CN202366684U - Continuous ethyl hexanoate esterification reaction kettle - Google Patents
Continuous ethyl hexanoate esterification reaction kettle Download PDFInfo
- Publication number
- CN202366684U CN202366684U CN2011205536731U CN201120553673U CN202366684U CN 202366684 U CN202366684 U CN 202366684U CN 2011205536731 U CN2011205536731 U CN 2011205536731U CN 201120553673 U CN201120553673 U CN 201120553673U CN 202366684 U CN202366684 U CN 202366684U
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- esterification
- kettle
- reaction
- esterifying kettle
- ethyl hexanoate
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- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
The utility model discloses a continuous ethyl hexanoate esterification reaction kettle, which comprises an esterification kettle, wherein the right upper end of the esterification kettle is provided with a discharge port, the left lower end of the esterification kettle is provided with a feeding port, the left upper end of the esterification kettle is provided with a heat conduction oil outlet, and the right lower end of the esterification kettle is provided with a heat conduction oil inlet. The continuous ethyl hexanoate esterification kettle is characterized in that a raw material mixing tank and a metering pump are also arranged outside the esterification kettle, a stirring device is arranged in the raw material mixing tank, and an outlet of the metering pump is communicated with the feeding port of the esterification kettle; a reaction elbow is arranged in the esterification kettle, and two ends of the reaction elbow are respectively connected with the feeding port and the discharging port. According to the continuous ethyl hexanoate esterification reaction kettle, mixed raw materials in the raw material mixing tank are continuously and accurately pumped into the esterification kettle by the metering pump, the reaction materials fully contact and react in the stainless steel reaction elbow, not only can the esterification kettle be prevented from being corroded by an acid catalyst and the like, but also continuous, stable and automatic esterification reaction is realized, and thus the esterification efficiency is greatly improved.
Description
Technical field
The utility model relates to a kind of esterifying kettle, is specifically related to a kind of ethyl hexanoate continuous esterification still.
Background technology
At present; The preparation method of tradition ethyl hexanoate adopts caproic acid and ethanol under heating condition, directly to carry out esterification mostly; Charging aperture is arranged on their mostly adopt, down the batch (-type) reaction kettle of the esterification of discharging opening arranged; Efficient is very low, can not realize continuous and automatic large-scale production, haves much room for improvement to be the continous way reaction kettle of the esterification.
In order to solve above-mentioned deficiency of the prior art, the utility model provides a kind of new solution.
The utility model content
The technical problem that the utility model will solve is: be directed to the deficiency of prior art, provide a kind of in esterifying kettle, be provided with the stainless steel reaction bend pipe continuously, the ethyl hexanoate continuous esterification still of stablizing, react completely, carrying out automatically.
For reaching the foregoing invention purpose; The technical scheme that the utility model adopted is: a kind of ethyl hexanoate continuous esterification still is provided; Comprise esterifying kettle, the upper right side of said esterifying kettle is provided with discharging opening, and the left lower end of esterifying kettle is provided with charging aperture; The left upper end of esterifying kettle is provided with the conduction oil outlet, and the bottom righthand side of esterifying kettle is provided with heat conductive oil inlet; The esterifying kettle upper end is provided with thermometer; The outer wall of esterifying kettle is provided with heat-insulation layer; It is characterized in that: the esterifying kettle outside also is provided with feed proportioning jar and measuring pump; Said feed proportioning jar is provided with feed proportioning jar charging aperture, is provided with agitating device in the feed proportioning jar, and said metering delivery side of pump is communicated with the charging aperture of esterifying kettle; Also be provided with the reaction bend pipe in the esterifying kettle, the two ends of said reaction bend pipe are connected with discharging opening with charging aperture respectively.
Preferably, said measuring pump is a stainless steel with the material of reaction bend pipe.
In sum; This practical ethyl hexanoate continuous esterification still that provides accurately pumps in the esterifying kettle caproic acid in the feed proportioning jar, ethanol and catalyst mix raw material through using the stainless steel measuring pump continuously; Reaction mass fully contacts in the stainless steel reaction bend pipe of esterifying kettle and reacts; Not only avoided the corrosion to the esterification jar such as acid catalyst, and realized esterification continuously, stable, carry out automatically, improved esterification efficient greatly.
Description of drawings
Fig. 1 is the structural representation of ethyl hexanoate continuous esterification still.
Wherein, 1, agitating device; 2, feed proportioning jar charging aperture; 3, feed proportioning jar; 4, measuring pump; 5, conduction oil outlet; 6, heat-insulation layer; 7, thermometer; 8, discharging opening; 9, esterifying kettle; 10, heat conductive oil inlet; 11, reaction bend pipe; 12, charging aperture.
The specific embodiment
Below in conjunction with accompanying drawing the specific embodiment of the utility model is done and to be described in detail:
As shown in Figure 1; This ethyl hexanoate continuous esterification still comprises esterifying kettle 9, and the upper right side of said esterifying kettle 9 is provided with discharging opening 8, and the left lower end of esterifying kettle 9 is provided with charging aperture 12; The left upper end of esterifying kettle 9 is provided with conduction oil outlet 5, and the bottom righthand side of esterifying kettle 9 is provided with heat conductive oil inlet 10; Esterifying kettle 9 upper ends are provided with thermometer 7; The outer wall of esterifying kettle 9 is provided with heat-insulation layer 6; It is characterized in that: esterifying kettle 9 outsides also are provided with feed proportioning jar 3 and measuring pump 4; Said feed proportioning jar 3 is provided with feed proportioning jar charging aperture 2, is provided with agitating device 1 in the feed proportioning jar 3, and the outlet of said measuring pump 4 is communicated with the charging aperture 12 of esterifying kettle 9; Also be provided with reaction bend pipe 11 in the esterifying kettle 9, the two ends of said reaction bend pipe 11 are connected with discharging opening 8 with charging aperture 12 respectively.Said measuring pump 4 is a stainless steel with the material of reaction bend pipe 11.
During use; Adopt stainless steel measuring pump 4 from feed proportioning jar 3, the mixed material of caproic acid, ethanol and catalyst p-methyl benzenesulfonic acid to be pumped in the stainless steel reaction bend pipe 11 through charging aperture 12 continuously; Under stationary temperature, above-mentioned material abundant esterification certain hour in reaction bend pipe 11, treat the esterification completion after; Constantly emit material, realize the continuous esterification of ethyl hexanoate from discharging opening 8.
The utility model is not limited to above-mentioned instance, in claims institute restricted portion of the utility model, and various distortion that those skilled in the art can make without creative work or revise the protection that all receives this patent.
Claims (2)
1. ethyl hexanoate continuous esterification still; Comprise esterifying kettle (9); The upper right side of said esterifying kettle (9) is provided with discharging opening (8); The left lower end of esterifying kettle (9) is provided with charging aperture (12), and the left upper end of esterifying kettle (9) is provided with conduction oil outlet (5), and the bottom righthand side of esterifying kettle (9) is provided with heat conductive oil inlet (10); Esterifying kettle (9) upper end is provided with thermometer (7); The outer wall of esterifying kettle (9) is provided with heat-insulation layer (6); It is characterized in that: esterifying kettle (9) outside also is provided with feed proportioning jar (3) and measuring pump (4); Said feed proportioning jar (3) is provided with feed proportioning jar charging aperture (2), is provided with agitating device (1) in the feed proportioning jar (3), and the outlet of said measuring pump (4) is communicated with the charging aperture (12) of esterifying kettle (9); Also be provided with reaction bend pipe (11) in the esterifying kettle (9), the two ends of said reaction bend pipe (11) are connected with discharging opening (8) with charging aperture (12) respectively.
2. ethyl hexanoate continuous esterification still according to claim 1 is characterized in that: the material of said measuring pump (4) and reaction bend pipe (11) is a stainless steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205536731U CN202366684U (en) | 2011-12-27 | 2011-12-27 | Continuous ethyl hexanoate esterification reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205536731U CN202366684U (en) | 2011-12-27 | 2011-12-27 | Continuous ethyl hexanoate esterification reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202366684U true CN202366684U (en) | 2012-08-08 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205536731U Expired - Fee Related CN202366684U (en) | 2011-12-27 | 2011-12-27 | Continuous ethyl hexanoate esterification reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202366684U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104804876A (en) * | 2015-02-25 | 2015-07-29 | 成都格瑞思文化传播有限公司 | Esterification reaction device |
| CN110302737A (en) * | 2019-07-29 | 2019-10-08 | 潍坊益华化工有限公司 | A kind of continuous esterification device and process |
-
2011
- 2011-12-27 CN CN2011205536731U patent/CN202366684U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104804876A (en) * | 2015-02-25 | 2015-07-29 | 成都格瑞思文化传播有限公司 | Esterification reaction device |
| CN110302737A (en) * | 2019-07-29 | 2019-10-08 | 潍坊益华化工有限公司 | A kind of continuous esterification device and process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120808 Termination date: 20151227 |
|
| EXPY | Termination of patent right or utility model |