CN105627767A - Converter cogeneration system - Google Patents
Converter cogeneration system Download PDFInfo
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- CN105627767A CN105627767A CN201410624069.1A CN201410624069A CN105627767A CN 105627767 A CN105627767 A CN 105627767A CN 201410624069 A CN201410624069 A CN 201410624069A CN 105627767 A CN105627767 A CN 105627767A
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- China
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- steam
- steam turbine
- converter
- superheater
- condenser
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- 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
Abstract
The invention relates to a converter cogeneration system. The converter cogeneration system comprises a heat exchanger, a steam pocket, a heat reservoir, a superheater, a steam turbine, a condenser, an air-seal heater and a deaerator. A steam outlet of a converter is connected with the steam pocket through the heat exchanger. The top of the steam pocket is connected with a steam inlet of the heat reservoir through a pipe. A steam outlet of the heat reservoir is connected with a steam inlet of the steam turbine through the superheater. The steam turbine is connected with a generator. A pipe connected with the steam turbine is sequentially connected with a condensate pump, the air-seal heater, the deaerator, a water supply pump and the steam pocket. The condenser is arranged on a pipe through which the steam turbine is connected with the condensate pump. The converter cogeneration system has the beneficial effects that superheated steam is obtained through heating of the superheater, the water content is reduced, dry steam is further formed, the condensed water content of the steam turbine is reduced, the steam specific enthalpy can be increased through the superheater, and generating efficiency is improved; and after being subjected to deoxygenation of the deaerator, steam returns to the steam pocket for cycle use, so that water resources are saved. Meanwhile, the air-seal heater can further play a role in lowering the pressure.
Description
Technical field
The present invention relates to a kind of converter waste heat generating system.
Background technology
UTILIZATION OF VESIDUAL HEAT IN is energy-saving and cost-reducing important directions, in existing commercial production, in cogeneration, the turbine generating system of a part adopts saturated vapor as generation driving force, both utilized (waste heat) boiler to produce saturated vapor and generates electricity, and effectively utilized residual heat resources. When generating, waste heat boiler produces saturated vapor and is directly entered the interior acting of Steam Turbine, but there is certain problem in such mode: saturated vapor is containing for moist steam, water content is higher, the moisture content produced in expansion process in steam turbine is many, it is therefore necessary to consider that steam turbine low-pressure grade blade band water dries measure; Due to a large amount of condensed waters that saturated vapor produces in acting process, when steam turbine loses load suddenly, accumulate in rotor surface, machine in standing part surface and piping, condensed water in the separator of particularly big volume can flash-off of steam, cause that steam turbine is jeopardously accelerated, affect the normal operation of steam turbine, reduce generating efficiency.
Summary of the invention
For overcoming the deficiencies in the prior art, it is an object of the invention to provide a kind of converter waste heat generating system, reduce the steam turbine internal condensation water yield, it is ensured that steam turbine is properly functioning, improve generating efficiency.
For achieving the above object, the present invention is achieved through the following technical solutions:
A kind of converter waste heat generating system, including converter, heat exchanger, drum, thermal storage device, superheater, steam turbine, electromotor, condenser, sealing gland heater, condensate pump, oxygen-eliminating device, the steam (vapor) outlet of converter is connected with drum by heat exchanger, drum top is connected with thermal storage device air intake by pipeline, thermal storage device venthole is connected with steam turbine air intake by superheater, steam turbine is connected with electromotor, the road pipeline being connected with steam turbine successively with condensate pump, sealing gland heater, oxygen-eliminating device, feed pump, drum connects, the pipeline that steam turbine is connected with condensate pump is provided with condenser, leaving condenser water mouth is connected with cooling tower, cooling tower is connected with condenser water inlet by circulating cooling pump.
Compared with prior art, the invention has the beneficial effects as follows:
Being heated into superheated steam by superheater and reduce water content, and then become dry saturated steam, reduce the condensed water content of steam turbine, superheater can also improve specific steam enthalpy, improves generating efficiency; The condensed device condensation of steam after steam turbine acting generating, sealing gland heater heat exchanging part high-temperature steam return steam turbine, and the steam of the relatively low temperature of all the other condensations returns drum after oxygen-eliminating device deoxygenation, recycles, saving water resource. Meanwhile, sealing gland heater can also play the effect of decompression.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
In figure: 1-converter 2-heat exchanger 3-drum 4-thermal storage device 5-steam turbine 6-electromotor 7-superheater 8-condenser 9-cooling tower 10-circulating cooling pump 11-condensate pump 12-sealing gland heater 13-oxygen-eliminating device 14-feed pump 15-circulating pump.
Detailed description of the invention
Below in conjunction with Figure of description, the present invention is described in detail, it should be noted that the enforcement of the present invention is not limited to following embodiment.
See Fig. 1, converter waste heat generating system, including converter 1, heat exchanger 2, drum 3, thermal storage device 4, superheater 7, steam turbine 5, electromotor 6, condenser 8, sealing gland heater 12, condensate pump 11, oxygen-eliminating device 13, the steam (vapor) outlet of converter 1 is connected with drum 3 by heat exchanger 2, drum 3 top is connected with thermal storage device 4 air intake by pipeline, thermal storage device 4 venthole is connected with steam turbine 5 air intake by superheater 7, steam turbine 5 is connected with electromotor 6, the road pipeline being connected with steam turbine 5 successively with condensate pump 11, sealing gland heater 12, oxygen-eliminating device 13, feed pump 14, drum 3 connects, the pipeline that steam turbine 5 is connected with condensate pump 11 is provided with condenser 8, condenser 8 outlet is connected with cooling tower 9, cooling tower 9 is connected with condenser 8 water inlet by circulating cooling pump 10.
The saturated vapor that converter 1 produces is by entering thermal storage device 4 voltage stabilizing after drum 3 transfer, transfer the interval of the generation of converter 1, unstable steam to continual and steady steam, steam is by being heated into superheated steam, and then become dry saturated steam entrance steam turbine 5, doing work through steam turbine 5, electromotor 6 produces electric energy supplying power for outside; Sealing gland heater 12 is entered after the condensed device 8 heat exchange heat exchange of steam after acting, steam is after sealing gland heater 12 heat exchange, part high-temperature steam returns steam turbine 5, the steam of the relatively low temperature of all the other condensations returns drum 3 after oxygen-eliminating device 13 deoxygenation, squeeze into heat exchanger 2 through circulating pump 15 after saturated vapor deposition in drum 3, return drum 3 through the heating such as flue of converter 1 and recycle. Once there is hydropenia phenomenon in whole power generation process, from boiler by oxygen-eliminating device 13 moisturizing, whole circulating generation process can be entered. Cooling water in condenser 8 is circulated offer by cooling tower 9.
The present invention is heated into superheated steam by superheater and reduces water content, and then becomes dry saturated steam, reduces the condensed water content of steam turbine, and superheater can also improve specific steam enthalpy, improves generating efficiency; The condensed device condensation of steam after steam turbine acting generating, sealing gland heater heat exchanging part high-temperature steam return steam turbine, and the steam of the relatively low temperature of all the other condensations returns drum after oxygen-eliminating device deoxygenation, recycles, saving water resource. Meanwhile, sealing gland heater can also play the effect of decompression.
Claims (1)
1. a converter waste heat generating system, it is characterized in that, including converter, heat exchanger, drum, thermal storage device, superheater, steam turbine, electromotor, condenser, sealing gland heater, condensate pump, oxygen-eliminating device, the steam (vapor) outlet of converter is connected with drum by heat exchanger, drum top is connected with thermal storage device air intake by pipeline, thermal storage device venthole is connected with steam turbine air intake by superheater, steam turbine is connected with electromotor, the road pipeline being connected with steam turbine successively with condensate pump, sealing gland heater, oxygen-eliminating device, feed pump, drum connects, the pipeline that steam turbine is connected with condensate pump is provided with condenser, leaving condenser water mouth is connected with cooling tower, cooling tower is connected with condenser water inlet by circulating cooling pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410624069.1A CN105627767A (en) | 2014-11-08 | 2014-11-08 | Converter cogeneration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410624069.1A CN105627767A (en) | 2014-11-08 | 2014-11-08 | Converter cogeneration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105627767A true CN105627767A (en) | 2016-06-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410624069.1A Pending CN105627767A (en) | 2014-11-08 | 2014-11-08 | Converter cogeneration system |
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| CN (1) | CN105627767A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111272000A (en) * | 2020-01-21 | 2020-06-12 | 董荣华 | Slab vaporization cooling device and slab sensible heat recovery power generation system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101749961A (en) * | 2009-12-30 | 2010-06-23 | 北京世纪源博科技有限责任公司 | Sintering product line saturated steam afterheat generating system |
| CN101768652A (en) * | 2009-12-18 | 2010-07-07 | 南京凯盛开能环保能源有限公司 | Revolving furnace flue gas waste heat power generation system and method based on high-temperature heat carrier overheating |
| CN201819201U (en) * | 2010-10-13 | 2011-05-04 | 广东开能环保能源有限公司 | Glass furnace pure low-temperature waste heat generating system |
| CN204227926U (en) * | 2014-11-08 | 2015-03-25 | 国网辽宁省电力有限公司鞍山供电公司 | A kind of converter waste heat generating system |
-
2014
- 2014-11-08 CN CN201410624069.1A patent/CN105627767A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101768652A (en) * | 2009-12-18 | 2010-07-07 | 南京凯盛开能环保能源有限公司 | Revolving furnace flue gas waste heat power generation system and method based on high-temperature heat carrier overheating |
| CN101749961A (en) * | 2009-12-30 | 2010-06-23 | 北京世纪源博科技有限责任公司 | Sintering product line saturated steam afterheat generating system |
| CN201819201U (en) * | 2010-10-13 | 2011-05-04 | 广东开能环保能源有限公司 | Glass furnace pure low-temperature waste heat generating system |
| CN204227926U (en) * | 2014-11-08 | 2015-03-25 | 国网辽宁省电力有限公司鞍山供电公司 | A kind of converter waste heat generating system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111272000A (en) * | 2020-01-21 | 2020-06-12 | 董荣华 | Slab vaporization cooling device and slab sensible heat recovery power generation system |
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Application publication date: 20160601 |
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