CN104816400A - A waste paper-plastic composite paper-plastic separation-plastic-skin granulation production system - Google Patents
A waste paper-plastic composite paper-plastic separation-plastic-skin granulation production system Download PDFInfo
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- CN104816400A CN104816400A CN201510249359.7A CN201510249359A CN104816400A CN 104816400 A CN104816400 A CN 104816400A CN 201510249359 A CN201510249359 A CN 201510249359A CN 104816400 A CN104816400 A CN 104816400A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/919—Thermal treatment of the stream of extruded material, e.g. cooling using a bath, e.g. extruding into an open bath to coagulate or cool the material
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- 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
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/18—Drum screens
- B07B1/22—Revolving drums
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- 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
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- 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
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B17/0412—Disintegrating plastics, e.g. by milling to large particles, e.g. beads, granules, flakes, slices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/04—Particle-shaped
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/69—Filters or screens for the moulding material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
- B29C48/80—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
- B29C48/83—Heating or cooling the cylinders
- B29C48/832—Heating
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- 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
- B29B2017/0213—Specific separating techniques
- B29B2017/0217—Mechanical separating techniques; devices therefor
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Paper (AREA)
Abstract
Description
技术领域technical field
本发明属于废旧纸箱处理技术领域,具体说是一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统。The invention belongs to the technical field of waste carton treatment, in particular to a waste paper-plastic composite paper-plastic separation-plastic-skin granulation production system.
背景技术Background technique
我国的经济高速发展,大部分包装材料都在纸箱上附加各类塑料薄膜,彩印压膜而成,采用的是纸塑复合材料,这种材料经济实用、可防霉防潮防渗水,所以大量应用于食品包装,被利用后产生的废弃物再次利用一直是难以处理的大麻烦,牛奶盒包装纸、淋膜纸、PP袋标签等覆纸覆塑材料在生产中或使用后就必须把纸和塑料完全分开,不然无法再回收利用。With the rapid development of our country's economy, most of the packaging materials are made of various types of plastic films on cartons, which are printed and laminated. Paper-plastic composite materials are used. Applied to food packaging, the reuse of waste generated after being used has always been a big trouble that is difficult to deal with. Paper-coated and plastic-coated materials such as milk carton wrapping paper, coated paper, and PP bag labels must be removed during production or after use. Separated completely from plastic, otherwise it cannot be recycled.
废旧纸塑复合材料的回收再利用是资源再生的一种重要途径,但由于纸塑的不同性能,此种材料不能直接处理回收:其原因一是纸袋可以降解,但塑料不能降解;其原因二是塑料可以再生造粒,但纸袋不能再生造粒。若不处理,两者都会造成环境的污染,且浪费了资源。要进行回收,必须先将纸塑进行分离,再分别处理。目前,市场的纸塑分离有采用直接加热,再人工拿出撕扯开的方式。这种方法存在灼伤的危险,且分离不彻底,使利用此方法回收材料再生产的产品性能大大降低,劳动强度大,效率低下。此前的湿式处理法,主要是依靠水的冲击力和湿度分离,纸浆无法收集,而且占地面积大;传统的碎浆机为了实现塑料皮和木浆纤维的分离,大多采用长时间充分浸泡的办法,但容易造成水资源的浪费和污染,而且效率也不高。The recycling and reuse of waste paper-plastic composite materials is an important way to regenerate resources, but due to the different properties of paper and plastic, this material cannot be directly processed and recycled: the first reason is that paper bags can be degraded, but plastics cannot be degraded; the second reason is that It is plastic that can be regenerated and granulated, but paper bags cannot be regenerated and granulated. If left untreated, both will cause environmental pollution and waste resources. To recycle, the paper and plastic must be separated first, and then processed separately. At present, the separation of paper and plastic in the market adopts the method of direct heating, and then manual tearing. There is a risk of burns in this method, and the separation is not complete, so that the performance of the product reproduced by using the recycled material in this method is greatly reduced, the labor intensity is high, and the efficiency is low. The previous wet processing method mainly relied on the impact force of water and the separation of humidity, the pulp could not be collected, and it occupied a large area; in order to separate the plastic skin and wood pulp fibers, most of the traditional pulpers used long-term and fully soaked pulp. method, but it is easy to cause waste and pollution of water resources, and the efficiency is not high.
目前也有进口发达国家的纸塑分离系统,众所周知,发达国家对垃圾分类细化程度较高,而这种发达国家的纸塑分离系统是根据不同的细分垃圾选择不同的分离系统进行处理。国内的垃圾分类还比较粗放,大部分城市仅仅使用了二元式分类,能够循环利用的废旧纸塑复合材料往往掺杂着其它材料,致使进口的发达国家的纸塑分离系统对国内分类的废旧纸塑复合材料的处理有水土不服的情况:一是由于进料口小,生产效率低;二是由于废旧纸塑复合材料内其它杂质较多,经常导致其停车;造成很多垃圾处理厂家花高额外汇购买的进口纸塑分离系统大批量闲置。At present, there are also paper-plastic separation systems imported from developed countries. As we all know, developed countries have a high degree of refinement in waste classification, and this paper-plastic separation system in developed countries selects different separation systems for processing according to different subdivided wastes. Domestic waste classification is still relatively extensive, most cities only use binary classification, and waste paper-plastic composite materials that can be recycled are often mixed with other materials, resulting in the import of paper-plastic separation systems in developed countries. The treatment of paper-plastic composite materials is not acclimatized: one is that the production efficiency is low due to the small feeding port; the other is that there are many other impurities in the waste paper-plastic composite materials, which often cause it to stop; many garbage disposal factories spend high A large number of imported paper-plastic separation systems purchased by foreign exchange are idle.
废纸箱纸塑分离后的塑皮碎片需要回收利用,但如果处理不当,很容易造成对环境的二次污染和原料的浪费。现有的回收处理方式通常是采用水选分选的方式,用水量特别大,此工艺方法存在成本高、对环境污染大等弊端。纸塑分离后,废旧塑料在挤塑成型过程中,由于需要加热和废旧塑料成分的复杂性,会产生大量的有毒烟雾,烟雾里含有氯化氢、甲烷、甲苯、二甲苯等有毒气体以及各种重金属化合物。这些有毒气体如不进行有效的处理,将会对大气造成二次污染。The plastic skin fragments after the separation of waste carton paper and plastic need to be recycled, but if they are not handled properly, it is easy to cause secondary pollution to the environment and waste of raw materials. The existing recycling method usually adopts the method of water separation and sorting, and the water consumption is particularly large. This process method has disadvantages such as high cost and large environmental pollution. After the separation of paper and plastic, during the extrusion molding process of waste plastics, due to the need for heating and the complexity of the components of waste plastics, a large amount of toxic fumes will be produced. The fumes contain toxic gases such as hydrogen chloride, methane, toluene, xylene and various heavy metals. compound. If these toxic gases are not treated effectively, they will cause secondary pollution to the atmosphere.
中国专利申请号:201120206717.3,公开日:2012.02.01的专利文献公开了一种用于垃圾塑料回收处理的设备。它主要是解决现有水选工艺用水量大,运行成本高、对环境污染较大等技术问题。其技术方案要点是:它包括给料输送装置、破碎装置、风选设备、杂质去除装置、造粒设备、控制系统,控制系统分别与给料输送装置、破碎装置、风选设备、杂质去除装置和造粒设备相联接;给料输送装置采用皮带运输机,破碎装置采用锯齿形旋转刀片,风选设备包括热风炉、鼓风机,杂质去除装置包括风选设备膛底,造粒设备包括喂料口上安装的螺旋加料装置、振捣装置和造粒装置;控制系统包括工业计算机和感应装置。它能对垃圾塑料进行回收再利用,且处理工艺相对简单,对环境污染较少。经处理的回收塑料包括垃圾塑料均可用于制造现浇钢筋砼芯模、或用于制造工业、建筑、及日用品等,也可用于制作成生产原料如造粒料等。该实用新型适用于直接收集的废旧塑料的加工,应用于废旧纸箱纸塑分离后的塑料加工时,由于其成分比较复杂,只经过该实用新型物理的处理方法,并不能进行后续的造粒加工。Chinese patent application number: 201120206717.3, publication date: 2012.02.01 patent document discloses a kind of equipment for waste plastic recycling. It mainly solves the technical problems such as large water consumption, high operation cost and large environmental pollution in the existing water separation process. The key points of its technical plan are: it includes feeding conveying device, crushing device, winnowing equipment, impurity removing device, granulating equipment, control system, and the control system is connected with feeding conveying device, crushing device, winnowing equipment, impurity removing device It is connected with the granulation equipment; the feeding conveying device adopts a belt conveyor, the crushing device adopts a sawtooth-shaped rotary blade, the air separation equipment includes a hot blast stove, a blower, the impurity removal device includes the bottom of the air separation equipment chamber, and the granulation equipment includes the installation on the feeding port. The screw feeding device, vibrating device and granulating device; the control system includes industrial computer and induction device. It can recycle garbage plastics, and the treatment process is relatively simple, with less environmental pollution. The processed recycled plastics, including waste plastics, can be used to manufacture cast-in-place reinforced concrete mandrels, or to manufacture industrial, construction, and daily necessities, and can also be used to make production raw materials such as granulated materials. This utility model is suitable for the processing of directly collected waste plastics. When it is applied to the plastic processing after the separation of paper and plastic from waste cartons, due to its complex composition, only the physical treatment method of this utility model cannot be used for subsequent granulation processing. .
中国专利申请号:201420607474.8,公开日:2015.02.25的专利文献公开了一种用于塑料造粒机的低成本烟雾处理装置,包括造粒机烟雾出管、集烟箱、第一管道、异径管、第二管道、第三管道、异径弯头、进水管、第四管道、水箱和出水管;所述集烟箱底部中央设有圆柱形凸起,圆柱形凸起与集烟箱的底面及侧面共同形成个环形集水槽,环形集水槽底部设有排液管,排液管上设有阀门,集烟箱内设有液位计;所述第一管道一端连接集烟箱,另一端依次连接异径管、第二管道、第三管道、异径弯头和第四管道;所述第四管道的一侧设有进水管,进水管顶端设有喷头,第四管道伸入水箱中,水箱底部设有出水管;所述喷头包括进水装置、轴承、轴承座和喷头盖;该装置结构简单,成本低。该实用新型通过环形集水槽和喷头的使用,通过物理方法对塑料造粒机的烟雾颗粒进行了吸收,但不能解决烟雾中的化学成分。Chinese patent application number: 201420607474.8, publication date: 2015.02.25 patent document discloses a low-cost smoke treatment device for plastic granulator, including granulator smoke outlet pipe, smoke collection box, first pipe, different diameter pipe, second pipe, third pipe, different diameter elbow, water inlet pipe, fourth pipe, water tank and water outlet pipe; the center of the bottom of the smoke collection box is provided with a cylindrical protrusion, and the cylindrical protrusion is connected with the smoke collection box The bottom surface and the side of the ring together form an annular sump, the bottom of the annular sump is provided with a drain pipe, the drain pipe is provided with a valve, and a liquid level gauge is provided in the smoke collection box; one end of the first pipe is connected to the smoke collection box, The other end is sequentially connected to the different diameter pipe, the second pipe, the third pipe, the different diameter elbow and the fourth pipe; one side of the fourth pipe is provided with a water inlet pipe, and the top of the water inlet pipe is provided with a nozzle, and the fourth pipe extends into In the water tank, a water outlet pipe is arranged at the bottom of the water tank; the nozzle includes a water inlet device, a bearing, a bearing seat and a nozzle cover; the device has a simple structure and low cost. The utility model absorbs the smog particles of the plastic granulator through physical methods through the use of the annular water collection tank and the nozzle, but cannot solve the chemical components in the smog.
