CN115709046A - Carbonizer for producing nano calcium, magnesium and strontium wires - Google Patents
Carbonizer for producing nano calcium, magnesium and strontium wires Download PDFInfo
- Publication number
- CN115709046A CN115709046A CN202211436268.0A CN202211436268A CN115709046A CN 115709046 A CN115709046 A CN 115709046A CN 202211436268 A CN202211436268 A CN 202211436268A CN 115709046 A CN115709046 A CN 115709046A
- Authority
- CN
- China
- Prior art keywords
- shell
- strontium
- magnesium
- liquid level
- carbonizer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 229910052791 calcium Inorganic materials 0.000 title claims abstract description 25
- 239000011575 calcium Substances 0.000 title claims abstract description 25
- 229910052749 magnesium Inorganic materials 0.000 title claims abstract description 25
- 239000011777 magnesium Substances 0.000 title claims abstract description 25
- 229910052712 strontium Inorganic materials 0.000 title claims abstract description 25
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 title claims abstract description 25
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 63
- 239000000376 reactant Substances 0.000 claims abstract description 53
- 238000003756 stirring Methods 0.000 claims abstract description 45
- 238000006243 chemical reaction Methods 0.000 claims abstract description 36
- 238000009413 insulation Methods 0.000 claims abstract 2
- 238000003763 carbonization Methods 0.000 claims description 27
- 239000013078 crystal Substances 0.000 claims description 22
- 230000005540 biological transmission Effects 0.000 claims description 20
- 239000003795 chemical substances by application Substances 0.000 claims description 17
- 239000000411 inducer Substances 0.000 claims description 17
- 239000012530 fluid Substances 0.000 claims description 14
- 239000003638 chemical reducing agent Substances 0.000 claims description 10
- 238000009434 installation Methods 0.000 claims description 9
- 238000007789 sealing Methods 0.000 claims description 9
- 239000000945 filler Substances 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 24
- 239000007787 solid Substances 0.000 abstract description 11
- 239000007795 chemical reaction product Substances 0.000 abstract description 3
- 239000002131 composite material Substances 0.000 abstract 1
- 239000000047 product Substances 0.000 description 14
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 230000009471 action Effects 0.000 description 5
- 230000008878 coupling Effects 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention relates to the technical field of carbonizers, in particular to a carbonizer for producing nano calcium, magnesium and strontium wires, which comprises the following components: the frequency conversion motor, the shell, the stirring shaft, the guide vane wheel and the guide plate, wherein the guide vane wheel is a P-T type guide vane wheel and comprises a plurality of guide vanes which are uniformly arranged at intervals in the circumferential direction, the cross section of each guide vane is in a shape of a ladder P with a T inside, a flat guide plate is fixed on the inner wall of the shell, the bottom of the reaction kettle is of a plane guide structure, the outer wall of the shell is provided with a spiral heat exchange device, a composite heat insulation layer is arranged outside the heat exchange device, the reaction product needs to be heated or cooled, the shell is provided with a liquid level and flow measuring device, so that solid, liquid and gas reactants flow in one state all the time, blades in the P-T type guide vane wheel enable objects close to the wall of the tower to move clockwise, the position close to the shaft inside has upward pressure, and further the downward vortex force is relieved, and the reaction process realizes intelligent automatic control.
Description
Technical Field
The invention relates to the technical field of carbonization towers, in particular to a carbonization tower for producing nano calcium, magnesium and strontium wires.
Background
The basic principle of the production technology of the nanometer calcium, magnesium and strontium wire carbonization tower is that the power generated by a rotor impeller is utilized, the centrifugal force with the center of a rotating shaft as a starting point is utilized to generate strong liquid, solid and gas mixture high-speed rotating fluid, meanwhile, the generated vortex force is counteracted by the inner lifting force of the impeller under the action of special blades, the two forces are transmitted to the rotating speed of a motor by a liquid level flow sensor to control, so that the vortex force approaches zero, a generated object always moves towards one direction, and only the situation that the generated object can grow is strengthened, thereby realizing the chemical reaction process of crystals under the conditions of crystal nucleus, an inducer, a control agent and external high-energy acting force; the mode of acquiring the downstream super energy is mainly to assist the crystal to grow to be slender through the high kinetic energy clockwise rotating force generated by the blades, and meanwhile, the high kinetic energy rotating fluid destroys the growth of the crystal in other directions under the action of the crystal form control agent and the inducer in the high kinetic energy downstream mode, so that the crystal grows into a filamentous object.
The carbonization reaction mode in the prior carbonization tower technology has the problems that because of no downstream flowing force condition, no guide plate flow guiding mode, high-kinetic energy rotational flow fluid cannot be generated, no high-temperature heat exchanger and no automatic control system, the reaction quality and the reaction speed cannot be improved, the reaction process cannot be intelligentized, reactants cannot react rapidly and the products cannot be controlled as required, the production efficiency of the carbonization tower is reduced, the shape of the reaction products cannot be controlled, the product quality is unstable, and the like.
Disclosure of Invention
Aiming at the technical defects, the invention provides a carbonization tower for producing nano calcium, magnesium and strontium wires, which solves the problems of low production efficiency, poor product quality, uncontrollable reaction conditions, long reaction time, uncontrollable reaction endpoint and high production cost caused by the fact that the conventional carbonization tower cannot generate high-kinetic energy rotational flow fluid.
In order to achieve the purpose, the invention provides the following technical scheme:
a carbonizer for producing nano-calcium, magnesium and strontium wires comprises a variable frequency motor, a speed reducer, a coupler, a frame, a transmission shaft, a sealing filler, a mounting support, a stirring impeller and an annular guide plate, wherein the upper end of a shell is provided with a crystal form control agent inlet and an inducer inlet; one end of the stirring shaft penetrates through the shell to be connected with a transmission shaft of the driving device, and is sequentially connected with a plurality of layers of stirring impellers, the stirring impellers are all fixed on the stirring shaft, and the stirring impellers are sequentially arranged at the central position of the annular guide plate from top to bottom; the stirring impeller is a P-T type stirring impeller and comprises a plurality of stirring blades which are circumferentially and uniformly arranged at intervals, and the cross section of each guide blade is parallel to the shaft and is in a trapezoidal plate shape; the front end of the cross section is P-shaped, and the rear end is T-shaped; a plane guide plate is fixed on the inner wall of the shell, the bottom of the carbonization tower is of a plane structure, so that fluid circulates clockwise, and a product outlet communicated with the interior of the carbonization tower is formed at the bottom of the carbonization tower; the shell is externally provided with a heat exchanger and a heat preservation layer, and is also respectively provided with a liquid level meter bottom inlet, a liquid level meter top inlet, a temperature meter interface, an acid liquor meter interface, a conductivity meter interface and a liquid level flowing direction sensor.
The technical scheme of the invention is further improved as follows: the shell is also provided with a heat exchange tube, a heat exchanger inlet tube and a heat exchanger outlet, the heat exchange tube is of a spiral structure and is fixed on the outer wall of the shell in a clearance-supporting manner, and the heat exchanger inlet and the heat exchanger outlet are respectively communicated with the upper end and the lower end of the heat exchange tube.
The technical scheme of the invention is further improved as follows: the variable frequency motor is connected with the speed reducer, the speed reducer is connected with the transmission shaft through a coupler, the variable frequency motor is fixed on the installation base through the rack, the installation base is fixed at the top end of the shell, and a filler sealing layer is arranged at the contact position of the transmission shaft and the installation base.
The technical scheme of the invention is further improved as follows: and a dynamic seal bearing is arranged at the joint of the shell and the transmission shaft.
The technical scheme of the invention is further improved as follows: the transmission shaft is connected with the stirring shaft through a coupler.
The technical scheme of the invention is further improved as follows: and a quantitative liquid level automatic control valve, a mass flow density instrument and a control valve are arranged on the crystal form control agent inlet and the inducer inlet to control the liquid reactant amount.
The technical scheme of the invention is further improved as follows: the top of the shell is provided with a manhole and a manhole cover, the upper side wall and the lower side wall of the shell are both provided with a liquid level meter bottom inlet and a liquid level meter top inlet, and the side wall of the shell is also provided with an acidity meter interface and a temperature meter interface.
The technical scheme of the invention is further improved as follows: the liquid level meter of the liquid level meter interface can automatically control the liquid level of the reactant, the quantity of the reactant is controlled by the control valve of the mass flow density meter, the temperature meter on the temperature meter interface and the regulating valve on the heat exchanger control the temperature in the reaction process, signals are preset on the acidity meter interface and the conductivity meter interface, the reaction terminal point is controlled, and the two-position cut-off valve on the product outlet pipe is opened, so that the product enters the next procedure.
The technical scheme of the invention is further improved as follows: the eddy force generated by the impeller on the stirring impeller is obtained by the liquid level flow direction sensor to control the rotating speed of the variable frequency motor, so that the inner side of the impeller on the stirring impeller is lifted upwards.
The technical scheme of the invention is further improved as follows: the gas reactant enters the pipeline through the gas reactant port, and the gas reactant is ejected through the jet port of the gas reactant annular ejector.
Compared with the prior art, the carbonization tower for producing the nano calcium, magnesium and strontium wires has the following beneficial effects:
1. the invention provides a carbonization tower for producing nano calcium, magnesium and strontium wires, wherein fluid in a reaction kettle is high-kinetic energy solid, gas and liquid film fragments, and meanwhile, the solid, gas and liquid are dispersed and crushed by a guide impeller to form extremely large and constantly updated gas, solid and liquid substance surfaces, so that constantly updated reaction surfaces are formed, the extremely thin gas, solid and liquid substances and the surfaces are updated, high-kinetic energy rotary flow is formed, so that reaction generated substances are instantly finished in an inducer, a crystal form control agent and a high-speed non-vortex process, and the reaction efficiency is accelerated.
2. The invention provides a carbonization tower for producing nano calcium, magnesium and strontium wires.A driving device of a reaction kettle drives a guide vane wheel to centrifugally rotate at different speeds, and simultaneously, the upward supporting force generated by the inner side of the blade counteracts the generation of vortex force, so that a clockwise or anticlockwise fluid is formed by a solid object under the combined action of a guide plate in the tower, and a resultant generates a filamentous substance under the action of a crystal form control agent and an inducer; to achieve the desired material properties.
3. The invention provides a carbonizer for producing nano calcium, magnesium and strontium wires, a driving device of a reaction kettle realizes the clockwise rotating force of a guide vane wheel, under the action of the thrust of the front P end and the upward thrust of the rear T end of the high-speed guide vane wheel, a reactant generates high-energy clockwise transmission force, meanwhile, the front end of the guide vane wheel widely generates clockwise thrust, the rear end generates upward lifting force, the downward vortex force generated by centrifugal force is reduced, and a solid-liquid-gas mixture generates a circulating high-energy fluid environment parallel to the bottom of a tower, so that the solid-liquid-gas phase high-speed reaction is realized under the conditions of high temperature, a metal salt crystal type control agent, an inducer and rotational kinetic energy, and the rate of a reaction product is controllable; the crystal nucleus and the crystal develop according to the required direction, so that the reaction among substances in the whole carbonization is rapid, the problems of low dissolution rate and slow reaction are avoided, the solid, liquid and gas in the reaction kettle can react at high speed, the reaction rate is improved, the reaction time is reduced, the production efficiency is improved, and the production cost is reduced.
4. The invention provides a carbonization tower for producing nano calcium, magnesium and strontium wires, wherein gas, liquid and solid reactants in a reaction kettle are in a diversion type rotational flow circulation mode in the tower, so that the initial speed of liquid flow is increased by the solid, liquid and gas reactants, high-kinetic-energy fluid is easier to form when the reactants are in contact with multiphase substances, the rapid reaction of the liquid, the solid and the gas in the tower is accelerated, and the reaction efficiency is improved.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts.
FIG. 1 is a schematic structural diagram of a carbonizer for producing nano-calcium, magnesium and strontium wires according to the present invention.
FIG. 2 is a schematic diagram of the annular ejector for gaseous reactants in FIG. 1.
FIG. 3 is a schematic diagram of the annular ejector for gaseous reactants in FIG. 2.
Fig. 4 is a schematic structural view of the stirring impeller in fig. 1.
The mark in the figure is: 1-a variable frequency motor; 2-a speed reducer; 3, coupling; 4-a frame; 5-a transmission shaft; 6-sealing the filler layer; 7, mounting a support; 8-a crystalline form control agent inlet; 9-a manhole; 10-inducer inlet; 11-a mixed liquid reactant inlet; 12-a housing; 13-gaseous reactant annular ejector; 14-a coupling; 15-stirring shaft; 16-a stirring impeller; 17-ring-shaped baffle; 18-heat exchanger outlet pipe; 19-heat exchanger inlet pipe; 20-stirring shaft bearing seat; 21-a liquid level meter bottom inlet; 211-level gauge top inlet; 22-acid liquor instrument interface; 23-a thermometer interface; 24-conductivity meter interface; 25-product outlet tube; 26-an insulating layer; 28-a heat exchanger; 29-liquid level flow direction sensor; 30-cleaning a blockage of the annular gas reactant ejector; 31-a gaseous reactant inlet; 32-gas reactant ring ejector jet orifice.
Detailed Description
The technical solution of the present invention will be clearly and completely described by the following detailed description. It is to be understood that the described embodiments are merely exemplary of the invention, and not restrictive of the full scope of the invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
As shown in FIG. 1-4, the invention provides a carbonization tower for producing nano calcium, magnesium and strontium wires, which comprises a variable frequency motor 1, a speed reducer 2, a shaft coupling 3, a rack 4, a transmission shaft 5, a sealing filler 6, a mounting support 7, a stirring impeller 16 and a ring-shaped guide plate 17, wherein the upper end of a shell 12 is provided with a crystal form control agent inlet 8 and an inducer inlet 10; one end of the stirring shaft 15 penetrates through the shell 12 to be connected with the driving device transmission shaft 5, a plurality of layers of stirring impellers are sequentially connected, the stirring impellers 16 are all fixed on the stirring shaft 15, and the stirring impellers 16 are sequentially arranged at the center of the annular guide plate 17 from top to bottom; the stirring impeller 16 is a P-T type stirring impeller and comprises a plurality of stirring blades which are circumferentially and uniformly arranged at intervals, and the cross section of each guide blade is parallel to the shaft and is in a trapezoidal plate shape; the front end of the cross section is P-shaped, and the rear end is T-shaped; a plane guide plate is fixed on the inner wall of the shell 12, the bottom of the carbonization tower is of a plane structure, so that fluid circulates clockwise, and a product outlet 25 communicated with the interior of the carbonization tower is arranged at the bottom of the carbonization tower; the heat exchanger 28 and the insulating layer 26 are installed outside the shell 12, and the shell 12 is also respectively provided with a liquid level meter bottom inlet 21, a liquid level meter top inlet 211, a temperature meter interface 23, an acid liquor meter interface 22, a conductivity meter interface 24 and a liquid level flow direction sensor 29. The shell 12 is further provided with a heat exchange tube 28, a heat exchanger inlet tube 19 and a heat exchanger outlet 18, the heat exchange tube 28 is of a spiral structure, the heat exchange tube is fixed on the outer wall of the shell 12 in a clearance fit manner, and the heat exchanger inlet 19 and the heat exchanger outlet 18 are respectively communicated with the upper end and the lower end of the heat exchange tube 28. The variable frequency motor 1 is connected with the speed reducer 2, the speed reducer 2 is connected with the transmission shaft 5 through the coupler 3, the variable frequency motor 1 is fixed on the installation base 7 through the rack 4, the installation base 7 is fixed on the top end of the shell 12, and the contact part of the transmission shaft 5 and the installation base 7 is provided with the filler sealing layer 6. And a dynamic seal bearing is arranged at the joint of the shell 12 and the transmission shaft 5. The transmission shaft 5 is connected with the stirring shaft 15 through a coupler 14. And a quantitative liquid level automatic control valve, a mass flow density meter and a control valve are arranged on the crystal form control agent inlet 8 and the inducer inlet 10 respectively to control the amount of liquid reactants.
The top of the shell 12 is provided with a manhole 9 and a manhole cover, the upper and lower side walls of the shell 12 are provided with a liquid level meter bottom inlet 21 and a liquid level meter top inlet 211, and the side wall of the shell 12 is also provided with an acidity meter interface 22 and a temperature meter interface 23. The liquid level of the reactant can be automatically controlled by the liquid level meter of the liquid level meter interface 21, the amount of the reactant is controlled by the control valve of the mass flow density meter, the temperature of the reaction process is controlled by the temperature meter on the temperature meter interface 23 and the regulating valve on the heat exchanger 28, signals are preset on the acidity meter interface 22 and the conductivity meter interface 24, the reaction end point is controlled, and the two-position cut-off valve on the product outlet pipe 25 is opened, so that the product enters the next process. The eddy force generated by the impeller on the stirring impeller 16 is obtained by the liquid level flow direction sensor 29 to control the rotating speed of the variable frequency motor 1, so that the inner side of the impeller on the stirring impeller 16 is lifted upwards. The gas reactant enters the pipeline through the gas reactant port 31, and the gas reactant is ejected through the jet port of the gas reactant annular ejector.
Further, the carbonization tower comprises: the device comprises a variable frequency motor 1, an outer shell 12, a stirring shaft 15, a guide vane wheel 16 and a guide vane 17, wherein the upper end of the shell 12 is provided with a reactant feeding pipe crystal form control agent inlet 8 and a reactant feeding pipe inducer inlet 10, and the positions of the reactant feeding pipe crystal form control agent inlet and the reactant feeding pipe inducer inlet are changed according to material characteristics; one end of the stirring shaft 15 penetrates through the shell 12 to be connected with a driving device, and in order to ensure the sealing performance of the shell 12 and avoid the inward leakage of impurities of the guide impeller from the shell 12, a dynamic sealing ring is arranged at the joint of the stirring shaft 15 and the shell 12; the other end is connected with a guide vane wheel 16; the guide vane wheel 16 is of a P-T shape and comprises a plurality of guide vanes which are circumferentially and uniformly arranged at intervals, the front ends of the guide vanes are of a P-type downstream type, and the rear ends of the guide vanes are of a T-type pressure flow type; the liquid can rapidly move in the clockwise or anticlockwise direction and generate upward supporting force so as to offset the vortex generation under the centrifugal force, and the gas-liquid-solid mixture in the tower forms rapidly flowing liquid parallel to the tower bottom all the time.
Parallel baffles are fixed to the inner wall of the housing 12, and the fluid reactant can rapidly form clockwise circulating fluid after passing through the baffles. The bottom of the carbonization tower is of a plane diversion structure, so that fluid cannot generate vortex flow direction and can move clockwise along the diversion plate, a product outlet pipe 25 communicated with the interior of the reaction kettle is arranged at the bottom of the reaction kettle, and products in the shell 12 can be conveniently taken out by arranging the product outlet pipe 25.
In this embodiment, the inlet 8 of the crystal form control agent of the reactant feeding pipe and the inlet 10 of the inducer of the reactant feeding pipe are both provided with a quantitative liquid level automatic control valve and a mass flow density meter control valve for controlling the amount of the liquid reactant. The top of the shell 12 is provided with a manhole 9 and a manhole cover, the upper and lower side walls of the shell 12 are provided with a liquid level meter bottom inlet 21 and a liquid level meter top inlet 211, and the side wall of the shell 12 is also provided with a conductivity meter interface 24, an acid liquor meter interface 22, a temperature meter interface 23 and a liquid level flowing direction sensor 29 interface. The variable frequency motor, the conductivity meter, the acidity meter, the temperature meter and the liquid level flow sensor are all connected with the control system, so that the high-efficiency internal circulation reaction kettle completely realizes the full automatic control process.
The embodiment also provides a working principle of the carbonization tower for producing the nano calcium, magnesium and strontium wires: the No. 1 liquid reactant is fed into the tower through a crystal form control agent inlet 8 of a reactant feeding pipe I after being metered, the No. 2 liquid reactant is fed into the tower through an inducer inlet 10 of a reactant feeding pipe II after being metered, the liquid reactant is fed into the tower through a mixed liquid reactant inlet 11, and the gas reactant is fed into the tower through a gas reactant annular ejector 13 until the reaction is finished; the gas-solid-liquid mixture reactant in the carbonization tower is pushed by the stirring impeller 16 to move clockwise along the tower wall, the reactants are broken at intervals to form a large and constantly updated surface area, all the reaction mixtures flowing at high speed form a high-energy ultrathin liquid film and update the surface, chemical reaction is carried out under high-strength circulation, and the reactants with specific shapes are formed under the conditions of a crystal form control agent, an inducer and high temperature; two or more substances generate extremely high kinetic energy under high fluidity and high shearing force and the reaction is completed instantly, so that the reaction time is greatly shortened and the production cost is reduced.
Example 2
This example differs from example 1 in that: in order to make the temperature in the shell 12 constant and ensure that the reaction temperature condition of the product is met, the outer side arm of the shell 12 is provided with a heat exchanger 28, the heat exchanger 28 comprises a heat exchanger inlet pipe 19 and a heat exchanger outlet pipe 18, the heat exchange pipes in the heat exchanger 28 are in a spiral structure and are fixed on the inner wall of the shell 12, and the heat exchanger inlet pipe 19 and the heat exchanger outlet pipe 18 are respectively communicated with the upper end and the lower end of the heat exchanger 28; other structural components, connection relationships, and positional relationships of this embodiment are the same as those of embodiment 1.
The above-mentioned embodiments are merely illustrative of the preferred embodiments of the present invention, and do not limit the scope of the present invention, and various modifications and improvements of the technical solution of the present invention made by those skilled in the art without departing from the spirit of the present invention should fall within the protection scope defined by the claims of the apparatus of the present invention.
Claims (10)
1. A carbonizer for producing nanometer calcium, magnesium and strontium wires is characterized in that: the device comprises a variable frequency motor (1), a speed reducer (2), a coupler (3), a rack (4), a transmission shaft (5), a sealing filler (6), a mounting support (7), a stirring impeller (16) and an annular guide plate (17), wherein the upper end of a shell (12) is provided with a crystal form control agent inlet (8) and an inducer inlet (10); one end of the stirring shaft (15) penetrates through the shell (12) to be connected with a transmission shaft (5) of the driving device, a plurality of layers of stirring impellers are sequentially connected, the stirring impellers (16) are all fixed on the stirring shaft (15), and the stirring impellers (16) are sequentially arranged at the center of the annular guide plate (17) from top to bottom; the stirring impeller (16) is a P-T type stirring impeller and comprises a plurality of stirring blades which are circumferentially and uniformly arranged at intervals, and the cross section of each guide blade is parallel to the shaft and is in a shape of a trapezoid; the front end of the cross section is P-shaped, and the rear end is T-shaped; a plane guide plate is fixed on the inner wall of the shell (12), the bottom of the carbonization tower is of a plane structure, so that fluid circulates clockwise, and a product outlet (25) communicated with the interior of the carbonization tower is arranged at the bottom of the carbonization tower; a heat exchanger (28) and a heat insulation layer (26) are arranged outside the shell (12), and the shell (12) is also respectively provided with a liquid level meter bottom inlet (21), a liquid level meter top inlet (211), a temperature meter interface (23), an acid liquor meter interface (22), a conductivity meter interface (24) and a liquid level flowing direction sensor (29).
2. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 1, wherein: the shell (12) is also provided with a heat exchange tube (28), a heat exchanger inlet tube (19) and a heat exchanger outlet (18) outside, the heat exchange tube (28) is of a spiral structure and is fixed on the outer wall of the shell (12) in a propping manner, and the heat exchanger inlet (19) and the heat exchanger outlet (18) are respectively communicated with the upper end and the lower end of the heat exchange tube (28).
3. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 1, wherein: the variable frequency motor (1) is connected with the speed reducer (2), the speed reducer (2) is connected with the transmission shaft (5) through the coupler (3), the variable frequency motor (1) is fixed on the installation base (7) through the rack (4), the installation base (7) is fixed at the top end of the shell (12), and the contact part of the transmission shaft (5) and the installation base (7) is provided with the filler sealing layer (6).
4. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 3, wherein: a dynamic seal bearing is arranged at the joint of the shell (12) and the transmission shaft (5).
5. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 3, wherein: the transmission shaft (5) is connected with the stirring shaft (15) through a coupler (14).
6. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 1, wherein: and a quantitative liquid level automatic control valve, a mass flow density meter and a control valve are arranged on the crystal form control agent inlet (8) and the inducer inlet (10) respectively to control the amount of liquid reactants.
7. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 1, wherein: a manhole (9) and a manhole cover are arranged at the top of the shell (12), a liquid level meter bottom inlet (21) and a liquid level meter top inlet (211) are arranged on the upper side wall and the lower side wall of the shell (12), and an acidity meter interface (22) and a temperature meter interface (23) are further arranged on the side wall of the shell (12).
8. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 1, wherein: the liquid level of the reactant can be automatically controlled by a liquid level meter of the liquid level meter interface (21), the amount of the reactant is controlled by a mass flow density meter control valve, a temperature meter on the temperature meter interface (23) and a regulating valve on the heat exchanger (28) control the temperature in the reaction process, signals are preset on the acidity meter interface (22) and the conductivity meter interface (24) to control the reaction end point and open a two-position cut-off valve on a product outlet pipe (25) so that the product enters the next process.
9. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 1, wherein: the eddy force generated by the impeller on the stirring impeller (16) is obtained by a liquid level flow direction sensor (29) to control the rotating speed of the variable frequency motor (1), so that the inner side of the impeller on the stirring impeller (16) is lifted upwards.
10. The carbonizer for producing nano-calcium, magnesium and strontium wires according to claim 1, characterized in that: the gas reactant enters the pipeline through a gas reactant port (31), and the gas reactant is ejected through a jet port of the gas reactant annular jet device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211436268.0A CN115709046A (en) | 2022-11-16 | 2022-11-16 | Carbonizer for producing nano calcium, magnesium and strontium wires |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211436268.0A CN115709046A (en) | 2022-11-16 | 2022-11-16 | Carbonizer for producing nano calcium, magnesium and strontium wires |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN115709046A true CN115709046A (en) | 2023-02-24 |
Family
ID=85233475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202211436268.0A Pending CN115709046A (en) | 2022-11-16 | 2022-11-16 | Carbonizer for producing nano calcium, magnesium and strontium wires |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115709046A (en) |
-
2022
- 2022-11-16 CN CN202211436268.0A patent/CN115709046A/en active Pending
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106975433A (en) | A kind of flat dynamic respons kettle of chemical industry water | |
| CN108654534B (en) | Double-coil energy-saving efficient reaction kettle | |
| CN117101589B (en) | Chemical industry reation kettle | |
| CN115709046A (en) | Carbonizer for producing nano calcium, magnesium and strontium wires | |
| CN113877513A (en) | Hypergravity membrane reactor | |
| CN115382487A (en) | High-efficient inner loop reation kettle of intelligence | |
| CN211586169U (en) | Heating agitator tank | |
| CN210874143U (en) | Evaporator for producing high-purity low-glycerol molecular distillation monoglyceride | |
| CN110229060B (en) | Preparation method of food-grade sodium diacetate | |
| CN111790333A (en) | Vortex continuous flow type reactor | |
| CN201728108U (en) | White carbon black reactor | |
| CN106732290A (en) | A kind of reactor of continuous production nitromethane | |
| CN217888001U (en) | Novel aluminum ash reaction conveying system | |
| CN108671865B (en) | Double-coil energy-saving efficient reaction kettle adopting jacket for exhausting | |
| CN211070054U (en) | Large-volume ternary cathode material precursor reaction kettle | |
| CN110193332B (en) | Large-volume ternary anode material precursor reaction kettle | |
| CN216273138U (en) | High-purity lithium hexafluorophosphate apparatus for producing | |
| CN206566900U (en) | A kind of reactor of continuous production nitromethane | |
| CN205973808U (en) | Graphene materials apparatus for producing and system | |
| CN208694300U (en) | Horizontal crystallizer suitable for inositol crystallization | |
| CN210545090U (en) | Large-volume ternary anode material precursor reaction kettle with high heat transfer efficiency | |
| CN114247412A (en) | Chemical production uses high-efficient type reation kettle | |
| CN2841141Y (en) | Quenching continuous heat-taking chemical production apparatus | |
| CN218307465U (en) | Reducing liquid stirring device | |
| CN206325567U (en) | A kind of esterifying kettle of improved structure |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |