CN102166794A - Rubber continuous mixing dual-rotor structure and mixing equipment adopting same - Google Patents
Rubber continuous mixing dual-rotor structure and mixing equipment adopting same Download PDFInfo
- Publication number
- CN102166794A CN102166794A CN201110026202XA CN201110026202A CN102166794A CN 102166794 A CN102166794 A CN 102166794A CN 201110026202X A CN201110026202X A CN 201110026202XA CN 201110026202 A CN201110026202 A CN 201110026202A CN 102166794 A CN102166794 A CN 102166794A
- Authority
- CN
- China
- Prior art keywords
- mixing
- section
- rotor
- rubber
- dual
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- 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
- B29C48/505—Screws
- B29C48/535—Screws with thread pitch varying along the longitudinal axis
-
- 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
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/465—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft each shaft comprising rotor parts of the Banbury type in addition to screw parts
-
- 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
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/48—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
- B29B7/488—Parts, e.g. casings, sealings; Accessories, e.g. flow controlling or throttling devices
- B29B7/489—Screws
-
- 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
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/60—Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
-
- 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
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
- B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber
-
- 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
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
-
- 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
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/41—Intermeshing counter-rotating screws
-
- 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
- B29C48/47—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using discs, e.g. plasticising the moulding material by passing it between a fixed and a rotating disc that are coaxially arranged
-
- 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
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/72—Measuring, controlling or regulating
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
橡胶连续混炼双转子结构的一对复合型转子的加料段是大导程螺纹结构,捏炼段采用齿形盘结构,混炼段分别是剪切型转子混炼元件、啮合型转子混炼元件、大导程转子混炼元件。混炼设备机筒内安装本发明的双转子结构,控制系统连接冷却系统、动力传动系统和加料机构。复合型转子结构能够实现橡胶连续、高效、高质量混炼。混炼设备能够连续、高效和高质量的混炼,与块状橡胶连续塑炼设备配套使用,能够实现块状橡胶连续混炼。
The feeding section of a pair of composite rotors with a double-rotor structure for rubber continuous mixing is a large-lead thread structure, the kneading section adopts a toothed disc structure, and the mixing section is a shearing rotor mixing element and an meshing rotor mixing element. Components, large lead rotor mixing components. The double-rotor structure of the present invention is installed in the barrel of the mixing equipment, and the control system is connected with the cooling system, the power transmission system and the feeding mechanism. The composite rotor structure can realize continuous, efficient and high-quality mixing of rubber. The mixing equipment is capable of continuous, high-efficiency and high-quality mixing. It is used in conjunction with the block rubber continuous plasticating equipment to realize the continuous mixing of block rubber.
Description
技术领域technical field
本发明涉及橡胶加工成型设备,具体的讲是一种用于橡胶连续、高效和高质量混炼双转子结构及采用该结构的混炼设备。The invention relates to rubber processing and molding equipment, in particular to a double-rotor structure for continuous, high-efficiency and high-quality mixing of rubber and the mixing equipment adopting the structure.
背景技术Background technique
混炼过程是橡胶加工中最为关键,也是能耗最高的环节,混炼胶的质量的好坏最终决定了成品质量的优劣和使用寿命,因此,对于混炼环节的研究与改进始终是国内外橡胶加工业关注的焦点。The mixing process is the most critical and the most energy-intensive link in rubber processing. The quality of the mixed rubber ultimately determines the quality and service life of the finished product. Therefore, the research and improvement of the mixing link is always the domestic The focus of foreign rubber processing industry.
目前,橡胶工业所用的混炼设备主要是开炼机和密炼机,它们都是间歇式混炼设备,生产过程不连续,每次操作条件的差异会引起混炼质量不稳定等缺点。因此,实现橡胶高效、高质量的连续化的混炼生产是几十年来橡胶加工业技术人员的梦想,这其中作为混炼设备核心的转子结构又是研发的重点。At present, the mixing equipment used in the rubber industry is mainly open mills and internal mixers. They are all batch mixing equipment, the production process is discontinuous, and the difference in each operation condition will cause the disadvantages of unstable mixing quality. Therefore, to realize efficient and high-quality continuous mixing production of rubber has been the dream of technicians in the rubber processing industry for decades, and the rotor structure, which is the core of mixing equipment, is the focus of research and development.
所谓连续混炼是指采用连续混炼机,将生胶或塑炼胶和配合剂按照设定的配比连续加料并进行连续混炼,混炼胶则可从排胶口连续地排出。连续混炼可以实现加料与卸料同时进行,大幅度提高生产效率,免除或简化庞大的密炼机、下辅机和上辅机,进而由一条联动生产线代替,大大地简化设备的结构,大幅度降低能耗,提高混炼胶质量和稳定性,并且容易实现安全、环保的操作。The so-called continuous mixing refers to the use of a continuous mixer to continuously feed raw rubber or plasticized rubber and compounding agents according to the set ratio and perform continuous mixing, and the mixed rubber can be continuously discharged from the rubber discharge port. Continuous mixing can realize feeding and unloading at the same time, greatly improving production efficiency, eliminating or simplifying the huge internal mixer, lower auxiliary machine and upper auxiliary machine, and then replaced by a linkage production line, which greatly simplifies the structure of the equipment and greatly Significantly reduce energy consumption, improve the quality and stability of compound rubber, and easily realize safe and environmentally friendly operation.
目前世界很多国家提出了连续混炼这一新理论,也设计生产出了各种连续混炼设备。美国、意大利、德国等研制、生产出各种型号的连续混炼机,但这些连续混炼设备只适用于塑料和具有流动性的胶料,即胶料必须是粉末状或粒状,并且必须与炭黑提前预混。在现代橡胶工业生产中,由于原料主要是块状橡胶,所以生产中主要还是依赖于密炼机完成橡胶的混炼,然后经过压片机进行压片或经挤出机挤出成型。因此,真正意义上的非粉末状和粒状橡胶的连续混炼还没有实现。At present, many countries in the world have proposed the new theory of continuous mixing, and have also designed and produced various continuous mixing equipment. The United States, Italy, Germany, etc. have developed and produced various types of continuous mixing machines, but these continuous mixing equipment are only suitable for plastics and fluid rubber materials, that is, the rubber materials must be powder or granular, and must be combined with Carbon black is premixed in advance. In the production of modern rubber industry, since the raw material is mainly block rubber, the production mainly relies on the internal mixer to complete the mixing of rubber, and then it is compressed by a tablet press or extruded by an extruder. Therefore, continuous mixing of non-powdered and granulated rubber has not been realized in the true sense.
中国实用新型专利,授权公告号CN2815670Y,《一种高聚物共混炼成型的装备》公开了一种在密炼机排料口处接存料室,存料室出料口下接挤出机的技术方案,其混炼部分仍然采用间歇方式,只是挤出部分的工作是连续的,所以它还不是真正意义上的连续混炼。中国发明专利,公开号CN101288985A,《连续混炼挤压机转子》是一种石化行业乙烯工程混炼挤压造粒机组的螺杆,适合塑料的连续加工,由于其加料段采用啮合或半啮合的多头螺纹,使喂料困难;其混炼段均为由正向与反向多棱螺旋组成螺纹,或者由正向与反向多棱螺旋组成混炼段与单向螺旋混炼段混合,长径比小于12,存在胶料混炼时间短、混合、剪切、拉伸效果差、难以将各种配料完全均匀地分散于生胶中、制成质量均匀的混炼胶等缺点,所以不能用于橡胶的连续混炼。Chinese utility model patent, authorized announcement number CN2815670Y, "A high polymer co-mixing and forming equipment" discloses a storage room connected to the discharge port of the internal mixer, and the discharge port of the storage room is connected to the extrusion In the technical scheme of the machine, the mixing part still adopts the batch mode, but the work of the extrusion part is continuous, so it is not continuous mixing in the true sense. Chinese invention patent, publication number CN101288985A, "Continuous Mixing Extruder Rotor" is a screw for ethylene engineering mixing extrusion granulation unit in petrochemical industry, suitable for continuous processing of plastics, because its feeding section adopts meshing or semi-meshing Multi-threaded threads make feeding difficult; the mixing section is composed of forward and reverse multi-edged spirals, or the mixing section is composed of forward and reversed multi-edged spirals and mixed with unidirectional spiral mixing section, long If the diameter ratio is less than 12, there are disadvantages such as short rubber mixing time, poor mixing, shearing, and stretching effects, and it is difficult to completely and evenly disperse various ingredients in the raw rubber to make a uniform quality mixed rubber, so it cannot be used. For continuous mixing of rubber.
发明内容Contents of the invention
本发明要解决现有设备不能实现橡胶连续混炼加工的技术问题,提供一种能够实现橡胶连续、高效、高质量混炼设备的双转子结构及采用该结构、进行橡胶连续、高效和高质量的混炼,与块状橡胶连续塑炼设备配套使用,能够实现块状橡胶的连续混炼设备。The present invention aims to solve the technical problem that the existing equipment cannot realize continuous rubber mixing and processing, and provides a double-rotor structure capable of realizing continuous, high-efficiency, and high-quality rubber mixing equipment and adopting this structure to carry out continuous, high-efficiency, and high-quality rubber It is used together with the block rubber continuous plasticating equipment to realize the continuous mixing equipment of block rubber.
本发明为了解决上述技术问题而采取的技术方案是:一种橡胶连续混炼双转子结构,包括一对异向螺纹、平行、异向旋转和转速相同的复合型转子,转子后端连接动力传动系统,一对复合型转子中的螺纹部分是部分啮合,转子上有加料段、捏炼段、混炼段及挤出段;加料段是大导程螺纹结构;捏炼段采用齿形盘结构;混炼段由三段组成,混炼段Ⅰ是剪切型转子混炼元件,混炼段Ⅱ是啮合型转子混炼元件,混炼段Ⅲ是大导程转子混炼元件。The technical solution adopted by the present invention to solve the above-mentioned technical problems is: a double-rotor structure for rubber continuous mixing, including a pair of composite rotors with different threads, parallel and different rotations, and the same speed. The rear end of the rotor is connected to the power transmission. system, the screw parts in a pair of composite rotors are partially meshed, and there are feeding section, kneading section, mixing section and extrusion section on the rotor; the feeding section is a large-lead thread structure; the kneading section adopts a toothed disc structure The mixing section is composed of three sections, mixing section I is a shearing rotor mixing element, mixing section II is an meshing rotor mixing element, and mixing section III is a large lead rotor mixing element.
复合型双转子与机筒之间的混炼空间较单螺杆结构的混炼空间大,混炼产量高。双转子输送能力强,增强了物料的流动性,避免物料停滞。平行、旋转方向相反和部分啮合的转子元件,对物料剪切和分散作用强、混炼均匀,旋转方向相反的双转子比同向旋转的双转子使物料流动性更好、输送能力更强、压力更大,而两个转子相向旋转,即向内旋转效果更好,一对异向螺纹的复合转子使混炼更充分、更均匀。加料段的大导程螺纹结构保证了物料顺利进入。捏炼段主要起分流混合作用。在三段混炼段中,物料被推动、剪切、挤压、分散、搅拌和混合,充分混炼。The mixing space between the compound double rotor and the barrel is larger than that of the single-screw structure, and the mixing output is high. The dual rotors have strong conveying capacity, which enhances the fluidity of materials and avoids stagnation of materials. Parallel, opposite rotating and partially meshed rotor elements have strong shearing and dispersing effects on materials and uniform mixing. Compared with double rotating rotors rotating in the same direction, the double rotors with opposite rotating directions make the material flow better and the conveying capacity stronger. The pressure is higher, and the two rotors rotate in opposite directions, that is, the effect of inward rotation is better, and a pair of composite rotors with different threads make the mixing more complete and more uniform. The large-lead thread structure of the feeding section ensures the smooth entry of materials. The kneading section mainly plays the role of split flow and mixing. In the three-stage mixing section, the materials are pushed, sheared, extruded, dispersed, stirred and mixed, fully mixed.
本发明的橡胶连续混炼双转子结构能够实现橡胶连续、高效、高质量混炼。The rubber continuous mixing double-rotor structure of the invention can realize continuous, high-efficiency and high-quality rubber mixing.
加料段是单头螺纹,螺距由后向前减小;捏炼段的两根转子上的齿形盘端面相对,留有间隙;混炼段Ⅰ的一端有两段长度不同的左旋突棱,另一端有两段长度不同的右旋突棱;混炼段Ⅱ有两条短的螺旋突棱,两条短的螺旋突棱之间有一条长的螺旋突棱;混炼段Ⅲ上有两条螺棱,螺棱由螺纹旋转方向不同、螺旋角不同的两段螺纹连接组成;挤出段是双头螺纹,其后一部分的螺距由后向前减小,前一部分螺距相等。螺距由后向前减小的加料段在输送、压实物料的同时还起到破胶和进一步提高胶料塑化效果的作用,物料的压实主要起着排出进料时带进的部分空气,使塑炼胶和加入的配合剂充分接触。当物料通过一根转子捏炼段的齿形盘时被分成若干股,物料流出来后被另一根转子捏炼段的齿形盘切断。剪切型混炼转子元件旋转时,由于两转子上的突棱在配合时工作直径大小不一样,形成了速度梯度,引起物料在圆周方向较大的流动,使物料受到来自突棱的较大的推力、反推力、剪切和挤压作用,物料在转子间受到折卷和轴向往返、切割、搅拌等作用,使配合剂得到更好的分散,均匀分布。一个啮合型转子混炼元件的突棱依次啮入另一个啮合型元件的棱间,突棱外径与突棱根部旋转的线速度不同,物料在啮合型转子混炼元件之间以及转子与机筒内壁之间受到不断变化的反复进行的强烈捏炼、剪切和挤压作用。大导程转子混炼元件螺棱的正向螺纹向前推物料,反向螺纹向后推物料,物料在正反方向力的作用下产生纵向和横向的混合、拉伸和剪切,不断被挤压、剪切、分散和混合。挤出段顺畅、平稳的将混炼胶挤出,挤出段的后一部分主要起压实和输送的作用,前一部分起到保证挤出稳定,获得较好质量混炼胶的作用。The feeding section is a single-head thread, and the pitch decreases from back to front; the end faces of the toothed discs on the two rotors of the kneading section face each other, leaving a gap; one end of the mixing section I has two sections of left-handed ribs with different lengths. The other end has two right-handed ribs with different lengths; mixing section II has two short spiral ribs, and there is a long spiral rib between the two short spiral ribs; mixing section III has two The screw flight is composed of two screw connections with different screw rotation directions and different helix angles; the extrusion section is a double-start thread, the pitch of the latter part decreases from back to front, and the pitch of the former part is equal. The feeding section whose screw pitch decreases from the back to the front also plays the role of breaking the rubber and further improving the plasticizing effect of the rubber while conveying and compacting the material. The compaction of the material mainly plays the role of discharging part of the air brought in when the material is fed. , so that the plasticized rubber and the added compounding agent are in full contact. When the material passes through the toothed disc of the kneading section of one rotor, it is divided into several strands, and the material flows out and is cut off by the toothed disc of the kneading section of the other rotor. When the shear type mixing rotor element rotates, because the working diameters of the ribs on the two rotors are different when they cooperate, a velocity gradient is formed, which causes a large flow of the material in the circumferential direction, and the material is subjected to a large force from the ribs. Thrust, reverse thrust, shearing and extrusion, the material is subjected to folding and axial reciprocation, cutting, stirring and other effects between the rotors, so that the compounding agent can be better dispersed and evenly distributed. The kneading ribs of one meshing rotor mixing element mesh into the ribs of another meshing element in turn. The outer diameter of the knuckle is different from the linear speed at which the root of the knuckle rotates. The material is between the kneading rotor mixing elements and between the rotor and the machine. The inner walls of the cylinder are subjected to constantly changing and repeated strong kneading, shearing and extrusion. The forward thread of the screw edge of the large-lead rotor mixing element pushes the material forward, and the reverse thread pushes the material backward. Under the action of positive and negative directions, the material produces longitudinal and transverse mixing, stretching and shearing, and is continuously Squeeze, shear, disperse and mix. The extrusion section extrudes the rubber compound smoothly and stably. The latter part of the extrusion section mainly plays the role of compaction and transportation, and the former part plays the role of ensuring stable extrusion and obtaining better quality rubber compound.
加料段、混炼段Ⅰ、混炼段Ⅱ、混炼段Ⅲ和挤出段的螺纹高度相等,螺纹母体呈圆柱状;转子的头部呈圆锥形;加料段后面的转子上开有反胶槽。前端呈圆锥形的转子使混炼胶的流动性好,保证挤出质量稳定。反胶槽防止胶料从转子后方溢出。The thread heights of the feeding section, mixing section Ⅰ, mixing section Ⅱ, mixing section Ⅲ and extrusion section are equal, and the screw matrix is cylindrical; the head of the rotor is conical; the rotor behind the feeding section is provided with reverse glue groove. The conical rotor at the front end makes the fluidity of the compounded rubber good and ensures the stable extrusion quality. Anti-adhesive groove prevents the adhesive from overflowing from the rear of the rotor.
转子的加料段、捏炼段、混炼段Ⅰ、混炼段Ⅱ、混炼段Ⅲ和挤出段的螺纹元件可拆卸的安装在转子的芯轴上,捏炼段、混炼段Ⅰ、混炼段Ⅱ和混炼段Ⅲ在转子上的排布顺序可以变化。这种积木式的组合方式便于制造、安装、维修。改变排布顺序可以适应不同物料、工艺和制品的要求。The feeding section, kneading section, kneading section I, kneading section II, kneading section III and screw elements of the extruding section of the rotor are detachably installed on the mandrel of the rotor, and the kneading section, kneading section I, The arrangement sequence of mixing section II and mixing section III on the rotor can be changed. This building block combination is convenient for manufacture, installation and maintenance. Changing the arrangement sequence can adapt to the requirements of different materials, processes and products.
转子上沿胶料前进方向依次排布加料段、混炼段Ⅰ、捏炼段、输送段Ⅰ、混炼段Ⅱ、输送段Ⅱ、混炼段Ⅲ和挤出段。这种排布顺序混炼效果最好。The feeding section, mixing section Ⅰ, kneading section, conveying section Ⅰ, mixing section Ⅱ, conveying section Ⅱ, mixing section Ⅲ and extrusion section are sequentially arranged on the rotor along the advancing direction of the rubber material. This order of arrangement has the best mixing effect.
输送段Ⅰ和输送段Ⅱ是双头螺纹,螺距由后向前减小,两者螺棱上开有垂直于螺纹的段Ⅰ螺槽和段Ⅱ螺槽。输送段Ⅰ和输送段Ⅱ的螺距由后向前变小,在输送物料的同时,还具有压实作用;螺棱开槽的输送段Ⅰ和输送段Ⅱ使相邻螺纹槽间产生物料交换,有一部分物料分流到相邻的螺纹槽中,被不断分割、混合、回流,混炼质量均匀,主要剪切作用发生在靠近机筒壁处,传热效果好,物料升温小,操作稳定。Conveying section I and conveying section II are double-start threads, and the pitch decreases from back to front. There are section I screw grooves and section II screw grooves perpendicular to the threads on the two screw edges. The screw pitch of conveying section I and conveying section II becomes smaller from the back to the front, and it also has a compacting effect while conveying materials; the conveying section I and conveying section II with grooved screw ribs enable material exchange between adjacent thread grooves, Part of the material is diverted to the adjacent screw grooves, and is continuously divided, mixed, and refluxed. The mixing quality is uniform, and the main shearing action occurs near the wall of the barrel. The heat transfer effect is good, the temperature rise of the material is small, and the operation is stable.
加料段螺纹是三角形螺纹。三角形螺纹根部厚,提高了加料段的机械强度和刚度。The feeding section thread is a triangular thread. The root of the triangular thread is thick, which improves the mechanical strength and rigidity of the feeding section.
一种采用权利要求1-7中任意一种双转子结构的塑炼设备,包括固定机筒的机架,以及加料机构、动力传动系统、冷却系统和控制系统,本发明的橡胶连续混炼双转子结构安装在机筒内;转子后端连接动力传动系统,加料机构在机筒的上方,连通机筒上的喂料口;机筒上的冷却水道连接冷却系统;控制系统连接冷却系统、动力传动系统和加料机构。A plasticating equipment adopting any one of the double-rotor structures in claims 1-7, including a frame for fixing the barrel, a feeding mechanism, a power transmission system, a cooling system and a control system, the rubber continuous mixing double-rotor of the present invention The rotor structure is installed in the barrel; the rear end of the rotor is connected to the power transmission system, and the feeding mechanism is above the barrel, which is connected to the feeding port on the barrel; the cooling water channel on the barrel is connected to the cooling system; the control system is connected to the cooling system, power Transmission system and feeding mechanism.
由于本发明的橡胶连续混炼双转子结构具有的上述性能,本发明的混炼设备能够进行橡胶连续、高效和高质量的混炼,与块状橡胶连续塑炼设备配套使用,能够实现块状橡胶连续混炼。Due to the above-mentioned properties of the rubber continuous mixing double-rotor structure of the present invention, the mixing equipment of the present invention can carry out continuous, efficient and high-quality mixing of rubber, and it can be used together with the continuous plasticizing equipment of block rubber to realize block shape Continuous rubber mixing.
机筒是分段组合的机筒,每段机筒上有冷却水道。机筒的各段依次密封固定连接在一起组成整体的机筒。机筒分段组合便于制作、安装、更换和维护。The barrel is a segmented barrel, and each segment of the barrel has a cooling channel. Each section of the barrel is sequentially sealed and fixedly connected together to form a whole barrel. The segmented combination of the barrel is convenient for manufacture, installation, replacement and maintenance.
分段组合的机筒采用纵向剖分式结构。纵向剖分式结构的机筒便于对机筒和转子的清洗和维护,方便拆分机筒来观察各段混炼状态和混炼程度,为研究、改进设备提供依据。The segmented barrel adopts a longitudinally split structure. The barrel with longitudinally split structure is convenient for cleaning and maintenance of the barrel and rotor, and it is convenient to disassemble the barrel to observe the mixing state and mixing degree of each section, which provides a basis for research and improvement of equipment.
机筒前端连接机头。The front end of the machine barrel is connected with the machine head.
加料机构包括一套用来加入炭黑的由储存料斗和螺旋加料器组成的炭黑自动称量加料装置,一套用来加入各种小料的由储存料斗、搅拌装置料斗和螺旋加料器组成的小料自动称量加料装置,一套引进塑炼设备挤出胶片的胶片供给装置;炭黑加料装置、小料加料装置和胶片供给装置连通机筒上的喂料口。在控制系统控制下,加料机构能够做到胶料及炭黑、小料等配合剂按照一定的配比连续定量加入混炼设备。The feeding mechanism includes a set of carbon black automatic weighing and feeding device composed of a storage hopper and a screw feeder for adding carbon black, a set of small storage hoppers, a stirring device hopper and a screw feeder for adding various small materials. Material automatic weighing and feeding device, a set of film supply device imported from plasticizing equipment to extrude film; carbon black feeding device, small material feeding device and film feeding device are connected to the feeding port on the barrel. Under the control of the control system, the feeding mechanism can continuously and quantitatively add rubber materials, carbon black, small materials and other compounding agents into the mixing equipment according to a certain ratio.