发明内容Contents of the invention
1.要解决的技术问题1. Technical problems to be solved
针对现有技术废旧纸箱纸塑分离以及分离后塑皮碎片和纸浆处理中生产成本较高、水资源浪费、分离后不适于造粒以及挤塑成型过程中烟雾成分复杂、容易造成二次污染的问题,本发明提供了一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统。本发明对废旧纸箱纸塑分离以及分离后塑皮碎片和纸浆进行综合处理,可以实现提高生产效率、用水量少且水资源循环利用、降低生产成本、适于造粒的目的,还是流水线作业,工人劳动强度低;还可以实现将挤塑成型过程中烟雾进行充分处理的目的,处理过程封闭式进行,不会对大气造成二次污染。适用于国内二元化分类的废旧纸塑复合材料的纸塑分离和综合利用。Aiming at the separation of paper and plastic from waste cartons in the prior art and the processing of plastic skin fragments and pulp after separation, the production cost is high, water resources are wasted, separation is not suitable for granulation, and the smoke components in the extrusion molding process are complex and easily cause secondary pollution. Problem, the present invention provides a paper-plastic separation-plastic-skin granulation production system for waste paper-plastic composite materials. In the present invention, the paper-plastic separation of waste cartons and the comprehensive treatment of the separated plastic skin fragments and paper pulp can achieve the purpose of improving production efficiency, reducing water consumption, recycling water resources, reducing production costs, and being suitable for granulation. It is also an assembly line operation. The labor intensity of the workers is low; it can also achieve the purpose of fully treating the smoke in the extrusion molding process. The treatment process is closed and will not cause secondary pollution to the atmosphere. It is suitable for the paper-plastic separation and comprehensive utilization of waste paper-plastic composite materials that are classified domestically.
2.技术方案2. Technical solution
为达到上述目的,本发明方案按以下方式进行:To achieve the above object, the program of the present invention is carried out in the following manner:
一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,包括依次连接的纸塑分离装置、挤塑成型装置和造粒装置,还包括和纸塑分离装置连接的纸浆处理装置以及和挤塑成型装置连接的烟雾处理装置;纸塑分离装置包括进料口A、物料推送机构、挤料器和摩擦机构,物料推送机构和摩擦机构均为桶体结构,进料口设置在物料推送机构的一端并与其相通,挤料器可拆卸安装在物料推送机构的另一端;摩擦机构和挤料器的出料端相连;挤塑成型装置包括进料斗、挤塑机构、过滤机构和冷却池,进料斗的开口和摩擦机构的出塑口通过输送装置连接,物料下落口和挤塑机构的一端相通,挤塑机构的另一端和冷却池之间固定设置有过滤机构;造粒装置包括造粒机构和包装机构,造粒机构和冷却池之间通过输送带连接;包装机构和造粒机构之间通过出料管连通;纸浆处理装置包括纸浆除杂机构和纸浆挤压机构,纸浆除杂机构和摩擦机构的出浆口通过输送泵连通;纸浆挤压机构和纸浆除杂机构的纸浆池通过输送泵连通;烟雾处理装置包括依次连通的化学溶液处理箱、喷淋塔和吸附箱;化学溶液处理箱和挤塑成型装置的排烟管连通。A paper-plastic separation-plastic-skin granulation production system for waste paper-plastic composite materials, including a paper-plastic separation device, an extrusion molding device and a granulation device connected in sequence, and a pulp processing device connected with the paper-plastic separation device and The smoke treatment device connected to the extrusion molding device; the paper-plastic separation device includes a feed port A, a material push mechanism, an extruder and a friction mechanism. Both the material push mechanism and the friction mechanism are barrel structures, and the feed port is set at the One end of the mechanism communicates with it, and the extruder is detachably installed on the other end of the material pushing mechanism; the friction mechanism is connected with the discharge end of the extruder; the extrusion molding device includes a feed hopper, an extrusion mechanism, a filter mechanism and a cooling The pool, the opening of the feeding hopper and the plastic outlet of the friction mechanism are connected by a conveying device, the material drop port communicates with one end of the extrusion mechanism, and a filter mechanism is fixed between the other end of the extrusion mechanism and the cooling pool; the granulation device includes The granulation mechanism and the packaging mechanism, the granulation mechanism and the cooling pool are connected by a conveyor belt; the packaging mechanism and the granulation mechanism are connected by a discharge pipe; the pulp processing device includes a pulp removal mechanism and a pulp extrusion mechanism, and the pulp removal The pulp outlets of the mechanism and the friction mechanism are connected through the delivery pump; the pulp pool of the pulp extrusion mechanism and the pulp removal mechanism are connected through the delivery pump; the smoke treatment device includes a chemical solution treatment box, a spray tower and an adsorption box connected in sequence; The solution processing box is communicated with the exhaust pipe of the extrusion molding device.
优选的方案,摩擦机构包括进水口、立角筛、出浆口、出塑口和电机A,进水口设置在摩擦机构的左端上方位置;立角筛及其电机A呈立角筛在内、电机A在右端固定设置在摩擦机构轴线上,立角筛呈桶筛状;出浆口和出塑口从左至右分别设置在摩擦机构的底部,出塑口靠近立角筛的右端出口处;纸浆除杂机构包括进料管、暂存箱、电机B、纸浆池、杂质收集箱和滚桶筛;进料管一端和纸浆原料池相通,另一端和暂存箱相通;暂存箱和滚桶筛通过连接管相通;滚桶筛正下方设置纸浆池;滚桶筛左端固定连接在固定支架上,其中轴右端和电机B传动连接,左端杂质出口和杂质收集箱相通;纸浆挤压机构包括引料槽、引料板、集料箱、动力设备、支架、集水池和挤压设备;引料槽与纸浆池相通,并通过引料板与挤压设备配合连接;挤压设备固定在框形结构的支架上,集水池设置在挤压设备底部;集料箱设置在挤压设备出口处。Preferably, the friction mechanism includes a water inlet, a vertical angle sieve, a pulp outlet, a plastic outlet and a motor A, and the water inlet is arranged at the position above the left end of the friction mechanism; the vertical angle sieve and its motor A are inside the vertical angle sieve, The motor A is fixedly installed on the axis of the friction mechanism at the right end, and the vertical angle sieve is in the shape of a barrel sieve; the pulp outlet and the plastic outlet are respectively arranged at the bottom of the friction mechanism from left to right, and the plastic outlet is close to the outlet of the right end of the vertical angle sieve ; The pulp removal mechanism includes a feed pipe, a temporary storage box, a motor B, a pulp tank, an impurity collection box and a drum screen; one end of the feed pipe communicates with the pulp raw material tank, and the other end communicates with the temporary storage tank; the temporary storage tank and The drum screen is connected through the connecting pipe; the pulp tank is set directly below the drum screen; the left end of the drum screen is fixedly connected to the fixed bracket, the right end of the shaft is connected to the motor B, and the impurity outlet on the left end is connected to the impurity collection box; the pulp extrusion mechanism Including feed trough, feed plate, collecting box, power equipment, support, sump and extrusion equipment; the feed chute communicates with the pulp tank, and is connected with the extrusion equipment through the feed plate; the extrusion equipment is fixed on the frame structure On the support, the sump is arranged at the bottom of the extrusion equipment; the collection box is arranged at the outlet of the extrusion equipment.
优选的方案,挤塑机构包括推进器、加热器、杂质收集箱和排烟管;推进器呈卧式桶状结构,其左端和进料斗的底端相通、右端和过滤机构相通;加热器覆盖在推进器的外表面;杂质收集箱设置在推进器的右端底面靠近过滤机构处;排烟管设置在推进器的右端顶面;冷却池设置在过滤机构出口处;化学溶液处理箱是分成若干个垂直隔箱的密闭式真空箱,一端通过进气口和挤塑成型装置的排烟管连通,另一端和喷淋塔通过连接管连通,临近的2个垂直隔箱之间通过连接弯管连通,每个隔箱内充有化学溶液,连接弯管的一端在隔箱内化学溶液液面之上,另一端插入至另一隔箱的化学溶液液面之下的隔箱底部;喷淋塔的底部进气口和化学溶液处理箱通过连接管连通,颈部出气口和吸附箱的底部进气口连通;喷淋塔的顶部设置喷淋口;吸附箱上部设置出气口通过排气管和大气连通,内部设置活性碳吸附板,每个活性碳吸附板上均匀分布有吸附孔。In the preferred solution, the extrusion mechanism includes a propeller, a heater, an impurity collection box and a smoke exhaust pipe; the propeller is a horizontal barrel-shaped structure, and its left end communicates with the bottom end of the feed hopper, and its right end communicates with the filter mechanism; the heater Covering the outer surface of the propeller; the impurity collection box is set on the bottom surface of the right end of the propeller close to the filter mechanism; the smoke exhaust pipe is set on the top surface of the right end of the propeller; the cooling pool is set at the outlet of the filter mechanism; the chemical solution treatment box is divided into A closed vacuum box with several vertical compartments, one end communicates with the exhaust pipe of the extrusion molding device through the air inlet, the other end communicates with the spray tower through a connecting pipe, and the adjacent two vertical compartments are connected through a connecting bend. The tubes are connected, each compartment is filled with chemical solution, one end of the connecting elbow is above the liquid level of the chemical solution in the compartment, and the other end is inserted into the bottom of the compartment below the liquid level of the chemical solution in the other compartment; spray The bottom air inlet of the shower tower is connected with the chemical solution treatment box through a connecting pipe, and the neck air outlet is connected with the bottom air inlet of the adsorption box; the top of the spray tower is provided with a spray port; the upper part of the adsorption box is provided with an air outlet through the exhaust The tube is connected to the atmosphere, and an activated carbon adsorption plate is arranged inside, and each activated carbon adsorption plate is evenly distributed with adsorption holes.
