GB2191207A - A substitute for amino and phenolic resins - Google Patents

A substitute for amino and phenolic resins Download PDF

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Publication number
GB2191207A
GB2191207A GB08710016A GB8710016A GB2191207A GB 2191207 A GB2191207 A GB 2191207A GB 08710016 A GB08710016 A GB 08710016A GB 8710016 A GB8710016 A GB 8710016A GB 2191207 A GB2191207 A GB 2191207A
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United Kingdom
Prior art keywords
substitute
formaldehyde
urea
water
sample
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GB08710016A
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GB2191207B (en
GB8710016D0 (en
Inventor
Efthalia Vergopoulo Markessini
Andrew C Markessini
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Enigma NV
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Enigma NV
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Priority claimed from GB868613791A external-priority patent/GB8613791D0/en
Application filed by Enigma NV filed Critical Enigma NV
Priority to NZ22043787A priority Critical patent/NZ220437A/en
Priority to AT8787600007T priority patent/ATE104687T1/en
Priority to EP19870600007 priority patent/EP0252867B1/en
Priority to ES87600007T priority patent/ES2052597T3/en
Priority to DE3789635T priority patent/DE3789635T2/en
Priority to NO872323A priority patent/NO169295C/en
Priority to DK283787A priority patent/DK283787A/en
Publication of GB8710016D0 publication Critical patent/GB8710016D0/en
Priority to FI872516A priority patent/FI88725C/en
Priority to MYPI87000763A priority patent/MY101499A/en
Priority to SU4202785 priority patent/RU2055856C1/en
Priority to JP62141297A priority patent/JPS63258945A/en
Priority to US07/058,905 priority patent/US4886854A/en
Priority to PL1987266096A priority patent/PL157068B1/en
Priority to HU872585A priority patent/HU207108B/en
Priority to CA 538971 priority patent/CA1290085C/en
Priority to KR1019870005710A priority patent/KR960002528B1/en
Priority to MX006797A priority patent/MX168753B/en
Priority to BG080034A priority patent/BG46750A3/en
Priority to BR8702894A priority patent/BR8702894A/en
Publication of GB2191207A publication Critical patent/GB2191207A/en
Publication of GB2191207B publication Critical patent/GB2191207B/en
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G14/00Condensation polymers of aldehydes or ketones with two or more other monomers covered by at least two of the groups C08G8/00 - C08G12/00
    • C08G14/02Condensation polymers of aldehydes or ketones with two or more other monomers covered by at least two of the groups C08G8/00 - C08G12/00 of aldehydes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G12/00Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen
    • C08G12/02Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L97/00Compositions of lignin-containing materials
    • C08L97/005Lignin

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Dry Formation Of Fiberboard And The Like (AREA)

Abstract

A substitute for amino and phenolic resins is used in the polycondensation of such resins based on formaldehyde for bonding water penetrable cellulosic particles. The substitute comprises an aqueous solution of a) either at least one aldehyde together with at least one amide and/or together with at least one phenol, or a non-resinous condensation product of formaldehyde and urea, and b) a sugar or a sugar derivative or their by-products or a starch or its degradation products or a mixture thereof, and/or c) a raw and/or treated lignosulfonate. This substitute also reduces the free formaldehyde of the resulting board without impairing the other properties thereof.

Description

SPECIFICATION Substitute for amino and phenolic resins The present invention relates to a substitute for amino and phenolic resins in the polycondensation of such resins based on formaldehyde for bonding water penetrable cellulosic particles thus allowing lower amounts of resin solids to be used while at the same time reducing the free formaldehyde of the resulting board without imparting any loss in bonding strength, without requiring any extra steps in the production, without changing the curing rate of the production, without causing any problem to the boilers when burning particleboard sander dust or edges from cutting saws and without reducing the tack properties of the resin mixture.
The said substitute is comprised mainly of a solution of: a) either an aldehyde together with an amide or together with a phenol, or a non-resinous condensation product of formaldehyde and urea, and b) a sugar or a sugar derivative or their by-products or a starch or a mixture thereof, and/or c) a raw and/or treated lignosulfonate or similar products.
The aldehyde is preferably formaldehyde, for example in the form of paraformaldehyde, or acetaldehyde. The amide is preferably mainly urea or thiourea or their homologues or melamine, benzoguanamine or dicyandiamide or their homologues. The phenol is preferably phenol itself or resorcinol.
Among the sugars, sugar derivatives, their by-products and mixtures thereof, molasses, dextrose, glucose, fructose or sucrose or mixtures thereof such as corn syrup are most preferred.
Among the starches, wheat starch, modified starches, dextrin and the like are interesting.
Examples of raw lignosulfonates are black liquor and similar products, and examples of treated lignosulfonates are sodium, calcium and ammonium lignosulfonate.
The substitute of the invention preferably contains 40 to 50% by weight of water.
The weight of a) to b) and/or c) is preferably 0.1 to 50.0:1, most preferably 1.0 to 15.0:1.
The combination of a) with b) and/or c) presents a synergistic behaviour. If the single components are added alone to the resin they do not give good boards, but if they are added in combination, they exhibit an improvement in the board properties obtained. The substitute according to the present invention (calculated as 100% solids) may substitute as much as 30% of the resin solids used. Said substitute is not added in quantities equal to the quantities substituted. It is added in quantities from 50 to 90% of the amount of resin substituted (calculations referred to by weight and referring to all products as 100% solids).
The substrate according to the present invention may therefore, because of its synergistic behaviour, substitute the resin in quantities from 110% up to 200% of its own weight. When added to lower amounts e.g. up to 15% there is a considerable increase in the properties of the end product. When added to higher levels, i.e. up to 30%, no difference is imparted to the properties of the end product but the free formaldehyde is considerably reduced and the amount of resin saved is considerably increased.
Bonding is effected by curing the resin mixture at elevated tempertures and pressures according to the methods well known in the art. The substitute may be used in all types of products where amino and phenolic resins are used for bonding lignocellulosic products, whether these are wood particles for particleboard production using a flat press, or a calender or wood veneers such as in plywood production.
It is very interesting to note that the product has also good tack. This property otherwise called "green strength" is desired in some types of particleboard plants, specially the plants with multi opening press and in plywood factories, specially those having a pre-press.
The quality of boards produced was controlled weekly for a period of six months and no reduction in the properties was observed. This proves that no polymer degradation occurs and that the ageing properties of the boards are comparable to the ones normally produced.
The substitute of the invention can be prepared by plain mixing of the components. In order to obtain an acceptable shelf-life of the substitute, a base is preferably added to adjust the pH to a value in the range of 6 to 14.
Substitutes so far known in the art to substitute resin have not succeeded in substituting such high levels of resin by using lower amounts of the substitute and reducing simultaneously the free formaldehyde of the boards, without imparting any loss in bonding strength, without requiring any extra steps in the production, without charging the curing rate of the production, without causing any problems to the boilers when burning particleboard sander dust or edges from cutting saws and without reducing the tack of the resin mixture.
In particular, the known substituents are lignosulfonates, sodium chloride or mixtures of formaldehyde with urea and sodium chloride. It is well known that lignosulfonates may not be used for quantities higher than 10%; otherwise, board properties will be reduced.
It is also known that the addition of halide salt alone succeeds in substituting part of the resin with the following limitations: -High substitutions, higher than 6 to 8%, may not be obtained, otherwise the board properties will deteriorate.
-Substitution is obtained in ratios 1:1, while in the case of the substitute according to the present invention it is 1.1 to 2.0:1.
-When particleboard sander dust or edges from cutting saws are burnt in boiliers, the latter are plugged within a few hours.
tack is reduced when sodium chloride is added to the resin mixtures.
When mixtures of sodium chloride with urea and formaldehyde are used the following shortcomings are present: -The presence of salt in the mixture causes severe problems in the boilers when sander dust or cutting saw edges of boards are burnt. That is caused because the presence of salt reduces the melting point of the mixture and as a result a molten mass deposits in the boiler forming a glass like deposit which adheres on the boiler thus plugging it.
The other shortcoming of this product is the fact that tack is severely reduced, thus making it difficult to use in the plywood industry where there is a pre-press and in particleboard plants where a multi opening press is present requiring green strength of the mat.
The product according to the present invention overcomes all of the above shortcomings.
The substitute according to the present invention provides yet another advantage. Apart from substituting up to 30% of the resin by adding only 50 to 90% of the resin solids substituted, and reducing the free formaldehyde of boards, it reduces also the free formaldehyde in the production hall where workers are exposed to formaldehyde fumes.
The following Examples illustrate the invention and are not intended as limitations.
Example 1 Three samples were prepared according to the following formulations: Sample No. 1 2 3 parts by weight Formaldehyde 100% 185 - 133 Urea 100% 370 - 226 Molasses 100% - 555 156 Water 445 445 445 1000 1000 1000 The above mentioned samples were prepared by plain mixing at room temperature until the solids were completely dissolved. The pH of the final products was adjusted to 7.5 to 8.0.
Glue formulations were then prepared as follows: Glue formulation No. 0 1 2 3 parts by weight Urea formaldehyde resin (65% solids) 108.9 81.7 81.7 81.7 Water 13.8 13.8 13.8 13.8 Sample 1 - 27.2 - Sample 2 - - 27.2 Sample 3 - - - 27.2 Ammonium chloride (20%) 7.1 7.1 7.1 7.1 No. 0: Glue formulation is the blank and does not include any of the above mentioned samples.
No. 1: Glue formulation includes sample 1, whereby only formaldehyde and urea are included.
No. 2: Glue formulation includes sample 2 whereby only molasses are included.
No. 3: Glue formulation includes sample 3 whereby all three ingredients are added, namely, formaldehyde, urea and molasses. Sample 3 represents the product according to the present invention.
These glue formulations were used separately to spray a constant quantity of dried wood chips.
The sprayed wood chips were then formed into a mat having a normal thickness of 16mm.
These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 200"C Press time 9sec/mm Pressure 33kp/cm2 Boards were then tested and the results are reported in the following table.
Glue formulation No. 0 1 2 3 Density (kg/m3) 582 591 583 582 Thickness (mm) 15.4 15.2 15.5 15.4 Internal bond (kg/cm2) 7.1 6.5 5.0 7.2 2 hrs thickness swelling (%) 11.1 11.3 17.5 12.1 24 hrs thickness swelling (%) 20.3 22.5 30.3 22.3 Free formaldehyde (mg/100g dry board) 24.1 18.3 21.8 18.7 Moisture content (%) 5.5 5.0 5.4 5.0 It can be noticed from the above mentioned table that while all three samples reduce the free formaldehyde of boards, only sample 3 including the components according to the present invention gives boards equivalent to the blank, without deterioration of the board properties.
Example 2 This example proves the synergistic behaviour existing between formaldehyde, urea and lignosulfonates.
For this purpose the following samples were prepared: Sample No. 1 2 3 parts by weight Formaldehyde (100%) 185 - 133 Urea (100%) 370 - 266 Calcium iignosulfonate (100%) - 555 156 Water 445 445 445 1000 1000 1000 The above mentioned samples were prepared by plain mixing at room temperature until the solids were completely dissolved. The pH of the final products was adjusted to 7.5 to 8.0.
Glue formulations were then prepared as follows: Glue formulation No. 0 1 2 3 parts by weight Urea formaldehyde resin (65% solids) 108.9 81.7 81.7 81.7 Water 13.8 13.8 13.8 13.8 Sample 1 - 27.2 - Sample 2 - - 27.2 Sample 3 - - - 27.2 Ammonium chloride (20%) 7.1 7.1 7.1 7.1 These formulations were used separately to spray a constant quantity of dried wood chips.
The sprayed wood chips where then formed into a mat having a nominal thickness of 16mm.
These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 2000C Press time 9sec/mm Pressure 33kp/cm2 Boards were then tested and the results are reported in the following table: Glue formulation No. 0 1 2 3 Density (kg/m3) 580 591 590 584 Thickness (mm) 15.5 15.2 15.0 15.1 Internal bond (kg/cm2) 7.0 6.3 5.4 6.9 2 hrs thickness swelling (%) 11.2 11.3 17.8 11.8 24 hrs thickness swelling (%) 20.6 22.5 29.5 23.8 Free formaldehyde (mg/100g dry board) 23.9 19.8 18.5 17.8 Moisture content (%) 5.8 5.0 4.5 4.8 It will be noticed from the above mentioned figures that boards produced with plane lignosulfonates, sample 2, have the worst results. Boards obtained with all three components according to out present invention, sample 3, have the best results.Actually boards of sample 3 are equivalent to the blank, 0, which is the resin mixture without any substitute, while giving at the same time a reduction in the free formaldehyde of the boards.
Example 3 In this example two samples are illustrated whereby the ratio of formaldehyde to urea is different from the one used in the previous examples. Also the weight ratio between components a) and b) is different from the one of examples 1 and 2.
The following samples were prepared: Sample No. 1 2 parts by weight Formaldehyde (100%) 133 133 Urea (100%) 177 177 Molasses (100%) 156 Dextrin glue (100%) 30 Calcium lignosulfonate (100%) - 186 Water 504 504 1000 1000 The above mentioned samples were prepared by plain mixing at room temperature until the solids were completely dissolved. The pH of the final products was adjusted to 7.5 to 8.0.
Glue formations were then prepared as follows: Glue formulation No. 0 1 2 parts by weight Urea formaldehyde resin (65% solids) 108.9 87.1 87.1 Water 13.8 13.8 13.8 Sample 1 - 21.8 Sample 2 - - 21.8 Ammonium chloride (20%) 7.1 7.1 7.1 These glue formations were used separately to spray a constant quantity of dried wood chips.
The sprayed wood chips were then formed into a mat having a nominal thickness of 16mm.
These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 220"C Press time 9sec/mm Pressure 33 kp/cm2 Boards were then tested and the results are reported in the following table: Glue formulation No. 0 1 2 Density (kg/m3) 573 595 587 Thickness (mm) 15.1 15.4 15.2 Internal bond (kg/cm2) 8.1 8.7 8.9 2 hrs thickness swelling (%) 10.5 10.0 9.8 24 hrs thickness swelling (%) 19.9 19.3 18.7 Free formaldehyde (mg 1009 dry board) 46.6 39.2 34.3 Moisture content (%) 5.9 5.3 5.0 It can be noticed from the above mentioned table that samples 1 and 2 including the substitute according to the present invention give boards equivalent to the blank, sample 0, while giving a significant free formaldehyde reduction and resin saving.
Example 4 This is a laboratory test for plywood using a phenolic resin.
The following samples were prepared: Sample No. 1 2 parts by weight Phenol (100%) 180 200 Formaldehyde (100%) 80 100 Molasses (100%) 120 180 Ammonium lignosulfonate (100%) 200 Water 420 520 Total 1000 1000 The samples were prepared by plain mixing at room temperature until the solids were completely dissolved. The pH of final products was brought to 10.0 by means of addition of sodium hydroxide.
These samples were used in a glue formation as follows: Glue formulation No. 0 1 2 parts by weight Phenol formaldehyde glue (100%) 100 80 80 Hardener (calcium carbonate: wheat flour - weight ratio 50:50) 60 60 60 Water 107 90 90 Sample 1 - 30.77 Sample 2 - - 30.77 Wheat flour - - 10 Total 267 260.77 270.77 Viscosity (mPa.s) 1200 1300 1100 The above mentioned glue formations were used to spread both sides of the core veneer for 3 ply boards.
Boards were then introduced in a cold press where they were pressed under the following conditions: Press time 8 minutes Pressure 10kp/cm2 All boards gave very good tack properties.
They were then pressed in a hot press under the following conditions: Press temperature 1300C Press time 3.5 minutes Pressure 12kp/cm2 These boards were tested as follows: They were immersed for 24 hours in water at 60"C. After this they were introduced in water at 20"C for one hour and then the knife test was carried out.
Results were as follows: Glue formulation No. 0 1 2 Grading 10/10 10/10 10/10 The knife test is carried out as follows: Plywood samples are placed in water under pressure for 30 minutes and then in vacuum for another 30 minutes. Samples are then scraped with a knife on the surface until the top veneer comes off and the core shows up. The grading depends on the amount of fibers showing in the core after the top veneer was scraped off.
When gluing is satisfactory, the surface that appears after scraping with the knife must still be covered with fibers. When it is completely covered with fibers grading is 10 (excellent). As more clean spots appear and less fibers, grading is diminished. A grading of 8 is still satisfactory, ant it means that the surface is mainly covered with fibers with only a few clean spots appearing. Lower grading is unsatisfactory.
Example 5 Two samples were prepared according to the following formulations: Sample No. 1 2 parts by weight Formaldehyde (100%) 100 140 Urea (100%) 140 190 Melamine (100%) 100 110 Molasses (100%) - 110 Ammonium lignosulfonate (100%) 150 Water 510 450 Total 1000 1000 The above mentioned samples were prepared by plain mixing at 25 to 300C until the solids were completely dissolved. The pH of the final products was adjusted to 8.5 to 10.0.
Glue formulations were then prepared as follows: Glue formulation No. 0 1 2 parts by weight Kauramin 535 (63% solids) 108 92 92 Hardener (1) 14.8 14.8 14.8 Formic acid (20%) 4 4 4 Paraffin emulsion 5.5 5.5 5.5 Sample 1 - 16 Sample 2 - - 16 Water 13 13 13 (1) The Hardener solution was: hot water 462 urea 384 ammonium chloride 154 Total 1000 These glue formulations were used separately to spray a constant quantity of dried wood chips with 12% dry glue/dry wood.
The sprayed wood chips were then formed into a mat having a normal thickness of 16mm.
These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 2000C Press time l0sec/mm Pressure 35kp/cm2 Boards were then tested and the results are reported in the following table.
Glue formulation No. 0 1 2 Density (kg/m3 686 687 685 Thickness (mm) 15.9 15.7 15.7 Internal bond (kg/cm2) 6.6 6.5 6.4 2 hrs thickness swelling (%) 3.2 3.2 2.9 24 hrs thickness swelling (%) 9.2 9.0 8.5 V-100 (kg/cm2) 1.6 1.5 1.6 The V-100 test is carried out as follows: The samples to be tested are placed in water at 20 + 5 C. This water is warmed up in 1 to 2 hours to 100 C. The water temperature is kept at 100"C for 2 hours. It is important that there is a space of at least 15mm on all sides of every sample so as to make sure that water is freely introduced in the samples. The samples are then introduced for at least 1 hour in a refrigerator at 2 + 50C. Water is then allowed to drip and the wet samples are tested again for internal bond.
Example 6 The following example will illustrate the fact that products according to our present invention may be produced by means of a variety of raw materials.
Samples were prepared according to the following formulations: Sample No. 1 2 3 parts by weight Paraformaldehyde 350 - Precondensate 80% (1) - 50 Acetaldehyde 100% - - 130 Urea 100% 150 12 200 Sucrose 100% 50 100 Molasses 100% 50 150 Ammonium lignosulfate 100% - 230 210 Dextrin 100% - 40 Water 400 418 460 (1) Precondensate containing 53 parts by weight of formaldehyde, 27 parts by weight of urea and 20 parts by weight of water The above mentioned samples were prepared by plain mixing until the solids were completely dissolved. The pH of the final products was adjusted to 7.5 to 8.0.Glue formulations were then prepared as follows: Glue formulation No. 0 1 2 3 parts by weight Urea formaldehyde resin parts by weight (65% solids) 108.9 93 93 93 Water 13.8 13.8 13.8 13.8 Sample 1 - 15.9 - Sample 2 - - 15.9 Sample 3 - - - 15.9 Ammonium chloride (20%) 7.1 7.1 7.1 7.1 These glue formulations were used separately to spray a constant quantity of dried of wood chips.
The sprayed wood chips were then formed into a mat having a normal thickness of 16mm.
These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 2000C Press time 9sec/mm Pressure 33kp/cm2 Boards were then tested and the results are reported in the following table: Glue formulation No. 0 1 2 3 Density (kg/m3) 600 610 590 580 Thickness (mm) 15.8 15.9 15.7 15.6 Internal bond (kg/cm2) 6.8 6.9 7.1 6.5 2 hrs thickness swelling (%) 10.5 10.3 10.1 9.9 24 hrs thickness swelling (%) 20.1 19.5 19.9 20.3 Free formaldehyde 22.3 18.0 16.2 17.1 Moisture content (%) 5.7 5.3 5.5 5.6 Boards obtained with all glue formulations are equivalent.
Example 7 In this example four samples were prepared according to the following formulations: Sample No. 1 2 3 4 parts by weight Formaldehyde 100 100 100 100 Resorcinol - 50 - Thiourea 50 - - Urea 140 150 70 70 Benzoguanamine - - 80 Dicyandiamide - - - 80 Wheat starch - 50 - Dextrose - - - 50 Glucose - 50 - Fructose - - 50 Modified starch * 50 - - Corn syrup 60 - - Molasses - - 50 100 Black liquor - 100 - Sodium lignosulfonate 100 - 150 100 Water 500 500 500 500 Total 1000 1000 1000 1000 * Starch which has been hydrolysed to give a lower molecular weight and, therefore, a low viscosity The above mentioned samples were prepared by plain mixing at 40 to 500C until the solids were completely dissolved. The pH of the final products was adjusted to 8.5 to 10.0.
Glue formulations were then prepared as follows: Glue formulation No. 0 1 2 3 4 parts by weight Urea formaldehyde resin (65%) 108.9 87.1 87.1 87.1 87.1 Water 13.8 13.8 13.8 13.8 13.8 Sample 1 - 21.8 - - Sample - - 21.8 - Sample - - - 21.8 Sample - - - - 21.8 Ammonium chloride (20%) 7.1 7.1 7.1 7.1 7.1 These glue formulations were used separately to spray a constant quantity of dried wood chips.
The sprayed wood chips were then formed into a mat having a nominal thickness of 16mm.
These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 2000C Press time 9sec/mm Pressure 33kp/cm2 Boards were then tested and the results are reported in the following table: Glue formulation No. 0 1 2 3 4 Density (kg/m3) 625 617 633 631 628 Thickness (mm) 15.9 15.8 16.0 16.2 16.0 Internal bond (kg/cm2) 7.0 6.9 7.1 7.2 6.8 2 hrs thickn. swelling % 12.5 12.1 13.6 13.1 12.6 24 hrs thickn. swelling % 22.5 20.7 24.7 24.0 20.9 Free formaldehyde 2 (mg/100g dry board) 28.8 22.5 21.7 23.0 21.9 Moisture content % 6.1 5.7 5.9 5.9 6.2 It can be noticed from the above mentioned table that samples 1 to 4 including the substitute according to the present invention give boards equivalent to the blank, sample 0, while giving a significant free formaldehyde reduction and resin saving.
Example 8 Three samples were prepared according to the following formulations: Sample No. 1 2 3 parts by weight Formaldehyde 100% 135 135 135 Urea 100% 365 365 365 Sucrose 1009/0 10 Molasses 100% - 10 Calcium lignosulfonate (100%) - - 10 Water 490 490 490 Total 1000 1000 1000 The above mentioned samples were prepared by plain mixing at 25 to 30"C until the solids were completely dissolved. The pH of the final products was adjusted to 8.5 to 10.0.
Glue formulations were then prepared as follows: Glue formulation No. 0 1 2 3 parts by weight Urea formaldehyde 108.9 95.9 95.9 95.9 resin (65% solids) Water 13.8 13.8 13.8 13.8 Sample 1 - 13 - Sample 2 - - 13 Sample 3 - - - 13 Ammonium chloride 7.1 7.1 7.1 7.1 (20% solution in water) These glue formulations were used separately to spray a constant quantity of dried wood chips.
The sprayed wood chips were then formed into a mat having a nominal thickness of 16mm These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 200"C Press time 8sec/mm Pressure 35kp/cm2 Boards were then tested and the results are reported in the following table: Glue formulation No. 0 1 2 3 Density (kg/m3) 575 582 579 6601 Thickness (mm) 15.4 15.3 15.5 15.4 Internal Bond (kg/cm2) 8.3 8.7 8.9 9.5 2 hrs thickness swelling (%) 10.3 10.8 10.6 11.1 24 hrs thickness swelling (%) 20.2 21.3 20.9 21.9 Free formaldehyde 60.5 39.8 41.3 38.1 (mg/100g dry board) Moisture content (%) 6.0 7.1 6.8 6.5 Boards obtained with all glue formulations are equivalent. Those however that include the substitute according to the present invention have lower free formaldehyde.
Example 9 Three examples were prepared according to the following formulations: Sample No. 1 2 3 parts by weight Formaldehyde 100% 85 85 85 Urea 100% 400 400 400 Sucrose 100% 32.3 - Molasses 100% - 32.3 Calcium lignosulfonate (100%) - - 32.3 Water 482.7 482.7 482.7 Total 1000 1000 1000 The above mentioned samples were prepared by plain mixing at 25 to 300C until the solids were completely dissolved. The pH of the final products was adjusted to 8.5 to 10.0.
Glue formulations were then prepared as follows: Glue formulation No. 0 1 2 3 parts by weight Urea formaldehyde 108.9 81.7 81.7 81.7 resin (65% solids) Water 13.8 13.8 3.8 13.8 Sample 1 - 27.2 - Sample 2 - - 27.2 Sample 3 - - - 27.2 Ammonium chloride 7.1 7.1 7.1 7.1 (20% solution in water) These glue formulations were used separately to spray a constant quantity of dried wood chips.
The sprayed wood chips were then formed into a mat having a nominal thickness of 16mm.
These mats were then introduced into a hot press and boards were pressed at the following conditions: Press temperature 2000C Press time 8sec/mm Pressure 35kp/cm2 Boards were then tested and the results are reported in the following table: Glue formulation No. 0 1 2 3 Density (kg/m3) 610 590 597 615 Thickness (mm) 15.9 15.7 15.6 15.9 Internal bond (kg/cm2) 7.9 8.1 8.3 8.4 2 hrs. thickness swelling (%) 9.8 10.2 10.5 10.9 24 hrs. thickness swelling (%) 20.1 21.3 20.9 21.8 Free formaldehyde 40.1 15.3 17.1 16.3 (mg/100g dry board) Moisture content (%) 7.9 7.1 7.6 8.0 Boards obtained with all glue formulations are equivalent. Those however that include the substitute according to the present invention have a very big formaldehyde reduction and resin cost saving.

Claims (18)

1. A substitute for amino and phenolic resins in the polycondensation of such resins based on formaldehyde for bonding water penetrable cellulosic particles, characterized in that it comprises an aqueous solution of a) either at least one aldehyde together with at least one amide and/or together with at least one phenol, or a non-resinous condensation product of formaldehyde and urea, and b) a sugar or a sugar derivative or their by-products or a starch or its degradation products or a mixture thereof, and/or c) a raw and/or treated lignosulfonate.
2. A substitute according to claim 1, characterized in that it contains 40 to 52% by weight of water.
3. A substitute according to claim 1 or 2, characterized in that the weight ratio of a) to b) and/or c) is 0.1 to 50.0:1.
4. A substitute according to claim 3, characterized in that the weight ratio of a) to b) and/or c) is 1.0 to 15.0:1.
5. A substitute according to one of claims 1 to 4, characterized in that the aldehyde is formaldehyde or acetaldehyde.
6. A substitute according to one of claims 1 to 5, characterized in that the amide is urea, thiourea, melamine, benzoguanamine or dicyandiamide.
7. A substitute according to one of claims 1 to 5, characterized in that the phenol is phenol itself or resorcinol.
8. A substitute according to one of claims 1 to 7, characterized in that component b) is molasses, dextrose, glucose, fructose, sucrose, corn syrup, wheat starch, modified starch or dextrin glue.
9. A substitute according to one of claims 1 to 8, characterized in that component c) is ammonium, sodium or calcium lignosulfonate or black liquor.
10. A process for preparing a substitute for amino and phenolic resins, characterized by dissolving in water a) either at least one aldehyde together with at least one amide and/or together with at least one phenol, or a non-resinous condensation product of formaldehyde and urea, and b) a sugar or a sugar derivative or their by-products or a starch or its degradation products or a mixture thereof, and/or c) a raw and/or treated lignosulfonate.
11. A process according to claim 10, characterized by preparing a solution which contains 40 to 52% by weight of water.
12. A process according to claim 10 or 11, characterized in that the weight ratio of a) to b) and/or c) is 0.1 to 50.0:1.
13. A process according to claim 12, characterized in that the weight ratio of a) to b) and/or c) is 1.0 to 15.0:1.
14. A process according to one of claims 10 to 13 characterized in that the aldehyde used is formaldehyde or acetaldehyde.
15. A process according to one of claims 10 to 14, characterized in that the amide used is urea, thiourea, melaminde, benzoguanamine or dicyandiamide.
16. A process according to one of claims 10 to 14, characterized in that the phenol itself or resorcinol.
17. A process according to one of claims 10 to 16, characterized in that the component b) used as molasses, dextrose, glucose, fructose, sucrose, corn syrup, wheat starch, modified starch or dextrin glue.
18. A process according to one of claims 10 to 17, characterized in that the component c) used is ammonium, sodium or calcium lignosulfonate or black liquor.
GB8710016A 1986-06-06 1987-04-28 Substitute for amino and phenolic resins Expired GB2191207B (en)

Priority Applications (19)

Application Number Priority Date Filing Date Title
NZ22043787A NZ220437A (en) 1986-06-06 1987-05-26 Aldehyde/sugar/lignosulphonate mixture as a substitute for amino and phenolic resins in bonding agents
AT8787600007T ATE104687T1 (en) 1986-06-06 1987-05-29 METHOD OF GLUING WATER-PERMEABLE CELLULOSE PARTICLES.
EP19870600007 EP0252867B1 (en) 1986-06-06 1987-05-29 Process for bonding water penetrable cellulosic particles
ES87600007T ES2052597T3 (en) 1986-06-06 1987-05-29 PROCEDURE TO LOCK PENETRABLE CELLULOSIC PARTICLES BY WATER.
DE3789635T DE3789635T2 (en) 1986-06-06 1987-05-29 Process for gluing water-permeable cellulose particles.
NO872323A NO169295C (en) 1986-06-06 1987-06-03 REPLACEMENT PRODUCT FOR POLYCONDENSABLE, FORMAL SKIN-BASED AMINO RESIN AND / OR PHENOLIC RESIN AND PROCEDURE FOR ITS PREPARATION
DK283787A DK283787A (en) 1986-06-06 1987-06-03 COMPENSATION FOR AMINO RESINS AND PHENOLIC RESINS
FI872516A FI88725C (en) 1986-06-06 1987-06-04 Foerfarande Foer bindande av vattengenomslaeppande cellulosapartiklar genom polykondensation av amino- och phenolhartser baserade pao formaldehyd
MYPI87000763A MY101499A (en) 1986-06-06 1987-06-04 Substitute for amino and phenolic resins.
BG080034A BG46750A3 (en) 1986-06-06 1987-06-05 Formaldehyde composition
SU4202785 RU2055856C1 (en) 1986-06-06 1987-06-05 Additive composition to urea-formaldehyde resin
MX006797A MX168753B (en) 1986-06-06 1987-06-05 SUBSTITUTE FOR AMINO AND PHENOLIC RESINS
US07/058,905 US4886854A (en) 1986-06-06 1987-06-05 Substitute for amino and phenolic resins
PL1987266096A PL157068B1 (en) 1986-06-06 1987-06-05 A substitute of amino and phenol resins and a method of its production
HU872585A HU207108B (en) 1986-06-06 1987-06-05 Process for producing boards with reduced formaldehyde content by fixing cellulose parts during the polycondensation of formaldehyde based amino and phenolic resins
CA 538971 CA1290085C (en) 1986-06-06 1987-06-05 Substitute for amino and phenolic resins
KR1019870005710A KR960002528B1 (en) 1986-06-06 1987-06-05 Substitute for amino and phenolic resins
JP62141297A JPS63258945A (en) 1986-06-06 1987-06-05 Substitute of amino resin and phenol resin, and production thereof
BR8702894A BR8702894A (en) 1986-06-06 1987-06-08 SUBSTITUTE MATERIAL FOR AMINO RESIN AND PHENOLIC WELL AS A PROCESS FOR ITS PREPARATION

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB868613791A GB8613791D0 (en) 1986-06-06 1986-06-06 Substitute for amino & phenolic resins
GB878701518A GB8701518D0 (en) 1986-06-06 1987-01-23 Substitute for amino & phenolic resins

Publications (3)

Publication Number Publication Date
GB8710016D0 GB8710016D0 (en) 1987-06-03
GB2191207A true GB2191207A (en) 1987-12-09
GB2191207B GB2191207B (en) 1989-12-13

Family

ID=26290878

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8710016A Expired GB2191207B (en) 1986-06-06 1987-04-28 Substitute for amino and phenolic resins

Country Status (2)

Country Link
AU (1) AU603804B2 (en)
GB (1) GB2191207B (en)

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Publication number Priority date Publication date Assignee Title
US5328497A (en) * 1992-01-21 1994-07-12 Georgia-Pacific Corporation Particulate fertilizer dust control
BE1018721A3 (en) * 2009-04-16 2011-07-05 Unilin Bvba PLATE MATERIAL AND PANEL THAT CONTAINS SUCH PLATE MATERIAL.
EP2930195A1 (en) * 2014-04-11 2015-10-14 Kronotec AG Adhesive composition for panels containing fibres and a method for the production thereof
EP2963169A1 (en) * 2014-07-03 2016-01-06 Johns Manville Formaldehyde-free melamine carbohydrate binders for improved fire-resistant fibrous materials

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GB506553A (en) *
GB624437A (en) * 1940-01-24 1949-06-08 L Impregnation Soc Improvements relating to synthetic resins
GB634368A (en) * 1945-06-20 1950-03-22 Scholten Chemische Fab Process for making dry starch preparations soluble in cold water
GB824108A (en) * 1956-02-20 1959-11-25 Koppers Co Inc Starch adhesives and method of preparation
GB929004A (en) * 1960-10-10 1963-06-19 Staley Mfg Co A E Dry potential adhesive compositions
GB963462A (en) * 1961-11-21 1964-07-08 West Virginia Pulp & Paper Co Resin binder
GB1038077A (en) * 1962-08-09 1966-08-03 Corn Products Co Urea-formaldehyde-furfuryl alcohol-sugar compositions, foundry cores and process of making same
GB1293744A (en) * 1970-01-19 1972-10-25 Fibreglass Ltd Fibreglass resin lignin coating
GB1309606A (en) * 1970-04-14 1973-03-14 Matalon R Silicate binder adjuvants binders and foundry casting forms prepared therefrom
GB1316911A (en) * 1971-01-29 1973-05-16 Fibreglass Ltd Binders for glass fibre insulation
GB1333470A (en) * 1971-07-13 1973-10-10 Fibreglass Ltd Binders for glass fibre insulation
GB1601751A (en) * 1977-10-18 1981-11-04 Metsaliiton Teollises Oy Adhesives based on phenol-formaldehyde resin and alkali lignins
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GB2136008A (en) * 1983-02-07 1984-09-12 Enigma Nv Formaldehyde binder

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5328497A (en) * 1992-01-21 1994-07-12 Georgia-Pacific Corporation Particulate fertilizer dust control
BE1018721A3 (en) * 2009-04-16 2011-07-05 Unilin Bvba PLATE MATERIAL AND PANEL THAT CONTAINS SUCH PLATE MATERIAL.
BE1018765A3 (en) * 2009-04-16 2011-08-02 Unilin Bvba PLATE MATERIAL AND PANEL THAT CONTAINS SUCH PLATE MATERIAL.
EP2930195A1 (en) * 2014-04-11 2015-10-14 Kronotec AG Adhesive composition for panels containing fibres and a method for the production thereof
EP2963169A1 (en) * 2014-07-03 2016-01-06 Johns Manville Formaldehyde-free melamine carbohydrate binders for improved fire-resistant fibrous materials
US9447221B2 (en) 2014-07-03 2016-09-20 Johns Manville Formaldehyde-free melamine carbohydrate binders for improved fire- resistant fibrous materials
US9611350B2 (en) 2014-07-03 2017-04-04 Johns Manville Formaldehyde-free melamine carbohydrate binders for improved fire-resistant fibrous materials
US9982082B2 (en) 2014-07-03 2018-05-29 Johns Manville Formaldehyde-free melamine carbohydrate binders for improved fire-resistant fibrous materials

Also Published As

Publication number Publication date
AU603804B2 (en) 1990-11-29
GB2191207B (en) 1989-12-13
GB8710016D0 (en) 1987-06-03
AU7378887A (en) 1987-12-10

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