Primairy fast pyrolysis products from pine-wood - PowerPoint PPT Presentation

1 / 24
About This Presentation
Title:

Primairy fast pyrolysis products from pine-wood

Description:

Primairy fast pyrolysis products from pine-wood A comparison between wire mesh and fluidized bed pyrolysis Elly Hoekstra, Roel Westerhof and Kees Hogendoorn – PowerPoint PPT presentation

Number of Views:404
Avg rating:3.0/5.0
Slides: 25
Provided by: stud1375
Category:

less

Transcript and Presenter's Notes

Title: Primairy fast pyrolysis products from pine-wood


1
Primairy fast pyrolysis products from pine-wood
  • A comparison between wire mesh and fluidized bed
    pyrolysis

Elly Hoekstra, Roel Westerhof and Kees Hogendoorn
2
Aim
  • Study the primary pyrolysis processes and to
    clarify the primary reaction mechanisms.
  • By understanding of the primary fast pyrolysis
    mechanism it may be possible to develop methods
    to steer the final pyrolysis oil composition.

Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Aim
3
Wire-Mesh reactor
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Set-up
4
Operating conditions
Heating rate 7000 0C/s
Temperature Uniformity Mesh 35 0C
Temperature Fluctuations 5 0C
Vapor residence time lt 15 ms
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Set-up
5
Movies
Vacuum and Cooling
Atmospheric without Cooling
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Set-up
6
Primary versus Secondary Yields
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Primary
7
Primary versus Secondary Mw-distribution
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Primary
8
Primary versus Secondary SEM
melting/evaporation
physical entrainment
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Primary
9
Primary versus Secondary sugars
  • Observation
  • A THF insoluble fraction but water soluble
    fraction was observed for the experiments carried
    out using vacuum and cooling
  • HPLC Analyses (RUG)
  • This fraction contained mainly sugars
  • Model compound study glucose and levoglucosan
  • These compounds were evaporated and condensed
    without reactions taken place

Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Primary
10
Primary fast pyrolysis processes
  • High oil yields (gt 80 wt)
  • Extremely low char yields ( 5 wt)
  • Presence of high molecular weight products
  • Presence of sugars
  • Less alkane like groups (NMR)

Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Primary
11
Effect holding time yields
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Conversion Rate
12
Effect holding time gas and char composition
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Conversion Rate
13
Experimental progress Grey Intensity Method
Experimental Progress
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Conversion Rate
14
Conversion rate experimental progress
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Conversion Rate
15
Comparison with C. Di Blasi and C. Branca 2001
Colomba Di Blasi and Carmen Branca, Kinetics of
Primary Product Formation from Wood Pyrolysis,
Ind. Eng. Chem. Res. 2001, 40, 5547-5556
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Conversion Rate
16
Conversion rate
  • The majority of the reactions in our wire-mesh
    reactor was finished within 0.5 s.
  • Our results indicate that the actual primary
    pyrolysis process is faster than previously
    thought

Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
Conversion Rate
17
Biomass loading
Although the absolute biomass was small, the
results are still influenced by secondary
reactions, the extent is increasing with biomass
loading.
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Biomass Loading
18
Temperature yields
Wire-Mesh reactor
Pilot Plant
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Temperature
19
Temperature gas composition
Wire-Mesh reactor
Pilot Plant
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Temperature
20
Temperature Mw-distribution
Wire-Mesh reactor
Pilot Plant
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Temperature
21
Temperature Mw-distribution
Wire-Mesh reactor
Pilot Plant
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Temperature
22
Temperature Mw-distribution
Wire-Mesh reactor
Pilot Plant
Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Temperature
23
Temperature
  • Decrease in oil yield
  • Still cracking reactions possible under the
    extreme conditions in our set-up
  • However the yield is still above 60 wt at 700 0C
  • Heavier products formed at higher temperatures
  • Heavier molecules can evaporate at higher
    temperatures
  • Cracking is minimized inside the wire-mesh
    reactor

Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Temperature
24
Conclusions
  • Primary pyrolysis compared to conventional
    pyrolysis
  • High oil yields (gt 80 wt) and extremely low char
    yields ( 5 wt)
  • Less alkane like groups (NMR)
  • High molecular weight products and sugars
  • Heavier products formed at higher temperatures
  • Extremely fast conversion rate
  • However, secondary cracking reactions are
    extremely fast
  • Inside biomass layer
  • At high temperatures

Aim Set-up Primary
Conversion Rate Biomass Loading
Temperature Conclusions
..Conclusions
Write a Comment
User Comments (0)
About PowerShow.com