BINDING WOOD. Binders and Wood Based Panels
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1 BINDING WOOD Binders and Wood Based Panels
2 Structure of the presentation 1. Introduction 2. Binders Amino (UF, UmF, MUF) Phenol (PF) Isocyanates: pmdi / emdi 3. Wood based panels Plywood Particleboard OSB MDF LPL / HPL 4. Case Study
3 Introduction (1/2) 1) Wood (Lignin, Cellulose, Hemi-cellulose) Trunks / logs Green Chips Sawdust / sander dust / plywood trim Various forms of recycling (furniture, pallets etc.) 2) Wood preparation: Veneers (Plywood, PW) Strands (Oriented strand boards, OSB) Chips (Particleboard, PB) Fiber (Fiberboards, MDF, HDF...) 3) Resination 4) Hot pressing 5) Quality Control (QC)
4 Introduction (2/2) Log yard Saw dust Fiber Green chips Veneer Pallets Strands Chips
5 Amino Binders (1/2) Aqueous solutions produced from: Formaldehyde Urea and or Melamine Methylolation stage: -NH2 + HCHO -NH CH2 OH Condensation stage: H + i) -NH CH2 OH + HO CH2 NH- -NH CH2 - O - CH2 NH- (ether bridge) ii) H -NH CH2 OH + H2N -NH- CH2 - HN (methylene bridge)
6 Formaldehyde 1 + ( ) + 1 = 30 is a colorless gas with a characteristic pungent odor. is a naturally occurring substance in the environment. Natural processes in the upper atmosphere may contribute up to 90 percent of the total formaldehyde in the environment, other sources being forest fires, automobile exhaust, and tobacco smoke. is an important precursor to many other chemical compounds, especially for polymers. is easily soluble in water. Commercial solutions of formaldehyde in water, commonly called formalin. Has a Molecular Weight of 30.
7 Urea ( ) = 60 Is a colourless and odorless solid Is widely used in fertilizers as a convenient source of nitrogen (90% of world production) Is highly soluble in water and practically non-toxic Has a Molecular Weight of 60. It can react with formaldehyde on the hydrogen sides (theoretically 4)
8 Melamine 1 x x x 3 = 126 Is a white odorless solid, most commonly in thin powder form to produce melamine, most industrial manufacturers use urea Is practically insoluble in water Has a Molecular Weight of 126 It can react with formaldehyde on the hydrogen sides (theoretically 6, 50% more that Urea)
9 Molar Ratio One important parameter of resin is the Molar Ratio It is an indication of the number the molecules of Formaldehyde exist in the resin with respect to Urea (and/or Melamine) molecules To calculate the Molar Ratio of a UF resin, one must divide the weight of pure Formaldehyde with the Molecular Weight (30) and the weight of pure Urea with the Molecular Weight (60) and take the ratio of those two UF Molar Ratio = = 2 x F When Melamine exists in the resin system, by convention, the Molar Ratio calculation takes into account that there are 50% more reaction sides in Melamine F 30 U 60 UMF Molar Ratio = = U 60 F M 126 U 14 x F 7 x U + 5 x M
10 Making a Resin starts before the reactor Formaldehyde Gas Goes Up the Absorber Urea (in the form of water solution) is feed from the top of the Tower Having the correct ph, some Formaldehyde will react with the Urea Q: What is the Molar Ratio of the above mixture?
11 Starting a batch UFC is pumped in the reactor Then, it is diluted with water Having the correct ph, more Urea is added Q: What is the Molar Ratio now?
12 Taking it to polymerisation temperature Heat is supplied to the mixture and the temperature rises The molecules start reacting with each other Reaction has to be completed (waiting time)
13 The polymerisation stage (1) Upon acidification, the monomers will start to react with each other Chains are formed which react with other chains to form long & complex chemical molecules
14 The polymerisation stage (2) The longer the molecules, the higher the friction between them The higher the friction, the more viscous the mixture becomes The more viscous the mixture, the longer a constant volume will take to go through a hole
15 Finishing Off By changing the ph, the favorable environment for reaction is discontinued It is true that not all of the formaldehyde has participated on the polymerisation It is left out intentionally, to make more monomers (again) These monomers, will be used as quick links for the long chains
16 The melamine effect As already said above, melamine has 6 reactive sides vs. 4 of urea It is true that melamine is highly hydrophobic (water- repellant) Those two abilities make melamine a good partner for better resins as: 1. They increase the density of the polymers (Higher cross-linking) 2. They protect the polymer from water deterioration (hydrolysis)
17 Setting the Resin The polymerisation is favoured by low ph and high temperatures In the press, the temperature is high enough but the ph is on the alkali side One could add acid in the resin to lower the ph, but that will set the resin on the spot. Ammonium-based compounds-hardeners are used (e.g. Ammonium Chloride, Ammonium Sulfate, etc). These are the salt of the corresponding acid with ammonia. When mixed with the resin, the ammonia reacts slowly-enough with the free formaldehyde, liberating the necessary acid. The amount of hardener has to be carefully selected to avoid resin setting prior to the press ( precuring )
18 Resination Resin Hardener Wood Glue Mix Glue Wood System To Press
19 In the press Mat is entered in the press and Pressure is applied Press-plates are hot, so water from the top and bottom of the mat, is turned into steam Steam is flowing from the surfaces to the core where he can leave the mat Steam heats up the path is following, providing heat for the resin to set
20 Amino Binders (2/2) A 3D cross-linked structure is formed! Condensation reaction is acid catalyzed. Advantages Disadvantages Low cost High Reactivity Acceptable panel properties With melamine (expensive additive) specialty panels can be produced like low formaldehyde emissions, moisture resistant. Formaldehyde release from set polymer Carbon footprint Without Melamine poor moisture resistance Need of catalyst, low pot life Applications Interior grade PW, PB, MDF, OSB (face), HPL, LPL 1) Melamine increases cross linking density due to three non linear amino groups 2) Due to the quasi aromatic ring it resists hydrolysis better than UF link.
21 Phenol binders (PF, 1/2) Aqueous solutions produced from: - + OH - CH 2 OH A 3D cross-linked structure is formed!
22 Phenol binders (PF, 2/2) Advantages Relatively Low cost Can be used without hardener i.e. long pot life Low formaldehyde emissions Good panel properties, withstanding boil tests Disadvantages Carbon footprint Low reactivity Toxic, corrosive RM (Phenol) Color Applications Exterior grade PW, OSB (face), HPL + many other non WBP
23 Isocyanates (pmdi, emdi, 1/2) Polymerized or emulsified Methylene diphenyl diisocyanate, Not miscible with water, produced from: Formaldehyde, Aniline and Phosgene A 3D cross-linked structure is formed!
24 Isocyanates (pmdi, emdi, 2/2) Advantages Low addition rates Low formaldehyde emissions High reactivity Compatibility with Amino and phenolic binders Good panel properties, withstanding boil tests Disadvantages High cost Carbon footprint Handling Health and safety Adheres to press platens Applications OSB (core & face less frequently), Special grades PB, MDF
25 Binders Summary Three main categories: 1. Amino 2. Phenolic 3. Isocyanates All have advantages / disadvantages and are selected for suitable applications Very competitive market Cost is an important factor that can change the preferred binder All come from fossil fuels A 3D cross-linked structure is formed!
26 PLUS BINDER!!!!!!!!! WOOD BASED PANELS Melamine faced PB OSB Produced from strands MDF Produced from chips Plywood Produced from fiber Produced from veneers
27 Plywood (1/4) Process flow: 1. Cutting steamed logs into veneers 2. Selecting and drying veneers 3. Gluing veneers and forming piles 4. Cold pressing (pre-press) 5. Hot Pressing and stacking 6. Quality control
28 Plywood (2/4) Produced ONLY from logs that are cut into veneers (expensive) Once the veneer is prepared and DRYED the binder is applied In the lab it is done by a spatula or a small roller Industrially by: 1. Roller 2. Curtain 3. Foam 4. Spray
29 Plywood (3/4) Cold (Amb. Temp, 10min various sp. pressures) and Hot pressing (130 o C, 1min/mm, various sp. pressures)
30 Plywood (4/4) Plywood QC: Test 1: 24h immersion in 20 o C water Test 2: 6h boiling 18hdrying 6h boiling Test 3: 72h boiling Evaluation: Shear Strength in (N/mm 2 ) and % Wood failure
31 Particleboard (1/5) Process flow: 1. Wood preparation into chips Debarking, chipping, removing metal, flaking, drying, sieving 2. Preparing glue mix Resin, Water, Hardener 3. Adding wax 4. Blending with resin 5. Forming a mat face and core layers 6. Pre-pressing 7. Hot pressing 8. Cooling star 9. Stacking 10. Sanding 11. Quality control
32 Particleboard (2/5) Produced from every possible wood furnish, cheap solution Knife ring flaker Glue kitchen Forming Station Blender
33 Particleboard (3/5) Infeed Fastest production of all WBP, 3-6s/mm!!!!! Temperature up to 245 o C Press infeed Continuous press Mat is compressed and heated Heat is transferred by steam and convection Vapor escapes Binder sets (chemical formation of a 3D cross-linked structure) Board is released when it can hold itself together Cooling Star
34 Particleboard (4/5) Quality control: Internal bond Modulus of rapture / elasticity Thickness Swell Formaldehyde release Screw pull Face pull Boil test Cyclic test Measured in: N/mm 2 / PSI N/mm 2 / PSI % ppm N/mm 2 / PSI N/mm 2 / PSI N/mm 2 / PSI N/mm 2 / PSI
35 Particleboard (5/5) Internal bond Face Pull Modulus of rapture Formaldehyde Release Thickness Swelling
36 OSB (1/3) Process flow: 1. Wood preparation into chips Debarking, chipping, removing metal, flaking, drying, 2. Preparing glue mix Resin, Water, Hardener 3. Adding wax 4. Blending with resin 5. Forming a mat face and core layers 6. Pre-pressing 7. Hot pressing 8. Cooling star 9. Stacking 10. Sanding 11. Quality control
37 OSB (2/3) Not all wood sources can be utilized, pressing factor above 10s/mm, cannot be laminated!!! OSB Blender OSB Forming OSB mat OSB mat into press
38 OSB (3/3) Quality control: Internal bond Modulus of rapture / elasticity Thickness Swell Formaldehyde release Screw pull Face pull Boil test Cyclic test Measured in: N/mm 2 / PSI N/mm 2 / PSI % ppm N/mm 2 / PSI N/mm 2 / PSI N/mm 2 / PSI N/mm 2 / PSI
39 MDF (1/5) Process flow: 1. Wood preparation into fiber Debarking, chipping, removing metal, pre-steeming, digesting, refining 2. Preparing glue mix Resin, Water, Hardener 3. Adding wax 4. Blending with resin 5. DRYING!!! 6. Forming a mat 1-layer most of times, 3-layer in some cases 7. Pre-pressing 8. Hot pressing 9. Cooling star 10. Stacking 11. Sanding 12. Quality control
40 MDF (2/5) refining Open refiner Open refiner Refiner plate
41 MDF (3/5) Produced from every possible wood furnish, cheap solution BUT wood refining is expensive, can be molded for doors and deep routed. Blow - Line
42 MDF (4/5) mat & pressing Pressing time, relatively slow: 6 20s/mm Press temperature up to 245 o C MDF press MDF mat
43 MDF (5/5) Quality control: Internal bond Modulus of rapture / elasticity Thickness Swell Formaldehyde release Screw pull Face pull Boil test Cyclic test Measured in: N/mm 2 / PSI N/mm 2 / PSI % ppm N/mm 2 / PSI N/mm 2 / PSI N/mm 2 / PSI N/mm 2 / PSI
44 LPL / HPL (1/6) Paper Type Decor Unicolor Dark Unicolor Overlay (α-cellulose) Kraft Resin UF and MF UF and MF MF MF PF or MF
45 LPL / HPL (2/6) 1. Glue mixes are prepared: Resin UF, MF, PF, water, hardener, wetting release agent and other additives (TiO 2, Al 2 O 3.) 1. Paper is impregnated in the bath, then dried in the oven to reach about 10 12% volatiles 2. Then it is coated with another glue mix and dried again to 6% volatiles 3. Finally it is cooled and cut to size and stack packed or rolled
46 LPL / HPL (3/6) Hand Impregnation bath Paper impregnation line, up to 100m/s
47 LPL / HPL (4/6) LPL The impregnated paper is thermally fused on to the substrate (PB or MDF) Conditions: Time = 14 40s Temp. = o C Sp. Pressure = 25 40kg/cm 2 ( PSI) HPL Depending on final thickness kraft papers and stacked below a melamine décor paper and the whole sandwich is hot pressed. Then the HPL is cold set glued to the substrate Conditions: Time = minutes per mm Temp. = o C Sp. Pressure = kg/cm 2 ( PSI)
48 LPL / HPL (5/6) Short cycle laminating press Continuous HPL and CL Press
49 LPL (6/6) Quality control: 1. Abrasion 2. Burn test 3. Scratch resistance 4. Resistance to staining Even floorings can be produced if corundum is added in the overlay!
50 In all WBP production: 1. Wood is prepared 2. Binder is applied 3. Hot pressing follows Key elements of hot pressing: 1. Moisture balance 2. Wood is compressed 3. Binder is set Boards must: 1. Show resistance to deformation, rupture 2. Resist humidity to some extent in most cases 3. Comply with regulations regarding release of formaldehyde
51 Case Study (1/6) Νέα και σύγχρονη μονάδα παραγωγής ινοσανίδας (MDF-HDF) στην κεντρική Ευρώπη ζήτησε την τεχνική βοήθεια της CHIMAR λόγω υψηλών ποσοστών μέσης κατανάλωσης ρητίνης κατά την παραγωγή, ακόμα και του πλέον συνήθους προϊόντος.
52 Case Study (2/6) Η αυτοψία έδειξε ότι ο ξηραντήρας είχε σχεδιαστεί με μικρότερο μήκος για εξοικονόμηση κόστους αγοράς και εγκατάστασης. Ως αποτέλεσμα, η θερμοκρασία λειτουργίας του ξηραντήρα έπρεπε να είναι ~12 C υψηλότερη από την ενδεδειγμένη (85 αντί 73 C), ώστε στον ίδιο χρόνο παραμονής της ρητινωμένης ίνας να επιτυγχάνεται η ίδια τιμή υγρασίας εξόδου της ίνας.
53 Case Study (3/6) Καθώς η ρητίνη εκτίθεται σε αυτές τις θερμοκρασίες, ένα σημαντικό ποσοστό της «έπηζε» (πολυμερίζεται πρόωρα) πριν από το στάδιο της θερμής συμπίεσης με αποτέλεσμα να είναι αδρανές στην πρέσα. Για να αντισταθμιστεί το ποσοστό αδρανούς ρητίνης, ήταν επιτακτικό να δοσολογείται μεγαλύτερη ποσότητα ρητίνης αυξάνοντας έτσι το κόστος της τελικής σανίδας. Η χρήση όξινης ξυλείας (Radiata Pine) επιδείνωνε το πρόβλημα αυτό.
54 Case Study (4/6) Μέρος της λύσης αποτέλεσε η προσθήκη χημικής ένωσης στη ρητίνη, η οποία ένωση καθυστερεί την ολοκλήρωση του πολυμερισμού και εξουδετερώνει μέρος των οξέων του ξύλου. Αυτή η ενέργεια όμως από μόνη της θα είχε ως αποτέλεσμα την μείωση της παραγωγικότητας λόγω υστέρησης στην πρέσα.
55 Case Study (5/6) Έτσι, προστέθηκε μια άλλη μία χημική ένωση, η οποία απελευθερώνει οξύ σε θερμοκρασίες λίγο μεγαλύτερες των 90 C.
56 Case Study (6/6) Αποτέλεσμα: Οι ιδιότητες του τελικού προϊόντος παρέμειναν στα προδιαγεγραμμένα επίπεδα. Η παραγωγικότητα παρέμεινε στους στόχους. Η κατανάλωση της ρητίνης περιορίστηκε κατά 32%. Η τιμή της ρητίνης αυξήθηκε κατά 8%.
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