Process for recycling materials containing benzoxazine resin, especially fiber composite plastics containing benzoxazine resin

Abstract

The present invention relates to a process for chemically degrading materials containing benzoxazine resin, in particular benzoxazine resins, benzoxazine resin pre-polymers and benzoxazine resin-containing plastics, that enables a high quality recycling process for used up benzoxazine resin-containing materials, in particular the separation of composite materials, such as duromer-based fiber composite plastics containing a benzoxazine resin matrix, and reuse of the benzoxazine-containing materials.

Claims

1. A process for degrading benzoxazine resin-containing materials, wherein the benzoxazine resin-containing material is subjected to aminolysis with an agent containing at least one reactive NH.sub.2 group and/or NH group.

2. The process as recited in claim 1, wherein the agent containing the at least one reactive NH.sub.2 group and/or NH group is an aliphatic or aromatic amine or hydrazine that can comprise other functional groups.

3. The process as recited in claim 1, wherein the agent containing the at least one reactive NH.sub.2 group and/or NH group is an amino alcohol having the formula NH.sub.2YOH, where Y is a divalent aliphatic or aromatic residue.

4. The process as recited in claim 1, wherein the agent containing the at least one reactive NH.sub.2 group and/or NH group is a diamine of formula NH.sub.2YNH.sub.2, where Y is a divalent aliphatic or aromatic residue.

5. The process as recited in claim 1, wherein the reaction is performed in a solvent.

6. The process as recited in claim 5, wherein the solvent is tetrahydrofuran, dimethyl sulfoxide, ethanol, water, dioxane, dichloromethane, chloroform, dimethylformamide, or N-methyl-2-pyrrolidone.

7. The process as recited in claim 1, wherein the agent containing the at least one reactive NH.sub.2 group and/or NH group is used as solvent, if needed under pressure in the condensed state, or after melting.

8. The process as recited in claim 1, wherein the process is performed at elevated temperature and/or elevated pressure.

9. The process as recited in claim 1, wherein the benzoxazine-containing material is reinforced with fibers.

10. The process as recited in claim 9, wherein the fibers are selected from carbon fibers, glass fibers, aramide fibers, basalt fibers, ceramic fibers, synthetic fibers and natural fibers, wherein after the breakdown of the benzoxazine-containing material the fibers are present in solid form in the solution of the agent containing the at least one NH.sub.2 group and/or NH group and the degradation products of the benzoxazine-containing material.

11. The process as recited in claim 9, wherein the fibers are polyamide fibers.

12. The process as recited in claim 11, wherein the agent containing the reactive NH.sub.2 groups and/or NH groups is selected from a primary amine and a diamine having two primary amino groups that do not contain any additional reactive substituents, preferably from an amine of formula R*NH.sub.2, wherein R* is an unsubstituted hydrocarbon residue with preferably at least 6 carbon atoms or an alkylene diamine such as ethylene diamine, whereby after the degradation of the benzoxazine-containing material the fibers are present in solid form in the solution of the agent containing at least one NH.sub.2 group and/or NH group and the degradation products of the benzoxazine-containing material.

13. The process as recited in claim 11, wherein the agent containing the reactive NH.sub.2 groups and/or NH groups is selected from amino alcohols, in particular amino ethanol, whereby after the breakdown of the benzoxazine-containing material the breakdown product of the fibers are also present in solubilized form in the agent containing at least one NH.sub.2 group and/or NH group.

14. A process for recycling a benzoxazine resin-containing material, comprising the degradation of the material as defined in claim 1, the removal of volatile products, preferably under reduced pressure and/or at elevated temperature, and the mixing of the material with one or more substances that react with the resultant degradation products under formation of a polymer network.

15. The process as recited in claim 14, wherein the material is mixed with an at least bifunctional isocyanate.

16. The process as recited in claim 5, wherein the reaction is performed in a cyclic ether, an alcohol, a chlorinated hydrocarbon or an N-containing solvent.

17. The process as recited in claim 15, wherein the bifunctional isocyanate is hexamethylene-1,6-diisocyanate-based (HDI-) trimer.

Description

EXEMPLARY EMBODIMENTS

Example 1

(1) Preparation of Pure Benzoxazine Resin Plates.

(2) For preparation of pure benzoxazine resin plates, bisphenol A-based benzoxazine resins were melted at 120 C., placed in an open aluminum mold, and cured according to the following curing protocol. Bisphenol F-based benzoxazine pure resin plates were prepared analogously.

(3) TABLE-US-00001 Temperature [ C.] Time [min] 120 30 120 to 150 30 150 60 150 to 180 30 180 60 180 to 200 30 200 180

Example 2

(4) 5 g cured bisphenol A-based benzoxazine resin and 2-aminoethanol were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 6 hours and 45 minutes at 172 C. under reflux.

(5) It was found that the starting material was quantitatively converted into products that are soluble in 2-aminoethanol. A clear solution was obtained.

