CN101007970A - Heavy oil modified fuel oil for substituting for heavy diesel oil and its production method - Google Patents
Heavy oil modified fuel oil for substituting for heavy diesel oil and its production method Download PDFInfo
- Publication number
- CN101007970A CN101007970A CN 200610023666 CN200610023666A CN101007970A CN 101007970 A CN101007970 A CN 101007970A CN 200610023666 CN200610023666 CN 200610023666 CN 200610023666 A CN200610023666 A CN 200610023666A CN 101007970 A CN101007970 A CN 101007970A
- Authority
- CN
- China
- Prior art keywords
- oil
- heavy
- mixing
- spray
- fuel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
The invention relates to a fuel oil which takes modified heavy oil to replace heavy diesel, and the method for preparing the same. It comprises heavy oil, diesel, emulsifying agent, benzene- containing compound, aniline- containing wastewater from printery and phosphoric acid, then carries out four- step repeat spraying and mixing for emulsion and filtering in four- cascade emulsifying mixer, and gets final product. The heating power of fuel oil can reach 9000- 12000 Kcal/ kg, the flowability, ignitability, atomization property are good. The invention is characterized by simple process, low investment for emulsifying device, good effect, low production cost, suitability for industrial production and can be used for fuel furnance, industrial furnance and low- medium speed diesel engine.
Description
Technical field
The present invention relates to liquid carbon-containing fuel, specifically is oil fuel and the production method thereof that substitutes heavy gas oil with the heavy oil modification about a kind of.
Background technology
Heavy oil is that remaining residual oil makes after going out gasoline, kerosene and diesel oil by the cracked residue oil of oil and petroleum fractionating.Be characterized in that viscosity is big, can only be used for boiler, industrial furnace etc. usually and make fuel usefulness.Atomizing during for the kinematic viscosity of improving heavy oil and burning, in concrete the application, heavy oil is before entering burner, must heat with high-pressure water vapor in advance, but the high-pressure water vapor heating installation is huge, enterprise investment is big, and, easily cause environmental pollution because heavy oil combustion is incomplete.At present some medium and small sized enterprises adopt the heavy gas oil oil that acts as a fuel to be used for boiler or industrial furnace, but because of in recent years, the oil price of China is influenced by the world market oil price rise, and this has directly influenced the production cost of medium-sized and small enterprises.And contemporary petroleum industry faces oil product and becomes heavy, and carbon residue is too high, problems such as petroleum resources exhaustion, after some crude oil fractionated out gasoline, kerosene and diesel oil, the quality of remaining mink cell focus was extremely low, the burning difficulty, even can't fire burns, these inferior quality heavy oil are deposited in the warehouse for a long time.In order to fully utilize these natural resourcess, find a way out for these inferior quality heavy oil, research purpose of the present invention is to heavy oil, and especially inferior quality heavy oil carries out modification, and making it becomes the oil fuel that substitutes heavy gas oil, to satisfy the needs of market oil fuel.
Summary of the invention
The invention provides a kind of oil fuel and production method thereof that substitutes heavy gas oil with the heavy oil modification.
A kind of oil fuel with the alternative heavy gas oil of heavy oil modification is by heavy oil, diesel oil, and emulsifying agent contains benzene compound, and the printing and dyeing mill's trade effluent and the phosphoric acid that contain aniline are formed.It is a kind of good flowability that has, ignition quality and sprayability, and have high heating value, low ash content, low sulphur content, low mechanical impurity, non-corrosive fresh fuel oil.
The present invention is as follows with the component and the weight % content of the oil fuel of the alternative heavy gas oil of heavy oil modification:
Composition weight % content
Heavy oil 70-85
Diesel oil 2-8
Emulsifying agent 1-3
Contain benzene compound 1-5
The trade effluent 5-15 of printing and dyeing mill that contains aniline
Phosphatase 11-5
The present invention is a heavy oil with the stock oil that the heavy oil modification substitutes the oil fuel of heavy gas oil, can be brand heavy oil, for example No. 20, No. 60, No. 100, No. 200, also can be low reduced fuel oil, residual oil for example, #1 80 heavy oil, #250 heavy oil, other mink cell focus of the 350-540 of #280 heavy oil or petroleum tar ℃ cut.Another stock oil is diesel oil, comprises heavy gas oil or solar oil.
Become the physical condition of water-in-oil-type for the oil fuel product that makes the heavy oil modification, the present invention selects the emulsifier production of HLB value (hydrophile-lipophile balance value)＜6 for use, the S60 that produces of the first chemical plant of Jiangyin City China for example, S65, S80 or S85, their HLB value is between 1.5-5.9.
The described benzene compound that contains is to be selected from benzene, toluene or dimethylbenzene, and containing benzene compound all has been the effect of ignition dope with the printing and dyeing mill's trade effluent that contains aniline, go out in addition mould and bacteriological action.
Described phosphoric acid is used to regulate the pH value and is 7-9, and is also favourable to desulfurization, and can improve the storage stability and the combustionproperty of oil fuel product.
The present invention is with the production method of the alternative heavy gas oil oil fuel of heavy oil modification, and the process flow sheet of production method is referring to Fig. 1.
With heavy oil, diesel oil, emulsifying agent, contain benzene compound, contain printing and dyeing mill's trade effluent of aniline and phosphoric acid is reinforced by the proportioning of above-mentioned prescription, order is carried out circulate repeatedly spray mixing emulsification and filtration of four steps in four placed in-line spray mixing emulsors.The first step, (" the spray mixing emulsor is applied for " utility model " patent ") is by spray mixing emulsification 0.5-2 hour that circulates repeatedly in the batching adding spray mixing emulsor 1, mixed solution material temperature of reaction rises to 50-70 ℃, and the mixed solution material is emitted, and filters by the 180-320 order; In second step, the first step gained filtrate enters spray mixing emulsor 2, and operation is with spray mixing emulsor 1, the mixed solution material of emitting filters by M28-M14, in the 3rd step, the second step gained filtrate enters spray mixing emulsor 3 again and operates equally, and the mixed solution material of emitting filters by M10-M5; In the 4th step, the 3rd step gained filtrate enters spray mixing emulsor 4 again, same operation, and the mixed solution material of emitting filters by M10-M5, promptly gets the oil fuel product that the heavy oil modification substitutes heavy gas oil.
The structure of described spray mixing emulsor is seen Fig. 2-Fig. 4, mainly comprises mixing kettle 3, charging stock tank 6, spraying plant 5, residual oil pump 1, hot resistance temperature measuring head 2, three-way valve 7 and drainage conduit 4.The filling tube 9 of described charging stock tank 6 bottoms be installed in mixing kettle 3 on cover, and stretch in the mixing kettle 3.Described spraying plant 5 comprises spray channel 19 and guide plate 15.Spray channel 19 comprises the nozzle entrance 10 that communicates successively, turbulent flow road 11, hybrid chamber 12 and jet exit 13.Nozzle entrance 10 is doline, and the diameter in turbulent flow road 11 is 1.2-3mm, and two sides of hybrid chamber 12 walls respectively are provided with a liquid conductance mouth 14.Guide plate 15 is vertically to being arranged on the spray channel 19, and between liquid conductance mouth 14 and jet exit 13, is covered with aperture 16 on the guide plate 15, and the aperture of aperture 16 is 1-3mm, and the percentage of open area on the guide plate 15 is 60-80%.Also a filtering net 20 can be set below mixing kettle 3.Described residual oil pump places on the connecting tube 8 between three-way valve 7 and the mixing kettle 3 bottom discharge mouths 18, and drainage conduit 4 links to each other with three-way valve 7.Described hot resistance temperature measuring head 2 is fixedly set in the mixing kettle 3, and the loam cake that passes mixing kettle 3 by lead links to each other with temperature indicator 17.
The present invention is the shinny oil in water emulsion of a kind of Dark grey with the oil fuel that the heavy oil modification substitutes heavy gas oil, its combustion heat value can reach 9000-12000KCal/kg, be a kind of good flowability that has, ignition quality and sprayability, and have high heating value, low ash content, low sulphur content, low mechanical impurity, non-corrosive oil fuel, can be used for oil-firing boiler, industrial furnace and in, slow speed diesel engine.The present invention lists in table 1 with the performance perameter that the heavy oil modification substitutes the oil fuel product of heavy gas oil.
