CN104971813B - A kind of magnesium hydroxide grinds grading plant - Google Patents
A kind of magnesium hydroxide grinds grading plant Download PDFInfo
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- CN104971813B CN104971813B CN201510348637.4A CN201510348637A CN104971813B CN 104971813 B CN104971813 B CN 104971813B CN 201510348637 A CN201510348637 A CN 201510348637A CN 104971813 B CN104971813 B CN 104971813B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/06—Jet mills
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
- B02C23/20—Adding fluid, other than for crushing or disintegrating by fluid energy after crushing or disintegrating
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- Food Science & Technology (AREA)
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- Disintegrating Or Milling (AREA)
Abstract
本发明公开了一种氢氧化镁研磨分级装置,包括设置有第一自动卸料阀的下料仓,下料仓连接有助排管,助排管与进口连接有第一截止阀和空气压缩机的压缩空气储罐连接,空气储罐还依次与第三截止阀、电磁脉冲阀和气锤连接,第一自动卸料阀的出口连接有进气口与空气储罐连接的气流磨,气流磨的出料口有分级器并与分离器连接,分离器还与收尘器连接,收尘器还连接有风机。本发明采用压缩空气冲击防止氢氧化镁粉末下料时堆积;采用气锤、电磁脉冲阀定时敲击下料仓,防止氢氧化镁粉体堆积;采用靶式气流磨可将氢氧化镁粉末研磨至3000~10000目;采用分级器、旋风分离器、布袋除尘器、离心风机,通过改变分级器的转速,得到所需目数的粉体。
The invention discloses a magnesium hydroxide grinding and grading device, which comprises a lower hopper provided with a first automatic unloading valve, the lower hopper is connected with an auxiliary discharge pipe, and the auxiliary discharge pipe is connected with the inlet with a first cut-off valve and an air compressor. The air storage tank is connected to the compressed air storage tank of the machine, and the air storage tank is also connected to the third cut-off valve, electromagnetic pulse valve and air hammer in turn. There is a classifier at the discharge port and is connected with the separator, and the separator is also connected with the dust collector, and the dust collector is also connected with a fan. The invention adopts compressed air impact to prevent the accumulation of magnesium hydroxide powder during blanking; adopts air hammer and electromagnetic pulse valve to knock the feeding bin regularly to prevent the accumulation of magnesium hydroxide powder; adopts target type airflow mill to grind magnesium hydroxide powder To 3000-10000 mesh; using classifier, cyclone separator, bag filter, centrifugal fan, by changing the speed of the classifier, the powder of the required mesh can be obtained.
Description
技术领域technical field
本发明涉及一种氢氧化镁研磨分级装置,属于化工生产设备技术领域。The invention relates to a magnesium hydroxide grinding and classifying device, which belongs to the technical field of chemical production equipment.
背景技术Background technique
氢氧化镁粉体被粉碎至100目时,由于分子间张力,氢氧化镁易在下料仓中出现堆积架桥现象,从而导致下料仓下料口处下料不均匀甚至无法下料,另外,将氢氧化镁由100目粉碎至3000~10000目,靠普通的研磨方式无法实现,同时粉碎过程为物理过程存在不均一性。When the magnesium hydroxide powder is crushed to 100 mesh, due to the intermolecular tension, the magnesium hydroxide tends to accumulate and bridge in the feeding bin, resulting in uneven or even impossible feeding at the feeding port of the lower feeding bin. , to crush magnesium hydroxide from 100 mesh to 3000-10000 mesh, which cannot be achieved by ordinary grinding methods, and at the same time, the crushing process is a physical process with inhomogeneity.
发明内容Contents of the invention
本发明的目的是,提供一种氢氧化镁研磨分级装置,可使得100目数的氢氧化镁粉体均匀下料,并通过气流粉碎至3000~10000目,通过改变分级器电机转速,得到所需目数的粉体,并达到无尘环保要求。The purpose of the present invention is to provide a magnesium hydroxide grinding and classifying device, which can make the magnesium hydroxide powder with a number of 100 mesh be uniformly fed, and be crushed to 3000-10000 mesh by airflow, and the obtained grade can be obtained by changing the motor speed of the classifier. It can meet the requirements of dust-free and environmental protection.
为达到上述目的,本发明所采用的具体技术方案是:In order to achieve the above object, the concrete technical scheme adopted in the present invention is:
一种氢氧化镁研磨分级装置,包括出口设置有第一自动卸料阀的漏斗形下料仓,所述下料仓顶部的排气口连接有向内延伸至所述第一自动卸料阀的助排管,所述助排管的进口设置有第二截止阀并通过管路与进口依次连接有第一截止阀和空气压缩机的压缩空气储罐的出口相连接,所述压缩空气储罐还通过管路依次与第三截止阀、电磁脉冲阀以及设置在所述下料仓的锥形端外侧的气锤相连接,所述第一自动卸料阀的出口连接有进气口通过设置有第四截止阀的管路与所述压缩空气储罐的出口连接的气流磨,所述气流磨的出料口设置有分级器并通过管路与出口设置有第一料仓的分离器的进口相连接,所述第一料仓的出口设置有第二自动卸料阀,所述分离器的进口还通过管道与出口设置有第二料仓的收尘器的进口连接,所述收尘器的进口还连接有风机,所述第二料仓的出口设置有第三自动卸料阀。A magnesium hydroxide grinding and grading device, comprising a funnel-shaped lower hopper with a first automatic discharge valve at the outlet, the exhaust port on the top of the lower hopper is connected with a valve extending inward to the first automatic discharge valve The auxiliary drainage pipe, the inlet of the auxiliary drainage pipe is provided with a second cut-off valve and is connected to the outlet of the compressed air storage tank connected with the first cut-off valve and the air compressor in turn through a pipeline, and the compressed air storage tank The tank is also connected with the third cut-off valve, electromagnetic pulse valve and the air hammer arranged outside the tapered end of the lower silo through pipelines, and the outlet of the first automatic unloading valve is connected with an air inlet through the A jet mill with a pipeline connected to the outlet of the compressed air storage tank provided with a fourth cut-off valve, the outlet of the jet mill is provided with a classifier and a separator of the first bin is provided through the pipeline and the outlet The inlet of the first silo is connected, the outlet of the first silo is provided with a second automatic discharge valve, the inlet of the separator is also connected to the inlet of the dust collector with the outlet of the second silo through a pipeline, and the collector The inlet of the duster is also connected with a fan, and the outlet of the second silo is provided with a third automatic discharge valve.
进一步,所述气流磨可以为扁平式、循环管式、对喷式,但优选为靶式气流磨。Further, the jet mill can be of flat type, circulating tube type, or counter-jet type, but is preferably a target jet mill.
进一步,所述分离器优选为螺旋分离器。Further, the separator is preferably a spiral separator.
进一步,所述收尘器优选为布袋式收尘器,当然也可以是电收尘器等。Further, the dust collector is preferably a bag-type dust collector, of course, it can also be an electric dust collector or the like.
进一步,所述风机优选为离心风机,当然也可以是轴流风机或回转风机。Further, the fan is preferably a centrifugal fan, of course, it can also be an axial fan or a rotary fan.
压缩空气通过管路流向所述助排管并进入所述下料仓的排料口,通过气流的冲击,可以避免氢氧化镁堆积,防止出现架桥现象。Compressed air flows to the auxiliary discharge pipe through the pipeline and enters the discharge port of the lower hopper. The impact of the air flow can avoid the accumulation of magnesium hydroxide and prevent bridging.
通过控制所述电磁脉冲阀,从而控制压缩空气使所述气锤定时敲击所述下料仓,可防止氢氧化镁粉体堆积,而造成无法下料现象出现。By controlling the electromagnetic pulse valve, the compressed air is controlled so that the air hammer regularly hits the feeding bin, which can prevent the accumulation of magnesium hydroxide powder and cause the phenomenon that the feeding cannot be performed.
通过气流磨,可使100目的氢氧化镁粉体粉碎至3000~10000目,达到生产要求。Through the jet mill, the 100-mesh magnesium hydroxide powder can be crushed to 3000-10000 mesh, which meets the production requirements.
通过改变所述分级器的转速,可以得到不同目数的氢氧化镁粉体。By changing the rotating speed of the classifier, magnesium hydroxide powders with different meshes can be obtained.
所述第一至三自动卸料阀可有电脑控制可进行自动放料,节省生产成本,通过所述布袋收尘器可以收集溢出的氢氧化镁粉末,达到环保除尘的要求The first to third automatic unloading valves can be controlled by a computer for automatic discharge, which saves production costs, and the overflowing magnesium hydroxide powder can be collected through the bag filter to meet the requirements of environmental protection and dust removal
本发明的优点和有益效果是:Advantage and beneficial effect of the present invention are:
采用压缩空气冲击防止氢氧化镁粉末下料时堆积,保证下料顺畅;采用气锤、电磁脉冲阀定时敲击下料仓,防止氢氧化镁粉体堆积而造成无法下料的现象;采用靶式气流磨可将100目的氢氧化镁粉末研磨至3000~10000目;采用分级器、旋风分离器、布袋除尘器、离心风机,通过改变分级器的转速,得到所需目数的粉体,并达到无尘环保要求。Compressed air impact is used to prevent the accumulation of magnesium hydroxide powder during blanking to ensure smooth blanking; air hammers and electromagnetic pulse valves are used to regularly knock on the unloading bin to prevent the accumulation of magnesium hydroxide powder from causing unloading; the use of targets Type jet mill can grind 100-mesh magnesium hydroxide powder to 3000-10000 mesh; use classifier, cyclone separator, bag filter, centrifugal fan, and change the speed of classifier to get the powder of required mesh, and Meet dust-free environmental protection requirements.
附图说明Description of drawings
图1是本发明实施例一结构示意图;Fig. 1 is a schematic structural view of Embodiment 1 of the present invention;
图中:1 为下料仓、2 为排气口、3 为助排管、4 为气流磨、5 为分级器、6 为分离器、9为收尘器、10 为风机、12 为气锤、13 为电磁脉冲阀、15 为第三截止阀、16 为压缩空气储罐、17 为空气压缩机、19 为第二截止阀、20 为第一截止阀、21 为第四截止阀、71 为第一料仓、72 为第二料仓、81 为第一自动卸料阀、82 为第二自动卸料阀、83 为第三自动卸料阀。In the figure: 1 is the lower silo, 2 is the exhaust port, 3 is the exhaust pipe, 4 is the jet mill, 5 is the classifier, 6 is the separator, 9 is the dust collector, 10 is the fan, 12 is the air hammer , 13 is the electromagnetic pulse valve, 15 is the third stop valve, 16 is the compressed air storage tank, 17 is the air compressor, 19 is the second stop valve, 20 is the first stop valve, 21 is the fourth stop valve, 71 is the The first silo, 72 is the second silo, 81 is the first automatic discharge valve, 82 is the second automatic discharge valve, and 83 is the third automatic discharge valve.
具体实施方式detailed description
为使本发明实施例的目的和技术方案更加清楚,下面将结合本发明实施例的附图,对本发明实施例的技术方案进行清楚、完整地描述。In order to make the purpose and technical solutions of the embodiments of the present invention more clear, the technical solutions of the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings of the embodiments of the present invention.
如图1所示,一种氢氧化镁研磨分级装置,包括出口设置有第一自动卸料阀81的漏斗形下料仓1,其特征在于:所述下料仓1顶部的排气口2连接有向内延伸至所述第一自动卸料阀81的助排管3,所述助排管3的进口设置有第二截止阀19并通过管路与进口依次连接有第一截止阀20和空气压缩机17的压缩空气储罐16的出口相连接,所述压缩空气储罐16还通过管路依次与第三截止阀15、电磁脉冲阀13以及设置在所述下料仓1的锥形端外侧的气锤12相连接,所述第一自动卸料阀81的出口连接有进气口通过设置有第四截止阀21的管路与所述压缩空气储罐16的出口连接的气流磨4,所述气流磨4的出料口设置有分级器5并通过管路与出口设置有第一料仓71的分离器6的进口相连接,所述第一料仓71的出口设置有第二自动卸料阀82,所述分离器6的进口还通过管道与出口设置有第二料仓72的收尘器9的进口连接,所述收尘器9的进口还连接有风机10,所述第二料仓72的出口设置有第三自动卸料阀83。As shown in Figure 1, a magnesium hydroxide grinding and classifying device includes a funnel-shaped lower silo 1 with a first automatic discharge valve 81 at the outlet, and is characterized in that: the exhaust port 2 at the top of the lower hopper 1 A discharge aid pipe 3 extending inward to the first automatic unloading valve 81 is connected, and the inlet of the drain aid pipe 3 is provided with a second shut-off valve 19 and is sequentially connected with the first shut-off valve 20 through a pipeline. It is connected with the outlet of the compressed air storage tank 16 of the air compressor 17, and the compressed air storage tank 16 is also connected with the third shut-off valve 15, the electromagnetic pulse valve 13 and the cone arranged in the lower silo 1 through pipelines. The air hammer 12 outside the shaped end is connected, and the outlet of the first automatic unloading valve 81 is connected with the airflow that the air inlet is connected to the outlet of the compressed air storage tank 16 through the pipeline provided with the fourth shut-off valve 21 Mill 4, the outlet of the jet mill 4 is provided with a classifier 5 and is connected to the inlet of the separator 6 provided with the outlet of the first feed bin 71 through a pipeline, and the outlet of the first feed bin 71 is provided with The second automatic unloading valve 82, the inlet of the separator 6 is also connected to the inlet of the dust collector 9 provided with the second feed bin 72 through a pipeline, and the inlet of the dust collector 9 is also connected to a fan 10, The outlet of the second storage bin 72 is provided with a third automatic unloading valve 83 .
所述气流磨4为靶式气流磨。The jet mill 4 is a target jet mill.
所述分离器6为螺旋分离器。The separator 6 is a spiral separator.
所述收尘器9为布袋式收尘器。The dust collector 9 is a bag type dust collector.
所述风机10为离心风机。The fan 10 is a centrifugal fan.
除上述实施例外,本发明还可以有其他实施方式,凡采用等同替换或等效变换形成的技术方案,均落在发明要求的保护范围内。In addition to the above-mentioned embodiments, the present invention can also have other implementation modes, and all technical solutions formed by equivalent replacement or equivalent transformation all fall within the scope of protection required by the invention.
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| CN201510348637.4A CN104971813B (en) | 2015-06-23 | 2015-06-23 | A kind of magnesium hydroxide grinds grading plant |
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| CN201510348637.4A CN104971813B (en) | 2015-06-23 | 2015-06-23 | A kind of magnesium hydroxide grinds grading plant |
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| CN104971813A CN104971813A (en) | 2015-10-14 |
| CN104971813B true CN104971813B (en) | 2017-10-03 |
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| CN107663799A (en) * | 2017-09-28 | 2018-02-06 | 枣庄市恒宇纸业有限公司 | A kind of parchment reclaims decomposition apparatus |
| CN113843027A (en) * | 2021-08-11 | 2021-12-28 | 当升科技(常州)新材料有限公司 | Airflow mill for improving stability of high-nickel single crystal crushing strength |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2297247Y (en) * | 1997-06-25 | 1998-11-18 | 上海化工机械三厂 | fluidized bed airflow pulverizer |
| CN201988430U (en) * | 2011-01-12 | 2011-09-28 | 成都坤森微纳科技有限公司 | Fluidized bed jet mill grader |
| CN103586476A (en) * | 2013-10-18 | 2014-02-19 | 江西稀有稀土金属钨业集团有限公司 | Combined type hydrogen storage alloy preparation system |
| CN203750644U (en) * | 2014-03-21 | 2014-08-06 | 山东省农业机械科学研究院 | Superfine air flow grinding system |
| CN204338282U (en) * | 2014-12-15 | 2015-05-20 | 巩义市强宏镁业科技有限责任公司 | Pulverize high purity magnesium hydrate rotating nozzle type airflow comminution system |
| CN204866102U (en) * | 2015-06-23 | 2015-12-16 | 镇江市高等专科学校 | Magnesium hydroxide grinds grading plant |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3037871B2 (en) * | 1994-11-30 | 2000-05-08 | 八光技研株式会社 | Grinding method and grinding equipment |
| US7159807B2 (en) * | 2004-09-29 | 2007-01-09 | Montag Roger A | Granular material grinder and method of use |
-
2015
- 2015-06-23 CN CN201510348637.4A patent/CN104971813B/en not_active Withdrawn - After Issue
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2297247Y (en) * | 1997-06-25 | 1998-11-18 | 上海化工机械三厂 | fluidized bed airflow pulverizer |
| CN201988430U (en) * | 2011-01-12 | 2011-09-28 | 成都坤森微纳科技有限公司 | Fluidized bed jet mill grader |
| CN103586476A (en) * | 2013-10-18 | 2014-02-19 | 江西稀有稀土金属钨业集团有限公司 | Combined type hydrogen storage alloy preparation system |
| CN203750644U (en) * | 2014-03-21 | 2014-08-06 | 山东省农业机械科学研究院 | Superfine air flow grinding system |
| CN204338282U (en) * | 2014-12-15 | 2015-05-20 | 巩义市强宏镁业科技有限责任公司 | Pulverize high purity magnesium hydrate rotating nozzle type airflow comminution system |
| CN204866102U (en) * | 2015-06-23 | 2015-12-16 | 镇江市高等专科学校 | Magnesium hydroxide grinds grading plant |
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