CN201561630U - Device for drying materials by using waste heat from flue gas and tail gas of boiler - Google Patents

Device for drying materials by using waste heat from flue gas and tail gas of boiler Download PDF

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Publication number
CN201561630U
CN201561630U CN2009202762803U CN200920276280U CN201561630U CN 201561630 U CN201561630 U CN 201561630U CN 2009202762803 U CN2009202762803 U CN 2009202762803U CN 200920276280 U CN200920276280 U CN 200920276280U CN 201561630 U CN201561630 U CN 201561630U
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CN
China
Prior art keywords
flue gas
boiler
heat exchanger
pipeline
waste heat
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 - Fee Related
Application number
CN2009202762803U
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Chinese (zh)
Inventor
狄东河
贾晓伟
朱锦文
刘安鹏
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XINJIANG JINXIN BIO-TECHNOLOGY DEVELOPMENT CO LTD
Original Assignee
XINJIANG JINXIN BIO-TECHNOLOGY DEVELOPMENT 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 XINJIANG JINXIN BIO-TECHNOLOGY DEVELOPMENT CO LTD filed Critical XINJIANG JINXIN BIO-TECHNOLOGY DEVELOPMENT CO LTD
Priority to CN2009202762803U priority Critical patent/CN201561630U/en
Application granted granted Critical
Publication of CN201561630U publication Critical patent/CN201561630U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

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  • Drying Of Solid Materials (AREA)

Abstract

The utility model discloses a device for drying materials by using the waste heat from the flue gas and tail gas of a boiler, which belongs to the field of energy-saving devices. A discharge flue of the boiler is connected at the heat supply end of a flue gas heat exchanger, and a smoke outlet of the flue gas heat exchanger is connected with a smoke exhaust fan; an air inlet of the flue gas heat exchanger is opened towards the atmosphere, a hot air outlet pipeline is divided into two ways, one pipeline is communicated with a hot air heater through a fan, an air outlet pipeline for the hot air heater is communicated with a material drying device through a fan, and the other pipeline with a gate valve is communicated with an air inlet of an air blower for a boiler combustion chamber; and a tail gas pipeline introduced out from a material steaming and frying device is connected at the heat supply end of the hot air heater and connected with a return water tank. The device for drying materials by using the waste heat from the flue gas and tail gas of the boiler is used for drying the materials by using two kinds of waste heat, further utilizes the waste heat, saves the 80 percent of drying energy resources, reduces the production cost and improves the economic benefit.

Description

Utilize the device of boiler smoke and tail vapour waste heat oven dry material
1, technical field: the utility model relates to a kind of energy-saving equipment, especially a kind of residual heat using device.
2, background technology: the flue gas of boiler is generally just arranged to atmosphere after passing through to economize coal gas, heat exchanger in boiler.The steam of boiler steam to be fried tail vapour later in the workshop to material and also is put into recovery tank to become cooling water recycling.In fact flue gas that is discharged and tail vapour also have very high temperature, and its heat has wasted.Plant material is wanted heating, drying moisture earlier in process, consume the new energy, if can rationally utilize waste heat, just may save the energy, brings tangible economic benefit to enterprise.
3, summary of the invention: the purpose of this utility model is a kind of device that utilizes boiler smoke and tail vapour waste heat oven dry material of design.It can make full use of the waste heat of flue gas and tail vapour, saves the energy, reduces cost.Its technical scheme is: the smokejack of boiler connects the heat supply end of flue gas heat exchanger, and the outlet flue of flue gas heat exchanger connects smoke exhaust fan.The air inlet of flue gas heat exchanger is opened to atmosphere, the hot-blast outlet pipeline is divided into two-way, one the tunnel is communicated with storage heater through blower fan, and storage heater air-out pipeline is communicated with drying materials equipment by blower fan, and another road has the blower inlet of the pipeline connection boiler furnace of gate valve.Connect the heat supply end of storage heater from the tail gas pipe road that material steaming stir-fry equipment is drawn, tail vapour is drawn pipeline and is connected recovery tank.
Utilize the device of boiler smoke and tail vapour waste heat oven dry material to utilize two kinds of waste heat oven dry materials, made full use of used heat, thereby saved the 80% oven dry energy, reduced production cost, improved economic benefit.
4, description of drawings: Fig. 1 is the structural representation that utilizes the device of boiler smoke and tail vapour waste heat oven dry material.
5, the specific embodiment: be further described below in conjunction with accompanying drawing.As shown in Figure 1, the smokejack 5 of boiler 1 connects the heat supply end of flue gas heat exchanger 2, and the outlet flue of flue gas heat exchanger connects smoke exhaust fan 7, the flue gas row heavenwards of finishing heat exchange.The air inlet of flue gas heat exchanger is opened to atmosphere, makes inhaled air enter heat exchanger and is heated.The hot-blast outlet pipeline is divided into two-way, and one the tunnel through blower fan 6 connection storage heaters 10, and hot blast is further heated, and storage heater air-out pipeline is communicated with drying materials equipment 8 by blower fan 9, and perhaps other use hot facility, for example the warm-air drier in workshop.In the time need not drying material, allow hot blast try a different way directly.Another road has the blower inlet of the pipeline connection boiler furnace of gate valve 12.Open gate valve, hot blast enters boiler by boiler blower, helps improving temperature in the stove.The steam of boiler is mainly used to heating and steam fries material, and the material that steam pipework 3 leads to workshop 4 is heated and steamed stir-fry equipment, finishes the steam that steams the stir-fry task of heating and is called as tail vapour, and tail vapour still has the above high temperature of 100 degree, can utilize it that hot blast is heated again.The tail gas pipe road connects the heat supply end of storage heater 10, is passed through steam outlet pipe road guiding recovery tank 11 by the tail vapour after utilizing once more.The condensed water reusable edible.

Claims (1)

1. utilize the device of boiler smoke and tail vapour waste heat oven dry material, be made up of pipeline, blower fan, heat exchanger, it is characterized in that: the smokejack (5) of boiler (1) connects flue gas heat exchanger (2), and the outlet flue of flue gas heat exchanger connects smoke exhaust fan (7); The air inlet of flue gas heat exchanger is opened to atmosphere, goes out hot air duct and is divided into two-way, and one the tunnel through blower fan (6) connection storage heater 10, and the hot-blast pipe line that goes out of storage heater is communicated with drying materials equipment (8) by blower fan (9); Another road has the blower inlet of the pipeline connection boiler furnace of gate valve (12); Connect the heat supply end of storage heater (10) from the tail gas pipe road that material steaming stir-fry equipment is drawn, tail vapour steam outlet pipe road connects recovery tank (11).
CN2009202762803U 2009-12-03 2009-12-03 Device for drying materials by using waste heat from flue gas and tail gas of boiler Expired - Fee Related CN201561630U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009202762803U CN201561630U (en) 2009-12-03 2009-12-03 Device for drying materials by using waste heat from flue gas and tail gas of boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009202762803U CN201561630U (en) 2009-12-03 2009-12-03 Device for drying materials by using waste heat from flue gas and tail gas of boiler

Publications (1)

Publication Number Publication Date
CN201561630U true CN201561630U (en) 2010-08-25

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CN2009202762803U Expired - Fee Related CN201561630U (en) 2009-12-03 2009-12-03 Device for drying materials by using waste heat from flue gas and tail gas of boiler

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CN (1) CN201561630U (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102072499A (en) * 2011-01-30 2011-05-25 杨祥良 Flue gas low temperature denitriding and coal slime drying combined circulating system
CN102287805A (en) * 2011-06-10 2011-12-21 蓬莱汇洋食品有限公司 Boiler exhaust heat recovery device
CN103162413A (en) * 2011-12-16 2013-06-19 李建利 Wind-heat crude oil thermostat
CN103335502A (en) * 2013-06-22 2013-10-02 中国科学院工程热物理研究所 Energy comprehensive utilization system used in rice drying process
CN103453751A (en) * 2013-08-30 2013-12-18 合肥禾盛新型材料有限公司 High heat waste gas energy source utilization system
CN104215058A (en) * 2013-05-30 2014-12-17 中国科学院工程热物理研究所 Solid material drying device
CN104833196A (en) * 2015-05-12 2015-08-12 浙江海洋学院 Exhaust gas heating system of marine main engine
CN105910416A (en) * 2016-04-15 2016-08-31 泉州装备制造研究所 Material after heat recycling and drying system
CN106247782A (en) * 2016-08-03 2016-12-21 五洲丰农业科技有限公司 Residual heat integrative utilizes fertiliser granulates drying unit

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102072499A (en) * 2011-01-30 2011-05-25 杨祥良 Flue gas low temperature denitriding and coal slime drying combined circulating system
CN102072499B (en) * 2011-01-30 2012-02-08 杨祥良 Flue gas low temperature denitriding and coal slime drying combined circulating system
CN102287805A (en) * 2011-06-10 2011-12-21 蓬莱汇洋食品有限公司 Boiler exhaust heat recovery device
CN103162413A (en) * 2011-12-16 2013-06-19 李建利 Wind-heat crude oil thermostat
CN104215058A (en) * 2013-05-30 2014-12-17 中国科学院工程热物理研究所 Solid material drying device
CN104215058B (en) * 2013-05-30 2016-02-24 中国科学院工程热物理研究所 Solid material drying device
CN103335502A (en) * 2013-06-22 2013-10-02 中国科学院工程热物理研究所 Energy comprehensive utilization system used in rice drying process
CN103453751A (en) * 2013-08-30 2013-12-18 合肥禾盛新型材料有限公司 High heat waste gas energy source utilization system
CN104833196A (en) * 2015-05-12 2015-08-12 浙江海洋学院 Exhaust gas heating system of marine main engine
CN105910416A (en) * 2016-04-15 2016-08-31 泉州装备制造研究所 Material after heat recycling and drying system
CN105910416B (en) * 2016-04-15 2018-04-17 泉州装备制造研究所 A kind of material waste heat recovery drying system
CN106247782A (en) * 2016-08-03 2016-12-21 五洲丰农业科技有限公司 Residual heat integrative utilizes fertiliser granulates drying unit

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100825

Termination date: 20121203