CN202074782U - Drying equipment for producing ceramsite filter material - Google Patents

Drying equipment for producing ceramsite filter material Download PDF

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Publication number
CN202074782U
CN202074782U CN2011200586594U CN201120058659U CN202074782U CN 202074782 U CN202074782 U CN 202074782U CN 2011200586594 U CN2011200586594 U CN 2011200586594U CN 201120058659 U CN201120058659 U CN 201120058659U CN 202074782 U CN202074782 U CN 202074782U
Authority
CN
China
Prior art keywords
drying
drying baker
drying box
box
heating tube
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
CN2011200586594U
Other languages
Chinese (zh)
Inventor
罗秀坤
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.)
JIANGXI SHUANGLONG ENVIRONMENTAL PROTECTION CHEMICAL MINERALS INDUSTRY GROUP CO LTD
Original Assignee
JIANGXI SHUANGLONG ENVIRONMENTAL PROTECTION CHEMICAL MINERALS INDUSTRY GROUP 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 JIANGXI SHUANGLONG ENVIRONMENTAL PROTECTION CHEMICAL MINERALS INDUSTRY GROUP CO LTD filed Critical JIANGXI SHUANGLONG ENVIRONMENTAL PROTECTION CHEMICAL MINERALS INDUSTRY GROUP CO LTD
Priority to CN2011200586594U priority Critical patent/CN202074782U/en
Application granted granted Critical
Publication of CN202074782U publication Critical patent/CN202074782U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to drying equipment for producing ceramsite filter material. The drying equipment comprises a control box (1), a drying box (3), net racks (5), a heating tube (6) and a fan (7), wherein the control box (1) is positioned on the side surface of the drying box (3); a box door (2) is arranged on the front side of the drying box (3), the net racks (5) are arranged inside the drying box (3), and the heating tube (6) is arranged at the top of the drying box (3); an air duct (4) is arranged at the top of the drying box (3), and vent holes (8) leading to the inside of the drying box (3) are arranged under the air duct (4); an air outlet of the fan (7) is communicated with the air duct (4); upper and lower box doors (2) are arranged in the drying box (3); the net racks (5) are respectively arranged on the inside of each box door (2) in the drying box (3); a heat insulating layer (9) is arranged outside the drying box (3). The drying equipment has the advantages of low investment, high heat insulation efficiency of the drying box, small floor space, low power consumption and high thermal efficiency.

