CN201310905Y - Complete device for mineral slurry processing - Google Patents
Complete device for mineral slurry processing Download PDFInfo
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- CN201310905Y CN201310905Y CNU2008201694289U CN200820169428U CN201310905Y CN 201310905 Y CN201310905 Y CN 201310905Y CN U2008201694289 U CNU2008201694289 U CN U2008201694289U CN 200820169428 U CN200820169428 U CN 200820169428U CN 201310905 Y CN201310905 Y CN 201310905Y
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Abstract
The utility model relates to a complete device for mineral slurry processing, which provides a mineral unscreened stock voltage build production line and a mineral pulping production line. The complete device comprises a mineral crushing and grinding production line, an additive solution modulating production line, a production line which modulates mineral powder after crushing and grinding into mineral unscreened stock, a mineral unscreened stock voltage build production line which is matched with a mineral unscreened stock modulating production line, and the mineral pulping production line which is matched with a voltage build production line, wherein the mineral pulping production line comprises a mineral slurry thinning device which is matched with the voltage build production line. The complete device has the beneficial effects that the voltage build production line is added, the binding force and the affinity of mine and water are increased, the hard settlement is not easy to generate, a guiding disc on the mineral slurry thinning device can guide mineral unscreened stock to enter a path, a valve body arranged on the guiding disc can change the volume of a knock cavity and can provide the space for material particles.
Description
[affiliated technical field]
The utility model relates to a kind of complete equipment for processing mineral matter slurry, relates in particular to a kind of complete equipment for processing mineral matter slurry that the thick slurry of mineral matter is built baric flow waterline, mineral matter pulp streamline that has.
[background technology]
The large-scale production of mineral chylema (as water-coal-slurry) up to now, adopts the wet type rod milling of vibrator or rod mill or ball grinding technique to carry out mostly.Traditional technology is to utilize jaw crusher raw ore (as coal) or ore concentrate (as coal) to be crushed to the particle of 20-30 millimeter, remove the iron block at center, ore deposit (as coal) through tramp iron separator, be crushed to the following particle of 3-5 millimeter through hammer mill again, add entry and additive in proportion and form the mineral matter centrotheca, go forward side by side into ball mill or rod mill, in grinding machine, obtain mineral chylema (as water-coal-slurry) magma under the rod milling of steel ball or rod iron or the ball action, magma adds stabilizing agent after filtering and carries out the brute force stirring, finally obtains finished product mineral chylema (as water-coal-slurry).
Traditional ball milling mineral chylema (as water-coal-slurry) crushing technology exists power consumption big, mainly is that in-fighting is big, and simultaneously, to the mineral particle degree poor controllability in the mineral chylema (as water-coal-slurry), mill dielectric loss consumption is big; In addition, single unit system is bulky.
[summary of the invention]
The purpose of this utility model is to provide a kind of complete equipment for processing mineral matter slurry, have the thick slurry of mineral matter on it and build baric flow waterline, mineral matter pulp streamline, the thick slurry of mineral matter is built the baric flow waterline and will slightly be starched stable being transported in the mineral matter pulp streamline, by regulating the spacing of the corresponding valve body that is provided with on the mineral matter slurry device for thinning, can effectively control the particle size after cracking of mineral matter, high efficiency, energy efficient, and compact conformation, volume are little.
Above-mentioned technical purpose of the present utility model mainly solves by the following technical programs: a kind of complete equipment for processing mineral matter slurry, comprise mineral matter crushing and grinding streamline, additive solution modulated stream waterline, mineral matter powder behind the grinding is modulated into mineral matter slightly starches streamline, with be modulated into mineral matter and slightly starch the thick slurry of mineral matter that streamline matches and build the baric flow waterline, with build the mineral matter pulp streamline that the baric flow waterline matches, described mineral matter pulp streamline comprises and builds the mineral matter slurry device for thinning that the baric flow waterline matches, this device for thinning comprises the housing of band charging aperture and discharging opening, it is characterized in that being provided with at least in the housing two flow guiding discs, the edge of described flow guiding disc is cambered surface, the cambered surface top has the valve body of high-wearing feature, and the outer surface of valve body forms the friction striking face; The surface of flow guiding disc of She Zhiing and valve body thereof forms the jet chamber of mineral matter slurry in opposite directions; Have through hole at least one flow guiding disc and the valve body thereof, through hole forms the slurry passage; The zone that the slurry passage is communicated with the jet chamber forms impact cavity.Raw ore (as coal) or ore concentrate (as coal) are through mineral matter crushing and grinding streamline, additive solution modulated stream waterline, mineral matter powder behind the grinding is modulated into mineral matter slightly starches the thick slurry that streamline processing back forms, build the baric flow waterline through the thick slurry of mineral matter, thick slurry enters housing from charging aperture, in the drainage in jet chamber with converge under the effect, flow into impact cavity at a high speed with mode of jet, the mineral matter that arrives in this regional centrotheca is clashed into mutually, these mineral matters simultaneously with valve body on the friction striking face (body wall in impact cavity zone is mainly rubbing surface, the body wall at slurry passage place is mainly striking face, usually also be striking face in corner that rubbing surface is connected with striking face) sidewall collision (striking face on the main and valve body clashes into), thereby make particle realize broken and refinement, discharge from discharging opening by the slurry passage at last.The edge camber of flow guiding disc extends out face, and this shape plays effective guide functions.In addition, charging aperture here and discharging opening can exchange, and promptly the mineral matter centrotheca can enter in the housing from charging aperture, outside discharging opening is discharged housing; Also can enter in the housing, outside charging aperture is discharged housing from the mouth that comes out.The charging aperture of mentioning below, discharging opening, feed end and discharge end also can exchange.
As further improving and replenishing to technique scheme, the utility model adopts following technical measures: the described baric flow waterline of building comprises and is modulated into mineral matter and slightly starches the following check valve that streamline is connected, the last check valve that matches with the mineral matter slurry device for thinning, be connected down the middle chamber between check valve and the last check valve, the pressure differential conveying device that is communicated with middle chamber.Under the effect of pressure differential conveying device, during the interior generation of middle chamber negative pressure, thick slurry is inhaled in the middle chamber by following check valve, and when middle cavity was pressurizeed, its interior thick slurry was injected the mineral matter slurry device for thinning and carried out pulp work by last check valve.In the process of manufacture of mineral matter slurry, increased and built the baric flow waterline, the thick slurry of mineral matter is built pressure, water (molecule) is penetrated under hyperbaric environment in the slight void in hydrophobic mineral particle and the powder by force, increase the adhesion and the affinity of mineral matter and water.Water-coal-slurry by device fabrication of the present utility model is under the prerequisite that does not add stabilizing agent, and static placement can not produce rigid precipitation more than or equal to 3 months yet.
Described pressure differential conveying device comprises defeated slurry cylinder, is arranged on the piston in the defeated slurry cylinder, the piston drive mechanism of driven plunger.Outwards move when the actuating unit driven plunger, the space that hydraulic cylinder is communicated with middle chamber increases, and the pressure in hydraulic cylinder and the middle chamber is reduced, and following check valve is opened, and thick slurry enters middle chamber; Inwardly move when the actuating unit driven plunger, reduce in the space that hydraulic cylinder is communicated with middle chamber, and the pressure in hydraulic cylinder and the middle chamber is increased, following closed check valve, and last one-way valve opens, thick slurry penetrates from last check valve.
Described piston drive mechanism is the plunger pump liquid pressing system, it comprises motor, the twin swash plate plunger-type fuel pump that is connected with motor, the electro hydraulic valve that is connected with twin swash plate plunger-type fuel pump, the oil cylinder that is connected with electro hydraulic valve, described in-oil cylinder piston is connected by connector with the defeated piston of starching in the cylinder.The flexible movements of plunger pump liquid pressing system, convenience, accurate, and volume is little, and in light weight.Piston drive mechanism also can be motor, perhaps is the membrane pump hydraulic system, perhaps is the gear pump hydraulic system, perhaps is the vane pump hydraulic system, perhaps is the crankshaft connecting rod type plunger pump system, perhaps the screw pump hydraulic system.
