CN112604629A - Preparation system of lime emulsion agent for mineral separation - Google Patents
Preparation system of lime emulsion agent for mineral separation Download PDFInfo
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- CN112604629A CN112604629A CN202011472374.5A CN202011472374A CN112604629A CN 112604629 A CN112604629 A CN 112604629A CN 202011472374 A CN202011472374 A CN 202011472374A CN 112604629 A CN112604629 A CN 112604629A
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- 235000008733 Citrus aurantifolia Nutrition 0.000 title claims abstract description 33
- 235000011941 Tilia x europaea Nutrition 0.000 title claims abstract description 33
- 239000004571 lime Substances 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 29
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims abstract description 16
- 239000011707 mineral Substances 0.000 title claims abstract description 16
- 238000000926 separation method Methods 0.000 title claims abstract description 13
- 239000000839 emulsion Substances 0.000 title description 4
- 239000003795 chemical substances by application Substances 0.000 title description 3
- 230000029087 digestion Effects 0.000 claims abstract description 36
- 239000003814 drug Substances 0.000 claims abstract description 24
- 239000008267 milk Substances 0.000 claims abstract description 21
- 210000004080 milk Anatomy 0.000 claims abstract description 21
- 235000013336 milk Nutrition 0.000 claims abstract description 21
- 238000007599 discharging Methods 0.000 claims abstract description 15
- 238000007865 diluting Methods 0.000 claims abstract description 8
- 238000003756 stirring Methods 0.000 claims description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000006073 displacement reaction Methods 0.000 claims description 6
- 239000006071 cream Substances 0.000 claims description 4
- 230000006378 damage Effects 0.000 abstract description 5
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 12
- 239000000292 calcium oxide Substances 0.000 description 12
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 12
- 235000010755 mineral Nutrition 0.000 description 10
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 239000000920 calcium hydroxide Substances 0.000 description 5
- 235000011116 calcium hydroxide Nutrition 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 238000004806 packaging method and process Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 208000014674 injury Diseases 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000003113 dilution method Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910001608 iron mineral Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 206010035653 pneumoconiosis Diseases 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 238000006748 scratching Methods 0.000 description 1
- 230000002393 scratching effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/002—Avoiding undesirable reactions or side-effects, e.g. avoiding explosions, or improving the yield by suppressing side-reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/20—Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
- B01J4/007—Feed or outlet devices as such, e.g. feeding tubes provided with moving parts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/008—Feed or outlet control devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/02—Feed or outlet devices; Feed or outlet control devices for feeding measured, i.e. prescribed quantities of reagents
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F11/00—Compounds of calcium, strontium, or barium
- C01F11/02—Oxides or hydroxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
- B01J2204/002—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Inorganic Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention relates to a preparation system of a lime milk medicament for mineral separation, which comprises a feeding system and a bag breaking system, wherein the feeding system consists of a crane and a large-inclination-angle feeding belt conveyor, the bag breaking system comprises a support frame body, a bag breaking machine case, a closed box body, a cylindrical sieve, a spiral conveyor feeding hopper and a bag collecting box, and the preparation system is characterized by further comprising a conveying, discharging and metering system, a digestion system and a dissolving and diluting system which are sequentially connected with the feeding system. According to the lime milk medicament preparation system for mineral separation, which is disclosed by the invention, except for the fact that a crane needs manual operation, all other operations such as motor driving, valve opening and closing and pressure metering of a pressure metering scale are interlocked with a control box, so that the system is automatically operated, has high automation degree, greatly reduces the number of post workers and reduces the damage to the post workers.
Description
Technical Field
The invention belongs to the technical field of preparation of reagents in a dressing plant, and particularly relates to a preparation system of a lime milk reagent for mineral dressing.
Background
Lime milk is commonly used as a medicament in ore dressing plants, for example, reverse flotation of iron ore commonly uses lime milk as an activator of iron minerals; often, lime milk is added to the transported pulp during long distance pipeline transportation of the concentrate or tailings to form a calcium carbonate scale layer on the inner wall of the pipeline to protect the pipeline from pulp abrasion. At present, most of lime milk selected in factories is prepared by conveying bagged calcium oxide to a medicament preparation workshop through an automobile for stockpiling, manually conveying the bagged calcium oxide to a lime milk preparation stirring tank, scratching a packaging bag by a knife, discharging the calcium oxide into the stirring tank, stirring and mixing the calcium oxide with water to prepare lime milk (calcium hydroxide aqueous solution). The mode can generate a large amount of calcium oxide dust in various procedures of calcium oxide stacking, carrying, bag breaking and unloading, so that the environment pollution is caused, and the strongly alkaline calcium oxide and hydrate thereof not only can cause serious pneumoconiosis, but also can cause strong alkali damage to the respiratory system of people. According to the preparation method, the calcium oxide is directly added into the stirring tank, and the temperature of a workshop is often too high and the dust pollution in the workshop is serious due to the fact that the calcium oxide releases heat when meeting water in a large amount. In addition, part of lime particles are usually agglomerated after being digested on the surface of water, so that the lime is not completely digested and subsequent feeding facilities are blocked. Finally, most of the modes depend on manual operation, metering is inaccurate, the concentration of the lime emulsion is difficult to control accurately, and manual operation has high labor cost. In addition, the bag breaking is carried out by the bag breaking machine, and the feeding mode of feeding is carried out by the chain plate type conveyor, so that dust during bag breaking is avoided, but the conveying efficiency of the chain plate type conveyor is low, the lower part of a chain plate is easy to be blocked, and the failure rate of the chain plate type structure is high. Therefore, a preparation system of lime milk medicament for mineral separation, which has the advantages of simple process, high automation degree, no need of manual operation, good preparation effect of lime milk, stable system, low failure rate and no environmental pollution and personal injury, is needed to be developed.
Disclosure of Invention
The invention aims to provide a preparation system of lime milk medicament for mineral separation, which has simple process, high automation degree, no need of manual operation, good preparation effect of lime milk and no environmental pollution and personal injury.
The preparation system of the lime milk medicament for mineral separation is realized by the following technical scheme:
the invention relates to a preparation system of a lime milk medicament for mineral separation, which comprises a feeding system and a bag breaking system, wherein the feeding system consists of a crane and a large-inclination-angle feeding belt conveyor;
the conveying, discharging and metering system consists of a spiral conveyor, a spiral conveyor driving motor, a discharge hopper, a pressure metering scale and a discharge valve, wherein the feeding end of the spiral conveyor is inserted into the closed box and is arranged at the lower part of the feeding hopper of the spiral conveyor, the discharging end of the spiral conveyor is positioned at the upper part of the digestion system, the discharge hopper is welded below the discharging end of the spiral conveyor, and the discharge valve and the pressure metering scale are arranged below the discharge hopper;
the digestion system consists of a digestion tank, a horizontal spiral stirrer and a stirring motor I, wherein the horizontal spiral stirrer and the stirring motor I are arranged in the digestion tank;
the dissolving and diluting system comprises two stirring tanks, stirrers and a stirring motor II, wherein the stirrers are respectively arranged on the two stirring tanks, the stirring motor II is connected with the stirrers, a feed inlet and a water inlet are respectively arranged at the upper part of each stirring tank, a lime cream medicament discharge port is arranged at the lower part of each stirring tank, the feed inlets of the two stirring tanks are respectively connected with two discharge ports of the digestion tank through a stirring tank feed pipe, and an electric switch valve I is arranged on the stirring tank feed pipe; the discharge outlets of the two stirring tanks are respectively connected with a finished product feeding device through a conveying pipeline and a displacement pump, and an electric switch valve II is arranged on the conveying pipeline.
Further, the driving motor of the spiral conveyor is a variable frequency motor.
And further, the electric switch valve I, the electric switch valve II, the variable frequency motor, the stirring motor I, the stirring motor II and the pressure metering scale are connected with the control box.
The invention has the advantages that:
(1) according to the system, except for the manual operation of the crane, all other operations such as motor driving, valve opening and closing and metering signals of the pressure metering scale are automatic operations interlocked with the control box, so that the degree of automation is high, the number of post workers is greatly reduced, and the damage to the post workers is reduced;
(2) according to the system, the driving motor of the screw conveyor is a variable frequency motor, so that the feeding speed can be effectively controlled;
(3) according to the system, the discharge hopper is arranged below the conveying device, the batch discharge mode of the discharge hopper is adopted, the weight of the discharge hopper measured by the pressure measuring scale is combined, the lime amount fed into the digestion tank can be accurately controlled, and the lime amount is accurately measured. Then controlling the water supply amount of the digestion and dissolution dilution system to realize the controllability of the concentration of the calcium hydroxide finished product;
(4) the digestion system discharges hot water vapor generated by digestion to the outside of a preparation workshop through the exhaust pipe arranged at the upper part of the digestion system, so that the corrosion of alkaline water vapor to each metal part is avoided, the equipment is protected, and the continuous rise of the temperature in the workshop is avoided;
(5) the digestion system of the invention realizes the full mixing of calcium oxide and water to form calcium hydroxide by the horizontal spiral stirrer arranged in the lower part of the digester, and the stirring and reaction mode effectively solves the agglomeration phenomenon of partial calcium oxide without stirring and optimizes the digestion effect;
(6) according to the preparation system of the lime emulsion agent for mineral separation, calcium hydroxide adopts a two-stage preparation process of digesting and diluting firstly, and compared with a traditional one-stage preparation process of adding water to react and diluting directly by using a stirring tank, the process has the advantages that the reaction heat release process and the dilution process are separated independently, so that the blockage caused by calcium oxide agglomeration is avoided, the concentrated heat release during digestion is facilitated, and the quality of a calcium hydroxide solution is optimized;
(7) the system is prepared by replacing two stirring grooved wheels, one stirring grooved wheel is used for storing prepared finished medicament when the other stirring grooved wheel is used for preparing the finished medicament after receiving the discharge of the digestion tank, so that the continuous addition of the finished medicament is realized;
(8) according to the system, the feeding pump adopts the displacement pump, so that the characteristic that the displacement pump can automatically remove calcium carbonate scale generated by the reaction of the calcium hydroxide solution in the pump cavity is fully utilized, the displacement pump is protected, and the stability of the whole system is guaranteed.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a view from a-a of fig. 1.
Fig. 3 is an enlarged view of a portion B of fig. 1.
Detailed Description
The following further describes the embodiments of the present invention with reference to the drawings.
As shown in fig. 1-3, the preparation system of lime milk chemical for mineral separation of the present invention comprises a feeding system and a bag breaking system 4, wherein the feeding system is composed of a crane 3 and a large-inclination feeding belt conveyor 2, the bag breaking system comprises a support frame 41, a bag breaking machine case 43, a closed box 42, a cylindrical screen 47, a screw conveyor feeding hopper 410 and a bag collecting box 49, and is characterized by further comprising a conveying, discharging and metering system, a digestion system and a dissolving and diluting system which are sequentially connected with the feeding system;
the conveying, discharging and metering system consists of a screw conveyor 5, a screw conveyor driving motor, a discharge hopper 6, a pressure metering scale 7 and a discharge valve 8, wherein the feeding end of the screw conveyor 5 is inserted into a closed box 42 and is arranged at the lower part of the screw conveyor feeding hopper 410, the discharging end of the screw conveyor 5 is positioned at the upper part of the digestion system, the discharge hopper 6 is welded below the discharging end of the screw conveyor, the discharge valve 8 and the pressure metering scale 7 are arranged below the discharge hopper 6, and the screw conveyor driving motor is a variable frequency motor;
the digestion system consists of a digestion tank 9, a horizontal spiral stirrer 12 arranged in the digestion tank 9 and a stirring motor I13, wherein the upper part of the digestion tank 9 is provided with a digestion tank feeding port 10 and an exhaust port 11, the lower part of the digestion tank 9 is provided with two discharge ports 14, the digestion tank feeding port 10 is connected with a discharge valve 8 of the conveying system, and the exhaust port 11 is communicated with the outside of the preparation workshop through an exhaust pipe; the digestion system discharges hot water vapor generated by digestion to the outside of the preparation workshop through the exhaust pipe arranged at the upper part of the digestion system, so that the corrosion of alkaline water vapor to each metal part is avoided, the equipment is protected, and the continuous rise of the temperature in the workshop is avoided.
The dissolving and diluting system comprises two stirring tanks 20, stirrers 21 respectively arranged on the two stirring tanks 20 and a stirring motor II 18 connected with the stirrers 21, wherein the upper part of each stirring tank 20 is respectively provided with a feed inlet 17 and a water inlet 19, the lower part of each stirring tank 20 is provided with a lime cream medicament discharge port 22, the feed inlets 17 of the two stirring tanks 20 are respectively connected with two discharge ports 14 of the digestion tank 9 through a stirring tank feed pipe 16, and the stirring tank feed pipe 16 is provided with an electric switch valve I15; the discharge outlets of the two stirring tanks are respectively connected with a finished product feeding device through a conveying pipeline 25 and a displacement pump 23, and an electric switch valve II 24 is arranged on the conveying pipeline 25.
The angle of the large-inclination-angle feeding belt conveyor 2 of the preparation system of the lime milk medicament for mineral separation is 60-70 degrees.
In the above preparation system of lime milk medicament for mineral separation, the bag breaking machine a and the bag breaking machine B are vertically arranged on the bag breaking machine case 43, and include the driving motor 46, the rotating shaft 44 connected to the output shaft of the driving motor, and the bag breaking knife switch 45 arranged on the rotating shaft 44; the bag breaking knife switches 45 are arranged along the respective rotating shafts 44 at intervals, and the bag breaking knife switches 45 of the bag breaking machines A and B rotate oppositely. The arrangement of the bag breaking system reduces the labor intensity of workers, dust can not be raised in the whole bag breaking and feeding process, and the health of workers is favorably ensured.
A spiral driving mechanism 48 is arranged in the cylindrical screen 47, and the packaging bags are discharged from the discharge bag opening along with the forward conveying of the spiral driving mechanism 48 arranged in the cylindrical screen 47.
Electric switch valve I15, electric switch valve II 24, inverter motor, agitator motor I13, agitator motor II 18 and pressure measurement balance with all be connected with the control box. And automatic control is realized. The control box is prior art and will not be described herein.
The working process of the invention is as follows:
the bagged powdery medicament 1 is transferred and conveyed into the discharge end of the large-inclination-angle feeding belt conveyor 2 through the crane 3, and then is fed into the bag breaking system from the discharge end of the large-inclination-angle feeding belt conveyor 2; under the action of bag breaking knife switches 45 which rotate oppositely of a bag breaking machine A and a bag breaking machine B which are arranged up and down, the bagged powdery medicament 1 enters a cylindrical sieve 47 together with a broken packaging bag through a chute, the powdery medicament enters a feeding hopper 410 of a spiral conveyor from the cylindrical sieve 47 through sieve holes, the packaging bag is conveyed to a bag discharging opening of the cylindrical sieve 47 along with the rotation of a spiral driving mechanism 48, and is discharged into a bag collecting box 49 from the bag discharging end;
the powdery medicament discharged from the discharge end of the feeding hopper 410 of the screw conveyor enters a digestion tank through a discharge hopper, a discharge valve and a pressure metering scale which are arranged on the screw conveyor, is stirred by a horizontal screw stirrer in the digestion tank to obtain sufficient mixture, then enters two stirring tanks through two discharge ports 14 and a stirring tank feeding pipe 16 respectively, is diluted into calcium hydroxide solution with the concentration of 5-10 percent by adding water in the stirring tanks, namely the finished lime milk medicament, and is fed into a feeding device through a conveying pipeline and a volumetric pump 23.
Claims (3)
1. A preparation system of lime milk medicament for mineral separation comprises a feeding system and a bag breaking system, wherein the feeding system consists of a crane and a large-inclination-angle feeding belt conveyor, the bag breaking system comprises a supporting frame body, a bag breaking machine case, a closed box body, a cylindrical screen, a spiral conveyor feeding hopper and a bag collecting box, and the preparation system is characterized by further comprising a conveying, discharging and metering system, a digestion system and a dissolving and diluting system which are sequentially connected with the feeding system;
the conveying, discharging and metering system consists of a spiral conveyor, a spiral conveyor driving motor, a discharge hopper, a pressure metering scale and a discharge valve, wherein the feeding end of the spiral conveyor is inserted into the closed box and is arranged at the lower part of the feeding hopper of the spiral conveyor, the discharging end of the spiral conveyor is positioned at the upper part of the digestion system, the discharge hopper is welded below the discharging end of the spiral conveyor, and the discharge valve and the pressure metering scale are arranged below the discharge hopper;
the digestion system consists of a digestion tank, a horizontal spiral stirrer and a stirring motor I, wherein the horizontal spiral stirrer and the stirring motor I are arranged in the digestion tank;
the dissolving and diluting system comprises two stirring tanks, stirrers and a stirring motor II, wherein the stirrers are respectively arranged on the two stirring tanks, the stirring motor II is connected with the stirrers, a feed inlet and a water inlet are respectively arranged at the upper part of each stirring tank, a lime cream medicament discharge port is arranged at the lower part of each stirring tank, the feed inlets of the two stirring tanks are respectively connected with two discharge ports of the digestion tank through a stirring tank feed pipe, and an electric switch valve I is arranged on the stirring tank feed pipe; the discharge outlets of the two stirring tanks are respectively connected with a finished product feeding device through a conveying pipeline and a displacement pump, and an electric switch valve II is arranged on the conveying pipeline.
2. The lime cream medicament preparation system for mineral processing according to claim 1, wherein the screw conveyor driving motor is a variable frequency motor.
3. The preparation system of lime milk medicament for mineral processing according to any one of claims 1 to 2, wherein the electric switch valve I, the electric switch valve II, the variable frequency motor, the stirring motor I, the stirring motor II and the pressure metering scale are all connected with the control box.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011472374.5A CN112604629A (en) | 2020-12-15 | 2020-12-15 | Preparation system of lime emulsion agent for mineral separation |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011472374.5A CN112604629A (en) | 2020-12-15 | 2020-12-15 | Preparation system of lime emulsion agent for mineral separation |
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| CN112604629A true CN112604629A (en) | 2021-04-06 |
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| CN202011472374.5A Withdrawn CN112604629A (en) | 2020-12-15 | 2020-12-15 | Preparation system of lime emulsion agent for mineral separation |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113213600A (en) * | 2021-05-25 | 2021-08-06 | 北京精瑞科迈净水技术有限公司 | Automatic magnetic powder feeding device and automatic magnetic powder feeding process for magnetic coagulation |
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2020
- 2020-12-15 CN CN202011472374.5A patent/CN112604629A/en not_active Withdrawn
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113213600A (en) * | 2021-05-25 | 2021-08-06 | 北京精瑞科迈净水技术有限公司 | Automatic magnetic powder feeding device and automatic magnetic powder feeding process for magnetic coagulation |
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Application publication date: 20210406 |