CN204320252U - A kind of reactor feed arrangement - Google Patents
A kind of reactor feed arrangement Download PDFInfo
- Publication number
- CN204320252U CN204320252U CN201420805464.5U CN201420805464U CN204320252U CN 204320252 U CN204320252 U CN 204320252U CN 201420805464 U CN201420805464 U CN 201420805464U CN 204320252 U CN204320252 U CN 204320252U
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- CN
- China
- Prior art keywords
- isocon
- feed pipe
- reactor
- current divider
- kettle
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Abstract
The utility model relates to reactor technical field, particularly relate to a kind of reactor feed arrangement, it comprises kettle, described kettle top is provided with exhaust outlet and charging aperture, autoclave body bottom is provided with heater and discharging opening, this feed arrangement comprises feed pipe, current divider and isocon, feed pipe is set in charging aperture, current divider is hollow-core construction, it is arranged on upper end in kettle, splitter overhead is provided with point inflow entrance be connected with feed pipe, shunt base is provided with the shunting that two or more is connected with isocon and exports, isocon extends to autoclave body bottom, feed opening is provided with bottom isocon, isocon lower end is provided with two or more spray orifice, spray orifice is uniformly distributed circumferentially, feed pipe is provided with flow control valve.The utility model eliminates the agitating device in existing reactor, through isocon conveying, raw material is delivered to autoclave body bottom reaction again after utilizing current divider to shunt, and sprayed by heating devices heat boiling, bubbling and spray orifice, raw material is mixed more fully evenly.
Description
Technical field
The utility model relates to reactor technical field, particularly relates to a kind of reactor feed arrangement.
Technical background
Reactor is the container having physics or chemical reaction, existing reactor general structure all comprises kettle, exhaust outlet, charging aperture, discharging opening, agitating device and heater, and heater is all generally by arranging chuck or carry out heat exchange by outer circulation outside kettle wall, main mode of heating has electrical heating, hot water heating, conduction oil circulating-heating, Far-infrared Heating, outer (interior) coil pipe heating etc.; For low boiling reaction system, be not to be provided with agitating device, agitating device can cause the increase of cost.In addition, the existing reactor for liquid type reaction, general is all arrange a charging aperture in kettle upper end and fed intake by a feed pipe, such feeding mode makes the liquid charging stock of a large amount of column concentrate instantaneously to fall and contact with the principal goods material in reactor, there will be phenomenons such as reacting uneven and overreact, directly have influence on the quality of product, especially for the material of viscosity and the reactor of large volume, this drawback is more outstanding.
Summary of the invention
The purpose of this utility model is for the deficiencies in the prior art, a kind of charging is provided evenly reactor feed arrangement.
For achieving the above object, the utility model is by the following technical solutions:
A kind of reactor feed arrangement, it comprises kettle, described kettle top is provided with exhaust outlet and charging aperture, described autoclave body bottom is provided with heater and discharging opening, this feed arrangement comprises feed pipe, current divider and isocon, described feed pipe is set in charging aperture, described current divider is hollow-core construction, it is arranged on upper end in kettle, described splitter overhead is provided with point inflow entrance be connected with feed pipe, described shunt base is provided with the shunting that two or more is connected with isocon and exports, and described isocon extends to autoclave body bottom.
Be provided with feed opening bottom described isocon, isocon lower end is provided with two or more spray orifice.
Described spray orifice is uniformly distributed circumferentially.
Described feed pipe is provided with flow control valve, is convenient to control inlet amount.
The utility model adopts above structure, described splitter overhead is provided with point inflow entrance be connected with feed pipe, described shunt base is provided with the shunting that two or more is connected with isocon and exports, after liquid charging stock is entered from feed pipe, first shunt through current divider, recycling two or more isocon extends to autoclave body bottom and carries out blanking, make blanking more even, seethed with excitement by heating devices heat, bubbling, raw material is fully mixed in reactant liquor, dissolve, homogeneous reaction, thus avoid the problems such as the uneven and overreact of the reaction that causes because charging is uneven, simultaneously, feed opening is provided with bottom described isocon, isocon lower end is provided with two or more spray orifice, this design makes feed pipe blanking more quick, and raw material sprays into bottom reactor by spray orifice, spray produce reflection that radial load obtains reactor wall raw material can be made to mix more fully evenly.The utility model is reasonable in design, structure is simple, eliminate the agitating device in existing reactor, through isocon conveying, raw material is delivered to autoclave body bottom reaction again after utilizing current divider to shunt, and sprayed by heating devices heat boiling, bubbling and spray orifice, raw material is mixed more fully evenly, thus improve reaction speed, improve reaction efficiency and product quality.
Accompanying drawing explanation
Now by reference to the accompanying drawings the utility model is further elaborated:
Fig. 1 is the utility model reactor feed arrangement structural representation.
Detailed description of the invention
As shown in Figure 1, the utility model comprises kettle 1, described kettle 1 top is provided with exhaust outlet 2 and charging aperture 3, heater (being mark in figure) and discharging opening 4 is provided with bottom described kettle 1, this feed arrangement 5 comprises feed pipe 51, current divider 52 and isocon 53, described feed pipe 51 is set in charging aperture 3, described current divider 52 is hollow-core construction, it is arranged on upper end in kettle 1, described current divider 52 top is provided with point inflow entrance be connected with feed pipe 51, be provided with the shunting that two or more is connected with isocon 53 bottom described current divider 52 to export, described isocon 53 extends to bottom kettle 1.
Be provided with feed opening 531 bottom described isocon 53, isocon 53 lower end is provided with two or more spray orifice 532.
Described spray orifice 532 is uniformly distributed circumferentially.
Described feed pipe 51 is provided with flow control valve 6, is convenient to control inlet amount.
The utility model adopts above structure, described current divider 52 top is provided with point inflow entrance be connected with feed pipe 51, be provided with the shunting that two or more is connected with isocon 53 bottom described current divider 52 to export, after liquid charging stock is entered from feed pipe 51, first shunt through current divider 52, recycling two or more isocon 53 extends to bottom kettle 1 and carries out blanking, make blanking more even, seethed with excitement by heating devices heat, bubbling, raw material is fully mixed in reactant liquor, dissolve, homogeneous reaction, thus avoid the problems such as the uneven and overreact of the reaction that causes because charging is uneven, simultaneously, feed opening 531 is provided with bottom described isocon 53, isocon 53 lower end is provided with two or more spray orifice 532, this design makes feed pipe blanking more quick, and raw material sprays into bottom reactor by spray orifice 532, spray produce reflection that radial load obtains reactor wall raw material can be made to mix more fully evenly.The utility model is reasonable in design, structure is simple, eliminate the agitating device in existing reactor, through isocon conveying, raw material is delivered to autoclave body bottom reaction again after utilizing current divider to shunt, and sprayed by heating devices heat boiling, bubbling and spray orifice, raw material is mixed more fully evenly, thus improve reaction speed, improve reaction efficiency and product quality.
More than describe and should not have any restriction to protection domain of the present utility model.
Claims (4)
1. a reactor feed arrangement, comprise kettle, described kettle top is provided with exhaust outlet and charging aperture, described autoclave body bottom is provided with heater and discharging opening, it is characterized in that: this feed arrangement comprises feed pipe, current divider and isocon, described feed pipe is set in charging aperture, described current divider is hollow-core construction, it is arranged on upper end in kettle, described splitter overhead is provided with point inflow entrance be connected with feed pipe, described shunt base is provided with the shunting that two or more is connected with isocon and exports, and described isocon extends to autoclave body bottom.
2. a kind of reactor feed arrangement according to claim 1, it is characterized in that: be provided with feed opening bottom described isocon, isocon lower end is provided with two or more spray orifice.
3. a kind of reactor feed arrangement according to claim 2, is characterized in that: described spray orifice is uniformly distributed circumferentially.
4. a kind of reactor feed arrangement according to claim 1, is characterized in that: described feed pipe is provided with flow control valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420805464.5U CN204320252U (en) | 2014-12-17 | 2014-12-17 | A kind of reactor feed arrangement |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420805464.5U CN204320252U (en) | 2014-12-17 | 2014-12-17 | A kind of reactor feed arrangement |
Publications (1)
Publication Number | Publication Date |
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CN204320252U true CN204320252U (en) | 2015-05-13 |
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CN201420805464.5U Expired - Fee Related CN204320252U (en) | 2014-12-17 | 2014-12-17 | A kind of reactor feed arrangement |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104984695A (en) * | 2015-06-16 | 2015-10-21 | 镇江港和新型建材有限公司 | Liquid-phase reactor |
CN104984694A (en) * | 2015-06-16 | 2015-10-21 | 镇江港和新型建材有限公司 | Liquid-liquid mixing device |
CN107824154A (en) * | 2017-12-01 | 2018-03-23 | 成都欧林生物科技股份有限公司 | A kind of reactor reaction vessel apparatus for feeding |
CN107961740A (en) * | 2017-12-01 | 2018-04-27 | 成都欧林生物科技股份有限公司 | A kind of feeder apparatus for adjusting reaction vessel charging |
-
2014
- 2014-12-17 CN CN201420805464.5U patent/CN204320252U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104984695A (en) * | 2015-06-16 | 2015-10-21 | 镇江港和新型建材有限公司 | Liquid-phase reactor |
CN104984694A (en) * | 2015-06-16 | 2015-10-21 | 镇江港和新型建材有限公司 | Liquid-liquid mixing device |
CN107824154A (en) * | 2017-12-01 | 2018-03-23 | 成都欧林生物科技股份有限公司 | A kind of reactor reaction vessel apparatus for feeding |
CN107961740A (en) * | 2017-12-01 | 2018-04-27 | 成都欧林生物科技股份有限公司 | A kind of feeder apparatus for adjusting reaction vessel charging |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150513 Termination date: 20161217 |