CN114705054B - Multi-bin heat exchange sinter waste heat recovery device and recovery method - Google Patents
Multi-bin heat exchange sinter waste heat recovery device and recovery method Download PDFInfo
- Publication number
- CN114705054B CN114705054B CN202210309193.3A CN202210309193A CN114705054B CN 114705054 B CN114705054 B CN 114705054B CN 202210309193 A CN202210309193 A CN 202210309193A CN 114705054 B CN114705054 B CN 114705054B
- Authority
- CN
- China
- Prior art keywords
- heat exchange
- bin
- sub
- sinter
- exchange bin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 111
- 239000002918 waste heat Substances 0.000 title claims abstract description 105
- 238000000034 method Methods 0.000 title claims abstract description 32
- 239000002245 particle Substances 0.000 claims abstract description 82
- 238000009826 distribution Methods 0.000 claims abstract description 30
- 238000004891 communication Methods 0.000 claims abstract description 11
- 239000012530 fluid Substances 0.000 claims abstract description 10
- 238000012546 transfer Methods 0.000 claims description 32
- 238000005245 sintering Methods 0.000 claims description 29
- 238000005192 partition Methods 0.000 claims description 20
- 230000001105 regulatory effect Effects 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 14
- 239000000428 dust Substances 0.000 claims description 11
- 239000011148 porous material Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 description 12
- 239000007787 solid Substances 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 230000002708 enhancing effect Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010310 metallurgical process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D15/00—Handling or treating discharged material; Supports or receiving chambers therefor
- F27D15/02—Cooling
- F27D15/0286—Cooling in a vertical, e.g. annular, shaft
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
The invention provides a sinter waste heat recovery device and a recovery method for multi-bin heat exchange, wherein a heat exchange bin (1) comprises: a sinter feed inlet (11); a first sub heat exchange bin (2); a second sub heat exchange bin (3); and a sinter screen (12), the vertical lower side of the second sub heat exchange bin (3) is provided with a second sub heat exchange bin air distribution device (32), the sinter screen (12) is configured to guide the sinter with relatively smaller particle size from the sinter feed inlet (11) into the first sub heat exchange bin (2), and guide the sinter with relatively larger particle size into the second sub heat exchange bin (3); the waste heat recovery device further comprises an off-bin heat exchanger (4), and the off-bin heat exchanger (4) is in fluid communication with the second sub heat exchange bin (3). The multi-bin heat exchange sinter waste heat recovery device and the recovery method have higher waste heat recovery efficiency, and simultaneously solve the problems of large-particle sinter jamming and high heat exchange air flow resistance.
Description
Technical Field
The invention relates to the field of metallurgy or heat energy, in particular to efficient recovery and utilization of waste heat resources in a metallurgical process, and specifically relates to a multi-bin heat exchange sinter waste heat recovery device and a recovery method.
Background
The steel production in China mainly adopts a long-flow production process of a blast furnace-converter, and the steel proportion of the converter is more than 90%. The proportion of the sintered ore in the blast furnace burden structure in China reaches 70% -75%, and the sintered ore yield in China exceeds 12 hundred million tons in 2020. The energy consumption of the sintering process is about 15% of the total energy consumption of iron and steel enterprises, and the sintering process is next to the iron-making process and is positioned at the 2 nd position. The sintering process is to mix various powdery iron-containing raw materials with a certain proportion of fuel and solvent before blast furnace ironmaking production, burn the raw materials on a sintering machine trolley, and sinter the raw materials into blocks after a series of physical and chemical changes. Waste heat resource main of sintering processThe sensible heat of the finished sinter product and the sensible heat of the flue gas of the sintering machine are required, and the sensible heat carried by the sinter before cooling is about 44.5 percent of the total heat expenditure. According to statistics, the sintering waste heat resource amount in China reaches 4000 ten thousand tons of standard coal per year, and if the heat amount can be fully utilized, the CO can be reduced 2 The emission of about 1 hundred million tons, and the efficient recovery and utilization of waste heat resources in the sintering process are one of the key routes to the "30/60 dual carbon" goal.
At present, the cooling of the sinter is generally carried out by a traditional ring cooler or a vertical pot furnace in China or even the world. The waste heat recovery process of the annular cooler has the remarkable defects of high air leakage rate, difficult waste heat recovery at a low temperature section and the like, so that the overall waste heat recovery efficiency is lower. The vertical tank furnace solves the problems of poor sealing and the like of the circular cooler, has the advantages of lower air leakage rate, high hot air temperature, less dust emission and the like, and because air passes through a thick material layer in the heat exchange process in the vertical tank furnace, the flow resistance of the air is very high, thereby further bringing the problems of extremely high self-power consumption and lower external power supply capacity of the system.
Aiming at the problems of the annular cooler and the vertical tank furnace, the technology of adopting vertical solid heat exchange waste heat recovery is developed and improved in recent years, and the heat exchange is directly carried out through the sinter and a heating surface pipeline arranged in a heat exchanger, so that the waste heat recovery efficiency of the sinter is improved, and the self power consumption of the waste heat recovery process is reduced.
However, the particle size distribution of the sintering mineral aggregate is wide, the particle size of the high-temperature material is in the range of 3 mm-200 mm, the randomness is realized, and secondary crushing is required to be avoided according to the sintering process requirement. In the waste heat recovery process, in order to enable the heating surface pipeline to fully absorb the heat of the sinter in a limited space and time, the transverse distance of the pipeline is generally not more than 100mm, so that the blocking of large-particle sinter is extremely easy to cause, the material flow is blocked, and the heat exchange effect is affected. Only the large-particle sinter can be discharged out of the system, so that a large amount of waste heat resources are wasted, and the working environment is influenced by the high-temperature sinter.
In order to ensure the flow stability of the small-particle sintered ore and the efficient recovery of the waste heat of the large-particle sintered ore in the process of recovering the waste heat of the sintered ore, the design method of the scheme is provided.
Disclosure of Invention
The invention aims to at least partially overcome the defects of the prior art and provides a multi-bin heat exchange sinter waste heat recovery device and a recovery method.
The invention also aims to provide a multi-bin heat exchange sinter waste heat recovery device and a multi-bin heat exchange sinter waste heat recovery method, which have the advantage of improved waste heat recovery efficiency.
The invention also aims to provide a multi-bin heat exchange sinter waste heat recovery device and a recovery method, which solve the problem of blockage of large-particle sinter in a heating surface pipeline.
The invention also aims to provide a device and a method for recovering the waste heat of the sintered ore with multi-bin heat exchange, which solve the problem of high flow resistance of heat exchange air.
In order to achieve one of the above objects or purposes, the technical solution of the present invention is as follows:
the utility model provides a sintering deposit waste heat recovery device of many storehouses heat transfer, waste heat recovery device includes the heat transfer storehouse, the heat transfer storehouse is including two at least sub-heat transfer storehouses of spaced apart, two at least sub-heat transfer storehouses are used for holding the sintering deposit of different particle diameter scope respectively, and the heat transfer mode in one sub-heat transfer storehouse in two at least sub-heat transfer storehouses is different from the heat transfer mode in another sub-heat transfer storehouse.
According to a preferred embodiment of the invention, the heat exchange cartridge comprises:
a sinter feed inlet;
the first sub heat exchange bin is communicated with the sinter feeding port;
the second sub heat exchange bin is arranged at the side of the first sub heat exchange bin and is communicated with the sinter feeding port; and
a sinter screen, which is arranged below the sinter feeding hole,
the first sub heat exchange bin comprises at least one heat exchange device, a second sub heat exchange bin air distribution device is arranged on the vertical lower side of the second sub heat exchange bin, and the second sub heat exchange bin air distribution device is configured to supply air flow flowing vertically upwards into the second sub heat exchange bin;
wherein the sinter screen is configured to direct sinter of relatively smaller particle size from the sinter feed into the first sub-heat exchange bin and to direct sinter of relatively larger particle size into the second sub-heat exchange bin; and is also provided with
The waste heat recovery device further comprises an external heat exchanger arranged on the outer side of the heat exchange bin, and the external heat exchanger is in fluid communication with the second sub heat exchange bin and is used for recovering heat of air flow discharged from the second sub heat exchange bin.
According to a preferred embodiment of the invention, the off-board heat exchanger comprises at least one heat exchange device, and the second sub-heat exchange bin is provided with a warm air outlet, which is in fluid communication with the inlet of the off-board heat exchanger, and the outlet of the off-board heat exchanger is in fluid communication with the second sub-heat exchange bin air distribution device.
According to a preferred embodiment of the invention, at least one heat exchange device of the first sub heat exchange cartridge comprises a superheater, an evaporator and/or an economizer; and/or
The at least one heat exchange device of the off-board heat exchanger comprises a superheater, an evaporator and/or an economizer.
According to a preferred embodiment of the invention, the waste heat recovery device further comprises a dust collector arranged on the connection path between the off-board heat exchanger and the second sub heat exchange bin air distribution device.
According to a preferred embodiment of the present invention, the waste heat recovery device further comprises an air circulation fan and a first air regulating valve, and the air circulation fan and the first air regulating valve are disposed on a connection path between the off-bin heat exchanger and the second sub heat exchange bin air distribution device.
According to a preferred embodiment of the invention, the first sub heat exchange bin comprises a first sub heat exchange bin discharger arranged on the vertical lower side of the first sub heat exchange bin; and the second sub heat exchange bin comprises a second sub heat exchange bin discharger which is arranged on the vertical lower side of the second sub heat exchange bin.
According to a preferred embodiment of the invention, the heat exchange bin further comprises a third sub heat exchange bin and an additional screen, wherein the third sub heat exchange bin is arranged between the first sub heat exchange bin and the second sub heat exchange bin and is communicated with the sinter feeding hole;
the sintering ore screen is arranged above the first sub heat exchange bin, and the additional screen is arranged above the third sub heat exchange bin; and the pore diameter of the additional screen is larger than that of the sintering ore screen;
wherein, be provided with additional heat transfer device in the third sub heat transfer storehouse.
According to a preferred embodiment of the invention, the horizontal spacing between the heat exchange tubes of the additional heat exchange means is larger than the horizontal spacing between the heat exchange tubes of the at least one heat exchange device of the first sub heat exchange cartridge.
According to another aspect of the present invention, there is provided a multi-bin heat exchanged sinter waste heat recovery method employing a multi-bin heat exchanged sinter waste heat recovery apparatus according to any one of the preceding embodiments.
According to a preferred embodiment of the present invention, the waste heat recovery method includes:
supplying sinter into the heat exchange bin through the sinter feed inlet;
the sintering ore screen mesh is utilized to guide the sintering ore with relatively smaller particle size from the sintering ore feeding port into the first sub heat exchange bin, and guide the sintering ore with relatively larger particle size into the second sub heat exchange bin;
recovering heat of the sintered ore in the first sub heat exchange bin by utilizing heat exchange equipment in the first sub heat exchange bin;
introducing air flow into the second sub heat exchange bin, and absorbing heat of the sintered ore in the second sub heat exchange bin by utilizing the air flow; and
and discharging the air flow in the second sub heat exchange bin to an external heat exchanger, and recovering heat of the air flow discharged from the second sub heat exchange bin by using the external heat exchanger.
According to the multi-bin heat exchange sinter waste heat recovery device and the recovery method, the heat exchange bin is divided into more than two sub heat exchange bins, the sinter screen is utilized to separate large and small-particle sinters, the waste heat of the small-particle sinters is recovered by direct heat exchange, and the waste heat of the large-particle sinters is recovered by circulating air flow, so that the distance between heating surface pipelines can be designed to be small for the recovery of the small-particle sinters without considering the problem of material blockage, high heat recovery efficiency is maintained, and meanwhile, the circulating air flow is adopted for heat exchange of the large-particle sinters, and the problems of high self-consumption of electricity are avoided because the particle size of the sinters is large and the flow resistance of air is not so large. In conclusion, the purposes of improving heat exchange efficiency, reducing power consumption of the system and improving operation stability and safety of the system are achieved.
Drawings
FIG. 1 shows exemplary agglomerate grain size versus heat transfer coefficient;
FIG. 2 shows, by way of example, sinter grain size as a function of bed resistance and fan power;
FIG. 3 shows exemplary sinter temperature versus heat transfer coefficient;
FIG. 4 illustrates exemplary airflow velocity versus heat transfer coefficient;
FIG. 5 is a schematic structural view of a multi-bin heat exchanging sinter waste heat recovery apparatus according to an embodiment of the invention;
FIG. 6 is a schematic structural view of a multi-bin heat exchanging sinter waste heat recovery apparatus according to another embodiment of the invention;
FIG. 7 is a schematic structural view of a sinter waste heat recovery apparatus for enhanced heat transfer according to an embodiment of the invention;
FIG. 8 is a schematic structural view of a sinter waste heat recovery apparatus for enhanced heat transfer according to another embodiment of the invention;
FIG. 9 is a schematic structural view of a heat exchange enhanced sinter waste heat recovery apparatus according to still another embodiment of the invention;
FIG. 10 is a schematic structural view of a heat exchange enhanced sintered ore waste heat recovery apparatus according to still another embodiment of the present invention; and
fig. 11 is a schematic structural view of a sinter waste heat recovery apparatus for enhancing heat exchange according to still another embodiment of the invention.
Detailed Description
Exemplary embodiments of the present invention are described in detail below with reference to the attached drawing figures, wherein the same or similar reference numerals denote the same or similar elements. Furthermore, in the following detailed description, for purposes of explanation, numerous specific details are set forth in order to provide a thorough understanding of the embodiments of the present disclosure. It may be evident, however, that one or more embodiments may be practiced without these specific details. In other instances, well-known structures and devices are shown in the drawings in order to simplify the drawings.
For intensive study of sintered ore
As described in the background art, the sintered mineral aggregate has wide particle size distribution, the particle size of the high-temperature material is in the range of 3 mm-200 mm, and the heat exchange properties of the sintered mineral aggregate with different particle sizes are different. In the vertical solid heat exchange technology, the larger the granularity of the agglomerate is, the smaller the heat transfer coefficient is, and the typical relation between the granularity of the agglomerate and the heat transfer coefficient is shown in fig. 1, which means that the agglomerate with lower granularity has higher heat exchange efficiency and waste heat recovery efficiency.
In a vertical shaft furnace, sinter is charged into the furnace from the top of the furnace, flowing air flowing upward is provided at the lower side of the vertical shaft furnace, and heat in the sinter is absorbed by the flowing air, as described in the background section, in which the problem of flow resistance (i.e., material layer resistance) of air needs to be considered, because the material layer resistance is directly related to the power consumption of a fan, it is desirable to reduce the material layer resistance to reduce the power consumption of the fan. Fig. 2 shows exemplarily the relation between sinter grain size and material layer resistance, and the relation between sinter grain size and fan power, with decreasing grain size, both of which rise, which is also easily understood, because smaller grain size means smaller gaps between sinter grains and thus an increase in resistance to flowing air.
From the above relation, the heat exchange application of the small-particle sintered ore is more efficient in the solid-solid heat exchange vertical type solid heat exchange furnace, and the heat exchange application of the small-particle sintered ore is more suitable for the heat exchange of the large-particle sintered ore in the circulating air heat exchange vertical type tank furnace. Based on the above, the invention provides a multi-bin heat exchange sinter waste heat recovery device, which comprises a heat exchange bin, wherein the heat exchange bin comprises at least two separated sub heat exchange bins, the at least two sub heat exchange bins are respectively used for accommodating sinter of different particle size ranges, and the heat exchange mode of one sub heat exchange bin in the at least two sub heat exchange bins is different from the heat exchange mode of the other sub heat exchange bin.
Fig. 5 shows a multi-bin heat exchange sinter waste heat recovery apparatus according to an embodiment of the invention, as shown in fig. 5, comprising a heat exchange bin 1 and an off-bin heat exchanger 4. The heat exchange bin 1 is in a tank shape, a sinter feeding hole 11 is arranged above the heat exchange bin, and a sinter discharging hole is arranged below the heat exchange bin. The heat exchange bin 1 is divided into two sub heat exchange bins by a partition wall 15, a first sub heat exchange bin 2 and a second sub heat exchange bin 3, the first sub heat exchange bin 2 is communicated with the sinter feeding hole 11, and the second sub heat exchange bin 3 is arranged at the side of the first sub heat exchange bin 2 and is communicated with the sinter feeding hole 11. A sinter screen 12 is arranged in the heat exchange bin 1, below the sinter feed 11, the sinter screen 12 being configured to guide sinter of relatively small particle size from the sinter feed 11 into the first sub heat exchange bin 2 and sinter of relatively large particle size into the second sub heat exchange bin 3. Specifically, the sinter screen 12 is obliquely arranged above the first sub heat exchange bin 2, the sinter fed from the sinter feed inlet 11 is screened by the sinter screen 12, the small particle size enters the first sub heat exchange bin 2, and the large particle size enters the second sub heat exchange bin 3. The first sub heat exchange bin 2 and the second sub heat exchange bin 3 can be divided into two by independent bin bodies to form a first sub heat exchange bin shell 13 and a second sub heat exchange bin shell 14, and a separation wall 15 is vertically and upwardly extended between the first sub heat exchange bin 2 and the second sub heat exchange bin 3.
The first sub heat exchange bin 2 and the second sub heat exchange bin 3 are in different heat exchange modes, the first sub heat exchange bin 2 adopts solid-solid heat exchange, and the second sub heat exchange bin 3 adopts circulating air heat exchange. Specifically, the first sub heat exchange bin 2 includes a superheater 21, a first evaporator 22 and a first economizer 23, the superheater 21, the first evaporator 22 and the first economizer 23 are sequentially arranged from top to bottom, no heat exchange equipment is arranged in the second sub heat exchange bin 3, a second sub heat exchange bin air distribution device 32 is arranged on the vertically lower side of the second sub heat exchange bin 3, and the second sub heat exchange bin air distribution device 32 is configured to supply an air flow flowing vertically upwards into the second sub heat exchange bin 3; the second sub heat exchange bin 3 is provided with a heating air outlet 31, heat exchange air flow generated by the air distribution device is used for recovering heat of the large-particle sintered ore, and heat exchange air flow absorbing the heat passes through the heating air outlet 31.
The off-board heat exchanger 4 is disposed outside the heat exchanging compartment 1 and is formed of a tub-shaped off-board heat exchanger housing 41, and the off-board heat exchanger 4 is in fluid communication with the second sub-heat exchanging compartment 3 through the warm air outlet 31 for recovering heat of the air flow discharged from the second sub-heat exchanging compartment 3. The off-board heat exchanger 4 comprises at least one heat exchange device, e.g. a second evaporator 42 and a second economizer 43, the warmed air outlet 31 being in fluid communication with the inlet of the off-board heat exchanger 4, the outlet of the off-board heat exchanger 4 being in fluid communication with the second sub-heat exchange bin wind distribution device 32.
The waste heat recovery device further comprises a dust remover 44, an air circulating fan 45 and a first air regulating valve 46, wherein the dust remover 44 and the air circulating fan 45 are sequentially arranged on a connecting passage between the off-bin heat exchanger 4 and the second sub heat exchange bin air distribution device 32.
The first sub heat exchange bin 2 comprises a first sub heat exchange bin discharger 25 which is arranged on the vertical lower side of the first sub heat exchange bin 2; and the second sub heat exchange bin 3 includes a second sub heat exchange bin discharger 33 provided at a vertically lower side of the second sub heat exchange bin 3.
Therefore, the first sub heat exchange bin 2 is used as a small-particle sintering ore heat exchange bin to adopt a heat exchange mode of directly contacting with a heating surface pipeline, the second sub heat exchange bin 3 is used as a large-particle sintering ore heat exchange bin to adopt air indirect heat exchange, and meanwhile an off-bin heat exchanger adopting air circulation heat exchange is added. And after heat exchange and cooling are carried out on the hot air and the heating surface pipeline in the external heat exchanger, smoke dust in the hot air is removed through the dust remover, and the hot air is sent into the heat exchange bin through the air circulating fan. The invention has the technical advantages that: the sintering ores with large and small particles are distinguished, two different waste heat recovery modes are adopted according to the characteristics of the sintering ores, the waste heat recovery efficiency is improved, and the blocking of materials is prevented. The material granularity is reduced at the side of the small-particle sintering ore heat exchange bin, and the heat transfer coefficient is improved; on the side of the large-particle sintered ore heat exchange bin, the stacking void ratio of the large-particle sintered ore is large, so that the air circulation resistance is reduced, and the power consumption of the air circulation fan is reduced.
Advantageously, the preferred ratio of the cross-sectional areas of the first sub-heat exchange chamber 2 and the second sub-heat exchange chamber 3 is 65:35.
Fig. 6 shows a multi-bin heat exchange sinter waste heat recovery device according to another embodiment of the invention, as shown in fig. 6, the heat exchange bin 1 further comprises a third sub heat exchange bin 53 and an additional screen 51, wherein the third sub heat exchange bin 53 is arranged between the first sub heat exchange bin 2 and the second sub heat exchange bin 3 and is communicated with the sinter feed inlet 11; the sinter screen 12 is arranged above the first sub heat exchange bin 2, and the additional screen 51 is arranged above the third sub heat exchange bin 53; and the pore size of the additional screen 51 is larger than that of the sinter screen 12; wherein, an additional heat exchanging device 54 is arranged in the third sub heat exchanging bin 53. The horizontal spacing between the heat exchange tubes of the additional heat exchange means 54 is greater than the horizontal spacing between the heat exchange tubes of the at least one heat exchange device of the first sub heat exchange cartridge 2.
The angle of inclination of the additional screen 51 with respect to the horizontal is smaller than the angle of inclination of the sinter screen 12 with respect to the horizontal. The first sub heat exchange bin 2 and the third sub heat exchange bin 53 are separated by a partition wall 15, the third sub heat exchange bin 53 and the second sub heat exchange bin 3 are separated by an additional partition wall 52, and a third sub heat exchange bin discharger 55 is arranged on the vertical lower side of the third sub heat exchange bin 53.
According to another aspect of the present invention, there is provided a multi-bin heat exchanged sinter waste heat recovery method employing a multi-bin heat exchanged sinter waste heat recovery apparatus according to any one of the preceding embodiments.
According to a preferred embodiment of the present invention, the waste heat recovery method includes:
supplying sinter into the heat exchange bin 1 through the sinter feed inlet 11;
the sinter screen 12 is used for guiding the sinter with relatively smaller particle size from the sinter feed inlet 11 into the first sub heat exchange bin 2, and guiding the sinter with relatively larger particle size into the second sub heat exchange bin 3;
recovering heat of the sintered ore in the first sub heat exchange bin 2 by utilizing heat exchange equipment in the first sub heat exchange bin 2;
introducing air flow into the second sub heat exchange bin 3, and absorbing heat of the sintered ore in the second sub heat exchange bin 3 by utilizing the air flow; and
the air flow in the second sub heat exchange bin 3 is discharged to the outside heat exchanger 4, and the heat of the air flow discharged from the second sub heat exchange bin 3 is recovered by the outside heat exchanger 4.
According to the multi-bin heat exchange sinter waste heat recovery device and the recovery method, the heat exchange bin is divided into more than two sub heat exchange bins, the sinter screen is utilized to separate large and small-particle sinters, the waste heat of the small-particle sinters is recovered by direct heat exchange, and the waste heat of the large-particle sinters is recovered by circulating air flow, so that the distance between heating surface pipelines can be designed to be small for the recovery of the small-particle sinters without considering the problem of material blockage, high heat recovery efficiency is maintained, and meanwhile, the circulating air flow is adopted for heat exchange of the large-particle sinters, and the problems of high self-consumption of electricity are avoided because the particle size of the sinters is large and the flow resistance of air is not so large. In conclusion, the purposes of improving heat exchange efficiency, reducing power consumption of the system and improving operation stability and safety of the system are achieved.
Fig. 3 shows by way of example the relation between sinter temperature and heat transfer coefficient, the lower the sinter temperature, the lower its heat transfer coefficient, which means that in the embodiment of fig. 5, the heat of the sinter is gradually exchanged to the heat exchange device in the first sub-heat exchange chamber 2 as the sinter falls down, the temperature thereof gradually decreases, and then the sinter temperature is lower in the lower position of the first sub-heat exchange chamber 2, where the heat transfer coefficient is not high.
In order to increase the heat exchange efficiency of the lower part of the first sub heat exchange bin 2, the invention also provides a sinter waste heat recovery device for enhancing heat exchange, the waste heat recovery device comprises a heat exchange bin 1, the heat exchange bin 1 also comprises at least two separated sub heat exchange bins, the at least two sub heat exchange bins are respectively used for accommodating sinter of different particle size ranges, one of the at least two sub heat exchange bins adopts solid heat exchange, and the other sub heat exchange bin adopts circulating gas heat exchange. Importantly, the waste heat recovery device is configured to enable a portion of the recycle gas to pass into the one sub-heat exchange bin to enhance heat exchange and to direct the portion of the recycle gas into the other sub-heat exchange bin.
Fig. 7 is a schematic structural view of a heat exchange-enhanced sintered ore heat recovery apparatus according to an embodiment of the present invention, referring to fig. 7, which has substantially the same structure as the multi-compartment heat exchange sintered ore heat recovery apparatus shown in fig. 5, but is provided with a bypass pipe on a connection path between the off-compartment heat exchanger 4 and the second sub-heat exchange compartment wind distribution device 32, a first sub-heat exchange compartment air inlet hole 24 on the first sub-heat exchange compartment housing 13, and a partition wall air guide hole 16 on the partition wall 15 such that a part of circulated wind from the air circulation fan 45 enters the first sub-heat exchange compartment 2 via the bypass pipe and the first sub-heat exchange compartment air inlet hole 24, and then returns to the second sub-heat exchange compartment 3 via the partition wall air guide hole 16, on the basis of the heat recovery apparatus of fig. 5. A second air regulating valve 47 is provided in the bypass line for regulating the amount of air supplied to the first sub heat exchange chamber 2.
In this way, the circulated air is divided into two paths, and one path of main air flow (most of the air is about 95 percent) is directly connected into the second sub heat exchange bin 3 (large particle heat exchange bin) to exchange heat with the large particle sinter; the other path of auxiliary air flow (a few, about 5% of air) enters the lower part of the first sub heat exchange bin 2 (the small particle heat exchange bin), the low-temperature sinter area in the small particle heat exchange bin is subjected to enhanced heat transfer, finally enters the large particle heat exchange bin through the dividing wall air guide hole, and finally enters the out-of-bin heat exchanger together after being converged with the main air flow.
In the invention, trace circulating air is adopted to strengthen heat transfer at the low-temperature section of the small-particle sintered ore heat exchange bin, so that the heat transfer coefficient of the low-temperature small-particle sintered ore is further improved, the waste heat recovery efficiency is improved, and the arrangement of heating surface pipelines at the lower part of the first sub heat exchange bin 2 can be reduced.
In the second sub heat exchange bin 3, the waste heat recovery efficiency of the large-particle sintered ore is related to the air flow speed of the circulating air, and fig. 4 exemplarily shows the relationship between the air flow speed and the heat transfer coefficient, and by reasonably setting the air flow speed of the circulating air, a better waste heat recovery efficiency can be obtained.
Fig. 8 is a schematic structural view of a heat exchange enhanced sinter waste heat recovery apparatus according to another embodiment of the invention, wherein the air inlet holes 24 of the first sub heat exchange bin are arranged into a plurality of rows of spaced air inlet hole groups; and the dividing wall air vents 16 are arranged in a plurality of spaced apart air vent groups. The rows of first sub-heat exchange cartridge inlet holes 24 are vertically spaced apart and the rows of dividing wall air guide holes 16 are also vertically spaced apart. The number of the division wall air holes 16 can be the same as the first sub heat exchange chamber air inlet holes 24, and the arrangement mode and the height of the division wall air holes 16 can be the same as the first sub heat exchange chamber air inlet holes 24. Preferably, the vertical height of the dividing wall air vent 16 is higher than the vertical height of the first sub heat exchange compartment air inlet aperture 24 so that the air flow is directed towards the upper portion of the second sub heat exchange compartment 3.
Fig. 9 shows a sinter waste heat recovery apparatus for enhancing heat exchange according to still another embodiment of the invention, wherein the air flow in the low temperature section for enhancing the first sub heat exchange chamber 2 directly enters the first sub heat exchange chamber 2 through the low level air guide holes 57 provided in the partition wall 15.
Fig. 10 is a schematic structural view of a heat exchange-enhanced sintered ore waste heat recovery apparatus according to still another embodiment of the present invention, which adds an enhanced air flow circulation path to the waste heat recovery apparatus of fig. 6. Wherein the waste heat recovery device is configured such that a part of the circulating gas sequentially passes through the first sub heat exchange bin 2 and the third sub heat exchange bin 53 and then enters the second sub heat exchange bin 3. Therefore, the first sub heat exchange bin air inlet hole 24 is arranged on the first sub heat exchange bin shell 13, the partition wall air guide hole 16 is arranged on the partition wall 15, the additional partition wall air guide hole 56 is arranged on the additional partition wall 52, and the vertical height of the additional partition wall air guide hole 56 is higher than that of the first sub heat exchange bin air inlet hole 24, and the vertical height of the partition wall air guide hole 16 is higher than that of the additional partition wall air guide hole 56.
Fig. 11 is a schematic structural view of a heat exchange enhanced sintered ore waste heat recovery apparatus according to still another embodiment of the present invention, which is different from the embodiment of fig. 7 in that: it is not provided with the first sub heat exchange chamber inlet port 24. Alternatively, a bypass duct is provided on the connection path between the off-board heat exchanger 4 and the second sub-heat exchange bin air distribution device 32, a first sub-heat exchange bin air distribution device 58 is provided in the first sub-heat exchange bin 2, the bypass duct is in communication with the first sub-heat exchange bin air distribution device 58, and the dividing wall 15 is provided with the dividing wall air guide hole 16 such that a portion of the circulating air from the air circulation fan 45 enters the first sub-heat exchange bin 2 via the bypass duct and the first sub-heat exchange bin air distribution device 58, and then returns to the second sub-heat exchange bin 3 via the dividing wall air guide hole 16.
According to another aspect of the present invention, there is provided a heat exchange enhanced sinter waste heat recovery method employing the heat exchange enhanced sinter waste heat recovery apparatus according to any one of the preceding embodiments.
According to a preferred embodiment of the present invention, the waste heat recovery method includes:
supplying sinter into the heat exchange bin 1 through the sinter feed inlet 11;
the sinter of relatively smaller particle size from the sinter feed 11 is directed into the first sub-heat exchange bin 2, while the sinter of relatively larger particle size is directed into the second sub-heat exchange bin 3;
recovering heat of the sintered ore in the first sub heat exchange bin 2 by utilizing heat exchange equipment in the first sub heat exchange bin 2;
introducing air flow into the second sub heat exchange bin 3, and absorbing heat of the sintered ore in the second sub heat exchange bin 3 by utilizing the air flow;
discharging the air flow in the second sub heat exchange bin 3 to an off-bin heat exchanger 4, and recovering heat of the air flow discharged from the second sub heat exchange bin 3 by using the off-bin heat exchanger 4; and
supplying a portion of the air flow from the off-board heat exchanger 4 to the first sub-heat exchange cartridge 2; the other part is sent back to the second sub heat exchange bin air distribution device 32.
According to a preferred embodiment of the invention, the amount of air flow of said one part is smaller than the amount of air flow of said other part.
According to the sinter waste heat recovery device and the recovery method for enhanced heat exchange, the heat exchange bin is divided into more than two sub heat exchange bins, the sinter screen is utilized to separate large and small particle sinters, the waste heat of the small particle sinters is recovered by direct heat exchange, the waste heat of the large particle sinters is recovered by circulating air flow, part of the circulating air is introduced into the low-temperature area of the small particle sinters heat exchange bin, the heat transfer coefficient of the sinters in the low-temperature area is enhanced by a small amount of air, the process of recovering the waste heat of the sinters is optimized, and the waste heat recovery efficiency is improved.
The working process of the waste heat recovery device is described below by taking the sinter waste heat recovery device with enhanced heat exchange of fig. 7 as an example.
The high-temperature sinter from the sintering machine enters a waste heat recovery device from a sinter feed inlet 11, is screened on a sinter screen 12 into small-particle sinter and large-particle sinter, the small-particle sinter enters a first sub heat exchange bin 2, and the large-particle sinter enters a second sub heat exchange bin 3. The small-particle sintered ore slowly moves from top to bottom under the action of gravity in the first sub heat exchange bin 2, and is discharged from the first sub heat exchange bin discharger 25 after being fully heat exchanged and cooled with the superheater 21, the first evaporator 22 and the first economizer 23 in sequence. The large-particle sintered ore is piled up in the second sub heat exchange bin 3 to a certain height, about 1/2-2/3 of the height of the second sub heat exchange bin 3, circulating air is fed into the second sub heat exchange bin 3 from the second sub heat exchange bin air distribution device 32, flows from bottom to top to exchange heat with the large-particle sintered ore fully, and the cooled large-particle sintered ore is discharged from the second sub heat exchange bin discharger 33 at the bottom; the hot circulating air flows out from a warm air outlet 31 arranged at the upper part of the second sub heat exchange bin housing 14 and enters the out-bin heat exchanger 4.
The hot circulating air enters the external heat exchanger 4 and then sequentially flushes the second evaporator 42 and the second economizer 43, and the cooled circulating air is subjected to dust removal by the dust remover 44, boosted by the air circulating fan 45 and then sent to the waste heat recovery device again.
The circulating air sent out from the air circulating fan 45 is divided into two paths, one path is sent into the second sub heat exchange bin air distribution device 32 after the specific flow (about 95-97% of the total amount) is regulated by the first air regulating valve 46, and the air flows upwards after flow equalization to exchange heat with the large-particle sintered ore; the other path of the air is sent to the low-temperature heat exchange section of the first sub heat exchange bin 2 through the air inlet 24 of the first sub heat exchange bin after the specific flow (about 3-5% of the total amount) is regulated by the second air regulating valve 47, the air flows between the first economizer 23 and the small-particle sintered ore, the heat transfer coefficient of the sintered ore and the first economizer 23 at low temperature is enhanced, and finally the air enters the second sub heat exchange bin 3 through the partition wall air guide hole 16 arranged on the partition wall 15, and flows out from the temperature-rising air outlet 31 together after being mixed with the circulating air of the second sub heat exchange bin 3.
By adopting the waste heat recovery device and the waste heat recovery method, the waste heat recovery efficiency of the sinter is high, and the advantages of two different waste heat recovery processes aiming at large-particle sinter and small-particle sinter are fully exerted due to the screening of the particle size of the sinter, and the defects of the two different waste heat recovery processes are avoided; the waste heat recovery is carried out on the large particles in an indirect mode of air circulation cooling, so that the resistance of air flow is reduced; the recovery process of direct heat exchange between the sintering ore and the heating surface pipeline is adopted for the small-particle sintering ore, so that the problem of blockage of large particles is prevented, and the heat transfer coefficient of the low-temperature section of the small-particle sintering ore is enhanced by adopting a trace amount of air, so that the waste heat recovery efficiency is further improved.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes may be made in these embodiments without departing from the principles and spirit of the invention. The scope of applicability of the present invention is defined by the appended claims and equivalents thereof.
