PROCESS FOR THE MANUFACTURE OF VEGETABLE-FIBRE BASED BOARDS, IN PARTICULAR PARTICLE BOARDS OR FIBRE BOARDS

Abstract: The manufacture of particle board, but the other known dry-processes to produce boards from vegetable fibres, such as bagasse, are not excluded, provided, however, that formaldehyde is one constituent of the glue used. The invention is based on the use of modified starch together with the main glue. The starch modificate can be carbamate, ester or ether. These modificates react with the formaldehyde residues left in the board after the setting reaction of the main glue, whereby the emission of the residual formaldehyde is essentially reduced.

Description: Process for the manufacture of vegetable-fibre based boards, in particular particle boards or fibre boards The subject of the present invention is a process for the manufacture of vegetable-fibre based boards, in which process the basic material of the board is treated with adhesive, the adhesive-treated material is spread as a board blank, and the blank is hot-pressed into a finished board, whereby the reactions of binding and hardening of the adhesive take place substantially during the hot-pressing. Here, in its wide sense, vegetable fibre means different fibres or chips derived from vegetable fibres, including, e.g., wood as chips or as defibrated by various methods. The invention is expressly concerned with processes in which the adhesive fraction in the board consists of an adhesive that in¬ cludes formaldehyde, such as urea-formaldehyde adhesive, urea-melamine-formaldehyde adhesive, and phenol-formalde¬ hyde adhesive. Of these adhesives, the one that is used most commonly is urea-formaldehyde adhesive (resin) , which is used in particular for the manufacture of particle board. Formaldehyde-based resin adhesives are used in the manufacture of various vegetable-fibre based boards because of the good physical properties of the board, obtained by means of the adhesive, as well as because of the reasonable cost of the adhesive. In respect of the said boards and their manufacture, problems have, however, been caused by the formaldehyde, which consti- tutes a part in the adhesive fraction in the board. If a favourable composition of the adhesive fraction and an optimal dosage of the adhesive, in view of the pro¬ perties of strength of the board, are aimed at, after the stage of hardening of the adhesive, a relatively high concentration of free formaldehyde unavoidably remains in the board. In view of the binding and hardening reactions of the adhesive fraction, it is preferable that there is a certain excess quantity of the formaldehyde component of the adhesive in the adhesive mixture. Most of this excess quantity is removed out of the board during its manufacture, above all at the stage of opening of the hot press included in the manufacturing process. At other stages of the manufacturing process, formaldehyde may also be liberated to the environment, but to a lower extent than in connection with the hot-pressing. The formaldehyde liberated right during the manufacture of the board does, however, not create insurmountable ob¬ stacles, for the equipment of manufacture can be provided with a purposeful ventilation system in order to keep the air in the working environment clean. An essential problem is, however, formed by formaldehyde at the sites of use of the boards, where the formaldehyde still remaining in the board escapes from the board slowly into the surrounding air. Formal- dehyde may also be- liberated from the adhesive as a result of decomposition reactions. Attempts have been made to find various solu¬ tions for the said problems, of which solutions the most natural one is reduction in the excess quantity of form- aldehyde in relation to the other component of the adhe¬ sive. Another simple means is reduction in the overall quantity of adhesive in relation to the board material. The former operation, however, deteriorates the optimal hardening reactions of the adhesive, whereby the adhesive present in the finished board does not reach its best possible strength. When the second suggested operation is applied additionally, i.e. when the quantity of ad¬ hesive is reduced in relation to the board material, problems arise in respect of the ultimate strength of the board. As a compromise between strength properties and formaldehyde emission, in the manufacture of particle boards when using urea formaldehyde as the adhesive fraction, at present a molar ratio of HCHO to urea = about 1.1 to 1.2 has been chosen, whereby the adhesive still obtains a reasonable strength on hardening. If the ratio is reduced from this further, a steep dete¬ rioration takes place in the strength of the adhesive. Earlier, molar ratios of HCHO to urea = about 1.4 to 1.6 were used for urea-formaldehyde adhesive, which ratio was earlier chosen expressly in order to obtain a reliable result in view of strength. With ur a^formaldehy_de adhes_ive (UF resin) , the dosage of adhesive used in the manufacture of par¬ ticle board is usually about 8 to 12 per cent by weight of the quantity of chips (dry matter/dry matter) . The following can be considered typical conditions of manu¬ facture: Adhesive mixtures: - Surface chips; UF resin (65 % dry matter) 100 parts by weight Paraffin emulsion (50% d. .) 8 " Hardening agent 3 " Water 15 - " - The hardening agent for the adhesive fraction for surface chips mentioned above has typically a composition as follows: Salammoniac 10 parts by weight Urea 10 - " - Water 80 - " - - Middle chips; UF resin (65 % dry matter) 100 parts by weight Paraffin emulsion (50% d.m.) 6 " Hardening agent 8 - " - Ammonia (25 %) 0 - " Water 5 - " - The hardening agent for the adhesive fraction for the middle chips has typically a composition as follows: Salammoniac 15 parts by weight Water 85 - " - The dosage of the adhesive varies depending on the layers of chips ordinarily within the following limits (the numbers indicate the quantity of dry adhesive as percentages of dry chips) : 3-layer board; surface chips 10 to 12 % middle chips 7 to 9 % 1-layer board 8 to 10 % In respect of the moisture of the chips, the following values are aimed at by the time when the stage of treatment with adhesive is reached: middle chips 0 to 2 % surface chips 2 to 6 % With ureaH:ormaldehy_d adhesive, the con¬ ditions of the hot-pressing stage of the board are typically within the following limits: Temperature 150 to 200 C Compression time 10 to 14 s/mm of board Pressure 2 to 3 MPa When ure_a^melamd.ne_-f_θ maldehyde_adhesi e (MUF resin) is used, the other components of the adhesive fraction as well as the adhesive dosage differ from the above to some extent. Ordinarily the following con¬ ditions are followed: Adhesive mixtures: - Surface chips; MUF resin (66 % dry matter) 100 parts by weight Paraffin emulsion (50% d.m.) Hardening agent II _ Ammonia (25 %) Water 15 _ il _ •Hardening agent for surface chips : Salammoniac 15 parts by weight Water 85 - " - Middle chips; MUF resin 100 parts by weight Paraffin emulsion (59 %) 6 _ II Hardening agent 7 Water 5 The composition of the hardening agent for middle chips is usually as follows: Salammoniac 15 parts by weight Water 85 - " - For the dosage of the adhesive, the following instructions are used (dry resin as percentages of dry chips) : The guide value is 12 to 15 % if the aim is V 100-glueing (DIN-68763-B1 3). In respect of the moisture of the chips, the following guide, values are aimed at before the stage of treatment with adhesive: Middle chips 0 to 2 % Surface chips 2 to 4 % In the hot-pressing, the following conditions are used: Temperature 150 to 200 °C Time ' 10 to 14 s/mm of board Pressure 2 to 3.5 MPa When £he_n£l f£rma_ldeh_de_ adhesive (PF resin) is used for the adhesive treatment of the board, the following conditions can be given as guide values: Adhesive mixtures (During adhesive treatment, water is added to the adhesive so as to control the viscosity and moisture of chips) - Surface and middle chips; PF resin (50 % dry matter) 100 parts by weight Water 0 to 10 - " - Hardening agent 6 to 10 - " As the hardening agent, 50-% I- CO, solution is used. The dosage of the adhesive takes place in accordance with the following instructions (dry resin as percentages of the dry matter of chips) : 1-layer board 9 to 11 % 3-layer board surface chips 10 to 13 % middle chips 8 to 10 % In order to reduce the thickness swelling of the board, paraffin emulsion may be added to the board, which emulsion is sprayed during the manufacture of the board to the chips separately from the adhesive. The quantity of dosage of paraffin is 0.8 to 1.5 % of solid wax, calculated on the weight of dry chips. With phenol-formaldehyde adhesive, the con¬ ditions of the compression stage are preferably as follows; Temperature 180 to 220 °C Time at least 0.3 s/mm of board Pressure 2 to 3.5 MPa As further means of reducing emissions of formaldehyde, substances added to the board have been used, which react with free formaldehyde and immobilize it in the board. As such agents have been used, e.g., ammonia, urea, many organic amines, such as triethanol- amine or diethylenetria ine, as well as organic nitriles. Finished boards have also been coated with various com¬ binations of substances, which contain agents that react with formaldehyde and thereby prevent access of formal¬ dehyde to the environment. In connection with the manufacture of boards, the added agents have, however, had the drawback of strong reactivity with formaldehyde, whereby these agents have competed with the other component in the adhesive fraction of the board in the reaction