CN201264977Y - Continuous treater for ethoxyquin synthetic liquid - Google Patents
Continuous treater for ethoxyquin synthetic liquid Download PDFInfo
- Publication number
- CN201264977Y CN201264977Y CNU2008200363039U CN200820036303U CN201264977Y CN 201264977 Y CN201264977 Y CN 201264977Y CN U2008200363039 U CNU2008200363039 U CN U2008200363039U CN 200820036303 U CN200820036303 U CN 200820036303U CN 201264977 Y CN201264977 Y CN 201264977Y
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- washing tank
- separator
- iii
- delivery pump
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Abstract
The utility model discloses a continuous treatment device of ethoxyquin synthetic fluid. The inlet of a first set of washing tank I (5) is communicated with a fluid delivery pump I (19); the outlet of the washing tank I (5) is communicated with a separator I (6), a washing tank II (9), a separator II (10), a washing tank III (13) and a separator III (14) in turn; and the outlet of the separator III (14) is communicated with a distillation tower. The bottom of the washing tank I (5), the washing tank II (9), the washing tank III (13), the separator I (6), the separator II (10) and the separator III (14) is communicated with a fluid storage tank I (17); the bottom of the separator I (6), the separator II (10) and the separator III (14) is communicated with the fluid storage tank (18) by a pipeline II; the fluid delivery pump (20) is respectively communicated with the washing tank I (5) and the washing tank III (13); and the fluid delivery pump III (21) is communicated with the washing tank II (9).
Description
Technical field
The utility model relates to the apparatus for continous treatment of the synthetic liquid of a kind of Santoflex, but especially relates to the device that the synthetic liquid of Santoflex is handled in a kind of serialization.
Background technology
Santoflex is a kind of outstanding novel antioxidant, sterilant and sterilant.Be used for aspects such as fodder industry, foodstuffs industry, health medicine.In particular for feedstuff industry, have good antioxygen, mildew-resistant dual function.For a long time, Santoflex production subsequent disposal all is to adopt the intermittent type washing operation, thus this method mainly be with the synthetic liquid of Santoflex in washing tank through repeatedly stirring, repeatedly obtain after the layering crude product of Santoflex, in this process, need the workman manually to operate repeatedly, static layering, this treatment process labour intensity is big, and wash(ing)cycle is long, unstable product quality, material loss is big, the running cost height, and level of automation is low.
Summary of the invention
In order to address the above problem, the utility model provide a kind of continuously, simply, the treatment unit of the synthetic liquid of Santoflex efficiently.
The utility model has adopted following technical scheme: the apparatus for continous treatment of the synthetic liquid of a kind of Santoflex, it comprises three groups of washing associated plants, liquid delivery pump I, liquid delivery pump II and liquid delivery pump III, first group comprises washing tank I and separator I, second group comprises washing tank II and separator II, the 3rd group comprises washing tank III and separator III, the import of washing tank I is communicated with liquid delivery pump I, the outlet of washing tank I successively with separator I, washing tank II, separator II, washing tank III and separator III are communicated with, the outlet of separator III is communicated with rectifying tower, at washing tank I, washing tank II, washing tank III, separator I, the bottom of separator II and separator III is connected with receiver I by the pipeline I that is provided with, separator I, the bottom of separator II and separator III is communicated with receiver II again by the pipeline II that is provided with, liquid delivery pump II is communicated with washing tank I and washing tank III respectively, and liquid delivery pump III is communicated with washing tank II.
The exit of described washing tank II and washing tank III is respectively equipped with acidity agent I and acidity agent II.Be provided with under meter I and pneumatic adjusting valve I between the import of described liquid delivery pump I and washing tank I successively.Be provided with under meter II and pneumatic adjusting valve II between described liquid delivery pump II and the washing tank I successively.Be provided with under meter III and pneumatic adjusting valve III between described liquid delivery pump II and the washing tank III successively.Be provided with under meter IV and pneumatic adjusting valve IV between described liquid delivery pump III and the washing tank II.
The utlity model has following beneficial effect: the utility model is provided with three groups of washing associated plants, they are the operation of serialization self acting, material mode with overflow after pump is carried is continuously passed through three groups of washing devices, can lower working strength of workers greatly like this, improved production efficiency, the washing operation time only is 1/4 of original place science and engineering skill, also reduces the unstable of artificial control washing quality and the loss of material simultaneously, greatly reduces production cost.Be connected with acidometer on the washing tank of second group and the 3rd group of the present utility model, it can cooperate the pH value on control washings upper strata with under meter like this.Be provided with under meter I and pneumatic adjusting valve I between the import of liquid delivery pump I of the present utility model and washing tank I successively, can show and control the flow of synthetic liquid like this, be provided with under meter II and pneumatic adjusting valve II between liquid delivery pump II of the present utility model and the washing tank I successively, they can be used to show and control the flow of washing water.Be provided with under meter IV and pneumatic adjusting valve IV between liquid delivery pump III of the present utility model and the washing tank II, they can be used to show and control the flow of alkali lye, be provided with under meter III and pneumatic adjusting valve III between liquid delivery pump II of the present utility model and the washing tank III successively, they are used to show and control the flow of water.
Description of drawings
Fig. 1 is a structural representation of the present utility model
Embodiment
In Fig. 1, the utility model is the apparatus for continous treatment of the synthetic liquid of a kind of Santoflex, it comprises three groups of associated plants, liquid delivery pump I19, liquid delivery pump II20 and liquid delivery pump III21, first group comprises washing tank I5 and separator I6, the preliminary washing that washing tank I5 and separator I6 are used for synthetic liquid with separate, second group comprises washing tank II9 and separator II10, washing tank II9 is used for alkali cleaning and separates with separator II10, but first group of flush away be the catalyzer of flush away fully not, isolates the Santoflex crude product; The 3rd group comprises washing tank III13 and separator III14, and washing tank III13 is used for last washing and separates with separator III14, but a spot of alkali lye is carried in second group of washing secretly in the flush away crude product, isolates the Santoflex crude product.The import of washing tank I5 is communicated with liquid delivery pump I19, be provided with under meter I1 and pneumatic adjusting valve I3 between the import of liquid delivery pump I19 and washing tank I5 successively, under meter I1 and pneumatic adjusting valve I3 can show and control the flow of synthetic liquid, the outlet of washing tank I5 successively with separator I6, washing tank II9, separator II10, washing tank III13 and separator III14 are communicated with, the outlet of separator III14 is communicated with rectifying tower, at washing tank I5, the bottom of washing tank II9 and washing tank III13 is connected with receiver I17 by the pipeline I that is provided with, separator I6, the bottom of separator II10 and separator III14 is communicated with receiver II18 by the pipeline II that is provided with, liquid delivery pump II20 is communicated with washing tank I5 and washing tank III13 respectively, liquid delivery pump III21 is communicated with washing tank II9, the exit of washing tank II9 and washing tank III13 is respectively equipped with acidity agent I15 and acidity agent II16, be provided with under meter II2 and pneumatic adjusting valve II4 between liquid delivery pump II20 and the washing tank I5 successively, under meter II2 and pneumatic adjusting valve II4 can be used to show and control the flow of washing water, be provided with under meter III11 and pneumatic adjusting valve III12 between liquid delivery pump II20 and the washing tank III13 successively, under meter III11 and pneumatic adjusting valve III12 can show and control the flow of water, be provided with under meter IV7 and pneumatic adjusting valve IV8 between liquid delivery pump III21 and the washing tank II9, under meter IV7 and pneumatic adjusting valve IV8 can be used to show and control the flow of alkali lye.
The using method that synthetic back Santoflex is handled in serialization of the present utility model may further comprise the steps:
(1) with liquid delivery pump I19 and liquid delivery pump II20 with the synthetic liquid of Santoflex and water respectively by the chain adjusting of under meter I1 and pneumatic adjusting valve I3 and under meter II2 and pneumatic adjusting valve II4, make it respectively with 3.5m
3/ h and 1m
3/ h feeds among the washing tank I5, and through fully stirring, the material overflow is gone into first group separator I6 and carried out layering, and the upper strata is Santoflex crude product and little amount of catalyst, and lower floor is the waste water that contains catalyzer;
(2) the receiver I17 of lower floor is gone in the subnatant overflow, and second group washing tank II9 is gone in the upper materials overflow, by under meter IV7, pneumatic adjusting valve IV8, the chain adjusting of acidometer I15, makes 10% saleratus solution with 0.5m
3/ h feeds among second group the separator II10, and control washing upper strata liquid PH is 7.0, and through fully stirring, the material overflow is gone into second group separator II10 and carried out layering, and the upper strata is the Santoflex crude product, and lower floor is the waste water that contains little amount of catalyst;
(3) the receiver I17 of lower floor is gone in the subnatant overflow, and the 3rd group washing tank III13 is gone in the upper materials overflow, by under meter III11 and pneumatic adjusting valve III12, the chain adjusting of acidometer II16, makes water with 1m
3/ h feeds among the 3rd group the washing tank III13, and control washing upper strata liquid pH is 7.0, and through fully stirring, the material overflow is gone into the 3rd group separator III14 and carried out layering, and the upper strata is the Santoflex crude product, and lower floor is the sodium bicarbonate waste water that contains minute quantity; Subnatant is from flowing into the receiver I17 of lower floor, and the upper materials overflow enters rectifying tower through piping and carries out rectifying.
Claims (6)
1, the apparatus for continous treatment of the synthetic liquid of a kind of Santoflex, it is characterized in that it comprises three groups of washing associated plants, liquid delivery pump I (19), liquid delivery pump II (20) and liquid delivery pump III (21), first group comprises washing tank I (5) and separator I (6), second group comprises washing tank II (9) and separator II (10), the 3rd group comprises washing tank III (13) and separator III (14), the import of washing tank I (5) is communicated with liquid delivery pump I (19), the outlet of washing tank I (5) successively with separator I (6), washing tank II (9), separator II (10), washing tank III (13) and separator III (14) are communicated with, the outlet of separator III (14) is communicated with rectifying tower, in washing tank I (5), washing tank II (9), washing tank III (13), separator I (6), the bottom of separator II (10) and separator III (14) is connected with receiver I (17) by the pipeline I that is provided with, separator I (6), the bottom of separator II (10) and separator III (14) is communicated with receiver II (18) again by the pipeline II that is provided with, liquid delivery pump II (20) is communicated with washing tank I (5) and washing tank III (13) respectively, and liquid delivery pump III (21) is communicated with washing tank II (9).
2, the apparatus for continous treatment of the synthetic liquid of Santoflex according to claim 1 is characterized in that the exit of described washing tank II (9) and washing tank III (13) is respectively equipped with acidity agent I (15) and acidity agent II (16).
3, the apparatus for continous treatment of the synthetic liquid of Santoflex according to claim 1 is characterized in that being provided with under meter I (1) and pneumatic adjusting valve I (3) successively between the import of described liquid delivery pump I (19) and washing tank I (5).
4, the apparatus for continous treatment of the synthetic liquid of Santoflex according to claim 1 is characterized in that being provided with successively between described liquid delivery pump II (20) and the washing tank I (5) under meter II (2) and pneumatic adjusting valve II (4).
5, the apparatus for continous treatment of the synthetic liquid of Santoflex according to claim 1 is characterized in that being provided with successively between described liquid delivery pump II (20) and the washing tank III (13) under meter III (11) and pneumatic adjusting valve III (12).
6, the apparatus for continous treatment of the synthetic liquid of Santoflex according to claim 1 is characterized in that being provided with between described liquid delivery pump III (21) and the washing tank II (9) under meter IV (7) and pneumatic adjusting valve IV (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200363039U CN201264977Y (en) | 2008-05-19 | 2008-05-19 | Continuous treater for ethoxyquin synthetic liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200363039U CN201264977Y (en) | 2008-05-19 | 2008-05-19 | Continuous treater for ethoxyquin synthetic liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201264977Y true CN201264977Y (en) | 2009-07-01 |
Family
ID=40831339
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200363039U Expired - Lifetime CN201264977Y (en) | 2008-05-19 | 2008-05-19 | Continuous treater for ethoxyquin synthetic liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201264977Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110683985A (en) * | 2019-10-21 | 2020-01-14 | 江苏利田科技股份有限公司 | Method for recovering ethoxyquinoline from ethoxyquinoline waste |
-
2008
- 2008-05-19 CN CNU2008200363039U patent/CN201264977Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110683985A (en) * | 2019-10-21 | 2020-01-14 | 江苏利田科技股份有限公司 | Method for recovering ethoxyquinoline from ethoxyquinoline waste |
| CN110683985B (en) * | 2019-10-21 | 2023-04-07 | 江苏利田科技有限公司 | Method for recovering ethoxyquinoline from ethoxyquinoline waste |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20090701 |