CN203173850U - Deaminization furnace for preparing vanadium pentoxide from ammonium vanadate - Google Patents
Deaminization furnace for preparing vanadium pentoxide from ammonium vanadate Download PDFInfo
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- CN203173850U CN203173850U CN2013200340907U CN201320034090U CN203173850U CN 203173850 U CN203173850 U CN 203173850U CN 2013200340907 U CN2013200340907 U CN 2013200340907U CN 201320034090 U CN201320034090 U CN 201320034090U CN 203173850 U CN203173850 U CN 203173850U
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- tunnel type
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- type furnace
- charging tray
- deamination
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
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Abstract
The utility model provides a deaminization furnace for preparing vanadium pentoxide from ammonium vanadate, which is simpler in structure, convenient to operate, continuous in production, energy saving and environmentally friendly. The deaminizing furnace includes a tunnel type furnace body, material trays, material tray transmission chains, chain guide rails, heating pipes, temperature conduction devices, exhaust pipes and a support frame, wherein the tunnel type durance body falls into three regions, namely a dehydration region, a deaminization region and a heat preservation region; the heating pipes are arranged on each of the three regions; the temperature conduction devices are arranged on each of the three regions; the chain guide rails are arranged on two sides of the inner bottom wall of the tunnel type furnace body; the material tray transmission chains are arranged on the chain guide rails via rotating wheels at two ends; one side of each material tray is movably clamped between the material tray transmission chains; the exhaust pipes are arranged at the top of each of the regions of the tunnel type furnace body; and the tunnel type furnace body is fixedly supported on the support frame.
Description
Technical field
The utility model relates to a kind of calcining furnace, particularly relates to a kind of ammonium vanadate and produces the full-automatic special-purpose deamination stove of Vanadium Pentoxide in FLAKES, belongs to the chemical metallurgy technical field.
Background technology
Ammonium vanadate comprises ammonium meta-vanadate (NH
4VO
3) or ammonium poly-vanadate (APV), produce Vanadium Pentoxide in FLAKES (V through the calcining deamination
2O
5) be an important procedure in the metallurgical whole process of vanadium.Obtain the powdery Vanadium Pentoxide in FLAKES from ammonium meta-vanadate or ammonium poly-vanadate and generally will pass through dehydration, deamination, three steps of oxidation insulation.In Vanadium Pentoxide in FLAKES Industrial processes in the past, what domestic vanadium factory adopted substantially is to build the box-type furnace of system with refractory brick or clay brick, well heater is the pure resistance silk, this tile stove distortion is big, poor sealing performance, cause the firing time long (general more than 72 hours), unit power consumption (is generally 1200~1400KWh/ ton V greatly
2O
5), ammonia leakage is serious, and neither environmental protection is also dangerous, and the rate of recovery is generally less than 99%, the product color instability.Utility model patent (CN201458771u) has designed the box deamination stove of stainless steel, adopts the heating of stainless steel electrothermal tube, the aluminium silicate wool insulation, solved the drawback of brick stove processed, heat insulation effect improves greatly, and the firing time shortens to 13~19 hours, and power consumption drops to 760KWh/ ton V
2O
5, set up the ammonia recovery tower simultaneously, solve ammonia effectively and reclaimed problem, reduced production cost, accomplished energy-conserving and environment-protective.But production process still is unrealized continuously, still is in the batch production state, and automatization level is low, and turnout very much not gets up, and does not still satisfy large-scale production.Though have three sections method of fusion to produce this kind equipment of Vanadium Pentoxide in FLAKES at present, have that facility investment is big, a complex structure, operation link is many, work production is low defective abroad.
Summary of the invention
So the purpose of this utility model is to provide, and a kind of structure is comparatively simple, easy to operate, production is continuous, ammonium vanadate energy-conserving and environment-protective are produced the full-automatic deamination stove of Vanadium Pentoxide in FLAKES.
In order to solve above-mentioned technological deficiency, a kind of ammonium vanadate provided by the utility model is produced the deamination stove of Vanadium Pentoxide in FLAKES, it is characterized in that it comprises: tunnel type furnace body, charging tray, charging tray driving chain, chain guide, heating tube, temperature conduction device, vapor pipe, resting support; Described tunnel type furnace body is divided into three districts: drying zone, deamination district, heat preservation zone, and the top evenly is provided with heating tube in described three districts, and subregion arranges the temperature conduction device; The diapire both sides are provided with chain guide in the tunnel type furnace body, and the charging tray driving chain places on the chain guide by the rotor wheel at two ends, and charging tray one side active card is between the charging tray driving chain; The outer top of each subregion of described tunnel type furnace body is equipped with vapor pipe; Described tunnel type furnace body is by the resting support fixed support.
