WO2016150100A1 - Heat-accumulating lime rotary kiln - Google Patents

Heat-accumulating lime rotary kiln Download PDF

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Publication number
WO2016150100A1
WO2016150100A1 PCT/CN2015/088329 CN2015088329W WO2016150100A1 WO 2016150100 A1 WO2016150100 A1 WO 2016150100A1 CN 2015088329 W CN2015088329 W CN 2015088329W WO 2016150100 A1 WO2016150100 A1 WO 2016150100A1
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Prior art keywords
rotary kiln
kiln
cooler
heat accumulator
lime
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PCT/CN2015/088329
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French (fr)
Chinese (zh)
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贾会平
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石家庄新华能源环保科技股份有限公司
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Publication of WO2016150100A1 publication Critical patent/WO2016150100A1/en

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    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2/00Lime, magnesia or dolomite
    • C04B2/10Preheating, burning calcining or cooling
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • F27B7/02Rotary-drum furnaces, i.e. horizontal or slightly inclined of multiple-chamber or multiple-drum type
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/40Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills

Definitions

  • the invention belongs to the technical field of industrial furnaces and relates to a rotary kiln, in particular to a regenerative lime rotary kiln.
  • Rotary kiln refers to rotary calcining kiln.
  • Lime rotary kiln is a kiln that uses a wide range of calcined small particles. It is suitable for steel, calcium carbide chemical, non-ferrous metals and other production enterprises.
  • the lime rotary kiln can directly calcine 10 ⁇ 40mm fine-grained raw material limestone or light burnt dolomite, which has the characteristics of good raw material adaptability, large output, uniform product, high activity and stable production operation.
  • the lime rotary kiln has a simple structure, the airflow is smooth, the sulfur-containing flue gas can be discharged in time, and the sulfur in the fuel is not easy to adhere.
  • the calcined product has low sulfur content, high purity, and meets the quality requirements of the finished product; at the same time, the material rolls in the circumferential direction. It moves along the axial direction and is evenly heated.
  • the temperature of the combustion device is easy to control, the calcination quality is good, and the product activity can reach 360mlL or more.
  • the Chinese utility model patent with the application number 200920227150.0 discloses an "energy-saving rotary kiln calcination system", in which the "rotary kiln calcination system includes a rotary kiln, the fuel gas is fed from the low end of the rotary kiln, from the high end of the rotary kiln; The high-end of the rotary kiln is taken from the lower end of the rotary kiln. The high-end rotary kiln is connected to a heat recovery chamber.
  • the heat recovery chamber is provided with a feed preheating pipe connected to the rotary kiln, and the raw material is preheated by feeding. After the tube is preheated, it enters the rotary kiln. In this way, the raw material is dried and heated before entering the rotary kiln.”
  • the preheating pipe has limited energy recovery by preheating raw materials, and there is sufficient space for energy saving.
  • the patented rotary kiln is a single rotary kiln, which is not conducive to expanding production capacity.
  • the object of the invention is to provide a regenerative lime rotary kiln, which utilizes two rotary kiln and a heat accumulator to fully utilize the waste heat of the flue gas to preheat the raw materials and air, thereby reducing energy consumption and expanding lime production capacity.
  • the technical solution of the invention is a regenerative lime rotary kiln comprising two rotary kiln, a cooler, one or two regenerators, a loading system, a discharging system, a blower, a cooling fan and an exhaust gas discharge system.
  • the rotary kiln is provided with a kiln head, and the two rotary kiln are connected to the cooler through a kiln tail cover, and the cooler is connected to the discharge system.
  • the upper port of the regenerator is connected to the loading system via a feed valve.
  • the upper port of the regenerator is connected to the blower and the exhaust system through a three-way valve, and the cooling fan is connected to the cooler.
  • the heat accumulator is of a sleeve type structure, comprising an outer cylinder and an inner cylinder, an annular space between the outer cylinder and the inner cylinder, and a lower part of the annular space is connected with the rotary kiln through the kiln head.
  • the regenerator has 2 to 10 pushers, and the pusher has a pusher plate.
  • the lime kiln is provided with a burner and an auxiliary burner, the burner is installed in the kiln head, and the auxiliary burner is installed in the kiln tail cover.
  • the upper part of the inner cylinder has a tapered structure, and the middle section has a circular structure.
  • the two rotary kiln are symmetrically arranged or asymmetrically arranged on both sides of the kiln tail cover.
  • the heat accumulator is provided with a partition which divides the heat accumulator into two parts.
  • One of the two rotary kiln is connected to the cooler through the kiln tail cover and the other end is connected to the heat accumulator through the kiln head.
  • Exhaust system includes dust collector and induced draft fan And the chimney.
  • the three-way valve is connected to the exhaust gas discharge system through the waste heat power generation equipment.
  • Waste heat power generation equipment includes waste heat boilers, steam turbines and generators.
  • the waste heat boiler is provided with a steam coil, the steam coil is connected with the steam turbine, and the steam turbine is coaxially connected with the generator set.
  • the burner and the auxiliary burner are gas fuel burners, liquid fuel burners or solid fuel burners.
  • the loading system includes a loading machine, a loading trolley and a hopper.
  • the rotary kiln is equipped with temperature measuring equipment, and the temperature measuring equipment is a wireless signal temperature measuring device.
  • the regenerative lime rotary kiln of the invention preheats the processed material by adding the regenerator, utilizing the flue gas generated by the calcination process and the decomposition gas generated by the decomposition of the material, and preheating the air by using the preheated heated material to improve the air.
  • the combustion temperature of the fuel makes full use of the waste heat and reduces energy consumption.
  • the heat accumulator adopts a sleeve parallel flow structure, and the heat transfer effect is good, which is favorable for uniform preheating of the material to be processed.
  • FIG. 1 is a schematic structural view of a regenerative lime rotary kiln according to the present invention
  • FIG. 2 is a schematic structural view of another embodiment of the present invention.
  • Figure 3 is a cross-sectional view of the heat accumulator
  • Figure 4 is a cross-sectional view of another embodiment of the heat accumulator
  • the regenerative lime rotary kiln of the present invention as shown in FIG. 1, comprises two rotary kiln 13, a cooler 16, two regenerators 4, a loading system 3, a discharging system 18, a blower 11, and a cooling fan 17, Waste heat power generation equipment 10 and an exhaust gas discharge system.
  • the two rotary kiln are arranged symmetrically on the left and right sides, respectively, on both sides of the kiln tail cover.
  • the rotary kiln is provided with a kiln head 22, and the two rotary kiln are connected to the cooler through the kiln tail cover 14, the cooler 16 is connected to the discharge system, and the cooling fan is connected to the cooler.
  • the upper port of the heat accumulator 4 is connected to the loading system 3 via a feed valve 2.
  • the two heat accumulators 4 are of a sleeve type structure.
  • the heat accumulator 4 includes an outer cylinder and an inner cylinder 20.
  • the upper portion of the inner cylinder has a tapered structure, and the middle section has a circular structure.
  • An annular space 21 is defined between the outer cylinder and the inner cylinder.
  • the annular space is a space through which the raw material passes, and the flue gas or air exchanges heat with the raw material in the annular space, and the lower part of the annular space passes through
  • the kiln head 22 is connected to the rotary kiln 13.
  • the upper port of the heat accumulator 4 is connected to the blower 11 all the way through the three-way valve 1, and the other path is connected to the waste heat power generating device 10 through the pipe flue gas line 8, and the outlet of the waste heat power generating device is connected to the exhaust gas discharge system.
  • the exhaust system includes a dust collector, an induced draft fan and a chimney.
  • the waste heat power generation facility 10 includes a waste heat boiler, a steam turbine, and a generator.
  • the waste heat boiler is provided with a steam coil, the steam coil is connected with the steam turbine, and the steam turbine is coaxially connected with the generator set.
  • the lime kiln is provided with a burner 7 and an auxiliary burner 15, the burner and the auxiliary burner are gas fuel burners, the burner is mounted on the kiln head 22, and the auxiliary burner is mounted on the kiln tail cover 14.
  • the heat accumulator 4 is provided with six pushers 5, and the pusher has a pusher plate 6, and the pusher plate 6 is evenly distributed in the lower portion of the heat accumulator.
  • the rotary kiln is provided with a temperature measuring device 12, and the temperature measuring device is an infrared wireless signal temperature measuring device, which is installed on the kiln body of the rotary kiln on both sides, and is rotated with the kiln body to measure the temperature and wirelessly transmitted to the control room.
  • the operation process of the regenerative lime rotary kiln of the present invention is that the limestone raw material enters the heat accumulator 4 via the left loading system 3, and the cone passing through the upper portion of the inner cylinder 20 is evenly distributed in the annular space 21.
  • the flue gas from the left rotary kiln 13 enters the annular space of the heat accumulator 4 through the kiln head 22, and preheats the raw materials in the heat accumulator.
  • the preheated limestone raw material is pushed into the kiln head 22 by the pusher 5, and is calcined through the kiln head into the left rotary kiln 13.
  • the calcined lime passes through the kiln tail cover 14 to the cooler 16, and the cooling air sent from the cooling fan 17 cools the high temperature lime in the cooler 16, and the cooled lime is discharged through the discharge port and the discharge system 18.
  • the gas operation mode is that the air blasted by the right side blower 11 passes through the three-way valve 1 to the right side heat accumulator 4, and the heat released from the raw material preheated in the heat accumulator preheats the combustion air.
  • the fuel gas enters the right burner 7 to eject the fuel, mixes with the air preheated by the regenerator, enters the right rotary kiln 13 through the kiln head 22 for combustion, and calcinates the limestone material in the right rotary kiln.
  • the flue gas and the decomposition gas generated by the combustion are mixed together with the gas for cooling the lime through the kiln tail cover 14 and the cooler 16 to continue heating the limestone material to the left rotary kiln 13.
  • the mixed gas preheats the limestone material through the kiln head and the left side heat accumulator 4 and stores heat, and the flue gas after releasing the heat is generated by the three-way valve 1 and the flue gas pipeline 8 to the waste heat power generation device 10, and the waste after power generation
  • the flue gas is discharged to the exhaust system, and the temperature of the flue gas is lower than 150 °C.
