CN204251528U - A kind of dehydration of oil methylnaphthalene, decolouring equipment integrating - Google Patents
A kind of dehydration of oil methylnaphthalene, decolouring equipment integrating Download PDFInfo
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- CN204251528U CN204251528U CN201420733784.4U CN201420733784U CN204251528U CN 204251528 U CN204251528 U CN 204251528U CN 201420733784 U CN201420733784 U CN 201420733784U CN 204251528 U CN204251528 U CN 204251528U
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Abstract
The utility model relates to a kind of dehydration of oil methylnaphthalene, decolouring equipment integrating, it comprises the tank body with import and outlet, be arranged on the dehydration molecular sieve layer in tank body, be arranged on the decolouring oxidant layer in tank body, and be arranged in tank body for filtering in oil methylnaphthalene that autospasy colorant layer flows out containing the filtering layer of discoloring agent, wherein dehydration molecular sieve layer, decolouring oxidant layer, filtering layer is folded successively to be established, and dehydration molecular sieve layer is positioned at the bottom of tank body, decolouring oxidant layer is positioned at the middle part of tank body, filtering layer is positioned at the top of tank body, import is positioned at the bottom of tank body, outlet is positioned at the top of tank body.The utility model dehydration molecular sieve layer and decolouring oxidant layer are arranged in same tank body, make product can realize dehydration and decolouring by continuous print, simultaneously by the setting of filtering layer, prevent in the oil methylnaphthalene after dehydration and decolouring containing discoloring agent, improve the quality of product, in addition, structure of the present utility model is simple, enforcement is convenient.
Description
Technical field
the utility model relates to a kind of dehydration, decolouring equipment integrating of oil methylnaphthalene.
Background technology
as everyone knows, after producing in oil methylnaphthalene process, its dehydration is absolutely necessary process, but along with the demand of product colour, further, decolour, namely dewatering and decolouring is two independent techniques, and between the two cannot be continuous normally, cause, operate more loaded down with trivial details.
Summary of the invention
technical problem to be solved in the utility model overcomes the deficiencies in the prior art, provides a kind of dehydration of oil methylnaphthalene, decolouring equipment integrating.
for solving above technical problem, the utility model takes following technical scheme:
a kind of dehydration of oil methylnaphthalene, decolouring equipment integrating, it comprises the tank body with import and outlet, be arranged on the dehydration molecular sieve layer in tank body, be arranged on the decolouring oxidant layer in tank body, and be arranged in tank body for filtering in oil methylnaphthalene that autospasy colorant layer flows out containing the filtering layer of discoloring agent, wherein dehydration molecular sieve layer, decolouring oxidant layer, filtering layer is folded successively to be established, and dehydration molecular sieve layer is positioned at the bottom of tank body, decolouring oxidant layer is positioned at the middle part of tank body, filtering layer is positioned at the top of tank body, import is positioned at the bottom of tank body, outlet is positioned at the top of tank body.
preferably, above-mentioned dehydration, decolouring equipment integrating also comprise the topping-up pump being arranged on ingress.Although common pressure can realize the flowing of oil methylnaphthalene, speed is slow, efficiency is lower, therefore, is increased the flow velocity of oil methylnaphthalene by topping-up pump.
preferably, oxidant layer of decolouring is carclazyte.
specifically implement and preferred aspect according to one of the present utility model, be also provided with attemperator in the periphery of tank body.
preferably, attemperator comprises the chuck being arranged on tank body periphery, and in chuck, the heating unit of thermal insulation medium is passed into by pipeline, wherein chuck is the coil pipe being located at tank body periphery along the spiral dish of tank body short transverse, attemperator also comprises the temperature-sensing probe of the temperature for detecting material in tank, and be arranged on pipeline can receive temperature-sensing probe temperature information after in coil pipe, fill into the automatically controlled valve of thermal insulation medium, wherein the import of coil pipe is positioned at the below of outlet, when temperature-sensing probe detects that the temperature of material is more than or equal to 43 DEG C, automatically controlled valve cuts out automatically, when temperature-sensing probe detects the temperature of material lower than 43 DEG C, automatically controlled valve is opened automatically.
further, preferably, the import of coil pipe is positioned at the below of outlet.
further, the import of coil pipe lays respectively at the relative both sides of tank body with outlet.
specifically implement and preferred aspect according to of the present utility model another, tank body is also provided with along tank body short transverse in the shape of a spiral and notch towards the drainage tray outside tank body, and the inwall of drainage tray and coil pipe forms drainage channel.
the drainage tray hand of spiral is contrary with the coil pipe hand of spiral, and is provided with water discharge valve and water collecting basin in the below of drainage channel.
concrete, temperature-sensing probe has two, is separately positioned on import and the outlet of tank body, and the information that automatically controlled valve receives is the mean value of two temperature-sensing probe measured temperatures.
due to the enforcement of above technical scheme, the utility model compared with prior art tool has the following advantages:
the utility model dehydration molecular sieve layer and decolouring oxidant layer are arranged in same tank body, make product can realize dehydration and decolouring by continuous print, simultaneously by the setting of filtering layer, prevent in the oil methylnaphthalene after dehydration and decolouring containing discoloring agent, improve the quality of product, in addition, structure of the present utility model is simple, enforcement is convenient.
Accompanying drawing explanation
below in conjunction with accompanying drawing and specific embodiment, the utility model is described in more detail:
fig. 1 is the structural representation according to dehydration of the present utility model, decolouring equipment integrating;
fig. 2 is the structural representation according to attemperator of the present utility model;
wherein: 1, tank body; 10, drainage tray; 11, import; 12, export;
2, chuck (coil pipe); 20, import; 21, export;
3, pipeline;
4, heating unit (steam);
5, temperature-sensing probe;
6, automatically controlled valve;
7, water discharge valve;
8, water collecting basin:
a, dehydration molecular sieve layer; B, decolouring oxidant layer; C, filtering layer; D, topping-up pump; E, attemperator.
Embodiment
as depicted in figs. 1 and 2, the dehydration of the oil methylnaphthalene of the present embodiment, decolouring equipment integrating, it comprises the tank body 1 with import 11 and outlet 12, be arranged on the dehydration molecular sieve layer a in tank body 1, be arranged on the decolouring oxidant layer b in tank body 1, and be arranged in tank body 1 for filtering in oil methylnaphthalene that autospasy colorant layer b flows out containing the filtering layer c of discoloring agent, wherein dehydration molecular sieve layer a, decolouring oxidant layer b, filtering layer c is folded successively to be established, and dehydration molecular sieve layer a is positioned at the bottom of tank body 1, decolouring oxidant layer b is positioned at the middle part of tank body 1, filtering layer c is positioned at the top of tank body 1, import 11 is positioned at the bottom of tank body 1, outlet 12 is positioned at the top of tank body 1.
further, above-mentioned dehydration, decolouring equipment integrating also comprise the topping-up pump d being arranged on import 11 place.Although common pressure can realize the flowing of oil methylnaphthalene, speed is slow, efficiency is lower, therefore, is increased the flow velocity of oil methylnaphthalene by topping-up pump.
concrete, decolouring oxidant layer b is carclazyte.Dehydration molecular sieve layer a and filtering layer c is conventional design.
further, attemperator e is also provided with in the periphery of tank body 1 in this example.
concrete, attemperator e comprises the chuck 2 being arranged on tank body 1 periphery, and in chuck 2, the heating unit 4 of thermal insulation medium is passed into by pipeline 3, wherein chuck 2 is the coil pipe 2 being located at tank body 1 periphery along the spiral dish of tank body 1 short transverse, attemperator also comprises the temperature-sensing probe 5 of the temperature for detecting material in tank body 1, and be arranged on pipeline can receive temperature-sensing probe 5 temperature information after in coil pipe 2, fill into the automatically controlled valve 6 of thermal insulation medium, wherein the import 20 of coil pipe 2 is positioned at the below of outlet 21, when temperature-sensing probe 5 detects that the temperature of material is more than or equal to 43 DEG C, automatically controlled valve 6 cuts out automatically, when temperature-sensing probe 5 detects the temperature of material lower than 43 DEG C, automatically controlled valve 6 is opened automatically.
concrete, temperature-sensing probe 5 has two, is separately positioned on import and the outlet of tank body 1, and the information that automatically controlled valve 6 receives is the mean value (43 DEG C is boundary's point) of two temperature-sensing probe 5 measured temperatures.
concrete, tank body 1 be provided with along tank body 1 short transverse in the shape of a spiral and notch towards the drainage tray 10 outside tank body 1, and drainage tray 10 forms drainage channel with the inwall of coil pipe 2 (does not show in figure, but be not difficult to expect.
further, drainage tray 10 hand of spiral is contrary with coil pipe 2 hand of spiral.More be conducive to the collection of the globule.
concrete, import 20 and the outlet 21 of coil pipe 2 lay respectively at the relative both sides of tank body 1.
in addition, in this example, water discharge valve 7 and water collecting basin 8 is provided with in the below of drainage channel.
above the utility model is described in detail; its object is to allow the personage being familiar with this art can understand content of the present utility model and be implemented; protection domain of the present utility model can not be limited with this; all equivalences done according to spirit of the present utility model change or modify, and all should be encompassed in protection domain of the present utility model.
Claims (10)
1. the dehydration of an oil methylnaphthalene, decolouring equipment integrating, it is characterized in that: described equipment integrating comprises the tank body with import and outlet, be arranged on the dehydration molecular sieve layer in described tank body, be arranged on the decolouring oxidant layer in described tank body, and be arranged in described tank body for filtering the filtering layer containing discoloring agent in the described oil methylnaphthalene that goes out from described discoloring agent laminar flow, wherein said dehydration molecular sieve layer, described decolouring oxidant layer, described filtering layer is folded successively to be established, and described dehydration molecular sieve layer is positioned at the bottom of described tank body, described decolouring oxidant layer is positioned at the middle part of described tank body, described filtering layer is positioned at the top of described tank body, described import is positioned at the bottom of described tank body, described outlet is positioned at the top of described tank body.
2. oil methylnaphthalene according to claim 1 dehydration, decolouring equipment integrating, it is characterized in that: described equipment integrating also comprises the topping-up pump being arranged on ingress.
3. oil methylnaphthalene according to claim 1 dehydration, decolouring equipment integrating, it is characterized in that: described decolouring oxidant layer is carclazyte.
4. oil methylnaphthalene according to claim 1 dehydration, decolouring equipment integrating, it is characterized in that: be also provided with attemperator in the periphery of described tank body.
5. the dehydration of oil methylnaphthalene according to claim 4, decolouring equipment integrating, it is characterized in that: described attemperator comprises the chuck being arranged on tank body periphery, and in described chuck, the heating unit of thermal insulation medium is passed into by pipeline, described chuck is the coil pipe being located at described tank body periphery along the spiral dish of described tank body short transverse, described attemperator also comprises the temperature-sensing probe of the temperature for detecting described material in tank, and be arranged on the automatically controlled valve filling into thermal insulation medium in the backward described coil pipe of the temperature information that described pipeline can receive described temperature-sensing probe, the import of described coil pipe is positioned at the below of outlet, when described temperature-sensing probe detects that the temperature of material is more than or equal to 43 DEG C, described automatically controlled valve cuts out automatically, when described temperature-sensing probe detects the temperature of material lower than 43 DEG C, described automatically controlled valve is opened automatically.
6. the dehydration of oil methylnaphthalene according to claim 5, decolouring equipment integrating, is characterized in that: the import of described coil pipe and export the relative both sides laying respectively at described tank body.
7. oil methylnaphthalene according to claim 5 dehydration, decolouring equipment integrating, it is characterized in that: be also provided with on described tank body along described tank body short transverse in the shape of a spiral and notch towards the drainage tray outside described tank body, the inwall of described drainage tray and described coil pipe forms drainage channel.
8. oil methylnaphthalene according to claim 7 dehydration, decolouring equipment integrating, it is characterized in that: the described drainage tray hand of spiral is contrary with the described coil pipe hand of spiral.
9. oil methylnaphthalene according to claim 7 dehydration, decolouring equipment integrating, it is characterized in that: be provided with water discharge valve and water collecting basin in the below of described drainage channel.
10. oil methylnaphthalene according to claim 5 dehydration, decolouring equipment integrating, it is characterized in that: described temperature-sensing probe has two, be separately positioned on import and the outlet of described tank body, the information that described automatically controlled valve receives is the mean value of two described temperature-sensing probe measured temperatures.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420733784.4U CN204251528U (en) | 2014-11-28 | 2014-11-28 | A kind of dehydration of oil methylnaphthalene, decolouring equipment integrating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420733784.4U CN204251528U (en) | 2014-11-28 | 2014-11-28 | A kind of dehydration of oil methylnaphthalene, decolouring equipment integrating |
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| Publication Number | Publication Date |
|---|---|
| CN204251528U true CN204251528U (en) | 2015-04-08 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420733784.4U Active CN204251528U (en) | 2014-11-28 | 2014-11-28 | A kind of dehydration of oil methylnaphthalene, decolouring equipment integrating |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105237497A (en) * | 2015-09-21 | 2016-01-13 | 丹阳市助剂化工厂有限公司 | Decolorizeng tank for epoxidized soybean oil production |
| CN107501033A (en) * | 2017-09-26 | 2017-12-22 | 贾海亮 | A kind of methyl naphthalene dehydration with temp regulating function, decolouring equipment integrating |
| WO2024187489A1 (en) * | 2023-03-14 | 2024-09-19 | 鹏辰新材料科技股份有限公司 | Decolorizing device for petroleum methylnaphthalene |
-
2014
- 2014-11-28 CN CN201420733784.4U patent/CN204251528U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105237497A (en) * | 2015-09-21 | 2016-01-13 | 丹阳市助剂化工厂有限公司 | Decolorizeng tank for epoxidized soybean oil production |
| CN107501033A (en) * | 2017-09-26 | 2017-12-22 | 贾海亮 | A kind of methyl naphthalene dehydration with temp regulating function, decolouring equipment integrating |
| WO2024187489A1 (en) * | 2023-03-14 | 2024-09-19 | 鹏辰新材料科技股份有限公司 | Decolorizing device for petroleum methylnaphthalene |
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Address after: Ping Wang Zhen Wujiang District of Suzhou City, Jiangsu Province, 215225 West (318 State Road 99.6 km) Patentee after: Peng East materials Polytron Technologies Inc Address before: Ping Wang Zhen Wujiang District of Suzhou City, Jiangsu Province, 215225 West (318 State Road 99.6 km) Patentee before: Wujiang Wanshida Solvent Company Limited |