CN102248615A - Production method of producing fine rubber powder by pulverizing at room temperature - Google Patents
Production method of producing fine rubber powder by pulverizing at room temperature Download PDFInfo
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- CN102248615A CN102248615A CN2011101882782A CN201110188278A CN102248615A CN 102248615 A CN102248615 A CN 102248615A CN 2011101882782 A CN2011101882782 A CN 2011101882782A CN 201110188278 A CN201110188278 A CN 201110188278A CN 102248615 A CN102248615 A CN 102248615A
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- 229920001971 elastomer Polymers 0.000 title claims abstract description 103
- 239000005060 rubber Substances 0.000 title claims abstract description 103
- 239000000843 powder Substances 0.000 title claims abstract description 49
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 35
- 238000010298 pulverizing process Methods 0.000 title claims description 8
- 239000000835 fiber Substances 0.000 claims description 46
- 239000000463 material Substances 0.000 claims description 25
- 239000002245 particle Substances 0.000 claims description 21
- 229910000831 Steel Inorganic materials 0.000 claims description 20
- 239000010959 steel Substances 0.000 claims description 20
- 239000011324 bead Substances 0.000 claims description 17
- 238000000926 separation method Methods 0.000 claims description 14
- 238000000227 grinding Methods 0.000 claims description 9
- 238000005520 cutting process Methods 0.000 claims description 8
- 239000006148 magnetic separator Substances 0.000 claims description 7
- 238000007885 magnetic separation Methods 0.000 claims description 6
- 238000010008 shearing Methods 0.000 claims description 6
- 239000010920 waste tyre Substances 0.000 claims description 6
- 238000012545 processing Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 23
- 238000007710 freezing Methods 0.000 abstract description 10
- 230000008014 freezing Effects 0.000 abstract description 10
- 239000003292 glue Substances 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000009776 industrial production Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000009434 installation Methods 0.000 abstract description 2
- 238000005057 refrigeration Methods 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 244000043261 Hevea brasiliensis Species 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 229920003052 natural elastomer Polymers 0.000 description 2
- 229920001194 natural rubber Polymers 0.000 description 2
- 229920000181 Ethylene propylene rubber Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229920005549 butyl rubber Polymers 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- 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
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
-
- 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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- Disintegrating Or Milling (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
技术领域 technical field
本发明涉及废橡胶制品处理方法技术领域,更具体地说涉及一种用废橡胶制品在常温条件下粉碎生产精细橡胶粉的生产方法,特别是由废轮胎在常温条件下粉碎生产精细橡胶粉的生产方法。。 The present invention relates to the technical field of waste rubber product treatment methods, more specifically to a production method for producing fine rubber powder by crushing waste rubber products under normal temperature conditions, especially the production method of fine rubber powder produced by crushing waste tires under normal temperature conditions production method. .
背景技术 Background technique
目前,每年仍有大量废橡胶制品(包括非轮胎橡胶制品及轮胎)产生,大量废轮胎,废橡胶制品需要处理,处理这些废料,既不能给环境造成污染,又要能回收再利用,这是当今世界各国共同追求的目标。 At present, there are still a large number of waste rubber products (including non-tire rubber products and tires) produced every year. A large number of waste tires and waste rubber products need to be disposed of. The disposal of these wastes can neither pollute the environment, but also be able to be recycled and reused. This is It is a common goal pursued by all countries in the world today.
废橡胶制品的处理,已经开发了多种生产方法,其中引人注目的有传统常温粉碎法和低温冷冻粉碎法。 A variety of production methods have been developed for the treatment of waste rubber products, among which the traditional normal temperature pulverization method and low temperature freezing pulverization method are the most notable.
传统常温粉碎法采用二次辊轧生产0.31~1.4mm(48目~15目)粒径的橡胶粉;另一种为日本神户制钢所开发的常温连续粉碎法(称CTC技术),经粗、细粉碎两道工序生产上述同样粒径的胶粉,上述方法缺点胶粉粒径大,满足不了用户要求,产量低,生产成本高,胶粒质量不稳定,难以适应工业化生产要求。 The traditional room temperature pulverization method uses secondary rolling to produce rubber powder with a particle size of 0.31-1.4mm (48 mesh to 15 mesh); the other is the room temperature continuous pulverization method (called CTC technology) developed by Kobe Steel in Japan. The rubber powder with the same particle size is produced by two processes of fine crushing and fine crushing. The disadvantages of the above method are that the particle size of the rubber powder is large, which cannot meet the requirements of users, the output is low, the production cost is high, the quality of the rubber particles is unstable, and it is difficult to adapt to the requirements of industrial production.