本发明的优点是:由本发明一对异向螺纹、部分啮合、平行和异向旋转转子组成的复合型转子结构的加料段、捏炼段、混炼段和挤出段,实现橡胶连续、高效、高质量混炼。采用本发明双转子结构的混炼设备在控制系统控制下,胶料及炭黑、小料等配合剂按照一定的配比连续定量加入混炼设备,混炼胶连续由机头挤出,进行连续、高效和高质量的混炼,与块状橡胶连续塑炼设备配套使用,能够实现块状橡胶连续混炼。The advantages of the present invention are: the feeding section, the kneading section, the mixing section and the extruding section of the composite rotor structure composed of a pair of counter-threaded, partially meshed, parallel and counter-rotating rotors of the present invention can realize continuous and high-efficiency rubber , High-quality mixing. The mixing equipment adopting the double rotor structure of the present invention is under the control of the control system, and the rubber material, carbon black, small materials and other compounding agents are continuously quantitatively added to the mixing equipment according to a certain proportion, and the mixing rubber is continuously extruded from the machine head to carry out continuous , High-efficiency and high-quality mixing, used together with block rubber continuous plasticating equipment, can realize block rubber continuous mixing.
附图说明Description of drawings
图1是本发明双转子结构一个实施例的结构示意图;Fig. 1 is a schematic structural view of an embodiment of the double rotor structure of the present invention;
图2是采用图1复合型双转子的混炼设备一个实施例的结构示意图;Fig. 2 is the structural representation of an embodiment of the mixing equipment adopting Fig. 1 composite double rotor;
图3是图2混炼设备的机筒部分结构示意图。Fig. 3 is a schematic structural view of the barrel part of the mixing equipment in Fig. 2 .
具体实施方式Detailed ways
结合附图说明。Description with reference to the accompanying drawings.
图1双转子结构是一对异向螺纹、平行、异向旋转和转速相同的复合型转子2,螺纹部分是部分啮合型。转子后端连接动力传动系统,参见图2。转子2从后向前的加料段29、混炼段Ⅰ28、捏炼段27、输送段Ⅰ26、混炼段Ⅱ25、输送段Ⅱ24、混炼段Ⅲ23和挤出段22元件套装在转子2的芯轴上,积木式的组合方式便于制造、安装、维修。圆锥形转子的头部21固定安装在芯轴前端,加料段29后面的芯轴上开有防止胶料溢出的反胶槽210。加料段29是螺距由后向前逐渐减小的大导程单头三角形螺纹结构。混炼段Ⅰ28是剪切型转子混炼元件,其一端是左旋突棱,另一端是右旋突棱,本实施例中剪切型转子混炼元件前端有两段长度不同的左旋突棱,后端有两段长度不同的右旋突棱。捏炼段27采用齿形盘结构,捏炼段27的两根转子2上的齿形盘端面相对,留有间隙。混炼段Ⅱ25是啮合型转子混炼元件,其上有长的螺旋突棱和短的螺旋突棱,本实施例中啮合型转子混炼元件上两条短的螺旋突棱之间有一条长的螺旋突棱。混炼段Ⅲ23是大导程转子混炼元件,其上螺棱由旋转方向不同、螺旋角不同的两段螺纹连接组成,本实施例中大导程转子混炼元件上有两条螺棱。挤出段22是双头螺纹,挤出段22后一部分的螺距由后向前逐渐减小,前一部分螺距相等。输送段Ⅰ26和输送段Ⅱ24是双头螺纹,螺距由后向前逐渐减小,两者螺棱上开有垂直于螺纹的段Ⅰ螺槽261和段Ⅱ螺槽241。加料段29、混炼段Ⅰ28、混炼段Ⅱ25、混炼段Ⅲ23、输送段Ⅰ26、输送段Ⅱ24和挤出段22的螺纹高度相等,螺纹母体呈圆柱状。The double-rotor structure in Fig. 1 is a pair of
本发明的橡胶连续混炼双转子结构能够实现橡胶连续、高效、高质量混炼。The rubber continuous mixing double-rotor structure of the invention can realize continuous, high-efficiency and high-quality rubber mixing.
