CN214551306U - Thickener for manganese sulfate evaporative crystallization - Google Patents
Thickener for manganese sulfate evaporative crystallization Download PDFInfo
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- CN214551306U CN214551306U CN202120413257.5U CN202120413257U CN214551306U CN 214551306 U CN214551306 U CN 214551306U CN 202120413257 U CN202120413257 U CN 202120413257U CN 214551306 U CN214551306 U CN 214551306U
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Abstract
The utility model discloses a manganese sulfate thickening technical field's a manganese sulfate is stiff ware for evaporative crystallization, include: a cartridge assembly; the two lifting assemblies are arranged on the left side and the right side of the top of the barrel assembly; the two feeding assemblies are arranged on the tops of the left side and the right side of the barrel assembly in a left-right mode; the two separation box assemblies are arranged on the left side and the right side of the barrel assembly in a left-right mode; the two air pressure assemblies are correspondingly arranged at the tops of the two separation box assemblies one by one; two ejection of compact subassembly, two install of ejection of compact subassembly one-to-one two the bottom of separator box subassembly, the utility model discloses can carry out high-pressure separation in promoting the separator box with the raw materials to the stoste to the separation circulates the crystallization, improves crystallization efficiency and precipitation rate.
Description
Technical Field
The utility model relates to a manganese sulfate thickening technical field specifically is a manganese sulfate is stiff ware for evaporative crystallization.
Background
Manganese sulfate is a trace element needed by crops for synthesizing fatty acid, so that the manganese sulfate can be applied to soil as a fertilizer, and the yield can be increased. Manganese sulfate is added into animal feed, and has fattening effect. Manganese sulfate is also a raw material and analytical reagent for preparing other manganese salts. Manganese sulfate is also used in the industrial production of electrolytic manganese, dye, paper making, ceramics and the like.
The thickener is also called thickener or thickener. A settler for concentrating solid particles in a suspension. Have a conical, cylindrical, square, etc. form. For certain needs, it is also designed to be multi-layered. The large thickener is mostly a cylinder with a conical bottom, suspension flows in from a central liquid feeding groove, and clear liquid overflows from the periphery and is discharged from an outflow groove. The rakes moving slowly are arranged in the device, so that sediments or sediments are collected to the center of the bottom of the device and are discharged through the discharge conduit after being collected.
The existing thickener mostly performs solid-liquid separation on crystals in a natural precipitation mode, so that the efficiency is low, and when mother liquor is separated, fine crystals can be brought out after the mother liquor is directly discharged, so that the precipitation rate of the crystals is reduced.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a manganese sulfate is stiff ware for evaporative crystallization to solve the current stiff ware that proposes in the above-mentioned background art and carry out solid-liquid separation through the mode of natural sedimentation to the crystal more, it is inefficient, and, when separating the mother liquor, can take out slight crystal after the mother liquor direct discharge, reduced the problem of the precipitation rate of crystal.
In order to achieve the above object, the utility model provides a following technical scheme: a thickener for manganese sulfate evaporative crystallization comprises:
a cartridge assembly;
the two lifting assemblies are arranged on the left side and the right side of the top of the barrel assembly;
the two feeding assemblies are arranged on the tops of the left side and the right side of the barrel assembly in a left-right mode;
the two separation box assemblies are arranged on the left side and the right side of the cylinder assembly one by one, and the inner cavity of each separation box assembly is communicated with the inner cavity of the cylinder assembly;
the two air pressure assemblies are correspondingly arranged at the tops of the two separation box assemblies one by one;
the two discharging assemblies are arranged at the bottoms of the two separating box assemblies in a one-to-one correspondence mode, and one end, far away from the separating box assemblies, of the discharging assemblies is connected with the feeding assembly.
Preferably, the cartridge assembly comprises:
a cylinder;
a top cap mounted on top of the cylinder;
the two feeding connectors are arranged on the tops of the left side and the right side of the cylinder in a left-right mode, and the inner cavities of the feeding connectors are communicated with the inner cavity of the cylinder;
a cooling conduit embedded within the sidewall of the cylinder.
Preferably, the lifting assembly comprises:
a motor;
and the screw is arranged on an output shaft of the motor.
Preferably, the feeding assembly comprises:
a feed pump;
the feeding pipeline is arranged on a feeding hole of the feeding pump;
the first circulation connecting port is arranged at one end, close to the feeding pump, of the bottom of the feeding pipeline.
Preferably, the separation tank assembly comprises:
a separation box body;
the feeding port is arranged at the top of the side surface of the separation box body, and the inner cavity of the feeding port is communicated with the inner cavity of the separation box body;
the filter plate is arranged at the bottom of the inner cavity of the separation box body;
the air inlet connector is arranged at the top of the separation box body, and the inner cavity of the air inlet connector is communicated with the inner cavity of the separation box body;
the discharge connecting port is arranged at the bottom of the side surface of the separation box body and is arranged at the upper end of the filter plate, and the inner cavity of the discharge connecting port is communicated with the inner cavity of the separation box body;
the second circulation connecting port is arranged at the middle end of the bottom of the separation box body, and the inner cavity of the second circulation connecting port is communicated with the inner cavity of the separation box body;
and one end of the circulating pipeline is arranged at one end, far away from the separation box body, of the second circulating connector.
Preferably, the pneumatic assembly comprises:
an air pump;
one end of the first air inlet pipeline is arranged on an air inlet of the air pump;
and one end of the second air inlet pipeline is arranged on the air outlet of the air pump.
Preferably, the discharging assembly comprises:
a discharge pump;
and the discharging pipeline is arranged on a discharging port of the discharging pump.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model discloses can promote the raw materials and carry out high-pressure separation in the separator box, and carry out the circulation crystallization to the stock solution of separation, improve crystallization efficiency and precipitation rate, the pan feeding mouth is connected with the drum, the inner chamber of pan feeding mouth is linked up with the inner chamber of drum mutually, the mother liquor that precipitates the crystal promotes the inner chamber of pan feeding mouth through the screw rod, and enter the inner chamber of separator box body through the pan feeding mouth, the mother liquor that precipitates the crystal filters through the filter, the mother liquor of crystal that is filtered enters the inner chamber bottom of separator box body through the filter, seal treatment is done between air inlet connector and the separator box body, atmospheric pressure enters the inner chamber of separator box body through the air inlet connector, improve the pressure of separator box body inner chamber, precipitate the mother liquor through pressure, improve the efficiency of crystal and mother liquor separation, the separated mother liquor enters the inner chamber of circulating line through the second circulation connector, the end of the circulating pipeline far away from the second circulating connector is connected with the first circulating connector, separated mother liquor enters the inner cavity of the feeding pipeline through the circulating pipeline and the first circulating connector and then enters the inner cavity of the cylinder again to continuously separate out crystals, the mother liquor can be repeatedly separated out of the crystals, and the separation rate of the crystals is improved.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic structural view of the barrel assembly of the present invention;
FIG. 3 is a schematic view of the lifting assembly of the present invention;
FIG. 4 is a schematic structural view of the feeding assembly of the present invention;
FIG. 5 is a schematic view of the separator tank assembly of the present invention;
FIG. 6 is a schematic view of the pneumatic assembly of the present invention;
fig. 7 is a schematic structural view of the discharging assembly of the present invention.
In the figure: 100 cylinder components, 110 cylinders, 120 top covers, 130 feeding connecting ports, 140 cooling pipelines, 200 lifting components, 210 motors, 220 screws, 300 feeding components, 310 feeding pumps, 320 feeding pipelines, 330 first circulating connecting ports, 400 separating box components, 410 separating box bodies, 420 feeding ports, 430 filter plates, 440 air inlet connecting ports, 450 discharging connecting ports, 460 second circulating connecting ports, 470 circulating pipelines, 500 air pressure components, 510 air pumps, 520 first air inlet pipelines, 530 second air inlet pipelines, 600 discharging components, 610 discharging pumps and 620 discharging pipelines.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
The utility model provides a manganese sulfate is stiff ware for evaporative crystallization can promote the raw materials and carry out high-pressure separation in the separator box to the stoste to the separation circulates the crystallization, improves crystallization efficiency, please refer to figure 1, include: a cartridge assembly 100, a lifting assembly 200, a feeding assembly 300, a separation box assembly 400, an air pressure assembly 500, and an outfeed assembly 600;
referring to fig. 1-2, cartridge assembly 100 includes:
a cylinder 110;
the top cover 120 is mounted on the top of the cylinder 110 by bolts;
the two feeding connectors 130 are arranged on the top of the left side and the right side of the cylinder 110, the inner cavity of the feeding connector 130 is communicated with the inner cavity of the cylinder 110, and the feeding connector 130 and the cylinder 110 are sealed;
the cooling pipeline 140 is embedded in the side wall of the cylinder 110, one end of the cooling pipeline 140 is connected with a water pump, cold water enters the cooling pipeline 140 through the water pump, heat exchange is carried out between the cold water and the cylinder 110 through the cooling pipeline 140, the mother liquor entering the cylinder 110 is cooled, and crystals are separated out by cooling the mother liquor;
referring to fig. 1-3, two lifting assemblies 200 are mounted on the top left and right sides of the barrel assembly 100, the lifting assemblies 200 comprising:
one motor 210 of the two motors 210 is mounted on the right side of the top cover 120 through a bolt, and the other motor 210 is mounted on the left side of the top cover 120 through a bolt;
one screw 220 of the two screws 220 is connected and installed on the output shaft of the left motor 210 through a spline or a flat key, the other screw 220 is connected and installed on the output shaft of the right motor 210 through a spline or a flat key, the two screws 220 are both arranged in the inner cavity of the cylinder 110, the motor 210 drives the screws 220 to rotate, and the mother liquor with crystals precipitated is lifted through the rotation of the screws 220;
referring to fig. 1, 2 and 4, two feeding assemblies 300 are installed on the top of the left and right sides of the barrel assembly 100, wherein the feeding assemblies 300 include:
the discharge port of one of the two feed pumps 310 is mounted on the left feed connection port 130 through a flange, and the discharge port of the other feed pump 310 is mounted on the right feed connection port 130 through a flange;
one feed pipe 320 of the two feed pipes 320 is flanged on the feed port of the left feed pump 310, the other feed pipe 320 is flanged on the feed port of the right feed pump 310, and mother liquor is pumped into the inner cavity of the cylinder 110 through the matching use of the feed pipe 320, the feed pump 310 and the feed connecting port 130;
the first circulation connection port 330 is provided at the bottom of the feed pipe 320 adjacent to one end of the feed pump 310;
referring to fig. 1, 2, 3 and 5, two separation tank assemblies 400 are installed on left and right sides of the cylinder assembly 100, and an inner cavity of the separation tank assembly 400 is communicated with an inner cavity of the cylinder assembly 100, and the separation tank assembly 400 includes:
one separation tank body 410 of the two separation tank bodies 410 is installed at the left side surface of the cylinder 110, and the other separation tank body 410 is installed at the right side surface of the cylinder 110;
one of the two feeding ports 420 is arranged at the top of the side surface of the left separation box body 410, the other feeding port 420 is arranged at the top of the side surface of the right separation box body 410, the inner cavity of the feeding port 420 is communicated with the inner cavity of the separation box body 410, the feeding port 420 is connected with the cylinder 110, the inner cavity of the feeding port 420 is communicated with the inner cavity of the cylinder 110, and mother liquor for separating out crystals is lifted to the inner cavity of the feeding port 420 through the screw 220 and enters the inner cavity of the separation box body 410 through the feeding port 420;
the filter plate 430 is arranged at the bottom of the inner cavity of the separation box body 410, the mother liquid for separating out crystals is filtered by the filter plate 430, and the mother liquid for the crystals at the filtered part enters the bottom of the inner cavity of the separation box body 410 through the filter plate 430;
the air inlet connecting port 440 is arranged at the top of the separation box body 410, the inner cavity of the air inlet connecting port 440 is communicated with the inner cavity of the separation box body 410, the air inlet connecting port 440 and the separation box body 410 are sealed, air pressure enters the inner cavity of the separation box body 410 through the air inlet connecting port 440, the pressure of the inner cavity of the separation box body 410 is improved, mother liquor is separated out through the pressure, and the efficiency of separating crystals from the mother liquor is improved;
the discharge connecting port 450 is arranged at the bottom of the side surface of the separation box body 410, the discharge connecting port 450 is arranged at the upper end of the filter plate 430, the inner cavity of the discharge connecting port 450 is communicated with the inner cavity of the separation box body 410, and the filtered crystals are discharged to the outside of the separation box body 410 through the discharge connecting port 450;
the second circulation connecting port 460 is arranged at the middle end of the bottom of the separation box body 410, the inner cavity of the second circulation connecting port 460 is communicated with the inner cavity of the separation box body 410, and separated mother liquor is discharged through the second circulation connecting port 460;
one end of the circulation pipeline 470 is installed at one end, far away from the separation box body 410, of the second circulation connecting port 460, separated mother liquor enters the inner cavity of the circulation pipeline 470 through the second circulation connecting port 460, one end, far away from the second circulation connecting port 460, of the circulation pipeline 470 is connected with the first circulation connecting port 330, the separated mother liquor enters the inner cavity of the feeding pipeline 320 through the circulation pipeline 470 and the first circulation connecting port 330, and then enters the inner cavity of the cylinder 110 again to continue to precipitate crystals, so that the mother liquor can be repeatedly precipitated crystals, and the precipitation rate of the crystals is improved;
referring to fig. 1, 5 and 6, two pneumatic assemblies 500 are mounted on the top of two separation tank assemblies 400 in a one-to-one correspondence, and the pneumatic assemblies 500 include:
an air pump 510;
one end of the first air inlet pipe 520 is installed on an air inlet of the air pump 510;
one end of the second air inlet pipeline 530 is installed on an air outlet of the air pump 510, one end of the second air inlet pipeline 530, which is far away from the air pump 510, is connected with the air inlet connector 440, and the inner cavity of the separation box body 410 is pressurized by matching the first air inlet pipeline 520, the air pump 510 and the second air inlet pipeline 530, so that the pressure of the inner cavity of the separation box body 410 is improved, the filtration of crystals is accelerated, and the separation efficiency of the crystals and the mother liquor is improved;
referring to fig. 1, 5 and 7, two discharging assemblies 600 are correspondingly mounted at the bottom of two separating box assemblies 400, and one end of the discharging assembly 600 far away from the separating box assemblies 400 is connected to the feeding assembly 300, and the discharging assembly 600 includes:
the feed inlet of the discharge pump 610 is arranged on the discharge connecting port 450 through a flange;
the discharge pipe 620 is installed on the discharge port of the discharge pump 610, and the crystal is discharged out of the inner cavity of the separation box body 410 through the matching use of the discharge connector 450, the discharge pump 610 and the discharge pipe 620.
While the invention has been described above with reference to an embodiment, various modifications may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In particular, as long as there is no structural conflict, the various features of the disclosed embodiments of the present invention can be used in any combination with each other, and the description of such combinations is not exhaustive in the present specification only for the sake of brevity and resource conservation. Therefore, it is intended that the invention not be limited to the particular embodiments disclosed, but that the invention will include all embodiments falling within the scope of the appended claims.
Claims (7)
1. The thickener for manganese sulfate evaporative crystallization is characterized in that: the method comprises the following steps:
a cartridge assembly (100);
the two lifting assemblies (200) are arranged on the left side and the right side of the top of the barrel assembly (100) one by one;
two feeding assemblies (300), wherein the two feeding assemblies (300) are arranged on the top of the left side and the right side of the barrel assembly (100) in a left-right mode;
the two separation box assemblies (400) are arranged on the left side and the right side of the cylinder assembly (100) one by one, and the inner cavity of the separation box assembly (400) is communicated with the inner cavity of the cylinder assembly (100);
the two air pressure assemblies (500) are correspondingly arranged on the tops of the two separation box assemblies (400) one by one;
the two discharging assemblies (600) are correspondingly arranged at the bottoms of the two separating box assemblies (400), and one end, far away from the separating box assemblies (400), of the discharging assemblies (600) is connected with the feeding assembly (300).
2. The thickener for manganese sulfate evaporative crystallization according to claim 1, wherein: the cartridge assembly (100) comprises:
a cylinder (110);
a top cover (120), the top cover (120) being mounted on top of the cylinder (110);
the two feeding connecting ports (130) are arranged on the top of the left side and the right side of the cylinder (110), one left side and one right side of the two feeding connecting ports (130), and the inner cavity of each feeding connecting port (130) is communicated with the inner cavity of the cylinder (110);
a cooling conduit (140), the cooling conduit (140) embedded within the sidewall of the cylinder (110).
3. The thickener for manganese sulfate evaporative crystallization according to claim 1, wherein: the lifting assembly (200) comprises:
a motor (210);
a screw (220), the screw (220) being mounted on an output shaft of the motor (210).
4. The thickener for manganese sulfate evaporative crystallization according to claim 1, wherein: the feed assembly (300) comprises:
a feed pump (310);
a feed conduit (320), the feed conduit (320) being mounted on a feed inlet of the feed pump (310);
a first circulation connection port (330), the first circulation connection port (330) being disposed at a bottom of the feed pipe (320) adjacent to an end of the feed pump (310).
5. The thickener for manganese sulfate evaporative crystallization according to claim 1, wherein: the separator tank assembly (400) comprises:
a separator tank body (410);
the feeding port (420) is arranged at the top of the side face of the separation box body (410), and the inner cavity of the feeding port (420) is communicated with the inner cavity of the separation box body (410);
the filter plate (430), the said filter plate (430) is installed in the bottom of inner chamber of the said separation box body (410);
the air inlet connecting port (440), the air inlet connecting port (440) is installed at the top of the separation box body (410), and the inner cavity of the air inlet connecting port (440) is communicated with the inner cavity of the separation box body (410);
the discharge connecting port (450), the discharge connecting port (450) is arranged at the bottom of the side surface of the separation box body (410), the discharge connecting port (450) is arranged at the upper end of the filter plate (430), and the inner cavity of the discharge connecting port (450) is communicated with the inner cavity of the separation box body (410);
the second circulation connecting port (460) is arranged at the middle end of the bottom of the separation box body (410), and the inner cavity of the second circulation connecting port (460) is communicated with the inner cavity of the separation box body (410);
a circulation pipe (470), one end of the circulation pipe (470) being installed on the second circulation connection port (460) at an end far from the separation tank body (410).
6. The thickener for manganese sulfate evaporative crystallization according to claim 1, wherein: the pneumatic assembly (500) comprises:
an air pump (510);
a first air inlet duct (520), one end of the first air inlet duct (520) being mounted on an air inlet of the air pump (510);
a second air inlet duct (530), one end of the second air inlet duct (530) being mounted on an air outlet of the air pump (510).
7. The thickener for manganese sulfate evaporative crystallization according to claim 1, wherein: the outfeed assembly (600) comprising:
a discharge pump (610);
a discharge conduit (620), the discharge conduit (620) being mounted on a discharge port of the discharge pump (610).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120413257.5U CN214551306U (en) | 2021-02-25 | 2021-02-25 | Thickener for manganese sulfate evaporative crystallization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120413257.5U CN214551306U (en) | 2021-02-25 | 2021-02-25 | Thickener for manganese sulfate evaporative crystallization |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214551306U true CN214551306U (en) | 2021-11-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120413257.5U Active CN214551306U (en) | 2021-02-25 | 2021-02-25 | Thickener for manganese sulfate evaporative crystallization |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214551306U (en) |
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2021
- 2021-02-25 CN CN202120413257.5U patent/CN214551306U/en active Active
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