阅读说明：本技术 一种冶铁装置及其烧结设备 (Iron smelting device and sintering equipment thereof ) 是由 章开颜 刘再新 刘贵云 黄睿 徐玉珍 于 2019-09-10 设计创作，主要内容包括：本发明公开了一种冶铁装置及其烧结设备,包括生石灰消化设备和除尘装置,其还包括：用于供应热风的热风管路；连接生石灰消化设备的排气口和除尘装置的混流装置,混流装置包括：内筒,具有用于与排气口连通的第一进口；外筒,具有用于与热风管路连通的第二进口,套设在内筒外侧,内筒在远离第一进口的一端和外筒连通,具有用于与除尘装置相连的出口,出口的位置高于第一进口和第二进口的位置。由于热风的温度高,含尘气体进入外筒混合后会提高含尘气体的温度,使含尘气体保持在饱和温度以上,再进入除尘装置,保证含尘气体在流动过程中管道和除尘装置中不会出现冷凝现象,维持含尘气体干燥状态,避免粉尘的板结,保证整个设备长期稳定的正常运行。(The invention discloses an iron smelting device and sintering equipment thereof, which comprise quicklime slaking equipment and a dust removing device, and further comprise: a hot air pipeline for supplying hot air; connect quick lime slaking equipment's gas vent and dust collector's mixed flow device, mixed flow device includes: an inner barrel having a first inlet for communication with the exhaust port; the outer cylinder is provided with a second inlet communicated with the hot air pipeline and sleeved outside the inner cylinder, one end of the inner cylinder, far away from the first inlet, is communicated with the outer cylinder and is provided with an outlet connected with the dust removal device, and the position of the outlet is higher than the positions of the first inlet and the second inlet. Because hot-blast temperature is high, can improve dirty gaseous temperature after dirty gas gets into the urceolus and mixes, makes dirty gas keep above the saturation temperature, reentrant dust collector guarantees that dirty gas can not appear the condensation phenomenon in pipeline and dust collector in the flow process, maintains dirty gaseous drying state, avoids hardening of dust, guarantees the long-term stable normal operating of whole equipment.)

1. the sintering equipment comprises quicklime slaking equipment and a dust removal device (13), and is characterized by further comprising:

A hot air pipeline for supplying hot air;

Connect the gas vent of quick lime slaking equipment with mixed flow device (11) of dust collector (13), mixed flow device (11) includes: an inner barrel (1), the inner barrel (1) having a first inlet (A1) for communication with the exhaust; urceolus (3), urceolus (3) have be used for with the second import (A2) of hot-blast pipeline intercommunication, urceolus (3) cover is established the inner tube (1) outside, just inner tube (1) is keeping away from the one end of first import (A1) with urceolus (3) intercommunication, urceolus (3) have be used for with export (A3) that dust collector (13) link to each other, just the position of export (A3) is higher than first import (A1) with the position of second import (A2).

2. The sintering equipment according to claim 1, characterized in that the inner cylinder (1) and the outer cylinder (3) are communicated through a pressure regulating device (4), or a booster fan is arranged on the hot air pipeline.

3. The sintering apparatus according to claim 2, characterized in that the pressure regulating means (4) is a pressure regulating hole provided on the inner cylinder (1), and the pressure regulating hole is uniformly arranged along the circumferential direction of the inner cylinder (1).

4. Sintering equipment according to claim 1 characterized in that the inner cylinder (1) is of a straight cylindrical structure; the outer tub (3) includes: a first right cylindrical section (9) near one end of the second inlet (A2), a second right cylindrical section (8) far from one end of the second inlet (A2) and an inclined section connecting the first right cylindrical section (9) and the second right cylindrical section (8), wherein the diameter of the first right cylindrical section (9) is smaller than that of the second right cylindrical section (8); the second inlet (A2) is located in the first right circular cylindrical section (9) and the outlet (A3) is located in the second right circular cylindrical section (8).

5. the sintering apparatus according to claim 1, wherein an end of the flow mixing device (11) remote from the first inlet (A1) has an atmospheric air bypass port (A4), and the atmospheric air bypass port (A4) communicates with the inner barrel (1) through a bypass valve (5).

6. The sintering equipment as claimed in claim 1, and further comprising a quicklime bin for storing quicklime;

And a conveying device is arranged at an outlet of the quicklime bin, and the tail end of the conveying device is opposite to a feeding hole of the quicklime slaking equipment.

7. Sintering equipment according to claim 1, characterized in that a dust hood (12) is arranged at the exhaust port, and the outlet of the dust hood (12) is connected with the first inlet (A1).

8. An iron smelting plant comprising a sintering apparatus, characterized in that the sintering apparatus is a sintering apparatus according to any one of claims 1-7.

Technical Field

the invention relates to the technical field of smelting, in particular to an iron smelting device and sintering equipment thereof.

Background

in the raw material proportioning stage, the sintering generally adopts a quicklime slaking process, namely, in the raw material proportioning stage, quicklime, namely calcium oxide (CaO), is generally added, and then water is added, so that the calcium oxide and the water generate a chemical reaction to generate calcium hydroxide. A large amount of heat is released during the chemical reaction, so that the process can strengthen the sintering process, improve the material temperature and reduce the over-wet phenomenon in the sintering process; the surface of the produced slaked lime is in a colloid state, has strong water absorption and large cohesive force, and can improve the balling property of the sintering mixture.

Although the process performance of the quicklime digestion process is improved, the process also produces serious environmental pollution, a large amount of water vapor can be produced by the heat produced by the quicklime digestion, and the water vapor can carry a large amount of dust while diffusing outwards, so that the surrounding environment is polluted; the main substances of dust here are: CaO, Ca (OH)₂、CaCO₃And iron-containing dust characterized by: high humidity, high concentration, light dust and fine particles. This part dirty gas is the saturation state, and after the access dust pelletizing system, also can bring a large amount of ambient air simultaneously, because of the interfusion of ambient air and the cooling in the dust removal pipeline will make dirty gas temperature reduce. Part of water vapor is condensed into water in the pipeline, the mixture of the water and the dust is in a colloid state, the cohesive force is large, the dust removal pipeline is easily blocked, the adhesion to dust removal equipment is caused, the blockage of the pipeline influences the dust removal capacity of the system, the adhesion to the equipment influences the dust removal efficiency, the operation of the whole dust removal system is abnormal, and the whole system can be paralyzed in a short time in serious cases. The paralysis of the system can cause pollution to the surrounding environment, the surrounding area is completely white lime dust, the lime dust is diffused in the air, and strong stimulation is caused to the respiratory tract of people, so that the harm caused by the high-humidity high-concentration lime dust needs to be solved.

At present, the dust removal at the quicklime digestion part is selected from the following anti-blocking and dust removal equipment in a dust removal pipeline:

Dust removal pipeline anti-blocking

In order to prevent the pipeline from being blocked, a mode of spraying water along the way from a dust removing point to an inlet pipeline of dust removing equipment is mainly adopted at present, so that the blockage of the pipeline is relieved, but the mode has the main defects of high water consumption, incapability of completely avoiding the blockage of the pipeline and need of regularly cleaning sediments at a low point or an elbow of the pipeline.

Dust removing equipment

The selection of the existing dust removing equipment is mainly a wet dust remover or a combination of the wet dust remover and the wet electric dust remover. The dust removal efficiency of the wet dust collector is only 97 percent at most if the emission of 20mg/m is satisfied³the concentration requirement of the inlet of the dust remover cannot be higher than 670mg/m³The actual inlet concentration of the dust collector is generally 8-15 g/m³Far above this value, the emission requirements cannot be guaranteed by single-pole wet dust removal, and a two-stage wet dust collector or a series connection of a wet dust collector and a wet electric dust collector is required to guarantee the emission requirements of dust removal.

