CN103432980A - Biodiesel reaction still - Google Patents
Biodiesel reaction still Download PDFInfo
- Publication number
- CN103432980A CN103432980A CN2013103915972A CN201310391597A CN103432980A CN 103432980 A CN103432980 A CN 103432980A CN 2013103915972 A CN2013103915972 A CN 2013103915972A CN 201310391597 A CN201310391597 A CN 201310391597A CN 103432980 A CN103432980 A CN 103432980A
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- China
- Prior art keywords
- container
- plane
- biodiesel
- shaft
- discharging opening
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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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)
Abstract
The invention discloses a biodiesel reaction still. The biodiesel reaction still comprises a container (1), wherein the top of the container (1) is provided with a motor (2) and a reducer (3) through a machine base; the output end of the reducer (3) is provided with a stirring shaft (4), the stirring shaft (4) positioned in the container (1) is provided with blades (5), and a feeding port A (6), a feeding port B (7), an observation hole (8) and an access hole (9) are formed in the top of the container (1); a discharge port (10) is formed in the bottom of the side wall of the container (1), the bottom surface of the container (1) is an oblique plane (11) which can oblique to the discharge port (10), and the container (1) is also internally provided with a helical heating pipe (12). The biodiesel reaction still provided by the invention has the beneficial effects of being simple in structure, convenient in operation, suitable for preparing the biodiesel, and low in equipment cost, providing conditions for the large-scale production of the biodiesel, being strong in thermal insulation capability, avoiding heat energy waste, and being favorable for smooth discharge since the bottom of a mechanism is an oblique plane.
Description
Technical field
The present invention relates to technical field of chemical, particularly the biodiesel reactor.
Background technology
The energy is human survival, economic development, the indispensable important substance resource of social progress, is the grand strategy goods and materials that concern economic life line of the country and national defense safety.In today of energy scarcity, develop reproducible biodiesel and more and more be subject to the attention of various countries with the shortage that makes up fossil energy.Biodiesel is to take animal and plant fat and discarded object thereof as the petrifaction diesel substitute that raw material and low carbon fat alcohol are prepared from by ester exchange reaction, is a kind of important renewable clean fuel.And above-mentioned ester exchange reaction need be carried out in reactor, the reactor do not designed separately for the biodiesel preparation at present.And the heater of reactor at present commonly used is provided in a side of on the surface of reactor more, and its heating effect is poor, and the sound time of ancient India is long, can not meet the needs of high efficiency production, and production cost is high.
Summary of the invention
The object of the invention is to overcome the shortcoming of prior art, a kind of simple in structure, handled easily is provided, has improved heat exchanger effectiveness, discharging biodiesel reactor smoothly.
Purpose of the present invention is achieved through the following technical solutions: the biodiesel reactor, it comprises container, the top of container is equipped with transmission device by support, described transmission device comprises motor and decelerator, the decelerator output is installed shaft, described shaft stretches in container, be positioned on the shaft of container blade is installed, the top of container is provided with charging aperture A, charging aperture B, peep hole and manhole, the bottom of container side wall is provided with discharging opening, the bottom surface of container is the inclined-plane tilted to discharging opening, also be provided with spiral heating tube in container, be provided with on the correspondence position of the sidewall of container with the two ends of heating tube and be connected respectively fluid inlet and fluid issuing.
The angle of described inclined-plane and horizontal plane is 5～10 °, and inclined-plane near the height of an end of discharging opening lower than inclined-plane the end away from discharging opening.
Be provided with bearing block on described inclined-plane, the end that is positioned at the shaft of container is installed on bearing block by bearing, and the bottom of shaft and middle part all are equipped with one group of blade.
The outside of described container is coated with insulating jacket, and described insulating jacket has the thermal insulation layer between inner layer heat-insulation plate, lateral septal hot plate and filling and inner layer heat-insulation plate and lateral septal hot plate.
The present invention has the following advantages: the present invention is simple in structure, handled easily, can be applicable to prepare biodiesel, and equipment cost is low, for the biodiesel large-scale production provides condition; By being set, improved insulating jacket the heat-insulation and heat-preservation ability of reactor, thereby avoided the waste of heat energy, adopt the heating tube heating arrangement, improved heat exchanger effectiveness, saved resource, also be beneficial to material in reactor temperature stabilization, homogeneous, by stirring vane is set simultaneously, the stirring of realization to material, the mechanism that bottom surface is inclined-plane is beneficial to smooth and easy discharging.
