Classifications

• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
  • C10L1/322—Coal-oil suspensions
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
  • C10L1/328—Oil emulsions containing water or any other hydrophilic phase
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/12—Inorganic compounds
  • C10L1/1291—Silicon and boron containing compounds
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/16—Hydrocarbons
  • C10L1/1608—Well defined compounds, e.g. hexane, benzene
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/16—Hydrocarbons
  • C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/18—Organic compounds containing oxygen
  • C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
  • C10L1/183—Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom
  • C10L1/1832—Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom mono-hydroxy
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/18—Organic compounds containing oxygen
  • C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
  • C10L1/1905—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polycarboxylic acids
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/18—Organic compounds containing oxygen
  • C10L1/192—Macromolecular compounds
  • C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
  • C10L1/1985—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/22—Organic compounds containing nitrogen
  • C10L1/23—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
  • C10L1/231—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/22—Organic compounds containing nitrogen
  • C10L1/234—Macromolecular compounds
  • C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
  • C10L1/2381—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds polyamides; polyamide-esters; polyurethane, polyureas
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L2270/00—Specifically adapted fuels
  • C10L2270/02—Specifically adapted fuels for internal combustion engines
  • C10L2270/026—Specifically adapted fuels for internal combustion engines for diesel engines, e.g. automobiles, stationary, marine
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
  • C10L2300/00—Mixture of two or more additives covered by the same group of C10L1/00 - C10L1/308
  • C10L2300/20—Mixture of two components

Definitions

• the present invention relates to a modified emulsion fuel oil and a method of producing the same. Background of the invention
• the products produced by using heavy oil imported from the Middle East have a sulfur content of more than 2%.
• the product produces a large amount of harmful gases such as sulfur dioxide, N0 X and soot when burned, causing serious pollution to the environment. 4.
• the condensation point is high and has not been improved.
• the product should be kept at a certain temperature during storage.
• Some emulsified oil can only be directly emulsified and burned at the site of use. It cannot be stored in a storage tank and piped like 0 # ⁇ . 5.
• the emulsified product does not improve the grade of the fuel. Cannot be used on high speed diesel engines (2200 rpm).
• the product has high ash content, many residual carbon, and contains rare elements such as vanadium and molybdenum, which will cause wear and tear on machinery. 7. High viscosity, high gel content, easy to block the nozzle.
• CN1329132 discloses a high energy liquid fuel comprising an emulsified fuel oil and other auxiliary agents.
• the high-energy liquid fuel does not solve the above problems, for example, its storage stability is poor, and thickening is found after storage for 6 months; although the sulfur content is somewhat improved, it cannot meet national and international standards; There is a certain reduction, but it does not achieve satisfactory results.
• heavy oil improves the quality of fuel products through emulsification, it reaches the standard of 1# marine fuel oil, but it can not achieve the quality of Ott light diesel oil, so it can not be used in high-speed diesel engines and The tractor is loaded on the vehicle; because the product is thickened after storage, it cannot be piped; the raw materials used are limited.
• an aspect of the present invention provides a modified emulsified fuel oil which is obtained by mixing the following components, based on the total weight of the emulsified fuel oil:
• the modified emulsified fuel oil has a combustion heat value of 8000 - 13000 kJ / kg.
• the emulsified fuel oil is obtained by the following method:
• the product in the reaction vessel is subjected to a shearing agitation treatment at a temperature of 75 ° C for 10 minutes to 10 hours, preferably 0.5 to 5 hours, to obtain a product;
• step 6) conveying the product obtained in the step 5) to the ripening tank, aging at 45-75 ° C, preferably 50-60 ° C for 6-100 hours, preferably 24-100 hours, to obtain the final product, that is, the emulsified fuel oil .
• the heavy oil is selected from one or more of 180# heavy oil and 250# heavy oil, and the heavy oil is contained in an amount of 42-48% by weight, preferably 45% by weight, in the The total weight of the emulsified fuel oil.
• the softened water is selected from water having a hardness of 7 or less, preferably 1-6, and the softened water content is 15-20% by weight, preferably 18% by weight, by The total weight of the emulsified fuel oil.
• the emulsifier is preferably selected from the group consisting of TG 306 emulsifier and 0 emulsifier, the emulsifier is 0. 1-0. 15% by weight, preferably 0.13% by weight, based on the total weight of the emulsified fuel oil.
• the light oil is selected from one or more of 0 # light diesel, aviation coal, 200 s solvent, tt and 2" marine fuel oil, the content of the light oil It is 10-25% by weight, preferably 20% by weight, based on the total weight of the emulsified fuel oil.