图2是采用图1的双转子结构实施例的一种混炼设备的结构示意图。该设备实施例的机筒3包围复合型双转子2。电机63通过减速器62将动力传递到分配器61,复合型双转子2后端连接分配器61的输出轴,分配器61驱动一对异向螺纹、部分啮合、平行的转子2异向等速旋转。动力传动系统的电机63、减速器62和分配器61固定在机架7上。机筒3前端固定连接机头1,后端与分配器61的壳体固定连接,机筒3的前部和中部由固定在机架7上的机筒支架支撑。Fig. 2 is a structural schematic diagram of a mixing equipment adopting the embodiment of the double-rotor structure in Fig. 1 . The
加料机构包括三部分:引进塑炼机挤出胶片的胶片供给装置5,用来加入炭黑的由储存料斗和螺旋加料器组成的炭黑自动称量加料装置,用来加入各种小料的由储存料斗、搅拌装置料斗和螺旋加料器组成的小料自动称量加料装置,图2中炭黑及小料加料装置4表示炭黑自动称量加料装置和小料自动称量加料装置两部分。加料机构在机筒3上方,加料机构的三部分连通机筒3上的同一个喂料口341。机筒3上有连接冷却系统的冷却水道311,参见图3。控制系统连接冷却系统、动力传动系统和加料机构。在控制系统控制下,加料机构能够做到胶料及炭黑、小料等配合剂按照一定的配比定量加入混炼设备。The feeding mechanism consists of three parts: a
图3所示是图2混炼设备的机筒部分的示意图。机筒3是分段组合式连接结构,各段依次密封固定连接在一起组成整体的机筒3,机筒3由进料段机筒34、混炼段Ⅰ和捏炼段机筒33、混炼段Ⅱ机筒32、混炼段Ⅲ和挤出段机筒31四段组成,四段机筒大体上与复合型双转子2的加料段29、混炼段Ⅰ28至输送段Ⅰ26、混炼段Ⅱ25至输送段Ⅱ24、混炼段Ⅲ23至挤出段22相对应。机筒3分段组合便于制作、安装、更换和维护。每段机筒上有冷却水道311,冷却水从冷却水道入口331进入冷却水道311,从冷却水道出口332流出,对机筒3进行冷却。本实施例的分段机筒采用纵向上平分为两片的剖分式结构,剖分式结构便于机筒3和转子2的清洗和维护,方便拆分机筒3来观察各段混炼状态和混炼程度,为研究、改进设备提供依据,图中没有示出分段机筒的剖分式结构。Figure 3 is a schematic diagram of the barrel part of the mixing equipment in Figure 2 .
本发明的混炼设备能够进行橡胶连续、高效和高质量的混炼,与块状橡胶连续塑炼设备配套使用,能够实现块状橡胶连续混炼。The mixing equipment of the present invention can carry out continuous, high-efficiency and high-quality mixing of rubber, and can be used together with the block rubber continuous plasticating equipment to realize the continuous mixing of block rubber.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110026202XA CN102166794B (en) | 2011-01-25 | 2011-01-25 | Rubber continuous mixing dual-rotor structure and mixing equipment adopting same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110026202XA CN102166794B (en) | 2011-01-25 | 2011-01-25 | Rubber continuous mixing dual-rotor structure and mixing equipment adopting same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102166794A true CN102166794A (en) | 2011-08-31 |
| CN102166794B CN102166794B (en) | 2013-02-20 |
Family
ID=44488212
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110026202XA Active CN102166794B (en) | 2011-01-25 | 2011-01-25 | Rubber continuous mixing dual-rotor structure and mixing equipment adopting same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102166794B (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225315A (en) * | 2011-06-10 | 2011-10-26 | 北京化工大学 | Three-rotor continuous mixing unit with rotors arranged in a straight line |
| CN104354236A (en) * | 2014-11-14 | 2015-02-18 | 青岛科技大学 | Tandem type continuous rubber mixing device |
| CN104441301A (en) * | 2014-11-14 | 2015-03-25 | 青岛科技大学 | Continuous serial-type rubber mixing method |
| CN105965714A (en) * | 2016-06-17 | 2016-09-28 | 东莞市昶丰橡塑机械科技有限公司 | Novel continuous mixing machine structure |
| CN110712314A (en) * | 2019-10-23 | 2020-01-21 | 青岛科技大学 | A kind of rubber low temperature continuous mixing production device |
| CN110713663A (en) * | 2019-11-11 | 2020-01-21 | 永一橡胶有限公司 | Preparation method of tire curing bladder |
| CN111791459A (en) * | 2020-07-31 | 2020-10-20 | 南通回力橡胶有限公司 | Incongruous double helix desulfurization extruder |
| CN112549346A (en) * | 2020-10-21 | 2021-03-26 | 青岛科技大学 | Variable-gap rotor for internal mixer |
| CN114193648A (en) * | 2021-11-25 | 2022-03-18 | 广东维品承科技有限公司 | Silicon rubber mixing production device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1076653A (en) * | 1992-03-20 | 1993-09-29 | 方祖彭 | High-bearing-capacity high-speed bidirectional double-screw extruder |
| CN1076885A (en) * | 1992-01-31 | 1993-10-06 | 法拉·洛克斯得脱有限公司 | The continuous mixing and blending machine of multiscrew that is used for the plasticization mixture |
| JP2589251B2 (en) * | 1992-08-27 | 1997-03-12 | 株式会社日本製鋼所 | Kneading extrusion method |
| CN1190054A (en) * | 1996-12-24 | 1998-08-12 | 株式会社神户制钢所 | Biaxial mixing machine |
-
2011
- 2011-01-25 CN CN201110026202XA patent/CN102166794B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1076885A (en) * | 1992-01-31 | 1993-10-06 | 法拉·洛克斯得脱有限公司 | The continuous mixing and blending machine of multiscrew that is used for the plasticization mixture |
| CN1076653A (en) * | 1992-03-20 | 1993-09-29 | 方祖彭 | High-bearing-capacity high-speed bidirectional double-screw extruder |
