CN111829349A - Heat exchange launder flat plate and slag heat recovery processing system - Google Patents
Heat exchange launder flat plate and slag heat recovery processing system Download PDFInfo
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- CN111829349A CN111829349A CN202010594994.XA CN202010594994A CN111829349A CN 111829349 A CN111829349 A CN 111829349A CN 202010594994 A CN202010594994 A CN 202010594994A CN 111829349 A CN111829349 A CN 111829349A
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- heat exchange
- heat
- slag
- launder
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- 239000002893 slag Substances 0.000 title claims abstract description 78
- 238000011084 recovery Methods 0.000 title claims abstract description 23
- 229910001338 liquidmetal Inorganic materials 0.000 claims abstract description 21
- 238000005338 heat storage Methods 0.000 claims abstract description 16
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 12
- 239000010959 steel Substances 0.000 claims abstract description 12
- 238000005096 rolling process Methods 0.000 claims abstract description 10
- 239000011232 storage material Substances 0.000 claims abstract description 10
- 230000008859 change Effects 0.000 claims abstract description 7
- 238000003723 Smelting Methods 0.000 claims description 4
- 239000011819 refractory material Substances 0.000 claims description 3
- 238000010079 rubber tapping Methods 0.000 claims 1
- 239000002918 waste heat Substances 0.000 abstract description 11
- 238000004134 energy conservation Methods 0.000 abstract description 4
- 230000009467 reduction Effects 0.000 abstract description 4
- 238000009776 industrial production Methods 0.000 abstract description 3
- 238000010248 power generation Methods 0.000 abstract description 3
- 229920006395 saturated elastomer Polymers 0.000 abstract description 3
- 210000004722 stifle Anatomy 0.000 abstract 2
- 238000000034 method Methods 0.000 description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 238000010791 quenching Methods 0.000 description 12
- 230000000171 quenching effect Effects 0.000 description 12
- 239000007788 liquid Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000005997 Calcium carbide Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
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
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/15—Tapping equipment; Equipment for removing or retaining slag
- F27D3/1545—Equipment for removing or retaining slag
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/04—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being hot slag, hot residues, or heated blocks, e.g. iron blocks
-
- 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
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
-
- 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
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
- F27D2017/007—Systems for reclaiming waste heat including regenerators
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Manufacture Of Iron (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
The invention discloses a heat exchange launder plate and a slag heat recovery treatment system, wherein the heat exchange launder plate comprises a cavity surrounded by steel plates, a heat exchange pipeline is arranged in the cavity, and liquid metal flows in the heat exchange pipeline; the interior of the cavity is also filled with a phase change heat storage material; the upper part cover plate of the cavity is a heat-resistant steel plate, and the slag heat recovery treatment system comprises a heat exchange launder flat plate and a steam generator; the heat exchange pipeline is connected with the steam generator through an external pipeline, the heat exchange launder plate is obliquely placed, the heat exchange launder plate further comprises a hot stifle tank, slag poured on the heat exchange launder plate flows into the hot stifle tank along the heat exchange launder plate, and a rolling crushing device is arranged above the heat exchange launder plate. The waste heat contained in the molten slag is recycled by utilizing the high-temperature flowing heat exchange of the liquid metal and the heat storage principle of the phase-change heat storage material, and saturated steam under set pressure is generated for industrial production application or power generation, so that the purposes of energy conservation and emission reduction are achieved.
Description
Technical Field
The invention relates to a method for treating waste heat of molten slag in the smelting industry, belongs to the field of solid waste treatment, and particularly relates to a heat exchange launder flat plate and a molten slag heat recovery treatment system.
Background
At present, a lot of slag treatment methods are available, and relatively mature industrial methods include a hot splashing method, a hot stuffiness method, a water quenching method, a wind quenching method and the like. The hot splashing method can treat various forms of slag, but has long treatment period, large occupied area and serious environmental pollution. After the tank-type hot-seal method is improved by three generations, solid slag enters a tank from the initial temperature of about 800 ℃ to the current liquid slag directly enters the tank, the adaptability of treating the slag is enlarged, and meanwhile, the stability of the treated slag is good; however, the pool type hot-sealing treatment method is mainly performed by engineering machinery, and has a low degree of automation and a poor post working environment. The air quenching method is similar to the water quenching method except that the cooling medium is different. The air quenching method and the water quenching method can only treat liquid slag, and meanwhile, the slag grinding power consumption after the treatment of the air quenching method and the water quenching method is high.
The existing slag heat treatment method does not fundamentally solve the problem of effective recycling of a large amount of waste heat carried by slag, which not only causes excessive waste of energy, but also seriously pollutes the atmospheric environment.
To solve this problem, the present invention is hereby proposed.
Disclosure of Invention
The invention aims to provide a heat exchange launder plate, which can realize heat storage and heat energy exchange by utilizing the high-temperature flowing heat exchange of liquid metal and the heat storage principle of a phase change heat storage material.
The purpose of the invention can be realized by the following technical scheme:
a heat exchange launder plate comprises a cavity defined by steel plates, wherein a heat exchange pipeline is arranged in the cavity, and liquid metal flows in the heat exchange pipeline; the interior of the cavity is also filled with a phase change heat storage material.
The liquid slag is poured on the heat exchange launder flat plate, and the heat of the liquid slag on the slag launder flat plate is transferred to the liquid metal flowing in the internal heat exchange pipeline by the waste heat contained in the slag.
Furthermore, the upper part cover plate of the cavity is a heat-resistant steel plate, and the heat-resistant steel plate and the heat exchange pipeline are welded into a whole.
Preferably, the heat exchange pipe is of a serpentine pipe structure.
Furthermore, the periphery of the cavity is wrapped with refractory materials, and the heat exchange pipeline comprises an inlet and an outlet.
The invention also aims to provide a slag heat recovery processing system, which realizes the recovery and utilization of waste heat contained in slag, achieves the purposes of energy conservation and emission reduction, solves the problems of dust, water vapor containing harmful gas and the like generated in the slag processing process by the traditional air quenching method and the water quenching method, and achieves the purposes of cleanness and environmental protection.
The purpose of the invention can be realized by the following technical scheme:
a slag heat recovery treatment system comprises a steam generator and the heat exchange launder flat plate; the heat exchange pipeline is connected with the steam generator through an external pipeline, and the heat exchange flow groove flat plate is obliquely arranged.
Preferably, the inlet and the outlet of the heat exchange launder plate are respectively connected with the steam generator through external pipes.
Furthermore, the recovery processing system also comprises a hot stuffy tank, and the slag poured on the heat exchange launder flat plate flows into the hot stuffy tank along the heat exchange launder flat plate.
Furthermore, an electromagnetic pump is arranged on the external pipeline; under the drive of the electromagnetic pump, the liquid metal carries heat into the steam generator.
The heat transfer of the liquid slag on the slag launder plate is utilized to transfer the residual heat contained in the slag to the liquid metal, the liquid metal after absorbing heat is driven by the electromagnetic pump to carry the heat to the steam generator, and the water in the steam generator is heated to generate saturated steam under a set pressure for industrial production application or power generation, so that the purposes of waste heat recovery, energy conservation and emission reduction are achieved.
Further, the slag ladle also comprises a slag ladle which receives the molten slag which flows out from the smelting furnace.
Further, a rolling crushing device is arranged above the heat exchange launder flat plate; the rolling crushing device reciprocates on the surface of the flow groove flat plate.
When liquid slag exchanges heat on the heat exchange launder flat plate, the roller above the heat exchange launder flat plate starts to roll on the heat exchange launder flat plate in a reciprocating manner, so that the slag is crushed into particles in the solidification process, the slag is prevented from caking in the heat exchange solidification process, and the heat exchange launder flat plate is used as a foundation for next slag hot smoldering.
Further, the steam generator is also provided with a pressure pump.
The slag particles after heat exchange and rolling crushing enter a hot stuffy tank to be hot stuffy into tiny particles, so that the stabilization treatment of the slag is realized.
The invention has the beneficial effects that:
according to the heat exchange launder plate and the slag heat recovery processing system, the waste heat contained in the slag is recycled by utilizing the high-temperature flowing heat exchange of liquid metal and the heat storage principle of a phase-change heat storage material, saturated steam under set pressure is generated for industrial production application or power generation, the purposes of energy conservation and emission reduction are achieved, meanwhile, the problems of dust, steam containing harmful gas and the like generated in the slag processing process by the traditional air quenching method and the water quenching method are solved, and the purposes of cleanness and environmental protection are achieved.
Drawings
The invention will be further described with reference to the accompanying drawings.
Fig. 1 is a schematic sectional view of the side of the heat exchange flow cell plate of the present invention.
Fig. 2 is a schematic top sectional view of the heat exchange launder plate of the present invention.
FIG. 3 is a schematic view of a slag heat recovery processing system according to the present invention.
Reference numerals:
1-slag ladle; 2-rolling a crushing device; 21-axis; 22-a belt; 22-roll teeth; 3-heat exchange flow groove flat plate; 31-a pipe; 32-heat resistant steel plate; 33-a phase change heat storage material; 34-; 4-hot-sealing the tank; 5-an electromagnetic pump; 6-a steam generator; 7-pressure pump.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
Referring to fig. 1-2, the heat exchange launder plate includes a cavity surrounded by steel plates, a heat exchange pipe 31 is disposed in the cavity, liquid metal flows in the heat exchange pipe 31, and a phase change heat storage material 33 is filled in the cavity. The upper part cover plate of the cavity is a heat-resistant steel plate 32, and the heat-resistant steel plate 32 and the heat exchange pipeline 31 are welded into a whole. The cavity is surrounded by a refractory material 34 which serves to protect the insulation.
The high-temperature flowing heat exchange of the liquid metal and the heat storage principle of the phase-change heat storage material realize the recycling of waste heat contained in the molten slag.
Preferably, the heat exchange pipe 31 is of a serpentine pipe structure, and the serpentine pipe structure heat exchange pipe 31 can form a convective heating surface and increase a heating area, so that the heat exchange efficiency of the liquid metal can be increased.
The heat exchange pipe 31 includes an inlet 311 and an outlet 312, and the inlet 311 and the outlet 312 are respectively connected with an external device through an external pipe.
Example 2
Referring to fig. 3, a slag heat recovery processing system includes a steam generator 6 and the heat exchange launder plate 3 of example 1; heat transfer pipeline 31 is connected with steam generator 6 through the outside pipeline, heat transfer launder flat plate 3 inclines to be placed, steam generator 6 arranges the oblique below of heat transfer launder flat plate 3 horizontal plane in.
The device also comprises a hot stuffy tank 4, and the slag poured on the heat exchange launder flat plate 3 flows into the hot stuffy tank 4 along the heat exchange launder flat plate 3.
When the heat exchange device works, the slag and the heat exchange launder plate exchange heat, liquid metal flows in the heat exchange pipeline, the slag and the heat exchange launder plate exchange heat and transfer the heat to the liquid metal flowing in the heat exchange pipeline, and the liquid metal carries the heat to enter the steam generator to exchange heat with water in the steam generator to generate high-pressure high-temperature water vapor; the temperature of the liquid metal after heat exchange is reduced, and the liquid metal returns to the heat exchange launder pipeline to absorb heat again, so that the circulation is realized.
An electromagnetic pump 5 is arranged on the external pipeline; the liquid metal carries heat into the steam generator 6 under the drive of the electromagnetic pump 5.
Also included is a slag ladle 1, which slag ladle 1 receives molten slag that has just flowed out of the smelting furnace.
When the slag ladle is used, the slag ladle filled with the slag is conveyed to the designated position of the heat exchange launder flat plate, the slag is poured, and the slag with the temperature of 1300-1600 ℃ is poured on the surface of the heat exchange launder flat plate to exchange heat with the heat exchange launder flat plate.
Preferably, a rolling crushing device 2 is arranged above the heat exchange launder flat plate 3; the rolling crushing device 2 reciprocates on the surface of the runner flat plate to crush the slag into particles and prevent the slag from caking.
The rolling crushing device 2 comprises a roller, the roller is driven to rotate by a belt 22 to drive a shaft 21 to rotate, a roller tooth 23 is arranged on the outer circumference of the roller, the minimum distance between the roller tooth 23 and a heat exchange launder flat plate is H, and the particle size of crushed slag is controlled by the H distance.
After the heat exchange of the slag and the heat exchange launder flat plate and the crushing of the rolling crushing device are completed, the temperature is reduced to 400-type slag and 500 ℃, the crushed slag enters a hot stuffy tank for hot stuffy, water is sprayed on the surface of the slag in the hot stuffy tank to generate steam, f-CaO and f-MgO are digested under alternating steam pressure to enable the slag to be automatically decomposed and pulverized, and the water spraying flow is automatically adjusted along with the change of the steam pressure in the hot stuffy tank. And when the temperature in the hot closed tank is lower than 100 ℃, stopping spraying water mist, opening a tank door to remove slag, and finishing the slag waste heat recovery treatment process.
The steam generator 6 is also fitted with a pressure pump 7.
In conclusion, the invention makes a technical innovation and improvement on the existing slag waste heat recovery treatment process by utilizing the high-temperature flowing heat exchange of liquid metal and the heat storage principle of the phase-change heat storage material, has high waste heat recovery efficiency, small occupied space, no pollution and high automation degree, and is suitable for the industries of metallurgy, calcium carbide, cement and chemical industry.
While there have been shown and described what are at present considered the fundamental principles and essential features of the invention and its advantages, it will be apparent to those skilled in the art that the invention is not limited to the details of the foregoing exemplary embodiments, but is capable of other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (10)
1. The heat exchange launder flat plate is characterized by comprising a cavity enclosed by steel plates, wherein a heat exchange pipeline (31) is arranged in the cavity, and liquid metal flows in the heat exchange pipeline (31); the interior of the cavity is also filled with a phase change heat storage material (33).
2. The heat exchange launder plate according to claim 1, characterized in that the upper part cover plate of the cavity is a heat resistant steel plate (32), said heat resistant steel plate (32) and heat exchange pipe (31) being welded in one piece.
3. The heat exchange launder plate according to claim 2, characterized in that said heat exchange tubes (31) are of serpentine tube structure.
4. The heat exchange launder plate according to claim 3, characterized in that the cavity is surrounded by refractory material (34), and that the heat exchange pipe (31) comprises an inlet (311) and an outlet (312).
5. A slag heat recovery treatment system, characterized by comprising a steam generator (6) and a heat exchange launder plate (3) according to any one of claims 1-4; the heat exchange pipe (31) is connected with the steam generator (6) through an external pipe, and the heat exchange flow groove flat plate (3) is obliquely arranged.
6. A slag heat recovery processing system according to claim 5, characterized in that the recovery processing system further comprises a hot stuffer tank (4), the slag poured on the heat exchange launder plate (3) flowing along the heat exchange launder plate (3) into the hot stuffer tank (4).
7. A slag heat recovery processing system according to claim 5 or 6, characterized in that the external pipe is provided with an electromagnetic pump (5); under the drive of the electromagnetic pump (5), the liquid metal carries heat into the steam generator (6).
8. A molten slag heat recovery treatment system according to claim 5 or 6, further comprising a slag ladle (1), said slag ladle (1) receiving molten slag just after tapping from the smelting furnace.
9. A slag heat recovery treatment system according to claim 5, characterized in that a roll crusher (2) is arranged above the heat exchange launder plate (3); the rolling crushing device (2) reciprocates on the surface of the runner flat plate.
10. A slag heat recovery processing system according to claim 5 or 6, characterized in that the steam generator (6) is further equipped with a pressure pump (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010594994.XA CN111829349A (en) | 2020-06-28 | 2020-06-28 | Heat exchange launder flat plate and slag heat recovery processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010594994.XA CN111829349A (en) | 2020-06-28 | 2020-06-28 | Heat exchange launder flat plate and slag heat recovery processing system |
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| Publication Number | Publication Date |
|---|---|
| CN111829349A true CN111829349A (en) | 2020-10-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010594994.XA Pending CN111829349A (en) | 2020-06-28 | 2020-06-28 | Heat exchange launder flat plate and slag heat recovery processing system |
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| Country | Link |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114381558A (en) * | 2022-01-17 | 2022-04-22 | 中冶节能环保有限责任公司 | Steel slag cooling and crushing rotary bed device |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08246014A (en) * | 1995-03-07 | 1996-09-24 | Nippon Steel Corp | Water-cooled molten slag trough for blast furnace |
| JP2001153568A (en) * | 1999-11-24 | 2001-06-08 | Masayuki Kosaka | Heat transfer equipment for molten slag |
| JP2001355009A (en) * | 2000-06-14 | 2001-12-25 | Kaihatsu Dengyo Kk | Heat exchanger for slag particles |
| CN102230036A (en) * | 2011-04-02 | 2011-11-02 | 中冶建筑研究总院有限公司 | Waste-heat pressure closed-loop thermal treatment method for molten steel slag |
| US20130154168A1 (en) * | 2011-12-15 | 2013-06-20 | Virgil Dewitt Perryman | Dry processing of, and thermal recovery from, slag |
| WO2013178205A1 (en) * | 2012-06-01 | 2013-12-05 | Kme Germany Gmbh & Co. Kg | Arrangement for solidifying in small pieces liquid slag occurring in metal production |
| CN111041137A (en) * | 2019-12-24 | 2020-04-21 | 孙厚才 | Blast furnace slag heat energy recovery system |
| CN212253673U (en) * | 2020-06-28 | 2020-12-29 | 孙厚才 | Heat exchange launder flat plate and slag heat recovery processing system |
-
2020
- 2020-06-28 CN CN202010594994.XA patent/CN111829349A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08246014A (en) * | 1995-03-07 | 1996-09-24 | Nippon Steel Corp | Water-cooled molten slag trough for blast furnace |
| JP2001153568A (en) * | 1999-11-24 | 2001-06-08 | Masayuki Kosaka | Heat transfer equipment for molten slag |
| JP2001355009A (en) * | 2000-06-14 | 2001-12-25 | Kaihatsu Dengyo Kk | Heat exchanger for slag particles |
| CN102230036A (en) * | 2011-04-02 | 2011-11-02 | 中冶建筑研究总院有限公司 | Waste-heat pressure closed-loop thermal treatment method for molten steel slag |
| US20130154168A1 (en) * | 2011-12-15 | 2013-06-20 | Virgil Dewitt Perryman | Dry processing of, and thermal recovery from, slag |
| WO2013178205A1 (en) * | 2012-06-01 | 2013-12-05 | Kme Germany Gmbh & Co. Kg | Arrangement for solidifying in small pieces liquid slag occurring in metal production |
| CN111041137A (en) * | 2019-12-24 | 2020-04-21 | 孙厚才 | Blast furnace slag heat energy recovery system |
| CN212253673U (en) * | 2020-06-28 | 2020-12-29 | 孙厚才 | Heat exchange launder flat plate and slag heat recovery processing system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114381558A (en) * | 2022-01-17 | 2022-04-22 | 中冶节能环保有限责任公司 | Steel slag cooling and crushing rotary bed device |
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