CN102735051B - Melting furnace - Google Patents

Melting furnace Download PDF

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CN102735051B
CN102735051B CN201110082422.4A CN201110082422A CN102735051B CN 102735051 B CN102735051 B CN 102735051B CN 201110082422 A CN201110082422 A CN 201110082422A CN 102735051 B CN102735051 B CN 102735051B
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chamber
melting
baffle plate
furnace
heater
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CN102735051A (en
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不公告发明人
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China ENFI Engineering Corp
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China ENFI Engineering Corp
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Abstract

The present invention discloses a kind of melting furnace, comprising: body of heater, limits furnace chamber in described body of heater, and described body of heater has charge door, exhanst gas outlet and melt outlet; Baffle plate, described baffle plate is arranged on so that described furnace chamber is divided into melting chamber and expansion chamber in described furnace chamber, and the upper end of wherein said baffle plate is connected with the roof of described furnace chamber and the roof of the lower end of described baffle plate and described furnace chamber preset distance apart; And burner, described burner is arranged on the sidewall of described melting chamber.According to the melting furnace of the embodiment of the present invention, reduce energy consumption, decrease pollution, improve operating environment.

Description

Melting furnace
Technical field
The present invention relates to a kind of melting furnace, especially relating to a kind of vanadic anhydride melting furnace for melting vanadic anhydride pulvis.
Background technology
Vanadium has been widely used as a kind of non-ferrous metal tool.Vanadium extracts from containing vanadium material such as vanadium slag with the form of vanadic anhydride usually.Vanadium slag makes vanadic anhydride tablet through roasting, leaching, drying, decomposition, oxidation and fusing.
Traditionally, extract drying, decomposition in vanadium process, be oxidized and be melted in an equipment and carry out, due to dry, decompose, oxidation is different with the temperature of fusing, therefore carry out causing hear rate high in an equipment.And flue dust (mainly comprising a small amount of vanadic anhydride pulvis and the vanadic anhydride droplet) content in flue gas is many, causes the rate of recovery of vanadium low, the wasting of resources, and seriously polluted, and operating environment is poor.
Summary of the invention
The present invention is intended at least one of solve the problems of the technologies described above.For this reason, one object of the present invention is to propose a kind of melting furnace for melting vanadic anhydride pulvis, utilizes this melting furnace to melt vanadic anhydride pulvis, hear rate is low, pollutes less, good operational environment.
To achieve these goals, the melting furnace according to the embodiment of the present invention comprises: body of heater, limits furnace chamber in described body of heater, and described body of heater has charge door, exhanst gas outlet and melt outlet; Baffle plate, described baffle plate is arranged on so that described furnace chamber is divided into melting chamber and expansion chamber in described furnace chamber, and the upper end of wherein said baffle plate is connected with the roof of described furnace chamber and the roof of the lower end of described baffle plate and described furnace chamber preset distance apart; And burner, described burner is arranged on the sidewall of described melting chamber.
According to the melting furnace of the embodiment of the present invention, for vanadic anhydride pulvis is melted, thus the fusing of vanadic anhydride pulvis and the drying of extracting in vanadium process, decomposition, oxidation are separated, reduce energy consumption, decrease pollution, improve operating environment.
In addition, melting furnace according to the above embodiment of the present invention can also have following additional technical characteristic:
In one embodiment of the invention, described charge door is positioned at the top of described melting chamber, described exhanst gas outlet along the longitudinal direction of described body of heater and described charge door spaced apart, described melt outlet is positioned at one end of the close described exhanst gas outlet of described body of heater.
In one embodiment of the invention, the height of described melting chamber is greater than the height of described expansion chamber.
In one embodiment of the invention, described burner is multiple and spaced apart in the vertical direction.
In one embodiment of the invention, described baffle plate is multiple, longitudinally-spaced so that described expansion chamber is divided into multiple sub-expansion chamber along described body of heater of described multiple baffle plate.
In one embodiment of the invention, described exhanst gas outlet is positioned at apart from the roof of described melting chamber expansion chamber farthest.
In one embodiment of the invention, the roof of adjacent with described melting chamber expansion chamber is provided with auxiliary burning nozzle.
In one embodiment of the invention, the bottom surface of described furnace chamber is downward-sloping gradually along the direction from melting chamber to expansion chamber in the vertical.
In one embodiment of the invention, the bottom surface of described furnace chamber is provided with the chase extended longitudinally.
In one embodiment of the invention, described baffle plate is heat-resisting steel sheet and plate.
Additional aspect of the present invention and advantage will part provide in the following description, and part will become obvious from the following description, or be recognized by practice of the present invention.
Accompanying drawing explanation
Above-mentioned and/or additional aspect of the present invention and advantage will become obvious and easy understand from accompanying drawing below combining to the description of embodiment, wherein:
Fig. 1 is the cross-sectional schematic of melting furnace according to an embodiment of the invention; With
Fig. 2 is the sectional view along the line A-A in Fig. 1.
Detailed description of the invention
Be described below in detail embodiments of the invention, the example of described embodiment is shown in the drawings, and wherein same or similar label represents same or similar element or has element that is identical or similar functions from start to finish.Being exemplary below by the embodiment be described with reference to the drawings, only for explaining the present invention, and can not limitation of the present invention being interpreted as.
In describing the invention, it will be appreciated that, term " " center ", " longitudinal direction ", " transverse direction ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end " " interior ", orientation or the position relationship of the instruction such as " outward " are based on orientation shown in the drawings or position relationship, only the present invention for convenience of description and simplified characterization, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore limitation of the present invention can not be interpreted as.In addition, term " first ", " second " only for describing object, and can not be interpreted as instruction or hint relative importance.
In describing the invention, it should be noted that, unless otherwise prescribed and limit, term " installation ", " being connected ", " connection " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect; Can be directly be connected, also indirectly can be connected by intermediary, also can be communicated with, for the ordinary skill in the art, the concrete meaning of above-mentioned term can be understood as the case may be.
Below with reference to Fig. 1 and Fig. 2, the melting furnace 100 according to the embodiment of the present invention is described.According to the melting furnace of the embodiment of the present invention for melting vanadic anhydride, therefore, also vanadic anhydride melting furnace can be called.
Vanadic anhydride melting furnace 100 comprises body of heater 101 according to an embodiment of the invention, baffle plate 103, and burner 102.Body of heater 101 such as comprises furnace shell and the refractory material be arranged in furnace shell or heat-resisting steel sheet and plate 1014.Limit furnace chamber in body of heater 101, body of heater 101 has charge door 1011, exhanst gas outlet 1012 and melt outlet 1013.
Baffle plate 103 is arranged in described furnace chamber so that described furnace chamber is divided into melting chamber R and expansion chamber C, the upper end of baffle plate 103 is connected with the roof of described furnace chamber and the roof of the lower end of baffle plate 103 and described furnace chamber preset distance apart, in other words, the top of melting chamber R and expansion chamber C is separated by partition wall 103, and melting chamber R is communicated with the bottom of expansion chamber C.
Burner 102 is arranged on the sidewall of melting chamber R, for burner oil in melting chamber R, thus to from charge door 1011, the vanadic anhydride pulvis joined in melting chamber R heats.Burner 102 is preferably coal gas burner.
May be used for by the fusing of vanadic anhydride pulvis to prepare vanadic anhydride tablet according to the vanadic anhydride melting furnace 100 of the embodiment of the present invention, thus the fusing of vanadic anhydride and the drying in vanadium leaching process, decomposition, oxidation are separated, reduce energy consumption.And, owing to the inner chamber of melting furnace be divide into melting chamber R and expansion chamber C by baffle plate 103, being melted in melting chamber R of vanadic anhydride pulvis is carried out, vanadic anhydride after fusing enters expansion chamber C sedimentation, discharge finally by melt outlet 1013, unfused vanadic anhydride pulvis and be contained in vanadic anhydride droplet sedimentation in expansion chamber C of the fusing in flue gas, because this reducing vanadic anhydride pulvis in flue gas that exhanst gas outlet 1012 discharges and the content of vanadic anhydride droplet, improve the rate of recovery of vanadium, reduce pollution, improve operating environment.
In some embodiments of the invention, charge door 1011 is positioned at the top of melting chamber R, exhanst gas outlet 1012 is spaced apart with charge door 1011 along the longitudinal direction (left and right directions in Fig. 1) of body of heater 101, and melt outlet 1013 is arranged in one end (left end of Fig. 1) of the close exhanst gas outlet 1012 of body of heater 101.By by exhanst gas outlet 1012 and the spaced apart setting of charge door 1011, make fusing and sedimentation affect reduction each other, further reduce the content of the vanadic anhydride droplet of vanadic anhydride pulvis in flue gas and fusing.
As illustrated in fig. 1 and 2, preferably, the height of melting chamber R is greater than the height of expansion chamber C, can melt better thus.Burner 102 can be multiple and spaced apart in the vertical direction, such as, show two in fig. 1 and 2, improves the effect of fusing further.
In preferred embodiments more of the present invention, baffle plate 103 is multiple, longitudinally-spaced so that expansion chamber C is divided into multiple sub-expansion chamber along body of heater 101 of multiple baffle plate 103, as shown in Figure 1, in body of heater 101, be provided with two baffle plates 103, thus expansion chamber C be divided into two sub-expansion chamber C1, C2.Exhanst gas outlet 1012 is located at apart from the roof of melting chamber R expansion chamber C2 farthest, and is provided with auxiliary burning nozzle 104 on the roof of the sub-expansion chamber C1 adjacent with melting chamber R.By expansion chamber C is divided into multiple sub-expansion chamber, can carries out Multistage settling, further increase effect of settling, the vanadic anhydride pulvis in reduction flue gas and the content of vanadic anhydride droplet, reduce and pollute, improve operating environment.By arranging auxiliary burning nozzle 104, can the unfused vanadic anhydride pulvis entered in sub-expansion chamber C1 be melted again, improve fusing effect, reduce the amount of vanadic anhydride pulvis in flue gas.
Baffle plate 103 such as can be made up of heat-resisting steel sheet and plate, manufactures simple thus, and it is convenient to change.
As illustrated in fig. 1 and 2, in order to improve the emission effect of the vanadic anhydride of fusing, the bottom surface of furnace chamber is in the vertical along downward-sloping gradually from melting chamber R to the direction of expansion chamber C, and the chase 1014 extended longitudinally can be provided with on the bottom surface of furnace chamber, the left end of chase 1014 is connected with melt outlet 1013, facilitates the discharge of melt (vanadic anhydride of melting).
The simple operation described according to the vanadic anhydride melting furnace 100 of the embodiment of the present invention below.
In melting chamber R, coal gas is sprayed into and oxygen heats in melting chamber R by burner 1012, such as be heated to the temperature of 800-850 degree Celsius, vanadic anhydride pulvis is joined in melting chamber R from charge door 1011, by heat fused in the process that vanadic anhydride pulvis declines in melting chamber R.
The vanadic anhydride of fusing flows to melt outlet 1013 along the bottom surface of furnace chamber and discharges, and melt outlet 1013 can be connected with pelleter and carry out film-making, thus obtains vanadic anhydride tablet.
Flue gas and unfused vanadic anhydride pulvis and the vanadic anhydride droplet being contained in the fusing in flue gas enter in sub-expansion chamber C1 from melting chamber R by the gap below the baffle plate of the rightmost side, in sub-expansion chamber C1, coal gas and oxygen is sprayed by auxiliary burning nozzle 104, thus auxiliary heating fusing is carried out to unfused vanadic anhydride pulvis, the vanadic anhydride melt again melted flows to melt outlet 1013 and discharges.
A small amount of vanadic anhydride pulvis of flue gas and remnants and the vanadic anhydride droplet be contained in flue gas enter sub-expansion chamber C2 from sub-expansion chamber C1 by the gap below next baffle plate 103 and carry out sedimentation again, and then flue gas is discharged from exhanst gas outlet 1012.
Therefore, reduced the smoke content the flue gas of discharging from exhanst gas outlet 1012 by repeatedly sedimentation and auxiliary fusing, reduce pollution, improve operating environment.Such as, and only carry out the heat fused of vanadic anhydride pulvis in the vanadic anhydride melting furnace of the embodiment of the present invention, temperature can control, in the scope of 800-850 degree Celsius, to reduce energy consumption.
In the description of this description, specific features, structure, material or feature that the description of reference term " embodiment ", " some embodiments ", " example ", " concrete example " or " some examples " etc. means to describe in conjunction with this embodiment or example are contained at least one embodiment of the present invention or example.In this manual, identical embodiment or example are not necessarily referred to the schematic representation of above-mentioned term.And the specific features of description, structure, material or feature can combine in an appropriate manner in any one or more embodiment or example.
Although illustrate and describe embodiments of the invention, those having ordinary skill in the art will appreciate that: can carry out multiple change, amendment, replacement and modification to these embodiments when not departing from principle of the present invention and aim, scope of the present invention is by claim and equivalents thereof.

Claims (8)

1. a melting furnace, is characterized in that, comprising:
Body of heater, limits furnace chamber in described body of heater, and the bottom surface of described furnace chamber is downward-sloping gradually along the direction from melting chamber to expansion chamber in the vertical, and described body of heater has charge door, exhanst gas outlet and melt outlet;
Baffle plate, described baffle plate is arranged in described furnace chamber so that described furnace chamber is divided into melting chamber and expansion chamber, the upper end of wherein said baffle plate is connected with the roof of described furnace chamber and the roof of the lower end of described baffle plate and described furnace chamber preset distance apart, and the height of described melting chamber is greater than the height of described expansion chamber; With
Burner, described burner is arranged on the sidewall of described melting chamber.
2. melting furnace according to claim 1, it is characterized in that, described charge door is positioned at the top of described melting chamber, described exhanst gas outlet along the longitudinal direction of described body of heater and described charge door spaced apart, described melt outlet is positioned at one end of the close described exhanst gas outlet of described body of heater.
3. melting furnace according to claim 1, is characterized in that, described burner is multiple and spaced apart in the vertical direction.
4. melting furnace according to claim 1, is characterized in that, described baffle plate is multiple, longitudinally-spaced so that described expansion chamber is divided into multiple sub-expansion chamber along described body of heater of described multiple baffle plate.
5. melting furnace according to claim 4, is characterized in that, described exhanst gas outlet is positioned at apart from the roof of described melting chamber expansion chamber farthest.
6. melting furnace according to claim 5, is characterized in that, the roof of the sub-expansion chamber adjacent with described melting chamber is provided with auxiliary burning nozzle.
7. melting furnace according to claim 1, is characterized in that, the bottom surface of described furnace chamber is provided with the chase extended longitudinally.
8. the melting furnace according to any one of claim 1-7, is characterized in that, described baffle plate is heat-resisting steel sheet and plate.
CN201110082422.4A 2011-04-01 2011-04-01 Melting furnace Active CN102735051B (en)

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CN201110082422.4A CN102735051B (en) 2011-04-01 2011-04-01 Melting furnace

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CN102735051B true CN102735051B (en) 2016-01-20

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109970101B (en) * 2019-03-28 2021-11-09 朱树伟 Vanadium sheet melting method and vanadium sheet manufacturing method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4247087A (en) * 1976-08-25 1981-01-27 Klockner-Humboldt-Deutz Ag Furnace installation for the pyrometallurgical treatment of fine-grained ore concentrates
JPS63157820A (en) * 1986-12-19 1988-06-30 Tokyo Kinzoku Kk Melting furnace
CN1058808A (en) * 1991-08-16 1992-02-19 白银有色金属公司 The double chamber furnace for matte melting compartment smelting type
CN101413052A (en) * 2007-10-17 2009-04-22 姜玉德 Energy-saving environment-protective pretreatment apparatus for smelting scrap steel
CN201241179Y (en) * 2008-07-18 2009-05-20 徐生富 Sedimentation facilities for recovering cupper from smelting waste gases
CN202119246U (en) * 2011-04-01 2012-01-18 中国恩菲工程技术有限公司 Melting furnace

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4247087A (en) * 1976-08-25 1981-01-27 Klockner-Humboldt-Deutz Ag Furnace installation for the pyrometallurgical treatment of fine-grained ore concentrates
JPS63157820A (en) * 1986-12-19 1988-06-30 Tokyo Kinzoku Kk Melting furnace
CN1058808A (en) * 1991-08-16 1992-02-19 白银有色金属公司 The double chamber furnace for matte melting compartment smelting type
CN101413052A (en) * 2007-10-17 2009-04-22 姜玉德 Energy-saving environment-protective pretreatment apparatus for smelting scrap steel
CN201241179Y (en) * 2008-07-18 2009-05-20 徐生富 Sedimentation facilities for recovering cupper from smelting waste gases
CN202119246U (en) * 2011-04-01 2012-01-18 中国恩菲工程技术有限公司 Melting furnace

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