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The Future of Eucalyptus Pulp Bleaching Technology Tapani Vuorinen tapani.vuorinen@aalto.fi 7th International Colloquium on Eucalyptus Pulp May 26-29, 2015 Vitria, ES, Brazil Outline Aim Advances in pulp bleaching technology


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SLIDE 1

The Future of Eucalyptus Pulp Bleaching Technology

Tapani Vuorinen tapani.vuorinen@aalto.fi

May 26-29, 2015 Vitória, ES, Brazil 7th International Colloquium on Eucalyptus Pulp

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SLIDE 2

Outline

  • Aim
  • Advances in pulp bleaching

technology

  • Chemistry of ECF bleaching
  • Outlook for the future
  • Conclusions
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SLIDE 3

Aim of the talk

To show the high potential and solution for a revolution in eucalyptus pulp bleaching practice from today’s best available ECF bleaching technology… …in fulfilling the ”more with less” challenge: less chemicals, less water, less energy, lower environmental impact, lower capex

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SLIDE 4

Milestones

  • 1992-1995: Discovery of the importance
  • f hexenuronic acid (HexA) in kraft pulps
  • 1995-: Early mill scale implementations of

A-stage to remove HexA

  • 2000-: Large scale implementation of A-

stage in hardwood (eucalyptus) pulp mills

  • 2000-: Increasing understanding on the

chemistry of pulp bleaching

  • 2020-: Revolutionary pulp bleaching?
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SLIDE 5

Advances in eucalyptus pulp ECF bleaching technology

  • Old (1990’s)

– e.g. D-EOP-D-D

  • Modern BAT

– e.g. A/D-EOP-D-P, D/A-EOP-D-P, A-EOP-D-P – Half less ClO2 is needed (1.5-2 % as active chlorine dosage) – A hot acid stage with long retention time is added to remove HexA

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SLIDE 6

Main targets of pulp bleaching

  • To reach high brightness

– Low lignin chromophore content

  • To reach high brightness stability

– Low residual lignin content – Low hexenuronic acid (HexA) content – Low carbonyl content

  • To remove most of chromophores, lignin and

HexA without oxidizing polysaccharides

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SLIDE 7

Chemistry of ECF pulp bleaching

  • Monitoring the bleaching result

– Lignin content, HexA content – Brightness, viscosity, chlorate formation… – Oxidized structures, chromophores…

  • Knowledge on chemical reactions involved

– Inorganic reactions – Reactions of lignin and HexA – Structure-reactivity relationships

  • Modeling and simulation of complex reaction

systems

– Visit Poster 6 by Anna Kalliola et al.

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SLIDE 8

UV Raman spectra of bleached kraft pulps

Kristiina Kellokoski M.Sc. Thesis 2013

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SLIDE 9

General reaction scheme of chlorine dioxide bleaching

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SLIDE 10

Oxidants in chlorine dioxide bleaching

  • Chlorine dioxide (ClO2)

– Oxidizes phenols and hydroxyquinones (2 equivalents ClO2 per phenol or hydroxyquinone) – Produces ½ equivalents HOCl and ½ equivalents ClO2

  • Chlorite (ClO2
  • )

– Oxidizes aldehydes (formed in situ) forming equivalent amount of HOCl – Decomposes to chlorate (ClO3

  • ) and HOCl (catalysis by HOCl)

– May react with HOCl to regenerate ClO2

  • Hypochlorous acid (HOCl)

– Oxidizes HexA – Chlorinates and oxidizes lignin – Oxidizes cellulose and hemicelluloses

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SLIDE 11

Stoichiometry of overall reactions

  • 2ArOH + HexA + 4ClO2  2OxLig + OxHexA +

ClO3

  • + 3Cl-

– In this simplified (but relevant) scheme HexA and lignin are oxidized in a 1:2 ratio!

  • Formation of HOCl in situ

– 0.75-1 equivalents per added ClO2

  • Formation of chlorate (ClO3
  • )

– 0-0.25 equivalents per added ClO2

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SLIDE 12

Production of bleaching chemicals

Hypochlorite: (1) NaCl + H2O → NaOCl + H2 (electrolysis) Chlorate: (2) 3NaOCl → NaClO3 + 2NaCl (3) NaCl + 3H2O → NaClO3 + 3H2 (electrolysis) Chlorine dioxide: (4) NaClO3 + reductant → ClO2 Hydrogen peroxide: (5) H2 + O2 → H2O2 (catalytic)

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SLIDE 13

Production of bleaching chemicals and their usage (share of oxidation power)

3.NaCl 3.NaOCl (eq. HOCl, Cl2) NaClO3 ClO2 40 % HOCl, 40 % HClO2, 20 % ≤ 30 %

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SLIDE 14

Inefficiency in current ECF bleaching technology

  • Long retention times – huge bleaching towers
  • Excessive oxidation power needed in removal of

residual lignin and HexA

– 4-6 equivalents of oxidant per C6C3 + HexA – 7-9 equivalents of oxidant per C6C3 + HexA (HexA hydrolyzed by acid calculated out)

⇒ Target should be in doubling the efficiency!

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SLIDE 15

Reactivity of HOCl

  • Electrophilic reactions

– Primary oxidation of HexA - OK – Chlorination of lignin – reduces reactivity of residual lignin (by factor of 10 per each substitution) – Oxidation of lignin - OK – Oxidation of cellulose and hemicelluloses – may decrease brightness stability

  • Nucleophilic reactions

– Secondary oxidation of HexA – consumes oxidant without promoting removal of HexA – Oxidation of chromophores - OK

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SLIDE 16

Derivatives of HOCl (Cl2)

  • General reaction (nucleophilic substitution on chlorine):

Nu- + Clδ+-Clδ-  Nu-Cl + Cl- Nucleophile Product Name H2O/HO- HOCl Hypochlorous acid ClO- Cl2O Chlorine monoxide ClO2

  • Cl2O2

Dichlorine dioxide RCO2H RCO2Cl Acyl hypochlorite ROH ROCl Alkyl hypochlorite ArOH ArOCl Aryl hypochlorite R3N R3N+Cl Chloroammonium cation

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SLIDE 17

Characteristics of R3N catalysis

  • The actve form, R3N+Cl is extremely reactive
  • R3N+Cl is not a nucleophile like HOCl is
  • We targeted at improving the selectivity of HOCl

towards electrophilic reaction thus preventing e.g. overoxidation of HexA

  • We found that ozone becomes a highly selective
  • xidant after the catalytic treatment
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SLIDE 18

UVRR spectra of eucalyptus kraft pulps in A-EOP-D-P bleaching sequence

Leonardo Clavijo M.Sc. Thesis 2010

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SLIDE 19

UVRR spectra of eucalyptus kraft pulps in Hcat-Z-P bleaching sequence

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SLIDE 20

Production of bleaching chemicals (sum reactions)

Hypochlorite and peroxide: (6) NaCl + O2 + H2O → NaOCl + H2O2 Chlorate and peroxide: (7) NaCl + 3O2 + 3H2O → NaClO3 + 3H2O2

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SLIDE 21

Eucalyptus pulp bleaching sequence in the future?

Hcat-Z-P

NaOCl/HOCl: 0.5-0.7 % (as Cl2) Catalyst: 0.01 % O3: < 0.3 % H2O2: 0.25-0.35 % Total reaction time: ≤ 30 min Viscosity loss: < 50 ml/g

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SLIDE 22

Conclusions

  • Eucalyptus pulp bleaching could and should be

intensified from today’s BAT

  • In the future bleaching can be dramatically faster

than today and consume much less chemicals

  • In addition to lower investment and production

costs the new technology may better maintain beneficial fiber properties

  • Research and collaboration is still needed to
  • vercome the remaining challenges and verify the

technology on larger scale

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SLIDE 23

Acknowledgements

Long-term financers and idustrial collaborators:

  • TEKES (Finnish Funding Agency for Technology and Innovation)
  • Finnish Bioeconomy Cluster Ltd (Strategic Centre for Science,

Technology and Innovation)

  • Andritz, Metsä Fibre, Kemira, Stora Enso, UPM

Research collaborators during the past years:

  • Aalto University
  • BOKU
  • INPG Pagora
  • Universidad de la República
  • VTT