CN203170324U - Industrial oil reaction kettle type decoloring device - Google Patents
Industrial oil reaction kettle type decoloring device Download PDFInfo
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- CN203170324U CN203170324U CN 201320155839 CN201320155839U CN203170324U CN 203170324 U CN203170324 U CN 203170324U CN 201320155839 CN201320155839 CN 201320155839 CN 201320155839 U CN201320155839 U CN 201320155839U CN 203170324 U CN203170324 U CN 203170324U
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- tank body
- side wall
- heater
- decolouring
- oil reactor
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Abstract
The utility model relates to an industrial oil reaction kettle type decoloring device, belonging to the technical field of industrial oil treatment. The industrial oil reaction kettle type decoloring device comprises a tank body, wherein a material inlet and a material outlet are formed in the bottom of the tank body, and a mixer is arranged at the top of the tank body. The industrial oil reaction kettle type decoloring device is characterized in that a heater is arranged on the left side wall of the tank body, a heating end of the heater is arranged in the tank body, a temperature detector used for detecting the temperature in the tank body is arranged on the right side wall of the tank body, a cooling pipeline is arranged in the tank body, and a decoloring agent storage tank is arranged on the side wall of the upper part of the tank body. The industrial oil reaction kettle type decoloring device is simple in structure, changes the mode of the conventional device that a heater used for separating water is used for heating an oil product and is capable of reasonably heating an oil product to be decolored, effectively ensuring the decoloring speed of the oil product, increasing the production efficiency and lowering the production cost.
Description
Technical field
The utility model relates to a kind of for iundustrial oil reactor formula decolouring device, belongs to the iundustrial oil processing technology field.
Background technology
Mainly be divided into two big classes when at present, iundustrial oil is handled: one, remove contained humidity and impurity in the oil product; Two, improve the oil product color.Be generally used for improving the decolouring device of oil product color, its decolouring work for the treatment of flow process is: oil product enters the heating system of cleaning system under the suction function of vacuum, enter vacuum system again and carry out water-oil separating, isolate the moisture in the oil product, by oil-feed pump oil is pumped to the decolouring device from vacuum separator then, and in the decolouring device, add decolorizer, make oil product mix the processing of decolouring with decolorizer by agitating device, will be transported to fine filter by oil drain pump through the oil product that decolouring is handled at last and remove remaining decolorizer and other impurity.
By said system principle and the course of work as can be known, to the heating oil product later processing of decolouring that dewaters, send into filter again, filtering decolorizer and other impurity are both removed moisture contained in the oil product and impurity thereby reached, and improve the purpose of oil product color again; The temperature that oil product need reach when separating contained humidity in the oil product is generally at 40 ℃～80 ℃, and the general the best in 110 ℃ of the required temperature of oil product decolouring; Be subjected to oil drain pump that system joins, vavuum pump etc. to the restriction of temperature aspect because of existing for the iundustrial oil cleaning system of improving the oil product color simultaneously, can only heat oil product by separating the used heater of moisture, so it is lower to the oil decolorization treatment effeciency, effect is also not obvious, has also increased the use cost of equipment simultaneously.
The utility model content
According to above deficiency of the prior art, the technical problems to be solved in the utility model is: provide a kind of for iundustrial oil reactor formula decolouring device, it is simple in structure, has improved the decolouring treatment effeciency, reduces use cost.
Described in the utility model for iundustrial oil reactor formula decolouring device, comprise tank body, tank base is provided with material inlet and material outlet, the tank body top is equipped with agitator, it is characterized in that: on the tank body left side wall heater is installed, the fire end of heater is arranged in the tank body, and the temperature monitor for temperature detection in the tank body is installed on the tank body right side wall, in tank body, be provided with the cooling pipeline, in the tank body upper portion side wall decolorizer storage tank be installed.
During use, in the decolorizer storage tank, deposit decolorizer in, oil product enters in the tank body by material inlet when waiting to decolour, again according to the demonstration of temperature monitor, select whether to start heater or cooling pipeline and treat the decolouring oil product and heat or cool off, under the effect of agitator and decolorizer, the processing of will oil product be decoloured decolouring, after treating that decolouring disposes, use the oil product temperature after the cooling pipeline will decolour to be down to normal temperature, can carry out further work.
The preferred described decolorizer storage tank of the utility model is communicated with the tank body upper portion side wall by one section horizontally disposed horizontal pipeline, and horizontal pipeline one end is communicated with the material outlet of decolorizer storage tank, and the other end is communicated with the tank body upper portion side wall is tangent.
When the decolorizer blanking, horizontal pipeline cut is communicated with tank body, and making decolorizer during pan feeding is not directly vertically to enter, but enters around a vortex of tank inner surface, has shortened the incorporation time of decolorizer and oil product greatly, has improved production efficiency.
The further shaft of preferred described cooling tube wire-wound agitator settings of spiraling of the utility model, the diameter that spirals is greater than the stirring vane rotating diameter of agitator, and the cooling water inlet and the coolant outlet that cool off on the pipeline are installed in respectively on the tank body lateral wall.
When using, the cooling pipeline can also also can directly arrange the cooling jacket layer at tank inner surface or outer surface around the tank body outer surface, and just cooling effect does not have aforesaid way obvious, and if the chuck layer is set has also increased manufacturing cost.
Further preferred described heater is three flange form heating tubes, evenly is installed on the vertical direction of tank body respectively.
During application, heater can adopt the heating of alternate manner, as steam jacket etc.
Observe the decolouring situation in the tank body for convenience, at described tank body front side wall middle part visor is installed.
Observe oil product liquid level in the tank body for convenience, at described tank body rear wall liquid level gauge is installed.
Control for convenience is servomotor at the actuating unit of described agitator, and corresponding servomotor is provided with control cabinet.
Further in order to improve automaticity and control accuracy, heating control end and the temperature monitor signal output part of described heater is connected with control cabinet by control line respectively.Control system in the control cabinet is the known technology of present technique personnel.
Compared with prior art, the utlity model has following beneficial effect:
Pass through the utility model, it is simple in structure, changed original employing by separating the mode that the used heater of moisture heats oil product, under the effect of heater, temperature monitor and agitator, can treat the decolouring oil product reasonably heats up, guarantee the oil product decolorization rate effectively, improved production efficiency, also reduced production cost simultaneously; Under the effect of cooling pipeline, after oil product decolouring flow process is finished, oil product can be cooled fast to normal temperature, the oil product after will decolouring by existing oil drain pump again is transported to fine filter and removes remaining decolorizer and other impurity; Under the effect of horizontal pipeline, horizontal pipeline cut is communicated with tank body, and making decolorizer during pan feeding is not directly vertically to enter, but enters around a vortex of tank inner surface, has shortened the incorporation time of decolorizer and oil product greatly, has improved production efficiency.
Description of drawings
Fig. 1 is the utility model part section structural representation;
Fig. 2 is the plan structure schematic diagram of Fig. 1;
Among the figure: 1, agitator 2, decolorizer storage tank 3, horizontal pipeline 4, cooling water inlet 5, temperature monitor 6, cooling pipeline 7, coolant outlet 8, shaft 9, stirring vane 10, material outlet 11, material inlet 12, heater 13, tank body 14, liquid level gauge 15, visor.
The specific embodiment
Below the utility model is described in further detail by specific embodiment; but not in order to limit the utility model; all within the present invention spirit and principle, any modification of doing, be equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
As shown in Figure 1 and Figure 2, be used for iundustrial oil reactor formula decolouring device, comprise tank body 13, tank body 13 bottoms are provided with material inlet 11 and material outlet 10, and tank body 13 tops are equipped with agitator 1, on tank body 13 left side walls heater 12 are installed, the fire end of heater 12 is arranged in the tank body 13, temperature monitor 5 for temperature detection in the tank body 13 is installed on tank body 13 right side walls, in tank body 13, is provided with cooling pipeline 6, in tank body 13 upper portion side wall decolorizer storage tank 2 is installed.
In the present embodiment, described decolorizer storage tank 2 is communicated with tank body 13 upper portion side wall by one section horizontally disposed horizontal pipeline 3, and horizontal pipeline 3 one ends are communicated with the material outlet of decolorizer storage tank 2, the other end and tangent connection of tank body 13 upper portion side wall; Described cooling pipeline 6 is around the setting of spiraling of the shaft 8 of agitator 1, and the diameter that spirals is greater than stirring vane 9 rotating diameters of agitator 1, and cooling water inlet 4 and coolant outlet 7 on the cooling pipeline 6 are installed in respectively on tank body 13 lateral walls; Described heater 12 is three flange form heating tubes, evenly is installed on the vertical direction of tank body 13 respectively; Described tank body 13 front side walls middle part is equipped with visor 15; On described tank body 13 rear walls liquid level gauge 14 is installed; The actuating unit of described agitator 1 is servomotor, and corresponding servomotor is provided with control cabinet; The heating control end of described heater 12 and temperature monitor 5 signal output parts are connected with control cabinet by control line respectively.
The position relation of the above-mentioned parts of present embodiment on tank body 13 can carry out freely changing according to on-the-spot mounting condition.
During use, in decolorizer storage tank 2, deposit decolorizer in, oil product enters in the tank body 13 by material inlet when waiting to decolour, again according to the demonstration of temperature monitor 5, select whether to start heater 12 or cooling pipeline 6 and treat the decolouring oil product and heat or cool off, under the effect of agitator 1 and decolorizer, the processing of will oil product be decoloured decolouring, after treating that decolouring disposes, use the oil product temperature after cooling pipeline 6 will decolour to be down to normal temperature, can carry out further work.
Claims (8)
1. one kind is used for iundustrial oil reactor formula decolouring device, comprise tank body (13), tank body (13) bottom is provided with material inlet (11) and material outlet (10), tank body (13) top is equipped with agitator (1), it is characterized in that: on tank body (13) left side wall heater (12) is installed, the fire end of heater (12) is arranged in the tank body (13), temperature monitor (5) for the interior temperature detection of tank body (13) is installed on tank body (13) right side wall, in tank body (13), be provided with cooling pipeline (6), in tank body (13) upper portion side wall decolorizer storage tank (2) be installed.
2. according to claim 1 for iundustrial oil reactor formula decolouring device, it is characterized in that: described decolorizer storage tank (2) is communicated with tank body (13) upper portion side wall by one section horizontally disposed horizontal pipeline (3), horizontal pipeline (3) one ends are communicated with the material outlet of decolorizer storage tank (2), the other end and tank body (13) the tangent connection of upper portion side wall.
3. according to claim 1 for iundustrial oil reactor formula decolouring device, it is characterized in that: the setting of spiraling of the shaft (8) of described cooling pipeline (6) around agitator (1), the diameter that spirals is greater than stirring vane (9) rotating diameter of agitator (1), and cooling water inlet (4) and coolant outlet (7) on the cooling pipeline (6) are installed in respectively on tank body (13) lateral wall.
4. according to claim 1 for iundustrial oil reactor formula decolouring device, it is characterized in that: described heater (12) is three flange form heating tubes, evenly is installed on the vertical direction of tank body (13) respectively.
5. according to claim 1 for iundustrial oil reactor formula decolouring device, it is characterized in that: described tank body (13) front side wall middle part is equipped with visor (15).
6. according to claim 1 for iundustrial oil reactor formula decolouring device, it is characterized in that: on described tank body (13) rear wall liquid level gauge (14) is installed.
7. according to claim 1 for iundustrial oil reactor formula decolouring device, it is characterized in that: the actuating unit of described agitator (1) is servomotor, and corresponding servomotor is provided with control cabinet.
8. according to claim 7 for iundustrial oil reactor formula decolouring device, it is characterized in that: the heating control end of described heater (12) and temperature monitor (5) signal output part are connected with control cabinet by control line respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320155839 CN203170324U (en) | 2013-04-01 | 2013-04-01 | Industrial oil reaction kettle type decoloring device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320155839 CN203170324U (en) | 2013-04-01 | 2013-04-01 | Industrial oil reaction kettle type decoloring device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203170324U true CN203170324U (en) | 2013-09-04 |
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ID=49067079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320155839 Expired - Fee Related CN203170324U (en) | 2013-04-01 | 2013-04-01 | Industrial oil reaction kettle type decoloring device |
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| CN (1) | CN203170324U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105396530A (en) * | 2014-09-12 | 2016-03-16 | 天津法莫西医药科技有限公司 | Biochemical reaction apparatus for preparing biological preparations |
-
2013
- 2013-04-01 CN CN 201320155839 patent/CN203170324U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105396530A (en) * | 2014-09-12 | 2016-03-16 | 天津法莫西医药科技有限公司 | Biochemical reaction apparatus for preparing biological preparations |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130904 Termination date: 20140401 |