List of reference numerals:
1. heat exchange bin
2. First sub heat exchange bin
3. Second sub heat exchange bin
4. External heat exchanger
11. Sinter feed inlet
12. Sintered ore screen
13. First sub heat exchange bin shell
14. Second sub heat exchange bin shell
15. Dividing wall
16. Air guide hole of partition wall
21. Superheater with a heat exchanger
22. First evaporator
23. First economizer
24. Air inlet hole of first sub heat exchange bin
25. First sub heat exchange bin discharger
31. Heating air outlet
32. Second sub heat exchange bin air distribution device
33. Second sub heat exchange bin discharger
41. Outside-cabin heat exchanger shell
42. Second evaporator
43. Second economizer
44. Dust remover
45. Air circulation fan
46. First air regulating valve
47. Second air regulating valve
51. Additional screen
52. Additional dividing wall
53. Third sub heat exchange bin
54. Additional heat exchanger
55. Third sub heat exchange bin discharger
56. Air guide hole with additional dividing wall
57. Low position air guide hole
58. The first sub heat exchange bin wind distribution device.
Claims (8)
1. The utility model provides a sintering deposit waste heat recovery device of many storehouses heat transfer, waste heat recovery device includes heat transfer storehouse (1), its characterized in that:
the heat exchange bin (1) comprises at least two separated sub heat exchange bins, the at least two sub heat exchange bins are respectively used for accommodating sintered ores with different particle size ranges, and the heat exchange mode of one sub heat exchange bin in the at least two sub heat exchange bins is different from that of the other sub heat exchange bin;
the heat exchange bin (1) comprises:
a sinter feed inlet (11);
the first sub heat exchange bin (2) is communicated with the sinter feeding hole (11);
the second sub heat exchange bin (3) is arranged at the side of the first sub heat exchange bin (2) and is communicated with the sinter feeding port (11); and
a dividing wall (15) which is vertically upwards extended between the first sub heat exchange bin (2) and the second sub heat exchange bin (3),
the waste heat recovery device comprises a first sub heat exchange bin (3), a first sub heat exchange bin air distribution device (32) and a waste heat recovery device, wherein the first sub heat exchange bin air distribution device (32) is arranged on the vertical lower side of the first sub heat exchange bin (3), the waste heat recovery device further comprises an out-bin heat exchanger (4) which is arranged on the outer side of the heat exchange bin (1), and the out-bin heat exchanger (4) is in fluid communication with the first sub heat exchange bin (3) and is used for recovering heat of air flow discharged from the first sub heat exchange bin (3);
wherein the waste heat recovery device also comprises an air circulation fan (45) and a first air regulating valve (46), the air circulation fan (45) and the first air regulating valve (46) are arranged on a connecting passage between the outside heat exchanger (4) and the second sub heat exchange bin air distribution device (32),
a bypass pipeline is arranged on a connecting passage between the outside heat exchanger (4) and the second sub heat exchange bin air distribution device (32), a first sub heat exchange bin air inlet hole (24) is arranged on the first sub heat exchange bin shell (13), and a partition wall air guide hole (16) is arranged on the partition wall (15), so that part of circulating air from an air circulating fan (45) enters the first sub heat exchange bin (2) through the bypass pipeline and the first sub heat exchange bin air inlet hole (24), then returns to the second sub heat exchange bin (3) through the partition wall air guide hole (16), and a second air regulating valve (47) is arranged on the bypass pipeline and is used for regulating the air supply amount supplied to the first sub heat exchange bin (2);
the heat exchange bin (1) further comprises a third sub heat exchange bin (53) and an additional screen (51), wherein the third sub heat exchange bin (53) is arranged between the first sub heat exchange bin (2) and the second sub heat exchange bin (3) and is communicated with the sinter feeding port (11);
wherein an additional heat exchange device (54) is arranged in the third sub heat exchange bin (53);
the horizontal spacing between the heat exchange tubes of the additional heat exchange device (54) is greater than the horizontal spacing between the heat exchange tubes of the at least one heat exchange device of the first sub heat exchange cartridge (2).
2. The multi-bin heat exchange sinter waste heat recovery apparatus as claimed in claim 1, wherein the heat exchange bin (1) further comprises:
a sinter screen (12) arranged below the sinter feed inlet (11),
wherein the first sub heat exchange bin (2) comprises at least one heat exchange device, and the second sub heat exchange bin air distribution device (32) is configured to supply air flow vertically upwards in the vertical direction into the second sub heat exchange bin (3);
wherein the sinter screen (12) is configured to direct sinter of relatively smaller particle size from the sinter feed (11) into the first sub-heat exchange bin (2) and to direct sinter of relatively larger particle size into the second sub-heat exchange bin (3).
3. The multi-bin heat exchange sinter waste heat recovery apparatus as claimed in claim 2, wherein:
the external heat exchanger (4) comprises at least one heat exchange device, the second sub heat exchange bin (3) is provided with a heating air outlet (31), the heating air outlet (31) is in fluid communication with the inlet of the external heat exchanger (4), and the outlet of the external heat exchanger (4) is in fluid communication with the second sub heat exchange bin air distribution device (32).
4. The multi-bin heat exchange sinter waste heat recovery apparatus as claimed in claim 3, wherein:
at least one heat exchange device of the first sub heat exchange bin (2) comprises a superheater, an evaporator and/or an economizer; and/or
At least one heat exchange device of the off-board heat exchanger (4) comprises a superheater, an evaporator and/or an economizer.
5. The multi-bin heat exchange sinter waste heat recovery apparatus as claimed in claim 3, wherein:
the waste heat recovery device further comprises a dust remover (44), and the dust remover (44) is arranged on a connecting passage between the off-bin heat exchanger (4) and the second sub heat exchange bin air distribution device (32).
6. The multi-bin heat exchange sinter waste heat recovery apparatus as claimed in any one of claims 1 to 5, wherein:
the first sub heat exchange bin (2) comprises a first sub heat exchange bin discharger (25) which is arranged on the vertical lower side of the first sub heat exchange bin (2); and the second sub heat exchange bin (3) comprises a second sub heat exchange bin discharger (33) which is arranged on the vertical lower side of the second sub heat exchange bin (3).
7. The multi-bin heat exchange sinter waste heat recovery apparatus as claimed in any one of claims 2 to 5, wherein:
the sintering ore screen (12) is arranged above the first sub heat exchange bin (2), and the additional screen (51) is arranged above the third sub heat exchange bin (53); and the pore size of the additional screen (51) is larger than that of the sinter screen (12).
8. A multi-bin heat exchange sinter waste heat recovery method is characterized in that: the waste heat recovery method adopts the multi-bin heat exchange sinter waste heat recovery device according to any one of claims 1 to 7.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210309193.3A CN114705054B (en) | 2022-03-25 | 2022-03-25 | Multi-bin heat exchange sinter waste heat recovery device and recovery method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210309193.3A CN114705054B (en) | 2022-03-25 | 2022-03-25 | Multi-bin heat exchange sinter waste heat recovery device and recovery method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114705054A CN114705054A (en) | 2022-07-05 |
| CN114705054B true CN114705054B (en) | 2023-10-27 |
Family
ID=82169817
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210309193.3A Active CN114705054B (en) | 2022-03-25 | 2022-03-25 | Multi-bin heat exchange sinter waste heat recovery device and recovery method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114705054B (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202018025U (en) * | 2011-01-12 | 2011-10-26 | 熊天渝 | High temperature sintering mineral aggregate cooling and waste heat steam generator integration device |
| KR20140025650A (en) * | 2012-08-21 | 2014-03-05 | 재단법인 포항산업과학연구원 | Apparatus for recovering sensible heat |
| WO2014064508A1 (en) * | 2012-10-22 | 2014-05-01 | Gioacchino Nardin | Apparatus and method to transfer heat energy by means of phase change materials |
| CN104990421A (en) * | 2015-07-10 | 2015-10-21 | 无锡亿恩科技股份有限公司 | Novel efficient sinter sensible heat recovery technology |
| JP2019143937A (en) * | 2018-02-23 | 2019-08-29 | 株式会社神戸製鋼所 | Exhaust heat recovery device |
| CN212482137U (en) * | 2020-05-11 | 2021-02-05 | 杨白美 | Waste heat recovery system of mechanical high-temperature furnace |
| CN113899220A (en) * | 2021-10-21 | 2022-01-07 | 榆林学院 | Magnesium slag waste heat utilization system |
| CN215598119U (en) * | 2021-06-25 | 2022-01-21 | 四川川锅锅炉有限责任公司 | Boiler heat exchange bin and high-temperature sinter waste heat recovery device |
| CN215723321U (en) * | 2021-08-17 | 2022-02-01 | 四川川锅锅炉有限责任公司 | Hot broken income stove device of hot sieve of high temperature mineral aggregate |
-
2022
- 2022-03-25 CN CN202210309193.3A patent/CN114705054B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202018025U (en) * | 2011-01-12 | 2011-10-26 | 熊天渝 | High temperature sintering mineral aggregate cooling and waste heat steam generator integration device |
| KR20140025650A (en) * | 2012-08-21 | 2014-03-05 | 재단법인 포항산업과학연구원 | Apparatus for recovering sensible heat |
| WO2014064508A1 (en) * | 2012-10-22 | 2014-05-01 | Gioacchino Nardin | Apparatus and method to transfer heat energy by means of phase change materials |
| CN104870925A (en) * | 2012-10-22 | 2015-08-26 | 达涅利机械设备股份公司 | Apparatus and method to transfer heat energy by means of phase change materials |
| CN104990421A (en) * | 2015-07-10 | 2015-10-21 | 无锡亿恩科技股份有限公司 | Novel efficient sinter sensible heat recovery technology |
| JP2019143937A (en) * | 2018-02-23 | 2019-08-29 | 株式会社神戸製鋼所 | Exhaust heat recovery device |
| CN212482137U (en) * | 2020-05-11 | 2021-02-05 | 杨白美 | Waste heat recovery system of mechanical high-temperature furnace |
| CN215598119U (en) * | 2021-06-25 | 2022-01-21 | 四川川锅锅炉有限责任公司 | Boiler heat exchange bin and high-temperature sinter waste heat recovery device |
| CN215723321U (en) * | 2021-08-17 | 2022-02-01 | 四川川锅锅炉有限责任公司 | Hot broken income stove device of hot sieve of high temperature mineral aggregate |
| CN113899220A (en) * | 2021-10-21 | 2022-01-07 | 榆林学院 | Magnesium slag waste heat utilization system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114705054A (en) | 2022-07-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102560089B (en) | Magnetic roasting system and process for powder of refractory iron ore | |
| CN101538632B (en) | Preparation process and device of sponge iron | |
| CN101591731B (en) | Reduction roasting method and device for high-valence manganese ores | |
| CN101995016B (en) | Circulating fluidized bed boiler device using low calorific value coal gangue for post ignition | |
| CN105021049B (en) | Vertical type cooling tower and sintering waste heat utilization system | |
| CN104313308B (en) | Iron ore low-carbon sintering method | |
| CN104988255A (en) | Method and equipment system for recycling liquid slag waste heat and super-micronizing tailings | |
| CN107144142A (en) | Using the sintering deposit exhaust heat recovering method of chamber type sintering ore deposit waste-heat recovery device | |
| CN101949537A (en) | Circulating fluidized bed boiler bottom slag cooling system | |
| CN106482530A (en) | A kind of sintering deposit multipot type heat recovering device and sensible heat recovery method | |
| CN114705054B (en) | Multi-bin heat exchange sinter waste heat recovery device and recovery method | |
| CN114608335B (en) | Sinter waste heat recovery device and recovery method for enhanced heat exchange | |
| CN107881349A (en) | A kind of based shaft kiln directly reduced technique of the coal of lateritic nickel ore | |
| CN205448721U (en) | Hot DRI cooling device of rotary hearth furnace | |
| CN201433222Y (en) | Internally-externally-heating sponge iron reduction device | |
| CN209960986U (en) | Closed three-stage vertical cold sinter cooling system | |
| CN209702654U (en) | A kind of high temperature carbonization assembly of reduction furnace | |
| CN201381333Y (en) | Iron-bearing material suspension two-stage fast reducing furnace | |
| CN2921740Y (en) | Internal and external heating vertical passway reduction furnace | |
| CN101307372A (en) | Device for manufacturing and reducing crust pellet and production process | |
| CN206683419U (en) | A kind of chamber type sintering ore deposit waste-heat recovery device | |
| CN109652099A (en) | A kind of high temperature carbonization assembly of reduction furnace | |
| CN201250262Y (en) | System for producing iron ore concentrate by utilizing gold extraction waste slag | |
| CN108330273A (en) | A kind of iron ore roasting Magnitizing method and equipment | |
| CN114812203B (en) | Waste heat recovery device and recovery method based on heat conduction particle enhanced heat transfer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |