CN107537697A - A kind of experimental rig for probing into Coarse Coal unit flotation desorption yield - Google Patents
A kind of experimental rig for probing into Coarse Coal unit flotation desorption yield Download PDFInfo
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Abstract
本发明提供一种探究粗粒煤单元浮选脱附产率的试验装置,浮选精矿收集槽、上柱体、下柱体、底锥;所述上柱体的上部与浮选精矿收集槽相连,上柱体的下部与布水管相贯,上柱体的底端与下柱体的顶端相连;所述下柱体的上部与循环矿浆入料弯管相贯,下柱体的下部与通气管相贯,通气管在下主体内的端口与气泡石相连,下柱体的底端与底锥的广口相连;所述底锥的窄口与循环矿浆出料管相连;循环矿浆出料管与循环矿浆入料弯管通过循环矿浆管相连,循环矿浆管上设有循环泵。煤粒在下柱体的循环流体中与气泡碰撞、粘附,粘附后的煤粒被气泡带入上柱体的上升流体中,此时上柱体中的部分脱附煤粒在上升水流的作用下与易浮煤粒一同进入浮选精矿收集槽。
The invention provides a test device for exploring the unit flotation desorption yield of coarse-grained coal, a flotation concentrate collection tank, an upper column, a lower column, and a bottom cone; the upper part of the upper column and the flotation concentrate The collection tank is connected, the lower part of the upper column is intersected with the water distribution pipe, the bottom of the upper column is connected with the top of the lower column; the upper part of the lower column is intersected with the circular slurry feeding elbow, and the The lower part is intersected with the ventilation pipe, the port of the ventilation pipe in the lower main body is connected with the air stone, the bottom of the lower column is connected with the wide mouth of the bottom cone; the narrow mouth of the bottom cone is connected with the circulating slurry discharge pipe; the circulating slurry The discharge pipe is connected with the circulating pulp inlet elbow through the circulating pulp pipe, and a circulating pump is arranged on the circulating pulp pipe. Coal particles collide with and adhere to air bubbles in the circulating fluid of the lower column, and the adhered coal particles are brought into the ascending fluid of the upper column by the air bubbles. Under the action, it enters the flotation concentrate collection tank together with the easy-to-float coal particles.
Description
技术领域technical field
本发明涉及探究煤粒脱附产率的装置,尤其是一种探究粗粒煤单元浮选脱附产率的试验装置。The invention relates to a device for exploring the desorption yield of coal particles, in particular to a test device for exploring the desorption yield of coarse coal unit flotation.
背景技术Background technique
浮选过程可分为碰撞、粘附、脱附三个阶段。1、矿粒在流动矿浆中以一定的速度和气泡接近,并进行碰撞接触;2、随着颗粒与气泡之间的距离不断缩小,位于二者之间的普通水分子逐渐被排开,由于普通的水分子排列无序,因此该过程很容易发生。当二者的距离接近到二者的水化膜接触时,开始进行水化膜薄化的过程,气泡与颗粒表面的水化膜开始脱水,彼此的水化膜厚度不断变小,直到临界厚度。随后气泡表面的水化膜会迅速破裂,颗粒与气泡实现真正的接触,从而形成气固液三相润湿周边,随着三相润湿周边的扩展,颗粒稳固的吸附到气泡上;3、并不是所有黏附到气泡上的颗粒都会进入泡沫层被刮出,有些从气泡表面脱落重新进入矿浆。与颗粒-气泡的碰撞、粘附不同,颗粒-气泡的脱附过程更加复杂,牵涉到表面物理化学等微观作用力,其机理至今不甚明了,并且现有研究设备、研究方法仍有很多不足。The flotation process can be divided into three stages: collision, adhesion and desorption. 1. The ore particles approach the air bubbles at a certain speed in the flowing pulp and collide with them; 2. As the distance between the particles and the air bubbles shrinks, the ordinary water molecules between them are gradually pushed away. Ordinary water molecules are arranged disorderly, so the process occurs easily. When the distance between the two is close to the contact of the hydration film of the two, the process of thinning the hydration film begins, the hydration film on the surface of the air bubbles and the particle starts to dehydrate, and the thickness of the hydration film of each other continues to decrease until the critical thickness . Then the hydration film on the surface of the bubbles will break rapidly, and the particles and the bubbles will come into real contact, thus forming a gas-solid-liquid three-phase wetted periphery. With the expansion of the three-phase wetted periphery, the particles will be firmly adsorbed on the bubbles; 3. Not all particles adhering to the bubbles will enter the foam layer and be scraped out, and some will fall off the surface of the bubbles and re-enter the slurry. Different from the particle-bubble collision and adhesion, the particle-bubble desorption process is more complicated, involving microscopic forces such as surface physics and chemistry. The mechanism is still unclear, and there are still many deficiencies in existing research equipment and research methods. .
发明内容Contents of the invention
本发明所要解决的技术问题在于克服现有技术缺陷,突破实验室单个气泡与煤粒群或单个煤粒与气泡群作用的局限,通过气泡群和煤粒群的作用,从统计学的层面探究了脱附产率,提供一种结构简单、实验室用的探究粗粒煤单元浮选脱附产率的装置。The technical problem to be solved by the present invention is to overcome the defects of the prior art, to break through the limitations of the interaction between a single air bubble and a coal particle group or a single coal particle and a bubble group in the laboratory, and to explore statistically through the effects of the air bubble group and coal particle group In order to improve the desorption yield, a device with simple structure and laboratory use for exploring the desorption yield of coarse coal unit flotation is provided.
为了解决上述技术问题,本发明提供的探究粗粒煤单元浮选脱附产率的试验装置包括浮选精矿收集槽、上柱体、下柱体、底锥、循环矿浆入料弯管、循环矿浆出料管、通气管、气泡石及布水管;所述上柱体的上部与浮选精矿收集槽相连,上柱体的下部与布水管相贯,布水管上设有布水孔,上柱体的底端与下柱体的顶端相连;所述下柱体的上部与循环矿浆入料弯管相贯,下柱体的下部与通气管相贯,通气管在下主体内的端口与气泡石相连,下柱体的底端与底锥的广口相连;所述底锥的窄口与循环矿浆出料管相连;循环矿浆出料管与循环矿浆入料弯管通过循环矿浆管相连,循环矿浆管上设有循环泵。In order to solve the above-mentioned technical problems, the test device provided by the present invention to explore the flotation desorption yield of coarse-grained coal unit includes a flotation concentrate collection tank, an upper column, a lower column, a bottom cone, a circulating slurry inlet elbow, Circulating pulp discharge pipe, ventilation pipe, air stone and water distribution pipe; the upper part of the upper column is connected with the flotation concentrate collection tank, the lower part of the upper column is connected with the water distribution pipe, and the water distribution pipe is provided with water distribution holes , the bottom of the upper column is connected to the top of the lower column; the upper part of the lower column is intersected with the circular slurry feeding elbow, and the lower part of the lower column is intersected with the air pipe, and the air pipe is connected to the port in the lower main body Connected with the air stone, the bottom of the lower column is connected with the wide mouth of the bottom cone; the narrow mouth of the bottom cone is connected with the circulating pulp discharge pipe; the circulating pulp discharge pipe and the circulating pulp inlet elbow pass through the circulating pulp pipe connected, and a circulating pump is provided on the circulating slurry pipe.
作为改进,所述布水管的端部为圆形,与上柱体的内壁相适应;所述布水孔位于布水管的端部上部。As an improvement, the end of the water distribution pipe is circular, which is compatible with the inner wall of the upper cylinder; the water distribution hole is located at the upper part of the end of the water distribution pipe.
作为改进,所述循环矿浆入料弯管的出料口垂直朝下。As an improvement, the outlet of the circulating slurry inlet elbow is vertically downward.
本发明的有益效果:1、在上柱体内形成的上升流与下柱体内形成的下降流形成柱体内的两向流体,通过气泡搭载煤粒完成了下降流内的煤粒进入上升流的输送,煤粒在上升流的作用下进入浮选精矿收集槽,突破了实验室单个气泡与煤粒群或单个煤粒与气泡群作用的局限,借以探究单元入料的脱附产率;2、通过布水管的充水,可以分离单元入料中难浮煤粒,解决了实验室难浮煤粒批量分离的难题。Beneficial effects of the present invention: 1. The upflow formed in the upper column and the downflow formed in the lower column form a two-way fluid in the column, and coal particles in the downflow are transported into the upflow through air bubbles carrying coal particles , the coal particles enter the flotation concentrate collection tank under the action of upflow, breaking through the limitation of the interaction between a single air bubble and coal particle group or a single coal particle and air bubble group in the laboratory, so as to explore the desorption yield of unit feed; 2 、Through the water filling of the water distribution pipe, it can separate the hard-to-float coal particles in the feed of the unit, which solves the problem of batch separation of hard-to-float coal particles in the laboratory.
附图说明Description of drawings
图1是本发明的结构示意图;Fig. 1 is a structural representation of the present invention;
图2是本发明布水管的结构示意图;Fig. 2 is the structural representation of water distribution pipe of the present invention;
图中:1-浮选精矿收集槽;2-上柱体;3-布水管;4-下柱体;5-气泡石;6-通气管;7-底锥;8-循环矿浆出料管;9-循环泵;10-循环矿浆管;11-循环矿浆入料弯管;12-布水孔。In the figure: 1-flotation concentrate collection tank; 2-upper cylinder; 3-water distribution pipe; 4-lower cylinder; Tube; 9-circulating pump; 10-circulating slurry pipe; 11-circulating slurry feeding elbow; 12-distribution water hole.
具体实施方式detailed description
下面结合附图对本发明的实施例作进一步描述:Embodiments of the present invention will be further described below in conjunction with accompanying drawings:
如图1-2所示,本发明的探究粗粒煤单元浮选脱附产率的试验装置包括浮选精矿收集槽1、上柱体2、下柱体4、底锥7、循环矿浆入料弯管11、循环矿浆出料管8、通气管6、气泡石5及布水管3;所述上柱体2的上部与浮选精矿收集槽1相连,上柱体2的下部与布水管3相贯,布水管3的端部为圆形,与上柱体2的内壁相适应,布水管3的端部上部设有布水孔12,上柱体2的底端与下柱体4的顶端相连;所述下柱体4的上部与循环矿浆入料弯管11相贯,循环矿浆入料弯管11的出料口垂直朝下,下柱体4的下部与通气管6相贯,通气管6的在下柱体4内端口与气泡石5相连,下柱体4的底端与底锥7的广口相连。所述底锥7的窄口与循环矿浆出料管10相连,循环矿浆出料管10与循环矿浆入料弯管11通过循环矿浆管10相连,循环矿浆管10上设有循环泵9。As shown in Figure 1-2, the test device of the present invention to explore the flotation desorption yield of coarse-grained coal unit includes a flotation concentrate collection tank 1, an upper column 2, a lower column 4, a bottom cone 7, and a circulating slurry Feed elbow 11, circulating pulp discharge pipe 8, ventilation pipe 6, air stone 5 and water distribution pipe 3; the upper part of the upper column 2 is connected with the flotation concentrate collection tank 1, and the lower part of the upper column 2 is connected with the The water distribution pipe 3 intersects, and the end of the water distribution pipe 3 is circular, which is compatible with the inner wall of the upper cylinder 2. The upper part of the end of the water distribution pipe 3 is provided with a water distribution hole 12, and the bottom of the upper cylinder 2 is connected to the lower column. The top of the body 4 is connected; the upper part of the lower column 4 is intersected with the circulating slurry inlet elbow 11, the outlet of the circulating slurry inlet elbow 11 is vertically downward, and the lower part of the lower column 4 is connected with the ventilation pipe 6 Intersecting, the vent pipe 6 is connected to the air stone 5 at the lower cylinder 4 inner port, and the bottom of the lower cylinder 4 is connected to the wide mouth of the bottom cone 7. The narrow mouth of the bottom cone 7 is connected with the circulating pulp discharge pipe 10, and the circulating pulp discharge pipe 10 is connected with the circulating pulp feeding elbow 11 through the circulating pulp pipe 10, and the circulating pulp pipe 10 is provided with a circulating pump 9.
本发明的工作过程:将一定量的粗粒煤调浆后通过上柱体2的顶端倒入,补加水使柱体内的液面和上柱体2的顶端齐平后开启循环泵9,在下柱体4和循环矿浆管10内形成循环流体,循环流体相对稳定后给通气管6充气,向下运动的煤粒与气泡石5发出向上运动的气泡碰撞、粘附。此时,部分易浮煤粒被气泡带至液体表面经刮板刮入浮选精矿收集槽1内;部分难浮煤粒在气泡上升的过程中与气泡发生脱附,脱附煤粒下沉到下柱体4内的循环流体中,然后继续被气泡带至上柱体2的上升流中,以此往复。浮选一定时间易浮煤粒浮选完毕后给布水管3充水,此时在上柱体2布水管3以上形成上升流,使上升流的流速大于粗粒煤粒群的最大沉降末速,此时部分脱附煤粒在上升水流的作用下进入浮选精矿收集槽1,分别收集布水管3充水前后浮选精矿收集槽1内的物料,则布水管3充水后进入浮选精矿收集槽内的物料即为难浮煤粒。浮选一定时间后关闭所有运动部件,拔下与循环矿浆出料管8相连循环矿浆管10的端口,收集浮选尾矿并将设备冲洗干净。The working process of the present invention: pour a certain amount of coarse-grained coal through the top of the upper column 2 after slurry adjustment, add water to make the liquid level in the column equal to the top of the upper column 2, and then turn on the circulation pump 9, A circulating fluid is formed in the cylinder 4 and the circulating slurry pipe 10. After the circulating fluid is relatively stable, the ventilation pipe 6 is inflated, and the downward moving coal particles collide with the upward moving air bubbles from the air stone 5 and adhere to them. At this time, part of the easy-to-float coal particles are brought to the surface of the liquid by the air bubbles and scraped into the flotation concentrate collection tank 1 by scrapers; Sink into the circulating fluid in the lower column 4, and then continue to be brought by the air bubbles to the upward flow of the upper column 2, and thus reciprocate. After flotation for a certain period of time, the water distribution pipe 3 is filled with water after the flotation of coal particles that are easy to float. At this time, an upward flow is formed above the upper column 2 and above the water distribution pipe 3, so that the flow rate of the upward flow is greater than the maximum settlement final velocity of the coarse-grained coal particle group. At this time, part of the desorbed coal particles enter the flotation concentrate collection tank 1 under the action of the rising water flow, respectively collect the materials in the flotation concentrate collection tank 1 before and after the water distribution pipe 3 is filled, and then enter the water distribution pipe 3 after filling with water. The material in the flotation concentrate collection tank is the hard-to-float coal particles. After flotation for a certain period of time, close all moving parts, unplug the port of the circulating pulp pipe 10 connected to the circulating pulp discharge pipe 8, collect the flotation tailings and rinse the equipment.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下还可以做出若干改进,这些改进也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, some improvements can be made without departing from the principle of the present invention, and these improvements should also be regarded as the present invention. scope of protection.
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| CN111468258A (en) * | 2020-04-17 | 2020-07-31 | 西安交通大学 | A simple device and method for physically separating coal slime in thermal coal plant |
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Application publication date: 20180105 |