  • the rotary kiln 13 on both sides alternately performs calcination and preheating, and the regenerators 4 on both sides alternately store heat and release heat to preheat the air through the three-way valve 1, the valve 9 and the feed valve.
  • the action of 2 is alternately operated, and the set temperature of the flue gas emission is 150 °C.
  • the auxiliary burner 15 is selected to be used, and the fuel is burned to supplement the heat.
  • the regenerative lime rotary kiln includes two rotary kiln 13 and one heat accumulator 4, and the heat accumulator 4 is provided with a partition 19, which will be stored.
  • the heat exchanger 4 is divided into two parts, and the two parts have the same structure.
  • One of the two rotary kiln 13 is connected to the cooler 16 through the kiln tail cover 14, and the other end is connected to the heat accumulator 4.
  • the two rotary kiln 13 are alternately calcined and preheated, and the material spaces on both sides of the accumulator partition 19 alternately store heat and release heat to preheat the air, and are realized by the actions of the three-way valve 1, the valve 9 and the feed valve 3.
  • the set temperature of the flue gas emission is 160 °C.
  • Other devices and connection states are the same as in the first embodiment. The advantage of this embodiment is that the device is compact and saves space.

Abstract

A heat-accumulating lime rotary kiln comprises two rotary kilns (13), a cooler (16), one or two heat accumulators (4), an air blower (11), a cooling fan (17) and an exhaust emission system. The two rotary kilns (13) are connected via a kiln tail hood (14) and the cooler (16). An upper air port of the heat accumulator (4) is connected to, via a three-way valve (1), the air blower (11) and the exhaust emission system respectively. The heat accumulator (4) has a sleeve structure, and an inner sleeve (20) and an outer sleeve are concentrically provided. The inner sleeve (20) and the outer sleeve form an annular space (21) therebetween. A lower portion of the annular space (21) is in communication with the rotary kiln (13) via a kiln head (22). A lime kiln is provided with a burner (7) and an auxiliary burner (15). The burner (7) is mounted at the kiln head (22), and the auxiliary burner (15) is mounted at the kiln tail hood (14). The heat accumulator (4) employs a sleeve parallel-flow structure, has a good heat transfer effect, and enables a machined material to be uniformly preheated. The two rotary kilns (13) are combined with the heat accumulator (4) via the kiln tail hood (14), and the burnt raw material and combustion air are preheated, thus facilitating continuity and stability of lime production, and improving a production capacity.

Description

蓄热式石灰回转窑Regenerative lime rotary kiln 技术领域Technical field
本发明属于工业炉窑技术领域,涉及一种回转窑,具体涉及一种蓄热式石灰回转窑。The invention belongs to the technical field of industrial furnaces and relates to a rotary kiln, in particular to a regenerative lime rotary kiln.
背景技术Background technique
回转窑是指旋转煅烧窑,其中石灰回转窑是使用较广泛的煅烧小颗粒物料的窑炉,适合应用于钢铁、电石化工、有色金属等生产企业。石灰回转窑可以直接煅烧10~40mm的细粒级原料石灰石或轻烧白云石,具有原料适应性好、产量大、产品均匀、活性度高、生产操作稳定等特点。石灰回转窑结构简单,气流通畅,含硫烟气可及时排出,燃料中的硫份不易附着,因而煅烧成品含硫量低,纯度高,符合成品的质量要求;同时物料既沿圆周方向翻滚,又沿轴向移动,受热均匀,燃烧装置温度容易控制,煅烧质量好,产品活性度可达360mlL以上。Rotary kiln refers to rotary calcining kiln. Lime rotary kiln is a kiln that uses a wide range of calcined small particles. It is suitable for steel, calcium carbide chemical, non-ferrous metals and other production enterprises. The lime rotary kiln can directly calcine 10~40mm fine-grained raw material limestone or light burnt dolomite, which has the characteristics of good raw material adaptability, large output, uniform product, high activity and stable production operation. The lime rotary kiln has a simple structure, the airflow is smooth, the sulfur-containing flue gas can be discharged in time, and the sulfur in the fuel is not easy to adhere. Therefore, the calcined product has low sulfur content, high purity, and meets the quality requirements of the finished product; at the same time, the material rolls in the circumferential direction. It moves along the axial direction and is evenly heated. The temperature of the combustion device is easy to control, the calcination quality is good, and the product activity can reach 360mlL or more.
但是由于石灰回转窑能耗大,严重制约石灰回转窑的推广与发展。申请号为200920227150.0的中国实用新型专利公开了一种“节能回转窑煅烧系统”,该专利中“回转窑煅烧系统包括回转窑,燃料气自回转窑低端进,自回转窑高端出;原料自回转窑高端进,自回转窑低端出,其特征在于:回转窑高端与一热回收室相通,该热回收室内部设有与回转窑相通的进料预热管,原料经进料预热管预热后进入回转窑。如此设计,原料在进入回转窑前,干燥升温。”。但该专利中预热管通过预热原料回收能量有限,节省能源还有充分的空间,此外该专利的回转窑为单个回转窑,不利于扩大生产能力。However, due to the large energy consumption of the lime rotary kiln, the promotion and development of the lime rotary kiln is seriously restricted. The Chinese utility model patent with the application number 200920227150.0 discloses an "energy-saving rotary kiln calcination system", in which the "rotary kiln calcination system includes a rotary kiln, the fuel gas is fed from the low end of the rotary kiln, from the high end of the rotary kiln; The high-end of the rotary kiln is taken from the lower end of the rotary kiln. The high-end rotary kiln is connected to a heat recovery chamber. The heat recovery chamber is provided with a feed preheating pipe connected to the rotary kiln, and the raw material is preheated by feeding. After the tube is preheated, it enters the rotary kiln. In this way, the raw material is dried and heated before entering the rotary kiln.". However, in this patent, the preheating pipe has limited energy recovery by preheating raw materials, and there is sufficient space for energy saving. In addition, the patented rotary kiln is a single rotary kiln, which is not conducive to expanding production capacity.
发明内容Summary of the invention
发明的目的是提供一种蓄热式石灰回转窑,利用两台回转窑与蓄热器相结合,充分利用烟气的余热预热原料和空气,从而降低能耗,扩大石灰生产能力。The object of the invention is to provide a regenerative lime rotary kiln, which utilizes two rotary kiln and a heat accumulator to fully utilize the waste heat of the flue gas to preheat the raw materials and air, thereby reducing energy consumption and expanding lime production capacity.
本发明的技术方案是蓄热式石灰回转窑,包括两台回转窑、冷却器、一台或两台蓄热器、上料系统、出料系统、鼓风机、冷却风机和废气排放系统。回转窑设有窑头,两台回转窑通过窑尾罩与冷却器连接,冷却器与出料系统连接。蓄热器上部料口通过进料阀与上料系统连接。蓄热器上部气口通过三通阀与鼓风机和废气排放系统连接,冷却风机与冷却器连接。蓄热器为套筒式结构,包括外筒和内筒,外筒和内筒之间为环形空间,环形空间的下部通过窑头与回转窑连接。蓄热器设有2~10台推料机,推料机带有推料板。石灰窑设有烧嘴和辅助烧嘴,烧嘴安装在窑头,辅助烧嘴安装在窑尾罩。The technical solution of the invention is a regenerative lime rotary kiln comprising two rotary kiln, a cooler, one or two regenerators, a loading system, a discharging system, a blower, a cooling fan and an exhaust gas discharge system. The rotary kiln is provided with a kiln head, and the two rotary kiln are connected to the cooler through a kiln tail cover, and the cooler is connected to the discharge system. The upper port of the regenerator is connected to the loading system via a feed valve. The upper port of the regenerator is connected to the blower and the exhaust system through a three-way valve, and the cooling fan is connected to the cooler. The heat accumulator is of a sleeve type structure, comprising an outer cylinder and an inner cylinder, an annular space between the outer cylinder and the inner cylinder, and a lower part of the annular space is connected with the rotary kiln through the kiln head. The regenerator has 2 to 10 pushers, and the pusher has a pusher plate. The lime kiln is provided with a burner and an auxiliary burner, the burner is installed in the kiln head, and the auxiliary burner is installed in the kiln tail cover.
内筒上部为锥形结构,中间截面为圆形结构。两台回转窑左右对称布置或非对称布置,分别位于窑尾罩的两侧。蓄热器设有隔板,隔板将蓄热器分成两部分。两台回转窑的一头通过窑尾罩与冷却器连接,另一头通过窑头与蓄热器连接。废气排放系统包括除尘器、引风机 和烟囱。三通阀通过余热发电设备与废气排放系统连接。余热发电设备包括废热锅炉、蒸汽轮机和发电机。废热锅炉设蒸汽盘管,蒸汽盘管与蒸汽轮机连接,蒸汽轮机与发电机组同轴连接。烧嘴和辅助烧嘴为气体燃料烧嘴、液体燃料烧嘴或固体燃料烧嘴。上料系统包括上料机、上料小车和料斗。回转窑设有测温设备,测温设备为无线信号测温设备。The upper part of the inner cylinder has a tapered structure, and the middle section has a circular structure. The two rotary kiln are symmetrically arranged or asymmetrically arranged on both sides of the kiln tail cover. The heat accumulator is provided with a partition which divides the heat accumulator into two parts. One of the two rotary kiln is connected to the cooler through the kiln tail cover and the other end is connected to the heat accumulator through the kiln head. Exhaust system includes dust collector and induced draft fan And the chimney. The three-way valve is connected to the exhaust gas discharge system through the waste heat power generation equipment. Waste heat power generation equipment includes waste heat boilers, steam turbines and generators. The waste heat boiler is provided with a steam coil, the steam coil is connected with the steam turbine, and the steam turbine is coaxially connected with the generator set. The burner and the auxiliary burner are gas fuel burners, liquid fuel burners or solid fuel burners. The loading system includes a loading machine, a loading trolley and a hopper. The rotary kiln is equipped with temperature measuring equipment, and the temperature measuring equipment is a wireless signal temperature measuring device.
本发明蓄热式石灰回转窑,通过增加蓄热器,利用煅烧过程产生的烟气和物料分解产生的分解气体预热被加工物料,再利用预热升温后的被加工物料预热空气,提高燃料的燃烧温度,从而充分利用了余热,降低了能耗。蓄热器采用套筒并流式结构,传热效果好,有利于被加工物料的均匀预热。通过窑尾罩两台回转窑与蓄热器联合,实现预热被煅烧原料和助燃空气,有利于石灰生产的连续性和稳定性,扩大生产能力。烧嘴设置在蓄热器和窑头的连接部位或安装在窑头,增加了生产操作的选择性。The regenerative lime rotary kiln of the invention preheats the processed material by adding the regenerator, utilizing the flue gas generated by the calcination process and the decomposition gas generated by the decomposition of the material, and preheating the air by using the preheated heated material to improve the air. The combustion temperature of the fuel makes full use of the waste heat and reduces energy consumption. The heat accumulator adopts a sleeve parallel flow structure, and the heat transfer effect is good, which is favorable for uniform preheating of the material to be processed. Through the combination of two rotary kiln and heat accumulator in the kiln tail cover, preheating the calcined raw material and combustion air is realized, which is beneficial to the continuity and stability of lime production and expands production capacity. The burner is placed at the junction of the regenerator and the kiln head or at the kiln head, increasing the selectivity of the production operation.
附图说明DRAWINGS
图1为本发明蓄热式石灰回转窑的结构示意图;1 is a schematic structural view of a regenerative lime rotary kiln according to the present invention;
图2为本发明另一实施方案的结构示意图;2 is a schematic structural view of another embodiment of the present invention;
图3为蓄热器截面图;Figure 3 is a cross-sectional view of the heat accumulator;
图4为另一实施方案蓄热器的截面图;Figure 4 is a cross-sectional view of another embodiment of the heat accumulator;
其中:among them:
1-三通阀、2-进料阀、3-上料系统、4-蓄热器、5-推料机、6-推料板、7-烧嘴、8-烟气管路、9-阀门、10-余热发电设备、11-鼓风机、12-测温设备、13-回转窑、14-窑尾罩、15-辅助烧嘴、16-冷却器、17-冷却风机、18-出料系统、19-隔板、20-内筒、21-环形空间、22-窑头。1-3-way valve, 2-feed valve, 3-feed system, 4-heat accumulator, 5-propeller, 6-propeller plate, 7-burner, 8-flue pipe, 9- Valve, 10-waste heat power generation equipment, 11-blower, 12-temperature measuring equipment, 13-rotary kiln, 14-kiln tail cover, 15-auxiliary burner, 16-cooler, 17-cooling fan, 18-discharge system 19-separator, 20-inner cylinder, 21-annular space, 22-kiln head.
具体实施方式detailed description
下面结合实施例和附图对本发明进行详细说明。本发明保护范围不限于实施例,本领域技术人员在权利要求限定的范围内做出任何改动也属于本发明保护的范围。The invention will now be described in detail in conjunction with the embodiments and the drawings. The scope of the present invention is not limited to the embodiments, and any modifications made by those skilled in the art within the scope of the claims are also within the scope of the present invention.
实施例1Example 1
本发明蓄热式石灰回转窑,如图1所示,包括两台回转窑13、冷却器16、两台蓄热器4、上料系统3、出料系统18、鼓风机11、冷却风机17、余热发电设备10和废气排放系统。两台回转窑左右对称布置,分别位于窑尾罩的两侧。回转窑设有窑头22,两台回转窑通过窑尾罩14与冷却器连接,冷却器16与出料系统连接,冷却风机与冷却器连接。蓄热器4上部料口通过进料阀2与上料系统3连接。两台蓄热器4为套筒式结构,如图3所示,蓄热器4包括外筒和内筒20,内筒上部为锥形结构,中间截面为圆形结构。外筒和内筒之间为环形空间21,环形空间为原料通过的空间,烟气或空气在环形空间与原料进行换热,环形空间的下部通过 窑头22与回转窑13连接。蓄热器4的上部气口通过三通阀1一路与鼓风机11连接,另一路通过管路烟气管路8与余热发电设备10连接,余热发电设备的出口与废气排放系统连接。废气排放系统包括除尘器、引风机和烟囱。余热发电设备10包括废热锅炉、蒸汽轮机和发电机。废热锅炉设蒸汽盘管,蒸汽盘管与蒸汽轮机连接,蒸汽轮机与发电机组同轴连接。石灰窑设有烧嘴7和辅助烧嘴15,烧嘴和辅助烧嘴为气体燃料烧嘴,烧嘴安装在窑头22,辅助烧嘴安装在窑尾罩14。蓄热器4设有6台推料机5,推料机带有推料板6,推料板6均匀分布在蓄热器下部。回转窑设有测温设备12,测温设备为红外无线信号测温设备,安装在两侧回转窑的窑体上,随窑体转动测温,无线传输到控制室。The regenerative lime rotary kiln of the present invention, as shown in FIG. 1, comprises two rotary kiln 13, a cooler 16, two regenerators 4, a loading system 3, a discharging system 18, a blower 11, and a cooling fan 17, Waste heat power generation equipment 10 and an exhaust gas discharge system. The two rotary kiln are arranged symmetrically on the left and right sides, respectively, on both sides of the kiln tail cover. The rotary kiln is provided with a kiln head 22, and the two rotary kiln are connected to the cooler through the kiln tail cover 14, the cooler 16 is connected to the discharge system, and the cooling fan is connected to the cooler. The upper port of the heat accumulator 4 is connected to the loading system 3 via a feed valve 2. The two heat accumulators 4 are of a sleeve type structure. As shown in FIG. 3, the heat accumulator 4 includes an outer cylinder and an inner cylinder 20. The upper portion of the inner cylinder has a tapered structure, and the middle section has a circular structure. An annular space 21 is defined between the outer cylinder and the inner cylinder. The annular space is a space through which the raw material passes, and the flue gas or air exchanges heat with the raw material in the annular space, and the lower part of the annular space passes through The kiln head 22 is connected to the rotary kiln 13. The upper port of the heat accumulator 