The existing dust removal technical schemes all belong to wet dust removal, a large amount of sewage is generated during system operation, and the sewage cannot be discharged outwards according to the environmental protection requirement, so the generated sewage is generally conveyed to a mixer by a sewage pump, and if the water quantity balance of the process cannot be ensured, the part of sewage is likely to generate secondary pollution.

Therefore, the technical problem to be solved by those skilled in the art is how to provide a flow mixing device of a sintering device to alleviate the pollution of lime dust.

Disclosure of Invention

In view of the above, the present invention provides a flow mixing device for a sintering apparatus to alleviate the pollution of lime dust. Another object of the present invention is to provide an iron smelting device with the sintering equipment.

In order to achieve the purpose, the invention provides the following technical scheme:

A sintering equipment comprises quicklime slaking equipment and a dust removal device, and further comprises:

A hot air pipeline for supplying hot air;

Connect the gas vent of quick lime digestion equipment with dust collector's mixed flow device, mixed flow device includes: an inner barrel having a first inlet for communication with the exhaust port; the outer barrel is provided with a second inlet used for being communicated with the hot air pipeline, the outer barrel is sleeved on the outer side of the inner barrel, the inner barrel is far away from one end of the first inlet and communicated with the outer barrel, the outer barrel is provided with an outlet used for being connected with the dust removal device, and the position of the outlet is higher than the positions of the first inlet and the second inlet.

preferably, in the sintering apparatus, the inner cylinder and the outer cylinder are communicated through a pressure regulating device, or a booster fan is disposed on the hot air pipeline.

Preferably, in the sintering apparatus, the pressure adjusting device is a pressure adjusting hole formed in the inner cylinder, and the pressure adjusting hole is uniformly arranged along the circumferential direction of the inner cylinder.

Preferably, in the sintering apparatus, the inner cylinder has a straight cylindrical structure; the outer tub includes: the first right cylindrical section is close to one end of the first inlet, the second right cylindrical section is far away from one end of the first inlet, the inclined section is connected with the first right cylindrical section and the second right cylindrical section, and the diameter of the first right cylindrical section is smaller than that of the second right cylindrical section; the second inlet is located in the first right circular cylinder section and the outlet is located in the second right circular cylinder section.

Preferably, in the sintering apparatus, an atmosphere bypass port is provided at an end of the flow mixing device away from the first inlet, and the atmosphere bypass port is communicated with the inner cylinder through a bypass valve.

preferably, the sintering equipment further comprises a quicklime bin for storing quicklime;

And a conveying device is arranged at an outlet of the quicklime bin, and the tail end of the conveying device is opposite to a feeding hole of the quicklime slaking equipment.

preferably, in the sintering apparatus, a dust hood is disposed at the exhaust port, and an outlet of the dust hood is connected to the first inlet.

An iron smelting device comprises sintering equipment, wherein the sintering equipment is any one of the sintering equipment.

According to the technical scheme, when the sintering equipment disclosed by the invention works, the dust-containing gas generated by the quicklime slaking equipment is discharged through the exhaust port and enters the inner cylinder, namely the dust-containing gas circulation cavity, through the first inlet; meanwhile, hot air enters the outer barrel through the second inlet, namely a hot air circulation cavity between the inner barrel and the outer barrel. Because hot-blast temperature is high, can improve dirty gaseous temperature after dirty gas gets into the urceolus and mixes, makes dirty gas keep above the saturation temperature, reentrant dust collector to guarantee that dirty gas can not appear the condensation phenomenon in pipeline and dust collector in the flow process, maintain dirty gaseous drying state, avoid hardening of dust, guarantee the long-term stable normal operating of whole equipment.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the description of the embodiments or the prior art are briefly introduced below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.

FIG. 1 is a front view of a flow mixing device disclosed in an embodiment of the present invention;

FIG. 2 is a cross-sectional view of the flow mixing device disclosed in an embodiment of the present invention;

FIG. 3 is a top view of the flow mixing device disclosed in an embodiment of the present invention;

FIG. 4 is a cross-sectional view taken in the direction BB in FIG. 3;

FIG. 5 is a schematic structural diagram of a sintering apparatus disclosed in an embodiment of the present invention.

Detailed Description

In view of the above, the core of the present invention is to disclose a flow mixing device of a sintering apparatus to alleviate the pollution of lime dust. The other core of the invention is to disclose an iron smelting device with the sintering equipment.

In order that those skilled in the art will better understand the disclosure, the invention will be described in further detail with reference to the accompanying drawings and specific embodiments.

As shown in fig. 1 to 5, the present invention discloses a sintering apparatus comprising: the quick lime slaking device is a structure for slaking quick lime, and the dust removal device 13 is used for treating dust generated by the quick lime so as to ensure that the discharged gas meets the discharge standard and reduce pollution. Because the temperature can reduce and take place the condensation phenomenon after the dirty gas that quick lime slaking equipment discharged reaches dust collector 13 through the pipeline, in view of this, increased mixed flow device 11 in this application, specifically, this mixed flow device 11 is connected the gas vent and the dust collector 13 of quick lime slaking equipment, and the dirty gas of gas vent reentries dust collector 13 after mixed flow device 11 promptly. The flow mixing device 11 includes: an inner cylinder 1 and an outer cylinder 3, wherein the inner cylinder 1 is provided with a first inlet A1 for communicating with the exhaust port, and the first inlet A1 is communicated with the dust-containing gas circulation chamber 7 of the inner cylinder 1; the outer cylinder 3 is sleeved outside the inner cylinder 1, and a hot air circulation cavity is formed between the inner cylinder and the outer cylinder. The outer cylinder 3 described above has a second inlet a2 for communicating with the hot blast line, and the outer cylinder 3 has an outlet A3 for connecting with the dust removing device 13, and the position of the outlet A3 is higher than the positions of the first inlet a1 and the second inlet a 2.

when the device works, the dust-containing gas generated by the quicklime slaking device is discharged through the exhaust port and enters the inner cylinder 1 through the first inlet A1, namely the dust-containing gas circulation cavity 7; meanwhile, the hot air enters the outer cylinder 3 through the second inlet A2, namely a hot air circulation cavity between the inner cylinder 1 and the outer cylinder 3. Because hot-blast temperature is high, can improve dirty gaseous temperature after dirty gas gets into urceolus 3 and mixes, make dirty gas keep above the saturation temperature, reentrant dust collector 13 to guarantee that dirty gas can not appear the condensation phenomenon in pipeline and dust collector 13 in the flow process, maintain dirty gas drying state, avoid the hardening of dust, guarantee the long-term stable normal operating of whole equipment.

the temperature of hot air in this application needs to be set according to the temperature and the circulation of dirty gas, as long as can guarantee that the gas after the mixture keeps in the hot air temperature of saturation temperature above all in protective range.

In a specific embodiment, the inner cylinder 1 and the outer cylinder 3 are communicated through a pressure regulating device 4, or a booster fan is arranged on a hot air pipeline. In practice, since the distance from the hot air introduction point to the second inlet a2 is far greater than the distance from the dust removal port to the first inlet a1, that is, the interface resistance of the second inlet a2 is far greater than the interface resistance of the first inlet a1, the air volume of the first inlet a1 is higher than that of the second inlet a 2. In order to solve the problem that the air volume is increased to the end with low interface resistance caused by different interface resistances, the end with low interface resistance needs to be adjusted. Specifically, the inner cylinder 1 and the outer cylinder 3 can be communicated through the pressure regulating device 4, and when the dust-containing gas passes through the pressure regulating device 4, the pipe section resistance of the dust-containing gas can be increased and the dust-containing gas enters the outer cylinder 3. In practice, a booster fan can be arranged on the hot air pipeline, and as can be understood by those skilled in the art, the core here is to ensure that the actual air volume of the dust-containing gas and the hot air is approximately the same as the designed air volume, so that the structures for achieving the above purpose on this basis are all within the protection range. Through the arrangement, the dust-containing gas with certain air quantity, temperature and humidity and the hot air with the corresponding quantity can be mixed and tempered, and the temperature of the mixed gas is required to be kept above the saturation temperature finally. In view of this, the mode and value of resistance adjustment need to be set according to the air volume and temperature of the dust-containing gas, and are all within the protection range.

In practice, the pressure regulating device 4 is a pressure regulating hole arranged on the inner cylinder 1, and the pipe section resistance of the dust-containing gas is changed by changing the passage area for the dust-containing gas to flow. Specifically, the area of the dust-containing gas flowing into the hot air flowing chamber needs to be reduced to increase the flow resistance of the dust-containing gas, thereby controlling the air volume.

Inner tube 1 in this application is straight cylinder structure, and urceolus 3 includes: a first cylindrical section 9, a second cylindrical section 8 and an inclined section. The first right cylinder section 9 is one end of the outer cylinder 3 close to the first inlet a1, and the second inlet a2 is located at the first right cylinder section 9; the second straight cylindrical section 8 is the end of the outer cylinder 3 far away from the first inlet A1, and the outlet A3 is positioned at the second straight cylindrical section 8; the inclined section connects the first right circular cylinder section 9 and the second right circular cylinder section 8, and the diameter of the first right circular cylinder section 9 is smaller than the diameter of the second right circular cylinder section 8. The reason for setting the outer cylinder 3 such that the diameter of the second right circular cylinder section 8 is larger than the diameter of the first right circular cylinder section 9 is to ensure a mixing space and a mixing effect. Only one specific shape of the outer cylinder 3 is disclosed, and in practice, the outer cylinder 3 can be modified according to different needs and is within the protection scope. When the double-layer structure mixed flow device 11 works, dust-containing air flows upwards in the inner cylinder 1, hot air flows upwards in the outer cylinder 3, the dust-containing air flow pipeline is wrapped in the hot air, and the phenomenon of dust hardening caused by dewing of the dust-containing air can be prevented by improving the temperature of the outer wall of the dust-containing air pipeline and transferring heat to the dust-containing air.

in the preferred embodiment, the end of the flow mixing device 11 away from the first inlet A1 has an atmospheric air bypass port A4, and the atmospheric air bypass port A4 communicates with the inner barrel 1 through a bypass valve 5. The flow mixing device 11 is provided with an atmosphere bypass port A4, a bypass valve 5 is arranged at the position of the atmosphere bypass port A4, when a dust removal system fails (a dust removal fan is stopped, hot air is failed to be introduced, and the like), the bypass valve 5 can be opened, dust-containing gas is temporarily discharged into the atmosphere through the atmosphere bypass port A4, and the dust-containing gas which is not mixed with the hot air is prevented from entering a dust removal pipeline to block the system. System failure can be addressed by adding atmospheric bypass port a4 and bypass valve 5.

In a further embodiment, the sintering equipment further comprises a quicklime bin for storing quicklime, a conveying device is arranged at an outlet of the quicklime bin, and the tail end of the conveying device is opposite to a feeding hole of the quicklime slaking equipment. The material supply device of the quicklime slaking device can adopt other feeding modes in practice and is in a protection range.

The exhaust port in this application is provided with dust excluding hood 12, and the outlet of dust excluding hood 12 is connected with first inlet a 1. The dust hood 12 is arranged at the exhaust port of the quicklime slaking equipment, so that leaked gas can be treated, and the environmental pollution is further reduced.

The second inlet a2 is a port of the hot air inlet pipe 2 provided in the outer cylinder 3 and communicating with the hot air flow chamber of the inner cylinder 3, and the outlet A3 is a port of the outlet pipe 6 provided in the outer cylinder 3 and communicating with the hot air flow chamber of the outer cylinder 3.

In addition, this application has still disclosed a smelt iron device, including sintering equipment, wherein, this sintering equipment is the sintering equipment disclosed in the above-mentioned embodiment, therefore, smelt iron device that has this sintering equipment also has above-mentioned all technological effects, no longer describe herein one by one.

The embodiments in the present description are described in a progressive manner, each embodiment focuses on differences from other embodiments, and the same and similar parts among the embodiments are referred to each other.

The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.