CN205252570U - Biodiesel distillation column - Google Patents
Biodiesel distillation column Download PDFInfo
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- CN205252570U CN205252570U CN201521018057.0U CN201521018057U CN205252570U CN 205252570 U CN205252570 U CN 205252570U CN 201521018057 U CN201521018057 U CN 201521018057U CN 205252570 U CN205252570 U CN 205252570U
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- heating coil
- electromagnetic heating
- vaporizer
- chamber
- vapour phase
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Abstract
The utility model discloses a biodiesel distillation column, including the tower body, tower body from the top down is equipped with vapour phase room, packing chamber, vaporizer, a vaporization separation chamber and reorganization receipt jar in proper order, the outside winding of vapour phase room has vapour phase room electromagnetic heating coil, and upper portion is equipped with vapour phase room sight glass and thermometer measurer, and the top is equipped with the vacuum mouth, the outside winding of vaporizer has vaporizer electromagnetic heating coil, and upper portion is equipped with the vaporizer sight glass, and the middle part is equipped with upper feeding port, and upper feeding port passes through the liquid distribution ware and is connected with the atomizer, and the lower part is equipped with down feed inlet and hydrocyclone, the outside winding of vaporization separation chamber has the vaporization electromagnetic heating coil of separation chamber, the outside winding of a reorganization receipt jar has reorganization part receipt jar electromagnetic heating coil, the utility model has the advantages of: simple structure, the thermal efficiency is high, and the energy consumption is low, and green has improved production efficiency, has reduced manufacturing cost, has increased economic benefits.
Description
Technical field
The utility model relates to a kind of biodiesel Preparation equipment, and specifically a kind of biofuel column belongs to biodiesel Preparation equipment field.
Background technology
Biodiesel is clean regenerative resource material, the liquid fuel that it is made taking the oil plant water plants such as oil-yielding shrubs fruit, the engineering microalgaes such as the oil crops such as soybean oil and rapeseed, oil palm and Chinese pistache and animal fat, meal kitchen waste grease etc. as raw material is the petroleum diesel substitute of high-quality. Biodiesel is typical case's " green energy resource ", greatly develops biodiesel to sustainable economic development, advances energy substitution, alleviates environmental pressure, controls urban atmospheric pollution and has important strategic importance. At present, in the traditional handicraft of preparation biodiesel, destilling tower adopts heat-conducting oil heating mode, need to increase heat-conducting oil furnace, has not only improved cost, and has pollution, is unfavorable for environmental protection; Destilling tower heats up slow, and material remaining time in tower is long, easily produces the coking phenomenon of material, and the rear cooling of stopping is also slow, thereby has reduced the efficiency of whole production system; Heat unnecessary in production cannot reclaim, and has increased energy consumption. Name is called " biofuel column " application number and discloses a kind of biofuel column for the Chinese utility model patent of " 200620127518.2 ". Belong to the technical field of separated. For solving, the power consumption of molecular clock tower is high, efficiency is low, investment is large and the problem of complicated operation for it. Biofuel column is to be connected to form with ring flange respectively by vapour phase chamber, filler chamber, vaporizer, vaporization separation chamber and heavy component receiving tank; Vapour phase chamber, vaporizer, vaporization separation chamber by the outside heat(ing) coil that is wound around of tower body, are provided with heat conductive oil inlet and conduction oil outlet respectively at heat(ing) coil two ends, tower body top is provided with vacuum port; The upper feeding mouth that vaporizer tower body middle part is provided with is connected with atomizer by liquid distributor, and vaporizer tower body bottom is provided with lower charging aperture and cyclone hydraulic separators, the outlet of lower charging aperture with tangential direction by the outside of cyclone hydraulic separators; Heavy component receiving tank is by tank body outer most surrounding heating jacket, and the lower end of tank body is provided with non-products export. But this device still energy consumption is higher, production efficiency is lower, and the economic benefit having reduced, has improved production cost.
Utility model content
The purpose of this utility model is, has designed a kind of biofuel column, and simple in structure, the thermal efficiency is high, and energy consumption is low, and environmental protection has improved production efficiency, has reduced production cost, has increased economic benefit.