The accompanying drawing explanation
Fig. 1 is structural representation of the present invention
In figure, 1-container, 2-motor, 3-decelerator, the 4-shaft, 5-blade, 6-charging aperture A, 7-charging aperture B, 8-peep hole, 9-manhole, the 10-discharging opening, 11-inclined-plane, 12-heating tube, the 13-fluid inlet, 14-fluid issuing, 15-bearing block, 16-inner layer heat-insulation plate, 17-lateral septal hot plate, 18-thermal insulation layer.
The specific embodiment
Below in conjunction with accompanying drawing, the present invention will be further described, and protection scope of the present invention is not limited to the following stated:
As shown in Figure 1, the biodiesel reactor, it comprises container 1, the top of container 1 is equipped with transmission device by support, described transmission device comprises motor 2 and decelerator 3, decelerator 3 outputs are installed shaft 4, described shaft 4 stretches in container 1, be positioned on the shaft 4 of container 1 blade 5 is installed, the top of container 1 is provided with charging aperture A6, charging aperture B7, peep hole 8 and manhole 9, the bottom of container 1 sidewall is provided with discharging opening 10, the bottom surface of container 1 is the inclined-plane 11 tilted to discharging opening 10, also be provided with spiral heating tube 12 in container 1, be provided with on the correspondence position of the sidewall of container 1 with the two ends of heating tube 12 and be connected respectively fluid inlet 13 and fluid issuing 14, superposed fluid issuing 14 is connected with the upper port of helical form heating tube 12, the fluid intake that is positioned at bottom is connected with the lower port of helical form heating tube 12.Blade 5 is arranged in the inner space of spiral helicine heating tube 12, and the tactical diameter of blade 5 is less than the diameter of helical form heating tube 12 inscribed cylinders.
Described inclined-plane 11 is 5～10 ° with the angle of horizontal plane, and inclined-plane 11 near the height of an end of discharging openings 10 lower than inclined-plane 11 end away from discharging opening 10.Container 1 bottom surface is set to inclined-plane 11 has increased the sedimentary area of container 1 bottom access, thereby, when the sediment volume is identical, compares the taper bottom surface and can effectively reduce sedimentary thickness, has avoided discharge gate blocked, is beneficial to smooth and easy discharging.
Be provided with bearing block 15 on described inclined-plane 11, the end that is positioned at the shaft 4 of container 1 is installed on bearing block 15 by bearing, and the bottom of shaft 4 and middle part all are equipped with one group of blade 5.Shaft 4 two ends all arrange the stability that mounting structure has improved shaft 4, have improved the service life of device.
The outside of described container 1 is coated with insulating jacket, and described insulating jacket has the thermal insulation layer 18 between inner layer heat-insulation plate 16, lateral septal hot plate 17 and filling and inner layer heat-insulation plate 16 and lateral septal hot plate 17.Described thermal insulation layer 18 can be the heat-barrier materials commonly used such as foamed plastics and makes.Insulating jacket the heat-insulating property that has improved reactor is set.
The course of work of the present invention is as follows: charging aperture A6 and charging aperture B7 are for joining material in container 1, hot fluid enters heating tube 12 from fluid issuing 14, after material-heat-exchanging in hot fluid in heating tube 12 and container 1, by fluid issuing 14, flowed out, material in reactor is heated by heating tube 12, the stirring that shaft 4 is realized material with moving vane 5, the staff is by response situation in observation panel observing response still, and after having reacted, material is through discharging opening 10 dischargings.
Claims (4)
1. biodiesel reactor, it is characterized in that: it comprises container (1), the top of container (1) is equipped with transmission device by support, described transmission device comprises motor (2) and decelerator (3), decelerator (3) output is installed shaft (4), described shaft (4) stretches in container (1), be positioned on the shaft (4) of container (1) blade (5) is installed, the top of container (1) is provided with charging aperture A(6), charging aperture B(7), peep hole (8) and manhole (9), the bottom of container (1) sidewall is provided with discharging opening (10), the bottom surface of container (1) is the inclined-plane (11) tilted to discharging opening (10), also be provided with spiral heating tube (12) in container (1), be provided with on the correspondence position of the sidewall of container (1) with the two ends of heating tube (12) and be connected respectively fluid inlet (13) and fluid issuing (14).
2. biodiesel reactor according to claim 1, it is characterized in that: the angle of described inclined-plane (11) and horizontal plane is 5～10 °, and inclined-plane (11) near the height of an end of discharging opening (10) lower than inclined-plane (11) end away from discharging opening (10).
3. biodiesel reactor according to claim 1, it is characterized in that: be provided with bearing block (15) on described inclined-plane (11), the end that is positioned at the shaft (4) of container (1) is installed on bearing block (15) by bearing, and the bottom of shaft (4) and middle part all are equipped with one group of blade (5).
4. biodiesel reactor according to claim 1, it is characterized in that: the outside of described container (1) is coated with insulating jacket, and described insulating jacket has the thermal insulation layer (18) between inner layer heat-insulation plate (16), lateral septal hot plate (17) and filling and inner layer heat-insulation plate (16) and lateral septal hot plate (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013103915972A CN103432980A (en) | 2013-09-02 | 2013-09-02 | Biodiesel reaction still |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013103915972A CN103432980A (en) | 2013-09-02 | 2013-09-02 | Biodiesel reaction still |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103432980A true CN103432980A (en) | 2013-12-11 |
Family
ID=49686749
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013103915972A Pending CN103432980A (en) | 2013-09-02 | 2013-09-02 | Biodiesel reaction still |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103432980A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106153434A (en) * | 2015-03-31 | 2016-11-23 | 中国石油化工股份有限公司 | A kind of reactor |
| CN111060393A (en) * | 2019-04-03 | 2020-04-24 | 浙江工业大学 | Temperature-controllable high-pressure environment mechanical test box |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201164801Y (en) * | 2008-01-22 | 2008-12-17 | 东莞市英科水墨有限公司 | Jacket type reactor |
| CN201728108U (en) * | 2010-06-29 | 2011-02-02 | 山东大地盐化集团有限公司 | White carbon black reactor |
| CN201969551U (en) * | 2011-01-24 | 2011-09-14 | 山东裕源集团有限公司 | Separation kettle for producing T acid |
| CN202224167U (en) * | 2011-09-22 | 2012-05-23 | 新疆西建新材料科技有限公司 | Movable reactor |
| CN102921365A (en) * | 2011-08-08 | 2013-02-13 | 四川西陇化工有限公司 | Enamel flat-bottom concentration reaction vessel |
-
2013
- 2013-09-02 CN CN2013103915972A patent/CN103432980A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201164801Y (en) * | 2008-01-22 | 2008-12-17 | 东莞市英科水墨有限公司 | Jacket type reactor |
| CN201728108U (en) * | 2010-06-29 | 2011-02-02 | 山东大地盐化集团有限公司 | White carbon black reactor |
| CN201969551U (en) * | 2011-01-24 | 2011-09-14 | 山东裕源集团有限公司 | Separation kettle for producing T acid |
| CN102921365A (en) * | 2011-08-08 | 2013-02-13 | 四川西陇化工有限公司 | Enamel flat-bottom concentration reaction vessel |
| CN202224167U (en) * | 2011-09-22 | 2012-05-23 | 新疆西建新材料科技有限公司 | Movable reactor |
Non-Patent Citations (1)
| Title |
|---|
| 王瑶琴等: "《化工设备设计全书 钛制化工设备设计》", 30 November 1985 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106153434A (en) * | 2015-03-31 | 2016-11-23 | 中国石油化工股份有限公司 | A kind of reactor |
| CN106153434B (en) * | 2015-03-31 | 2018-09-11 | 中国石油化工股份有限公司 | A kind of reaction kettle |
| CN111060393A (en) * | 2019-04-03 | 2020-04-24 | 浙江工业大学 | Temperature-controllable high-pressure environment mechanical test box |
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| PB01 | Publication | ||
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| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20131211 |