4 is connected to the blower 11 all the way through the three-way valve 1, and the other path is connected to the waste heat power generating device 10 through the pipe flue gas line 8, and the outlet of the waste heat power generating device is connected to the exhaust gas discharge system. The exhaust system includes a dust collector, an induced draft fan and a chimney. The waste heat power generation facility 10 includes a waste heat boiler, a steam turbine, and a generator. The waste heat boiler is provided with a steam coil, the steam coil is connected with the steam turbine, and the steam turbine is coaxially connected with the generator set. The lime kiln is provided with a burner 7 and an auxiliary burner 15, the burner and the auxiliary burner are gas fuel burners, the burner is mounted on the kiln head 22, and the auxiliary burner is mounted on the kiln tail cover 14. The heat accumulator 4 is provided with six pushers 5, and the pusher has a pusher plate 6, and the pusher plate 6 is evenly distributed in the lower portion of the heat accumulator. The rotary kiln is provided with a temperature measuring device 12, and the temperature measuring device is an infrared wireless signal temperature measuring device, which is installed on the kiln body of the rotary kiln on both sides, and is rotated with the kiln body to measure the temperature and wirelessly transmitted to the control room.
本发明蓄热式石灰回转窑的运行过程为,石灰石原料经左侧上料系统3进入蓄热器4,通过内筒20上部的锥体均匀分布在环形空间21。由左侧回转窑13过来的烟气经窑头22进入蓄热器4的环形空间,对蓄热器内的原料进行预热。预热后的石灰石原料由推料机5推入窑头22,经窑头进入左侧回转窑13进行煅烧。煅烧后的石灰经窑尾罩14到冷却器16,由冷却风机17送出的冷却风对冷却器16中的高温石灰进行冷却,冷却后的石灰经出料口和出料系统18出装置。气体运行方式为右侧鼓风机11鼓出的空气经三通阀1到右侧蓄热器4,在蓄热器内预热后的原料放出的热量预热助燃空气。燃料气进入右侧烧嘴7喷出燃料,与经蓄热器预热后的空气混合,经窑头22进入右侧回转窑13进行燃烧,对右侧回转窑中石灰石物料进行煅烧。燃烧产生的烟气及分解气体一起经窑尾罩14与冷却器16冷却石灰的气体混合,到左侧回转窑13继续加热石灰石物料。然后的混合气体经窑头和左侧蓄热器4预热石灰石物料并蓄热,放出热量后的烟气经三通阀1和烟气管路8到余热发电设备10发电,发电后的废烟气到废气排放系统排放,烟气排放的温度低于150℃。根据烟气排放的设定温度,两侧回转窑13交替进行煅烧和预热,两侧蓄热器4交替进行蓄热和放出热量预热空气,通过三通阀1、阀门9和进料阀2的动作实现交替运行,烟气排放的设定温度为150℃。在预热温度不足的情况下选择使用辅助烧嘴15,喷出燃料燃烧补充热量。The operation process of the regenerative lime rotary kiln of the present invention is that the limestone raw material enters the heat accumulator 4 via the left loading system 3, and the cone passing through the upper portion of the inner cylinder 20 is evenly distributed in the annular space 21. The flue gas from the left rotary kiln 13 enters the annular space of the heat accumulator 4 through the kiln head 22, and preheats the raw materials in the heat accumulator. The preheated limestone raw material is pushed into the kiln head 22 by the pusher 5, and is calcined through the kiln head into the left rotary kiln 13. The calcined lime passes through the kiln tail cover 14 to the cooler 16, and the cooling air sent from the cooling fan 17 cools the high temperature lime in the cooler 16, and the cooled lime is discharged through the discharge port and the discharge system 18. The gas operation mode is that the air blasted by the right side blower 11 passes through the three-way valve 1 to the right side heat accumulator 4, and the heat released from the raw material preheated in the heat accumulator preheats the combustion air. The fuel gas enters the right burner 7 to eject the fuel, mixes with the air preheated by the regenerator, enters the right rotary kiln 13 through the kiln head 22 for combustion, and calcinates the limestone material in the right rotary kiln. The flue gas and the decomposition gas generated by the combustion are mixed together with the gas for cooling the lime through the kiln tail cover 14 and the cooler 16 to continue heating the limestone material to the left rotary kiln 13. Then, the mixed gas preheats the limestone material through the kiln head and the left side heat accumulator 4 and stores heat, and the flue gas after releasing the heat is generated by the three-way valve 1 and the flue gas pipeline 8 to the waste heat power generation device 10, and the waste after power generation The flue gas is discharged to the exhaust system, and the temperature of the flue gas is lower than 150 °C. According to the set temperature of the flue gas discharge, the rotary kiln 13 on both sides alternately performs calcination and preheating, and the regenerators 4 on both sides alternately store heat and release heat to preheat the air through the three-way valve 1, the valve 9 and the feed valve. The action of 2 is alternately operated, and the set temperature of the flue gas emission is 150 °C. When the preheating temperature is insufficient, the auxiliary burner 15 is selected to be used, and the fuel is burned to supplement the heat.
实施例2Example 2
本发明的另一实施方式如图2和图4所示,蓄热式石灰回转窑包括两台回转窑13、一台蓄热器4,蓄热器4设有隔板19,隔板将蓄热器4分成两部分,两部分的结构相同。两台回转窑13的一头通过窑尾罩14与冷却器16连接,另一头与蓄热器4连接。两台回转窑13交替进行煅烧和预热,蓄热器隔板19两侧的物料空间交替进行蓄热和放出热量预热空气,通过三通阀1、阀门9和进料阀3的动作实现交替运行,烟气排放的设定温度为160℃。其它设备及连接状态与实施例1相同。本实施例的优点是装置紧凑,节省占地空间。 According to another embodiment of the present invention, as shown in FIGS. 2 and 4, the regenerative lime rotary kiln includes two rotary kiln 13 and one heat accumulator 4, and the heat accumulator 4 is provided with a partition 19, which will be stored. The heat exchanger 4 is divided into two parts, and the two parts have the same structure. One of the two rotary kiln 13 is connected to the cooler 16 through the kiln tail cover 14, and the other end is connected to the heat accumulator 4. The two rotary kiln 13 are alternately calcined and preheated, and the material spaces on both sides of the accumulator partition 19 alternately store heat and release heat to preheat the air, and are realized by the actions of the three-way valve 1, the valve 9 and the feed valve 3. Alternate operation, the set temperature of the flue gas emission is 160 °C. Other devices and connection states are the same as in the first embodiment. The advantage of this embodiment is that the device is compact and saves space.

Claims (9)

  1. 一种蓄热式石灰回转窑,包括两台回转窑(13)、冷却器(16)、一台或两台蓄热器(4)、上料系统(3)、出料系统(18)、鼓风机(11)、冷却风机(17)和废气排放系统,所述回转窑设有窑头(22),两台回转窑通过窑尾罩(14)与冷却器连接,冷却器与出料系统连接;所述蓄热器上部料口通过进料阀与上料系统连接;其特征是:所述蓄热器(4)上部气口通过三通阀(1)与鼓风机和废气排放系统连接,冷却风机与冷却器连接;所述蓄热器为套筒式结构,包括外筒和内筒(20),外筒和内筒之间为环形空间(21),所述环形空间的下部通过窑头与回转窑连接;所述蓄热器设有2~10台推料机,所述推料机带有推料板;所述石灰窑设有烧嘴(7)和辅助烧嘴(15),烧嘴安装在窑头,辅助烧嘴安装在窑尾罩。A regenerative lime rotary kiln comprising two rotary kiln (13), a cooler (16), one or two regenerators (4), a feeding system (3), a discharging system (18), a blower (11), a cooling fan (17) and an exhaust gas discharge system, the rotary kiln is provided with a kiln head (22), and two rotary kiln are connected to the cooler through a kiln tail cover (14), and the cooler is connected to the discharge system The upper port of the regenerator is connected to the loading system through a feed valve; and the upper port of the regenerator (4) is connected to the blower and the exhaust system through a three-way valve (1), the cooling fan Connected to a cooler; the heat accumulator is of a sleeve type structure, comprising an outer cylinder and an inner cylinder (20), an annular space (21) between the outer cylinder and the inner cylinder, and a lower portion of the annular space passes through the kiln head The rotary kiln is connected; the regenerator is provided with 2 to 10 pushers, and the pusher is provided with a pusher plate; the lime kilns are provided with a burner (7) and an auxiliary burner (15), which are burned The mouth is installed in the kiln head, and the auxiliary burner is installed in the kiln tail cover.
  2. 根据权利要求1所述的蓄热式石灰回转窑,其特征是:所述内筒(20)上部为锥形结构,中间截面为圆形结构。The regenerative lime rotary kiln according to claim 1, wherein the upper portion of the inner cylinder (20) has a tapered structure and a circular cross section in the middle.
  3. 根据权利要求1所述的蓄热式石灰回转窑,其特征是:所述两台回转窑(13)左右对称布置或非对称布置,分别位于窑尾罩(14)的两侧。The regenerative lime rotary kiln according to claim 1, characterized in that the two rotary kiln (13) are arranged symmetrically or asymmetrically on both sides, respectively located on both sides of the kiln tail cover (14).
  4. 根据权利要求1所述的蓄热式石灰回转窑,其特征是:所述蓄热器(4)设有隔板(19),隔板将蓄热器分成两部分;两台回转窑(13)的一头通过窑尾罩(14)与冷却器(16)连接,另一头通过窑头(22)与蓄热器连接。A regenerative lime rotary kiln according to claim 1, wherein said heat accumulator (4) is provided with a partition (19), the partition dividing the heat accumulator into two parts; and two rotary kiln (13) One end is connected to the cooler (16) through the kiln tail cover (14), and the other end is connected to the heat accumulator through the kiln head (22).
  5. 根据权利要求1所述的蓄热式石灰回转窑,其特征是:所述废气排放系统包括除尘器、引风机和烟囱。A regenerative lime rotary kiln according to claim 1 wherein said exhaust gas discharge system comprises a precipitator, an induced draft fan and a chimney.
  6. 根据权利要求1所述的蓄热式石灰回转窑,其特征是:所述三通阀(1)通过余热发电设备(10)与废气排放系统连接。A regenerative lime rotary kiln according to claim 1, characterized in that said three-way valve (1) is connected to the exhaust gas discharge system via a waste heat power generating device (10).
  7. 根据权利要求6所述的蓄热式石灰回转窑,其特征是:所述余热发电设备(10)包括废热锅炉、蒸汽轮机和发电机;废热锅炉设蒸汽盘管,蒸汽盘管与蒸汽轮机连接,蒸汽轮机与发电机组同轴连接。The regenerative lime rotary kiln according to claim 6, wherein the waste heat power generation device (10) comprises a waste heat boiler, a steam turbine and a generator; the waste heat boiler is provided with a steam coil, and the steam coil is connected to the steam turbine. The steam turbine is coaxially connected to the generator set.
  8. 根据权利要求1所述的蓄热式石灰回转窑,其特征是:所述烧嘴(7)和辅助烧嘴(15)为气体燃料烧嘴、液体燃料烧嘴或固体燃料烧嘴。A regenerative lime rotary kiln according to claim 1, wherein said burner (7) and auxiliary burner (15) are gas fuel burners, liquid fuel burners or solid fuel burners.
  9. 根据权利要求1所述的蓄热式石灰回转窑,其特征是:回转窑设有测温设备(12),测温设备为无线信号测温设备。 The regenerative lime rotary kiln according to claim 1, wherein the rotary kiln is provided with a temperature measuring device (12), and the temperature measuring device is a wireless signal temperature measuring device.
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CN203478938U (en) * 2013-06-05 2014-03-12 石家庄新华能源环保科技股份有限公司 Rotary kiln apparatus with energy recovery equipment
CN104016596A (en) * 2014-05-27 2014-09-03 石家庄新华能源环保科技股份有限公司 Rotary kiln with power generation device
CN203947031U (en) * 2014-05-27 2014-11-19 石家庄新华能源环保科技股份有限公司 A kind of rotary kiln with power generation assembly
CN104803615A (en) * 2015-03-24 2015-07-29 石家庄新华能源环保科技股份有限公司 Heat accumulating type lime rotary kiln

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CN109574523A (en) * 2018-12-25 2019-04-05 石家庄新华能源环保科技股份有限公司 A kind of limekiln that the hot sending of gasification furnace coal gas of high temperature is directly burnt
CN109574523B (en) * 2018-12-25 2024-04-16 石家庄新华能源环保科技股份有限公司 Lime kiln for directly burning high-temperature coal gas of gasification furnace in hot feeding manner
CN109708464A (en) * 2019-01-02 2019-05-03 宁波大学 A kind of cigarette-gas shunts the Dual-barrel rotary kiln of purification
CN109708464B (en) * 2019-01-02 2024-01-02 宁波大学 Double-cylinder rotary kiln for smoke-gas split-flow purification
CN111217542A (en) * 2020-03-23 2020-06-02 南京威普粉体工程有限公司 Sleeve shaft kiln for horizontal flow lime calcination
CN111217542B (en) * 2020-03-23 2024-02-06 南京威普粉体工程有限公司 Sleeve shaft kiln for calcining lime in advection manner
CN112944927A (en) * 2021-03-12 2021-06-11 华北水利水电大学 Multi-point flue gas collecting and heat-extracting system for lime kiln production
CN113372024A (en) * 2021-07-03 2021-09-10 石家庄新华能源环保科技股份有限公司 Double-hearth kiln for calcining lime by using low-calorific-value fuel and calcining method
CN114749074A (en) * 2022-03-10 2022-07-15 鞍山铭泽机械设备有限公司 Spatial arrangement structure of continuous graphite coating production system

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