CN102744241B - Shaftless spiral vertical-type continuous separation treatment system of aluminum-plastic compound package material - Google Patents
Shaftless spiral vertical-type continuous separation treatment system of aluminum-plastic compound package material Download PDFInfo
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- 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
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- Processing Of Solid Wastes (AREA)
Abstract
本发明提供一种采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统。该系统包括对铝塑复合包装材料进行化学分离处理的分离反应装置,以及对经过化学分离后的铝塑复合包装材料进行物理分离处理的立式分离甩干装置,其中:该分离反应装置中设置的反应螺旋和出料螺旋均为无轴螺旋结构;该立式分离甩干装置的内筒体内设置有转轴,且转轴上间断设置有多个镰刀型叶片。本发明提供的采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统可有效实现对铝塑复合包装材料的连续分离处理,具有较高的铝塑分离处理能力。
The invention provides a vertical continuous separation processing system for aluminum-plastic composite packaging materials using a shaftless spiral. The system includes a separation reaction device for chemical separation of aluminum-plastic composite packaging materials, and a vertical separation and drying device for physical separation of aluminum-plastic composite packaging materials after chemical separation, wherein: the separation reaction device is set The reaction screw and the discharge screw are shaftless screw structures; the inner cylinder of the vertical separation and drying device is provided with a rotating shaft, and a plurality of sickle-shaped blades are intermittently arranged on the rotating shaft. The vertical continuous separation processing system for the aluminum-plastic composite packaging material provided by the invention adopts the shaftless spiral, which can effectively realize the continuous separation processing of the aluminum-plastic composite packaging material, and has high aluminum-plastic separation processing capacity.
Description
技术领域 technical field
本发明属于物料分离技术,特别是涉及一种可对铝塑复合包装材料进行工业化连续分离处理的采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统。 The invention belongs to material separation technology, in particular to a vertical continuous separation processing system for aluminum-plastic composite packaging materials using a shaftless spiral that can carry out industrialized continuous separation processing on aluminum-plastic composite packaging materials.
背景技术 Background technique
纸塑铝复合包装材料是一种常见的包装材料,广泛应用于牛奶和软饮料等包装中。随着人们环保意识的提高以及原料的匮乏,纸塑复合包装的再生利用变得非常必要,在对纸塑复合包装进行再生利用时,通常是将其中的纸基分离后,再将剩余的由铝箔和塑料形成的材料再进行分离。 Paper-plastic-aluminum composite packaging material is a common packaging material, which is widely used in packaging such as milk and soft drinks. With the improvement of people's awareness of environmental protection and the shortage of raw materials, the recycling of paper-plastic composite packaging has become very necessary. When recycling paper-plastic composite packaging, the paper base is usually separated, and then the remaining The material formed by aluminum foil and plastic is then separated.
其中,纸塑铝复合包装废物的再生利用技术主要包括两类,一类是直接再生技术,即将纸塑铝复合包装整体破碎处理后再生成新的原材料;另一类是分离再生技术,即将纸塑铝复合包装中的三种材料分离后分别回收利用。相对分离再生技术而言,直接再生技术主要以生产挤塑塑木和彩乐板为主,其无法有效地回收纸浆、塑料和铝,没有体现纸纤维、铝箔和塑料的自身价值。 Among them, the recycling technology of paper-plastic-aluminum composite packaging waste mainly includes two types, one is direct regeneration technology, that is, the whole paper-plastic-aluminum composite packaging is crushed and processed to generate new raw materials; the other is separation and recycling technology, that is, paper The three materials in the plastic-aluminum composite packaging are separated and recycled separately. Compared with separation and recycling technology, direct recycling technology mainly produces extruded plastic wood and color board, which cannot effectively recycle pulp, plastic and aluminum, and does not reflect the self-value of paper fiber, aluminum foil and plastic.
分离再生技术根据其分离过程可以分为两个部分,首先是纸与铝塑的分离,即纸浆分离技术;其次是铝箔和塑料的分离,即铝塑分离技术。纸与铝塑的分离,通过水力碎浆的方法即可实现,该技术目前比较成熟,应用较广泛。去除了纸浆后的铝塑复合包装材料的铝箔和塑料的分离是分离再生技术的关键和难点。 Separation and regeneration technology can be divided into two parts according to the separation process, the first is the separation of paper and aluminum-plastic, that is, pulp separation technology; the second is the separation of aluminum foil and plastic, that is, aluminum-plastic separation technology. The separation of paper and aluminum-plastic can be realized by the method of hydraulic pulping. This technology is relatively mature and widely used. The separation of the aluminum foil and the plastic of the aluminum-plastic composite packaging material after the pulp is removed is the key and difficult point of the separation and regeneration technology.
目前,在对铝箔和塑料复合形成的铝塑复合包装材料进行分离时,通常采用湿法分离技术,即将铝塑复合包装材料浸泡于分离剂中,通过溶解或溶胀作用破坏各层之间的黏合力从而使铝、塑分开,实现铝塑的化学分离,这个过程也可称为铝塑的化学分离反应;然后再进行甩干、分离等实现铝塑的物理分离。为此,现有技术提出了一种实现铝塑复合包装材料连续分离系统,包括浸泡分离器、离心甩干机和滚筒离心筛分机,其中,浸泡分离器内设置有有轴螺旋来传送物料,其分离过程包括以下步骤:(1)将铝塑复合包装材料投入盛装有分离剂的该浸泡分离器中,经过进行化学分离,并通过有轴螺旋传输至离心甩干机;(2)离心甩干机可将送入的经过化学分离的物料进行甩干处理,脱除其中的分离剂,将甩干后的物料传送至离心筛分机;(3)离心筛分机利用高速转动的中心转子作用下,将铝箔和塑料分离,并分别排出至塑料造粒机和涡流分选器,且涡流分选器可与铝熔炼装置连接得到铝。 At present, when separating aluminum-plastic composite packaging materials formed by compounding aluminum foil and plastic, wet separation technology is usually used, that is, the aluminum-plastic composite packaging materials are soaked in a separating agent, and the adhesion between the layers is destroyed by dissolution or swelling. This process can also be called the chemical separation reaction of aluminum and plastic; and then dry and separate to realize the physical separation of aluminum and plastic. For this reason, the prior art proposes a system for realizing the continuous separation of aluminum-plastic composite packaging materials, including a soaking separator, a centrifugal dryer and a drum centrifugal screening machine, wherein the soaking separator is provided with a shaft screw to convey materials, The separation process includes the following steps: (1) Put the aluminum-plastic composite packaging material into the soaking separator filled with a separating agent, undergo chemical separation, and transfer it to the centrifugal dryer through a shaft screw; (2) Centrifugal drying The dryer can dry the chemically separated materials fed in, remove the separating agent, and transfer the dried materials to the centrifugal screening machine; (3) The centrifugal screening machine uses the high-speed rotating central rotor to , separate the aluminum foil and plastic, and discharge them to the plastic granulator and the vortex separator respectively, and the vortex separator can be connected with the aluminum smelting device to obtain aluminum.
