CN1760119A - Unit of exhausting waste gas of pusher plate kiln for producing alloy of vanadium-nitrogen and method for exhausting waste gas - Google Patents
Unit of exhausting waste gas of pusher plate kiln for producing alloy of vanadium-nitrogen and method for exhausting waste gas Download PDFInfo
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- CN1760119A CN1760119A CN 200410081200 CN200410081200A CN1760119A CN 1760119 A CN1760119 A CN 1760119A CN 200410081200 CN200410081200 CN 200410081200 CN 200410081200 A CN200410081200 A CN 200410081200A CN 1760119 A CN1760119 A CN 1760119A
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Abstract
A method and apparatus for discharging the waste gas of push bar kiln used to prepare the VN alloy is disclosed. Said push bar kiln is longitudinally and sequentially divided into water discharging low-temp segment, Na-K discharging transition segment, constant-temp high-temp segment and cooling segment. Each segment has several temp regions. A gas curtain is arranged between the low-temp segment and transition segment for isolating them from each other. Several exhaust outlets as respective arranged for said low-temp segment to exhaust water vapour and said transition segment to exhaust the vapour of alkali metals and the waste gas of other compunds.
Description
Technical field
The invention belongs to the VN alloy technical field, relate to a kind of calciner unit of exhausting waste gas of pusher plate kiln and method for exhausting waste gas in industrial continuous production VN alloy.
Background technology
Produce in the method for VN alloy existing, be not mentioned to the method for exhausting waste gas problem of relevant calciner, the common way of batch production technology be in agglomerating plant logical nitrogen, vacuumize, make VN alloy through repeatedly repeating such process, this method for exhausting waste gas applies to the VN alloy production technique described in US3334992, US4040814, the US5462057.But (application number: 01139886.8 in " production method of VN alloy " the patent process of enforcement, publication number CN1422800A), find that method for exhausting waste gas has considerable influence to the corrosion of cavity material in the pushed bat kiln, its major cause is to contain a certain amount of water vapour and lower boiling alkali metal (Na, K) in the kiln atmosphere.Contain free water and crystal water in the furnace charge of VN alloy, go into the preceding total water-content of kiln below 1%, and contain a certain amount of lower boiling alkali metal.In the low-temperature zone of 400～680 ℃ of pushed bat kilns, water vapour is overflowed from furnace charge, and internally cavity material is implemented oxidation and erosion action; At 850～1450 ℃ transition section, alkali metal is sent out the biophase migration by the mode of steam, runs into water or CO
2After then generate low melting point, high boiling highly basic is attached on the furnace chamber material, and internally cavity material is implemented corrosion.
Summary of the invention
Technical problem to be solved by this invention is at existing above-mentioned defective in the prior art, aim to provide a kind of unit of exhausting waste gas of pusher plate kiln and method for exhausting of production VN alloy, the etchant gas that can as soon as possible each warm area be produced expels from kiln, the corrosion progress of cavity material in slowing down, shorten corrosion area, thereby significantly improve the work-ing life of cavity material in the pushed bat kiln.
The technical scheme that solution the technology of the present invention problem is adopted is the unit of exhausting waste gas of pusher plate kiln of said production VN alloy, and this pushed bat kiln has draining low-temperature zone, row Na
+, K
+Transition section, constant temperature high temperature section and cooling section are divided into a plurality of warm areas again in each section, according to the different characteristics of each warm area calcining temperature of pushed bat kiln and atmosphere distribution, at the draining low-temperature zone and the row Na of pushed bat kiln
+, K
+Transition section is provided with outlet port, and is at least two in the quantity of the venting port of each section setting, can as early as possible kiln internal corrosion gas be expelled from kiln, and significantly reduces the corrosion to the furnace chamber material of water vapour and basic metal.Between low-temperature zone and transition section, be provided with one section air curtain district, respectively be provided with a fore shaft district before and after it, the centre be provided with one section with the measure-alike cavity of draining low-temperature zone furnace chamber, respectively be provided with one at front and back fore shaft district kiln body side surface and prevent that doing of the gas flow between two districts from isolating the inlet mouth of air curtain.Venting port is distributed in the kiln body top of pushed bat kiln.The length in the one section air curtain district that is provided with between low-temperature zone and transition section is 450～550mm, the length in the fore shaft district that is provided with respectively before and after the air curtain district is 100～150mm, furnace chamber aspect ratio draining section is hanged down 70～90mm, width is than the narrow 30～50mm of draining section, be provided with in the middle of the fore shaft district the one section length with the measure-alike cavity of draining section furnace chamber is 200～300mm, and the air input of the inlet mouth that is used as the isolation air curtain that is provided with respectively at front and back fore shaft district kiln body side surface is 20～40m
3/ h.Low-temperature zone has i.e. 1～5 warm area of 5 warm areas, each warm area is respectively established a venting port, totally 5 venting ports, preceding 4 diameters of outlet are Φ 25～35mm, last diameter of outlet is Φ 45～55mm, transition section has i.e. 6～9 warm areas of 4 warm areas, and one section not heating zone is respectively arranged between 6 warm areas and 7 warm areas and 8 warm areas and 9 warm areas, respectively is provided with the venting port of Φ a 45～55mm.The venting port shape vertically is seen as chevron shaped from the kiln body, form a plurality of exhausting buckets in the kiln chamber.Venting port ejects mouthful passage and is processed by different refractory materialss from the kiln intracoelomic cavity to kiln, wherein the refractory materials of kiln intracoelomic cavity is graphite, magnesia brick or other inorganic materials; The refractory materials that kiln ejects mouthful passage is graphite, magnesia brick, stainless steel or other material; The kiln outer body is formed by metal material processing, and is connected by flange on the metal shell of kiln body, and metallic substance wherein can be stainless steel or nonferrous materials.
Waste gas of pusher plate kiln method for exhausting in the VN alloy production process of the present invention is the different characteristics according to each warm area calcining temperature of pushed bat kiln and atmosphere distribution, is that draining section, transition section are promptly arranged Na with waste gas by the low-temperature zone at pushed bat kiln
+, K
+Section and high temperature section are that the venting port of constant temperature zone is discharged, venting port is provided with several at each section, can as early as possible kiln internal corrosion gas be expelled from kiln, significantly reduce the corrosion of water vapour and basic metal to the furnace chamber material, by between low-temperature zone and transition section, forming one section air curtain district, and a furnace chamber aspect ratio draining section that respectively is provided with before and after this air curtain district is low, the fore shaft district that width is narrower than draining section, the centre be provided with one section with the measure-alike cavity of draining section furnace chamber, do the isolation air curtain by an inlet mouth that respectively is provided with at front and back fore shaft district kiln body side surface, prevent the gas flow between two districts, waste gas is continuous by venting port, expel from kiln incessantly, the venting port of low-temperature zone is in time discharged the water vapour of this section generation, and the venting port of transition section is in time discharged alkali metal vapour and compound exhaust air thereof.Venting port is to be provided with according to the different characteristics that the calcining temperature of VN alloy manufacturing technique requirent and each warm area and atmosphere distribute, each warm area of low-temperature zone is respectively established a venting port, establish 5 venting ports altogether, preceding 4 diameters of outlet are Φ 25～35mm, last diameter of outlet is Φ 45～55mm, between 6 warm areas of transition section and 7 warm areas and between 8 warm areas and 9 warm areas one section not heating zone is arranged respectively, respectively be provided with the venting port of Φ a 45～55mm.Venting port is distributed in the kiln body top of pushed bat kiln.
Compared with the prior art, the present invention has following tangible advantage:
1. compare with the method for exhausting waste gas of VN alloy discontinuous production technique, waste gas can be continuously, expel from kiln from each section quickly, reduces objectionable constituent in the atmosphere significantly to the corrosive nature of furnace chamber material.
2. compare with the discontinuous method for exhausting waste gas, technology, equipment are further simplified.
3. adopt a plurality of venting ports and rational exhaust position and size, help waste gas and in time expel from kiln, reduce objectionable constituent in the atmosphere significantly the corrosive nature of furnace chamber material.
Description of drawings
Fig. 1 is front view of the present invention (partial cutaway).
Among the figure: 1-kiln body 2-furnace chamber 3-venting port 4-heating unit box 5-thermal insulation layer 6-cover plate 7-track 8-fore shaft I-low-temperature zone II-transition section III-high temperature section IV-cooling section
Embodiment
According to the different characteristics of each warm area calcining temperature of pushed bat kiln and atmosphere distribution, with low-temperature zone (draining section), transition section (the row Na of outlet port design at pushed bat kiln
+, K
+Section) and high temperature section (constant temperature zone), and the number that venting port is provided with on each section kiln top is also different, can as early as possible kiln internal corrosion gas be expelled from kiln, and plays remarkable reduction water vapour and the basic metal corrosive nature to the furnace chamber material.By processing requirement, low-temperature zone has 400～700 ℃ of 5 warm areas (1～5 warm area, the about 7.8m of total length), calcining temperatures, complete for guaranteeing this section draining, each warm area can respectively be established a venting port, establishes 5 venting ports altogether, and preceding 4 diameters of outlet are Φ 30mm, the 5th diameter of outlet is Φ 50mm, the venting port shape vertically is seen as chevron shaped from the kiln body, formed a plurality of exhausting buckets like this in the kiln chamber, helps the discharge of water vapour.Transition section has 850～1450 ℃ of 4 warm areas (6～9 warm areas, the about 5.8m of total length), calcining temperatures, main objectionable constituent in this section atmosphere are Na, K steam and compound thereof, between 6 warm areas and 7 warm areas and 8 warm areas and 9 warm areas, one section not heating zone is arranged respectively, respectively be provided with the venting port of a Φ 50mm, the venting port shape is identical with low-temperature zone, helps Na like this
+, K
+Discharge.Simultaneously, between low-temperature zone and transition section, be provided with the air curtain district of a segment length 500mm, (80mm is hanged down in furnace chamber aspect ratio drained zone respectively to be provided with the fore shaft district of a 125mm before and after it, width is than the narrow 40mm in drained zone), the centre is provided with a segment length 250mm and the measure-alike cavity of drained zone furnace chamber, and respectively being provided with an air input at front and back fore shaft district kiln body side surface is 30m
3The inlet mouth of/h is done the isolation air curtain, prevents the gas flow between two districts.Venting port by different positions expels from kiln the obnoxious flavour of each section as early as possible, can significantly reduce water vapour and the basic metal corrosive nature to the furnace chamber material like this, shortens corrosion area, thus the work-ing life of cavity material in prolonging.
Pushed bat kiln wherein is special hermetic pushed bat kiln or tunnel furnace, and what require with " production method of VN alloy " [Chinese invention patent (application number 01139886.8, publication number CN1422800A)] is consistent.
Venting port ejects mouthful passage and is processed by different refractory materialss from the kiln intracoelomic cavity to kiln, wherein the refractory materials of kiln intracoelomic cavity is graphite, magnesia brick or other inorganic materials; The refractory materials that kiln ejects mouthful passage is graphite, magnesia brick, stainless steel or other material; The kiln outer body is formed by metal material processing, and is connected by flange on the metal shell of kiln body, and metallic substance wherein can be stainless steel or nonferrous materials.
In the production process, waste gas by venting port continuously, expel from kiln incessantly.
Be the contrast situation of the invention process effect below:
Embodiment 1:
In the fs test of before the invention process, producing as a trial, only be provided with a venting port in low-temperature zone.Pushed bat kiln operation about 15 days, interior cavity material cause stopping the kiln maintenance with regard to cave-in accident takes place.When dissected finds that there is serious corrosion phenomenon in the interior cavity material of low-temperature zone rear portion and high temperature section, and corrosion area is about 6.8m, wherein behind high temperature section dome brick heavy corrosion slump in furnace chamber and cause and be forced to stop kiln.
Embodiment 2:
In the test of the subordinate phase produced as a trial before the invention process, the exhaust gas emission method of pushed bat kiln has obtained certain improvement, in the low-temperature zone of body of heater 3 venting ports, transition sections is set 1 venting port is set.Pushed bat kiln operation about 50 days, interior cavity material generation cave-in accident and cause stopping the kiln maintenance.When dissected is found, there is certain corrosion phenomenon in the interior cavity material of low-temperature zone rear portion and high temperature section, but extent of corrosion alleviates to some extent than pilot plant test, and corrosion area shortens to 4.1m, wherein behind high temperature section dome brick heavy corrosion slump in furnace chamber and cause and be forced to stop kiln.
Embodiment 3:
Be used for the industrial production test process in the present invention, low-temperature zone is provided with 5 venting ports, and transition section is provided with two venting ports.Pushed bat kiln operation continuously stops the kiln dissection after 230 days, find only to have certain corrosion phenomenon at transition section, and extent of corrosion is lighter, and corrosion area shortens to about 2.5m.
Claims (10)
1. unit of exhausting waste gas of pusher plate kiln of producing VN alloy, this pushed bat kiln have draining low-temperature zone, row Na
+, K
+Transition section, constant temperature high temperature section and cooling section, each section is made up of a plurality of warm areas, it is characterized in that draining low-temperature zone and row Na at pushed bat kiln
+, K
+Transition section is provided with outlet port, and is at least two in the quantity of the venting port of each section setting.
2. according to the unit of exhausting waste gas of pusher plate kiln of the said production VN alloy of claim 1, it is characterized in that between draining low-temperature zone and transition section, being provided with one section air curtain district, respectively be provided with a fore shaft district before and after it, the centre be provided with one section with the measure-alike cavity of draining low-temperature zone furnace chamber, respectively be provided with one at front and back fore shaft district kiln body side surface and prevent that doing of the gas flow between two districts from isolating the inlet mouth of air curtain.
3. according to the unit of exhausting waste gas of pusher plate kiln of claim 1 or 2 said production VN alloy, it is characterized in that venting port is distributed in the kiln body top of pushed bat kiln.
4. according to the unit of exhausting waste gas of pusher plate kiln of the said production VN alloy of claim 2, the length that it is characterized in that the air curtain district that is provided with between low-temperature zone and transition section is 450～550mm, the length in the fore shaft district that is provided with respectively before and after the air curtain district is 100～150mm, furnace chamber aspect ratio draining section is hanged down 70～90mm, width is than the narrow 30～50mm of draining section, the length of the cavity that middle that be provided with and the draining section furnace chamber in fore shaft district is measure-alike is 200～300mm, and the air input that is used as the inlet mouth of isolating air curtain that is provided with respectively at front and back fore shaft district kiln body side surface is 20～40m
3/ h.
5. according to the unit of exhausting waste gas of pusher plate kiln of claim 1 or 2 said production VN alloy, it is characterized in that described low-temperature zone has i.e. 1～5 warm area of 5 warm areas, each warm area is respectively established a venting port, establish 5 venting ports altogether, preceding 4 diameters of outlet are Φ 25～35mm, and last diameter of outlet is Φ 45～55mm, and transition section has i.e. 6～9 warm areas of 4 warm areas, one section not heating zone is respectively arranged between 6 warm areas and 7 warm areas and 8 warm areas and 9 warm areas, respectively be provided with the venting port of Φ a 45～55mm.
6. according to the unit of exhausting waste gas of pusher plate kiln of claim 1 or 2 said production VN alloy, it is chevron shaped to it is characterized in that the venting port shape vertically is seen as from the kiln body, forms a plurality of exhausting buckets in furnace chamber.
7. according to the unit of exhausting waste gas of pusher plate kiln of claim 1 or 2 said production VN alloy, it is characterized in that venting port ejects mouthful passage and processed by different refractory materialss from the kiln intracoelomic cavity to kiln, wherein the refractory materials of kiln intracoelomic cavity is graphite, magnesia brick or other inorganic materials; The refractory materials that kiln ejects mouthful passage is graphite, magnesia brick, stainless steel or other material; The kiln outer body is formed by metal material processing, and is connected by flange on the metal shell of kiln body, and metallic substance wherein can be stainless steel or nonferrous materials.
8. waste gas of pusher plate kiln method for exhausting in the VN alloy production process is characterized in that the different characteristics that distributes according to each warm area calcining temperature of pushed bat kiln and atmosphere, is that draining section, transition section are promptly arranged Na with waste gas by the low-temperature zone at pushed bat kiln
+, K
+Section and high temperature section are that the venting port of constant temperature zone is discharged, venting port is provided with several at each section, by between low-temperature zone and transition section, forming one section air curtain district, and a furnace chamber aspect ratio draining section that respectively is provided with before and after this air curtain district is low, the fore shaft district that width is narrower than draining section, the centre be provided with one section with the measure-alike cavity of draining section furnace chamber, do the isolation air curtain by an inlet mouth that respectively is provided with at front and back fore shaft district kiln body side surface, prevent the gas flow between two districts, waste gas is continuous by venting port, expel from kiln incessantly, the venting port of low-temperature zone is in time discharged the water vapour of this section generation, and the venting port of transition section is in time discharged alkali metal vapour and compound exhaust air thereof.
9. waste gas of pusher plate kiln method for exhausting in the said according to Claim 8 VN alloy production process, it is characterized in that venting port is to be provided with according to the calcining temperature of VN alloy manufacturing technique requirent and each warm area and the different characteristics of atmosphere distribution, 5 warm areas of low-temperature zone are respectively established a venting port, establish 5 venting ports altogether, preceding 4 diameters of outlet are Φ 25～35mm, last diameter of outlet is Φ 45～55mm, between 6 warm areas of transition section and 7 warm areas and between 8 warm areas and 9 warm areas one section not heating zone is arranged respectively, respectively be provided with the venting port of Φ a 45～55mm.
10. according to waste gas of pusher plate kiln method for exhausting in the said VN alloy production process of claim 9, it is characterized in that venting port is distributed in the kiln body top of pushed bat kiln.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100812000A CN100431948C (en) | 2004-10-12 | 2004-10-12 | Unit of exhausting waste gas of pusher plate kiln for producing alloy of vanadium-nitrogen and method for exhausting waste gas |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100812000A CN100431948C (en) | 2004-10-12 | 2004-10-12 | Unit of exhausting waste gas of pusher plate kiln for producing alloy of vanadium-nitrogen and method for exhausting waste gas |
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| CN1760119A true CN1760119A (en) | 2006-04-19 |
| CN100431948C CN100431948C (en) | 2008-11-12 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101963446A (en) * | 2010-11-04 | 2011-02-02 | 四川展祥特种合金科技有限公司 | Vanadium and nitrogen alloy full-automatic vertical medium frequency induction heating furnace |
| CN101782320B (en) * | 2010-01-08 | 2013-08-07 | 河南省西保冶材集团有限公司 | Vanadium-nitrogen alloy vacuum furnace |
| CN103925786A (en) * | 2014-04-15 | 2014-07-16 | 刁君 | Double-pushing-plate high-temperature sintering kiln for producing vanadium-nitrogen alloy |
| CN106705656A (en) * | 2017-01-20 | 2017-05-24 | 重庆鹏越科技发展有限公司 | Calcining kiln for titanium dioxide |
| CN107421324A (en) * | 2017-07-24 | 2017-12-01 | 湖南众鑫新材料科技股份有限公司 | A kind of dou-ble-pusher kiln for producing ferrovanadium nitride |
| CN108120276A (en) * | 2017-12-18 | 2018-06-05 | 攀钢集团钒钛资源股份有限公司 | For producing the pushed bat kiln of VN alloy |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4040814A (en) * | 1975-12-23 | 1977-08-09 | Union Carbide Corporation | Method of producing a composition containing a large amount of vanadium and nitrogen |
| CN2083732U (en) * | 1990-06-14 | 1991-08-28 | 湖南省醴陵市陶瓷一厂 | Vertical flame energy-saving glaze burnign multi-hole kiln |
| US5462057A (en) * | 1994-06-06 | 1995-10-31 | Hewlett-Packard Company | Ultrasound imaging system using line splicing and parallel receive beam formation |
| CN2516927Y (en) * | 2001-12-21 | 2002-10-16 | 淄博广通化工有限责任公司 | Zirconium oxide sintering continuous pushed bat kiln |
-
2004
- 2004-10-12 CN CNB2004100812000A patent/CN100431948C/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101782320B (en) * | 2010-01-08 | 2013-08-07 | 河南省西保冶材集团有限公司 | Vanadium-nitrogen alloy vacuum furnace |
| CN101963446A (en) * | 2010-11-04 | 2011-02-02 | 四川展祥特种合金科技有限公司 | Vanadium and nitrogen alloy full-automatic vertical medium frequency induction heating furnace |
| CN101963446B (en) * | 2010-11-04 | 2012-05-23 | 四川展祥特种合金科技有限公司 | Vanadium and nitrogen alloy full-automatic vertical medium frequency induction heating furnace |
| CN103925786A (en) * | 2014-04-15 | 2014-07-16 | 刁君 | Double-pushing-plate high-temperature sintering kiln for producing vanadium-nitrogen alloy |
| CN106705656A (en) * | 2017-01-20 | 2017-05-24 | 重庆鹏越科技发展有限公司 | Calcining kiln for titanium dioxide |
| CN107421324A (en) * | 2017-07-24 | 2017-12-01 | 湖南众鑫新材料科技股份有限公司 | A kind of dou-ble-pusher kiln for producing ferrovanadium nitride |
| CN107421324B (en) * | 2017-07-24 | 2019-06-04 | 湖南众鑫新材料科技股份有限公司 | A kind of dou-ble-pusher kiln producing ferrovanadium nitride |
| CN108120276A (en) * | 2017-12-18 | 2018-06-05 | 攀钢集团钒钛资源股份有限公司 | For producing the pushed bat kiln of VN alloy |
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Effective date of registration: 20100727 Address after: Panzhihua City, Sichuan province 617067 Xiangyang Village East Co-patentee after: Pangang Group Co., Ltd. Patentee after: Pangang Group Steel Vanadium & Titanium Co., Ltd. Address before: 617067 Xiangyang Village, Panzhihua, Sichuan Patentee before: Panzhihua Iron and Steel (Group) Co., Ltd. |