CN102166579B - Method for recycling and separating paper, aluminum and plastic packaging boxes - Google Patents
Method for recycling and separating paper, aluminum and plastic packaging boxes Download PDFInfo
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- CN102166579B CN102166579B CN2011100082722A CN201110008272A CN102166579B CN 102166579 B CN102166579 B CN 102166579B CN 2011100082722 A CN2011100082722 A CN 2011100082722A CN 201110008272 A CN201110008272 A CN 201110008272A CN 102166579 B CN102166579 B CN 102166579B
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- 239000004033 plastic Substances 0.000 title claims abstract description 109
- 229920003023 plastic Polymers 0.000 title claims abstract description 109
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 64
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 63
- 238000004806 packaging method and process Methods 0.000 title abstract description 20
- 238000000034 method Methods 0.000 title abstract description 19
- 238000004064 recycling Methods 0.000 title abstract description 11
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 35
- 239000002131 composite material Substances 0.000 claims abstract description 30
- 238000000926 separation method Methods 0.000 claims abstract description 22
- 239000000835 fiber Substances 0.000 claims abstract description 17
- 238000012216 screening Methods 0.000 claims abstract description 15
- 229920002678 cellulose Polymers 0.000 claims abstract description 7
- 239000001913 cellulose Substances 0.000 claims abstract description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 54
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000002002 slurry Substances 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000004411 aluminium Substances 0.000 claims 8
- 239000006185 dispersion Substances 0.000 claims 6
- 229920001131 Pulp (paper) Polymers 0.000 claims 2
- 238000013019 agitation Methods 0.000 claims 2
- 239000012467 final product Substances 0.000 claims 1
- 238000003756 stirring Methods 0.000 abstract description 6
- 238000011084 recovery Methods 0.000 abstract description 5
- 239000011888 foil Substances 0.000 description 8
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- 239000003960 organic solvent Substances 0.000 description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 5
- 229920001684 low density polyethylene Polymers 0.000 description 5
- 239000004702 low-density polyethylene Substances 0.000 description 5
- 239000000123 paper Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 235000013336 milk Nutrition 0.000 description 3
- 239000008267 milk Substances 0.000 description 3
- 210000004080 milk Anatomy 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical class [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 239000011091 composite packaging material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 235000021056 liquid food Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/02—Separating plastics from other materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2009/00—Layered products
- B29L2009/003—Layered products comprising a metal layer
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- Paper (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明提供了一种纸铝塑包装盒回收分离方法,包括步骤:取纸铝塑包装盒,在水力分散机中分散处理后,筛选分离出纸浆纤维用于纤维素高值化利用,余下的为铝塑复合物材料;将得到的铝塑复合物材料与分离剂混合后,轻微搅拌直至完全分离出铝和塑料,最后将分离出来的铝和塑料分别清洗即可。本发明分离方法成本低、回收效率高,且不会对环境产生污染。The invention provides a method for recycling and separating paper-aluminum-plastic packaging boxes, comprising the steps of: taking paper-aluminum-plastic packaging boxes, dispersing them in a hydraulic disperser, screening and separating pulp fibers for high-value utilization of cellulose, and the remaining It is an aluminum-plastic composite material; after mixing the obtained aluminum-plastic composite material with a separating agent, stir gently until the aluminum and plastic are completely separated, and finally wash the separated aluminum and plastic separately. The separation method of the invention has low cost, high recovery efficiency and no pollution to the environment.
Description
技术领域 technical field
本发明属于复合包装材料分离技术领域,涉及一种纸铝塑包装盒回收分离方法。The invention belongs to the technical field of separation of composite packaging materials, and relates to a method for recycling and separating paper, aluminum and plastic packaging boxes.
背景技术 Background technique
以利乐包为代表的纸铝塑包装盒是一种由纸、铝箔和聚乙烯塑料复合而成的高湿强包装纸盒,可以用于牛奶、果汁、豆奶、咖啡、葡萄酒等液体食品的包装。该包装一般有6层,可有效阻挡所有影响牛奶和饮料变质的因素。其中纸板、聚乙烯塑料和铝箔的含量分别为73%、20%和5%。The paper-aluminum-plastic packaging box represented by Tetra Pak is a high-humidity packaging carton made of paper, aluminum foil and polyethylene plastic, which can be used for liquid food such as milk, juice, soybean milk, coffee, wine, etc. Package. The packaging generally has 6 layers, which can effectively block all factors that affect the deterioration of milk and beverages. Among them, the contents of cardboard, polyethylene plastic and aluminum foil are 73%, 20% and 5% respectively.
传统的纸铝塑包装盒的回收再利用技术方案主要有一下三种:(1)水力再生浆技术:将纸铝塑包装盒中的纸浆分离出来,再次造纸,而将剩余的铝塑复合物挤压成粒,用于制造塑铝产品;(2)塑木技术:将纸铝塑包装盒中含有的纸浆和塑料碾碎挤压,制成塑木产品;(3)彩乐板技术:将纸铝塑包装盒直接粉碎、热压处理,制成彩乐板。尽管由这些技术生产出来的产品用途广泛,但市场反响和利润空间仍无法与彻底分离开的铝、塑料产品相媲美。只有将纸、塑、铝彻底分离才能够实现物尽其用和资源节约的最大化,实现更高的回收利用价值。There are three main technical solutions for the recycling of traditional paper-aluminum-plastic packaging boxes: (1) Hydraulic recycled pulp technology: the pulp in the paper-aluminum-plastic packaging box is separated to make paper again, and the remaining aluminum-plastic composite Extruded into granules for the manufacture of plastic-aluminum products; (2) Wood-plastic technology: crush and extrude the pulp and plastic contained in paper-aluminum-plastic packaging boxes to make plastic-wood products; (3) Color board technology: The paper-aluminum-plastic packaging box is directly crushed and heat-pressed to make a color board. Although the products produced by these technologies are widely used, the market response and profit margins are still not comparable to the completely separated aluminum and plastic products. Only by completely separating paper, plastic, and aluminum can we maximize the use of materials and save resources, and achieve a higher recycling value.
目前纸铝塑包装盒中纸浆的回收方法是采用水力碎浆机,经过水的剪切力和纤维之间的摩擦力将纤维分离,剩余铝塑的分离方法主要有物理和化学-机械法。(1)利用铝、塑的熔点不同(铝的熔点为660℃,LDPE的熔点为107~120℃),使塑料热解气化,回收铝箔,气化的塑料用于发电。但该方法造成了塑料大量的浪费。(2)利用铝和铝的氧化物溶于酸碱的性质,用酸或碱把铝溶解,从而回收塑料。但这种方法存在反应时间长、分离不彻底、从溶液中提取铝难等问题。(3)利用一些酸性有机溶剂可以渗透LDPE到达铝塑的结合面,将结合面的氧化铝溶解,从而达到铝塑分离的效果。有机酸可以是甲酸、乙酸、丙酸和丁酸,但这种方法是以消耗酸为前提的,回收成本大,分离废液不好处理。(4)利用单一有机溶剂(如苯、丙酮、二氯甲烷等)处理来分离铝塑。然而经过试验研究发现,使用丙酮、二氯甲烷这些单一有机溶剂时,几乎无法使塑料和铝箔分离,而使用苯类单一有机溶剂时会直接将LDPE溶解,无法回收塑料。因此单一有机溶剂具有使用量大,成本高,分离效果差等缺陷。At present, the pulp recovery method in the paper-aluminum-plastic packaging box is to use a hydropulper to separate the fibers through the shear force of water and the friction between the fibers. The separation methods of the remaining aluminum and plastic mainly include physical and chemical-mechanical methods. (1) Using the different melting points of aluminum and plastic (the melting point of aluminum is 660°C, and the melting point of LDPE is 107-120°C), the plastic is pyrolyzed and gasified, the aluminum foil is recycled, and the gasified plastic is used for power generation. But this method has caused a large amount of waste of plastics. (2) Utilize the property that aluminum and aluminum oxides are soluble in acid and alkali, and dissolve aluminum with acid or alkali, thereby recycling plastics. However, this method has problems such as long reaction time, incomplete separation, and difficulty in extracting aluminum from the solution. (3) Use some acidic organic solvents to penetrate LDPE to reach the joint surface of aluminum and plastic, and dissolve the alumina on the joint surface, so as to achieve the effect of separating aluminum and plastic. The organic acid can be formic acid, acetic acid, propionic acid and butyric acid, but this method is based on the premise of acid consumption, the recovery cost is high, and the separated waste liquid is not easy to handle. (4) Use a single organic solvent (such as benzene, acetone, dichloromethane, etc.) to separate aluminum and plastic. However, experimental studies have found that when single organic solvents such as acetone and methylene chloride are used, it is almost impossible to separate the plastic from the aluminum foil, while when using a single organic solvent such as benzene, LDPE will be directly dissolved, and the plastic cannot be recycled. Therefore, a single organic solvent has defects such as large usage, high cost, and poor separation effect.
发明内容 Contents of the invention
本发明所要解决的技术问题是提供一种纸铝塑包装盒回收分离方法,成本低、回收效率高,且不会对环境产生污染。The technical problem to be solved by the present invention is to provide a method for recycling and separating paper, aluminum and plastic packaging boxes, which has low cost, high recycling efficiency and will not pollute the environment.
为实现上述目的,本发明提供了一种纸铝塑包装盒回收分离方法,取纸铝塑包装盒,在水力分散机中分散处理后,筛选分离出纸浆纤维用于纤维素高值化利用,余下的为铝塑复合物材料;将得到的铝塑复合物材料与分离剂混合后,轻微搅拌直至完全分离出铝和塑料,最后将分离出来的铝和塑料分别清洗即可所述水力分散机采用低浓分离,其中,所述浆料的质量浓度为1~5%;所述铝塑复合物材料与分离剂混合后,保证分离剂的液体量浸没铝塑材料;所述铝塑复合物材料与分离剂的固液比为60g/L,所述分离剂的组分及体积百分比为:苯:20~80%,无水乙醇:10~45%,水:10~80%,所述分离剂的各组分按照体积百分比合计为100%。In order to achieve the above purpose, the present invention provides a method for recycling and separating paper-aluminum-plastic packaging boxes. The paper-aluminum-plastic packaging box is taken out, and after being dispersed in a hydraulic disperser, pulp fibers are screened and separated for high-value utilization of cellulose. The rest is aluminum-plastic composite material; after mixing the obtained aluminum-plastic composite material with a separating agent, stir gently until the aluminum and plastic are completely separated, and finally clean the separated aluminum and plastic separately. Low-concentration separation is adopted, wherein the mass concentration of the slurry is 1% to 5%; after the aluminum-plastic composite material is mixed with the separating agent, ensure that the liquid amount of the separating agent is immersed in the aluminum-plastic material; the aluminum-plastic composite The solid-liquid ratio of the material and the separating agent is 60g/L, and the components and volume percentages of the separating agent are: benzene: 20-80%, absolute ethanol: 10-45%, water: 10-80%, and the The components of the separating agent add up to 100% by volume percentage.
作为本发明的优选实施例,筛选时,采用缝宽为0.10~0.15mm的缝筛,筛选时的浆料质量浓度为0.8~1.0%;As a preferred embodiment of the present invention, when screening, a slotted screen with a slot width of 0.10-0.15 mm is used, and the mass concentration of the slurry during screening is 0.8-1.0%;
作为本发明的优选实施例,所述水力分散机的分散处理条件为:转速500~1000r/min,温度:30~50℃,pH值为7~8,疏解时间为10~20min;As a preferred embodiment of the present invention, the dispersing treatment conditions of the hydraulic disperser are: rotating speed 500-1000r/min, temperature: 30-50°C, pH value 7-8, and dispersing time 10-20min;
作为本发明的优选实施例,所述铝塑复合物材料与分离剂是在恒温60℃的容器中进行;As a preferred embodiment of the present invention, the aluminum-plastic composite material and the separating agent are carried out in a container with a constant temperature of 60°C;
作为本发明的优选实施例,所述铝塑复合物材料经分离剂分离后,清洗时,首先用浓度为50~80%的乙醇溶液清洗,去除铝塑上的苯,然后再用清水冲洗。As a preferred embodiment of the present invention, after the aluminum-plastic composite material is separated by a separating agent, when cleaning, it is firstly cleaned with an ethanol solution with a concentration of 50-80% to remove benzene on the aluminum-plastic composite material, and then rinsed with clean water.
本发明纸铝塑包装盒回收分离方法至少具有以下优点:本发明方法可以对铝和塑料分别分离,且成本低、回收效率高、不会对环境产生污染。另外,本发明在纤维回收并高值化利用的基础上,采用乙醇和水适当稀释苯后,处理铝塑复合物,可以有效溶胀LDPE,减小铝塑间的结合力,快速将铝塑复合物材料完整分离,分离后的铝箔和塑料的得率都很高,达到95%以上,分离后的废液也能很方便的回收和重复使用,足见这是铝塑分离和回收的有效途径。The method for recycling and separating the paper-aluminum-plastic packaging box of the present invention has at least the following advantages: the method of the present invention can separate aluminum and plastic separately, has low cost, high recycling efficiency, and does not pollute the environment. In addition, on the basis of fiber recovery and high-value utilization, the present invention uses ethanol and water to properly dilute benzene, and then treats the aluminum-plastic composite, which can effectively swell LDPE, reduce the bonding force between aluminum and plastic, and quickly compound aluminum and plastic. The material is completely separated, and the yield of separated aluminum foil and plastic is very high, reaching more than 95%. The separated waste liquid can also be easily recycled and reused, which shows that this is an effective way to separate and recycle aluminum and plastic.
具体实施方式 Detailed ways
下面针对本发明方法进行详细描述:The method for the present invention is described in detail below:
实施例1Example 1
将纸铝塑包装盒剪成40×40mm块状大小,在转速为500r/m,pH为7,温度为40℃,浆料的质量浓度为1%的水力分散机中分散处理,疏解时间为20min,然后采用缝宽为0.1mm的缝筛进行筛选,筛选时,浆料的质量浓度为0.8%,筛选后得到的纸浆纤维用于纤维素高值化利用,余下的为铝塑复合物材料;将得到的铝塑复合物材料与分离剂按60g/L的固液比放入恒温60℃的容器中,保证分离剂的液体量浸没铝塑材料,轻微搅拌3min,即可完全分离出铝塑,将分离出来的铝塑首先用浓度为50%的乙醇溶液清洗,去除铝塑上的苯,然后再用清水冲洗。Cut the paper-aluminum-plastic packaging box into a block size of 40×40mm, and disperse it in a hydraulic disperser with a rotational speed of 500r/m, a pH of 7, a temperature of 40°C, and a mass concentration of the slurry of 1%. 20 minutes, and then use a slotted screen with a slot width of 0.1mm to screen. During screening, the mass concentration of the slurry is 0.8%. The pulp fibers obtained after screening are used for high-value utilization of cellulose, and the rest are aluminum-plastic composite materials. ;Put the obtained aluminum-plastic composite material and separating agent into a container at a constant temperature of 60°C at a solid-to-liquid ratio of 60g/L, ensure that the liquid amount of the separating agent is immersed in the aluminum-plastic material, and stir gently for 3 minutes to completely separate the aluminum. For plastic, the separated aluminum plastic is first cleaned with a 50% ethanol solution to remove benzene on the aluminum plastic, and then rinsed with water.
通过本方法,其纸浆纤维的分离率高达100%,纸浆纤维的得率为95%;铝塑分离率达100%,塑料得率为95%,铝得率为100%。Through the method, the separation rate of the pulp fiber is as high as 100%, and the yield of the pulp fiber is 95%; the separation rate of aluminum and plastic reaches 100%, the yield of plastic is 95%, and the yield of aluminum is 100%.
所述分离剂是由体积百分比为30%的苯、20%的无水乙醇、50%的水组成。The separating agent is composed of 30% benzene, 20% absolute ethanol and 50% water by volume.
实施例2Example 2
将纸铝塑包装盒剪成50×50mm块状大小,在转速为700r/m,pH为7,温度为50℃,浆料的质量浓度为3%的水力分散机中分散处理,疏解时间为15min,然后采用缝宽为0.13mm的缝筛进行筛选,筛选时,浆料的质量浓度为0.9%,筛选后得到的纸浆纤维用于纤维素高值化利用,余下的为铝塑复合物材料;将得到的铝塑复合物材料与液体的分离剂按60g/L的固液比放入恒温60℃的容器中,保证分离剂的液体量浸没铝塑材料,轻微搅拌6min,即可完全分离出铝塑,将分离出来的铝塑首先用浓度为60%的乙醇溶液清洗,去除铝塑上的苯,然后再用清水冲洗。Cut the paper-aluminum-plastic packaging box into 50×50mm block size, and disperse it in a hydraulic disperser with a rotation speed of 700r/m, a pH of 7, a temperature of 50°C, and a mass concentration of the slurry of 3%, and the dispersing time is 15min, and then screened with a slotted screen with a slot width of 0.13mm. During screening, the mass concentration of the slurry was 0.9%. The pulp fibers obtained after screening were used for high-value utilization of cellulose, and the rest were aluminum-plastic composite materials. ;Put the obtained aluminum-plastic composite material and liquid separating agent into a container with a constant temperature of 60°C at a solid-to-liquid ratio of 60g/L, ensure that the liquid amount of the separating agent is immersed in the aluminum-plastic material, and stir gently for 6 minutes to completely separate To remove the aluminum plastic, the separated aluminum plastic is first cleaned with a 60% ethanol solution to remove the benzene on the aluminum plastic, and then rinsed with water.
通过本方法,其纸浆纤维的分离率达100%,纸浆纤维的得率为93%;铝塑分离率达100%,塑料得率为96%,铝得率为100%。Through the method, the separation rate of pulp fiber reaches 100%, and the yield rate of pulp fiber reaches 93%; the separation rate of aluminum and plastic reaches 100%, the yield rate of plastic is 96%, and the yield rate of aluminum is 100%.
所述分离剂是由体积百分比为25%的苯、30%的无水乙醇、45%的水组成。The separating agent is composed of 25% benzene, 30% absolute ethanol and 45% water by volume.
实施例3Example 3
将纸铝塑包装盒剪成50×50mm块状大小,在转速为1000r/m,pH为8,温度为50℃,浆浓为5%的水力分散机中分散处理,疏解时间为10min,然后采用缝宽为0.15mm的缝筛进行筛选,筛选时,浆料的质量浓度为1.0%,筛选后得到的纸浆纤维用于纤维素高值化利用,余下的为铝塑复合物材料;将得到的铝塑复合物材料与液体的分离剂按60g/L的固液比放入恒温60℃的容器中,保证分离剂的液体量浸没铝塑材料,轻微搅拌10min,即可完全分离出铝塑,将分离出来的铝塑首先用浓度为80%的乙醇溶液清洗,去除铝塑上的苯,然后再用清水冲洗。Cut the paper-aluminum-plastic packaging box into 50×50mm block size, and disperse it in a hydraulic disperser with a rotating speed of 1000r/m, a pH of 8, a temperature of 50°C, and a slurry concentration of 5%. A slotted sieve with a slot width of 0.15mm is used for screening. When screening, the mass concentration of the slurry is 1.0%. The pulp fibers obtained after screening are used for high-value utilization of cellulose, and the rest are aluminum-plastic composite materials; The aluminum-plastic composite material and the liquid separating agent are placed in a container with a constant temperature of 60°C at a solid-liquid ratio of 60g/L to ensure that the liquid amount of the separating agent is immersed in the aluminum-plastic material, and the aluminum-plastic composite material can be completely separated by stirring slightly for 10 minutes. , the separated aluminum plastic is first cleaned with an 80% ethanol solution to remove benzene on the aluminum plastic, and then rinsed with water.
通过本方法,其纸浆纤维的分离率达100%,纸浆纤维的得率为92%;铝塑分离率达100%,塑料得率为93%,铝得率为100%。Through the method, the separation rate of the pulp fiber reaches 100%, and the yield of the pulp fiber reaches 92%; the separation rate of aluminum and plastic reaches 100%, the yield of plastic is 93%, and the yield of aluminum is 100%.
所述分离剂是由体积百分比为40%的苯、20%的无水乙醇、40%的水组成。The separating agent is composed of 40% benzene, 20% absolute ethanol and 40% water by volume percentage.
本发明分离剂在反复使用一定次数后会溶解一定质量的塑料,静置一段时间后自动分层,苯位于分离剂的上层,乙醇和水位于下层,溶解的塑料层位于上下两层之间,分别回收苯层和乙醇-水层。塑料层经90℃加热蒸发分离剂后即可回收被溶解的塑料和有机溶剂。The separating agent of the present invention will dissolve plastics of a certain quality after repeated use for a certain number of times, and automatically stratify after standing for a period of time. The benzene layer and the ethanol-water layer were recovered separately. After the plastic layer is heated at 90°C to evaporate the separating agent, the dissolved plastic and organic solvent can be recovered.
本发明纸铝塑包装盒经水力分散机并筛选后得到的铝塑复合物材料中,铝箔与两侧塑料的粘合方式不同,一侧是用熔融聚乙烯做粘合剂,另一侧用有机粘合剂粘合,常用的分离方法很难将铝箔和塑料完全分离,而且分离纯度和得率也较低。而采用本发明分离剂处理后,即可将铝、塑完全分离。In the aluminum-plastic composite material obtained after the paper-aluminum-plastic packaging box of the present invention is screened by a hydraulic disperser, the bonding methods of the aluminum foil and the plastics on both sides are different. One side uses molten polyethylene as the adhesive, and the other side uses Organic adhesive bonding, it is difficult to completely separate aluminum foil and plastic by common separation methods, and the separation purity and yield are also low. After being treated with the separating agent of the present invention, aluminum and plastic can be completely separated.
值得说明的是:本发明方法在纤维回收并高值化利用的基础上,采用乙醇和水适当稀释苯后,处理铝塑复合物,可以有效溶胀LDPE,减小铝塑间的结合力,快速将铝塑复合物材料完整分离,分离后铝箔和塑料的得率都很高,达到95%以上,分离后的废液也能很方便的回收和重复使用。It is worth noting that: on the basis of fiber recovery and high-value utilization, the method of the present invention uses ethanol and water to properly dilute benzene, and then treats the aluminum-plastic composite, which can effectively swell LDPE, reduce the bonding force between aluminum and plastic, and quickly The aluminum-plastic composite material is completely separated. After separation, the yield of aluminum foil and plastic is very high, reaching more than 95%. The separated waste liquid can also be easily recycled and reused.
在本发明方法中,轻微搅拌的目的是使铝塑复合物材料与分离剂充分接触,防止分离剂分层。分离后的铝、塑料上粘有的少量苯,用50~80%的乙醇清洗,最后再用清水冲洗,去除其表面附有的少量乙醇。In the method of the present invention, the purpose of slight stirring is to make the aluminum-plastic composite material fully contact with the separating agent and prevent the separating agent from delamination. Clean the small amount of benzene on the separated aluminum and plastic with 50-80% ethanol, and finally rinse with water to remove the small amount of ethanol attached to the surface.
以上所述仅为本发明的一种实施方式,不是全部或唯一的实施方式,本领域普通技术人员通过阅读本发明说明书而对本发明技术方案采取的任何等效的变换,均为本发明的权利要求所涵盖。The above is only one embodiment of the present invention, not all or the only embodiment. Any equivalent transformation of the technical solution of the present invention adopted by those of ordinary skill in the art by reading the description of the present invention is the right of the present invention. covered by the requirements.
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| CN103722000B (en) * | 2013-12-26 | 2016-04-13 | 青岛福创环境科技有限公司 | The recovery method of waste and old paper or paper aluminium packaging material |
| ES2946698T3 (en) * | 2014-11-20 | 2023-07-24 | Juarez Souza De Oliveira | Recycling process by separating the constituents of aluminized and plasticized containers, optionally cardboard, and their respective equipment |
| BR102014028989A2 (en) * | 2014-11-20 | 2017-11-07 | Souza De Oliveira Juarez | PROCESS FOR RECYCLING THROUGH SEPARATION OF THE CONSTITUENTS OF ALUMINIZED AND PLASTICATED CARTONED PACKAGING |
| CN104690082B (en) * | 2015-01-16 | 2017-02-22 | 诸城市天工造纸机械有限公司 | Waste soft beverage package recycling technological process |
| CN104744724A (en) * | 2015-04-21 | 2015-07-01 | 戴翔辉 | Aluminium-plastic separating agent and method for carrying out aluminium-plastic separation by utilizing aluminium-plastic separating agent |
| BR102015010230B1 (en) * | 2015-05-05 | 2021-06-01 | Ecs Consultoria Em Materiais E Tecnologia Ambientais Ltda Me | RECYCLING PROCESS OF METALLIC PLASTIC PACKAGING |
| CN106180156B (en) * | 2016-09-05 | 2018-06-22 | 漳州市陆海环保产业开发有限公司 | One specific admixture aluminium paper moulds the value-added technique of sub-prime of waste material |
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| CN109261688B (en) * | 2018-08-31 | 2021-07-09 | 曲靖宏程工贸有限公司 | Recovery treatment process of waste aluminum foil composite paper |
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