CN203518635U - Dry quenching furnace waste heat power generation system - Google Patents

Dry quenching furnace waste heat power generation system Download PDF

Info

Publication number
CN203518635U
CN203518635U CN201320408213.9U CN201320408213U CN203518635U CN 203518635 U CN203518635 U CN 203518635U CN 201320408213 U CN201320408213 U CN 201320408213U CN 203518635 U CN203518635 U CN 203518635U
Authority
CN
China
Prior art keywords
dry quenching
waste heat
quenching furnace
dry
coke
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.)
Expired - Lifetime
Application number
CN201320408213.9U
Other languages
Chinese (zh)
Inventor
闫庆林
马绿竹
王云鹏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Aofu Energy Co ltd
Original Assignee
BEIJING AOFU ENERGY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by BEIJING AOFU ENERGY Co Ltd filed Critical BEIJING AOFU ENERGY Co Ltd
Priority to CN201320408213.9U priority Critical patent/CN203518635U/en
Application granted granted Critical
Publication of CN203518635U publication Critical patent/CN203518635U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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 dry quenching furnace waste heat power generation system. The dry quenching furnace waste heat power generation system comprises a dry quenching furnace, a dry quenching waste heat boiler and a cooling chamber, one end of the dry quenching waste heat boiler is connected with the dry quenching furnace through a pipeline, and the other end of the dry quenching waste heat boiler is connected with a heat accumulator. The dry quenching waste heat boiler is connected with the cooling chamber through an inertia gas recycling pipe. The cooling chamber is connected to an inertia gas inlet pipe through the inertia gas recycling pipe. The heat accumulator is respectively connected with one or two or more turbine sets through a valve, wherein the turbine sets are connected with a generator set. A pressure meter is arranged on the heat accumulator. A carbon monoxide detector is arranged on the dry quenching furnace. The system structure is simplified, the construction cost is reduced, meanwhile, the heat accumulator is set, the waste heat utilization efficiency is improved, the operation safety is improved, much energy is saved, and the dry quenching furnace waste heat power generation system is friendlier to the environment.

Description

A kind of coke dry quenching furnace afterheat generating system
Technical field
The utility model relates to a kind of afterheat generating system, relates in particular to a kind of electricity generation system of utilizing coke dry quenching furnace cogeneration.
Background technology
Dry coke quenching for coke wet quenching, dry coke quenching be adopt inert gas by red Jiao at the cooling a kind of coke quenching method of the environment borehole cooling of anaerobic.In dry coke quenching process, red Jiao packs into from dry top of putting out stove, and low temperature inert gas blasts dry putting out in the red burnt layer of stove cooling section by circulating fan, and cooled coke is discharged from the dry furnace bottom that puts out; Absorb temperature raises after red burnt latent heat inertia recyclegas from coke dry quenching furnace ring-shaped flue is discharged, enter dry coke quenching residual heat boiler and carry out heat exchange, the steam that boiler produces enters steam turbine and drives generator generating, enters circulating fan again blast the dry stove that puts out from the cooled low temperature inert gas of dry coke quenching residual heat boiler.
Current coke wet quenching stove waste heat power generation system, waste gas and the dust of generation are serious to atmosphere pollution, are unfavorable for environmental protection; Though existing dry coke quenching afterheat generating system has reduced waste gas and dust discharge amount, has reduced air pollution, utilization rate of waste heat is low, complex structure, construction cost are high, and security performance is lower.
Utility model content
For the weak point in addressing the above problem, the utility model provides a kind of coke dry quenching furnace afterheat generating system.
For solving above technical problem, the technical solution adopted in the utility model is: a kind of coke dry quenching furnace afterheat generating system, comprise coke dry quenching furnace, dry coke quenching residual heat boiler, cooling chamber, dry coke quenching residual heat boiler is connected with coke dry quenching furnace by pipeline one end, and the other end is connected with storage heater; Dry coke quenching residual heat boiler is connected with cooling chamber by inert gas recovery tube;
Cooling chamber is connected on inert gas entrance pipe by inert gas recovery tube; Storage heater is connected by respectively with one group, valve, two or more sets Steam Turbine;
Steam Turbine is connected with generating set;
On storage heater, be provided with pressure gauge; On described coke dry quenching furnace, be provided with carbon monoxide detector.
The utility model has been simplified system architecture, has reduced construction cost, is provided with storage heater simultaneously, has improved UTILIZATION OF VESIDUAL HEAT IN efficiency, has improved the security of operation, energy-saving and environmental protection more.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Fig. 1 is that system of the present utility model forms structural representation.
In figure: 1, inert gas entrance; 2, carbon monoxide detector; 3, coke dry quenching furnace; 4, high temperature inert gas outlet; 5, dry coke quenching residual heat boiler; 6, pressure gauge; 7, Steam Turbine; 8, generating set; 9, storage heater; 10, inert gas recovery tube; 11, cooling chamber; 12, valve.
The specific embodiment
As shown in Figure 1, the utility model comprises inert gas entrance 1, carbon monoxide detector 2, coke dry quenching furnace 3, high temperature inert gas outlet 4, dry coke quenching residual heat boiler 5, pressure gauge 6, Steam Turbine 7, generating set 8, storage heater 9, inert gas recovery tube 10, cooling chamber 11 and valve 12.
Dry coke quenching residual heat boiler 5 is connected with coke dry quenching furnace 3 by pipeline one end, and the other end is connected with storage heater 9; Dry coke quenching residual heat boiler 5 is connected with cooling chamber 11 by inert gas recovery tube 10, and cooling chamber 11 is connected on inert gas entrance pipe by inert gas recovery tube 10.Storage heater 9 is connected by respectively with one group, valve, two or more sets Steam Turbine 7.Steam Turbine 7 is connected with generating set 8.
On storage heater 9, be provided with pressure gauge 6.On coke dry quenching furnace 3, be provided with carbon monoxide detector 2.The setting of pressure gauge 6 and carbon monoxide detector 2, makes the utility model can constantly recognize the pressure of system and the content of carbon monoxide in use, to reasonably discharge and prevent, has improved the security performance of system.
Electricity generating principle: low temperature inert gas enters the red burnt latent heat of coke dry quenching furnace absorption and becomes high temperature inert gas, and enter dry coke quenching residual heat boiler heat is passed to water, make water become steam, steam successively enters the last Steam Turbine that arrive such as storage heater (playing the effect of storage or accumulation of energy) and drives generator generating.On coke dry quenching furnace, be provided with carbon monoxide detector, prevent explosion danger.It is cooling that inert gas enters cooling chamber through piping 10, finally enters coke dry quenching furnace and re-use (fully having accomplished energy-conserving and environment-protective).What in figure, arrow represented is the route that UTILIZATION OF VESIDUAL HEAT IN and inert gas reclaim.
Above-mentioned embodiment is not to restriction of the present utility model; the utility model is also not limited in above-mentioned giving an example; the variation that those skilled in the art make within the scope of the technical solution of the utility model, remodeling, interpolation or replacement, also all belong to protection domain of the present utility model.

