CN200943067Y

CN200943067Y - Biology diesel production device

Info

Publication number: CN200943067Y
Application number: CNU2006201095743U
Authority: CN
Inventors: 杨国威
Original assignee: Individual
Current assignee: Individual
Priority date: 2006-08-10
Filing date: 2006-08-10
Publication date: 2007-09-05
Anticipated expiration: 2016-08-10

Abstract

The utility model is the device for production of bio-diesel and pertains to the diesel production equipment and is applicable for production of bio-diesel from the wasted animal and plant oil.The device comprises a control cabinet, a crude oil tank, a methanol tan, a catalyst tank, a reactor, a separator, a finished oil tank, an automatic checkout meter, a glycerin tank, a glycerin mixture separation device and a pump.The exit terminals of the crude oil tank, the methanol tan and the catalyst tank are communicated with the pump and then communicated with the entry terminal of the reactor; the exit terminal of the reactor is communicated with the pump and then is communicated with the entry terminal of the separator; the methanol exit terminal of the separator, the finished oil exit terminal and the glycerin mixture exit terminal are respectively communicated with the pump and then are communicated with the entry terminal of the methanol tank, the finished oil tank and the glycerin mixture separation device; the two exit terminals of the glycerin mixture separating device are respectively communicated with the pump and then communicated with the glycerin tank entry terminal and the catalyst tank entry terminal; the automatic checkout probe is inserted into the finished oil tank; the control cabinet is respectively connected with the pump, the reactor, the separator, the glycerin mixture separating device and the automatic checkout.

Description

Production biofuel device

One, 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 aste vegetable oil and animal fat production biofuel.

Two, background technology

Production biofuel device is to adopt secondary processing at present, just produces diesel oil by processes such as reaction, distillations, and equipment used is expensive, temperature required height, and therefore power consumption is big, and the cost height is discharged waste water simultaneously, pollutes.So far, do not have pollution-freely as yet, power consumption is few, low cost, and the production biofuel device of good quality and high output is for the usefulness of utilizing aste vegetable oil and animal fat production biofuel.

Three, summary of the invention

The purpose of this utility model is to overcome the existing existing cost height of production biofuel device, big, the with serious pollution weak point of power consumption, thereby provide a kind of production biofuel device, it is 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 aste vegetable oil and animal fat production biofuel.

The purpose of this utility model realizes by following approach:

The utility model includes housing, material tank, methanol tank, catalyst tank, reactor, separator, product tank, automatic tester, the glycerine jar, several parts of glycerol mixture tripping device and pump, with material tank, methanol tank, after the exit end difference pipeline of catalyst tank is communicated with pump, be communicated with the inlet end pipeline of reactor, is communicated with the inlet end pipeline of separator after again the exit end pipeline of reactor being communicated with pump, with three exit end of separator respectively behind the pipelines connection pumps with methanol tank, the inlet end pipeline of product tank and glycerol mixture tripping device is communicated with; Two exit end of glycerol mixture tripping device are communicated with the inlet end of glycerine jar, the inlet end pipeline of catalyst tank behind the pipeline connection pump respectively; The probe of automatic tester is inserted product tank; Again housing is electrically connected with pump, reactor, separator, glycerol mixture tripping device, automatic tester respectively.Said separator includes agitator and several parts of water cooler, and the set spiral tube inlet end pipeline of the methyl alcohol gas exit end that agitator top is set and water cooler is communicated with.Said water cooler is to establish spiral tube in container, and the spiral tube two ends are communicated with spiral tube inlet end, methyl alcohol exit end respectively, fills cold water in the container.Said agitator is to be provided with the motor that is connected with axle and governor box at the top of container, be provided with at least three slurries after inserting axle in the container, and in container, be provided with the spiral vapour pipe, its inlet end, exit end be propelling container respectively, be convenient to feed heating steam, establish inlet end and methyl alcohol gas exit end more respectively on container top, the middle part is set as product oil export end, the glycerol mixture exit end is established in the 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.

Four, description of drawings

Fig. 1 is the structural frames diagram synoptic diagram of the utility model embodiment, wherein:

1-housing, 2-material tank, 3-methanol tank, 4-catalyst tank, 5-reactor, 6-separator, 7-product tank, 8-automatic tester, 9-glycerine jar, 10-glycerol mixture tripping device, 11-pump.

Fig. 2 is the structural representation of the utility model embodiment separator, wherein:

12-agitator, 13-water cooler, 14-methyl alcohol gas exit end, 15-spiral tube inlet end, 16-methyl alcohol exit end, 17-export of finished oil end, 18-glycerol mixture exit end, 19-inlet end, 20-vapour pipe, 21-motor, 22-axle, 23-slurry, 24-vapour pipe inlet end, 25-vapour pipe exit end, 26-container, 27-container, 28-spiral tube.

Five, embodiment

The utility model describes in detail below in conjunction with accompanying drawing embodiment:

The utility model embodiment includes housing 1, material tank 2, methanol tank 3, catalyst tank 4, reactor 5, separator 6, product tank 7, automatic tester 8, glycerine jar 9, glycerol mixture tripping device 10 and pump more than 11 parts, the exit end of material tank 2, methanol tank 3, catalyst tank 4 is communicated with the inlet end pipeline of reactor 5 pipeline connection pump 11 backs respectively, and exit end pipeline connection pump 11 backs with reactor 5 are communicated with inlet end 19 pipelines of separator 6 again; Methyl alcohol exit end 16, export of finished oil end 17, the glycerol mixture exit end 18 of separator 6 are communicated with the inlet end pipeline of methanol tank 3, product tank 7 and glycerol mixture tripping device 10 pipeline connection pump 11 backs respectively; Two exit end of glycerol mixture tripping device 10 are communicated with the inlet end of glycerine jar 9, the inlet end pipeline of catalyst tank 4 pipeline connection pump 11 backs respectively; The probe of automatic tester 8 is inserted product tank 7; Again housing 1 is electrically connected with pump 11, reactor 5, separator 6, glycerol mixture tripping device 10, automatic tester 8 respectively.Said separator 6 includes agitator 12 and water cooler more than 13 parts, and the methyl alcohol gas exit end 14 that agitator 12 tops are set and water cooler 13 set spiral tube inlet end 15 pipelines are communicated with.Said water cooler 13 is to establish spiral tube 28 in container 26, and spiral tube 28 two ends are communicated with spiral tube inlet end 15, methyl alcohol exit end 16 respectively, fills cold water in the container 26.Said agitator 12 is to be provided with the motor 21 that is connected with axle 22 and governor box at the top of container 27, be provided with at least three slurries 23 after inserting axle 22 in the container 27, and in container 27, be provided with spiral vapour pipe 20, its vapour pipe inlet end 24, vapour pipe exit end 25 be propelling container 27 respectively, so that feeding heating steam, establish inlet end 19 and methyl alcohol gas exit end 14 more respectively on container 27 tops, the middle part is set as product oil export end 17, glycerol mixture exit end 18 is established in the bottom.

During use, by the control of housing 1 realization to reactor 5, separator 6, glycerol mixture tripping device 10, automatic tester 8 and all pumps 11, according to the property of raw material programmed, follow procedure pumps into stock oil, methyl alcohol, catalyzer respectively in the reactor 5, react in reactor 5 by predetermined temperature, stirring earthquake intensity, after question response finishes, start the pump 11 between reactor 5 and the separator 6, reaction mixture is pumped in the separator 6, in separator 6, methanol gasifying, and after condensation, methyl alcohol is pumped to methanol tank 3 reuses.Processed oil proportion is light than glycerol mixture, therefore pump into product tank 7 respectively and pump into glycerol mixture tripping device 10 after processed oil, glycerol mixture being separated and separate, the glycerine after the separation, catalyzer pump into reuse in glycerine jar 9, the catalyzer 4 by pump 11 respectively.Processed oil in the product tank 7 is obtained information by the probe of automatic tester 8 and is detected, and the result is fed back to housing 1, 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

1, a kind of production biofuel device, it is waited to levy and is: include housing (1), material tank (2), methanol tank (3), catalyst tank (4), reactor (5), separator (6), product tank (7), automatic tester (8), glycerine jar (9), glycerol mixture tripping device (10) and several parts of pump (11), with material tank (2), methanol tank (3), after the exit end difference pipeline of catalyst tank (4) is communicated with pump (11), be communicated with the inlet end pipeline of reactor (5), exit end pipeline connection pump (11) back with reactor (5) is communicated with inlet end (19) pipeline of separator (6) again; Methyl alcohol exit end (16), export of finished oil end (17), the glycerol mixture exit end (18) of separator (6) are communicated with the inlet end pipeline of methanol tank (3), product tank (7) and glycerol mixture tripping device (10) pipeline connection pump (11) back respectively; Two exit end of glycerol mixture tripping device (10) are communicated with the inlet end of glycerine jar (9), the inlet end pipeline of catalyst tank (4) pipeline connection pump (11) back respectively; The probe of automatic tester (8) is inserted product tank (7); Again housing (1) is electrically connected with pump (11), reactor (5), separator (6), glycerol mixture tripping device (10), automatic tester (8) respectively.

2, by the described production biofuel of claim 1 device, it is characterized in that: said separator (6) includes agitator (12) and several parts of water cooler (13), and set spiral tube inlet end (15) pipeline of the methyl alcohol gas exit end (14) that agitator (12) top is set and water cooler (13) is communicated with.

3, by the described production biofuel of claim 2 device, it is characterized in that: said water cooler (13) is to establish spiral tube (28) in container (26), and spiral tube (28) two ends are communicated with spiral tube inlet end (15), methyl alcohol exit end (16) respectively.

4, by the described production biofuel of claim 2 device, it is characterized in that: said agitator (12) is to be provided with the motor (21) that is connected with axle (22) and governor box at the top of container (27), be provided with at least three slurries (23) after inserting axle 22 in the container (27), and in container (27), be provided with spiral vapour pipe (20), its vapour pipe inlet end (24), vapour pipe exit end (25) is propelling container (27) respectively, establish inlet end (19) and methyl alcohol gas exit end (14) respectively on container (27) top again, the middle part is set as product oil export end (17), and glycerol mixture exit end (18) is established in the bottom.