CN205073984U - Make device that mixes diesel oil - Google Patents
Make device that mixes diesel oil Download PDFInfo
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- CN205073984U CN205073984U CN201520804231.8U CN201520804231U CN205073984U CN 205073984 U CN205073984 U CN 205073984U CN 201520804231 U CN201520804231 U CN 201520804231U CN 205073984 U CN205073984 U CN 205073984U
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Abstract
The utility model relates to a make device that mixes diesel oil. The utility model discloses a make device that mixes diesel oil can utilize chemical catalytic effect for oil and water surmount the integration that the ion attitude had do not been realized to the molecular level, have obtained a new molecular structure's mixed diesel oil, the complete transparent clarification of outward appearance, and the water oil separating phenomenon of emulsification situation thoroughly disappears, has the same viscosity and proportion with common fuel moreover.
Description
Technical field
The utility model relates to a kind of device manufacturing mixed diesel.
Background technology
Along with the develop rapidly of China's industrial or agricultural, transportation, growing to the demand of diesel oil, the diesel oil that present China consumes every year and the several hundred million ton of gasoline, imported crude oil and product oil have become the heavy burden of China's finance.In the world, the deposit of natural oil is limited, the energy crisis that facing mankind is day by day serious.Except energy problem, environmental problem is also the major issue of petroleum industry.Floating carbon, hydrocarbon, carbon monoxide, nitrogen oxide, sulfide and solia particle that oil inflame is improper given off have become the major air pollutants source of big and medium-sized cities, have a strong impact on ecological environment, human health and economic development.Therefore, for energy requirements and environmental requirement, development fuel oil is newly filled a prescription, it is imperative to develop oligosaprobic novel diesel fuel.
From 20 century 70s, oil crisis have stimulated the development of fuel water technology greatly.Various countries are also classified as fuel water technology as state key developmental research project in succession.Nearly two during the last ten years, and China's liquid fuel technology obtains very large development, wherein in the majority with the research of diesel oil emulsification.But common oil emulsion belongs to thermodynamic unstable system, with the change of environmental condition, standing time elongated the wild effects such as water-oil separating, distortion, breakdown of emulsion occurring, thus affect result of use; Emulsification simultaneously needs high-power emulsification holdout device, and preparation is complicated, consumes energy, and therefore along with the raising that development and the people of technology need the quality of diesel oil own, common diesel oil emulsification technology drawback starts gradually obviously, has had a strong impact on it and has promoted and use.
The eighties in 20th century starts the research entering microemulsion fuel, makes this field enter new developing period.Microemulsion is a kind of thermodynamic stable system, the spontaneous formation of energy, and particle diameter is little, and viscosity and non-water mixing fuel-viscosity variation are more or less the same, and can steady in a long-termly exist.But its basic mechanism, still be that utilizing emulsifying agent and assistant for emulsifying agent to enter in profit two-phase carries out sufficient hybrid reaction, under machinery or non-mechanical effect, make water be suspended among oil phase with the form of particulate, form the blended liquid phase of nanoscale (transparent) particle diameter.
Mechanism at present about (micro-) emulsification mainly contains:
Monomolecular adsorbed film is theoretical: namely emulsifying agent is only by forming the W/O emulsion of two-phase membrane parcel moisture.
Polymolecular adsorbed film is theoretical: in this theory, wrap film is that the strong penetrability compound jointly formed by emulsifying agent and decentralized photo is formed.Thickness, intensity is large, and difficult breakdown of emulsion, stops coalescent.
Diffuse double layer is theoretical: be applicable to ionic emulsifying agent, outer same sex electric charge can stop the close of drop.
No matter be which kind of is theoretical, they have a common place, are exactly the formation of emulsion and theoretical complexion.Profit is two immiscible two-phases, and can form particulate tiny one by one under stirring or other shock effect, due to the surface tension of two-phase, this is very unstable.And having of adding is hydrophilic and emulsifier package that the is double character of oleophylic is rolled on the interface of two-phase, reduces surface tension, improve the stability of discrete particles, thus reach the effect of emulsification.
In the actual use procedure of diesel oil emulsification, there will be the following problem that these cannot overcome principle:
First, due to the existence of emulsifying agent and assistant for emulsifying agent, the viscosity of emulsion fuel can be brought to raise, finally cause the rising of burning-point, therefore part use the burner of emulsion fuel need to carry out improveing even increase pre-heating system guarantee subsequent combustion process continue carry out; Meanwhile, the caloric value of emulsion fuel and crude fuel are compared and are generally had obvious reduction, in order to reach same result of use, can complete just may need to add more fuel, substantially can not effectively reduce fuel cost burden.
Finally, also have the problem of an essence, no matter be emulsification or Micro-emulsion, all there is a shelf life, after exceeding the time limit, water-oil separating is bound to occur.The longest emulsion fuel of present time can accomplish the stationary phase of about 9 months, and after exceeding stationary phase, profit starts to be separated, and cause adding water quality of fuel and calorific value decline.And be separated moisture will cause the blockings such as fuel channel because of freezing in cold season, or with tube metal material effects after there is corrosion.So emulsion fuel all must be deposited separately in the past, and can not use together with common fuel.
Therefore, a kind of new fuel process technology is still needed at present, to overcome Problems existing in existing emulsion fuel.
Utility model content
For the problems referred to above, the utility model provides a kind of device manufacturing mixed diesel.
The mixed diesel that the utility model manufactures is not identical with diesel oil emulsification in the past.Mixed diesel in the utility model is the effect utilizing chemical catalysis, You Heshui is surmounted fusion that molecule rank achieves ionic state, obtain the fuel of recruit's structure, the complete transparent clarification of outward appearance, the water-oil separating phenomenon of emulsification situation thoroughly disappears, and has the same proportion with common fuel.
According to an embodiment of the application, which provide a kind of manufacturing installation of mixed diesel, described device comprises:
Oil tank diameter 1, it is provided with the first oil-in 11, oil export 12, first agitator 13 and primary heater 14, wherein, described first oil-in 11 is for receiving raw material GB diesel oil, described oil export 12 is for discharging raw material GB diesel oil after treatment, described first agitator 13 is for stirring the raw material GB diesel oil in described oily tank diameter, and described primary heater 14 keeps steady temperature for making the raw material GB diesel oil in described oily tank diameter 1;
Water tank diameter 2, it is provided with the first water inlet 21, first water out 22, second agitator 23 and secondary heater 24, wherein, described first water inlet 21 is for receiving deionized water, described first water out 22 is for discharging deionized water after treatment, described second agitator 23 is for stirring the deionized water in described water tank diameter, and described secondary heater 24 keeps steady temperature for making the deionized water in described water tank diameter 2;
Venturi tube 3, it is provided with the second oil-in 31, second water inlet 32 and venturi outlet 33, wherein, described second oil-in 31 is for receiving the treated diesel oil from described oily tank diameter 1, described second water inlet 32 is for receiving the treated deionized water from described water tank diameter 2, and described venturi outlet 33 is for discharging the mixture a mixed through Venturi tube 3;
Reaction chamber 4, it is provided with reaction chamber entrance 41, reaction chamber outlet 42, and wherein, described reaction chamber entrance 41 is for receiving the mixture a from described Venturi tube 3, and described reaction chamber outlet 42 is for discharging the mixed liquor b reacted through reaction chamber 4;
Rectifier tank 5, it is provided with rectifier tank entrance 51, reflux inlet 52, rectifier tank outlet 53, bypass outlet 54 and reflux pump 55, wherein, described rectifier tank entrance 51 is for receiving the mixed liquor b from described reaction chamber 4, and described reflux inlet 52, bypass outlet 54 and reflux pump 55 make the part mixed-liquor return in rectifier tank 5; Described rectifier tank outlet 53 is for discharging the mixed liquor c through rectification;
Pressurized tank 6, it is provided with pressurized tank entrance 61, pressurized tank outlet 62 and force (forcing) pump 63, wherein, described pressurized tank entrance 61 is for receiving the mixed liquor c from described rectifier tank 5, described pressurized tank outlet 62 is for discharging the mixed liquor d through pressurized treatments, and described force (forcing) pump 63 is for maintaining the pressure of pressurized tank 6;
Stabilization tank 7, it is provided with stabilization tank entrance 71, mixed diesel outlet 72 and the second water out 73, wherein, described stabilization tank entrance 71 is for receiving the material from described pressurized tank 6, described mixed diesel outlet 72 is for discharging mixed diesel, and described second water out 73 is for discharging 2 water of separation;
Wherein, described second oil-in 31 of described Venturi tube 3 is connected with the described oil export 12 of described oily tank diameter 1, and described second water inlet 32 of described Venturi tube 3 is connected with described first water out 22 of described water tank diameter 2;
The described reaction chamber entrance 41 of described reaction chamber 4 is connected with the venturi outlet 33 of described Venturi tube 3;
The described rectifier tank entrance 51 of described rectifier tank 5 exports 42 with the described reaction chamber of described reaction chamber 4 and is connected; The described reflux inlet 52 of described rectifier tank 5 is connected with the described bypass outlet 54 of described rectifier tank 5;
The described pressurized tank entrance 61 of described pressurized tank 6 exports 52 with the described rectifier tank of described rectifier tank 5 and is connected;
The described stabilization tank entrance 71 of described stabilization tank 7 exports 62 with the described pressurized tank of described pressurized tank 6 and is connected,
Preferably, described second water out 73 of described stabilization tank 7 is connected to described first water inlet 21 of described water tank diameter 2.
Preferably, described device also comprises filter 8, and it is provided with filter inlet 81, filter outlet 82, and wherein, described filter inlet 81 is for receiving the mixed diesel from stabilization tank 7, and described filter outlet 82 is for discharging filtered mixed diesel;
Wherein, the described filter inlet 81 of described filter 8 exports 72 with the described mixed diesel of described stabilization tank 7 and is connected.
Preferably, described rectifier tank, pressurized tank, stabilization tank can have reflux well known in the art, also can comprise the conventional usual means well known in the art such as material import and export, pressure gauge, flowmeter, choke valve between each reactive tank (case), tank diameter, pipeline etc., not repeat them here.
The method using device of the present utility model to produce mixed diesel comprises:
1) by raw material GB diesel oil 0-50 DEG C temperature, under normal pressure with catalyst A process 0.5 to 3 hour, wherein the mass space velocity of GB diesel oil is 2.5-4h
-1;
2) by raw material deionized water 0-50 DEG C temperature, under normal pressure with catalyst A process 0.5 to 3 hour, wherein the mass space velocity of deionized water is 2.5-4h
-1;
3) according to GB diesel oil: the ratio of deionized water=1:0.5 to 1:2 is by step 1) and 2) respectively process after GB diesel oil and deionized water jointly introduce Venturi tube, obtain mixture a;
4) under the existence of catalyst A, make step 3) in described mixture a by the reaction chamber at the temperature of 0-50 DEG C and 2-7 atmospheric pressure, obtain mixed liquor b, wherein, the mass space velocity of mixture a is 2.5-4h
-1;
5) make step 4) in the described mixed liquor b that obtains by the rectifier tank that refluxes at ambient temperature and pressure, obtain mixed liquor c, the processing time in rectifier tank is 0.5-3 hour;
6) under the existence of catalyst B, make step 5) in pressurize in the mixed liquor c that the obtains pressurized tank under normal temperature and 10-50 atmospheric pressure 15-40 minute, obtain mixed liquor d, wherein the mass space velocity of mixture c is 2.5-4h
-1;
7) make step 6) in mixed liquor d stratification in stabilization tank of obtaining obtain water layer and mixed diesel layer, be separated and obtain 2 water and mixed diesel.
Wherein,
Step 1), 2) and 4) described in catalyst A be tourmaline, such as, purchased from Brazil or purchased from the tourmaline/tourmaline powder of Shijiazhuang Guan Yu mineral products processing factory,
Step 6) in described catalyst B comprise major catalyst and co-catalyst, described major catalyst is tourmaline, described co-catalyst comprises the oxide of palladium simple substance and copper/titanium/iron, wherein, the mass ratio of described major catalyst and co-catalyst is 5:1 to 15:1, preferred 8:1 to 12:1, more preferably 10:1, in described co-catalyst, calculate in mass ratio, titanium oxide: Cu oxide: ferriferous oxide: palladium simple substance=(5 ± 1): (5 ± 1): (1 ± 0.2): (1 ± 0.2), wherein, titanium in described each oxide, copper, the chemical valence of iron can be the conventional valence state that they can obtain, such as, titanium can be+2, + 3, + 4 valencys, copper can be+1, + divalent, iron can be+2, + 3 valencys, and can be the form of different valent mixture, as the form that iron can be tri-iron tetroxide.The oxide of preferred titanium, copper, iron is the form that its maximum closes valency, i.e. titanium dioxide, copper monoxide, di-iron trioxide, described catalyst B such as raises the tourmaline catalyst of mineral powder process plants for Lingshou County, Hebei province shakes.
Preferably, step 1) in mixing temperature be 10-40 DEG C, incorporation time is 1-2 hour; More preferably mixing temperature is 20-30 DEG C; Most preferably 25 DEG C;
Preferably, step 2) in mixing temperature be 10-40 DEG C, incorporation time is 1-2 hour; More preferably mixing temperature is 20-30 DEG C; Most preferably 25 DEG C;
Preferably, step 3) in GB diesel oil and the mixed proportion of deionized water be 1:0.8 to 1:1.2; More preferably 1:0.9 to 1:1.1; Most preferably 1:1;
Preferably, step 4) in reaction temperature be 10-40 DEG C; More preferably reaction temperature is 20-30 DEG C; Most preferably 25 DEG C;
Preferably, step 5) in the processing time in rectifier tank be 0.5-2 hour;
Preferably, step 6) in the pressure of pressurized tank be 20-40 atmospheric pressure;
Preferably, step 7) in be separated 2 water obtained and can be back to step 2) in use as raw water,
Preferably, described method also comprises step 8): make step 7) in the mixed diesel that obtains filter, obtain filtered mixed diesel.
The mixed diesel adopting device of the present utility model to produce possesses following features:
1, easy-to-use: the manufacturing process of product oil is simple, and equipment dependability is high, and be applicable to mass automatic production, obtained mixed diesel can be used in combination arbitrarily with the diesel oil of routine.
2, energy-conservation: can effective fuel-efficient use amount;
3, environmental protection: due to the change to crude oil molecular structure, novel diesel effectively can improve the discharge, particularly sulfur content of relevant devices.
4, stable: product performance is stablized, Cetane number, flash-point, freezing point, viscosity, boiling range, the ash indices that grades is excellent, and acidity, corrosivity are lower.
Applied widely: to be applicable to farm machinery, generator and other plant equipment such as various engineering trucks, heavy truck, boats and ships, tractor that diesel oil is fuel, and without the need to any special transformation.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the device according to a manufacture mixed diesel preferred embodiment of the present utility model.
Detailed description of the invention
Embodiment 1 prepares the device of mixed diesel
As shown in Figure 1, comprise according to the manufacturing installation of mixed diesel of the present utility model:
Oil tank diameter 1, it is provided with the first oil-in 11, oil export 12, first agitator 13 and primary heater 14, wherein, described first oil-in 11 is for receiving raw material GB diesel oil, described oil export 12 is for discharging raw material GB diesel oil after treatment, described first agitator 13 is for stirring the raw material GB diesel oil in described oily tank diameter 1, and described primary heater 14 keeps steady temperature for making the raw material GB diesel oil in described oily tank diameter 1;
Water tank diameter 2, it is provided with the first water inlet 21, first water out 22, second agitator 23 and secondary heater 24, wherein, described first water inlet 21 is for receiving deionized water, described first water out 22 is for discharging deionized water after treatment, described second agitator 23 is for stirring the deionized water in described water tank diameter 2, and described secondary heater 24 keeps steady temperature for making the deionized water in described water tank diameter 2;
Venturi tube 3, it is provided with the second oil-in 31, second water inlet 32 and venturi outlet 33, wherein, described second oil-in 31 is for receiving the treated diesel oil from described oily tank diameter 1, described second water inlet 32 is for receiving the treated deionized water from described water tank diameter 2, and described venturi outlet 33 is for discharging the mixture a mixed through Venturi tube 3;
Reaction chamber 4, it is provided with reaction chamber entrance 41, reaction chamber outlet 42, and wherein, described reaction chamber entrance 41 is for receiving the mixture a from described Venturi tube 3, and described reaction chamber outlet 42 is for discharging the mixed liquor b reacted through reaction chamber 4;
Rectifier tank 5, it is provided with rectifier tank entrance 51, reflux inlet 52, rectifier tank outlet 53, bypass outlet 54 and reflux pump 55, wherein, described rectifier tank entrance 51 is for receiving the mixed liquor b from described reaction chamber 4, and described reflux inlet 52, bypass outlet 54 and reflux pump 55 make the part mixed-liquor return in rectifier tank 5; Described rectifier tank outlet 53 is for discharging the mixed liquor c through rectification;
Pressurized tank 6, it is provided with pressurized tank entrance 61, pressurized tank outlet 62 and force (forcing) pump 63, wherein, described pressurized tank entrance 61 is for receiving the mixed liquor c from described rectifier tank 5, described pressurized tank outlet 62 is for discharging the mixed liquor d through pressurized treatments, and described force (forcing) pump 63 is for maintaining the pressure of pressurized tank 6;
Stabilization tank 7, it is provided with stabilization tank entrance 71, mixed diesel outlet 72 and the second water out 73, wherein, described stabilization tank entrance 71 is for receiving the material from described pressurized tank 6, described mixed diesel outlet 72 is for discharging mixed diesel, and described second water out 73 is for discharging 2 water of separation;
Filter 8, it is provided with filter inlet 81, filter outlet 82, and wherein, described filter inlet 81 is for receiving the mixed diesel from stabilization tank 7, and described filter outlet 82 is for discharging filtered mixed diesel;
Wherein, described second oil-in 31 of described Venturi tube 3 is connected with the described oil export 12 of described oily tank diameter 1, and described second water inlet 32 of described Venturi tube 3 is connected with described first water out 22 of described water tank diameter 2;
The described reaction chamber entrance 41 of described reaction chamber 4 is connected with the venturi outlet 33 of described Venturi tube 3;
The described rectifier tank entrance 51 of described rectifier tank 5 exports 42 with the described reaction chamber of described reaction chamber 4 and is connected; The described reflux inlet 52 of described rectifier tank 5 is connected with the described bypass outlet 54 of described rectifier tank 5;
The described pressurized tank entrance 61 of described pressurized tank 6 exports 52 with the described rectifier tank of described rectifier tank 5 and is connected;
The described stabilization tank entrance 71 of described stabilization tank 7 exports 62 with the described pressurized tank of described pressurized tank 6 and is connected,
Described second water out 73 of described stabilization tank 7 is connected to described first water inlet 21 of described water tank diameter 2,
The described filter inlet 81 of described filter 8 exports 72 with the described mixed diesel of described stabilization tank 7 and is connected.
The operating procedure of this device is as follows:
1) by 500L (418KG) raw material GB diesel oil under normal temperature, normal pressure with catalyst A process 2 hours, wherein the mass space velocity of GB diesel oil is 3h
-1;
2) by 500L (500KG) raw material deionized water under normal temperature, normal pressure with catalyst A process 2 hours, wherein the mass space velocity of deionized water is 3h
-1;
3) according to GB diesel oil: the ratio of deionized water=1:1 is by step 1) and 2) the treated GB diesel oil that obtains and deionized water introduce Venturi tube jointly, obtains mixture a;
4) under the existence of catalyst A, make step 3) in described mixture a by reaction chamber under room temperature and 5 atmospheric pressure, obtain mixed liquor b, wherein, the mass space velocity of mixture a is 3h
-1;
5) make step 4) in the described mixed liquor b that obtains by the rectifier tank that refluxes at ambient temperature and pressure, obtain mixed liquor c, the processing time in rectifier tank is 1 hour;
6) under the existence of catalyst B, make step 5) in pressurization 25 minutes in the mixed liquor c that the obtains pressurized tank under normal temperature and 20 atmospheric pressure, obtain mixed liquor d, wherein the mass space velocity of mixture c is 3.5h
-1;
Wherein,
Step 1), 2) and 4) described in catalyst A be tourmaline powder purchased from Shijiazhuang Guan Yu mineral products processing factory,
Step 6) in described catalyst B be tourmaline catalyst purchased from Lingshou County, Hebei province Zhen Yang mineral powder processing factory;
7) make step 6) in mixed liquor d stratification in stabilization tank of obtaining obtain water layer and mixed diesel layer, be separated and obtain 2 water and mixed diesel;
In addition, step 7) in be separated 2 water obtained and be connected to water tank diameter, be back to step 2) in use as raw water;
8) make step 7) in the mixed diesel that obtains filter, obtain filtered mixed diesel.
Adopt the result manufacturing mixed diesel according to device of the present utility model:
The device manufacture of the application is adopted to obtain finished product mixed diesel 518KG with 500L (418KG) raw material GB diesel oil and 500L (500KG) raw material deionized water.
That is, by after special fabrication processes, the amount of gain (water fusion oil) of the mixed diesel obtained is: about 100KG.
The nature examination of embodiment 2 mixed diesel
Detection of Stability
Mixed diesel embodiment 1 prepared leaves standstill 180 days at normal temperatures, and result does not occur the situations such as layering, and this illustrates that described mixed diesel is not diesel oil emulsification.
Performance Detection used in combination
The mixed diesel prepare embodiment 1 and common state No. 4 diesel oil are mixed in the engine of Great Wall Harvard SUV, normally travelled through 180 days, engine output Non Apparent Abnormality, discharge are better than common state 4 diesel oil, this illustrates, described mixed diesel completely can be used in combination arbitrarily with ordinary diesel oil.
Other Performance Detection
By the mixed diesel censorship of preparation in embodiment 1, detect according to the regulation of GB19147-2013.Result is as follows:
Survey report
As can be seen from above-mentioned survey report, environment-friendly type mixed diesel synthetic technology of the present invention, with under the specific natural crystal catalyst action that is main component, pass through high speed shear, the physical methods such as pressurization, fuel molecule and hydrone are re-combined into, make environment-friendly type mixed diesel, environment-friendly type mixed diesel is not containing any chemical addition agent, product performance is stablized, its technical indicator water fusion rate Absorbable organic halogens is at 15%-20%, the national test index of this type diesel oil is all up to standard, wherein Cetane number, flash-point, the application such as freezing point index is all better than its raw material diesel oil standard used, the harmful substances such as sulfur content and every discharge index are then lower than raw material diesel oil standard.When without the need to carrying out any transformation to use equipment, not only not affecting result of use, greatly can also reduce discharge, is a subversive new energy technology.
Claims (3)
1. manufacture a device for mixed diesel, described device comprises:
Oil tank diameter (1), it is provided with the first oil-in (11), oil export (12), the first agitator (13), primary heater (14), wherein, described first oil-in (11) is for receiving raw material GB diesel oil, described oil export (12) is for discharging raw material GB diesel oil after treatment, described first agitator (13) is for stirring the raw material GB diesel oil in described oily tank diameter (1), and described primary heater (14) keeps steady temperature for making the raw material GB diesel oil in described oily tank diameter (1);
Water tank diameter (2), it is provided with the first water inlet (21), the first water out (22), the second agitator (23), secondary heater (24), wherein, described first water inlet (21) is for receiving deionized water, described first water out (22) is for discharging deionized water after treatment, described second agitator (23) is for stirring the deionized water in described water tank diameter (2), and described secondary heater (24) keeps steady temperature for making the deionized water in described water tank diameter (2);
Venturi tube (3), it is provided with the second oil-in (31), the second water inlet (32) and venturi outlet (33), wherein, described second oil-in (31) is for receiving the treated diesel oil from described oily tank diameter (1), described second water inlet (32) is for receiving the treated deionized water from described water tank diameter (2), and described venturi outlet (33) is for discharging the mixture a mixed through Venturi tube (3);
Reaction chamber (4), it is provided with reaction chamber entrance (41), reaction chamber outlet (42), wherein, described reaction chamber entrance (41) is for receiving the mixture a from described Venturi tube (3), and described reaction chamber outlet (42) is for discharging the mixed liquor b reacted through reaction chamber (4);
Rectifier tank (5), it is provided with rectifier tank entrance (51), reflux inlet (52), rectifier tank outlet (53), bypass outlet (54), reflux pump (55), wherein, described rectifier tank entrance (51) is for receiving the mixed liquor b from described reaction chamber (4), and described reflux inlet (52), bypass outlet (54) and reflux pump (55) make the part mixed-liquor return in rectifier tank (5); Described rectifier tank outlet (53) is for discharging the mixed liquor c through rectification;
Pressurized tank (6), it is provided with pressurized tank entrance (61), pressurized tank outlet (62), force (forcing) pump (63), wherein, described pressurized tank entrance (61) is for receiving the mixed liquor c from described rectifier tank (5), described pressurized tank outlet (62) is for discharging the mixed liquor d through pressurized treatments, and described force (forcing) pump (63) is for maintaining the pressure of pressurized tank (6);
Stabilization tank (7), it is provided with stabilization tank entrance (71), mixed diesel outlet (72), the second water out (73), wherein, described stabilization tank entrance (71) is for receiving the material from described pressurized tank (6), described mixed diesel outlet (72) is for discharging mixed diesel, and described second water out (73) is for discharging 2 water of separation;
Wherein, described second oil-in (31) of described Venturi tube (3) is connected with the described oil export (12) of described oily tank diameter (1), and described second water inlet (32) of described Venturi tube (3) is connected with described first water out (22) of described water tank diameter (2);
The described reaction chamber entrance (41) of described reaction chamber (4) is connected with the venturi outlet (33) of described Venturi tube (3);
The described rectifier tank entrance (51) of described rectifier tank (5) exports (42) with the described reaction chamber of described reaction chamber (4) and is connected; The described reflux inlet (52) of described rectifier tank (5) is connected with the described bypass outlet (54) of described rectifier tank (5);
The described pressurized tank entrance (61) of described pressurized tank (6) exports (53) with the described rectifier tank of described rectifier tank (5) and is connected,
The described stabilization tank entrance (71) of described stabilization tank (7) exports (62) with the described pressurized tank of described pressurized tank (6) and is connected.
2. the device of manufacture mixed diesel according to claim 1, wherein,
Described second water out (73) of described stabilization tank (7) is connected to described first water inlet (21) of described water tank diameter (2).
3. the device of manufacture mixed diesel according to claim 1, wherein, described device also comprises:
Filter (8), it is provided with filter inlet (81), filter outlet (82), wherein, described filter inlet (81) is for receiving the mixed diesel from stabilization tank (7), and described filter outlet (82) is for discharging filtered mixed diesel;
The described filter inlet (81) of described filter (8) exports (72) with the described mixed diesel of described stabilization tank (7) and is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520804231.8U CN205073984U (en) | 2015-10-16 | 2015-10-16 | Make device that mixes diesel oil |
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|---|---|---|---|
| CN201520804231.8U CN205073984U (en) | 2015-10-16 | 2015-10-16 | Make device that mixes diesel oil |
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| CN205073984U true CN205073984U (en) | 2016-03-09 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582458A (en) * | 2015-10-16 | 2017-04-26 | 世能华奇（北京）科技发展有限公司 | Manufacturing method of mixed diesel, mixed diesel manufactured through method and manufacturing device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582458A (en) * | 2015-10-16 | 2017-04-26 | 世能华奇（北京）科技发展有限公司 | Manufacturing method of mixed diesel, mixed diesel manufactured through method and manufacturing device |
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