CN201250266Y - Gold concentrate sulfating fluosolid roaster - Google Patents

Gold concentrate sulfating fluosolid roaster Download PDF

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Publication number
CN201250266Y
CN201250266Y CNU2008200274497U CN200820027449U CN201250266Y CN 201250266 Y CN201250266 Y CN 201250266Y CN U2008200274497 U CNU2008200274497 U CN U2008200274497U CN 200820027449 U CN200820027449 U CN 200820027449U CN 201250266 Y CN201250266 Y CN 201250266Y
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CN
China
Prior art keywords
roaster
layer
utility
model
sulfating
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
CNU2008200274497U
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Chinese (zh)
Inventor
徐永祥
吕寿明
姚树建
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.)
SHANDONG GUODA GOLD CO Ltd
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SHANDONG GUODA GOLD 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.)
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Publication date
Application filed by SHANDONG GUODA GOLD CO Ltd filed Critical SHANDONG GUODA GOLD CO Ltd
Priority to CNU2008200274497U priority Critical patent/CN201250266Y/en
Application granted granted Critical
Publication of CN201250266Y publication Critical patent/CN201250266Y/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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

The utility model relates to a gold concentrate sulfating fluosolid roaster which belongs to the technical field of gold smelting mechanized equipment. The gold concentrate sulfating fluosolid roaster comprises a cylindrical structure shell. The utility model is characterized in that the surface of the inner wall of the shell is provided with a fireproof insulating layer to for temperature insulating; the bottom part is an air chamber; a grid plate and a funnel cap are arranged on the upper surface of the air chamber; the funnel cap is cast on the grid plate of a fireproof casting layer by fireproof casting material; the part above the funnel cap inside the body of the roaster is a hearth which comprises a fluidized burning layer, a diffusion layer, and an upper layer; the upper part of the fluidized burning layer is uniformly provided with a group of spraygun jacks; the lower part is provided with a bleed hole connected with a star valve; the center of the top of the roaster is provided with a floss hole; the lower part of the body of the roaster is provided with an overhauling roaster gate. The utility model has a simple structure and high suitability, is suitable for the fluidized baking of sulphide ore powder materials, can realize self heat balance continuous operation; the temperature fluctuation is very small; the work is stable and the maintenance cost is low.

Description

A kind of gold ore sulfation fluidizing reactor
One, technical field
The utility model relates to a kind of gold ore sulfation fluidizing reactor, belongs to gold smelting industry stoving oven technical field of structures.
Two, background technology
At present, domestic gold smelting industry generally adopts the cyanide process Technology to reclaim gold and silver from gold ore.In order to improve recovery of gold and silver, reduce raw material consumption such as prussiate, remove impurity components such as copper-lead zinc, the general method of sulfurization roasting that adopts is carried out oxide treatment to such gold mine, copper in the gold ore, zinc etc. are become soluble sulphate, remove by methods such as acidleach, and reclaim non-ferrous metals such as wherein copper, zinc.The major equipment of roasting oxidation method is a stoving oven, and stoving oven commonly used mainly contains rotary kiln, shaft kiln, fluidizing furnace etc.Because fluidizing furnace is simple in structure, be fit to the fluosolids roasting of sulphide ores powder raw material, and can autothermal equilibrium, serialization production etc., so the fluidized bed roasting technology develops very soon at home in recent years, corresponding fluidizing furnace form also constantly occurs.Domestic fluidizing furnace commonly used mainly is the dry feed mode at present.There are three main drawbacks in this feeding manner: the one, and raw material needs drying, and needs to pulverize and screening, has increased the raw material processing costs; The 2nd, raw material need mix and transport, the appearance mixing is inhomogeneous easily, charging is discontinuous, charging opening stops up easily etc., make the interior temperature fluctuation of stove bigger, do not allow easy operation control, owing to adopt about 600 ℃ sulfurization roasting condition, particularly when the raw material sulfur-bearing is low, be easy to dead stove, increased the difficulty of operation control; The 3rd, heat sinks such as water tank must be set in the stove, prevent that temperature is too high in the stove, guarantee the processing condition of sulfurization roasting, increased auxiliary facility.
Three, summary of the invention
The purpose of this utility model is to solve the weak point that above-mentioned prior art exists, a kind of gold ore sulfation fluidizing reactor is provided, this stoving oven changes original dry feed the mode of wet method slurry type feeding into by texture improvement, solves that gold ore fluidizing furnace job insecurity, temperature fluctuation when sulfation are big, raw material needs problems such as drying.
The utility model technical solution is as follows:
A kind of gold ore sulfation fluidizing reactor, comprise cylinder type housing 7, special character is that housing 7 inner wall surface are provided with refractory insulating layer 6 and are incubated, the bottom is an air compartment 11, be air distribution plate 2 and blast cap 1 above the air compartment, the fire-resistant pouring material of blast cap 1 usefulness is cast on the air distribution plate 2 of fire-resistant LIFT 3; At the inner blast cap of body of heater is burner hearth more than 1, comprises Boiling Combustion layer, diffusion layer, upper strata; Boiling Combustion layer top is laid with one group of spray gun jack 4, and the bottom is provided with a slag-drip opening 8 that is connected with star-like valve 9; Furnace roof central authorities top is provided with a floss hole 5, and the body of heater bottom is provided with a maintenance fire door 10;
Described housing 7 is to be made by steel plate;
The number of described spray gun jack 4 can be provided with 3-4 as required.
The utility model carries out technological transformation and finishes on original fluidized bed roasting furnace foundation, original dry feed fluidizing reactor is transformed into wet method slurry type feeding mode, dry feed mouth and feeding device on original fluidizing reactor have been deleted, deleted heat sink such as cooling water tank on original fluidizing reactor, increase by one group of (three or four) spraying gun jack, to burn the slag slag-drip opening 300~400mm that moves up, floss hole will be changed into furnace roof central authorities.
Advantage of the present utility model mainly is: simple in structure, adaptability is strong, the fluosolids roasting that is fit to the sulphide ores powder raw material, adopt wet method slurry type feeding mode, work for about 600 ℃ in the stove, can autothermal equilibrium, the serialization operation, temperature fluctuation is very little, stable working has solved the problem that original dry feed fluidizing reactor exists, and has deleted on original fluidizing reactor heat sinks such as cooling water tank simultaneously, and original raw material drying operation, reduced maintenance cost and production cost.
Four, description of drawings
Fig. 1: a kind of gold ore sulfation of the utility model embodiment fluidizing reactor structural representation.
Among the figure, blast cap 1, air distribution plate 2, fire-resistant LIFT 3, spray gun jack 4, floss hole 5, refractory insulating layer 6, housing 7, slag-drip opening 8, star-like valve 9, air compartment 11, maintenance fire door 10.
Five, embodiment
Following with reference to accompanying drawing 1, provide embodiment of the present utility model, be used for formation of the present utility model is further specified.
Embodiment
A kind of gold ore sulfation fluidizing reactor is with reference to figure 1, housing 7 is made into cylinder type by steel plate, and the outer cover of steel plate inner wall surface is provided with refractory insulating layer 6, and the bottom is an air compartment 11, be air distribution plate 2 and blast cap 1 above the air compartment, the fire-resistant pouring material of blast cap 1 usefulness is cast on the air distribution plate of fire-resistant LIFT 3; More than the inner blast cap of body of heater is burner hearth, comprises Boiling Combustion layer, diffusion layer, upper strata etc.; Boiling Combustion layer top uniform three spray gun jacks 4, the bottom is provided with a slag-drip opening 8 and is connected with star-like valve 9, furnace roof is provided with a floss hole 5, the body of heater bottom is provided with a maintenance fire door 10.
Advantage of the present utility model mainly is: simple in structure, strong adaptability is fit to the sulphide ore powder The fluosolids roasting of raw material adopts wet method slurry type feeding mode, works energy for about 600 ℃ in the stove Enough autothermal equilibriums, continuous operations, temperature fluctuation is very little, and stable working has solved original dry method The problem that the charging fluidizing reactor exists has been deleted on original fluidizing reactor cooling water tank etc. simultaneously Heat sink, and original raw material drying operation have reduced maintenance cost and production cost.

Claims (3)

1, a kind of gold ore sulfation fluidizing reactor, comprise cylinder type housing (7), be characterised in that housing (7) inner wall surface is provided with refractory insulating layer (6) and is incubated, the bottom is air compartment (11), above the air compartment air distribution plate (2) and blast cap (1), blast cap (1) is cast on the air distribution plate (2) of fire-resistant LIFT (3) with fire-resistant pouring material, more than the inner blast cap of body of heater (1) is burner hearth, comprise the Boiling Combustion layer, diffusion layer, the upper strata, Boiling Combustion layer top is laid with one group of spray gun jack (4), the bottom is provided with a slag-drip opening (8) that is connected with star-like valve (9), furnace roof central authorities are provided with a floss hole (5), and the body of heater bottom is provided with a maintenance fire door (10).
2, according to the described a kind of gold ore sulfation fluidizing reactor of claim 1, it is characterized in that described housing (7) is to be made by steel plate.
3,, it is characterized in that described spray gun jack (4) is provided with 3-4 according to the described a kind of gold ore sulfation fluidizing reactor of claim 1.
CNU2008200274497U 2008-09-04 2008-09-04 Gold concentrate sulfating fluosolid roaster Expired - Fee Related CN201250266Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008200274497U CN201250266Y (en) 2008-09-04 2008-09-04 Gold concentrate sulfating fluosolid roaster

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008200274497U CN201250266Y (en) 2008-09-04 2008-09-04 Gold concentrate sulfating fluosolid roaster

Publications (1)

Publication Number Publication Date
CN201250266Y true CN201250266Y (en) 2009-06-03

Family

ID=40745938

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008200274497U Expired - Fee Related CN201250266Y (en) 2008-09-04 2008-09-04 Gold concentrate sulfating fluosolid roaster

Country Status (1)

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CN (1) CN201250266Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102564126A (en) * 2012-03-01 2012-07-11 中国恩菲工程技术有限公司 Copper-nickel high-sulfonium fluidization roasting furnace
CN104846215A (en) * 2014-11-14 2015-08-19 江西瑞林稀贵金属科技有限公司 Smelting furnace
CN106766906A (en) * 2016-11-30 2017-05-31 河池市技术开发中心 A kind of new concentrate fluidizing reactor furnace binding

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102564126A (en) * 2012-03-01 2012-07-11 中国恩菲工程技术有限公司 Copper-nickel high-sulfonium fluidization roasting furnace
CN104846215A (en) * 2014-11-14 2015-08-19 江西瑞林稀贵金属科技有限公司 Smelting furnace
CN106766906A (en) * 2016-11-30 2017-05-31 河池市技术开发中心 A kind of new concentrate fluidizing reactor furnace binding

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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: 20090603