CN201565294U - Novel MBS reactor group - Google Patents
Novel MBS reactor group Download PDFInfo
- Publication number
- CN201565294U CN201565294U CN2009202566738U CN200920256673U CN201565294U CN 201565294 U CN201565294 U CN 201565294U CN 2009202566738 U CN2009202566738 U CN 2009202566738U CN 200920256673 U CN200920256673 U CN 200920256673U CN 201565294 U CN201565294 U CN 201565294U
- Authority
- CN
- China
- Prior art keywords
- reactor
- reactors
- mbs
- reactor group
- liquid outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A novel MBS reactor group relates to a modifier MBS (copolymer of methyl methacrylate, butadiene and styrol) reactor group. The reactor group comprises a plurality of reactors orderly connected, adjacent reactors are communicated, liquid inlets and liquid outlets are arranged on the reactors, the liquid inlets of all reactors are arranged at the upper parts of the reactors, the liquid outlets are arranged on the lower parts of the reactors, and the liquid outlets of previous stage reactors are in the same height or higher than the liquid inlets of the next stage reactors. The utility model provides a MBS reactor group of simple structure and no requirement of power devices.
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.
The utility model content
The utility model is at above-mentioned defective, and purpose is to provide a kind of simple in structure, MBS reactor group of need not power set.
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, 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.
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.
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 an observation panel 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, 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.
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. novel 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, it is characterized in that, the inlet of each reactor is arranged on reactor top, and 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202566738U CN201565294U (en) | 2009-11-17 | 2009-11-17 | Novel MBS reactor group |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202566738U CN201565294U (en) | 2009-11-17 | 2009-11-17 | Novel MBS reactor group |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201565294U true CN201565294U (en) | 2010-09-01 |
Family
ID=42657574
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202566738U Expired - Fee Related CN201565294U (en) | 2009-11-17 | 2009-11-17 | Novel MBS reactor group |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201565294U (en) |
-
2009
- 2009-11-17 CN CN2009202566738U patent/CN201565294U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101460395A (en) | Micro channel reactor system | |
| CN201880499U (en) | Continuous washing and oil-water separating device | |
| CN101225359B (en) | Marsh gas generating device | |
| CN201565294U (en) | Novel MBS reactor group | |
| CN202717598U (en) | Reactor for preparation of iron oxide red | |
| CN201565297U (en) | Mbs reaction kettle group | |
| CN201162011Y (en) | Methane generating device | |
| CN206853681U (en) | A kind of polycarboxylate water-reducer synthetic molecules targeting homogenizing consersion unit | |
| CN203170303U (en) | Pentachloropyridine synthesis gas intake distributing device | |
| CN201052457Y (en) | Novel inner circulation slurry-bed reactor | |
| CN205127966U (en) | A reation kettle for producing silane | |
| CN210097678U (en) | Stirring tank with fixed gas distributor | |
| CN207324746U (en) | A kind of drawing mechanism of versatic acid synthesis | |
| CN206168428U (en) | Wastewater treatment device | |
| CN204469678U (en) | The stirred tank of uniform feeding | |
| CN202638430U (en) | Bubbling blending device | |
| CN1112234C (en) | Circular tri-phase gas-liquid-solid reactor | |
| CN202717735U (en) | Pressurizing polymerization device for manufacturing gas of polyvinyl acetate | |
| CN205517463U (en) | Automatic batching mediation device | |
| CN216172168U (en) | Novel gas making device | |
| CN202460617U (en) | Tank type reactor | |
| CN204768680U (en) | A reation kettle for producing reduce impurity DAP in carbendazim | |
| CN203508017U (en) | Improved reaction groove | |
| CN201762318U (en) | Jet flow internal circulation fermentation tank | |
| CN202224157U (en) | Ammonia sugar recovering and reflowing device |
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 |