Disclosure of Invention
The invention aims to overcome the defects in the prior art and provides a PLA-lignin composite material modified by a reactive extrusion method and a preparation method thereof, and the PLA-lignin composite material is simple to operate and has good comprehensive performance.
In order to achieve the purpose, the invention adopts the following technical scheme:
on one hand, the invention provides a reaction extrusion method modified polylactic acid-lignin composite material, which comprises the following components in parts by weight:
in order to further optimize the above technical solution, the technical measures taken by the present invention further include:
preferably, the lignin is an aromatic high polymer containing structural units of the oxo-phenylpropanol or the derivative thereof in a molecular structure, and the particle size of the aromatic high polymer is 50-500 meshes.
Preferably, the initiator is a peroxide initiator; more preferably, the initiator is one or more of dicumyl peroxide, di-tert-butylperoxyisopropyl benzene, tert-butyl peroxybenzoate, tert-butyl peroxydicarbonate, tert-butyl hydroperoxide, 2, 5-dimethyl-2, 5-bis (tert-butylperoxy) hexane and benzoyl peroxide.
Preferably, the reactive monomer is one or more of maleic anhydride, acrylic acid and glycidyl methacrylate.
Preferably, the antioxidant is a phenolic antioxidant, such as 1010.
On the other hand, the invention also provides a preparation method of the polylactic acid-lignin composite material modified by the reactive extrusion method, which comprises the following steps:
firstly, weighing 100 parts of PLA and 40-100 parts of lignin in proportion, and uniformly mixing at normal temperature;
and (2) uniformly mixing 0.01-5 parts by weight of initiator, 0.01-15 parts by weight of reaction monomer and 0.1-1 part by weight of antioxidant, adding the mixture and the polylactic acid/lignin mixture obtained in the step (1) into a reaction device, and blending at a preset reaction temperature to obtain the polylactic acid-lignin composite material.
Preferably, the reaction equipment is at least one of an internal mixer and a reaction type extruder, the reaction temperature is 150-190 ℃, the rotor speed of the internal mixer is 50-200rpm, and the screw speed of the reaction type extruder is 100-600 rpm.
Compared with the prior art, the invention has the following advantages and beneficial effects:
(1) the polylactic acid-lignin composite material prepared by the invention has good comprehensive mechanical property;
(2) compared with other preparation methods, the preparation method is simple to operate and good in effect;
(3) the invention organically combines the biodegradable paper making byproduct, namely lignin, and the biodegradable plastic polylactic acid to manufacture the completely biodegradable plastic, thereby not only fully utilizing the paper making byproduct, namely lignin, but also improving the comprehensive mechanical property of the polylactic acid;
(4) the preparation method does not involve the use of a solvent at all in the preparation process of the polylactic acid-lignin composite material, and all the used components are directly physically mixed by a stirrer without further treatment;
(5) the polylactic acid-lignin composite material is prepared by melt blending of an internal mixer or an extruder, and the method has the possibility of industrial large-scale production.
Detailed Description
The following further describes embodiments of the present invention with reference to examples. The following examples are only for illustrating the technical solutions of the present invention more clearly, and the protection scope of the present invention is not limited thereby.
Example 1
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The above formula is reacted according to the following steps:
firstly, weighing PLA and lignin in proportion, and uniformly mixing at normal temperature;
and (2) uniformly mixing the weighed DCP, GMA and 1010, adding the mixture of the weighed DCP, GMA and 1010 and a mixture of PLA and lignin into a reaction type extruder, setting the temperature of the extruder to be 150 ℃, setting the rotating speed of a screw to be 400RPM, and extruding and granulating to obtain the PLA-lignin composite material particles.
And (3) performing injection molding on the composite material particles (the injection molding temperature is 160-180 ℃, the injection molding pressure is 40-80MPa, the injection molding speed is 50-150mm/S, the pressure maintaining pressure is 40-50MPa, the pressure maintaining time is 5S, and the cooling time is 15S) to prepare a standard test sample strip for later use.