The technical solution of the utility model is:
A kind of biofuel column, comprises tower body, and described tower body is columniform tank body, and described tower body is provided with vapour phase chamber, filler chamber, vaporizer, vaporization separation chamber and heavy component receiving tank from top to bottom successively; The outside of described vapour phase chamber is wound with vapour phase chamber electromagnetic heating coil, the magnetic field of described vapour phase chamber electromagnetic heating coil is corresponding with the sidewall of described vapour phase chamber, thereby can carry out Electromagnetic Heating to the sidewall of vapour phase chamber by electromagnetic heating coil, not only the thermal efficiency is high, energy consumption is low, and environmental protection, the top of described vapour phase chamber is provided with vapour phase chamber visor and thermometer measuring device, and top is provided with vacuum port;
There is filling material described filler chamber inside;
Described vaporizer outside is wound with vaporizer electromagnetic heating coil, the magnetic field of described vaporizer electromagnetic heating coil is corresponding with the sidewall of described vaporizer, thereby can carry out Electromagnetic Heating to the sidewall of vaporizer by vaporizer electromagnetic heating coil, not only the thermal efficiency is high, energy consumption is low, and environmental protection, described vaporizer top is provided with vaporizer visor, middle part is provided with upper feeding mouth, described upper feeding mouth is connected with atomizer by liquid distributor, bottom is provided with lower charging aperture and cyclone hydraulic separators, the outlet of described lower charging aperture is passed through the outside of described cyclone hydraulic separators with tangential direction.
The outside of described vaporization separation chamber is wound with vaporization separation chamber electromagnetic heating coil, the magnetic field of described vaporization separation chamber electromagnetic heating coil is corresponding with the sidewall of described vaporization separation chamber, thereby can carry out Electromagnetic Heating to the sidewall of vaporization separation chamber by vaporization separation chamber electromagnetic heating coil, not only the thermal efficiency is high, energy consumption is low, and environmental protection, filler is equipped with in inside in described vaporization separation chamber.
The outside of described heavy component receiving tank is wound with heavy component receiving tank electromagnetic heating coil, the magnetic field of described heavy component receiving tank electromagnetic heating coil is corresponding with the sidewall of described heavy component receiving tank, thereby can carry out Electromagnetic Heating to the sidewall of heavy component receiving tank by heavy component receiving tank electromagnetic heating coil, not only the thermal efficiency is high, energy consumption is low, and environmental protection, heavy component receiving tank top is provided with heavy component receiving tank visor for observing heavy component separation case and human body and enters and carry out the manhole that inspection and maintenance is used, one side of heavy component receiving tank is provided with the liquid level gauge for observing heavy component liquid level, bottom is provided with slag-drip opening.
Further, described vapour phase chamber, filler chamber, vaporizer, vaporization separation chamber and heavy component receiving tank inside are equipped with temperature sensor, the output of described temperature sensor is all connected with the input of controller, the output of described controller respectively with described vapour phase chamber electromagnetic heating coil, filler chamber's electromagnetic heating coil, vaporizer electromagnetic heating coil, control is connected vaporization separation chamber electromagnetic heating coil with heavy component receiving tank electromagnetic heating coil, control respectively vapour phase chamber electromagnetic heating coil by controller according to the detected temperatures of temperature sensor, filler chamber's electromagnetic heating coil, vaporizer electromagnetic heating coil, the heating work of vaporization separation chamber's electromagnetic heating coil and heavy component receiving tank electromagnetic heating coil, make vapour phase chamber, filler chamber, vaporizer, temperature in vaporization separation chamber and heavy component receiving tank remains in constant scope, improve production efficiency.
The utility model has the advantage of: simple in structure, the thermal efficiency is high, and energy consumption is low, environmental protection has improved production efficiency, has reduced production cost, has increased economic benefit.
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment.
Detailed description of the invention
Below preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for description and interpretation the utility model, and be not used in restriction the utility model.
Embodiment 1
As shown in Figure 1, a kind of biofuel column, comprises tower body, and described tower body is columniform tank body, and described tower body is provided with vapour phase chamber 1, filler chamber 2, vaporizer 3, vaporization separation chamber 4 and heavy component receiving tank 5 from top to bottom successively; The outside of described vapour phase chamber 1 is wound with vapour phase chamber electromagnetic heating coil 11, the magnetic field of described vapour phase chamber electromagnetic heating coil 11 is corresponding with the sidewall of described vapour phase chamber 1, thereby can carry out Electromagnetic Heating to the sidewall of vapour phase chamber by electromagnetic heating coil, not only the thermal efficiency is high, energy consumption is low, and environmental protection, the top of described vapour phase chamber 1 is provided with vapour phase chamber visor 12 and thermometer measuring device 13, and top is provided with vacuum port 14;
There is filling material described filler chamber 2 inside;
Described vaporizer 3 outsides are wound with vaporizer electromagnetic heating coil 31, the magnetic field of described vaporizer electromagnetic heating coil 31 is corresponding with the sidewall of described vaporizer 3, thereby can carry out Electromagnetic Heating to the sidewall of vaporizer 3 by vaporizer electromagnetic heating coil 31, not only the thermal efficiency is high, energy consumption is low, and environmental protection, described vaporizer 3 tops are provided with vaporizer visor 32, middle part is provided with upper feeding mouth 33, described upper feeding mouth 33 is connected with atomizer 35 by liquid distributor 34, bottom is provided with lower charging aperture 36 and cyclone hydraulic separators 37, the outlet of described lower charging aperture 36 is passed through the outside of described cyclone hydraulic separators 37 with tangential direction.
