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HAL Id: hal-01927075

https://hal.archives-ouvertes.fr/hal-01927075

Submitted on 19 Nov 2018

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ENERGY VALORIZATION OF GRASSES BY DRY PROCESS

Ahmed Wahrani Khirech, J.F. Largeau, Mohand Tazerout

To cite this version:

Ahmed Wahrani Khirech, J.F. Largeau, Mohand Tazerout. ENERGY VALORIZATION OF GRASSES BY DRY PROCESS. WasteEng - Conference on Engineering for Waste and Biomass Val-orisation, Jul 2018, prague, Czech Republic. �hal-01927075�

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1- Context and aims

► A waste : mainly in Europe grass clippings represent a residues and so cost for disposing.

► Conventional valorisation : leave on lawn, compost or in anaerobic digestion

Aim of the work : study others ways for energy valorisation by dry processes:

Biomass energy (energy storage) and fuel&char by pyrolysis

Energy Valorisation of

Grasses by Dry Process

Authors Partners Grass clippings J ul y 2 -5, 2018 W aste En g 18 , Prag ue, Cz ech Rep ub lic

Ahmed WAHRANI KHIRECH Jean-François LARGEAU

Mohand TAZEROUT

CNRS Joint Unit GEPEA Department of Energy

Systems and Environment IMT Atlantique

4 rue Alfred-Kastler BP 20722, 44307 Nantes, France

2- Challenges :

► Process for energy storage: dry&shape process

- Stabilization of biomass (short time decomposition <48h) due to the high level of moisture (50-80%)

- Obtain a useful shape : grass clippings have not a helpful shape for storage or process

► Best Energy carriers by dry process : biomass energy VS fuel (gas/liquid) and char

► Economic : low-cost process in energy point of view (energy balance)

Keywords Contact

jean-francois.

largeau@icam.fr

Guo, F., Dong, Y., Lv, Z., Fan, P., Yang, S., and Dong, L. (2015). Pyrolysis kinetics of biomass (herb residue) under isothermal condition in a micro fluidized bed. Energy Convers. Manag. 93, 367–376.

Grass clippings Energy storage

Energy valorisation Kinetic coefficient Pyrolysis

3a Materials and methods Process for energy storage

-► Shredders : improve the moisture diffusion

► Pellet : pellet press developed by Icam (Ø 6mm, L≈15mm)

► Log : hydraulic press logs of grass + starch or paper (Ø 50mm, L=150mm)

► Drying : ambient air/ tower with forced ventilation

5- Conclusions and Perspectives

► Dry&shape process defined to stabilize, store and handling for energy storage (thermal energy)

► Kinetic degradation studied : parameters for dry process valorization identified

► Work in progress : identification of conversion potential into fuel and char by pyrolysis

► Calorimetric bomb : PARR model 6200

► TGA system :SETARAM Setsys-Evo

► Pyrolyser : batch process developed by Icam

► Kinetic method :

Arrhenius law with FWO model

► Efficiency : Ratio between thermal energy of log/pellet prod and energy spent and >15

► Mechanic handling : ok with/without starch,

ok with paper (if paper < 4%wt)

Grass pellets Log of grass

4b- Results : TGA & kinetic results

► TGA : 3 degradation steps :

200°C to 290°C (a part of) hemicellulose 300°C to 360°C hemicellulose + cellulose 360°C to 600°C lignin

► Kinetic coefficients

► Slow pyrolysis at 600°C :

Yields: 69% char, 21%liquid,10%gas

3b Materials and methods Energy valorisation

-Pellet press

4a- Results - Biomass characteristics, energy potential -

- this study -Grass

Herbs residues Guo&Al Douglas wood %H 50-80 N/A N/A LHV (kWh) 4,6 N/A 5,5 C wt% 74 42 48,1 H wt% 6,6 6,2 5,5 O wt% 17,5 47,4 45,8 N wt% 0,4 1,86 0,4 S wt% 1,5 0,15 0 H/C 0,09 0,15 0,11 O/C 0,24 1,13 0,95 Ashes (%) 7,0 10,8 0,25 Grass -this study-Herbs residues Guo&Al A [s-1] 1,06E+06 1,00E+06 Ea [J/mol] 146 105-130 ( ) exp( Ea ) K T A RT  

Some TGA results -1,4 -1,2 -1 -0,8 -0,6 -0,4 -0,2 0 0 200 400 600 800 0,0 10,0 20,0 30,0 40,0 50,0 60,0 70,0 80,0 90,0 100,0 D TG mg /mi n Temperature °C Ma ss lo ss % TG 10°/min TG 5°C/min dTG 10°C/min dTG 5°C/min

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