CN210711460U - Oil and fat refining production system utilizing waste argil - Google Patents
Oil and fat refining production system utilizing waste argil Download PDFInfo
- Publication number
- CN210711460U CN210711460U CN201921010711.1U CN201921010711U CN210711460U CN 210711460 U CN210711460 U CN 210711460U CN 201921010711 U CN201921010711 U CN 201921010711U CN 210711460 U CN210711460 U CN 210711460U
- Authority
- CN
- China
- Prior art keywords
- oil
- decoloring
- tower
- decoloration
- filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Abstract
The utility model discloses an utilize concise production system of grease of useless carclazyte, including dry oil tank, decoloration tower, decoloration oil tank and filter in advance. The utility model discloses in, can directly arrange into the bleaching tower with the drier oil in the drier oil tank, can add new carclazyte in the bleaching tower, discharge into the filter with the oil after the decoloration (the oil after the decoloration has useless carclazyte) after the decoloration of carclazyte, can filter out useless carclazyte through the filtering action of filter, the oil after filtration and decoloration then discharges into in the subsequent process; because the utility model discloses increased the decoloration oil tank in advance, carclazyte in the filter has certain decoloration ability in addition, consequently, can directly discharge the filter with the drying oil in the drying oil tank and carry out the decoloration in advance to in the decoloration oil tank is discharged in advance to the decoloration oil in advance, decoloration tower is carried out to the decoloration oil in advance can be arranged into together with the drying oil in the drying oil tank, and the useless carclazyte after accomplishing the decoloration in advance is then discharged as the discarded object and is walked.
Description
Technical Field
The utility model belongs to the technical field of the concise production of grease, concretely relates to utilize concise production system of grease of useless carclazyte.
Background
In the current oil refining process, most of the waste argil filtered by the filter is directly discharged as waste by a factory; usually, the waste clay still has 15 to 30 percent of residual decolorization capacity, in order to save the clay consumption, some factories also increase pre-decolorization processes and equipment, but the processes and the equipment are more complicated to control, and the processes and the equipment have poor stability and low investment return from the practical operation; and the operation is complicated, which increases the operation load and labor intensity of the plant.
SUMMERY OF THE UTILITY MODEL
In order to solve the problems existing in the prior art, the utility model aims to provide an oil and fat refining production system utilizing waste argil.
According to an aspect of the utility model, an utilize refined production system of grease of useless carclazyte is provided, including dry oil tank, decoloration tower, decoloration oil tank and filter in advance, the dry oil tank is filled with dry oil, and dry oil tank is linked together with the decoloration tower, and dry oil and carclazyte in the dry oil tank arrange into the decoloration tower, and the decoloration tower is linked together with the filter, and the oil after the decoloration of decoloration tower arranges into the filter and filters the decoloration; the drying oil tank is communicated with the filter, the drying oil in the drying oil tank is directly discharged into the filter for pre-decoloring, the filter is communicated with the pre-decoloring oil tank, the filter discharges the pre-decoloring oil into the pre-decoloring oil tank, the pre-decoloring oil tank is communicated with the decoloring tower, and the pre-decoloring oil in the pre-decoloring oil tank is discharged into the decoloring tower.
The utility model discloses in, can directly arrange into the bleaching tower with the drier oil in the dry oil tank, can add new carclazyte in the bleaching tower, discharge the oil after the decoloration (the oil after the decoloration has useless carclazyte) into the filter after the decoloration of carclazyte, can filter out useless carclazyte (the carclazyte after having decolored the drier oil promptly) through the filtering action of filter, the oil after filtering and decoloration then discharges into in subsequent process; because the utility model discloses increased the decoloration oil tank in advance, carclazyte in the filter has certain decoloration ability in addition, consequently, can directly discharge the dry oil in the dry oil tank into the filter and carry out the decoloration in advance to discharge the decoloration oil in advance into the decoloration oil tank in advance, the decoloration tower is carried out to the decoloration in advance can be discharged into together with the dry oil in the dry oil tank (also can discharge into alone and carry out the decoloration in the decoloration tower), and the completion is useless carclazyte after the decoloration in advance then is discharged away as the discarded object.
In some embodiments, a first regulating valve, a drying pump and a first switch valve are sequentially arranged between the drying oil tank and the decoloring tower, the first regulating valve is used for regulating the flow rate of a pipeline between the drying oil tank and the decoloring tower, the drying pump is used for discharging the drying oil in the drying oil tank into the decoloring tower, and the drying pump is used for discharging the oil after being subjected to pre-decoloring in the pre-decoloring oil tank into the decoloring tower. Therefore, the first switch valve can close the pipeline between the drying oil tank and the decoloring tower, so that the drying oil tank and the decoloring tower cannot be communicated.
In some embodiments, a decoloring pump is arranged between the decoloring tower and the filter, the decoloring pump discharges the decolored oil in the decoloring tower into the filter, and the decoloring pump discharges the dry oil in the dry oil tank into the filter. Therefore, the decolorizing pump can pump the decolorized oil in the decolorizing tower and discharge the decolorized oil into the filter for filtration.
In some embodiments, the device further comprises a clay mixing tank, clay is filled in the clay mixing tank, a stirrer is arranged on the clay mixing tank, the clay mixing tank is communicated with the decoloring tower through an inclined pipeline, and a flow regulating valve is arranged between the clay mixing tank and the decoloring tower. Therefore, the stirring machine can fully mix the argil with other substances, so that the argil has better decolorization capacity.
In some embodiments, a second switch valve and a pressure gauge are further arranged on the pipeline between the decoloring tower and the filter, the second switch valve is used for adjusting the switch of the pipeline between the decoloring tower and the filter, and the pressure gauge is used for detecting the flow in the pipeline between the decoloring tower and the filter.
In some embodiments, a third switch valve is arranged between the pre-decoloring oil tank and the filter, and a second regulating valve is arranged between the pre-decoloring oil tank and the drying pump.
Drawings
FIG. 1 is a schematic view of a part of a structure of an oil and fat refining production system using spent bleaching earth according to an embodiment of the present invention;
FIG. 2 is a schematic view of a part of the structure of an oil and fat refining production system using spent bleaching earth according to an embodiment of the present invention;
FIG. 3 is a schematic view of an oil and fat refining production system using spent bleaching earth according to an embodiment of the present invention;
in the figure: 1-drying the oil tank; 11-a first regulating valve; 12-a dry pump; 13-a first on-off valve; 2-a decolouring tower; 21-a decolorizing pump; 22-pressure gauge; 23-a second on-off valve; 3-a filter; 4-pre-decolorizing oil tank; 41-second regulating valve; 42-a third on-off valve; 5-clay mixing tank; 51-a flow regulating valve; 52-stirrer.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention.
Fig. 1 to 3 schematically show the configuration of an oil and fat refining production system using spent bleaching earth according to an embodiment of the present invention.
As shown in fig. 1 to 3, an oil and fat refining production system using spent bleaching earth comprises a drying oil tank 1, a bleaching tower 2, a pre-bleaching oil tank 4 and a filter 3. In addition, this utilize fat and oil refining production system of spent bleaching clay still includes bleaching clay blending tank 5.
In the utility model, after the combination of the figure 1 and the figure 2, the structure of the complete oil refining production system using the waste carclazyte of the utility model is shown schematically; the main reasons are: because fig. 1 and 2 are too large, for the convenience of viewing, fig. 1 and 2 are separated, and at the same time, for the convenience of understanding, a simplified diagram (i.e., fig. 3) of the oil and fat refining production system using spent bleaching earth of the present invention is added.
In this embodiment, as shown in FIG. 3, in this embodiment, a dry oil (dry oil: oil treated in the previous step, which is to be decolorized) is contained in a dry oil tank 1, the dry oil tank 1 is communicated with a decolorization tower 2, the dry oil and clay in the dry oil tank 1 can be discharged into the decolorization tower 2, the decolorization tower 2 is communicated with a filter 3, and the oil decolorized by the decolorization tower 2 is discharged into the filter 3 to be filtered and decolorized. The part is normal decolorization and filtration, the oil decolorized by the decolorization tower 2 and filtered by the filter 3 is discharged into the subsequent process, and the subsequent treatment mode is the prior art and is not described again.
In addition, in order to make full use of useless carclazyte (the carclazyte that has handled the drying oil above promptly), the utility model discloses increased decoloration oil tank 4 in advance, drying oil tank 1 is linked together with filter 3, and the drying oil in the drying oil tank 1 directly discharges to carry out the decoloration in advance in filter 3, and filter 3 is linked together with decoloration oil tank 4 in advance, and filter 3 will discharge the decoloration oil in advance in decoloration oil tank 4 in advance, and decoloration oil tank 4 and decoloration tower 2 intercommunication in advance, the decoloration oil in advance in the decoloration oil tank 4 discharges into in the decoloration tower 2.
The communication (generally through a pipeline, and belonging to the prior art) refers to: under a certain working state, the two parts are communicated, but under some conditions, if the communication between the two parts is not needed, the two parts can be blocked by a valve (such as a pneumatic switch valve or a manual valve) and can not be communicated; therefore, the communication is not always in a communicating state, but is adjusted as necessary to select whether or not the communication between the two is established.
In this embodiment, as shown in fig. 1 to fig. 3, a first regulating valve 11, a drying pump 12 and a first switch valve 13 are sequentially disposed between the drying oil tank 1 and the decoloring tower 2 (i.e. the first regulating valve 11 is closest to the drying oil tank 1, and the first switch valve 13 is farthest from the drying oil tank 1), the first regulating valve 11 can regulate the flow rate of the pipeline between the drying oil tank 1 and the decoloring tower 2, and the drying oil in the drying oil tank 1 continuously flows into the decoloring tower 2 by controlling the first regulating valve 11, so that the decoloring can be continuously performed, on the one hand, the drying pump 12 of the present invention can extract the drying oil in the drying oil tank 1, and then discharge the drying oil into the decoloring tower 2 through the pipeline; on the other hand, a dry pump 12 (which may be different from or the same as the dry pump 12 for sucking up the dry oil in the dry oil tank 1) is used for discharging the oil after the preliminary decoloring in the preliminary decoloring oil tank 4 into the decoloring tower 2.
As shown in fig. 3, in this embodiment, a decolorizing pump 21 is provided between the decolorizing tower 2 and the filter 3, the decolorizing pump 21 discharges the oil decolorized in the decolorizing tower 2 into the filter 3, and the decolorizing pump 21 can also directly discharge the dry oil in the dry oil tank 1 into the filter 3, so that the decolorizing pump 21 can pump the oil decolorized in the decolorizing tower 2 and discharge the oil decolorized into the filter 3 for filtration.
As shown in fig. 3, in the present embodiment, a (fresh) clay, that is, an unused clay is contained in the clay mixing tank 5, a stirrer 52 is installed in the clay mixing tank 5, the clay mixing tank 5 is communicated with the decoloring tower 2 through an inclined pipe, and a flow rate control valve 51 is provided between the clay mixing tank 5 and the decoloring tower 2. The agitator 52 can sufficiently mix the clay with other substances to make the clay have better decoloring ability, and when the flow control valve 51 is opened, the clay mixing tank 5 is communicated with the decoloring tower 2 through an inclined pipeline, so that the clay in the clay mixing tank 5 can be discharged into the decoloring tower 2 at a certain speed and sufficiently mixed with the dry oil or the pre-decolored oil.
As shown in fig. 3, in this embodiment, a second switch valve 23 and a pressure gauge 22 are further disposed on the pipeline between the decoloring tower 2 and the filtering machine 3, the second switch valve 23 is used for adjusting the opening and closing of the pipeline between the decoloring tower 2 and the filtering machine 3, and the pressure gauge 22 is used for detecting the flow rate in the pipeline between the decoloring tower 2 and the filtering machine 3.
As shown in fig. 3, in the present embodiment, a third on/off valve 42 is provided between the preliminary decolorizing oil tank 4 and the filter 3, a second regulating valve 41 is provided between the preliminary decolorizing oil tank 4 and the drying pump 12, and the second regulating valve 41 is used to regulate the flow rate of the drying pump 12.
Fig. 1 and 2 also show the specific connection mode of the oil refining production system using waste white clay according to the present invention, since the technician of the present invention can clearly know how to perform the connection according to the above-described effect or structure, and fig. 1 and 2 also show the specific connection mode, therefore, it will not be described in detail herein; in addition, the present invention also includes a large number of valves, controllers, and other devices, and since how these devices are installed and the specific installation manner are the existing manner, the detailed description is not repeated here.
The utility model discloses in, can directly arrange into the decoloration tower 2 through drying pump 12 with the drier oil in the drier oil tank 1, can add the carclazyte in the carclazyte blending tank 5 to the decoloration tower 2, in the decoloration tower 2 through the decoloration of carclazyte after with the oil after the decoloration discharge filter 3 through decoloration pump 21 (the oil after the decoloration has carclazyte), can filter out useless carclazyte (namely the carclazyte after having decolored the drier oil) through the filtering action of filter 3, the oil after filtration and the decoloration is then discharged into in subsequent process; because the utility model discloses increased decoloration oil tank 4 in advance, carclazyte in filter 3 also has certain decoloration ability, filter out in the filter 3 carclazyte when reaching a quantitative, can directly arrange the drying oil in the drying oil tank 1 into filter 3 through decoloration pump 21 and carry out decoloration in advance (this moment, drying pump 12 can not discharge the drying oil in the drying oil tank 1 into decoloration tower 2), and will in advance decoloration oil row (can directly flow in through the pipeline) in the decoloration oil tank 4 in advance, in advance decoloration oil can be arranged into decoloration tower 2 with the drying oil in the drying oil tank 1 through drying pump 12 together and carry out the decoloration (can also discharge in decoloration tower 2 alone and carry out the decoloration), the useless carclazyte after accomplishing decoloration then is arranged as the discarded object and is walked.
The utility model discloses an opening and closing of each part all can be controlled through control module, and specific control mode is current mode, and no longer the repeated description here.
The present invention is not limited to the above-mentioned optional embodiments, and any other products in various forms can be obtained by anyone under the teaching of the present invention, and any changes in the shape or structure thereof, all the technical solutions falling within the scope of the present invention, are within the protection scope of the present invention.
Claims (6)
1. The utility model provides an utilize refined production system of grease of useless carclazyte which characterized in that: the device comprises a drying oil tank (1), a decoloring tower (2), a pre-decoloring oil tank (4) and a filter (3), wherein drying oil is filled in the drying oil tank (1), the drying oil tank (1) is communicated with the decoloring tower (2), the drying oil and clay in the drying oil tank (1) are discharged into the decoloring tower (2), the decoloring tower (2) is communicated with the filter (3), and the oil decolored by the decoloring tower (2) is discharged into the filter (3) for filtering;
the drying oil tank (1) is communicated with the filter (3), the drying oil in the drying oil tank (1) is directly discharged into the filter (3) for pre-decoloring, the filter (3) is communicated with the pre-decoloring oil tank (4), the pre-decoloring oil is discharged into the pre-decoloring oil tank (4) by the filter (3), the pre-decoloring oil tank (4) is communicated with the decoloring tower (2), and the pre-decoloring oil in the pre-decoloring oil tank (4) is discharged into the decoloring tower (2).
2. The system for refining and producing oil and fat by using spent bleaching earth according to claim 1, wherein: a first adjusting valve (11), a drying pump (12) and a first switch valve (13) are sequentially arranged between the drying oil tank (1) and the decoloring tower (2), the first adjusting valve (11) is used for adjusting the flow of a pipeline between the drying oil tank (1) and the decoloring tower (2), the drying pump (12) is used for discharging the drying oil in the drying oil tank (1) into the decoloring tower (2), and the drying pump (12) is used for discharging the oil subjected to pre-decoloring in the pre-decoloring oil tank (4) into the decoloring tower (2).
3. The system for refining and producing oil and fat by using spent bleaching earth according to claim 2, wherein: a decoloring pump (21) is arranged between the decoloring tower (2) and the filter (3), the decolored oil in the decoloring tower (2) is discharged into the filter (3) by the decoloring pump (21), and the dried oil in the dried oil tank (1) is discharged into the filter (3) by the decoloring pump (21).
4. The system for refining and producing oil and fat by using spent bleaching earth according to claim 3, wherein: still include carclazyte blending tank (5), be equipped with carclazyte in carclazyte blending tank (5), be equipped with mixer (52) on carclazyte blending tank (5), carclazyte blending tank (5) through the pipeline of slope with decoloration tower (2) are linked together, carclazyte blending tank (5) with be equipped with flow control valve (51) between decoloration tower (2).
5. The system for refining and producing oil and fat by using spent bleaching clay according to claim 4, wherein: the utility model discloses a decoloration tower, including decoloration tower (2) and filter (3), still be equipped with second ooff valve (23) and manometer (22) on the pipeline between decoloration tower (2) and filter (3), second ooff valve (23) are used for adjusting decoloration tower (2) with the switch of pipeline between filter (3), manometer (22) with detect decoloration tower (2) with flow in the filter (3) pipeline.
6. The system for refining and producing oil and fat using spent bleaching earth according to claim 5, wherein: a third switch valve (42) is arranged between the pre-decolorizing oil tank (4) and the filter (3), and the second regulating valve (41) is arranged between the pre-decolorizing oil tank (4) and the drying pump (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921010711.1U CN210711460U (en) | 2019-07-01 | 2019-07-01 | Oil and fat refining production system utilizing waste argil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921010711.1U CN210711460U (en) | 2019-07-01 | 2019-07-01 | Oil and fat refining production system utilizing waste argil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210711460U true CN210711460U (en) | 2020-06-09 |
Family
ID=70966163
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921010711.1U Active CN210711460U (en) | 2019-07-01 | 2019-07-01 | Oil and fat refining production system utilizing waste argil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210711460U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115651759A (en) * | 2022-11-07 | 2023-01-31 | 山东凯斯达机械制造有限公司 | Automatic filtering system for grease decoloring and use method thereof |
-
2019
- 2019-07-01 CN CN201921010711.1U patent/CN210711460U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115651759A (en) * | 2022-11-07 | 2023-01-31 | 山东凯斯达机械制造有限公司 | Automatic filtering system for grease decoloring and use method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN210711460U (en) | Oil and fat refining production system utilizing waste argil | |
| CN102676296B (en) | Grease decoloring system and continuous grease decoloring method | |
| CN106435042A (en) | Automatic liquid glucose carbon addition type syrup color removal method | |
| CN103736321A (en) | Intelligent settling self-cleaning filter | |
| CN201208532Y (en) | Connection structure of filter | |
| CN202247606U (en) | Monitoring and controlling system for movable type warm-mixed asphalt production equipment | |
| CN209791058U (en) | High-efficient decoloration filter equipment of oil environmental protection | |
| CN209741094U (en) | Grease decoloration system who contains vertical leaf filter | |
| CN216843029U (en) | Mining speed reducer washs equipment of changing oil | |
| CN112642196A (en) | Waste acid filtering device | |
| CN202626144U (en) | Oil decolorizing system and preliminary decolorizing tower | |
| CN205068110U (en) | Product tank cleaning equipment's controlling means | |
| CN103752469B (en) | Coating machine charging system | |
| CN211946944U (en) | Grease decoloration system | |
| JP2022522533A (en) | Decolorization filtration device for xylose hydrolyzate and its decolorization filtration method | |
| CN201098584Y (en) | Rotary press filter intelligent controller | |
| CN109810776B (en) | Grease decoloring system and process containing vertical leaf filter | |
| CN203355358U (en) | Continuous activated carbon decolorizing device for manufacturing sodium gluconate | |
| CN209076127U (en) | A kind of filter press filtering condition monitoring system | |
| CN209143788U (en) | PAM chemicals dosing plant | |
| CN203664141U (en) | Feeding system of coating machine | |
| CN104818348A (en) | Classified filtering pre-liming tank | |
| CN208995462U (en) | A kind of electric energy grease conche | |
| CN218811297U (en) | Sludge conditioning, filter-pressing and dewatering system | |
| CN211462363U (en) | Xylose hydrolysate decoloration filter equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210819 Address after: 510000 room 905, 81 Donghui 2nd Street, Huangpu District, Guangzhou City, Guangdong Province Patentee after: SEVIS (Guangzhou) Engineering Technology Co.,Ltd. Address before: 239000 Room 204, unit 2, building 4, Dongyuan community, wujingzi Road, Xianghe Town, Quanjiao County, Chuzhou City, Anhui Province Patentee before: Liu Ronghui |