PROCESS FOR PREPARING A RESIN

Abstract

The present invention relates to an improved process for preparing an aqueous dispersion of lignin and the use of said suspension in the preparation of a resin.

Claims

1. A method for preparing a lignin dispersion comprising the steps of a) providing an aqueous medium having a pH of 1 to 7; b) adding lignin to the aqueous medium; and, c) mixing the aqueous medium at a temperature of from 41° C. to 95° C. until a dispersion of lignin in the aqueous medium has been obtained.

2. A method for preparing a resin comprising the steps of a) providing an aqueous medium having a pH of 1 to 7; b) adding lignin to the aqueous medium; c) mixing at a temperature of from 41° C. to 95° C. until a dispersion of lignin in the aqueous medium has been obtained; d) adding alkali, phenol, formaldehyde, or a combination thereof to the dispersion and e) maintaining a mixture formed in step d) at a temperature of from 30° C. to 95° C. for at least 30 minutes.

3. The method according to claim 1, wherein steps a) and b) are carried out without actively heating the aqueous medium.

4. The method according to claim 1, wherein an amount of lignin in the dispersion in step c) is 5-60 wt %.

5. The method according to claim 4, wherein the amount of lignin in the dispersion in step c) is 35-60 wt %.

6. The method according to claim 1, wherein the pH of the aqueous medium in step a) is between 2 to 5.

7. The method according to claim 2, wherein the temperature in step d) is lower than the temperature in step c).

8. The method according to claim 2, wherein the temperature in step d) is from 20° C. to 50° C.

9. A dispersion obtainable obtained by the method of claim 1.

10. A resin obtainable obtained by the method of claim 2.

11. A laminate, engineered wood product or insulation product manufactured with the resin according to claim 10.

12. The method according to claim 2, wherein steps a) and b) are carried out without actively heating the aqueous medium.

13. The method according to claim 2, wherein an amount of lignin in the dispersion in step c) is 5-60 wt %.

14. The method according to claim 13, wherein the amount of lignin in the dispersion in step c) is 35-60 wt %.

15. The method according to claim 2, wherein the pH of the aqueous medium in step a) is between 2 to 5.

Description

DETAILED DESCRIPTION

[0019] It is intended throughout the present description that the expression “lignin” embraces any kind of lignin, e.g. lignin originated from hardwood, softwood or annular plants. Preferably the lignin is an alkaline lignin generated in e.g. the Kraft process. The lignin may then be separated from the black liquor by using the process disclosed in WO2006031175.

[0020] As used herein, the term “dispersion” refers to a composition in which particles are dispersed in a continuous phase of a different composition than the particles. This is different from a “solution”, which generally refers to a homogenous mixture.

[0021] The method or process according to the present invention can be carried out batchwise or continuously.

[0022] The pH of the aqueous medium of step a) is from 1 to 7, such as from 2 to 7 or 6 to 7 or 2 to 5.

[0023] The dispersion obtained in step c) may be prepared and subsequently stored before step d) is carried out. The dispersion obtained in step c) may also be moved or shipped to another location at which step d) may be carried out. Thus, according to the present invention, the dispersion being stored, moved or shipped has been prepared such that the pH in step a) is from pH 1 to 7. Thus, according to the present invention, the dispersion being stored, moved or shipped has been prepared without addition of alkali. If sedimentation would occur after the dispersion of step c) has been stored for an extended period of time, briefly stirring the mixture prior to performing step d) may be advantageous.

[0024] The dispersion obtained in step c) may thus be prepared outside the reactor in which the subsequent steps take place. Alternatively, steps a) to c) can be carried out in the same reactor in which the subsequent steps take place. Alternatively, the dispersion of obtained in step c) can be prepared separately from the reactor in which the subsequent steps take place and be transported to the reactor using e.g. a pump, for example if the process according to the present invention is to be carried out continuously.

[0025] The aqueous medium in step a) may, in addition to water, comprise up to a total of 10 wt % solvent, such as an alcohol, such as ethanol, methanol or ethylene glycol. However, the pH of the aqueous medium in step a) is in the range of from 1 to 7, preferably 2 to 7 or 6 to 7 or 2 to 5.

[0026] The aqueous medium in step a) may, in addition to water, comprise up to a total of 15 wt %, such as 10 wt % additives, such as urea, a thickener or a tenside. However, the pH of the aqueous medium in step a) is in the range of from 1 to 7, preferably 2 to 7 or 6 to 7 or 2 to 5.

[0027] Steps a) and b) in the process according to the present invention are preferably carried out without actively heating the aqueous medium. Thus, the aqueous medium is preferably at room temperature, such as at a temperature of 15-25° C. at the time of adding the lignin. Step c) is carried out at a temperature of from 41° C. to 95° C.

[0028] Alkali is not added to the aqueous medium until in step d), i.e. after a dispersion of lignin in the aqueous medium has been obtained. After the addition of alkali, the aqueous medium comprises 5-50 wt % alkali, such as 10-50 wt % alkali, such as 40-50 wt % alkali. In one embodiment of the present invention, the pH of the aqueous medium after addition of lignin and alkali is at least pH 8, such as at least pH 10, such as at least pH 12 or at least pH13. The temperature in step d) is preferably lower than the temperature in step c). Preferably, the temperature in step d) is from room temperature to about 60° C., such as from 20° C. to 50° C.

[0029] The alkali is preferably sodium hydroxide, potassium hydroxide, calcium hydroxide, magnesium hydroxide or a mixture thereof.

[0030] The addition of alkali, phenol and/or formaldehyde in step d) can be carried out in any order. Each component may for example be added consecutively or at the same time as one or two of the other components. In one embodiment, the components are added in such a way that a part of the total amount of each component is added and one or more additional amounts of each component is subsequently added. Preferably, at least alkali and phenol are added in step d), in any order. More preferably, alkali, phenol and formaldehyde are added in step d), in any order.

[0031] In one embodiment of the invention, the dispersion in step c) comprises 5-60 wt %, such as 5-50 wt % lignin, such as 35-50 wt % lignin.

[0032] The present invention also relates to a resin composition obtainable by the process according to the present invention. The resin composition is preferably a lignin-phenol-formaldehyde resin.

[0033] The resin obtained is useful for example in the manufacture of laminates. The resin is then impregnated into and/or applied between the sheets that should form the laminate and said sheets are pressed together and heated at a temperature of about 130-150° C.

[0034] The present invention also relates to the use of the resin composition in engineered wood products such as plywood, particle board, wafer board, gluelam beams, structural composite lumber, oriented strand board (OSB), oriented strand lumber (OSL), laminated veneer lumber (LVL) and other applications such as laminates, insulation and molding compounds.

EXAMPLES

Example 1

[0035] In the first step, 488 g lignin (kraft lignin, 95% purity) was added to 254 g water at room temperature in a 5 L glass reactor equipped with a pitched blade stirrer, a condenser and a heating control unit. The mixture was heated to 80° C. and stirred at 80° C. for 30 minutes. The temperature was then reduced to 45° C. and 240 g sodium hydroxide was added the mixture and the mixture was stirred.

[0036] Secondly, 473 g phenol and 794 g formalin (52.5%) was slowly added to the mixture. The mixture was heated to about 80° C. and continued at 80° C. for about 75 minutes. Then, 181 g of NaOH solution (50%) was added and the reaction was continued for further 105 minutes. Then, the reaction was stopped by cooling to ambient temperature. The reaction was monitored by measuring the viscosity at 25° C. using a Brookfield DV-II+LV viscometer. The resin properties were given in the Table 1.

TABLE-US-00001 Resin from Example 1 Viscosity [cP] at 25° C. 414 pH at 23° C. 11.8 Solid Content [%] 155° C. 45.7

[0037] In view of the above detailed description of the present invention, other modifications and variations will become apparent to those skilled in the art. However, it should be apparent that such other modifications and variations may be effected without departing from the spirit and scope of the invention.