CN107488770A - A kind of Coal Grinding System of Pci humidification process and device - Google Patents
A kind of Coal Grinding System of Pci humidification process and device Download PDFInfo
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- 239000003245 coal Substances 0.000 title claims abstract description 45
- 238000000034 method Methods 0.000 title claims abstract description 24
- 238000000227 grinding Methods 0.000 title claims description 9
- 239000007789 gas Substances 0.000 claims abstract description 63
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000003546 flue gas Substances 0.000 claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000002347 injection Methods 0.000 claims abstract description 19
- 239000007924 injection Substances 0.000 claims abstract description 19
- 238000001035 drying Methods 0.000 claims description 23
- 239000008235 industrial water Substances 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 239000000779 smoke Substances 0.000 claims description 2
- 239000000567 combustion gas Substances 0.000 claims 3
- 238000009434 installation Methods 0.000 claims 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 1
- 230000001717 pathogenic effect Effects 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- 238000009692 water atomization Methods 0.000 claims 1
- 238000010298 pulverizing process Methods 0.000 abstract description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 21
- 239000001301 oxygen Substances 0.000 abstract description 21
- 229910052760 oxygen Inorganic materials 0.000 abstract description 21
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 238000005516 engineering process Methods 0.000 abstract description 5
- 230000026676 system process Effects 0.000 abstract description 5
- 238000005272 metallurgy Methods 0.000 abstract description 2
- 230000008030 elimination Effects 0.000 abstract 1
- 238000003379 elimination reaction Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- 230000001105 regulatory effect Effects 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000000889 atomisation Methods 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B5/003—Injection of pulverulent coal
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- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Iron (AREA)
Abstract
本发明属于冶金领域,具体涉及一种高炉喷煤制粉系统加湿工艺及装置。通过设置加湿装置,向待进入磨煤机的干燥气中喷吹雾化水,对干燥气降温,达到降低干燥气中氧气组分浓度的目的。本发明可有效解决现有烟气自循环式制粉系统工艺中因干燥气氧含量超标而停机影响生产的问题,有利于稳定生产、消除安全隐患,不仅具有显著地经济效益和安全可靠的优点,而且还具有工艺简单、技术成熟可靠、易于实现,且投资费用低的特点。
The invention belongs to the field of metallurgy, and in particular relates to a humidification process and device for a coal-injection pulverization system of a blast furnace. By installing a humidifying device, atomized water is sprayed into the dry gas to be entered into the coal mill to cool down the dry gas and achieve the purpose of reducing the concentration of oxygen components in the dry gas. The present invention can effectively solve the problem of production shutdown due to excessive oxygen content in the dry gas in the existing flue gas self-circulating pulverizing system process, which is conducive to stable production and elimination of potential safety hazards, and not only has the advantages of significant economic benefits, safety and reliability , but also has the characteristics of simple process, mature and reliable technology, easy realization, and low investment cost.
Description
技术领域technical field
本发明属于冶金领域,具体涉及一种高炉喷煤制粉系统加湿工艺及装置。The invention belongs to the field of metallurgy, and in particular relates to a humidification process and device for a coal-injection pulverization system of a blast furnace.
背景技术Background technique
高炉喷煤是高炉炼铁工艺以煤代焦、改变高炉燃料结构的重要节能技术,在缓解焦煤资源短缺、降低生铁成本和减轻环境污染起着重要作用,具有显著地经济、环保和社会效益。Blast furnace coal injection is an important energy-saving technology that replaces coke with coal in the blast furnace ironmaking process and changes the fuel structure of the blast furnace. It plays an important role in alleviating the shortage of coking coal resources, reducing the cost of pig iron and reducing environmental pollution, and has significant economic, environmental and social benefits.
高炉喷煤制粉系统是高炉喷煤技术的关键环节,目前国内主要有烟气直排式制粉系统和烟气自循环式制粉系统两种工艺。烟气直排式制粉系统是当前高炉喷煤制粉系统采用的主流工艺,但由于烟气自循环式制粉系统工艺可以有效解决因高炉喷煤车间远离高炉热风炉系统导致废气管道投资高、热风炉废气量不足或者受炼铁厂场地限制而无法使用烟气直排式制粉系统的问题,所以目前在国内钢铁厂已逐步得到推广应用。Blast furnace coal injection pulverization system is the key link of blast furnace coal injection technology. At present, there are mainly two technologies in China: flue gas direct exhaust pulverization system and flue gas self-circulation pulverization system. The flue gas direct exhaust pulverizing system is the mainstream technology adopted by the blast furnace coal injection pulverizing system at present, but the flue gas self-circulation pulverizing system process can effectively solve the high investment in waste gas pipelines caused by the fact that the blast furnace coal injection workshop is far away from the blast furnace hot blast stove system , Insufficient amount of exhaust gas from hot blast stoves or the inability to use the flue gas direct exhaust pulverizing system due to the limitation of the ironworks site, so it has been gradually popularized and applied in domestic iron and steel plants.
烟气自循环式制粉系统是一种通过烟气炉燃烧高炉煤气生成的高温烟气与自循环烟气混合生成温度在200℃~300℃之间、氧含量≤8%的干燥气来干燥磨煤机研磨煤粉的工艺。其中,烟气炉燃烧高炉煤气生成的高温烟气,其主要成分为CO2和N2,温度为900℃~1100℃,具有高温、低含氧量(≤2%)等特点,是良好的高温、惰性加热气体,在干燥气中占比为30%~45%;自循环烟气是惰性干燥气经布袋除尘器和主排烟风机等设备完成气粉分离后的尾气,其主要成分为水蒸汽、CO2和N2,温度为85℃左右,具有低温、较低含氧量(10%~12%)等特点,是高温烟气良好的温度调节介质,在干燥气中占比为55%~70%。该工艺的关键指标之一是系统惰性干燥气的氧含量,该指标已成为此工艺能否正常安全生产的限制性因素。根据国家标准《高炉喷吹煤粉工程设计规范》(GB50607-2010)强制条文规定:在系统工况下惰性干燥气的最高允许氧含量≤12%,该条文的目的是为了避免制粉系统中的煤粉因氧含量超标而发生爆炸的可能,保证系统运行安全,杜绝人员伤亡等事故发生。The flue gas self-circulation pulverizing system is a kind of drying gas with a temperature between 200°C and 300°C and an oxygen content of ≤8% by mixing high-temperature flue gas generated by burning blast furnace gas in a flue gas furnace and self-circulating flue gas. Coal pulverizer is the process of grinding coal powder. Among them, the high-temperature flue gas generated by burning blast furnace gas in the flue gas furnace is mainly composed of CO 2 and N 2 , and the temperature is 900°C to 1100°C. It has the characteristics of high temperature and low oxygen content (≤2%), and is a good choice. High-temperature, inert heating gas accounts for 30% to 45% of the dry gas; self-circulating flue gas is the tail gas of the inert dry gas after the gas-powder separation is completed by equipment such as bag filter and main exhaust fan, and its main components are Water vapor, CO 2 and N 2 , with a temperature of about 85°C, have the characteristics of low temperature and low oxygen content (10%-12%), and are good temperature-regulating media for high-temperature flue gas, and their proportion in dry gas is 55% to 70%. One of the key indicators of this process is the oxygen content of the system's inert drying gas, which has become a limiting factor for the normal and safe production of this process. According to the mandatory provisions of the national standard "Code for Design of Blast Furnace Injection Coal Pulverized Engineering" (GB50607-2010): the maximum allowable oxygen content of the inert dry gas under system conditions is ≤12%. The pulverized coal may explode due to excessive oxygen content, ensuring the safe operation of the system and preventing accidents such as casualties.
但是由于烟气自循环式制粉系统工艺循环使用部分系统尾气(自循环烟气)作为磨煤机惰性干燥气的气源,而干燥气中的氧气组分浓度因循环使用逐步富集,故易产生干燥气具有较高氧含量的问题。与此同时,由于制粉系统的磨煤机、给煤机和布袋收粉器等设备以及管道连接法兰处均无法避免的存在不同程度的漏风现象(漏风率>8%),进一步加剧了干燥气氧含量升高的问题,故在生产中经常会出现干燥气氧含量超标而停机的问题,从而影响企业正常生产。因此,降低烟气自循环式制粉系统的惰性干燥气氧含量,对于保障企业正常安全生产和降低其经济损失至关重要,但目前有关此问题的技术解决方案在行业内却鲜有报道。However, because the flue gas self-circulation pulverizing system process uses part of the system tail gas (self-circulation flue gas) as the gas source of the inert drying gas of the coal mill, and the concentration of oxygen components in the drying gas is gradually enriched due to recycling, so It is easy to produce the problem that the dry gas has a high oxygen content. At the same time, due to the unavoidable air leakage of different degrees (air leakage rate > 8%) in equipment such as coal mills, coal feeders, and bag powder collectors in the pulverization system, as well as at the pipe connection flanges, the air leakage rate is further exacerbated. Oxygen content of dry gas rises. Therefore, in production, the oxygen content of dry gas exceeds the standard and the shutdown problem often occurs, which affects the normal production of the enterprise. Therefore, reducing the oxygen content of the inert dry gas in the flue gas self-circulating pulverizing system is very important to ensure the normal and safe production of enterprises and reduce their economic losses, but there are few reports on the technical solutions to this problem in the industry.
发明内容Contents of the invention
有鉴于此,本发明的目的在于提供一种高炉喷煤制粉系统加湿工艺及装置,以解决现有烟气自循环式制粉系统工艺惰性干燥气氧含量超标的问题。In view of this, the object of the present invention is to provide a blast furnace coal-injection pulverization system humidification process and device to solve the problem of excessive oxygen content in the inert dry gas of the existing flue gas self-circulating pulverization system process.
为达到上述目的,本发明提供如下技术方案:一种高炉喷煤制粉系统加湿工艺,在烟气炉烟气出口与磨煤机烟气入口间的干燥气管道上至少连通一路加湿装置,控制加湿装置向干燥气管道内喷吹雾化水的喷吹量,增大并调节烟气炉中高炉煤气燃烧生成的烟气量,降低并调节自循环烟气量。In order to achieve the above purpose, the present invention provides the following technical solutions: a humidification process for the blast furnace coal injection pulverization system, at least one humidification device is connected to the dry gas pipeline between the flue gas outlet of the flue gas furnace and the flue gas inlet of the coal mill to control the humidification The device sprays the injection amount of atomized water into the drying gas pipeline, increases and adjusts the amount of flue gas generated by the combustion of blast furnace gas in the flue gas furnace, and reduces and adjusts the amount of self-circulating flue gas.
进一步,雾化水为液态工业水雾化生成,雾化粒径为1μm~5μm。Further, the atomized water is generated by atomizing liquid industrial water, and the atomized particle size is 1 μm to 5 μm.
进一步,液态工业水水质要求悬浮物含量≤50mg/L,PH值为6.5~9,碳酸盐硬度≤140mg/L。Further, the water quality of liquid industrial water requires that the suspended matter content is ≤50mg/L, the pH value is 6.5-9, and the carbonate hardness is ≤140mg/L.
进一步,雾化水加压喷入干燥气管道内。Further, atomized water is pressurized and sprayed into the drying gas pipeline.
一种高炉喷煤制粉系统加湿装置,包括通过管道依次连接的供水装置、雾化装置及加压器,所述加压器通过加湿管道与连接在烟气炉烟气出口及磨煤机烟气入口间的干燥气管道相连通。A humidification device for a blast furnace coal injection pulverization system, including a water supply device, an atomization device, and a pressurizer connected in sequence through pipelines, and the pressurizer is connected to the flue gas outlet of the flue gas furnace and the coal mill smoke through the humidification pipeline. The dry gas pipelines between the gas inlets are connected.
进一步,还包括依次设置在供水装置与雾化装置之间的流量传感器及流量调节阀。Further, it also includes a flow sensor and a flow regulating valve sequentially arranged between the water supply device and the atomizing device.
进一步,所述加湿装置有多路,依次并联在干燥气管道上。Further, the humidifying device has multiple paths, which are sequentially connected in parallel to the dry gas pipeline.
本发明的有益效果在于:The beneficial effects of the present invention are:
1)可以有效解决现有烟气自循环式制粉系统工艺中因干燥气氧含量超标而停机影响生产的问题,有利于稳定生产,具有显著地经济效益;1) It can effectively solve the problem of production shutdown due to excessive oxygen content in the dry gas in the existing flue gas self-circulating pulverizing system process, which is conducive to stable production and has significant economic benefits;
2)可实现实时调控,从而将系统惰性干燥气氧含量严格控制在国家标准规定值12%以内,有效地保障了系统运行的安全性,消除了安全隐患,因而具有安全可靠的优点;2) It can realize real-time regulation, so that the oxygen content of the inert dry gas in the system can be strictly controlled within 12% of the national standard value, which effectively guarantees the safety of the system operation and eliminates potential safety hazards, so it has the advantages of safety and reliability;
3)烟气自循环式制粉系统采用加湿工艺,工艺简单、技术成熟可靠、易于实现;3) The flue gas self-circulating pulverizing system adopts a humidification process, which is simple, mature and reliable, and easy to implement;
4)加湿装置组成简单,可对现有设备进行改进,投资费用低。4) The composition of the humidifying device is simple, the existing equipment can be improved, and the investment cost is low.
附图说明Description of drawings
为了使本发明的目的、技术方案和有益效果更加清楚,本发明提供如下附图进行说明:In order to make the purpose, technical scheme and beneficial effect of the present invention clearer, the present invention provides the following drawings for illustration:
图1为本发明的示意图。Figure 1 is a schematic diagram of the present invention.
具体实施方式detailed description
下面将结合附图,对本发明的优选实施例进行详细的描述。The preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
如图所示,高炉喷煤制粉系统包括原煤仓11、给煤机10、烟气炉1、磨煤机9、布袋收粉器12以及主排烟风机13。本实施例中的高炉喷煤制粉系统中有加湿装置,包括通过管道依次连接的供水装置3、雾化装置6及加压器7,所述加压器7通过加湿管道8与连接在烟气炉1烟气出口及磨煤机9烟气入口间的干燥气管道2相连通。雾化装置6可将供水装置3中的液态工业水生成雾化水,加压器7则将雾化水加压后引入干燥气管道2中。As shown in the figure, the blast furnace coal injection pulverization system includes a raw coal bunker 11, a coal feeder 10, a flue gas furnace 1, a coal mill 9, a bag powder collector 12 and a main exhaust fan 13. The blast furnace coal injection pulverization system in this embodiment has a humidification device, including a water supply device 3, an atomization device 6, and a pressurizer 7 connected in sequence through pipelines. The pressurizer 7 is connected to the fume The dry gas pipeline 2 between the flue gas outlet of the gas furnace 1 and the flue gas inlet of the coal mill 9 is connected. The atomizing device 6 can generate atomized water from the liquid industrial water in the water supply device 3 , and the pressurizer 7 can pressurize the atomized water and introduce it into the drying gas pipeline 2 .
本实施例中还包括依次设置在供水装置3与雾化装置6之间的流量传感器4及流量调节阀5。流量传感器4及流量调节阀5用于实现流量串级控制回路反馈,可实时监测并调节流量,达到控制雾化水喷入量的目的。This embodiment also includes a flow sensor 4 and a flow regulating valve 5 sequentially arranged between the water supply device 3 and the atomizing device 6 . The flow sensor 4 and the flow regulating valve 5 are used to realize flow cascade control loop feedback, which can monitor and adjust the flow in real time, so as to achieve the purpose of controlling the injection amount of atomized water.
作为上述方案的进一步改进,所述加湿装置有多路,依次并联在干燥气管道2上。即可作为备用降温线路,又可同时开启实现精准调控。As a further improvement of the above solution, the humidification device has multiple channels, which are sequentially connected to the dry gas pipeline 2 in parallel. It can be used as a backup cooling circuit, and can be turned on at the same time to achieve precise regulation.
具体过程为:将供水装置3中的液态工业水经雾化装置6生成雾化水后,通过管道引至加压器7内,加压至工艺所需要的压力,然后通过加湿管道8将雾化水引入干燥气管道2内,利用流量调节阀5和流量传感器4对加湿量进行调节,以获得满足工艺要求的低氧含量干燥气。合格的干燥气借助于制粉系统中的主排烟风机13的抽力被引入磨煤机9,磨煤机9对来自于原煤仓11和给煤机10的原煤碾磨,干燥气对碾磨合格的煤粉进行干燥和输送,质量合格的煤粉经输送管道送入布袋收粉器12内,通过布袋收粉器12进行气—粉分离,煤粉进入喷吹系统,干燥气经主排烟风机13向高空排放,其中部分尾气再进入烟气炉1循环利用。The specific process is: after the liquid industrial water in the water supply device 3 passes through the atomization device 6 to generate atomized water, it is led to the pressurizer 7 through the pipeline, pressurized to the pressure required by the process, and then the mist is discharged through the humidification pipeline 8. The chemical water is introduced into the drying gas pipeline 2, and the humidification amount is adjusted by the flow regulating valve 5 and the flow sensor 4, so as to obtain the low oxygen content drying gas that meets the process requirements. The qualified dry gas is introduced into the coal mill 9 by means of the suction force of the main exhaust fan 13 in the pulverizing system. The coal mill 9 grinds the raw coal from the raw coal bunker 11 and the coal feeder 10, and the dry gas Qualified pulverized coal is dried and transported, and pulverized coal with qualified quality is sent into the bag powder collector 12 through the conveying pipeline, and the gas-powder separation is carried out through the bag powder collector 12, and the pulverized coal enters the injection system, and the drying gas passes through the main The exhaust fan 13 discharges to the high altitude, and part of the exhaust gas enters the flue gas furnace 1 for recycling.
高炉喷煤制粉系统的加湿工艺,在烟气炉1烟气出口与磨煤机9烟气入口间的干燥气管道2上至少连通一路加湿装置,控制加湿装置向干燥气管道2内喷吹雾化水的喷吹量,增大并调节烟气炉1中高炉煤气燃烧生成的烟气量,降低并调节自循环烟气量。In the humidification process of the blast furnace coal injection pulverization system, at least one humidification device is connected to the dry gas pipeline 2 between the flue gas outlet of the flue gas furnace 1 and the flue gas inlet of the coal mill 9, and the humidification device is controlled to spray into the dry gas pipeline 2 The injection amount of atomized water increases and adjusts the amount of flue gas generated by the combustion of blast furnace gas in the flue gas furnace 1, and reduces and adjusts the amount of self-circulating flue gas.
具体的,雾化水为液态工业水经雾化装置6雾化生成,生成由加压器7加压至工艺所需压力,后通过加湿管道8喷入干燥器管道内。雾化粒径控制在1μm~5μm间。液态工业水水质要求悬浮物含量≤50mg/L,PH值为6.5~9,碳酸盐硬度≤140mg/L。Specifically, the atomized water is produced by atomizing liquid industrial water through the atomizing device 6 , pressurized by the pressurizer 7 to the pressure required by the process, and then sprayed into the dryer pipeline through the humidifying pipeline 8 . The atomized particle size is controlled between 1 μm and 5 μm. The water quality of liquid industrial water requires that the suspended matter content is ≤50mg/L, the pH value is 6.5-9, and the carbonate hardness is ≤140mg/L.
该工艺通过将颗粒尺寸为1μm~5μm的细粒雾化水通入干燥气中,减少了干燥气中自循环烟气用量,从而实现了降低干燥气中氧气组分浓度的目的。具体原因在于:一方面,由于雾化水具有单个颗粒体积小、表面积大、易汽化、吸热快的特点,可以迅速将干燥气的热量带走,从而降低干燥气温度,故为弥补干燥气因雾化水汽化所产生的温差,烟气炉需要多烧高炉煤气提高高温烟气量的供应,同时减少自循环烟气量,以维持干燥气温度,使其满足工艺要求;另一方面,由于雾化水因吸热汽化由液态变为气态,提高了干燥气中水蒸汽的体积比例,同时减少了干燥气中自循环烟气用量,因而相应地稀释了干燥气中氧气组分的浓度,降低了干燥气中氧气组分的体积比例,从而实现了降低干燥气氧含量的目的。The process reduces the amount of self-circulating flue gas in the drying gas by passing the fine-grained atomized water with a particle size of 1 μm to 5 μm into the drying gas, thereby achieving the purpose of reducing the concentration of oxygen components in the drying gas. The specific reasons are: on the one hand, because the atomized water has the characteristics of small single particle size, large surface area, easy vaporization, and fast heat absorption, it can quickly take away the heat of the drying gas, thereby reducing the temperature of the drying gas. Due to the temperature difference caused by the vaporization of atomized water, the flue gas furnace needs to burn more blast furnace gas to increase the supply of high-temperature flue gas, and at the same time reduce the amount of self-circulating flue gas to maintain the temperature of the drying gas to meet the process requirements; on the other hand, Since the atomized water changes from a liquid state to a gaseous state due to heat absorption and vaporization, the volume ratio of water vapor in the drying gas is increased, and the amount of self-circulating flue gas in the drying gas is reduced, thereby diluting the concentration of oxygen components in the drying gas accordingly. , reducing the volume ratio of the oxygen component in the drying gas, thereby achieving the purpose of reducing the oxygen content of the drying gas.
最后说明的是,以上优选实施例仅用以说明本发明的技术方案而非限制,尽管通过上述优选实施例已经对本发明进行了详细的描述,但本领域技术人员应当理解,可以在形式上和细节上对其作出各种各样的改变,而不偏离本发明权利要求书所限定的范围。Finally, it should be noted that the above preferred embodiments are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention has been described in detail through the above preferred embodiments, those skilled in the art should understand that it can be described in terms of form and Various changes may be made in the details without departing from the scope of the invention defined by the claims.
Claims (7)
- A kind of 1. Coal Grinding System of Pci humidification process, it is characterised in that:Enter in combustion gas furnace exhanst gas outlet and coal pulverizer flue gas Humidification device all the way is at least connected in drying feed channel between mouthful, control humidification device is blown atomized water into dry feed channel Injection amount, increase and adjust the exhaust gas volumn that blast furnace gas combustion generates in combustion gas furnace, reduce and adjust self-loopa exhaust gas volumn.
- 2. Coal Grinding System of Pci humidification process according to claim 1, it is characterised in that:Atomized water is liquid-state industrial Water atomization generates, and atomizing particle size is 1 μm~5 μm.
- 3. Coal Grinding System of Pci humidification process according to claim 2, it is characterised in that:Liquid-state industrial water water quality will Suspension content≤50mg/L is sought, pH value is 6.5~9, carbonate hardness≤140mg/L.
- 4. Coal Grinding System of Pci humidification process according to claim 1, it is characterised in that:Atomized water pressurization sprays into dry In pathogenic dryness pipeline.
- 5. a kind of humidification device for being applied to the Coal Grinding System of Pci humidification process as described in any one of Claims 1 to 4, It is characterized in that:Including the water supply installation, atomising device and pressurizer being sequentially connected by pipeline, the pressurizer passes through humidification Pipeline is connected with the drying feed channel being connected between combustion gas furnace exhanst gas outlet and coal pulverizer smoke inlet.
- 6. Coal Grinding System of Pci humidification device according to claim 5, it is characterised in that:Also include being successively set on Flow sensor and flow control valve between water supply installation and atomising device.
- 7. Coal Grinding System of Pci humidification device according to claim 6, it is characterised in that:The humidification device has more Road, it is connected in parallel on successively in dry feed channel.
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