CN206276374U - A kind of reactor for manufacturing biodiesel - Google Patents
A kind of reactor for manufacturing biodiesel Download PDFInfo
- Publication number
- CN206276374U CN206276374U CN201621154559.0U CN201621154559U CN206276374U CN 206276374 U CN206276374 U CN 206276374U CN 201621154559 U CN201621154559 U CN 201621154559U CN 206276374 U CN206276374 U CN 206276374U
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- China
- Prior art keywords
- kettle
- chuck
- agitating device
- circulation pipe
- heat
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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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- Physical Or Chemical Processes And Apparatus (AREA)
- Accessories For Mixers (AREA)
Abstract
The utility model is related to production of biodiesel technical field, disclose a kind of reactor for manufacturing biodiesel, including kettle, it is arranged on the agitating device in kettle, drive the motor of the agitating device, the motor is arranged on kettle top, the agitating device includes agitating shaft and the blade on agitating shaft, multiple through holes are offered on the blade, esterified accelerator is provided with the kettle, chuck is provided with outside the kettle, the chuck outside is provided with recirculation heater, its simple structure, it is simple to operate, material mixing Quick uniform in reactor, in material into being preheated to it before kettle, energy consumption is low, shorten the heat time, ensure that reaction temperature, reduce energy consumption, improve production efficiency.
Description
Technical field
The utility model is related to production of biodiesel technical field, more particularly to a kind of reactor for manufacturing biodiesel.
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, temperature are unstable, heating is slow, energy consumption is big, pollution is big, anti-
Long, low production efficiency between seasonable, production cost is high to wait shortcomings.
Utility model content
The utility model aims to provide a kind of reactor for manufacturing biodiesel, and above mentioned problem is solved well, its knot
Structure is simple, simple to operate, material mixing Quick uniform in reactor, in material into being preheated to it before kettle, produces energy
Consumption is low, shortens the heat time, it is ensured that reaction temperature, reduces energy consumption, improves production efficiency.
The technical solution of the utility model be it is a kind of manufacture the reactor of biodiesel, including kettle, be arranged in kettle
Agitating device, drive the motor of the agitating device, the motor is arranged on kettle top, and the agitating device includes stirring
Axle and the blade on agitating shaft, offer multiple through holes on the blade, esterified acceleration dress is provided with the kettle
Put, the esterified accelerator includes circulation pipe, circulating pump and accelerating tube, and the circulation pipe upper end connects with kettle top, described
Circulation pipe lower end is connected with autoclave body bottom, and the accelerating tube is arranged on circulation pipe middle part, and the circulating pump is arranged under circulation pipe
Portion, the accelerating tube is conical pipe, and the accelerating tube miner diameter end is provided with porous plate, chuck, institute are provided with outside the kettle
State chuck outside and be provided with recirculation heater, the recirculation heater includes disc type heating tube, and the disc type heating tube upper end sets
It is equipped with heat-conducting medium import, the disc type heating tube lower end and is provided with heat-conducting medium outlet, the heat-conducting medium outlet passes through pump
Connected with chuck bottom, the heat-conducting medium import and chuck top connect, the kettle top is provided with feed pipe, it is described enter
Expects pipe passes through disc type heating tube.
Further, the kettle top is provided with peephole.
Further, the kettle top is additionally provided with catalyst inlet, and the autoclave body bottom is provided with discharge nozzle.
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；
3. the utility model is preheated by recirculation heater to the material for entering kettle, while by chuck to kettle
Body carries out heating and thermal insulation, shortens the heat time, it is ensured that reaction temperature, reduces energy consumption, improves production efficiency.
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
Manage, 331. porous plates, 4. chuck, 5. recirculation heater, 51. disc type heating tubes, 511. heat-conducting medium imports, 512. heat-conducting mediums
Outlet, 52. pumps.
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 provide it is a kind of manufacture the reactor of biodiesel, including kettle 1, be arranged on kettle
Agitating device 2, the motor 21 of the driving agitating device 2 in body 1, the motor 21 are arranged on the top of kettle 1, the stirring
Device 2 includes agitating shaft 22 and the blade 23 on agitating shaft 22, and multiple through holes 231, institute are offered on the blade 23
State and esterified accelerator 3 be provided with kettle 1, the esterified accelerator 3 includes circulation pipe 31, circulating pump 32 and accelerating tube 33,
The upper end of the circulation pipe 31 connects with the top of kettle 1, and the lower end of the circulation pipe 31 connects with the bottom of kettle 1, the accelerating tube 33
The middle part of circulation pipe 31 is arranged on, the circulating pump 32 is arranged on the bottom of circulation pipe 31, and the accelerating tube 33 is conical pipe, described to add
The miner diameter end of fast pipe 33 is provided with porous plate 331, and chuck 4 is provided with outside the kettle 1, and the outside of the chuck 4 is provided with circulation
Heater 5, the recirculation heater 5 includes disc type heating tube 51, and the upper end of disc type heating tube 51 is provided with heat-conducting medium and enters
Mouthfuls 511, the lower end of disc type heating tube 51 is provided with heat-conducting medium outlet 512, the heat-conducting medium outlet 512 by pump 52 with
The bottom of chuck 4 is connected, and the heat-conducting medium import 511 is connected with the top of chuck 4, and the top of the kettle 1 is provided with feed pipe 11,
The feed pipe 11 passes through disc type heating tube 51.
The top of kettle 1 is provided with peephole 12.The top of kettle 1 is additionally provided with catalyst inlet 13, and the bottom of the kettle 1 sets
It is equipped 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 is by 5 pairs of materials for entering kettle 1 of recirculation heater
Preheated, while carrying out heating and thermal insulation to kettle 1 by chuck 4, shortened the heat time, it is ensured that reaction temperature, dropped
Low energy consumption, improves production efficiency.
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. it is a kind of manufacture biodiesel reactor, it is characterised in that：Including kettle, the agitating device being arranged in kettle, drive
The motor of the agitating device is moved, the motor is arranged on kettle top, and the agitating device includes agitating shaft and installed in stirring
Mix the blade on axle, multiple through holes offered on the blade, be provided with esterified accelerator on the kettle, it is described esterified plus
Fast 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
Body 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
Conical pipe, the accelerating tube miner diameter end is provided with porous plate, and chuck is provided with outside the kettle, and the chuck outside is provided with
Recirculation heater, the recirculation heater include disc type heating tube, the disc type heating tube upper end be provided with heat-conducting medium import,
The disc type heating tube lower end is provided with heat-conducting medium outlet, and the heat-conducting medium outlet is connected by pump with chuck bottom, institute
State heat-conducting medium import to be connected with chuck top, the kettle top is provided with feed pipe, the feed pipe is heated through disc type
Pipe.
2. it is according to claim 1 manufacture biodiesel reactor, it is characterised in that：The kettle top is provided with sight
Examine mirror.
3. it is according to claim 1 manufacture biodiesel reactor, it is characterised in that：The kettle top is additionally provided with
Catalyst inlet, the autoclave body bottom is provided with discharge nozzle.
4. it is according to claim 1 manufacture biodiesel reactor, it is characterised in that：Temperature is installed on the kettle
Measuring instrument.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154559.0U CN206276374U (en) | 2016-10-31 | 2016-10-31 | A kind of reactor for manufacturing biodiesel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154559.0U CN206276374U (en) | 2016-10-31 | 2016-10-31 | A kind of reactor for manufacturing biodiesel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206276374U true CN206276374U (en) | 2017-06-27 |
Family
ID=59085410
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621154559.0U Active CN206276374U (en) | 2016-10-31 | 2016-10-31 | A kind of reactor for manufacturing biodiesel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206276374U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111282530A (en) * | 2018-12-06 | 2020-06-16 | 张存续 | Microwave reactor and biodiesel production method |
-
2016
- 2016-10-31 CN CN201621154559.0U patent/CN206276374U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111282530A (en) * | 2018-12-06 | 2020-06-16 | 张存续 | Microwave reactor and biodiesel production method |
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