CN100430144C - Powder Breaker - Google Patents
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- CN100430144C CN100430144C CNB2006100273930A CN200610027393A CN100430144C CN 100430144 C CN100430144 C CN 100430144C CN B2006100273930 A CNB2006100273930 A CN B2006100273930A CN 200610027393 A CN200610027393 A CN 200610027393A CN 100430144 C CN100430144 C CN 100430144C
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- 239000000843 powder Substances 0.000 title claims abstract description 60
- 238000002156 mixing Methods 0.000 claims abstract description 29
- 238000000034 method Methods 0.000 abstract description 18
- 239000000463 material Substances 0.000 abstract description 11
- 240000008397 Ganoderma lucidum Species 0.000 abstract description 6
- 235000001637 Ganoderma lucidum Nutrition 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 230000001133 acceleration Effects 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 10
- 239000002245 particle Substances 0.000 description 10
- 238000010298 pulverizing process Methods 0.000 description 7
- 238000000227 grinding Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
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- 238000000926 separation method Methods 0.000 description 3
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- 230000007547 defect Effects 0.000 description 2
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- 238000009434 installation Methods 0.000 description 2
- 238000000053 physical method Methods 0.000 description 2
- 239000004480 active ingredient Substances 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
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- 238000005265 energy consumption Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000010902 jet-milling Methods 0.000 description 1
- 230000009916 joint effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
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- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
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Abstract
本发明综合高压气流进料、高压加速和靶式破壁的技术,开发了一种新的粉体破壁设备—粉体破壁机,在常温的工艺条件下可获得超细粉碎和破壁的粉体。包括吸入室、气物混合室和破壁室15,其特征在于,破壁室中设置了一个倾斜的靶板。倾斜靶板的设计有利于高压气流中夹带需粉碎和破壁的粉体与靶体进行有效撞击,使高速气流撞击靶板时形成折流,降低了靶板表面的滞后层厚度,可在非超高压的工况下,也能实现对花粉、灵芝孢子粉等粉体有效的粉碎和破壁,降低了粉体粉碎和破壁的生产成本。
The present invention integrates the technologies of high-pressure airflow feeding, high-pressure acceleration and target-type wall-breaking, and develops a new powder wall-breaking equipment—powder wall-breaking machine, which can obtain ultra-fine crushing and wall-breaking under normal temperature process conditions. powder. It includes a suction chamber, a gas-material mixing chamber and a wall-breaking chamber 15, and is characterized in that an inclined target plate is set in the wall-breaking chamber. The design of the inclined target plate is conducive to the effective impact of the powder that needs to be pulverized and broken in the high-pressure airflow to the target body, so that the high-speed airflow will form a baffle when it hits the target plate, reducing the thickness of the hysteresis layer on the surface of the target plate. Under ultra-high pressure conditions, it can also achieve effective crushing and wall breaking of powders such as pollen and ganoderma lucidum spore powder, reducing the production cost of powder crushing and wall breaking.
Description
技术领域 technical field
本发明属于超细粉体技术领域。本发明提出一种能使粉体被超细粉碎、并达到破壁的设备。The invention belongs to the technical field of ultrafine powder. The invention proposes a device capable of superfinely pulverizing powder and achieving wall breaking.
背景技术 Background technique
粉体破壁是有效提取单个粉体内有效成份,提高粉体活性的关键技术,通常粉体破壁与超细粉碎一样延用物理的方法将粉体进行粉碎,在粉碎过程中实现粉体的破壁。而物理方法又以粉碎法为主,粉碎法是一种借用各种外力,如机械力、流能力、声能等力作用于被需要粉碎的物体上,将固体块料粉碎,并达到很细的粒度和破壁的目的。目前工业上,实验室采用最多的粉碎设备有球磨式粉碎机,高速旋转式粉碎机、气流粉碎机、微射流粉碎机等。Powder wall breaking is the key technology to effectively extract the active ingredients in a single powder and improve the activity of the powder. Usually, the powder wall breaking is the same as the ultra-fine grinding, and the powder is crushed by physical methods, and the powder is crushed during the crushing process. Broken. The physical method is mainly based on the crushing method. The crushing method is a kind of borrowing various external forces, such as mechanical force, flow capacity, sound energy, etc., to act on the object to be crushed to crush the solid block and achieve a very fine The particle size and the purpose of breaking the wall. At present, in the industry, the most commonly used pulverizers in laboratories include ball mill pulverizers, high-speed rotary pulverizers, jet pulverizers, micro jet pulverizers, etc.
球磨式粉碎机是用介质与物料之间的相互冲击和研磨,使物料颗粒粉碎。通常使用这类粉碎设备操作时间长,虽然也可进行连续的操作,粉碎的粒径也可达到几个μm,但由于粉碎过程中,介质和被粉碎物料的直接和长时间的冲击、碰撞使被粉碎物料的纯度受到影响,特别是研磨过程中产生的热量不能马上被移走,热量的急骤上升会使热敏性物质受到影响。The ball mill pulverizer uses the mutual impact and grinding between the medium and the material to crush the material particles. Usually, the operation time of this kind of crushing equipment is long. Although continuous operation can also be carried out, and the particle size of the crushing can reach several μm, due to the direct and long-term impact and collision between the medium and the crushed material during the crushing process, the The purity of the crushed material is affected, especially the heat generated during the grinding process cannot be removed immediately, and a sudden increase in heat will affect heat-sensitive substances.
高速旋转式粉碎机是利用高速旋转的装置,对需要被粉碎的物体,要通过研磨进行粉碎。因此,同样存在上述的一些缺陷。The high-speed rotary pulverizer is a device that uses high-speed rotation to pulverize the objects that need to be pulverized by grinding. Therefore, there are also some defects mentioned above.
超细粉碎采用最多、最典型的是气流粉碎法,这一技术是利用高速气流(300-500m/s)的能量,使物体颗粒产生相互的冲击,碰撞,而被较快地超细粉碎,这种技术,可获得几个μm的粒径,但粒径分布较宽,需进行粒径分级处理。尽管如此,对于像花粉、灵芝孢子粉等这类具有一定韧性的粉体,不仅粉碎的效果受到影响,更难达到破壁的效果。工艺上通常采用重复多次的粉碎,采用冷冻工况下的粉碎。重复多次的工艺过程由于气流粉碎是在瞬间进行碰撞实现粉碎的机理,决定了提高粉碎的效果是有限的,也很难使韧性粉体实现破壁,而使设备的能耗增加利用效率降低。采用冷冻工况下的粉碎,可使粉碎效果和破壁效果得到提高,但冷冻工况的工艺过程使生产设备的投资和操作费用也增加。Ultra-fine pulverization is the most widely used and most typical jet pulverization method. This technology uses the energy of high-speed airflow (300-500m/s) to make object particles collide with each other and be ultra-fine pulverized quickly. This technology can obtain a particle size of several μm, but the particle size distribution is wide, and particle size classification is required. However, for powders with certain toughness such as pollen and ganoderma lucidum spore powder, not only the effect of crushing is affected, but also it is more difficult to achieve the effect of breaking the wall. In the process, crushing is usually repeated many times, and crushing under freezing conditions is used. Due to the mechanism of jet milling that achieves crushing by collision in an instant, the process of repeating the process for many times determines that the effect of improving the crushing is limited, and it is also difficult to break the wall of the tough powder, which increases the energy consumption of the equipment and reduces the utilization efficiency . The pulverization under the freezing condition can improve the pulverization effect and the wall-breaking effect, but the technological process of the freezing condition increases the investment and operation cost of the production equipment.
微射流粉碎法是利用高压液体通过喷射器加速后,形成高速射流,带动需要粉碎的固体颗粒作高速运动,携带颗粒的射流体与靶板或相反方向的另一股射流形成高压碰撞,由于强烈的撞击,使其中的固体物料被粉碎,这种粉碎方法,其优点是粉碎的粒径小,且比较均匀,但不足之处是,高压液体通常要求达到200MPa,这给设备制造和生产工艺带来极高的要求,从而使粉碎成本大大的提高,另外,由于高压液体的介入,其后期分离,远比以空气为介质的分离增加了难度,且影响了产品的纯度。再有其靶板设计和安装与高速射流成直角,使得高速射流与靶板之间形成的滞流层不易扩散,一定程度上影响了微射流粉碎机应有的粉碎效果。The micro-jet crushing method is to use high-pressure liquid to accelerate through the injector to form a high-speed jet, which drives the solid particles to be crushed to move at high speed. The jet carrying the particles forms a high-pressure collision with the target plate or another jet in the opposite direction. Due to the strong The impact of the impact makes the solid material in it crushed. The advantage of this crushing method is that the crushed particle size is small and relatively uniform, but the disadvantage is that the high-pressure liquid is usually required to reach 200MPa, which brings great pressure on equipment manufacturing and production processes. In addition, due to the intervention of high-pressure liquid, the later separation is far more difficult than the separation using air as the medium, and affects the purity of the product. In addition, the design and installation of the target plate are at right angles to the high-speed jet, so that the stagnant layer formed between the high-speed jet and the target plate is not easy to spread, which affects the pulverizing effect of the micro jet pulverizer to a certain extent.
发明内容 Contents of the invention
针对现有技术的缺陷,本发明综合高压气流进料、高压加速和靶式破壁的技术,开发了一种新的粉体破壁设备-粉体破壁机,在常温的工艺条件下可获得超细粉碎和破壁的粉体。Aiming at the defects of the existing technology, the present invention integrates the technologies of high-pressure airflow feeding, high-pressure acceleration and target-type wall breaking, and develops a new powder breaking equipment-powder breaking machine, which can be used under normal temperature process conditions. Obtain ultra-fine crushed and broken powder.
本发明是通过以下技术方案实现的:The present invention is achieved through the following technical solutions:
一种粉体破壁机,包括吸入室7、气物混合室10和破壁室15,其相应壳体通过法兰17、18顺序相连,一个带有高压进气口4的喷管5设置在吸入室7内,吸入室7腔壁上、下分别设有负压进料管8和负压回料管9并伸出壳体,与吸入室7相连通的气物混合室10的腔壁上设有高压加速管12,混合室10前端的气物喷管13与破壁室15相连通,破壁室15上方设有气物出口16,其特征在于,破壁室15中设置了一个倾斜的靶板14,该靶板14与破壁室15的设有气物出口16的腔壁延气物喷管13方向有一夹角α,α为20°~40°。A powder wall-breaking machine, including a suction chamber 7, a gas-material mixing chamber 10, and a wall-breaking chamber 15, the corresponding shells are sequentially connected by flanges 17, 18, and a nozzle 5 with a high-pressure air inlet 4 is set In the suction chamber 7, a negative pressure feed pipe 8 and a negative pressure return pipe 9 are respectively provided on the upper and lower walls of the suction chamber 7 and extend out of the housing, and the chamber of the gas-material mixing chamber 10 communicated with the suction chamber 7 The wall is provided with a high-pressure acceleration tube 12, the gas nozzle 13 at the front end of the mixing chamber 10 communicates with the wall-breaking chamber 15, and a gas-material outlet 16 is provided above the wall-breaking chamber 15. An inclined target plate 14, the target plate 14 has an included angle α with the direction of the aerosol nozzle 13 along the cavity wall provided with the gas outlet 16 of the broken wall chamber 15, and α is 20°-40°.
所述的粉体破壁机的吸入室7上部可设有多个负压进料管8。The upper part of the suction chamber 7 of the powder wall breaking machine can be provided with a plurality of negative pressure feeding pipes 8 .
所述的粉体破壁机的气物混合室10的腔壁上下对应设有一对高压加速管12,高压加速管12与混合室10腔壁的夹角β为45°~60°。A pair of high-pressure accelerating tubes 12 are arranged on the upper and lower walls of the gas-substance mixing chamber 10 of the powder wall breaker, and the angle β between the high-pressure accelerating tubes 12 and the mixing chamber 10 wall is 45°-60°.
所述的粉体破壁机的气物混合室10的腔壁上,上下对应设有一对以上相互平行的高压加速管12。On the cavity wall of the gas-substance mixing chamber 10 of the powder wall breaking machine, there are more than one pair of high-pressure acceleration tubes 12 parallel to each other.
所述的粉体破壁机的混合室10前端的气物喷管13,为管径向喷口处逐渐减小的喇叭形喷管。The gas nozzle 13 at the front end of the mixing chamber 10 of the powder wall breaker is a trumpet-shaped nozzle that gradually decreases in the radial direction of the nozzle.
本发明的粉体破壁机,包括高压气速(0.6MPa-2MPa)进气口,和与其相应的二个以上进料口,需要粉碎和破壁的粉体随高压气流被吸入腔体至吸入室,吸入室相连接的是混合腔。混合腔壁面有二个以上的高压加速管,高压加速管的导入与混合腔的腔体壁面有一个角度,顺着高压气速进气口进来的高压气体和吸入的需要粉碎和破壁的粉体的初步混合后,喷射进入混合腔的方向切入,高压加速管进入的高压气体(0.6MPa-2MPa)和吸入室喷射过来的气体在混合腔内作进一步充分的混合后,又通过混合腔至破壁腔的喷头,高速喷射到破壁腔内倾斜安装的靶板上。由于靶板的设计是倾斜的,夹带着需要粉碎和破壁的粉体的气流以极高的速度冲撞在倾斜的靶板上,在常温的工艺条件下瞬间获得有效的粉碎和破壁后,便折向出口端进行后序的收集工序。The powder wall breaker of the present invention includes a high-pressure gas velocity (0.6MPa-2MPa) air inlet, and more than two corresponding feed ports, the powder that needs to be crushed and broken is sucked into the cavity with the high-pressure airflow. The suction chamber is connected with the mixing chamber. There are more than two high-pressure accelerating tubes on the wall of the mixing chamber. The introduction of the high-pressure accelerating tubes has an angle with the wall of the mixing chamber. The high-pressure gas coming in along the high-pressure gas velocity inlet and the powder that needs to be crushed and broken After the initial mixing of the body, the injection enters the direction of the mixing chamber, and the high-pressure gas (0.6MPa-2MPa) entering the high-pressure accelerating tube and the gas injected from the suction chamber are further fully mixed in the mixing chamber, and then pass through the mixing chamber to the The nozzle of the crushing chamber sprays at high speed onto the target plate installed obliquely in the crushing chamber. Because the design of the target plate is inclined, the airflow carrying the powder that needs to be crushed and broken walls collides with the inclined target plate at a very high speed. Just turn to the outlet end to carry out the subsequent collection process.
有益效果Beneficial effect
本发明与现有技术相比,其设计优点和有益效果在于:Compared with the prior art, the present invention has design advantages and beneficial effects as follows:
1、倾斜靶板的设计有利于高压气流中夹带需粉碎和破壁的粉体与靶体进行有效撞击,同时在撞击靶板的瞬间与先前已撞击靶板,且改变了流动方向的粉体进行再次撞击和摩擦,使花粉、灵芝孢子粉等含有多糖和皂甙等物质的韧性物质,和带有加强的双层壳体结构的物质的粉碎和破壁效果增强,提高花粉、灵芝孢子粉的生物活性发挥更好疗效;且斜靶板的设计,使高速气流撞击靶板时形成折流,降低了靶板表面的滞后层厚度,可在非超高压的工况下,也能实现对花粉、灵芝孢子粉等粉体有效的粉碎和破壁,降低了粉体粉碎和破壁的生产成本。1. The design of the inclined target plate is conducive to the effective impact of the powder entrained in the high-pressure airflow that needs to be crushed and broken and the target body. At the same time, at the moment of impacting the target plate, the powder that has hit the target plate before and changed the flow direction Re-impact and rub, so that pollen, Ganoderma lucidum spore powder and other tough substances containing polysaccharides and saponins, and materials with a reinforced double-layer shell structure have enhanced crushing and wall-breaking effects, and improve the pollen and Ganoderma lucidum spore powder. The biological activity exerts a better curative effect; and the design of the slanted target plate makes the high-speed airflow form a baffle when it hits the target plate, which reduces the thickness of the hysteresis layer on the surface of the target plate, and can also achieve anti-pollen under non-ultra-high pressure conditions. , Ganoderma lucidum spore powder and other powders can be effectively crushed and wall-broken, which reduces the production cost of powder crushing and wall-breaking.
2、两个以上进料口的设计,便于进料粉体密度和速度的控制,可实现粉体被粉碎、破壁后,通过通常的分级、气固分离后,粉体再次返回破壁机进行连续的循环操作工艺;2. The design of more than two feed ports facilitates the control of the density and speed of the feed powder, and can realize that after the powder is crushed and broken, the powder returns to the breaker after passing through the usual classification and gas-solid separation. Carry out continuous cycle operation process;
3、具有一定角度的成对排列的高压加速管的设计使用,有利于气流速度的提高,有利于高压气流和需要粉碎和破壁的粉体的充分混合。3. The design and use of high-pressure accelerating tubes arranged in pairs at a certain angle is conducive to the increase of air velocity and the full mixing of high-pressure air and powder that needs to be crushed and broken.
4、从混合室向破壁室喷射物料的喷管呈喇叭形,有利于......?。4. The nozzle for spraying material from the mixing chamber to the wall-breaking chamber is trumpet-shaped, which is beneficial to...? .
附图说明: Description of drawings:
图1为粉体破壁设备的结构示意图Figure 1 is a schematic diagram of the powder wall breaking equipment
其中:1-吸入室壳体,2-混合室壳体,3-破壁室壳体,4-高压进气口,5-喷气管,6-喷气口,7-吸入室,8-负压进料管,9-负压回料管,10-气物混合室,11-高压二次进气口,12-高压加速管,13-气物喷管,14-靶板,15-破壁室,16气物出口,17、18-连接法兰,19-机架。Among them: 1-suction chamber shell, 2-mixing chamber shell, 3-wall breaking chamber shell, 4-high pressure air inlet, 5-jet pipe, 6-jet port, 7-suction chamber, 8-negative pressure Feed pipe, 9-negative pressure return pipe, 10-gas mixing chamber, 11-high pressure secondary air inlet, 12-high pressure accelerating tube, 13-gas nozzle, 14-target plate, 15-broken wall Chamber, 16 gas outlet, 17, 18-connecting flange, 19-frame.
下面结合附图及具体实施方式对本发明作进一步阐述。The present invention will be further elaborated below in conjunction with the accompanying drawings and specific embodiments.
具体实施方式 Detailed ways
本发明设计的粉体破壁设备运行时,首先打开高压气体的进气阀门,高压气体由高压气体进气口4进入破壁设备腔体的吸入室7,需要粉碎和破壁的粉体,由于腔体吸入室7内的文丘利喷气管5产生的负压,粉体通过2个以上的负压进料8吸入,此时只要打开进料口前的调节阀门,粉体就吸入腔体(吸入室7),粉体吸入室7与混和腔10连接,混和腔10的腔壁上设有一对高压加速管12,此时,打开高压进气阀门,高压气流从二次高压进口11通过高压加速管12,以300--500m/s的高速进入混和腔10,并与粉体吸入室7的喷气口6喷射过来的、夹带着需要粉碎和破壁粉体的气体在混和腔10内充分混合,经加速充分混合后的高速气流,通过气物喷管13喷射撞击在破壁室15的倾斜靶板14上,实现粉碎和破壁的操作;When the powder wall-breaking equipment designed by the present invention is in operation, the intake valve of the high-pressure gas is first opened, and the high-pressure gas enters the suction chamber 7 of the wall-breaking equipment cavity from the high-pressure gas inlet 4, and the powder that needs to be crushed and broken, Due to the negative pressure generated by the Venturi jet pipe 5 in the cavity suction chamber 7, the powder is sucked through more than two negative pressure feeds 8. At this time, as long as the regulating valve in front of the feed inlet is opened, the powder will be sucked into the cavity (Suction chamber 7), the powder suction chamber 7 is connected with the mixing chamber 10, a pair of high-pressure accelerating tubes 12 are arranged on the chamber wall of the mixing chamber 10, at this time, the high-pressure air inlet valve is opened, and the high-pressure air flow passes through the secondary high-pressure inlet 11 The high-pressure accelerating tube 12 enters the mixing chamber 10 at a high speed of 300--500m/s, and the gas injected from the gas injection port 6 of the powder suction chamber 7, entraining the powder that needs to be pulverized and wall-broken, enters the mixing chamber 10 Fully mixed, the accelerated and fully mixed high-speed airflow is jetted through the gas nozzle 13 and hits the inclined target plate 14 of the wall-breaking chamber 15 to realize the operation of crushing and wall-breaking;
夹带着需要粉碎和破壁的粉体的高速气流在与倾斜靶板14高速撞击时,由于具有一定角度的倾斜靶板14的倾斜安装的作用,形成折射,和出口端压力降的共同作用下,流向与折射方向一致的气物出口16,完成了整个的粉碎和破壁的工序。When the high-speed airflow carrying the powder that needs to be pulverized and broken walls hits the inclined target plate 14 at high speed, due to the effect of the inclined installation of the inclined target plate 14 with a certain angle, refraction is formed, and under the joint action of the pressure drop at the outlet end , flows to the gas outlet 16 consistent with the refraction direction, and completes the whole process of crushing and wall breaking.
从气物出口16物料可以经管道进入负压回料管9,进入吸入室后再次经上述步骤循环进行破壁粉碎。The material from the gas outlet 16 can enter the negative pressure return pipe 9 through the pipeline, and after entering the suction chamber, go through the above steps again for wall breaking and pulverization.
实施例Example
在常温条件下,工作压力为0.85MPa的工况,采用本发明的粉体破壁机进行灵芝孢子粉的粉碎破壁实验。把所获得的最终产品,用JSM-6360LV型扫描电子显微镜下观察其破壁率达到98%。Under the condition of normal temperature and working pressure of 0.85 MPa, the crushing and wall breaking experiment of Ganoderma lucidum spore powder was carried out by adopting the powder wall breaking machine of the present invention. The obtained final product is observed under a JSM-6360LV scanning electron microscope, and its wall breaking rate reaches 98%.
Claims (4)
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