CN108587208A - A kind of method that GT plasticising DMSO/TEAC systems dissolving wood powder prepares injection grade bio-based plastics - Google Patents
A kind of method that GT plasticising DMSO/TEAC systems dissolving wood powder prepares injection grade bio-based plastics Download PDFInfo
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- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 title claims abstract description 86
- 239000002023 wood Substances 0.000 title claims abstract description 57
- YMBCJWGVCUEGHA-UHFFFAOYSA-M tetraethylammonium chloride Chemical compound [Cl-].CC[N+](CC)(CC)CC YMBCJWGVCUEGHA-UHFFFAOYSA-M 0.000 title claims abstract description 53
- 239000000843 powder Substances 0.000 title claims abstract description 37
- 239000004033 plastic Substances 0.000 title claims abstract description 26
- 229920003023 plastic Polymers 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 24
- 238000002347 injection Methods 0.000 title description 5
- 239000007924 injection Substances 0.000 title description 5
- URAYPUMNDPQOKB-UHFFFAOYSA-N triacetin Chemical compound CC(=O)OCC(OC(C)=O)COC(C)=O URAYPUMNDPQOKB-UHFFFAOYSA-N 0.000 claims abstract description 48
- 239000000047 product Substances 0.000 claims abstract description 42
- 235000013773 glyceryl triacetate Nutrition 0.000 claims abstract description 24
- 229960002622 triacetin Drugs 0.000 claims abstract description 24
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000002994 raw material Substances 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000000967 suction filtration Methods 0.000 claims abstract description 8
- 230000008569 process Effects 0.000 claims abstract description 5
- 239000012467 final product Substances 0.000 claims abstract description 3
- 239000002245 particle Substances 0.000 claims abstract description 3
- 235000013312 flour Nutrition 0.000 claims description 17
- 239000001087 glyceryl triacetate Substances 0.000 claims description 16
- 239000002904 solvent Substances 0.000 claims description 12
- 238000001746 injection moulding Methods 0.000 claims description 10
- 238000001125 extrusion Methods 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- 238000000498 ball milling Methods 0.000 claims description 5
- 239000002029 lignocellulosic biomass Substances 0.000 claims description 5
- 239000000243 solution Substances 0.000 claims description 5
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 4
- 230000004048 modification Effects 0.000 claims description 4
- 238000012986 modification Methods 0.000 claims description 4
- 239000010902 straw Substances 0.000 claims description 4
- 241000609240 Ambelania acida Species 0.000 claims description 2
- 235000008708 Morus alba Nutrition 0.000 claims description 2
- 240000000249 Morus alba Species 0.000 claims description 2
- 240000007594 Oryza sativa Species 0.000 claims description 2
- 235000007164 Oryza sativa Nutrition 0.000 claims description 2
- 235000014676 Phragmites communis Nutrition 0.000 claims description 2
- 235000019270 ammonium chloride Nutrition 0.000 claims description 2
- 239000010905 bagasse Substances 0.000 claims description 2
- 239000010903 husk Substances 0.000 claims description 2
- 238000010907 mechanical stirring Methods 0.000 claims description 2
- 239000002244 precipitate Substances 0.000 claims description 2
- 235000009566 rice Nutrition 0.000 claims description 2
- 231100000252 nontoxic Toxicity 0.000 claims 1
- 230000003000 nontoxic effect Effects 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 235000012438 extruded product Nutrition 0.000 description 16
- 229920002678 cellulose Polymers 0.000 description 14
- 239000001913 cellulose Substances 0.000 description 14
- 239000002131 composite material Substances 0.000 description 12
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 10
- 238000002441 X-ray diffraction Methods 0.000 description 7
- 229920002522 Wood fibre Polymers 0.000 description 6
- 238000005452 bending Methods 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 239000002025 wood fiber Substances 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 235000002020 sage Nutrition 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- 238000007385 chemical modification Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000001878 scanning electron micrograph Methods 0.000 description 3
- 229920002488 Hemicellulose Polymers 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000002329 infrared spectrum Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 1
- 125000002777 acetyl group Chemical group [H]C([H])([H])C(*)=O 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 238000006266 etherification reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000012978 lignocellulosic material Substances 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 238000000520 microinjection Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- CBXCPBUEXACCNR-UHFFFAOYSA-N tetraethylammonium Chemical compound CC[N+](CC)(CC)CC CBXCPBUEXACCNR-UHFFFAOYSA-N 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
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- 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
