CN101660764B - Combined combustion method for fuel oil emulsification and combustion supporting - Google Patents
Combined combustion method for fuel oil emulsification and combustion supporting Download PDFInfo
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- CN101660764B CN101660764B CN200910168027A CN200910168027A CN101660764B CN 101660764 B CN101660764 B CN 101660764B CN 200910168027 A CN200910168027 A CN 200910168027A CN 200910168027 A CN200910168027 A CN 200910168027A CN 101660764 B CN101660764 B CN 101660764B
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Abstract
The invention discloses a combined combustion method for fuel oil emulsification and combustion supporting. The combined combustion method comprises step A including oil-water mixing, magnetization and emulsification, step B including activated water mixture preparation, and step C including fuel oil catalytic cracking. The combined combustion method for fuel oil emulsification and combustion supporting has high efficiency and low energy consumption.
Description
Technical field
The present invention relates to a kind of fuel emulsification and fuel oil catalytic cracking field, relate in particular to a kind of fuel emulsification and catalytic cracking compound combustion field.
Background technology
Fuel oil is widely used as a kind of energy, and in the oil inflame of kiln, stove, mixes water again with oil water mixture, after magnetization and emulsification, burns again, can practice thrift fuel oil, and reduces the discharge of flue gas pollutant; Simultaneously, when burning, add catalyst and perhaps fuel oil is burnt through catalytic cracking earlier again, can practice thrift fuel oil equally, more can reduce the discharge of flue gas pollutant so that oil inflame is more abundant.Realize that above-mentioned two kinds of targets have multiple means; Like one Chinese patent application number magnetization emulsifier unit for mentioning among the 03202827.X; One Chinese patent application number is the ultrasonic magnetic resonance fuel filter of electric heating mentioned in 95218520.2; Perhaps one Chinese patent application number be a kind of many magnetic mentioned in 00103909.1 to ultrasonic emulsification fuel-saving dirt-reducing device, all on fuel emulsification and magnetized device, new improvement is arranged, make under the effect of magnetization and emulsification; Profit mixes can be more trickle, and highly energy-consuming, efficient are low, the inadequately little shortcoming and defect in Water-In-Oil liquid bead footpath of decentralized photo but also have simultaneously.Simultaneously, be disclosed catalyst among CN1421745A, CN1101661A, CN1465676A, CN1303907A, the CN1860210A like the Chinese patent publication number, all be to use potassium permanganate (KMnO
4), potassium chlorate (KClO
3) strong oxidizer of this type, in combustion process, decomposite oxygen and come auxiliary combustion, come therefrom, the whole decomposition and consumptions of catalyst have increased production cost, and the efficient of this type of burning-aid method neither be very high.
Summary of the invention
The objective of the invention is to overcome the deficiency of prior art, a kind of fuel emulsification and combustion-supporting combined combustion method and system thereof that high efficiency, low energy consumption are arranged is provided.
For realizing above-mentioned purpose, the present invention has used following technical proposals:
This fuel emulsification and combustion-supporting combined combustion method comprise the steps:
A, profit mix magnetization emulsification
1.1, will distinguish fuel oil and water behind the filtration, purification, press W
Oil: account for 75-90%, W
WaterAccount for the profit percentage by weight of 10-25%, heat temperature raising after the mixing, gets into magnetizing assembly with the speed less than 10cm/s to 75-85 ℃ simultaneously, implements magnetization for the first time;
1.2, will carry out emulsification first time through the one-level emulsifier unit through magnetized oil water mixture once, the Water-In-Oil liquid bead that makes decentralized photo directly 90% reaches micron order;
1.3, will be through the oil water mixture after the emulsification, get into magnetizing assembly with the speed of 15-20cm/s, implement magnetization for the second time;
1.4, will be through the magnetized oil water mixture of secondary, get into the secondary emulsifier unit and carry out emulsification second time, the Water-In-Oil liquid bead that makes decentralized photo directly 90% reaches nanoscale.Promptly obtain a component of the emulsified fuel of secondary magnetization second emulsifying;
The manufacturing of B, activated water
With the water behind the filtration, purification, adjustment P
H=8-9, and the activated water generating means of flowing through make water electrolysis produce the b component of the activated water mixture that contains hydrogen and oxygen;
C, catalytic cracking
With 0.2-0.8m/min speed, the catalytic cracking unit of flowing through makes the catalytic cracking of 3--10% fuel oil become the littler combustible hydrocarbon of molecular weight with fuel oil; At this moment, the flow through fuel oil of catalytic cracking unit and the volume ratio V of catalyst
Oil: V
Urge=0.5-1: 1-2, the catalytic cracking unit temperature is 250-300 ℃, promptly obtains the c component of fuel oil and the fuel oil mixture of the combustible hydrocarbon littler than former fuel molecule amount;
D, compound combustion
To pass through after steps A, B, the C, a component of resulting emulsified fuel, the b component of activated water mixture, and the c component of fuel oil mixture are used measuring pump respectively, and adjustment a, b, c three component part by weight are 90: 1.5-2.5: 10, and at 6-8kg/cm
2The pressure effect under continuous pump to nozzle, spray into the combustion chamber, mixed combustion in the combustion chamber sprays among a, b, c three mixture of combustion chamber, total shared percentage by weight of moisture content is 15-25%.