Example 2
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The above formula is reacted according to the following steps:
firstly, weighing PLA and lignin in proportion, and uniformly mixing at normal temperature;
and (2) uniformly mixing the weighed DCP, GMA and 1010, adding the mixture of the weighed DCP, GMA and 1010 and a mixture of PLA and lignin into a reaction type extruder, setting the temperature of the extruder to be 190 ℃ and the rotating speed of a screw to be 300RPM, and extruding and granulating to obtain the PLA-lignin composite material particles.
The composite particles were injection molded (same injection molding process as in example 1) to prepare a standard test specimen for use.
Example 3
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The above formula is reacted according to the following steps:
firstly, weighing PLA and lignin in proportion, and uniformly mixing at normal temperature;
and (2) uniformly mixing the weighed DCP, GMA and 1010, adding the mixture of the weighed DCP, GMA and 1010 and a mixture of PLA and lignin into a reaction type extruder, setting the temperature of the extruder to be 160 ℃, setting the rotating speed of a screw to be 100RPM, and extruding and granulating to obtain the PLA-lignin composite material particles.
The composite particles were injection molded (same injection molding process as in example 1) to prepare a standard test specimen for use.
Example 4
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The above formula is reacted according to the following steps:
firstly, weighing PLA and lignin in proportion, and uniformly mixing at normal temperature;
and (2) uniformly mixing the weighed DCP, GMA and 1010, adding the mixture of the weighed DCP, GMA and 1010 and a mixture of PLA and lignin into a reaction type extruder, setting the temperature of the extruder at 180 ℃, setting the rotating speed of a screw at 600RPM, and extruding and granulating to obtain the PLA-lignin composite material particles.
The composite particles were injection molded (same injection molding process as in example 1) to prepare a standard test specimen for use.
Example 5
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The above formula is reacted according to the following steps:
firstly, weighing PLA and lignin in proportion, and uniformly mixing at normal temperature;
and (2) uniformly mixing the weighed DCP, GMA and 1010, adding the mixture of the weighed DCP, GMA and 1010 and a mixture of PLA and lignin into a reaction type extruder, setting the temperature of the extruder to be 170 ℃, setting the rotating speed of a screw to be 300RPM, and extruding and granulating to obtain the PLA lignin composite material particles.
The composite particles were injection molded (same injection molding process as in example 1) to prepare a standard test specimen for use.
Tensile strength, elongation at break and impact strength of the samples finally prepared in examples 1 to 5 were measured using an all-purpose electronic tensile testing machine (KY800C, manufactured by kayaku-shi koku corporation) and an electronic impact testing machine (manufactured by shandong anniemai instruments ltd.) using unmodified polylactic acid and unmodified polylactic acid/lignin (simply blended by polylactic acid and lignin) as comparative examples, and the results are shown in table 1:
TABLE 1
The result shows that the PLA-lignin composite material modified by the reactive extrusion method has obviously improved performance.
Example 6
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The reaction procedure for the above formulation and the preparation of standard test bars were the same as in example 1.
Example 7
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The reaction procedure for the above formulation and the preparation of standard test bars were the same as in example 5.
Example 8
A preparation method of a PLA-lignin composite material modified by a reactive extrusion method comprises the following steps of:
wherein the lignin is aromatic high polymer containing structural unit of oxyphenbutamol or its derivatives in molecular structure, and has particle size of 50-500 mesh.
The reaction procedure for the above formulation and the preparation of standard test bars were the same as in example 4.
The performance of the finally prepared samples in the above embodiments 6 to 8 is superior to that of the prior art.
The embodiments of the present invention have been described in detail, but the embodiments are merely examples, and the present invention is not limited to the embodiments described above. Any equivalent modifications and substitutions to those skilled in the art are also within the scope of the present invention. Accordingly, equivalent changes and modifications made without departing from the spirit and scope of the present invention should be covered by the present invention.