CN87204985U - Annular furnace for powder material - Google Patents

Annular furnace for powder material Download PDF

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Publication number
CN87204985U
CN87204985U CN 87204985 CN87204985U CN87204985U CN 87204985 U CN87204985 U CN 87204985U CN 87204985 CN87204985 CN 87204985 CN 87204985 U CN87204985 U CN 87204985U CN 87204985 U CN87204985 U CN 87204985U
Authority
CN
China
Prior art keywords
heater
charging
charging tray
annular furnace
scraper plate
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.)
Withdrawn
Application number
CN 87204985
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Chinese (zh)
Inventor
龚晓虹
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.)
NANCHANG ACADEMY OF NONFERROUS METALLURGY
Original Assignee
NANCHANG ACADEMY OF NONFERROUS METALLURGY
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 NANCHANG ACADEMY OF NONFERROUS METALLURGY filed Critical NANCHANG ACADEMY OF NONFERROUS METALLURGY
Priority to CN 87204985 priority Critical patent/CN87204985U/en
Publication of CN87204985U publication Critical patent/CN87204985U/en
Withdrawn legal-status Critical Current

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Abstract

The utility model discloses an annular furnace, in particular to an annular furnace for powder materials. The annular furnace is composed of a furnace body which covers outside of a stock disk and is provided with a feed inlet port and a discharge port, the stock disk which can rotate corresponding to the furnace body, a transmission device which drives the rotation of the stock disk and a plurality of electric heating components which are assembled in the furnace body. The utility model is mainly used for heating (drying, burning) the powder materials (primarily useful minerals) in industry, has the differentia of which the utility model can continuously do the feeding, heating and discharging courses compared with existing common box furnaces, car type ovens or tunnel furnaces, and can achieve the effects of low energy consumption and small material breakage.

Description

Annular furnace for powder material
The utility model relates to annular furnace, particularly is used for the annular furnace of granular material.
Current, during industrial heating (or dry, or calcination) granular material (mainly being valuable mineral), adopt batch-type furnace, car-type stove or tunnel cave more.Before heating, all need earlier granular material to be placed container, again the container that fills material is packed in the stove, use such stove heating granular material that three big shortcomings are arranged: one, material surface area in container is little, thickness is big, does not mix, and container center place material reaches required heating-up temperature, the palpus long period, consume more energy<for example: the average current drain with batch-type furnace calcination mishmetal is 8--12 degree/kilogram 〉.Two, by manually-operated, labour intensity is big during input and output material.Three, granular material dust from flying when charging and discharging, consume is big.
The purpose of this utility model is: input and output material mechanization is provided, and energy consumption is low, and the material consume is few, is used for the annular furnace of granular material.
Above-mentioned purpose, by following nine scheme implementations one: stove is by the body of heater that covers in outside the charging tray, and the charging tray that rotates with respect to body of heater drives transmission device and some groups of heater blocks that charging tray rotates and forms.Have charging aperture and discharging opening on the body of heater, charging tray has the flange that stops that granular material is overflowed.During work, charging tray rotates, and material is added on the charging tray and with charging tray from the charging aperture on the body of heater and rotates, and heating is rotated a nearly garden Zhou Houcong discharging opening and discharged.Be not difficult to find out, adopt this scheme can heat granular material, can make charging, heating, discharging is worked continuously, and material is uniformly distributed on the charging tray, material heating surface area big<this material places container 〉, and homogeneous heating reach energy-conservation effect.Above-mentioned heater block can be the electroheat member that resistance wire is entwined, and also can be the nozzle of fuel injection nozzle or spray fuel gas.Above-mentioned structure with charging tray of flange is: the metal structure support body of garden annular, support body cross section are a rectangular channel, and trench bottom serves as a contrast into diatomite brick, and shop, top refractory brick constitutes card, and inboard embedding of card exceeds the card quarl, constitutes the charging tray flange.Scheme two: between body of heater and the charging tray, have two groups of sealing devices.Hot-air and stove circulate outward in the isolated stove of this scheme, in order to energy-conservation.The structure of this sealing device is: on the disk body of charging tray card inboard, load onto an annular tongue<cross section is a rectangle 〉, the sand of packing in the groove, pack on week in garden, the card outside be with Baltimore groove refractory brick<when granular material adds fashionable, can be full of in the Baltimore groove 〉, with two corresponding bodies of heater of cannelure on, each fixes an annular metal sheet, and makes it in the insertion groove.Scheme three: when granular material that discharging scraper plate ┈ then heats being housed on the body of heater forwarding discharging opening to, be subjected to stopping of discharging scraper plate, can flow out from discharging opening.The discharging scraper plate can be a hand-operated lifting ' ⊥ ' font scraper plate also can be electronic scroll casing shape rotor segment.Scheme four: some groups of claws are housed on the body of heater, and claw is contained in the top of charging tray, and stove when work can harrow into corrugatedly adding thermal material on the card, makes it to increase heated surface area, in order to energy-conservation.The structure of claw can be the straight shape grid type of grid, pears capitiform grid type or blade roll cylinder formula stirring-up rake.Scheme five: the claw in the scheme four, accomplish during installation: on week, the rake teeth on the adjacent claw staggers mutually in arbitrary garden that charging tray rotates.Installation can make material stir ┈ in stove and translate into the bottom being in the upper face material originally like this, can translate into upper face to the material that was in the bottom originally again.Material is heated evenly as a complete unit, shortens heat time heating time, in order to energy-conservation.Scheme six: with the charging tray rotation direction is positive direction, in the place ahead of charging aperture, height-adjustable charging scraper plate is housed on the body of heater, then enters the material in the stove, and its fabric thickness is more even.The structure of charging scraper plate can be manual or electric up-down ' ⊥ ' font scraper plate also can be a funnel board plug type scraper plate.Scheme seven: with the charging tray rotation direction is positive direction, and striker plate is equipped with at the outer rim place of the charging tray between charging aperture and charging scraper plate on the body of heater.The effect of this striker plate is: control the cloth width 1..2. prevent that powder from spilling outside the stove.The structure of striker plate: can be parallel-moving type ' Qian ' shape striker plate (horizontal fixed is in the body of heater side), also can be suspension type ' ⊥ ' striker plate (the body of heater top is fixed in suspension).Scheme eight: the striker plate in the scheme seven has the device of regulating its backgauge width.This scheme can be regulated the width of cloth on the charging tray.Regulating the cloth width is exactly in fact to regulate the heated surface area of material in stove, makes it and thickness of feed layer constitutes best heating (or roasting) operation system with the charging tray rotary speed, to reach maximum output and energy-conservation to greatest extent.The structure of adjusting device is an example with the manual rotary baffle plate: the striker plate place is installed at the body of heater top fixes a garden shape steel plate, steel plate center and garden week boring shape are with center ring flange with holes, the steel pole that striker plate is housed inserts in the centre bore, the steel pole of rotation striker plate also is locked in a certain hole of ring flange, can regulate the cloth width.Scheme nine (optimum structure of the present utility model): scheme one, two, six described structures install additional on the body of heater: A. discharging scraper plate.B. some groups of claws, the tooth on the adjacent set claw staggers mutually.C. be positive direction with the charging tray rotation direction, between the charging scraper plate was with charging aperture, (adorning on the body of heater) had striker plate, striker plate to have the device of regulating the cloth width.The structure of these each parts of scheme is as described in above each scheme.Should be noted that: A. is except that scheme eight (for affiliate program), and above-mentioned all schemes are independent alternative.The fragment material also can adopt the utility model not only to be used for granular material.
With such scheme nine is example, make 300 tons of annular furnaces that are used for calcination mishmetal granular material of an annual processing, through commerical test, reach following effect: power consumption 3--5 degree/kilogram (existing stove power consumption is 8--12 degree/kilogram), 150--210 ten thousand degree therefore can economize on electricity every year.Can improve rare earth calcination quality, the rare earth oxide total amount can reach 95%, if the rare earth oxide of (the utility model stove is produced) 95% content is than expensive 0.3 ten thousand yuan/ton of (existing stove is produced) 92% content, then the price aspect can increase by 900,000 yuan/year economic benefit.
Accompanying drawing is represented embodiment.

Claims (3)

1, annular furnace, annular furnace especially for granular material, by covering in one of body of heater [1] outside the charging tray [2] (body of heater [1] has charging aperture [9] and discharging opening [10]), [2] one of the charging trays that rotates with respect to body of heater [1], drive [16] one groups of transmission devices and several electric heating elements [17,18,19,20] composition that charging tray [2] rotates, it is characterized in that:
A, charging tray [2] have the flange [14] that stops that granular material is overflowed.
Between b, body of heater [1] and the charging tray [2], has sealing device [3].
On c, the body of heater [1],, charging scraper plate [11] is housed in the place ahead of charging aperture [9] (is positive direction with charging tray [2] rotation direction).
Striker plate [13] is equipped with in the place ahead of d, described charging scraper plate [11] (is positive direction with charging tray [2] rotation direction) on the body of heater [1].
Several claws [5,6,7,8 ,] are housed one by one on arbitrary circumference that charging tray [2] rotates on e, the body of heater [1], the tooth on the adjacent claw staggers mutually.
On f, the body of heater [1] discharging scraper plate [4] is housed.
2, annular furnace according to claim 1 is characterized in that charging scraper plate [ 11 ] has the lowering or hoisting gear [ 12 ] of regulating its height.
3,, it is characterized in that striker plate [ 13 ] has the device [ 15 ] of regulating its backgauge width according to claim 1,2 described annular furnaces.
CN 87204985 1987-03-30 1987-03-30 Annular furnace for powder material Withdrawn CN87204985U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 87204985 CN87204985U (en) 1987-03-30 1987-03-30 Annular furnace for powder material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 87204985 CN87204985U (en) 1987-03-30 1987-03-30 Annular furnace for powder material

Publications (1)

Publication Number Publication Date
CN87204985U true CN87204985U (en) 1988-03-02

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 87204985 Withdrawn CN87204985U (en) 1987-03-30 1987-03-30 Annular furnace for powder material

Country Status (1)

Country Link
CN (1) CN87204985U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102297576A (en) * 2011-07-28 2011-12-28 杭州科力化工设备有限公司 Horizontal disk type drying machine
CN103017517A (en) * 2013-01-16 2013-04-03 江苏中腾炉业有限公司 Annular automatic natural gas heating furnace
CN103090666A (en) * 2013-01-31 2013-05-08 柯妍 Millstone type rotary hearth furnace
CN108645225A (en) * 2018-08-10 2018-10-12 江西银杉白水泥有限公司 A kind of white cement cooling grate-cooler
CN114046662A (en) * 2021-11-30 2022-02-15 无锡市三晓新材料有限公司 Material tray and material raking equipment for zeolite activated powder production

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102297576A (en) * 2011-07-28 2011-12-28 杭州科力化工设备有限公司 Horizontal disk type drying machine
CN103017517A (en) * 2013-01-16 2013-04-03 江苏中腾炉业有限公司 Annular automatic natural gas heating furnace
CN103090666A (en) * 2013-01-31 2013-05-08 柯妍 Millstone type rotary hearth furnace
CN108645225A (en) * 2018-08-10 2018-10-12 江西银杉白水泥有限公司 A kind of white cement cooling grate-cooler
CN114046662A (en) * 2021-11-30 2022-02-15 无锡市三晓新材料有限公司 Material tray and material raking equipment for zeolite activated powder production

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