(6) A complete degradation of the polymer network was detected by GPC. The degradation products dissolved in THF all had a molecular weight of less than 4000 g.Math.mol.sup.1.

Example 3

(7) 5 g cured bisphenol A-based benzoxazine resin and 2-ethylene diamine were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 120 hours at 160 C. under reflux.

(8) It was found that the starting material was quantitatively converted into products that are soluble in ethylene diamine. A clear solution was obtained.

Example 4

(9) 5 g cured bisphenol F-based benzoxazine resin and 2-aminoethanol were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 35 minutes at 172 C. under reflux.

(10) It was found that the starting material was quantitatively converted into products that are soluble in 2-aminoethanol. A clear solution was obtained.

(11) A complete degradation of the polymer network was detected by GPC. The degradation products dissolved in THF all had a molecular weight of less than 4000 g.Math.mol.sup.1.

Example 5

(12) 5 g cured bisphenol F-based benzoxazine resin and 2-ethylene diamine were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 12 hours at 160 C. under reflux.

(13) It was found that the starting material was quantitatively converted into products that are soluble in ethylene diamine. A clear solution was obtained.

Example 6

(14) 5 g cured bisphenol F-based benzoxazine resin and octylamine were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 12 hours at 180 C. under reflux.

(15) It was found that the starting material was quantitatively converted into products that are soluble in octylamine. A clear solution was obtained.

Example 7

(16) 5 g cured bisphenol F-based benzoxazine resin and N-methylethanolamine were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 14 hours at 160 C. under reflux.

(17) It was found that the starting material was quantitatively converted into products that are soluble in N-methylethanolamine. A clear solution was obtained.

Example 8

(18) Preparation of Benzoxazine-Cyanate Copolymers

(19) For the preparation of pure benzoxazine-cyanate resin plates, 31.8 g bisphenol A-based benzoxazine resin was melted at 120 C. and 57.4 g of bisphenol A-based cyanate (DCBA) molten at 80 C. was added. The mixture was then homogenized with a precision glass stirrer (KPG stirrer), added to an open aluminum mold, and cured according to the following curing protocol.

(20) Further, benzoxazine cyanate pure resin plates were prepared using bisphenol F-based benzoxazine resin. To this end, 35.8 g bisphenol F-based benzoxazine resin was melted at 120 C. and 68.8 g of bisphenol A-based cyanate (DCBA) molten at 80 C. was added. The mixture was then homogenized with a precision glass stirrer (KPG stirrer), added to an open aluminum mold, and also cured according to the following curing protocol.

(21) TABLE-US-00002 Temperature [ C.] Time [min] 120 60 120 to 140 30 140 480 140 to 150 30 150 60 150 to 170 30 170 60 170 to 190 30 190 60 190 to 210 30 210 60 210 to 230 30 230 60 230 to 250 30 250 60

Example 9

(22) 5 g of a cured benzoxazine cyanate pure resin plate, consisting of a bisphenol A-based benzoxazine resin and bisphenol A-based cyanate, and 2-aminoethanol were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 35 minutes at 172 C. under reflux.

(23) It was found that the starting material was quantitatively converted into products that are soluble in 2-aminoethanol. A clear solution was obtained.

Example 10

(24) 5 g of a cured benzoxazine cyanate pure resin plate, consisting of bisphenol F-based benzoxazine resin and bisphenol A-based cyanate, and 2-aminoethanol were added at a mass ratio of 1:4 to a 50 ml round bottom flask with a Dimroth condenser and boiled for 35 minutes at 172 C. under reflux.

(25) It was found that the starting material was quantitatively converted into products that are soluble in 2-aminoethanol. A clear solution was obtained.

Example 11

(26) The fiber rovings and yarns to be tested were stored at different temperatures in different decomposition reagents in 50 ml round bottom flasks with Dimroth condenser. The fiber rovings treated with reagents were then washed with ethanol and dried at room temperature in a vacuum oven. Tensile tests were subsequently performed using an Instron 3369 with a 500 N load cell and a special module for testing filigree samples. The distance between the two chuck jaws and, accordingly, the measuring length was always 30 mm and the testing speed was set to 2.5 mm.Math.min.sup.1.

(27) To determine whether the washing procedure has an effect on the results, fibers were washed with ethanol, and their mechanical properties were compared with those of unwashed fibers. An effect of the washing process on the mechanical properties of any of the fiber types used here was not observed.

(28) PAN-based 3K carbon fiber rovings (2,000 dtex), fiberglass rovings (E-glass, approx. 680 dtex), aramide fiber rovings (approx. 1,730 dtex), polyamide fiber rovings (PA 6, approx. 1.880 dtex) and twisted natural fibers (flax-based; approx. 530 dtex) were used.

(29) In the experiments described below, each of the five selected types of fibers were stored for 1 h in each of three different reagents at the respective temperature and their mechanical properties were tested using tensile tests on fiber rovings or fiber yarns.

(30) In the case of the carbon fibers, a significant effect on the mechanical properties was not recorded in any of the reagents at all three selected temperatures. FIG. 1 shows the results of the mechanical tensile tests on untreated and treated carbon fiber rovings.

(31) In the case of glass fibers, a worsening of the mechanical properties by treatment with the different reagents was not observed at any temperature within the measurement accuracy (see FIG. 2).

(32) Aramid fibers are damaged by use of ethylene diamine or 2-aminoethanol. Especially in the case of 2-aminoethanol, a strong reduction of the mechanical properties was observed depending on the storage temperature. In these experiments, a correlation between tensile elongation and tensile strength of the fibers is also observed. If aramid fiber-reinforced composite plastics are to be recycled, it is recommended to use, for example, n-octylamine (see FIG. 3).

(33) In the case of natural fibers, a significant negative effect on the mechanical properties was not recorded in any of the reagents at all three selected temperatures (see FIG. 4). Particularly noteworthy here is the strong increase in the elongation at break after storage in ethylene diamine. This supports the assumption that flax fibers are chemically modified in these experiments when stored in ethylene diamine.

(34) The polyamide fibers (PA 6) are an exception in the context of the work performed here on the resistance to chemicals of reinforcing fibers. It was discovered that polyamide 6 fibers dissolve in refluxing 2-aminoethanol, while the polyamide is not soluble in less polar and/or low-boiling reagents. It was also found that ethylene and n-octylamine were particularly suitable for decomposing polyamide-containing composite plastics, since even under refluxing conditions, no significant effect on the mechanical properties can be observed (see FIG. 5).

Example 12

(35) As in Example 11, the test fibers were stored in 50 ml round bottom flasks with Dimroth condenser. FIGS. 6 and 7 show the results of tensile tests (tensile force on the left, darker bar respectively, tensile elongation right, brighter bars respectively) on untreated carbon fiber rovings and on carbon fiber rovings stored for 24 h in the refluxing reagents (FIG. 6) or glass fibers (FIG. 7). The following table shows an overview of the reagents used and their boiling points. The fibers are not damaged by the reagents tested and could therefore be used again as reinforcing fibers, after a benzoxazine resin-containing matrix is decomposed.

(36) TABLE-US-00003 Reagent T.sub.bp. [ C.] n-Octylamine 180 Ethylenediamine 116 2-Aminoethanol 172

Example 13

(37) 6 g of a bisphenol A-based benzoxazine resin cured as in Example 1 was subjected to aminolysis in 24 g of 2-aminoethanol at a temperature of 172 C. under reflux for 2 h. The excess reagent was removed by distillation using a rotary evaporator under vacuum at 10 mbar and an oil bath temperature of 150 C.

(38) 20.0% by mass of the breakdown products that are highly viscous at room temperature were melted at 130 C. and mixed with 11.8% by mass of 1,4-butanediol. The resulting mixture was added to 68.2% by mass of a hexamethylene-1,6-diisocyanate-based (HDI) trimer. The components were then homogenized for 2 minutes with a planetary mixer. The material was then cured for 24 h at room temperature and post-cured in a circulating air oven for 0.5 h at 150 C. The produced material is a polyurethane foam with closed cells.

(39) The cured material was characterized by DMA using Single Cantilever equipment. The curves measured by DMA and the respective tan are shown in FIG. 8. The polymer foam produced in this manner has a glass transition temperature of approximately 30 C. (tan .sub.max).

(40) The produced polymer is insoluble in the following organic solvents: ethanol, methanol, methyl ethyl ketone, acetone, tetrahydrofuran, dimethyl sulfoxide, chloroform.

(41) Due to the polymer network formation verified by DMA, the degradation products used here must contain functional groups that can react with isocyanates. These are in particular terminal hydroxyl and amino compounds.

Example 14

(42) The recycled material was prepared as described for Example 13.

(43) 16.6% by mass of the highly viscous recycled material were melted at 130 C. and dissolved in 9.8% by mass of 1,4-butanediol. The resulting solution was added to 73.6% by mass of a hexamethylene-1,6-diisocyanate-based (HDI) trimer. The components were then homogenized for 2 minutes with a planetary mixer.

(44) The cured material was characterized by DMA with Single Cantilever equipment. The curves measured by DMA and the respective tan are shown in FIG. 9. The hard foam produced in this manner has a glass transition temperature of approx. 53 C. (tan .sub.max).

(45) The produced polymer is insoluble in the following organic solvents: ethanol, methanol, methyl ethyl ketone, acetone, tetrahydrofuran, dimethyl sulfoxide, chloroform.

(46) Due to the polymer network formation verified by DMA, the degradation products used here must contain functional groups that can react with isocyanates. These are in particular terminal hydroxyl and amino compounds.