CN206276376U - A kind of production of biodiesel reactor - Google Patents
A kind of production of biodiesel reactor Download PDFInfo
- Publication number
- CN206276376U CN206276376U CN201621154880.9U CN201621154880U CN206276376U CN 206276376 U CN206276376 U CN 206276376U CN 201621154880 U CN201621154880 U CN 201621154880U CN 206276376 U CN206276376 U CN 206276376U
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- China
- Prior art keywords
- kettle
- circulation pipe
- production
- accelerating tube
- agitating device
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Liquid Carbonaceous Fuels (AREA)
- Fats And Perfumes (AREA)
Abstract
The utility model is related to production of biodiesel technical field, disclose a kind of production of biodiesel reactor, including kettle, it is arranged on the agitating device in kettle, drive the motor of the agitating device, motor is arranged on kettle top, agitating device includes agitating shaft and the blade on agitating shaft, multiple through holes are offered on blade, esterified accelerator is provided with kettle, esterified accelerator includes circulation pipe, circulating pump and accelerating tube, circulation pipe upper end connects with kettle top, circulation pipe lower end connects with autoclave body bottom, accelerating tube is arranged on circulation pipe middle part, circulating pump is arranged on circulation pipe bottom, accelerating tube is conical pipe, accelerating tube miner diameter end is provided with porous plate.Its simple structure, simple to operate, energy consumption is low, and material mixing Quick uniform in reactor, production efficiency is high.
Description
Technical field
The utility model is related to production of biodiesel technical field, more particularly to a kind of production of biodiesel reactor.
Background technology
Biodiesel refers to oil crops such as soybean, rape, cotton, palm etc., Wild oil plant and engineering microalgae etc.
Water plant grease and animal fat, food garbage oil etc. for feedstock oil by ester exchange or thermochemical processes be made can generation
For the reproducibility diesel fuel of petrifaction diesel.Biodiesel as the highly preferred renewable sources of energy at this stage, increasingly by weight
Depending on, it is that biodiesel molecular weight is close with diesel oil the reason for its is preferred, there is similar burning and dynamic characteristics to mineral diesel,
And product is more environmentally-friendly, so the petroleum diesel substitute as high-quality.
The preparation method of biodiesel mainly has four kinds, including direct mixing method, mini-emulsion process, high temperature pyrolytic cracking and ester
Exchange process, wherein ester-interchange method are current most study and the method for industrialized production, and ester-interchange method is due to glyceride stock
Different and catalyst Bu Tong and be divided into base-catalyzed transesterification method, acid-catalyzed transesterification method, biological enzyme ester-interchange method and surpass
Critical ester-interchange method.During biodiesel is manufactured by Ester exchange technique, reaction unit is biodiesel manufacturing process
One of middle nucleus equipment.The quality of reaction unit determines the quality of the efficiency, energy consumption and biodiesel of biodiesel manufacture.
Existing biodiesel reaction unit has that complex structure, energy consumption are big, pollution is big, the reaction time is long, production efficiency
Low, production cost is high to wait shortcomings.
Utility model content
The utility model aims to provide a kind of production of biodiesel reactor, and above mentioned problem is solved well, its structure
Simply, simple to operate, energy consumption is low, and material mixing Quick uniform in reactor, production efficiency is high.
The technical solution of the utility model is a kind of production of biodiesel reactor, including kettle, is arranged in kettle
Agitating device, the motor for driving the agitating device, the motor are arranged on kettle top, and the agitating device includes agitating shaft
With the blade on agitating shaft, multiple through holes are offered on the blade, esterified accelerator are provided with the kettle,
The esterified accelerator includes circulation pipe, circulating pump and accelerating tube, and the circulation pipe upper end connects with kettle top, the circulation
Pipe lower end connects with autoclave body bottom, and the accelerating tube is arranged on circulation pipe middle part, and the circulating pump is arranged on circulation pipe bottom, institute
Accelerating tube is stated for conical pipe, the accelerating tube miner diameter end is provided with porous plate.
Further, the kettle top is provided with peephole.
Further, the kettle top is provided with feed pipe and catalyst inlet, and the autoclave body bottom is provided with discharging
Pipe.
Further, temperature measuring set is installed on the kettle.
The beneficial effects of the utility model are：
1. the utility model uses agitating device and esterified accelerator simultaneously to the grease and catalyst action in kettle,
The mixture homogeneity of grease and catalyst is improve, the fusion haptoreaction of grease and catalyst is accelerated, improve esterified anti-
The speed and reaction mass answered；
2. multiple through holes are offered on the blade of agitating device, when agitating shaft drives blade to rotate, blade is except driving
Grease and catalyst in kettle are rotated beyond mixing, and the through hole on blade separates grease, catalyst refinement, after rotation fully
Fusion, so as to further speed up the fusion haptoreaction of grease and catalyst, improves the speed and reaction substance of esterification reaction
Amount；The utility model simple structure, simple to operate, energy consumption is low, material mixing Quick uniform in reactor, reaction time
Short, production efficiency is high.
Brief description of the drawings
Fig. 1 is the schematic diagram of the utility model structure；
In figure：1. kettle, 11. feed pipes, 12. peepholes, 13. catalyst inlets, 14. discharge nozzles, 2. agitating device,
21. motors, 22. agitating shafts, 23. blades, 231. through holes, 3. esterified accelerator, 31. circulation pipes, 32. circulating pumps, 33. accelerate
Pipe, 331. porous plates.
Specific embodiment
In order that the purpose of this utility model, technical scheme and advantage become more apparent, below in conjunction with accompanying drawing, to this reality
It is further elaborated with new.
As shown in figure 1, the utility model provides a kind of production of biodiesel reactor, including kettle 1, it is arranged on kettle
Agitating device 2, the motor 21 of the driving agitating device 2 in 1, the motor 21 are arranged on the top of kettle 1, the stirring dress
Putting 2 includes agitating shaft 22 and the blade 23 on agitating shaft 22, and multiple through holes 231 are offered on the blade 23, described
Esterified accelerator 3 is provided with kettle 1, the esterified accelerator 3 includes circulation pipe 31, circulating pump 32 and accelerating tube 33, institute
State the upper end of circulation pipe 31 to be connected with the top of kettle 1, the lower end of the circulation pipe 31 connects with the bottom of kettle 1, and the accelerating tube 33 sets
Put at the middle part of circulation pipe 31, the circulating pump 32 is arranged on the bottom of circulation pipe 31, the accelerating tube 33 is conical pipe, the acceleration
The miner diameter end of pipe 33 is provided with porous plate 331.
The top of kettle 1 is provided with peephole 12.The top of kettle 1 is provided with feed pipe 11 and catalyst inlet 13, the kettle
The bottom of body 1 is provided with discharge nozzle 14.Temperature measuring set is installed on kettle 1.
The utility model is made to the grease in kettle 1 and catalyst simultaneously using agitating device 2 and esterified accelerator 3
With, the mixture homogeneity of grease and catalyst is improve, the fusion haptoreaction of grease and catalyst is accelerated, improve esterified
The speed and reaction mass of reaction；Multiple through holes 231 are offered on the blade 23 of agitating device 2, blade is driven in agitating shaft 22
During 23 rotation, in addition to driving grease and catalyst in kettle 1 to rotate mixing, the through hole 231 on blade 23 will for blade 23
Grease, catalyst refinement are separated, and are fully merged after rotation, so as to the fusion for having further speeded up grease and catalyst contacts anti-
Should, improve the speed and reaction mass of esterification reaction；The utility model simple structure, simple to operate, energy consumption is low, reaction
Material mixing Quick uniform in kettle, the reaction time is short, and production efficiency is high.
Certainly, the utility model can also have other various embodiments, spiritual and its essence without departing substantially from the utility model
In the case of, those of ordinary skill in the art can make various corresponding changes and deformation, but these phases according to the utility model
The change and deformation answered should all belong to the scope of the claims appended by the utility model.
Claims (4)
1. a kind of production of biodiesel reactor, it is characterised in that：Including kettle, the agitating device being arranged in kettle, drive
The motor of the agitating device, the motor is arranged on kettle top, and the agitating device includes agitating shaft and installed in stirring
Blade on axle, offers multiple through holes on the blade, esterified accelerator, the esterified acceleration are provided with the kettle
Device includes being connected at the top of circulation pipe, circulating pump and accelerating tube, the circulation pipe upper end and kettle, the circulation pipe lower end and kettle
Bottom connects, and the accelerating tube is arranged on circulation pipe middle part, and the circulating pump is arranged on circulation pipe bottom, and the accelerating tube is cone
Shape pipe, the accelerating tube miner diameter end is provided with porous plate.
2. production of biodiesel reactor according to claim 1, it is characterised in that：The kettle top is provided with observation
Mirror.
3. production of biodiesel reactor according to claim 1, it is characterised in that：The kettle top is provided with charging
Pipe and catalyst inlet, the autoclave body bottom are provided with discharge nozzle.
4. production of biodiesel reactor according to claim 1, it is characterised in that：Temperature survey is installed on the kettle
Amount instrument.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154880.9U CN206276376U (en) | 2016-10-31 | 2016-10-31 | A kind of production of biodiesel reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154880.9U CN206276376U (en) | 2016-10-31 | 2016-10-31 | A kind of production of biodiesel reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206276376U true CN206276376U (en) | 2017-06-27 |
Family
ID=59085899
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621154880.9U Active CN206276376U (en) | 2016-10-31 | 2016-10-31 | A kind of production of biodiesel reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206276376U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112206737A (en) * | 2020-10-26 | 2021-01-12 | 北京启迪德清生物能源科技有限公司 | Ultra-low energy consumption reactor special for biodiesel |
-
2016
- 2016-10-31 CN CN201621154880.9U patent/CN206276376U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112206737A (en) * | 2020-10-26 | 2021-01-12 | 北京启迪德清生物能源科技有限公司 | Ultra-low energy consumption reactor special for biodiesel |
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