CN204007183U - A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas - Google Patents

A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas Download PDF

Info

Publication number
CN204007183U
CN204007183U CN201420491561.1U CN201420491561U CN204007183U CN 204007183 U CN204007183 U CN 204007183U CN 201420491561 U CN201420491561 U CN 201420491561U CN 204007183 U CN204007183 U CN 204007183U
Authority
CN
China
Prior art keywords
flue
heat exchange
drum
fluidized bed
exchange pipeline
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
CN201420491561.1U
Other languages
Chinese (zh)
Inventor
杨建高
方世中
方俊文
牛志洋
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.)
Lingbao Jinyuan Mining Co Ltd
Original Assignee
Lingbao Jinyuan Mining 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 Lingbao Jinyuan Mining Co Ltd filed Critical Lingbao Jinyuan Mining Co Ltd
Priority to CN201420491561.1U priority Critical patent/CN204007183U/en
Application granted granted Critical
Publication of CN204007183U publication Critical patent/CN204007183U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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

Landscapes

  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

The utility model discloses a kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas, comprise the fluidized bed furnace, flue and the cyclone dust collectors that connect in turn, wherein, also comprise that drum and some internal diameters are less than the heat exchange pipeline of flue, described heat exchange pipeline is uniform or be spirally coiled in the outer wall of flue along the circumferencial direction of flue; The import and export of described heat exchange pipeline is connected with drum by transmission pipeline.This device is by setting up some heat exchange pipelines that are connected with drum at flue outer wall, the heat that can make flue is absorbed to remove by heat exchange pipeline and with drum, is converted to steam and discharges afterwards, these steam can be for the heating of factory's life or industrial water, and heating use in winter etc., saved the energy.

Description

A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas
Technical field
The utility model belongs to heat recovery technical field, is specifically related to a kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas.
Background technology
In the acidizing fired relieving haperacidity production technology of aurin powder, normal open piping carrys out the temperature of cooled flue gas.As shown in Figure 1, in prior art, the flue-gas temperature of fluidized bed furnace 1 outlet is at 550~560 ℃ and contain a large amount of steam and dust, after flue 2 natural heat dissipations coolings, dedusting, treat that flue-gas temperature is down to 350~380 ℃ of technological requirements that just can reach cyclone dust collectors 3 and follow-up electric cleaner.If flue-gas temperature easily causes burning out of pipeline and high temperature corrosion higher than said temperature; If flue-gas temperature lower than said temperature, easily causes the dew point corrosion of pipeline, cyclone dust collectors and follow-up equipment such as electric cleaner.Due to flue-gas temperature higher (550~560 ℃), if high-temperature flue gas is only cooled to 350~380 ℃ through natural heat dissipation in pipeline, the flue needing is first long, second also causes a large amount of thermal waste.
Utility model content
The utility model object is to overcome prior art defect, and a kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas is provided.
For achieving the above object, the utility model adopts following technical scheme:
A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas, comprise the fluidized bed furnace, flue and the cyclone dust collectors that connect in turn, wherein, also comprise that drum and some internal diameters are less than the heat exchange pipeline of flue, described heat exchange pipeline is uniform or be spirally coiled in the outer wall of flue along the circumferencial direction of flue; The import and export of described heat exchange pipeline is connected with drum by transmission pipeline.
Preferably, when heat exchange pipeline is uniform along the circumferencial direction of flue, the axis of described heat exchange pipeline parallels with the axis of flue.For guaranteeing the security of the long-time circular flow of drum, the water in drum is preferably used desalted water, can effectively avoid like this fouling in pipeline.Water at low temperature in drum enters heat exchange pipeline, and is heated after flue heat exchange, and the water after heating enters after drum again, and part is converted into steam by the carbonated drink separation equipment in drum and discharges.
Compared to the prior art, the beneficial effects of the utility model:
By set up some heat exchange pipelines that are connected with drum at flue outer wall, the heat that can make flue is absorbed to remove by heat exchange pipeline and with drum, is converted to steam and discharges afterwards, these steam can be for the heating of factory's life or industrial water, and heating use in winter etc., saved the energy.Use this device; can by flue natural heat dissipation, change into and utilize heat exchange pipeline absorption remove the heat shedding and be converted into steam with drum existing; in flue heat radiation; the waste heat that effectively recovered flue gas pipeline sheds; cyclone dust collectors and the follow-up equipment such as electric cleaner have not only been protected; also realize recycling of the energy, there is good economic and social benefit.
Accompanying drawing explanation
Fig. 1 is the structural representation of existing apparatus;
Fig. 2 is the structural representation of device described in the utility model;
Fig. 3 be in device described in the utility model heat exchange pipeline at the distribution schematic diagram of flue outer wall.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described in further details, but protection domain of the present utility model is not limited to this.
embodiment 1
As shown in Figures 2 and 3, a kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas, comprise the fluidized bed furnace 1, flue 2 and the cyclone dust collectors 3 that connect in turn, wherein, also comprise that drum 7 and some internal diameters are less than the heat exchange pipeline 4 of flue 2, described heat exchange pipeline 4 is uniform along the circumferencial direction of flue 2; The import of described heat exchange pipeline 4 is connected with drum 7 outlets by the first transmission pipeline 5, and the outlet of described heat exchange pipeline 4 is connected with drum 7 imports by the second transmission pipeline 6.When heat exchange pipeline 4 is uniform along the circumferencial direction of flue 2, the axis of described heat exchange pipeline 4 parallels with the axis of flue 2.
In production process, the flue gas (temperature is at 550~560 ℃) of fluidized bed furnace 1 outlet enters flue 2, low temperature desalted water in drum 7 enters heat exchange pipeline 4 through the first conveyance conduit 5, with flue 2 heat exchanges after be heated that (simultaneously the flue-gas temperature in flue 2 is reduced to 350~380 ℃, met the technological requirement of cyclone dust collectors 3 and follow-up electric cleaner), water after heating enters after drum 7 again through the second conveyance conduit 6, and part is converted into steam 8 by the carbonated drink separation equipment separation in drum 7 and discharges.These are converted steam 8 after recovery can be for the heating of factory's life or industrial water, and heating in winter used etc., has saved the energy.
It should be noted last that: above-described embodiment is only illustrative rather than definitive thereof the technical solution of the utility model; any the utility model is carried out be equal to modification or local replacement of replacing and not departing from the utility model spirit and scope, within it all should be encompassed in the scope of the utility model claim protection.

