Pyrolysis & Char Processes Fernando Preto CanmetENERGY, Natural - - PowerPoint PPT Presentation

pyrolysis char processes
SMART_READER_LITE
LIVE PREVIEW

Pyrolysis & Char Processes Fernando Preto CanmetENERGY, Natural - - PowerPoint PPT Presentation

Pyrolysis & Char Processes Fernando Preto CanmetENERGY, Natural Resources Canada Charcoal Production & Use Pyrolysis in late medieval foundry processes Georgius Agricola, De Re Metallica Libri XII, MDLVI English translation 1912 by


slide-1
SLIDE 1

Pyrolysis & Char Processes

Fernando Preto CanmetENERGY, Natural Resources Canada

slide-2
SLIDE 2

Pyrolysis in late medieval foundry processes Georgius Agricola, De Re Metallica Libri XII, MDLVI English translation 1912 by Herbert Hoover

Charcoal Production & Use

slide-3
SLIDE 3

Char Production How can we optimize char production?

slide-4
SLIDE 4

Pyrolysis Stages

Temperature Process (Overlap) Major Products Heat

<200ºC Drying H20 IN 230ºC-250ºC Depolymerization Acetic acid, Methanol, CO2, CO IN 250ºC-280ºC Torrefaction Extractives, CO2, CO IN 280ºC-500ºC Devolatilization Organics, Tars, CO2,CO OUT 500ºC-700ºC Dissociation/Carbonization CO, H2 IN >700ºC Gasification H2, CO IN

slide-5
SLIDE 5

Time to Complete Pyrolysis as f(size)

  • X. Wang et al 2006
slide-6
SLIDE 6

5 10 15 20 25 30 35 40

Yield %

2.5 secs 5 secs 20 secs

Vapour Residence Time Liquid Gas Solid

Yields vs Residence Time

T=500 C

slide-7
SLIDE 7

Charcoal Yield as f(size)

  • X. Wang et al 2006
slide-8
SLIDE 8

Product(s) Yield as f(Temperature)

  • X. Wang et al 2006
slide-9
SLIDE 9

Product Distribution

A.V.Bridgwater

Mode Conditions Liquid Char Gas Fast pyrolysis Moderate temperature, short residence time 75% 12% 13% Slow Pyrolysis Low temperature, very long residence time 30% 35% 35% Gasification High temperature, long residence time. 5% 10% 85%

slide-10
SLIDE 10

Species Migration: S, N

  • J. Hrbek et al 2006
slide-11
SLIDE 11
  • J. Hrbek et al 2006

Species Migration: Cl, K

slide-12
SLIDE 12

Yield of Traditional Charcoal Processes

  • Batch processes:
  • Earth pits and mounds

>10%

  • Brick, concrete, and metal kilns

20-25%

  • Retorts

30%

  • Continuous processes:
  • Retorts (Lambiotte)

30-35%

  • Multiple hearth reactors (Herreshoff)

25-30%

FAO Rinsing Retort

slide-13
SLIDE 13

Pyrolysis: Industrial Research in Canada

ABRI-Tech Airex Alterna Organic Power Titan Agritherm… ABRI-Tech Airex Agritherm Ensyn Dynamotive…

slide-14
SLIDE 14

Courtesy NREL

slide-15
SLIDE 15

Maximizing Charcoal Yield

slide-16
SLIDE 16

Maximizing Charcoal Yield

  • Low pyrolysis temperature (<400ºC)

(but also lower fixed carbon content)

  • High process pressure (1 MPa)

(higher concentration of pyrolysis vapor increases rate of secondary reactions)

  • Long vapor residence time

(extended vapor/solid contact promotes secondary coke forming reactions)

  • Low heating rate

(slower formation and escape of organic vapors)

  • Large biomass particle size

(low thermal conductivity of biomass results in slow heat and mass transfer rate within particles)

slide-17
SLIDE 17

Fernando Preto

preto@nrcan.gc.ca Tel: 613-996-5589

Questions?

Thank You!

http://canmetenergy.nrcan.gc.ca/