Description

Ceramic grain filter production drying plant
Technical field
The utility model relates to the equipment of filtrate production usefulness, is specifically related to ceramic grain filter production drying plant.
Background technology
With the BAF method (be called for short: PROCESS FOR TREATMENT city domestic sewage BAF) because its effluent quality amount advantages of higher more and more is subjected to extensive concern, especially for the after-treatment of sanitary sewage, more apparent its obvious superiority.The key that biological aerated filter process is achieved success is the selection that is filtrate.Select good filtrate assurance to obtain good decontamination effect, improve effluent characteristics, can also significantly lower operation management expense and energy consumption.Filtrate and filtrate system are that the success or not of BAF technology has one of conclusive key factor.The production process of filtrate comprises fragmentation, raw material mix grinding, the dedusting of workshop, the machine-processed balling-up of raw material, the screening of half-finished particle diameter, the oven dry of product and the baking of product of clay.Wherein in the drying course of product, existing drying plant has many types, but these equipment are not suitable for the oven dry production of filtrate, have the shortcoming that power consumption is big, the thermal efficiency is low.
The utility model content
The purpose of this utility model provides a kind of ceramic grain filter production drying plant, and the dryer that the utility model has solved prior art is not suitable for the oven dry production problem of filtrate, and the utility model provides a kind of power consumption low, the dryer that the thermal efficiency is high.
Ceramic grain filter production drying plant of the present utility model is made of control cabinet (1), drying baker (3), rack (5), heating tube (6) and blower fan (7); Control cabinet (1) is positioned at drying baker (3) side; There is chamber door (2) drying baker (3) front side, and there is rack (5) drying baker (3) inside, and heating tube (6) is arranged at drying baker (3) top; Also have an air channel (4) at drying baker (3) top, have below air channel (4) and lead to the inner air vent (8) of drying baker (3); The air outlet of blower fan (7) is communicated with air channel (4); Two rows chamber door (2) is arranged in drying baker (3); There is row's rack (5) every layer of chamber door (2) inboard in drying baker (3); There is one deck heat-insulation layer (9) drying baker (3) outside.
Ceramic grain filter production drying plant of the present utility model, major function are to the moisture content below 15% the oven dry of media regeneration coal.
Ceramic grain filter production of the present utility model has the following advantages with drying plant:
1, equipment investment is few, adopts the manufacturing of 16Mn steel plate, improves 3-4 doubly service life than general steel plate.
2, drying baker oneself insulating efficiency improves the thermal efficiency 45% up to more than 80% than traditional monotubular dryer thermal efficiency.
3, floor space is little, reduces floor space about 50% than monotubular dryer, and construction investment reduces about 50%, and power consumption reduces about 60%.
4, power consumption is low, the thermal efficiency is high.
5, air outlet temperature is low, and drop temperature is low, can produce continuously, and packing need not into cooling shed or (storehouse) cooling.
Description of drawings
Fig. 1 is the utility model structural representation.
Number in the figure: control cabinet 1, chamber door 2, drying baker 3, air channel 4, rack 5, heating tube 6, blower fan 7, air vent 8, heat-insulation layer 9.
The specific embodiment
Below in conjunction with accompanying drawing and with illustrated embodiments the utility model is done detailed explanation.
Consult Fig. 1, ceramic grain filter production drying plant is made of control cabinet (1), drying baker (3), rack (5), heating tube (6) and blower fan (7); Control cabinet (1) is positioned at drying baker (3) side; There is chamber door (2) drying baker (3) front side, and there is rack (5) drying baker (3) inside, and heating tube (6) is arranged at drying baker (3) top; Also have an air channel (4) at drying baker (3) top, have below air channel (4) and lead to the inner air vent (8) of drying baker (3); The air outlet of blower fan (7) is communicated with air channel (4); Two rows chamber door (2) is arranged in drying baker (3); There is row's rack (5) every layer of chamber door (2) inboard in drying baker (3); There is one deck heat-insulation layer (9) drying baker (3) outside.

Claims (1)

1. ceramic grain filter production drying plant is characterized in that, is made of control cabinet (1), drying baker (3), rack (5), heating tube (6) and blower fan (7); Control cabinet (1) is positioned at drying baker (3) side; There is chamber door (2) drying baker (3) front side, and there is rack (5) drying baker (3) inside, and heating tube (6) is arranged at drying baker (3) top; Also have an air channel (4) at drying baker (3) top, have below air channel (4) and lead to the inner air vent (8) of drying baker (3); The air outlet of blower fan (7) is communicated with air channel (4); Two rows chamber door (2) is arranged in drying baker (3); There is row's rack (5) every layer of chamber door (2) inboard in drying baker (3); There is one deck heat-insulation layer (9) drying baker (3) outside.
CN2011200586594U 2011-03-08 2011-03-08 Drying equipment for producing ceramsite filter material Expired - Fee Related CN202074782U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011200586594U CN202074782U (en) 2011-03-08 2011-03-08 Drying equipment for producing ceramsite filter material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011200586594U CN202074782U (en) 2011-03-08 2011-03-08 Drying equipment for producing ceramsite filter material

Publications (1)

Publication Number Publication Date
CN202074782U true CN202074782U (en) 2011-12-14

Family

ID=45112881

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011200586594U Expired - Fee Related CN202074782U (en) 2011-03-08 2011-03-08 Drying equipment for producing ceramsite filter material

Country Status (1)

Country Link
CN (1) CN202074782U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111497001A (en) * 2020-04-24 2020-08-07 李东 Filter material ceramsite, processing system and processing method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111497001A (en) * 2020-04-24 2020-08-07 李东 Filter material ceramsite, processing system and processing method

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Legal Events

Date Code Title Description
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: 20111214

Termination date: 20120308