EMERGING TECHNOLOGIES TO IMPROVE EUCALYPTUS FIBERS QUALITY FOR PAPER - - PowerPoint PPT Presentation

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EMERGING TECHNOLOGIES TO IMPROVE EUCALYPTUS FIBERS QUALITY FOR PAPER - - PowerPoint PPT Presentation

UNIVERSIDADE FEDERAL DE VIOA Laboratrio de Celulose e Papel LCP/UFV CENTRO DE CINCIAS AGRRIAS DEPARTAMENTO DE ENGENHARIA FLORESTAL EMERGING TECHNOLOGIES TO IMPROVE EUCALYPTUS FIBERS QUALITY FOR PAPER That means: Trials to innovate


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SLIDE 1

EMERGING TECHNOLOGIES TO IMPROVE EUCALYPTUS FIBERS QUALITY FOR PAPER

Rubens Chaves de Oliveira

Laboratório de Celulose e Papel LCP/UFV

Vitória, June 29, 2015

UNIVERSIDADE FEDERAL DE VIÇOÇA CENTRO DE CIÊNCIAS AGRÁRIAS DEPARTAMENTO DE ENGENHARIA FLORESTAL

That means: Trials to innovate technologies

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SLIDE 2

THE PAPER STRUCTURE

INTRODUCTION

THE MAIN TOPICS

THE NATURAL BEAUTY OF THE WOOD AND FIBER STRUCTURES

EMERGING TECHNOLOGIES TO IMPROVE PAPER QUALITY

THE PAPERMAKING INDUSTRY ULTRASONIC TECHNIQUE TO REFINE THE PULP FIBERS MICROWAVES TECHNIQUE TO DRY PAPER

FINAL REMARKS

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SLIDE 3

THE WOOD CELL WALL STRUCTURE

15- 30 % 30- 50 % 10- 25 %

The wood structure is a complex and sustainable raw materials that the nature takes many years to construct it and I believe we are going to use it for so many years to make papers.

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SLIDE 4

THE FIBER CELL WALL STRUCTURE

The fibers cell wall are very important composite materials. They are the main elements on the paper structure. We should be able to find a technology to cause less damage to the fibers during the papermaking process.

Source:Zimmermann et. al. (2005).

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SLIDE 5

THE PAPER STRUCTURE AND STRENGTH

BASICALLY DEPENDS ON:

  • The fiber properties
  • The number of fiber bonds
  • The bond resistances
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SLIDE 6

THE IND INDUSTRY Y FR FROM WOOD TO O PAPE PER

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SLIDE 7

THE IND INDUSTRY Y FR FROM WOOD TO O PAPE PER

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SLIDE 8

PAPER MANUFACTURE: FROM WET END TO DRY END

STOCK PREPARATION PAPER FORMATION REELING DRY SECTION PRESSING SECTION

THE MECHANICAL REFINING TECHNIQUE

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SLIDE 9

MECHANICAL REFINING TECHNIQUE

Intra-Fiber Bond Break Fiber Cut Fines Generation Fiber Defibrillations

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SLIDE 10

ULTRASONIC VIBRATIONS OF PULP FIBERS TO IMPROVE PAPER STRENGHT

Laboratório de Celulose e Papel LCP/UFV

UNIVERSIDADE FEDERAL DE VIÇOÇA CENTRO DE CIÊNCIAS AGRÁRIAS DEPARTAMENTO DE ENGENHARIA FLORESTAL

Virsonic 475 (190 Watts; 20 kHz) Variables:

Eucalyptus pulp pH: 7,0 and 10,0 Pulp Consistency: 0,5%, 1%, 2% and 4% Time: 5 min, 10 min and 20 min

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SLIDE 11

ULTRASOUND PHENOMENON

When mechanical longitudinal waves with frequency higher than 20 kHz propagate in a liquid occur the cavitations' phenomenon

Low pressure moment High pressure moment FIBER SURFACE FIBER SURFACE FIBER SURFACE

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SLIDE 12

b) a)

0,5% 1% 2% 4%

800 850 900 950 1000 1050 1100 5 10 15 20

RCT (N/m) Time (min)

Ring Crush Test - pH 7

y = 1071,8 / (1 + (0,267e - 0,169 X )) r² = 0,90

800 850 900 950 1000 1050 1100 5 10 15 20

RCT (N/m) Time (min)

Ring Crush Test - pH 10

y = 1065,4 / (1 + (0,156e - 0,187 X )) r²= 0,95

25% 15%

ULTRASOUND TECHINIQUE RESULTS

Pulp Consistency :

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SLIDE 13

0,5% 1% 2% 4%

25 27 29 31 33 35 37 5 10 15 20

Tensile index (N.m/g) Time (min)

Tensile Index - pH 7

y = 23,85 (2,15 - e - 0,021 X ) r² = 0,97

25 27 29 31 33 35 37 5 10 15 20

Tensile index (N.m/g) Time (min)

Tensile Index - pH 10

y = 9,89 (3,573 - e - 0,288 X ) r² = 0,96

35% 40%

ULTR TRASOUND TE TECH CHINIQUE RE RESU SULTS

Pulp Consistency :

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SLIDE 14

0,5% 1% 2% 4%

8.0 8.5 9.0 9.5 10.0 5 10 15 20

Tear index (mN.m²/g) Time (min)

Tear Index - pH 7

y = 9,66 / (1 + (0,073e - 0,068 X )) r² = 0,85

8.0 8.5 9.0 9.5 10.0 5 10 15 20

Tear index (mN.m²/g) Time (min)

Tear Index - pH 10

y = 9,47 / (1 + (0,067e - 0,117 X )) r² = 0,79

6% 6%

ULTRASOUND TECHINIQUE RESULTS

Pulp Consistency :

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SLIDE 15

2.06 2.08 2.10 2.12 2.14 2.16 2.18 2.20 5 10 15 20

Bulk (cm³/g) Time (min)

Bulk - pH 10

y = 2,16 – 0,0037.X r² = 0,90

2.06 2.08 2.10 2.12 2.14 2.16 2.18 2.20 5 10 15 20

Bulk (cm³/g) Time (min)

Bulk - pH 7

y = 2,19 – 0,0039.X r² = 0,93 0,5% 1% 2% 4%

4% 4%

ULTRASOUND TECHINIQUE RESULTS

Pulp Consistency :

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SLIDE 16

PFI Ultrasound (U.S.)

800 900 1000 1100 1200 1300 19 21 23 25 27 29 31 33 35 37

RCT (N/m) ° Schopper Riegler

Ring Crush Test - pH 10

PFI: Y= 2039,8.e-18,24/X r²= 0,97 U.S.:Y= 1065,5 / (1 + 48,62.e-0,259.X) r² = 0,91

800 900 1000 1100 1200 1300 19 21 23 25 27 29 31 33 35 37

RCT (N/m) ° Schopper Riegler

Ring Crush Test - pH 7

PFI: Y= 1367,6 - 2,44.X - (186297,4 / X2) r²= 0,99 U.S.: Y= 1029/ (1 + 9,5.e-0,18X) r² = 0,91

25% 17% 38% 36%

ULTRASOUND TECHINIQUE RESULTS

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SLIDE 17

PFI Ultrasound (U.S.)

25 27 29 31 33 35 37 39 41 43 45 19 21 23 25 27 29 31 33 35 37

Tensile index (Nm/g) ° Schopper Riegler

Tensile Index- pH 7

U.S.: Y= 3,207 (X + 8,77)0,64 r²= 0,93 PFI: Y= 5,32 (X - 3,946)0,605 r² = 0,99

25 27 29 31 33 35 37 39 41 43 45 19 21 23 25 27 29 31 33 35 37

Tensile index (Nm/g) ° Schopper Riegler

Tensile Index- pH 10

U.S.: Y= 35,17 / (1 + 10096,5e-0,463X) r² = 0,98 PFI: Y= 48,89 / (1 + 15,39e-0,128X) r² = 0,99

52% 30% 68% 40%

ULTRASOUND TECHINIQUE RESULTS

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SLIDE 18

PFI Ultrasound (U.S.) y = -0,0197x + 2,56 r² = 0,98 y = -0,0002x2 + 0,003x + 2,2 r² = 0,90

1.85 1.90 1.95 2.00 2.05 2.10 2.15 2.20 2.25 19 21 23 25 27 29 31 33 35 37

Bulk (cm³/g) °Schopper Riegler

Bulk - pH 7

y = -0,0202x + 2,6 r² = 0,99 y = 2E-05x2 - 0,007x + 2,3 r² = 0,85

1.85 1.90 1.95 2.00 2.05 2.10 2.15 2.20 2.25 19 21 23 25 27 29 31 33 35 37

Bulk (cm³/g) °Schopper Riegler

Bulk - pH 10

4% 14% 4% 13%

ULTRASOUND TECHINIQUE RESULTS

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SLIDE 19

CONCLUSIONS

 The Ultrasonic technology can be successfully used to improve the paper strength. Our hypothesis: Ultrasonic treatment acts mainly on fiber surface leading external fiber defibrillation with less impact on bulk than PFI refine; Pulp consistency in the range (0.5%-4%) didn't affects the results; Increasing the pH makes the treatment more efficient for some specific properties; Efficient to increase the paper strength with less fiber damages; Little impact on Bulk; very much recommended to tissue word Less fiber cut and fines production than refine in PFI, to the same °SR increasing; New studies are need using more powerful ultrasound device, but with saving energy.

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SLIDE 20

THE IND INDUSTRY Y FR FROM WOOD TO O PAPE PER

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SLIDE 21

PAPER MANUFACTURE: FROM WET END TO DRY END

STOCK PREPARATION PAPER FORMATION REELING DRY SECTION PRESSING SECTION DRYIER CYLINDERS

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SLIDE 22

DRYING PAPER BY HEAT CONDUCTION

Fiber Cell Wall Delaminations. Increase fiber stiffness and hornification Intra-Fiber Bond Break. Intrinsic fiber strength reduction. Decrease inter-fiber bonds potential. Quality decreasing due to new production cycle.

1 2 3 4 5 6

CICLOS DE RECICLAGEM PROPRIEDADE

Drying Cycles

Paper Properties

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SLIDE 23

80ºC

Fan Optic Sensor

  • f

temperature BEKP Handsheets Polipropelleene Handsheets Holder Temperature Control Microwave Dryier 2.450 MHz Computer Control

T e m p e r a t u r e Time

LA LABORATORY MIC ICROWAVE EXPERIMENT

MICROWAVE DRYER:Temperature:80 oC; Final Handsheet consistency:95 %

Cylinder Dryer: Temperature: 100 oC; Final Handsheet Consistency: 95 %

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SLIDE 24

Source: GOULD (1995).

400 a 20.000 MHz

MICROWAVES PHENOMENON

When Microwaves with frequency between 400 to 20.000 MHz propagate in liquid or solid medium occur the friction phenomenon

Ionic Orientation Molecular Orientation

ELETRIC FIELD

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SLIDE 25

Suggestion mechanisms for Drying Fibers by Conventional Heat Conduction and by Microwaves Radiation

HEAT CONDUCTION MICROWAVES RADIATION WATER MOLECULE Microfibrils Fiber Cross Section Water Vapour More Collapsed Fibers Dried fiber Microfibrils Water Vapour Less Collapsed Fibers Dried fiber

Microfibril

Before Drying Before Drying Fiber Cross Section WATER MOLECULE a) Drying by Heat conduction b) Drying by microwaves Radiation Microfibrils

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SLIDE 26

CROSS SECTION OF FIBERS WALL

A)Drying by microwaves B) Drying by Heat Conduction

SEM Picture: 3000 x Virgin fiber

4 th Cycle of

Drying Virgin fiber 4 Th Cycle of Drying

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SLIDE 27

Microwaves Drying Microwaves Drying Microwaves Drying Microwaves Drying Heat Conduction Heat Conduction Heat Conduction Heat Conduction Fiber lentgh (mm) Fiber wall thickness (µm) Drying Cycles Drying Cycles Drying Cycles Drying Cycles Xilans (%)

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SLIDE 28

Heat Conduction Heat transfer Heating transfer Heating transfer Microwaves Drying Microwaves Drying Microwaves Drying Microwaves Drying Tensile Index (N.m/g) Tear ndex (mN.m2/g) Modulus of Elasticity (MN.m/kg) Softness (s/100 cm3) Drying Cycles Drying Cycles Drying Cycles Drying Cycles Heat Conduction Heat Conduction Heat Conduction

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SLIDE 29

CONCLUSIONS

  • The results of laboratory studies show that the application of microwave

radiation is a drying feasible alternative to dry paper.

  • The drying by microwave radiation provided a better preservation of the

structural properties related to the fiber length and cell wall thickness when compared to conventional heat conduction.

  • The fibers of dried papers by microwave radiation had higher content of xylan,

but this preservation was not reflected in better mechanical properties.

  • The dried papers by microwave radiation behaved similarly for all drying cycles

in relation to the mechanical and optical properties compared to paper dried to conventional heat conduction. Except for the smoothness property, where the microwave drying tend to produce papers with higher values.

  • The previous conclusion reinforces that this technology presents itself as a

possible alternative to the industries of paper, mainly from the tissue segment. However, requiring more studies with respect to its economic viability and how dangerous it may be to papermaker.

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SLIDE 30

THANK YOU

  • Dr. Carolina M. Jardim

Mauro Manfredi Rodrigo Guedes de Moraes Rogerio Peixoto Silva

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SLIDE 31

EMERGING TECHNOLOGIES TO IMPROVE EUCALYPTUS FIBERS QUALITY FOR PAPER

Rubens Chaves de Oliveira

Laboratório de Celulose e Papel LCP/UFV

Vitória, June 29, 2015

UNIVERSIDADE FEDERAL DE VIÇOÇA CENTRO DE CIÊNCIAS AGRÁRIAS DEPARTAMENTO DE ENGENHARIA FLORESTAL

FOR THE NEXT ICEP!!!! Enhance of Eucalyptus Fiber Properties Using Dielectric-Barrier Discharge

PLASMA TECHNIQUE TO IMPROVE INTERFIBERS BOND SURFACES