CN214597315U - Speed-controlled crystallizer - Google Patents

Abstract

The utility model discloses a fast crystallizer of accuse, the utility model relates to a fast crystallizer technical field of accuse, including the crystallizer, the through-hole is seted up to the top surface of crystallizer, the top surface fixed mounting motor of crystallizer, the output shaft fixed mounting puddler of motor, the puddler is located the crystallizer, the upper end of puddler and the output shaft fixed connection of motor, the upper end of puddler passes through bearing fixed connection with the inner wall of through-hole, the lower extreme fixed mounting of crystallizer has the discharging pipe of valve, the discharging pipe communicates with each other with the crystallizer is inside, the lower extreme fixed mounting several supporting leg of crystallizer. The utility model has the advantages of reasonable design, convenient to use can adjust the velocity of flow that gets into the material in the crystallizer, carries out the fast reaction of accuse, makes the interior granule of material variation in size of crystallizer because the action of gravity is hierarchical, from the top down by the thin thickening, has reached and has prepared the inorganic salt product of large granule, improves the purpose of product yield.

Description

Speed-controlled crystallizer

Technical Field

The utility model relates to a fast crystallizer technical field of accuse specifically is a fast crystallizer of accuse.

Background

The device has the defects that the reactor is not suitable for the condition that the granularity and the specific gravity of reaction materials are different, the whole length of the guide cylinder is too long, the forced circulation distance is too long, the materials are layered, the mixing is not uniform, and the reaction effect is not good.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a quick crystallizer of accuse to solve prior art not enough.

In order to achieve the above object, the utility model provides a following technical scheme: comprises a crystallizing tank, a through hole is arranged on the top surface of the crystallizing tank, a motor is fixedly arranged on the top surface of the crystallizing tank, a stirring rod is fixedly arranged on an output shaft of the motor, the stirring rod is positioned in the crystallizing tank, the upper end of the stirring rod is fixedly connected with the output shaft of the motor, the upper end of the stirring rod is fixedly connected with the inner wall of the through hole through a bearing, a discharging pipe with a valve is fixedly arranged at the lower end of the crystallizing tank, the discharging pipe is communicated with the inside of the crystallizing tank, a plurality of supporting legs are fixedly arranged at the lower end of the crystallizing tank, a feeding pipe is fixedly arranged at the upper end of one side of the crystallizing tank, the feeding pipe is communicated with the inside of the crystallizing tank, a flow rate controller is fixedly arranged at the middle part of the feeding pipe, a transverse plate is arranged at the other side of the crystallizing tank, the transverse plate is fixedly connected with the corresponding supporting legs, a heating chamber is arranged above the transverse plate, a Roots compressor is arranged at one side of the heating chamber, the Roots compressor is fixedly communicated with the upper end of the heating chamber through a transverse pipe, the heating chamber passes through L type union coupling with the crystallizer, and roots's compressor's upper end and crystallizer pass through first connecting pipe intercommunication, and roots's compressor's bottom surface passes through riser fixed connection with the top surface of diaphragm, and one side of riser is equipped with the axial-flow pump, and the lower extreme of heating chamber passes through the standpipe with the axial-flow pump and communicates, and the axial-flow pump communicates through the second connecting pipe with the crystallizer.

According to the speed-control crystallizer, the stirring paddles are fixedly arranged on the two sides of the stirring rod and are positioned in the crystallizer, and the stirring paddles on the two sides of the stirring rod are arranged in a staggered mode.

According to the speed-control crystallizer, the lower ends of the supporting legs are fixedly connected with the lower end of the crystallizing tank through the inclined struts.

As above a accuse quick crystallizer, the inlet pipe constitute by first inlet pipe, hose and second inlet pipe, second inlet pipe and first inlet pipe all communicate with the hose, first inlet pipe and crystallizer intercommunication, flow rate controller comprises sleeve, bolt and extrusion head, the sleeve suit is on the hose, the screw is opened to the top at sleeve middle part, the screw communicates with each other with sleeve inside, the inside bolt that is equipped with of screw, the bolt passes through screw-thread fit connection with the screw, the lower extreme fixed mounting extrusion head of bolt, the extrusion head can cooperate with the hose.

According to the speed-control crystallizer, one end of the feeding pipe is fixedly provided with the flowmeter, and the flowmeter is positioned between the flow speed controller and the crystallizing tank.

The utility model has the advantages that: the utility model has the advantages of reasonable design, convenient to use can adjust the velocity of flow that gets into the material in the crystallizer, carries out the fast reaction of accuse, makes the interior granule of material variation in size of crystallizer because the action of gravity is hierarchical, from the top down by the thin thickening, has reached and has prepared the inorganic salt product of large granule, improves the purpose of product yield.

Drawings

In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings required to be used in the description of the embodiments are briefly introduced below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without inventive labor.

Fig. 1 is a schematic view of the overall structure of the present invention; fig. 2 is an enlarged view of the view from the direction a of fig. 1.

Reference numerals: 1-crystallizing tank, 2-through hole, 3-motor, 4-stirring rod, 5-discharging pipe, 6-supporting leg, 7-feeding pipe, 8-flow rate controller, 9-transverse plate, 10-heating chamber, 11-roots compressor, 12-transverse pipe, 13-L type pipe, 14-first connecting pipe, 15-vertical plate, 16-axial flow pump, 17-vertical pipe, 18-second connecting pipe, 19-first feeding pipe, 20-hose, 21-second feeding pipe, 22-sleeve, 23-bolt, 24-extrusion head and 25-screw hole.

Detailed Description

As shown in fig. 1 to 2, the speed-controlling crystallizer specifically disclosed in this embodiment includes a crystallization tank 1, a through hole 2 is formed on the top surface of the crystallization tank 1, a motor 3 is fixedly mounted on the top surface of the crystallization tank 1, a stirring rod 4 is fixedly mounted on an output shaft of the motor 3, the stirring rod 4 is located in the crystallization tank 1, the upper end of the stirring rod 4 is fixedly connected with the output shaft of the motor 3, the upper end of the stirring rod 4 is fixedly connected with the inner wall of the through hole 2 through a bearing, a discharge pipe 5 with a valve is fixedly mounted at the lower end of the crystallization tank 1, the discharge pipe 5 is communicated with the interior of the crystallization tank 1, a plurality of support legs 6 are fixedly mounted at the lower end of the crystallization tank 1, a feed pipe 7 is fixedly mounted at the upper end of one side of the crystallization tank 1, the feed pipe 7 is communicated with the interior of the crystallization tank 1, a flow rate controller 8 is fixedly mounted at the middle of the feed pipe 7, a horizontal plate 9 is disposed at the other side of the crystallization tank 1, and the horizontal plate 9 is fixedly connected with the corresponding support leg 6, the heating chamber 10 is arranged above the transverse plate 9, the roots compressor 11 is arranged on one side of the heating chamber 10, the roots compressor 11 is fixedly communicated with the upper end of the heating chamber 10 through the transverse pipe 12, the heating chamber 10 is connected with the crystallizing tank 1 through the L-shaped pipe 13, the upper end of the roots compressor 11 is communicated with the crystallizing tank 1 through the first connecting pipe 14, the bottom surface of the roots compressor 11 is fixedly connected with the top surface of the transverse plate 9 through the vertical plate 15, the axial flow pump 16 is arranged on one side of the vertical plate 15, the lower end of the heating chamber 10 is communicated with the axial flow pump 16 through the vertical pipe 17, and the axial flow pump 16 is communicated with the crystallizing tank 1 through the second connecting pipe 18. The utility model has the advantages of reasonable design, convenient to use can adjust the velocity of flow that gets into the material in the crystallizer, carries out the fast reaction of accuse, makes the interior granule of material variation in size of crystallizer because the action of gravity is hierarchical, from the top down by the thin thickening, has reached and has prepared the inorganic salt product of large granule, improves the purpose of product yield. When the device is used, materials enter the crystallization tank 1 through the inlet pipe 7, the materials are conveyed into the crystallization tank 1 through the first inlet pipe 19, the hose 20 and the second inlet pipe 21, the extrusion head 24 can be driven to move up and down through the rotating bolt 23, the flow velocity of the materials can be adjusted through the contact area between the extrusion head 24 and the hose 20, and speed control reaction is carried out, so that particles with different sizes of the materials in the crystallization tank are classified under the action of gravity, and become thick from top to bottom, and the purpose of preparing large-particle inorganic salt products and improving the product yield is achieved, meanwhile, the motor 3 works, the output shaft of the motor 3 drives the stirring rod 4 to rotate, so that the materials in the crystallization tank 1 can be stirred, the materials are heated uniformly, crystallization can be facilitated, the crystals are discharged through the discharge pipe 5, the axial flow pump 16 works, mother liquor in the crystallization tank 1 enters the heating chamber 10 through the second connecting pipe 18, the heating chamber 10 heats the mother liquor, the heated mother liquor enters the crystallization tank 1 through the L-shaped pipe 13, the Roots compressor 11 works, steam in the crystallization tank 1 enters the heating chamber 10 through the first connecting pipe 14, steam at the inner end of the heating chamber 10 enters the crystallization tank 1 again, and the mother liquor in the crystallization tank 1 can be crystallized again.

Particularly, this embodiment the equal fixed mounting several stirring rake in both sides of puddler 4, the stirring rake is located crystallizer 1, the stirring rake of puddler 4 both sides is crisscross to be placed. When the device is used, the materials can be stirred conveniently through the stirring paddle, the materials can be heated conveniently, and therefore crystallization can be facilitated.

Specifically, the lower end of the support leg 6 and the lower end of the crystallization tank 1 are fixedly connected through an inclined strut. When using this device, can make supporting leg 6 more firm with being connected of crystallizer 1 through the bracing to can make crystallizer 1 more stable in the course of the work.

Further, the inlet pipe 7 described in this embodiment is composed of a first inlet pipe 19, a hose 20 and a second inlet pipe 21, the second inlet pipe 21 and the first inlet pipe 19 are both communicated with the hose 20, the first inlet pipe 19 is communicated with the crystallization tank 1, the flow rate controller 8 is composed of a sleeve 22, a bolt 23 and an extrusion head 24, the sleeve 22 is sleeved on the hose 20, a screw hole 25 is opened above the middle part of the sleeve 22, the screw hole 25 is communicated with the inside of the sleeve 22, the bolt 23 is arranged inside the screw hole 25, the bolt 23 is connected with the screw hole 25 through thread fit, the extrusion head 24 is fixedly installed at the lower end of the bolt 23, and the extrusion head 24 can be matched with the hose 20. When using this device, the material is carried to crystallizer 1 in through first inlet pipe 19, hose 20 and second inlet pipe 21, can drive extrusion head 24 through rotating bolt 23 and reciprocate, through the size of extrusion head 24 with the area of contact of hose 20, can adjust the size of material velocity of flow.

Furthermore, in the present embodiment, a flow meter is fixedly installed at one end of the feeding pipe 7, and the flow meter is located between the flow rate controller 8 and the crystallization tank 1. When using this device, can measure the material that flows into in crystallizer 1 through the flowmeter, can make this device convenient to use more.

The embodiments of the present invention have been described with reference to the accompanying drawings, but these descriptions should not be construed as limiting the scope of the present invention, and the technical contents not described in detail in the present invention are known in the art.

Claims (5)

1. A speed-controlled crystallizer is characterized in that: comprises a crystallizing tank (1), a through hole (2) is arranged on the top surface of the crystallizing tank (1), a motor (3) is fixedly arranged on the top surface of the crystallizing tank (1), a stirring rod (4) is fixedly arranged on an output shaft of the motor (3), the stirring rod (4) is positioned in the crystallizing tank (1), the upper end of the stirring rod (4) is fixedly connected with the output shaft of the motor (3), the upper end of the stirring rod (4) is fixedly connected with the inner wall of the through hole (2) through a bearing, a discharging pipe (5) with a valve is fixedly arranged at the lower end of the crystallizing tank (1), the discharging pipe (5) is communicated with the inside of the crystallizing tank (1), a plurality of supporting legs (6) are fixedly arranged at the lower end of the crystallizing tank (1), a feeding pipe (7) is fixedly arranged at the upper end of one side of the crystallizing tank (1), the feeding pipe (7) is communicated with the inside of the crystallizing tank (1), a flow rate controller (8) is fixedly arranged at the middle part of the feeding pipe (7), the other side of crystallizer (1) is equipped with diaphragm (9), diaphragm (9) and corresponding supporting leg (6) fixed connection, the top of diaphragm (9) is equipped with heating chamber (10), one side of heating chamber (10) is equipped with roots compressor (11), roots compressor (11) and the upper end of heating chamber (10) are through violently managing (12) fixed intercommunication, heating chamber (10) are connected through L type pipe (13) with crystallizer (1), the upper end of roots compressor (11) and crystallizer (1) are through first connecting pipe (14) intercommunication, the bottom surface of roots compressor (11) and the top surface of diaphragm (9) are through riser (15) fixed connection, one side of riser (15) is equipped with axial-flow pump (16), the lower extreme of heating chamber (10) and axial-flow pump (16) are through standpipe (17) intercommunication, axial-flow pump (16) and crystallizer (1) are through second connecting pipe (18) intercommunication.

2. A rate-controlling crystallizer as defined in claim 1, wherein: the equal fixed mounting several stirring rake in both sides of puddler (4), the stirring rake is located crystallizer (1), the stirring rake of puddler (4) both sides is crisscross to be placed.

3. A rate-controlling crystallizer as defined in claim 1, wherein: the lower end of the supporting leg (6) is fixedly connected with the lower end of the crystallizing tank (1) through an inclined strut.

4. A rate-controlling crystallizer as defined in claim 1, wherein: inlet pipe (7) by first inlet pipe (19), hose (20) and second inlet pipe (21) are constituteed, second inlet pipe (21) and first inlet pipe (19) all communicate with hose (20), first inlet pipe (19) and crystallizer (1) intercommunication, velocity of flow controller (8) are by sleeve (22), bolt (23) and extrusion head (24) are constituteed, sleeve (22) suit is on hose (20), screw (25) are opened to the top at sleeve (22) middle part, screw (25) communicate with each other with sleeve (22) are inside, screw (25) inside is equipped with bolt (23), bolt (23) are connected through screw-thread fit with screw (25), the lower extreme fixed mounting extrusion head (24) of bolt (23), extrusion head (24) can cooperate with hose (20).

5. A rate-controlling crystallizer as defined in claim 1, wherein: one end fixed mounting flowmeter of inlet pipe (7), the flowmeter is located between flow rate controller (8) and crystallizer (1).

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