Table 1
| Project | Unit | The present invention substitutes the oil fuel of heavy gas oil with the heavy oil modification | No. 10 heavy gas oil indexs | Test method |
| Condensation point | ℃ | 4-19 | ＜10 | GB/T 3533 |
| Kinematic viscosity (50 ℃) | mm 2/s | 8-18.6 | ＜13.5 | GB/T 265 |
| Flash-point (remaining silent) | ℃ | ＞80 | ＞65 | GB/T 261 |
| Mechanical impurity | ％ | 0.06-0.07 | ＜0.1 | GB/T 511 |
| Carbon residue | ％ | 0.3-0.5 | ＜0.5 | GB/T 268 |
| Ash content | ％ | 0.03-0.04 | ＜0.04 | GB/T 508 |
| Sulphur content | ％ | 0.2-0.5 | ＜0.5 | GB/T 387 |
| Water soluble acid or alkali | Do not have | Do not have | GB/T 259 | |
| Moisture | ％ | 0.2-0.4 | ＜0.5 | GB/T 260 |
Table 1 shows that performance perameter that the present invention substitutes heavy gas oil oil fuel with the heavy oil modification is basically near the desired value of No. 10 heavy gas oil.
The present invention substitutes the good stability of the oil fuel of heavy gas oil with the heavy oil modification, under 6000 rev/mins of rotating speeds, carry out centrifugation with whizzer and do not have any demixing phenomenon in 5 hours, 48 hours breakdowns of emulsion not of heating in 70 ℃ of waters bath with thermostatic control, at room temperature preserve 2 years not stratified.
The present invention is the emulsion of even fine particle with the oil fuel that the heavy oil modification substitutes heavy gas oil, and the particle diameter of its 60-70% is less than 5 μ m, and all the other particle diameters are between 5-10 μ m.Therefore burning is complete, and oil consumption reduces, and helps environmental protection.
The present invention can be with must pre-warmed brand heavy oil before using or more those inferior quality heavy oil can be modified as a kind of oil fuel of alternative heavy gas oil of excellent property, it can be directly by burner spraying and burning, in also can be used for, slow speed diesel engine, for market provides a kind of novel oil fuel.And in prescription, adopted the trade effluent of printing and dyeing mill, for product of the present invention reduces the cost, reduced the pollution of trade effluent again to environment.
Preparation method of the present invention is easy, the emulsor equipment manufacturing cost is low, emulsify well, economical and practical, manufacturing cost is low, the price that substitutes the oil fuel product of heavy gas oil is lower than the price as the heavy oil and the heavy gas oil of stock oil, so the present invention is a kind of production method that is suitable for suitability for industrialized production, has very big economic benefit and social benefit.
The oil fuel that the present invention substitutes heavy gas oil with the heavy oil modification is used for the diesel engine of 135 or 180 models of generating set, and diesel engine condition is good, and oil consumption reduces, and lists in table 2 with the contrast of solar oil result of use.
Table 2
| Use oil product | Machine Wen Wendu ℃ | Circulating water temperature ℃ | Exhaust temperature ℃ | The main frame operating mode | The waste gas color | Oil consumption T/h | Warm ℃ of oil |
| Oil fuel product of the present invention | 55 | 51 | 380 | Normally | Middle ash | 60 | 50 |
| Solar oil | 50 | 48 | 360 | Normally | Dark-grey | 70 | 35 |
| Contrast | +5 | +3 | +20 | Normally | Improve | -10 | +15 |
The oil fuel that the present invention substitutes heavy gas oil with the heavy oil modification is used for molten aluminum industrial to be used, oil fuel from the atomizing of burner ejection in order, flame is bright, burning fully, furnace temperature is stable, oil consumption reduces, and lists in table 3 with the contrast of heavy gas oil result of use.
Table 3
| Use oil product | Oil pressure MPa | Fire box temperature ℃ | Hot blast inlet pipe temperature ℃ | Flue horizontally-arranged temperature degree ℃ | Smoke intensity | Oil consumption kg/h |
| Oil fuel product of the present invention | 1.7 | 840-940 | 230-280 | 90-120 | Nattierblue | 60 |
| Heavy gas oil | 1.2 | 720-800 | 200-240 | 80-95 | Black | 72 |
| Contrast | +0.5 | +(120-140) | +(30-40) | +(10-25) | Improve | -12 |
Description of drawings
Fig. 1 is the process flow sheet of production method of the present invention.
Fig. 2 is the structural representation of the spray mixing emulsor that adopts in the production method of the present invention.
Fig. 3 is the longitudinal sectional drawing of spraying plant among Fig. 2.
Fig. 4 is the left view of guide plate among Fig. 3.
Embodiment
Referring to Fig. 1-Fig. 4: the first step, with 75 kilograms in #180 heavy oil, 1 kilogram of benzene, 15 kilograms of printing and dyeing mill's trade effluents that contain aniline, 7 kilograms of heavy gas oil, the stock liquid that phosphatase 11 kilogram and emulsifying agent S80 (the HLB value is 4.3) are 1 kilogram enters in the mixing kettle 3 of spray mixing emulsor 1 by charging stock tank 6 and filling tube 9 thereof, the three-way valve 7 and the passage of nozzle entrance 10 are opened, and close passage with drainage conduit 4, start residual oil pump 1, by behind filtering net 20 (screen distance 0.1-0.5mm) the elimination impurity by mixing kettle 3 bottom discharge mouths 18 effusive liquid material through residual oil pump 1, pipeline 8 and three-way valve 7 enter the nozzle entrance 10 of spraying plant 5, (when pumping capacity is 3 cubic metres/hour, turbulent flow road diameter is 2.2mm, and liquid stream viscosity is 18.6mm to enter turbulent flow road 11
2During/s, Reynolds number=6811), liquid-flow is the turbulent flow attitude, therefore molecules strike and friction take place in liquid stream in turbulent flow road 11, the liquid material is mixed and more refinement of particle, the liquid material goes out the vaporific emulsion of turbulent flow road 11 to the even fine particle of hybrid chamber 12 ejections, and go out at a high speed by jet exit 13, the anti-phase aperture 16 that passes on the guide plate 15 of part liquid material enters outside hybrid chamber 12 walls, thereby make the inside and outside generation pressure difference of hybrid chamber 12 walls, the liquid material is formed by liquid conductance mouth 14 again flee among a small circle, make the mixing and emulsifying better effects if.Make the mixed solution material by mixing kettle 3 bottom discharge mouths 18 like this, residual oil pump 1 constitutes a circulation loop with spraying plant 5, the spray mixing that circulates so repeatedly emulsification 45 minutes, temperature in the mixing kettle 3 rises gradually, measure by hot resistance temperature measuring head 2, on temperature indicator 17, demonstrate the situation of temperature, when temperature rises to 50 ℃, the blended feed liquid is finished mixing and emulsifying, with closing all of three-way valve 7 and nozzle entrance 10, and open passage with drainage conduit 4, mixed solution is discharged from drainage conduit 4, filters by the 180-320 order; In second step, gained filtrate enters spray mixing emulsor 2, and the spray mixing emulsification that circulates repeatedly again, operation are with spray mixing emulsor 1, and the Push And Release of each valve of mat is controlled entering and discharging of mixed solution.The flow of beating round-robin residual oil pump 2 is 4.2 cubic metres/hour, and turbulent flow road diameter is 2.2mm, and liquid stream viscosity is 18.6mm
2During/s, Reynolds number=9536 of liquid stream.The mixed solution material of discharging filters by M28-M14; In the 3rd step, the filtrate that obtains enters spray mixing emulsor 3 again, and operation is with spray mixing emulsor 2, and the flow of beating round-robin residual oil pump 3 is 7.5 cubic metres/hour, and the turbulent flow diameter is 2.2mm, and liquid stream viscosity is 18.6mm
2During/s, Reynolds number=17028 of liquid stream.The mixed solution material of discharging filters by M10-M5; In the 4th step, the filtrate that obtains enters spray mixing emulsor 4 again, and operation is with spray mixing emulsor 2, and the flow of beating round-robin residual oil pump 4 is 3 cubic metres/hour, and turbulent flow road diameter is 2.2mm, liquid stream viscosity 12.7mm
2During/s, Reynolds number=9975 of liquid stream.The mixed solution material of discharging filters by M10-M5, and filtrate is the oil fuel product that the heavy oil modification substitutes heavy gas oil.The performance of product test is as follows: kinematic viscosity (50 ℃) is 12.7mm
2/ s, density is 0.8900g/cm
3The pH value is 7.5, and carbon residue is 0.3%, and ash content is 0.04%, moisture 0.2%, sulphur content 0.4%, close flash point are 88 ℃, 18 ℃ at zero pour, recording low heat value with German Lesto 325 M/XL and Testo 350 is the 9759KCal/ kilogram, high heating value is the 11472KCal/ kilogram, and product does not have any demixing phenomenon with whizzer centrifugation 5 hours under 6000 rev/mins rotating speed.
80 kilograms in residual oil, 4 kilograms of benzene, 8 kilograms of printing and dyeing mill's trade effluents that contain aniline, 5 kilograms of solar oils, in the mixing kettle 3 of 1 kilogram of adding of 2 kilograms of phosphoric acid and emulsifying agent S85 (the HLB value is 1.8) spray mixing emulsor 1, the spray mixing that circulates repeatedly emulsification 2 hours, temperature rises to 70 ℃, the blended feed liquid is finished mixing and emulsifying, wherein turbulent flow road diameter is 3mm, wherein mixed solution is in the emulsion process of circulation spray mixing repeatedly in each step, and the Reynolds number of liquid stream all is greater than 3000, shows that liquid stream is the turbulent flow attitude.All the other circulation spray mixing emulsification procedures are with embodiment 1, filter at last filtrate be the oil fuel product that substitutes heavy gas oil.The kinematic viscosity of product (50 ℃) is 16.8mm
2/ s, density is 0.9174g/cm
3, the pH value is 8.2, and carbon residue content is 0.4%, and ash content is 0.03%, sulphur content 0.2%, close flash point is 85 ℃, and condensation point is 8 ℃, and water soluble acid or alkali is not for having.
With 83 kilograms in #250 heavy oil, 2 kilograms of dimethylbenzene contain 6 kilograms of the printing and dyeing industrial waste waters of aniline, 2 kilograms of solar oils, and 5 kilograms of phosphoric acid, and in the mixing kettle 3 of 2 kilograms of addings of emulsifying agent S60 (HLB value is 4.7) spray mixing emulsor 1.The spray mixing that circulates repeatedly emulsification 1 hour, temperature rise to 60 ℃, and the blended feed liquid is finished mixing and emulsifying, wherein turbulent flow road diameter is 1.2mm, wherein mixed solution is in the emulsion process of circulation spray mixing repeatedly in each step, and the Reynolds number of liquid stream all is greater than 3000, shows that liquid stream is the turbulent flow attitude.All the other circulation spray mixing emulsification procedures are with embodiment 1, filter at last filtrate be the oil fuel product that substitutes heavy gas oil.The density of product is 0.9218g/cm
2, kinematic viscosity (50 ℃) is 13.9mm/s, the pH value is that 7.0 carbon residue content are 0.5%, ash content is 0.03%, mechanical impurity 0.06%, 12 ℃ of condensation points, close flash point is 82 ℃, in 70 ℃ of waters bath with thermostatic control, preserve 48 hours not stratified.
With 72 kilograms in No. 100 heavy oil, toluene 4kg contains the printing and dyeing industrial waste water 12kg of aniline, and heavy gas oil 8kg, 1 kilogram of phosphoric acid 3kg and emulsifying agent S65 (the HLB value is 2.1) add in the mixing kettle 3 of spray mixing emulsor 1.The spray mixing that circulates repeatedly emulsification 0.5 hour, temperature rise to 60 ℃, and the blended feed liquid is finished mixing and emulsifying, wherein turbulent flow road diameter is 2mm, wherein mixed solution is in the emulsion process of circulation spray mixing repeatedly in each step, and the Reynolds number of liquid stream all is greater than 3000, shows that liquid stream is the turbulent flow attitude.All the other circulation spray mixing emulsification procedures filter the filtrate that obtains at last and are the oil fuel product that substitutes heavy gas oil with embodiment 1.The kinematic viscosity of product (50 ℃) is 8.5mm
2/ s, the pH value is 8.0, and carbon residue content is 0.3%, and ash content is 0.04%, sulphur content 0.2%, mechanical impurity 0.06%, condensation point is 4 ℃, the close point of remaining silent is 86 ℃.
Claims (4)
1. one kind substitutes the oil fuel of heavy gas oil with the heavy oil modification, it is characterized in that it is made up of following component and weight % content:
Composition weight % content
Heavy oil 70-85
Diesel oil 3-8
Emulsifying agent 1-3
Contain benzene compound 1-5
The trade effluent 5-15 of printing and dyeing mill that contains aniline
Phosphatase 11-5
Described emulsifying agent is commercially available prod S60, S65, and S80 or S85, the hydrophile-lipophile balance value of emulsifying agent is between 1.5-5.9;
The described benzene compound that contains is to be selected from benzene, toluene or dimethylbenzene;
The pH value of described oil fuel is 7-9.
2. the described production method that substitutes heavy gas oil oil fuel with the heavy oil modification of claim 1, it is characterized in that heavy oil, diesel oil, emulsifying agent, contain benzene compound, the printing and dyeing mill's trade effluent and the phosphoric acid that contain aniline are reinforced by proportioning, in four placed in-line spray mixing emulsors, carry out four in proper order and go on foot circulate repeatedly spray mixing emulsification and filtration: the first step, batching adds in the spray mixing emulsor 1, the spray mixing that circulates repeatedly emulsification 0.5-2 hour, temperature of reaction rises to 50-70 ℃, and the mixed solution material is emitted, and filters by the 180-320 order; In second step, the first step gained filtrate enters spray mixing emulsor 2, and operation is with spray mixing emulsor 1, and the mixed solution material of emitting filters by M28-M14; In the 3rd step, the second step gained filtrate enters spray mixing emulsor 3 again, same operation, and the mixed solution material of emitting filters by M10-M5; In the 4th step, the 3rd step gained filtrate enters spray mixing emulsor 4 again, same operation, and the mixed solution material of emitting filters by M10-M5, promptly gets the oil fuel that the heavy oil modification substitutes heavy gas oil.
3. the production method that substitutes the oil fuel of heavy gas oil with the heavy oil modification as claimed in claim 2, it is characterized in that, the structure of the spray mixing emulsor that adopts in the production method mainly comprises mixing kettle (3), charging stock tank (6), spraying plant (5), residual oil pump (1), hot resistance temperature measuring head (2), three-way valve (7) and drainage conduit (4), the filling tube (9) of described charging stock tank (6) bottom be installed in mixing kettle (3) on cover, and stretch in the mixing kettle (3); Described spraying plant (5) comprises spray channel (19) and guide plate (15), spray channel (19) comprises the nozzle entrance (10) that communicates successively, turbulent flow road (11), hybrid chamber (12) and jet exit (13), nozzle entrance (10) is doline, the diameter in turbulent flow road (11) is 1.2-3mm, the both sides of hybrid chamber (12) wall respectively are provided with a liquid conductance mouth (14), guide plate (15) is vertically to being arranged on the spray channel (19), and be positioned between liquid conductance mouth (14) and the jet exit (13), be covered with aperture (16) on the guide plate (15); In the below of mixing kettle (3) filtering net (20) is set; Described residual oil pump (1) places on the connecting tube (8) between the bottom discharge mouth (18) of three-way valve (7) and mixing kettle (3), and drainage conduit (4) links to each other with three-way valve (7); Described hot resistance temperature measuring head (2) is fixedly set in the mixing kettle (3), and the loam cake that passes mixing kettle (3) by lead links to each other with temperature indicator (17).
