CN206276375U - A kind of novel biodiesel produces reactor - Google Patents
A kind of novel biodiesel produces reactor Download PDFInfo
- Publication number
- CN206276375U CN206276375U CN201621154560.3U CN201621154560U CN206276375U CN 206276375 U CN206276375 U CN 206276375U CN 201621154560 U CN201621154560 U CN 201621154560U CN 206276375 U CN206276375 U CN 206276375U
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- kettle
- heat
- chuck
- heating tube
- disc type
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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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Abstract
The utility model is related to production of biodiesel technical field, disclose a kind of novel biodiesel production 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, chuck is provided with outside kettle, chuck outside is provided with recirculation heater, recirculation heater includes disc type heating tube, disc type heating tube upper end is provided with heat-conducting medium import, disc type heating tube lower end is provided with heat-conducting medium outlet, heat-conducting medium outlet is connected by pump with chuck bottom, heat-conducting medium import is connected with chuck top, kettle top is provided with feed pipe, feed pipe passes through disc type heating tube.Its simple structure, simple to operate, material mixing Quick uniform in reactor, in material into being preheated to it before kettle, shortens the heat time, it is ensured that reaction temperature, reduces energy consumption, improves production efficiency.
Description
Technical field
The utility model is related to production of biodiesel technical field, more particularly to a kind of production reaction of novel biodiesel
Kettle.
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, temperature is unstable, heating is slow, 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 novel biodiesel production reactor, and above mentioned problem is solved well, its
Simple structure, simple to operate, material mixing Quick uniform in reactor, in material into being preheated to it before kettle, shortens
Heat time, it is ensured that reaction temperature, energy consumption is reduced, improve production efficiency.
The technical solution of the utility model is a kind of novel biodiesel production reactor, including kettle, is arranged on kettle
Interior agitating device, the motor of the driving agitating device, the motor is arranged on kettle top, and the agitating device includes stirring
Axle and the blade on agitating shaft are mixed, multiple through holes are offered on the blade, 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 improves grease and catalyst using agitating device to grease and catalyst action in kettle
Mixture homogeneity, accelerate the fusion haptoreaction of grease and catalyst, improve the speed and reaction mass of esterification reaction；
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, 4. chuck, 5. recirculation heater, 51. disc type heating tubes, 511. heat conduction
Medium entrance, the outlet of 512. heat-conducting mediums, 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 provides a kind of novel biodiesel produces reactor, including kettle 1, it is arranged on
Agitating device 2, the motor 21 of the driving agitating device 2 in kettle 1, the motor 21 is arranged on the top of kettle 1, described to stir
Mixing device 2 includes agitating shaft 22 and the blade 23 on agitating shaft 22, and multiple through holes 231 are offered on the blade 23,
Chuck 4 is provided with outside the kettle 1, the outside of the chuck 4 is provided with recirculation heater 5, and the recirculation heater 5 includes disk
Formula heating tube 51, the upper end of disc type heating tube 51 is provided with heat-conducting medium import 511, the lower end of disc type heating tube 51 and sets
There is heat-conducting medium to export 512, the heat-conducting medium outlet 512 is connected by pump 52 with the bottom of chuck 4, the heat-conducting medium import
511 connect with the top of chuck 4, and the top of the kettle 1 is provided with feed pipe 11, and 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, to grease and catalyst action in kettle 1, improves grease and catalyst using agitating device 2
Mixture homogeneity, accelerate the fusion haptoreaction of grease and catalyst, improve the speed and reaction mass of esterification reaction；
Multiple through holes 231 are offered on the blade 23 of agitating device 2, when agitating shaft 22 drives blade 23 to rotate, blade 23 is except band
Grease and catalyst in dynamic kettle 1 are rotated beyond mixing, and the through hole 231 on blade 23 separates grease, catalyst refinement, turns
Fully fusion, so as to further speed up the fusion haptoreaction of grease and catalyst, improves the speed of esterification reaction after dynamic
And reaction mass；The utility model is preheated by 5 pairs of materials into kettle 1 of recirculation heater, while passing through chuck 4
Heating and thermal insulation is carried out to kettle 1, the heat time is shortened, it is ensured that reaction temperature, reduce energy consumption, improve 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. a kind of novel biodiesel produces reactor, it is characterised in that：Including kettle, the agitating device being arranged in kettle,
The motor of the agitating device, the motor is driven to be arranged on kettle top, the agitating device includes agitating shaft and is arranged on
Blade on agitating shaft, offers multiple through holes on the blade, chuck is provided with outside the kettle, and the chuck outside sets
Recirculation heater is equipped with, the recirculation heater includes disc type heating tube, and the disc type heating tube upper end is provided with heat-conducting medium
Import, the disc type heating tube lower end are provided with heat-conducting medium outlet, and the heat-conducting medium outlet is connected by pump with chuck bottom
Logical, the heat-conducting medium import is connected with chuck top, and the kettle top is provided with feed pipe, and the feed pipe passes through disc type
Heating tube.
2. novel biodiesel according to claim 1 produces reactor, it is characterised in that：The kettle top is provided with
Peephole.
3. novel biodiesel according to claim 1 produces reactor, it is characterised in that：The kettle top also sets up
There is catalyst inlet, the autoclave body bottom is provided with discharge nozzle.
4. novel biodiesel according to claim 1 produces reactor, it is characterised in that：Temperature is installed on the kettle
Degree measuring instrument.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154560.3U CN206276375U (en) | 2016-10-31 | 2016-10-31 | A kind of novel biodiesel produces reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154560.3U CN206276375U (en) | 2016-10-31 | 2016-10-31 | A kind of novel biodiesel produces reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206276375U true CN206276375U (en) | 2017-06-27 |
Family
ID=59085938
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621154560.3U Active CN206276375U (en) | 2016-10-31 | 2016-10-31 | A kind of novel biodiesel produces reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206276375U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107855087A (en) * | 2017-12-14 | 2018-03-30 | 无锡市飞天油脂有限公司 | A kind of lubricating grease reactor |
| CN112275236A (en) * | 2020-09-03 | 2021-01-29 | 陈萍 | Esterification reaction kettle with efficient heat exchange function |
| CN116532067A (en) * | 2023-07-07 | 2023-08-04 | 淄博九圣化工有限公司 | Reaction temperature control mechanism and di-tert-butyl peroxide reaction kettle thereof |
-
2016
- 2016-10-31 CN CN201621154560.3U patent/CN206276375U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107855087A (en) * | 2017-12-14 | 2018-03-30 | 无锡市飞天油脂有限公司 | A kind of lubricating grease reactor |
| CN112275236A (en) * | 2020-09-03 | 2021-01-29 | 陈萍 | Esterification reaction kettle with efficient heat exchange function |
| CN116532067A (en) * | 2023-07-07 | 2023-08-04 | 淄博九圣化工有限公司 | Reaction temperature control mechanism and di-tert-butyl peroxide reaction kettle thereof |
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