THIRD INTERNATIONAL SYMPOSIUM ON ENERGY FROM … · Future Research Despite the results achieved in...

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12/15/2010 1 PRE-TREATMENT EXPERIMENTS FOR THE USE OF CYNARA CARDUNCULUS L. AS A SUBSTRATE FOR THE PRODUCTION OF BIOGAS THIRD INTERNATIONAL SYMPOSIUM ON ENERGY FROM BIOMASS AND WASTE I.D.B. OLIVEIRA M. LAGEIRO S. DI BERARDINO J. GOMINHO E. DUARTE Mediterranean perennial crop with annual growth cycle, sprouting every autumn (10 months period). Adapted to dry and hot regions, it is an alternative crop for biomass production. The deep rooting system allows exploitation of soil profile (up to 7m depth). Water stress strategy: the cardoon above-ground biomass dries off in summer. In scientific trials the average production is 20 tons/ha.year of dry material, with 40% stalks, 25% leaves, and 35% capitula. CYNARA CARDUNCULUS L. [Gominho and Pereira, 2008]

Transcript of THIRD INTERNATIONAL SYMPOSIUM ON ENERGY FROM … · Future Research Despite the results achieved in...

Page 1: THIRD INTERNATIONAL SYMPOSIUM ON ENERGY FROM … · Future Research Despite the results achieved in the Final assay in terms of cumulative methane yield, there is still research work

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PRE-TREATMENT EXPERIMENTS FOR THE USE OF

CYNARA CARDUNCULUS L. AS A SUBSTRATE FOR

THE PRODUCTION OF BIOGAS

THIRD INTERNATIONAL SYMPOSIUM ON

ENERGY FROM BIOMASS AND WASTE

I.D.B. OLIVEIRA

M. LAGEIRO

S. DI BERARDINO

J. GOMINHO

E. DUARTE

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• Mediterranean perennial crop with annual growth

cycle, sprouting every autumn (10 months period).

• Adapted to dry and hot regions, it is an

alternative crop for biomass production.

• The deep rooting system allows exploitation of

soil profile (up to 7m depth).

• Water stress strategy: the cardoon above-ground

biomass dries off in summer.

• In scientific trials the average production is 20 tons/ha.year of dry

material, with 40% stalks, 25% leaves, and 35% capitula.

CYNARA CARDUNCULUS L.

[Gominho and Pereira, 2008]

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CYNARA CARDUNCULUS L.

[Gominho and Pereira, 2008]

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CYNARA CARDUNCULUS L.

[Gominho and Pereira, 2008]

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The biomass produced in the successive phases of the growth cycle has

different potential uses such:

Solid bio-fuel

Food oil

Biodiesel

Paper and pulp

Fiber boards

Drugs (cynarine, silymarine, antioxidants)

Green fodder

Rennet for cheese-maker

Fresh/processed vegetable

Gardening

[Gominho and Pereira, 2008]

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Objective

Pre

treatment

Anaerobic

digestion

Optimize methane

yield

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Material and methods

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Pre

treatment

Chemical

Biological

Thermal

Mechanical

Pre-treatments

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Pre-treatments

Mechanical

Sonolysis

FragmentationHigh pressure

Homogenization

Ozonization

Wet oxidation

Acidic hydrolysis

Alkaline hydrolysis

Chemical

Biological

Enzymatic hydrolysis

Thermal

Pre pasteurization

(<100ºC)

Thermal hydrolysis

(>100º)

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Pre-treatments

Mechanical

Fragmentation

Combined Pre-treatments Applied

Alkaline hydrolysis

ChemicalBiological

Enzymatic hydrolysis

Thermal

Thermal hydrolysis

(>100º)

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Batch experienceTwo Batch systems

300 ml working volume12 days of incubation time (37 ºC)

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2000 ml working volume

Batch experience

33 days of incubation time (37 ºC)

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Mechanical: Cynara stalks particle fragmentation

Batch experience: Influence of Mechanical Pre-treatment

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Different reaction times: 10 min (X1), 15 min (X2), 20 min (X3), 30 min (X4) and 0 min

(X5) were tested at 160 ºC.

10 min 15 min

Batch experience: Influence of Thermal Hydrolysis

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Influence of Thermal pre-treatment time on carbon solubilization and on C/N ratio

Batch experience: Influence of Thermal Hydrolysis

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Different chemical solutions were used: NaOH (14%) (X1) , NH3(aq) (1.5%) (X2),

HNO3 (1%) (X3)

NaOH

NH3 HNO3

Batch experience: Influence of Thermal Chemical Pre-

treatment

-120

-100

-80

-60

-40

-20

0

20

40

60

80

0,00

1000,00

2000,00

3000,00

4000,00

5000,00

6000,00

7000,00

CH

4 y

ield

po

ten

tial in

cre

as

e (%

)

CO

Dfi

ltra

te(m

g/l)

COD (filtrate)

Methane yield potential increase

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Enzymatic pre-treatment (during 40 h and 60 h)

Celluclast

+Novozymes 188

Batch experience: Influence of enzymatic

Pre-treatment on the anaerobic digestion process

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Enzymatic Hydrolysis

Methane content and Specific biogas yield obtained

after 12 days of incubation time

Batch experience: Influence of Enzymatic Hydrolysis

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Thermal chemical pre-treatment with NaOH within 20 min of thermal (160 ºC) reaction

time.

Pre-treated

substrateUntreated

substrate

Batch experience: Final assay

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Pre-treated substrate Untreated substrate

Before Anaerobic digestion

After Anaerobic digestion

Batch experience: Final assay

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Specific and cumulative methane yield during the Final assay (B0-reactor containing

inoculums, control; B1- reactor containing pre-treated substrate + inoculums; B2-

reactor containing untreated substrate)

Pre-treated substrate

Untreated substrate

Batch experience: Final assay

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The use of cardoon stalks as substract increased biogas

production;

Mechanical pré-treatment lead to an increase of biogas and methane

yield around 30% between 2 mm and 0.42 mm (40 mesh) particle

sizes;

Chemical pre-treatment with NaOH showed the best results in terms

of carbon solubilization, VS reduction, biogas and methane yield

increment;

Thermal chemical pre-treatment with NaOH was very effective even

for larger particle sized Cynara stalks;

Conclusions

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Thermal chemical pre-treatment with NaOH improved the

biodegradability of substrate, leading to an increment of biogas

and methane yields;

Mechanical pre-treatment and the addition of enzymes (exo-

1,4-β-D-glucanase and endo-1,4- β-D-glucanase and 1,4-β-D-

glucosidase) enhanced hydrolyses of the substrate improving

inoculums efficiency however more experiments are required within

higher incubation time.

Conclusions (cont.)

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Future Research

Despite the results achieved in the Final assay in terms of cumulative

methane yield, there is still research work to be developed in terms of

validating the most suitable pre-treatment for Cynara cardunculus L.

in Mediterranean countries and test it in a pilot-scale.

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Thank You!