CN111453707A - Phosphorus coal pelletizing equipment of yellow phosphorus production usefulness - Google Patents
Phosphorus coal pelletizing equipment of yellow phosphorus production usefulness Download PDFInfo
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- CN111453707A CN111453707A CN202010455768.3A CN202010455768A CN111453707A CN 111453707 A CN111453707 A CN 111453707A CN 202010455768 A CN202010455768 A CN 202010455768A CN 111453707 A CN111453707 A CN 111453707A
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- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 26
- OBSZRRSYVTXPNB-UHFFFAOYSA-N tetraphosphorus Chemical compound P12P3P1P32 OBSZRRSYVTXPNB-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 239000003245 coal Substances 0.000 title claims abstract description 23
- 229910052698 phosphorus Inorganic materials 0.000 title claims abstract description 22
- 239000011574 phosphorus Substances 0.000 title claims abstract description 22
- 238000005453 pelletization Methods 0.000 title claims description 15
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 238000001125 extrusion Methods 0.000 claims abstract description 53
- 238000007790 scraping Methods 0.000 claims abstract description 42
- 239000000463 material Substances 0.000 claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims description 24
- 238000001035 drying Methods 0.000 claims description 11
- 239000002274 desiccant Substances 0.000 claims description 7
- 238000007664 blowing Methods 0.000 claims description 2
- 230000001681 protective effect Effects 0.000 claims 6
- 238000000034 method Methods 0.000 abstract description 17
- 239000000126 substance Substances 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 26
- 238000009423 ventilation Methods 0.000 description 19
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 10
- 238000005245 sintering Methods 0.000 description 7
- 239000000843 powder Substances 0.000 description 6
- 239000002912 waste gas Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000002367 phosphate rock Substances 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 230000008092 positive effect Effects 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000000741 silica gel Substances 0.000 description 2
- 229910002027 silica gel Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 238000007792 addition Methods 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- -1 phosphide Chemical compound 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/01—Treating phosphate ores or other raw phosphate materials to obtain phosphorus or phosphorus compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B11/00—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
- B30B11/22—Extrusion presses; Dies therefor
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/02—Preparation of phosphorus
- C01B25/027—Preparation of phosphorus of yellow phosphorus
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
本发明提供了一种黄磷生产用的磷煤制球设备,属于化工技术领域。磷煤制球设备包括机座、入料斗、挤出桶、刮料转筒和减速电机,挤出桶的下端固定设置有一外护罩,刮料转筒与减速电机的输出轴相连,减速电机的壳体固定在外护罩上,刮料转筒呈小径端朝上的锥形,外护罩套设在刮料筒外,刮料筒的外壁面周向均匀设置有若干刮板,外护罩的上端伸入挤出桶内,外护罩上开设有若干个与各刮板一一对应的挤出孔,挤出孔连通挤出桶内腔和外护罩内腔;刮料转筒的上端固定设置有位于挤出桶内的挤出螺杆,入料斗固定在挤出桶上;相邻刮板之间形成一料槽,料槽的下端具有一固定在机座上的接料板。本发明具有能够避免出料过程中坯件相互粘结等优点。
The invention provides a phosphorus coal-making equipment for producing yellow phosphorus, which belongs to the technical field of chemical industry. The phosphorus coal ball making equipment includes a machine base, a feeding hopper, an extruding barrel, a scraping drum and a deceleration motor. An outer shield is fixed at the lower end of the extrusion drum. The shell is fixed on the outer shield, the scraping drum is in the shape of a cone with the small diameter end facing upward, the outer shield is sleeved outside the scraping drum, and the outer wall of the scraping drum is evenly provided with a number of scrapers in the circumferential direction. The upper end of the extruder extends into the extrusion barrel, and the outer shield is provided with a number of extrusion holes corresponding to each scraper one-to-one, and the extrusion holes communicate with the inner cavity of the extrusion barrel and the inner cavity of the outer shield; The upper end is fixed with an extrusion screw located in the extrusion barrel, and the feeding hopper is fixed on the extrusion barrel; a material trough is formed between adjacent scrapers, and the lower end of the material trough has a material receiving plate fixed on the machine base. The invention has the advantages that the blanks can be prevented from sticking to each other during the discharging process.
Description
技术领域technical field
本发明属于化工技术领域,涉及一种黄磷生产用的磷煤制球设备。The invention belongs to the technical field of chemical industry, and relates to a phosphorus coal-making equipment for producing yellow phosphorus.
背景技术Background technique
黄磷是一种重要的基础工业原料,主要用于制备磷酸、磷化物、磷酸盐等,广泛应用于肥料、饲料工业、食品加工业、建筑工业、医药、电子工业等诸多领域。Yellow phosphorus is an important basic industrial raw material, mainly used to prepare phosphoric acid, phosphide, phosphate, etc. It is widely used in fertilizer, feed industry, food processing industry, construction industry, medicine, electronics industry and many other fields.
目前工业上生产黄磷的主要方法为电炉法,即将磷矿石、硅石、焦炭按一定比例和粒度置于电炉中,在1400℃高温下发生还原反应,磷蒸汽与炉尘一起被冷却、洗涤后得到黄磷产品,将磷矿石、硅石、焦炭和水,按一定比例混合后制成球状坯件,然后投入电炉中烧结,为了让坯件成球,需要加入一定量的水,使各混合物粘结,但是在坯件在制球过程的出料环节和置于电炉内灼烧之前,都会在挤压和称重的作用下相互粘结,以至于烧结过程中不能够充分反应或者反应不均,本来制球的目的就在于烧结过程中腾出粒间间隙,以利于受热均匀和反应充分,但是,由于坯件相互挤压导致的相互粘结,使反应效率和热利用率均大幅下降。At present, the main method of industrial production of yellow phosphorus is the electric furnace method, that is, phosphate rock, silica, and coke are placed in an electric furnace in a certain proportion and particle size, and a reduction reaction occurs at a high temperature of 1400 ° C, and the phosphorus vapor is cooled and washed together with the furnace dust. After the yellow phosphorus product is obtained, phosphate rock, silica, coke and water are mixed in a certain proportion to make spherical blanks, which are then put into an electric furnace for sintering. The mixture is bonded, but the blanks will be bonded to each other under the action of extrusion and weighing during the discharge process of the ball making process and before being sintered in the electric furnace, so that the sintering process cannot fully react or the reaction does not occur. The original purpose of ball making is to free up the gap between particles during the sintering process to facilitate uniform heating and sufficient reaction. However, due to the mutual bonding caused by the mutual extrusion of the blanks, the reaction efficiency and heat utilization rate are greatly reduced.
发明内容SUMMARY OF THE INVENTION
本发明的目的是针对现有的技术存在的上述问题,提供一种黄磷生产用的磷煤制球设备,本发明所要解决的技术问题是如何使磷煤球外表平整,减少残渣的剥落。The purpose of the present invention is to aim at the above-mentioned problems existing in the prior art, and to provide a kind of phosphor coal pelletizing equipment for yellow phosphorus production.
本发明的目的可通过下列技术方案来实现:一种黄磷生产用的磷煤制球设备,其特征在于,磷煤制球设备包括机座、入料斗、挤出桶、刮料转筒和减速电机,所述挤出桶的下端固定设置有一外护罩,所述外护罩固定在机座上,所述刮料转筒与减速电机的输出轴相连,所述减速电机的壳体固定在外护罩上,所述刮料转筒呈小径端朝上的锥形,所述外护罩套设在刮料筒外,所述刮料筒的外壁面周向均匀设置有若干刮板,所述外护罩的上端伸入挤出桶内,所述外护罩上开设有若干个与各刮板一一对应的挤出孔,所述挤出孔连通挤出桶内腔和外护罩内腔;所述刮料转筒的上端固定设置有位于挤出桶内的挤出螺杆,所述入料斗固定在挤出桶上;相邻刮板之间形成一料槽,所述料槽的下端具有一固定在机座上的接料板。The purpose of the present invention can be achieved through the following technical solutions: a kind of phosphorus coal ball making equipment for yellow phosphorus production, it is characterized in that, the phosphorus coal ball making equipment comprises a machine base, a feeding hopper, an extrusion barrel, a scraping drum and a deceleration motor , the lower end of the extrusion barrel is fixedly provided with an outer shield, the outer shield is fixed on the machine base, the scraping drum is connected with the output shaft of the deceleration motor, and the shell of the deceleration motor is fixed on the outer shield On the cover, the scraping drum is in the shape of a cone with a small diameter end facing upward, the outer shield is sleeved outside the scraping drum, and a number of scrapers are evenly arranged on the outer wall of the scraping drum. The upper end of the outer shield extends into the extrusion barrel, the outer shield is provided with a number of extrusion holes corresponding to each scraper one-to-one, and the extrusion holes communicate with the inner cavity of the extrusion barrel and the outer shield. The upper end of the scraping drum is fixed with an extrusion screw located in the extrusion barrel, and the feeding hopper is fixed on the extrusion barrel; a trough is formed between adjacent scrapers, and the trough is The lower end has a material receiving plate fixed on the machine base.
在上述的一种黄磷生产用的磷煤制球设备中,所述刮板为内壁面具有凹口的平直板。In the above-mentioned phosphor coal pelletizing equipment for yellow phosphorus production, the scraper is a flat plate with a notch on the inner wall surface.
在上述的一种黄磷生产用的磷煤制球设备中,所述刮料转筒内具有一加热腔,所述减速电机的输出轴上固定设置有一回流管,所述回流管与刮料转筒固定相连,所述回流管上转动连接有一固定在机座上的中空转筒,所述中空转筒与回流管相连通,所述中空转筒连接一通气管,所述通气管与外护罩的顶部相通,所述刮料转筒的底部开设有与各料槽一一对应的溢流孔,所述料槽的上端与外护罩顶部相通,所述加热腔内设置有加热器,所述通气管上设置有将外护罩内的热气鼓入加热腔内的鼓风机。In the above-mentioned phosphor coal pelletizing equipment for yellow phosphorus production, a heating chamber is provided in the scraping drum, and a return pipe is fixed on the output shaft of the deceleration motor, and the return pipe is connected to the scraping drum. The cylinder is fixedly connected, the return pipe is rotatably connected with a hollow rotating cylinder fixed on the machine base, the hollow rotating cylinder is communicated with the return pipe, the hollow rotating cylinder is connected with a ventilation pipe, and the ventilation pipe is connected with the outer shield. The top of the scraping drum is connected with the top of the scraper drum, and the bottom of the scraping drum is provided with overflow holes corresponding to each material trough one-to-one. The upper end of the material trough is communicated with the top of the outer shield. The ventilation pipe is provided with a blower for blowing the hot air in the outer shield into the heating chamber.
在上述的一种黄磷生产用的磷煤制球设备中,所述鼓风机包括固定在挤出桶上端的阀体,所述阀体内具有一阀腔,所述外护罩的顶部转动连接有一转杆,所述转杆为中空管,所述转杆的顶部连接一叶轮,所述叶轮位于阀腔内,所述挤出螺杆固定在转杆上,所述阀腔连接通气管。In the above-mentioned phosphorus coal ball-making equipment for yellow phosphorus production, the blower includes a valve body fixed on the upper end of the extrusion barrel, the valve body has a valve cavity, and the top of the outer shield is rotatably connected with a rotary The rotating rod is a hollow tube, the top of the rotating rod is connected with an impeller, the impeller is located in the valve cavity, the extrusion screw is fixed on the rotating rod, and the valve cavity is connected with the ventilation pipe.
在上述的一种黄磷生产用的磷煤制球设备中,所述叶轮包括若干周向均匀分布在转杆上的叶片,所述叶片包括位于固定在转杆外壁面上的连接部和位于转杆顶部的负压部,所述连接部的外端与负压部的外端固定相连。In the above-mentioned phosphor coal-making equipment for producing yellow phosphorus, the impeller includes a plurality of blades evenly distributed on the rotating rod in the circumferential direction, and the blades include a connecting part located on the outer wall surface of the rotating rod and a connecting part located on the rotating rod. The negative pressure part at the top of the rod, the outer end of the connecting part is fixedly connected with the outer end of the negative pressure part.
在上述的一种黄磷生产用的磷煤制球设备中,所述回流管外套设有一滤网。In the above-mentioned phosphorus coal pelletizing equipment for yellow phosphorus production, a filter screen is provided on the outer casing of the return pipe.
在上述的一种黄磷生产用的磷煤制球设备中,所述外护罩将料槽的顶部封闭。In the above-mentioned phosphorus coal-making equipment for producing yellow phosphorus, the outer shield closes the top of the trough.
这里所指的封闭不是密封,而是配合刮板的凹口,使坯件不会与外护罩接触,同时增大对气流的导向,使气流大部分在料槽内由下至上流通。The sealing referred to here is not a seal, but a notch of a matching scraper, so that the blank will not be in contact with the outer shield, and at the same time, the direction of the airflow is increased, so that most of the airflow flows from bottom to top in the trough.
在上述的一种黄磷生产用的磷煤制球设备中,所述通气管上设置有一干燥箱,所述干燥箱内填充油干燥剂。In the above-mentioned phosphorus coal pelletizing equipment for yellow phosphorus production, a drying box is provided on the ventilation pipe, and the drying box is filled with oil desiccant.
通气管内的气流通过可更换的固体干燥剂实现脱水,避免进入加热腔内的气体湿度过高而影响对坯件的干燥效果,干燥剂为壳还原的硅胶干燥颗粒。The air flow in the ventilation pipe is dehydrated by a replaceable solid desiccant, which avoids the high humidity of the gas entering the heating chamber and affects the drying effect of the blank. The desiccant is silica gel dry particles with reduced shells.
一种黄磷生产用的磷煤外干法制球工艺,其特征在于,包括如下步骤:将磷矿石粉末、硅石粉末、焦炭粉末和水按比例混合,送入挤出桶内,在挤出螺杆的作用下将混合物挤入料槽内,减速电机驱动刮料转筒上的刮板将挤出孔出来的物料分断式刮入料槽内,鼓风机作用下,气流有料槽底部进入料槽内,并伴随加热,携带粉末的废气由转杆进入通气管,最后进入加热腔内,加热腔内气压升高,部分废气再次进入料槽内,通过废气的循环使由上至下滚动的磷煤坯件进行初步干燥,在接料板收集外表面被干燥和整平的坯件。A phosphate coal external dry pelletizing process for the production of yellow phosphorus, characterized in that it comprises the following steps: mixing phosphate rock powder, silica powder, coke powder and water in proportion, sending them into an extrusion barrel, and extruding Under the action of the screw, the mixture is extruded into the trough, and the gear motor drives the scraper on the scraping drum to scrape the material from the extrusion hole into the trough. Under the action of the blower, the air flow enters the trough from the bottom of the trough. , and accompanied by heating, the exhaust gas carrying powder enters the ventilation pipe from the rotating rod, and finally enters the heating chamber, the pressure in the heating chamber rises, and part of the exhaust gas enters the trough again. The blanks are preliminarily dried, and the dried and flattened outer surfaces of the blanks are collected at the splice plate.
物料经过挤出螺杆的挤压后,从挤出孔排出,在刮板的作用下被分切至各料槽内,成陀进入料槽,在料槽的导向作用下,坯件被压实、滚圆,由料槽底部掉入接料板上。After the material is extruded by the extrusion screw, it is discharged from the extrusion hole, and is cut into each trough under the action of the scraper. , rounded, and dropped into the receiving plate from the bottom of the trough.
由于磷煤混合物在刮板的作用下被分切,并使其依次进入各料槽内,使料槽内的各坯件不存在相互挤压,加热腔内的加热器对刮料转筒进行加热,坯件滚下的过程中,接触刮料转筒外壁的坯件外表面不断的切换,使坯件在成型的过程中外壁面被干燥至不易形变,即坯件整体具有一定的抗形变承重能力。Because the phosphorus-coal mixture is cut under the action of the scraper, and it enters into each trough in turn, so that the blanks in the trough are not squeezed against each other. During the process of heating and rolling down the blank, the outer surface of the blank contacting the outer wall of the scraping drum is constantly switched, so that the outer wall surface of the blank is dried to be difficult to deform during the forming process, that is, the blank as a whole has a certain anti-deformation load-bearing ability.
废气的循环采用鼓风机进行,鼓风机为转杆带动叶轮旋转,使转杆内的废气被吸至转杆顶部的阀体内,叶片的连接部位倾斜的片状结构,能够将阀腔内的废气挤入通气管内,各叶片的负压部形成一个位于转杆上方的涡轮,对转杆内的废气进行吸出,使其进入阀腔内,转杆的顶部与阀腔的顶部壁面之间具有间隙。The exhaust gas is circulated by a blower. The blower drives the impeller to rotate for the rotating rod, so that the exhaust gas in the rotating rod is sucked into the valve body at the top of the rotating rod. The inclined sheet structure of the connecting part of the blade can squeeze the exhaust gas in the valve cavity into the valve body. In the ventilation pipe, the negative pressure part of each blade forms a turbine located above the rotating rod, which sucks the exhaust gas in the rotating rod and makes it enter the valve cavity. There is a gap between the top of the rotating rod and the top wall of the valve cavity.
废气有两条路径,一条是料槽底部的新鲜空气进入料槽顶部,然后通过转杆进入通气管,最后由回流管和滤网进入加热腔内,另一条为加热腔内被加热、增压的废气,通过溢流孔进入料槽的底部,然后与第一条路径中的气体进行混合,如此循环,不仅对废气进行了过滤,使滤渣不再进入循环,而且使废气的余热进行了再利用,不会造成废气排放的问题。There are two paths for the exhaust gas, one is that the fresh air at the bottom of the trough enters the top of the trough, and then enters the ventilation pipe through the rotating rod, and finally enters the heating chamber through the return pipe and the filter screen, and the other is heated and pressurized in the heating chamber. The exhaust gas enters the bottom of the trough through the overflow hole, and then mixes with the gas in the first path. In this way, the exhaust gas is not only filtered, so that the filter residue does not enter the circulation, and the waste heat of the exhaust gas is recycled. Use, will not cause the problem of exhaust emissions.
本设备通过一个减速电机完成物料挤出、刮料、成球、废气循环,大大简化了结构,废气的循环不仅对残渣进行了收集、废气预热进行了再利用,主要还对坯件进行预干燥,使坯件掉入接料板上时不会发生较大形变,在进行电炉烧结过程中,一定量的堆积也不会造成相互粘结,对烧结反应的均匀性、高效性都有极大的积极效果。This equipment completes material extrusion, scraping, balling, and waste gas circulation through a geared motor, which greatly simplifies the structure. The waste gas circulation not only collects the residue, preheats the waste gas for reuse, but also preheats the blank. Dry, so that the blank will not be greatly deformed when it falls into the receiving plate. During the sintering process of the electric furnace, a certain amount of accumulation will not cause mutual bonding, which is very good for the uniformity and high efficiency of the sintering reaction. big positive effect.
减速电机的转速与制球效率对应,废气循环效率也能够与之配合,可以确保坯件粒径均匀,坯件干燥程度均匀。The speed of the geared motor corresponds to the ball making efficiency, and the exhaust gas circulation efficiency can also be matched with it, which can ensure that the particle size of the blank is uniform and the drying degree of the blank is uniform.
附图说明Description of drawings
图1是本制球设备的整体结构示意图。Figure 1 is a schematic diagram of the overall structure of the ball making equipment.
图2是刮料转筒的俯视图。Figure 2 is a top view of the scraping drum.
图3是图1中局部A的放大图。FIG. 3 is an enlarged view of part A in FIG. 1 .
图4是鼓风机的结构示意图。Figure 4 is a schematic diagram of the structure of the blower.
图5是图1中局部B的放大图。FIG. 5 is an enlarged view of part B in FIG. 1 .
图中,1、机座,11、挤出桶;12、外护罩;13、减速电机;14、入料斗;2、刮料转筒;21、刮板;22、挤出孔;23、料槽;24、接料板;25、加热腔;31、回流管;32、中空转筒;33、通气管;34、溢流孔;41、阀体;42、阀腔;43、转杆;44、叶轮;45、连接部;46、负压部;5、滤网;6、加热器;7、挤出螺杆;8、干燥箱。In the figure, 1, machine base, 11, extrusion barrel; 12, outer shield; 13, geared motor; 14, feeding hopper; 2, scraping drum; 21, scraper; 22, extrusion hole; 23, Material trough; 24, receiving plate; 25, heating chamber; 31, return pipe; 32, hollow drum; 33, ventilation pipe; 34, overflow hole; 41, valve body; 42, valve cavity; 43, rotating
具体实施方式Detailed ways
以下是本发明的具体实施例并结合附图,对本发明的技术方案作进一步的描述,但本发明并不限于这些实施例。The following are specific embodiments of the present invention and the accompanying drawings to further describe the technical solutions of the present invention, but the present invention is not limited to these embodiments.
如图1、图2、图3、图4和图5所示,磷煤制球设备包括机座1、入料斗14、挤出桶11、刮料转筒2和减速电机13,挤出桶11的下端固定设置有一外护罩12,外护罩12固定在机座1上,刮料转筒2与减速电机13的输出轴相连,减速电机13的壳体固定在外护罩12上,刮料转筒2呈小径端朝上的锥形,外护罩12套设在刮料筒外,刮料筒的外壁面周向均匀设置有若干刮板21,外护罩12的上端伸入挤出桶11内,外护罩12上开设有若干个与各刮板21一一对应的挤出孔22,挤出孔22连通挤出桶11内腔和外护罩12内腔;刮料转筒2的上端固定设置有位于挤出桶11内的挤出螺杆7,入料斗14固定在挤出桶11上;相邻刮板21之间形成一料槽23,料槽23的下端具有一固定在机座1上的接料板24,刮板21为内壁面具有凹口的平直板。As shown in Figure 1, Figure 2, Figure 3, Figure 4 and Figure 5, the phosphorus coal pelletizing equipment includes a machine base 1, a
刮料转筒2内具有一加热腔25,减速电机13的输出轴上固定设置有一回流管31,回流管31与刮料转筒2固定相连,回流管31上转动连接有一固定在机座1上的中空转筒32,中空转筒32与回流管31相连通,中空转筒32连接一通气管33,通气管33与外护罩12的顶部相通,刮料转筒2的底部开设有与各料槽23一一对应的溢流孔34,料槽23的上端与外护罩12顶部相通,加热腔25内设置有加热器6,通气管33上设置有将外护罩12内的热气鼓入加热腔25内的鼓风机。There is a
鼓风机包括固定在挤出桶11上端的阀体41,阀体41内具有一阀腔42,外护罩12的顶部转动连接有一转杆43,转杆43为中空管,转杆43的顶部连接一叶轮44,叶轮44位于阀腔42内,挤出螺杆7固定在转杆43上,阀腔42连接通气管33。The blower includes a
叶轮44包括若干周向均匀分布在转杆43上的叶片,叶片包括位于固定在转杆43外壁面上的连接部45和位于转杆43顶部的负压部46,连接部45的外端与负压部46的外端固定相连。The
回流管31外套设有一滤网5,外护罩12将料槽23的顶部封闭,这里所指的封闭不是密封,而是配合刮板21的凹口,使坯件不会与外护罩12接触,同时增大对气流的导向,使气流大部分在料槽23内由下至上流通。A filter screen 5 is provided on the outer casing of the
通气管33上设置有一干燥箱8,干燥箱8内填充油干燥剂,通气管33内的气流通过可更换的固体干燥剂实现脱水,避免进入加热腔25内的气体湿度过高而影响对坯件的干燥效果,干燥剂为壳还原的硅胶干燥颗粒。A drying box 8 is arranged on the
黄磷生产用的磷煤外干法制球工艺包括如下步骤:将磷矿石粉末、硅石粉末、焦炭粉末和水按比例混合,送入挤出桶11内,在挤出螺杆7的作用下将混合物挤入料槽23内,减速电机13驱动刮料转筒2上的刮板21将挤出孔22出来的物料分断式刮入料槽23内,鼓风机作用下,气流有料槽23底部进入料槽23内,并伴随加热,携带粉末的废气由转杆43进入通气管33,最后进入加热腔25内,加热腔25内气压升高,部分废气再次进入料槽23内,通过废气的循环使由上至下滚动的磷煤坯件进行初步干燥,在接料板24收集外表面被干燥和整平的坯件。Phosphorus coal external dry pelletizing process for yellow phosphorus production includes the following steps: mixing phosphate rock powder, silica powder, coke powder and water in proportion, sending it into the
物料经过挤出螺杆7的挤压后,从挤出孔22排出,在刮板21的作用下被分切至各料槽23内,成陀进入料槽23,在料槽23的导向作用下,坯件被压实、滚圆,由料槽23底部掉入接料板24上。After the material is extruded by the
由于磷煤混合物在刮板21的作用下被分切,并使其依次进入各料槽23内,使料槽23内的各坯件不存在相互挤压,加热腔25内的加热器6对刮料转筒2进行加热,坯件滚下的过程中,接触刮料转筒2外壁的坯件外表面不断的切换,使坯件在成型的过程中外壁面被干燥至不易形变,即坯件整体具有一定的抗形变承重能力。Because the phosphorus-coal mixture is cut under the action of the
废气的循环采用鼓风机进行,鼓风机为转杆43带动叶轮44旋转,使转杆43内的废气被吸至转杆43顶部的阀体41内,叶片的连接部45位倾斜的片状结构,能够将阀腔42内的废气挤入通气管33内,各叶片的负压部46形成一个位于转杆43上方的涡轮,对转杆43内的废气进行吸出,使其进入阀腔42内,转杆43的顶部与阀腔42的顶部壁面之间具有间隙。The circulation of the exhaust gas is carried out by a blower. The blower drives the
废气有两条路径,一条是料槽23底部的新鲜空气进入料槽23顶部,然后通过转杆43进入通气管33,最后由回流管31和滤网5进入加热腔25内,另一条为加热腔25内被加热、增压的废气,通过溢流孔34进入料槽23的底部,然后与第一条路径中的气体进行混合,如此循环,不仅对废气进行了过滤,使滤渣不再进入循环,而且使废气的余热进行了再利用,不会造成废气排放的问题。There are two paths for the exhaust gas. One is that the fresh air at the bottom of the
本设备通过一个减速电机13完成物料挤出、刮料、成球、废气循环,大大简化了结构,废气的循环不仅对残渣进行了收集、废气预热进行了再利用,主要还对坯件进行预干燥,使坯件掉入接料板24上时不会发生较大形变,在进行电炉烧结过程中,一定量的堆积也不会造成相互粘结,对烧结反应的均匀性、高效性都有极大的积极效果。This equipment completes material extrusion, scraping, balling, and waste gas circulation through a geared
本文中所描述的具体实施例仅仅是对本发明精神作举例说明。本发明所属技术领域的技术人员可以对所描述的具体实施例做各种各样的修改或补充或采用类似的方式替代,但并不会偏离本发明的精神或者超越所附权利要求书所定义的范围。The specific embodiments described herein are merely illustrative of the spirit of the invention. Those skilled in the art to which the present invention pertains can make various modifications or additions to the described specific embodiments or substitute in similar manners, but will not deviate from the spirit of the present invention or go beyond the definitions of the appended claims range.
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