CN201292347Y - Complete equipment for biodiesel production - Google Patents
Complete equipment for biodiesel production Download PDFInfo
- Publication number
- CN201292347Y CN201292347Y CNU2008200817173U CN200820081717U CN201292347Y CN 201292347 Y CN201292347 Y CN 201292347Y CN U2008200817173 U CNU2008200817173 U CN U2008200817173U CN 200820081717 U CN200820081717 U CN 200820081717U CN 201292347 Y CN201292347 Y CN 201292347Y
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- CN
- China
- Prior art keywords
- pipeline
- methanol
- tank
- biodiesel
- glycerine
- Prior art date
- 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.)
- Expired - Fee Related
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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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model relates to complete equipment for producing biodiesel, belonging to biodiesel process equipment. The complete equipment for producing biodiesel is characterized in that a raw oil tank, a methanol tank and a catalyst tank are respectively provided with pipelines led into a preheating system and then are led into a main reaction tower from the preheating system by pipelines, and the main reaction tower is provided with pipelines led into a methanol separator, wherein circulating pipelines are arranged on the main reaction tower; three pipelines are arranged on the methanol separator, a first pipeline is led back into the methanol tank by the preheating system, a second pipeline is led into a cooling system, and a third pipeline is led into a glycerin mixture separate device; the glycerin mixture separate device is provided with a first pipeline led back into the catalyst tank and a second pipeline led into the cooling system; the cooling system is respectively provided with pipelines communicated with a finished product oil tank and a glycerin tank; each pipeline is provided with one pump; and the methanol separator, the glycerin mixture separate device and the preheating system are connected with a control system. The utility model can be used for processing animal and vegetable fat and waste oil into biodiesel.
Description
Technical field
The utility model relates to a kind of oil plant processing equipment, and a kind of specifically production of biodiesel suite of equipment belongs to biofuel processing units field.
Background technology
Since last century end manifests the petroleum-based energy crisis; people begin actively to seek the substitute of petroleum-based energy; wherein biofuel has obtained great concern; according at the online preliminary search of Chinese patent; its production method and production unit down hundreds of, be that " the production of biodiesel device " of 200620089151.X is exactly representative wherein as application number.
But esterification techniques is adopted in the production of biofuel at present, and raw oil material is just produced diesel oil by processes such as esterification, distillation purifications, and equipment used is expensive, the temperature of reaction height, and efficient is lower, thereby causes big energy consumption, and is expensive, discharges waste water simultaneously, pollutes.So far, for utilizing the pollution-free of animal-plant oil and aste vegetable oil and animal fat production biofuel, power consumption is few, low cost, and the production biofuel device of good quality and high output is less relatively.And, having a style of one's own, the device of cyclic production is not seen as yet.
As the equipment development exploitation of production biofuel, be the battle position of technological innovation always, industry all has new ripe available technology to occur in hope at any time, and therefore, it is a kind of inevitable that the innovation of present technique occurs.
Summary of the invention
Goal of the invention of the present utility model is exactly to overcome that the existing efficient of present production biofuel device is low, cost is high, power consumption is big, with serious pollution weak point, thereby provides a kind of complete, the production of biodiesel device of production capable of circulation.Its production efficiency height, simple in structure, pollution-free, power consumption is few, and cost is low, and good quality and high output is suitable for utilizing the usefulness of animal-plant oil and waste oil production biofuel.
Realize that the technical solution of the utility model is such: the production of biodiesel suite of equipment, forming has pipeline, pump, Controlling System, concrete structure is that material tank 1, methanol tank 3, catalyst tank 4 have pipeline to enter pre-heating system 11 respectively, enter main reaction tower 10 by pipeline respectively from pre-heating system again, main reaction tower 10 has pipeline to feed methanol separator 8, wherein also is provided with circulating line on the main reaction tower; Methanol separator 8 is provided with three pipelines, article one, get back to methanol tank 3 by pre-heating system 11, article one, 7, one of feeding cooling systems feed glycerol mixture tripping device 5, have a pipeline to return into catalyst tank 4, have a pipeline to feed cooling system 7 on this device; There is pipeline to communicate on the cooling system 7 respectively with product tank 9, glycerine jar 6; Each pipeline is provided with pump 12; Methanol separator 8, glycerol mixture tripping device 5, pre-heating system 11 interrelates with Controlling System 2.
Wherein, pre-heating system 11 structures are that the bottom is provided with heating element 13, and inside is chamber, oily territory 15, and it is provided with the catalyzer pipeline 14 that runs through, methanol pipeline 16, stock oil pipeline 17, recovery methanol pipeline 18; Cooling system 7 structures are for being provided with cooling water inlet end 19 and cooling water outlet 23, glycerine entrance 21 and outlet, and products pipeline inlet 22 and outlet, glycerine pipeline and products pipeline cooling are coil pipe 20 structures, are provided with dividing plate 24 in the cooling system; Methanol separator 8 structures are that the bottom is provided with heating element, mix products inlet 25, glycerine and catalyst mixture outlet 30, top is provided with methanol steam outlet 28, oil gas vent 29, stir shaft and agitating vane 26 are housed in the methanol separator, and electric motor 27 followed in the axle first line of a couplet; Glycerol mixture tripping device 5 structures are that the bottom is provided with heating element, glycerine and catalyst mixture inlet 31, and catalyst outlet 33, top is provided with glycerine outlet 32, and stir shaft and agitating vane are housed in the glycerol mixture tripping device, and electric motor followed in the axle first line of a couplet; Main reaction tower 10 structures are that the bottom is provided with methanol steam inlet 34, and top is provided with catalyzer and stock oil inlet 36, and reflux inlet 37 is equipped with steam baffle 35 in the tower, and multilayer tower tray 38 has a plurality of pores on the tower tray, steam cover 39 is arranged on each pore.
The beneficial effects of the utility model are: the one, and complete property, cyclic production, the industrialization practicality obtains radical change; The 2nd, simple in structure, handling good; The 3rd, power consumption is few, less investment, and cost is low; The 4th, pollution-free, good quality and high output, economic benefit height, social benefit are good.
Description of drawings
Fig. 1 is that the utility model suite of equipment connects synoptic diagram;
Fig. 2 is the agent structure synoptic diagram of pre-heating system in the utility model;
Fig. 3 is the agent structure synoptic diagram of cooling system in the utility model;
Fig. 4 is the agent structure synoptic diagram of methyl alcohol tripping device in the utility model;
Fig. 5 is the agent structure synoptic diagram of glycerol mixture tripping device in the utility model;
Fig. 6 is the agent structure synoptic diagram of main reaction tower in the utility model;
Fig. 7 is the A-A sectional view among Fig. 6.
Among the last figure, the 1st, material tank, the 2nd, Controlling System, the 3rd, methanol tank, the 4th, catalyst tank, the 5th, the glycerol mixture tripping device, the 6th, the glycerine jar, the 7th, cooling system, the 8th, methanol separator, the 9th, product tank, the 10th, the main reaction tower, the 11st, pre-heating system, the 12nd, pump, the 13rd, heating element, the 14th, the catalyzer pipeline, chamber, 15 oily territory, the 16th, methanol pipeline, the 17th, the stock oil pipeline, the 18th, reclaim methanol pipeline, the 19th, the cooling water inlet end, the 20th, coil pipe, the 21st, the glycerine entrance, the 22nd, the products pipeline inlet, the 23rd, cooling water outlet, the 24th, dividing plate, the 25th, the mix products inlet, the 26th, stir shaft and agitating vane, the 27th, electric motor, the 28th, the methanol steam outlet, the 29th, oil gas vent, the 30th, glycerine and catalyst mixture outlet, the 31st, glycerine and catalyst mixture inlet, the 32nd, the glycerine outlet, the 33rd, catalyst outlet, the 34th, the methanol steam inlet, the 35th, steam baffle, the 36th, catalyzer and stock oil inlet, the 37th, reflux inlet, the 38th, tower tray, the 39th, steam cover.
