CN217773265U - Organic silicon liquid distillation device - Google Patents

Abstract

The utility model discloses an organosilicon liquid distillation plant, the stirring space has been seted up to the inside of agitator tank, and the top and the bottom in stirring space respectively with inlet pipe and the fixed intercommunication of discharge gate, the inside in stirring space is formed by the crisscross intercommunication in space of two kinds of variation in size, the top of agitator tank is provided with the stirring subassembly, and the stirring subassembly passes the stirring space and lie in the axis in stirring space, the top fixed mounting of agitator tank has the pressure components, and the inside intercommunication of pressure components and agitator tank, has passed through in the stirring, has set up two different size spaces, and the stirring direction in two spaces is different, and cooperates the intercommunication between two spaces, utilizes the effect of pressure intensity, makes mutual extrusion collision between the organosilicon liquid to the mixing speed has been accelerated.

Description

Organic silicon liquid distillation device

Technical Field

The utility model belongs to the technical field of organosilicon production is relevant, concretely relates to organosilicon liquid distillation plant.

Background

The service life of the organic silicon in a natural environment can reach dozens of years, the organic silicon has excellent thermal stability and various resistance performances, so that products made of organic silicon liquid are continuously researched and developed, the organic silicon needs to be heated and distilled in the production process, and the organic silicon needs to be fully stirred in the distillation process, so that the organic silicon can be uniformly heated in the distillation process.

Patent publication No. CN 214913453U's an organic silicon liquid distillation plant, the last scraper blade rotation axis of above-mentioned device can be cleared up remaining liquid on the device body inner wall, and have certain stirring effect to organic silicon liquid, improve distillation efficiency, above-mentioned device has only carried out simple stirring processing to organic silicon liquid, only can not effectual mixed liquid through simple stirring action, thereby make the acceleration of speed comparatively unobvious, for this reason, we provide an organic silicon liquid distillation plant.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide an organosilicon liquid distillation plant to the problem through simple and easy stirring processing that proposes in solving above-mentioned background art, can't effectively improve mixing rate.

In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides an organosilicon liquid distillation plant, includes agitator tank, support, inlet pipe and discharge gate, the bottom fixedly connected with support of agitator tank, and the agitator tank passes through the support and is connected with ground, the top and the bottom of agitator tank are connected with inlet pipe and discharge gate respectively, the stirring space has been seted up to the inside of agitator tank, and the top and the bottom in stirring space communicate with inlet pipe and discharge gate respectively, the inside in stirring space is formed by the crisscross intercommunication in space of two kinds of variation in size for increase the mutual extrusion force of organosilicon liquid when two spaces of difference in size, be provided with on the agitator tank and be used for going on the horizontal direction and the vertical direction stirring to the organosilicon liquid that gets into the agitator tank inside stirring subassembly, and the stirring subassembly passes the stirring space and lie in the axis in stirring space, be provided with on the agitator tank and be used for carrying out the pressurization to agitator tank inside and accelerate the pressurization subassembly that organosilicon liquid flows, and the inside intercommunication of the partial subassembly of pressurization subassembly and agitator tank.

Preferably, the space of two kinds of equidimensions in stirred space includes teeter chamber and mixing chamber, the teeter chamber is different with the space size of mixing chamber, and the space of teeter chamber is greater than the mixing chamber, teeter chamber and mixing chamber set up and communicate each other in a staggered way, and the teeter chamber occupies agitator tank inner space's top and bottom, the axis coincidence of teeter chamber and mixing chamber.

Preferably, the stirring subassembly includes servo motor, servo motor fixed mounting is at the top of agitator tank, and servo motor's output shaft penetrates the inside fixedly connected with (mixing) shaft of agitator tank, the (mixing) shaft passes teeter chamber and mixing chamber to coincide with the axis coincidence of teeter chamber and mixing chamber, equidistant fixed mounting has the puddler in the outside that the (mixing) shaft is located teeter chamber portion, the outside fixed mounting that the (mixing) shaft is located mixing chamber portion has the arc, and fixed mounting has vertical board on the arc.

Preferably, the arc-shaped plate is in a shape of a continuous wavy curved surface.

Preferably, the pressurizing assembly comprises an air cylinder, the air cylinder is fixedly installed at the top of the stirring tank, the bottom of the air cylinder is fixedly communicated with the stirring chamber, an electric push rod is fixedly installed at the top of the air cylinder, the output end of the electric push rod is inserted into the inner part of the air cylinder to move, an air hole is formed in one side of the air cylinder, and the air hole and the position of the air cylinder communicated with the stirring tank are provided with a one-way valve.

Preferably, the one end fixed mounting that the puddler is close to the teeter chamber has the scraper blade, the scraper blade is the slope setting, and the length of scraper blade is less than the height of teeter chamber.

Compared with the prior art, the utility model provides an organosilicon liquid distillation plant possesses following beneficial effect:

1. the utility model discloses a when the stirring, set up the space of two variation in size, organosilicon liquid carries out the stirring on the horizontal plane in the inside of teeter chamber, and electric putter's output is piston motion in the inside of inflator, can increase the inside pressure of teeter chamber gradually, thereby extrude organosilicon liquid and get into the inside of teeter chamber, after organosilicon liquid gets into the inside of teeter chamber, arc and vertical board can stir on the organosilicon liquid carries out vertical plane, and the stirring direction in two spaces is different, carry out abundant mixing, improve mixing efficiency, and cooperate the intercommunication between two spaces, utilize the effect of pressure, make mutual extrusion collision between the organosilicon liquid, thereby the mixing speed has been accelerated.

2. The utility model discloses a set up the scraper blade on the puddler, when the puddler passes through servo motor and drives (mixing) shaft and puddler pivoted, can make the scraper blade rotate in the inside of teeter chamber, the inner wall laminating of scraper blade and teeter chamber to make the scraper blade clear up the inner wall of teeter chamber, thereby avoided the adhesion of organosilicon liquid on the teeter chamber.

Drawings

The accompanying drawings are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention, and together with the description, do not constitute a limitation of the invention, in which:

FIG. 1 is a schematic structural view of an organosilicon liquid distillation apparatus provided by the present invention;

FIG. 2 is a schematic view of a front cross-sectional structure of the stirring tank of the present invention;

fig. 3 is a schematic view of a partial cross-sectional structure of a pressurizing assembly according to the present invention;

FIG. 4 is a schematic view of the installation position of the stirring rod and the arc plate according to the present invention;

in the figure: 1. a stirring tank; 2. a support; 3. a feed pipe; 4. stirring the space; 401. a stirring chamber; 402. a mixing chamber; 5. a stirring assembly; 501. a servo motor; 502. a stirring shaft; 503. a stirring rod; 504. an arc-shaped plate; 505. a vertical plate; 6. a pressurizing assembly; 601. an air cylinder; 602. an electric push rod; 603. air holes; 604. a one-way valve; 7. a squeegee; 8. and (4) a discharge port.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the 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.

Please refer to fig. 1-4, the utility model provides an organosilicon liquid distillation plant, including agitator tank 1, support 2, inlet pipe 3 and discharge gate 8, agitator tank 1's bottom fixedly connected with support 2, and agitator tank 1 is connected with ground through support 2, and agitator tank 1's top and bottom are connected with inlet pipe 3 and discharge gate 8 respectively, and the material gets into the inside with agitator tank 1 from inlet pipe 3, through a series of operations, leaves the inside of agitator tank 1 from discharge gate 8.

Further, stirred tank 1's inside has been seted up and has been stirred space 4, stirred space 4 includes teeter chamber 401 and mixing chamber 402, teeter chamber 401 and mixing chamber 402's space variation in size, and teeter chamber 401's space is greater than mixing chamber 402, teeter chamber 401 and mixing chamber 402 crisscross setting and intercommunication each other, teeter chamber 401 and mixing chamber 402's axis coincidence, teeter chamber 401 occupies 1 inner space's of stirred tank top and bottom and respectively with inlet pipe 3 and 8 fixed intercommunications of discharge gate.

Further, the top of agitator tank 1 is provided with stirring subassembly 5, and stirring subassembly 5 passes stirring space 4 and is located the axis of stirring space 4, stirring subassembly 5 includes servo motor 501, servo motor 501 fixed mounting is at the top of agitator tank 1, and servo motor 501's output shaft penetrates the inside fixedly connected with (mixing) shaft 502 of agitator tank 1, (mixing) shaft 502 passes agitator chamber 401 and mixing chamber 402, and coincide with the axis of agitator chamber 401 and mixing chamber 402, stirring shaft 502 is located the equidistant fixed mounting in the outside of agitator chamber 401 portion has puddler 503, the one end fixed mounting that puddler 503 is close to agitator chamber 401 has scraper blade 7, scraper blade 7 is the slope setting, and the length of scraper blade 7 is less than the height of agitator chamber 401, stirring shaft 502 is located the outside fixed mounting of mixing chamber 402 portion has arc 504, and fixed mounting has vertical board 505 on the arc 504, the outside shape of arc 504 is the curve of two symmetries, and the curve is.

Further, the top fixed mounting of agitator tank 1 has pressurization subassembly 6, and the inside intercommunication of pressurization subassembly 6 and agitator tank 1, pressurization subassembly 6 includes inflator 601, inflator 601 fixed mounting is at the top of agitator tank 1, and the bottom and the fixed intercommunication of teeter chamber 401 of inflator 601, the top fixed mounting of inflator 601 has electric putter 602, and the piston motion is made to electric putter 602's output shaft insert the inside of inflator 601, gas pocket 603 is seted up to one side of inflator 601, and the position of gas pocket 603 and inflator 601 and agitator tank 1 intercommunication all is provided with check valve 604.

The working principle is as follows:

in the scheme, when organosilicon liquid (the organosilicon liquid is organosilicon liquid which is not fully stirred after being mixed) enters the interior of the stirring tank 1 from the feeding pipe 3, the organosilicon liquid firstly enters the interior of the stirring chamber 401, at the moment, the servo motor 501 starts to work, the output shaft of the servo motor 501 drives the stirring shaft 502 to rotate, so that the stirring rod 503 on the stirring shaft 502 fully stirs the organosilicon liquid, the organosilicon liquid can be fully stirred on a horizontal plane, in the stirring process, the output shaft of the electric push rod 602 performs piston motion in the interior of the air cylinder 601, so that the air cylinder 601 constantly pressurizes the interior of the stirring tank 1, and the organosilicon liquid stirred in the interior of the stirring chamber 401 enters the interior of the mixing chamber 402 under the action of pressure;

when the organic silicon liquid is in the mixing chamber 402, the organic silicon liquid moves up and down along with the arc-shaped plate 504, and the organic silicon liquid can be vertically stirred by matching with the stirring of the vertical plate 505, so that the mixing speed of material transportation is accelerated;

this scheme has been through when the stirring, has set up two spaces of variation in size, and the stirring direction in two spaces is different, and cooperates the intercommunication between two spaces, utilizes the effect of pressure intensity of pressure, makes mutual extrusion collision between the organosilicon liquid to the mixing speed has been accelerated.

Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims (6)

1. The utility model provides an organosilicon liquid distillation plant, includes agitator tank (1), support (2), inlet pipe (3) and discharge gate (8), the bottom fixedly connected with support (2) of agitator tank (1), and agitator tank (1) is connected with ground through support (2), the top and the bottom of agitator tank (1) are connected with inlet pipe (3) and discharge gate (8) respectively, its characterized in that: stirring space (4) have been seted up to the inside of agitator tank (1), and the top and the bottom in stirring space (4) communicate with inlet pipe (3) and discharge gate (8) respectively, the inside of stirring space (4) is formed by the crisscross intercommunication in two kinds of spaces of variation in size for increase the mutual extrusion force of organosilicon liquid when two spaces of variation in size, be provided with on agitator tank (1) and be used for going on stirring subassembly (5) in horizontal direction and vertical direction to the inside organosilicon liquid that gets into agitator tank (1), and on stirring subassembly (5) passed stirring space (4) and lie in the axis of stirring space (4), be provided with on agitator tank (1) and be used for carrying out the pressure boost to agitator tank (1) inside and accelerate pressurization subassembly (6) that organosilicon liquid flows, and the inside intercommunication of partial subassembly and agitator tank (1) of pressurization subassembly (6).

2. The silicone liquid distillation apparatus as set forth in claim 1 wherein: the space of two kinds of equidimensions of teeter chamber (4) includes teeter chamber (401) and mixing chamber (402), teeter chamber (401) and the space variation in size of mixing chamber (402), and the space of teeter chamber (401) is greater than mixing chamber (402), teeter chamber (401) and mixing chamber (402) crisscross setting and intercommunication each other, and teeter chamber (401) occupy agitator tank (1) inner space's top and bottom, the axis coincidence of teeter chamber (401) and mixing chamber (402).

3. A silicone fluid distillation apparatus according to claim 2, wherein: stirring subassembly (5) includes servo motor (501), servo motor (501) fixed mounting is at the top of agitator tank (1), and the output shaft of servo motor (501) penetrates inside fixedly connected with (mixing) shaft (502) of agitator tank (1), mixing shaft (502) pass agitator chamber (401) and mixing chamber (402) to coincide with the axis of agitator chamber (401) and mixing chamber (402), equal interval fixed mounting in the outside that (mixing) shaft (502) are located agitator chamber (401) part has puddler (503), outside fixed mounting that (mixing) shaft (502) are located mixing chamber (402) part has arc (504), and fixed mounting has vertical board (505) on arc (504).

4. A silicone fluid distillation apparatus according to claim 3, wherein: the arc-shaped plate (504) is in the shape of a continuous wavy curved surface.

5. A silicone fluid distillation apparatus according to claim 2, wherein: pressurizing assembly (6) includes inflator (601), inflator (601) fixed mounting is at the top of agitator tank (1), and the bottom and the fixed intercommunication of teeter chamber (401) of inflator (601), the top fixed mounting of inflator (601) has electric putter (602), and the inside of the output of electric putter (602) inserted inflator (601) is the piston motion, gas pocket (603) are seted up to one side of inflator (601), and gas pocket (603) and the position of inflator (601) and agitator tank (1) intercommunication all are provided with check valve (604).

6. A silicone liquid distillation apparatus according to claim 3, wherein: one end fixed mounting that puddler (503) are close to teeter chamber (401) has scraper blade (7), scraper blade (7) are the slope setting, and the length of scraper blade (7) is less than the height of teeter chamber (401).

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