Claims (2)

1. the heat recovery device of an acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas, comprise the fluidized bed furnace, flue and the cyclone dust collectors that connect in turn, it is characterized in that, also comprise that drum and some internal diameters are less than the heat exchange pipeline of flue, described heat exchange pipeline is uniform or be spirally coiled in the outer wall of flue along the circumferencial direction of flue; The import and export of described heat exchange pipeline is connected with drum by transmission pipeline.
2. the heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas as claimed in claim 1, is characterized in that, heat exchange pipeline is uniform along the circumferencial direction of flue, and the axis of described heat exchange pipeline parallels with the axis of flue.
CN201420491561.1U 2014-08-29 2014-08-29 A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas Expired - Fee Related CN204007183U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420491561.1U CN204007183U (en) 2014-08-29 2014-08-29 A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420491561.1U CN204007183U (en) 2014-08-29 2014-08-29 A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas

Publications (1)

Publication Number Publication Date
CN204007183U true CN204007183U (en) 2014-12-10

Family

ID=52047172

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420491561.1U Expired - Fee Related CN204007183U (en) 2014-08-29 2014-08-29 A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas

Country Status (1)

Country Link
CN (1) CN204007183U (en)

Similar Documents

Publication Publication Date Title
CN204730682U (en) A kind of sintering circular-cooler waste heat recovery cigarette wind apparatus
CN204007183U (en) A kind of heat recovery device of acidizing fired relieving haperacidity fluidized bed furnace outlet flue gas
CN204824714U (en) Coke oven crude gas waste heat recovery heat transfer device
CN205036418U (en) Industry waste heat recovery of cogeneration of heat and power utilizes system
CN203836475U (en) Tar conveying device with steam heating function
CN204420980U (en) Waste Heat Boiler superheater
CN204211686U (en) With the charring furnace of energy recovery
CN203518639U (en) Waste heat recovery unit for metallurgical rotary type lime kiln
CN203704686U (en) Off-gas sensible heat recovery device for metallurgical off-gas acid making device
CN204474706U (en) Converter gas purification and residual neat recovering system
CN204078543U (en) A kind of warming solar energy storage wax apparatus
CN205424967U (en) Rapid cooling heat transfer device of heat accumulation formula oxidation furnace
CN204676132U (en) A kind of red soil nickel ore high temperature calcining thermal insulation barn structure
CN204388030U (en) A kind of boiler energy-saving appliance
CN204420971U (en) A kind of waste-heat recovery device
CN204227920U (en) A kind of furnace construction with heat recovery function
CN203132122U (en) Environment-friendly water boiler
CN203396251U (en) Cooling air reusing device
CN204202411U (en) Sinter fume denitration and bootstrap system
CN103920376A (en) Low-energy-consumption hybrid white smoke elimination device
CN203980918U (en) Waste heat overbottom pressure utilization system in gas washing in SA production
CN203550608U (en) Cooling device suitable for large submerged arc furnace coil base
CN204611716U (en) Using residual heat from kiln furnace steam boiler
CN203128611U (en) Converter flue gas waste heat utilization system
CN204816104U (en) Waste heat utilization stoving moulded coal system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141210

Termination date: 20200829