CN101328425A - Formula of emulsified diesel oil - Google Patents
Formula of emulsified diesel oil Download PDFInfo
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- CN101328425A CN101328425A CNA2007100696501A CN200710069650A CN101328425A CN 101328425 A CN101328425 A CN 101328425A CN A2007100696501 A CNA2007100696501 A CN A2007100696501A CN 200710069650 A CN200710069650 A CN 200710069650A CN 101328425 A CN101328425 A CN 101328425A
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Abstract
The invention relates to a formula of emulsified diesel oil. The formula consists of diesel oil, water and an addition agent, wherein the compositions of the formula in percentage by weight include: 65 to 95 percent of diesel oil and 35 to 5 percent of the water, and the addition agent being one thousandth of the total amount of water and diesel oil; moreover, the addition agent in percentage by weight includes: 35 percent of polyoxyethylene sorbitan monostearate, 12 percent of Sorbitan monostearate, 13 percent of polyoxyethylene sorbitan tristearate, 6 percent of ethylene-acrylic ester copolymers, 8 percent of alkylene phenol polyvinyl ether, 6 percent of calcium dodecyl benzene sulfonate, 5 percent of benzene-80, 2 percent of alkyl naphthalene, 5 percent of ferrocene, 4 percent of methane nitrate or dinitrotoluene and 4 percent of isopropyl alcohol. The formula has the advantages that: the formula has reasonable proportioning, advanced technological method, low product price and high stability, and capability of being mixed with ordinary diesel oil when used.
Description
Technical field
The present invention relates to a kind of prescription of diesel oil emulsification, the invention belongs to a kind of Emulsification of Fuel Oil preparation and utilisation technology in chemical industry, the energy.
Background technology
Present domestic diesel oil short supply, on the high side, stability is low, and the content height of oxynitride, oxysulfide and flue dust in the flue gas of burning back is badly in need of a kind of energy that can substitute diesel oil and is occurred.Existing diesel oil " fuel-water emulsifying " technology is exactly a fuel economy oil, reduce and consume, the advanced power-saving technology of environment protection standard, our country researched and developed and uses its technology intermittently from the sixties, but because multiple factor does not become effective energy-conservation form.
Summary of the invention
Technical problem to be solved by this invention provides a kind of reasonable ratio, processing method advanced person, and product price is low, stability is high, can mix the prescription of the diesel oil emulsification that uses with ordinary diesel oil.
The present invention solves the problems of the technologies described above the prescription that the technical scheme that is adopted is this diesel oil emulsification, its prescription characteristics are: be made up of diesel oil, water and additive, wherein, the weight percent of each component is: diesel oil 65%-95%, water 35%-5%, and the amount of additive is the thousandth of water and diesel oil gross weight; By weight percentage, additive is made up of the stearic Soxylat A 25-7 of 35% sorbitan list, 12% sorbitan monostearate, 13% polyoxyethylene sorbitol Triolein, 6% ethylene acrylate copolymer, 8% alkylene phenol polyvinyl ether, 6% calcium dodecylbenzene sulphonate, department's benzene-80 of 5%, 2% alkylnaphthalene, 5% ferrocene, 4% nitric acid methane or the Virahol of dinitrotoluene (DNT) and 4%.
Additive ph value of the present invention is neutral, and viscosity is 300-120 pascal in the time of 0-40 degree centigrade.
The particle of water of the present invention is less than 2.5 microns, and distributive law is more than 95%.
The present invention compares with prior art and has the following advantages and effect: the invention solves present domestic diesel oil short supply, energy problem on the high side.The present invention can mix use with ordinary diesel oil, every physical and chemical index is all similar with natural diesel oil, and the finished product oil in water emulsion is creamy white, the ph value is neutral, can not corrode body, body is had no side effect, can be-10 ℃ to 45 ℃ normal uses, and has high stability, possess catalysis, combustion-supporting effect, the finished product oil in water emulsion is higher than 30 days stationary phase, and alternative diesel oil uses on industrial machinery, generating set, shipping vehicle etc.And can reduce smoke intensity more than 40%, the exhaust emissions obnoxious flavour descends 30%.Improve efficiency of combustion, thereby reach the environmental protection purpose.The formulation ratio of each component is reasonable, and preparation technology is reasonable in design.
