaerobic digestion followed by thermal dryer

Thickened Primary Sludge

Thickened Secondary Sludge

Class A Biosolids

MAD Dewatering

Thermal Hydrolysis Process

Paddle Dryer

Boiler

Hopper Hopper

Natural Gas

GHD @ WEFTEC 2015

Summary of alternatives

LEGEND Thermophilic Digester

Mesophilic Digester

Thermal Dryer

Thermal Hydrolysis DW Dewatering

DW

DW

DW DW

Lime

Cogeneration

DW DW

DW DW

Cogeneration

Heat Recovery

Heat Recovery

Alt. 0 – Status Quo (Class B Lime Stabilization)

Alt. 1 – Temperature-Phased Anaerobic Digestion (TPAD)

Alt. 2 – Thermal Drying

Alt. 3 – Mesophilic Anaerobic Digestion and Thermal Drying

Alt. 4 – Thermal Hydrolysis and Anaerobic Digestion

Alt. 5 – Thermal Hydrolysis, Digestion, and Thermal Drying

Approach

GHD @ WEFTEC 2015

Assumptions

Land Application Unit Cost: Class A (90% solids): $25 per wet ton Class A (20-30% solids): $50 per wet ton Class B (20-30% solids): $75 per wet ton Contract Operations Unit Cost $100 per hour Regional Biosolids Revenue $70 per wet ton General Inflation Rate 3% Land Application Cost Inflation Rate 6% Nominal Discount Rate 1.8% Cost of Electricity $0.13 per kWh Cost of Natural Gas $8 per MMBTU Cost of Polymer $2 per pound Cost of Lime $180 per ton Annual Maintenance Cost 3% of equipment cost

GHD @ WEFTEC 2015

D&T D&T D&T D&T D&T D&T

THP THP AD

AD

AD AD

CHP CHP

Dryer

Dryer Dryer Site Site

Site

Site

EI&C EI&C

EI&C

EI&C EI&C

E&A E&A

E&A

E&A E&A

$0

$10

$20

$30

$40

$50

$60

$70

$80

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

Cap

ital C

ost,

2014

Milli

on U

SD

Dewatering andThickening (D&T)

LimeStabilization

Th. HydrolysisProcess (THP)

AnaerobicDigesters (AD)

Combined Heat& Power (CHP)

ThermalDRY

Site Work andYard Piping

Electrical &Controls (EI&C)

Engineering &Administration

Capital cost comparison

GHD @ WEFTEC 2015

E E E E E E NG

NG NG

NG

NG

P

P

P P

P

P

L CS

CS

CS

CS

EM

EM

EM

EM

EM

EM

LA

LA LA

LA LA LA

CL

CL CL

CL CL CL

$0

$10

$20

$30

$40

$50

$60

$70

$80

$90

$100

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of O

&M

Cos

ts, 2

014

Milli

on U

SD

Electricity (E) Natural Gas (NG) Polymer (P) Lime (L)

County Staff (CS) Equipment Maintenance (EM) Land Application (LA) Contractor Labor (CL)

Net Cost Electricity Cost Offset (E-) Heat Cost Offset (H-) blank

O&M cost comparison

GHD @ WEFTEC 2015

E E E E E E NG

NG NG

NG

NG

P

P

P P

P

P

L CS

CS

CS

CS

EM

EM

EM

EM

EM

EM

LA

LA LA

LA LA LA

CL

CL CL

CL CL CL

H- H-

H-

$0

$10

$20

$30

$40

$50

$60

$70

$80

$90

$100

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of O

&M

Cos

ts, 2

014

Milli

on U

SD

Electricity (E) Natural Gas (NG) Polymer (P) Lime (L)

County Staff (CS) Equipment Maintenance (EM) Land Application (LA) Contractor Labor (CL)

Net Cost Electricity Cost Offset (E-) Heat Cost Offset (H-) blank

O&M cost comparison

GHD @ WEFTEC 2015

E E E E E E NG

NG NG

NG

NG

P

P

P P

P

P

L CS

CS

CS

CS

EM

EM

EM

EM

EM

EM

LA

LA LA

LA LA LA

CL

CL CL

CL CL CL E- E-

H- H-

H-

$0

$10

$20

$30

$40

$50

$60

$70

$80

$90

$100

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of O

&M

Cos

ts, 2

014

Milli

on U

SD

Electricity (E) Natural Gas (NG) Polymer (P) Lime (L)

County Staff (CS) Equipment Maintenance (EM) Land Application (LA) Contractor Labor (CL)

Net Cost Electricity Cost Offset (E-) Heat Cost Offset (H-) blank

O&M cost comparison

GHD @ WEFTEC 2015

E E E E E E NG

NG NG

NG

NG

P

P

P P

P

P

L CS

CS

CS

CS

EM

EM

EM

EM

EM

EM

LA

LA LA

LA LA LA

CL

CL CL

CL CL CL E- E-

H- H-

H-

$0

$10

$20

$30

$40

$50

$60

$70

$80

$90

$100

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of O

&M

Cos

ts, 2

014

Milli

on U

SD

Electricity (E) Natural Gas (NG) Polymer (P) Lime (L)

County Staff (CS) Equipment Maintenance (EM) Land Application (LA) Contractor Labor (CL)

Net Cost Electricity Cost Offset (E-) Heat Cost Offset (H-) blank

O&M cost comparison

GHD @ WEFTEC 2015

$0

$10

$20

$30

$40

$50

$60

$70

$80

$90

$100

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of O

&M

Cos

ts, 2

014

Milli

on U

SD

Electricity (E) Natural Gas (NG) Polymer (P) Lime (L)

County Staff (CS) Equipment Maintenance (EM) Land Application (LA) Contractor Labor (CL)

Net Cost Electricity Cost Offset (E-) Heat Cost Offset (H-) blank

O&M cost comparison

GHD @ WEFTEC 2015

CAPEX

CAPEX CAPEX CAPEX

CAPEX CAPEX

OPEX

OPEX OPEX

OPEX

OPEX OPEX

$0

$20

$40

$60

$80

$100

$120

$140

$160

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of T

otal

Cos

ts, 2

014

Milli

on U

SD

Capital Costs O&M Costs RecoveredO&M Costs

Blank

Lifecycle cost comparison

GHD @ WEFTEC 2015

CAPEX

CAPEX CAPEX CAPEX

CAPEX CAPEX

LA

LA

LA

LA

LA LA

CL CL

CL

CL

CL CL

NG NG

NG

NG NG

Other Other Other

Other

Other

Other

$0

$20

$40

$60

$80

$100

$120

$140

$160

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of T

otal

Cos

ts, 2

014

Milli

on U

SD

Capital Costs Land App. Contractor Labor Natural Gas Other O&MCosts

RecoveredO&M Costs

Blank

Lifecycle cost comparison

Results

GHD @ WEFTEC 2015

$0

$20

$40

$60

$80

$100

$120

$140

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25

25-Y

ear N

PV

Life

cycl

e C

ost,

2014

Mil.

US

D (D

isco

unte

d)

Year

ALT 0 CLASS B ALT 1 TPAD ALT 2 DRYERALT 3 AD+DRYER ALT 4 THP ALT 5 THP+DRYER

Lifecycle cost comparison over time

AD+Dryer

Class B

THP+Dryer Dryer TPAD THP

Sensitivity Analysis

GHD @ WEFTEC 2015

Impact of increased cost of Class B land application

Baseline

Class A (90% solids)

$25 per wet ton

Class A (20-30% solids) $50 per wet ton

Class B (20-30% solids) $75 per wet ton

Adjusted inputs

Class A (90% solids)

$25 per wet ton

Class A (20-30% solids) $50 per wet ton

Class B (20-30% solids)

$85/95 per wet ton

GHD @ WEFTEC 2015

$0

$20

$40

$60

$80

$100

$120

$140

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25

25-Y

ear N

PV

Life

cycl

e C

ost,

2014

Mil.

US

D (D

isco

unte

d)

Year

ALT 0 CLASS B ALT 1 TPAD ALT 2 DRYERALT 3 AD+DRYER ALT 4 THP ALT 5 THP+DRYER

Lifecycle costs at various Class B unit costs

AD+Dryer

Class B

THP+Dryer Dryer TPAD THP

$75/WT $85/WT $95/WT

GHD @ WEFTEC 2015

Impact of reduced costs of Class A land application

Land application fees Baseline values

Class A 90% solids

$25 per wet ton

Class A 20-30% solids

$50 per wet ton

Class B 20-30% solids

$75 per wet ton

Adjusted inputs

Class A 90% solids

$0 per wet ton

Class A 20-30% solids

$25 per wet ton

Class B 20-30% solids

$85/95 per wet ton

GHD @ WEFTEC 2015

$0

$20

$40

$60

$80

$100

$120

$140

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25

25-Y

ear N

PV

Life

cycl

e C

ost,

2014

Mil.

US

D (D

isco

unte

d)

Year

ALT 0 CLASS B ALT 1 TPAD ALT 2 DRYERALT 3 AD+DRYER ALT 4 THP ALT 5 THP+DRYER

Lifecycle costs at baseline Class A unit costs

AD+Dryer

Class B

THP+Dryer Dryer TPAD THP

$75/WT $85/WT $95/WT

GHD @ WEFTEC 2015

$0

$20

$40

$60

$80

$100

$120

$140

0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25

25-Y

ear N

PV

Life

cycl

e C

ost,

2014

Mil.

US

D (D

isco

unte

d)

Year

ALT 0 CLASS B ALT 1 TPAD ALT 2 DRYERALT 3 AD+DRYER ALT 4 THP ALT 5 THP+DRYER

Lifecycle costs at reduced Class A unit costs

AD+Dryer

Class B

THP+Dryer Dryer TPAD THP

$75/WT $85/WT $95/WT

GHD @ WEFTEC 2015

E E E E E E NG

NG NG

NG

NG

P

P

P P

P

P

L CS

CS

CS

CS

EM

EM

EM

EM

EM

EM

LA

LA LA

LA LA LA

CL

CL CL

CL CL CL

$0

$10

$20

$30

$40

$50

$60

$70

$80

$90

$100

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of O

&M

Cos

ts, 2

014

Milli

on U

SD

Electricity (E) Natural Gas (NG) Polymer (P) Lime (L)

County Staff (CS) Equipment Maintenance (EM) Land Application (LA) Contractor Labor (CL)

Net Cost blank

O&M cost comparison (baseline)

GHD @ WEFTEC 2015

E E E E E E NG

NG NG

NG

NG

P

P

P P

P

P

L CS

CS

CS

CS

EM

EM

EM

EM

EM

EM

LA

LA

LA

CL

CL CL

CL CL

CL

$0

$10

$20

$30

$40

$50

$60

$70

$80

$90

$100

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of O

&M

Cos

ts, 2

014

Milli

on U

SD

Electricity (E) Natural Gas (NG) Polymer (P) Lime (L)

County Staff (CS) Equipment Maintenance (EM) Land Application (LA) Contractor Labor (CL)

Net Cost blank

O&M cost comparison (reduced Class A unit costs)

Baseline O&M Cost

GHD @ WEFTEC 2015

CAPEX

CAPEX CAPEX CAPEX

CAPEX CAPEX

LA

LA

LA

LA

LA LA

CL CL

CL

CL

CL CL

NG NG

NG

NG NG

Other Other Other

Other

Other

Other

$0

$20

$40

$60

$80

$100

$120

$140

$160

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of T

otal

Cos

ts, 2

014

Milli

on U

SD

Capital Costs Land App. Contractor Labor Natural Gas Other O&MCosts

RecoveredO&M Costs

Blank

Lifecycle cost comparison (baseline)

GHD @ WEFTEC 2015

Lifecycle cost comparison (reduced Class A unit costs)

CAPEX

CAPEX CAPEX CAPEX

CAPEX CAPEX

LA

LA LA

CL

CL CL

CL

CL CL

NG NG

NG

NG NG

Other

Other

Other

Other

Other

Other

$0

$20

$40

$60

$80

$100

$120

$140

$160

ALT 0CLASS B

ALT 1TPAD

ALT 2DRY

ALT 3AD+DRY

ALT 4THP

ALT 5THP+DRY

25-Y

ear N

PV

of T

otal

Cos

ts, 2

014

Milli

on U

SD

Capital Costs Land App. Contractor Labor Natural Gas Other O&MCosts

RecoveredO&M Costs

Blank

Baseline Lifecycle Cost

Conclusions

GHD @ WEFTEC 2015

Image placeholder

Conclusions

• Charles County opted to maintain Class B system for foreseeable future until new regulations or technologies result in cost advantages for Class A

• The impact of sudden and severe restrictions on Class B land application is a manageable risk for Charles County

• Clarifications – Study limited to financial analysis – GHG or carbon footprint not monetized – Did not examine grants or other funding sources