优选的方案,挤料器为十字刀结构;物料推送机构为螺旋推进式结构;烟雾处理装置的化学溶液处理箱的垂直隔箱为4个,从左至右依次为第一隔箱、第二隔箱、第三隔箱和第四隔箱,其中:第一隔箱内溶液为碳酸钙溶液,第二隔箱和第三隔箱内为卫生球溶解液,第四隔箱内为碱基混合液,第一隔箱的液面之上设置有油收集口;挤塑机构设置2道,之间通过连接管相通;过滤机构也有2个,为过滤机构A和过滤机构B,分别和第1和第2道挤塑机构相通;造粒装置的造粒机构包括进料口B、操作台、暂存箱、旋转刀具和出料管;进料口B和旋转刀具固定在操作台上表面、暂存箱固定在操作台下表面;进料口B的进口通过输送带和挤塑成型装置的冷却池连接,出口和旋转刀具相连;旋转刀具下料处设置暂存箱,暂存箱通过出料管和包装机构相通。In the preferred scheme, the extruder is a cross knife structure; the material pushing mechanism is a screw propulsion structure; the vertical compartments of the chemical solution treatment box of the smoke treatment device are 4, and from left to right are the first compartment, the second compartments, third compartments and fourth compartments, wherein: the solution in the first compartment is calcium carbonate solution, the second compartment and the third compartment are hygienic ball solution, and the fourth compartment is base For the mixed liquid, there is an oil collection port above the liquid level of the first compartment; there are two extruding mechanisms connected through connecting pipes; there are also two filtering mechanisms, namely filtering mechanism A and filtering mechanism B, respectively The 1st and 2nd extrusion mechanisms are connected; the granulation mechanism of the granulation device includes the feed port B, the operation table, the temporary storage box, the rotary cutter and the discharge pipe; the feed port B and the rotary cutter are fixed on the upper surface of the operation table The temporary storage box is fixed on the lower surface of the operating table; the inlet of the feed port B is connected to the cooling pool of the extrusion molding device through the conveyor belt, and the outlet is connected to the rotary cutter; a temporary storage box is set at the feeding place of the rotary cutter, and the temporary storage box passes through The discharge pipe communicates with the packaging mechanism.
优选的方案,滚桶筛呈右端下倾式结构;挤压设备包括引料辊、上挤压辊和下挤压辊,三辊呈“品”字形结构、上挤压辊在上固定连接在支架上,引料板的前端和引料辊圆面相切,宽度和引料辊的长度一致;挤塑成型装置还包括冷却成型机构,冷却成型机构和第2道挤塑机构通过连接管相通;冷却成型机构的右端连通有过滤机构C,冷却池设置在过滤机构C的出口处;包装机构包括集料斗和称量包装台,集料斗上端和出料管,底端出口和称量包装台相通。In the preferred solution, the drum sieve has a downward-inclining structure at the right end; the extrusion equipment includes a feed roller, an upper extrusion roller and a lower extrusion roller, and the three rollers are in the shape of a "product"; Above, the front end of the material guide plate is tangent to the circular surface of the material guide roller, and the width is consistent with the length of the material guide roller; the extrusion molding device also includes a cooling forming mechanism, which communicates with the second extrusion molding mechanism through a connecting pipe; the cooling forming mechanism The right end is connected with a filter mechanism C, and the cooling pool is set at the outlet of the filter mechanism C; the packaging mechanism includes a collecting hopper and a weighing and packaging platform, the upper end of the collecting hopper is connected to the discharge pipe, and the outlet at the bottom is connected to the weighing and packaging platform.
优选的方案,立角筛为六角筛;电机A为高速电机;滚桶筛为3个,均匀分布在暂存箱的右侧,其内壁均匀设置有挡条,倾角为5~30度;动力设备包括减速机和电机C,电机C和减速机传动式连接,减速机和引料辊、上挤压辊和下挤压辊的中轴通过轴承传动式连接;喷淋塔的喷淋口连接有插至塔底的喷淋管;喷淋塔和化学溶液处理箱之间的连接弯管设置有真空泵;推进器为螺旋式推进器;加热器为电磁加热器或蒸汽加热器;造粒机构还包括引料辊,设置在进料口B和旋转刀具之间;进料口B呈向内收口状。The preferred solution is that the vertical angle screen is a hexagonal screen; the motor A is a high-speed motor; there are 3 drum screens, which are evenly distributed on the right side of the temporary storage box, and the inner wall is evenly equipped with retaining bars, and the inclination angle is 5 to 30 degrees; the power The equipment includes a reducer and a motor C, the motor C is connected to the reducer in transmission mode, the central shaft of the reducer and the lead roller, the upper extrusion roller and the lower extrusion roller is connected through a bearing transmission; the spray port of the spray tower is connected with The spray pipe inserted into the bottom of the tower; the connecting elbow between the spray tower and the chemical solution treatment tank is provided with a vacuum pump; the propeller is a screw propeller; the heater is an electromagnetic heater or a steam heater; It includes a lead roller, which is arranged between the feed port B and the rotary cutter; the feed port B is in the shape of closing inwards.
优选的方案,引料槽和引料板相连通处设置有滤网;沿立角筛内网壁均匀设置摩擦块;喷淋塔内部从上至下等间距平行设置有隔板,每个隔板和喷淋管上都均匀设置有通孔,喷淋塔喷淋液为碱液;过滤机构A、过滤机构B和过滤机构C为液压换网器;液压换网器设置有两套滤网;在暂存箱上和出料管相对的一侧设置鼓风机,鼓风机出风口和暂存箱及出料管相通。In the preferred scheme, a filter screen is provided at the connection between the feed trough and the feed plate; friction blocks are evenly arranged along the inner wall of the vertical angle screen; partitions are arranged in parallel at equal intervals from top to bottom inside the spray tower, and each partition and The spray pipes are uniformly provided with through holes, and the spray liquid of the spray tower is lye; the filter mechanism A, filter mechanism B and filter mechanism C are hydraulic screen changers; the hydraulic screen changer is equipped with two sets of filter screens; A blower is arranged on the side opposite to the discharge pipe on the temporary storage box, and the air outlet of the blower communicates with the temporary storage box and the discharge pipe.
优选的方案,立角筛右侧呈收口状,出塑口靠近立角筛的收口处;滚桶筛转数为1~2转/秒,其筛网目数为20~50目;挡条呈螺旋状分布;引料辊、上挤压辊和下挤压辊材质为橡胶辊;连接弯管插入溶液液面以下的管口连通有分气盘,每个分气盘的上表面和连接弯管相连通,下表面均匀设置有分气盘出气口;冷却成型机构外周设置有冷却水循环管;摩擦机构内水的体积为总容量的60%~80%。The preferred solution is that the right side of the vertical angle sieve is closed, and the plastic outlet is close to the closing position of the vertical angle sieve; the rotation speed of the drum sieve is 1 to 2 revolutions per second, and the mesh number of the screen is 20 to 50 mesh; Distributed in a spiral shape; the material of the lead roller, the upper extrusion roller and the lower extrusion roller is a rubber roller; the connecting elbow is inserted into the nozzle below the liquid level of the solution to communicate with a gas distribution plate, and the upper surface of each gas distribution plate and the connection bend The pipes are connected, and the lower surface is uniformly provided with the air outlet of the gas distribution plate; the outer periphery of the cooling forming mechanism is provided with a cooling water circulation pipe; the volume of water in the friction mechanism is 60% to 80% of the total capacity.
优选的方案,隔板为鲍尔环;活性碳吸附板为口朝下的喇叭口状结构;在引料辊的辊面设置橡胶面或直接为橡胶材质的引料辊,旋转刀具为滚刀组;化学溶液处理箱内化学溶液的液面为箱体高度的60~80%;第二隔箱和第三隔箱内为卫生球溶解液的使用量为30~70克/公斤;喷淋塔的氢氧化钠溶液浓度5~8%。In the preferred solution, the separator is a Pall ring; the activated carbon adsorption plate is a trumpet-shaped structure with the mouth facing downward; a rubber surface or a rubber material direct roller are arranged on the roller surface of the leading roller, and the rotating cutter is a hob unit; The liquid level of the chemical solution in the chemical solution treatment box is 60-80% of the height of the box body; the usage amount of the sanitary ball solution in the second compartment and the third compartment is 30-70 g/kg; The concentration of sodium hydroxide solution is 5-8%.
优选的方案,第三隔箱内化学溶液为葡萄酚酸溶液;喷淋塔喷淋液为氢氧化钠溶液;进料斗上设置自动捣料杆。In the preferred scheme, the chemical solution in the third compartment is a grapevine acid solution; the spray liquid in the spray tower is a sodium hydroxide solution; an automatic tamping rod is set on the feeding hopper.
3.有益效果3. Beneficial effect
采用本发明提供的技术方案,与已有的公知技术相比,具有如下显著效果:Compared with the existing known technology, the technical solution provided by the invention has the following remarkable effects:
(1)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,通过物料推送机构和挤料器配合作用,将各种废旧纸箱处理成碎片,再通过摩擦机构中水和立角筛的协同作用产生高强度涡流揉搓循环,将碎片中的纸塑摩擦分离;分离后纸浆通过暂存箱的引导和滚桶筛的旋转作用,实现了纸塑分离后纸浆除杂效率高的目的,而且是流水线作业,工人劳动强度低,大量过滤后的水还能够循环利用,水资源浪费少;除杂后的纸浆,在引料槽、引料板的配合作用进入挤压机构后,出料厚薄均匀一致;挤压出的水在集水池收集后,还能循环在生产中利用;废旧纸箱纸塑分离后塑皮碎片通过挤塑机构和过滤机构的配合作用,先将塑皮碎片进行高温融化成流体,再经过过滤机构的过滤和挤出成型,最后通过冷却池的冷却,成为适于造粒加工的条状塑料成品,最后进入造粒机构造粒和包装机构包装,整个过程流水线作业,工人劳动强度低,生产效率高,很少用水(只用到了循环冷却水和化学溶液溶解用水),不会造成水资源的浪费和对水资源的污染;烟雾处理装置中利用化学溶液处理箱内若干个垂直隔箱对烟雾进行多级处理,再利用喷淋塔的喷淋对烟雾中的有毒气体成分进行充分的处理,最后利用吸附箱对烟雾中的颗粒物进行吸附吸收,实现了将废旧纸箱纸塑分离后挤塑成型过程中烟雾进行充分处理的目的,处理系统封闭式,不会对大气造成二次污染;(1) The waste paper-plastic composite paper-plastic separation-plastic-skin granulation production system of the present invention, through the cooperation of the material pushing mechanism and the extruder, processes various waste cartons into pieces, and then passes through the friction mechanism in water and vertically The synergistic effect of the angle screen produces a high-intensity vortex kneading cycle, which frictionally separates the paper and plastic in the debris; after separation, the pulp is guided by the temporary storage box and the rotation of the drum screen, which realizes the high efficiency of pulp removal after paper and plastic separation Purpose, and it is an assembly line operation, the labor intensity of the workers is low, a large amount of filtered water can be recycled, and the waste of water resources is less; the pulp after the removal of impurities enters the extrusion mechanism through the cooperation of the feed tank and the feed plate, and is discharged The thickness is uniform; the extruded water can be recycled and used in production after being collected in the sump; after the waste carton paper and plastic are separated, the plastic skin fragments are first subjected to high temperature through the cooperation of the extrusion mechanism and the filter mechanism. It is melted into a fluid, then filtered and extruded by the filter mechanism, and finally cooled by the cooling pool to become a strip-shaped plastic product suitable for granulation processing, and finally enters the granulator to structure the granules and the packaging mechanism for packaging. The whole process is an assembly line operation , the labor intensity of workers is low, the production efficiency is high, and water is rarely used (only circulating cooling water and chemical solution dissolving water are used), which will not cause waste of water resources and pollution of water resources; the chemical solution treatment box is used in the smoke treatment device There are several vertical compartments in the interior for multi-stage treatment of the smoke, and then the spraying of the spray tower is used to fully treat the toxic gas components in the smoke, and finally the adsorption box is used to absorb and absorb the particles in the smoke, realizing the waste. The purpose of fully treating the smoke during the extrusion molding process after the separation of carton paper and plastic, the treatment system is closed, and will not cause secondary pollution to the atmosphere;
(2)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,烟雾处理装置中垂直隔箱为4个,第一隔箱内溶液为碳酸钙溶液,针对烟雾中的甲烷和氯化氢等气体;第二隔箱和第三隔箱内为卫生球溶解液,针对烟雾中的苯基刺激性气体成分;第四隔箱内为碱基混合液,针对烟雾中残留或处理过程生成的酸性气体,对烟雾中的有毒成分都进行了有效处理;挤塑成型装置中2道挤塑机构设置,有利于塑皮碎片内的杂质分批次去除,提高挤塑的纯度,有利于提高产品质量,并防止金属杂质伤及过滤机构;挤塑成型装置出料为条状物料,经过进料口的引导和旋转刀具的连续切断成粒状产品,再经过出料管的输送和包装机构包装,整个装置不间断处理物料,塑皮挤塑成型后造粒均匀、包装方便;(2) In the paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials of the present invention, there are 4 vertical compartments in the smoke treatment device, and the solution in the first compartment is calcium carbonate solution. Hydrogen chloride and other gases; the second compartment and the third compartment are sanitary ball solution, aiming at the phenyl irritating gas components in the smoke; the fourth compartment is a base mixed liquid, aiming at residues in the smoke or generated during the treatment process The acid gas in the smoke has effectively treated the toxic components in the smoke; the setting of two extrusion mechanisms in the extrusion molding device is conducive to the removal of impurities in the plastic skin fragments in batches, improving the purity of the extrusion, and is conducive to improving Product quality, and prevent metal impurities from hurting the filter mechanism; the extrusion molding device discharges the material into strips, which are guided by the feed port and continuously cut by the rotary cutter into granular products, and then conveyed by the discharge pipe and packaged by the packaging mechanism , the whole device processes materials continuously, and the plastic skin is extruded to form uniform granulation and convenient packaging;
(3)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,挤塑成型装置中冷却成型机构的设置,有利于塑料的由固态化缓冲式进行方便挤出成型,防止塑料流体急剧降温而导致不规则变形;集料斗和称量包装台的设置,便于产品的收集和集中包装,提高了生产效率;(3) The paper-plastic separation-plastic-skin granulation production system of the waste paper-plastic composite material of the present invention, the setting of the cooling molding mechanism in the extrusion molding device, is conducive to the convenient extrusion molding of plastics by solidification and buffering, and prevents plastic The rapid cooling of the fluid causes irregular deformation; the setting of the collecting hopper and weighing and packaging table facilitates the collection and centralized packaging of products, and improves the production efficiency;
(4)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,纸塑分离装置的十字刀结构和螺旋推进式物料推送机构的配合作用,使各类废纸箱的碎片化更加容易;烟雾处理装置中插至塔底的喷淋管的设置,可使喷淋在塔内达到无空隙喷淋;真空泵的设置,使整个化学溶液处理箱产生负压真空姿态;挤塑成型装置中推进器为螺旋式推进器,均匀推进,避免挤出成型时时断时续,给后续处理带来困难;加热器为电磁加热器或蒸汽加热器,选用电磁加热器时加热效率较高,选用蒸汽加热器时初始投资少;引料辊的设置,条状物料在切断前进行辊压处理,表面更加平整,使造粒更加均匀;进料口呈向内收口状,使条状物料集中处理,便于旋转刀具集中切断;(4) The paper-plastic separation-plastic-skin granulation production system of the waste paper-plastic composite material of the present invention, the cross-knife structure of the paper-plastic separation device and the spiral propulsion material pushing mechanism cooperate to make various types of waste paper boxes fragmented Easier; the setting of the spray pipe inserted into the bottom of the tower in the smoke treatment device can make the spraying in the tower achieve no gap spraying; the setting of the vacuum pump makes the whole chemical solution treatment box produce a negative pressure vacuum posture; extrusion molding The propeller in the device is a helical propeller, which pushes evenly, avoiding intermittent extrusion molding, which brings difficulties to subsequent processing; the heater is an electromagnetic heater or a steam heater, and the heating efficiency is higher when the electromagnetic heater is selected. When the steam heater is selected, the initial investment is small; the setting of the feeding roller, the strip material is rolled before cutting, the surface is smoother, and the granulation is more uniform; the feeding port is closed inward, so that the strip material can be processed in a centralized manner , which is convenient for centralized cutting by rotary cutters;
(5)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,纸浆处理装置的滚桶筛右端下倾式结构,为纸浆的流动提供动力;引料辊、上挤压辊和下挤压辊的协同作用,即保证了挤压后厚薄均匀,又保证了纸浆挤压除水后的含水率适于后续加工;烟雾处理装置中喷淋塔内隔板和通孔的设置,增加喷淋液在塔内的停留时间和提高喷淋效果;喷淋液为碱液,进一步加强对烟雾中和处理过程生成的酸性气体的处理;挤塑成型装置中液压换网器的使用,能降低换网难度,提高换网效率,而且实现不间断生产过程;内部滤网目数过滤机构A小于过滤机构B,实现阶段式除杂;鼓风机的设置,起到产品冷却和物料吹送的作用,提高了生产效率;(5) In the paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials of the present invention, the right end of the drum screen of the pulp processing device is a downward-inclining structure, which provides power for the flow of pulp; The synergistic effect of the lower extrusion roller not only ensures the uniform thickness after extrusion, but also ensures that the moisture content of the pulp after dehydration is suitable for subsequent processing; Increase the residence time of the spray liquid in the tower and improve the spray effect; the spray liquid is lye, which further strengthens the treatment of the acid gas generated in the smoke neutralization process; the use of hydraulic screen changers in the extrusion molding device, It can reduce the difficulty of changing the screen, improve the efficiency of changing the screen, and realize the uninterrupted production process; the filter mechanism A of the internal filter mesh is smaller than the filter mechanism B, which realizes staged impurity removal; the setting of the blower plays the role of product cooling and material blowing , improving production efficiency;
(6)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,纸塑分离装置的六角筛和高速电机的协同作用,增强了纸塑分离效果,生产效率更高;滚桶筛可以设置多个,提高除杂效率;挡条的使用,可缓冲纸浆的流速,除杂彻底,还可以引导杂质向出口运动;纸浆处理装置的滚桶筛设置3个,是正常生产所需要数量;倾角为5~30度的设置,是发明人长期生产实践得到的最适宜的倾角范围,过大流速过快,影响除杂效果,过低则流速过慢,影响效率;纸浆挤压机构中引料槽和引料板相连通处滤网的设置,有利于防止其它杂质进入挤压后的纸浆;摩擦块的使用,增加涡流揉搓强度,提高纸塑分离的效率;挤压机构中电机C和减速机的配合作用,可以调节三辊的适宜的转速,以适应于加工参数的需要;烟雾处理装置中分气盘和分气盘出气口的设置,使烟雾在化学溶液中均匀出气,提高烟雾在化学溶液中的处理效果;挤塑成型装置中冷却水循环管的使用,冷却效率高并能实现根据工艺需要可控式冷却;(6) The paper-plastic separation-plastic-skin granulation production system of the waste paper-plastic composite material of the present invention, the synergistic effect of the hexagonal screen and the high-speed motor of the paper-plastic separation device enhances the separation effect of paper and plastic, and the production efficiency is higher; Multiple sieves can be installed to improve the efficiency of impurity removal; the use of baffles can buffer the flow rate of pulp, remove impurities thoroughly, and guide impurities to move to the outlet; three drum sieves are installed in the pulp processing device, which is required for normal production Quantity; the setting of the inclination angle of 5 to 30 degrees is the most suitable range of inclination angle obtained by the inventor in long-term production practice. If the flow rate is too large, the flow rate will be too fast, which will affect the effect of impurity removal. If it is too low, the flow rate will be too slow, which will affect the efficiency; the pulp extrusion mechanism The setting of the filter screen at the connection between the middle guide tank and the guide plate is beneficial to prevent other impurities from entering the extruded pulp; the use of friction blocks increases the strength of eddy current rubbing and improves the separation efficiency of paper and plastic; the motor C and The cooperation of the reducer can adjust the appropriate speed of the three rollers to meet the needs of processing parameters; the setting of the gas distribution plate and the gas distribution plate outlet in the smoke treatment device can make the smoke evenly vented in the chemical solution and improve the quality of the smoke. The treatment effect in the chemical solution; the use of the cooling water circulation pipe in the extrusion molding device has high cooling efficiency and can realize controllable cooling according to the process requirements;
(7)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,纸塑分离装置的立角筛右侧呈收口状,方便分离后塑料片的收集;纸浆除杂机构中挡条呈螺旋状分布,生产效果最好,除杂更彻底还不影响物料的流动;滚桶筛转数为1~2转/秒,其筛网目数为20~50目,是发明人根据废旧纸箱纸塑分离后的纸浆特点总结出的最佳工艺参数范围;纸浆挤压机构中橡胶辊的设置,对纸浆缓冲式挤压,有效防止过度挤压而使其含水率不适于后续加工;喷淋塔中隔板为鲍尔环,使喷淋液在鲍尔环的作用下形成涡流而高速旋转,对烟雾高速洗涤,进一步提高喷淋效果;喇叭口状活性碳吸附板的设置,提高有效的吸附面积,增强吸附效果;橡胶面或橡胶材质的使用,使引料辊对条状物料的挤压缓冲式进行,避免挤压过度,影响造粒质量;(7) In the waste paper-plastic composite paper-plastic separation-plastic-skin granulation production system of the present invention, the right side of the vertical angle sieve of the paper-plastic separation device is closed to facilitate the collection of separated plastic pieces; The strips are distributed in a spiral shape, the production effect is the best, and the impurity removal is more thorough without affecting the flow of materials; the rotation speed of the drum sieve is 1 to 2 revolutions per second, and the mesh number of the screen is 20 to 50 meshes. The optimal process parameter range is summarized from the pulp characteristics after paper and plastic separation of waste cartons; the setting of rubber rollers in the pulp extrusion mechanism can buffer the pulp extrusion, effectively preventing excessive extrusion and making its moisture content unsuitable for subsequent processing; The partition in the spray tower is a Pall ring, so that the spray liquid forms a vortex under the action of the Pall ring and rotates at a high speed, washing the smoke at a high speed, and further improving the spraying effect; the setting of the trumpet-shaped activated carbon adsorption plate improves The effective adsorption area enhances the adsorption effect; the use of rubber surface or rubber material makes the extrusion and buffering of the strip material by the leading roller, avoiding excessive extrusion and affecting the quality of granulation;
(8)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,葡萄酚酸溶液的使用,对烟雾中的苯基成分的处理更有针对性,处理效果更好;氢氧化钠溶液的使用,能够处理烟雾中或生产过程中产生的所有酸性气体;自动捣料杆的设置,提高物料下落的均匀性,并避免挤塑机构空转,提高其效率;(8) The paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials of the present invention, the use of grapevine acid solution, is more targeted for the treatment of phenyl components in smoke, and the treatment effect is better; The use of sodium solution can deal with all the acid gases in the smoke or in the production process; the setting of the automatic tamping rod can improve the uniformity of the falling of the material, and avoid the idling of the extrusion mechanism to improve its efficiency;
(9)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,摩擦机构内水的体积为总容量的60%~80%、化学溶液的液面为箱体高度的60~80%、氢氧化钠溶液浓度5~8%以及卫生球溶解液的使用量为30~70克/公斤,是发明人经过长期的生产实践得出的结果,过低将影响处理效果,过高则会提高生产成本;(9) In the waste paper-plastic composite paper-plastic separation-plastic-skin granulation production system of the present invention, the volume of water in the friction mechanism is 60% to 80% of the total capacity, and the liquid level of the chemical solution is 60% to 80% of the height of the box. 80%, the concentration of sodium hydroxide solution is 5-8%, and the dosage of the sanitary ball solution is 30-70 g/kg, which is the result obtained by the inventor through long-term production practice. Too low will affect the treatment effect, too high will increase production costs;
(10)本发明的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,适应于国内垃圾分类二元化分级不彻底的现状,装置设计紧凑,制造成本低,有效解决了覆膜废料不容易作为造纸原料的难题;拓宽了再生纸生产的原料领域;生产过程中无二次污染产生,真正做到了再生资源的合理利用,实现效益最大化,减轻了固体废弃物的处理负担,保护了环境;使用过程容易操作,还可以完全通过电脑监控式操作,安全系数高,便于推广。(10) The paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials of the present invention is adapted to the current situation of incomplete domestic garbage classification, binary classification, compact device design, low manufacturing cost, and effectively solves the problem of film-coated waste. It is not easy to be used as a papermaking raw material; it broadens the field of raw materials for recycled paper production; there is no secondary pollution in the production process, and it truly achieves a reasonable use of renewable resources, maximizes benefits, reduces the burden of solid waste treatment, and protects The environment is improved; the use process is easy to operate, and it can also be operated completely through computer monitoring, with a high safety factor and easy promotion.
附图说明Description of drawings
下面结合附图对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings.
图1是本发明的纸塑分离装置结构示意图;Fig. 1 is a schematic structural view of a paper-plastic separating device of the present invention;
图2是本发明的挤塑成型装置和造粒装置结构示意图;;Fig. 2 is a structural schematic diagram of an extrusion molding device and a granulation device of the present invention;
图3是本发明的纸浆处理装置结构示意图;Fig. 3 is a schematic structural view of the pulp processing device of the present invention;
图4是本发明的烟雾处理装置结构示意图;Fig. 4 is a schematic structural view of the smoke treatment device of the present invention;
图5是本发明的纸浆除杂机构左视图;Fig. 5 is a left view of the pulp removal mechanism of the present invention;
图6本发明的纸浆挤压机构左视图。Fig. 6 is the left side view of the pulp extruding mechanism of the present invention.
图中:1、进料口A;2、物料推送机构;3、挤料器;4、摩擦机构;5、纸浆除杂机构;6、纸浆挤压机构;8、造粒机构;9、包装机构;10、化学溶液处理箱;20、喷淋塔;30、吸附箱;40、真空泵;41、进水口;42、立角筛;43、摩擦块;44、出浆口;45、出塑口;46、电机A;51、进料管;52、暂存箱;53、滚桶筛;54、连接管;55、电机B;56、纸浆池;57、杂质收集箱;58、挡条;59、隔板;61、引料槽;62、引料板;63、引料辊;64、上挤压辊;65、下挤压辊;66、集料箱;67、动力机构;68、支架;69、集水池;71、进料斗;72、挤塑机构;73、过滤机构A;74、过滤机构B;75、冷却成型机构;76、过滤机构C;77、冷却池;80、输送带;81、进料口B;82、操作台;83、引料辊;84、鼓风机;85、暂存箱;86、旋转刀具;87、出料管;91、集料斗;92、称量包装台;101、第一隔箱;102、第二隔箱;103、第三隔箱;104、第四隔箱;105、连接弯管;106、油收集口;107、分气盘;108、分气盘出气口;201、喷淋口;202、喷淋管;203、隔板;301、活性碳吸附板;302、吸附孔;451、挡片;611、滤网;721、推进器;722、加热器;723、杂质收集箱;724、排烟管。In the figure: 1. Feed inlet A; 2. Material pushing mechanism; 3. Extruder; 4. Friction mechanism; 5. Pulp removal mechanism; 6. Pulp extrusion mechanism; 8. Granulation mechanism; 9. Packaging Mechanism; 10, chemical solution treatment box; 20, spray tower; 30, adsorption box; 40, vacuum pump; 41, water inlet; 42, vertical angle screen; 43, friction block; 44, pulp outlet; 45, plastic outlet 46, motor A; 51, feed pipe; 52, temporary storage box; 53, drum screen; 54, connecting pipe; 55, motor B; 56, pulp pool; 57, impurity collection box; 58, bar ; 69. Water collection pool; 71. Feeding hopper; 72. Extrusion mechanism; 73. Filter mechanism A; 74. Filter mechanism B; 75. Cooling forming mechanism; 76. Filter mechanism C; 77. Cooling pool; 80. Conveyor belt ;81, material inlet B; 82, operating table; 83, leading roller; 84, blower; 85, temporary storage box; 86, rotary cutter; 87, discharge pipe; 91, collecting hopper; 92, weighing and packaging platform ; 101, the first compartment; 102, the second compartment; 103, the third compartment; 104, the fourth compartment; 105, the connecting elbow; 106, the oil collection port; Gas tray air outlet; 201, spray port; 202, spray pipe; 203, clapboard; 301, activated carbon adsorption plate; 302, adsorption hole; 451, baffle; 611, filter screen; 721, propeller; 722 , heater; 723, impurity collection box; 724, exhaust pipe.
具体实施方式Detailed ways
下面结合具体的实施例,对本发明作详细描述。The present invention will be described in detail below in conjunction with specific embodiments.
实施例1Example 1
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,包括依次连接的纸塑分离装置、挤塑成型装置和造粒装置,还包括和纸塑分离装置连接的纸浆处理装置以及和挤塑成型装置连接的烟雾处理装置;如图1所示,纸塑分离装置包括进料口A1、物料推送机构2、挤料器3和摩擦机构4,物料推送机构2和摩擦机构4均为桶体结构,进料口1设置在物料推送机构2的一端并与其相通,挤料器3可拆卸安装在物料推送机构2的另一端;摩擦机构4和挤料器3的出料端相连;如图2所示,挤塑成型装置包括进料斗71、挤塑机构72、过滤机构和冷却池77,进料斗71的开口和摩擦机构4的出塑口45通过输送装置连接,物料下落口和挤塑机构72的一端相通,挤塑机构72的另一端和冷却池77之间固定设置有过滤机构;造粒装置包括造粒机构8和包装机构9,造粒机构8和冷却池77之间通过输送带连接;包装机构9和造粒机构8之间通过出料管87连通;如图3所示,纸浆处理装置包括纸浆除杂机构5和纸浆挤压机构6,纸浆除杂机构5和摩擦机构4的出浆口44通过输送泵连通;纸浆挤压机构6和纸浆除杂机构5的纸浆池56通过输送泵连通;如图4所示,烟雾处理装置包括依次连通的化学溶液处理箱10、喷淋塔20和吸附箱30;化学溶液处理箱10和挤塑成型装置的排烟管724连通。A paper-plastic separation-plastic-skin granulation production system for waste paper-plastic composite materials in this embodiment includes a paper-plastic separation device, an extrusion molding device, and a granulation device connected in sequence, and also includes a pulp Processing device and the smog processing device that is connected with extruding molding device; As shown in Figure 1, paper-plastic separating device comprises feed inlet A1, material pushing mechanism 2, extruder 3 and friction mechanism 4, material pushing mechanism 2 and friction mechanism Mechanisms 4 are barrel structures, feed port 1 is set at one end of material pushing mechanism 2 and communicates with it, extruder 3 is detachably installed on the other end of material pushing mechanism 2; friction mechanism 4 and outlet of extruder 3 The feed end is connected; as shown in Figure 2, the extrusion molding device includes a feed hopper 71, an extrusion mechanism 72, a filter mechanism and a cooling pool 77, and the opening of the feed hopper 71 and the plastic outlet 45 of the friction mechanism 4 pass through the conveying device connection, the material drop port communicates with one end of the extruding mechanism 72, and a filter mechanism is fixedly arranged between the other end of the extruding mechanism 72 and the cooling pool 77; It is connected with the cooling pool 77 by a conveyor belt; the packaging mechanism 9 and the granulation mechanism 8 are communicated through a discharge pipe 87; as shown in Figure 3, the pulp processing device includes a pulp removal mechanism 5 and a pulp extrusion mechanism 6, The pulp outlet 44 of the pulp removal mechanism 5 and the friction mechanism 4 is communicated through the delivery pump; the pulp pool 56 of the pulp extrusion mechanism 6 and the pulp removal mechanism 5 is communicated through the delivery pump; as shown in Figure 4, the smoke treatment device includes sequentially The connected chemical solution treatment box 10, the spray tower 20 and the adsorption box 30; the chemical solution treatment box 10 communicates with the exhaust pipe 724 of the extrusion molding device.
本实施例的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统的应用,其步骤如下:The application of the paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials in this embodiment, the steps are as follows:
A、纸塑分离:启动纸塑分离装置,废旧纸塑包装材料从进料口A1进入系统,在物料推送机构2推送作用下,经过挤料器3的分割,分解成废旧纸塑片后进入摩擦机构4;进水口41开始注入系统的循环水,在水的作用下,随着摩擦机构4揉搓循环摩擦作用,使废旧纸塑片摩擦分离,把纸浆充分疏解为纤维,纸浆从出浆口44流出,而分离后的塑片从出塑口45排出;A. Paper-plastic separation: Start the paper-plastic separation device, and the waste paper-plastic packaging materials enter the system from the feeding port A1. Under the push action of the material pushing mechanism 2, they are separated by the extruder 3 and decomposed into waste paper-plastic pieces before entering the system. Friction mechanism 4; the water inlet 41 begins to inject circulating water into the system. Under the action of water, with the rubbing and cyclic friction of the friction mechanism 4, the waste paper and plastic sheets are rubbed and separated, and the pulp is fully decomposed into fibers, and the pulp is released from the pulp outlet 44 flows out, and the separated plastic sheets are discharged from the plastic outlet 45;
B、纸浆除杂:步骤A中出浆口44流出的纸浆通过泵送至纸浆除杂机构5进行除杂,比如金属、塑片、铝箔等杂质;B. Pulp impurity removal: the pulp flowing out of the pulp outlet 44 in step A is pumped to the pulp impurity removal mechanism 5 for impurity removal, such as metal, plastic sheet, aluminum foil and other impurities;
C、纸浆静置沉淀:除杂后的纸浆进入纸浆池56内,纸浆静置3小时后,上清液通过泵送至进水口41循环使用;C. The pulp is left to settle: the pulp after impurity removal enters the pulp tank 56, and after the pulp is left to stand for 3 hours, the supernatant is pumped to the water inlet 41 for recycling;
D、步骤A中出塑口45排出的塑片通过进料斗71自由落体掉入挤塑机构72进行挤塑加工,然后依次通过过滤机构和冷却池77,成为适于造粒加工的条状塑料成品;最后进入造粒机构8造粒和包装机构9包装;D. The plastic sheets discharged from the plastic outlet 45 in step A fall freely into the extrusion mechanism 72 through the feed hopper 71 for extrusion processing, and then pass through the filter mechanism and cooling pool 77 in turn to become strips suitable for granulation processing Plastic finished products; finally enter the granulation mechanism 8 granulation and packaging mechanism 9 packaging;
E、纸浆挤压:纸浆池56内沉淀后的纸浆泵送至引料槽61,并顺着引料板62流入挤压设备;纸浆通过挤压设备的挤压脱水后,产生的纸浆饼掉入集料箱66;挤压出来的水落入集水池69,也通过泵送至进水口41循环使用;E. Pulp extrusion: The pulp settled in the pulp tank 56 is pumped to the feed tank 61, and flows into the extrusion equipment along the feed plate 62; after the pulp is extruded and dehydrated by the extrusion equipment, the pulp cake produced falls into the collecting tank. Feed box 66; the squeezed water falls into the sump 69, and is also pumped to the water inlet 41 for recycling;
F、步骤D中,挤塑机构72产生的烟气通过排烟管724进入烟雾处理装置,在依次连通的化学溶液处理箱10、喷淋塔20和吸附箱30的连续处理作用下,经检测合格的烟气排入大气。F. In step D, the flue gas produced by the extruding mechanism 72 enters the fume treatment device through the smoke exhaust pipe 724. Qualified flue gas is discharged into the atmosphere.
实施例2Example 2
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,基本结构同实施例1,不同之处在于:挤料器3为十字刀结构;物料推送机构2为螺旋推进式结构;摩擦机构4包括进水口41、立角筛42、出浆口44、出塑口45和电机A46,进水口41设置在摩擦机构4的左端上方位置,摩擦机构4内水的体积为总容量的60%%;立角筛42及其电机A46呈立角筛42在内、电机A46在右端固定设置在摩擦机构4轴线上,立角筛42呈桶筛状,沿立角筛42内网壁均匀设置摩擦块43;出浆口44和出塑口45从左至右分别设置在摩擦机构4的底部,出塑口45靠近立角筛42的右端出口处,本实施例中,立角筛42为六角筛;电机A46为高速电机,立角筛42右侧呈收口状,出塑口45靠近立角筛42的收口处;滚桶筛53为3个,均匀分布在暂存箱52的右侧,其内壁均匀设置有挡条58,倾角为5度;如图5所示,纸浆除杂机构5包括进料管51、暂存箱52、电机B55、纸浆池56、杂质收集箱57和滚桶筛53;进料管51一端和纸浆原料池相通,另一端和暂存箱52相通;暂存箱52和滚桶筛53通过连接管54相通;滚桶筛53正下方设置纸浆池56;滚桶筛53左端固定连接在固定支架上,其中轴右端和电机B55传动连接,左端杂质出口和杂质收集箱57相通;滚桶筛53转数为1转/秒,其筛网目数为50目;挡条58呈螺旋状分布;如图6所示,纸浆挤压机构6包括引料槽61、引料板62、集料箱66、动力设备67、支架68、集水池69和挤压设备;引料槽61与纸浆池相通,并通过引料板62与挤压设备配合连接;引料辊63、上挤压辊64和下挤压辊65材质为橡胶辊;挤压设备固定在框形结构的支架68上,集水池69设置在挤压设备底部;集料箱66设置在挤压设备出口处;挤压设备包括引料辊63、上挤压辊64和下挤压辊65,三辊呈“品”字形结构、上挤压辊64在上固定连接在支架68上,引料板62的前端和引料辊63圆面相切,宽度和引料辊63的长度一致;动力设备67包括减速机和电机C,电机C和减速机传动式连接,减速机和引料辊63、上挤压辊64和下挤压辊65的中轴通过轴承传动式连接,引料槽61和引料板62相连通处设置有滤网611;挤塑机构72包括推进器721、加热器722、杂质收集箱723和排烟管724,本实施例中,挤塑机构72设置2道,之间通过连接管相通;过滤机构也有2个,为过滤机构A73和过滤机构B74,分别和第1和第2道挤塑机构72相通;挤塑成型装置还包括冷却成型机构75,冷却成型机构75和第2道挤塑机构72通过连接管相通;冷却成型机构75的右端连通有过滤机构C76,冷却池77设置在过滤机构C76的出口处;本实施例中,过滤机构A73、过滤机构B74和过滤机构C76为液压换网器;液压换网器设置有两套滤网;推进器721呈卧式桶状结构,其左端和进料斗71的底端相通、右端和过滤机构相通;加热器722覆盖在推进器721的外表面;杂质收集箱723设置在推进器721的右端底面靠近过滤机构处;排烟管724设置在推进器721的右端顶面;冷却池77设置在过滤机构出口处;冷却成型机构75外周设置有冷却水循环管;推进器721为螺旋式推进器;加热器722为电磁加热器或蒸汽加热器;造粒机构8还包括引料辊83,设置在进料口B81和旋转刀具86之间;进料口B81呈向内收口状。造粒装置的造粒机构8包括进料口B81、操作台82、暂存箱85、旋转刀具86和出料管87;进料口B81和旋转刀具86固定在操作台82上表面、暂存箱85固定在操作台82下表面;进料口B81的进口通过输送带80和挤塑成型装置的冷却池77连接,出口和旋转刀具86相连;旋转刀具86下料处设置暂存箱85,暂存箱85通过出料管87和包装机构9相通。烟雾处理装置的化学溶液处理箱10的垂直隔箱为4个,从左至右依次为第一隔箱101、第二隔箱102、第三隔箱103和第四隔箱104,临近的2个垂直隔箱之间通过连接弯管105连通;其中:第一隔箱101内溶液为碳酸钙溶液,第二隔箱102和第三隔箱103内为卫生球溶解液,第四隔箱104内为碱基混合液,第一隔箱101的液面之上设置有油收集口106;喷淋塔20的底部进气口和第四隔箱104通过连接管连通,颈部出气口和吸附箱30的底部进气口连通;喷淋塔20的顶部设置喷淋口201;吸附箱30上部设置出气口通过排气管和大气连通,内部设置活性碳吸附板301,每个活性碳吸附板301上均匀分布有吸附孔302;喷淋塔20的喷淋口201连接有插至塔底的喷淋管202;隔板203为鲍尔环;活性碳吸附板301为口朝下的喇叭口状结构;喷淋塔20和化学溶液处理箱10之间的连接弯管105设置有真空泵40;喷淋塔20内部从上至下等间距平行设置有隔板203,每个隔板203和喷淋管202上都均匀设置有通孔,喷淋塔20喷淋液为碱液;连接弯管105插入溶液液面以下的管口连通有分气盘107,每个分气盘107的上表面和连接弯管105相连通,下表面均匀设置有分气盘出气口108;化学溶液处理箱10内化学溶液的液面为箱体高度的60%;第二隔箱102和第三隔箱103内为卫生球溶解液的使用量为30克/公斤;喷淋塔20的氢氧化钠溶液浓度5%。喷淋塔20喷淋液为氢氧化钠溶液。The paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite material in this embodiment has the same basic structure as that of embodiment 1, except that the extruder 3 is a cross-knife structure; the material pushing mechanism 2 is a screw propulsion Type structure; friction mechanism 4 comprises water inlet 41, vertical angle screen 42, slurry outlet 44, plastic outlet 45 and motor A46, and water inlet 41 is arranged on the position above the left end of friction mechanism 4, and the volume of water in friction mechanism 4 is 60%% of the total capacity; the vertical angle sieve 42 and its motor A46 are inside the vertical angle sieve 42, and the motor A46 is fixedly arranged on the friction mechanism 4 axis at the right end. Friction blocks 43 are evenly arranged on the inner network wall; the pulp outlet 44 and the plastic outlet 45 are respectively arranged at the bottom of the friction mechanism 4 from left to right, and the plastic outlet 45 is close to the right end outlet of the vertical angle screen 42. In this embodiment, The vertical angle sieve 42 is a hexagonal sieve; the motor A46 is a high-speed motor, the right side of the vertical angle sieve 42 is closed, and the plastic outlet 45 is close to the closing of the vertical angle sieve 42; there are three drum screens 53, which are evenly distributed in the temporary storage On the right side of the box 52, its inner wall is evenly provided with retaining strips 58, and the inclination angle is 5 degrees; Collection box 57 and drum screen 53; one end of feeding pipe 51 communicates with pulp raw material pool, and the other end communicates with temporary storage tank 52; temporary storage tank 52 and drum screen 53 communicate through connecting pipe 54; drum screen 53 is directly below A pulp pool 56 is set; the left end of the drum screen 53 is fixedly connected to the fixed bracket, the right end of the shaft is connected to the motor B55 transmission, and the impurity outlet on the left end communicates with the impurity collection box 57; The number of meshes is 50 meshes; the retaining bars 58 are distributed in a spiral shape; as shown in Figure 6, the pulp extruding mechanism 6 includes a feeder trough 61, a feeder plate 62, a collection box 66, power equipment 67, a bracket 68, and a sump 69 And extruding equipment; Leading chute 61 communicates with the pulp pool, and is connected with extruding equipment by introducing material plate 62; Leading material roller 63, upper extruding roller 64 and lower extruding roller 65 materials are rubber rollers; Extruding equipment is fixed on On the support 68 of the frame structure, the sump 69 is arranged at the bottom of the extruding equipment; the collecting box 66 is arranged at the outlet of the extruding equipment; The three rollers are in the shape of a "product", the upper squeeze roller 64 is fixedly connected to the bracket 68, the front end of the guide plate 62 is tangent to the circular surface of the guide roller 63, and the width is consistent with the length of the guide roller 63; the power equipment 67 includes a deceleration Machine and motor C, motor C and reducer drive connection, reducer and feed roller 63, upper extrusion roller 64 and lower extrusion roller 65 are connected through bearing transmission type, feed groove 61 and feed plate 62 are connected A filter screen 611 is provided at the place; the extrusion mechanism 72 includes a propeller 721, a heater 722, an impurity collection box 723 and a smoke exhaust pipe 724. In this embodiment, the extrusion mechanism 72 is provided with 2 roads, which are connected through connecting pipes; There are also 2 filter mechanisms, which are filter mechanism A73 and filter mechanism B7 4. Communicate with the first and second extrusion molding mechanisms 72 respectively; the extrusion molding device also includes a cooling molding mechanism 75, and the cooling molding mechanism 75 communicates with the second extrusion molding mechanism 72 through a connecting pipe; the right end of the cooling molding mechanism 75 There is a filter mechanism C76 in communication, and the cooling pool 77 is arranged at the outlet of the filter mechanism C76; in this embodiment, the filter mechanism A73, the filter mechanism B74 and the filter mechanism C76 are hydraulic screen changers; the hydraulic screen changer is provided with two sets of filter screens Propeller 721 is a horizontal barrel structure, its left end communicates with the bottom end of feed hopper 71, and the right end communicates with filter mechanism; heater 722 covers the outer surface of propeller 721; impurity collection box 723 is arranged on propeller 721 The bottom surface of the right end of the filter is close to the filter mechanism; the smoke exhaust pipe 724 is arranged on the top surface of the right end of the propeller 721; the cooling pool 77 is arranged at the outlet of the filter mechanism; the outer periphery of the cooling forming mechanism 75 is provided with a cooling water circulation pipe; The heater 722 is an electromagnetic heater or a steam heater; the granulation mechanism 8 also includes a guide roller 83, which is arranged between the feed port B81 and the rotary cutter 86; the feed port B81 is inwardly closed. The granulation mechanism 8 of the granulation device comprises a feeding port B81, an operating table 82, a temporary storage box 85, a rotary cutter 86 and a discharge pipe 87; the feeding port B81 and the rotating cutter 86 are fixed on the upper surface of the operating table 82, temporarily stored The box 85 is fixed on the lower surface of the console 82; the inlet of the feed port B81 is connected to the cooling pool 77 of the extrusion molding device through the conveyor belt 80, and the outlet is connected to the rotary cutter 86; a temporary storage box 85 is set at the feeding place of the rotary cutter 86, The temporary storage box 85 communicates with the packaging mechanism 9 through a discharge pipe 87 . There are 4 vertical compartments of the chemical solution treatment box 10 of the smog processing device, which are the first compartment 101, the second compartment 102, the third compartment 103 and the fourth compartment 104 from left to right, and the adjacent 2 Two vertical compartments are communicated by connecting elbow 105; wherein: the solution in the first compartment 101 is a calcium carbonate solution, the second compartment 102 and the third compartment 103 are hygienic ball dissolving solution, and the fourth compartment 104 Inside is a base mixture, and an oil collection port 106 is arranged above the liquid level of the first compartment 101; the air inlet at the bottom of the spray tower 20 communicates with the fourth compartment 104 through a connecting pipe, and the neck gas outlet and the adsorption The bottom air inlet of box 30 is communicated; The top of spray tower 20 is provided with spray port 201; 301 is evenly distributed with adsorption holes 302; the spray port 201 of the spray tower 20 is connected with a spray pipe 202 inserted into the bottom of the tower; the partition 203 is a Pall ring; the activated carbon adsorption plate 301 is a bell mouth facing downward shape structure; the connection elbow 105 between the spray tower 20 and the chemical solution treatment box 10 is provided with a vacuum pump 40; the inside of the spray tower 20 is equidistantly arranged with partitions 203 in parallel from top to bottom, and each partition 203 and spray Shower pipes 202 are uniformly provided with through holes, and the spraying liquid of spray tower 20 is lye; connecting elbow 105 is inserted into the nozzle below the liquid level of the solution to communicate with gas distribution discs 107, and the upper surface of each gas distribution disc 107 It is connected with the connecting elbow 105, and the lower surface is uniformly provided with a gas distribution plate outlet 108; the liquid level of the chemical solution in the chemical solution treatment box 10 is 60% of the height of the box; the second compartment 102 and the third compartment 103 The usage amount of the hygienic ball dissolving solution is 30 g/kg; the sodium hydroxide solution concentration of the spray tower 20 is 5%. The spray liquid of the spray tower 20 is sodium hydroxide solution.
本实施例的废旧纸塑复合材料纸塑分离-塑皮造粒生产系统的应用,具体步骤同实施例1,不同之处在于:The application of the paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials in this embodiment, the specific steps are the same as in embodiment 1, the difference lies in:
步骤A中,进水口41开始注入系统的循环水,电机A46带动立角筛42高速旋转,在水的作用下形成高强度涡流揉搓循环摩擦作用,使废旧纸塑片在全方位高强度受到冲击和纸塑的摩擦分离,把纸浆充分疏解为纤维,在水的润胀作用下,避免了纸浆纤维的切断;In step A, the water inlet 41 starts to inject the circulating water of the system, and the motor A46 drives the vertical angle screen 42 to rotate at a high speed, forming a high-intensity eddy current rubbing cycle friction under the action of the water, so that the waste paper and plastic sheets are impacted in all directions with high strength Separated from the friction of paper and plastic, the pulp is fully decomposed into fibers, and under the swelling action of water, the cutting of pulp fibers is avoided;
步骤B中,出浆口44流出的纸浆通过泵送至纸浆除杂机构5的进料管51,并顺流至暂存箱52,在暂存箱52的分配作用下,纸浆通过连接管54流入每个滚桶筛53;在电机B55带动下,滚桶筛53均速旋转,除杂后的纸浆通过筛网网眼,在重力作用下,垂直落入纸浆池56;没有通过筛网网眼的杂质,比如金属、塑片、铝箔等,通过滚桶筛53侧端的杂质出口落入杂质收集箱57;In step B, the pulp flowing out of the pulp outlet 44 is pumped to the feed pipe 51 of the pulp removal mechanism 5, and flows downstream to the temporary storage tank 52. Under the distribution of the temporary storage tank 52, the pulp passes through the connecting pipe 54 It flows into each drum screen 53; driven by the motor B55, the drum screen 53 rotates at a uniform speed, and the pulp after removal of impurities passes through the mesh of the screen, and falls vertically into the pulp pool 56 under the action of gravity; the pulp that does not pass through the mesh of the screen Impurities, such as metal, plastic sheet, aluminum foil, etc., fall into the impurity collection box 57 through the impurity outlet at the side end of the drum sieve 53;
步骤D中,步骤A出塑口45排出的塑片通过进料斗71自由落体掉入挤塑机构72的推进器721,在加热器722的持续加热下,塑皮碎片进行高温融化成流体,再经过过滤机构过滤作用,不能融化的杂质在推进至过滤机构时,掉落至杂质收集箱723内暂存;塑料流体经过过滤机构的过滤和挤出成型,最后通过冷却池77的冷却,成为适于造粒加工的条状塑料成品;2道挤塑机构72加冷却成型机构75、过滤机构A73、过滤机构B74和过滤机构C76的设置,使流体化的塑料经过2次挤塑、2次过滤和1次冷却后挤出成型;挤塑成型装置出料为条状物料经输送带80输送至进料口81,在进料口81的引导和旋转刀具86的连续切断成粒状产品,再经过出料管87的输送和包装机构9包装,整个装置不间断处理物料,且造粒均匀、质量稳定;In step D, the plastic sheet discharged from the plastic outlet 45 of step A falls freely into the propeller 721 of the extrusion mechanism 72 through the feed hopper 71, and under the continuous heating of the heater 722, the plastic skin fragments are melted into a fluid at high temperature, After being filtered by the filter mechanism, the impurities that cannot be melted will fall into the impurity collection box 723 for temporary storage when they are advanced to the filter mechanism; the plastic fluid is filtered and extruded by the filter mechanism, and finally cooled by the cooling pool 77 to become Strip-shaped plastic products suitable for granulation processing; 2-way extrusion mechanism 72 plus cooling molding mechanism 75, filter mechanism A73, filter mechanism B74 and filter mechanism C76 are set to make the fluidized plastic go through 2 times of extrusion, 2 times Extrusion molding after filtering and primary cooling; the extruding molding device discharges the material as strips and is transported to the feed inlet 81 by the conveyor belt 80, and is guided by the feed inlet 81 and continuously cut by the rotary cutter 86 into granular products, and then After being conveyed by the discharge pipe 87 and packaged by the packaging mechanism 9, the whole device can process materials without interruption, and the granulation is uniform and the quality is stable;
步骤E中,滚桶筛53右端下倾式结构,为纸浆的流动提供动力;引料辊63、上挤压辊64和下挤压辊65的协同作用,即保证了挤压后厚薄均匀,又保证了纸浆挤压除水后的含水率适于后续加工;纸浆挤压机构中电机C和减速机的配合作用,可以调节三辊的适宜的转速,以适应于加工参数的需要;滚桶筛53设置3个,是正常生产所需要数量,挡条58的使用,可缓冲纸浆的流速,除杂彻底,还可以引导杂质向出口运动;纸浆挤压机构6中引料槽61和引料板62相连通处滤网611的设置,有利于防止其它杂质进入挤压后的纸浆;纸浆挤压机构中橡胶辊的设置,对纸浆缓冲式挤压,有效防止过度挤压而使其含水率不适于后续加工;In step E, the right end of the drum screen 53 has a downward-inclining structure, which provides power for the flow of pulp; the synergistic effect of the feed roller 63, the upper extrusion roller 64 and the lower extrusion roller 65 ensures uniform thickness after extrusion, and It ensures that the moisture content of the pulp extruded after water removal is suitable for subsequent processing; the cooperation between the motor C and the reducer in the pulp extruding mechanism can adjust the appropriate speed of the three rollers to meet the needs of processing parameters; drum screen 53 is provided with 3, which is the required quantity for normal production. The use of retaining bar 58 can buffer the flow velocity of pulp, remove impurities thoroughly, and guide impurities to move to the outlet; in the pulp extrusion mechanism 6, the feed groove 61 is connected with the feed plate 62 The setting of the filter screen 611 at the pass is beneficial to prevent other impurities from entering the extruded pulp; the setting of the rubber roller in the pulp extruding mechanism can effectively prevent excessive extrusion and make the moisture content unsuitable for subsequent pulp extrusion. processing;
步骤F中,挤塑成型装置在加热过程中,产生的烟气通过排烟管724进入烟雾处理装置中第一隔箱101后快速冷却至30℃以下,一部分烟雾在弱碱性碳酸钙溶液的作用下生成钙质塑胶油;钙质塑胶油通过油收集口106定期收集排出箱体,作为原材料二次塑化时利用;未参与反应的烟雾通过连接弯管105通入第二隔箱102和第三隔箱103卫生球溶解液的液面以下进行两次除臭,去除烟雾中的有刺鼻气味、低毒的甲苯、二甲苯等苯基成分;烟雾除臭后,通过连接弯管105通入第四隔箱104的碱基混合液进行碱化反应,去除占烟雾中的主要成分的酸性气体;在真空泵40的作用下,未处理完全的烟雾被输送至喷淋塔20的底部,在从喷淋口201喷出的碱液的作用下,酸性气体进行充分的反应;充分反应后烟雾主要成分为二氧化碳、水气以及烟雾颗粒,通入吸附箱30进行颗粒吸附,在活性碳吸附板301和吸附孔302的作用下,进行充分的吸附后,经过检测达标后,通过排气烟囱排放入大气,如不达标,通过回气管道返回烟雾处理装置进行二次处理。In step F, during the heating process of the extrusion molding device, the smoke generated enters the first compartment 101 of the smoke treatment device through the smoke exhaust pipe 724 and is rapidly cooled to below 30°C. The calcareous plastic oil is generated under the action; the calcareous plastic oil is regularly collected and discharged from the box through the oil collection port 106, and used as a raw material for secondary plasticization; the smoke that has not participated in the reaction is passed into the second compartment 102 and the second compartment 102 through the connecting elbow 105. Carry out deodorization twice below the liquid level of the third compartment 103 hygienic ball dissolving solution, remove the phenyl components such as pungent smell, low toxicity toluene, xylene in the smoke; Pass into the base mixed liquor of the fourth compartment 104 to carry out alkalization reaction, remove the acid gas that accounts for the main component in the smog; Under the action of the lye sprayed from the spray port 201, the acid gas reacts fully; the main components of the smog after the full reaction are carbon dioxide, water vapor and smog particles, which are passed into the adsorption box 30 for particle adsorption. Under the action of the plate 301 and the adsorption hole 302, after sufficient adsorption is carried out, after the test reaches the standard, it is discharged into the atmosphere through the exhaust chimney. If it does not meet the standard, it is returned to the smoke treatment device through the return air pipeline for secondary treatment.
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,推进器721为螺旋式推进器,均匀推进,避免挤出成型时时断时续,给后续处理带来困难;加热器722为蒸汽加热器,初始投资少;2道挤塑机构72设置,有利于塑皮碎片内的杂质分批次去除,提高挤塑的纯度,有利于提高产品质量,并防止金属杂质伤及过滤机构;冷却成型机构75的设置,有利于塑料的由固态化缓冲式进行方便挤出成型,防止塑料流体急剧降温而导致不规则变形;液压换网器的使用,能降低换网难度,提高换网效率,而且实现不间断生产过程;内部滤网目数过滤机构A小于过滤机构B,实现阶段式除杂;冷却水循环管的使用,冷却效率高并能实现根据工艺需要可控式冷却。In this embodiment, a paper-plastic separation-plastic-skin granulation production system for waste paper-plastic composite materials, the propeller 721 is a screw propeller, which propels evenly and avoids intermittent extrusion molding, which brings difficulties to subsequent processing; The heater 722 is a steam heater, and the initial investment is small; 2 extruding mechanisms 72 are set up, which is conducive to the removal of impurities in the plastic skin fragments in batches, improves the purity of extrusion, is conducive to improving product quality, and prevents metal impurities from being damaged. and filter mechanism; the setting of cooling forming mechanism 75 is conducive to the convenient extrusion molding of plastic by solidification buffer type, preventing the plastic fluid from sharply cooling and causing irregular deformation; the use of hydraulic screen changer can reduce the difficulty of changing the screen, Improve the efficiency of screen replacement and realize uninterrupted production process; the internal filter mesh filter mechanism A is smaller than the filter mechanism B to realize staged impurity removal; the use of cooling water circulation pipes has high cooling efficiency and can realize controllable cooling according to process needs .
实施例3Example 3
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,基本结构同实施例2,不同之处在于:摩擦机构4内水的体积为总容量的70%;滚桶筛53倾角为30度,转数为2转/秒,筛网目数为20目;进料斗71上设置自动捣料杆,避免在进料斗71内因塑皮较轻而不落料;加热器722为电磁加热器;挤塑机构设置和PLC连接的温度检测和监控机构。包装机构9包括集料斗91和称量包装台92,集料斗91上端和出料管87,底端出口和称量包装台92相通;造粒机构8还包括引料辊83,设置在进料口81和旋转刀具86之间;进料口81呈向内收口状;在暂存箱85上和出料管87相对的一侧设置鼓风机84,鼓风机84出风口和暂存箱85及出料管87相通;在引料辊83的辊面设置橡胶面,旋转刀具86为滚刀组;第一隔箱101的内壁设置冷却水循环装置,以保证进入隔箱的烟雾迅速降低至30℃以下。化学溶液处理箱10内化学溶液的液面为箱体高度的70%;喷淋塔20的氢氧化钠溶液浓度7%。第二隔箱102卫生球加入量为70克/公斤,第三隔箱103内加入葡萄酚酸溶液,加入量为70克/公斤。整个装置通过PLC和电脑控制,并在化学溶液处理箱10和喷淋塔20内设置化学溶液浓度抽样点,在排气烟囱进气口处设置气体成分抽样点并和外连的PLC系统连接,以随时监控化学溶液浓度和气体排放是否达标。A paper-plastic separation-plastic-skin granulation production system for waste paper-plastic composite materials in this embodiment, the basic structure is the same as that of embodiment 2, the difference is that the volume of water in the friction mechanism 4 is 70% of the total capacity; The inclination angle of the sieve 53 is 30 degrees, the number of revolutions is 2 revolutions per second, and the mesh number of the screen is 20 meshes; an automatic pounding rod is set on the feed hopper 71 to avoid blanking in the feed hopper 71 due to the relatively light plastic skin; The heater 722 is an electromagnetic heater; the extruding mechanism is provided with a temperature detection and monitoring mechanism connected to the PLC. The packaging mechanism 9 includes a collecting hopper 91 and a weighing and packaging platform 92. The upper end of the collecting hopper 91 communicates with the discharge pipe 87, and the outlet at the bottom end communicates with the weighing and packaging platform 92; Between 81 and the rotary cutter 86; the feed port 81 is inwardly closed; on the side of the temporary storage box 85 opposite to the discharge pipe 87, a blower 84 is arranged, and the air outlet of the blower 84 and the temporary storage box 85 and the discharge pipe 87 are connected; a rubber surface is set on the roller surface of the lead roller 83, and the rotary cutter 86 is a hob unit; a cooling water circulation device is installed on the inner wall of the first compartment 101 to ensure that the smoke entering the compartment is quickly reduced to below 30°C. The liquid level of the chemical solution in the chemical solution treatment tank 10 is 70% of the height of the tank; the concentration of the sodium hydroxide solution in the spray tower 20 is 7%. The second compartment 102 sanitary ball add-on is 70 grams/kg, adds grapevine acid solution in the 3rd compartment 103, and add-on is 70 grams/kg. The whole device is controlled by PLC and computer, and the chemical solution concentration sampling point is set in the chemical solution treatment box 10 and the spray tower 20, and the gas component sampling point is set at the air inlet of the exhaust chimney and connected with the external PLC system. To monitor whether the chemical solution concentration and gas discharge are up to standard at any time.
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,具体使用步骤同实施例2。In this embodiment, a waste paper-plastic composite material paper-plastic separation-plastic-skin granulation production system, the specific use steps are the same as in embodiment 2.
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,实现了完全自动化生产,电磁加热器还能有效提高加热效率;集料斗91和称量包装台92的设置,便于产品的收集和集中包装,提高了生产效率;进料口81呈向内收口状,使条状物料集中处理,便于旋转刀具86集中切断;鼓风机84的设置,起到产品冷却和物料输送的作用,提高了生产效率;橡胶面引料辊83的使用,使引料辊83对条状物料的挤压缓冲式进行,避免挤压过度,影响造粒质量,引料辊83的设置还能使条状物料在切断前进行辊压处理,表面更加平整,使造粒更加均匀;葡萄酚酸溶液的使用,对烟雾中的苯基成分的处理更有针对性,处理效果更好;温度检测和监控机构还能对工艺温度进行有效的监控和调节。经测定,生产效率进一步提高了30%以上。The paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials in this embodiment realizes fully automatic production, and the electromagnetic heater can also effectively improve heating efficiency; the setting of the collecting hopper 91 and the weighing and packaging table 92, It is convenient for the collection and centralized packaging of products, which improves the production efficiency; the feeding port 81 is closed inward, so that the strip materials can be processed in a centralized manner, which is convenient for the centralized cutting by the rotary cutter 86; the setting of the blower 84 plays a role in product cooling and material transportation. The effect improves the production efficiency; the use of the rubber surface lead roller 83 enables the lead roller 83 to squeeze and buffer the strip material, avoiding excessive extrusion and affecting the granulation quality, and the setting of the lead roller 83 can also make the strip material The material is rolled before being cut, so that the surface is smoother and the granulation is more uniform; the use of grapevine acid solution is more targeted for the treatment of phenyl components in the smoke, and the treatment effect is better; the temperature detection and monitoring mechanism It can also effectively monitor and adjust the process temperature. It has been determined that the production efficiency is further improved by more than 30%.
实施例4Example 4
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,基本结构同实施例2,不同之处在于:摩擦机构4内水的体积为总容量的80%;滚桶筛53倾角为15度,筛网目数为40目;第二隔箱102和第三隔箱103内为卫生球溶解液的使用量为50克/公斤;喷淋塔20的氢氧化钠溶液浓度8%。The paper-plastic separation-plastic-skin granulation production system of waste paper-plastic composite materials in this embodiment has the same basic structure as that of embodiment 2, except that the volume of water in the friction mechanism 4 is 80% of the total capacity; The inclination angle of the sieve 53 is 15 degrees, and the mesh number of the screen is 40 orders; the usage amount of the sanitary ball dissolving liquid in the second compartment 102 and the third compartment 103 is 50 grams/kg; the sodium hydroxide solution of the spray tower 20 Concentration 8%.
本实施例的一种废旧纸塑复合材料纸塑分离-塑皮造粒生产系统,具体使用步骤同实施例2。In this embodiment, a waste paper-plastic composite material paper-plastic separation-plastic-skin granulation production system, the specific use steps are the same as in embodiment 2.
本发明实施例仅仅是对本发明的优选实施方式进行描述,并非对本发明构思和范围进行限定,在不脱离本发明设计思想的前提下,本领域工程技术人员对本发明的技术方案作出的各种变形和改进,均应落入本发明的保护范围。The embodiment of the present invention is only a description of the preferred implementation of the present invention, and does not limit the concept and scope of the present invention. On the premise of not departing from the design concept of the present invention, engineers and technicians in the field may make various modifications to the technical solution of the present invention. and improvements should fall within the protection scope of the present invention.
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| CN110883974A (en) * | 2018-09-07 | 2020-03-17 | 昆明昊拜农业科技有限公司 | Method for recycling and granulating waste agricultural films |
| EP3892434A4 (en) * | 2018-12-05 | 2022-08-03 | Furukawa Electric Co., Ltd. | Cellulose fiber-dispersing resin composite material, formed body, and composite member |
| CN110405984A (en) * | 2019-08-30 | 2019-11-05 | 陕西龙宾立德新材料科技有限公司 | A kind of glass reinforced plastic separation device for dissociation and method |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN106738434A (en) | 2017-05-31 |
| CN104816400B (en) | 2017-05-24 |
| CN106738434B (en) | 2018-10-23 |
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