| JP2589251B2 (en) * | 1992-08-27 | 1997-03-12 | 株式会社日本製鋼所 | Kneading extrusion method |
| CN1190054A (en) * | 1996-12-24 | 1998-08-12 | 株式会社神户制钢所 | Biaxial mixing machine |
Non-Patent Citations (2)
| Title |
|---|
| 侯垣圻: "橡胶双螺杆塑炼机连续炼机理及有限元模拟研究", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 * |
| 李青: "橡胶连续混炼机混炼机理及有限元模拟研究", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 * |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225315A (en) * | 2011-06-10 | 2011-10-26 | 北京化工大学 | Three-rotor continuous mixing unit with rotors arranged in a straight line |
| CN104354236A (en) * | 2014-11-14 | 2015-02-18 | 青岛科技大学 | Tandem type continuous rubber mixing device |
| CN104441301A (en) * | 2014-11-14 | 2015-03-25 | 青岛科技大学 | Continuous serial-type rubber mixing method |
| CN104354236B (en) * | 2014-11-14 | 2016-11-23 | 青岛科技大学 | A kind of tandem rubber compound continuous mixing device |
| CN105965714A (en) * | 2016-06-17 | 2016-09-28 | 东莞市昶丰橡塑机械科技有限公司 | Novel continuous mixing machine structure |
| CN110712314A (en) * | 2019-10-23 | 2020-01-21 | 青岛科技大学 | A kind of rubber low temperature continuous mixing production device |
| CN110712314B (en) * | 2019-10-23 | 2024-05-07 | 青岛科技大学 | A rubber low-temperature continuous mixing production device |
| CN110713663A (en) * | 2019-11-11 | 2020-01-21 | 永一橡胶有限公司 | Preparation method of tire curing bladder |
| CN111791459A (en) * | 2020-07-31 | 2020-10-20 | 南通回力橡胶有限公司 | Incongruous double helix desulfurization extruder |
| CN112549346A (en) * | 2020-10-21 | 2021-03-26 | 青岛科技大学 | Variable-gap rotor for internal mixer |
| CN112549346B (en) * | 2020-10-21 | 2022-02-01 | 青岛科技大学 | Variable-gap rotor for internal mixer |
| CN114193648A (en) * | 2021-11-25 | 2022-03-18 | 广东维品承科技有限公司 | Silicon rubber mixing production device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102166794B (en) | 2013-02-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102166794B (en) | Rubber continuous mixing dual-rotor structure and mixing equipment adopting same | |
| CN102120345B (en) | Blocky rubber continuous mixing method and device | |
| CN101837633B (en) | Embedded planetary-screw pulsation plasticizing exhaust extruder and method | |
| CN210211293U (en) | Environment-friendly powder coating extrusion breaker | |
| CN101362377B (en) | High-efficiency multi-screw extruder | |
| CN101875233A (en) | Conical three-screw extruder arranged in line | |
| CN101767430A (en) | Combined type machine set integrating functions of banburying, feeding and extruding into whole | |
| CN216329315U (en) | Banburying extruder | |
| CN101875232A (en) | Triangular arrangement of conical three-screw extruders | |
| CN102225317A (en) | Conical double rotor continuous mixing unit | |
| CN206066912U (en) | Conical double screw extruder with dynamic continuous mixing function | |
| CN201979624U (en) | Continuous mixing equipment | |
| CN212949081U (en) | Double-screw extruder for polyacrylic resin | |
| CN215203386U (en) | Special extrusion screw for efficient granulation of flat-double polyvinyl chloride powder | |
| CN102886888B (en) | Internal exhaust type parallel counter-rotating multi-screw extruder | |
| CN102248655A (en) | Tapered planetary screw extruder | |
| CN102228818A (en) | Continuous mixing unit with three tapered rotors in triangular arrangement | |
| CN201979625U (en) | Double rotor structure for continuously mixing and mixing equipment adopting same | |
| CN202212120U (en) | Conical tri-rotor continuous mixing unit with triangularly arranged rotors | |
| CN202155160U (en) | Conical dual-rotor continuous mixing unit | |
| CN202826362U (en) | Internal air-exhaust-type parallel counter-rotating multi-screw extruder | |
| CN102173004B (en) | Dual-rotor structure for continuous plastication of block-shaped rubbers and plastication device adopting rotors | |
| CN109049602A (en) | It is a kind of for producing the single screw extrusion machine of starch plastics | |
| CN201633185U (en) | Conical three-screw extruder arranged in line | |
| CN202114827U (en) | Double-rotor structure for continuous plastication and plasticating equipment utilizing same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |
