CN209348637U - A kind of interleaving agent continuous production device - Google Patents

A kind of interleaving agent continuous production device Download PDF

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Publication number
CN209348637U
CN209348637U CN201822172970.6U CN201822172970U CN209348637U CN 209348637 U CN209348637 U CN 209348637U CN 201822172970 U CN201822172970 U CN 201822172970U CN 209348637 U CN209348637 U CN 209348637U
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China
Prior art keywords
reactor
pipeline
wall
colloid mill
agitator tank
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Active
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CN201822172970.6U
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Chinese (zh)
Inventor
赵会岩
张志胜
何艳
张玉红
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Shandong Wanshengbo Chemical Co Ltd
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Shandong Wanshengbo Chemical Co Ltd
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Priority to CN201822172970.6U priority Critical patent/CN209348637U/en
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Abstract

The utility model provides a kind of interleaving agent continuous production device, is related to interleaving agent production technical field.In the utility model, reactor (6) is connect with colloid mill (10) pipeline, and colloid mill (10) is connect with agitator tank (14) pipeline;Reactor (6) has inner wall (601) and outer wall (601), has fluid channel between inner wall (601) and outer wall (601);The inside of reactor (6) is equipped with screw rod (5);Pipeline between colloid mill (10) and agitator tank (14) is material pipe (12), and heat exchanger (13) is arranged in the outside of material pipe (12).Compared with prior art, interleaving agent is produced using the utility model, in reactor (6), the extent of reaction reaches 90%, in material pipe (12) transmission process, material specific surface area is big, certain temperature is maintained, reaction can continue to carry out to fully reacting, and material does not stop in reactor (6), continuous production, high production efficiency.

Description

A kind of interleaving agent continuous production device
Technical field
The utility model relates to interleaving agent production technical field, in particular to a kind of interleaving agent continuous production device.
Background technique
Interleaving agent manufacturer mostly uses greatly Batch Process mode to be produced at present, the time required for one kettle of every production Longer, this production method major defect is that production efficiency is low.Substantially process is that raw material is added in reaction kettle, in stirring, is added It under heat condition, is reacted, to fully reacting, after being delivered to grinder grinding, then the stirring of agitated tank is conveyed into finished pot. Since raw material has agglomerating caking phenomenon, fully reacting needs the time longer in reaction kettle;And following temperature is not achieved, Wu Fajin Row reaction, so the residence time is long in reaction kettle, batch production, low efficiency.
Summary of the invention
The utility model provides a kind of interleaving agent continuous production device, solves above-mentioned technical problem.
Specific technical solution is a kind of interleaving agent continuous production device, comprising: motor, speed reducer, fluid pipeline, powder Feeding device, screw rod, reactor, conduction oil outlet, heat conducting oil inlet, first switch valve, colloid mill, pipeline pump, material Pipeline, heat exchanger, agitator tank, second switch valve, blender;Motor and speed reducer circuit connection, speed reducer are connect with reactor, Reactor is connect with colloid mill pipeline, and colloid mill is connect with agitator tank pipeline.Raw material is stirred in reactor inner screw Under, there is heating, quickly reacted, degree of reaction can achieve 90% in a short time;Storeroom will appear agglomeration, by colloid Grinder, agglomeration are grated.
Reactor has inner and outer wall, has fluid channel between inner and outer wall;The inside of reactor is equipped with screw rod, screw rod Fluid pipeline and powder feeding device are equipped with above front end;The front bottom end of reactor is equipped with heat conducting oil inlet, sets above rear end There is conduction oil outlet.It is passed through conduction oil in fluid channel between the inner and outer walls, screw rod and its interior material can be added Heat.The Position Design of conduction oil entrance, lower section go out into top, can make full use of conduction oil bring heat.
First switch valve is mounted on the pipeline between reactor and colloid mill;Pipeline pump is mounted on colloid mill Back.Pipeline pump can provide power for the material in pipeline, guarantee that material has certain flow velocity.
Pipeline between colloid mill and agitator tank is material pipe, and the outside of material pipe is arranged in heat exchanger;Stirring Blender is equipped in tank, stirring pot bottom connects second switch valve.Guarantee that material when entering material pipe, has certain temperature Degree, unreacted raw material can continue to be reacted, and when being delivered to agitator tank, fully reacting after being uniformly mixed, is delivered to Finished pot.
It further, is 2~3mm at a distance from inner wall at the outer most edge of screw rod.It on the one hand is preferably to be heated for material, On the other hand, guarantee that screw rod acts on the shear-mixed of material, make material fast reaction.
Due to using above technical scheme, compared with prior art, the utility model, in reaction kettle, the extent of reaction Reach 90%, in material pipe transmission process, material specific surface area is big, maintains certain temperature, and reaction can continue to carry out To fully reacting, material does not stop in reactor, continuous production, high production efficiency.
Detailed description of the invention
The attached drawing constituted part of this application is used to provide a further understanding of the present invention, the utility model Illustrative embodiments and their description are not constituteed improper limits to the present invention for explaining the utility model.In attached drawing In:
Fig. 1 is a kind of schematic diagram of interleaving agent continuous production device of the utility model.
Wherein: 1, motor, 2, speed reducer, 3, fluid pipeline, 4, powder feeding device, 5, screw rod, 6, reactor, 601, interior Wall, 602, outer wall, 7, conduction oil outlet, 8, heat conducting oil inlet, 9, first switch valve, 10, colloid mill, 11, pipeline pump, 12, material pipe, 13, heat exchanger, 14, agitator tank, 15, second switch valve, 16, blender.
Specific embodiment
For the purpose of this utility model, technical solution and advantage is more clearly understood, below with reference to embodiment and attached Figure, is described in further detail the utility model.Here, the exemplary embodiment and its explanation of the utility model are for solving The utility model is released, but is not intended to limit the scope of the present invention.Here is to retouch in conjunction with attached drawing to the utility model It states:
Such as attached drawing 1, a kind of interleaving agent continuous production device, comprising: motor 1, speed reducer 2, fluid pipeline 3, powder charging Device 4, screw rod 5, reactor 6, conduction oil outlet 7, heat conducting oil inlet 8, first switch valve 9, colloid mill 10, pipeline pump 11, material pipe 12, heat exchanger 13, agitator tank 14, second switch valve 15, blender 16;Motor 1 and 2 circuit connection of speed reducer, Speed reducer 2 is connect with reactor 6, and reactor 6 is connect with 10 pipeline of colloid mill, colloid mill 10 and 14 pipeline of agitator tank Connection.Raw material has heating, is quickly reacted, degree of reaction can achieve 90% in a short time under the stirring of screw rod 5;Material Between will appear agglomeration, by colloid mill 10, agglomeration is grated.
Reactor 6 has inner wall 601 and outer wall 601, has fluid channel between inner wall 601 and outer wall 601;The inside of reactor 6 Equipped with screw rod 5, fluid pipeline 3 and powder feeding device 4 are equipped with above the front end of screw rod 5;The front bottom end of reactor 6 is equipped with and leads Hot oil entrance 8, rear end top are equipped with conduction oil outlet 7.It is passed through conduction oil in fluid channel between inner wall 601 and outer wall 602, Screw rod 5 and its interior material can be heated.
First switch valve 9 is mounted on the pipeline between reactor 6 and colloid mill 10;Pipeline pump 11 is mounted on colloid and grinds The back of grinding machine 10.Pipeline pump 11 can provide power for the material in pipeline, guarantee that material has certain flow velocity.
Pipeline between colloid mill 10 and agitator tank 14 is material pipe 12, and material pipe 12 is arranged in heat exchanger 13 Outside;Blender 16 is equipped in agitator tank 14,14 bottom of agitator tank connects second switch valve 15.Guarantee that material is entering materail tube When road 12, there is certain temperature, unreacted raw material can continue to be reacted, when being delivered to agitator tank 14, fully reacting, After being uniformly mixed, it is delivered to finished pot.
It is 2~3mm at a distance from inner wall 601 at the outer most edge of screw rod 5.It on the one hand is preferably to be heated for material, it is another Aspect guarantees that screw rod 5 acts on the shear-mixed of material, makes material fast reaction.
Conduction oil: in 6 stage of reactor, being first passed through from heat conducting oil inlet 8, preheat to screw rod 5 by embodiment, then will Raw material is added to screw rod 5 from fluid pipeline 3, powder feeding device 4, opens motor 1, and motor 1 drives screw rod by speed reducer 2 5 work;Raw material has heating, is quickly reacted, degree of reaction can achieve 90% in a short time under the stirring of screw rod 5;Material Between will appear agglomeration, open first switch valve 9, material is delivered to colloid mill 10 by reactor 6, grinds caking materials, increases The specific surface area of big material;Material is pumped into agitator tank 14 through material pipe 12 by pipeline pump 11, in the outside of material pipe 12 There is heat exchanger 13 for material heating, be allowed to during transportation, reaction can be carried out continuously to complete reaction;It is delivered to agitator tank 14 When, it is uniformly mixed, then be delivered in finished pot.In entire process units, first switch valve 9 and second switch valve 15 1 Straight in the open state, material does not stop in reactor 6, and reaction is carried out continuously.

Claims (2)

1. a kind of interleaving agent continuous production device, which is characterized in that
It include: motor (1), speed reducer (2), fluid pipeline (3), powder feeding device (4), screw rod (5), reactor (6), thermally conductive Oil export (7), heat conducting oil inlet (8), first switch valve (9), colloid mill (10), pipeline pump (11), material pipe (12), Heat exchanger (13), agitator tank (14), second switch valve (15), blender (16);
Motor (1) and speed reducer (2) circuit connection, speed reducer (2) are connect with reactor (6), reactor (6) and colloid mill (10) pipeline connects, and colloid mill (10) is connect with agitator tank (14) pipeline;
Reactor (6) has inner wall (601) and outer wall (602), has fluid channel between inner wall (601) and outer wall (602);Reactor (6) inside is equipped with screw rod (5), and fluid pipeline (3) and powder feeding device (4) are equipped with above the front end of screw rod (5);Reactor (6) front bottom end is equipped with heat conducting oil inlet (8), is equipped with conduction oil outlet (7) above rear end;
First switch valve (9) is mounted on the pipeline between reactor (6) and colloid mill (10);Pipeline pump (11) is mounted on glue The back of body grinder (10);
Pipeline between colloid mill (10) and agitator tank (14) is material pipe (12), and heat exchanger (13) is arranged in material pipe (12) outside;
Blender (16) are equipped in agitator tank (14), agitator tank (14) bottom connects second switch valve (15).
2. a kind of interleaving agent continuous production device according to claim 1, which is characterized in that at the outer most edge of screw rod (5) Be 2~3mm at a distance from inner wall (601).
CN201822172970.6U 2018-12-24 2018-12-24 A kind of interleaving agent continuous production device Active CN209348637U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822172970.6U CN209348637U (en) 2018-12-24 2018-12-24 A kind of interleaving agent continuous production device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822172970.6U CN209348637U (en) 2018-12-24 2018-12-24 A kind of interleaving agent continuous production device

Publications (1)

Publication Number Publication Date
CN209348637U true CN209348637U (en) 2019-09-06

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822172970.6U Active CN209348637U (en) 2018-12-24 2018-12-24 A kind of interleaving agent continuous production device

Country Status (1)

Country Link
CN (1) CN209348637U (en)

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