4. the production method that substitutes heavy gas oil with the heavy oil modification as claimed in claim 3, the aperture of the aperture (16) that is covered with on the guide plate (15) in the spray mixing emulsor that it is characterized in that adopting in the production method is 1-3mm, and the percentage of open area on the guide plate (5) is 60-80%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2006100236664A CN101007970B (en) | 2006-01-26 | 2006-01-26 | Heavy oil modified fuel oil for substituting for heavy diesel oil and its production method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2006100236664A CN101007970B (en) | 2006-01-26 | 2006-01-26 | Heavy oil modified fuel oil for substituting for heavy diesel oil and its production method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101007970A true CN101007970A (en) | 2007-08-01 |
| CN101007970B CN101007970B (en) | 2012-06-20 |
Family
ID=38696633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2006100236664A Expired - Fee Related CN101007970B (en) | 2006-01-26 | 2006-01-26 | Heavy oil modified fuel oil for substituting for heavy diesel oil and its production method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101007970B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102329666A (en) * | 2011-08-30 | 2012-01-25 | 江苏福斯特化工制造有限公司 | Environmentally-friendly heavy oil additive |
| CN101469277B (en) * | 2007-12-26 | 2012-11-14 | 李文智 | Method for preparing emulsion fuel from oil-containing water |
| CN103881769A (en) * | 2014-03-20 | 2014-06-25 | 常胜 | Liquid fuel static blending system and method |
| CN115340890A (en) * | 2021-05-12 | 2022-11-15 | 陈进益 | Heavy oil substituted diesel oil formula and using device thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1019130B (en) * | 1990-12-11 | 1992-11-18 | 辽河石油勘探局钻采工艺研究院 | Process for prodn. of emulsion fuel consisting of diesel and heavy oil |
| CN1146481A (en) * | 1995-09-29 | 1997-04-02 | 上海赢得实业总公司 | Formula for energy-saving fuel oil and praparation technology |
-
2006
- 2006-01-26 CN CN2006100236664A patent/CN101007970B/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101469277B (en) * | 2007-12-26 | 2012-11-14 | 李文智 | Method for preparing emulsion fuel from oil-containing water |
| CN102329666A (en) * | 2011-08-30 | 2012-01-25 | 江苏福斯特化工制造有限公司 | Environmentally-friendly heavy oil additive |
| CN103881769A (en) * | 2014-03-20 | 2014-06-25 | 常胜 | Liquid fuel static blending system and method |
| CN115340890A (en) * | 2021-05-12 | 2022-11-15 | 陈进益 | Heavy oil substituted diesel oil formula and using device thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101007970B (en) | 2012-06-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR102317081B1 (en) | Method for producing asphalt by combined continuous mixing and forced mixing | |
| CN202199276U (en) | Fuel oil emulsifying device | |
| CN101007970B (en) | Heavy oil modified fuel oil for substituting for heavy diesel oil and its production method | |
| JP2013511656A (en) | Diesel engine emulsified oil production promotion system and method | |
| CN108359504A (en) | Low-carbon alcohols cleaning new energy fuel additive | |
| CN1958745A (en) | Environmental protective diesel oil, and preparation method | |
| CN103320183A (en) | Cleaning and dispersing agent for bio-based methanol gasoline and preparation method of cleaning and dispersing agent | |
| CN104059702B (en) | Spark ignition engine automobile exhaust cleaning agent as well as preparation and using methods thereof | |
| CN1109735C (en) | Oil-water-coal slurry and its preparing process | |
| CN101633859B (en) | High-cleanness diesel oil | |
| CN106811242A (en) | A kind of environmentally friendly low-carbon (LC) high heating value New Marine fuel oil | |
| CN1067593A (en) | Multifunctiuonal emulsifying agent for adding water in heavy oil | |
| CN101445751A (en) | Non-shear-form environment-friendly and energy-saving watered procetane | |
| CN1240815A (en) | Efficient liquid emulsifier for heavy oil | |
| KR20070096450A (en) | Emulsion combustion apparatus | |
| CN101323801B (en) | Micro-emulsified diesel oil biomass composite additive | |
| CN210237193U (en) | Device for rapidly heating grease-containing organic wastewater | |
| JPS5913823A (en) | Incineration of waste ion exchange resin | |
| CN115975686B (en) | Marine emulsified heavy oil preparation method and device | |
| CN101092580A (en) | Environmental protection typed high-energy liquid fuel in alcohol group | |
| CN103666636A (en) | Additive for soluble clean fuel oil and preparation method of additive | |
| KR100763340B1 (en) | Baiodeungyu's manufacture method for boiler | |
| JPH027353B2 (en) | ||
| CN103205288A (en) | Clean synthetic diesel and synthetic process thereof | |
| CN103758664A (en) | Front emission reduction system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120620 Termination date: 20150126 |
|
| EXPY | Termination of patent right or utility model |