CN211487382U - Double-helix conical mixer - Google Patents
Double-helix conical mixer Download PDFInfo
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- CN211487382U CN211487382U CN201921976356.3U CN201921976356U CN211487382U CN 211487382 U CN211487382 U CN 211487382U CN 201921976356 U CN201921976356 U CN 201921976356U CN 211487382 U CN211487382 U CN 211487382U
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- 238000002156 mixing Methods 0.000 claims abstract description 50
- 239000011295 pitch Substances 0.000 claims description 64
- 238000003756 stirring Methods 0.000 claims description 32
- 239000003638 chemical reducing agent Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 abstract description 38
- 239000002245 particle Substances 0.000 abstract description 10
- 238000001125 extrusion Methods 0.000 abstract description 4
- 238000000227 grinding Methods 0.000 abstract description 4
- 238000005204 segregation Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000013329 compounding Methods 0.000 abstract 1
- 238000006073 displacement reaction Methods 0.000 abstract 1
- 239000000835 fiber Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 239000008187 granular material Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 3
- 208000019888 Circadian rhythm sleep disease Diseases 0.000 description 2
- 208000001456 Jet Lag Syndrome Diseases 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 208000033915 jet lag type circadian rhythm sleep disease Diseases 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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Abstract
Description
技术领域technical field
本实用新型涉及一种用于物料混合的机械,特别是一种双螺旋锥形混合机。The utility model relates to a machine for material mixing, in particular to a double-spiral conical mixer.
背景技术Background technique
双螺旋锥形混合机广泛应用于化工、医药、农药、复合肥、染料、颜料、橡胶、建材、涂料、食品、饲料、添加剂、精细化工、陶瓷、耐火材料等各行业的固-固(即粉体与粉体)粉体-液体的混合。Double helical conical mixers are widely used in solid-solid (ie solid-solid (ie. Powder and powder) powder-liquid mixing.
目前,常见的以双螺旋的公转而使粉体沿着锥体壁作圆周运动,螺旋叶片的自转,使粉体向锥体中央排放作径向运动的工作原理的双螺旋锥形混合机,不适合混合过程中加入纤维含量较大,物料密度、粒度差异较大的混合。其原因是,在混合过程中会产生分屑离析现象,出料口易堵塞,造成颗粒物料的挤压和磨碎。而且现有的螺旋叶片的中心是实心轴,加重设备自身的负载,增大了电机的驱动功率。同时也占用了物料的混合空间,即使采用更大功率的电机驱动也无法解决此现象。At present, the common double-helix conical mixer is a double-helix conical mixer that makes the powder move in a circular motion along the cone wall by the revolution of the double helix, and the rotation of the helical blade makes the powder discharge to the center of the cone for radial motion. It is not suitable for mixing with large fiber content and large differences in material density and particle size during the mixing process. The reason is that the phenomenon of chip separation and segregation occurs during the mixing process, and the discharge port is easily blocked, resulting in the extrusion and grinding of granular materials. Moreover, the center of the existing helical blade is a solid shaft, which increases the load of the equipment itself and increases the driving power of the motor. At the same time, it also occupies the mixing space of materials, which cannot be solved even if a higher-power motor drive is used.
因此,发明人经过实践摸索,研发出一种用于大密度、大粒度物料混合的双螺旋锥形混合机,彻底解决了粒物料的挤压和磨碎、物料离析、出料困难等难题。Therefore, the inventor has developed a double-helix conical mixer for mixing large-density and large-sized materials through practical exploration, which completely solves the problems of extrusion and grinding of granular materials, material segregation, and difficulty in discharging.
发明内容SUMMARY OF THE INVENTION
本实用新型的目的是要解决上述现有技术中的不足之处,提供一种双螺旋锥形混合机,是一种采用无轴变径变距螺旋叶片实现大密度、大粒度物料混合的双螺旋锥形混合机。The purpose of this utility model is to solve the above-mentioned deficiencies in the prior art, and provide a double-helix conical mixer, which is a double-helix conical mixer that adopts shaftless variable-diameter and variable-pitch helical blades to realize the mixing of large-density and large-granularity materials. Spiral cone mixer.
为解决上述技术问题,本实用新型采用的技术方案是:一种双螺旋锥形混合机,包括进料斗、锥体混料箱、无轴变径变距螺旋搅拌器,其特征是:进料斗安装在锥体混料箱的顶部,无轴变径变距螺旋搅拌器分别沿锥体混料箱的中心线对称倾斜安装在锥体混料箱的内部。In order to solve the above-mentioned technical problems, the technical scheme adopted by the present utility model is: a double-spiral conical mixer, comprising a feeding hopper, a conical mixing box, and a shaftless variable-diameter and variable-pitch screw agitator, which is characterized in that: The hopper is installed on the top of the cone mixing box, and the shaftless variable diameter and variable pitch screw agitators are respectively installed inside the cone mixing box symmetrically and obliquely along the center line of the cone mixing box.
进一步地,所述的锥体混料箱的底部设有一出料口。Further, the bottom of the cone mixing box is provided with a discharge port.
进一步地,所述的无轴变径变距螺旋搅拌器的中心线与锥体混料箱的中心线形成一α角。Further, the center line of the shaftless variable diameter and variable pitch screw agitator forms an angle α with the center line of the conical mixing box.
进一步地,所述的无轴变径变距螺旋搅拌器由左至右依次安装防爆双速电机、减速机、无变径变距螺旋搅拌叶片。Further, the shaftless variable diameter and variable pitch screw agitator is sequentially installed with an explosion-proof two-speed motor, a reducer, and a non-variable diameter and variable pitch screw stirring blade from left to right.
进一步地,所述无轴变径变距螺旋搅拌器的无轴变径变距螺旋搅拌叶片的大径值是D1,所述的无轴变径变距螺旋搅拌叶片的小径值是D2。Further, the large diameter value of the shaftless variable diameter and variable pitch screw stirring blade of the shaftless screw agitator is D1, and the small diameter value of the shaftless variable diameter variable pitch screw stirring blade is D2.
进一步地,所述无轴变径变距螺旋搅拌器的无轴变径变距螺旋搅拌叶片有三种螺距,分别是P1、P2、P3。Further, the shaftless variable diameter variable pitch screw stirring blades of the shaftless variable diameter variable pitch screw agitator have three pitches, namely P1, P2, and P3.
进一步地,所述的α角的值是在5°—20°范围内。Further, the value of the α angle is in the range of 5°-20°.
进一步地,所述无轴变径变距螺旋搅拌器的无轴变径变距螺旋搅拌叶片的大径D1的值是在100mm—200mm范围内,所述的无轴变径变距螺旋搅拌叶片的小径D2的值是在70mm—140mm范围内。Further, the value of the large diameter D1 of the shaftless variable diameter and variable pitch screw stirring blade of the shaftless variable diameter variable pitch screw agitator is in the range of 100mm-200mm, and the shaftless variable diameter variable pitch screw stirring blade The value of the minor diameter D2 is in the range of 70mm-140mm.
进一步地,所述无轴变径变距螺旋搅拌器的无轴变径变距螺旋搅拌叶片的三种螺距P1、P2、P3的值分别是在:80mm-100mm范围内、60mm-80mm范围内、40mm-60mm范围内。Further, the values of the three pitches P1, P2, and P3 of the shaftless variable diameter variable pitch screw stirring blade of the shaftless variable diameter variable pitch screw agitator are respectively in the range of 80mm-100mm and 60mm-80mm. , 40mm-60mm range.
本实用新型的有益效果是:能适用于混合过程中加入纤维含量较大,物料密度、粒度差异较大的混合,搅拌叶片不占据过多的搅拌空间,同时在混合过程中颗避免了粒物料的挤压和磨碎、物料离析,以及出料困难等问题,结构简单,制造成本低,节省能源消耗。The beneficial effects of the utility model are: it can be applied to the mixing process with large fiber content and large difference in material density and particle size, the stirring blades do not occupy too much stirring space, and the granular materials are avoided in the mixing process. It has the advantages of simple structure, low manufacturing cost and energy saving.
附图说明Description of drawings
下面结合附图和具体实施方式对本实用新型作进一步详细说明。The present utility model will be described in further detail below with reference to the accompanying drawings and specific embodiments.
图1是本实用新型一种双螺旋锥形混合机的结构示意图。FIG. 1 is a schematic structural diagram of a double-spiral conical mixer of the present invention.
图2是本实用新型中,无轴变径变距螺旋搅拌器的结构示意图。Figure 2 is a schematic structural diagram of a shaftless variable diameter variable pitch screw agitator in the present invention.
具体实施方式Detailed ways
由图1-2可知:本实用新型一种双螺旋锥形混合机,包括进料斗1、锥体混料箱2、无轴变径变距螺旋搅拌器3,进料斗1安装在锥体混料箱2的顶部,无轴变径变距螺旋搅拌器3分别沿锥体混料箱2的中心线对称倾斜安装在锥体混料箱2的内部。It can be seen from Figures 1-2 that the utility model is a double-spiral conical mixer, comprising a feeding hopper 1, a
进一步地,所述的锥体混料箱2的底部设有一出料口2-1。Further, the bottom of the
进一步地,所述的无轴变径变距螺旋搅拌器3的中心线与锥体混料箱2的中心线形成一α角。Further, the center line of the shaftless variable diameter and variable
进一步地,所述的无轴变径变距螺旋搅拌器3由左至右依次安装防爆双速电机3-1、减速机3-2、无变径变距螺旋搅拌叶片3-3。Further, the shaftless variable diameter variable
进一步地,所述的无轴变径变距螺旋搅拌叶片3-3的大径值是D1,所述的无轴变径变距螺旋搅拌叶片3-3的小径值是D2。Further, the large diameter value of the shaftless variable diameter and variable pitch screw stirring blade 3-3 is D1, and the small diameter value of the shaftless variable diameter variable pitch screw stirring blade 3-3 is D2.
进一步地,所述的无轴变径变距螺旋搅拌叶片3-3有三种螺距,分别是P1、P2、P3。Further, the shaftless variable diameter and variable pitch helical stirring blades 3-3 have three pitches, namely P1, P2, and P3.
进一步地,所述的α角的值是在5°—20°范围内。Further, the value of the α angle is in the range of 5°-20°.
进一步地,所述的无轴变径变距螺旋搅拌叶片3-3的大径D1的值是在100mm—200mm范围内,所述的无轴变径变距螺旋搅拌叶片3-3的小径D2的值是在70mm—140mm范围内。Further, the value of the large diameter D1 of the shaftless variable diameter and variable pitch spiral stirring blade 3-3 is in the range of 100mm-200mm, and the small diameter D2 of the described shaftless variable diameter variable pitch screw stirring blade 3-3. The value of is in the range of 70mm-140mm.
进一步地,所述的无轴变径变距螺旋搅拌叶片3-3的三种螺距P1、P2、P3的值分别是在:80mm-100mm范围内、60mm-80mm范围内、40mm-60mm范围内。Further, the values of the three pitches P1, P2, and P3 of the shaftless variable diameter and variable pitch spiral stirring blades 3-3 are respectively in the range of 80mm-100mm, 60mm-80mm, and 40mm-60mm. .
本实用新型一种双螺旋锥形混合机的工作过程是:The working process of the double-spiral conical mixer of the utility model is as follows:
通过开启无轴变径变距螺旋搅拌器3的防爆双速电机3-1,防爆双速电机3-1带动减速机3-2,使减速机3-2驱动无轴变径变距螺旋搅拌叶片3-3将进料斗1中落入到锥体混料箱2的物料进行搅拌混合,当混合纤维含量较大,物料密度、粒度差异较大的物料时,将沿锥体混料箱2的中心线对称倾斜安装在锥体混料箱2内的无轴变径变距螺旋搅拌器3的其中一个防爆双速电机3-1开启低速挡,进行顺时针转动,将另一个无轴变径变距螺旋搅拌器3的防爆双速电机3-1开启高速挡,进行逆时针转动,当纤维含量较大,物料密度、粒度差异较大的物料从进料斗1中落入到锥体混料箱2时,顺时针低速转动的螺旋搅拌器3将纤维含量较大,物料密度、粒度差异较大的物料向锥体混料箱2的下方推进,逆时针高速转动的螺旋搅拌器3将纤维含量较大,物料密度、粒度差异较大的物料向锥体混料箱2的上方推进,使纤维含量较大,物料密度、粒度差异较大的物料实现强制搅拌,无轴变径变距螺旋搅拌叶片3-3的螺距P1的值最大,物料在搅拌过程中,逆时针高速转动的螺旋搅拌器3推上来的均是密度大、颗粒大的物料,将这些密度大、颗粒大的物料暂驻留在无轴变径变距螺旋搅拌叶片3-3的螺距P1段,等待与另一个顺时针低速转动的螺旋搅拌器3将进料斗1的物料向下推时的逆向时差混合,通过逆向时差混合的物料会沿顺时针低速转动的螺旋搅拌器3的向下推进到无轴变径变距螺旋搅拌叶片3-3的螺距P2段,再进行一次逆向时差混合,使这些密度大、颗粒大的物料充分搅拌混合。无轴变径变距螺旋搅拌叶片3-3的螺距P3段的螺距值最小,同时离混料箱2的底部的出料口2-1最近,落入到无轴变径变距螺旋搅拌叶片3-3的螺距P3段的纤维含量较大,密度大的物料会在逆时针高速转动的螺旋搅拌器3的逆向时差的作用下,逆时针高速转动的螺旋搅拌器3向上推送大量的纤维含量较大、密度大的物料进行二次混合,给顺时针低速转动的螺旋搅拌器3向下推送的混合好的物料移除出料空间,使其顺畅地从混料箱2的底部的出料口2-1处出料。与同体积的传统锥体混料箱相比较,本实用新型采用的是无轴变径变距螺旋搅拌叶片3-3进行物料混合,锥体混料箱2内能装载更多容量的物料,同时功率消耗也随之降低,生产成本也随之降低,方便实用,解决了现有技术中存在的颗粒物料的挤压和磨碎、物料离析、出料困难等难题,适合大力推广。By turning on the explosion-proof two-speed motor 3-1 of the shaftless variable-diameter and variable-
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