CN204079840U - Mefenamic acid refining system - Google Patents
Mefenamic acid refining system Download PDFInfo
- Publication number
- CN204079840U CN204079840U CN201420530598.0U CN201420530598U CN204079840U CN 204079840 U CN204079840 U CN 204079840U CN 201420530598 U CN201420530598 U CN 201420530598U CN 204079840 U CN204079840 U CN 204079840U
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- Prior art keywords
- stirred pot
- mefenamic acid
- tank
- valve
- refining system
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- Withdrawn - After Issue
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Abstract
Mefenamic acid refining system, is made up of the reactor connected successively, pressure filter, leaching machine, whizzer and DoubletaperedVacuumdrier, and reactor comprises stirred pot, sodium hydroxide tank, mefenamic acid hold-up vessel, hydrochloric acid tank and refrigerator; Sodium hydroxide tank is connected stirred pot with hydrochloric acid tank respectively by communicating pipe, and mefenamic acid hold-up vessel connects stirred pot by connecting cylinder, mounted motor on stirred pot, and the output shaft of motor connects paddle, and paddle is positioned at stirred pot; Refrigerator connects coil pipe, and coil pipe is positioned at stirred pot.The utility model can by the molten acidifying again of the first alkali of mefenamic acid crude product, and obtain highly purified fine work through process after crystallization, in the finished product, impurity is minimum, does not have DMF impurity, improves the quality of mefenamic acid.The utility model adopts mechanization production completely, avoids various chemicals manually to drop into operation, adds the security of production process, improve production work efficiency.
Description
Technical field
The utility model relates to a kind of mefenamic acid production equipment, is exactly a kind of mefenamic acid refining system.
Background technology
At present, the refining of mefenamic acid is that mefenamic acid crude product decolours crystal refining repeatedly in organic solvent, finally obtains mefenamic acid finished product.Organic solvent is DMF.Decolouring is decolorizing with activated carbon.A certain amount of DMF of mefenamic acid finished product residual after refining, and incidental impurities in Crystallization Process, foreign matter content is more.
Utility model content
For overcoming above-mentioned deficiency of the prior art, the utility model is to provide a kind of mefenamic acid refining system, and the mefenamic acid foreign matter content after exquisiteness is extremely low, ensures the purity of mefenamic acid.
The utility model for achieving the above object, be achieved through the following technical solutions: mefenamic acid refining system, be made up of the reactor connected successively, pressure filter, leaching machine, whizzer and DoubletaperedVacuumdrier, reactor comprises stirred pot, sodium hydroxide tank, mefenamic acid hold-up vessel, hydrochloric acid tank and refrigerator; Sodium hydroxide tank is connected stirred pot with hydrochloric acid tank respectively by communicating pipe, and mefenamic acid hold-up vessel connects stirred pot by connecting cylinder, mounted motor on stirred pot, and the output shaft of motor connects paddle, and paddle is positioned at stirred pot; Refrigerator connects coil pipe, and coil pipe is positioned at stirred pot.
In order to realize the purpose of this utility model further, can also by the following technical solutions: one end of the hinged baffle plate of inwall of described connecting cylinder, baffle plate is for tilting to install, baffle plate is by the complete shutoff of cross section mouth of connecting cylinder, one end of the bottom-hinged cylinder of baffle plate, the other end of cylinder is hingedly mounted on the inwall of connecting cylinder.The two ends of described communicating pipe install the first valve and the second valve respectively, and communicating pipe arranges arm close to the part of stirred pot, and the Link Port of arm, between the first valve and the second valve, arm installs the 3rd valve.In described stirred pot, temperature-indicating instrument and pH determinator are installed.Described coil pipe is positioned at the middle and upper part of stirred pot.
The utility model has the advantages that: the utility model can by the molten acidifying again of the first alkali of mefenamic acid crude product, and obtain highly purified fine work through process after crystallization, in the finished product, impurity is minimum, does not have DMF impurity, improves the quality of mefenamic acid.The utility model adopts mechanization production completely, avoids various chemicals manually to drop into operation, adds the security of production process, improve production work efficiency.The utility model also has advantage compact, cheap for manufacturing cost and easy to use simple for structure.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model; Fig. 2 is the structural representation of reactor in Fig. 1.
Reference numeral: 1 reactor 2 pressure filter 3 leaching machine 4 DoubletaperedVacuumdrier 5 sodium hydroxide tank 6 connecting cylinder 7 mefenamic acid hold-up vessel 8 baffle plate 9 cylinder 10 motor 11 hydrochloric acid tank 12 first valve 13 communicating pipe 14 second valve 15 the 3rd valve 16 arm 17 stirred pot 18 temperature-indicating instrument 19pH determinator 20 paddle 21 coil pipe 22 refrigerator 23 whizzer.
Embodiment
Mefenamic acid refining system, as depicted in figs. 1 and 2, be made up of the reactor 1 connected successively, pressure filter 2, leaching machine 3 and DoubletaperedVacuumdrier 4, reactor 1 comprises stirred pot 17, sodium hydroxide tank 5, mefenamic acid hold-up vessel 7, hydrochloric acid tank 11 and refrigerator 22; Sodium hydroxide tank 5 is connected stirred pot 17 with hydrochloric acid tank 11 respectively by communicating pipe 13, mefenamic acid hold-up vessel 7 connects stirred pot 17 by connecting cylinder 6, mounted motor 10 on stirred pot 17, the output shaft of motor 10 connects paddle 20, and paddle 20 is positioned at stirred pot 17; Refrigerator 22 connects coil pipe 21, and coil pipe 21 is positioned at stirred pot 17.
Added the sodium hydroxide solution of about 70 ~ 80kg20% to stirred pot 17 by sodium hydroxide tank 5, open and stir, mefenamic acid solid 50.0kg is added to stirred pot 17 while stirring by mefenamic acid hold-up vessel 7, after mefenamic acid sample dissolves cmpletely, in stirred pot 17, slowly drip the hcl acidifying of about 20% to material liquid pH=1.0 ~ 2.5 by hydrochloric acid tank 11 again, pass through refrigerator 22 borehole cooling to 0 ~ 5 DEG C stirring and crystallizing 4 hours in this pH condition.Again reaction solution is entered successively pressure filter 2, leaching machine 3 carries out filtering, purified water drip washing mefenamic acid filter cake.Filter cake is centrifugal by carrying out in whizzer 23, the mefenamic acid after centrifugal is put DoubletaperedVacuumdrier 4 in 85 ± 5 DEG C, vacuum tightness≤-0.08Mpa drying under reduced pressure, obtains the mefenamic acid product refined.
The product sample prepared of the utility model equipment and organic solvent DMF are refined sample and are contrasted, through inspection, as shown in the table, can find out, not have impurity.
When adding mefenamic acid solid, the mefenamic acid added fully dissolves, need to reduce the rate of feeding adding mefenamic acid, to achieve these goals, one end of the hinged baffle plate 8 of inwall of described connecting cylinder 6, baffle plate 8 is for tilting to install, and baffle plate 8 is by the complete shutoff of cross section mouth of connecting cylinder 6, one end of the bottom-hinged cylinder 9 of baffle plate 8, the other end of cylinder 9 is hingedly mounted on the inwall of connecting cylinder 6.Dissolving situation according to the mefenamic acid dropped in stirred pot 17, by controlling the cooperation position of cylinder 9 suitably between regulating fender 8 and connecting cylinder 6, having reached the object controlling rate of feeding.
After each use, need to clean sodium hydroxide tank 5 and hydrochloric acid tank 11, in order to avoid the water of cleaning enters stirred pot 17, the first valve 12 and the second valve 14 is installed at the two ends of described communicating pipe 13 respectively, communicating pipe arranges arm 16 close to the part of stirred pot 17, the Link Port of arm 16, between the first valve 12 and the second valve 14, arm 16 installs the 3rd valve 15.Before cleaning, open the first valve 12 and the 3rd valve 15, in sodium hydroxide tank 5 and hydrochloric acid tank 11, inject cleaning water, the waste water after cleaning is flowed out by arm 16.During normal use, closedown the 3rd valve 15, opens the first valve 12 and the second valve 14 controls liquid inlet volume.
At interpolation salt acid phase, need uninterrupted sampling and measuring pH value; In the crystallization stage, need real-time measuring tempeature.In order to realize full-automatic production, in described stirred pot 17, temperature-indicating instrument 18 and pH determinator 19 are installed.PH determinator 19 stops dripping hydrochloric acid work when being measured to suitable pH value; Temperature-indicating instrument 18 measures temperature range in stirred pot 17, controls refrigerator 22 and works, to ensure crystallization effect processed.
Described coil pipe 21 is positioned at the middle and upper part of stirred pot 17.First coil pipe 21 lowers the temperature to the reaction solution of stirred pot 17 middle and upper part, and the reaction solution after cooling can flow to stirred pot 17 bottom high-temperature area, thus achieves the stirring of local, reacting liquid temperature is exchanged evenly, also makes reaction more even.
The technical solution of the utility model is not restricted in the scope of embodiment described in the utility model.The technology contents of the not detailed description of the utility model is known technology.
Claims (5)
1. mefenamic acid refining system, it is characterized in that: be made up of the reactor connected successively (1), pressure filter (2), leaching machine (3), whizzer (23) and DoubletaperedVacuumdrier (4), reactor (1) comprises stirred pot (17), sodium hydroxide tank (5), mefenamic acid hold-up vessel (7), hydrochloric acid tank (11) and refrigerator (22); Sodium hydroxide tank (5) is connected stirred pot (17) with hydrochloric acid tank (11) respectively by communicating pipe (13), mefenamic acid hold-up vessel (7) connects stirred pot (17) by connecting cylinder (6), the upper mounted motor (10) of stirred pot (17), the output shaft of motor (10) connects paddle (20), and paddle (20) is positioned at stirred pot (17); Refrigerator (22) connects coil pipe (21), and coil pipe (21) is positioned at stirred pot (17).
2. mefenamic acid refining system according to claim 1, it is characterized in that: one end of the hinged baffle plate of inwall (8) of described connecting cylinder (6), baffle plate (8) is for tilting to install, baffle plate (8) is by the complete shutoff of cross section mouth of connecting cylinder (6), one end of the bottom-hinged cylinder (9) of baffle plate (8), the other end of cylinder (9) is hingedly mounted on the inwall of connecting cylinder (6).
3. mefenamic acid refining system according to claim 1, it is characterized in that: the two ends of described communicating pipe (13) install the first valve (12) and the second valve (14) respectively, communicating pipe arranges arm (16) close to the part of stirred pot (17), the Link Port of arm (16) is positioned between the first valve (12) and the second valve (14), the upper installation the 3rd valve (15) of arm (16).
4. mefenamic acid refining system according to claim 1, is characterized in that: install temperature-indicating instrument (18) and pH determinator (19) in described stirred pot (17).
5. mefenamic acid refining system according to claim 1, is characterized in that: described coil pipe (21) is positioned at the middle and upper part of stirred pot (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420530598.0U CN204079840U (en) | 2014-09-16 | 2014-09-16 | Mefenamic acid refining system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420530598.0U CN204079840U (en) | 2014-09-16 | 2014-09-16 | Mefenamic acid refining system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204079840U true CN204079840U (en) | 2015-01-07 |
Family
ID=52172576
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420530598.0U Withdrawn - After Issue CN204079840U (en) | 2014-09-16 | 2014-09-16 | Mefenamic acid refining system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204079840U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104193639A (en) * | 2014-09-16 | 2014-12-10 | 德州博诚制药有限公司 | Mefenamic acid refining system |
-
2014
- 2014-09-16 CN CN201420530598.0U patent/CN204079840U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104193639A (en) * | 2014-09-16 | 2014-12-10 | 德州博诚制药有限公司 | Mefenamic acid refining system |
| CN104193639B (en) * | 2014-09-16 | 2015-10-28 | 德州博诚制药有限公司 | Mefenamic acid refining system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150107 Effective date of abandoning: 20151028 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |