CN102504948A - Device for pretreating biodiesel raw material - Google Patents
Device for pretreating biodiesel raw material Download PDFInfo
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- CN102504948A CN102504948A CN2011103496236A CN201110349623A CN102504948A CN 102504948 A CN102504948 A CN 102504948A CN 2011103496236 A CN2011103496236 A CN 2011103496236A CN 201110349623 A CN201110349623 A CN 201110349623A CN 102504948 A CN102504948 A CN 102504948A
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- reaction kettle
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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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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
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Abstract
The invention provides a device for pretreating a biodiesel raw material. The device comprises a raw material storage tank, an additive storage tank, a reaction kettle, a sedimentation tank, a three-way valve, a decolorizing tank, an air compressor and the like, wherein the raw material storage tank and the additive storage tank are communicated with the inlet of the reaction kettle through a connecting pipeline; a stirrer, a heater and a temperature measuring instrument are arranged on the reaction kettle; the outlet of the reaction kettle is communicated with the inlet of the sedimentation tank through a pipeline; the outlet of the sedimentation tank is communicated with a sewage draining outlet and the inlet of the three-way pipe through a pipeline respectively; the first outlet of the three-way pipe is communicated with the inlet of the reaction kettle through a pipeline; the second outlet of the three-way pipe is communicated with the first inlet of the decolorizing tank through a pipeline; and the second inlet of the decolorizing tank is connected with the outlet of the air compressor through a pipeline. The device can pretreat the biodiesel raw material, and quality assurance is provided for the source of the biodiesel industry raw material.
Description
Technical field
The present invention relates to a kind of pretreatment unit of biodiesel raw material, belong to the biomass energy apparatus field.
Background technology
Along with the increase of global population and improving constantly of living standards of the people, strong day by day to demands for energy.But traditional oil, natural gas source are day by day deficient, and oil shortage has had influence on the energy security strategy of country; On the other hand, along with the enhancing of environmental consciousness, people recognize the air-polluting seriousness that oil acts as a fuel and caused, particularly photo-chemical smog, CO gradually
2The havocs such as Greenhouse effect that produce the eubiosis, so seek to clean the key that substitute energy will become the future world Economic development.Biofuel is nontoxic, biodegradable with it, contain advantages such as SOx hardly in the tail gas becomes one of current most important clean fuel.Topmost composition is fatty acid methyl ester (FAME) in the biofuel.At present, it is higher to be with the animal and plant grease that raw material is made the cost of biofuel, and food and beverage waste oil and grease is recycled, and making biofuel is a good scheme.According to incompletely statistics, the annual waste oil that produces of China's catering trade reaches more than 2,000,000 tons, contains a large amount of harmful materials in the waste cooking oil, can not eat again.At present; The part food and beverage waste oil and grease is recovered industrial raw material such as being processed into lipid acid in China; And most of the utilization again by the lawless person comes into the market again, serious harm human consumer's health of human body, or the food and drink owner directly enters water drain with it; Not only cause the wasting of resources, and serious environment pollution.Utilize waste cooking oil production biofuel; For a new approach is opened up in the utilization again of waste cooking oil; Help the disadvantageous effect that prevents that waste cooking oil from causing ecotope, and can reduce the production cost of biofuel, for the suitability for industrialized production of biofuel provides effective raw material guarantee.
Summary of the invention
It is little to have the purpose of this invention is to provide a kind of pollution, and cost is low, can directly waste cooking oil be converted into the device of biodiesel raw material.
To achieve these goals; The present invention provides a kind of pretreatment unit of biodiesel raw material; This device comprises raw material storage tank, additive storage tank, reaction kettle, setting tank, T-valve, bleacher, air compressor machine etc.; Wherein: said raw material storage tank, additive storage tank are communicated with said reaction kettle import through connecting tube; Whisking appliance, well heater and temperature measurer are installed on the said reaction kettle, and the outlet of said reaction kettle is communicated with the import of said setting tank through pipeline, and the outlet of said setting tank is communicated with the import of sewage draining exit and said T-valve respectively through pipeline; First outlet of said T-valve is communicated with said reaction kettle import through pipeline; Second outlet of said T-valve is communicated with first import of said bleacher through pipeline, and second import of said bleacher is through the outlet of the said air compressor machine of pipe connection, the outlet of said bleacher through pipe connection to the suitable thing diesel production line of delivering a child of biodiesel raw material jar.