Embodiment
Below in conjunction with accompanying drawing of the present utility model, further describe embodiment of the present utility model.
Embodiment: production of biodiesel suite of equipment, forming has pipeline, pump, Controlling System, concrete structure is that material tank 1, methanol tank 3, catalyst tank 4 have pipeline to enter pre-heating system 11 respectively, enter main reaction tower 10 by pipeline respectively from pre-heating system again, main reaction tower 10 has pipeline to feed methanol separator 8, wherein also is provided with circulating line on the main reaction tower; Methanol separator 8 is provided with three pipelines, article one, get back to methanol tank 3 by pre-heating system 11, article one, 7, one of feeding cooling systems feed glycerol mixture tripping device 5, have a pipeline to return into catalyst tank 4, have a pipeline to feed cooling system 7 on this device; There is pipeline to communicate on the cooling system 7 respectively with product tank 9, glycerine jar 6; Each pipeline is provided with pump 12; Methanol separator 8, glycerol mixture tripping device 5, pre-heating system 11 interrelates with Controlling System 2.
Wherein, pre-heating system 11 structures are that the bottom is provided with heating element 13, and inside is chamber, oily territory 15, and it is provided with the catalyzer pipeline 14 that runs through, methanol pipeline 16, stock oil pipeline 17, recovery methanol pipeline 18; Cooling system 7 structures are for being provided with cooling water inlet end 19 and cooling water outlet 23, glycerine entrance 21 and outlet, and products pipeline inlet 22 and outlet, glycerine pipeline and products pipeline cooling are coil pipe 20 structures, are provided with dividing plate 24 in the cooling system; Methanol separator 8 structures are that the bottom is provided with heating element, mix products inlet 25, glycerine and catalyst mixture outlet 30, top is provided with methanol steam outlet 28, oil gas vent 29, stir shaft and agitating vane 26 are housed in the methanol separator, and electric motor 27 followed in the axle first line of a couplet; Glycerol mixture tripping device 5 structures are that the bottom is provided with heating element, glycerine and catalyst mixture inlet 31, and catalyst outlet 33, top is provided with glycerine outlet 32, and stir shaft and agitating vane are housed in the glycerol mixture tripping device, and electric motor followed in the axle first line of a couplet; Main reaction tower 10 structures are that the bottom is provided with methanol steam inlet 34, and top is provided with catalyzer and stock oil inlet 36, and reflux inlet 37 is equipped with steam baffle 35 in the tower, and multilayer tower tray 38 has a plurality of pores on the tower tray, steam cover 39 is arranged on each pore.
Can be provided with pump as required on above-mentioned each pipeline, each consumer is controlled by Controlling System (2).
The outlet of material tank, catalyst tank is communicated with main reaction tower top pipeline, and methanol tank is communicated with the lower end inlet duct of main reaction tower with pump, the exit end of main reaction tower is communicated with the inlet end pipeline of methyl alcohol tripping device after with pipeline connection pump again; Methyl alcohol exit end, the export of finished oil end of methyl alcohol tripping device are communicated with the inlet end pipeline of methanol tank product tank after being communicated with pump with pipeline respectively; Two exit end of glycerol mixture tripping device are communicated with the inlet end of glycerine jar, the inlet end pipeline of catalyst tank respectively.The probe of Controlling System is inserted product tank; Again Controlling System is connected with pump, reactor, methyl alcohol tripping device, glycerol mixture tripping device, automatic tester electricity etc. respectively.Said methyl alcohol tripping device includes several parts of well heater, agitator and water cooler.
During use, by the control that Controlling System 2 realizes main reaction tower 10, glycerol mixture tripping device 5, methanol separator 8, all pumps, according to the property of raw material programmed, follow procedure pumps into reactor respectively with stock oil, methyl alcohol, catalyzer.React in reaction tower by predetermined temperature, stirring earthquake intensity, after question response finishes, start the pump between reaction tower and the separator, reaction mixture is pumped in the separator, in separator, methanol gasifying, and after condensation, methyl alcohol is pumped to the methanol tank reuse.Processed oil proportion is light than glycerol mixture, therefore pump into product tank respectively and pump into the glycerol mixture tripping device after processed oil, glycerol mixture being separated and separate, the glycerine after the separation, catalyzer pump into reuse in glycerine jar, the catalyst tank by pump respectively.Processed oil in the product tank is obtained information by the probe of Controlling System and is detected, and with result's feedback, so that original procedure operation or adjustment program are kept in decision.Whole process of production is sealing, no waste gas, waste water, refuse.
Claims (6)
1, production of biodiesel suite of equipment, forming has pipeline, pump, Controlling System, it is characterized in that: material tank (1), methanol tank (3), catalyst tank (4) have pipeline to enter pre-heating system (11) respectively, enter main reaction tower (10) by pipeline respectively from pre-heating system again, main reaction tower (10) has pipeline to feed methanol separator (8), wherein also is provided with circulating line on the main reaction tower; Methanol separator (8) is provided with three pipelines, article one, get back to methanol tank (3) by pre-heating system (11),, a feeding cooling system (7), article one, feed glycerol mixture tripping device (5), have a pipeline to return into catalyst tank (4), have a pipeline to feed cooling system (7) on this device; There is pipeline to communicate on the cooling system (7) respectively with product tank (9), glycerine jar (6); Each pipeline is provided with pump (12); Methanol separator (8), glycerol mixture tripping device (5), pre-heating system (11) interrelates with Controlling System (2).
2, production of biodiesel suite of equipment according to claim 1, it is characterized in that: its structure of described pre-heating system (11) is that the bottom is provided with heating element (13), inside is chamber, oily territory (15), it is provided with the catalyzer pipeline (14) that runs through, methanol pipeline (16), stock oil pipeline (17), recovery methanol pipeline (18).
3, production of biodiesel suite of equipment according to claim 1, it is characterized in that: described cooling system (7) structure is provided with cooling water inlet end (19) and cooling water outlet (23) for it, glycerine entrance (21) and outlet, products pipeline inlet (22) and outlet, glycerine pipeline and products pipeline cooling are coil pipe (20) structure, are provided with dividing plate (24) in the cooling system.
4, production of biodiesel suite of equipment according to claim 1, it is characterized in that: described methanol separator (8) structure is that the bottom is provided with heating element, mix products inlet (25), glycerine and catalyst mixture outlet (30), top is provided with methanol steam outlet (28), oil gas vent (29), stir shaft and agitating vane (26) are housed in the methanol separator, and electric motor (27) followed in the axle first line of a couplet.
5, production of biodiesel suite of equipment according to claim 1, it is characterized in that: described glycerol mixture tripping device (5) structure is that the bottom is provided with heating element, glycerine and catalyst mixture inlet (31), catalyst outlet (33), top is provided with glycerine outlet (32), stir shaft and agitating vane are housed in the glycerol mixture tripping device, and electric motor followed in the axle first line of a couplet.
6, production of biodiesel suite of equipment according to claim 1, it is characterized in that: described main reaction tower (10) structure is that the bottom is provided with methanol steam inlet (34), top is provided with catalyzer and stock oil inlet (36), reflux inlet (37), steam baffle (35) is housed in the tower, multilayer tower tray (38) has a plurality of pores on the tower tray, steam cover (39) is arranged on each pore.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200817173U CN201292347Y (en) | 2008-09-26 | 2008-09-26 | Complete equipment for biodiesel production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200817173U CN201292347Y (en) | 2008-09-26 | 2008-09-26 | Complete equipment for biodiesel production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201292347Y true CN201292347Y (en) | 2009-08-19 |
Family
ID=41005815
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200817173U Expired - Fee Related CN201292347Y (en) | 2008-09-26 | 2008-09-26 | Complete equipment for biodiesel production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201292347Y (en) |
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2008
- 2008-09-26 CN CNU2008200817173U patent/CN201292347Y/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090819 Termination date: 20120926 |