Claims (1)

1. a coke dry quenching furnace afterheat generating system, comprises coke dry quenching furnace, dry coke quenching residual heat boiler, cooling chamber, it is characterized in that: described dry coke quenching residual heat boiler is connected with coke dry quenching furnace by pipeline one end, and the other end is connected with storage heater; Dry coke quenching residual heat boiler is connected with cooling chamber by inert gas recovery tube;
Described cooling chamber is connected on inert gas entrance pipe by inert gas recovery tube; Described storage heater is connected by respectively with one group, valve, two or more sets Steam Turbine;
Described Steam Turbine is connected with generating set;
On described storage heater, be provided with pressure gauge; On described coke dry quenching furnace, be provided with carbon monoxide detector.
CN201320408213.9U 2013-07-10 2013-07-10 Dry quenching furnace waste heat power generation system Expired - Lifetime CN203518635U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320408213.9U CN203518635U (en) 2013-07-10 2013-07-10 Dry quenching furnace waste heat power generation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320408213.9U CN203518635U (en) 2013-07-10 2013-07-10 Dry quenching furnace waste heat power generation system

Publications (1)

Publication Number Publication Date
CN203518635U true CN203518635U (en) 2014-04-02

Family

ID=50377558

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320408213.9U Expired - Lifetime CN203518635U (en) 2013-07-10 2013-07-10 Dry quenching furnace waste heat power generation system

Country Status (1)

Country Link
CN (1) CN203518635U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106520149A (en) * 2016-12-28 2017-03-22 中国科学院上海高等研究院 Coke dry quenching furnace structure and red coke sensible heat power generation system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106520149A (en) * 2016-12-28 2017-03-22 中国科学院上海高等研究院 Coke dry quenching furnace structure and red coke sensible heat power generation system

Similar Documents

Publication Publication Date Title
CN202732012U (en) Ventilation air methane oxidization power generation system
CN102506588B (en) Cement kiln waste heat comprehensive utilization power generation system and method
CN102401369B (en) Method for improving quality of recyclable exhaust waste heat in power plant boiler and progressively utilizing exhaust waste heat
CN102230615B (en) Combined type flue gas residual heat comprehensive utilization system
CN202361822U (en) Flue gas treatment and waste heat generation system with rotary hearth furnace
CN203323218U (en) Boiler flue gas waste heat heating system
CN104235928A (en) Boiler flue gas waste heat heating system
CN201982147U (en) Joint backheating thermodynamic system of power plant
CN205332168U (en) Waste heat comprehensive recovery utilization system of thermal power factory
CN203518635U (en) Dry quenching furnace waste heat power generation system
CN205119850U (en) A three stoves quick -witted dry coke quenching waste heat power generation system
CN202109463U (en) Combined smoke waste heat comprehensive utilization system
CN201819192U (en) Two-stage serial-parallel boiler tail heat exchanger
CN203489244U (en) Boiler smoke waste-heat applicable system
CN203452860U (en) Electrical power generating system comprehensively utilizing waste heat of smoke of ferroalloy submerged arc furnace and casting process
CN216523148U (en) Novel dry quenching waste heat power generation dust removal optimizing system
CN101666483A (en) Oil boiler heat energy recycling device
CN103017553A (en) Regenerative submerged arc furnace flue gas waste heat power generation method
CN203533668U (en) System for fume deep-cooling heat recovery of combined cycle gas turbine unit
CN203240910U (en) Flue gas recycling system of ferromanganese smelting electric furnace
CN203116054U (en) Cooling device used for flue gas heat exchanging
CN203097976U (en) Karina type industrial waste heat integrating recovery device
CN104729307A (en) Heat exchange set for flue gas waste heat recovery
CN203099869U (en) Device using high-temperature smoke to heat baffle door sealing air
CN204513434U (en) A kind of thermal power generation flue gas waste heat recovery system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: 100070 Beijing Outer Ring Road West, building 26, building 56, No.

Patentee after: AOFU ENERGY CO.,LTD.

Address before: 100070 Beijing Outer Ring Road West, building 26, building 56, No.

Patentee before: BEIJING AOFU ENERGY Co.,Ltd.

CX01 Expiry of patent term

Granted publication date: 20140402

CX01 Expiry of patent term