CN211056972U - Phosphogypsum roasting system - Google Patents

Phosphogypsum roasting system Download PDF

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CN211056972U
CN211056972U CN201922013910.4U CN201922013910U CN211056972U CN 211056972 U CN211056972 U CN 211056972U CN 201922013910 U CN201922013910 U CN 201922013910U CN 211056972 U CN211056972 U CN 211056972U
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phosphogypsum
roasting
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dust remover
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李进
高晔
高振华
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Hubei Huangmailing Posphorus Chemical Co ltd
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Abstract

一种磷石膏焙烧系统,包括焙烧炉,焙烧炉设有进料口和出料口,出料口处设有成品运输装置,成品运输装置将成品运输到成品仓;焙烧炉底部设有燃烧器,燃烧器为焙烧炉提供热源,焙烧炉顶部通过管道与除尘器连通,除尘器为多级除尘器,除尘器至少包括两级出料口,除尘器的一级出料口通过第一运输机与进料口连通,除尘器的二级出料口通过第二运输机与成品运输装置入口连通。本系统能够收集磷石膏粉末粉尘,提高成品率,还能够提高成品质量。

Figure 201922013910

A phosphogypsum roasting system comprises a roasting furnace, the roasting furnace is provided with a feeding port and a discharging port, a finished product transport device is arranged at the discharging port, and the finished product transport device transports the finished product to a finished product warehouse; a burner is provided at the bottom of the roasting furnace , the burner provides a heat source for the roaster, the top of the roaster is connected to the dust collector through a pipeline, the dust collector is a multi-stage dust collector, the dust collector at least includes two-stage discharge ports, and the first-stage discharge port of the dust collector is connected to the first conveyor through the first conveyor. The feeding port is connected, and the secondary discharge port of the dust collector is communicated with the inlet of the finished product conveying device through the second conveyor. The system can collect phosphogypsum powder dust, improve the yield of finished products, and also improve the quality of finished products.

Figure 201922013910

Description

磷石膏焙烧系统Phosphogypsum Roasting System

技术领域technical field

本实用新型属于磷石膏制造工艺领域,特别涉及一种磷石膏焙烧系统。The utility model belongs to the field of phosphogypsum manufacturing technology, in particular to a phosphogypsum roasting system.

背景技术Background technique

磷石膏是生产磷肥、磷酸时排放出的固体废弃物,随着对磷石膏的开发利用,目前石膏粉可用于建筑装修工程以及制作装饰制品和石膏板等;随着全国范围内即将禁用粘土砖,石膏墙体应用的市场空间会更大。建筑石膏作为各类石膏制品的基础原料,其需求市场是巨大的;磷石膏速成墙板可广泛应用于各种工业和民用建筑。Phosphogypsum is a solid waste discharged from the production of phosphate fertilizers and phosphoric acid. With the development and utilization of phosphogypsum, gypsum powder can be used in building decoration projects and the production of decorative products and gypsum boards. With the impending ban of clay bricks nationwide , the market space for gypsum wall applications will be larger. As the basic raw material of various gypsum products, building gypsum has a huge demand market; phosphogypsum instant wallboard can be widely used in various industrial and civil buildings.

而磷石膏需要经过焙烧工艺,将半湿式的磷石膏物料焙烧成干式磷石膏粉末成品,然后对外销售。现有的磷石膏焙烧工艺,容易产生磷石膏粉末的浪费,成品率不高。The phosphogypsum needs to go through a roasting process, and the semi-wet phosphogypsum material is roasted into a dry phosphogypsum powder product, which is then sold to the outside world. The existing phosphogypsum roasting process is prone to waste of phosphogypsum powder, and the yield is not high.

发明内容SUMMARY OF THE INVENTION

鉴于背景技术所存在的技术问题,本实用新型所提供的磷石膏焙烧系统,能够收集磷石膏粉末粉尘,提高成品率,还能够提高成品质量。In view of the technical problems existing in the background art, the phosphogypsum roasting system provided by the utility model can collect phosphogypsum powder dust, improve the yield of finished products, and also improve the quality of finished products.