Described heating tube is far-infrared heating tube or microwave device.
Described charging tray driving chain drive line speed is 5~12m/h.
Described tunnel type furnace body opening for feed one side is provided with an automatic charge device.
Described tunnel type furnace body burner hearth wall is equipped with the heat-resistant light insulating cotton.
The number of described each subregion vapor pipe, temperature conduction device is decided according to the design length of each subregion, and general interval arranges one for 5 meters.
Its basic functional principle is: ammonium meta-vanadate or ammonium poly-vanadate are in automatic charge device branch is packed the stainless steel charging tray into, charging tray slowly moves in tunnel type furnace body with the linear velocity of 5~13m/h by chain, dewater under 120~200 ℃ of temperature through drying zone earlier, water vapor is discharged by vapor pipe, about 2~3h of time; After the dehydration, charging tray has entered the deamination district, carries out deamination under 210~550 ℃ of temperature, and ammonia is sent into the ammonia retrieving arrangement of establishing in addition by vapor pipe and variable valve and reclaimed, and the deamination time is 5~6h; Ammonia enters the insulation oxidation zone after taking off and finishing, be arranged on 300~80 ℃ in this district's temperature, form gradually cold state, strengthen the inlet of air simultaneously, assurance oxygen abundance, oxidation is abundant, about 2~3h of time, at this moment charging tray has moved to discharge end, and the ammonium vanadate in the charging tray has been produced the powdery Vanadium Pentoxide in FLAKES of yellowish-orange; Finished product along with the upset of charging tray, is poured in the storage bunker in charging tray automatically in operational process, and empty charging tray continues to be circulated to loading area.Burner hearth adds thermal recovery far-infrared heating tube or microwave device and carries out the penetrating type heating, and temperature control is by circuit of SCR control, temperature error ± 3 ℃; Body of heater carries out the four sides insulation by aluminium silicate wool; Transmission system is dragged by variable-frequency motor, can realize the stepless change transmission.The length of each subregion is determined by the time according to the raw material that arranges in the tunnel type furnace body, and the length in general deamination district is greater than the length of drying zone and heat preservation zone.
Beneficial effect: the utility model structure is comparatively simple, efficient, high, the safety and environmental protection, energy-conservation, anticorrosion durable of level of automation.The time of coming out of the stove is 9~13h, ton V
2O
5Power consumption is 650~700kWh, produces continuously, and output is big, and full burner hearth carries out constant product quality in the aerobic atmosphere of abundance.
Description of drawings
Fig. 1 is the utility model longitudinal structure synoptic diagram
Fig. 2 is the utility model horizontal section synoptic diagram
Embodiment
As shown in Figure 1, 2, a kind of ammonium vanadate is produced the deamination stove of Vanadium Pentoxide in FLAKES, and it is to be made of tunnel type furnace body 1, charging tray 2, charging tray driving chain 3, chain guide 4, heating tube 5, temperature conduction device 6, vapor pipe 7, automatic charge device 8, resting support 9 etc.Described tunnel type furnace body 1 is divided into three districts: drying zone, deamination district, heat preservation zone, and 60 meters of total lengths are long; The top evenly is provided with far infrared heating pipe 5 in described three districts, and subregion arranges the temperature conduction device, 4 of drying zones, 8 in deamination district, 4 of heat preservation zone; The diapire both sides are provided with chain guide 4 in the tunnel type furnace body, and charging tray driving chain 3 places on the chain guide 4 by the rotor wheel at two ends, and charging tray 2 one side active card are between charging tray driving chain 3; The outer top of described tunnel type furnace body 1 each subregion is equipped with vapor pipe 7,4 of drying zones, 8 in deamination district, 4 of heat preservation zone; Described tunnel type furnace body 1 is by resting support 9 fixed supports; Be provided with the thermal insulation layer made from the light thermal-insulation cotton around the rectangular setting of body of heater 1 and burner hearth, the inside casing of body of heater 1; Feed end and discharge end are divided in the body of heater two ends, automatic charge device 8 delivery platies 2 quantitative charging feedstocks are set before feed end, charging tray 2 evenly distributes along driving chain 3, driving chain 3 is poured finished product into storage bunker by the material containing charging tray 2 that burner hearth moves out from the automatic upset in discharge end cooling back by chain guide 4 bracketings; Empty charging tray 2 is circulated to feed end by driving chain 3 and feeds into stove successively.
Claims (5)
1. an ammonium vanadate is produced the deamination stove of Vanadium Pentoxide in FLAKES, it is characterized in that it comprises: tunnel type furnace body, charging tray, charging tray driving chain, chain guide, heating tube, temperature conduction device, vapor pipe, resting support; Described tunnel type furnace body is divided into three districts: drying zone, deamination district, heat preservation zone, and the top evenly is provided with heating tube in described three districts, and subregion arranges the temperature conduction device; The diapire both sides are provided with chain guide in the tunnel type furnace body, and the charging tray driving chain places on the chain guide by the rotor wheel at two ends, and charging tray one side active card is between the charging tray driving chain; The outer top of each subregion of described tunnel type furnace body is equipped with vapor pipe; Described tunnel type furnace body is by the resting support fixed support.
2. according to claim
1Described a kind of ammonium vanadate is produced the deamination stove of Vanadium Pentoxide in FLAKES, it is characterized in that: described heating tube is far-infrared heating tube or microwave device.
3. according to claim
1Described a kind of ammonium vanadate is produced the deamination stove of Vanadium Pentoxide in FLAKES, it is characterized in that: described charging tray driving chain drive line speed is 5~12m/h.
4. according to claim
1Described a kind of ammonium vanadate is produced the deamination stove of Vanadium Pentoxide in FLAKES, it is characterized in that: described tunnel type furnace body opening for feed one side is provided with an automatic charge device.
5. according to claim
1Described a kind of ammonium vanadate is produced the deamination stove of Vanadium Pentoxide in FLAKES, it is characterized in that: described tunnel type furnace body burner hearth wall is equipped with the heat-resistant light insulating cotton.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2013200340907U CN203173850U (en) | 2013-01-23 | 2013-01-23 | Deaminization furnace for preparing vanadium pentoxide from ammonium vanadate |
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CN2013200340907U CN203173850U (en) | 2013-01-23 | 2013-01-23 | Deaminization furnace for preparing vanadium pentoxide from ammonium vanadate |
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CN203173850U true CN203173850U (en) | 2013-09-04 |
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CN2013200340907U Expired - Fee Related CN203173850U (en) | 2013-01-23 | 2013-01-23 | Deaminization furnace for preparing vanadium pentoxide from ammonium vanadate |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105502328A (en) * | 2015-12-19 | 2016-04-20 | 安徽天寅生物技术有限公司 | Continuous type mesh belt heating furnace |
CN105546978A (en) * | 2016-01-07 | 2016-05-04 | 攀钢集团攀枝花钢钒有限公司 | Preparation system of vanadium pentoxide |
CN105823328A (en) * | 2016-04-21 | 2016-08-03 | 青岛智邦炉窑设计研究有限公司 | Far infrared thermal radiation hydrogen reduction roasting device and process |
CN116924472A (en) * | 2023-09-14 | 2023-10-24 | 崇义章源钨业股份有限公司 | Comprehensive utilization method of tungsten-containing magnesium ammonium phosphate slag |
-
2013
- 2013-01-23 CN CN2013200340907U patent/CN203173850U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105502328A (en) * | 2015-12-19 | 2016-04-20 | 安徽天寅生物技术有限公司 | Continuous type mesh belt heating furnace |
CN105546978A (en) * | 2016-01-07 | 2016-05-04 | 攀钢集团攀枝花钢钒有限公司 | Preparation system of vanadium pentoxide |
CN105823328A (en) * | 2016-04-21 | 2016-08-03 | 青岛智邦炉窑设计研究有限公司 | Far infrared thermal radiation hydrogen reduction roasting device and process |
CN116924472A (en) * | 2023-09-14 | 2023-10-24 | 崇义章源钨业股份有限公司 | Comprehensive utilization method of tungsten-containing magnesium ammonium phosphate slag |
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Date | Code | Title | Description |
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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: 20130904 Termination date: 20140123 |