CN210065189U - A system for forming pulverized coal and quicklime powder - Google Patents

A system for forming pulverized coal and quicklime powder Download PDF

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CN210065189U
CN210065189U CN201920315422.6U CN201920315422U CN210065189U CN 210065189 U CN210065189 U CN 210065189U CN 201920315422 U CN201920315422 U CN 201920315422U CN 210065189 U CN210065189 U CN 210065189U
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powder
inlet
coal
quicklime powder
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孙富强
侯红强
张扬
张栋辉
徐伟
耿海涛
刘骏
赵克岩
杜志武
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Beijing Daosike Energy Equipment Co ltd
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Beijing Shuangzero Mining Equipment Technology Co Ltd
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Abstract

本实用新型提供了一种用于煤粉和生石灰粉成型的系统,包括生石灰粉仓、煤粉仓、第一搅拌装置、第二搅拌装置和压球成型装置,所述生石灰粉仓具有生石灰粉入口和生石灰粉出口,所述煤粉仓具有煤粉入口和煤粉出口,所述第一搅拌装置具有混料入口和混料出口,所述第二搅拌装置具有第一入料口、第二入料口第三入料口和第一出料口,所述生石灰粉出口和混料入口相连接,所述混料出口和第一入料口连接,所述煤粉出口和所述第二入料口连接,所述第一出料口和所述压球成型装置的进料口连接,本实用新型所述的煤粉和生石灰粉成型的系统所需要的原料成本低,不需要特别加工,减少了加工工序,减少了污染物的排放。

Figure 201920315422

The utility model provides a system for forming coal powder and quicklime powder. an inlet and an outlet for powdered lime, the pulverized coal silo has a pulverized coal inlet and an outlet for pulverized coal, the first stirring device has a mixing inlet and a mixing outlet, and the second stirring device has a first inlet, a second The third feeding port and the first feeding port of the feeding port, the quicklime powder outlet is connected with the mixing inlet, the mixing outlet is connected with the first feeding port, the coal powder outlet is connected with the second feeding port The feeding port is connected, and the first discharging port is connected with the feeding port of the pressing ball forming device. The cost of raw materials required by the pulverized coal and quicklime powder forming system of the utility model is low, and no special processing is required. , reducing the processing process and reducing the emission of pollutants.

Figure 201920315422

Description

一种用于煤粉和生石灰粉成型的系统A system for forming pulverized coal and quicklime powder

技术领域technical field

本实用新型涉及电石生产设备技术领域,特别涉及一种用于煤粉和生石灰粉成型的系统。The utility model relates to the technical field of calcium carbide production equipment, in particular to a system for forming coal powder and quicklime powder.

背景技术Background technique

目前电石企业使用兰炭作为电石原料,经过转运、干燥、筛分等工序,产生10%~30%的粉末不能加入电石炉,只能当做普通燃料烧掉。另外兰炭生产过程中,兰炭的显热无法充分回收利用,造成巨大浪费。同时,在煤的生产和生石灰的生产过程中,大量粉状煤和生石灰不能利用,造成大量能源浪费和环境污染。At present, calcium carbide enterprises use blue carbon as the raw material of calcium carbide. After transporting, drying, screening and other processes, 10% to 30% of the powder produced cannot be added to the calcium carbide furnace, and can only be burned as ordinary fuel. In addition, in the production process of blue carbon, the sensible heat of blue carbon cannot be fully recycled, resulting in huge waste. At the same time, in the process of coal production and quicklime production, a large amount of pulverized coal and quicklime cannot be utilized, resulting in a large amount of energy waste and environmental pollution.

实用新型内容Utility model content

有鉴于此,本实用新型旨在提出一种用于煤粉和生石灰粉成型的系统,以解决在煤的生产和生石灰的生产过程中,大量粉状煤和生石灰不能利用,造成大量能源浪费和环境污染的技术问题。In view of this, the utility model aims to propose a system for forming coal powder and quicklime powder, so as to solve the problem that in the production process of coal and quicklime, a large amount of pulverized coal and quicklime cannot be utilized, resulting in a large amount of energy waste and Technical problems of environmental pollution.

为达到上述目的,本实用新型的技术方案是这样实现的:In order to achieve the above object, the technical scheme of the present utility model is achieved in this way:

一种用于煤粉和生石灰粉成型的系统,包括生石灰粉仓、煤粉仓、第一搅拌装置、第二搅拌装置和压球成型装置,所述生石灰粉仓具有生石灰粉入口和生石灰粉出口,所述煤粉仓具有煤粉入口和煤粉出口,所述第一搅拌装置具有混料入口和混料出口,所述第二搅拌装置具有第一入料口、第二入料口第三入料口和第一出料口,所述生石灰粉出口和混料入口相连接,所述混料出口和第一入料口连接,所述煤粉出口和所述第二入料口连接,所述第一出料口和所述压球成型装置的进料口连接。A system for forming coal powder and quicklime powder, comprising a quicklime powder bin, a coal powder bin, a first stirring device, a second stirring device and a briquetting device, wherein the quicklime powder bin has a quicklime powder inlet and a quicklime powder outlet , the pulverized coal silo has a pulverized coal inlet and a pulverized coal outlet, the first stirring device has a mixing inlet and a mixing outlet, the second stirring device has a first feeding port, a second feeding port, a third feeding port The feed inlet and the first discharge port, the quicklime powder outlet is connected with the mixing inlet, the mixing outlet is connected with the first feeding port, the coal powder outlet is connected with the second feeding port, The first discharge port is connected with the feed port of the ball pressure forming device.

进一步的,还包括储料罐,所述储料罐具有入罐口和出罐口,所述出罐口和所述混料入口连接。Further, it also includes a material storage tank, the material storage tank has a tank inlet and a tank outlet, and the tank outlet is connected to the mixing inlet.

进一步的,所述储料罐内装载有第一粘结剂,所述第一粘结剂用于在生石灰粉的表面形成一层疏水性的钝化薄膜。Further, the storage tank is loaded with a first binder, and the first binder is used to form a hydrophobic passivation film on the surface of the quicklime powder.

进一步的,所述储料罐的出罐口处设置有泵体。Further, a pump body is provided at the tank outlet of the storage tank.

进一步的,还包括储料仓,所述储料仓具有入仓口和出仓口,所述出仓口和所述第三入料口连接。Further, it also includes a storage bin, the storage bin has a bin inlet and a bin outlet, and the bin outlet is connected to the third inlet.

进一步的,所述生石灰粉仓的生石灰粉出口、煤粉仓的煤粉出口和储料仓的出仓口均设置有振动给料装置。Further, the quicklime powder outlet of the quicklime powder bin, the coal powder outlet of the coal powder bin and the bin outlet of the storage bin are all provided with a vibrating feeding device.

进一步的,所述储料仓装载有第二粘结剂,所述第二粘结剂用于将煤粉和生石灰粉进行粘结。Further, the storage bin is loaded with a second binder, and the second binder is used for bonding the coal powder and the quicklime powder.

进一步的,所述第一粘结剂为煤焦油、蒽油或重质油,所述第一粘结剂的添加量和生石灰粉的质量比例约为1~10%。Further, the first binder is coal tar, anthracene oil or heavy oil, and the added amount of the first binder and the mass ratio of the quicklime powder are about 1-10%.

进一步的,所述第二粘结剂为沥青、粘结性煤和腐殖酸的混合物,所述第二粘结剂的添加量与混合物料的质量比例约为1~20%。Further, the second binder is a mixture of pitch, caking coal and humic acid, and the ratio of the added amount of the second binder to the mass of the mixture is about 1-20%.

进一步的,所述第一搅拌装置为双轴搅拌机,所述第二搅拌装置为强力混合机。Further, the first stirring device is a twin-shaft mixer, and the second stirring device is an intensive mixer.

相对于现有技术,本实用新型所述的用于煤粉和生石灰粉成型的系统具有以下优势:Compared with the prior art, the system for forming pulverized coal and quicklime powder according to the present utility model has the following advantages:

本实用新型所述的煤粉和生石灰粉成型的系统使用粉煤和生石灰进行加工成型,所需要的原料成本低,不需要特别加工,减少了加工工序,减少了污染物的排放。The pulverized coal and quicklime powder molding system of the utility model uses pulverized coal and quicklime for processing and molding, the required raw material cost is low, no special processing is required, the processing procedure is reduced, and the discharge of pollutants is reduced.

附图说明Description of drawings

构成本实用新型的一部分的附图用来提供对本实用新型的进一步理解,本实用新型的示意性实施例及其说明用于解释本实用新型,并不构成对本实用新型的不当限定。The accompanying drawings that constitute a part of the present invention are used to provide further understanding of the present invention, and the schematic embodiments and descriptions of the present invention are used to explain the present invention and do not constitute an improper limitation of the present invention.

在附图中:In the attached image:

图1为本实用新型实施例所述的用于煤粉和生石灰粉成型的系统示意图;1 is a schematic diagram of a system for forming pulverized coal and quicklime powder according to an embodiment of the present utility model;

图2为本实用新型利用图1所示的系统制备球团的方法流程示意图。FIG. 2 is a schematic flow chart of the method for preparing pellets by using the system shown in FIG. 1 according to the present invention.

附图标记说明:Description of reference numbers:

1-储料罐,2-生石灰粉仓,3-煤粉仓,4-储料仓,5-振动给料装置,6-泵体,7-第一搅拌装置,8-第二搅拌装置,9-压球成型装置。1- Storage tank, 2- Quick lime powder bin, 3- Coal powder bin, 4- Storage bin, 5- Vibration feeding device, 6- Pump body, 7- First stirring device, 8- Second stirring device, 9-Ball forming device.

具体实施方式Detailed ways

需要说明的是,在不冲突的情况下,本实用新型中的实施例及实施例中的特征可以相互组合。It should be noted that the embodiments of the present invention and the features of the embodiments may be combined with each other under the condition of no conflict.

下面将参考附图并结合实施例来详细说明本实用新型。The present utility model will be described in detail below with reference to the accompanying drawings and in conjunction with the embodiments.

如图1-2所示,一种用于煤粉和生石灰粉成型的系统,包括生石灰粉仓2、煤粉仓3、第一搅拌装置7、第二搅拌装置8和压球成型装置9,优选地,所述第一搅拌装置为双轴搅拌机,对生石灰粉和第一粘结剂进行初步混合,生石灰粉可以利用生石灰块的筛下物,不需要进行破碎磨粉处理,降低了成本,同时减少了固废的排放,第一粘结剂在生石灰粉的表面形成一层疏水性的钝化薄膜,阻止生石灰粉与水的消化反应;优选地,所述第二搅拌装置为强力混合机,所述强力混合机对混合后的生石灰粉与粒度小于3mm的煤粉及第二粘结剂进一步混合搅拌均匀,得到主要成分为煤粉和生石灰粉的混合物料,混合时间约5分钟,优选地,所述压球成型装置为高压压球机,将混合物料进行压球,得到大小均匀的混合球团,生成的生球团粒度约45mm,抗压强度不小于400N,2m跌落强度(>5mm)不少于95%,具有较高的冷强度,不容易破碎,热解后的强度也较高,符合电石炉的生产要求,压成的生球团送入直立炉热解单元进行热解,较优的高压压球机规格的选择为压辊直径为800mm,压辊间的最大压力为380t,线压力为11t/cm,压球机的成球率大于90%,压球机具有预压紧功能,压球机设置有球形的模具,用于控制所需型球的形状和规格,所述生石灰粉仓2具有生石灰粉入口和生石灰粉出口,所述煤粉仓3具有煤粉入口和煤粉出口,所述第一搅拌装置7具有混料入口和混料出口,所述第二搅拌装置8具有第一入料口、第二入料口第三入料口和第一出料口,第二搅拌装置通过第一入料口与第一搅拌装置连接,第二搅拌装置通过第二入料口和煤粉仓连接,第二搅拌装置通过第三入料口和储料仓连接,第一搅拌装置的混合物料、煤粉和第二粘结剂的用量分别进行调节,互相不产生干扰,可根据系统实际生产情况对混合物料、煤粉和第二粘结剂配比随时进行调节,提高成品率,所述生石灰粉出口和混料入口相连接,所述混料出口和第一入料口连接,所述煤粉出口和所述第二入料口连接,所述第一出料口和所述压球成型装置9的进料口连接,煤粉和生石灰粉的配比方便调节,适应电石生产复杂的工况,可以生产高品质电石,还包括储料仓4,所述储料仓4具有入仓口和出仓口,所述出仓口和所述第三入料口连接。As shown in Figure 1-2, a system for forming coal powder and quicklime powder includes quicklime powder bin 2, coal powder bin 3, first stirring device 7, second stirring device 8 and briquetting device 9, Preferably, the first stirring device is a double-shaft mixer, which preliminarily mixes the quicklime powder and the first binder, and the quicklime powder can use the sieve of the quicklime block, and does not need to be crushed and milled, which reduces the cost. At the same time, the discharge of solid waste is reduced, and the first binder forms a hydrophobic passivation film on the surface of the quicklime powder to prevent the digestion reaction of the quicklime powder and water; preferably, the second stirring device is a strong mixer The intensive mixer further mixes and stirs the mixed quicklime powder, coal powder with a particle size of less than 3 mm and the second binder to obtain a mixed material whose main components are coal powder and quicklime powder, and the mixing time is about 5 minutes, preferably The said ball-forming device is a high-pressure ball press, and the mixed material is pressed to obtain a mixed pellet with a uniform size. 5mm) is not less than 95%, has high cold strength, is not easy to break, and has high strength after pyrolysis, which meets the production requirements of calcium carbide furnaces. The pressed green pellets are sent to the vertical furnace pyrolysis unit for heating. Solution, the optimal selection of high-pressure briquetting machine specifications is that the diameter of the briquetting roller is 800mm, the maximum pressure between the briquetting rollers is 380t, the line pressure is 11t/cm, the briquetting rate of the briquetting machine is greater than 90%, and the briquetting machine has Pre-compression function, the ball press is equipped with a spherical mold, which is used to control the shape and specification of the required balls. The quicklime powder bin 2 has a quicklime powder inlet and a quicklime powder outlet, and the coal powder bin 3 has coal powder. Inlet and pulverized coal outlet, the first stirring device 7 has a mixing inlet and a mixing outlet, the second stirring device 8 has a first inlet, a second inlet, a third inlet and a first outlet The second stirring device is connected to the first stirring device through the first feeding port, the second stirring device is connected to the pulverized coal silo through the second feeding port, and the second stirring device is connected to the storage bin through the third feeding port Connected, the amount of the mixed material, pulverized coal and the second binder of the first stirring device is adjusted separately without interfering with each other, and the ratio of the mixed material, pulverized coal and the second binder can be adjusted at any time according to the actual production situation Adjustment is performed to improve the yield, the quicklime powder outlet is connected with the mixing inlet, the mixing outlet is connected with the first feeding port, the coal powder outlet is connected with the second feeding port, and the first feeding port is connected. A discharge port is connected to the feed port of the ball pressing device 9, the ratio of coal powder and quicklime powder is easy to adjust, adapts to the complex working conditions of calcium carbide production, and can produce high-quality calcium carbide, and also includes a storage bin 4, The storage bin 4 has an inlet port and an outlet port, and the outlet port is connected with the third inlet port.

还包括储料罐1,所述储料罐1具有入罐口和出罐口,所述出罐口和所述混料入口连接,所述储料罐1的出罐口处设置有泵体6,通过泵体便于对储料罐内的第一粘结剂的用量进行控制。Also includes a storage tank 1, the storage tank 1 has a tank inlet and a tank outlet, the tank outlet is connected to the mixing inlet, and a pump body is provided at the tank outlet of the storage tank 1 6. It is convenient to control the amount of the first binder in the storage tank through the pump body.

所述储料罐1内装载有第一粘结剂,所述第一粘结剂用于在生石灰粉的表面形成一层疏水性的钝化薄膜,由于煤粉中含有水分,煤粉与生石灰粉直接混合后,生石灰粉容易吸收煤粉中的水分,发生石灰的消化反应,使球团体积膨胀,降低了球团的冷态强度和稳定性能。用第一粘结剂和生石灰粉混合的目的是,可以在生石灰粉的表面形成一层疏水性的钝化薄膜,阻止生石灰粉与水的消化反应,有利于下一步的混合成型,所述第一粘结剂为煤焦油、蒽油或重质油,所述第一粘结剂的添加量和生石灰粉的质量比例约为1~10%,从而可以使生石灰粉和第一粘结剂充分混合,在生石灰粉表面形成疏水性薄膜,优选的,选择煤焦油作为第一粘结剂,煤焦油可以在生石灰表面形成疏水性的钝化薄膜,可以阻碍生石灰粉与水的消化反应;煤焦油具有一定的粘结性能;煤焦油可以在球团料的热解工序中得到,属于副产品,成本低。The storage tank 1 is loaded with a first binder, which is used to form a hydrophobic passivation film on the surface of the quicklime powder. After the powder is directly mixed, the quicklime powder easily absorbs the moisture in the pulverized coal, and the digestion reaction of lime occurs, which expands the volume of the pellet and reduces the cold strength and stability of the pellet. The purpose of mixing with the first binder and the quicklime powder is to form a hydrophobic passivation film on the surface of the quicklime powder to prevent the digestion reaction of the quicklime powder and water, which is beneficial to the next step of mixing and molding. A binder is coal tar, anthracene oil or heavy oil, and the added amount of the first binder and the mass ratio of the quicklime powder are about 1-10%, so that the quicklime powder and the first binder can be fully Mixing to form a hydrophobic film on the surface of the quicklime powder, preferably, coal tar is selected as the first binder, the coal tar can form a hydrophobic passivation film on the surface of the quicklime, which can hinder the digestion reaction of the quicklime powder and water; coal tar It has certain bonding properties; coal tar can be obtained in the pyrolysis process of pellets, which is a by-product and has low cost.

所述储料仓4装载有第二粘结剂,所述第二粘结剂用于将煤粉和生石灰粉进行粘结,常温下可使煤粉与生石灰粉经高压混合成型,所述第二粘结剂为沥青、粘结性煤和腐殖酸的混合物,为煤化工副产品,成本低,所述第二粘结剂的添加量与混合物料的质量比例约为1~20%,从而可以是第二粘结剂和混合物料充分混合,较好的发挥第二粘结剂的效用。The storage bin 4 is loaded with a second binder, and the second binder is used to bond the coal powder and the quicklime powder. The second binder is a mixture of asphalt, caking coal and humic acid, which is a by-product of coal chemical industry and has low cost. It can be that the second binder and the mixed material are fully mixed to better exert the effect of the second binder.

生石灰粉仓2中的生石灰粉通过振动给料机输送到双轴搅拌机中,储料罐内的第一粘结剂也通过泵体输送到双轴搅拌机中进行搅拌均匀,使生石灰粉表面形成一层疏水性的钝化薄膜,进过双轴搅拌机搅拌后,生石灰粉和第一粘结剂的混合物通过第一入料口输送进强力混合机内,煤粉仓和储料仓同时向强力混合机内输送煤粉和第二粘结剂,在强力混合机进行二次混合,生石灰粉和煤粉粘结在一起进入到高压压球机内,压制成型。The quicklime powder in the quicklime powder bin 2 is transported to the double-shaft mixer through the vibrating feeder, and the first binder in the storage tank is also transported to the double-shaft mixer through the pump body for uniform mixing, so that the surface of the quicklime powder forms a layer of hydrophobic passivation film, after being stirred by the double-shaft mixer, the mixture of quicklime powder and the first binder is transported into the strong mixer through the first feeding port, and the coal powder silo and the storage silo are simultaneously intensively mixed. The pulverized coal and the second binder are transported in the machine, and are mixed in a strong mixer for a second time.

所述的煤粉和生石灰粉成型的系统,采用两种粘结剂,分别是第一粘结剂和第二粘结剂,分两次混合,且各物料分别进行添加,互不干扰,便于控制各物料添加比例,从而提高系统的成品率,同时避免两种粘结剂之间相互发生作用,从而影响成品效果。The system for forming pulverized coal and quicklime powder adopts two kinds of binders, namely the first binder and the second binder, which are mixed in two times, and each material is added separately without interfering with each other, which is convenient for use. The proportion of each material added is controlled, thereby improving the yield of the system, and at the same time avoiding the interaction between the two binders, thereby affecting the effect of the finished product.

所述生石灰粉仓2的生石灰粉出口、煤粉仓3的煤粉出口和储料仓4的出仓口均设置有振动给料装置5,优选的,振动给料装置为振动给料机,喂料均匀,连续性能好,可随时改变和控制流量,操作方便。The quicklime powder outlet of the quicklime powder bin 2, the coal powder outlet of the coal powder bin 3 and the outlet of the storage bin 4 are all provided with a vibrating feeding device 5, preferably, the vibrating feeding device is a vibrating feeder, The feeding is uniform, the continuous performance is good, the flow can be changed and controlled at any time, and the operation is convenient.

以上所述仅为本实用新型的较佳实施例而已,并不用以限制本实用新型,凡在本实用新型的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。The above are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the within the protection scope of the present invention.

Claims (4)

1.一种用于煤粉和生石灰粉成型的系统,其特征在于,包括生石灰粉仓(2)、煤粉仓(3)、第一搅拌装置(7)、第二搅拌装置(8)和压球成型装置(9),所述生石灰粉仓(2)具有生石灰粉入口和生石灰粉出口,所述煤粉仓(3)具有煤粉入口和煤粉出口,所述第一搅拌装置(7)具有混料入口和混料出口,所述第二搅拌装置(8)具有第一入料口、第二入料口第三入料口和第一出料口,所述生石灰粉出口和混料入口相连接,所述混料出口和第一入料口连接,所述煤粉出口和所述第二入料口连接,所述第一出料口和所述压球成型装置(9)的进料口连接,还包括储料罐(1),所述储料罐(1)具有入罐口和出罐口,所述出罐口和所述混料入口连接,所述储料罐(1)内装载有第一粘结剂,所述第一粘结剂用于在生石灰粉的表面形成一层疏水性的钝化薄膜,还包括储料仓(4),所述储料仓(4)具有入仓口和出仓口,所述出仓口和所述第三入料口连接,所述储料仓(4)装载有第二粘结剂,所述第二粘结剂用于将煤粉和生石灰粉进行粘结。1. A system for forming coal powder and quicklime powder, characterized in that it comprises a quicklime powder bin (2), a coal powder bin (3), a first stirring device (7), a second stirring device (8) and A briquetting forming device (9), the quicklime powder bin (2) has a quicklime powder inlet and a quicklime powder outlet, the coal powder bin (3) has a coal powder inlet and a coal powder outlet, the first stirring device (7) ) has a mixing inlet and a mixing outlet, the second stirring device (8) has a first feeding port, a second feeding port, a third feeding port and a first discharging port, the quicklime powder outlet and the mixing The material inlet is connected, the mixing outlet is connected with the first material inlet, the pulverized coal outlet is connected with the second material inlet, and the first outlet is connected with the ball pressing device (9). The feed port is connected to the feed port, and also includes a material storage tank (1), the material storage tank (1) has a tank inlet port and a tank outlet port, the tank outlet port is connected with the mixing inlet, and the material storage tank (1) A first binder is loaded inside, and the first binder is used to form a layer of hydrophobic passivation film on the surface of the quicklime powder, and also includes a storage bin (4), the storage bin (4) It has an inlet port and an outlet port, the outlet port is connected to the third inlet port, and the storage bin (4) is loaded with a second binder, the second binder Used to bond coal powder and quicklime powder. 2.根据权利要求1所述的用于煤粉和生石灰粉成型的系统,其特征在于,所述储料罐(1)的出罐口处设置有泵体(6)。2 . The system for forming pulverized coal and quicklime powder according to claim 1 , wherein a pump body ( 6 ) is provided at the outlet of the storage tank ( 1 ). 3 . 3.根据权利要求1所述的用于煤粉和生石灰粉成型的系统,其特征在于,所述生石灰粉仓(2)的生石灰粉出口、煤粉仓(3)的煤粉出口和储料仓(4)的出仓口均设置有振动给料装置(5)。3. The system for forming pulverized coal and quicklime powder according to claim 1, characterized in that the quicklime powder outlet of the quicklime powder bin (2), the coal powder outlet of the coal powder bin (3) and the storage material A vibrating feeding device (5) is provided at the outlet of the bin (4). 4.根据权利要求1所述的用于煤粉和生石灰粉成型的系统,其特征在于,所述第一搅拌装置(7)为双轴搅拌机,所述第二搅拌装置(8)为强力混合机。4 . The system for forming pulverized coal and quicklime powder according to claim 1 , wherein the first stirring device ( 7 ) is a double-shaft agitator, and the second stirring device ( 8 ) is a strong mixing device. 5 . machine.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114133972A (en) * 2021-12-10 2022-03-04 河南北斗众创高新技术研究院有限公司 A modularly assembled industrial flue gas solid waste recycling treatment device and its operation method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114133972A (en) * 2021-12-10 2022-03-04 河南北斗众创高新技术研究院有限公司 A modularly assembled industrial flue gas solid waste recycling treatment device and its operation method

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