低温冷冻粉碎法,如USP4863106,5368040公开的低温冷冻粉碎法,采用液氮为制冷剂,冷冻温度为-196˚C,经冲击式机械进行粉碎,得到0.075-0.30mm(200目-48目)细度的精细橡胶粉,其中以0.18~0.22mm(80目~60目)为主,但此方法设备昂贵,投资大(为常温粉碎法的5倍),生产成本高(为常温法的5倍),而且开机、生产、维修、管理等方面有诸多困难。 Low-temperature freezing and crushing method, such as USP4863106, the low-temperature freezing and crushing method disclosed in USP4863106, 5368040, adopts liquid nitrogen as a refrigerant, and the freezing temperature is -196°C. It is crushed by impact machinery to obtain 0.075-0.30mm (200 mesh-48 mesh) Fine rubber powder with a fineness of 0.18-0.22mm (80 mesh to 60 mesh) is the main one, but this method is expensive in equipment, large in investment (5 times that of the normal temperature pulverization method), and high production cost (5 times that of the normal temperature method) Times), and there are many difficulties in start-up, production, maintenance, management and other aspects.
发明内容 Contents of the invention
本发明的目的是提供一种由废橡胶制品常温粉碎生产精细橡胶粉的工业方法,特别是由废橡胶轮胎常温粉碎生产精细橡胶粉的生产方法。 The purpose of the present invention is to provide an industrial method for producing fine rubber powder by crushing waste rubber products at normal temperature, especially a production method for producing fine rubber powder by crushing waste rubber tires at normal temperature.
本工业方法包括下列各步骤: The industrial method comprises the following steps:
1)、钢圈裁断:将废旧轮胎在钢圈裁断机上将轮胎止口钢丝圈裁断;(已获得实用新型专利,专利号为ZL200820043072.4); 1) Steel ring cutting: Cut the waste tires on the steel ring cutting machine to cut the tire seam bead ring; (has obtained a utility model patent, the patent number is ZL200820043072.4);
2)、钢丝分离:将裁断了止口钢丝圈后的轮胎经过胎圈分离机后,将止口钢丝圈从轮胎里脱离开来,(已申请实用新型专利,专利号为ZL201120168364.2); 2) Steel wire separation: After the tire with the bead bead cut off is passed through the bead separator, the bead bead is separated from the tire (a utility model patent has been applied for, and the patent number is ZL201120168364.2);
3)、轮胎破碎、将脱离了止口钢丝圈的轮胎整胎直接输送至轮胎破碎机(已获得实用新型专利权,专利号为ZL201020298420.X)作首次整胎破碎。整胎经过破碎后,出料约为50mm×50mm的块状胶,出料大小可通过改变破碎机圆滚筛网作一定范围的调整; 3) For tire crushing, the whole tire that has broken away from the bezel wire ring is directly transported to the tire crusher (has obtained the utility model patent right, the patent number is ZL201020298420.X) for the first complete tire crushing. After the whole tire is crushed, the output is about 50mm×50mm block rubber, and the size of the output can be adjusted within a certain range by changing the roller screen of the crusher;
4)、橡胶中粉碎:由步骤3出来的块状胶料输送至轮胎撕碎机(已获得实用新型专利权,专利号为ZL201020298434.1),进行再一次破碎,由动刀与固定在机体上的定刀以高速剪切的方式将物料粉碎,将轮胎制造时布于其内的钢丝和纤维切断,依靠剪切与撕裂作用将它们与橡胶进行分离,胶块破碎成约6mm~12mm的胶粒。出料粒度的大小可以通过改变出料筛网孔目的大小进行调整; 4) Crushing in the rubber: the bulk rubber material from step 3 is transported to the tire shredder (the utility model patent has been obtained, the patent number is ZL201020298434.1), and it is crushed again, and the moving knife is fixed on the machine body The fixed knife on the top crushes the material in a high-speed shearing manner, cuts off the steel wires and fibers that are distributed in the tire during manufacturing, and separates them from the rubber by shearing and tearing, and the rubber block is broken into about 6mm to 12mm colloidal particles. The size of the discharge particle size can be adjusted by changing the mesh size of the discharge screen;
