CN201565297U - Mbs reaction kettle group - Google Patents
Mbs reaction kettle group Download PDFInfo
- Publication number
- CN201565297U CN201565297U CN2009202566719U CN200920256671U CN201565297U CN 201565297 U CN201565297 U CN 201565297U CN 2009202566719 U CN2009202566719 U CN 2009202566719U CN 200920256671 U CN200920256671 U CN 200920256671U CN 201565297 U CN201565297 U CN 201565297U
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- reactor
- reaction kettle
- mbs
- reaction
- liquid outlet
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Abstract
The utility model relates to an MBS reaction kettle group, in particular to an MBS reaction kettle group of modifying agent, which comprises a plurality of reaction kettles that are sequentially connected with one another, and the adjacent reaction kettles are communicated with each other; each reaction kettle is provided with a liquid inlet and a liquid outlet and internally provided with a stirring device; the liquid inlets of all the reaction kettles are arranged at the upper parts of the reaction kettles, and liquid outlets are arranged at the lower parts thereof; the liquid outlet of a forestage reaction kettle is level to or higher than the liquid inlet of a post-stage reaction kettle; and the stirring device comprises a stirring shaft and a turbine stirring paddle arranged on the stirring shaft. The MBS reaction kettle group has simple structure, needs no power device and leads all the materials to be fully mixed.
Description
Technical field
The utility model relates to a kind of reaction group, especially designs a kind of MBS reactor group of modifier.
Background technology
MBS is a kind of important modification agent in the chemical industry, has good chemical property, in the production process of MBS, will be according to the some reactors of real reaction condition setting, and be communicated with between each adjacent reaction still, the inlet of each present reactor and the top that liquid outlet all is arranged on reactor, in the time of in the reactant of prime reactor need being sent into back order reaction still, need utilize pump or other power set that it is sent in the order reaction still of back, not only increased energy resource consumption, and the structure that makes reactor becomes complicated, the increase floor space.
Simultaneously in the MBS production process, the uniformity coefficient that mixes between the extent of reaction of material in reactor, each material all is the key factor that influences the MBS quality, wherein the shape of the agitating device in the reactor, particularly paddle is the key factor that determines the material reaction degree, mixes degree; Existing paddle is shaped as flat oar, and material can only flow along a direction in course of reaction, can not mix fully between each material, causes reaction not exclusively, influences the quality of MBS.
The utility model content
The utility model is at above-mentioned defective, purpose be to provide a kind of simple in structure, need not power set and can make the well-mixed MBS reactor of each material group.
The technical solution of the utility model is: the utility model comprises a plurality of reactors that connect successively, the adjacent reaction still is communicated with, offer inlet and liquid outlet on the reactor, be provided with agitating device in the reactor, the inlet of each reactor is arranged on reactor top, liquid outlet is arranged on the reactor bottom, the liquid outlet of prime reactor put down in or be higher than the inlet of back order reaction still, agitating device comprises shaft and is arranged on turbine type paddle on the shaft.
The utility model has changed the set-up mode of original MBS reactor group inlet and liquid outlet, its liquid outlet is arranged on the reactor bottom, and be provided with liquid valve, when reactant the prime reaction kettle for reaction fully after, the liquid valve of liquid outlet is opened, reactant flows out from liquid outlet, and by in the order reaction still after afterwards the inlet of order reaction still flows to, wherein the inlet of back order reaction still is arranged on reactor top, the purpose of offering like this makes reactant can flow in the order reaction still of back by natural the past order reaction still under the effect of gravity, and do not need to increase power set, and reactor can not flow out from the order reaction still of back, in order to increase various additives, be provided with at the top of each reactor and add mouth, simultaneously for energy Real Time Observation reporting situations to the reaction kettle for reaction thing according to each situation needs, the spy is provided with observation panel on the top of each reactor, with can be according to the observation to the result makes relevant the adjustment timely so that entire reaction can be smoothly, carry out normally, guarantee the quality of MBS.
The utility model adopts the turbine type paddle, because the structure of turbine type paddle, make each material in reactor, can collide mutually, contact from all directions, make each material in the space, contact fully, merge, each mixing of materials is even, guarantee the completeness of reaction, to guarantee the MBS Products Quality.
Description of drawings
Fig. 1 is a structural representation of the present utility model
1 is that reactor, 2 is that inlet, 3 is that liquid outlet, 4 is that observation panel, 6 is that shaft, 7 is paddle for adding mouth, 5 among the figure.
The specific embodiment
The utility model comprises a plurality of reactors 1 that connect successively, adjacent reaction still 1 is communicated with, offer inlet 2 and liquid outlet 3 on the reactor 1, be provided with agitating device in the reactor 1, the inlet 2 of each reactor 1 is arranged on reactor 1 top, liquid outlet 3 is arranged on reactor 1 bottom, the liquid outlet of prime reactor 13 flat in or be higher than the inlet 2 of back order reaction still 1, agitating device comprises shaft 6 and is arranged on turbine type paddle 7 on the shaft 6.
Further, the utility model is provided with at the top of reactor 1 and adds mouthfuls 4, offers observation panel 5 on the top of reactor 1 under oblique.
The course of work of the present utility model is: do not offer inlet 2 in the first order reactor 1 of the present utility model, various reactants enter the reactor 1 from adding mouth 4, when reactor 1 reacts in first order reactor 1, close the liquid valve of liquid outlet 3 in the first order reactor 1, by observation panel 5 observing response thing response situation, after reacting completely, open liquid valve simultaneously, reactant flows out from liquid outlet 3, and flows in the second level reactor 1 by the inlet 2 of second level reactor 1; Repeat said process, just can realize in the MBS preparation in the work of reactor in 1 stage.
By the above course of work, the utility model is compared traditional MBS relatively, cancelled the pump equal power device, when energy savings consumes, also simplified simultaneously MBS reactor group structure, reduce operating personnel's workload and reduced breakdown rate, improved economic benefit.
Claims (1)
1.MBS reactor group, comprise a plurality of reactors that connect successively, the adjacent reaction still is communicated with, offer inlet and liquid outlet on the reactor, be provided with agitating device in the reactor, it is characterized in that, the inlet of each reactor is arranged on reactor top, liquid outlet is arranged on the reactor bottom, the liquid outlet of prime reactor put down in or be higher than the inlet of back order reaction still, agitating device comprises shaft and is arranged on turbine type paddle on the shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202566719U CN201565297U (en) | 2009-11-17 | 2009-11-17 | Mbs reaction kettle group |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202566719U CN201565297U (en) | 2009-11-17 | 2009-11-17 | Mbs reaction kettle group |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201565297U true CN201565297U (en) | 2010-09-01 |
Family
ID=42657577
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202566719U Expired - Fee Related CN201565297U (en) | 2009-11-17 | 2009-11-17 | Mbs reaction kettle group |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201565297U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537435A (en) * | 2016-06-24 | 2018-01-05 | 湖南力健机械有限公司 | A kind of Assembled rotary continuously cracks automatically and carbonizing apparatus |
-
2009
- 2009-11-17 CN CN2009202566719U patent/CN201565297U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537435A (en) * | 2016-06-24 | 2018-01-05 | 湖南力健机械有限公司 | A kind of Assembled rotary continuously cracks automatically and carbonizing apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100901 Termination date: 20101117 |