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/10—Esters; Ether-esters
- C08K5/101—Esters; Ether-esters of monocarboxylic acids
- C08K5/103—Esters; Ether-esters of monocarboxylic acids with polyalcohols
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08H—DERIVATIVES OF NATURAL MACROMOLECULAR COMPOUNDS
- C08H8/00—Macromolecular compounds derived from lignocellulosic materials
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
- C08J3/09—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
- C08J3/091—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids characterised by the chemical constitution of the organic liquid
- C08J3/097—Sulfur containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2397/00—Characterised by the use of lignin-containing materials
- C08J2397/02—Lignocellulosic material, e.g. wood, straw or bagasse
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Polymers & Plastics (AREA)
- Medicinal Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Biochemistry (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
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- Compositions Of Macromolecular Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
Abstract
本发明公开了一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,包括以下步骤:(1)取木质纤维原料进行粉碎,再采用行星球磨机对其进行球磨处理,得到的球磨木粉置于干燥器中备用;(2)将球磨木粉加入二甲亚砜/四乙基氯化铵溶液中,恒温水浴中机械搅拌一定时间,加入丙酮,抽滤析出产物,将产物置于烘箱中烘至恒重得到溶解改性产物;(3)将溶解改性产物和三乙酸甘油酯于双螺杆挤出机中共混循环挤出,造粒即得最终产物木质纤维生物基塑料粒子。本发明工艺简单,不需化学反应,原料分布广泛,绿色环保,得到的注塑级生物基塑料力学性能较佳,为实现农林废弃物资源化利用奠定了一定的基础。
The invention discloses a method for preparing injection-grade bio-based plastics by using GT plasticized DMSO/TEAC system to dissolve wood powder. The obtained ball-ground wood powder is placed in a desiccator for subsequent use; (2) the ball-ground wood powder is added in dimethyl sulfoxide/tetraethylammonium chloride solution, mechanically stirred for a certain period of time in a constant temperature water bath, acetone is added, and the product is separated out by suction filtration, The product is placed in an oven and dried to a constant weight to obtain a dissolved modified product; (3) the dissolved modified product and glycerol triacetate are blended and circulated in a twin-screw extruder, and pelletized to obtain the final product lignocellulosic bio base plastic particles. The invention has the advantages of simple process, no chemical reaction, wide distribution of raw materials, environmental protection, better mechanical properties of the obtained injection-grade bio-based plastics, and lays a certain foundation for realizing resource utilization of agricultural and forestry wastes.
Description
技术领域technical field
本发明属于生物基塑料开发技术领域,涉及一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法。The invention belongs to the technical field of bio-based plastics development, and relates to a method for preparing injection-grade bio-based plastics by dissolving wood powder using a GT plasticized DMSO/TEAC system.
背景技术Background technique
随着社会不断发展,生产生活所需要的石化资源的日渐匮乏,和石化资源产生的一系列环境问题,迫切需要寻找一类能代替石化资源的可再生资源。木质纤维作为一种丰富的可再生资源,越来越受到研究者的关注和重视,由木质纤维开发生物基复合材料也成为材料产业的新方向。With the continuous development of society, the petrochemical resources needed for production and life are increasingly scarce, and a series of environmental problems caused by petrochemical resources, it is urgent to find a type of renewable resources that can replace petrochemical resources. As a rich renewable resource, wood fiber has attracted more and more attention and attention from researchers, and the development of bio-based composite materials from wood fiber has become a new direction of the material industry.
我国是一个农业大国,每年产生的农林废弃物如秸秆、木材边角料等木质纤维约有9亿吨。而且这些木质纤维类生物质可以不断再生,这是21世纪可被人类利用的最丰富的可再生绿色资源。因此,将秸秆、林木等木质纤维类生物质制成生物基塑料具有良好的前景。目前,对生物质原料的利用基本集中在复合材料领域,许多学者研究木质纤维原料与高分子复合新材料及界面改性等,制备的材料是生物质与高分子复合材料,生物质含量不高。my country is a large agricultural country, and the annual production of agricultural and forestry wastes such as straw, wood scraps and other wood fibers is about 900 million tons. Moreover, these lignocellulosic biomass can be continuously regenerated, which is the most abundant renewable green resource that can be utilized by human beings in the 21st century. Therefore, it has a good prospect to make bio-based plastics from lignocellulosic biomass such as straw and forest trees. At present, the utilization of biomass raw materials is basically concentrated in the field of composite materials. Many scholars study lignocellulosic raw materials and polymer composite materials and interface modification. The materials prepared are biomass and polymer composite materials, and the biomass content is not high. .
化学改性可使木质纤维材料转化为具有热塑性的新型高分子材料,如酯化、醚化、接枝共聚等,不过其代价是化学改性造成的分子结构变化使材料丧失了某些固有的优良属性,同时成本很高,至今未能实现产业化。Chemical modification can transform lignocellulosic materials into thermoplastic new polymer materials, such as esterification, etherification, graft copolymerization, etc., but at the cost of molecular structure changes caused by chemical modification, the material loses some inherent properties. Excellent properties, but at the same time the cost is very high, so far it has not been industrialized.
最近几年,国际上在对木质纤维素进行结构鉴定、化学改性和高效利用时提出了一种全新的研究体系一木质纤维素全溶体系。该体系的特点是能破坏木质纤维素分子内及分子间的氢键,从而导致其溶解。木质纤维不能进行热塑性加工的主要原因就是木质纤维中的纤维素分子内及分子间的氢键。DMSO/TEAC体系作为一种良好的纤维素溶剂体系经常被报道,四乙基氯化铵中的四乙基氨基离子[(C2H5)4N+]可以与纤维素链结合,从而屏蔽纤维素分子内与分子间的氢键作用。In recent years, a new research system—lignocellulose total soluble system—was proposed in the world for structural identification, chemical modification and efficient utilization of lignocellulose. The characteristic of this system is that it can break the hydrogen bonds in lignocellulose molecules and between molecules, thereby causing its dissolution. The main reason why wood fiber cannot be thermoplastically processed is the hydrogen bond in the cellulose molecule and between molecules in wood fiber. The DMSO/TEAC system is often reported as a good cellulose solvent system, and the tetraethylammonium ion [(C 2 H 5 ) 4 N + ] in tetraethylammonium chloride can combine with the cellulose chain, thereby shielding Intramolecular and intermolecular hydrogen bonding of cellulose.
发明内容Contents of the invention
发明目的:针对现有技术中存在的不足,本发明的目的是提供了一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,降低改性成本,实现农林废弃物的资源化利用。Purpose of the invention: Aiming at the deficiencies in the prior art, the purpose of the invention is to provide a method for preparing injection-grade bio-based plastics by dissolving wood powder using GT plasticized DMSO/TEAC system, reducing the cost of modification and realizing the reduction of agricultural and forestry wastes. resource utilization.
技术方案:为了实现上述发明目的,本发明采用的技术方案为:Technical solution: In order to realize the above-mentioned purpose of the invention, the technical solution adopted in the present invention is:
一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,包括以下步骤:A kind of method utilizing GT plasticized DMSO/TEAC system to dissolve wood powder to prepare injection-grade bio-based plastics, comprises the following steps:
1)取木质纤维原料进行粉碎,再采用行星球磨机对其进行球磨处理,得到的球磨木粉置于干燥器中备用;1) Take lignocellulosic raw material and pulverize it, then adopt planetary ball mill to carry out ball milling process to it, and the ball milled wood powder obtained is placed in drier for subsequent use;
2)将球磨木粉加入四乙基氯化铵/二甲亚砜溶剂体系中,恒温水浴中机械搅拌一定时间后,加入丙酮,抽滤后析出产物,将产物置于烘箱中烘至恒重得到改性产物;2) Add the ground wood powder into the tetraethylammonium chloride/dimethyl sulfoxide solvent system, stir mechanically in a constant temperature water bath for a certain period of time, add acetone, and precipitate the product after suction filtration, put the product in an oven and dry it to constant weight obtain modified products;
3)将改性产物和三乙酸甘油酯于双螺杆挤出机中共混循环后挤出,造粒即得最终产物木质纤维生物基塑料粒子。3) The modified product and glycerol triacetate are blended and circulated in a twin-screw extruder, extruded, and granulated to obtain the final product lignocellulosic bio-based plastic particles.
步骤1)中所述的木质纤维原料包含有木材、胡桑枝条、芦苇、稻壳、秸秆和甘蔗渣等一切木质纤维类生物质。The lignocellulosic raw material described in step 1) includes all lignocellulosic biomass such as wood, mulberry branch, reed, rice husk, straw and bagasse.
步骤1)中所述的球磨处理时间为4h,每30min正反交替一次,转速为516r/min。The ball milling treatment time described in step 1) is 4 hours, the forward and reverse are alternated every 30 minutes, and the rotating speed is 516r/min.
步骤2)中,恒温水浴温度为50~80℃,搅拌时间为2-4h,机械搅拌的转速约为200r/min。In step 2), the temperature of the constant temperature water bath is 50-80° C., the stirring time is 2-4 hours, and the rotational speed of the mechanical stirring is about 200 r/min.
步骤2)中,球磨木粉的用量为12.5g~15g,四乙基氯化铵的用量为7.5g~22.5g,二甲亚砜的用量为40g。In step 2), the amount of ball-milled wood powder is 12.5g-15g, the amount of tetraethylammonium chloride is 7.5g-22.5g, and the amount of dimethyl sulfoxide is 40g.
步骤3)中,三乙酸甘油酯的用量占DMSO/TEAC溶剂改性产物和三乙酸甘油酯总量的0~15%。In step 3), the amount of triacetin accounts for 0-15% of the total amount of the DMSO/TEAC solvent modified product and triacetin.
步骤3)中,挤出温度为120~160℃,螺杆转速为40~80r/min。In step 3), the extrusion temperature is 120-160° C., and the screw speed is 40-80 r/min.
有益效果:与现有技术相比,本发明具备的优点包括:Beneficial effect: compared with the prior art, the advantages of the present invention include:
(1)使用的原料来自于自然界中大量可再生的木质纤维类生物质,具备绿色环保和成本低多重优越性,可实现农林废弃物的资源化利用奠定一定的基础。(1) The raw materials used come from a large amount of renewable lignocellulosic biomass in nature, which has multiple advantages of environmental protection and low cost, and can lay a certain foundation for the resource utilization of agricultural and forestry waste.
(2)本发明中制备的生物基塑料力学性能佳,有较好的可塑性能,应用前景广阔。(2) The bio-based plastic prepared in the present invention has good mechanical properties, good plasticity, and broad application prospects.
(3)本发明中使用的丙酮可在实验结束后回收利用,不会造成环境污染和资源浪费,实现资源循环利用。(3) The acetone used in the present invention can be recycled after the experiment ends, without causing environmental pollution and resource waste, and realizing resource recycling.
(4)本发明中,木粉在DMSO/TEAC体系中溶解处理,不涉及化学反应,利用DMSO/TEAC体系破坏木质纤维中纤维素的氢键,再加入增塑剂制备注塑级材料,方法操作简单,便于实现工业化。(4) In the present invention, wood powder is dissolved in DMSO/TEAC system, does not involve chemical reaction, utilizes DMSO/TEAC system to destroy the hydrogen bond of cellulose in wood fiber, then adds plasticizer to prepare injection molding grade material, method operation Simple, easy to realize industrialization.
附图说明Description of drawings
图1是实施例2的球磨木粉、改性产物和挤出产物的红外谱图对比图,曲线a为球磨木粉的红外谱图,曲线b为四乙基氯化铵添加量为12.5g时改性产物的红外谱图,曲线c为四乙基氯化铵添加量为12.5g时与5%三乙酸甘油酯共混挤出产物的红外谱图。Fig. 1 is the infrared spectrogram comparison figure of the ball-milled wood powder, modified product and extrusion product of embodiment 2, and curve a is the infrared spectrogram of ball-milled wood powder, and curve b is that the addition amount of tetraethylammonium chloride is 12.5g When the infrared spectrum of the modified product is shown, the curve c is the infrared spectrum of the extruded product blended with 5% triacetin when the added amount of tetraethylammonium chloride is 12.5g.
图2是实施例2是球磨木粉、改性产物、挤出产物和四乙基氯化铵的XRD对比图,曲线a为球磨木粉的XRD图,曲线b为四乙基氯化铵添加量为12.5g时改性产物的XRD图,曲线c为四乙基氯化铵添加量为12.5g时与5%三乙酸甘油酯共混挤出产物的XRD图,曲线d为四乙基氯化铵的XRD图。Fig. 2 is that embodiment 2 is the XRD comparison figure of ball-milled wood flour, modified product, extruded product and tetraethylammonium chloride, curve a is the XRD figure of ball-milled wood flour, and curve b is the addition of tetraethylammonium chloride The XRD pattern of the modified product when the amount is 12.5g, the curve c is the XRD pattern of the extruded product blended with 5% triacetin when the added amount of tetraethylammonium chloride is 12.5g, and the curve d is the tetraethylammonium chloride XRD pattern of ammonium chloride.
图3是改性产物和三乙酸甘油酯挤出产物注塑成型后弯曲断面放大500倍的扫描电镜图,3-A是四乙基氯化铵添加量为15g时改性产物的扫描电镜图,3-B是四乙基氯化铵添加量为12.5g时与5%三乙酸甘油酯共混挤出产物的扫描电镜图。Fig. 3 is the scanning electron micrograph of modified product and glyceryl triacetate extruded product after injection molding, and the scanning electron microscope picture of bending section is enlarged 500 times, and 3-A is the scanning electron microscope picture of modified product when tetraethylammonium chloride addition is 15g, 3-B is a scanning electron micrograph of the extruded product blended with 5% triacetin when the added amount of tetraethylammonium chloride is 12.5g.
具体实施方式Detailed ways
下面结合具体实施例对本发明做进一步的说明。The present invention will be further described below in conjunction with specific embodiments.
实施例1Example 1
一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,包括以步骤:A method for dissolving wood powder by GT plasticized DMSO/TEAC system to prepare injection-grade bio-based plastics, comprising the steps of:
1)以胡桑枝条为原料,剥皮,晾干,机械粉碎后干燥。1) Take the sage bark as raw material, peel off the bark, dry it in the air, crush it mechanically and then dry it.
2)取8g干燥后的木粉原料置于200mL的玛瑙球磨罐中,加入不同直径的氧化锆球(Φ10mm∶Φ7mm∶Φ5mm,20∶40∶120),在行星式球磨机中球磨4h,每30min正反交替一次,转速为516r/min。球磨木粉置于干燥器中备用。2) Take 8g of dried wood flour raw material and place it in a 200mL agate ball mill jar, add zirconia balls of different diameters (Φ10mm:Φ7mm:Φ5mm, 20:40:120), and mill in a planetary ball mill for 4h, every 30min Alternate forward and reverse once, the speed is 516r/min. The ball-ground wood powder is placed in a desiccator for later use.
3)15g四乙基氯化铵溶于40g二甲亚砜得到复合溶剂,称取6g球磨木粉加入复合溶剂中,于60℃机械搅拌2h,加入丙酮,抽滤后得到改性产物。3) Dissolve 15g of tetraethylammonium chloride in 40g of dimethyl sulfoxide to obtain a composite solvent, weigh 6g of ball-milled wood powder and add it to the composite solvent, mechanically stir at 60°C for 2 hours, add acetone, and obtain a modified product after suction filtration.
4)改性产物注塑成型(采用MiniJet微量注塑机(Thermo Fisher)注塑条件为:注塑压力750bar,保持压力600bar,注塑温度170℃,模具温度75℃,注塑时间12s,保持时间8s,下同)后,经电子万能试验机测定(在电子万能试验机(SANS UTM6503,深圳三思纵横)上进行力学性能测试,参考标准为GB/T 1040-1992(塑料拉伸性能试验方法)和GB/T 9341-2000(塑料弯曲性能试验方法)。下同),弯曲强度为26.28MPa,拉伸强度为9.63MPa。4) Injection molding of the modified product (using a MiniJet micro injection molding machine (Thermo Fisher), the injection molding conditions are: injection pressure 750bar, holding pressure 600bar, injection temperature 170°C, mold temperature 75°C, injection time 12s, holding time 8s, the same below) Afterwards, it was determined by electronic universal testing machine (mechanical performance test was carried out on electronic universal testing machine (SANS UTM6503, Shenzhen Sansi Zongheng), the reference standard was GB/T 1040-1992 (test method for plastic tensile properties) and GB/T 9341 -2000 (test method for plastic bending performance). The same below), the bending strength is 26.28MPa, and the tensile strength is 9.63MPa.
实施例2Example 2
一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,包括以步骤:A method for dissolving wood powder by GT plasticized DMSO/TEAC system to prepare injection-grade bio-based plastics, comprising the steps of:
1)以胡桑枝条为原料,剥皮,晾干,机械粉碎后干燥。1) Take the sage bark as raw material, peel off the bark, dry it in the air, crush it mechanically and then dry it.
2)取8g干燥后的木粉原料置于200mL的玛瑙球磨罐中,加入不同直径的氧化锆球(Φ10mm∶Φ7mm∶Φ5mm,20∶40∶120),在行星式球磨机中球磨4h,每30min正反交替一次,转速为516r/min。球磨木粉置于干燥器中备用。2) Take 8g of dried wood flour raw material and place it in a 200mL agate ball mill jar, add zirconia balls of different diameters (Φ10mm:Φ7mm:Φ5mm, 20:40:120), and mill in a planetary ball mill for 4h, every 30min Alternate forward and reverse once, the speed is 516r/min. The ball-ground wood powder is placed in a desiccator for later use.
3)17.5g四乙基氯化铵溶于40g二甲亚砜得到复合溶剂,称取6g球磨木粉溶于复合溶剂中,于60℃机械搅拌2h,加入丙酮,抽滤后得到改性产物。3) Dissolve 17.5g of tetraethylammonium chloride in 40g of dimethyl sulfoxide to obtain a composite solvent, weigh 6g of ball-milled wood powder and dissolve it in the composite solvent, stir mechanically at 60°C for 2 hours, add acetone, and obtain a modified product after suction filtration .
4)改性产物注塑成型后得挤出产物,经电子万能试验机测定,弯曲强度为5.38MPa,拉伸强度为2.76MPa。4) The extruded product obtained after injection molding of the modified product was measured by an electronic universal testing machine, and the flexural strength was 5.38 MPa, and the tensile strength was 2.76 MPa.
球磨木粉、改性产物和挤出产物的红外谱图对比图如图1所示,曲线a为球磨木粉的红外谱图,曲线b为四乙基氯化铵添加量为12.5g时改性产物的红外谱图,曲线c为四乙基氯化铵添加量为12.5g时与5%三乙酸甘油酯共混挤出产物的红外谱图,谱图中没有显示出新的特征吸收峰,这说明在改性和挤出过程中几乎没有发生化学反应,在纤维素大分子链中没有化学键的增加。曲线a显示了木质纤维素的特征峰,包括3424cm-1处的OH伸缩振动峰,2922cm-1处的C-H伸缩振动峰,1633cm-1处的峰与结晶水有关。与原球磨木粉(曲线a)比较,GT挤出产物(曲线c)中纤维素分子间的羟基峰向高波数移动,这说明纤维素分子链上的氢键作用减弱。此外,1727cm-1处的吸收峰是半纤维素中乙酰基、糖醛酸基C=O伸缩振动峰,1048cm-1处是纤维素的C-O伸缩振动特征峰。加入TEAC和GT后,1727cm-1出的吸收峰消失,1048cm-1处吸收峰明显减弱,说明纤维素分子链上羟基之间生成的氢键被破坏。同时这也说明在溶解反应以及与GT共混挤出的过程中,体系对半纤维素和纤维素起到一定破坏作用。The infrared spectrogram comparison chart of ball-milled wood flour, modified product and extruded product is shown in Figure 1. Curve a is the infrared spectrogram of ball-milled wood flour, and curve b is when the addition of tetraethylammonium chloride is 12.5g. The infrared spectrogram of the neutral product, the curve c is the infrared spectrogram of the extruded product blended with 5% glycerol triacetate when the addition of tetraethylammonium chloride is 12.5g, and no new characteristic absorption peak is shown in the spectrogram , which indicated that almost no chemical reaction occurred during the modification and extrusion process, and there was no increase of chemical bonds in the cellulose macromolecular chains. Curve a shows the characteristic peaks of lignocellulose, including the OH stretching vibration peak at 3424 cm -1 , the CH stretching vibration peak at 2922 cm -1 , and the peak at 1633 cm -1 related to crystal water. Compared with the original ball-ground wood flour (curve a), the hydroxyl peak between cellulose molecules in the GT extruded product (curve c) shifted to a higher wave number, which indicated that the hydrogen bond interaction on the cellulose molecular chain was weakened. In addition, the absorption peak at 1727cm -1 is the C=O stretching vibration peak of acetyl group and uronic acid group in hemicellulose, and the characteristic peak of CO stretching vibration at 1048cm -1 is cellulose. After adding TEAC and GT, the absorption peak at 1727cm -1 disappeared, and the absorption peak at 1048cm -1 was obviously weakened, indicating that the hydrogen bond formed between the hydroxyl groups on the cellulose molecular chain was broken. At the same time, it also shows that in the process of dissolution reaction and blending and extrusion with GT, the system has a certain damage effect on hemicellulose and cellulose.
球磨木粉、改性产物、挤出产物和四乙基氯化铵的XRD对比图如图2所示,曲线a为球磨木粉的XRD图,曲线b为四乙基氯化铵添加量为12.5g时改性产物的XRD图,曲线c为四乙基氯化铵添加量为12.5g时与5%三乙酸甘油酯共混挤出产物的XRD图,曲线d为四乙基氯化铵的XRD图。从图中可以看出,球磨木粉(a)中纤维素I晶型的特征峰基本消失,这说明球磨破坏了木粉中纤维素的晶型。与曲线a相比较,曲线d在2θ=18.0°、26.0°、30.2°等多处出现TEAC的特征衍射峰。而从曲线b和c可以看出,改性产物和GT挤出产物的XRD图中并未出现TEAC晶体的衍射峰,TEAC并未以晶体的形式存在,而是以离子对的形式存在于纤维素分子链之间,其结晶度相比于球磨木粉也有很大程度的下降,故而其热塑性得到明显提高。The XRD comparison chart of ball-milled wood flour, modified product, extruded product and tetraethylammonium chloride is shown in Figure 2. Curve a is the XRD figure of ball-milled wood flour, and curve b is the amount of tetraethylammonium chloride added. The XRD pattern of the modified product at 12.5g, the curve c is the XRD pattern of the extruded product blended with 5% triacetin when the added amount of tetraethylammonium chloride is 12.5g, and the curve d is the tetraethylammonium chloride XRD pattern. It can be seen from the figure that the characteristic peak of the cellulose I crystal form in the ball-milled wood flour (a) basically disappears, which indicates that the ball milling has destroyed the crystalline form of cellulose in the wood flour. Compared with curve a, curve d has the characteristic diffraction peaks of TEAC at 2θ=18.0°, 26.0°, 30.2° and many other places. From the curves b and c, it can be seen that there is no diffraction peak of TEAC crystal in the XRD pattern of the modified product and GT extrusion product, and TEAC does not exist in the form of crystals, but exists in the form of ion pairs in the fiber Compared with the ball-milled wood flour, its crystallinity is also greatly reduced among the molecular chains of the element, so its thermoplasticity is significantly improved.
实施例3Example 3
一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,包括以步骤:A method for dissolving wood powder by GT plasticized DMSO/TEAC system to prepare injection-grade bio-based plastics, comprising the steps of:
1)1)以胡桑枝条为原料,剥皮,晾干,机械粉碎后干燥。1) 1) Take the sage bark as raw material, peel it off, dry it in the air, crush it mechanically and then dry it.
2)取8g干燥后的木粉原料置于200mL的玛瑙球磨罐中,加入不同直径的氧化锆球(Φ10mm∶Φ7mm∶Φ5mm,20∶40∶120),在行星式球磨机中球磨4h,每30min正反交替一次,转速为516r/min。球磨木粉置于干燥器中备用。2) Take 8g of dried wood flour raw material and place it in a 200mL agate ball mill jar, add zirconia balls of different diameters (Φ10mm:Φ7mm:Φ5mm, 20:40:120), and mill in a planetary ball mill for 4h, every 30min Alternate forward and reverse once, the speed is 516r/min. The ball-ground wood powder is placed in a desiccator for later use.
3)12.5g四乙基氯化铵溶于40g二甲亚砜得到复合溶剂,称取6g球磨木粉加入复合溶剂中,60℃水浴锅中机械搅拌2h,加入丙酮,抽滤后得到改性产物。3) Dissolve 12.5g of tetraethylammonium chloride in 40g of dimethyl sulfoxide to obtain a composite solvent. Weigh 6g of ball-milled wood powder and add it to the composite solvent. Stir mechanically in a water bath at 60°C for 2 hours, add acetone, and obtain a modified solution after suction filtration. product.
4)将改性产物和三乙酸甘油酯(三乙酸甘油酯用量占改性产物和三乙酸甘油酯总量的5%)于双螺杆挤出机中共混挤出,挤出机转速为60r/min,挤出温度为120℃。4) The modified product and glyceryl triacetate (the amount of glycerol triacetate accounts for 5% of the total amount of the modified product and glyceryl triacetate) is blended and extruded in a twin-screw extruder, and the extruder speed is 60r/ min, the extrusion temperature is 120°C.
5)挤出产物用研磨机粉碎造粒,注塑成型后经电子万能试验机检测,弯曲强度为24.91MPa,拉伸强度为8.39MPa。5) The extruded product was crushed and granulated with a grinder, and tested by an electronic universal testing machine after injection molding. The bending strength was 24.91 MPa, and the tensile strength was 8.39 MPa.
实施例4Example 4
一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,包括以步骤:A method for dissolving wood powder by GT plasticized DMSO/TEAC system to prepare injection-grade bio-based plastics, comprising the steps of:
1)以胡桑枝条为原料,剥皮,晾干,机械粉碎后干燥。1) Take the sage bark as raw material, peel off the bark, dry it in the air, crush it mechanically and then dry it.
2)取8g干燥后的木粉原料置于200mL的玛瑙球磨罐中,加入不同直径的氧化锆球(Φ10mm∶Φ7mm∶Φ5mm,20∶40∶120),在行星式球磨机中球磨4h,每30min正反交替一次,转速为516r/min。球磨木粉置于干燥器中备用。2) Take 8g of dried wood flour raw material and place it in a 200mL agate ball mill jar, add zirconia balls of different diameters (Φ10mm:Φ7mm:Φ5mm, 20:40:120), and mill in a planetary ball mill for 4h, every 30min Alternate forward and reverse once, the speed is 516r/min. The ball-ground wood powder is placed in a desiccator for later use.
3)称取6g球磨木粉,12.5g四乙基氯化铵溶于40g二甲亚砜,于60℃水浴锅中机械搅拌2h,加入丙酮,抽滤后得到改性产物。3) Weigh 6g of ball-milled wood powder, dissolve 12.5g of tetraethylammonium chloride in 40g of dimethyl sulfoxide, stir mechanically in a water bath at 60°C for 2 hours, add acetone, and obtain a modified product after suction filtration.