• the modifier is selected from one or more of 200# solvent and benzene, and the modifier is contained in an amount of 4 to 10% by weight, preferably 6% by weight. , based on the total weight of the emulsified fuel oil.
• the auxiliary agent is selected from one or more of a detergent dispersant, a condensing agent, a combustion improver, and a high energy agent, and is preferably selected from the group consisting of isooctyl nitrate, isobutanol, and poly One or more of ether amine, diisoamyl oxalate, di-tert-butyl-p-cresol, ethylene glycol methyl ether, water-in-oil emulsifier, polybutylene polyamine, butyl borohydride, lithium aluminum hydride,
• the adjuvant is present in an amount of from 12 to 14% by weight, preferably 13% by weight, based on the total weight of the emulsified fuel oil.
• Another aspect of the invention provides a method of preparing an emulsion fuel oil comprising:
• the material in the reaction vessel is subjected to shear agitation treatment at 8000 - 15000 rpm, preferably 10,000 - 13,000 rpm and 50 - 85 ° C, preferably 55 - 75 ° C, for a period of 20 minutes to 10 hours, preferably 0. 5-5 hours, the product is obtained; 6) conveying the product obtained in the step 5) to the ripening tank, and aging at 45-75 ° C, preferably 50-60 ° C for 6-100 hours, preferably 24-100 hours, to obtain a final product, that is, an emulsified fuel oil. .
• the invention further provides 40-50 parts by weight of heavy oil, 10-25 parts by weight of demineralized water, 0.1-0.5 parts by weight of emulsifier, 5-30 parts by weight of light oil, 1-15 parts by weight.
• the invention fully utilizes China's precious energy resources and cheap raw materials, turns waste into treasure, improves oil quality, and converts the emulsified fuel oil with low calorific value, high viscosity, high sulfur content, water content and high condensation point into Oil with high calorific value, low viscosity, good fluidity, low sulfur content and low condensation point.
• the technical index of the product of the invention reaches the technical standard of 0 light diesel oil.
• the product of the invention can be used on the idle diesel transport vehicle and used on the oil-fired boiler, and can be burned to the end, does not generate black smoke, and meets the environmental protection and energy-saving standards.
• the product of the invention can be stored for a long time without delamination, and the particle size of the particles is less than 5 ⁇ , and the fluidity is good at a temperature of - 20 to -40 Torr, which is convenient for storage and transportation. Ultimately achieve the goal of environmental protection and energy conservation. detailed description
• the invention provides a modified emulsified fuel oil which is prepared by mixing the following components, based on the total weight of the emulsified fuel oil:
• the modified emulsified fuel oil has a combustion heat value of 8000 - 13000 kJ / kg.
• the modified emulsified fuel oil is a mixture of the following components:
• the heavy oil refers to the residue obtained by the crude oil after constant pressure distillation under reduced pressure. Or appropriate addition of other distillate oil or secondary hot working residue.
• the heavy oil generally refers to one or more of 180 tt heavy oil or 250 # heavy oil.
• the heavy oil is 180# heavy oil, and in another preferred embodiment of the invention, the heavy oil is 250# heavy oil. In another preferred embodiment of the invention, the heavy oil is a mixture of 180# heavy oil and 250# heavy oil.
• the heavy oil is contained in an amount of 40 to 50% by weight, preferably 42 to 48% by weight, more preferably 45% by weight, based on the total mass of the emulsified fuel oil.
• the demineralized water means water having a hardness of 7 or less, i.e., the content of calcium carbonate is 50 ppm or less, preferably 15 to 50 ppm.
• the demineralized water can be produced from tap water by conventional softening techniques.
• the softening technique includes conventional distillation, ion exchange, and the like.
• the demineralized water is water having a hardness of 1-6 after the tap water is treated with the ion exchange resin, preferably water having a hardness of 2 to 4, more preferably water having a hardness of 3.
• hard water e.g., general tap water, river water, well water, etc.
• hard water contains many metal ions such as calcium ions and magnesium ions
• softened water is preferably used in the present invention.
• the softened water is contained in an amount of 10 to 25% by weight, preferably 15 to 20% by weight, more preferably 18% by weight, based on the total mass of the emulsified fuel oil.
• the light oil refers to a fraction in which crude oil is frequently distilled under a certain temperature condition or is blended with a secondary processed diesel component in a certain ratio.
• the gas oil is conventional, and the light oil used can be selected depending on the kind and amount of the heavy oil used, as long as it can attain the object of the present invention.
• the light oil is selected from one or more of 0 s light diesel, jet fuel, 200 s solvent, 1 # and 2 3 ⁇ 4 marine fuel oil.
• the light oil is contained in an amount of 5 to 30% by weight, preferably 10 to 25 parts by weight, more preferably 20% by weight based on the total mass of the emulsified fuel oil.
• the emulsifier may be any conventional emulsifier (e.g., an oil-in-water emulsifier or a water-in-oil emulsifier) or a mixture thereof in the art.
• the emulsifier is selected from one or more of a TG306 emulsifier and an OPC emulsifier, and the emulsifier is more preferably a TG306 emulsifier.
• the content of the emulsifier is 0. 1-0. 5 ⁇ %, preferably 0. 1-0. 15% by weight, more preferably 0. 13% by weight, as described The total weight of the emulsified fuel oil.
• the modifier is a commonly used modifier in the art as long as the rheology of the emulsified fuel oil of the present invention can be changed.
• the modifier is selected from one or more of 200# solvent and benzene, and the modifier is more preferably benzene.
• the modifier is contained in an amount of from 1 to 15% by weight, preferably from 4 to 10% by weight, more preferably 6% by weight, based on the total mass of the emulsified fuel oil.
• the auxiliary agent is a conventional auxiliary agent in the art, and includes one or more of a detergent dispersant, a condensing agent, a combustion improver, and a high energy agent.
• the adjuvant is selected from the group consisting of isooctyl nitrate, isobutanol, polyether amine, diisoamyl oxalate, di-tert-butyl-p-cresol, ethylene glycol methyl ether, water-in-oil One or more of an emulsifier, butane borane, lithium aluminum hydride, and polybutene polyamine.
• the total content of the auxiliary agent is from 7.5 to 15% by weight, preferably from 12 to 14% by weight, more preferably 13% by weight, based on the total weight of the emulsified fuel oil. . 1-5 ⁇
• the content of each of the auxiliaries is usually from 0.05 to 10% by weight, preferably from 0.1 to 5% by weight.
• the content of each of the auxiliary agents can be specifically selected depending on the desired properties, and this is known to those skilled in the art as long as the sum of them is included in the total content of the above-mentioned auxiliary agent. can. 1-5.
• the content of the diisooctyl oxalate is 0. 5% by weight, preferably 0. 5-2% by weight, the content of the diisooctyl oxalate is 0. 5-
• the content of the polybutene polyamine is 0. 5-3 wt%, preferably 1. 87-2 wt%, the polybutene polyamine content is 0. 3% by weight, preferably 1-2 wt%.
• the content of the ethylene glycol methyl ether is from 0.5 to 3% by weight, preferably from 1 to 2% by weight, of the di-tert-butyl-p-cresol The content is 0.5-3% by weight, preferably 1-2. 2% by weight, based on the total weight of the emulsified fuel oil
• the additive used in the present invention may be selected from one or more of a pigment and a diluent (e.g., isobutanol).
• the content of the additive may be any content as long as the amount thereof does not adversely affect the properties of the emulsified fuel oil.
• the content of the additive may be from 0.1 to 10% by weight, preferably from 0.5 to 7% by weight, more preferably from 1 to 5% by weight, most preferably 2% by weight, Based on the total weight of the emulsified fuel oil.
• the combustion heat value of the emulsified fuel oil is 8000 - 13,000 kJ / kg, preferably It is 10,000 to 13,000 kJ/kg, and more preferably 11,000 kJ/kg.
• Another aspect of the invention provides a method of preparing an emulsion fuel oil of the invention, which comprises:
• the product obtained in the step 5) is sent to a ripening tank and aged at 65-75 ° C, preferably 50-60 ° C for 6-100 hours, preferably 24-100 hours, to obtain a final product.
• the temperature is preferably 60 °C.
• the reaction vessel may be fully enclosed, semi-sealed or unsealed.
• the reactor is preferably fully hermetically sealed or semi-hermetic.
• the reactor is preferably equipped with a high shear emulsification pump, a static mixer and a high speed disperser.
• the order of addition of the light oil, the modifier and the auxiliary may be arbitrary.
• the order of addition of the above materials is in the order of light oil, modifiers and auxiliaries.
• reaction vessel equipped with a high shear emulsification pump, a static mixer, and a high speed disperser can be used in the present invention
• a person skilled in the art can also select a reaction vessel equipped with other stirring equipment as needed, as long as The reactor can be sufficiently emulsified under the reaction conditions to achieve the object of the present invention.
• the reaction time is from 1 to 4 hours, more preferably from 2 hours. In a preferred embodiment of the invention, the ripening time is from 36 to 72 hours, more preferably 48 hours.
• the total heat value is high, up to 13000 kJ/kg;
• the sulfur content is low, and the fuel then reduces the emission of sulfur dioxide, sputum and dust, and meets environmental protection standards;
• Low condensation point can also be used in climatic conditions of -40 °C;
• the modified emulsified fuel oil of the invention is mainly used for replacing diesel oil, heavy oil, kerosene, etc., and can be widely used in porcelain factories, glass factories, silicon carbide plants, metal smelters, oil-fired power plants, ships, ships, high, medium, Low-speed diesel engines, oil-fired boilers, fuel cookers, farm tractors, trucks, etc.
• the modified emulsified fuel oil of the present invention is used in the same manner as 0# ⁇ , and it is not necessary to change the mechanical structure of the engine.
• the modified emulsified fuel oil of the present invention can be stored in an oil tank without the need for heat preservation.
• modified emulsified fuel oil of the present invention does not cause corrosion and abrasion of mechanical articles, mainly because the emulsified fuel oil of the present invention contains sulfur and rare elements such as vanadium, molybdenum and nickel.
• the technology for producing modified emulsification according to the present invention has the advantages of low fixed assets investment, simple process, large-scale industrial production, and no three-waste pollution.
• the fixed asset investment required for the production technology of the present invention is 10% of the refinery.
• the modified emulsified fuel oil of the present invention was placed at 25 Torr for 1 month, 6 months, 1 year, and 2 years, respectively, to observe whether or not stratified appearance appeared.
• Example 1 The modified emulsified fuel oil of the present invention was placed at 25 Torr for 1 month, 6 months, 1 year, and 2 years, respectively, to observe whether or not stratified appearance appeared.
• the high-shear emulsification pump, static mixer and high-speed disperser were started, and the materials in the reaction vessel were reacted (emulsified) in a fully sealed state at a temperature of 100 ° C and 60 ° C for a reaction time of 60 minutes.
• Example 2 - 4 The product obtained in the reaction vessel was transferred to a ripening tank and aged for 24 hours to obtain a modified emulsion fuel oil.
• Example 2 - 4 The product obtained in the reaction vessel was transferred to a ripening tank and aged for 24 hours to obtain a modified emulsion fuel oil.
• Example 2 - 4 The product obtained in the reaction vessel was transferred to a ripening tank and aged for 24 hours to obtain a modified emulsion fuel oil.
• Example 2 - 4 The product obtained in the reaction vessel was transferred to a ripening tank and aged for 24 hours to obtain a modified emulsion fuel oil.
• a modified emulsion fuel oil was prepared in the same manner as in Example 1, and the contents and processing conditions of the raw materials are shown in Table 1.
• the results of the physicochemical parameter test for the emulsified fuel oil obtained in Example 2-4 are basically the same as those in the first embodiment, and the total calorific value is 9600-11000 KJ/KG, respectively, and the freezing point thereof is -35 to -42 ⁇ , respectively, indicating that the implementation
• the emulsified fuel oil obtained in Examples 1 to 4 had a high calorific value of combustion and excellent frost resistance.
• Table 3 Emission test results of the emulsified fuel oil obtained in Example 1 and environmentally-friendly allowable discharge concentration
• Example 2 The results of the environmental emission test of the emulsified fuel oil obtained in Examples 2 to 4 were similar to those of Example 1, and both included environmental protection allowable emissions.
• Table 4 Power test results of the emulsified fuel oil and 0# diesel oil obtained in Example 1 Whether the diesel engine can operate normally with or without significant changes in fuel consumption relative to 0# light diesel oil.
• Example 1 No 105%
• Example 2 No 106 %
• Example 3 can be no 107%
• Example 4 can be 104%
• Table 5 Test results of hazardous chemicals in Example 1

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• Chemical & Material Sciences (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Health & Medical Sciences (AREA)
• Emergency Medicine (AREA)
• Inorganic Chemistry (AREA)
• Liquid Carbonaceous Fuels (AREA)

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• 2005
  • 2005-06-24 CN CNA2005100271112A patent/CN1884443A/zh active Pending
• 2006
  • 2006-06-20 KR KR1020087001790A patent/KR20080017491A/ko not_active Application Discontinuation
  • 2006-06-20 WO PCT/CN2006/001395 patent/WO2006136096A1/zh active Application Filing
  • 2006-06-20 EP EP06742192A patent/EP1900796A4/de not_active Withdrawn
• 2007
  • 2007-12-21 US US11/962,417 patent/US20090313885A1/en not_active Abandoned

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