为了解决上述技术问题,本实用新型采取了如下技术方案来实现:In order to solve the above-mentioned technical problems, the utility model adopts the following technical solutions to realize:

一种磷石膏焙烧系统,包括焙烧炉,焙烧炉设有进料口和出料口,出料口处设有成品运输装置,成品运输装置将成品运输到成品仓;焙烧炉底部设有燃烧器,燃烧器为焙烧炉提供热源,焙烧炉顶部通过管道与除尘器连通,除尘器为多级除尘器,除尘器至少包括两级出料口,除尘器的一级出料口通过第一运输机与进料口连通,除尘器的二级出料口通过第二运输机与成品运输装置入口连通。A phosphogypsum roasting system includes a roasting furnace, the roasting furnace is provided with a feeding port and a discharging port, a finished product transport device is arranged at the discharging port, and the finished product transport device transports the finished product to a finished product warehouse; a burner is provided at the bottom of the roasting furnace , the burner provides a heat source for the roaster, the top of the roaster is connected to the dust collector through a pipeline, the dust collector is a multi-stage dust collector, the dust collector at least includes two-stage discharge ports, and the first-stage discharge port of the dust collector is connected to the first conveyor through the first conveyor. The feed port is connected, and the secondary discharge port of the dust collector is communicated with the inlet of the finished product conveying device through the second conveyor.

优选的方案中,所述的燃烧器为直燃式热风炉,直燃式热风炉由风机提供风源。In a preferred solution, the burner is a direct-fired hot blast stove, and the direct-fired hot blast stove is provided with an air source by a fan.

优选的方案中,所述的除尘器为两级布袋式除尘器。In a preferred solution, the dust collector is a two-stage bag filter.

优选的方案中,所述的两级布袋式除尘器设有进风口和出风口,进风口通过管道与焙烧炉顶部连通,出风口与尾气净化装置连通。In a preferred solution, the two-stage bag filter is provided with an air inlet and an air outlet, the air inlet is communicated with the top of the roaster through a pipeline, and the air outlet is communicated with the exhaust gas purification device.

优选的方案中,所述的尾气净化装置为喷淋吸收塔。In a preferred solution, the tail gas purification device is a spray absorption tower.

优选的方案中,所述的成品运输装置与成品仓之间设有筛分装置,筛分装置的入口与成品运输装置连通,筛分装置的出口与成品仓连通,筛分装置的返料口与焙烧炉的进料口连通。In a preferred solution, a screening device is provided between the finished product transport device and the finished product warehouse, the inlet of the screening device is connected with the finished product transport device, the outlet of the screening device is communicated with the finished product warehouse, and the material return port of the screening device It communicates with the feed port of the roaster.

本专利可达到以下有益效果:This patent can achieve the following beneficial effects:

将需要焙烧的半湿式磷石膏投入至焙烧炉进行焙烧,燃烧器提供热源,将半湿式磷石膏进行烘干,一部分磷石膏粉尘随热气会进入至除尘器,除尘器第一级出料口收集到的物料粉尘颗粒比较大,该物料粉尘可以继续返回至焙烧炉继续焙烧;其他级的出料口将粉尘物料运输至成品运输装置。该工艺可避免石膏粉尘的浪费,提高了成品率。Put the semi-wet phosphogypsum to be roasted into the roasting furnace for roasting, the burner provides a heat source, and the semi-wet phosphogypsum is dried. The dust particles of the received materials are relatively large, and the dust of the materials can be continuously returned to the roasting furnace for continuous roasting; the discharge ports of other levels transport the dust materials to the finished product transport device. The process can avoid the waste of gypsum dust and improve the yield.

本技术方案为了保证磷石膏粉的质量,增设了筛分装置,从而对磷石膏粉进行筛选,合格的磷石膏粉由成品运输装置运输至成品仓,不合格的磷石膏粉进入至焙烧炉继续焙烧。进一步提高了成品质量。In order to ensure the quality of phosphogypsum powder in this technical scheme, a screening device is added to screen the phosphogypsum powder. The qualified phosphogypsum powder is transported to the finished product warehouse by the finished product transportation device, and the unqualified phosphogypsum powder enters the roasting furnace to continue. Roasting. Further improve the quality of finished products.

附图说明Description of drawings

下面结合附图和实施例对本实用新型作进一步说明:Below in conjunction with accompanying drawing and embodiment, the utility model is further described:

图1为本实用新型系统结构图。Fig. 1 is the system structure diagram of the utility model.

图中:焙烧炉1、进料口101、出料口102、燃烧器2、风机201、除尘器3、第一运输机41、第二运输机42、成品运输装置5、尾气净化装置6、成品仓7、筛分装置8、返料运输机9 。In the figure: roaster 1, feed port 101, discharge port 102, burner 2, fan 201, dust collector 3, first conveyor 41, second conveyor 42, finished product transport device 5, exhaust gas purification device 6, finished product warehouse 7. Screening device 8, return conveyor 9.

具体实施方式Detailed ways

优选的方案如图1所示,一种磷石膏焙烧系统,包括焙烧炉1,焙烧炉1设有进料口101和出料口102,出料口102处设有成品运输装置5,成品运输装置5将成品运输到成品仓7;焙烧炉1底部设有燃烧器2,燃烧器2为焙烧炉1提供热源,焙烧炉1顶部通过管道与除尘器3连通,除尘器3为多级除尘器,除尘器3至少包括两级出料口,除尘器3的一级出料口通过第一运输机41与进料口101连通,除尘器3的二级出料口通过第二运输机42与成品运输装置5入口连通。本技术方案中采用除尘器3,其主要目的并不是为了除尘,而是为了收集焙烧炉1中的物料粉尘。一部分颗粒比较大的物料粉尘重新回到焙烧炉1进行焙烧,而颗粒小的物料粉尘则收集到成品运输装置5内运输。A preferred solution is shown in Fig. 1, a phosphogypsum roasting system includes a roasting furnace 1, the roasting furnace 1 is provided with a feeding port 101 and a discharging port 102, and a finished product transportation device 5 is arranged at the discharging port 102, and the finished product is transported The device 5 transports the finished product to the finished product warehouse 7; the bottom of the roasting furnace 1 is provided with a burner 2, the burner 2 provides a heat source for the roasting furnace 1, and the top of the roasting furnace 1 is communicated with the dust collector 3 through a pipeline, and the dust collector 3 is a multi-stage dust collector , the dust collector 3 includes at least two-stage discharge ports, the first-level discharge port of the dust collector 3 is communicated with the feed port 101 through the first conveyor 41, and the second-level discharge port of the dust collector 3 is transported with the finished product through the second conveyor 42 The inlet of the device 5 is connected. In this technical solution, the dust collector 3 is used, and its main purpose is not to remove dust, but to collect the material dust in the roasting furnace 1 . A part of the material dust with relatively large particles is returned to the roasting furnace 1 for roasting, while the material dust with small particles is collected in the finished product transport device 5 for transportation.

进一步地,燃烧器2为直燃式热风炉,直燃式热风炉由风机201提供风源。直燃式热风炉的工作原理为:直燃式热风炉由燃煤机、高温气体净化沉降室和混风室组成,煤通过上煤机加入到燃煤机的煤斗中,煤由链条炉排匀速送入燃烧室,在鼓风机鼓入的空气作用下剧烈燃烧,燃煤所产生的含尘高温烟气进入高温气体净化沉降室;高温气体净化沉降室由耐火材料砌筑而成,高温烟气在净化室内进行二次燃烧,烟气中所夹带的少量粉尘在净化室内经高温聚合沉降;净化室内出来的洁净热风掺入一定量的冷风,能够提供不同温度的洁净热烟气,可为各类大型焙烧系统如流化床、闪蒸、喷雾塔、回转圆筒、烘房、气流干燥器等提供热源,并对物料进行烘干,直燃式热风炉的热利用率高,可以降低整个装置的成本。Further, the burner 2 is a direct-fired hot blast stove, and the direct-fired hot blast stove is provided with an air source by a fan 201 . The working principle of the direct-fired hot blast stove is as follows: the direct-fired hot blast stove is composed of a coal burner, a high temperature gas purification sedimentation chamber and a mixed air chamber. The exhaust is sent into the combustion chamber at a uniform speed, and it is violently burned under the action of the air blown by the blower. The dusty high-temperature flue gas generated by the coal combustion enters the high-temperature gas purification and settling chamber; the high-temperature gas purification and settling chamber is made of refractory materials. The gas undergoes secondary combustion in the purification room, and a small amount of dust entrained in the flue gas is polymerized and precipitated at high temperature in the purification room; the clean hot air from the purification room is mixed with a certain amount of cold air, which can provide clean hot flue gas of different temperatures, which can be used for cleaning. Various large-scale roasting systems such as fluidized bed, flash evaporation, spray tower, rotary cylinder, drying room, air dryer, etc. provide heat sources, and dry the materials. The direct-fired hot blast stove has high heat utilization rate and can reduce the cost of the entire installation.

进一步地,除尘器3为两级布袋式除尘器。布袋式除尘器是一种干式滤尘装置。它适用于捕集细小、干燥、非纤维性粉尘。滤袋采用纺织的滤布或非纺织的毡制成,利用纤维织物的过滤作用对含尘气体进行过滤,当含尘气体进入袋式除尘器后,颗粒大、比重大的粉尘,由于重力的作用沉降下来,落入灰斗。因为布袋式除尘器的大小规格有很多种,出料口的个数包括一个或多个,本技术方案选择的布袋式除尘器,其出料口至少为两个。两级布袋式除尘器设有进风口和出风口,进风口通过管道与焙烧炉1顶部连通,出风口与尾气净化装置6连通。靠近进风口处的出料口,其收集到的物料粉尘颗粒比较大,该物料粉尘可以继续返回至焙烧炉1继续焙烧。Further, the dust collector 3 is a two-stage bag filter. The bag filter is a dry dust filter. It is suitable for capturing fine, dry, non-fibrous dust. The filter bag is made of woven filter cloth or non-woven felt, and the dust-containing gas is filtered by the filtering effect of the fiber fabric. The action settles down and falls into the ash hopper. Because there are many sizes and specifications of bag-type dust collectors, and the number of discharge ports includes one or more, the bag-type dust collector selected in this technical solution has at least two discharge ports. The two-stage bag filter is provided with an air inlet and an air outlet, the air inlet communicates with the top of the roasting furnace 1 through a pipeline, and the air outlet communicates with the exhaust gas purification device 6 . The material dust particles collected at the discharge port near the air inlet are relatively large, and the material dust can continue to be returned to the roasting furnace 1 to continue roasting.

进一步地,尾气净化装置6为喷淋吸收塔。磷石膏制造过程中,会产生酸性有毒有害的尾气,喷淋吸收塔主要是利用碱液对尾气进行中和反应,从而起到净化的目的。Further, the exhaust gas purification device 6 is a spray absorption tower. In the production process of phosphogypsum, acidic, toxic and harmful exhaust gas will be generated. The spray absorption tower mainly uses lye to neutralize the exhaust gas, so as to achieve the purpose of purification.

进一步地,成品运输装置5与成品仓7之间设有筛分装置8,筛分装置8的入口与成品运输装置5连通,筛分装置8的出口与成品仓7连通,筛分装置8的返料口与焙烧炉1的进料口101连通。筛分装置8能够筛分出合格的磷石膏粉,筛分装置8一般采用超声波振动筛分机。Further, a screening device 8 is provided between the finished product transport device 5 and the finished product warehouse 7, the inlet of the screening device 8 is communicated with the finished product transport device 5, the outlet of the screening device 8 is communicated with the finished product warehouse 7, and the The material returning port is communicated with the feeding port 101 of the roasting furnace 1 . The screening device 8 can screen out qualified phosphogypsum powder, and the screening device 8 generally adopts an ultrasonic vibration screening machine.

整个装置的工作原理如下:The whole device works as follows:

将需要焙烧的半湿式磷石膏投入至焙烧炉1进行焙烧,燃烧器2提供热源,将半湿式磷石膏进行烘干,一部分磷石膏粉尘会进入至除尘器3,颗粒大的磷石膏粉尘更容易被收集。两级布袋式除尘器设有进风口和出风口,进风口通过管道与焙烧炉1顶部连通,出风口与尾气净化装置6连通。靠近进风口处的出料口,其收集到的物料粉尘颗粒比较大,该物料粉尘可以继续返回至焙烧炉1继续焙烧;布袋式除尘器其他的出料口将粉尘物料运输至成品运输装置5。本技术方案为了保证磷石膏粉的质量,增设了筛分装置8,从而对磷石膏粉进行筛选,合格的磷石膏粉由成品运输装置5运输至成品仓,不合格的磷石膏粉进入至焙烧炉继续焙烧。本技术方中的第一运输机41、第二运输机42和成品运输装置5均可采用螺旋式运输机。筛分装置8返料口处的返料运输机9可旋转斗提式运输机,将不合格的物料返送至焙烧炉1。The semi-wet phosphogypsum that needs to be roasted is put into the roasting furnace 1 for roasting, the burner 2 provides a heat source, and the semi-wet phosphogypsum is dried. is collected. The two-stage bag filter is provided with an air inlet and an air outlet, the air inlet communicates with the top of the roasting furnace 1 through a pipeline, and the air outlet communicates with the exhaust gas purification device 6 . The material dust particles collected by the discharge port near the air inlet are relatively large, and the material dust can continue to be returned to the roasting furnace 1 for continuous roasting; other discharge ports of the bag filter transport the dust material to the finished product transport device 5 . In this technical scheme, in order to ensure the quality of phosphogypsum powder, a screening device 8 is added to screen the phosphogypsum powder. The qualified phosphogypsum powder is transported by the finished product transportation device 5 to the finished product warehouse, and the unqualified phosphogypsum powder enters the roasting process. The furnace continues to roast. The first conveyor 41 , the second conveyor 42 and the finished product transportation device 5 in the technical method can all use screw conveyors. The return conveyor 9 at the return port of the screening device 8 can rotate the bucket conveyor to return the unqualified materials to the roasting furnace 1 .

Claims (6)

1. A phosphogypsum roasting system comprises a roasting furnace (1), wherein the roasting furnace (1) is provided with a feeding hole (101) and a discharging hole (102), a finished product conveying device (5) is arranged at the discharging hole (102), and the finished product conveying device (5) conveys a finished product to a finished product bin (7); roaster (1) bottom is equipped with combustor (2), and combustor (2) provide the heat source for roaster (1), its characterized in that: the top of the roasting furnace (1) is communicated with the dust remover (3) through a pipeline, the dust remover (3) is a multi-stage dust remover, the dust remover (3) at least comprises two-stage discharge holes, the one-stage discharge hole of the dust remover (3) is communicated with the feed inlet (101) through a first conveyor (41), and the two-stage discharge hole of the dust remover (3) is communicated with the inlet of the finished product conveying device (5) through a second conveyor (42).
2. The phosphogypsum roasting system according to claim 1, characterized in that: the burner (2) is a direct-combustion hot blast stove which is provided with an air source by a fan (201).
3. The phosphogypsum roasting system according to claim 2, characterized in that: the dust remover (3) is a two-stage cloth bag type dust remover.
4. The phosphogypsum roasting system according to claim 3, characterized in that: the two-stage bag type dust collector is provided with an air inlet and an air outlet, the air inlet is communicated with the top of the roasting furnace (1) through a pipeline, and the air outlet is communicated with the tail gas purification device (6).
5. The phosphogypsum roasting system according to claim 4, characterized in that: the tail gas purification device (6) is a spray absorption tower.
6. The phosphogypsum roasting system according to claim 1, characterized in that: a screening device (8) is arranged between the finished product conveying device (5) and the finished product bin (7), an inlet of the screening device (8) is communicated with the finished product conveying device (5), an outlet of the screening device (8) is communicated with the finished product bin (7), and a material returning port of the screening device (8) is communicated with a material inlet (101) of the roasting furnace (1).
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116063014A (en) * 2021-11-04 2023-05-05 中国科学院过程工程研究所 Phosphogypsum fluidized roasting device and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116063014A (en) * 2021-11-04 2023-05-05 中国科学院过程工程研究所 Phosphogypsum fluidized roasting device and method

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PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Phosphogypsum calcination system

Granted publication date: 20200721

Pledgee: Industrial and Commercial Bank of China Limited Dawu Branch

Pledgor: Hubei Huangmailing Phosphorus Chemical Co.,Ltd.

Registration number: Y2025980041296

PE01 Entry into force of the registration of the contract for pledge of patent right