CN205042451U - Fluidized bed gas distributor base - Google Patents

Fluidized bed gas distributor base Download PDF

Info

Publication number
CN205042451U
CN205042451U CN201520773047.1U CN201520773047U CN205042451U CN 205042451 U CN205042451 U CN 205042451U CN 201520773047 U CN201520773047 U CN 201520773047U CN 205042451 U CN205042451 U CN 205042451U
Authority
CN
China
Prior art keywords
aeration
zone
microwave heating
fluidized bed
microwave
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
CN201520773047.1U
Other languages
Chinese (zh)
Inventor
谢洪清
查协芳
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.)
JIANGSU XIANFENG DRYING ENGINEERING Co Ltd
Original Assignee
JIANGSU XIANFENG DRYING ENGINEERING 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 JIANGSU XIANFENG DRYING ENGINEERING Co Ltd filed Critical JIANGSU XIANFENG DRYING ENGINEERING Co Ltd
Priority to CN201520773047.1U priority Critical patent/CN205042451U/en
Application granted granted Critical
Publication of CN205042451U publication Critical patent/CN205042451U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

The utility model discloses a fluidized bed gas distributor base, package rubbing board personally experiences sth. Part of the body, sets up the zone of aeration on the plate body, its characterized in that: still include the microwave heating pipe, every the bar air vent that includes a plurality of evenly distributed on the zone of aeration, the zone of aeration with the microwave heating intertube separates evenly distributed. Compared with the prior art, the hot air circulation in bar hole of ventilating is big for the material of tiny particle and the material of large granule can all the fluidizations, can not produce the phenomenon that flows and block up of granule. Microwave heating pipe evenly distributed makes the hot -air obtain secondary heating on the plate body, and the material makes the material rapid heating with distributing plate contact while, microwave heating pipe, makes the large granule resolve into the tiny particle, further improves the work efficiency of fluidized bed. And to the material of difference, can adjust little wave frequency in the microwave heating pipe for the effect effect of microwave can be according to the material of difference and the difference, remains the maximize of effect throughout.

Description

A kind of fluidized bed gas distribution grid
Technical field
The present invention relates to a kind of new gas distribution grid, particularly a kind of gas distribution grid be applied on fluid bed.
Background technology
Among the fluid a large amount of solid particle being suspended in motion, thus make particle have some appearance features of fluid, the solid contact condition of this stream is called fluidization of solid, and fluidization of solid technology generally applies on fluid bed.The gas distribution grid of fluid bed, can make the gas uniform distribution entering into fluid bed, effectively reduces fluid bed because internal gas skewness causes bed inside to produce the generation of the problems such as hole, channel and dead bed.Under normal circumstances, gas distribution grid in fluid bed is evenly covered with ventilation circular hole, according to the equally distributed distribution grid of ventilation circular hole, often produce short grained material and start fluidisation and the phenomenon of oarse-grained material also not yet fluidisation, easily cause the phenomenon that the flowing of particle blocks, increase fluidizing gas velocity if continue, make oarse-grained material start fluidisation, short grained material then produces elutriation, makes drying efficiency greatly reduce like this.Therefore, develop a kind of fluid bed that can solve to produce the gas distribution grid of clogging because material particles varies in size and seem particularly important.
Utility model content
Technical problem to be solved in the utility model provides a kind of fluid bed that solves to produce the gas distribution grid of clogging because material particles varies in size.
The utility model solves the problems of the technologies described above adopted technical scheme: a kind of fluidized bed gas distribution grid, comprise plate body, the zone of aeration be arranged on plate body, it is characterized in that: also comprise heating using microwave pipe, zone of aeration described in every bar comprises some equally distributed bar shaped passages, described zone of aeration and described heating using microwave pipe interval are uniformly distributed.
Compared with prior art, the thermal air current flux of ventilation bar hole is large, makes short grained material and oarse-grained material can fluidisation, can not produce the phenomenon of the flowing blocking of particle.Heating using microwave pipe is evenly distributed on plate body, makes hot-air obtain post bake, and material contacts with distribution grid simultaneously, and heating using microwave pipe makes material Fast Heating, makes bulky grain resolve into granule, improves the operating efficiency of fluid bed further.And for different materials, heating using microwave Guan Zhongwei wave frequency can be regulated, make the action effect of microwave can be different according to different materials, remain the maximization of effect.The utility model can solve fluid bed and produce the problem of particle flow blocking because material particles varies in size, and adopt heating using microwave pipe to make heating particles speed fast, efficiency is high, homogeneous heating, makes dry materials abundant.
Accompanying drawing explanation
Fig. 1 is example structure schematic diagram.
In accompanying drawing: 1 represents plate body, 2 represent zone of aeration, and 21 represent bar shaped passage, and 3 represent heating using microwave pipe.
Detailed description of the invention
Below in conjunction with accompanying drawing embodiment, the utility model is described in further detail.
As shown in Figure 1, fluidized bed gas distribution grid in the present embodiment, comprise plate body 1, the zone of aeration 2 be arranged on plate body, it is characterized in that: also comprise heating using microwave pipe 3, zone of aeration 2 described in every bar comprises some equally distributed bar shaped passages 21, described zone of aeration 2 and described heating using microwave pipe 3 interval are uniformly distributed.When material enters on the plate body 1 of fluidized bed gas distribution grid, zone of aeration 2 comprises some equally distributed bar shaped passages 21, thermal air current flux is large, short grained material and oarse-grained material is made all to carry out fluidisation, in time being evenly distributed on the heating using microwave pipe 3 on plate body 1, heating using microwave pipe 3 makes material Fast Heating, makes bulky grain resolve into granule, the operating efficiency of further raising fluid bed, also makes hot-air obtain post bake.Heating using microwave pipe 3 firing rate is fast, and homogeneous heating is pollution-free, and regulates micro-wave frequency in heating using microwave pipe 3, makes the action effect of microwave can be different according to different materials, remains the maximization of effect.
Although disclose embodiments of the invention and accompanying drawing for the purpose of illustration, but it will be appreciated by those skilled in the art that: in the spirit and scope not departing from the present invention and claims, various replacement, change and amendment are all possible, therefore, scope of the present invention is not limited to the content disclosed in embodiment and accompanying drawing.

Claims (1)

1. a fluidized bed gas distribution grid, comprise plate body, the zone of aeration be arranged on plate body, it is characterized in that: also comprise heating using microwave pipe, zone of aeration described in every bar comprises some equally distributed bar shaped passages, described zone of aeration and described heating using microwave pipe interval are uniformly distributed.
CN201520773047.1U 2015-09-30 2015-09-30 Fluidized bed gas distributor base Expired - Fee Related CN205042451U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520773047.1U CN205042451U (en) 2015-09-30 2015-09-30 Fluidized bed gas distributor base

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520773047.1U CN205042451U (en) 2015-09-30 2015-09-30 Fluidized bed gas distributor base

Publications (1)

Publication Number Publication Date
CN205042451U true CN205042451U (en) 2016-02-24

Family

ID=55336069

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520773047.1U Expired - Fee Related CN205042451U (en) 2015-09-30 2015-09-30 Fluidized bed gas distributor base

Country Status (1)

Country Link
CN (1) CN205042451U (en)

Similar Documents

Publication Publication Date Title
CN105142830A (en) Fluidized bed for degassing and heat treating powders
CN206613469U (en) A kind of gas distribution grid
CN205042451U (en) Fluidized bed gas distributor base
CN103644733B (en) A kind of hot gas sintering device and sintering method
CN104056549A (en) Smoke SCR denitration system for fluidized fuel gas kiln
CN205447737U (en) Biomass circulating fluid bed boiler returning charge mechanism
CN204735111U (en) Doublestage subregion sprays desulfurizing tower
CN207838339U (en) The multi-functional centrifugal spray drying tower of multisection type
CN202339067U (en) Fluid bed drying device used in traditional Chinese medicine production
CN206375863U (en) A kind of gas distributor for fluidized-bed gasification furnace
CN106363127A (en) Boiling cooling bed
CN207247834U (en) Semi-coke drying system
CN205536895U (en) Take vortex generator's airflow distribution plate structure
CN105716404A (en) Drying device for cement raw slurry
CN105222526B (en) A kind of multilayer bubbling fluidization gumming vertical drying device
CN211358765U (en) Gas distributor
CN203944363U (en) A kind of fluidized bed gas fluidizing agent blowing device
CN201880848U (en) Pneumatic sand dividing device of hot regeneration roasting furnace for casting waste sand
CN203478874U (en) Uniform biomass raw material drying device
CN209054911U (en) A kind of high temperature drying oven suitable for hydrophobic pearlite production
CN101701762B (en) Calandria wind distribution device
CN203842327U (en) Centrifugal hot air distributor of upper air discharge dryer
CN204672253U (en) Spirt wind control structure at the bottom of a kind of fluid bed
CN204522697U (en) A kind of novel seawater desulfurizing and absorption tower
CN203437113U (en) Novel gas distribution plate and application

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: 20160224

Termination date: 20210930