CN2640594Y - Fluid stream neutralization reactor - Google Patents
Fluid stream neutralization reactor Download PDFInfo
- Publication number
- CN2640594Y CN2640594Y CN 03271352 CN03271352U CN2640594Y CN 2640594 Y CN2640594 Y CN 2640594Y CN 03271352 CN03271352 CN 03271352 CN 03271352 U CN03271352 U CN 03271352U CN 2640594 Y CN2640594 Y CN 2640594Y
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- CN
- China
- Prior art keywords
- liquid
- neutralization reaction
- reaction chamber
- neutralization
- rotating shaft
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Abstract
The utility model discloses a liquid flow neutralization reacting device, comprising a standby reacted liquid guiding in structure, a neutralization reacting chamber and a generative liquid guiding outlet. The liquid enters into the neutralization reacting chamber through the respective guiding in structure; the neutralization reacting chamber is provided with a lowest liquid level keeping structure; the generative liquid guiding outlet just guides the generative liquid part which exceeds the relative liquid level to the outside. The guiding in structure has two parts; wherein, a main liquid guiding in structure is provided with a guiding inlet which guides the main liquid into the relative neutralization reacting chamber; an assistant liquid guiding in structure is provided with a vertical rotating axis which is arranged in the cavity of the reacting device; the rotating axis is provided with a hollow cavity and a liquid distributing part which is positioned in the neutralization reacting chamber; when the rotating axis is rotating, the assistant liquid enters the neutralization reacting chamber from the liquid distributing part through the hollow cavity of the rotating axis to mix with the main liquid. The utility is characterized in full reaction and high production efficiency.
Description
Technical field
The utility model relates to chemical industry equipment, and particularly different liquids can carry out the device of neutralization reaction therein.
Background technology
Different liquids carries out the device of neutralization reaction in the prior art as two kinds of liquid, mostly directly continue it in the neutralization reaction chamber of gatherer by separately introducing port question response liquid, stirring wheel shaft by the neutralization reaction chamber stirs, and generates liquid and is directed at the external world by the export mouth that is positioned at bottom, neutralization reaction chamber.Defectives such as it is longer to there is question response liquid mixing required time, and production efficiency is not satisfactory, neutralization reaction degree await to improve.
Summary of the invention
Task of the present utility model is to provide a kind of question response liquid to mix liquid stream neutralization reaction device comparatively fully in the neutralization reaction chamber.
Its technical solution is:
A kind of liquid stream neutralization reaction device, its remain reaction liquid guiding structure, neutralization reaction chamber, generate the liquid export mouth, liquid enters the neutralization reaction chamber by guiding structure separately, and the neutralization reaction chamber has minimum liquid level to keep structure, generates the liquid export mouth and final Generation Liquid stream part can be directed at the external world; Above-mentioned guiding structure has two parts, wherein main liquid charging stock guiding structure has the introducing port that directly main liquid charging stock is imported corresponding neutralization reaction chamber, auxiliary liquid raw material guiding structure has the vertical rotating shaft that is arranged on the reaction unit inner chamber, rotating shaft is provided with hollow cavity and is arranged in the cloth liquid portion of neutralization reaction chamber, and the auxiliary liquid raw material proceeds to the neutralization reaction chamber through the rotating shaft hollow cavity by cloth liquid portion and mixes with main liquid charging stock in the rotating shaft rotary course.The utility model is in the rotating shaft rotary course, add auxiliary liquid raw material at rotation process to main liquid charging stock stream by the cloth liquid portion that is arranged in the neutralization reaction chamber, and cloth liquid portion adds in the auxiliary liquid process at stream, and play stirring action, therefore, can make two kinds of liquid mixing of neutralization reaction chamber comparatively abundant, favourable enhancing productivity.
As improvement of the present utility model, above-mentioned neutralization reaction chamber can have two at least; Be respectively elementary neutralization reaction chamber from top to bottom, secondary neutralization reaction chamber pushes away down successively; Above-mentioned neutralization reaction chamber is connected successively, and each neutralization reaction chamber all has minimum liquid level to keep structure, and the liquid stream part that exceeds this liquid level enters subordinate neutralization reaction chamber; Above-mentioned main liquid charging stock guiding structure is located at elementary neutralization reaction chamber, generates the liquid export mouth and is located at final stage neutralization reaction chamber; Auxiliary liquid raw material guiding structure has the cloth liquid portion identical with neutralization reaction number of chambers amount, and it is separately positioned in the different neutralization reaction chambers.This mode by the cloth liquid portion that is positioned at each neutralization reaction chamber simultaneously stream add the auxiliary liquid raw material, and mixing material stirred, the upper level mixing material through stir and corresponding neutralization reaction after the next stage neutralization reaction chamber of flowing through successively, until final stage neutralization reaction chamber, just by export mouth with final Generation Liquid conductance to the external world, the flow process of mixed liquor, hybrid reaction time all obtain prolonging, and can make neutralization reaction more abundant.
As improvement of the present utility model, above-mentioned cloth liquid portion can be wheeled construction, offers liquid distributing hole on the wheel face of described wheeled construction or wheel sheet, and liquid distributing hole is connected the hollow cavity of rotating shaft.This mode is carried in the wheeled construction rotary course and can be formed negative pressuren zone at respective regions in rotating shaft, adds the auxiliary liquid except that being convenient to uniform stream, also helps the stirring to mixing material.
The last wheel face of above-mentioned wheeled construction can be offered liquid distributing hole, and wheel face can be provided with the stirring fin under it.Promptly be beneficial to cloth liquid, be beneficial to stirring again.
As improvement of the present utility model, the volume of upper level neutralization reaction chamber can be greater than the volume of next stage neutralization reaction chamber in the above-mentioned a pair of adjacent neutralization reaction chamber.This mode makes the volume of next stage neutralization reaction chamber less than upper level neutralization reaction chamber, make mixing neutralizer physical efficiency keep more a spot of lasting replenishing to enter this subordinate neutralization reaction chamber, the probability of the intermolecular further hybrid reaction of unreacted different liquids is improved through upper level neutralization reaction chamber.
As improvement of the present utility model, the cloth liquid portion flow liquid amount in the above-mentioned upper level neutralization reaction chamber can be greater than the flow liquid amount of the cloth liquid portion in the next stage neutralization reaction chamber.This mode can make and obtain relatively large stream in the upper level neutralization reaction chamber and add the auxiliary liquid raw material, and the mixing material of formation enters and can also obtain further small amount of supplemental stream behind the next stage neutralization reaction chamber and add the auxiliary liquid raw material, helps the more abundant of neutralization reaction and carries out.
As improvement of the present utility model, the bottom of above-mentioned each neutralization reaction chamber is provided with the discharging of waste liquid valve port.Be convenient to discharging of accumulating waste liquid under each reative cell liquid level and the discharging of cleaning waste water.
Description of drawings
Fig. 1 is a kind of embodiment structural principle of the utility model schematic diagram.
Fig. 2 is the another kind of embodiment structural principle of a utility model schematic diagram.
The specific embodiment
Embodiment 1, in conjunction with referring to accompanying drawing 1, the utility model liquid stream neutralization reaction device, the inner chamber that is made of housing 1 is separated into three neutralization reaction chambers, it is elementary neutralization reaction chamber 2, secondary neutralization reaction chamber 3, three grades of (final stage) neutralization reaction chambers 4, the port 2-3 that connects these two neutralization reaction chambers is offered in interlayer between wherein elementary neutralization reaction chamber 2 and the secondary neutralization reaction chamber 3 and 6 of following rotating shafts, the port 3-4 that connects these two neutralization reaction chambers is offered in interlayer between secondary neutralization reaction chamber 3 and the final stage neutralization reaction chamber 4 and 6 of following rotating shafts, above-mentioned port 2-3, the periphery of port 3-4 has the enclosing portion 21 of suitable height, 31, this enclosing portion 21, enclosing portion 31 can make neutralization reaction chamber 2 respectively, neutralization reaction chamber 3 is kept the liquid level of corresponding height, elementary neutralization reaction chamber 2 is provided with main liquid charging stock introducing port 5, by introducing port 5 continual the replenishing of main liquid charging stock entered neutralization reaction chamber 2, auxiliary liquid raw material guiding structure is provided with rotating shaft 6, rotating shaft 6 drives running by motor 9, rotating shaft 6 is provided with hollow cavity 61, rotating shaft 6 is provided with the cloth liquid portion 62 of wheeled construction respectively in three neutralization reaction chambers, 63,64, cloth liquid portion 62,63,64 can be centrifugal impeller formula structure, offer liquid distributing hole 65 on the wheel sheet, the quantity of liquid distributing hole 65 and distribution can be selected as required, the quantity of liquid distributing hole 65 and big I are greater than cloth liquid portion 63 in the cloth liquid portion 62, in like manner push away down, liquid distributing hole is connected hollow cavity 61, rotating shaft 6 overcoat axle sleeves 7,7 on rotating shaft 6 and axle sleeve are auxiliary liquid raw material introduction chamber 71, rotating shaft 6 connects for the rotation liquid sealing that adapts to axle sleeve 7, the auxiliary liquid raw material at first enters introduction chamber 71, be added in the corresponding neutralization reaction chamber by liquid distributing hole 65 streams by introduction chamber 71 hollow cavity 61 back of constantly flowing through, the volume of above-mentioned neutralization reaction chamber 2 is greater than the volume of neutralization reaction chamber 3, the volume of neutralization reaction chamber 3 is greater than the volume of neutralization reaction chamber 4,2 bottoms, above-mentioned elementary neutralization reaction chamber are provided with discharging of waste liquid valve port 22,3 bottoms, secondary neutralization reaction chamber are provided with discharging of waste liquid valve port 32,4 bottoms, final stage neutralization reaction chamber are provided with discharging of waste liquid valve port 42, final stage neutralization reaction chamber 4 is provided with and generates liquid export mouth 8, generating liquid export mouth 8 has the enclosing portion 81 of suitable height in a side that is positioned at final stage neutralization reaction chamber 4, and this enclosing portion 81 makes final stage neutralization reaction chamber 4 be kept the liquid level of corresponding height.
Embodiment 2, in conjunction with referring to Fig. 2, except that following technology contents, other all can be identical with embodiment 1 appropriate section.Rotating shaft 6 is provided with fixed support 66, the top corresponding site of rotating shaft 6 is connected on the support by bearing fixing, establish follower in the rotating shaft 6, motor can be arranged on this support, motor is by the follower of transmission component driving coupling rotating shaft, can drive rotating shaft 6 corresponding runnings, the auxiliary liquid raw material injects hollow cavity 61 by the upper end open 67 of rotating shaft 6; Cloth liquid portion 63 is near the disc wheeled construction, and wheel face can be offered liquid distributing hole 65 on it, and wheel face can be provided with and stir fin 68 under it.
The quantity of neutralization reaction of the present utility model chamber also can be 1 or 2 etc.
Getting type between the adjacent neutralization reaction of the present utility model chamber, the liquid level hold mode of each neutralization reaction chamber, the auxiliary liquid raw material enters the mode of rotating shaft hollow cavity, the frame mode of cloth liquid portion, and the discharge mode of waste liquid etc. all can have other multiple conspicuous variations.
Claims (9)
1, a kind of liquid stream neutralization reaction device, its remain reaction liquid guiding structure, neutralization reaction chamber, generate the liquid export mouth, liquid enters the neutralization reaction chamber by guiding structure separately, the neutralization reaction chamber has minimum liquid level to keep structure, generates the liquid export mouth and final Generation Liquid stream part can be directed at the external world; It is characterized in that: described guiding structure has two parts of corresponding main liquid charging stock and auxiliary liquid raw material, wherein main liquid charging stock guiding structure has the introducing port that directly main liquid charging stock is imported corresponding neutralization reaction chamber, auxiliary liquid raw material guiding structure has the vertical rotating shaft that is arranged on the reaction unit inner chamber, rotating shaft is provided with hollow cavity and is arranged in the cloth liquid portion of neutralization reaction chamber, and the auxiliary liquid raw material proceeds to the neutralization reaction chamber through the rotating shaft hollow cavity by cloth liquid portion and mixes with main liquid charging stock in the rotating shaft rotary course.
2, liquid stream neutralization reaction device according to claim 1, it is characterized in that: described neutralization reaction chamber has two at least; Be respectively elementary neutralization reaction chamber from top to bottom, secondary neutralization reaction chamber pushes away down successively; Above-mentioned neutralization reaction chamber is connected successively, and each neutralization reaction chamber all has minimum liquid level to keep structure, and the liquid stream part that exceeds this liquid level enters subordinate neutralization reaction chamber; Described main liquid charging stock guiding structure is located at elementary neutralization reaction chamber, generates the liquid export mouth and is located at final stage neutralization reaction chamber; Auxiliary liquid raw material guiding structure has the cloth liquid portion identical with neutralization reaction number of chambers amount, and it is separately positioned in the different neutralization reaction chambers.
3, liquid according to claim 1 stream neutralization reaction device is characterized in that: described cloth liquid portion is a wheeled construction, offers liquid distributing hole on the wheel face of described wheeled construction or wheel sheet, and liquid distributing hole is connected the hollow cavity of rotating shaft.
4, liquid stream neutralization reaction device according to claim 3, it is characterized in that: the last wheel face of described wheeled construction is offered liquid distributing hole, and wheel face can be provided with the stirring fin under it.
5, liquid according to claim 2 stream neutralization reaction device is characterized in that: described cloth liquid portion is a wheeled construction, offers liquid distributing hole on the wheel face of described wheeled construction or wheel sheet, and liquid distributing hole is connected the hollow cavity of rotating shaft.
6, according to claim 2 or 5 described liquid stream neutralization reaction devices, it is characterized in that: the volume of the upper level neutralization reaction chamber in the described a pair of adjacent neutralization reaction chamber is greater than the volume of next stage neutralization reaction chamber.
7, liquid stream neutralization reaction device according to claim 6, it is characterized in that: the cloth liquid portion flow liquid amount in the described upper level neutralization reaction chamber is greater than the cloth liquid portion flow liquid amount in the next stage neutralization reaction chamber.
8, require described liquid to flow the neutralization reaction device according to claim 1 to 5 is arbitrary, it is characterized in that: the bottom of described each neutralization reaction chamber is provided with the discharging of waste liquid valve port.
9, liquid stream neutralization reaction device according to claim 7, it is characterized in that: the bottom of described each neutralization reaction chamber is provided with the discharging of waste liquid valve port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03271352 CN2640594Y (en) | 2003-07-28 | 2003-07-28 | Fluid stream neutralization reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03271352 CN2640594Y (en) | 2003-07-28 | 2003-07-28 | Fluid stream neutralization reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2640594Y true CN2640594Y (en) | 2004-09-15 |
Family
ID=34300687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03271352 Expired - Fee Related CN2640594Y (en) | 2003-07-28 | 2003-07-28 | Fluid stream neutralization reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2640594Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080447A (en) * | 2015-07-27 | 2015-11-25 | 河北科技大学 | Tower type reactor for organic acid neutralization and reaction method thereof |
| CN105080432A (en) * | 2015-07-27 | 2015-11-25 | 河北科技大学 | Sodium chloroacetate continuous cyanation tower-type reactor and reaction method thereof |
| CN105642213A (en) * | 2014-11-14 | 2016-06-08 | 程叶红 | Microemulsion reaction kettle for producing chemical biosurfactant microemulsion |
| CN105664819A (en) * | 2014-11-14 | 2016-06-15 | 程叶红 | Microemulsion reactor for biological surfactant microemulsion production |
-
2003
- 2003-07-28 CN CN 03271352 patent/CN2640594Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105642213A (en) * | 2014-11-14 | 2016-06-08 | 程叶红 | Microemulsion reaction kettle for producing chemical biosurfactant microemulsion |
| CN105664819A (en) * | 2014-11-14 | 2016-06-15 | 程叶红 | Microemulsion reactor for biological surfactant microemulsion production |
| CN105080447A (en) * | 2015-07-27 | 2015-11-25 | 河北科技大学 | Tower type reactor for organic acid neutralization and reaction method thereof |
| CN105080432A (en) * | 2015-07-27 | 2015-11-25 | 河北科技大学 | Sodium chloroacetate continuous cyanation tower-type reactor and reaction method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |