CN103234360B - Device and process for transferring high temperature sintering ore - Google Patents

Device and process for transferring high temperature sintering ore Download PDF

Info

Publication number
CN103234360B
CN103234360B CN201310127996.8A CN201310127996A CN103234360B CN 103234360 B CN103234360 B CN 103234360B CN 201310127996 A CN201310127996 A CN 201310127996A CN 103234360 B CN103234360 B CN 103234360B
Authority
CN
China
Prior art keywords
cooling system
sintering
conveyer
flap valve
high temperature
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
Application number
CN201310127996.8A
Other languages
Chinese (zh)
Other versions
CN103234360A (en
Inventor
彭岩
刘怀亮
王继生
俞章法
魏小林
乔文存
时小宝
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.)
CITIC Heavy Industries Co Ltd
Luoyang Mining Machinery and Engineering Design Institute Co Ltd
Original Assignee
CITIC Heavy Industries Co Ltd
Luoyang Mining Machinery and Engineering Design Institute 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 CITIC Heavy Industries Co Ltd, Luoyang Mining Machinery and Engineering Design Institute Co Ltd filed Critical CITIC Heavy Industries Co Ltd
Priority to CN201310127996.8A priority Critical patent/CN103234360B/en
Publication of CN103234360A publication Critical patent/CN103234360A/en
Application granted granted Critical
Publication of CN103234360B publication Critical patent/CN103234360B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention provides a device and process for transferring high temperature sintering ore and relates to the field of sintering waste heat utilization. A flap valve is arranged below a single-roll crusher, the bottom of the flap valve is arranged at a connecting position of a blanking chute of a ring cooling/belt cooling system and a blanking chute of a furnace type cooling system, the flap valve can switch between the blanking chute of the ring cooling/belt cooling system and the blanking chute of the furnace type cooling system, a high temperature vibrating screen is arranged on the bottom wall of the blanking chute of the furnace type cooling system, an outlet of the blanking chute of the furnace type cooling system is connected with one end of a conveyer, the other end of the conveyer is connected with a furnace mouth of a cooling furnace, and a thermal insulation cover is arranged above the conveyer. The device and process for transferring the high temperature sintering ore improves operation rate of a sintering machine, is high in reliability and low in construction cost, uses the arc-shaped thermal insulation cover for thermal insulation, prevents heat of the sintering ore from losing, and improves waste heat utilization rate.

Description

High temperature sintering ore deposit transporter and technique
Technical field
The present invention relates to sintering waste heat and utilize field, specifically, be that high temperature sintering ore deposit can be taken out by one from sintering machine, and carry out fragmentation, screening, transhipment and insulation, enter high temperature sintering ore deposit transporter and the technique of stove formula cooling system.
Background technology
Steel and iron industry is AND ENERGY RESOURCES CONSUMPTION IN CHINA rich and influential family, accounts for 15% of national total energy consumption, in steel manufacture process, and the energy consumption of sintering circuit occupies the second, and in SINTERING PRODUCTION, heat sinter sensible heat accounts for more than 40% of overall heat consumption, and sintered, energy saving is very important.High efficiente callback utilizes sintering mine sensible heat to be the effective way improving steel and iron industry efficiency.
The cooling of Current Domestic sintering deposit is main adopt ring cold/be with cold technique, have that fault rate is high, maintenance is frequent and difficulty large, run that power consumption is high, leak out a little many, inleakage large (more than 30%), the key difficult problem such as cooling effect is poor, the rate of return mine is high, while also constrain sintering machine waste heat high efficiente callback utilization.That sintering deposit stove formula process for cooling thoroughly can solve ring is cold/be with cold technique Problems existing, there is raising sintering deposit cooling quality, raising waste heat flue gas quality, the cogeneration ability that improves, reduction cooling system power consumption, raising afterheat generating system adaptability and reduce the advantages such as pollutant emission such as flue dust, and significantly can improve cogeneration amount more than 50%, reduction system from electricity consumption 25%, raising sintering machine year running rate 1-2%, be a kind of revolutionary technology, subversiveness product, there is vast potential for future development.
The prerequisite and the key that realize sintering deposit stove formula process for cooling to provide a kind of high temperature sintering ore deposit transporter and technique reliably, high temperature sintering ore deposit can be taken out from sintering machine, and after carrying out fragmentation, screening, transhipment and insulation, enter stove formula cooling system.Because stove formula cooling sintering deposit cogeneration technology is a kind of brand new technical, the research for high temperature sintering ore deposit transporter and technique is also less.From the high temperature sintering ore deposit that sintering machine takes out before entering stove formula cooling system, if do not have sintering deposit transporter reasonable in design and technique, the thermal loss of sintering deposit can be made more, utilization rate of waste heat reduces.Therefore, develop a kind of do not affect sintering machine produce main technique, there is higher reliability of technology, prevent sintering deposit heat loss and reduce the high temperature sintering ore deposit transporter of construction costs and technique significant.
Summary of the invention
The object of the invention is for solving the problem, not affecting for sintering deposit stove formula process for cooling provides a kind of the high temperature sintering ore deposit transporter and technique that sintering machine is produced, reliable, sintering deposit granule size is suitable, thermal loss is less.
To achieve these goals, the technical solution used in the present invention is: high temperature sintering ore deposit transporter, comprise with lower device: single roll crusher, flap valve, high-temperature vibrating sieve and conveyer, there is flap valve the below of described single roll crusher, the junction of the bottom of flap valve is arranged at ring cold/band cooling system feeding chute and stove formula cooling system feeding chute, flap valve can cold at ring/band cooling system feeding chute and stove formula cooling system feeding chute between switch, the diapire of stove formula cooling system feeding chute is provided with high-temperature vibrating sieve; The outlet of stove formula cooling system feeding chute is connected with one end of conveyer, and the other end of conveyer connects the fire door of cool furnace, and the top of conveyer is provided with stay-warm case.
The sieve diameter scope of described high-temperature vibrating sieve is 5-10mm.
Described conveyer can adopt chain scraper conveyor or bucket chain conveyor.
The inclination angle of described conveyer is 0-30 °.
The cross section of described stay-warm case is arc.
High temperature sintering ore deposit transhipment technique, comprises the following steps: the sintering deposit that sintering machine sinters into is crushed to after below 150mm through single roll crusher, falls to flap valve, by flap valve carry out feeding control enter stove formula cooling system or ring cold/band cooling system; When stove formula cooling system normally runs, sintering deposit enters stove formula cooling system feeding chute by flap valve, by gravity fall on high temperature vibratory sieve, after the fine ore of granularity <5mm screens out by high-temperature vibrating sieve, the sintering deposit that granularity is qualified is transported to cool furnace by conveyer, in transport process, by the stay-warm case above conveyer, sintering deposit is incubated; When stove formula cooling system breaks down, sintering deposit by ring cold/band cooling system feeding chute enters ring cold/band cooling system.
The beneficial effect that the present invention brings is: 1. sintering deposit is broken through single roll crusher, and high temperature sintering ore deposit larger for granularity is crushed to below 150mm, and the sintering deposit preventing granularity excessive enters cool furnace, cannot fully cool; 2. sintering deposit flap valve can cold at former ring/band cooling system and stove formula cooling system between switch flexibly, improve the running rate of sintering machine; 3. sintering deposit is through the screening of high-temperature vibrating sieve, prevents the fine ore being less than 5mm from entering cool furnace and causes Gas-solid flow drag losses to increase; 4. transporter adopts high inclination angle conveyer, and conveyer adopts heat resistant and wear resistant material, and reliability is high, construction costs is low; 5. adopt arc stay-warm case to be incubated in transport process, its inner space is reduced as far as possible, effectively weaken the decay of high temperature sintering ore deposit heat radiation at upper space, further reduce sintering deposit thermal loss, improve utilization rate of waste heat; 6. sintering deposit realizes comparatively long-distance sand transport by conveyer, solves a difficult problem for sintered production line site layout project complexity.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of the present invention;
Fig. 2 is the A-A sectional drawing of Fig. 1.
Reference numeral: 1, sintering machine, 2, sintering deposit, 3, single roll crusher, 4, flap valve, 5, ring is cold/band cooling system feeding chute, 6, high-temperature vibrating sieve, 7, stove formula cooling system feeding chute, 8, conveyer, 9, stay-warm case, 10, cool furnace.
Detailed description of the invention
Below in conjunction with drawings and the specific embodiments, the present invention is described in further detail.
As depicted in figs. 1 and 2, high temperature sintering ore deposit transporter, comprise with lower device: single roll crusher 3, flap valve 4, high-temperature vibrating sieve 6 and conveyer 8, there is flap valve 4 below of described single roll crusher 3, the junction of the bottom of flap valve 4 is arranged at ring cold/band cooling system feeding chute 5 and stove formula cooling system feeding chute 7, flap valve 4 can cold at ring/switch between band cooling system feeding chute 5 and stove formula cooling system feeding chute 7, the diapire of stove formula cooling system feeding chute 7 is provided with high-temperature vibrating sieve 6; The outlet of stove formula cooling system feeding chute 7 is connected with one end of conveyer 8, and the other end of conveyer 8 connects the fire door of cool furnace 10, and the top of conveyer 8 is provided with stay-warm case 9.
The sieve diameter scope of described high-temperature vibrating sieve 6 is 5-10mm.
Described conveyer 8 can adopt chain scraper conveyor or bucket chain conveyor.
The inclination angle of described conveyer 8 is 0-30 °.
The cross section of described stay-warm case 9 is arc.
High temperature sintering ore deposit transhipment technique, comprise the following steps: the sintering deposit 2 that sintering machine 1 sinters into is after single roll crusher 3 is crushed to below 150mm, fall to flap valve 4, by flap valve 4 carry out feeding control enter stove formula cooling system or ring cold/band cooling system; When stove formula cooling system normally runs, sintering deposit 2 enters stove formula cooling system feeding chute 7 by flap valve 4, by gravity fall on high temperature vibratory sieve 6, after the fine ore of granularity <5mm screens out by high-temperature vibrating sieve 6, the sintering deposit 2 that granularity is qualified is transported to cool furnace 10 by conveyer 8, in transport process, be incubated by the 9 pairs of sintering deposits 2 of the stay-warm case above conveyer 8; When stove formula cooling system breaks down, sintering deposit 2 by ring cold/band cooling system feeding chute 5 enters ring cold/band cooling system.
After sintering deposit 2 blanking that sintering machine 1 sinters into, be crushed to suitable particle size through single roll crusher 3, carry out feeding control by flap valve 4.When stove formula cooling system breaks down, sintering deposit 2 by ring cold/band cooling system feeding chute 5 enters ring cold/band cooling system.When stove formula cooling system normally runs, sintering deposit 2 enters stove formula cooling system feeding chute 7 by flap valve 4, by gravity fall on high temperature vibratory sieve 6, after the fine ore of granularity <5mm is screened out, the sintering deposit 2 that granularity is qualified is transported to cool furnace 10 by conveyer 8, in transport process, be incubated by stay-warm case 9 pairs of sintering deposits 2, prevent heat loss, in order to ensure that stay-warm case 9 is constructed and the convenience of examine and replace, be divided into the fabrication and installation of insulation petticoat pipe unit, each insulation petticoat pipe element length controls at 2-5m, insulation petticoat pipe element number can adjust flexibly according to sintering deposit 2 fed distance.