Based on above-mentioned, be separately installed with gauger on the connecting tube of said raw material storage tank and said additive storage tank, be respectively equipped with by-pass valve control in the gauger outlet.
Whisking appliance, well heater and temperature measurer are installed on the said reaction kettle, and said reaction kettle top is provided with import, the bottom is provided with outlet and sewage draining exit.
Said setting tank is provided with chuck, can lead to hot water in the chuck, and the outlet and the sewage draining exit of said setting tank bottom are respectively equipped with by-pass valve control.
Said T-valve first outlet, second outlet are respectively equipped with by-pass valve control.
Said bleacher inside is equipped with baffle plate, filter cloth, gac from bottom to top successively, and gac accounts for about 2/3 of tank body height.
Described air compressor machine is piston type air compressor or screw air compressor, and its outlet conduit is equipped with by-pass valve control.
The emulsion splitter that adopts is for being the polyester ether of initiator, propylene oxide and oxyethane copolymerization synthetic multi-segment structure with the quadrol.
The present invention has outstanding substantive distinguishing features and obvious improvement with respect to prior art, and specifically, this device has been realized the cycling and reutilization of waste cooking oil; Can prevent the disadvantageous effect that waste cooking oil causes ecotope; The polyester ether of this device employing multi-segment structure is an emulsion splitter simultaneously, has reduced the purification condition of waste cooking oil, has significantly reduced the cost of biodiesel raw material; Improved the quality of biodiesel raw material, for the suitability for industrialized production of biofuel provides effective raw material guarantee.
Description of drawings
Fig. 1 is a structural representation of the present invention
Among Fig. 1: raw material storage tank 1, additive storage tank 2, gauger 3, by-pass valve control 4, temperature measurer 5, whisking appliance 6, reaction kettle 7, well heater 8, setting tank 9, chuck 10, T-valve 11, bleacher 12, baffle plate 13, filter cloth 14, gac 15, air compressor machine 16
Embodiment
Through embodiment, technical scheme of the present invention is done further detailed description below.
As shown in Figure 1; A kind of pretreatment unit of biodiesel raw material; This device comprises raw material storage tank 1, additive storage tank 2, reaction kettle 7, setting tank 9, T-valve 11, bleacher 12, air compressor machine 16; Wherein: said raw material storage tank 1, additive storage tank 2 are communicated with said reaction kettle 7 imports through connecting tube; Whisking appliance 6, well heater 8 and temperature measurer 5 are installed on the said reaction kettle 7, and the outlet of said reaction kettle 7 is communicated with the import of said setting tank 9 through pipeline, and the outlet of said setting tank 9 is communicated with the import of sewage draining exit and described T-valve 11 respectively through pipeline; First outlet of said T-valve 11 is communicated with said reaction kettle 7 imports through pipeline; Second outlet of said T-valve 11 is communicated with first import of said bleacher 12 through pipeline, and second import of said bleacher 12 is through the outlet of the said air compressor machine 16 of pipe connection, the outlet of said bleacher 12 through pipe connection to the suitable thing diesel production line of delivering a child of biodiesel raw material jar.
Based on above-mentioned, be separately installed with gauger 3 on the connecting tube of said raw material storage tank 1 and said additive storage tank 2, be respectively arranged with by-pass valve control 4 in gauger 3 outlets.The emulsion splitter of the raw material of raw material storage tank 1 and additive storage tank 2 is delivered in the said reaction kettle 7 through connecting tube according to proportioning through gauger 3, accomplishes reinforced.
Based on above-mentioned, whisking appliance 6, well heater 8 and temperature measurer 5 are installed on the said reaction kettle 7, said reaction kettle 7 tops are provided with import, and the bottom is provided with outlet and sewage draining exit.The whisking appliance 6 and well heater 8 of said reaction kettle 7 opened in reinforced back; Waste cooking oil removal of impurities under emulsion splitter and specific process conditions is separated; Removal of impurities is left standstill after separating; Impurity is discharged through the sewage draining exit of said reaction kettle 7, and isolated work in-process are delivered to setting tank 9 through said reaction kettle 7 outlets through connecting tube.
Based on above-mentioned, said setting tank 9 is provided with chuck 10, can lead to hot water in the chuck 10.The outlet and the sewage draining exit of said setting tank 9 bottoms are respectively equipped with by-pass valve control.Isolated work in-process are in setting tank 9 coolings, deposition, and impurity is discharged by sewage draining exit.
Based on above-mentioned, said T-valve 11 first outlets, second outlet are respectively equipped with by-pass valve control.The work in-process that generate are back to reaction kettle 7 at said setting tank 9 post precipitations through T-valve 11 first outlets and carry out the removal of impurities separation once more, under the outlet valve control of said reaction kettle 7, are delivered to setting tank 9 once more through connecting tube.The secondary removal of impurities separates the product post precipitation that generates and is transported to bleacher 12 through T-valve 11 second outlets.
Said bleacher 12 inside are equipped with baffle plate 13, filter cloth 14, gac 15.Said bleacher 12 tops are provided with import, inlet mouth, and the bottom is provided with outlet.Finished product through gac 15 decolourings, after filter cloth 14 filters, reaches the standard of biodiesel raw material in bleacher 12, be transported to the biodiesel raw material jar along delivering a child thing diesel production line through bleacher 12 outlets.
Described air compressor machine 16 is piston type air compressor or screw air compressor, and its outlet conduit is provided with valve.After finished product after the secondary removal of impurities separates arrives bleacher 12, open air compressor machine 16 control bleachers 12 flows, according to flow size adjustment pressure amplitude.
Claims (8)
1. the pretreatment unit of a biodiesel raw material; This device comprises raw material storage tank, additive storage tank, reaction kettle, setting tank, T-valve, bleacher, air compressor machine etc.; Wherein: said raw material storage tank, additive storage tank are communicated with said reaction kettle import through connecting tube; Whisking appliance, well heater and temperature measurer are installed on the said reaction kettle; The outlet of said reaction kettle is communicated with the import of said setting tank through pipeline, and the outlet of said setting tank is communicated with the import of sewage draining exit and said T-valve respectively through pipeline, and first outlet of said T-valve is communicated with said reaction kettle import through pipeline; Second outlet of said T-valve is communicated with first import of said bleacher through pipeline, the outlet of said bleacher through pipe connection to the suitable thing diesel production line of delivering a child of biodiesel raw material jar.
2. according to claim 1, a kind of pretreatment unit of biodiesel raw material is characterized in that: be separately installed with gauger on the connecting tube of said raw material storage tank and said additive storage tank, be respectively equipped with by-pass valve control in the gauger outlet.
3. according to claim 1, a kind of pretreatment unit of biodiesel raw material is characterized in that: whisking appliance, well heater and temperature measurer are installed on the said reaction kettle, and said reaction kettle top is provided with import, the bottom is provided with outlet and sewage draining exit.
4. according to claim 1, a kind of pretreatment unit of biodiesel raw material is characterized in that: said setting tank is provided with chuck, can lead to hot water in the chuck, and the outlet and the sewage draining exit of said setting tank bottom are respectively equipped with by-pass valve control.
5. according to claim 1, a kind of pretreatment unit of biodiesel raw material is characterized in that: said T-valve first outlet, second outlet are respectively equipped with by-pass valve control.
6. according to claim 1, a kind of pretreatment unit of biodiesel raw material is characterized in that: said bleacher inside is equipped with baffle plate, filter cloth, gac from bottom to top successively, and gac accounts for about 2/3 of tank body height.
7. according to claim 1, a kind of pretreatment unit of biodiesel raw material is characterized in that: described air compressor machine is piston type air compressor or screw air compressor, and its outlet conduit is equipped with by-pass valve control.
8. according to claim 1, a kind of pretreatment unit of biodiesel raw material is characterized in that: the emulsion splitter of employing is for being the polyester ether of initiator, propylene oxide and oxyethane copolymerization synthetic multi-segment structure with the quadrol.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103496236A CN102504948A (en) | 2011-11-08 | 2011-11-08 | Device for pretreating biodiesel raw material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011103496236A CN102504948A (en) | 2011-11-08 | 2011-11-08 | Device for pretreating biodiesel raw material |
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| Publication Number | Publication Date |
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| CN102504948A true CN102504948A (en) | 2012-06-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011103496236A Pending CN102504948A (en) | 2011-11-08 | 2011-11-08 | Device for pretreating biodiesel raw material |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104726198A (en) * | 2015-03-06 | 2015-06-24 | 岳阳东方阳光生物能源科技有限公司 | Decolorization method and equipment for waste cooking oil biodiesel |
-
2011
- 2011-11-08 CN CN2011103496236A patent/CN102504948A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104726198A (en) * | 2015-03-06 | 2015-06-24 | 岳阳东方阳光生物能源科技有限公司 | Decolorization method and equipment for waste cooking oil biodiesel |
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Application publication date: 20120620 |