CN212640575U - Intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore - Google Patents

Abstract

The utility model discloses a tantalum-niobium alloy ore shaftless spiral continuous feeding intelligent control device, which comprises a decomposer, a size mixing tank, a first motor, a second motor, a weight metering device, a third motor, a first pressure stabilizing barrel and a second pressure stabilizing barrel, wherein a discharging pipe is fixed at the bottom of the decomposer; a first stirring shaft is fixed at the output end of the third motor; a plurality of first stirring blades are fixed on the first stirring shaft; the output end of the first motor is connected with a second stirring shaft; the second stirring shaft extends into the size mixing tank; and a plurality of second stirring blades are fixed on the second stirring shaft. The beneficial effects of the utility model are that not only solved continuous feeding, balanced reaction, safety in production's problem, can also greatly improve mechanical efficiency, reduce the manpower, practice thrift the cost, software system is through simple programming, and the jointing equipment is through simple machine-building alright completion, and it is convenient to make.

Description

Intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore

Technical Field

The utility model relates to a tantalum niobium alloy mineral aggregate continuous feed, equilibrium reaction, intelligent control technical field in tantalum niobium hydrometallurgy specifically are tantalum niobium alloy ore shaftless spiral continuous feed intelligent control device.

Background

Tantalum niobium is a key element of high-tech industry, and is increasingly favored by countries around the world, and tantalum and niobium are listed as strategic minerals in the united states, the european union and japan. One of the raw materials of the tantalum-niobium product is tantalum-niobium ore which belongs to a scarce and non-renewable resource, and with the increase of the exploitation amount, the tantalum-niobium ore is in increasingly short supply and has higher price. The tantalum-niobium alloy ore as another raw material of the tantalum-niobium product is abundant in resources, but the tantalum-niobium alloy ore is complex in impurity components and contains more metal simple substances and silicon simple substances, such as Nb, Ta, Fe, W, Si, Al, Mg, Ca, Mn, Sn, Ti and the like, in the acid leaching decomposition section of the tantalum-niobium hydrometallurgy process, the rate of hydrogen generation of the tantalum-niobium alloy ore is difficult to control, the explosion risk is very high, and many tantalum-niobium hydrometallurgy manufacturers basically abandon the use of the tantalum-niobium alloy ore. At present, in the acid leaching decomposition process of the tantalum-niobium alloy ore hydrometallurgy process, a small amount of ore feeding mode, a plurality of times of ore feeding mode and a discontinuous ore feeding mode are adopted to avoid the explosion of hydrogen generated by the excessive ore feeding of the alloy ore. Therefore, a device is urgently needed to be designed, the problems of continuous ore feeding, balanced reaction, controllable and safe production of hydrogen generation rate and the like in the acid leaching decomposition process of the tantalum-niobium alloy ore wet smelting process are solved, the mechanical efficiency can be greatly improved, the labor is reduced, the cost is saved, and automatic intelligent control is realized.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a no axle spiral continuous feed intelligent control device of tantalum niobium alloy ore deposit to solve the problem that provides among the above-mentioned background art.

In order to achieve the above object, the utility model provides a following technical scheme: the intelligent control device for the shaftless spiral continuous feeding of the tantalum-niobium alloy ore comprises a decomposition tank, a size mixing tank, a first motor, a second motor, a weight metering device, a third motor, a first pressure stabilizing barrel and a second pressure stabilizing barrel, wherein a discharge pipe is fixed at the bottom of the decomposition tank; a first stirring shaft is fixed at the output end of the third motor; a plurality of first stirring blades are fixed on the first stirring shaft; the output end of the first motor is connected with a second stirring shaft; the second stirring shaft extends into the size mixing tank; a plurality of second stirring blades are fixed on the second stirring shaft; a first arch breaking spray head and a second arch breaking spray head are arranged at the bottom inside the size mixing tank; the first arch breaking sprayer and the second arch breaking sprayer are respectively connected with the pulse type arch breaking device through pipelines; the outlet end of the size mixing tank is connected with a shaftless screw feeder; the output end of the second motor is connected with a shaftless screw feeder; the other end of the shaftless screw feeder extends into the hopper; a weight metering device is arranged on the shaftless screw feeder; a discharging pipe of the shaftless spiral feeder is provided with a first switch valve; a first material conveying pipe is fixed on the hopper; a second switch valve is arranged on the first material conveying pipe; the first conveying pipe extends to the interior of the decomposition tank; the first pressure stabilizing barrel is connected with a sulfuric acid pipe; a third material conveying pipe is fixed on the first pressure stabilizing barrel; the other end of the third conveying pipeline extends to the first meter; the first metering device is connected with a second conveying pipeline; the other end of the second conveying pipe extends to the decomposition tank; a hydrofluoric acid pipe is connected to the second pressure stabilizing barrel; a fourth material conveying pipe is connected to the second pressure stabilizing barrel; the fourth conveying pipeline extends to the inside of the second meter; a fifth conveying pipeline is connected to the second metering device; the fifth conveying pipe extends to the interior of the decomposition tank; a third switch valve is arranged on the fifth conveying pipeline; a second pneumatic control valve is arranged on the fourth conveying pipeline; a fourth switching valve is arranged on the second conveying pipeline; a fifth switching valve is arranged on the third material conveying pipe; a fixing plate is fixed at the upper end inside the decomposition tank; a water outlet structure and an exhaust pipe are arranged on the decomposition tank; the water outlet structure and the exhaust pipe both extend into the decomposing tank.

Preferably, the fixing plate is provided with a first through hole for the first material conveying pipe to pass through; a second through hole for a second conveying pipeline to pass through is formed in the fixing plate; a third through hole for a fifth conveying pipeline to pass through is formed in the fixing plate; a fourth through hole for the water outlet structure to pass through is formed in the fixing plate; and a fifth through hole for the exhaust pipe to pass through is formed in the fixing plate.

Preferably, the weight measuring device, the hopper, the first weighing device and the second weighing device are made of transparent materials.

Preferably, the output end of the first motor is connected with a second stirring shaft through a first connecting flange.

Preferably, the output end of the third motor is connected with a first stirring shaft through a second connecting flange.

Preferably, the shaftless screw feeder is provided with a limiting hole for connecting the outlet end of the size mixing groove.

Preferably, the water outlet structure comprises a hollow rotating shaft installed on a fixed plate through a sealing bearing, the lower end of the hollow rotating shaft extends to the upper inner portion of the decomposition tank and is fixedly provided with a water spraying head, the upper end of the hollow rotating shaft extends to the upper outer portion of the fixed plate and is connected with a sealing bearing flange connected with an external pipeline, the fixed plate is fixedly provided with an electric motor at a constant speed, the output end of the electric motor at the constant speed is coaxially fixed with a first transmission wheel, the hollow rotating shaft is fixedly provided with a second transmission wheel, and the first transmission wheel is in transmission connection with the second transmission wheel through a transmission belt.

Compared with the prior art, the beneficial effects of the utility model are that:

1. the utility model discloses a tantalum niobium alloy mineral shaftless spiral is fed in succession, balanced reaction and intelligent control device collect and add the ore deposit system, add sour system, reaction system, exhaust system, emergency system, control system in an organic whole, has not only solved in the tantalum niobium alloy mineral wet process smelting acid leaching process in-process feeding in succession, balanced reaction, the problem that produces the controllable safety in production of hydrogen speed, can also greatly improve mechanical efficiency simultaneously, reduces the manpower, practices thrift the cost.

2. The utility model discloses a tantalum niobium alloy mineral continuous feed, balanced reaction and intelligent control device simple structure, software system through simple programming, the jointing equipment through simple mechanical manufacturing alright completion, it is convenient to make.

3. The utility model discloses a tantalum niobium alloy mineral shaftless spiral continuous feed, equilibrium reaction and intelligent control device make tantalum niobium hydrometallurgy technology acid leaching decomposition section, and the rate that tantalum niobium alloy ore deposit generated hydrogen is controllable, realizes tantalum niobium wet process and uses tantalum niobium alloy ore as raw materials safety production tantalum niobium in a large number.

4. The utility model discloses a tantalum niobium alloy mineral shaftless spiral is fed in succession, balanced reaction and intelligent control device is with water and tantalum niobium alloy ore according to the liquid-solid ratio 1:4-1:10 compounding, and the material is thrown according to liquid-solid ratio 1:1-1:2 to the water and tantalum niobium alloy ore in the difference of prior art, has reduced the use amount of water, has reduced the acid consumption, has reduced manufacturing cost, can increase the productivity simultaneously, shortens production cycle.

Drawings

FIG. 1 is a schematic structural view of a shaftless spiral continuous feeding intelligent control device for tantalum-niobium alloy ore of the present invention;

FIG. 2 is an enlarged schematic view of the structure at A in FIG. 1;

FIG. 3 is the schematic diagram of the structure of the slurry mixing tank of the intelligent control device for the shaftless spiral continuous feeding of tantalum-niobium alloy ore.

In the figure: 1-a decomposition tank; 2-a first stirring shaft; 3-a first stirring blade; 4-a size mixing tank; 5-a first motor; 6-a second stirring shaft; 7-a second stirring blade; 8-a first arch-breaking spray head; 9-a second arch-breaking spray head; 10-a second motor; 11-shaftless screw feeder; 12-a weight measuring device; 13-a hopper; 14-a first delivery conduit; 15-a third motor; 16-a second delivery pipe; 17-a first meter; 18-a third delivery conduit; 19-a fifth on-off valve; 20-sulfuric acid tube; 21-a first surge tank; 22-hydrofluoric acid tube; 23-a second surge tank; 24-a second pneumatic control valve; 25-fourth delivery pipe; 26-a second meter; 27-a fifth delivery conduit; 28-fixing plate; 29-a first on-off valve; 30-a second on-off valve; 31-a third on/off valve; 32-a fourth switching valve; 33-a discharge pipe; 35-an exhaust pipe; 36-a pulse arch breaker; 38-a water outlet structure; 381-hollow shaft; 382-a sealed bearing; 383-a sprinkler head; 384-sealing the bearing flange; 385-constant speed electric motor; 386-a first drive wheel; 387-a second drive wheel; 388-drive belt.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

In the description of the present invention, it is to be understood that the terms "longitudinal", "lateral", "oblique", "center", "longitudinal", "lateral", "length", "width", "thickness", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", and the like indicate the orientation or positional relationship indicated based on the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore should not be construed as limiting the present invention. The terms "first", "second", "third", "fourth", "fifth" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implying any indication of the number of technical features indicated. Furthermore, features defined as "first," "second," "third," "fourth," and "fifth" may explicitly or implicitly include one or more of the features. In the description of the present invention, "a plurality" means one, two or more unless otherwise specified.

In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.

Referring to fig. 1 to 3, the present invention provides a shaft-free spiral continuous feeding intelligent control device for tantalum-niobium alloy ore, which comprises: the device comprises a decomposition tank 1, a size mixing tank 4, a first motor 5, a second motor 10, a weight metering device 12, a third motor 15, a first pressure stabilizing barrel 21 and a second pressure stabilizing barrel 23, wherein a discharge pipe 33 is fixed at the bottom of the decomposition tank 1; a first stirring shaft 2 is fixed at the output end of the third motor 15; a plurality of first stirring blades 3 are fixed on the first stirring shaft 2; the output end of the first motor 5 is connected with a second stirring shaft 6; the second stirring shaft 6 extends into the size mixing tank 4; a plurality of second stirring blades 7 are fixed on the second stirring shaft 6; a first arch breaking spray head 8 and a second arch breaking spray head 9 are arranged at the bottom inside the size mixing tank 4; the first arch breaking sprayer 8 and the second arch breaking sprayer 9 are respectively connected with a pulse type arch breaking device 36 through pipelines; the outlet end of the size mixing tank 4 is connected with a shaftless screw feeder 11; the output end of the second motor 10 is connected with a shaftless screw feeder 11; the other end of the shaftless screw feeder 11 extends into the hopper 13; the shaftless screw feeder 11 is provided with a weight metering device 12; a first switch valve 29 is arranged on a discharge pipe of the shaftless screw feeder 11; a first material conveying pipe 14 is fixed on the hopper 13; a second switch valve 30 is arranged on the first material conveying pipe 14; the first conveying pipe 14 extends to the interior of the decomposition tank 1; the first pressure stabilizing barrel 21 is connected with a sulfuric acid pipe 20; a third material conveying pipe 18 is fixed on the first pressure stabilizing barrel 21; the other end of the third conveying pipeline 18 extends to the first metering device 17; the first metering device 17 is connected with a second conveying pipeline 16; the other end of the second conveying pipeline 16 extends to the decomposition tank 1; a hydrofluoric acid pipe 22 is connected to the second pressure stabilizing barrel 23; the second pressure stabilizing barrel 23 is connected with a fourth material conveying pipe 25; said fourth feeding duct 25 extends inside a second counter 26; a fifth material conveying pipe 27 is connected to the second metering device 26; the fifth material conveying pipe 27 extends into the decomposition tank 1; a third on-off valve 31 is arranged on the fifth material conveying pipe 27; a second pneumatic control valve 24 is arranged on the fourth material conveying pipe 25; a fourth switch valve 32 is arranged on the second material conveying pipe 16; a fifth switch valve 19 is arranged on the third material conveying pipe 18; a fixing plate 28 is fixed at the upper end inside the decomposition tank 1; a water outlet structure 38 and an exhaust pipe 35 are arranged on the decomposition tank 1; the water outlet structure 38 and the exhaust pipe 35 both extend into the decomposition tank 1.

In this embodiment, the fixing plate 28 is provided with a first through hole for the first material conveying pipe 14 to pass through; a second through hole for the second conveying pipeline 16 to pass through is formed in the fixing plate 28; a third through hole for the fifth conveying pipeline 27 to pass through is formed in the fixing plate 28; a fourth through hole for the water outlet structure 38 to pass through is formed in the fixing plate 28; a fifth through hole for the exhaust pipe 35 to pass through is formed in the fixing plate 28.

In this embodiment, the weight measuring device 12, the hopper 13, the first weighing unit 17, and the second weighing unit 26 are made of transparent materials.

In this embodiment, the output end of the first motor 5 is connected to a second stirring shaft 6 through a first connecting flange.

In this embodiment, the output end of the third motor 15 is connected to the first stirring shaft 2 through a second connecting flange.

In this embodiment, the shaftless screw feeder 11 is provided with a limiting hole for connecting the outlet end of the size mixing tank 4.

In this embodiment, go out water structure 38 and include and install the cavity pivot 381 on fixed plate 28 through sealed bearing 382, the lower extreme of cavity pivot 381 extend to the interior upper portion of decomposer 1 just is fixed with sprinkler bead 383, the upper end of cavity pivot 381 extends to the outside top of fixed plate 28 just is connected with the sealed bearing flange 384 of being connected with outside tube coupling, be fixed with at the uniform velocity electric motor 385 on the fixed plate 28, the coaxial first drive wheel 386 that is fixed with of output of electric motor 385 at the uniform velocity, be fixed with the second drive wheel 387 on the cavity pivot 381, first drive wheel 386 through drive belt 388 with the transmission of second drive wheel 387 is connected.

The utility model discloses a tantalum-niobium alloy mineral shaftless spiral continuous feeding, balanced reaction and intelligent control device, including adding ore deposit system, adding six parts of sour system, reaction system, exhaust system, emergency system, control system. The ore feeding system comprises a size mixing tank 4, a shaftless screw feeder 11, a weight metering device 12, a hopper 13 and a first conveying pipeline 14, and controls materials to be continuously and uniformly fed into the decomposition tank 1 according to a set speed. The acid adding system comprises a sulfuric acid adding system and a hydrofluoric acid adding system, and the sulfuric acid adding system comprises a sulfuric acid pipe 20, a first pressure stabilizing barrel 21, a third conveying pipe 18, a first metering device 17 and a second conveying pipe 16; the hydrofluoric acid adding system comprises a hydrofluoric acid pipe 22, a second pressure stabilizing barrel 23, a fourth delivery pipe 25, a second metering device 26 and a fifth delivery pipe 27, and the sulfuric acid and the hydrofluoric acid are continuously and uniformly added into the decomposition tank 1 at a set speed by the acid adding system. The reaction system comprises a decomposition tank 1, and the tantalum-niobium alloy mineral material, the sulfuric acid and the hydrofluoric acid react in the decomposition tank 1. The exhaust system comprises an exhaust pipe 35, the exhaust pipe 35 is connected with the tail gas treatment system, and waste gas generated in the decomposition tank 1 is timely and quickly extracted. Emergency system includes water structure 38, and when hydrogen volume exceeded the critical value in the decomposer 1, computer automatic control exhaust system increased the amount of air extracted, starts emergency system simultaneously, and emergency system lasts 360 rotations through water structure 38 rapidly and sprays a large amount of running water to the decomposer 1 in, and the running water is sprinkled to the decomposer 1 in with even mode. The control system takes the hydrogen content in the decomposition tank 1 as a dependent variable, realizes computer control through software programming, and is connected with the ore adding system, the acid adding system, the reaction system, the air draft system and the emergency system. The specific working process is as follows: the top of the size mixing tank 4 is opened, water and the tantalum-niobium alloy ore are added into the size mixing tank 4 according to the liquid-solid ratio of 1:4-1:10, and the first motor 5 is started to finish material mixing. The method is different from the prior art that the water and the tantalum-niobium alloy ore are mixed according to the liquid-solid ratio of 1:4-1:10, so that the method reduces the use amount of water, reduces the acid consumption, reduces the production cost, can increase the productivity and shortens the production period. The materials are mixed according to the liquid-solid ratio of 1:4-1:10, the materials are dense, the specific gravity is high, the materials are easy to agglomerate and settle, the stirring is difficult, and the bridging phenomenon is easy to occur in the blanking process, in order to control smooth blanking, a first arch breaking nozzle 8 and a second arch breaking nozzle 9 are arranged in the size mixing tank 4, the first arch breaking nozzle 8 and the second arch breaking nozzle 9 vibrate simultaneously to destroy the bridging phenomenon, so that the materials are fed smoothly through a shaftless screw feeder 11. The weight metering device 12 can accurately reflect the weight of the fed materials, the hopper 13 has a weighing function, the weight of the fed materials is weighed again, and the continuous and balanced feeding of the materials is guaranteed. The weight metering device 12 and the hopper 13 are made of transparent materials, so that the feeding condition is visualized. The first pressure stabilizing barrel 21 and the second pressure stabilizing barrel 23 respectively and independently maintain the same liquid level, so that the blanking speeds of sulfuric acid and hydrofluoric acid are consistent. And confirming that the second motor 10, the first switch valve 29, the second switch valve 30, the second pneumatic valve 24, the third switch valve 31, the fourth switch valve 32, the fifth switch valve 19 and the third motor 15 are started, wherein the switch valves adopt electromagnetic control valves, and tantalum-niobium alloy mineral, sulfuric acid and hydrofluoric acid are added into the decomposition tank 1 at the same time, and the acid leaching decomposition reaction of the tantalum-niobium alloy mineral hydrometallurgy process is started. The hydrogen content in the decomposing tank 1 is taken as a primary control factor, a hydrogen gas detector is arranged in the decomposing tank 1 and serves as a hydrogen detection point, when the hydrogen reaches a set maximum value (the volume fraction is 3.8%), the mineral feeding system and the acid feeding system are automatically controlled by a computer to reduce the feeding speed of minerals and acid, and corresponding metering pumps are arranged for controlling, the metering pumps are connected with a motor and used for respectively feeding sulfuric acid and hydrofluoric acid into the first pressure stabilizing barrel 21 and the second pressure stabilizing barrel 23, a PLC controller controls the related metering pumps, and the PLC controller is in signal connection with terminals such as a computer and the like for controlling, so that the hydrogen in the decomposing tank 1 is reduced to a reasonable range (the volume fraction is less than 3.8%); when the hydrogen content in the decomposition tank 1 is too low (the volume fraction is less than 1%), the computer automatically controls the ore adding system and the acid adding system to increase the feeding speed of the minerals and the acid, and the mineral decomposition efficiency is improved. When hydrogen volume exceedes the critical value in the decomposer 1, computer automatic control exhaust system increases the amount of wind of taking out, start emergency system simultaneously, emergency system sprays a large amount of running water in to decomposer 1 rapidly, the running water is sprinkled to in the decomposer 1 with even mode, the purpose is that remove a large amount of foams of production, avoid emerging the groove, can reduce the concentration of acid in the decomposer 1 and the temperature of reaction material simultaneously, and then reduce mineral decomposition speed, reduce hydrogen concentration in the decomposer 1, when hydrogen reduces to reasonable scope in the decomposer 1 (volume fraction is less than 3.8%), emergency system automatic stop sprays the running water to in the decomposer 1, exhaust system resumes initial value simultaneously.

The working principle is as follows: a slurry mixing tank 4, a first motor 5, a second stirring shaft 6, a second stirring blade 7, a first arch breaking spray head 8, a second arch breaking spray head 9, a pulse arch breaking device 36, a second motor 10, a shaftless screw feeder 11, a weight metering device 12, a first switch valve 29, a first conveying pipe 14 and a hopper 13 of the device form an ore adding system of the device, a second conveying pipe 16, a first metering device 17, a third conveying pipe 18, a fifth switch valve 19, an acid sulfate pipe 20, a first pressure stabilizing barrel 21, an acid hydrofluoric acid pipe 22, a second pressure stabilizing barrel 23, a second pneumatic control valve 24, a fourth conveying pipe 25, a second metering device 26 and a fifth conveying pipe 27 of the device form an acid adding system of the device, a third motor 15, a first stirring shaft 2 and a first stirring blade 3 of the device are reaction systems of the device, and a water outlet structure 38 and a water pump are combined to form an emergency system of the device, the exhaust system of the device comprises an exhaust pipe 35, the exhaust pipe 35 is connected with a tail gas treatment system, waste gas generated in a decomposition tank 1 is quickly exhausted in time, an emergency system of the device comprises a water outlet structure 38, a control system of the device comprises a computer automatic control and a PLC (programmable logic controller), the device comprises an ore adding system, an acid adding system, a reaction system, an exhaust system, an emergency system and a control system, the ore adding system, the acid adding system, the exhaust system and the emergency system are all connected with the reaction system, the control system controls all the links, the ore adding system comprises a slurry adjusting tank 4, a first arch breaking spray head 8, a second arch breaking spray head 9, a pulse type arch breaking device 36, a second motor 10, a shaftless spiral feeder 11, a weight metering device 12, a first feed conveying pipe 14 and a hopper 13 to realize continuous balanced feeding of minerals, the acid adding system to realize continuous balanced feeding, the reaction system realizes continuous equilibrium reaction, the ore feeding system, the acid feeding system and the reaction system can realize continuous equilibrium stable production, the hydrogen rate generated after the reaction is controllable, the safe production is realized, meanwhile, under the action of the control system, the hydrogen content generated in the decomposing tank is taken as the dependent variable, the intelligent linkage control is realized, and in addition, the air draft system and the emergency system are arranged, the safety coefficient is further improved. The method specifically comprises the following steps: the hydrogen content in the decomposing tank 1 is taken as a primary control factor, and when the hydrogen in the decomposing tank 1 reaches a set maximum value, the feeding speed of minerals and acid is reduced by automatically controlling the mineral feeding system and the acid feeding system by a computer, so that the hydrogen in the decomposing tank 1 is reduced to a reasonable range; when the hydrogen content in the decomposition tank 1 is too low, the computer automatically controls the ore adding system and the acid adding system to increase the feeding speed of minerals and acid, and the mineral decomposition efficiency is improved. When the hydrogen amount in the decomposing tank 1 exceeds the critical value, the computer automatically controls the air draft system to increase the air draft amount, and simultaneously, the emergency system is started. Emergency system sprays a large amount of running water rapidly in to the reaction tank, and the running water is sprinkled to the decomposer 1 in with 360 degrees of even mode, and the purpose removes a large amount of foams that produce, avoids overflowing the groove, can reduce the concentration of sour in the reaction tank simultaneously, and then reduces mineral decomposition speed, reduces inslot hydrogen concentration. When the hydrogen in the decomposing tank 1 is reduced to a reasonable range, the emergency system automatically stops spraying tap water into the tank, and meanwhile, the air draft system recovers the initial set value.

The technical effects are as follows: the utility model discloses a tantalum-niobium alloy mineral shaftless spiral is feeding in succession, balanced reaction and intelligent control device collect and add the ore deposit system, add sour system, reaction system, exhaust system, emergency system, control system in an organic whole, has not only solved the problem of feeding in succession, balanced reaction, safety in production, can also greatly improve mechanical efficiency, reduces the manpower, practices thrift the cost. The continuous feeding, balanced reaction and intelligent control device has a simple structure, a software system is simply programmed, the connection equipment can be completed through simple mechanical manufacturing, and the manufacturing is convenient.

It will be apparent to those skilled in the art that various changes and modifications may be made without departing from the spirit and scope of the invention. Thus, if such modifications and variations of the present invention fall within the scope of the claims and their equivalents, the present invention is also intended to include such modifications and variations.

Claims (7)

1. Tantalum niobium alloy ore deposit shaftless spiral continuous feed intelligent control device which characterized in that: the device comprises a decomposition tank (1), a size mixing tank (4), a first motor (5), a second motor (10), a weight metering device (12), a third motor (15), a first pressure stabilizing barrel (21) and a second pressure stabilizing barrel (23), wherein a discharge pipe (33) is fixed at the bottom of the decomposition tank (1); a first stirring shaft (2) is fixed at the output end of the third motor (15); a plurality of first stirring blades (3) are fixed on the first stirring shaft (2); the output end of the first motor (5) is connected with a second stirring shaft (6); the second stirring shaft (6) extends into the size mixing tank (4); a plurality of second stirring blades (7) are fixed on the second stirring shaft (6); a first arch breaking spray head (8) and a second arch breaking spray head (9) are arranged at the bottom inside the size mixing tank (4); the first arch breaking sprayer (8) and the second arch breaking sprayer (9) are respectively connected with a pulse type arch breaking device (36) through pipelines; the outlet end of the size mixing tank (4) is connected with a shaftless screw feeder (11); the output end of the second motor (10) is connected with a shaftless screw feeder (11); the other end of the shaftless screw feeder (11) extends into the hopper (13); a weight metering device (12) is arranged on the shaftless screw feeder (11); a first switch valve (29) is arranged on a discharge pipe of the shaftless screw feeder (11); a first material conveying pipe (14) is fixed on the hopper (13); a second switch valve (30) is arranged on the first material conveying pipe (14); the first conveying pipe (14) extends to the interior of the decomposition tank (1); the first pressure stabilizing barrel (21) is connected with a sulfuric acid pipe (20); a third material conveying pipe (18) is fixed on the first pressure stabilizing barrel (21); the other end of the third conveying pipeline (18) extends to the first metering device (17); a second material conveying pipe (16) is connected to the first metering device (17); the other end of the second conveying pipe (16) extends to the decomposition tank (1); a hydrofluoric acid pipe (22) is connected to the second pressure stabilizing barrel (23); a fourth material conveying pipe (25) is connected to the second pressure stabilizing barrel (23); the fourth conveying pipe (25) extends to the interior of the second metering device (26); a fifth material conveying pipe (27) is connected to the second metering device (26); the fifth conveying pipe (27) extends to the interior of the decomposition tank (1); a third on-off valve (31) is arranged on the fifth conveying pipe (27); a second pneumatic control valve (24) is arranged on the fourth material conveying pipe (25); a fourth switching valve (32) is arranged on the second material conveying pipe (16); a fifth switch valve (19) is arranged on the third material conveying pipe (18); a fixing plate (28) is fixed at the upper end inside the decomposition tank (1); a water outlet structure (38) and an exhaust pipe (35) are arranged on the decomposition tank (1); the water outlet structure (38) and the exhaust pipe (35) both extend into the decomposition tank (1).

2. The intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore according to claim 1, wherein: a first through hole for the first material conveying pipe (14) to pass through is formed in the fixing plate (28); a second through hole for the second conveying pipeline (16) to pass through is formed in the fixing plate (28); a third through hole for a fifth conveying pipeline (27) to pass through is formed in the fixing plate (28); a fourth through hole for the water outlet structure (38) to pass through is formed in the fixing plate (28); and a fifth through hole for the exhaust pipe (35) to pass through is formed in the fixing plate (28).

3. The intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore according to claim 1, wherein: the weight metering device (12), the hopper (13), the first metering device (17) and the second metering device (26) are made of transparent materials.

4. The intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore according to claim 1, wherein: the output end of the first motor (5) is connected with a second stirring shaft (6) through a first connecting flange.

5. The intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore according to claim 1, wherein: the output end of the third motor (15) is connected with a first stirring shaft (2) through a second connecting flange.

6. The intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore according to claim 1, wherein: and a limiting hole for connecting the outlet end of the size mixing groove (4) is formed in the shaftless spiral feeder (11).

7. The intelligent control device for shaftless spiral continuous feeding of tantalum-niobium alloy ore according to claim 1, wherein: go out water structure (38) and include and install cavity pivot (381) on fixed plate (28) through sealed bearing (382), the lower extreme of cavity pivot (381) extends to the interior upper portion of decomposer (1) and be fixed with sprinkler bead (383), the upper end of cavity pivot (381) extends to the outside top of fixed plate (28) and be connected with sealed bearing flange (384) of being connected with outside pipe connection, be fixed with at the uniform velocity electric motor (385) on fixed plate (28), the coaxial first drive wheel (386) that is fixed with of output of at the uniform velocity electric motor (385), be fixed with second drive wheel (387) on cavity pivot (381), first drive wheel (386) through driving belt (388) with second drive wheel (387) transmission is connected.

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