co-digestion calculations - cswea

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Jackie Strait HR Green [email protected] Co – Digestion: Biogas Production & Digester Capacity Calculations

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Page 1: Co-Digestion Calculations - CSWEA

Co-Digestion Calculations

Jackie Strait HR [email protected]

Co – Digestion: Biogas Production & Digester Capacity Calculations

Presenter
Presentation Notes
Lake Maggiore in the Italian Apls where Alessandro Volta discovered Methane Gas in 1776. He found it in 1776 by poking the mud bottom near the reeds with a stick and discovered bubbles rising to the surface. He captured it and then discovered it was flammable
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R2E | June 20th, 2019

Biogas Potential VS COD Carbohydrates, Lipids, Proteins

Digester Capacity Organic Loading Rate Specific Energy Loading Rate

Agenda

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Co-Digestion Organic Material

Presenter
Presentation Notes
Co-Digestion – process of using energy rich organic waste material to digesters
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WEF MOP 8 VSLR = 0.12-0.16 lb/d-cf (1.9-2.5 kg/m3-d) Specific Digester Gas Yield = 13-18 cf/lb VSr ( 0.8-1.0 m3/kg VSr) CH4 fraction = 60-70% Specific Methane Gas Yield = 7.8 – 12.6 cf / LB VSr (0.48 -0.7 m3/kg VSr)

Biogas Potential – VS

Digestion Time (d) VS destruction %

30 65.5

20 60.0

15 56.0Metcalf & Eddy 4th Edition (2003)

Presenter
Presentation Notes
Values are for TPS and TWAS
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Biogas Potential – VSHow to do you get VS and VSr values for co-digestion organic materials?

How to do you get Specific Digester Gas Yield and Digester Methane Fraction for co-digestion organic materials?

• Lab Test – 550° muffle furnace• Typically Empirical data

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Biogas Potential – COD CH4 + 2O2 -> CO2 + 2H20

2 moles of O2/mole of CH4 = 2 (32g O2/mole)/mole CH4 = 64 g/mole CH4

At standard conditions (0 deg and 1 atm) 1 mole CH4 = 22.414 L

22.414 𝐿𝐿𝑚𝑚𝑚𝑚𝑚𝑚𝑚𝑚 𝐶𝐶𝐶𝐶4

×𝑚𝑚𝑚𝑚𝑚𝑚𝑚𝑚 𝐶𝐶𝐶𝐶4

64 𝑔𝑔 =0.35 𝐿𝐿 𝐶𝐶𝐶𝐶4

𝑔𝑔 𝐶𝐶𝐶𝐶𝐶𝐶

Relationship holds for any type of anaerobically – digested material

Presenter
Presentation Notes
COD Balance In an anaerobic digester the COD loss is accounted for as methane., thus the COD of methane is the amount of oxygen is needed to oxidize the methane to carbon dioxide and water
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Biogas Potential – COD Specific Methane Gas Yield = 5.61 cf/lb COD (0.35 L/g COD) at 0 deg C and 1 atm

Methane Energy Projection = 960 BTU/cf ft Specific Energy Projection = 5,380 BTU/lb COD removed

5,380 𝐵𝐵𝐵𝐵𝐵𝐵𝑚𝑚𝑙𝑙 𝐶𝐶𝐶𝐶𝐶𝐶 ×

𝑐𝑐𝑐𝑐 𝐶𝐶𝐶𝐶4

960 𝐵𝐵𝐵𝐵𝐵𝐵 =5.61 𝑐𝑐𝑐𝑐 𝐶𝐶𝐶𝐶4

𝑚𝑚𝑙𝑙 𝐶𝐶𝐶𝐶𝐶𝐶

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Biogas Potential – COD Conventional Sludge 2:1 TPS/TWAS - 1.56 g COD/ g VSS Specific Methane Gas Yield = 5.61 cf/lb COD (0.35 L/g COD)

WEF MOP 8 - Specific Methane Gas Yield = 0.48 - 0.7 m3/kg VSr

1.56 𝑔𝑔 𝐶𝐶𝐶𝐶𝐶𝐶𝑔𝑔 𝑉𝑉𝑉𝑉𝑉𝑉 ×

0.35 𝐿𝐿 𝐶𝐶𝐶𝐶𝐶𝑔𝑔 𝐶𝐶𝐶𝐶𝐶𝐶 =

0.546 𝐿𝐿 𝐶𝐶𝐶𝐶4

𝑔𝑔 𝑉𝑉𝑉𝑉𝑉𝑉 =0.546 𝑚𝑚3 𝐶𝐶𝐶𝐶4

𝑘𝑘𝑔𝑔 𝑉𝑉𝑉𝑉𝑉𝑉

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Biogas Potential – Carbohydrates, Protein, Lipids Digester Gas Methane Fraction (Symons and Buswell , & McCarty)

𝐶𝐶𝑛𝑛𝐶𝐶𝑎𝑎𝐶𝐶𝑏𝑏𝑁𝑁𝑐𝑐 + 𝑛𝑛 − 𝑎𝑎4− 𝑏𝑏

2+ 7𝑐𝑐

4𝐶𝐶2O 𝑛𝑛

2+ 𝑎𝑎

8− 𝑏𝑏

4− 3𝑐𝑐

8𝐶𝐶𝐶𝐶4 + 𝑛𝑛

2− 𝑎𝑎

8+ 𝑏𝑏

4− 5𝑐𝑐

8𝐶𝐶𝐶𝐶2 + c 𝑁𝑁𝐶𝐶4𝐶𝐶𝐶𝐶𝐶𝐶3

Carbohydrates (C6H12O6) = approx. 50% methane Proteins ( C4H6.1O1.2N) = approx. 42% methane Lipids ( C18H36O2) = approx. 72% methane

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R2E | June 20th, 2019

Biogas Potential – Carbohydrates, Protein, Lipids Digester Gas Methane Fraction (Symons and Buswell, & McCarty)

𝐶𝐶𝑛𝑛𝐶𝐶𝑎𝑎𝐶𝐶𝑏𝑏𝑁𝑁𝑐𝑐 + 𝑛𝑛 − 𝑎𝑎4− 𝑏𝑏

2+ 7𝑐𝑐

4𝐶𝐶2O 𝑛𝑛

2+ 𝑎𝑎

8− 𝑏𝑏

4− 3𝑐𝑐

8𝐶𝐶𝐶𝐶4

𝑛𝑛2− 𝑎𝑎

8+ 𝑏𝑏

4− 5𝑐𝑐

8𝐶𝐶𝐶𝐶2 + c 𝑁𝑁𝐶𝐶4𝐶𝐶𝐶𝐶𝐶𝐶3

Doesn’t account for biomass yield or degradability Substrate Biomass Yield

(g cells/g COD consumed)

Carbohydrates 0.35

Protein 0.20

Lipids 0.038Speece, R.E. (2008)

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Co-Digestion Acclimation Period

David L Parry (2013)

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Organic Loading Rate Mass of VS added per day per unit volume 0.12-0.16 lb VS/d-cf (1.9-2.5 kg/m3-d)

Digester Capacity - Organic Loading Rate

Metcalf & Eddy 4th Edition (2003)

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SELR = energy loading/ reactor biomass (gCOD/d per gVS in digester)

Digester Capacity - Specific Energy Loading Rate

David L Parry (2013)

Presenter
Presentation Notes
Use VS as a proxy for active biomass. By basing the organic loading rate on the biomass in the digester it becomes independent of the feed concentration to the digester. Otherwise a different loading rate would be needed for each solids concentration in the feed. The SELR is shown to be independent of the percent total solids in the feed because the amount of biomass in the digester is taken into account. In contrast, the allowable VS loading rate increasing with the amount of biomass in the digester. Increase facilities confidence in higher loading rates.
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Example FOG – Loading Rate

David L Parry (2013)

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Questions from the Audience?

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BibliographyMetcalf & Eddy, Inc. Wastewater Engineering: Treatment and Reuse. Boston :McGraw-Hill, 2003

WEF/ASCE. Design of Water Resource Recovery Facilities, 6th ed. WEF Manual of Practice No. 8. McGraw-Hill, 2018

Speece, R.E. Anaerobic Biotechnology and Odor/Corrosion Control for Municipalities and Industries. ArchaePress, 2008

Rittmann, B.E. and P.L. McCarty. Environmental Biotechnology: Principles and Applications. McGraw-Hill, 2001

Symons, G.E. and A.M. Buswell. “The Methane Fermentation of Carbohydrates”. Journal of the American Chemical Society, 55 (5), 2028-2036 (1933).

Parry, David L. “Codigestion Research Builds Facility Operator Confidence.” BioCycle Energy, May 2013.