The outside of described vaporization separation chamber 4 is wound with vaporization separation chamber electromagnetic heating coil 41, the magnetic field of described vaporization separation chamber electromagnetic heating coil 41 is corresponding with the sidewall of described vaporization separation chamber 4, thereby can carry out Electromagnetic Heating to the sidewall of vaporization separation chamber 4 by vaporization separation chamber electromagnetic heating coil 41, not only the thermal efficiency is high, energy consumption is low, and environmental protection, filler is equipped with in 4 inside in described vaporization separation chamber.
The outside of described heavy component receiving tank 5 is wound with heavy component receiving tank electromagnetic heating coil 51, the magnetic field of described heavy component receiving tank electromagnetic heating coil 51 is corresponding with the sidewall of described heavy component receiving tank 5, thereby can carry out Electromagnetic Heating to the sidewall of heavy component receiving tank 5 by heavy component receiving tank electromagnetic heating coil 51, not only the thermal efficiency is high, energy consumption is low, and environmental protection, heavy component receiving tank top is provided with heavy component receiving tank visor 52 for observing heavy component separation case and human body and enters and carry out the manhole 53 that inspection and maintenance is used, one side of heavy component receiving tank is provided with the liquid level gauge 54 for observing heavy component liquid level, bottom is provided with slag-drip opening 55.
In addition, described vapour phase chamber, filler chamber, vaporizer, vaporization separation chamber and heavy component receiving tank inside are equipped with temperature sensor, the output of described temperature sensor is all connected with the input of controller, the output of described controller respectively with described vapour phase chamber electromagnetic heating coil, filler chamber's electromagnetic heating coil, vaporizer electromagnetic heating coil, control is connected vaporization separation chamber electromagnetic heating coil with heavy component receiving tank electromagnetic heating coil, control respectively vapour phase chamber electromagnetic heating coil by controller according to the detected temperatures of temperature sensor, filler chamber's electromagnetic heating coil, vaporizer electromagnetic heating coil, the heating work of vaporization separation chamber's electromagnetic heating coil and heavy component receiving tank electromagnetic heating coil, make vapour phase chamber, filler chamber, vaporizer, temperature in vaporization separation chamber and heavy component receiving tank remains in constant scope, improve production efficiency.
When work, by the biodiesel raw material to be distilled of 1% glycerine, 3% sweet three cruel, 1% sweet one cruel, 2% DAG and 93% fatty acid methyl ester composition, be heated to 260 degree Celsius and enter from lower charging aperture with the pressure of 4 kg/cm, and pass through cyclone hydraulic separators outside with tangential direction, thereby raw material is carried out to vapor-liquid separation. Simultaneously by the biodiesel raw material to be distilled of 1% glycerine, 3% sweet three esters, a 1% sweet ester, 2% DAG and 93% fatty acid methyl ester composition, be heated to 260 degree Celsius and undertaken by liquid distributor the mean allocation of liquid from upper feeding mouth with the pressure of 4 kg/cm, enter atomizer, by atomizer by atomizing raw materials. At this moment most light component separates by the filler of filler chamber, is under the vacuum port effect of 20 millimetress of mercury at the indoor 248 degree high temperature Celsius of vapour phase and end vacuum, is sucked out and becomes biodiesel finished product. A small amount of light component and heavy component enter vaporization separation chamber by the empty portion in centre of cyclone hydraulic separators under the effect of its deadweight. Enter the heavy component of vaporization separation chamber and light component under the effect of its filler and electromagnetic heating coil, light component is wherein vaporized once again, and by the filler of vaporization separation chamber, the cyclone hydraulic separators of vaporizer, the filler of filler chamber and vacuum port, leave and become biodiesel finished product. Remaining heavy component enters in the heavy component receiving tank that liquid level gauge and electromagnetic heating coil are housed and stores. Top is equipped with human body and is entered and carry out manhole that inspection and maintenance uses and for observing the visor of heavy component separation case, heavy component can be discharged by slag-drip opening.
Claims (1)
1. a biofuel column, is characterized in that: comprise tower body, described tower body is columniform tank body, and described tower body is provided with vapour phase chamber, filler chamber, vaporizer, vaporization separation chamber and heavy component receiving tank from top to bottom successively; The outside of described vapour phase chamber is wound with vapour phase chamber electromagnetic heating coil, and the magnetic field of described vapour phase chamber electromagnetic heating coil is corresponding with the sidewall of described vapour phase chamber, and the top of described vapour phase chamber is provided with vapour phase chamber visor and thermometer measuring device, and top is provided with vacuum port;
Described vaporizer outside is wound with vaporizer electromagnetic heating coil, the magnetic field of described vaporizer electromagnetic heating coil is corresponding with the sidewall of described vaporizer, described vaporizer top is provided with vaporizer visor, middle part is provided with upper feeding mouth, described upper feeding mouth is connected with atomizer by liquid distributor, bottom is provided with lower charging aperture and cyclone hydraulic separators, and the outlet of described lower charging aperture is passed through the outside of described cyclone hydraulic separators with tangential direction;
The outside of described vaporization separation chamber is wound with vaporization separation chamber electromagnetic heating coil, and the magnetic field of described vaporization separation chamber electromagnetic heating coil is corresponding with the sidewall of described vaporization separation chamber;
The outside of described heavy component receiving tank is wound with heavy component receiving tank electromagnetic heating coil, and the magnetic field of described heavy component receiving tank electromagnetic heating coil is corresponding with the sidewall of described heavy component receiving tank; Described heavy component receiving tank top is provided with heavy component receiving tank visor for observing heavy component separation case and human body and enters and carry out the manhole that inspection and maintenance is used, and a side is provided with the liquid level gauge for observing heavy component liquid level, and bottom is provided with slag-drip opening;
Described vapour phase chamber, filler chamber, vaporizer, vaporization separation chamber and heavy component receiving tank inside are equipped with temperature sensor, the output of described temperature sensor is all connected with the input of controller, the output of described controller respectively with described vapour phase chamber electromagnetic heating coil, filler chamber's electromagnetic heating coil, vaporizer electromagnetic heating coil, control is connected vaporization separation chamber electromagnetic heating coil with heavy component receiving tank electromagnetic heating coil, control respectively vapour phase chamber electromagnetic heating coil by controller according to the detected temperatures of temperature sensor, filler chamber's electromagnetic heating coil, vaporizer electromagnetic heating coil, the heating work of vaporization separation chamber's electromagnetic heating coil and heavy component receiving tank electromagnetic heating coil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521018057.0U CN205252570U (en) | 2015-12-10 | 2015-12-10 | Biodiesel distillation column |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521018057.0U CN205252570U (en) | 2015-12-10 | 2015-12-10 | Biodiesel distillation column |
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| Publication Number | Publication Date |
|---|---|
| CN205252570U true CN205252570U (en) | 2016-05-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201521018057.0U Expired - Fee Related CN205252570U (en) | 2015-12-10 | 2015-12-10 | Biodiesel distillation column |
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| CN (1) | CN205252570U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109011676A (en) * | 2018-08-21 | 2018-12-18 | 浙江工业大学 | A kind of achievable material is rapidly heated the rectifying column of vaporization |
| CN114733221A (en) * | 2022-04-24 | 2022-07-12 | 南通利奥化工科技有限公司 | Rectifying tower for quickly heating and vaporizing materials |
-
2015
- 2015-12-10 CN CN201521018057.0U patent/CN205252570U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109011676A (en) * | 2018-08-21 | 2018-12-18 | 浙江工业大学 | A kind of achievable material is rapidly heated the rectifying column of vaporization |
| CN109011676B (en) * | 2018-08-21 | 2021-06-04 | 浙江工业大学 | Rectifying tower capable of realizing rapid temperature rise and vaporization of materials |
| CN114733221A (en) * | 2022-04-24 | 2022-07-12 | 南通利奥化工科技有限公司 | Rectifying tower for quickly heating and vaporizing materials |
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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: 20160525 Termination date: 20171210 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |