CN201292349Y - Novel biodiesel production apparatus - Google Patents

Novel biodiesel production apparatus Download PDF

Info

Publication number
CN201292349Y
CN201292349Y CNU2008201999836U CN200820199983U CN201292349Y CN 201292349 Y CN201292349 Y CN 201292349Y CN U2008201999836 U CNU2008201999836 U CN U2008201999836U CN 200820199983 U CN200820199983 U CN 200820199983U CN 201292349 Y CN201292349 Y CN 201292349Y
Authority
CN
China
Prior art keywords
main body
apparatus main
methanol steam
inlet tube
outlet pipe
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
Application number
CNU2008201999836U
Other languages
Chinese (zh)
Inventor
王�华
李一哲
包桂蓉
苏有勇
胡建杭
李法社
李仕一
徐娟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kunming University of Science and Technology
Original Assignee
Kunming University of Science and Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kunming University of Science and Technology filed Critical Kunming University of Science and Technology
Priority to CNU2008201999836U priority Critical patent/CN201292349Y/en
Application granted granted Critical
Publication of CN201292349Y publication Critical patent/CN201292349Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

Landscapes

  • Liquid Carbonaceous Fuels (AREA)

Abstract

The utility model relates to a novel device for producing biodiesel, comprising a raw oil inlet pipe, a spray header, a device body, a solid catalyst inlet, a methanol vapor conveying pipe, a methanol vapor inlet pipe, a methanol vapor outlet pipe, a product outlet pipe, a blower and a catalyst recycling opening. The device for producing biodiesel has the advantages of novel structure, simplicity, practicability, high production efficiency, less investment, no pollution, low energy consumption and cost as well as high quality and yield, and is suitable for producing biodiesel by utilizing animal and vegetable fat and waste oil.

Description

Novel production biofuel device
Technical field
The utility model relates to a kind of production biofuel device, belongs to the production unit of diesel oil, is suitable for utilizing the usefulness of animal-plant oil and waste oil production biofuel.
Background technology
Production biofuel device adopts esterification techniques at present, and raw oil material is produced diesel oil by processes such as esterification, distillation purifications, but the equipment used costliness, the temperature of reaction height, main is that efficient is lower, thereby causes big energy consumption, expensive, discharge waste water simultaneously, pollute.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.
Summary of the invention
The purpose of this utility model is 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 provide a kind of production biofuel device, its production efficiency height, simple in structure, pollution-free, power consumption is few, cost is low, and good quality and high output is suitable for utilizing the usefulness of animal-plant oil and waste oil production biofuel.
The purpose of this utility model is achieved in that this device comprises stock oil inlet tube, spray header, apparatus main body, solid catalyst inlet, methanol steam transfer lime, methanol steam inlet tube, methanol steam outlet pipe, products export pipe, gas blower, several parts of catalyst recovery mouth.Apparatus main body divides left and right sides two portions, in the left part by under the methanol steam transfer lime is arranged, the apparatus main body sidepiece of solid catalyst inlet above the methanol steam transfer lime outside, the stock oil inlet tube that the below connects spray header is connected with the apparatus main body upper left quarter, the methanol steam inlet tube that is connected with gas blower is connected with the apparatus main body bottom surface, the methanol steam outlet pipe is communicated with the device body upper top, the products export pipe is communicated with the bottom of apparatus main body, and there is the catalyst recovery mouth on the apparatus main body right side near the side of bottom.
The utility model contrast prior art has following advantage:
1, simple in structure, the less investment of the utility model;
2, the utility model power consumption is few, and cost is low;
3, the utility model is pollution-free, good quality and high output, and economic benefit height, social benefit are good.
Description of drawings
Describe concrete structure of the present utility model in detail below in conjunction with accompanying drawing, but structure of the present utility model is not limited to shown in the accompanying drawing.
Fig. 1 is a structural representation of the present utility model:
Among Fig. 1, the utility model comprises stock oil inlet tube 1, spray header 2, apparatus main body 3, solid catalyst inlet 4, methanol steam transfer lime 5, products export pipe 6, gas blower 7, methanol steam inlet tube 8, catalyst recovery mouth 9, methanol steam outlet pipe more than 10 parts.
Embodiment
3 fens left and right sides two portions of apparatus main body, the left side is inner to have methanol steam transfer lime 5 by the lower section, solid catalyst inlet 4 outside methanol steam transfer lime 5 above apparatus main body 3 sidepieces, the stock oil inlet tube 1 that the below connects spray header 2 is connected with apparatus main body 3 upper left quarters, the methanol steam inlet tube 8 that is connected with gas blower 7 is connected with apparatus main body 3 bottom surfaces, methanol steam outlet pipe 10 is communicated with apparatus main body 3 upper end, products export pipe 6 is communicated with the bottom of apparatus main body 3, and there is catalyst recovery mouth 9 on apparatus main body 3 right sides near the side of bottom.
Reaction raw materials oil enters reaction unit main body 3 by stock oil inlet tube 1 after spray head atomizing, landing downwards, catalyzer is constantly put into methanol steam transfer lime 5 tops by catalyst inlet 4 places, under the drive of methanol steam, react with methanol steam and the stock oil that descends, the gas blower 7 that is installed on bottom of device can bring to reactor head with methanol steam and catalyzer according to reaction condition, catalyzer separates with methanol steam under action of gravity on the right side of main reaction device, and being pooled to catalyst recovery mouth 9 can reuse.Methanol steam can reuse after being collected by methanol steam outlet pipe 10, and the product that reacts completely can be discharged by products export pipe 6.Whole process of production is sealing, no waste gas, waste water, refuse.

Claims (1)

1, a kind of novel production biofuel device, it is characterized in that: by stock oil inlet tube (1), spray header (2), apparatus main body (3), solid catalyst inlet (4), methanol steam transfer lime (5), products export pipe (6), gas blower (7), methanol steam inlet tube (8), catalyst recovery mouth (9), methanol steam outlet pipe (10) is formed, apparatus main body (3) divides left and right sides two portions, in the left part by under methanol steam transfer lime (5) is arranged, solid catalyst inlet (4) is at apparatus main body (3) sidepiece of top, methanol steam transfer lime (5) outside, the stock oil inlet tube (1) that the below connects spray header (2) is connected with apparatus main body (3) upper left quarter, the methanol steam inlet tube (8) that is connected with gas blower (7) is connected with apparatus main body (3) bottom surface, methanol steam outlet pipe (10) is communicated with apparatus main body (3) upper end, products export pipe (6) is communicated with the bottom of apparatus main body (3), and there is catalyst recovery mouth (9) on apparatus main body (3) right side near the side of bottom.
CNU2008201999836U 2008-11-14 2008-11-14 Novel biodiesel production apparatus Expired - Fee Related CN201292349Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201999836U CN201292349Y (en) 2008-11-14 2008-11-14 Novel biodiesel production apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201999836U CN201292349Y (en) 2008-11-14 2008-11-14 Novel biodiesel production apparatus

Publications (1)

Publication Number Publication Date
CN201292349Y true CN201292349Y (en) 2009-08-19

Family

ID=41005817

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008201999836U Expired - Fee Related CN201292349Y (en) 2008-11-14 2008-11-14 Novel biodiesel production apparatus

Country Status (1)

Country Link
CN (1) CN201292349Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103266017A (en) * 2013-06-17 2013-08-28 长沙理工大学 Method for increasing synthesis reaction efficiency of biodiesel

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103266017A (en) * 2013-06-17 2013-08-28 长沙理工大学 Method for increasing synthesis reaction efficiency of biodiesel
CN103266017B (en) * 2013-06-17 2014-10-29 长沙理工大学 Method for increasing synthesis reaction efficiency of biodiesel

Similar Documents

Publication Publication Date Title
CN101195572A (en) Method for synthesizing fatty acid methyl ester
CN100999676B (en) Process of preparing rich acetone alcohol biological oil by biomass microwave catalytic pyrolysis
CN105623861B (en) A kind of glycerine esterification reaction unit
CN103242966A (en) Technology process for producing biodiesel and key preparation device
CN201372257Y (en) Device for continuously cracking organic glass to regenerate methyl methacrylate
CN201292349Y (en) Novel biodiesel production apparatus
CN201626935U (en) Catalysis chamber of gasification furnace for recycling waste plastics and discarded tires
CN201292348Y (en) Novel biodiesel production reaction column
CN201292350Y (en) Novel biodiesel production apparatus
CN217600667U (en) Straw gasification gas making system
CN210163395U (en) Multistage purification equipment for producing coal gas by cracking coal with small particle size for preparing molded coal
CN209221538U (en) A kind of base oil rectifier unit
CN201988310U (en) Synthesis ammonia decarbonizing flash steam recovery device
CN202595048U (en) Divide defeated type skid-mounted pressure boost collection defeated device
CN103194255B (en) Catalytic cracking animal-plant oil produces the method for clean fuel
CN201106029Y (en) Four-stage series chlorohydrination reaction device
CN201272776Y (en) Apparatus for continuous preparation of biodiesel by neutral grease
CN105733820A (en) High-purity biodiesel preparation equipment
CN201817459U (en) Illegal cooking oil methyl esterification device
CN201912883U (en) Tail gas absorption tower
CN210287238U (en) Waste mineral oil steady voltage pyrolysis system
CN205062012U (en) Ultrasonic wave serialization biodiesel fuel production device
CN201279455Y (en) Device for replacing hydrogen using steam
CN203904293U (en) Detarring and moisture removing purifying device
CN215388517U (en) Device for improving recovery rate of dimethyl carbonate device tail gas materials

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: 20111114