Described magnetizing assembly is the force-magnetized device of labyrinth type; It comprises import and the outlet that is arranged at magnetic chamber body both sides; In magnetic chamber body, be provided with several ends that stagger each other and be fixed in the tabular magnet on the cavity, the magnetic flux density of said magnet is 8000-10000Gs.
Described one-level emulsifier unit is the high-shear emulsifying pump; Described secondary emulsifier unit is the immersion phaco device; It comprises the emulsification chamber, is arranged at the import and the outlet of emulsification chamber both sides, is provided with piezoelectric chip in the emulsification chamber roof; This piezoelectric chip contacts with a bracing frame top and by this bracing frame it is supported in outside the emulsification chamber; The other end of this bracing frame is connected with a horn, and this horn stretches into the emulsification chamber interior, and this horn other end is connected with an oscillator; The bottom of oscillator is immersed in the profit liquid level that needs emulsification, and sound field intensity is 10-20w/cm
2, described piezoelectric chip power is 2KW, the vibration frequency of described oscillator is 20Khz; The flowing velocity of emulsifying mixt in the emulsification chamber is less than 10cm/s.
Described activated water generating means, this activated water generating means is made up of several tubulose activated water generators; The bottom of each activated water generator and top communicate with rectifier power source respectively, and the cathode column of mutually insulated and anode posts; In the body of generator, also be provided with respectively the cathode screen and the anode network that are connected with anode posts with cathode column, the water that needs to handle flows in the pipe from bottom inlet, and the activated water mixture after electrolysis flows out body from top exit.
Described activated water generating means, rectifier power source voltage 6V-12V, current density 1-3A/dm
2, general power 6KW, purify waste water with 0.1-0.5m/min speed, the activated water generating means of flowing through, it is 0.1-1m that electrolysis obtains containing the hydrogen and oxygen total amount
3/ min, water P
HThe activated water mixture of=8-9.Described cathode screen and anode network are cylindrical, ratio of cathodic to anodic area S
Cloudy: S
Sun=1: 0.8, negative electrode, anodized insulation are installed with one heart.
Water behind the described filtration, purification gets into before the activated water generating means, through the alkali liquid tank of the aqueous alkali of the NaOH that stores weight percent concentration 0.2% or KOH or two kinds of any proportionings, through P
HAdjuster, adjustment water P
HBe worth to 8-9.
Described catalytic cracking unit comprises pipe in the catalytic cracking that is provided with import and outlet, in this, outside the pipe, is provided with heating jacket; In interior pipe, be filled with simultaneously the catalytic cracking agent, described catalytic cracking agent is any among MLC500 and the MLC-500ZA, perhaps any proportioning of two kinds.
In the import of pipe and the outlet, be provided with stainless (steel) wire in the said catalytic cracking.
Described fuel oil comprises heavy oil and diesel oil.
Through technique scheme, it is following that this invention possesses beneficial effect:
1. piezoelectric type wafer emulsifier unit, the energy of its oscillator is not an indirect transfer, but directly is passed to the fuel emulsification liquid level, energy consumption is little, the oil-water emulsion better effects if;
2. the labyrinth type magnetizing assembly has magnetic field by force and uniformly, in effective magnetization cavity, extended time of contact oily and water, thereby profit fully magnetizes simultaneously;
3. repeated twice magnetization and twice emulsification, can let the oil-water mixture pearl reach nano level particle diameter;
4. use activated water mixture that electrolysis obtains as combustion adjuvant, electrolytic method is simple, and electrolysis gained activated water mixture is a kind of clean energy resource, also is a kind of high energy efficiency combustion adjuvant that can be recycled;
5. the technological process automaticity of emulsification, magnetization, combustion adjuvant is high, and the combustion system of compound setting is more arranged, and guarantees that in many ways oil inflame is complete, and the actual measurement fuel-saving efficiency is high, is applicable to little kiln, also is applicable to big kiln.
