CN111808334B - Processing technology of biomass-based composite material for non-woven fabric with high degradability - Google Patents
Processing technology of biomass-based composite material for non-woven fabric with high degradability Download PDFInfo
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- 239000002131 composite material Substances 0.000 title claims abstract description 32
- 239000004745 nonwoven fabric Substances 0.000 title claims abstract description 31
- 239000002028 Biomass Substances 0.000 title claims abstract description 29
- 238000012545 processing Methods 0.000 title claims abstract description 16
- 238000005516 engineering process Methods 0.000 title claims abstract description 14
- 238000002156 mixing Methods 0.000 claims description 68
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims description 62
- 238000003756 stirring Methods 0.000 claims description 47
- 235000013808 oxidized starch Nutrition 0.000 claims description 43
- 239000001254 oxidized starch Substances 0.000 claims description 43
- 239000000126 substance Substances 0.000 claims description 42
- 235000010413 sodium alginate Nutrition 0.000 claims description 37
- 239000000661 sodium alginate Substances 0.000 claims description 37
- 229940005550 sodium alginate Drugs 0.000 claims description 37
- 229920000747 poly(lactic acid) Polymers 0.000 claims description 35
- 239000004626 polylactic acid Substances 0.000 claims description 35
- 239000000203 mixture Substances 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 24
- 235000012424 soybean oil Nutrition 0.000 claims description 22
- 239000003549 soybean oil Substances 0.000 claims description 22
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 20
- 238000001035 drying Methods 0.000 claims description 16
- 238000001914 filtration Methods 0.000 claims description 16
- 229920002518 Polyallylamine hydrochloride Polymers 0.000 claims description 15
- 239000003638 chemical reducing agent Substances 0.000 claims description 15
- 239000011592 zinc chloride Substances 0.000 claims description 10
- 235000005074 zinc chloride Nutrition 0.000 claims description 10
- 238000004458 analytical method Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 7
- 239000012279 sodium borohydride Substances 0.000 claims description 7
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 7
- 229920002472 Starch Polymers 0.000 claims description 6
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 6
- 239000008107 starch Substances 0.000 claims description 6
- 235000019698 starch Nutrition 0.000 claims description 6
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 5
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 229920002261 Corn starch Polymers 0.000 claims description 2
- 240000003183 Manihot esculenta Species 0.000 claims description 2
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims description 2
- 239000008120 corn starch Substances 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims description 2
- 229920002988 biodegradable polymer Polymers 0.000 abstract description 4
- 239000004621 biodegradable polymer Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000004132 cross linking Methods 0.000 description 6
- SEOVTRFCIGRIMH-UHFFFAOYSA-N indole-3-acetic acid Chemical group C1=CC=C2C(CC(=O)O)=CNC2=C1 SEOVTRFCIGRIMH-UHFFFAOYSA-N 0.000 description 6
- 238000005457 optimization Methods 0.000 description 6
- 230000015556 catabolic process Effects 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 238000006731 degradation reaction Methods 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002861 polymer material Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 235000012239 silicon dioxide Nutrition 0.000 description 3
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 230000008034 disappearance Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 239000005543 nano-size silicon particle Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 229920001059 synthetic polymer Polymers 0.000 description 2
- 235000016068 Berberis vulgaris Nutrition 0.000 description 1
- 241000335053 Beta vulgaris Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 125000003172 aldehyde group Chemical group 0.000 description 1
- 229920003232 aliphatic polyester Polymers 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- -1 clothing Substances 0.000 description 1
- 229920000891 common polymer Polymers 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001938 differential scanning calorimetry curve Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000003856 thermoforming Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L3/00—Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
- C08L3/04—Starch derivatives, e.g. crosslinked derivatives
- C08L3/10—Oxidised starch
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
- D01F8/14—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/18—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from other substances
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/16—Halogen-containing compounds
- C08K2003/168—Zinc halides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/011—Nanostructured additives
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/06—Biodegradable
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/08—Stabilised against heat, light or radiation or oxydation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/12—Applications used for fibers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2312/00—Crosslinking
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Health & Medical Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Toxicology (AREA)
- Biological Depolymerization Polymers (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The invention discloses a processing technology of a biomass-based composite material for non-woven fabrics with high degradability, which belongs to the technical field of biodegradable polymer composite materials. The biomass-based composite material for the non-woven fabric with high degradability, which is prepared by the invention, has better heat resistance, excellent flexibility and better degradability, and is suitable for manufacturing the non-woven fabric.
Description
Technical Field
The invention relates to the technical field of composite materials for non-woven fabrics, in particular to a processing technology of a biomass-based composite material with high degradability for non-woven fabrics.
Background
With the progress of technology and the development of human civilization, polymer material products such as plastic bags, cutlery boxes, medical and a series of plastic products in daily life are continuously produced and become waste.
Since the beginning of the 20 th century, a great deal of application of synthetic polymer materials has caused serious environmental pollution, and the search and application of novel polymer materials friendly to the environment have received wide attention from all countries of the world. Under this situation, biodegradable polymer materials rapidly develop. The practice proves that the biodegradable polymer material is different from the common synthetic polymer material, has two characteristics of biological source and biodegradability, can reduce environmental pollution, save petroleum resources and reduce the global warming effect, and is widely applied to industry. Taking polylactic acid as an example, the monomer of the polylactic acid is lactic acid, is a biodegradable polymer prepared from renewable plant resources such as corn, beet and the like through a chemical synthesis method, belongs to thermoplastic aliphatic polyester, is in a glass state at normal temperature, has a glass transition temperature and a melting point of about 60 ℃ and 170 ℃ respectively, and has similar performance to polystyrene. The polylactic acid can be extruded, injection molded, blow molded, thermoformed and other molding processing on general equipment like common polymers, and the produced films, sheets and fibers are subjected to thermoforming, spinning and other secondary processing to obtain products, so that the polylactic acid can be widely applied to the fields of textiles, clothing, non-woven fabrics, packaging, agriculture, forestry, civil construction, medical and health products, living goods and the like.
However, the traditional polylactic acid product has the disadvantages that the polylactic acid cannot be popularized due to higher production cost of the polylactic acid, and the polylactic acid product has poor heat resistance and crisp texture, so that research and development of a biomass-based composite material for non-woven fabrics, which has low cost and good heat resistance, flexibility and degradability, are urgently needed.
Disclosure of Invention
The invention aims to provide a biomass-based composite material with high degradability for non-woven fabrics and a processing technology thereof, so as to solve the problems in the prior art.
In order to achieve the above purpose, the present invention provides the following technical solutions:
the biomass-based composite material for the non-woven fabric with high degradability is characterized by mainly comprising the following raw material components in parts by weight: 8-12 parts of polylactic acid, 5-8 parts of epoxidized soybean oil, 1-2 parts of catalyst and 15-18 parts of oxidized starch; the epoxidized soybean oil can play a role of a plasticizer after being added into the product, thereby improving the flexibility of the product.
The biomass-based composite material for the non-woven fabric with high degradability is characterized by further comprising the following raw material components in parts by weight: 3-6 parts of polyallylamine hydrochloride and 8-10 parts of modified sodium alginate, wherein the addition of the polyallylamine hydrochloride can form a crosslinked network with oxidized starch in the product, so that the crosslinking density of the product is improved, and the flexibility and the tensile strength of the product are improved.
As optimization, the polylactic acid is polylactic acid with molecular weight of 80000-120000, the catalyst is any one of zinc chloride or magnesium chloride, and the added catalyst can play a role of filler, so that the tensile property of the product is improved.
As optimization, the oxidized starch is prepared by oxidizing starch with hydrogen peroxide, and the starch is any one of tapioca starch and corn starch.
As optimization, the modified sodium alginate is prepared by mixing sodium alginate and nano silicon dioxide and then treating the mixture by a silane coupling agent KH-550, and the addition of the modified sodium alginate can play a role in filling filler into the pore structure of a product, so that the heat resistance of the product is improved, and the crosslinking density of the product is further improved, so that the flexibility of the product is improved.
As optimization, the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following raw material components in parts by weight: 8 parts of polylactic acid, 6 parts of epoxidized soybean oil, 2 parts of zinc chloride, 16 parts of oxidized starch, 3 parts of polyallylamine hydrochloride and 8 parts of modified sodium alginate.
As optimization, the processing technology of the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following steps:
(1) Mixing sodium alginate and ethyl orthosilicate for reaction, and then defoaming in vacuum;
(2) Mixing the substance obtained in the step (1) with a silane coupling agent KH-550, extruding, filtering and drying to obtain modified sodium alginate;
(3) Mixing polylactic acid and epoxidized soybean oil, adding a catalyst, and stirring and mixing;
(4) Mixing oxidized starch with polyallylamine hydrochloride, adding water and the substance obtained in the step (2), regulating the pH value, stirring for reaction, adding a reducing agent, continuing the reaction, filtering and drying;
(5) Mixing the substance obtained in the step (3) with the substance obtained in the step (4), mixing and granulating;
(6) And (5) performing index analysis on the substance obtained in the step (5).
As optimization, the processing technology of the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following steps:
(1) Sodium alginate and water are mixed according to the mass ratio of 1: 50-1: 55, adding ethyl orthosilicate with the mass of 2-4 times of sodium alginate and absolute ethyl alcohol with the mass of 5-10 times of sodium alginate, stirring and mixing, adding ammonia water with the mass of 20-25 times of sodium alginate, stirring and reacting, and then vacuum defoaming;
(2) Mixing the substance obtained in the step (1) with a silane coupling agent KH-550 according to a mass ratio of 10:1 to 12:1, adding water with the mass of 2-3 times of that of a silane coupling agent KH-550, stirring and mixing to obtain a pre-modified sodium alginate mixture, extruding the pre-modified sodium alginate mixture into a calcium chloride solution with the mass fraction of 2% through an extruder, filtering and drying to obtain modified sodium alginate;
(3) Polylactic acid and epoxidized soybean oil are mixed according to the mass ratio of 1: 1-2: 1, adding zinc chloride with the mass of 0.1 to 0.3 times of that of the polylactic acid, and stirring and mixing;
(4) Oxidized starch and polyallylamine hydrochloride are mixed according to the mass ratio of 5:1 to 8:1 mixing in a beaker, adding a substance obtained in the step (2) with the mass of 0.5-0.6 times of that of oxidized starch and water with the mass of 4-8 times of that of oxidized starch into the beaker, stirring and mixing, adjusting the pH value of the material in the beaker to 9.8-10.0, stirring and reacting for 2-3 hours, adding a reducing agent with the mass of 0.1-0.2 times of that of oxidized starch into the beaker, stirring and reacting, filtering, and drying;
(5) Mixing the substance obtained in the step (3) with the substance obtained in the step (4) according to the mass ratio of 1.0:1.8-1.0:2.0, mixing under a closed condition, and granulating;
(6) And (5) performing index analysis on the substance obtained in the step (5).
Preferably, the reducing agent in the step (4) is any one of sodium borohydride or potassium borohydride.
Compared with the prior art, the invention has the beneficial effects that: according to the invention, oxidized starch and polyallylamine hydrochloride are added into a product when the biomass-based composite material for the non-woven fabric with high degradability is prepared, and modified sodium alginate is added at the same time, firstly, the oxidized starch contains aldehyde groups and can react with amino groups in the polyallylamine hydrochloride to form crosslinking, so that after the oxidized starch is added into the product, the internal crosslinking network of the product can be enriched, the flexibility of the product is improved, and after the crosslinking network is enriched, the heat resistance of the product can be improved, namely the crystallization temperature of the product is improved; in addition, the addition of polylactic acid is reduced in the preparation process of the product, so that the cost of the product is greatly reduced, and the popularization of the product is improved.
Detailed Description
The technical solutions of the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention, and it is apparent that the described embodiments are only some embodiments of the present invention, not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
In order to more clearly illustrate the method provided by the invention, the following examples are used for describing in detail the methods for testing various indexes of the biomass-based composite material for non-woven fabrics with high degradability, which are prepared in the following examples, as follows:
crystallization temperature: taking 5mg of the biomass-based composite material with high degradability for the non-woven fabric, which is obtained in each example, heating the composite material to 200 ℃ from room temperature at 5 ℃/min under nitrogen atmosphere on a differential scanning calorimeter calibrated by indium, tin and zinc, and preserving heat for 5min; then 5 ℃/min is used for reducing the temperature from 200 ℃ to 30 ℃, a DSC curve is recorded, and the peak temperature on the temperature reduction curve is taken as the crystallization temperature;
mechanical properties: the high-degradability biomass-based composite material for the non-woven fabric obtained in each embodiment is added into a miniature injection molding machine to be molded into test strips required by mechanical property test, wherein the injection molding temperature is 200 ℃, the mold temperature is 40 ℃, and the injection pressure is 0.5MPa. The microcomputer is used for controlling an electronic universal tester and a cantilever beam impact tester to test the mechanical properties of the test strip, and the tensile strength is measured according to GB/T1040.1; flexural modulus was measured according to GB/T9341.
Degradability: the biomass-based composite material for nonwoven fabric having high degradability obtained in each example was left naturally for 30 days, and the degradation rate was measured.
Example 1:
the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following raw materials in parts by weight: 8 parts of polylactic acid, 6 parts of epoxidized soybean oil, 2 parts of zinc chloride, 16 parts of oxidized starch, 3 parts of polyallylamine hydrochloride and 8 parts of modified sodium alginate;
a processing technology of a biomass-based composite material for non-woven fabrics with high degradability, which mainly comprises the following steps:
(1) Sodium alginate and water are mixed according to the mass ratio of 1:55, adding ethyl orthosilicate with the mass of 4 times of sodium alginate and absolute ethyl alcohol with the mass of 10 times of sodium alginate into the mixture of sodium alginate and water, stirring and mixing for 30min at the temperature of 30 ℃ and the rotating speed of 300r/min, adding ammonia water with the mass of 25 times of sodium alginate into the mixture of sodium alginate and water, stirring and reacting for 3h at the temperature of 50 ℃ and the rotating speed of 350r/min, and then defoaming in vacuum;
(2) Mixing the substance obtained in the step (1) with a silane coupling agent KH-550 according to a mass ratio of 12:1, mixing, adding water 3 times the mass of the silane coupling agent KH-550 into the mixture of the substance obtained in the step (1) and the silane coupling agent KH-550, stirring and mixing for 2 hours at the temperature of 40 ℃ and the rotating speed of 250r/min to obtain a pre-modified sodium alginate mixture, extruding the pre-modified sodium alginate mixture into a calcium chloride solution with the mass fraction of 2% by an extruder, standing for 3 hours, filtering, and drying to obtain modified sodium alginate;
(3) Polylactic acid and epoxidized soybean oil are mixed according to a mass ratio of 2:1, mixing, adding zinc chloride with the mass of 0.3 times of that of the polylactic acid into the mixture of the polylactic acid and the epoxidized soybean oil, and stirring and mixing;
(4) Oxidized starch and polyallylamine hydrochloride are mixed according to the mass ratio of 8:1 mixing in a beaker, adding a substance obtained in the step (2) with the mass of 0.6 times of that of oxidized starch and water with the mass of 8 times of that of the oxidized starch into the beaker, stirring and mixing for 1h at the temperature of 30 ℃ and the rotating speed of 350r/min, regulating the pH value of the material in the beaker to 10.0, continuing stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, adding a reducing agent with the mass of 0.2 times of that of the oxidized starch into the beaker, stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, filtering and drying;
(5) Mixing the substance obtained in the step (3) with the substance obtained in the step (4) according to the mass ratio of 1.0:1.8, mixing under a closed condition, and granulating;
(6) And (5) performing index analysis on the substance obtained in the step (5).
Preferably, the reducing agent in the step (4) is sodium borohydride.
Example 2:
the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following raw materials in parts by weight: 8 parts of polylactic acid, 6 parts of epoxidized soybean oil, 2 parts of zinc chloride, 16 parts of oxidized starch and 8 parts of modified sodium alginate;
a processing technology of a biomass-based composite material for non-woven fabrics with high degradability, which mainly comprises the following steps:
(1) Sodium alginate and water are mixed according to the mass ratio of 1:55, adding ethyl orthosilicate with the mass of 4 times of sodium alginate and absolute ethyl alcohol with the mass of 10 times of sodium alginate into the mixture of sodium alginate and water, stirring and mixing for 30min at the temperature of 30 ℃ and the rotating speed of 300r/min, adding ammonia water with the mass of 25 times of sodium alginate into the mixture of sodium alginate and water, stirring and reacting for 3h at the temperature of 50 ℃ and the rotating speed of 350r/min, and then defoaming in vacuum;
(2) Mixing the substance obtained in the step (1) with a silane coupling agent KH-550 according to a mass ratio of 12:1, mixing, adding water 3 times the mass of the silane coupling agent KH-550 into the mixture of the substance obtained in the step (1) and the silane coupling agent KH-550, stirring and mixing for 2 hours at the temperature of 40 ℃ and the rotating speed of 250r/min to obtain a pre-modified sodium alginate mixture, extruding the pre-modified sodium alginate mixture into a calcium chloride solution with the mass fraction of 2% by an extruder, standing for 3 hours, filtering, and drying to obtain modified sodium alginate;
(3) Polylactic acid and epoxidized soybean oil are mixed according to a mass ratio of 2:1, mixing, adding zinc chloride with the mass of 0.3 times of that of the polylactic acid into the mixture of the polylactic acid and the epoxidized soybean oil, and stirring and mixing;
(4) Adding oxidized starch into a beaker, adding a substance obtained in the step (2) with the mass 0.6 times of that of the oxidized starch and water with the mass 8 times of that of the oxidized starch into the beaker, stirring and mixing for 1h at the temperature of 30 ℃ and the rotating speed of 350r/min, adjusting the pH value of the material in the beaker to 10.0, continuing stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, adding a reducing agent with the mass 0.2 times of that of the oxidized starch into the beaker, stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, filtering and drying;
(5) Mixing the substance obtained in the step (3) with the substance obtained in the step (4) according to the mass ratio of 1.0:1.8, mixing under a closed condition, and granulating;
(6) And (5) performing index analysis on the substance obtained in the step (5).
Preferably, the reducing agent in the step (4) is sodium borohydride.
Example 3:
the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following raw materials in parts by weight: 8 parts of polylactic acid, 6 parts of epoxidized soybean oil, 2 parts of zinc chloride, 16 parts of oxidized starch, 3 parts of polyallylamine hydrochloride and 8 parts of sodium alginate;
a processing technology of a biomass-based composite material for non-woven fabrics with high degradability, which mainly comprises the following steps:
(1) Sodium alginate and a silane coupling agent KH-550 are mixed according to a mass ratio of 12:1, adding 3 times of water by mass of a silane coupling agent KH-550 and 1 time of calcium chloride by mass of the silane coupling agent KH-550 into a mixture of sodium alginate and the silane coupling agent KH-550, stirring and mixing for 2 hours at the temperature of 40 ℃ and the rotating speed of 250r/min, filtering and drying;
(2) Polylactic acid and epoxidized soybean oil are mixed according to a mass ratio of 2:1, mixing, adding zinc chloride with the mass of 0.3 times of that of the polylactic acid into the mixture of the polylactic acid and the epoxidized soybean oil, and stirring and mixing;
(3) Oxidized starch and polyallylamine hydrochloride are mixed according to the mass ratio of 8:1 mixing in a beaker, adding a substance obtained in the step (1) with the mass of 0.6 times of the mass of oxidized starch and water with the mass of 8 times of the mass of oxidized starch into the beaker, stirring and mixing for 1h at the temperature of 30 ℃ and the rotating speed of 350r/min, adjusting the pH value of the material in the beaker to 10.0, continuing stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, adding a reducing agent with the mass of 0.2 times of the mass of oxidized starch into the beaker, stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, filtering and drying;
(4) Mixing the substance obtained in the step (2) with the substance obtained in the step (3) according to the mass ratio of 1.0:1.8, mixing under a closed condition, and granulating;
(5) And (3) performing index analysis on the substance obtained in the step (4).
Preferably, the reducing agent in the step (3) is sodium borohydride.
Example 4:
the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following raw materials in parts by weight: 8 parts of polylactic acid, 6 parts of epoxidized soybean oil, 16 parts of oxidized starch, 3 parts of polyallylamine hydrochloride and 8 parts of modified sodium alginate;
a processing technology of a biomass-based composite material for non-woven fabrics with high degradability, which mainly comprises the following steps:
(1) Sodium alginate and water are mixed according to the mass ratio of 1:55, adding ethyl orthosilicate with the mass of 4 times of sodium alginate and absolute ethyl alcohol with the mass of 10 times of sodium alginate into the mixture of sodium alginate and water, stirring and mixing for 30min at the temperature of 30 ℃ and the rotating speed of 300r/min, adding ammonia water with the mass of 25 times of sodium alginate into the mixture of sodium alginate and water, stirring and reacting for 3h at the temperature of 50 ℃ and the rotating speed of 350r/min, and then defoaming in vacuum;
(2) Mixing the substance obtained in the step (1) with a silane coupling agent KH-550 according to a mass ratio of 12:1, mixing, adding water 3 times the mass of the silane coupling agent KH-550 into the mixture of the substance obtained in the step (1) and the silane coupling agent KH-550, stirring and mixing for 2 hours at the temperature of 40 ℃ and the rotating speed of 250r/min to obtain a pre-modified sodium alginate mixture, extruding the pre-modified sodium alginate mixture into a calcium chloride solution with the mass fraction of 2% by an extruder, standing for 3 hours, filtering, and drying to obtain modified sodium alginate;
(3) Polylactic acid and epoxidized soybean oil are mixed according to a mass ratio of 2:1, mixing, stirring and mixing;
(4) Oxidized starch and polyallylamine hydrochloride are mixed according to the mass ratio of 8:1 mixing in a beaker, adding a substance obtained in the step (2) with the mass of 0.6 times of that of oxidized starch and water with the mass of 8 times of that of the oxidized starch into the beaker, stirring and mixing for 1h at the temperature of 30 ℃ and the rotating speed of 350r/min, regulating the pH value of the material in the beaker to 10.0, continuing stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, adding a reducing agent with the mass of 0.2 times of that of the oxidized starch into the beaker, stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, filtering and drying;
(5) Mixing the substance obtained in the step (3) with the substance obtained in the step (4) according to the mass ratio of 1.0:1.8, mixing under a closed condition, and granulating;
(6) And (5) performing index analysis on the substance obtained in the step (5).
Preferably, the reducing agent in the step (4) is sodium borohydride.
Comparative example:
the biomass-based composite material for the non-woven fabric with high degradability mainly comprises the following raw materials in parts by weight: 8 parts of polylactic acid, 6 parts of epoxidized soybean oil, 16 parts of oxidized starch and 8 parts of sodium alginate;
a processing technology of a biomass-based composite material for non-woven fabrics with high degradability, which mainly comprises the following steps:
(1) Sodium alginate and a silane coupling agent KH-550 are mixed according to a mass ratio of 12:1, adding 3 times of water by mass of a silane coupling agent KH-550 and 1 time of calcium chloride by mass of the silane coupling agent KH-550 into a mixture of sodium alginate and the silane coupling agent KH-550, stirring and mixing for 2 hours at the temperature of 40 ℃ and the rotating speed of 250r/min, filtering and drying;
(2) Polylactic acid and epoxidized soybean oil are mixed according to a mass ratio of 2:1, mixing, stirring and mixing;
(3) Adding oxidized starch into a beaker, adding a substance obtained in the step (1) with the mass 0.6 times of that of the oxidized starch and water with the mass 8 times of that of the oxidized starch into the beaker, stirring and mixing for 1h at the temperature of 30 ℃ and the rotating speed of 350r/min, adjusting the pH value of the material in the beaker to 10.0, continuing stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, adding a reducing agent with the mass 0.2 times of that of the oxidized starch into the beaker, stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, filtering and drying;
(4) Mixing the substance obtained in the step (2) with the substance obtained in the step (3) according to the mass ratio of 1.0:1.8, mixing under a closed condition, and granulating;
(5) And (3) performing index analysis on the substance obtained in the step (4).
Preferably, the reducing agent in the step (3) is sodium borohydride.
Effect example:
table 1 below gives the results of index analysis of the biomass-based composite materials having high degradability and the processing processes thereof using examples 1 to 4 and comparative examples of the present invention.
TABLE 1
Tensile strength (MPa) | Flexural Strength (MPa) | Crystallization temperature (. Degree. C.) | Degradation rate (%) | |
Example 1 | 72.0 | 5000 | 145 | 68 |
Example 2 | 68.8 | 4763 | 132 | 69 |
Example 3 | 65.3 | 4338 | 112 | 70 |
Example 4 | 64.3 | 4225 | 118 | 69 |
Comparative example | 33.4 | 2831 | 90.3 | 62 |
As can be seen from the experimental data in Table 1, compared with the comparative example, the product prepared by the invention has better heat resistance and flexibility, and the degradation performance is improved, and as can be seen from the comparison of the example 1 and the example 2, when the polyallylamine hydrochloride is not added into the product, the crosslinking density in the product is reduced, the hydrophilic group of oxidized starch is exposed, so that the mechanical property and heat resistance of the product are reduced, but the degradation performance of the product is improved; from comparison of example 1 and example 3, it can be found that when sodium alginate added into the product is not modified, pores of a crosslinked network in the product cannot be filled due to disappearance of nano silicon dioxide, so that degradation performance of the product is improved, and epoxy soybean oil only plays a role of a plasticizer in the product due to disappearance of silicon dioxide, and a new crosslinked network is not formed, so that heat resistance and flexibility of the product are reduced; as can be seen from a comparison of example 1 and example 4, when no catalyst was added to the product, the epoxidized soybean oil could not form a better crosslink with the modified sodium alginate, thereby reducing the heat resistance and flexibility of the product.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein.
Claims (1)
1. A processing technology of a biomass-based composite material for non-woven fabrics with high degradability mainly comprises the following steps:
(1) Sodium alginate and water are mixed according to the mass ratio of 1:55, adding ethyl orthosilicate with the mass of 4 times of sodium alginate and absolute ethyl alcohol with the mass of 10 times of sodium alginate into the mixture of sodium alginate and water, stirring and mixing for 30min at the temperature of 30 ℃ and the rotating speed of 300r/min, adding ammonia water with the mass of 25 times of sodium alginate into the mixture of sodium alginate and water, stirring and reacting for 3h at the temperature of 50 ℃ and the rotating speed of 350r/min, and then defoaming in vacuum;
(2) Mixing the substance obtained in the step (1) with a silane coupling agent KH-550 according to a mass ratio of 12:1, mixing, adding water 3 times the mass of the silane coupling agent KH-550 into the mixture of the substance obtained in the step (1) and the silane coupling agent KH-550, stirring and mixing for 2 hours at the temperature of 40 ℃ and the rotating speed of 250r/min to obtain a pre-modified sodium alginate mixture, extruding the pre-modified sodium alginate mixture into a calcium chloride solution with the mass fraction of 2% by an extruder, standing for 3 hours, filtering, and drying to obtain modified sodium alginate;
(3) Polylactic acid and epoxidized soybean oil are mixed according to a mass ratio of 2:1, mixing, adding zinc chloride with the mass of 0.3 times of that of the polylactic acid into the mixture of the polylactic acid and the epoxidized soybean oil, and stirring and mixing;
(4) Oxidized starch and polyallylamine hydrochloride are mixed according to the mass ratio of 8:1 mixing in a beaker, adding a substance obtained in the step (2) with the mass of 0.6 times of that of oxidized starch and water with the mass of 8 times of that of the oxidized starch into the beaker, stirring and mixing for 1h at the temperature of 30 ℃ and the rotating speed of 350r/min, regulating the pH value of the material in the beaker to 10.0, continuing stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, adding a reducing agent with the mass of 0.2 times of that of the oxidized starch into the beaker, stirring and reacting for 3h at the temperature of 60 ℃ and the rotating speed of 300r/min, filtering and drying;
(5) Mixing the substance obtained in the step (3) with the substance obtained in the step (4) according to the mass ratio of 1.0:1.8, mixing under a closed condition, and granulating;
(6) Performing index analysis on the substance obtained in the step (5);
the reducing agent in the step (4) is sodium borohydride;
the oxidized starch in the step (4) is prepared by oxidizing starch with hydrogen peroxide, wherein the starch is any one of tapioca starch and corn starch.
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CN103223302A (en) * | 2013-05-21 | 2013-07-31 | 中国海洋大学 | Preparation method of self-assembly covalent cross-linked sodium filter membrane |
CN104894865A (en) * | 2015-06-24 | 2015-09-09 | 安徽皖翎羽绒制品有限公司 | Deodorant and breathable feather-down composite heat-insulating material and making method thereof |
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