但是,现有连续分离系统中,采用有轴螺旋进行物料传输的浸泡分离器中,由于有轴螺旋自身结构的限制,导致有轴螺旋直径和长度均不能做的过大,从而大大限制了分离器对物料的分离处理能力,使得整个分离系统的物料处理能力较差;且有轴螺旋的柔韧性较差,容易发生物料堵塞,影响整个分离系统的物料分离处理效果;此外,现有分离系统中,对经过化学分离后的物料通过离心甩干机甩干时,为避免物料堵塞和铝箔从塑料上脱离,离心甩干机的最大转速和长度均受到限制,使得离心甩干机的甩干率和处理能力较低,铝屑和分离剂的损失较高;对经离心甩干后的物料通过离心筛分机进行物理分离处理时,为减少堵塞故障率,离心筛分机需采用较低的转速,大大降低了铝塑分离效果和处理能力,此外,为单独回收铝屑,还需在离心筛分机中大量喷加高压水,导致后续废水处理成本增大。总体上而言,现有连续分离工艺不易实现对铝塑复合包装材料进行工业化的大规模连续分离处理。 However, in the existing continuous separation system, in the immersion separator that uses a shafted screw for material transmission, due to the limitation of the shafted screw's own structure, the diameter and length of the shafted screw cannot be made too large, which greatly limits the separation. The separation and processing capacity of the material by the device makes the material processing capacity of the entire separation system poor; and the flexibility of the shafted screw is poor, which is prone to material clogging and affects the material separation and processing effect of the entire separation system; in addition, the existing separation system Among them, when the chemically separated material is dried by a centrifugal dryer, in order to avoid material clogging and aluminum foil detaching from the plastic, the maximum speed and length of the centrifugal dryer are limited, so that the drying speed of the centrifugal dryer is limited. The efficiency and processing capacity are low, and the loss of aluminum chips and separating agent is high; when the material after centrifugal drying is physically separated through the centrifugal screening machine, in order to reduce the clogging failure rate, the centrifugal screening machine needs to use a lower speed , which greatly reduces the separation effect and processing capacity of aluminum and plastics. In addition, in order to recover aluminum chips separately, a large amount of high-pressure water needs to be sprayed in the centrifugal screening machine, resulting in an increase in the cost of subsequent wastewater treatment. Generally speaking, the existing continuous separation process is not easy to realize industrialized large-scale continuous separation treatment of aluminum-plastic composite packaging materials.
发明内容 Contents of the invention
本发明提供一种采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统,可克服现有分离系统存在的物料处理能力差以及容易发生物料堵塞、废水处理成本高的缺陷,可有效提高物料处理能力,减少废水的产生量。 The invention provides a vertical continuous separation processing system for aluminum-plastic composite packaging materials using a shaftless spiral, which can overcome the defects of poor material processing capacity, easy material blockage, and high waste water treatment cost existing in the existing separation system, and can effectively improve Material handling capacity, reduce the amount of wastewater generated.
本发明提供一种采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统,包括对铝塑复合包装材料进行化学分离处理的分离反应装置,以及对经过化学分离后的铝塑复合包装材料进行物理分离处理的立式分离甩干装置, The invention provides a vertical continuous separation processing system for aluminum-plastic composite packaging materials using a shaftless spiral, including a separation reaction device for chemically separating aluminum-plastic composite packaging materials, and a chemically separated aluminum-plastic composite packaging material. Vertical separation and drying device for physical separation treatment,
其中: in:
所述分离反应装置包括具有腔体的分离器,以及设置在所述分离器的腔体内的反应螺旋和出料螺旋; The separation reaction device includes a separator with a cavity, and a reaction screw and a discharge screw arranged in the cavity of the separator;
所述分离器包括反应段和出料段,所述反应段上远离所述出料段的进料端设置有进料口,所述出料段上远离所述反应段的出料端设置有出料口,所述出料端的高度高于进料端的高度; The separator includes a reaction section and a discharge section, the reaction section is provided with a feed port away from the feed end of the discharge section, and the discharge end of the discharge section is provided with a discharge port, the height of the discharge end is higher than the height of the feed end;
所述反应螺旋设置在所述反应段的腔体内,所述出料螺旋设置在所述出料段的腔体内,且所述出料螺旋相对所述反应螺旋垂直设置; The reaction screw is set in the cavity of the reaction section, the discharge screw is set in the cavity of the discharge section, and the discharge screw is vertically arranged relative to the reaction screw;
所述反应螺旋和出料螺旋均为无轴螺旋结构,所述出料螺旋和反应螺旋的一端分别设置有电机; Both the reaction screw and the discharge screw are shaftless helical structures, and one end of the discharge screw and the reaction screw is respectively provided with a motor;
所述立式分离甩干装置包括: The vertical separation and drying device comprises:
垂直设置的筒体,所述筒体包括间隙设置的内筒体和外筒体,所述内筒体的筒壁上设置有筛孔,且所述筒体的下端设置有进料仓,所述进料仓处设置有第一进料口,所述第一进料口与所述分离反应装置上的出料口连接; A vertically arranged cylinder, the cylinder includes an inner cylinder and an outer cylinder with a gap, the wall of the inner cylinder is provided with a screen hole, and the lower end of the cylinder is provided with a feed bin, so A first feed port is provided at the feed bin, and the first feed port is connected to the discharge port on the separation reaction device;
所述外筒体上靠近所述筒体的下端的位置开设有第一排料口,所述筒体上靠近所述筒体的上端的位置开设有贯穿所述外筒体和内筒体的第二排料口,所述第一排料口用于将经过物理分离处理后的铝箔和分离剂混合物排出,所述第二排料口用于将经过物理分离处理后的塑料排出; A position close to the lower end of the outer cylinder is provided with a first discharge port, and a position close to the upper end of the cylinder is opened on the outer cylinder and a hole penetrating through the outer cylinder and the inner cylinder. The second discharge port, the first discharge port is used to discharge the aluminum foil and the separating agent mixture after the physical separation treatment, and the second discharge port is used to discharge the plastic after the physical separation treatment;
所述内筒体内设置有转轴,所述转轴上间断设置有多个镰刀型叶片,且 所述多个镰刀型叶片呈螺旋状分布;所述转轴的下端深入所述进料仓,且所述转轴上深入所述进料仓的转轴部分设置有连续螺旋叶片;所述筒体的上端设置有与所述转轴连接的电机。 A rotating shaft is arranged in the inner cylinder, and a plurality of sickle-shaped blades are intermittently arranged on the rotating shaft, and the plurality of sickle-shaped blades are spirally distributed; the lower end of the rotating shaft goes deep into the feeding bin, and the Continuous helical blades are provided on the part of the rotating shaft that goes deep into the feed bin; the upper end of the cylinder is provided with a motor connected to the rotating shaft.
本发明提供的采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统,通过采用无轴螺旋的分离反应装置对铝塑复合包装材料进行化学分离处理,以及通过设置有镰刀型叶片的立式分离甩干装置对经过化学分离的铝塑复合包装材料进行甩干和分离处理,可有效提高铝塑复合包装材料分离处理能力,在对铝塑复合包装材料处理过程中,可有效避免物料堵塞的问题,减少废水的产生量。 The vertical continuous separation processing system for aluminum-plastic composite packaging materials provided by the present invention uses a shaftless spiral separation reaction device to carry out chemical separation treatment on aluminum-plastic composite packaging materials, and through the vertical separation process provided with sickle-shaped blades The type separation and drying device can dry and separate the chemically separated aluminum-plastic composite packaging materials, which can effectively improve the separation and treatment capacity of aluminum-plastic composite packaging materials, and can effectively avoid material clogging during the processing of aluminum-plastic composite packaging materials. problems and reduce the amount of waste water produced.
附图说明 Description of drawings
图1为本发明实施例提供的采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统的结构示意图; Fig. 1 is a schematic structural view of a vertical continuous separation processing system for aluminum-plastic composite packaging materials provided by an embodiment of the present invention using a shaftless spiral;
图2A为图1中分离反应装置的结构示意图; Fig. 2 A is the structural representation of separation reaction device in Fig. 1;
图2B为图2A中A-A向的剖视图; Fig. 2B is a sectional view of A-A direction in Fig. 2A;
图2C为图2A中B-B向的剖视图; Figure 2C is a cross-sectional view of B-B direction in Figure 2A;
图3A为图1中立式分离甩干装置的结构示意图; 3A is a schematic structural view of the vertical separation and drying device in FIG. 1;
图3B为图3A中A处的局部放大示意图; Fig. 3B is a partially enlarged schematic diagram of A in Fig. 3A;
图3C为图3A中转轴和镰刀型叶片的截面放大示意图; Fig. 3C is a cross-sectional enlarged schematic view of the rotating shaft and the sickle-shaped blade in Fig. 3A;
图4为本发明实施例具体应用的结构示意图。 FIG. 4 is a schematic structural diagram of a specific application of an embodiment of the present invention.
具体实施方式 Detailed ways
鉴于现有技术分离系统存在的物料分离处理能力较差、容易产生物料堵塞和废水产生量大的问题,本发明提供一种采用无轴螺旋式的铝塑复合包装材料立式连续分离处理系统,通过采用无轴螺旋结构的分离反应装置,以及采用可同时对经过化学分离后的铝塑复合包装材料进行甩干和分离处理的立 式分离甩干装置,可有效提高铝塑复合包装材料处理的连续性,减少分离剂以及铝屑的损耗,减少废水的产生量,提高铝塑复合包装材料分离处理能力。下面将以具体实例对本发明技术方案做详细的说明。 In view of the problems of poor material separation and treatment capacity, easy material clogging and large waste water generation in the existing separation system, the present invention provides a vertical continuous separation treatment system for aluminum-plastic composite packaging materials using a shaftless spiral type. By adopting a separation reaction device with a shaftless spiral structure and a vertical separation and drying device that can dry and separate the chemically separated aluminum-plastic composite packaging materials at the same time, the processing efficiency of aluminum-plastic composite packaging materials can be effectively improved. Continuity, reduce the loss of separating agent and aluminum chips, reduce the amount of waste water, and improve the separation and treatment capacity of aluminum-plastic composite packaging materials. The technical solution of the present invention will be described in detail below with specific examples.
图1为本发明实施例提供的采用无轴螺旋的铝塑复合包装材料立式连续分离处理系统的结构示意图;图2A为图1中分离反应装置的结构示意图;图2B为图2A中A-A向的剖视图;图2C为图2A中B-B向的剖视图;图3A为图1中立式分离甩干装置的结构示意图;图3B为图3A中A处的局部放大示意图;图3C为图3A中转轴和镰刀型叶片的截面放大示意图。如图1所示,本实施例分离系统包括分离反应装置10和立式分离甩干装置20,其中,分离反应装置10用于对铝塑复合包装材料进行化学分离处理,可将铝塑复合包装材料浸泡在分离剂中进行化学分离反应,将其中的铝、塑分离;立式分离甩干装置20可用于对经过分离反应装置10处理后的化学分离的铝塑复合包装材料进行甩干和物理分离处理,将其中的铝箔和塑料物理分离,同时对塑料进行脱酸处理,从立式分离甩干装置20排出的塑料可直接制成塑料产品,排出的铝箔可进行脱酸处理后可制成铝屑产品,从而实现对铝塑复合包装材料的分离处理。 Fig. 1 is a schematic structural view of a vertical continuous separation treatment system for aluminum-plastic composite packaging materials provided by an embodiment of the present invention using a shaftless spiral; Fig. 2A is a schematic structural view of the separation reaction device in Fig. 1; Fig. 2B is a direction A-A in Fig. 2A Figure 2C is a cross-sectional view of B-B in Figure 2A; Figure 3A is a schematic structural view of the vertical separation and drying device in Figure 1; Figure 3B is a partially enlarged schematic view of A in Figure 3A; Figure 3C is a rotating shaft in Figure 3A and enlarged cross-sectional schematic diagrams of sickle-shaped blades. As shown in Figure 1, the separation system of this embodiment includes a separation reaction device 10 and a vertical separation and drying device 20, wherein the separation reaction device 10 is used to chemically separate the aluminum-plastic composite packaging material, and the aluminum-plastic composite packaging material The material is soaked in the separating agent to carry out chemical separation reaction, and the aluminum and plastic in it are separated; the vertical separation and drying device 20 can be used to dry and physically separate the chemically separated aluminum-plastic composite packaging material processed by the separation reaction device 10. Separation treatment, the aluminum foil and the plastic are physically separated, and the plastic is deacidified at the same time. The plastic discharged from the vertical separation and drying device 20 can be directly made into a plastic product, and the discharged aluminum foil can be made into a plastic product after deacidification. Aluminum scrap products, so as to realize the separation of aluminum-plastic composite packaging materials.
为便于对本发明实施例技术方案的理解,下面将分别对本实施例中的分离反应装置10和立式分离甩干装置20进行说明。 In order to facilitate the understanding of the technical solution of the embodiment of the present invention, the separation reaction device 10 and the vertical separation and drying device 20 in this embodiment will be described respectively below.
分离反应装置10 Separation reaction device 10
本实施例中,如图2A-图2C所示,分离反应装置10具体可包括分离器101、反应螺旋102和出料螺旋103,其中,该分离器101具有中空的腔体,且该分离器101包括反应段1011和出料段1012,反应段1011上远离出料段1012的进料端A1处设置有进料口10111,出料段1012上远离反应段1011的出料端A2处设置有出料口10121(请见图2C所示),该出料端A2的高度高于进料端A1的高度;反应螺旋102设置在反应段1011的腔体内,出料螺旋103设置在出料段1012的腔体内,且出料螺旋103相对反应螺旋102垂 直设置;反应螺旋102和出料螺旋103均为如图2A所示的无轴螺旋结构,分别安装在反应段1011和出料段1012的两端,其具体安装结构与传统无轴螺旋结构的安装类似,在此不再赘述;出料螺旋103和反应螺旋102的一端分别设置有驱动螺旋结构旋转工作的电机104。本实施例中,分离反应装置10的反应段1011的腔体内可充满分离剂,以对铝塑复合包装材料进行化学分离处理,具体地,可利用反应螺旋102在反应段内的旋转运动,将从进料口10111投入的铝塑复合包装材料传送至出料螺旋103,在该传送过程中,铝塑复合包装材料可在反应段1011内充满的分离剂作用下进行化学分离,经过化学分离处理后的铝塑复合包装材料可通过出料螺旋103由出料口10121排出。 In this embodiment, as shown in Figures 2A-2C, the separation reaction device 10 may specifically include a separator 101, a reaction screw 102 and a discharge screw 103, wherein the separator 101 has a hollow cavity, and the separator 101 includes a reaction section 1011 and a discharge section 1012, the reaction section 1011 is provided with a feed port 10111 away from the feed end A1 of the discharge section 1012, and the discharge section 1012 is provided with a Discharge port 10121 (see Figure 2C), the height of the discharge end A2 is higher than the height of the feed end A1; the reaction screw 102 is set in the cavity of the reaction section 1011, and the discharge screw 103 is set in the discharge section In the cavity of 1012, and the discharge screw 103 is vertically arranged relative to the reaction screw 102; the reaction screw 102 and the discharge screw 103 are shaftless spiral structures as shown in Figure 2A, and are respectively installed in the reaction section 1011 and the discharge section 1012 The specific installation structure is similar to that of the traditional shaftless helical structure, and will not be repeated here; one end of the discharge helix 103 and the reaction helix 102 are respectively provided with a motor 104 that drives the helical structure to rotate. In this embodiment, the cavity of the reaction section 1011 of the separation reaction device 10 can be filled with a separating agent to perform chemical separation treatment on the aluminum-plastic composite packaging material. Specifically, the rotating motion of the reaction screw 102 in the reaction section can be used to separate the The aluminum-plastic composite packaging material input from the feed port 10111 is conveyed to the discharge screw 103. During the conveying process, the aluminum-plastic composite packaging material can be chemically separated under the action of the separating agent filled in the reaction section 1011, and undergoes chemical separation treatment. The final aluminum-plastic composite packaging material can be discharged from the discharge port 10121 through the discharge screw 103.
本实施例中,在对铝塑复合包装材料进行分离处理时,可事先在分离器101的反应段1011内充满有分离剂;经过纸基分离且未经破碎的整片铝塑复合包装材料,可从反应段1011的进料口10111连续不断的投入到分离器101中;投入到分离器101中的整片铝塑复合包装材料可在反应段1011内,随反应螺旋102的转动,一边向反应段1011的出料端即靠近出料螺旋103的一端运动,一边与反应段1011内的分离剂进行化学分离反应,而分离剂不与铝塑复合包装材料一起运动始终存在于反应段1011内;经过化学分离后的铝塑复合包装材料,进入到出料段1012后,可随出料段1012内设置的出料螺旋103的转动,向设置在出料段1012端部的出料口10121运动,并从出料口10121排出,与此同时,铝塑复合包装材料夹带的分离剂从出料螺旋103和出料段1012腔体之间的间隙返流回反应段1011内;从出料口10121排出的经过化学分离的铝塑复合包装材料,可进入如图1所示的立式分离甩干装置20中,并由立式分离甩干装置20对经过化学分离后的铝塑复合包装材料进行甩干和分离处理,得到物理分离的铝箔和塑料,其具体实现过程将在下面做详细说明。 In this embodiment, when the aluminum-plastic composite packaging material is separated, the reaction section 1011 of the separator 101 can be filled with a separating agent; It can be continuously put into the separator 101 from the feed port 10111 of the reaction section 1011; the whole piece of aluminum-plastic composite packaging material put into the separator 101 can be in the reaction section 1011, with the rotation of the reaction screw 102, one side The discharge end of the reaction section 1011 moves close to the end of the discharge screw 103, while chemically separating and reacting with the separating agent in the reaction section 1011, and the separating agent does not move together with the aluminum-plastic composite packaging material and always exists in the reaction section 1011 After the aluminum-plastic composite packaging material after chemical separation enters the discharge section 1012, it can flow to the discharge port 10121 arranged at the end of the discharge section 1012 along with the rotation of the discharge screw 103 arranged in the discharge section 1012. movement, and discharged from the discharge port 10121, at the same time, the separating agent entrained by the aluminum-plastic composite packaging material flows back into the reaction section 1011 from the gap between the discharge screw 103 and the cavity of the discharge section 1012; The chemically separated aluminum-plastic composite packaging material discharged from port 10121 can enter the vertical separation and drying device 20 as shown in Figure 1, and the aluminum-plastic composite packaging material after chemical separation is processed by the vertical separation and drying device 20. The material is dried and separated to obtain physically separated aluminum foil and plastic. The specific realization process will be described in detail below.
本实施例的分离反应装置10中,用于传送物料的反应螺旋102和出料螺 旋103均为无轴螺旋结构,这样,无轴螺旋在制作时,可具有更好的柔韧度,对螺旋同轴性要求不高,使得无轴螺旋的长度和直径均可做的较大,特别是对于反应螺旋102而言,由于反应螺旋102可做的足够长和直径足够大,其传送的物料就越多,且不会产生物料堵塞,可有效提高物料处理能力。可以看出,相对于现有分离系统中采用有轴螺旋的分离器而言,由于有轴螺旋结构的限制,导致有轴螺旋韧性较差,对螺旋同轴性要求极高,使得有轴螺旋的直径和长度均不能做的较大,严重影响物料分离处理能力,且容易发生堵塞现象,而本实施例分离系统通过采用无轴螺旋结构进行物料的传送,可有效提高物料分离处理能力,且不易产生物料堵塞,从而可提高整个分离系统的物料分离处理能力。 In the separation reaction device 10 of the present embodiment, the reaction screw 102 and the discharge screw 103 for conveying materials are both shaftless helical structures, so that the shaftless screw can have better flexibility when making, and it is better for the screw. The requirement of coaxiality is not high, so that the length and diameter of the shaftless helix can be made larger, especially for the reaction helix 102, because the reaction helix 102 can be made long enough and the diameter is large enough, the material it conveys is just The more, and there will be no material clogging, which can effectively improve the material handling capacity. It can be seen that, compared with the separator using the axial spiral in the existing separation system, due to the limitation of the axial spiral structure, the axial spiral has poor toughness, and the requirements for the coaxiality of the spiral are extremely high, so that the axial spiral The diameter and length of the cylinder cannot be made too large, which seriously affects the material separation and processing capacity, and is prone to clogging. However, the separation system of this embodiment uses a shaftless spiral structure for material transmission, which can effectively improve the material separation and processing capacity, and It is not easy to produce material clogging, thereby improving the material separation and processing capacity of the entire separation system.
本实施例中,为确保铝塑复合包装材料在反应段1011内的化学分离效果,反应段1011的外壳可为双层结构的外壳,该双层结构的外壳之间具有空隙,且靠近反应段1011的腔体的内层为导热壳体层,这样,在对铝塑复合包装材料进行分离时,可在该双层结构的外壳的空隙内通水蒸汽,以确保反应段1011内的分离剂的温度可保持在一定的温度范围,提高铝塑复合包装材料的化学分离效果。实际应用中,整个分离器101可一体成型,外壳可采用不锈钢双层夹套结构,这样,在对铝塑复合包装材料进行分离时,就可以通过在夹套中通水蒸汽方式来确保分离器101的腔体内的温度,确保铝塑复合包装材料的分离效果。本领域技术人员可以理解,双层结构的外壳除了可以采用不锈钢制作以外,也可采用其他材料制作而成,例如外层可为非耐磨耐腐蚀隔热材料,内层为耐磨耐腐蚀导热材料的双层结构的外壳,这样,可避免因分离器外壳内通有水蒸汽而对外界环境,特别是操作人员带来危害,提高分离装置工作的安全性,也可减少分离器外壳的材料成本。 In this embodiment, in order to ensure the chemical separation effect of the aluminum-plastic composite packaging material in the reaction section 1011, the shell of the reaction section 1011 can be a double-layer shell with a gap between the shells and close to the reaction section. The inner layer of the cavity of 1011 is a heat-conducting shell layer. In this way, when the aluminum-plastic composite packaging material is separated, water vapor can be passed through the gap of the double-layer shell to ensure that the separation agent in the reaction section 1011 The temperature can be kept in a certain temperature range to improve the chemical separation effect of aluminum-plastic composite packaging materials. In practical applications, the entire separator 101 can be integrally formed, and the outer shell can adopt a stainless steel double-layer jacket structure. In this way, when separating aluminum-plastic composite packaging materials, the separator can be ensured by passing water vapor in the jacket. The temperature in the cavity is 101 to ensure the separation effect of aluminum-plastic composite packaging materials. Those skilled in the art can understand that the shell of the double-layer structure can be made of stainless steel or other materials. For example, the outer layer can be a non-wear-resistant, corrosion-resistant and heat-insulating material, and the inner layer can be made of wear-resistant, corrosion-resistant, and heat-conducting materials. The shell of the double-layer structure of the material, in this way, can avoid the harm to the external environment, especially the operator, due to the water vapor passing through the shell of the separator, improve the safety of the separation device, and can also reduce the material of the shell of the separator. cost.
本领域技术人员可以理解,上述双层结构的外壳中,除了可以通水蒸汽以确保反应段内分离剂的温度外,也可通有其他高温液体或气体,本实施例并不做特别限制。 Those skilled in the art can understand that, in addition to passing water vapor to ensure the temperature of the separating agent in the reaction section, other high-temperature liquids or gases may pass through the above-mentioned double-layer shell, which is not particularly limited in this embodiment.
本实施例的分离反应装置10中,如图2A-图2C所示,反应段1011内设置有2个反应螺旋102,出料段1012内同样设置有2个出料螺旋103,且出料螺旋103和反应螺旋102相对设置。 In the separation reaction device 10 of the present embodiment, as shown in Fig. 2A-Fig. 2C, two reaction spirals 102 are arranged in the reaction section 1011, and two discharge spirals 103 are also arranged in the discharge section 1012, and the discharge spirals 103 and the reaction helix 102 are arranged oppositely.
具体地,如图2A-图2C所示,本实施例中,2个反应螺旋102平行设置在反应段1011的腔体内,2个出料螺旋103分别相对该2个反应螺旋102设置,且反应螺旋102与出料螺旋103的旋转轴之间的夹角为90°,2个出料螺旋103的旋转轴之间的夹角设置为120°,且与铅垂线的夹角均为60°。反应螺旋和出料螺旋这样设置,可以确保从反应段1011传送过来的经过化学分离的物料,能更好的随出料段1012内的出料螺旋103排出,并方便反应驱动电机和出料驱动电机的设置;同时,分离反应装置10工作时,只需要将反应螺旋102浸泡在反应段1011内充满的分离剂中,而出料螺旋103则不需要浸泡在分离剂中,从而避免由出料口排出的物料携带大量的分离剂,从而节省分离剂的使用量。可以看出,通过对出料螺旋103和反应螺旋102相对位置的设置,可有效提高出料螺旋103对反应螺旋102传送过来的物料进行及时处理,避免物料在出料螺旋103的端部堆积。 Specifically, as shown in Figures 2A-2C, in this embodiment, two reaction screws 102 are arranged in parallel in the cavity of the reaction section 1011, and two discharge screws 103 are respectively arranged opposite to the two reaction screws 102, and the reaction The angle between the rotation axes of the spiral 102 and the discharge screw 103 is 90°, the angle between the rotation axes of the two discharge spirals 103 is set to 120°, and the angle with the vertical line is 60° . The setting of the reaction screw and the discharge screw can ensure that the chemically separated materials conveyed from the reaction section 1011 can be better discharged with the discharge screw 103 in the discharge section 1012, and facilitate the reaction drive motor and discharge drive. The setting of motor; Simultaneously, when separating reaction device 10 work, only need reaction screw 102 be soaked in the separating agent that is full of in reaction section 1011, and discharge screw 103 then need not be soaked in separating agent, thereby avoids by discharging The material discharged from the port carries a large amount of separating agent, thereby saving the amount of separating agent used. It can be seen that by setting the relative positions of the discharge screw 103 and the reaction screw 102, the timely processing of the discharge screw 103 on the materials delivered by the reaction screw 102 can be effectively improved, and the accumulation of materials at the end of the discharge screw 103 can be avoided.
本实施例中,反应段1011的腔体可包括2个U型凹槽10112,且2个U型凹槽侧面彼此连通无中间腔体壁;2个反应螺旋102可分别设置在该2个U型凹槽10112内。可以看出,2个U型凹槽10112的设置,可使得2个反应螺旋102分别在各凹槽内工作,减少2个反应螺旋102之间的相互干扰,提高反应螺旋102安装的便利性,以及工作的可靠性和稳定性;同时,在提高物料处理能力的情况下,也可减少分离装置的材料消耗,减少分离装置的占地空间。 In this embodiment, the cavity of the reaction section 1011 may include two U-shaped grooves 10112, and the sides of the two U-shaped grooves communicate with each other without intermediate cavity walls; Type groove 10112. It can be seen that the setting of the two U-shaped grooves 10112 can make the two reaction helices 102 work in each groove, reduce the mutual interference between the two reaction helices 102, and improve the convenience of installation of the reaction helix 102. And the reliability and stability of the work; at the same time, in the case of improving the material handling capacity, it can also reduce the material consumption of the separation device and reduce the space occupied by the separation device.
本实施例中,如图2A和图2C所示,出料段1012可包括相互独立设置的第一出料段10122和第二出料段10123,第一出料段10122和第二出料段10123分别相对反应段1011垂直设置,2个出料螺旋103分别设置在第一出料段10122的腔体内和第二出料段10123的腔体内,出料螺旋103会相对反 应螺旋102垂直设置。本领域技术人员可以理解,第一出料段10122和第二出料段10123远离反应螺旋102的端部分别设置有出料口,以便随出料螺旋103排出的物料可分别从各出料段的出料口排出,这样,各出料口排出的经过化学分离的铝塑复合包装材料,可分别送入立式分离甩干装置而进行物理分离处理,从而提高分离反应装置10化学处理效率。 In this embodiment, as shown in Fig. 2A and Fig. 2C, the discharge section 1012 may include a first discharge section 10122 and a second discharge section 10123 which are set independently of each other, and the first discharge section 10122 and the second discharge section 10123 are arranged vertically relative to the reaction section 1011 respectively, and the two discharge screws 103 are respectively arranged in the cavity of the first discharge section 10122 and the cavity of the second discharge section 10123, and the discharge screw 103 is vertically arranged relative to the reaction screw 102 . Those skilled in the art will understand that the ends of the first discharge section 10122 and the second discharge section 10123 away from the reaction screw 102 are respectively provided with discharge ports, so that the materials discharged with the discharge screw 103 can be discharged from each discharge section respectively. In this way, the chemically separated aluminum-plastic composite packaging materials discharged from each outlet can be sent to the vertical separation and drying device for physical separation treatment, thereby improving the chemical treatment efficiency of the separation reaction device 10.
本实施例中,为提高无轴螺旋工作的稳定性,以及物料可更好地随螺旋运动,可在反应螺旋102远离进料口的一端,即靠近出料螺旋103的一端,设置反应驱动电机;可在出料螺旋103靠近出料口的一端,即远离反应螺旋102的一端,设置出料驱动电机。这样,反应驱动电机就设置在反应螺旋的出料端,而出料驱动电机就设置在出料螺旋的出料端,可有效提高无轴螺旋传输物料的能力。 In this embodiment, in order to improve the stability of the shaftless screw, and the material can better move with the screw, a reaction drive motor can be provided at the end of the reaction screw 102 away from the feed inlet, that is, at the end close to the discharge screw 103. ; The end of the discharge screw 103 close to the discharge port, that is, the end far away from the reaction screw 102, is provided with a discharge drive motor. In this way, the reaction drive motor is arranged at the discharge end of the reaction screw, and the discharge drive motor is arranged at the discharge end of the discharge screw, which can effectively improve the ability of the shaftless screw to transport materials.
立式分离甩干装置20 Vertical separation and drying device 20
本实施例中,立式分离甩干装置20可对经过化学分离处理后的铝塑复合包装材料进行甩干和分离处理,具体地,如图3A-图3C所示,本实施例分离处理系统中的立式分离甩干装置20具体可为立式结构,包括垂直设置的筒体201、转轴202、进料仓203和电机204,其中,筒体201包括内筒体2011和外筒体2012,该内筒体2011和外筒体2012之间具有间隙,且内筒体2011的筒壁上设置有筛孔(图中未示出),即内筒体2011的外壁可为筛网组成;内筒体2011的腔体内设置有转轴202,转轴202上间断设置有多个镰刀型叶片2021,该多个镰刀型叶片2021从下到上呈螺旋状分布;筒体201的下端设置有进料仓203,转轴202的下端深入该进料仓203,且转轴202深入进料仓203的转轴部分设置有连续螺旋叶片2022;外筒体2012上,靠近筒体201的下端的位置开设有第一排料口2013,筒体201上,靠近筒体201的上端的位置开设有贯穿外筒体2012和内筒体2011的第二排料口2014,且进料仓203上设置有第一进料口2031,该第一进料口2031与图1-图2C中的分离反应装置10上的出料口10121连接,且它们之间可通过传送带连接;电 机204安装在筒体201的上端,与转轴202连接,用于驱动转轴202工作。 In this embodiment, the vertical separation and drying device 20 can dry and separate the aluminum-plastic composite packaging material after chemical separation treatment. Specifically, as shown in Figures 3A-3C, the separation treatment system of this embodiment The vertical separation and drying device 20 in the above can be a vertical structure, including a vertical cylinder 201, a rotating shaft 202, a feed bin 203 and a motor 204, wherein the cylinder 201 includes an inner cylinder 2011 and an outer cylinder 2012 , there is a gap between the inner cylinder 2011 and the outer cylinder 2012, and the wall of the inner cylinder 2011 is provided with a screen hole (not shown in the figure), that is, the outer wall of the inner cylinder 2011 can be composed of a screen; A rotating shaft 202 is arranged in the cavity of the inner cylinder 2011, and a plurality of sickle-shaped blades 2021 are intermittently arranged on the rotating shaft 202, and the plurality of sickle-shaped blades 2021 are spirally distributed from bottom to top; the lower end of the cylinder 201 is provided with a feeding bin 203, the lower end of the rotating shaft 202 goes deep into the feeding bin 203, and the rotating shaft part of the rotating shaft 202 going deep into the feeding bin 203 is provided with a continuous spiral blade 2022; on the outer cylinder 2012, a first Discharge port 2013, on the cylinder body 201, a second discharge port 2014 penetrating through the outer cylinder body 2012 and the inner cylinder body 2011 is opened at a position close to the upper end of the cylinder body 201, and the feed bin 203 is provided with a first feed Port 2031, the first feed port 2031 is connected with the discharge port 10121 on the separation reaction device 10 among Fig. 1-Fig. It is connected with the rotating shaft 202 and is used to drive the rotating shaft 202 to work.
本实施例中,经过分离反应装置10处理后的铝塑复合包装材料可直接被传送至立式分离甩干装置20,并由立式分离甩干装置20上独立设置的进料仓203进入立式分离甩干装置20内;通过控制电机204带动转轴202旋转,可将进入进料仓203内的物料吸入连续螺旋叶片2022之间,并随着连续螺旋叶片2022传送到内筒体2011内;在内筒体2011内,物料中的铝箔会在间断设置的镰刀型叶片2021的打击作用下而破碎剥离,此时,被击打出的铝屑就会从内筒体2011筒壁上的筛孔中进入内筒体2011和外筒体2012之间的间隙,并最终落到第一排料口2013,由第一排料口2013排出,而塑料一般都还为整片或体积较大的形状,这些塑料会从筒体201上部设置的第二排料口2014排出,从而实现铝塑的物理分离。在铝塑物理分离的过程中,转轴202旋转产生的离心力同时可除去塑料上的分离剂,对塑料进行除酸处理,而脱出的分离剂可随铝屑一起从第一排料口2013排出,这些分离剂可重新被回收利用,以减少分离剂的消耗和废水处理。 In this embodiment, the aluminum-plastic composite packaging material processed by the separation reaction device 10 can be directly sent to the vertical separation and drying device 20, and enters the vertical separation and drying device 20 from the feeding bin 203 independently provided on the vertical separation and drying device 20. In the type separation and drying device 20; by controlling the motor 204 to drive the rotating shaft 202 to rotate, the material entering the feed bin 203 can be sucked between the continuous helical blades 2022, and sent to the inner cylinder 2011 along with the continuous helical blades 2022; In the inner cylinder 2011, the aluminum foil in the material will be crushed and peeled off under the impact of the sickle-shaped blades 2021 arranged intermittently. enters the gap between the inner cylinder 2011 and the outer cylinder 2012, and finally falls to the first discharge port 2013, and is discharged from the first discharge port 2013, and the plastic is generally in the shape of a whole piece or a large volume , these plastics will be discharged from the second discharge port 2014 provided on the upper part of the cylinder 201, so as to realize the physical separation of aluminum and plastic. In the process of physical separation of aluminum and plastic, the centrifugal force generated by the rotation of the rotating shaft 202 can remove the separating agent on the plastic at the same time, and carry out acid removal treatment on the plastic, and the released separating agent can be discharged from the first discharge port 2013 together with the aluminum chips. These separating agents can be recycled to reduce the consumption of separating agents and waste water treatment.
本实施例中,为达到较好的铝塑物理分离效果,如图3A和图3C所示,镰刀型叶片2021的长度d可为10cm-15cm,而镰刀型叶片2021的高度h可为5cm,此外,镰刀型叶片2021与转轴202的轴向夹角a为75°,使得间隔设置的多个镰刀型叶片2021在转轴202上整体呈螺旋状分布。通过试验,上述镰刀型叶片2021的设置,可使得化学分离后的铝塑复合包装材料的铝塑物理分离率达到99.3%,塑料的甩干度可达到95.5%,使得分离后的塑料可直接进行塑料造粒,制成塑料产品出售或使用。 In this embodiment, in order to achieve a better physical separation effect of aluminum and plastic, as shown in Figure 3A and Figure 3C, the length d of the sickle-shaped blade 2021 can be 10cm-15cm, and the height h of the sickle-shaped blade 2021 can be 5cm, In addition, the axial angle a between the sickle-shaped blades 2021 and the rotating shaft 202 is 75°, so that a plurality of sickle-shaped blades 2021 arranged at intervals are distributed in a spiral shape on the rotating shaft 202 as a whole. Through experiments, the setting of the above-mentioned sickle-shaped blade 2021 can make the aluminum-plastic physical separation rate of the aluminum-plastic composite packaging material after chemical separation reach 99.3%, and the drying degree of plastic can reach 95.5%, so that the separated plastic can be directly processed. Plastic pellets are made into plastic products for sale or use.
本实施例中,为使得铝塑物理分离后的铝屑品质,即铝屑的纯度更高,内筒体2011的筒壁上筛孔的直径可设置为3mm-5mm,经过试验,立式分离甩干装置工作时,甩干过程中产生的塑料的直径一般会大于5mm,因此,当筛孔直径在该尺寸范围时,可有效避免塑料混入铝屑,并可确保铝屑全部从筛孔排出。 In this embodiment, in order to improve the quality of the aluminum chips after the physical separation of aluminum and plastic, that is, the purity of the aluminum chips is higher, the diameter of the sieve hole on the wall of the inner cylinder 2011 can be set to 3mm-5mm. After testing, vertical separation When the drying device is working, the diameter of the plastic produced during the drying process is generally greater than 5mm. Therefore, when the diameter of the screen hole is within this size range, it can effectively prevent the plastic from being mixed with aluminum chips, and ensure that all the aluminum chips are discharged from the screen hole. .
本实施例中,由于进入立式分离甩干装置20内的铝塑复合包装材料通常为大面积的形状,因此,为避免铝塑复合包装材料在立式分离甩干装置20内缠绕转轴202,该转轴202的直径d1可设置为等于或大于20cm。这样,在对物料甩干、分离过程中,避免整片物料对转轴202的缠绕。 In this embodiment, since the aluminum-plastic composite packaging material entering the vertical separation and drying device 20 is generally in the shape of a large area, in order to prevent the aluminum-plastic composite packaging material from winding the rotating shaft 202 in the vertical separation and drying device 20, The diameter d1 of the rotating shaft 202 may be set to be equal to or greater than 20 cm. In this way, in the process of drying and separating the materials, the winding of the entire piece of materials on the rotating shaft 202 is avoided.
本实施例中,上述的进料仓203与筒体201可一体成型,也可分体成型并组装在一起,具体地,如图3A所示,本实施例进料仓203与筒体201一体成型,此时镰刀型叶片2021和连续螺旋叶片2022的转换点位于进料仓203的进料口处;同时,进料仓203与转轴202靠近的侧壁上也可包括外筒体,通过改变外筒体深入进料仓的距离可调节立式分离甩干装置的分离和甩干处理能力。 In this embodiment, the above-mentioned feeding bin 203 and the cylinder body 201 can be integrally formed, or can be formed separately and assembled together. Specifically, as shown in FIG. 3A , the feeding bin 203 and the cylinder body 201 are integrated in this embodiment. Forming, the transition point between the sickle-shaped blade 2021 and the continuous spiral blade 2022 is located at the feed inlet of the feed bin 203; meanwhile, the side wall of the feed bin 203 and the rotating shaft 202 can also include an outer cylinder, by changing The distance that the outer cylinder penetrates into the feeding bin can adjust the separation and drying processing capacity of the vertical separation and drying device.
本实施例中,立式分离甩干装置20在对铝塑分离时,可进行连续、高效的分离,对铝屑和塑料分别回收,同时,在分离的过程中可对塑料进行甩干和脱酸处理,去除塑料中的分离剂,使得脱出的分离剂可随铝屑一起排出,并可回收利用,从而减少了分离剂的浪费。 In this embodiment, the vertical separation and drying device 20 can perform continuous and efficient separation when separating aluminum and plastic, and recycle aluminum chips and plastics separately. At the same time, the plastic can be dried and detached during the separation process. Acid treatment removes the separating agent in the plastic, so that the released separating agent can be discharged together with aluminum chips and can be recycled, thereby reducing the waste of separating agent.
本实施例中,如图1-图3C所示,为对经过物理分离处理后的铝屑进行处理,分离系统还可设置有沉降离心机30和涡流分选器40,其中,沉降离心机30的进料口可与立式分离甩干装置20的第一排料口2013连接,用于对从立式分离甩干装置20排出的铝箔进行脱酸处理,即将其中的分离剂脱除;涡流分选器40与沉降离心机30的固相出口连接,用于去除铝箔中可能存在的纸浆。本实施例中所述的沉降离心机30和涡流分选器40均可采用传统的设备,其具体实现在此不再赘述。 In this embodiment, as shown in Figures 1-3C, in order to process the aluminum chips after physical separation, the separation system can also be provided with a settling centrifuge 30 and a vortex separator 40, wherein the settling centrifuge 30 The feed port of the feed port can be connected with the first discharge port 2013 of the vertical separation and drying device 20, and is used for deacidifying the aluminum foil discharged from the vertical separation and drying device 20, that is, removing the separating agent therein; The separator 40 is connected with the solid phase outlet of the decanter centrifuge 30, and is used to remove the pulp that may exist in the aluminum foil. Both the decanter centrifuge 30 and the vortex separator 40 described in this embodiment can use traditional equipment, and their specific implementation will not be repeated here.
本实施例中,如图1-图3C所示,从分离反应装置10的进料口10111进入的铝塑复合包装材料,可在分离反应装置10内通过无轴螺旋传送到出料口10121,并在传送过程中完成与其中充满分离剂的化学分离反应,将铝箔从塑料中分离,完成铝塑复合包装材料的化学分离;经过化学分离的铝塑复合包装材料会从出料口10121直接排入立式分离甩干装置20的第一进料口 2031,并在立式分离甩干装置20内设置的镰刀型叶片的转轴带动下,实现铝塑的物理分离,分离后的铝屑和塑料分别从立式分离甩干装置20的第一排料口2013和第二排料口2014排出,同时,在铝塑物理分离过程中,铝塑复合包装材料中的分离剂也会随铝屑一起从第一排料口2013排出,从而实现对塑料的脱酸处理;从第二排料口2014排出的塑料,已经过脱酸处理,可直接进行打包处理,或者也可进行简单的漂洗处理后进行打包处理,得到最终的塑料产品;从第一排料口2013排出的铝屑和分离剂可重新进行脱酸处理,以将分离剂从铝屑中脱离,得到所需的铝屑,同时,脱除的分离剂可重新利用。 In this embodiment, as shown in Figures 1-3C, the aluminum-plastic composite packaging material entering from the feed inlet 10111 of the separation reaction device 10 can be conveyed to the discharge port 10121 by a shaftless screw in the separation reaction device 10, And complete the chemical separation reaction with the separating agent in the conveying process, separate the aluminum foil from the plastic, and complete the chemical separation of the aluminum-plastic composite packaging material; the chemically separated aluminum-plastic composite packaging material will be directly discharged from the discharge port 10121 Enter the first feed port 2031 of the vertical separation and drying device 20, and under the drive of the rotating shaft of the sickle-shaped blade arranged in the vertical separation and drying device 20, the physical separation of aluminum and plastic is realized, and the separated aluminum scrap and plastic Discharge from the first discharge port 2013 and the second discharge port 2014 of the vertical separation and drying device 20 respectively. Meanwhile, in the process of physical separation of aluminum and plastic, the separating agent in the aluminum-plastic composite packaging material will also be discharged together with the aluminum chips. Discharged from the first discharge port 2013, thereby realizing the deacidification treatment of plastics; the plastics discharged from the second discharge port 2014 have been deacidified and can be directly packaged or processed after simple rinsing Packing is carried out to obtain the final plastic product; the aluminum scrap and the separating agent discharged from the first discharge port 2013 can be deacidified again to separate the separating agent from the aluminum scrap to obtain the required aluminum scrap, and at the same time, The removed separating agent can be reused.
本实施例中,分离反应装置10内通过设置无轴螺旋对铝塑复合包装材料进行传送,可有效提高铝塑复合包装材料进行化学分离处理的能力;同时,经过化学分离的铝塑复合包装材料可通过立式分离甩干装置20直接进行甩干和分离,可避免现有分别单独采用离心甩干机进行甩干和采用离心筛分机进行物料分离所存在的甩干率、分离率、处理能力较低及废水产生量大的问题,可有效减少铝屑和分离剂的损失,并降低处理能耗。 In this embodiment, the shaftless screw is set in the separation reaction device 10 to convey the aluminum-plastic composite packaging material, which can effectively improve the ability of the aluminum-plastic composite packaging material to carry out chemical separation treatment; at the same time, the chemically separated aluminum-plastic composite packaging material The vertical separation and drying device 20 can be used for direct drying and separation, which can avoid the drying rate, separation rate, and processing capacity of existing separate centrifugal drying machines for drying and centrifugal screening machines for material separation. It can effectively reduce the loss of aluminum chips and separating agent, and reduce the energy consumption of treatment.
为便于对本发明实施例技术方案有更好的了解,下面对本发明实施例的具体应用进行说明。 In order to facilitate a better understanding of the technical solutions of the embodiments of the present invention, specific applications of the embodiments of the present invention will be described below.
图4为本发明实施例具体应用的结构示意图。本实施例中,如图4所示,该分离系统中设置有2个分离反应装置10和2个立式分离甩干装置20,并通过共用离心甩干机30和涡流分选器40,以及其他辅助设备实现对铝塑复合包装材料进行连续的分离处理,具有较好的工业实用性。具体地,如图4所示,分离反应装置10进料口连接有甲酸储存罐501和硝酸存储罐502,并与铝塑传送带60连接;2个立式分离甩干装置20分别与2个分离反应装置10连接,且2个立式分离甩干装置20的第一排料口均与沉降离心机30连接,立式分离甩干装置20的第二排料口通过传送带701可将排出的塑料送入漂洗机702和塑料打包机703,以对塑料做进一步的处理;沉降离心机30的 固相出口连接到涡流分选器40,液相出口连接到分离剂缓存池802,且分离剂缓存池802通过水泵连接到分离反应装置10的进料口。下面将对本实施例分离系统对铝塑复合包装材料的整个分离过程进行说明。 FIG. 4 is a schematic structural diagram of a specific application of an embodiment of the present invention. In the present embodiment, as shown in Figure 4, two separation reaction devices 10 and two vertical separation drying devices 20 are arranged in the separation system, and the centrifugal drying machine 30 and the vortex separator 40 are shared by sharing, and Other auxiliary equipment realizes continuous separation treatment of aluminum-plastic composite packaging materials, which has good industrial practicability. Specifically, as shown in Figure 4, the feed port of the separation reaction device 10 is connected with a formic acid storage tank 501 and a nitric acid storage tank 502, and is connected with the aluminum-plastic conveyor belt 60; The reaction device 10 is connected, and the first discharge ports of the two vertical separation and drying devices 20 are all connected with the sedimentation centrifuge 30, and the second discharge port of the vertical separation and drying devices 20 can discharge the discharged plastic through the conveyor belt 701. Send into rinsing machine 702 and plastic packing machine 703, do further processing to plastic; The solid phase outlet of settling centrifuge 30 is connected to vortex separator 40, and liquid phase outlet is connected to separating agent buffer pool 802, and separating agent buffers The pool 802 is connected to the feed port of the separation reaction device 10 through a water pump. The whole separation process of the aluminum-plastic composite packaging material by the separation system of this embodiment will be described below.
(1)在对铝塑复合包装材料进行处理前,先为分离反应装置10注入分离剂,具体地,可通过甲酸存储罐501和硝酸储存罐502,向分离反应装置10内注入甲酸和硝酸溶液,作为分离剂,并充满分离反应装置10中反应段的腔体。其中的硝酸是作为PH调节剂来使用,且甲酸的浓度为2-4mol/L,硝酸浓度为0.010-0.025mol/L。 (1) Before processing the aluminum-plastic composite packaging material, first inject a separating agent into the separation reaction device 10, specifically, inject formic acid and nitric acid solutions into the separation reaction device 10 through the formic acid storage tank 501 and the nitric acid storage tank 502 , as a separating agent, and fill the cavity of the reaction section in the separation reaction device 10. Nitric acid is used as a pH regulator, and the concentration of formic acid is 2-4mol/L, and the concentration of nitric acid is 0.010-0.025mol/L.
(2)从铝塑传送带60将未经破碎的整片铝塑复合包装材料连续送入分离反应装置10的进料口,同时控制铝塑传送带60的传送速度以及分离反应装置10中反应螺旋的旋转速度,确保分离反应装置10中分离剂与铝塑复合包装材料之间的液固比为30:1-15:1;同时,可向分离反应装置10的分离器外壳的间隙内通入水蒸汽,以确保其中的分离剂的温度维持在40℃-75℃。 (2) From the aluminum-plastic conveyor belt 60, the unbroken whole piece of aluminum-plastic composite packaging material is continuously fed into the feed port of the separation reaction device 10, and the transmission speed of the aluminum-plastic conveyor belt 60 and the speed of the reaction screw in the separation reaction device 10 are controlled at the same time. The rotation speed ensures that the liquid-solid ratio between the separating agent and the aluminum-plastic composite packaging material in the separation reaction device 10 is 30:1-15:1; at the same time, water vapor can be introduced into the gap of the separator shell of the separation reaction device 10 , to ensure that the temperature of the separating agent is maintained at 40°C-75°C.
(3)进入分离反应装置10的铝塑复合包装材料会在反应段内的反应螺旋的带动下一边与分离剂发生分离反应,一边向出料段运动,在此过程中可实现铝塑复合包装材料的化学分离;进入出料段的铝塑复合包装材料会在出料螺旋的带动下,从分离反应装置10的出料口排出,并从立式分离甩干装置20的料口进入立式分离甩干装置20。在此过程中,为确保铝塑复合包装材料化学分离的效果,可适当控制反应螺旋的旋转速度,使得铝塑复合包装材料进入出料段时刚好完成铝塑的化学分离,具体地,本实施例系统中可控制反应螺旋的转速使铝塑复合包装材料在分离剂中的时间为30分钟-40分钟。 (3) The aluminum-plastic composite packaging material entering the separation reaction device 10 will be driven by the reaction spiral in the reaction section to undergo a separation reaction with the separating agent while moving to the discharge section. During this process, the aluminum-plastic composite packaging material can be realized. Chemical separation of materials; the aluminum-plastic composite packaging material entering the discharge section will be discharged from the discharge port of the separation reaction device 10 driven by the discharge screw, and enter the vertical reaction device 20 from the discharge port of the vertical separation and drying device. Separate the drying device 20. In this process, in order to ensure the effect of chemical separation of aluminum-plastic composite packaging materials, the rotation speed of the reaction screw can be properly controlled, so that the chemical separation of aluminum-plastic composite packaging materials just completes when the aluminum-plastic composite packaging materials enter the discharge section. Specifically, this implementation In the example system, the rotation speed of the reaction screw can be controlled so that the time for the aluminum-plastic composite packaging material to be in the separating agent is 30 minutes to 40 minutes.
(4)进入立式分离甩干装置20且经过化学分离的铝塑复合包装材料,在立式分离甩干装置20中的转轴高速旋转作用下,可将铝屑从塑料薄膜上打落,实现铝塑的物理分离,同时对塑料薄膜进行脱酸甩干处理,且物理分离后的塑料薄膜从第二排料口排出,铝屑、分离剂以及少量的塑料和纸浆从 第一排料口排出。 (4) The aluminum-plastic composite packaging material that enters the vertical separation and drying device 20 and undergoes chemical separation can knock off aluminum scraps from the plastic film under the action of the high-speed rotation of the rotating shaft in the vertical separation and drying device 20 to achieve Physical separation of aluminum and plastic, while deacidifying and drying the plastic film, and the physically separated plastic film is discharged from the second discharge port, and aluminum chips, separating agent and a small amount of plastic and pulp are discharged from the first discharge port .
(5)从第二排料口排出的塑料薄膜可经过传送带701传送到塑料打包机703,对塑料薄膜进行打包处理,得到处理后的塑料,且在此过程中可经过漂洗机702对塑料薄膜中少许的分离剂进行脱洗后再进行打包处理。 (5) The plastic film discharged from the second discharge port can be sent to the plastic baler 703 through the conveyor belt 701, and the plastic film is packed to obtain the processed plastic, and the plastic film can be processed by the rinsing machine 702 during this process. A small amount of separating agent in the medium is washed and then packaged.
(6)从第一排料口排出的铝屑、分离剂以及少量的纸浆和塑料可进入沉降离心机30,进行脱酸处理,脱除的酸液即分离剂和少量的塑料会从沉降离心机30的液相出口排出,而脱酸处理后的铝屑和少量的纸浆则会从沉降离心机30的固相出口排出; (6) The aluminum chips, separating agent and a small amount of pulp and plastics discharged from the first discharge port can enter the decanting centrifuge 30 for deacidification treatment, and the removed acid, that is, the separating agent and a small amount of plastics, will be discharged from the settling centrifuge. The liquid phase outlet of the centrifuge 30 is discharged, and the deacidified aluminum chips and a small amount of paper pulp are discharged from the solid phase outlet of the decanter centrifuge 30;
(7)从沉降离心机30排出的铝屑和少量纸浆进入涡流分选器40进行除纸浆处理,铝屑或纸浆与循环水被泵入涡流分选器,纸浆以及少量铝屑随部分循环水从涡流分选器40的上部排出,大部分铝屑随循环水从涡流分选器40下部排出; (7) The aluminum chips and a small amount of pulp discharged from the settling centrifuge 30 enter the vortex separator 40 for pulp removal treatment. The aluminum chips or pulp and circulating water are pumped into the vortex separator, and the pulp and a small amount of aluminum chips are mixed with part of the circulating water. Discharged from the upper part of the vortex separator 40, most of the aluminum chips are discharged from the lower part of the vortex separator 40 with the circulating water;
(8)从涡流分选器40下部排出的铝屑随循环水进入螺旋离心机901进行脱水处理,为进一步降低铝屑含水率,从螺旋离心机901排出的铝屑还需进入烘干机902进行烘干处理,烘干后的铝屑即是最终的物理分离后的铝屑产品。 (8) The aluminum chips discharged from the lower part of the vortex separator 40 enter the screw centrifuge 901 with the circulating water for dehydration treatment. In order to further reduce the moisture content of the aluminum chips, the aluminum chips discharged from the screw centrifuge 901 need to enter the dryer 902 Drying treatment is carried out, and the dried aluminum scrap is the final physically separated aluminum scrap product.
(9)从涡流分选器40上部排出的纸浆和少量铝屑可进入湿式滚筒筛111进行纸塑分离,纸浆与循环水通过湿式滚筒筛111的筛孔排至湿式滚筒筛111下部的斜筛112,从斜筛112上筛出的少量的纸浆后可返回再生纸生产工艺;从湿式滚筒筛111末端排出的少量的铝屑可再次进入涡流分选器40进行循环分离处理。 (9) The pulp and a small amount of aluminum chips discharged from the upper part of the vortex separator 40 can enter the wet drum screen 111 for paper-plastic separation, and the pulp and circulating water are discharged to the inclined screen at the lower part of the wet drum screen 111 through the screen holes of the wet drum screen 111 112, a small amount of pulp screened out from the inclined screen 112 can be returned to the recycled paper production process; a small amount of aluminum chips discharged from the end of the wet drum screen 111 can enter the vortex separator 40 again for circulation and separation treatment.
(10)从沉降离心机30排出的分离剂和少量碎塑料经过筛网801滤出碎塑料后,进入分离剂缓存池802,并通过水泵返回分离反应装置10进行循环利用,筛网801滤出的少量碎塑料可重新返回立式分离甩干装置20进行循环处理。 (10) The separating agent and a small amount of broken plastic discharged from the settling centrifuge 30 pass through the screen 801 to filter out the broken plastic, enter the separating agent buffer pool 802, and return to the separation reaction device 10 for recycling through the water pump, and the screen 801 filters out A small amount of crushed plastics can be returned to the vertical separation and drying device 20 for recycling.
可以看出,本实施例分离系统可有效对铝塑复合包装材料进行分离处 理,可实现铝塑复合包装材料处理的连续分离工艺,可有效节省加料、出料的时间消耗,分离反应时间可缩短至35min,可有效提高分离处理效率。 It can be seen that the separation system of this embodiment can effectively separate the aluminum-plastic composite packaging materials, realize the continuous separation process of aluminum-plastic composite packaging materials, effectively save the time consumption of feeding and discharging, and the separation reaction time can be shortened. The time is shortened to 35 minutes, which can effectively improve the efficiency of separation and treatment.
本实施例中,分离系统可设置有一控制装置,用于对分离反应装置10、立式分离甩干装置20、沉降离心机30以及各传送带、泵等进行控制,以确保各设备运转后,可连续对铝塑复合包装材料进行分离处理。 In this embodiment, the separation system can be provided with a control device, which is used to control the separation reaction device 10, the vertical separation and drying device 20, the sedimentation centrifuge 30, and various conveyor belts, pumps, etc., to ensure that after each equipment is in operation, it can Continuously separate the aluminum-plastic composite packaging materials.
最后应说明的是:以上各实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。 Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than limiting them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some or all of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the various embodiments of the present invention. scope.
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