CN203668339U - Pretreatment device for raw material of biodiesel - Google Patents
Pretreatment device for raw material of biodiesel Download PDFInfo
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- CN203668339U CN203668339U CN201320718474.0U CN201320718474U CN203668339U CN 203668339 U CN203668339 U CN 203668339U CN 201320718474 U CN201320718474 U CN 201320718474U CN 203668339 U CN203668339 U CN 203668339U
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- tank
- raw material
- biodiesel
- pipeline
- glue kettle
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Abstract
The utility model relates to a pretreatment device for a raw material of biodiesel, and belongs to the technical field of biodiesel pretreatment. The pretreatment device comprises a raw material oil unloading tank and a degumming tank provided with a stirrer, wherein a discharge opening is formed in the bottom of the degumming tank. The pretreatment device is characterized in that the raw material oil unloading tank is connected and communicated with the top of the degumming tank through pipelines, a heating tank is arranged on a pipeline between the raw material oil unloading tank and the degumming tank, a material inlet is formed in the top of the heating tank, a material outlet is formed in the bottom, a primary delivery pump is arranged on a feeding pipeline of the heating tank, a secondary delivery pump is arranged on a discharging pipeline of the heating tank, and an additive preparation tank is arranged at the top of the degumming tank and is connected and communicated with the top of the degumming tank. The pretreatment device for the raw material of the biodiesel is simple in structure and lower in cost investment, and increases the whole speed for removing colloid and impurities during pretreatment of the raw material of the biodiesel.
Description
Technical field
The utility model relates to a kind of biodiesel raw material pretreatment unit, belongs to biofuel preconditioning technique field.
Background technology
At present, in the raw material for the production of biofuel, contain colloid and impurity, in the time carrying out esterification, if do not carry out pre-treatment, will blocking pipe, be even bonded on reactor inwall, affect integral production technique.The conventional method of removing colloid and impurity mainly contains natural subsidence and filtration, in use, have following deficiency: 1, natural subsidence speed is slow, and part colloid can not be removed; 2, adopt the mode of filtering, it filters, and labor capacity is large, and filter cloth replacing is frequent, and production cost is high.
Utility model content
According to above deficiency of the prior art, the technical problems to be solved in the utility model is: a kind of biodiesel raw material pretreatment unit is provided, and it is simple in structure, in the time carrying out the pre-treatment of biodiesel raw material, accelerated to remove the speed of colloid and impurity, and cost drops into lower.
Biodiesel raw material pretreatment unit described in the utility model, comprise that raw material unloads the glue kettle of oil sump and belt stirrer, glue kettle bottom is provided with discharge port, it is characterized in that: raw material unloads oil sump and is connected and communicates with glue kettle top by pipeline, unload on the pipeline between oil sump and glue kettle and be provided with warming tank at raw material, warming tank top is material inlet, its bottom is material outlet, on the feeding line of warming tank, be provided with one-level transferpump, on the discharging pipeline of warming tank, be provided with two-stage conveying pump, be provided with additive preparing tank at glue kettle top, additive preparing tank is connected and communicates with glue kettle top by pipeline.
In the utility model, the preferably following two kinds of modes of warming tank:
One, described warming tank is steam heating type.
Two, described warming tank is electrical heating type.
Compared with prior art, the utlity model has following beneficial effect:
By the utility model, it is simple in structure, in the time carrying out the pre-treatment of biodiesel raw material, has accelerated whole speed of removing colloid and impurity, and cost drops into lower.Under the effect of warming tank, improve the temperature of biodiesel raw material, be conducive to the glue kettle work of coming unstuck, and can effectively prevent that colloid from sticking on the inwall of glue kettle.Under the effect of the agitator of glue kettle, impurity in biodiesel raw material and the separation of colloid are accelerated, and be deposited in glue kettle bottom, then first impurity and colloid are discharged by discharge port, then the biofuel stoste of handling well is delivered in next operation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure: 1, additive preparing tank 2, glue kettle 3, warming tank 4, raw material unload oil sump 5, one-level transferpump 6, two-stage conveying pump.
Embodiment
Below by specific embodiment, the utility model is described in further detail; 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., within all should being included in protection domain of the present utility model.
As shown in Figure 1, biodiesel raw material pretreatment unit, comprise that raw material unloads the glue kettle 2 of oil sump 4 and belt stirrer, glue kettle 2 bottoms are provided with discharge port, raw material unloads oil sump 4 and is connected and communicates with glue kettle 2 tops by pipeline, unload on the pipeline between oil sump 4 and glue kettle 2 and be provided with warming tank 3 at raw material, warming tank 3 tops are material inlet, its bottom is material outlet, on the feeding line of warming tank 3, be provided with one-level transferpump 5, on the discharging pipeline of warming tank 3, be provided with two-stage conveying pump 6, be provided with additive preparing tank 1 at glue kettle 2 tops, additive preparing tank 1 is connected and communicates with glue kettle 2 tops by pipeline.
In the present embodiment, described warming tank 3 is steam heating type, and in the time of practical application, warming tank 3 is electrical heating type; On described warming tank 3, be provided with thermometer and liquidometer.
When production and application, first by one-level transferpump 5, the biodiesel raw material that contains colloid and impurity is delivered to warming tank 3, by warming tank 3, its temperature is warmed between 50 to 60 degree, by two-stage conveying pump 6, the biodiesel raw material mixture heating is delivered to glue kettle 2 again, by additive preparing tank 1, the additive that comes unstuck configuring is sent into glue kettle 2 (approximately add biodiesel raw material mixture weight 0.5%), stir, stir about is quiescent settling after 30 minutes, finally first impurity and colloid are discharged by the discharge port of glue kettle 2 bottoms, again the biodiesel raw material of handling well is transported to next operation.
Claims (3)
1. a biodiesel raw material pretreatment unit, comprise that raw material unloads the glue kettle (2) of oil sump (4) and belt stirrer, glue kettle (2) bottom is provided with discharge port, it is characterized in that: raw material unloads oil sump (4) and is connected and communicates with glue kettle (2) top by pipeline, unload on the pipeline between oil sump (4) and glue kettle (2) and be provided with warming tank (3) at raw material, warming tank (3) top is material inlet, its bottom is material outlet, on the feeding line of warming tank (3), be provided with one-level transferpump (5), on the discharging pipeline of warming tank (3), be provided with two-stage conveying pump (6), be provided with additive preparing tank (1) at glue kettle (2) top, additive preparing tank (1) is connected and communicates with glue kettle (2) top by pipeline.
2. biodiesel raw material pretreatment unit according to claim 1, is characterized in that: described warming tank (3) is steam heating type.
3. biodiesel raw material pretreatment unit according to claim 1, is characterized in that: described warming tank (3) is electrical heating type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320718474.0U CN203668339U (en) | 2013-11-15 | 2013-11-15 | Pretreatment device for raw material of biodiesel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320718474.0U CN203668339U (en) | 2013-11-15 | 2013-11-15 | Pretreatment device for raw material of biodiesel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203668339U true CN203668339U (en) | 2014-06-25 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320718474.0U Expired - Fee Related CN203668339U (en) | 2013-11-15 | 2013-11-15 | Pretreatment device for raw material of biodiesel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203668339U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104479863A (en) * | 2014-12-11 | 2015-04-01 | 平顶山市亿鑫达生物能源有限公司 | Device and method for pre-treating raw oil for production of biodiesel |
-
2013
- 2013-11-15 CN CN201320718474.0U patent/CN203668339U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104479863A (en) * | 2014-12-11 | 2015-04-01 | 平顶山市亿鑫达生物能源有限公司 | Device and method for pre-treating raw oil for production of biodiesel |
| CN104479863B (en) * | 2014-12-11 | 2017-10-24 | 平顶山市亿鑫达生物能源有限公司 | A kind of production of biodiesel feedstock oil pretreatment unit and its processing method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140625 Termination date: 20141115 |
|
| EXPY | Termination of patent right or utility model |