CN201454476U - Automatic continuous-type production equipment for emulsifying fuel oil - Google Patents
Automatic continuous-type production equipment for emulsifying fuel oil Download PDFInfo
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- CN201454476U CN201454476U CN2009201194634U CN200920119463U CN201454476U CN 201454476 U CN201454476 U CN 201454476U CN 2009201194634 U CN2009201194634 U CN 2009201194634U CN 200920119463 U CN200920119463 U CN 200920119463U CN 201454476 U CN201454476 U CN 201454476U
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- oil
- tempering tank
- static mixer
- pipe
- automatic production
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Abstract
The utility model relates to fuel oil emulsification equipment, particularly to the automatic continuous-type production equipment for emulsifying fuel oil. The equipment comprises mixing components, oil inlet/outlet components and catalytic components, wherein the mixing components comprise a heating pan, a stirring pan and a storage pan which are sequentially connected through pipelines; a water inlet pipe is arranged on the heating pan; a material feed pipe is arranged on the stirring pan; a material discharge pipe is arranged on the storage pan; the oil inlet/outlet components comprise an oil inlet pipe, an oil surge tank and an oil outlet pipe which are sequentially connected; the catalytic components comprise a front static mixer, a front mixing barrel, a rear mixing barrel and a rear static mixer which are sequentially connected; the front static mixer is respectively connected with the oil outlet pipe and the material discharge pipe; and a product oil outlet is arranged on the rear static mixer. The continuous-type production equipment has the advantages of capability of emulsifying fuel oil continuously, good emulsification effect, high production efficiency and simple and convenient operation.
Description
Technical field
The utility model relates to a kind of fuel emulsification device, is specifically related to a kind of fuel emulsification continuous type automatic production device, belongs to chemical machinery field
Background technology
Energy shortage, especially the petroleum resources shortage brings great influence to human social development, solves the two big eternal problems that energy shortage and environmental pollution make human development.Except that the new regenerative resource of research, save the existing energy exactly, especially fossil energy.Fuel emulsification is the new and high technology of fuel oil industry a kind of energy-saving and cost-reducing, the environmental protection of rising both at home and abroad in recent years, mainly is by mixing a certain proportion of soft water in the fuel oil and multiple additives emulsification forms.
Chinese patent ZL200320103011.X, a kind of diesel emulsion machine is disclosed, in this mulser, the stirrer-driven motor is installed in the center of reactor loam cake, turbo blade on the agitator stretches in the reactor, electric heater is installed in the below of turbo blade, covers to be provided with diesel oil inlet, water inlet and additive inlet on reactor.The static emulsion device places outside the reactor, and the feed end of static emulsion device is connected with the discharging opening of reactor bottom by reversal valve and circulating pump, and its other end stretches in the reactor from the reactor loam cake.Circulating pump places on the duct coupling between the discharging opening of reversal valve and reactor bottom.This mulser stirs by the turbine stirrer in the reactor, adopts the electric heater low-temperature heat simultaneously, is aided with the emulsification of the outer static emulsion device of reactor again.
From above patent as can be seen, the emulsifying device of fuel oil is normally introduced an emulsifier with fuel oil, water, emulsifying agent at present, make three kinds of compositions in emulsifier, be stirred mixing, after finishing emulsification, emulsified fuel is drawn, and then introduce new fuel oil, water and emulsifying agent again and repeat aforementioned mixing.Prior art is not introduced an emulsifier with fuel oil, water, emulsifying agent at present, the new and high technology that three kinds of compositions are mixed in emulsifier; If having also is the hysteresis of synthetic technology equipment, exist the inhomogeneous and emulsion of particle water state size and can not be dispersed in contradiction among the fuel oil, therefore the raising of the stability of emulsified fuel product and combustibility is caused and have a strong impact on, and can not realize the continuity production of Emulsification of Fuel Oil, production efficiency is not high, and operation also bothers.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of reasonable in design, continuously to fuel emulsification, and emulsify well, production efficiency height, fuel emulsification continuous type automatic production device easy and simple to handle.
It is this a kind of fuel emulsification continuous type automatic production device that the utility model solves the problems of the technologies described above the technical scheme that is adopted, its design feature is: by electric hybrid module, advance the oil storage assembly and catalytic module is formed, wherein, electric hybrid module comprises heating kettle, agitated kettle and the storage pot that connects successively by pipeline, heating kettle is provided with water inlet pipe, agitated kettle is provided with feed pipe, stores pot and is provided with discharge nozzle; Advance the oil storage assembly and comprise oil inlet pipe, oily vacuum tank and the flowline that connects successively; Catalytic module comprises the preceding static mixer that links to each other successively, preceding tempering tank, back tempering tank and back static mixer, and preceding static mixer links to each other with discharge nozzle with flowline respectively, and back static mixer is provided with export of finished oil.
Heating kettle described in the utility model, agitated kettle, storage pot, oily vacuum tank, preceding tempering tank and back tempering tank are the double seal structure, and described heating kettle, agitated kettle, storage pot, oily vacuum tank, preceding tempering tank go out pipe with steam inlet tube and steam respectively with the back tempering tank and link to each other.
Be respectively arranged with heating-up temperature table, storage temperature table, oil temperature table, preceding thermometer and back thermometer on heating kettle described in the utility model, storage pot, oily vacuum tank, preceding tempering tank and the back tempering tank.
Be respectively arranged with water filter and oil strainer on discharge nozzle described in the utility model and the flowline.
Be respectively arranged with water flow controller and oily flow controller on discharge nozzle described in the utility model and the flowline.
Discharge nozzle described in the utility model is provided with centrifugal pump.
Be provided with rear pump or output pump between back tempering tank described in the utility model and the back static mixer.
The utility model is compared with prior art and is had the following advantages and effect: the high efficiency fuel emulsification continuous type automatic production device of the utility model research and development design, be applied to the emulsification of fuel oil, make fuel oil, water, three kinds of compositions of emulsifying agent introduce one at emulsifier, mix, form new fuel oil.The innovation of technology has remedied the deficiencies in the prior art, has filled up domestic blank, reaches international most advanced level.The fuel emulsification continuous type automatic production device of the utility model design, water mixed catalyst and fuel oil process are mixed, the constant temperature high efficiency that by static mixer twice mixes and stirs twice tempering tank stirs, make water mixed catalyst and fuel oil under the effect of catalyst, make fuel oil energy access sufficient mixing and emulsification, improve the quality of emulsified fuel.The utility model uses dynamo-electric mechanical technique, dexterously circuit, oil circuit, water route in the equipment is organically combined, and reaches stable and safe and reliable, production efficiency high yield height, but quantity-produced automatic production line.The oil emulsion of equipment preparation has rate of economizing gasoline height (rate of economizing gasoline reaches 15-30%), and the discharging of this nothing of combustion rate strong basis flue dust does not have corrosion to combustion apparatus, advantages such as oil emulsion steady quality, anti-storage transportation, environmental protection, and the innovation of technology reaches international most advanced level.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the structural representation of agitated kettle of the present utility model.
The specific embodiment
Below in conjunction with embodiment the utility model is described in further detail, following examples are to explanation of the present utility model and the utility model is not limited to following examples.
Embodiment 1:
As shown in Figure 1, 2, present embodiment by electric hybrid module I, advance oil storage assembly II, catalytic module III and form, realize the emulsification of fuel oils making fuel oil, water, three kinds of compositions of emulsifying agent introduce one by three big combination of components at emulsifier, mix, form new fuel oil.The primary structure of each assembly is:
Electric hybrid module I: by water inlet pipe 1, feed pipe 4, heating kettle 5, agitated kettle 6, storage pot 7, preceding pipeline pump 9, back tubing pump 9-1, water filter 10, centrifugal pump 11, water flow controller 15, outlet pipe 32, discharge nozzle 33, check valve 16, heating-up temperature table 37 and storage temperature table 37-1.
Advance oil storage assembly II: by oil inlet pipe 12, oil pump 13, oily vacuum tank 14, oil strainer 10, oily flow controller 15-1, flowline 34, oil temperature table 37-2.
Catalytic module III: by mixing tube 8, rear pump or output pump 13-1, preceding static mixer 17, preceding tempering tank 18, back tempering tank 19, communicating pipe 25, back static mixer 35, export of finished oil pipe 36, preceding thermometer 37-3, back thermometer 37-4.
Above-described heating kettle 5, store pot 7, oil vacuum tank 14, preceding tempering tank 18 and back tempering tank 19 are double-deck spacer structure. and with heating kettle 5 is example, heating kettle 5 is provided with outer wall 26-1 and inwall 26, place raw material in the inwall, airtight jacket space that outer wall 26-1 and inwall 26 surround and steam inlet tube 2, steam goes out pipe 3 and is connected, for the vapor stay heating. heating kettle 5, store pot 7, oil vacuum tank 14, before tempering tank 18 and back tempering tank 19 respectively with steam inlet tube 2, steam goes out pipe 3 and links to each other. raw water, the sealing in endothecium structure of emulsifying agent and oil is flowed, and the steam of heating usefulness flows in interlayer.
Annexation between each parts of electric hybrid module I is: water inlet pipe 1 is sealedly connected and fixed with heating kettle 5, and water enters in the heating kettle 5 by water inlet pipe 1; Be connected by outlet pipe 32 between heating kettle 5 and the agitated kettle 6, outlet pipe 32 is provided with preceding pipeline pump 9 and valve (a) 8, and agitated kettle 6 is provided with feed pipe 4.Agitated kettle 6 is connected by back outlet pipe 32-1 with storage pot 7.Back outlet pipe 32-1 is provided with back tubing pump 9-1 and valve (b) 8-1.Store pot 7 and be provided with discharge nozzle 33, be disposed with valve (c) 8-2, water filter 10, centrifugal pump 11, water flow controller 15 and check valve 16 on the discharge nozzle 33.Heating-up temperature table 37 is arranged on the heating kettle 5, and storage temperature table 37-1 is arranged on and stores on the pot 7.Can measure heating kettle 5 and store pot temperature of 7 interior water.
Steam inlet tube 2 and steam go out pipe 3 usefulness flanges and set bolt and heating kettle 5 and 7 storages pots 7 and are sealedly connected and fixed, steam inlet tube 2 and steam go out pipe 3 and are communicated with interlayer pot wall 26, steam can enter from steam inlet tube 2, stops in the space of interlayer pot wall 26, goes out pipe from steam and goes out for 3 times.
The annexation of advancing between each parts of oil storage assembly II is: oil inlet pipe 12 usefulness flanges and set bolt and oily vacuum tank 14 are sealedly connected and fixed, and oil enters in the oily vacuum tank 14 by oil inlet pipe 12.Valve (f) 8-5 and oil pump 13 are installed on the oil inlet pipe 12, and oil temperature table 37-2 is fixedlyed connected with oily vacuum tank 14, can measure the temperature in the oily vacuum tank 14; Flowline 34 usefulness flanges and set bolt and oily vacuum tank 14 are sealedly connected and fixed, and valve (d) 8-3, oil strainer 10 and oily flow controller 15-1 are installed on 34 flowlines successively.
Steam inlet tube 2, steam go out pipe 3 and are sealedly and fixedly connected with oily vacuum tank 14, and type of attachment is consistent with the type of attachment that steam inlet tube 2, steam go out pipe 3 and heating kettle 5.
Annexation between each parts of catalytic module III is: discharge nozzle 33 and flowline 34 are fixed with mixing tube 25-1 welded seal, and mixing tube 25-1 is connected with preceding tempering tank 18, and mixing tube 25-1 is provided with preceding static mixer 17.Preceding tempering tank 18 is connected by communicating pipe 25 with back tempering tank 19, and back tempering tank 19 is provided with production tube 38, is disposed with valve (e) 8-4, rear pump or output pump 13-1, back static mixer 35 and export of finished oil pipe 36 on the production tube 38.Thermometer 37-3 and back thermometer 37-4 before on preceding tempering tank 18 and back tempering tank 19, being separately installed with, the temperature of liquid in tempering tank 18, the back tempering tank 19 before preceding thermometer 37-3, back thermometer 37-4 can be determined at respectively.
Steam inlet tube 2, steam go out pipe 3 and are sealedly and fixedly connected with preceding tempering tank 18, back tempering tank 19 respectively, and type of attachment is consistent with the type of attachment that steam inlet tube 2, steam go out pipe 3 and heating kettle 5.
Agitated kettle 6 of the present utility model, preceding tempering tank 18 are consistent with the structure of back tempering tank 19, all has agitating function, with agitated kettle 6 is example, and the structure of its agitating device is: agitated kettle 6 is provided with motor 20, motor shaft 21, adapter sleeve 29, bearing 22 and sealing ring 23.Motor shaft 21 is an one with motor 20, bearing 22 and sealing ring 23 are installed in the adapter sleeve 29, and motor shaft 21 penetrates bearing 22 and sealing ring 23, and adapter sleeve 29 is fixing with motor 20 welding, be welded with on the motor shaft 21 and stir bar 24, fixed screw 28 is sealedly connected and fixed adapter sleeve 29 and agitated kettle 6.
The number of tempering tank can also be 3 or 4.
The method of emulsification is: use foregoing equipment, by water inlet pipe 1 water is poured into heating kettle 5, with steam the water in the heating kettle 5 is warmed to the 40-60 degree, Open valve (a) 8, with preceding pipeline pump 9 water is sent in the agitated kettle 6 then, by feed pipe 4 the 1-3% emulsifying agent is added agitated kettle 6 and mix stirring with the water of 97-99%, the speed of stirring is 1200-1600 rev/min, obtains emulsifying agent water.Open valve (b) 8-1 starts back tubing pump 9-1, emulsifying agent water is drawn into store in the pot 7, and control temperature 40-60 degree constant temperature stores; Open and control valve (c) 8-2 and centrifugal pump 11, emulsifying agent water passes through the flow-control of water flow controller 15 through the filtration of water filter 10, enters mixing tube 25-1 with the ratio of 10-30%.
Open valve (f) 8-5, start oil pump 13, make fuel oil enter oily vacuum tank 14, be heated to the 40-60 degree, obtain the constant temperature fuel oil, constant temperature stores then.Open and control valve (d) 8-3, fuel oil passes through the flow-control of oily flow controller 15-1 through the filtration of oil strainer 10-1, enters mixing tube 25-1 with the ratio of 70-90% and mixes with emulsifying agent water.Static mixer 17 mixed stirring before emulsifying agent water and constant temperature fuel oil entered, tempering tank 18 and back tempering tank 19 before entering successively then, carrying out 40-60 degree constant temperature high efficiency stirs, open valve (e) 8-4, start rear pump or output pump 13-1, emulsified fuel is stirred by the mixing of back static mixer 35 again, enter export of finished oil 36, form emulsified fuel.
With the emulsified fuel that the equipment of present embodiment and method are made, constant product quality, oil, water are not easily separated; Oven Method through routine detects, and keeps 72 hours at 85 ℃, and water yield is below 2.0%.
In addition, need to prove, the specific embodiment described in this specification, its zero, the shape of parts, institute's title of being named etc. can be different.Allly conceive equivalence or the simple change that described structure, feature and principle are done, be included in the protection domain of the utility model patent according to the utility model patent.The utility model person of ordinary skill in the field can make various modifications or replenishes or adopt similar mode to substitute described specific embodiment; only otherwise depart from structure of the present utility model or surmount the defined scope of these claims, all should belong to protection domain of the present utility model.
Though the utility model with embodiment openly as above; but it is not in order to limit protection domain of the present utility model; any technical staff who is familiar with this technology, change and the retouching done in not breaking away from design of the present utility model and scope all should belong to protection domain of the present utility model.
Claims (7)
1. fuel emulsification continuous type automatic production device, it is characterized in that: by electric hybrid module, advance the oil storage assembly and catalytic module is formed, wherein, electric hybrid module comprises heating kettle, agitated kettle and the storage pot that connects successively by pipeline, heating kettle is provided with water inlet pipe, agitated kettle is provided with feed pipe, stores pot and is provided with discharge nozzle; Advance the oil storage assembly and comprise oil inlet pipe, oily vacuum tank and the flowline that connects successively; Catalytic module comprises the preceding static mixer that links to each other successively, preceding tempering tank, back tempering tank and back static mixer, and preceding static mixer links to each other with discharge nozzle with flowline respectively, and back static mixer is provided with export of finished oil.
2. fuel emulsification continuous type automatic production device according to claim 1, it is characterized in that: described heating kettle, agitated kettle, storage pot, oily vacuum tank, preceding tempering tank and back tempering tank are the double seal structure, and described heating kettle, agitated kettle, storage pot, oily vacuum tank, preceding tempering tank go out pipe with steam inlet tube and steam respectively with the back tempering tank and link to each other.
3. fuel emulsification continuous type automatic production device according to claim 1 is characterized in that: be respectively arranged with heating-up temperature table, storage temperature table, oil temperature table, preceding thermometer and back thermometer on described heating kettle, storage pot, oily vacuum tank, preceding tempering tank and the back tempering tank.
4. fuel emulsification continuous type automatic production device according to claim 1 is characterized in that: be respectively arranged with water filter and oil strainer on described discharge nozzle and the flowline.
5. fuel emulsification continuous type automatic production device according to claim 1 is characterized in that: be respectively arranged with water flow controller and oily flow controller on described discharge nozzle and the flowline.
6. fuel emulsification continuous type automatic production device according to claim 1 is characterized in that: described discharge nozzle is provided with centrifugal pump.
7. fuel emulsification continuous type automatic production device according to claim 1 is characterized in that: be provided with rear pump or output pump between described back tempering tank and the back static mixer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201194634U CN201454476U (en) | 2009-05-07 | 2009-05-07 | Automatic continuous-type production equipment for emulsifying fuel oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201194634U CN201454476U (en) | 2009-05-07 | 2009-05-07 | Automatic continuous-type production equipment for emulsifying fuel oil |
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| Publication Number | Publication Date |
|---|---|
| CN201454476U true CN201454476U (en) | 2010-05-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201194634U Expired - Lifetime CN201454476U (en) | 2009-05-07 | 2009-05-07 | Automatic continuous-type production equipment for emulsifying fuel oil |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101559339B (en) * | 2009-05-07 | 2011-11-23 | 杭州桐庐洪风新技术新燃料开发有限公司 | Fuel emulsification continuous type automatic production device and fuel emulsification method |
| CN103908918A (en) * | 2014-04-23 | 2014-07-09 | 四川金堂海纳生物医药技术研究所 | Production process of novel fuel and fabrication method of system device for producing novel fuel |
| CN105363379A (en) * | 2014-08-18 | 2016-03-02 | 广西科技大学 | Rapid, efficient and continuous mixer apparatus |
-
2009
- 2009-05-07 CN CN2009201194634U patent/CN201454476U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101559339B (en) * | 2009-05-07 | 2011-11-23 | 杭州桐庐洪风新技术新燃料开发有限公司 | Fuel emulsification continuous type automatic production device and fuel emulsification method |
| CN103908918A (en) * | 2014-04-23 | 2014-07-09 | 四川金堂海纳生物医药技术研究所 | Production process of novel fuel and fabrication method of system device for producing novel fuel |
| CN105363379A (en) * | 2014-08-18 | 2016-03-02 | 广西科技大学 | Rapid, efficient and continuous mixer apparatus |
| CN105363379B (en) * | 2014-08-18 | 2017-10-24 | 广西科技大学 | A kind of rapidly and efficiently continuous mixer apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20100512 Effective date of abandoning: 20090507 |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20100512 Effective date of abandoning: 20090507 |