with ormaldehyde. Owing to this, the reaction of hardening of the adhesive has been disturbed, and the strength achieved for the board has suffered. On the other hand, the coating method requires an additional operation, either in the manufacture of the board or when the board is coated at the site of use. By means of the present invention, attempts have been made to find a solution for the drawbacks caused by free formaldehyde while following the operations model mentioned above, wherein an agent reacting with free formaldehyde is added to the board material. In order that a good result could be obtained, the additive has, however, in a way differing from prior art, been chosen so that it reacts with formaldehyde more slowly than the other component in the adhesive fraction, whereby no reaction competition situation detrimental to the strength of the adhesive can arise. The reactivity of the additive must, of course, be sufficient to immobilize the extra formaldehyde remaining from the reactions of hardening of the adhesive. According to the invention, this result has been reached so that, in connection with the manufacture of board, besides a formaldehyde-based adhesive, starch modified to carbamate, ester or ether is added to the fibre material", whereby the modification may be any one of those mentioned above or a mixture of two or all of them. It has been noticed that in particular adhesives that contain carbamate modification or mainly the said modification react in the desired way in the manufacture of boards. It has not been noticed that these starch modifications disturb the reactions of hardening of ad¬ hesive, but they can immobilize formaldehyde reactively with a sufficiently high speed so that the concentration of free formaldehyde in a finished board is lowered to an acceptable level. It is to be noticed in particular that the process of the invention permits manufacture of board so that, in the adhesive fraction in the board, a molar ratio of the adhesive components advantageous in view of attaining of strength of the adhesive as well as a dosage of adhesive fraction sufficient in view of strength can be used. In spite of this, the emission of formaldehyde can be brought to an acceptable level. An additional advantage that is obtained by means of the process of the invention is an increased strength after the pre-pressing (cold-pressing) applied to the board blank after the spreading of the material. Further, the starch derivatives described above have physical properties which make them usable, e.g., in a particle-board process, whereas, as a rule, it has not been noticed that starch derivatives have such properties. In practice, the particle-board pro¬ cess is very sensitive in respect of the water introduced into the process, and introduction of extra water into the process should be avoided. On the other.hand, the viscosity of the chemical solutions added to the process must be within the correct range in order that they could be pumped by means of ordinary dosage pumps and in order that they should behave in the desired way in the adhe¬ sive treatment. It has been noticed that a suitable viscosity range is 50 to 10,000 cP/Brookfield (mPas). As a rule, starch derivative solutions adopt this range of viscosity in usual temperatures of use, 0 to 30 C, when their dry solids contents are within the range of 5 to 20 %. The use of solutions as dilute as this, however, in practice, means an excessive quantity of additional water. The water quantity remains within permitted limits only when the dry solids content of the additional chemicals can be brought to the range of 25 to 72 %. It has been noticed that this can be achieved in the processes in accordance with the invention by using carbamate, ester, and ether modifications of starch as additional chemicals. 1 0 Besides having the values of viscosity and dry solids content mentioned above, the starch derivatives used in the process in accordance with the invention must also be real solutions or colloids so that the particle sizes in the ready starch product must be smaller than 5 μm, preferably clearly smaller than 1 μm. In view of the preparation of the starch derivative, it is further advantageous that the particle size of the starch raw- material is about 50 μm and preferably below 30 μm. The reduction of the particle size to the above values may take place during the preparation of the derivative by means of various methods, which are described below. It has been noticed that the particle size of the deri¬ vative used in the treatment with adhesive has a clear significance for the reactivity of the derivative with formaldehyde. Moreover, it has been noticed that, between the above three derivatives, carbamate, ester, and ether, there are differences in reacting in the particle board process with the adhesive fraction containing formalde¬ hyde. It has been noticed that in particular carbamate reacts in the desired way in the hot-pressing stage in the board manufacture. In this manufacturing step, the carbamate derivatives react sufficiently rapidly with formaldehyde in order that the concentration of free formaldehyde should remain at a tolerable level in the finished board, but, on the other hand, they do not react excessively rapidly in order to compete with the reactions of hardening of the adhesive fraction proper. Under these circumstances, it is advantageous that starch modified expressly to carbamate is used, or a mixture of derivatives in which more than 50 % of the DS-number, which represents the degree of modi ication, consists of carbamate. The remaining part of the deri- vative may consist of ester or ether of starch or of their mixture. . In the following, methods for the preparation of starch derivatives usable in the process of the present invention will be described. Preparation of s_tarch_et:he_r Starch ether can be prepared by using, e.g., ethylene oxide, propylene oxide, or alkylglycidyltri- methy1ammonium chloride as reagents. Test 1 : 1500 g water and 1000 g wheat starch are charged into a reactor. Sodium hydroxide is added to the reactor so that the pH of the solution is 11.0 to 12.0. Ethylene oxide is charged into the reaction vessel as cautious additions totalling 150 g. In order to accelerate the reaction, 5 g sodium sulphate or sodium carbonate is also charged into the reactor, whereinafter the product is washed three times with distilled water so that the dry solids content.of the product remains the same as at the beginning of the reaction. The DS number of the product was 0.02, and it was used for particle-board tests as such. Preparation of star£h_es_ter Starch ester can be prepared by using, e.g., acetic acid, acetic anhydride, chloracetic acid, maleic acid, maleic anhydride, fumaric acid, acetic ethenylester. Test 2: 1500 g water and 1000 g wheat starch are charged into a reactor. Sodium hydroxide is added to the reactor so that the pH of the solution is 11.0 to 12.0. 260 g acetic ethenylester is charged into the reactor by cautiously dropping. In order to accelerate the reaction, 5 g sodium sulphate or sodium carbonate is added to the reactor. The reaction mixture is stirred for 8 h at 25 to 30 C, whereinafter the product is washed three times 12 with distilled water so that the dry solids content of the product remains at the same level as when the reac¬ tion was started. The DS number of the product was 0.04, and it was used for particle-board tests as such. Preparation of s_tar£h_carbamat_e Starch carbamate can be prepared by using substituted carbamide compounds, such as, e.g., acetyl carbamide, thiocarbamide, carbonyl diamide, as the reacting component. Test 3: 4000 g liquid ammonia was pumped into the reaction vessel. 1000 g wheat starch and 400 g carbonyl diamide were added to the reaction vessel. The reaction mixture was stirred for 8 h at -40°C, whereinafter the product was washed three times with distilled water and prepared to a solution whose dry solids content was about 40 per cent by weight. The DS number of the product was 0.06, and it was used for particle-board tests as such. Test 4: 1500 g water and 1000 g wheat starch were charged into a reaction vessel. 350 g thiocarbamide and 10.g potassium acetate were added to the reaction vessel, to accelerate the reaction. The reaction mixture was stirred for 8 h at 25 to 30 C, whereinafter the product was washed three times with distilled water. The DS number of the product was 0.085, and it was used for tests as such. 1 3 Test 5 : 1500 g water and 1000 g wheat starch were charged into a reaction vessel. 400 g carbonyl amide and 15 g potassium acetate were added to the reaction vessel, to accelerate the reaction. The reaction mixture was stirred for 9 h at 25 to 30 °C, whereinafter the product was washed with distilled water three times. The DS number of the product was 0.080, and it was used for the tests as such. Test 6: The test was carried out in the same way as test 4, but the particle size of the product was reduced by means of a laboratory colloid mill from the range of 50 μm to the range below 2 μm. The product was washed and used for the tests in colloid form. Test 7: The test was carried out in the same way as test 1 , but the reaction was continued after washing in the same way as in test 4 , whereby a product was obtained whose DS number was 0.02 in respect of ether and 0.069 in respect of carbamate. The product was washed and used for the tests as such. Test 8: The test was carried out in the same way as test 3 . but the particle size of the product was reduced from the range of 50 μm to the range below 2 μm by means of a laboratory colloid mill, and used for the tests in colloid form. Test 9: The test was carried out in the same way as test 5, but the product was brought,by means of heat 1 4 treatment and a laboratory colloid mill, to a particle size below 1 μm, and its state resembled that of a real solution. In the following example, manufacturing factors of particle board will be examined, the conduct of the starch derivatives prepared in the above tests 1 to 9 in the manufacture of particle board being studied in respect of the said factors. In connection with the manufacture of the boards, starch derivatives described in tests 1 to 9 were added as a quantity of 13 per cent of the quantity of adhesive (abs.dry/abs.dry) . Example 1 Factors of manufacture of boards: bulk density 670 kg/xa? thickness 16 mm molar ratio of resin HCHO to urea 1.2 - resin percentage: in middle chips adhesive 8 % abs.dry/abs.dry, in surface chips 11 % abs.dry/abs. dry - the boards were tested as per the standards SFS 3516 and DIN 52,360 to 52,365. The results of the tests are given in the following- table 1. Table 1 Added starch d.erivative: Normal beard Test: 1 2 3 4 5 6 7 8 9 (no starch) Bending strength N/mm 2 13.9 13.5 13.8 13.7 13.7 14.2 13.9 14.1 14.0 14.2 Trans'ϋerse tensile strength N/irm 2 0.60 0.55 0.62 0.64 0.59 0.61 0.57 0.60 0.59 0.56 Thickness swelling in 2 h water solution test % after the test 6.2 6.4 6.0 5.9 6.1 6.3 6.0 5.8 6.1 5.8 Formaldehyde content πg/100 g* (FESYP) 9.7 8.5 7.6 7.3 7.3 7.5 6.5 6.3 6.1 22 Moisture of boards % of dry weight 9.6 8.1 8.6 8.7 9.3 8.1 8.7 8.6 8.1 9.5 In the following table 2, the formaldehyde content obtained on the basis of the test results is given as a function of dosage of starch. Table 2 Formaldehyde content ιtg/100 g (FESYP) 6.3 6.9 7.2 7.5 9.1 10.5 13 10 Dosage of starchderivative according to Test 8, % of adhesive abs . dry/abs . dry 1 3 12 1 1 1 0 9 8 7 * Formaldehyde content measured by the method recommended by the European Federation of Manufacturers of Particle Board (Federation Europeenne des Syndicats de Fabricants de Panneaux de Particule) CEN 120 (Comite Europeen de m m Normalisation - European Committee of Standardization) The following table 3 gives the results of the tests carried out in order to establish the viscosity values of the different modifications within different particle-size ranges at a certain dry solids content . 20 Table 3 Test 1 2 3 4 5 7 Viscosities of dis¬ persion cP (Brookfield) dry solids cont. 30 % 5 aver, particle size 50 μm 400 430 200 350 280 260 Viscosities of solution cP (Brookfield) average particle size below 2 μm Q dry solids content 50 % 122 ,000 92 ,000 5 ,000 8 ,000 9 ,500 11 ,000 The test results are the mathematical averages of the test values of ten parallel boards . 5 As comes out from the results of table 1 , the starch derivatives prepared in accordance with the tests 1 to 9 give very good properties of the board as compared with a board manufactured in a conventional way, without addition of starch. With these additions of starch derivatives, it is in particular possible to manufacture board of a low formaldehyde content. It is also worth noticing that in the tests in which carbamate has been used for the modification of starch, in the board tests, the formaldehyde content is lower than with ester or ether modifications. According to the results in table 2, it is noticed that the emittable and free formaldehyde content in the board becomes lower in accordance with the dosage quantity. It is noticed that in this test series the so-called S7 limit is a dosage of about 9 % in the adhesive (abs. dry/abs. dry). From table 3, it can be seen surprisingly that within small particle-size ranges it is the carbamate modifications that have lower viscosities than esters and ethers. Moreover, it is noticed that a mixed modi¬ fication of ether and ester also has a low and usable viscosity. Moreover, it can be seen from the results of table 1 that small particle size also has a favourable effect on the lowering of the formaldehyde content. In the above description of the invention, the description has dealt with the manufacture of par¬ ticle board, but for a person skilled in the art it is obvious how the invention can also be applied to the manufacture of boards out of other vegetable fibre materials, such as sawdust, straw, and bagasse. The starch derivative can be added in con¬ nection with ordinary manufacture of particle board either as mixed with the adhesive fraction proper or as separate in connection with the treatment of the chips with adhesive. When the addition takes place as separate, it is preferable that the temperature of the starch has been raised, an advantageous range being 50 to 100 °C. Good results are, however, also obtained even if the starch derivative is added at a lower temperature.

Claims: WHAT IS CLAIMED IS: 1. Process for the manufacture of vegetable- fibre boards, such as particle board, in which process the fibre material is treated with a formaldehyde-based adhesive, the adhesive-treated fibre material is spread as a board blank, and the blank is hot-pressed into a board, c h a r a c t e r i z e d in that besides the dosage of a formaldehyde-based adhesive, starch modified to carbamate, ester or ether, or a mixture of these modifications, is added to the fibre material. 2. Process as claimed in claim 1 , c h a r ¬ a c t e r i z e d in that besides the dosage of formaldehyde-based adhesive, whose quantity is about 8 to 13 per cent by weight of the quantity of the fibre material, calculated dry matter to dry matter, a dosage of modified starch is used, whose quantity is 0.5 to 40 per -cent by weight, preferably 5 to 25 per cent by weight, of the quantity of the fibre material, dry matter to dry matter. 3. Process as claimed in claim 1 or 2, c h a r a c t e r i z e d in that starch is used that has been modified to carbamate, ester or ether, whose modification number DS is 0.01 to 2.0. 4. Process as claimed in claim 3, c h a r ¬ a c t e r i z e d in that the share of ester or ether modification is at the maximum 50 % of the numerical value of the DS number. 5. Process as claimed in any of the preceding claims 1 to 4, c h a r a c t e r i z e d in that the starch is added as a water solution or colloid containing 25 to 72 per cent of dry matter. 6. Process as claimed in any of the preceding claims 1 to 5, c h a r a c t e r i z e d in that the starch is added as mixed with the formaldehyde-based adhesive. 7. Process as claimed in any of the preceding claims 1 to 6, c h a r a c t e r i z e d in that the starch is added in connection with the adhesive treatment as separate from the addition of the formaldehyde-based adhesive. 8. Process as claimed in claim 7, c h a r ¬ a c t e r i z e d in that the starch is added in con¬ nection with the adhesive treatment at a temperature of 10 to 100 °C, preferably 50 to 100 °C. 9. Process as claimed in any of the preceding claims 1 to 8, c h a r a c t e r i z e d in that modi¬ fied starch is used whose particle size was in modifi¬ cation less than about 50 μm, preferably less than 30 μ , and in the solution-like modified starch product less than 2 μm. 10. Process as claimed in any of the pre¬ ceding claims 1 to 9, c h a r a c t e r i z e d in that a starch is used whose pH is within the range of 4 to 12. 11. Process as claimed in any of the pre- ceding claims 1 to 10, c h a r a c t e r i z e d in that, besides the formaldehyde-based adhesive and the starch, auxiliary agents in themselves known are added to the fibre, such as hydrophobing agents. 12. Process as claimed in any of the pre- ceding claims 1 to 11, c h a r a c t e r i z e d in that a modified starch product is used whose colloid or solution has a viscosity of at least 20 to 10,000 cP (Brookfield) .

Inventors: HALONEN SEPPO, NIINIVAARA VEIKKO, NURMI KARI, HALONEN, SEPPO, NIINIVAARA, VEIKKO, NURMI, KARI
Applicants: KASVIOELJY VAEXTOLJE OY AB, OY KASVIOELJY-VAEXTOLJE AB
Application year: 1986
Main classification: B27N3
IPC codes: B27N3, C08L97