Described flow guiding disc is two, and the valve body on flow guiding disc is connected with driving mechanism, and another valve body is fixed on the flow guiding disc, and described driving mechanism is handled by automatic control system, and the press detection sensor of described control system is arranged on the charging aperture place.The translation of movable valve body energy makes two valve body relative distances adjustable, with the spacing between the regulation valve body, thus the volume of change impact cavity.Driving mechanism wherein is stepper motor band reductor controlling organization or adds spring controling mechanism or add the accumulator controlling organization or add accumulator controlling organization or jointly controlling mechanism or being variable-frequency motor band reductor controlling organization for mechanical, electrical, liquid, gas for the hydraulic circuit controlling organization or for hydraulic circuit for the pneumatic circuit controlling organization or for pneumatic circuit for servomotor band reductor controlling organization or for mechanical mechanism.Press detection sensor detects the pressure of charging aperture, and pressure signal is reacted to the spacing of automatic control system with regulation valve body, to guarantee the constant pressure of impact cavity mesohigh slurry.
Valve body on the described flow guiding disc and flow guiding disc main body are for dividing body structure, and the friction striking face of valve body can be zigzag structure or helical structure.This can make flow guiding disc and valve body adopt unlike material, and comparatively cheap material is adopted at the position that does not contact with mineral matter, avoids the whole defective that adopts the high rigidity material to cause cost to rise of flow guiding disc.In addition, divide body structure to also help in time, be convenient for changing the valve body of wearing and tearing.The irregularly shaped of friction striking face helps further fragmentation of material.Valve body be pottery or diamond or tungsten carbide or hardness greater than HRC60 (or HV70) hard material, have sufficiently high hardness, to reach the particle requirement, simultaneously, prevent that valve body from crossing quick-wearing, avoid frequent replacing, help saving cost.
One of flow guiding disc of She Zhiing and valve body thereof are discoid in opposite directions, and one is circular, and the through hole of described valve body can be one or a plurality of.
Described mineral matter crushing and grinding streamline comprises jaw crusher, the tramp iron separator that is connected with jaw crusher, the flour mill that is connected with tramp iron separator, the auger conveyor that is connected with flour mill; Described additive solution modulated stream waterline comprises the water meter that can be connected with water pipe, the additive mixed cylinder that is connected with water meter, the additive underflow pump that is connected with the additive mixed cylinder, the additive transition cylinder that is connected with the additive underflow pump, the additive underflow measuring pump that is connected with additive transition cylinder, the water measuring pump that is connected with the running water pipe network, the duct type static mixer that is connected with water measuring pump and additive underflow measuring pump, the additive cylinder that is connected with the duct type static mixer; The described mineral matter that is modulated into is slightly starched streamline and is comprised the variable-frequency motor tubing pump that is connected with the additive cylinder, the powder-storage bin that is connected with auger conveyor, the twin-screw conveying and metering device that is connected with powder-storage bin, just stir device with the variable-frequency motor tubing pump with the horizontal mixing that twin-screw conveying and metering device is connected, just stir the high-speed stirring apparatus that device is connected with horizontal mixing, described high-speed stirring apparatus with build the baric flow waterline and be connected.
The described mineral matter pulp streamline of building the baric flow waterline and matching with it is at least one group.
Also comprise mineral matter finished product slurry modulated stream waterline, it is connected with mineral matter pulp streamline.
The beneficial effect that the utlity model has: 1, increased and build the baric flow waterline, the thick slurry of mineral matter is built pressure, water (molecule) is penetrated under hyperbaric environment in the slight void of hydrophobic mineral particle and powder inside by force, increase the adhesion and the affinity of mineral matter and water, be difficult for producing rigid precipitation.2, the flow guiding disc on the mineral matter slurry device for thinning can guide the path that the thick slurry of mineral matter enters, and the valve body which is provided with not only can change the volume of impact cavity but also material particle space can be provided.Regulate spacing between the corresponding valve body by driving mechanism, can change the jet pressure that enters cavity and effectively control particle size after cracking.3, the technical solution of the utility model high efficiency is avoided in-fighting, and effective use of energy sources cuts down the consumption of energy.4, this apparatus structure compactness, volume are little, and floor space is little, conveniently produce, processing, transportation.
[description of drawings]
Fig. 1 is a kind of streamline schematic diagram of the present utility model;
Fig. 2 is an another kind of streamline schematic diagram of the present utility model;
Fig. 3 is another streamline schematic diagram of the present utility model;
Fig. 4 is a schematic diagram of building baric flow waterline and pulp streamline in the utility model;
Fig. 5 is a special case structural representation building actuating unit on the baric flow waterline among Fig. 4;
Fig. 6 is the sectional structure schematic diagram of first kind of flow guiding disc being provided with in the utility model;
Fig. 7 is second kind of sectional structure schematic diagram of two flow guiding discs that cooperatively interact in the utility model;
Fig. 8 be among Fig. 7 A-A to structural representation;
Fig. 9 is the third sectional structure schematic diagram of two flow guiding discs that cooperatively interact in the utility model;
Figure 10 be among Fig. 9 B-B to structural representation;
Figure 11 is the 4th kind of sectional structure schematic diagram of two flow guiding discs that cooperatively interact in the utility model;
Figure 12 be among Figure 11 C-C to structural representation;
Figure 13 is the 5th kind of sectional structure schematic diagram of two flow guiding discs that cooperatively interact in the utility model;
Figure 14 be among Figure 13 D-D to structural representation;
Figure 15 is the 6th kind of sectional structure schematic diagram of two flow guiding discs that cooperatively interact in the utility model.
[specific embodiment]
Below by embodiment, and in conjunction with the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment 1: a kind of complete equipment for processing mineral matter slurry, as shown in Figure 1, it comprises mineral matter crushing and grinding assembly line A, additive solution modulated stream waterline B, mineral matter powder behind the grinding is modulated into mineral matter slightly starches streamline C, slightly starch the thick slurry of mineral matter that streamline C matches and build baric flow waterline D with being modulated into mineral matter, and build the mineral matter pulp streamline E that baric flow waterline D matches, the mineral matter finished product that is connected with mineral matter pulp streamline E slurry modulated stream waterline F.The mineral matter pulp streamline E that builds baric flow waterline D and match with it is at least one group (as shown in Figure 1-Figure 3).
Mineral matter crushing and grinding assembly line A comprises jaw crusher 1, the tramp iron separator 2 that is connected with jaw crusher 1, the flour mill 3 that is connected with tramp iron separator 2, the auger conveyor 4 that is connected with flour mill 3.Former mineral matter or enter jaw crusher 1 through the mineral matter after selected, be crushed to the particle of technological requirement through jaw crusher 1 after, flow through tramp iron separator 2, the irony foreign material in the mineral matter are removed.Go into elevator in the flour mill 3 by the materials flow of the mineral matter behind the tramp iron separator 2, mineral particle through promoting by the oscillating feeder in the flour mill 3 to flour mill 3 dosings, a mineral matter material enters flour mill 3 and carries out grinding, the mineral matter powder that is come out by flour mill 3 enters Ji Fencang, and it is stand-by to be delivered to powder-storage bin 13 through auger conveyor 4 again.
Additive solution modulated stream waterline B comprises the water meter 5 that can be connected with water pipe, the additive mixed cylinder 6 that is connected with water meter 5, the additive underflow pump 7 that is connected with additive mixed cylinder 6, the additive transition cylinder 8 that is connected with additive underflow pump 7, the additive underflow measuring pump 9 that is connected with additive transition cylinder 8, the water measuring pump 10 and the duct type static mixer 11 that are connected with additive transition cylinder 8, the additive cylinder 12 that is connected with duct type static mixer 11.According to the mineral matter of different physical properties, the concentration of its additive solution is inconsistent.Therefore when the modulation additive solution, has flexibility.Pour in the additive mixed cylinder 6 through the packed or liquid barreled additive of powdery of metering, technological requirement according to additive solution, by water meter 5 water that measures is added in the additive mixed cylinder 6, the stirring shear by in the additive mixed cylinder 6 stirs into the additive underflow.It is stand-by by the additive underflow pump 7 that is contained in additive mixed cylinder bottom the additive underflow in the additive mixed cylinder all to be pumped into additive transition cylinder 8 again.Press the technological requirement of additive solution, the additive underflow should be diluted to the additive solution of final ratio, by additive underflow measuring pump 9 and water measuring pump 10, respectively the additive underflow in the transition cylinder from the beginning and the water of grid are measured pumping in proportion, the additive underflow and the water of pumping pool together in proportion, enter into a duct type static mixer 11 by a pipeline, effect by duct type static mixer 11, additive underflow and water are fully mixed, import finally in the additive cylinder 12 that to form additive solution stand-by.
The modulation mineral matter is slightly starched streamline C and is comprised the variable-frequency motor tubing pump 14 that is connected with additive cylinder 12, the powder-storage bin 13 that is connected with auger conveyor 4, the twin-screw conveying and metering device 15 that is connected with powder-storage bin 13, just stir device 16 with variable-frequency motor tubing pump 14 with the horizontal mixing that twin-screw conveying and metering device 15 is connected, just stir the high-speed stirring apparatus 17 that device 16 is connected with horizontal mixing, high-speed stirring apparatus 17 with build baric flow waterline D and be connected.The twin-screw conveying and metering device 15 that enters by frequency control behind the broken arch of the air bubble Arch-Breaking Device of mineral matter meal in powder-storage bin 13 in the powder-storage bin 13 carries out the continous way metering, mineral matter meal through measuring enters horizontal mixing and just stirs device 16, meanwhile, the continuous signal of being sent by twin-screw conveying and metering device 15 is controlled the variable-frequency motor tubing pump 14 of the pumping additive solution of additive cylinder 12 bottoms by PLC.By the mineral matter meal set in the PLC control system and the ratio of additive solution, automatic synchronization is followed in proportion between the two.The additive solution that is come out by tubing pump 14 pumpings enters horizontal mixing together and just stirs device 16.Just stir in horizontal mixing under the mixing stirring of device 16, mineral matter meal and additive solution are tentatively mixed form mineral matter and slightly starch with certain flowability, enter high-speed stirring apparatus 17, under the high-speed stirred shear action of high-speed stirring apparatus 17, it is stand-by to form the thick slurry of the mineral matter with good fluidity.
Building baric flow waterline D comprises and is modulated into mineral matter and slightly starches the following check valve 18 that streamline C is connected, the last check valve 20 that matches with the mineral matter slurry device for thinning, be connected down the middle chamber 19 between check valve 18 and the last check valve 20, the pressure differential conveying device that is communicated with middle chamber 19.The pressure differential conveying device comprises defeated slurry cylinder 23, is arranged on the piston 22 in the defeated slurry cylinder 23, the piston drive mechanism 21 of driven plunger 22.The pressure range of building in the baric flow waterline D is 5～100Mpa.Pressure can or be 30Mpa or for 50Mpa or for 80Mpa for 10Mpa, perhaps be any one interior pressure of above-mentioned scope.The range of flow of the thick slurry of mineral matter is 500～25L/min.
Mineral matter pulp streamline E comprises and builds the mineral matter slurry device for thinning that baric flow waterline D matches, as shown in Figure 6, this device for thinning comprises the housing 51 of band charging aperture 57 and discharging opening 58, be provided with two flow guiding discs 52 in the housing 51, the edge of described flow guiding disc 52 is cambered surface, the cambered surface top has the valve body 53 of high-wearing feature, and the outer surface of valve body 53 forms the friction striking face; The surface of flow guiding disc 52 of She Zhiing and valve body 53 thereof forms the jet chamber 54 of mineral matter slurry in opposite directions; Have a through hole on flow guiding disc 52 and valve 5 bodies 3 thereof, through hole forms slurry passage 55; The zone that slurry passage 55 is communicated with jet chamber 54 forms impact cavity 56.
Valve body 53 on flow guiding disc 52 is connected with driving mechanism, and another valve body 53 is fixed on the flow guiding disc 2.
53 1 of flow guiding disc 52 of She Zhiing and valve bodies thereof are discoid in opposite directions, and one is circular.
Driving mechanism is handled by automatic control system, and the press detection sensor of control system is arranged on the charging aperture place.Driving mechanism is stepper motor band reductor controlling organization or adds spring controling mechanism or add the accumulator controlling organization or add accumulator controlling organization or jointly controlling mechanism or being variable-frequency motor band reductor controlling organization for mechanical, electrical, liquid, gas for the hydraulic circuit controlling organization or for hydraulic circuit for the pneumatic circuit controlling organization or for pneumatic circuit for servomotor band reductor controlling organization or for mechanical mechanism.
The shape in jet chamber 54 is the little reducing shape of outer imperial palace, and outside dimension is at 20-200mm, and interior hole dimension is at 10-100mm, and its minimum place spacing is 0.001-20mm.Can adjust spacing between two valve bodies 53 according to actual conditions is 0.03mm or for 0.005mm or be 5mm, perhaps is any one value in the above-mentioned scope.In the certain clearance scope, mineral matter flow velocity V=170-500 meter per second.
Raw ore (as coal) or ore concentrate (as coal) enter housing through the thick slurry that forms after the preliminary working from charging aperture, in the drainage in jet chamber with converge under the effect, flow into impact cavity at a high speed with mode of jet, the mineral matter that arrives in this regional centrotheca is clashed into mutually, these mineral matters simultaneously with valve body on the friction striking face (body wall in impact cavity zone is mainly rubbing surface, the body wall at slurry passage place is mainly striking face, usually also be striking face in corner that rubbing surface is connected with striking face) sidewall collision (striking face on the main and valve body clashes into), thereby make particle realize broken and refinement, discharge from discharging opening by the slurry passage at last, finish the broken refinement work of solid-state mineral matter.
Mineral matter finished product slurry modulated stream waterline F, consider that mineral matter finished product slurry is storing, transporting, stability in the use and other specific (special) requirements are added such as stabilizing agent and other special additive in mineral matter finished product slurry, and carry out high-speed stirred by homogenizer and shear evenly.Satisfy the final technological requirement of mineral matter finished product slurry.
Embodiment 2: a kind of complete equipment for processing mineral matter slurry, as shown in Figure 7 and Figure 8, have plurality of through holes on flow guiding disc 52 and the valve body 53 thereof, and plurality of through holes forms a plurality of slurry passages 55.All the other structures are with embodiment 1.
Embodiment 3: a kind of complete equipment for processing mineral matter slurry, as Fig. 6, Fig. 7, Fig. 9, Figure 11, Figure 13 and shown in Figure 15, the valve body 53 on the flow guiding disc 52 is the branch body structure with flow guiding disc 52 main bodys.All the other structures are with embodiment 1 or embodiment 2.
Embodiment 4: a kind of complete equipment for processing mineral matter slurry, as shown in Figure 8, the friction striking face of valve body 53 can be zigzag structure or helical structure.All the other structures are with embodiment 1 or embodiment 2 or embodiment 3.
Embodiment 4: a kind of complete equipment for processing mineral matter slurry, as Fig. 9-shown in Figure 14, valve body 53 is that pottery or diamond or tungsten carbide or hardness are greater than HRC60 hard material.All the other structures are with embodiment 1 or embodiment 2.
Embodiment 5: a kind of complete equipment for processing mineral matter slurry, as shown in figure 15, valve body 53 is fixed on the flow guiding disc 52 by valve block 59.All the other structures are with embodiment 1 or embodiment 2 or embodiment 3 or embodiment 4.
Claims (10)
1. complete equipment for processing mineral matter slurry, comprise mineral matter crushing and grinding streamline (A), additive solution modulated stream waterline (B), mineral matter powder behind the grinding is modulated into mineral matter slightly starches streamline (C), with be modulated into mineral matter and slightly starch the thick slurry of mineral matter that streamline (C) matches and build baric flow waterline (D), with build the mineral matter pulp streamline (E) that baric flow waterline (D) matches, described mineral matter pulp streamline (E) comprises and builds the mineral matter slurry device for thinning that baric flow waterline (D) matches, this device for thinning comprises the housing (51) of band charging aperture (57) and discharging opening (58), it is characterized in that being provided with at least in the housing (51) two flow guiding discs (52), the edge of described flow guiding disc (52) is cambered surface, the cambered surface top has the valve body (53) of high-wearing feature, and the outer surface of valve body (53) forms the friction striking face; The surface of flow guiding disc of She Zhiing (52) and valve body (53) thereof forms the jet chamber (54) of mineral matter slurry in opposite directions; Have through hole at least one flow guiding disc (52) and the valve body (53) thereof, through hole forms slurry passage (55); The zone that slurry passage (55) is communicated with jet chamber (54) forms impact cavity (56).
2. a kind of complete equipment for processing mineral matter slurry according to claim 1, it is characterized in that the described baric flow waterline (D) of building comprises and is modulated into mineral matter and slightly starches the following check valve (18) that streamline (C) is connected, the last check valve (20) that matches with the mineral matter slurry device for thinning, be connected down the middle chamber (19) between check valve (18) and the last check valve (20), the pressure differential conveying device that is communicated with middle chamber (19).
3. a kind of complete equipment for processing mineral matter slurry according to claim 2 is characterized in that described pressure differential conveying device comprises defeated slurry cylinder (23), is arranged on the piston (22) in the defeated slurry cylinder (23), the piston drive mechanism (21) of driven plunger (22).
4. a kind of complete equipment for processing mineral matter slurry according to claim 3, it is characterized in that described piston drive mechanism (21) is the plunger pump liquid pressing system, it comprises motor (30), the twin swash plate plunger-type fuel pump (29) that is connected with motor (30), the electro hydraulic valve (28) that is connected with twin swash plate plunger-type fuel pump (29), piston in the oil cylinder (27) that is connected with electro hydraulic valve (28), described oil cylinder (27) is connected by connector with the defeated piston of starching in the cylinder (23) (22).
5. a kind of complete equipment for processing mineral matter slurry according to claim 1, it is characterized in that described flow guiding disc (52) is two, valve body (53) on the flow guiding disc (52) is connected with driving mechanism, another valve body (53) is fixed on the flow guiding disc (52), described driving mechanism is handled by automatic control system, and the press detection sensor of described control system is arranged on the charging aperture place.
6. a kind of complete equipment for processing mineral matter slurry according to claim 5, it is characterized in that the valve body (53) on the described flow guiding disc (52) is the branch body structure with flow guiding disc (52) main body, the friction striking face of valve body (53) can be zigzag structure or helical structure.
7. a kind of complete equipment for processing mineral matter slurry according to claim 6 is characterized in that the flow guiding disc (52) and (53) one of the valve bodies thereof that are provided with in opposite directions are discoid, and one is circular, and the through hole of described valve body (53) can be one or a plurality of.
8. a kind of complete equipment for processing mineral matter slurry according to claim 7, it is characterized in that described mineral matter crushing and grinding streamline (A) comprises jaw crusher (1), the tramp iron separator (2) that is connected with jaw crusher (1), the flour mill (3) that is connected with tramp iron separator (2), the auger conveyor (4) that is connected with flour mill (3); Described additive solution modulated stream waterline (B) comprises the water meter (5) that can be connected with water pipe, the additive mixed cylinder (6) that is connected with water meter (5), the additive underflow pump (7) that is connected with additive mixed cylinder (6), the additive transition cylinder (8) that is connected with additive underflow pump (7), the additive underflow measuring pump (9) that is connected with additive transition cylinder (8), the water measuring pump (10) that is connected with the running water pipe network, the duct type static mixer (11) that is connected with water measuring pump (10) and additive underflow measuring pump (9), the additive cylinder (12) that is connected with duct type static mixer (11); The described mineral matter that is modulated into is slightly starched streamline (C) and is comprised the variable-frequency motor tubing pump (14) that is connected with additive cylinder (12), the powder-storage bin (13) that is connected with auger conveyor (4), the twin-screw conveying and metering device (15) that is connected with powder-storage bin (13), just stir device (16) with the horizontal mixing that variable-frequency motor tubing pump (14) is connected with twin-screw conveying and metering device (15), just stir the high-speed stirring apparatus (17) that device (16) is connected with horizontal mixing, described high-speed stirring apparatus (17) with build baric flow waterline (D) and be connected.
9. the solid-state mineral matter liquefying plant of jetting type according to claim 8 is characterized in that the described mineral matter pulp streamline (E) of building baric flow waterline (D) and matching with it is at least one group.
10. a kind of complete equipment for processing mineral matter slurry according to claim 9 is characterized in that also comprising mineral matter finished product slurry modulated stream waterline (F), and it is connected with mineral matter pulp streamline (E).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201694289U CN201310905Y (en) | 2008-12-11 | 2008-12-11 | Complete device for mineral slurry processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201694289U CN201310905Y (en) | 2008-12-11 | 2008-12-11 | Complete device for mineral slurry processing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201310905Y true CN201310905Y (en) | 2009-09-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201694289U Expired - Fee Related CN201310905Y (en) | 2008-12-11 | 2008-12-11 | Complete device for mineral slurry processing |
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| CN (1) | CN201310905Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104263920A (en) * | 2014-09-30 | 2015-01-07 | 长沙有色冶金设计研究院有限公司 | Zinc sulfide concentrate raw material treatment method and device |
-
2008
- 2008-12-11 CN CNU2008201694289U patent/CN201310905Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104263920A (en) * | 2014-09-30 | 2015-01-07 | 长沙有色冶金设计研究院有限公司 | Zinc sulfide concentrate raw material treatment method and device |
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