Claims (5)

1. high temperature sintering ore deposit transporter, it is characterized in that: comprise single roll crusher (3), flap valve (4), high-temperature vibrating sieve (6) and conveyer (8), there is flap valve (4) below of described single roll crusher (3), the junction of the bottom of flap valve (4) is arranged at ring cold/band cooling system feeding chute (5) and stove formula cooling system feeding chute (7), flap valve (4) can cold at ring/band cooling system feeding chute (5) and stove formula cooling system feeding chute (7) between switching, the diapire of stove formula cooling system feeding chute (7) is provided with high-temperature vibrating sieve (6), the outlet of stove formula cooling system feeding chute (7) is connected with one end of conveyer (8), the other end of conveyer (8) connects the fire door of cool furnace (10), the top of conveyer (8) is provided with stay-warm case (9), wherein, the sintering deposit (2) that sintering machine (1) sinters into is after single roll crusher (3) is crushed to below 150mm, fall to flap valve (4), by flap valve (4) carry out feeding control enter stove formula cooling system or ring cold/band cooling system, when stove formula cooling system normally runs, sintering deposit (2) enters stove formula cooling system feeding chute (7) by flap valve (4), by gravity fall on high temperature vibratory sieve (6), after the fine ore of granularity <5mm screens out by high-temperature vibrating sieve (6), the sintering deposit (2) that granularity is qualified is transported to cool furnace (10) by conveyer (8), in transport process, by the stay-warm case (9) of conveyer (8) top, sintering deposit (2) is incubated, when stove formula cooling system breaks down, sintering deposit (2) by ring cold/band cooling system feeding chute (5) enter ring cold/band cooling system.
2. according to the high temperature sintering ore deposit transporter described in claim 1, it is characterized in that: the sieve diameter scope of described high-temperature vibrating sieve (6) is 5-10mm.
3. according to the high temperature sintering ore deposit transporter described in claim 1, it is characterized in that: described conveyer (8) can adopt chain scraper conveyor or bucket chain conveyor.
4. according to the high temperature sintering ore deposit transporter described in claim 1, it is characterized in that: the inclination angle of described conveyer (8) is 0-30 °.
5. according to the high temperature sintering ore deposit transporter described in claim 1, it is characterized in that: the cross section of described stay-warm case (9) is arc.
CN201310127996.8A 2013-04-15 2013-04-15 Device and process for transferring high temperature sintering ore Active CN103234360B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310127996.8A CN103234360B (en) 2013-04-15 2013-04-15 Device and process for transferring high temperature sintering ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310127996.8A CN103234360B (en) 2013-04-15 2013-04-15 Device and process for transferring high temperature sintering ore

Publications (2)

Publication Number Publication Date
CN103234360A CN103234360A (en) 2013-08-07
CN103234360B true CN103234360B (en) 2015-06-10

Family

ID=48882412

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310127996.8A Active CN103234360B (en) 2013-04-15 2013-04-15 Device and process for transferring high temperature sintering ore

Country Status (1)

Country Link
CN (1) CN103234360B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104142069B (en) * 2014-07-28 2016-06-29 中冶南方工程技术有限公司 Blast furnace raw material residual neat recovering system and its recovery method
CN104313315B (en) * 2014-10-14 2017-06-20 首钢总公司 A kind of pre- whole grain method of sintering deposit for improving central cooler cooling effectiveness
CN107860236B (en) * 2017-11-01 2023-09-15 中冶焦耐(大连)工程技术有限公司 Continuous cooling method for sinter
CN107702546B (en) * 2017-11-01 2023-09-15 中冶焦耐(大连)工程技术有限公司 Sinter continuous cooling system

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2367063A (en) * 1942-09-14 1945-01-09 American Ore Reclamation Compa Sinter treating means
US2743534A (en) * 1952-09-29 1956-05-01 Martin L Cover Apparatus for cooling sinter
JPS5925011B2 (en) * 1977-06-03 1984-06-13 石川島播磨重工業株式会社 Sinter cooling equipment
CN101576351A (en) * 2009-06-23 2009-11-11 河北理工大学 Vertical sinter ore cooling machine capable of efficiently recycling sensible heat of sinter ores
CN102345981A (en) * 2010-08-03 2012-02-08 刘柏谦 Sintering ore cooling device and waste heat recovery system thereof
CN202853402U (en) * 2012-09-24 2013-04-03 中冶东方工程技术有限公司上海分公司 High-efficient heat recovery type sinter mine cooling system
CN203259014U (en) * 2013-04-15 2013-10-30 中信重工机械股份有限公司 High-temperature sinter transfer device

Also Published As

Publication number Publication date
CN103234360A (en) 2013-08-07

Similar Documents

Publication Publication Date Title
CN103234349B (en) Furnace type cooling and heat exchange device for sintered ores
CN103234360B (en) Device and process for transferring high temperature sintering ore
CN103234358B (en) The mineral aggregate system of stove formula cooling sintering deposit waste heat high efficiente callback
CN205014851U (en) Sintering deposit shows heat reclamation device
CN106556258A (en) Sintering mine sensible heat retracting device and its using method
CN103934082A (en) Novel mineral slag grinding system
CN108267013B (en) Sinter cooling and waste heat utilization system and low-oxygen full-circulation cooling method
CN105066718B (en) Comprehensive utilization system for sintering waste heat
CN103234359A (en) Sintering furnace type cooling device
CN103868364A (en) Furnace type cooling device
CN106482530B (en) It is a kind of to be sintered mining multipot type heat recovering device and sensible heat recovery method
CN101596472A (en) A kind of cement clinker roller-type crusher
CN102839244B (en) Device and method for hot loading of metallized pellets of rotary hearth furnace into blast furnace
CN207850029U (en) A kind of pretreatment system of laterite
CN203259014U (en) High-temperature sinter transfer device
CN203259012U (en) Furnace type cooling ore charge system capable of efficiently recycling sinter waste heat
CN104131120A (en) Blast furnace burden distribution method for improving agglomerate utilization efficiency
CN203259018U (en) Furnace type cooling device for sinter
CN103205584B (en) Production device and production method of manganese monoxide mineral powder
CN206643358U (en) With the equipment of the hot-forming metallurgical raw material metal bloom of waste metal rubbish
CN203489703U (en) Chute distributing device
CN203258990U (en) Heat exchange device for sintering ore furnace type cooling
CN201459028U (en) Energy-saving environment-friendly solid pitch melting device
CN210741047U (en) Double-flow direct-supply type vertical cooling kiln for sintered ore
CN203559103U (en) Novel elevated short-process and energy-saving nickel ferroalloy production device based on RKEF (rotary kiln-electric arc furnace) technology

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
C53 Correction of patent for invention or patent application
CB03 Change of inventor or designer information

Inventor after: Peng Yan

Inventor after: Liu Huailiang

Inventor after: Wang Jisheng

Inventor after: Yu Zhangfa

Inventor after: Wei Xiaolin

Inventor after: Qiao Wencun

Inventor after: Shi Xiaobao

Inventor before: Peng Yan

Inventor before: Liu Huailiang

Inventor before: Wang Jisheng

Inventor before: Yu Zhangfa

Inventor before: Qiao Wencun

Inventor before: Shi Xiaobao

COR Change of bibliographic data

Free format text: CORRECT: INVENTOR; FROM: PENG YAN LIU HUAILIANG WANG JISHENG YU ZHANGFA QIAO WENCUN SHI XIAOBAO TO:PENG YAN LIU HUAILIANG WANG JISHENG YU ZHANGFA WEI XIAOLIN QIAO WENCUN SHI XIAOBAO

SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant