Fast Curing of Composite Wood Products Program Review by A.J. Ragauskas
Research Team Institute of Paper Science and Technology Georgia Institute of Technology Art J. Ragauskas, Associate Professor Chemistry Dong Ho Kim, Post Doctoral Research Fellow Jason Montegna, MS student Auburn University School of Forestry Thomas Elder, Professor of Forestry Utilization of Southern Forest Products, USDA-Forest Service Southern Research Station, Pineville, LA
Industrial Partners Georgia-Pacific Resins, Inc. -Resins, press time, & technical expertise Decatur, GA Georgia-Pacific Building Products Louisiana-Pacific Corporation -Wood chips, technical Sherwood, OR expertise
Weyerhaeuser OSB Business Tacoma, WA -Wood chips & technical expertise
Project Objectives Develop low temperature curing technologies for composite wood products manufactured with UF and PF resins by: •
Identifying rate limiting UF and PF curing reactions with current market resins.
•
Examining the use of new catalysts to accelerate curing reactions to reduced press temperatures and times.
•
Improve Board Properties.
U.S. Technology Market • 20 MDF mills • 41 OSB mills • 48 PB mills 1. Debarking 2. Mechanically refined wood 3. Drying 3’. Resins/mat formation/pressing
Project Deliverables • Characterize SW and HW woodchips • Prepare OSB, MDF, and PB • Characterize boards for physical strength properties & curing chemistry • NMR & DSC • Evaluate impact of extractives on composite board properties • Evaluate curing chemistry of PF and UF for composite board • Examine impact of plate pressure & temperature on curing resin chemistry • Design & evaluate effect of curing catalyst for composite board formation
Program Deliverables • Evaluate pretreatments to mitigate detrimental wood extractives effects • Test catalyst curing technology • Employ catalyst to lower curing temperature • Characterize board properties and chemistry with new catalyst • Perform energy audit for new catalyzed composite board formation process • Final report
Characterize Woodchips/Resins Commercial OSB Wood Strands % Extractives
% Moisture Content
Pine
4.2%
4.0%
Aspen
4.4%
3.7%
Hardwood
4.4%
7.1%
Strand Dimensions: (0.5-0.7mm) x (20-30mm) x (20-40mm) Resins*:
UF
PF-3110
PF-3121
pH
7.5
11.0
9.7
Solids Content
64.4%
46.2%
58.8% * Commercial resins
Evaluate Curing Chemistry PF and UF Gel Time Experiment • ASTM: D 3056-00 • 100.0oC • Insert sample into sample vial •Rapidly add catalyst • Begin stirring • Allow test specimen to remain in bath till stirring stops
Evaluate Curing Chemistry PF and UF
40
Gel Time (min)
35 30 25 20 15 10 5 0
UF Resin
PF: 3121
PF: 3110
Evaluate Curing Chemistry PF and UF O O
O
40 35
O Gel time (min)
30
H
25
O Me
20
O
O
15 Control
10
O
O
tetraethylenepentamine
O
10% Triacetin
5
10% Propylene Carbonate
0 UF Resin
O
10% Methyl Formate PF: 3121
PF: 3110
HN
N
NH2 2
Gel Times (min)
Evaluate Curing Chemistry PF and UF
40 35 30 25 20 15 10 5 0
Control 5% Additive 1 10% Additive 1
UF PF: Resin 3121
15% Additive 1
PF: 3110
Evaluate Curing Chemistry PF and UF
Gel time (min.)
35 30 25 20 15 10 5 0 C
ro t on
1% 0.
l
di d A
e tiv
5% . 0
2 d d A
e ti iv
0% . 1
PF:3121 PF:3110 UF
2 d d A
e ti iv
2
0% . 5
d Ad
e itiv
2
Evaluate Curing Chemistry UF: Binary Effects
40
Gel Time (min)
35 30 25 20 15 10 5 0 Control
1% Methyl Formate
10% Additive 1
1% MeF + 10% Add. 1
Evaluate Curing Chemistry PF: Binary Effects 35
Gel Time (min)
30 25 20 15 10 5 PF:3121
0 Co ntro l
1% P ro pylene Carbo nate 10% A dditive 1
PF3110 10% A dd. 1+ 1% P ro pyl.
Evaluation of Additive 1 For OSB Production Preliminary Studies
OSB Production: Experimental Procedure •Wood strands were weighed to yield final board densities of approximately 0.62 gr/cm3. •The PF and UF resins/additives applied onto wood strands via air sprayer unit •Blended furnish was then hand felted into a form box with aluminum cauls. •Mat consolidation and curing were accomplished using a laboratory hydraulic press (Carver press, 6” x 6”). •PF resins treated strands were cured at a press temperature of 350oF with 2.8 Mpa pressure for 3 minutes. •UF treated strands were treated in a comparable method except the press temperature was 300oF.
OSB Production: Experimental Procedure After board formation •All boards were conditioned at 20oC and 50% humidity for 72 hrs.
Thickness swelling and water adsorption were measured according to ASTM D1037 and DIN52364. The specimens were soaked in deionized water at 20oC. After 2 hrs, the specimens were withdrawn from the water and wiped with a paper towel to remove excess water. Increases in weight and thickness during the immersion were calculated on a mass basis and expressed as percentage.
OSB Laboratory Results 160 140
% increase
120 100 80 60 40 20 0 )
% % (5 (5 0 I 1 e 31 i tiv PF d d )/A % (5 0 11 3 PF
t. Wa ter A bso rp elling Thic kne ss Sw
) ) ) 5% % ( 5 1 1( 12 e 3 v ti PF di d )/A % 5 1( 2 31 PF
U
5% F(
% (5 F U
)
e itiv d d )/A
5% 1(
)
Preparation and Evaluation of Control and Additive OSB Production Follow-Up Studies
OSB Follow-Up Studies: Pilot Plant OSB Strands: Mat Dimension: Mat Formation: Target Density: Resin Content: Wax Content: Resin: Blend Moisture Content:
2.1kg per a board 40.6 x 40.6 x 2.9 cm One layer with random orientation 0.688 gr/cm3 3.5%(based on OD wt of strands) 1% on oven dry wood PF3110 7.0-7.5%
Press temp: Press pressure: - recommended by GP
400oF 95, 120 tons
OSB Follow-Up Studies: Pilot Plant Thickness Sw elling: 2h
20
Water Absorption: 2h
18
% Change
16 14 12 10 8 6 4 2 0
Wa te rA b so rp o ti n :2 h
T h ci k n e sS w e n il g :2 h
0.5% Additive 2, 5% additive 2, 120 tons
1.5% Additive 2, 120 tons
50
0.5% Additive 2, 120tons
Control, 120tons
5% Additive 1, 95tons
2% Additive 1, 95tons
1% Additive 1, 95tons
Control, 95tons
% Increase
OSB Follow-Up Studies: Pilot Plant 60 Thickness Sw elling: 24 h
Water Absorption: 24h
40
30
20
10
0
T h ci W
k a
n e t
e rA
sS b
w so
e rp
n il o ti
g n
:2 :2
4 4
h h
OSB Follow-Up Studies: Pilot Plant OSB Board
IB Density/(kg/m3)
IB/psi
Control 4.50 min, 95 ton
705
36.9
4.75 min, 95 ton
692
37.8
Additive 1 1%
4.50 min, 95 ton
712
54.1
2%
4.50 min, 95 ton
700
45.3
4.75min, 95 ton
722
42.5
4.50 min, 95 ton
707
39.2
5%
OSB Follow-Up Studies: Pilot Plant OSB Board
IB Density/(kg/m3)
IB/psi
Control 4.75 min, 120 ton
734
40.0
5.00 min, 120 ton
705
42.9
Additive 2 0.5%
4.75 min, 120 ton
689
43.1
1.0%
4.50 min, 120 ton
709
45.3
NMR Studies: PF and UF Curing OH
OH
PF resin Chemistry
OH
CH2
CH2
O
OH
OH HOH2C H2CO
CH2OH Heat Water Released CH2OH
Phenol
CH2
CH2
CH2
O
O
O
CH2
CH2
CH2
OH
OH
OH
CH2
CH2
UF Curing Chemistry O
O
O
H 2CO H 2N
NH2 Urea
H 2N
HO
H 2CO
OH NH
OH HN
Monomethylol Urea
Dimethylol Urea O
HO
O
NH
NH
N
NH
N
NH
H2C HO
NH
H 2C
O
N
NH O
Heat Loss of Water
NMR Studies: PF and UF Curing C2-6
-CH2C2-6 downfield sidebands
-CH2-OC1=O
-COx
C2-6 upfield sidebands
Solid state CP/MAS 13C NMR spectrum of PF 3110 resin as curing of 64 minutes.
NMR Studies: PF and UF Curing
Mol Ratio
3.0
F/P -CH2-/ P CH2-O / P
2.0
1.0
0.0 0
20
40
60
80
100
120
140
Curing Time, min
The mol ratio of methylene C to phenol C of the resin PF 3110. –CH2-/P: ratio of methylene/phenol; CH2-O /P : ratio of oxygenated methylene /phenol
NMR Studies: PF and UF Curing F/P -CH2-/ P CH2-O / P
Mol Ratio
3.0
2.0
1.0
0.0 0
20
40
60
80
100
120
140
Curing Time, min
The mol ratio of methylene C to phenol C of the resin PF 3121. –CH2-/P: ratio of methylene/phenol; CH2-O /P : ratio of oxygenated methylene /phenol
NMR Studies: PF and UF Curing Mol Ratio
3.0
2.0
F/U -CH2-/ U CH2-OH /U
1.0
0.0 0
20
40
60
80
100
120
140
Curing Time, min
The mol ratio of methylene C to urea C of the UF resin. –CH2-/U: ratio of methylene/urea; CH2-O /U : ratio of oxygenated methylene / urea; F/U: ratio of total methylene/ urea. Data indicated that the ratio of methylene and hydroxymethyl C/ urea C decreased as the curing proceeded.
Evaluate Impact of Extractives on Composite Board Properties
Evaluating Extractives: Exper. Procedure • Received industrial SW MDF, OSB, and PB furnish • Solvent extracted the wood furnish for 36 h • Used starting and extracted wood furnish for OSB, PB, and MDF • Tested for Physical Properties including: Thickness Swelling, Water Adsorption
Evaluating Extractives: Experimental Results 140 120
% Change
100 80 60 40 20 0
O
SB
F (P
O
0) 1 1 :3
SB
ex
es ti v c tra
e fre PB PB
(U
Water Absorption Thickness Sw elling
F)
e fre s e tiv c tra ex
DF M
F) (U
DF M
c ra t ex
es tiv
e fre
O
O
O
O
SB
SB
SB
SB
pr et rE
nz
y
y
y
y
nz
nz
nz
rE
rE
rE
et
et
et
pr
pr
pr
II
II
1
(5
(1
(5
(1
SB
1
O
U
/g
)
)
)
/g
/g
ro
)
nt
/g
U
U
U
co l
Enzyme Pretreatment: OSB Results 80
75
70
65
% 60
55
50
45
40
% TS % WA
D
F
F
D pr
et
et
pr r. E
zy
D F( co n tr o
m nz e 1 y m .. . e 1. ..
En
r. E
r.
et
et
pr
pr
M
nz r. . II E n (5 zy . m .. e II . .. P PB B( co p nt P B re t r ro . l* En pr ) et z r. I( En 0 z y . 1m PB I (0 l/ g .5 ) pr m e PB tr . l/g ) E pr nz et r. E n II (5 zI U / I( 50 g) U .. .
M
M
F
F
D
D l* )
% C hang e
M
M
Enzyme Pretreatment: Results 13 0 .0
12 0 .0 T S(%)
W A ( %)
110 .0
10 0 .0
9 0 .0
8 0 .0
70 .0
6 0 .0
50 .0
T S( %)
Nano Clay Studies
What is Nano??? What is Nano??? What is Nano??? What is Nano??? What is Nano?? What is Nano???
Nanotechnologies are characterized by structural elements in the nanometer range 1 m = 1000 mm = 1, 000, 000 µm = 1, 000, 000, 000 nm Sweet Spot Quantum Properties For Nano Technology
Newtonian Properties
Microchip 10 mm
Fiber
Hair
1 – 7 mm 50 µm
Cells 10 µm
Pentium III Chip 180 nm
DNA 2 nm
Atom 0.1 0.4 nm
Nano-Patenting Trends Patents containing nano 900
• Nano-patents in the exponential phase moving into application development and the second wave of patenting
800 700 600 Patents
500 400
• Commercialization potential is broad – multi facilitated field
Published • Patents may be only barrier Applic.
300
of entrance
200 100 0 1998
1999
2000
2001
2002
The Business Review – 2003 “Small is big and it's getting bigger”
Nano Clays for Barriers/Coatings • Pioneering work on nanoclay systems at Toyota's Research Center in Japan showed that a hybrid nylon nanocomposite has a HDT as high as 164°C that is 100°C higher than that of pure nylon 6. •Impact of differing alkylammonium nanoclays as fillers/coatings • Barrier • Printability
Polymer-Nanoclay Composites The thickness of nanoclay in the composite is about 1nm. Barrier coating for food containers and paper packages • Water and vapor resistance • Fatty and oil resistance • Paper-board strength
3.0
0.4
2.0 0.3 1.5 0.2 1.0 0.1
0.5 0.0
0.0 0
1
2
3
4
5
2
2.5
COBB Test (g/100 in. 2 h per unit loading)
0.5
2
2
WVTR x 10 (g/100 in 24 h per unit loading)
Polymer-Nanoclay Composites Paper Application
Nanoclay Content (wt %)
Relationship between barrier properties (WVTR and COBB) of waxed liner paper and nanoclay content. Wax used: Paraffin wax.
• 3% nanoclay in wax can increase water-barrier by 50%, and gas barrier by 100%, target for wax-coated paper container
Nano Clays and Effect on UF and PF Gel Times Employing 10% Charge of Filler Gel Time Experiment ASTM: D 3056-00 100.0oC • Insert sample into sample vial • Rapidly add catalyst • Begin stirring • Allow test specimen in bath till stirring stops
Experiment Control (no clay) Nanoclay NC-1 Nanoclay NC-2 Nanoclay NC-3 Nanoclay NC-4 Nanoclay NC-5 Nanoclay NC-6 Natural montmorillonite C-7
Gel Time UF PF 27.1 9.9 > 30 9.7 > 30 9.8 > 30 9.6 > 30 9.8 > 30 9.9 2.3 9.4 > 30 8.7
Nano Clays and Effect on UF Gel Times Employing Varying Charge of Filler Gel Time Experiment ASTM: D 3056-00 100.0oC • Insert sample into sample vial • Rapidly add catalyst • Begin stirring • Allow test specimen in bath till stirring stops
Experiment Control (no clay) Charge Nanoclay NC-6 2% 5% 10% 20%
UF Gel Time 27.1 4.8 3.1 2.3 1.6
Nano Clays and Effect on UF:Particle Board
• Wood furnish was blended with 1% of paraffin wax, hand felted into a form box • Mat consolidation and curing were accomplished using a laboratory hydraulic press 121o C • After hot-pressing boards were allowed to cool at room temperature, conditioned for 1 week • Thickness swelling and water adsorption were measured according to ASTM D1037
Nano Clays and Effect on UF:Particle Board 35
34
33
% Thickness Swelling
32
31
30
29
28
27
26
25 PB (Control)
PB + 5% Regular Clay
PB + 5% Nanoclay-101
PB + 5% Nanoclay-936
• Wood furnish was blended with 1% of paraffin wax, hand felted into a form box • Mat consolidation and curing were accomplished using a laboratory hydraulic press 121o C • After hot-pressing boards were allowed to cool at room temperature, conditioned for 1 week • Thickness swelling and water adsorption were measured according to ASTM D1037
Nano Clays and Effect on UF:Particle Board 56
55
54
% Water Absorption
53
52
51
50
49
48
47
46 PF 300F-Control
PF 250F-Control
PB 5% Clay 300F
NC
PB 5% Clay 250F
NC
• Wood furnish was blended with 1% of paraffin wax, hand felted into a form box • Mat consolidation and curing were accomplished using a laboratory hydraulic press 121o C • After hot-pressing boards were allowed to cool at room temperature, conditioned for 1 week • Thickness swelling and water adsorption were measured according to ASTM D1037
Nano Clays and Effect on UF:Particle Board 50
45
40
% Thickness Swelling
35
30
25
20
15
10
5
0 PF 300F-Control
PF 250F-Control
PB 5% Clay 300F
PB 5% Clay 250F
NC
NC
• Wood furnish was blended with 1% of paraffin wax, hand felted into a form box • Mat consolidation and curing were accomplished using a laboratory hydraulic press •After hot-pressing boards were allowed to cool at room temperature, conditioned for 1 week • Thickness swelling and water adsorption were measured according to ASTM D1037
PB – Additive: Thickness Swelling
Particle board - 2 Hour Thickness Swelling PB: Control
24
PB: 5% NC % Thickness Swelling
23
PB: 5% Zeolite PB: 5% CS
22 21 20 19 18
Lower Better!
17 16 200
250 Curing Temperature/F
Values for 2/24 h for water absorption and thickness swelling acquired
300
PB – Additive: Water Swelling
95
Particle board - 24 Hour Water Absorption
% Wtaer Absorption
90 85
PB: Control PB: 5% NC
80
PB: 5% Zeolite PB: 5% CS
75 70 65 60 200
250 Curing Temperature/F
300
OSB – Additive: Thickness Swelling
50
OSB - 2 Hour Thickness Swelling
% Thickness Swelling
45
OSB: Control OSB: 5% NC OSB: 5% Zeolite
40
OSB: 5% CS 35
30
25 200
250 Curing Temperature
375
OSB – Additive: Water Absorption
95
OSB - 24 Hour Water 90 OSB: Control
% Water Absorption
85
OSB: 5% NC 80
OSB: 5% Zeolite OSB: 5% CS
75 70 65 60 55 200
250 Curing Temperature/F
375
MDF – Additive: Thickness Swelling
10
FB - 2 Hour Thickness Swelling
9
% Thickness Swelling
8 7
FB: Control FB: 5% NC FB: 5% Zeolite
6
FB: 5% CS
5 4 3 2 1 0 200
250 Curing Temperature/F
375
MDF – Additive: Water Absorption
FB - 24 Hour Water Absorption 24
% Water Absorption
22 20
FB: Control FB: 5% NC
18
FB: 5% Zeolite FB: 5% CS
16 14 12 10 200
250 Curing Temperature/F
375
Additive Mixtures: OSB
5% Corn starch 90 80
2.5% Nano clay + 2.5% Cationic starch 2.5% Nano clay + 2.5% Zeolite
70
2.5% Zeolite + 2.5% Cationic starch % TS or WA
60 50 40 30 20 10 0 2hr
24hr Thickness sw elling(%)
2hr
24hr Water adsorption(%)
Additive Mixtures: MDF
5% Corn starch 40
2.5% Nano clay+ 2.5% Cationic starch 2.5% Nano clay + 2.5% Zeolite 35
2.5% Zeolite + 2.5% Cationic starch 30
% TS % WS
25
20
15
10
5
0 Thickness sw elling(%)
2h
Water adsorption(%)
24 h
2h
24 h
Additive Mixtures: PB
120
5% Corn starch 100
2.5% Nano clay + 2.5% Cationic starch 2.5% Nano clay + 2.5% Zeolite 2.5% Zeolite + 2.5% Cationic starch
% TS WS
80
60
40
20
0 2hr
24hr Thickness sw elling(%)
2hr
24hr Water adsorption(%)
OSB – Additive: IB Effect 80.0
OSB OSB 5% NC
70.0
OSB 5% CS OSB 5% Zeolite
IB/psi
60.0
50.0
40.0
30.0
20.0 T:200
T:250 Curing Temperature/F
T:350
MDF – Additive: IB Effect
75.0 70.0
FB FB 5% NC
65.0
IB/PSI
60.0
FB 5% CS FB 5% Zeolite
55.0 50.0 45.0 40.0 35.0 30.0 T:200
T:250 Curing Temperature/F
T:300
Key IB Effect Internal Bond Strength (kPa) Properties of Particle Board PB5%Nanoclay
PB-5% Zeolite
PB-5% Cationic Starch
200
38%
42%
44%
250
31%
--
28%
300
9%
7%
12%
Press Temp/oF
Conclusions • First demonstration that nanoclays can enhance UF gelling times and water stability properties of UF particle board • Provides benefits not available with routine clays • Mechanism and full benefits demonstrated for – – – –
Curing Energy Strength Properties Moisture stability Reduced charge
• Dependence on nanoclay structure unknown
Projected Benefits • New catalysts technologies developed for resin curing reduce energy curing costs by >15% • Detrimental effects of extractives on physical properties is significantly reduced • Reduced Emissions • Enhanced UF and PF resin chemistry is developed providing manufacturers improved product performance
IPST Member Companies U.S. Department of Energy
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