Embodiment
The present invention is described in further detail below in conjunction with embodiment, and following examples are explanation of the invention and the present invention is not limited to following examples.
Embodiment 1
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 80 kilograms diesel oil, the additive of 20 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 2
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 78 kilograms diesel oil, the additive of 22 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 3
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 65 kilograms diesel oil, the additive of 35 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 4
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 70 kilograms diesel oil, the additive of 30 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 5
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 88 kilograms diesel oil, the additive of 12 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 6
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 95 kilograms diesel oil, the additive of 5 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 7
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 93 kilograms diesel oil, the additive of 7 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 8
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 67 kilograms diesel oil, the additive of 33 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 9
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 74 kilograms diesel oil, the additive of 26 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 10
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 90 kilograms diesel oil, the additive of 10 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 11
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 84 kilograms diesel oil, the additive of 16 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
Embodiment 12
The preparation process of additive of the present invention has been described with the lower section:
Get 35 kilograms the stearic Soxylat A 25-7 of sorbitan list, 12 kilograms sorbitan monostearate, 13 kilograms polyoxyethylene sorbitol Triolein, 6 kilograms ethylene acrylate copolymer, 8 kilograms alkylene phenol polyvinyl ether, 6 kilograms calcium dodecylbenzene sulphonate, 5 kilograms alkylnaphthalene, 5 kilograms ferrocene, 4 kilograms nitric acid methane and 4 kilograms the Virahol of department's benzene-80,2 kilogram, mix to stir and make 100 kilograms additive, standby.
The preparation process of diesel oil emulsification of the present invention has been described with the lower section:
With 92 kilograms diesel oil, the additive of 8 kilograms water and 0.1 kilogram mixes, and uses mulser to cut emulsification 40 minutes, prepares 100.1 kilograms of diesel oil emulsifications.This diesel oil emulsification surpasses 30 days at normal temperatures stationary phase, is creamy white, and the ph value is neutral.
In above embodiment, the diesel oil emulsification that obtains can mix use with ordinary diesel oil.
Example:
Diesel oil emulsification of the present invention uses on many buses of Xiamen public transport company, compares with ordinary diesel oil, and rate of economizing gasoline reaches more than 10%, and exhaust emissions all is better than diesel oil.
Claims (3)
1, a kind of prescription of diesel oil emulsification, the prescription feature is: be made up of diesel oil, water and additive, wherein, the weight percent of each component is: diesel oil 65%-95%, water 35%-5%, the amount of additive is the thousandth of water and diesel oil gross weight; By weight percentage, additive is made up of the stearic Soxylat A 25-7 of 35% sorbitan list, 12% sorbitan monostearate, 13% polyoxyethylene sorbitol Triolein, 6% ethylene acrylate copolymer, 8% alkylene phenol polyvinyl ether, 6% calcium dodecylbenzene sulphonate, department's benzene-80 of 5%, 2% alkylnaphthalene, 5% ferrocene, 4% nitric acid methane or the Virahol of dinitrotoluene (DNT) and 4%.
2, the prescription of diesel oil emulsification according to claim 1 is characterized in that: described additive ph value is for neutral, and viscosity is 300-120 pascal in the time of 0-40 degree centigrade.
3, the prescription of diesel oil emulsification according to claim 1 is characterized in that: the particle of described water is less than 2.5 microns, and distributive law is more than 95%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007100696501A CN101328425A (en) | 2007-06-22 | 2007-06-22 | Formula of emulsified diesel oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007100696501A CN101328425A (en) | 2007-06-22 | 2007-06-22 | Formula of emulsified diesel oil |
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| Publication Number | Publication Date |
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| CN101328425A true CN101328425A (en) | 2008-12-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNA2007100696501A Pending CN101328425A (en) | 2007-06-22 | 2007-06-22 | Formula of emulsified diesel oil |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101967410A (en) * | 2009-07-27 | 2011-02-09 | 赵全文 | Cooking fuel oil |
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2007
- 2007-06-22 CN CNA2007100696501A patent/CN101328425A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101967410A (en) * | 2009-07-27 | 2011-02-09 | 赵全文 | Cooking fuel oil |
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Application publication date: 20081224 |