5)磁选分离:将上述步骤生产出的物料经过皮带输送机输送至皮带式磁选机(已申请实用新型专利,专利号为ZL201120161231.2),皮带式磁选机凭其强大的磁力,将物料中混杂的钢丝分离出来; 5) Magnetic separation: The materials produced in the above steps are transported to the belt-type magnetic separator through the belt conveyor (a utility model patent has been applied for, the patent number is ZL201120161231.2). The belt-type magnetic separator relies on its strong magnetic force, Separation of steel wire mixed in the material;
6)、纤维粗分选:将步骤5磁选过后的物料通过圆滚筛将轮胎里的粗纤维进行粗分选,由于斜交轮胎里纤维含量过高,因此对于斜交轮胎的处理必须通过圆滚筛处理,对斜交轮胎里的粗纤维进行粗分选,这样,可提高粗纤维的使用价值及解决纤维含量过高导致后续处理过程的不便之处; 6) Coarse fiber separation: Pass the material after magnetic separation in step 5 through a roller sieve to roughly separate the coarse fiber in the tire. Since the fiber content in the bias tire is too high, the treatment of the bias tire must pass Rotary roller sieve treatment, rough separation of crude fibers in bias tires, so that the use value of crude fibers can be improved and the inconvenience of subsequent processing caused by high fiber content can be solved;
7)、橡胶细粉碎:将步骤6粗分选了纤维的物料输送至XJX-450橡胶细碎机(已获得实用新型专利权,专利号为ZL200520056431.6)进行细粉碎。通过调整细碎机出料筛网孔的大小,可直接生产出5目~15目的胶粉; 7) Fine crushing of rubber: transport the coarsely sorted fiber material in step 6 to XJX-450 rubber fine crushing machine (has obtained utility model patent, patent number is ZL200520056431.6) for fine crushing. By adjusting the size of the discharge screen hole of the fine crusher, the rubber powder of 5 mesh to 15 mesh can be directly produced;
8)、纤维再分选:将步骤7生产出来的物料用皮带输送机输送到直线振动筛进行第二次纤维粗分选,以提高胶粉质量,保证胶粉的纯度。 8) Fiber re-sorting: The materials produced in step 7 are transported to the linear vibrating screen with a belt conveyor for the second coarse fiber sorting to improve the quality of the rubber powder and ensure the purity of the rubber powder.
9)、将步骤8生产出来的经过二次纤维分选的物料用风力全部送至旋风收集器,经旋风收集器收集后进入QWF气流分选机(已获得实用新型专利权,专利号为ZL200320118550.0)。胶粉在转子交叉气流的作用下,将橡胶颗粒与纤维进行精细分离,经过三次纤维分离后可以保证胶粉的纤维含量为0.1%,而国家规定的胶粉中纤维含量为低于0.6%(GB/T19208-2003); 9) All the materials produced in step 8 that have undergone secondary fiber sorting are sent to the cyclone collector by wind force, and after being collected by the cyclone collector, they enter the QWF airflow sorting machine (the utility model patent has been obtained, and the patent number is ZL200320118550 .0). The rubber powder is finely separated from the rubber particles and fibers under the cross-flow of the rotor. After three times of fiber separation, the fiber content of the rubber powder can be guaranteed to be 0.1%, while the fiber content in the rubber powder stipulated by the state is less than 0.6% ( GB/T19208-2003);
10)、研磨,卧式橡胶研磨机(已申请实用新型专利,专利号为ZL201120168579.4)将步骤11的5~15目的橡胶颗粒剪切、研磨而得到40~120目的精细胶粉; 10) Grinding, horizontal rubber grinding machine (applied for utility model patent, patent number ZL201120168579.4) cuts and grinds the 5-15 mesh rubber particles in step 11 to obtain 40-120 mesh fine rubber powder;
11)、气流分选处理,经步骤12得到的40目~120目的精细胶粉中,再经过气流分选机(已获得实用新型专利权,专利号为ZL200320118550.0)分选处理后,得到不同规格粒度的仍保持原胶料物理化学性能的精细胶粉。 11) Airflow sorting treatment, the fine rubber powder of 40 mesh to 120 mesh obtained in step 12, and then through airflow sorting machine (has obtained the utility model patent right, the patent number is ZL200320118550.0) sorting treatment, to get Fine rubber powder with different specifications and particle sizes that still maintains the physical and chemical properties of the original rubber material.
本工业方法由于采用先进的常温粉碎工艺,并采用新型系列专用设备:钢圈裁断机、胎圈分离机、轮胎破碎机、橡胶撕碎机、橡胶细碎机、皮带式磁选机、卧式橡胶研磨机;采用除钢丝、多次除纤维的工艺流程设计,能将轮胎中的钢丝和纤维彻底清除干净,制取的精细胶粉性能与生胶类似,优于其它工艺生产的再生胶粉,适用任何橡胶制品的生产、高速公路铺设、防水建材等。 Due to the adoption of advanced normal temperature crushing process and the adoption of new series of special equipment in this industrial method: steel ring cutting machine, bead separator, tire crusher, rubber shredder, rubber fine crusher, belt type magnetic separator, horizontal rubber Grinding machine; adopting the process design of steel wire removal and multiple fiber removal, it can completely remove the steel wire and fiber in the tire, and the performance of the fine rubber powder produced is similar to that of raw rubber, which is better than that of reclaimed rubber powder produced by other processes. It is suitable for the production of any rubber products, highway paving, waterproof building materials, etc.
本发明的突出效果是:本生产方法开创了批量生产精细橡胶粉的先例,整条生产线设备投资是传统常温粉碎方法的1/2,设备投资约为低温冷冻粉碎生产线的1/8,本工业化生产线结构紧凑,设备安装维修方便,使用寿命长、出胶率高、动力消耗低、噪音低,各项技术指标同低温冷冻粉碎法生产的胶粉相比,优于目前较为先进的空气涡轮膨胀制冷胶粉生产技术; The outstanding effects of the present invention are: this production method creates a precedent for batch production of fine rubber powder, the equipment investment of the whole production line is 1/2 of the traditional room temperature grinding method, and the equipment investment is about 1/8 of the low-temperature freezing grinding production line. The production line has a compact structure, easy installation and maintenance, long service life, high glue output rate, low power consumption, and low noise. Compared with the rubber powder produced by the low-temperature freezing crushing method, the technical indicators are better than the more advanced air turbine expansion at present. Production technology of refrigeration rubber powder;
经切除内圈的轮胎,去除了主要的钢丝,破碎需要的设备功率小,刀具使用寿命长; After cutting off the inner ring of the tire, the main steel wire is removed, the power of the equipment required for crushing is small, and the service life of the tool is long;
本生产方法能耗低,用人少,年产3000吨的生产线每吨胶粉耗电582度,而低温冷冻法为900度,生产总成本为低温冷冻粉碎法的1/5; This production method has low energy consumption and less labor. The production line with an annual output of 3,000 tons consumes 582 degrees of electricity per ton of rubber powder, while the low-temperature freezing method is 900 degrees. The total production cost is 1/5 of the low-temperature freezing and pulverizing method;
研磨机具有整体结构紧凑、振动小、噪音低的优点,可从5-15目的胶粉研磨至120-40目,其产品质量高,粒度和工作温度由电胶监控自动调节; The grinding machine has the advantages of compact overall structure, small vibration and low noise. It can grind rubber powder from 5-15 mesh to 120-40 mesh. Its product quality is high, and the particle size and working temperature are automatically adjusted by electric glue monitoring;
品种多,粒度分布窄,按需要可20目为一个等级任意调节; There are many varieties and narrow particle size distribution, which can be adjusted arbitrarily according to the needs;
原材料利用率高,轮胎内钢丝、纤维可全部回收利用; The utilization rate of raw materials is high, and the steel wire and fiber in the tire can be completely recycled;
生产环境好,空气2级,噪音55分贝,无废水及粉尘。 The production environment is good, the air level is 2, the noise is 55 decibels, and there is no waste water and dust.
附图说明 Description of drawings
附图为本发明的工艺流程图 Accompanying drawing is process flow chart of the present invention
具体实施方式: Detailed ways:
见附图,其生产方法是: See accompanying drawing, its production method is:
1)、钢圈裁断:将废旧轮胎在钢圈裁断机上将轮胎止口钢丝圈裁断;(已申请实用新型专利,专利号为ZL200820043072.4) 1) Steel ring cutting: Cut the waste tires on the steel ring cutting machine to cut the tire seam bead ring; (A utility model patent has been applied for, and the patent number is ZL200820043072.4)
2)、钢丝分离:将裁断了止口钢丝圈后的轮胎经过胎圈分离机后,将止口钢丝圈从轮胎里脱离开来,(已申请实用新型专利,专利号为ZL201120168364.2); 2) Steel wire separation: After the tire with the bead bead cut off is passed through the bead separator, the bead bead is separated from the tire (a utility model patent has been applied for, and the patent number is ZL201120168364.2);
3)、轮胎破碎、将脱离了止口钢丝圈的轮胎整胎直接输送至轮胎破碎机(已获得实用新型专利权,专利号为ZL201020298420.X)作首次整胎破碎。整胎经过破碎后,出料约为50mm×50mm的块状胶,出料大小可通过改变破碎机圆滚筛网作一定范围的调整; 3) For tire crushing, the whole tire that has broken away from the bezel wire ring is directly transported to the tire crusher (has obtained the utility model patent right, the patent number is ZL201020298420.X) for the first complete tire crushing. After the whole tire is crushed, the output is about 50mm×50mm block rubber, and the size of the output can be adjusted within a certain range by changing the roller screen of the crusher;
4)、橡胶中粉碎:由步骤3出来的块状胶料输送至轮胎撕碎机(已获得实用新型专利权,专利号为ZL201020298434.1),进行再一次破碎,由动刀与固定在机体上的定刀以高速剪切的方式将物料粉碎,将轮胎制造时布于其内的钢丝和纤维切断,依靠剪切与撕裂作用将它们与橡胶进行分离,胶块破碎成约6mm~12mm的胶粒。出料粒度的大小可以通过改变出料筛网孔目的大小进行调整; 4) Crushing in the rubber: the bulk rubber material from step 3 is transported to the tire shredder (the utility model patent has been obtained, the patent number is ZL201020298434.1), and it is crushed again, and the moving knife is fixed on the machine body The fixed knife on the top crushes the material by high-speed shearing, cuts off the steel wires and fibers that are distributed in the tire during manufacturing, and separates them from the rubber by shearing and tearing, and the rubber block is broken into about 6mm to 12mm colloidal particles. The size of the discharge particle size can be adjusted by changing the mesh size of the discharge screen;
5)磁选分离:将上述步骤生产出的物料经过皮带输送机输送至皮带式磁选机(已申请实用新型专利,专利号为ZL201120161231.2),皮带式磁选机凭其强大的磁力,将物料中混杂的钢丝分离出来; 5) Magnetic separation: The materials produced in the above steps are transported to the belt-type magnetic separator through the belt conveyor (a utility model patent has been applied for, the patent number is ZL201120161231.2). The belt-type magnetic separator relies on its strong magnetic force, Separation of steel wire mixed in the material;
6)、纤维粗分选:将步骤5磁选过后的物料通过圆滚筛将轮胎里的粗纤维进行粗分选,由于斜交轮胎里纤维含量过高,因此对于斜交轮胎的处理必须通过圆滚筛处理,对斜交轮胎里的粗纤维进行粗分选,这样,可提高粗纤维的使用价值及解决纤维含量过高导致后续处理过程的不便之处; 6) Coarse fiber separation: Pass the material after magnetic separation in step 5 through a roller sieve to roughly separate the coarse fiber in the tire. Since the fiber content in the bias tire is too high, the treatment of the bias tire must pass Rotary roller sieve treatment, rough separation of crude fibers in bias tires, so that the use value of crude fibers can be improved and the inconvenience of subsequent processing caused by high fiber content can be solved;
7)、橡胶细粉碎:将步骤6粗分选了纤维的物料输送至XJX-450橡胶细碎机(已获得实用新型专利权,专利号为ZL200520056431.6)进行细粉碎。通过调整细碎机出料筛网孔的大小,可直接生产出5目~15目的胶粉; 7) Fine crushing of rubber: transport the coarsely sorted fiber material in step 6 to XJX-450 rubber fine crushing machine (has obtained utility model patent, patent number is ZL200520056431.6) for fine crushing. By adjusting the size of the discharge screen hole of the fine crusher, the rubber powder of 5 mesh to 15 mesh can be directly produced;
8)、纤维再分选:将步骤7生产出来的物料用皮带输送机输送到直线振动筛进行第二次纤维粗分选,以提高胶粉质量,保证胶粉的纯度。 8) Fiber re-sorting: The materials produced in step 7 are transported to the linear vibrating screen with a belt conveyor for the second coarse fiber sorting to improve the quality of the rubber powder and ensure the purity of the rubber powder.
9)、将步骤8生产出来的经过二次纤维分选的物料用风力全部送至旋风收集器,经旋风收集器收集后进入QWF气流分选机(已获得实用新型专利权,专利号为ZL200320118550.0)。胶粉在转子交叉气流的作用下,将橡胶颗粒与纤维进行精细分离,经过三次纤维分离后可以保证胶粉的纤维含量为0.1%,而国家规定的胶粉中纤维含量为低于0.6%(GB/T19208-2003); 9) All the materials produced in step 8 that have undergone secondary fiber sorting are sent to the cyclone collector by wind force, and after being collected by the cyclone collector, they enter the QWF airflow sorting machine (the utility model patent has been obtained, and the patent number is ZL200320118550 .0). The rubber powder is finely separated from the rubber particles and fibers under the cross-flow of the rotor. After three times of fiber separation, the fiber content of the rubber powder can be guaranteed to be 0.1%, while the fiber content in the rubber powder stipulated by the state is less than 0.6% ( GB/T19208-2003);
10)、研磨,卧式橡胶研磨机(已申请实用新型专利,专利号为ZL201120168579.4)将步骤9的5~15目的橡胶颗粒剪切、研磨而得到40~120目的精细胶粉; 10) Grinding, horizontal rubber grinding machine (applied for utility model patent, patent number ZL201120168579.4) cuts and grinds the 5-15 mesh rubber particles in step 9 to obtain 40-120 mesh fine rubber powder;
11)、气流分选处理,经步骤10得到的40目~120目的精细胶粉中,再经过气流分选机(已获得实用新型专利权,专利号为ZL200320118550.0)分选处理后,得到不同规格粒度的仍保持原胶料物理化学性能的精细胶粉。 11) Airflow sorting treatment, the 40 mesh to 120 mesh fine rubber powder obtained in step 10, and then go through the airflow sorting machine (the utility model patent right has been obtained, the patent number is ZL200320118550.0), and the obtained Fine rubber powder with different specifications and particle sizes that still maintains the physical and chemical properties of the original rubber material.
本工业方法生产线可同样用于非轮胎的橡胶制品的回收,如胶带、胶管、胶鞋、电线电缆、工业橡胶部件、胶板等;本工业方法中所述轮胎包括汽车用轮胎(轿车用轮胎)、卡车轮胎、重型卡车轮胎、拖拉机轮胎及人力车轮胎等。众所周知轮胎由天然橡胶、诸如丁苯橡胶、顺丁橡胶、异戊橡胶、丁基橡胶、乙丙橡胶之类的橡胶合成。随着各种车用轮胎不同,例如对于轿车胎基本上是由全合成橡胶制造,卡车轮胎以天然橡胶为主的橡胶。为保证精细胶粉质量,适合各种用户对精细胶粉产品的需求,将收集的废非轮胎橡胶制品和废轮胎除去污物和杂质,按不同橡胶品种分门别类堆放,加以保管待用。 The production line of this industrial method can also be used for the recovery of rubber products other than tires, such as tapes, rubber hoses, rubber shoes, wires and cables, industrial rubber parts, rubber sheets, etc.; the tires mentioned in this industrial method include automobile tires (car tires) , truck tires, heavy truck tires, tractor tires and rickshaw tires, etc. It is well known that tires are synthesized from natural rubber, rubber such as styrene-butadiene rubber, butadiene rubber, isoprene rubber, butyl rubber, ethylene-propylene rubber, and the like. As various vehicle tires are different, for example, car tires are basically made of all-synthetic rubber, while truck tires are mainly made of natural rubber. In order to ensure the quality of fine rubber powder and meet the needs of various users for fine rubber powder products, the collected waste non-tire rubber products and waste tires are removed from dirt and impurities, and are sorted and stacked according to different rubber varieties, and stored for later use.
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CN101234517A (en) * | 2008-02-23 | 2008-08-06 | 东莞市方达环宇环保科技有限公司 | Method for crushing producing fineness rubber powder under normal temperature |
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