CN211620349U - A steel mill sludge treatment system - Google Patents
A steel mill sludge treatment system Download PDFInfo
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- CN211620349U CN211620349U CN202020045606.8U CN202020045606U CN211620349U CN 211620349 U CN211620349 U CN 211620349U CN 202020045606 U CN202020045606 U CN 202020045606U CN 211620349 U CN211620349 U CN 211620349U
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Abstract
本实用新型公开了一种钢厂污泥处理系统,属于污泥处理技术领域。它包括储存仓、干燥机、分离器以及料仓,所述干燥机分别与储存仓和分离器相接,干燥机底部设置有进气管道,一端设置有抽气管,抽气管另一端设置有阀门,且与分离器相接,所述分离器下端设置有料仓。系统设置合理,使用方便。
The utility model discloses a steel mill sludge treatment system, which belongs to the technical field of sludge treatment. It includes a storage bin, a dryer, a separator and a silo. The dryer is respectively connected with the storage bin and the separator. The bottom of the dryer is provided with an air inlet pipe, one end is provided with an air extraction pipe, and the other end of the air extraction pipe is provided with a valve , and is connected with the separator, and the lower end of the separator is provided with a silo. The system setting is reasonable and easy to use.
Description
技术领域technical field
本实用新型属于污泥处理技术领域,更具体地说,涉及一种钢厂污泥处理系统。The utility model belongs to the technical field of sludge treatment, in particular to a sludge treatment system of a steel mill.
背景技术Background technique
冷轧带钢或电炉特钢酸洗后需要用水清洗表面,使用水清除表面残留酸液形成含酸废水,对于含酸的废水,不便于运输和清理,一般的方法是采用石灰进行中和,并对中和后的浆液进行澄清,使得浆液中不可溶解物沉淀到底部,形成污泥,而污泥上部的液体可进行回收再利用。而对于产生的污泥,一般很难进行处理,对污泥进行堆放和填埋,都需要占用土地资源,且由于污泥中含有大量金属和有害物质,在露天进行填埋后,经雨水浸泡,污泥会污染附近土地和水源,造成生态环境的破坏,合理的处理方式,是亟需的。After pickling cold-rolled strip steel or electric furnace special steel, the surface needs to be cleaned with water, and the residual acid solution on the surface should be removed with water to form acid-containing wastewater. For acid-containing wastewater, it is inconvenient to transport and clean up. The general method is to use lime for neutralization. The neutralized slurry is clarified, so that the insoluble matter in the slurry settles to the bottom to form sludge, and the liquid on the upper part of the sludge can be recycled and reused. For the generated sludge, it is generally difficult to deal with it. The sludge storage and landfill require land resources, and because the sludge contains a large amount of metals and harmful substances, after being landfilled in the open air, it will be soaked in rainwater. , the sludge will pollute the nearby land and water sources, causing damage to the ecological environment, and reasonable disposal methods are urgently needed.
现有技术中,中国专利申请号为:201710335693.3,公布日为:2017.08.04的“一种用于烧结消化炼钢污泥系统和方法”,其包括污泥直输管路和烧结污泥预处理水池,其中:污泥直输管路上设置有炼钢污泥水泵,污泥直输管路和烧结污泥预处理水池连接,烧结污泥预处理水池内设置有加热管道、压缩气体管道和污泥烧结管路,烧结污泥泵设置于污泥烧结管路上,烧结污泥管路还和烧结污泥喷嘴相连接;压缩气体管道和压缩气体源连接;炼钢污泥经炼钢污泥水泵通过污泥直输管路进入烧结污泥预处理水池,并通过所述压缩气体管道对其进行搅拌,通过加热管道对其进行加热。利用该系统烧结消化炼钢污泥的方法,解决了污泥的去向;但污泥未经脱水处理,能源的耗费率高,不利于生产。In the prior art, the Chinese patent application number is: 201710335693.3, and the publication date is: “A system and method for sintering and digesting steelmaking sludge” on 2017.08.04, which includes a sludge direct transportation pipeline and a sintered sludge pre-treatment system. The treatment tank, wherein: a steel-making sludge pump is arranged on the sludge direct transportation pipeline, the sludge direct transportation pipeline is connected with the sintered sludge pretreatment tank, and the sintered sludge pretreatment tank is provided with heating pipelines, compressed gas pipelines and The sludge sintering pipeline, the sintering sludge pump is arranged on the sludge sintering pipeline, and the sintering sludge pipeline is also connected with the sintering sludge nozzle; the compressed gas pipeline is connected with the compressed gas source; the steelmaking sludge is passed through the steelmaking sludge The water pump enters the sintered sludge pretreatment tank through the sludge direct transportation pipeline, stirs it through the compressed gas pipeline, and heats it through the heating pipeline. Using the method of sintering and digesting steelmaking sludge in this system solves the whereabouts of the sludge; however, the sludge has not been dewatered, and the energy consumption rate is high, which is not conducive to production.
中国专利申请号为:201910567255.9,公告日为:2019.09.13的“一种利用钢厂污泥制备而得的轻骨料及其制备方法”,其公开了一种轻骨料,以钢厂污泥为原料制备骨料,原料配方为10~40%的钢厂污泥和60~90%的粉煤灰,具体制备方法包括以下步骤:钢厂污泥经过烘干、粉碎研磨、过筛后,加入过筛的粉煤灰按一定的重量比混合均匀后造球,将生料球干燥一定时间后进行与热处理,最后烧结,冷却后得到骨料成品。将钢厂的污泥用于轻骨料的制备上,很好的解决了污泥的去向;但在对污泥进行加工的过程中,需要消耗大量能源进行处理,不利于节能环保。The Chinese patent application number is: 201910567255.9, and the announcement date is: 2019.09.13, "A Lightweight Aggregate Prepared by Using Steel Mill Sludge and Its Preparation Method", which discloses a light weight aggregate, which is made of steel mill sludge. The sludge is used as the raw material to prepare the aggregate, and the raw material formula is 10-40% steel mill sludge and 60-90% fly ash. The specific preparation method includes the following steps: the steel mill sludge is dried, pulverized and ground, and sieved. , Add the sieved fly ash according to a certain weight ratio and mix it evenly to form pellets. After drying the raw pellets for a certain period of time, heat treatment is performed, and finally sintered and cooled to obtain finished aggregates. The sludge from the steel mill is used for the preparation of light aggregates, which is a good solution to the whereabouts of the sludge; however, in the process of processing the sludge, it needs to consume a lot of energy for processing, which is not conducive to energy conservation and environmental protection.
中国专利申请号为:201810587630.1,公布日为:2018.11.02的“冷轧酸性废水的处理方法及烧结半干法脱硫灰的应用”,其公开了一种冷轧酸性废水的处理方法及烧结半干法脱硫灰的应用,其采用烧结半干法脱硫灰来中和处理冷轧酸性废水,利用烧结半干法脱硫灰中的Ca(OH)2、Ca0、CaS03等碱性物质,中和处理冷轧酸性废水,使废水经过曝气、中和、PH调节、絮凝沉降等过程而达到中水回用标准;处理过程中产生的SO2可回收用于制备硫酸;处理过程中产生的污泥经浓缩、压滤脱水后,可配入高炉水渣,经过立磨工艺处理后制备矿渣微粉,能显著提高矿渣微粉的质量。其可同时使烧结半干法脱硫灰和冷轧酸性废水得到处理,解决了环保上的难题,实现了以废治废;但废水处理需要利用大量能源,不能达到能源的综合有效利用。The Chinese patent application number is: 201810587630.1, the publication date is: 2018.11.02, "The treatment method of cold rolling acid wastewater and the application of sintered semi-dry desulfurization ash", which discloses a cold rolling acid wastewater treatment method and sintered semi-dry wastewater The application of dry desulfurization ash, which uses sintered semi-dry desulfurization ash to neutralize and treat cold rolling acid wastewater, and uses alkaline substances such as Ca(OH)2, Ca0, CaS03 in sintered semi-dry desulfurization ash to neutralize and treat Cold-rolled acid wastewater, so that the wastewater can reach the reclaimed water reuse standard through aeration, neutralization, PH adjustment, flocculation and sedimentation and other processes; SO 2 produced in the treatment process can be recovered for the preparation of sulfuric acid; sludge produced in the treatment process After concentration, pressure filtration and dehydration, it can be mixed with blast furnace water slag, and the slag micropowder can be prepared after the vertical grinding process, which can significantly improve the quality of the slag micropowder. It can treat sintered semi-dry desulfurization ash and cold-rolled acid wastewater at the same time, which solves the problem of environmental protection and realizes waste treatment with waste; however, waste water treatment requires a large amount of energy and cannot achieve comprehensive and effective utilization of energy.
发明内容SUMMARY OF THE INVENTION
1.要解决的问题1. The problem to be solved
针对现有钢厂污泥处理工艺中产生污泥无法有效处理或处理成本高、能耗高、CO2排放高的问题,本实用新型提供一种钢厂污泥处理系统,对污泥进行规范化处理,解决了上述问题。Aiming at the problems that the sludge produced in the existing steel mill sludge treatment process cannot be effectively treated or the treatment cost is high, the energy consumption is high, and the CO2 emission is high, the utility model provides a steel mill sludge treatment system, which can standardize the treatment of the sludge. , which solves the above problem.
2.技术方案2. Technical solutions
为了解决上述问题,本实用新型所采用的技术方案如下:In order to solve the above-mentioned problems, the technical scheme adopted by the present utility model is as follows:
本实用新型的一种钢厂污泥处理系统,包括储存仓、干燥机、分离器以及料仓,所述干燥机分别与储存仓和分离器相接,干燥机底部设置有进气管道,一端设置有抽气管,抽气管另一端设置有阀门,且与分离器相接,所述分离器下端设置有料仓。The utility model discloses a sludge treatment system for a steel mill, which comprises a storage bin, a dryer, a separator and a silo. The dryer is respectively connected with the storage bin and the separator. An air inlet pipe is arranged at the bottom of the dryer, one end of which is arranged at one end. An air extraction pipe is provided, and the other end of the air extraction pipe is provided with a valve, which is connected with the separator, and the lower end of the separator is provided with a silo.
作为本实用新型的优选,所述干燥机与水平面之间形成的夹角为锐角。As a preference of the present invention, the angle formed between the dryer and the horizontal plane is an acute angle.
作为本实用新型的优选,所述干燥机由外层和内层的套筒套接而成,外层和内层套筒之间设置搅拌叶片。As a preference of the present invention, the dryer is formed by sleeves of the outer layer and the inner layer, and a stirring blade is arranged between the outer layer and the inner layer of the sleeve.
作为本实用新型的优选,所述储存仓与干燥机之间通过第一输送机进行连接,所述干燥机污泥进料口位于第一输送机下部,所述储存仓为双开口型,上部用于进料,下部用于出料,所述第一输送机为无轴型螺旋输送机。As a preference of the present invention, the storage bin and the dryer are connected by a first conveyor, the sludge feed port of the dryer is located at the lower part of the first conveyor, the storage bin is of double opening type, and the upper part is It is used for feeding, and the lower part is used for discharging, and the first conveyor is a shaftless screw conveyor.
作为本实用新型的优选,还包括烧结机以及高炉,所述料仓底部设置风机,料仓与烧结机之间通过第二输送机进行连接,烧结机与高炉相接。As a preferred option of the present invention, it also includes a sintering machine and a blast furnace, a fan is arranged at the bottom of the silo, the silo and the sintering machine are connected by a second conveyor, and the sintering machine is connected to the blast furnace.
作为本实用新型的优选,还包括烟气净化装置,所述烟气净化装置、阀门以及分离器通过三通连接。As a preferred option of the present invention, a flue gas purification device is also included, and the flue gas purification device, the valve and the separator are connected through a three-way connection.
作为本实用新型的优选,所述烟气净化装置、阀门以及分离器连接处设置有测温仪。As a preferred option of the present invention, a thermometer is provided at the joints of the flue gas purification device, the valve and the separator.
3.有益效果3. Beneficial effects
相比于现有技术,本实用新型的有益效果为:Compared with the prior art, the beneficial effects of the present utility model are:
(1)本实用新型的一种钢厂污泥处理系统,通过储存仓进行污泥储存,储存仓采用上下双开口式,上部用于投入污泥,下端开口将污泥取出,进行下一步处理,能够实现污泥的连续化投放,干燥机底部设置进气通道,通过进气通道将烟气放入,烟气由下至上流动,在干燥机中存留的时间更长,烟气与污泥之间的接触时间更久,一方面烟气对污泥的干燥效果更好,另一方面便于去除污泥烟气中的固体颗粒,使用效果较佳;(1) A steel mill sludge treatment system of the present utility model uses a storage bin for sludge storage. The storage bin adopts an upper and lower double-opening type, the upper part is used for inputting sludge, and the lower end opening takes out the sludge for the next step. , which can realize the continuous feeding of sludge. The bottom of the dryer is provided with an intake channel, and the flue gas is put in through the intake channel. The flue gas flows from bottom to top, and it stays in the dryer for a longer time. The contact time between them is longer, on the one hand, the flue gas has a better drying effect on the sludge, on the other hand, it is easy to remove the solid particles in the sludge flue gas, and the use effect is better;
(2)本实用新型的一种钢厂污泥处理系统,干燥机将干燥完成的污泥输送至分离器中,由分离器对污泥和烟气进行分离,分离后的污泥可输送至下一工位进行使用,分离的烟气可通过阀门和抽气管回到干燥机中进行进一步利用,使得烟气的利用率高,完成对资源的合理有效利用;(2) In a steel mill sludge treatment system of the present invention, the dryer transports the dried sludge to the separator, the sludge and the flue gas are separated by the separator, and the separated sludge can be transported to For use at the next station, the separated flue gas can be returned to the dryer through the valve and exhaust pipe for further use, so that the utilization rate of flue gas is high and the rational and effective use of resources is completed;
(3)本实用新型的一种钢厂污泥处理系统,干燥机由内外套筒构成,污泥在内外套筒之间,接触面积大,干燥效率高,干燥机在放置时,若竖直方向放置,则污泥容易堆积在底部,不利于烟气通过,若水平方向放置,则烟气无法从干燥器一端流向另一端的过程中,充满整个干燥机,且在干燥过程中,干燥机中设置搅拌叶片,通过搅拌叶片对污泥进行搅拌,将污泥的尺寸变小,使得污泥处于运动的状态,增大污泥和烟气的接触面积,减少污泥的干燥时间,实现对烟气资源的更有效的利用;(3) A steel mill sludge treatment system of the present utility model, the dryer is composed of inner and outer sleeves, the sludge is between the inner and outer sleeves, the contact area is large, and the drying efficiency is high. When the dryer is placed, if the vertical If it is placed in the horizontal direction, the sludge will easily accumulate at the bottom, which is not conducive to the passage of flue gas. If it is placed in a horizontal direction, the flue gas cannot flow from one end of the dryer to the other end, filling the entire dryer, and during the drying process, the dryer A stirring blade is set in the middle, and the sludge is stirred by the stirring blade, so that the size of the sludge is reduced, so that the sludge is in a moving state, the contact area between the sludge and the flue gas is increased, the drying time of the sludge is reduced, and the More efficient use of flue gas resources;
(4)本实用新型的一种钢厂污泥处理系统,将污泥进行干燥处理后,将其运送至烧结机作为烧结原料进行烧结,由于污泥是清洗钢材表面产生的,污泥中含有大量的铁,通过配比能够代替原本的一部分烧结原料,即处理了污泥,同时用于烧结不会产生烧结之外的污染物,节约资源,便于使用;(4) In a steel mill sludge treatment system of the present invention, after the sludge is dried, it is transported to a sintering machine as a sintering raw material for sintering. Since the sludge is generated by cleaning the surface of the steel, the sludge contains A large amount of iron can replace a part of the original sintering raw materials through the ratio, that is, the sludge is treated, and at the same time, it will not produce pollutants other than sintering when used for sintering, saving resources and easy to use;
(5)本实用新型的一种钢厂污泥处理系统,分离器下部设置料仓,用于储存干燥后的污泥,用于后续的烧结工序,污泥在料仓中下行至出口的过程中,可能会发生堵塞,通过风机吹动,使得干燥的污泥下行过程中处于动态,不会发生堵塞,同时能够清理掉料仓中残余的烟气,使得烟气从料仓入口回到分离器中;(5) In a steel mill sludge treatment system of the present invention, a silo is set at the lower part of the separator for storing the dried sludge for the subsequent sintering process, and the process in which the sludge descends from the silo to the outlet During the process, blockage may occur. By blowing the fan, the dry sludge is in a dynamic state during the downward process, and no blockage will occur. At the same time, the residual flue gas in the silo can be cleaned up, so that the flue gas can return to the separation from the entrance of the silo. in the device;
(6)本实用新型的一种钢厂污泥处理系统,烟气能否通过抽气管回到干燥机中进行再利用,取决于烟气的温度,若干燥后的烟气温度仍然较高,高于测温仪的设定值,则阀门打开,烟气通过抽气管回到干燥机继续利用,否则阀门关闭,对烟气进行净化。(6) In a steel mill sludge treatment system of the present invention, whether the flue gas can be returned to the dryer through the exhaust pipe for reuse depends on the temperature of the flue gas, if the temperature of the flue gas after drying is still high, If it is higher than the set value of the thermometer, the valve will be opened, and the flue gas will return to the dryer through the exhaust pipe to continue to be used, otherwise the valve will be closed to purify the flue gas.
附图说明Description of drawings
以下将结合附图和实施例来对本实用新型的技术方案作进一步的详细描述,但是应当知道,这些附图仅是为解释目的而设计的,因此不作为本实用新型范围的限定。此外,除非特别指出,这些附图仅意在概念性地说明此处描述的结构构造,而不必要依比例进行绘制。The technical solutions of the present invention will be described in further detail below with reference to the accompanying drawings and embodiments, but it should be known that these drawings are only designed for the purpose of explanation, and therefore are not intended to limit the scope of the present invention. Furthermore, unless otherwise indicated, the drawings are intended only to conceptually illustrate the structural configurations described herein and are not necessarily drawn to scale.
图1为一种污泥处理装置的结构示意图;Fig. 1 is the structural representation of a kind of sludge treatment device;
附图中:1、储存仓;2、第一输送机;3、干燥机;4、分离器;5、料仓;6、风机;7、阀门;8、抽气管;9、烟气净化装置;10、第二输送机;11、烧结机;12、高炉。In the attached drawings: 1. Storage bin; 2. First conveyor; 3. Dryer; 4. Separator; 5. Silo; 6. Fan; 7. Valve; 8. Exhaust pipe; 9. Flue gas purification device ; 10, the second conveyor; 11, the sintering machine; 12, the blast furnace.
具体实施方式Detailed ways
下文对本实用新型的示例性实施例的详细描述参考了附图,该附图形成描述的一部分,在该附图中作为示例示出了本实用新型可实施的示例性实施例。尽管这些示例性实施例被充分详细地描述以使得本领域技术人员能够实施本实用新型,但应当理解可实现其他实施例且可在不脱离本实用新型的精神和范围的情况下对本实用新型作各种改变。下文对本实用新型的实施例的更详细的描述并不用于限制所要求的本实用新型的范围,而仅仅为了进行举例说明且不限制对本实用新型的特点和特征的描述,以提出执行本实用新型的最佳方式,并足以使得本领域技术人员能够实施本实用新型。因此,本实用新型的范围仅由所附权利要求来限定。The following detailed description of exemplary embodiments of the invention refers to the accompanying drawings, which form a part hereof, and which illustrate, by way of example, exemplary embodiments of the invention in which the invention may be practiced. Although these exemplary embodiments have been described in sufficient detail to enable those skilled in the art to practice the invention, it should be understood that other embodiments may be implemented and the invention may be modified without departing from the spirit and scope of the invention. Various changes. The following more detailed descriptions of the embodiments of the present invention are not intended to limit the scope of the present invention as claimed, but are merely for illustration and not to limit the description of the features and characteristics of the present invention, in order to propose the implementation of the present invention. the best mode, and is sufficient to enable those skilled in the art to implement the present invention. Accordingly, the scope of the present invention is to be limited only by the appended claims.
下文对本实用新型的详细描述和示例实施例可结合附图来更好地理解,其中本实用新型的元件和特征由附图标记标识。The following detailed description and example embodiments of the invention can be better understood in conjunction with the accompanying drawings, wherein elements and features of the invention are identified by reference numerals.
实施例1Example 1
如图1所示,本实施例的一种钢厂污泥处理系统包括储存仓1、第一输送机2、干燥机3、分离器4、料仓5、风机6、阀门7、抽气管8、烟气净化装置9、第二输送机10、烧结机11以及高炉12。通过上述装置和机械部件的使用,能够实现对钢厂产生的污泥进行干燥处理,在处理的过程中,引入钢厂生产过程中产生的烟气,利用烟气的余温实现对污泥的干燥,节约了能源的使用,实现废物利用,同时,烟气在通过污泥的过程中,污泥能够实现对烟气中固体颗粒物和其他有害物质的有效吸附,节约了烟气后续处理所消耗的能源,节能环保,能源的利用率高。As shown in FIG. 1 , a steel mill sludge treatment system in this embodiment includes a storage bin 1 , a
储存仓1下端设置第一输送机2,储存仓1与干燥机3之间通过第一输送机2进行连接,干燥机3污泥进料口位于第一输送机2下部,干燥机3底部设置有进气管道,干燥机3与分离器4相接,分离器4下端设置有料仓5,料仓5底部设置风机6,料仓5与烧结机11之间通过第二输送机10进行连接,烧结机11与高炉12相接。分离器4的烟气出口处设置三通,并设置气体测温仪,三通的另外两端分别设置烟气净化装置9以及阀门7,阀门7连接抽气管8,抽气管8另一端连接干燥机3。A
上述钢厂污泥处理系统主要通过烟气对污泥进行干燥,以及污泥对烟气进行吸附,以达到节能环保,废物利用的目的,如图1所示,A处为污泥进料处,即为储料仓5,通过储存仓1进行污泥储存,储存仓1采用上下双开口式,上部用于投入污泥,下端开口将污泥取出,进行下一步处理,能够实现污泥的连续化投放。B处为烟气进气处,干燥机3底部设置进气通道,通过进气通道将烟气投入。The above-mentioned steel mill sludge treatment system mainly dries the sludge through the flue gas, and the sludge adsorbs the flue gas, so as to achieve the purpose of energy saving, environmental protection and waste utilization. As shown in Figure 1, place A is the sludge feeding place. , that is, the storage bin 5, which is used for sludge storage through the storage bin 1. The storage bin 1 adopts the upper and lower double opening type, the upper part is used to input the sludge, and the lower end is opened to take out the sludge and carry out the next step. Continuous delivery. The position B is the intake of the flue gas, and the bottom of the dryer 3 is provided with an intake channel, and the flue gas is put into the dryer through the intake channel.
上述中第一输送机2和第二输送机10为无轴型螺旋输送机,结合污泥本身的特性,输送效率高。干燥机3由外层和内层的套筒套接而成,外层和内层套筒之间设置搅拌叶片,且干燥机3与水平面之间形成的夹角为锐角。干燥机3由内外套筒构成,污泥在内外套筒之间,接触面积大,干燥效率高,干燥机3在放置时,若竖直方向放置,则污泥容易堆积在底部,不利于烟气通过,若水平方向放置,则烟气无法从干燥器一端流向另一端的过程中,充满整个干燥机3,且在干燥过程中,干燥机3中设置搅拌叶片,通过搅拌叶片对污泥进行搅拌,将污泥的尺寸变小,使得污泥处于运动的状态,增大污泥和烟气的接触面积,减少污泥的干燥时间,实现对烟气资源的更有效的利用。本实施例的干燥机3倾斜角度为45°,烟气由下至上流动,在干燥机3中存留的时间更长,烟气与污泥之间的接触时间更久,一方面烟气对污泥的干燥效果更好,另一方面便于去除污泥烟气中的固体颗粒,使用效果较佳。In the above, the
分离器4对干燥机3中输送干燥的污泥进行分离处理,干燥的污泥进入料仓5中,烟气则排出分离器4,通过分离器4烟气出口处的气体测温仪对烟气进行测温,烟气能否通过抽气管8回到干燥机3中进行再利用,取决于烟气的温度,若干燥后的烟气温度仍然较高,高于测温仪的设定值,则阀门7打开,烟气通过抽气管8回到干燥机3继续利用,否则阀门7关闭,对烟气进行净化;使得烟气的利用率高,完成对资源的合理有效利用。分离器4下部设置料仓5,用于储存干燥后的污泥,用于后续的烧结工序,污泥在料仓5中下行至出口的过程中,可能会发生堵塞,通过风机6吹动,使得干燥的污泥下行过程中处于动态,不会发生堵塞,同时能够清理掉料仓5中残余的烟气,使得烟气从料仓5入口回到分离器4中。烟气净化装置9为现有技术,工厂内进行烟气净化的机械设备均可使用。The separator 4 separates and processes the dried sludge transported in the dryer 3, the dried sludge enters the silo 5, and the flue gas is discharged from the separator 4. The temperature of the flue gas is measured, and whether the flue gas can be returned to the dryer 3 through the
干燥的污泥从料仓5通过第二输送机10输送至烧结机11,作为烧结原料进行烧结,由于污泥是清洗钢材表面产生的,污泥中含有大量的铁,通过配比能够代替原本的一部分烧结原料,即处理了污泥,同时用于烧结不会产生烧结之外的污染物,节约资源,便于使用。The dried sludge is transported from the silo 5 to the
实施例2Example 2
本实施例的一种钢厂污泥处理系统,与实施例1基本相同,其不同之处在于,干燥机3与水平面之间的夹角为60°。A steel mill sludge treatment system in this embodiment is basically the same as that in Embodiment 1, except that the angle between the dryer 3 and the horizontal plane is 60°.
实施例3Example 3
本实施例的一种钢厂污泥处理系统,与实施例1基本相同,其不同之处在于,干燥机3与水平面之间的夹角为30°。A steel mill sludge treatment system in this embodiment is basically the same as that in Embodiment 1, except that the angle between the dryer 3 and the horizontal plane is 30°.
实施例4Example 4
本实施例的一种钢厂污泥处理系统,与实施例1基本相同,其不同之处在于,干燥机3与水平面之间的夹角为85°。A steel mill sludge treatment system in this embodiment is basically the same as that in Embodiment 1, except that the angle between the dryer 3 and the horizontal plane is 85°.
实施例5Example 5
本实施例的一种钢厂污泥处理系统,与实施例1基本相同,其不同之处在于,干燥机3与水平面之间的夹角为15°。A steel mill sludge treatment system in this embodiment is basically the same as that in Embodiment 1, except that the angle between the dryer 3 and the horizontal plane is 15°.
实施例6Example 6
本实施例的一种钢厂污泥利用方法,在实施例1-5任一实施例的基础上,包括以下步骤:On the basis of any one of Embodiments 1-5, a method for utilizing sludge in a steel mill of the present embodiment includes the following steps:
S1、将含水量65%(控制污泥的含水量主要是为了便于运输,避免不必要的资源浪费)的污泥通过翻斗汽车输送至钢厂污泥处理系统,倒入容积为150m3的储存仓1。合上储存仓1进料口,打开污泥出料口,污泥靠重力至储存仓1下部的螺旋输送机,输送至干燥机3;引入冷轧罩式炉或连退炉400℃的余热烟气对污泥进行烘干,余热烟气流量12Wm3/h,烘4小时,烘干过程中,干燥机3旋转,通过搅拌叶片或其它打散装置把大颗粒污泥打散,干燥后的污泥颗粒通过风机6输送至分离器4。S1. The sludge with a water content of 65% (the control of the water content of the sludge is mainly to facilitate transportation and avoid unnecessary waste of resources) is transported to the sludge treatment system of the steel mill through a dump truck, and poured into a storage volume of 150m3 Warehouse 1. Close the feeding port of storage bin 1, open the sludge discharge port, and the sludge will be transported to the screw conveyor at the lower part of the storage bin 1 by gravity, and then transported to the dryer 3; The sludge is dried by the flue gas, the residual heat flue gas flow is 12Wm 3 /h, and the drying is performed for 4 hours. During the drying process, the dryer 3 rotates, and the large-particle sludge is dispersed by stirring blades or other dispersing devices. After drying The sludge particles are transported to the separator 4 by the fan 6 .
S2、将干燥完成的污泥以及烟气输送至分离器4中,在分离器4中将干燥后的污泥和烟气进行分离,干燥的污泥进入料仓5,烟气通过管道排出分离器4;分离器4位于料仓5上部,颗粒大小根据需要选择进入分离器4下部的料仓5。分离器4进行分离属于物料的分离,是现有技术。S2. The dried sludge and flue gas are transported to the separator 4, the dried sludge and flue gas are separated in the separator 4, the dried sludge enters the silo 5, and the flue gas is discharged and separated through the pipeline 4; The separation performed by the separator 4 belongs to the separation of materials, which is the prior art.
S3、分离器4排出的烟气经过气体测温仪进行温度的测量,气体测温仪的设定温度为140℃(140℃是为了能源利用角度,再低的温度,则对于污泥的烘干效果不理想),将干燥机3干燥后的烟气温度为220℃,关闭烟气净化装置9,打开阀门7,烟气通过阀门7和抽气管8回到干燥机3中进行再利用,料仓5内污泥含水量1.0%、平均粒度1.5mm、CaO含量26%(含水量的控制避免作为烧结原料影响烧结,粒度的选择也是基于烧结原料的考虑,CaO含量则是提高烧结后的品位)。S3. The temperature of the flue gas discharged from the separator 4 is measured by a gas thermometer, and the set temperature of the gas thermometer is 140°C (140°C is for the angle of energy utilization, and the lower the temperature, the more effective the sludge drying is. The drying effect is not ideal), the temperature of the flue gas after drying by the dryer 3 is 220 ° C, the flue gas purification device 9 is closed, the valve 7 is opened, and the flue gas is returned to the dryer 3 through the valve 7 and the
S4、烘干后的污泥通过罐车输送至烧结料仓5,以0.5%(过多的配比,杂质变多,影响高炉12生产)的比例进行烧结配矿至烧结机11;烧结料再通过输送机输送至高炉12,在高炉12经超过1550℃熔融,有益元素被利用,杂质成为高炉12矿渣进行应用。高炉12经≥1350℃熔融,有益元素Fe、Ca、Mg、C等被利用,杂质Si、Al等成为高炉12矿渣。S4. The dried sludge is transported to the sintering silo 5 by a tanker, and is sintered and blended to the
上述方法中,根据污泥产生企业特点,利用现有低温余热资源对污泥进行减量预处理,再根据污泥特点进行资源化利用,解决了污泥占地的问题,且设备操作简单,没有二次废弃物再产生,实现了污泥的真正处理和利用,目前该发明已经进行了实际应用,除去处理成本,为公司每年节省费用5148万元、减少CO2排放1100吨。In the above method, according to the characteristics of the sludge producing enterprise, the existing low-temperature waste heat resources are used to reduce the amount of sludge pretreatment, and then according to the characteristics of the sludge, the resource utilization is carried out, which solves the problem of sludge occupation, and the equipment is simple to operate. There is no secondary waste to be regenerated, which realizes the real treatment and utilization of sludge. At present, the invention has been put into practical application, and the cost of treatment has been removed, saving the company 51.48 million yuan per year and reducing CO2 emissions by 1,100 tons.
在对钢厂对烟气进行处理的过程中,往往因为烟气中含有大量颗粒物和有机物,颗粒物会使得烟气处理的负荷较大,有机物则在烟气中是不便于处理的存在,而将烟气通过污泥后,烟气中的颗粒物吸附在污泥上,使得烟气后续处理较为轻松,且对烟气中的有机物进行检测,烟气中的有机物得到大幅下降,解决了烟气中有机物后续处理的困难。In the process of processing flue gas in steel plants, the flue gas often contains a large amount of particulate matter and organic matter. After the flue gas passes through the sludge, the particulate matter in the flue gas is adsorbed on the sludge, which makes the subsequent treatment of the flue gas easier, and the organic matter in the flue gas is detected, and the organic matter in the flue gas is greatly reduced. Difficulties in the subsequent processing of organics.
烟气中的颗粒物和有机物经过烧结后置于高炉12中,最终成为高炉12渣。The particulate matter and organic matter in the flue gas are placed in the
实施例7Example 7
本实施例的一种钢厂污泥利用方法,在实施例1-5任一实施例的基础上,包括以下步骤:On the basis of any one of Embodiments 1-5, a method for utilizing sludge in a steel mill of the present embodiment includes the following steps:
S1、将含水量55%的污泥通过翻斗汽车输送至钢厂污泥处理系统,倒入容积为120m3的储存仓1。合上储存仓1进料口,打开污泥出料口,污泥靠重力至储存仓1下部的螺旋输送机,输送至干燥机3;引入冷轧酸洗焙烧炉余热烟气360℃的余热烟气对污泥进行烘干,余热烟气流量12Wm3/h,烘3小时,烘干过程中,干燥机3旋转,通过搅拌叶片或其它打散装置把大颗粒污泥打散,干燥后的污泥颗粒通过风机6输送至分离器4。S1. The sludge with a water content of 55% is transported to the sludge treatment system of the steel mill through a dump truck, and poured into the storage bin 1 with a volume of 120 m 3 . Close the feeding port of storage bin 1 and open the sludge discharge port. The sludge is transported to the screw conveyor at the lower part of the storage bin 1 by gravity and transported to the dryer 3; The flue gas dries the sludge, the residual heat flue gas flow rate is 12Wm 3 /h, and the drying is performed for 3 hours. During the drying process, the dryer 3 rotates, and the large-particle sludge is dispersed by stirring blades or other dispersing devices. After drying The sludge particles are transported to the separator 4 by the fan 6 .
S2、将干燥完成的污泥以及烟气输送至分离器4中,在分离器4中将干燥后的污泥和烟气进行分离,干燥的污泥进入料仓5,烟气通过管道排出分离器4;分离器4位于料仓5上部,颗粒大小根据需要选择进入分离器4下部的料仓5。分离器4进行分离属于物料的分离,是现有技术。S2. The dried sludge and flue gas are transported to the separator 4, the dried sludge and flue gas are separated in the separator 4, the dried sludge enters the silo 5, and the flue gas is discharged and separated through the pipeline 4; The separation performed by the separator 4 belongs to the separation of materials, which is the prior art.
S3、分离器4排出的烟气经过气体测温仪进行温度的测量,气体测温仪的设定温度为140℃,将干燥机3干燥后的烟气温度为180℃,关闭烟气净化装置9,打开阀门7,烟气通过阀门7和抽气管8回到干燥机3中进行再利用,料仓5内污泥含水量4.3%、平均粒度0.95mm、CaO含量18%。S3. The temperature of the flue gas discharged from the separator 4 is measured by a gas thermometer. The set temperature of the gas thermometer is 140 °C, the temperature of the flue gas after drying by the dryer 3 is 180 °C, and the flue gas purification device is turned off. 9. Open the valve 7, and the flue gas is returned to the dryer 3 through the valve 7 and the
S4、烘干后的污泥通过罐车输送至烧结料仓5,以0.2%的比例进行烧结配矿至烧结机11;烧结料再通过输送机输送至高炉12,在高炉12经超过1550℃熔融,有益元素被利用,杂质成为高炉12矿渣进行应用。S4. The dried sludge is transported to the sintering silo 5 through a tanker, and sintered and blended to the
实施例8Example 8
本实施例的一种钢厂污泥利用方法,在实施例1-5任一实施例的基础上,包括以下步骤:On the basis of any one of Embodiments 1-5, a method for utilizing sludge in a steel mill of the present embodiment includes the following steps:
S1、将含水量58%的污泥通过翻斗汽车输送至钢厂污泥处理系统,倒入容积为100m3的储存仓1。合上储存仓1进料口,打开污泥出料口,污泥靠重力至储存仓1下部的螺旋输送机,输送至干燥机3;引入烧结余热200℃的烟气对污泥进行烘干,余热烟气流量10Wm3/h,烘2.5小时,烘干过程中,干燥机3旋转,通过搅拌叶片或其它打散装置把大颗粒污泥打散,干燥后的污泥颗粒通过风机6输送至分离器4。S1. The sludge with a water content of 58% is transported to the sludge treatment system of the steel mill through a dump truck, and poured into the storage bin 1 with a volume of 100 m 3 . Close the feeding port of storage bin 1 and open the sludge discharge port. The sludge is transported to the screw conveyor at the lower part of the storage bin 1 by gravity and transported to the dryer 3; the flue gas with sintering waste heat of 200°C is introduced to dry the sludge. , the flow rate of waste heat flue gas is 10Wm 3 /h, drying for 2.5 hours, during the drying process, the dryer 3 rotates, and the large particles of sludge are dispersed by stirring blades or other dispersing devices, and the dried sludge particles are transported by the fan 6 to separator 4.
S2、将干燥完成的污泥以及烟气输送至分离器4中,在分离器4中将干燥后的污泥和烟气进行分离,干燥的污泥进入料仓5,烟气通过管道排出分离器4;分离器4位于料仓5上部,颗粒大小根据需要选择进入分离器4下部的料仓5。分离器4进行分离属于物料的分离,是现有技术。S2. The dried sludge and flue gas are transported to the separator 4, the dried sludge and flue gas are separated in the separator 4, the dried sludge enters the silo 5, and the flue gas is discharged and separated through the pipeline 4; The separation performed by the separator 4 belongs to the separation of materials, which is the prior art.
S3、分离器4排出的烟气经过气体测温仪进行温度的测量,气体测温仪的设定温度为140℃,将干燥机3干燥后的烟气温度为110℃,关闭阀门7,打开烟气净化装置9,烟气进行净化,料仓5内污泥含水量1.5%、平均粒度1.2mm、CaO含量22%。S3. The temperature of the flue gas discharged from the separator 4 is measured by a gas thermometer. The set temperature of the gas thermometer is 140°C, and the temperature of the flue gas after drying by the dryer 3 is 110°C. Close the valve 7 and open it. The flue gas purification device 9 is used to purify the flue gas. The sludge in the silo 5 has a water content of 1.5%, an average particle size of 1.2 mm, and a CaO content of 22%.
S4、烘干后的污泥通过罐车输送至烧结料仓5,以0.4%的比例进行烧结配矿至烧结机11;烧结料再通过输送机输送至高炉12,在高炉12经超过1550℃熔融,有益元素被利用,杂质成为高炉12矿渣进行应用。S4. The dried sludge is transported to the sintering silo 5 through a tanker, and sintered and blended to the
实施例9Example 9
本实施例的一种钢厂污泥利用方法,在实施例1-5任一实施例的基础上,包括以下步骤:On the basis of any one of Embodiments 1-5, a method for utilizing sludge in a steel mill of the present embodiment includes the following steps:
S1、将含水量60%的污泥通过翻斗汽车输送至钢厂污泥处理系统,倒入容积为80m3的储存仓1。合上储存仓1进料口,打开污泥出料口,污泥靠重力至储存仓1下部的螺旋输送机,输送至干燥机3;引入280℃的电厂燃煤锅炉余热烟气对污泥进行烘干,余热烟气流量10Wm3/h,烘2小时,烘干过程中,干燥机3旋转,通过搅拌叶片或其它打散装置把大颗粒污泥打散,干燥后的污泥颗粒通过风机6输送至分离器4。S1. The sludge with a water content of 60% is transported to the sludge treatment system of the steel mill through a dump truck, and poured into the storage bin 1 with a volume of 80 m 3 . Close the feeding port of storage bin 1, open the sludge discharge port, and the sludge will be transported to the screw conveyor at the lower part of the storage bin 1 by gravity, and then transported to the dryer 3; Drying is carried out, the residual heat flue gas flow is 10Wm 3 /h, and the drying is performed for 2 hours. During the drying process, the dryer 3 rotates, and the large particles of sludge are dispersed by stirring blades or other dispersing devices, and the dried sludge particles pass through The fan 6 is delivered to the separator 4 .
S2、将干燥完成的污泥以及烟气输送至分离器4中,在分离器4中将干燥后的污泥和烟气进行分离,干燥的污泥进入料仓5,烟气通过管道排出分离器4;分离器4位于料仓5上部,颗粒大小根据需要选择进入分离器4下部的料仓5。分离器4进行分离属于物料的分离,是现有技术。S2. The dried sludge and flue gas are transported to the separator 4, the dried sludge and flue gas are separated in the separator 4, the dried sludge enters the silo 5, and the flue gas is discharged and separated through the pipeline 4; The separation performed by the separator 4 belongs to the separation of materials, which is the prior art.
S3、分离器4排出的烟气经过气体测温仪进行温度的测量,气体测温仪的设定温度为140℃,将干燥机3干燥后的烟气温度为150℃,关闭烟气净化装置9,打开阀门7,烟气通过阀门7和抽气管8回到干燥机3中进行再利用,料仓5内污泥含水量0.8%、平均粒度1.1mm、CaO含量24%。S3. The temperature of the flue gas discharged from the separator 4 is measured by a gas thermometer. The set temperature of the gas thermometer is 140 °C, the temperature of the flue gas after drying by the dryer 3 is 150 °C, and the flue gas purification device is turned off. 9. Open the valve 7, the flue gas is returned to the dryer 3 through the valve 7 and the
S4、烘干后的污泥通过罐车输送至烧结料仓5,以0.3%的比例进行烧结配矿至烧结机11;烧结料再通过输送机输送至高炉12,在高炉12经超过1550℃熔融,有益元素被利用,杂质成为高炉12矿渣进行应用。S4. The dried sludge is transported to the sintering silo 5 through a tanker, and sintered and blended to the
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