Description of drawings
Fig. 1 is a kind of fuel emulsification of invention and combustion-supporting combined combustion method system flow chart.
Fig. 2 is the sketch map of emulsifier unit of the present invention.
Fig. 3 is the sketch map of magnetizing assembly of the present invention.
Fig. 4 is an activated water generating means sketch map of the present invention.
Fig. 5 is an activated water generating means assembly drawing of the present invention.
Fig. 6 is the assembly drawing of another angle of activated water generating means of the present invention.
Fig. 7 is a catalytic cracking unit sketch map of the present invention.
The specific embodiment
Below in conjunction with accompanying drawing further explanation is made in invention.
As shown in Figure 1, this fuel emulsification and combustion-supporting combined combustion method comprise the steps:
The A step of profit mixing, magnetization, emulsification, the B step that the activated water mixture is made, the C step of fuel oil catalytic cracking.
The A step specifically is, with fuel oil and water, respectively after magnetic valve 11 and 21; Again respectively behind water filtration clarifier 12 and oil strainer 22 purification filterings, respectively through water meter 13 and oil meter 23, again through water meter 14 and oil measurement device 24; Ratio by weight being the oil of 10% water and 90% gets into electric heater 31; This moment, the Main Ingredients and Appearance of fuel oil was a heavy oil, and mode of heating is the water-bath type electric heater, and Jiang Shui and oil is heat temperature raising to 80 ℃ simultaneously; Oil water mixture after the intensification after 32 first mixing, with the speed entering labyrinth type magnetizing assembly 33 of 9cm/s, is implemented magnetization for the first time through static mixer; To pass through for the first time then, magnetization water oil mixture afterwards carries out the emulsification first time through one-level emulsifier unit emulsification pump 34; This kind emulsification pump makes the Water-In-Oil liquid bead footpath 90% of decentralized photo reach micron order for can realize the multistage high-precision high-shear emulsifying pump that reaches; The water oil mixture that then will magnetize for the first time again after the emulsification gets into labyrinth type magnetizing assembly 37 with the speed regulation secondary of 16cm/s, implements magnetization for the second time; Then for the second time get into secondary emulsifier unit immersion piezo-electric crystal ultrasonic emulsification device 36 and carry out the emulsification second time; Make the Water-In-Oil liquid bead footpath 90% of decentralized photo reach nanoscale; Speed entering labyrinth type magnetizing assembly 37 with 9cm/s magnetizes for the third time again, and after pump into combustion chamber burner 7 through original oil transfer pump 40 again after the control of magnetic valve 38.
Specifically, as shown in Figure 2, described secondary emulsifier unit 36 is the immersion phaco device; It includes emulsification chamber 361; Be arranged at the import 362 and outlet 363 of emulsification chamber both sides, be provided with piezoelectric chip 364 in chamber roof, this piezoelectric chip contacts with a bracing frame 365 tops and by this support it is supported in outside the chamber; Be connected with a horn 366 with the other end of this bracing frame; This horn stretches into chamber interior, and this horn other end is connected with an oscillator 367, and the bottom of oscillator is immersed in the water oil level 368 that needs emulsification; This moment, sound field intensity was 10-20w/cm
2, the flowing velocity of emulsifying mixt in the emulsification chamber is less than 10m/s; Described piezo-electric crystal power is 2KW, and the vibration frequency of described oscillator is 20Khz.
As shown in Figure 3; Described magnetizing assembly 37 is the force-magnetized device of labyrinth type; It comprises the import 372 and outlet 373 that is arranged at magnetic chamber body 371 both sides; In magnetic chamber body, be provided with somely to tabular permanent magnet 374, the stiff end that described adjacent two blocks of permanent magnets are fixed on the cavity is oppositely arranged, and the other end of magnet is a free end.Described magnet is RbFeB magnet, and the magnetic flux density of magnet is 9000Gs.
The B step that also has the activated water mixture to make of carrying out simultaneously; Specifically comprise: will be sent to activated water generating means 52 with measuring pump 51 by the water behind filtration purifier 12 filtration, purifications; Before getting into the activated water generating means; Through storing weight percent concentration is 0.2% KOH or the alkali liquid tank 50 of NaOH, with the P of filtering and purifying water
HValue is adjusted to 8.5; Get into after the activated water generating means, under the situation that rectifier power source 53 is connected, implement electrolytic treatments, purify waste water with the activated water generating device of 0.25m/min velocity flow, electrolysis obtains containing 0.73m
3The hydrogen and oxygen mist of/min, water P
H=8.5 activated water mixture; Described rectifier power source general power 6KW, voltage 10V, current density 2A/dm
2
Like Fig. 4, Fig. 5, the described activated water generating means 52 of Fig. 6, form by 4 series-parallel tubulose activated water generators 521; The bottom of each activated water generator has respectively with rectifier power source with the top and communicates, and the cathode column 522 and anode posts 523 of mutually insulated; Described cathode screen and anode network are cylindrical, and the anode and cathode insulation is installed with one heart; In the body of activated water generator; Also be provided with respectively the cathode screen 524 and the anode network 525 that are connected with anode posts with cathode column; The water that needs to handle flows in the pipe from bottom inlet 526, and the activated water mixture that after electrolysis, produces flows out body from top exit 527.
Carry out simultaneously with above-mentioned A step, B step; Also have the C step of fuel oil catalytic cracking, concrete grammar is: fuel oil is sent into catalytic cracking unit 63 through magnetic valve 61, measuring pump 62, and fuel oil is under 250 ℃ of temperature; With millisecond speed; Under catalytic cracking agent effect, 6% fuel oil can be cracked into the littler combustible hydrocarbon of molecule amount, gets into combustion chamber burner 7 through magnetic valve 64 again.This moment, the volume ratio of fuel oil and catalyst was 1: 1 in catalytic cracking unit, and the catalytic cracking unit temperature is 250-300 ℃; Specifically, described catalytic cracking unit 63 includes pipe 631 in the catalytic cracking, is filled with catalytic cracking agent 632 in the interior pipe, and pipe is outside equipped with heating outer tube 633 in this, is filled with superheated vapor in the heating outer tube; In the import of pipe and the outlet, be provided with stainless (steel) wire 634 in the said catalytic cracking, described catalytic cracking agent is that MLC500 and the MLC-500ZA that China Petrochemical Industry Company produces respectively accounts for 50%.
Described fuel oil catalytic cracking chemical formula is:
A, B, C step through above-mentioned three systems are carried out simultaneously, and using measuring pump adjustment a, b, the corresponding part by weight of c respectively is 90: 2: 10, with the oil water mixture a after the emulsifying magnetizing; Through original oil transfer pump 40; Pump into the burner noz(zle) 7 of combustion chamber, with activated water mixture b, pump into combustion chamber 8 simultaneously with measuring pump 54; Atomize at the burner noz(zle) place; Simultaneously, will pass through being become little molecule combustible hydrocarbon, and do not pumped into combustion chamber 7 by the fuel oil mixture of catalytic cracking by catalytic cracking of obtaining after the catalytic cracking, above-mentioned three is at 7kg/cm
2The pressure effect under, continuously pump to nozzle converges compound combustion in the combustion chamber.When spraying into the combustion chamber, total water content that a, b, c product mix is controlled at percentage by weight 20%, and this embodiment is 60m through total capacity
3Ceramic heavy oil tunnel kiln use, and test each technological parameter of these 1200 ℃ of high-temperature regions of furnace, satisfactory for result, actual fuel-economizing can reach 19%.
This scheme compared with prior art owing to adopted piezoelectric type wafer emulsifier unit, thereby can let water oil emulsifying effectiveness better, and the energy of oscillator is not indirect transmission, directly is sent to liquid level, and energy consumption is little; The labyrinth type magnetizing assembly has magnetic field by force and uniformly simultaneously, the time of contact of the water oil that in the useful space, extended simultaneously, can be fully magnetized; And having repeated twice magnetization and twice emulsification can let the water-oil mixture pearl reach nano level particle diameter; Use the activated water that obtains after the brine electrolysis as combustion adjuvant, electrolytic method is simple, and electrolysis gained activated water mixture is a kind of clean energy resource, also is a kind of high energy efficiency combustion adjuvant that can be recycled.
The specific embodiment two
Be that with the specific embodiment one difference in the described profit magnetization emulsification A step, carried out twice magnetization and twice emulsification, the oil water mixture a after twice magnetization and the emulsification directly pumps into the combustion chamber; In addition, when profit mixes, be that 25% water and 75% oil heat simultaneously with weight ratio, heating-up temperature to 85 ℃; This moment, the Main Ingredients and Appearance of fuel oil was a diesel oil; And make in the B step at activated water, be that 12V, current density are 1.6A/dm in rated voltage
2, power is under the electrolysis of power supply of 6KW, obtains containing 1m
3The activated water mixture b of/min hydrogen and oxygen gas mixture and water PH=8; In catalytic cracking step C, the volume ratio of fuel oil and catalyst is 0.5: 2, and the catalytic cracking unit temperature is 250-300 ℃; Described catalytic cracking agent is MLC500 or the MLC-500ZA that China Petrochemical Industry Company produces, and obtains the c component of fuel oil and the mixture of the combustible hydrocarbon littler than former fuel molecule amount; Use measuring pump respectively, adjustment a, b, c three component part by weight are 90: 2.5: 10, at 6.5kg/c m
2The pressure effect under continuous pump when nozzle sprays into the combustion chamber, total water content that a, b, c product mix is controlled at percentage by weight 25%.This embodiment is 10m through total capacity
3Diesel oil stove use, and test each technological parameter of 330 ℃ of warm areas of this PVC rag baby accessory baking furnace, satisfactory for result, actual fuel-economizing can reach 24%.
According to different needs and different types of kiln, and the diesel oil of the heavy oil of different qualities and different qualities adjusts, and the specific embodiments of multiple different technical parameters can also be arranged, and these all belong to protection scope of the present invention.
Claims (7)
1. a fuel emulsification and combustion-supporting combined combustion method comprise the steps:
A, profit mix magnetization emulsification
1.1, will distinguish fuel oil and water behind the filtration, purification, press W
Oil: account for 90-75%, W
WaterAccount for the profit percentage by weight of 10-25%, heat temperature raising after the mixing, gets into magnetizing assembly with the speed less than 10cm/s to 75-85 ℃ simultaneously, implements magnetization for the first time;
1.2, will carry out emulsification first time through the one-level emulsifier unit through magnetized oil water mixture once, the Water-In-Oil liquid bead that makes decentralized photo directly 90% reaches micron order;
1.3, will be through the oil water mixture after the emulsification, get into magnetizing assembly with the speed of 15-20cm/s, implement magnetization for the second time;
1.4, will be through the magnetized oil water mixture of secondary, get into the secondary emulsifier unit and carry out emulsification second time, make the Water-In-Oil liquid bead footpath 90% of decentralized photo reach nanoscale, promptly obtain a component that secondary magnetizes the emulsified fuel of second emulsifying;
The manufacturing of B, activated water
With the water behind the filtration, purification, adjustment P
H=8-9, and the activated water generating means of flowing through make water electrolysis produce the b component of the activated water mixture that contains hydrogen, oxygen;
C, catalytic cracking
With 0.2-0.8m/min speed, the catalytic cracking unit of flowing through makes the catalytic cracking of 3-10% fuel oil become the littler combustible hydrocarbon of molecular weight with fuel oil; At this moment, the fuel oil of the catalytic cracking unit of flowing through and the volume ratio of catalyst are 0.5-1: 1-2, and the catalytic cracking unit temperature is 250-3000 ℃, promptly obtain the c component of fuel oil and the mixture of the combustible hydrocarbon littler than former fuel molecule amount;
D, compound combustion
To pass through after steps A, B, the C; The c component of a component of the emulsified fuel of resulting secondary magnetization second emulsifying, the b component of activated water mixture and fuel oil and the mixture of the combustible hydrocarbon littler than former fuel molecule amount; Use measuring pump respectively; Adjustment a, b, c three component part by weight are 90: 1.5-2.5: 10, and at 6-8kg/cm
2The pressure effect under continuous pump to nozzle, spray into the combustion chamber, mixed combustion in the combustion chamber sprays among a, b, c three mixture of combustion chamber, total shared percentage by weight of moisture content is 15-25%.
2. fuel emulsification as claimed in claim 1 and combustion-supporting combined combustion method; It is characterized in that: described magnetizing assembly is the force-magnetized device of labyrinth type; It comprises import and the outlet that is arranged at magnetic chamber body both sides; In magnetic chamber body, be provided with several ends that stagger each other and be fixed in the tabular magnet on the cavity, oil water mixture is 8000-10000Gs through the magnetic flux density of magnetizing assembly.
3. fuel emulsification as claimed in claim 1 and combustion-supporting combined combustion method is characterized in that: described one-level emulsifier unit is the high-shear emulsifying pump; Described secondary emulsifier unit is the immersion phaco device, and the immersion phaco device comprises the emulsification chamber, is arranged at the import and the outlet of emulsification chamber both sides; Be provided with piezoelectric chip in the emulsification chamber roof, this piezoelectric chip contacts with a bracing frame top, and by this bracing frame it is supported in outside the chamber; The other end of this bracing frame is connected with a horn; This horn stretches into the emulsification chamber interior, and this horn other end is connected with an oscillator, and the bottom of oscillator is immersed in the profit liquid level that needs emulsification; The vibration frequency of described oscillator is 20Khz, and sound field intensity is 10-20w/cm
2, described piezoelectric chip power is 2KW; The flowing velocity of emulsifying mixt in the emulsification chamber is less than 10cm/s.
4. fuel emulsification as claimed in claim 1 and combustion-supporting combined combustion method is characterized in that: described catalytic cracking unit, comprise pipe in the catalytic cracking that is provided with import and outlet, and in this, outside the pipe, be provided with heating jacket; In interior pipe, be filled with simultaneously the catalytic cracking agent, described catalytic cracking agent is any among MLC500 and the MLC-500ZA, perhaps any proportioning of two kinds.
5. fuel emulsification as claimed in claim 4 and combustion-supporting combined combustion method is characterized in that: in the import of pipe and the outlet, be provided with stainless (steel) wire in the said catalytic cracking.
6. fuel emulsification as claimed in claim 4 and combustion-supporting combined combustion method is characterized in that: the heating jacket of described catalytic cracking unit is the heating jacket of superheated steam heating, or electrically heated heating jacket.
7. fuel emulsification as claimed in claim 1 and combustion-supporting combined combustion method is characterized in that: the Main Ingredients and Appearance of described fuel oil is heavy oil or diesel oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910168027A CN101660764B (en) | 2009-08-07 | 2009-08-07 | Combined combustion method for fuel oil emulsification and combustion supporting |
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| Application Number | Priority Date | Filing Date | Title |
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| CN200910168027A CN101660764B (en) | 2009-08-07 | 2009-08-07 | Combined combustion method for fuel oil emulsification and combustion supporting |
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| CN101660764B true CN101660764B (en) | 2012-09-05 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102032586A (en) * | 2011-01-04 | 2011-04-27 | 三一重工股份有限公司 | Heavy oil combustion pretreatment device |
| CN105331396A (en) * | 2015-11-03 | 2016-02-17 | 谭人凤 | Energy-saving and emission-reducing nano oil production system and method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1101661A (en) * | 1993-10-14 | 1995-04-19 | 吕家候 | Compound gasoline |
| CN2262610Y (en) * | 1995-07-24 | 1997-09-17 | 宋永海 | Electrothermic ultrasonic magnetic resonance fuel oil cleaner |
| CN1275693A (en) * | 2000-02-29 | 2000-12-06 | 张子升 | Multiple magnet pair ultrasonic emulsification fuel-saving dirt-reducing device |
| CN2594485Y (en) * | 2003-01-27 | 2003-12-24 | 张子生 | Fuel magnetizing emulsifier |
-
2009
- 2009-08-07 CN CN200910168027A patent/CN101660764B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1101661A (en) * | 1993-10-14 | 1995-04-19 | 吕家候 | Compound gasoline |
| CN2262610Y (en) * | 1995-07-24 | 1997-09-17 | 宋永海 | Electrothermic ultrasonic magnetic resonance fuel oil cleaner |
| CN1275693A (en) * | 2000-02-29 | 2000-12-06 | 张子升 | Multiple magnet pair ultrasonic emulsification fuel-saving dirt-reducing device |
| CN2594485Y (en) * | 2003-01-27 | 2003-12-24 | 张子生 | Fuel magnetizing emulsifier |
Non-Patent Citations (2)
| Title |
|---|
| JP特开2002-115812A 2002.04.19 |
| JP特开平11-6615A 1999.01.12 |
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