4)将改性产物和三乙酸甘油酯(三乙酸甘油酯用量占改性产物和三乙酸甘油酯总量的5%)于双螺杆挤出机中共混挤出,挤出机转速为60r/min,挤出温度为140℃。4) The modified product and glyceryl triacetate (the amount of glycerol triacetate accounts for 5% of the total amount of the modified product and glyceryl triacetate) is blended and extruded in a twin-screw extruder, and the extruder speed is 60r/ min, the extrusion temperature is 140°C.
5)挤出产物用研磨机粉碎造粒,注塑成型后经电子万能试验机检测,弯曲强度为34.71MPa,拉伸强度为16.33MPa。5) The extruded product was pulverized and granulated with a grinder, and tested by an electronic universal testing machine after injection molding. The bending strength was 34.71 MPa and the tensile strength was 16.33 MPa.
实施例5Example 5
一种利用GT增塑DMSO/TEAC体系溶解木粉制备注塑级生物基塑料的方法,包括以步骤:A method for dissolving wood powder by GT plasticized DMSO/TEAC system to prepare injection-grade bio-based plastics, comprising the steps of:
1)以胡桑枝条为原料,剥皮,晾干,机械粉碎后干燥。1) Take the sage bark as raw material, peel off the bark, dry it in the air, crush it mechanically and then dry it.
2)取8g干燥后的木粉原料置于200mL的玛瑙球磨罐中,加入不同直径的氧化锆球(Φ10mm∶Φ7mm∶Φ5mm,20∶40∶120),在行星式球磨机中球磨4h,每30min正反交替一次,转速为516r/min。球磨木粉置于干燥器中备用。2) Take 8g of dried wood flour raw material and place it in a 200mL agate ball mill jar, add zirconia balls of different diameters (Φ10mm:Φ7mm:Φ5mm, 20:40:120), and mill in a planetary ball mill for 4h, every 30min Alternate forward and reverse once, the speed is 516r/min. The ball-ground wood powder is placed in a desiccator for later use.
3)12.5g四乙基氯化铵溶于40g二甲亚砜得到复合溶剂,称取6g球磨木粉加入复合溶剂中,于60℃水浴锅中机械搅拌2h,加入丙酮,抽滤后得到改性产物。3) Dissolve 12.5g of tetraethylammonium chloride in 40g of dimethyl sulfoxide to obtain a composite solvent, weigh 6g of ball-milled wood powder and add it to the composite solvent, mechanically stir in a water bath at 60°C for 2 hours, add acetone, and obtain a modified solution after suction filtration. sexual product.
4)将改性产物和三乙酸甘油酯(三乙酸甘油酯用量占改性产物和三乙酸甘油酯总量的5%)于双螺杆挤出机中共混挤出,挤出机转速为60r/min,挤出温度为160℃。4) The modified product and glyceryl triacetate (the amount of glycerol triacetate accounts for 5% of the total amount of the modified product and glyceryl triacetate) is blended and extruded in a twin-screw extruder, and the extruder speed is 60r/ min, the extrusion temperature is 160°C.
5)挤出产物用研磨机粉碎造粒,注塑成型后经电子万能试验机检测,弯曲强度为33.66MPa,拉伸强度为15.12MPa。5) The extruded product was crushed and granulated with a grinder, and tested by an electronic universal testing machine after injection molding. The bending strength was 33.66 MPa and the tensile strength was 15.12 MPa.
改性产物和三乙酸甘油酯挤出产物注塑成型后弯曲断面放大500倍的扫描电镜图如图3所示,3-A是四乙基氯化铵添加量为15g时改性产物的扫描电镜图,3-B是四乙基氯化铵添加量为12.5g时与5%三乙酸甘油酯共混挤出产物的扫描电镜图,图3-B的弯曲断面十分平整光滑,分子间结合致密,纤维结构消失,这说明GT小分子渗透到纤维素大分子链之间,起到增塑的作用,使注塑成型的样条较为光滑、紧实且力学性能较佳。而从图3-A中可以看出TEAC添加量为15g时改性产物的弯曲断面出现了大量孔洞,导致力学性能下降。The SEM image of the modified product and triacetin extruded product after injection molding is magnified 500 times of the curved section as shown in Figure 3, 3-A is the SEM of the modified product when the addition of tetraethylammonium chloride is 15g Figure 3-B is a scanning electron microscope image of the extruded product blended with 5% triacetin when the amount of tetraethylammonium chloride added is 12.5g. The curved section of Figure 3-B is very flat and smooth, and the intermolecular combination is dense , the fiber structure disappears, which means that the small GT molecules penetrate into the cellulose macromolecular chains and play a plasticizing role, making the injection molded splines smoother, tighter and better in mechanical properties. From Figure 3-A, it can be seen that when the amount of TEAC added is 15g, a large number of holes appear in the curved section of the modified product, resulting in a decrease in mechanical properties.
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