CN203960236U - Blast furnace slag residual neat recovering system - Google Patents

Blast furnace slag residual neat recovering system Download PDF

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Publication number
CN203960236U
CN203960236U CN201420290065.XU CN201420290065U CN203960236U CN 203960236 U CN203960236 U CN 203960236U CN 201420290065 U CN201420290065 U CN 201420290065U CN 203960236 U CN203960236 U CN 203960236U
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heat exchanger
working medium
water
organic working
blast furnace
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CN201420290065.XU
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盖东兴
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Wisdri Engineering and Research Incorporation Ltd
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Wisdri Engineering and Research Incorporation Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Abstract

The utility model discloses a kind of blast furnace slag residual neat recovering system, comprise First Heat Exchanger, decompressor, generator, and the second interchanger, wherein, First Heat Exchanger is provided with water vapor passage and the first organic working medium heat exchanger channels, and the entrance of water vapor passage is communicated with the vapour outlet of grain slag tower; Decompressor is provided with the inlet mouth and the venting port that are communicated with the outlet of the first organic working medium heat exchanger channels; The second interchanger is provided with cooling-water duct and the second organic working medium heat exchanger channels, the entrance of the second organic working medium heat exchanger channels is communicated with venting port, outlet is communicated with the entrance of the first organic working medium heat exchanger channels, and the output shaft of decompressor is fixedly connected with to drive generator generating with the rotating shaft of generator.The blast furnace slag residual neat recovering system that the utility model provides, can avoid the corrosion of blast furnace slag quenching water impurity heat exchanger and pipeline, has improved the work-ing life of interchanger and pipeline.

Description

Blast furnace slag residual neat recovering system
Technical field
The utility model relates to metallurgical production heat recovery technology field, relates in particular to a kind of blast furnace slag residual neat recovering system.
Background technology
Blast-furnace smelting energy consumption accounts for 59% left and right of whole Iron and Steel Production energy consumption, is the first power consumption operation of Steel Plant.Blast furnace can produce a large amount of high temperature furnace slags in smelting process, and blast furnace slag is good cement additive after Water Quenching.In to blast furnace slag process Water Quenching process, can produce a large amount of blast furnace slag quenching waters, the temperature of blast furnace slag quenching water is generally below 85 DEG C, because containing plurality of inorganic salt and incrustation scale, it is difficult to utilize, cause energy dissipation, every production 1t molten iron produces approximately 0.3 blast furnace slag to 0.35t according to statistics, and blast furnace slag per ton is containing the heat of the 64kgce that has an appointment, and these heats substantially all enter flushing cinder water.
China's blast furnace slag quenching water UTILIZATION OF VESIDUAL HEAT IN technology is also relatively backward, interchanger is reclaimed to the heat in flushing cinder water, for heating buildings in northern China employing in winter.But blast furnace slag quenching water can corrode interchanger, thereby shortened the work-ing life of interchanger, in addition, in the season and southern Steel Plant of non-heating, blast furnace slag quenching water is not applied substantially, has not only wasted the energy and has also caused thermal pollution.
Utility model content
Main purpose of the present utility model is to provide a kind of blast furnace slag residual neat recovering system, be intended to stably reclaim in blast furnace slag with heat, avoid the corrosion of blast furnace slag quenching water impurity heat exchanger and pipeline simultaneously.
For achieving the above object, the utility model provides a kind of blast furnace slag residual neat recovering system, comprise for by water vapor thermal exchange in grain slag tower to the First Heat Exchanger of organic working medium, for described organic working medium heat being converted into the decompressor of mechanical work, for mechanical energy being converted into the generator of electric energy, and for the second interchanger of organic working medium described in condensation, wherein
Described First Heat Exchanger is provided with water vapor passage and the first organic working medium heat exchanger channels, the entrance of described water vapor passage is communicated with the vapour outlet of grain slag tower, and the organic working medium in the water vapor in described water vapor passage and described the first organic working medium heat exchanger channels is carried out heat exchange in described First Heat Exchanger;
Described decompressor is provided with the inlet mouth and the venting port that are communicated with the outlet of described the first organic working medium heat exchanger channels, and steam enters its inner output shaft rotation that drives described decompressor through the inlet mouth of described decompressor;
Described the second interchanger is provided with cooling-water duct and the second organic working medium heat exchanger channels, described second entrance of organic working medium heat exchanger channels and the venting port of described decompressor are communicated with, the outlet of described the second organic working medium heat exchanger channels is communicated with the entrance of described the first organic working medium heat exchanger channels, and described second entrance of organic working medium heat exchanger channels and the venting port of described decompressor are communicated with;
The output shaft of described decompressor is fixedly connected with to drive described generator generating with the rotating shaft of described generator.
Preferably, described blast furnace slag residual neat recovering system also comprises the organic working medium recycle pump between described the second interchanger and described First Heat Exchanger, one end of this organic working medium recycle pump is connected the entrance of described the first organic working medium heat exchanger channels by pipeline, the other end of described organic working medium recycle pump is connected the outlet of described the second organic working medium heat exchanger channels by pipeline.
Preferably, described blast furnace slag residual neat recovering system also comprises the circulating water channel being communicated with the outlet of the water vapor passage of described First Heat Exchanger, and the water outlet of this circulating water channel is communicated with the water jet of described grain slag tower.
Preferably, described blast furnace slag residual neat recovering system also comprises the water trap for blast furnace slag cooling grain slag tower being carried out to processed, and the entrance of this water trap is communicated with the slag notch of described grain slag tower, and the water outlet of described water trap is communicated with described circulating water channel.
Preferably, described circulating water channel is provided with the multistage overflow groove for separating of blast furnace slag.
Preferably, described overflow groove is also provided with the slag-drip opening for flowing out for isolated blast furnace slag, and this slag-drip opening is communicated with described water trap.
Preferably, described blast furnace slag residual neat recovering system also comprises the first slag stock pump between described water trap and the slag notch of described grain slag tower, the second slag stock pump between described slag-drip opening and described water trap, and water circulating pump between the water outlet of described circulating water channel and the water jet of described grain slag tower.
Preferably, described the first slag stock pump, the second slag stock pump and water circulating pump are variable frequency pump.
Preferably, described blast furnace slag residual neat recovering system also comprises the by-pass valve control of the steam outlet steam rates for controlling described grain slag tower, and this by-pass valve control is between the entrance of described water vapor passage and the vapour outlet of described grain slag tower.
The blast furnace slag residual neat recovering system the utility model proposes, be communicated with the vapour outlet of grain slag tower by First Heat Exchanger, heat in recycle-water steam is converted into after mechanical energy for generating, with respect to using liquid water to carry out recovery of heat in prior art, can avoid the corrosion of blast furnace slag quenching water impurity heat exchanger and pipeline, improve the work-ing life of interchanger and pipeline.In addition, this blast furnace slag residual neat recovering system is that the heat in the water vapor by grain slag tower is produced is converted into electric energy, is directly used in heating with respect to present technology, has improved the scope of application, make its time that can be used for not warming oneself and area, also can avoid thermal pollution simultaneously.Meanwhile, this blast furnace slag residual neat recovering system is the heat that absorbs water vapor by organic working medium, and the vaporization heat of organic working medium is large, uses less organic working medium can absorb the object of a large amount of heats.This blast furnace slag residual neat recovering system, realizes the cooling of blast furnace slag by the phase-change heat-exchange of water, can reduce the consumption of blast furnace slag quenching water, is conducive to water saving.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model blast furnace slag residual neat recovering system preferred embodiment.
Realization, functional characteristics and the advantage of the utility model object, in connection with embodiment, are described further with reference to accompanying drawing.
Embodiment
Should be appreciated that specific embodiment described herein is only in order to explain the utility model, and be not used in restriction the utility model.
The utility model proposes a kind of blast furnace slag residual neat recovering system.
With reference to Fig. 1, Fig. 1 is the structural representation of the utility model blast furnace slag residual neat recovering system preferred embodiment.It should be noted that, the direction in figure shown in arrow represents the loop direction of water (comprising that gaseous state is with liquid), blast furnace slag and organic working medium.
In this preferred embodiment, blast furnace slag residual neat recovering system, comprise for by water vapor thermal exchange in grain slag tower to the First Heat Exchanger 10 of organic working medium, for organic working medium heat being converted into the decompressor 20 of mechanical work, for mechanical energy being converted into the generator 30 of electric energy, and for the second interchanger 40 of condensation organic working medium, wherein
First Heat Exchanger 10 is provided with water vapor passage and the first organic working medium heat exchanger channels (water vapor passage and the first organic working medium heat exchanger channels are separate), the entrance of water vapor passage is communicated with the vapour outlet 50a of grain slag tower 50, and the organic working medium in the water vapor in water vapor passage and the first organic working medium heat exchanger channels is carried out heat exchange in First Heat Exchanger 10;
Decompressor 20 is provided with the inlet mouth being communicated with the outlet of the first organic working medium heat exchanger channels, and the venting port being communicated with the entrance of the second organic working medium heat exchanger channels, and steam enters its inner output shaft rotation that drives decompressor 20 through the inlet mouth of decompressor 20;
The second interchanger 40 is provided with cooling-water duct and the second organic working medium heat exchanger channels (cooling-water duct and the second organic working medium heat exchanger channels are separate), the entrance of the second organic working medium heat exchanger channels is communicated with the venting port of decompressor 20, the outlet of the second organic working medium heat exchanger channels is communicated with the entrance of the first organic working medium heat exchanger channels, and the entrance of the second organic working medium heat exchanger channels is communicated with the venting port of decompressor 20.Organic working medium in water coolant in cooling-water duct and the second organic working medium heat exchanger channels is carried out heat exchange in the second interchanger 40.Water-cooled tube 65 is communicated with the entrance of cooling-water duct, to inject water coolant in cooling-water duct.
The output shaft of decompressor 20 is fixedly connected with to drive generator 30 to generate electricity with the rotating shaft of generator 30.Decompressor 20 can be the various ways such as screw expander, turbo-expander, and the utility model is not construed as limiting this.
The specific works process of this blast furnace slag residual neat recovering system is as follows: first, the blast furnace slag in slag runner is poured grain slag tower 50 by water jet through grain slag tower 50, flushing cinder water vapor evaporation is produced a large amount of water vapors by the blast furnace slag of high temperature, water vapor enters in the first organic working medium heat exchanger channels, organic working medium generation heat exchange in First Heat Exchanger 10 inside and organic working medium heat exchanger channels, thereby make liquid organic working medium vaporization, the organic working medium of gaseous state enters into the inner expansion step-down of decompressor 20 and drives the output shaft of decompressor 20 to move, thereby drive generator 30 to generate electricity, finally, weary gas after expansion enters into the second interchanger 40, with the water coolant generation heat exchange in cooling-water duct in the second interchanger 40, be condensed into after liquid state, again enter into First Heat Exchanger 10, thereby form the recycle system of organic working medium, it is the blast furnace slag residual neat recovering system that the present embodiment proposes, circulate and the heat in water vapor is changed into the electric energy of high-quality by organic Rankine.
The blast furnace slag residual neat recovering system that the present embodiment proposes, be communicated with the vapour outlet 50a of grain slag tower 50 by First Heat Exchanger 10, heat in recycle-water steam is converted into after mechanical energy for generating, with respect to using liquid water to carry out recovery of heat in prior art, can avoid the corrosion of blast furnace slag quenching water impurity heat exchanger and pipeline, improve the work-ing life of interchanger and pipeline.In addition, this blast furnace slag residual neat recovering system is that the heat in the water vapor by grain slag tower 50 is produced is converted into electric energy, with respect to present technology, heat energy is directly used in to heating, has improved the scope of application, make its time that can be used for not warming oneself and area, also can avoid thermal pollution simultaneously.Meanwhile, this blast furnace slag residual neat recovering system is the heat that absorbs water vapor by organic working medium, and the vaporization heat of organic working medium is large, uses less organic working medium can reach the object that absorbs a large amount of heats.This blast furnace slag residual neat recovering system, realizes the cooling of blast furnace slag by the phase-change heat-exchange of water, can reduce the consumption of blast furnace slag quenching water, is conducive to water saving.
Further, this blast furnace slag residual neat recovering system also comprises the organic working medium recycle pump 61 between the second interchanger 40 and First Heat Exchanger 10, one end of this organic working medium recycle pump 61 is connected the entrance of the first organic working medium heat exchanger channels by pipeline, the other end of organic working medium recycle pump 61 is connected the outlet of the second organic working medium heat exchanger channels by pipeline.
Organic working medium recycle pump 61 produces power, make the organic working medium forced refluence in the second interchanger 40 enter into First Heat Exchanger 10, thereby avoid the situation of the organic working medium underfed that may occur in First Heat Exchanger 10, improved the job stability of this blast furnace slag residual neat recovering system.
Further, this blast furnace slag residual neat recovering system also comprises the circulating water channel 70 being communicated with the outlet of the water vapor passage of First Heat Exchanger 10, and the water outlet of this circulating water channel 70 is communicated with the water jet 50b of grain slag tower 50.
In the present embodiment, circulating water channel 70 can use the water conservancy after heat exchange with the outlet of the water vapor passage of First Heat Exchanger 10, the water in circulating water channel 70 can be again for the high temperature blast furnace slag of cooling grain slag tower 50, thereby reach the object of saving water source.
Further, this blast furnace slag residual neat recovering system also comprises the water trap 80 for blast furnace slag cooling grain slag tower 50 being carried out to processed, the entrance of this water trap 80 is communicated with the slag notch 50c of grain slag tower 50, and the water outlet of water trap 80 is communicated with circulating water channel 70.In water trap 80, be provided with the filtering net of one deck densification, separate to realize pulp water, water trap 80 needs to spray into a certain amount of water coolant in use in it, to ensure that the flushing cinder water in water trap 80 do not vaporize, and simultaneously can be to the moisturizing of whole blast furnace slag residual neat recovering system.The slag-drip opening place of water trap 80 is provided with transmission belt 90, to facilitate, the blast furnace slag after dehydration is sent to appointed place.Blast furnace slag after water trap 80 dehydrations can be used for producing other products.
In the present embodiment, the water outlet of water trap 80 is communicated with circulating water channel 70, thereby isolated water coolant in blast furnace slag is recycled in circulating water channel 70, can be used for again for cooling blast furnace slag, thereby further improved the utilization ratio of water in this blast furnace slag residual neat recovering system.
Further, circulating water channel 70 is provided with the multistage overflow groove 71 for separating of blast furnace slag.
Because isolated water in water trap 80 may contain part blast furnace slag, in the present embodiment, by be provided with the multistage overflow groove 71 for separating of blast furnace slag at circulating water channel 70, can reduce the probability of blast furnace slag obstruction waterway pipe.
Further, overflow groove 71 is also provided with the slag-drip opening for flowing out for isolated blast furnace slag, and this slag-drip opening is communicated with water trap 80.
In overflow groove 71, isolated blast furnace slag can be discharged in water trap 80 through slag-drip opening, through dehydration again, thereby has formed the recycle system that blast furnace slag reclaims, and has improved the utilization ratio of blast furnace slag.
Further, this blast furnace slag residual neat recovering system also comprises the first slag stock pump 62 between water trap 80 and the slag notch 50c of grain slag tower 50, the second slag stock pump 63 between slag-drip opening and water trap 80, and water circulating pump 64 between the water outlet of circulating water channel 70 and the water jet 50b of grain slag tower 50.
The blast furnace slag that the first slag stock pump 62 flows out the slag notch 50c of grain slag tower 50 is evacuated in water trap 80, the second slag stock pump 63 is evacuated in water trap 80 blast furnace slag in overflow groove 71 again to dewater, and water circulating pump 64 is evacuated to the water in circulating water channel 70 the water jet 50b of grain slag tower 50 for the blast furnace slag in cooling grain slag tower 50.
Further, the first slag stock pump, the second slag stock pump and water circulating pump are variable frequency pump.Variable frequency pump can accurately be controlled flow, thereby makes the flow control process of this blast furnace slag residual neat recovering system more accurate.
Further, this blast furnace slag residual neat recovering system also comprises the by-pass valve control 91 of the vapour outlet 50a place steam rates for controlling grain slag tower 50, and this by-pass valve control 91 is between the entrance of water vapor passage and the vapour outlet 50a of grain slag tower 50.
By-pass valve control 91 acting as herein: the one, control the flow that enters water vapor in First Heat Exchanger 10, can ensure that the interior steam of grain slag tower 50 has certain pressure, the 2nd, ensure that water vapor can successfully flow through First Heat Exchanger 10 and enter into circulating water channel 70.
These are only preferred embodiment of the present utility model; not thereby limit the scope of the claims of the present utility model; every equivalent structure transformation that utilizes the utility model specification sheets and accompanying drawing content to do; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present utility model.

Claims (9)

1. a blast furnace slag residual neat recovering system, it is characterized in that, comprise for by water vapor thermal exchange in grain slag tower to the First Heat Exchanger of organic working medium, for described organic working medium heat being converted into the decompressor of mechanical work, for mechanical energy being converted into the generator of electric energy, and for the second interchanger of organic working medium described in condensation, wherein
Described First Heat Exchanger is provided with water vapor passage and the first organic working medium heat exchanger channels, the entrance of described water vapor passage is communicated with the vapour outlet of grain slag tower, and the organic working medium in the water vapor in described water vapor passage and described the first organic working medium heat exchanger channels is carried out heat exchange in described First Heat Exchanger;
Described decompressor is provided with the inlet mouth and the venting port that are communicated with the outlet of described the first organic working medium heat exchanger channels, and steam enters its inner output shaft rotation that drives described decompressor through the inlet mouth of described decompressor;
Described the second interchanger is provided with cooling-water duct and the second organic working medium heat exchanger channels, described second entrance of organic working medium heat exchanger channels and the venting port of described decompressor are communicated with, the outlet of described the second organic working medium heat exchanger channels is communicated with the entrance of described the first organic working medium heat exchanger channels, and described second entrance of organic working medium heat exchanger channels and the venting port of described decompressor are communicated with;
The output shaft of described decompressor is fixedly connected with to drive described generator generating with the rotating shaft of described generator.
2. blast furnace slag residual neat recovering system as claimed in claim 1, it is characterized in that, also comprise the organic working medium recycle pump between described the second interchanger and described First Heat Exchanger, one end of this organic working medium recycle pump is connected the entrance of described the first organic working medium heat exchanger channels by pipeline, the other end of described organic working medium recycle pump is connected the outlet of described the second organic working medium heat exchanger channels by pipeline.
3. blast furnace slag residual neat recovering system as claimed in claim 1, is characterized in that, also comprises the circulating water channel being communicated with the outlet of the water vapor passage of described First Heat Exchanger, and the water outlet of this circulating water channel is communicated with the water jet of described grain slag tower.
4. blast furnace slag residual neat recovering system as claimed in claim 3, it is characterized in that, also comprise the water trap for blast furnace slag cooling grain slag tower being carried out to processed, the entrance of this water trap is communicated with the slag notch of described grain slag tower, and the water outlet of described water trap is communicated with described circulating water channel.
5. blast furnace slag residual neat recovering system as claimed in claim 4, is characterized in that, described circulating water channel is provided with the multistage overflow groove for separating of blast furnace slag.
6. blast furnace slag residual neat recovering system as claimed in claim 5, is characterized in that, described overflow groove is also provided with the slag-drip opening for flowing out for isolated blast furnace slag, and this slag-drip opening is communicated with described water trap.
7. blast furnace slag residual neat recovering system as claimed in claim 6, it is characterized in that, also comprise the first slag stock pump between described water trap and the slag notch of described grain slag tower, the second slag stock pump between described slag-drip opening and described water trap, and water circulating pump between the water outlet of described circulating water channel and the water jet of described grain slag tower.
8. blast furnace slag residual neat recovering system as claimed in claim 7, is characterized in that, described the first slag stock pump, the second slag stock pump and water circulating pump are variable frequency pump.
9. blast furnace slag residual neat recovering system as claimed in any of claims 1 to 8 in one of claims, it is characterized in that, also comprise the by-pass valve control of the steam outlet steam rates for controlling described grain slag tower, this by-pass valve control is between the entrance of described water vapor passage and the vapour outlet of described grain slag tower.
CN201420290065.XU 2014-06-03 2014-06-03 Blast furnace slag residual neat recovering system Active CN203960236U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103993109A (en) * 2014-06-03 2014-08-20 中冶南方工程技术有限公司 Blast furnace slag waste heat recovery system and recovering control method for blast furnace slag waste heat recovery system
CN110779339A (en) * 2019-11-16 2020-02-11 赵汉章 Blast furnace slag crushing and waste heat recovery system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103993109A (en) * 2014-06-03 2014-08-20 中冶南方工程技术有限公司 Blast furnace slag waste heat recovery system and recovering control method for blast furnace slag waste heat recovery system
CN110779339A (en) * 2019-11-16 2020-02-11 赵汉章 Blast furnace slag crushing and waste heat recovery system
CN110779339B (en) * 2019-11-16 2021-02-05 迁安市九江线材有限责任公司 Blast furnace slag crushing and waste heat recovery system

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