Thermodynamic modelling of potassium in the after burner of a - - PowerPoint PPT Presentation

Thermodynamic modelling of potassium in the after‐burner of a biomass gasifier

• S. Vakalis, U. Sénéchal, R. Schneider, B. Solomo, M. Kurz, K. Moustakas,
• A. Sotiropoulos, D. Malamis, M. Baratieri, T. Zschunke

Limassol, June 24th 2016

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Gasification

Fuel

(C – rich) Gasifying medium (air, O2, CO2) Tar, Dust, Ash, Soot Char Syngas

• r

Producer gas

Concept of gasification

λ < 1 Gasification is a thermal process which under sub- stoichiometric conditions “packs” energy into chemical bonds

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Syngas - Producer gas

Syngas CO, H2 Producer gas CO , H2 , CO2, CH4 but also N2

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Other by-products

Dust - Soot

Char – high in carbon Ash – inert minerals Tar - heavy organic compounds

Char characteristics and management

Management of the residue char remains an imporant problem in the small scale gasification sector. The main reason is the concentration of heavy metals. Solutions to the problem should be developed on a local level or even better onsite, since the amount of produced char from small scale gasifiers is not sufficient in order to provide incentives for more centralized projects.

Char is a carbon rich material and its structure is similar to graphite

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Gasifier with an onsite application

Source: Spanner RE website

• Joos gasifier
• Two separate vessels
• 30 kWe, 80 kWth
• Main product: producer gas
• 23 – 25 % el. Efficiency
• 70 % CHP efficiency
• 2 – 5 % char as by - product

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The introduction of an after- burner

GASIFIER FILTER AFTER- BURNER

CHAR PRODUCTS

Char reacts on a secondary stage with air at an elevated temperature (450 °C – 750 °C). The scope is the distribution of heavy metals between the gaseous and the solid phase. Usually a reduction > 20 % is sufficient for reduction into accepted environmental limits.

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Benefits of after-burner integration

The content of heavy metals is correlated to the quality of the input. After gasification their concentration increases by orders of magnitude. As a result, char may be potentially treated as hazardous waste. The integration of an after-burner assists:

• Reduction of char volume
• Reduction of heavy metals and alkali metals content
• Reduction of tar compounds trapped in the solid residue

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Modelling the after - burner

• Optimization of the after – burner has the scope to minimize simultaneously char -

tar – metals contents

• A commercial software was utilized for modelling the equilibriums of heavy and

alkali metals. (Master Thesis of Barbora Zezulova)

• The commercial software provided very interesting results concerning the

thermodynamic equilibriums of all the investigated heavy and alkali metals.

• Nonetheless, several issues had to be taken into cosideration for the case of the

after-burner.

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Issue 1 - Yield of carbon

0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100% moles per mole fuel C

Predicted elements gas/liquid/solid phase 650 °C

Solid Liquid Gas

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Issue 2 – Gas composition

0,05 0,1 0,15 0,2 0,25 0,3 0,35 0,4 0,45

600 700 800 900 1000 1100 1200

Mole fraction, dry basis

Temperature, C

Equilibrium concentrations of gas species

CO2(g) N2(g) O2(g) H2(g) CO(g) CH4(g)

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Issue 3 – Air input in the after-burner

Air input can be measured by means of a Pitot tube. Nonetheless, the input is separated in two streams in order to cover the operation of the gasifier and the operation the after-burner. The air that enters the after- burner can be only indirectly calculated.

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Introduction of thermodynamic model

• MATLAB/ Cantera model
• Databases: GRI-Mech, NASA
• Mechanisms: KOH.cti., graphite.cti, gri30.cti
• 3-phase model with char phase represented by

graphite and potassium/ potassium oxides is represented by the KOH.cti

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Solid – Liquid – Gas equilibriums of metals

0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100% Al Ba Ca Cl Cr Cu Fe K Mg Mn Na P S Si Sr Ti Zn

element i

Predicted elements gas/liquid/solid phase 650 °C

Solid Liquid Gas

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Fundamental concept of the model

• The balance of char is used as a control variable in order to assess the

amount of reactive oxygen.

• Potassium yield is calculated for different temperatures.
• Gaseous species are calculated in accordance

Monitoring of a Spanner gasifer was used for verification of results

• Spanner HK30
• Hochschule Zittau/ Görlitz
• Measurements follow the ‘Recommendation CTI 13‘

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Results – Char residue yield

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Results- Solid pottasium (K) yield

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Results - Gaseous species (ER 0.25)

0,05 0,1 0,15 0,2 0,25 0,3 0,35 0,4 600 700 800 900 1000 1100 1200

molar fraction (%) Temperature (°C)

CO CO2

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Comparison of results (at 650 °C/ 0.25 ER)

Commercial software Cantera model Case study Char Yield 0% 75 % 79.5 % Potassium Yield 78 % 72 % 70.2 % Gaseous Species Primarily carbon dioxide at all temperatures Transition to carbon monoxide above 700 °C n.a.

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Conclusions

• The utilization of an after-burner is a unique commercial application

that is financially sustainable.

• Modelling the after-burner may result to the optimization of the

process

• The Cantera model was able to return more reliable results for the

estimated char yield, potassium yield and the composition of the main gaseous species in comparison to the commercial software.

• It should be denoted that this model aims only to assist and not to

replace commercial softwares.

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THANK YOU FOR YOUR ATTENTION!

For further info: stergios.vakalis@outlook.com

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