CN106221787A - A kind of preparation method of fuel oil - Google Patents
A kind of preparation method of fuel oil Download PDFInfo
- Publication number
- CN106221787A CN106221787A CN201610701351.4A CN201610701351A CN106221787A CN 106221787 A CN106221787 A CN 106221787A CN 201610701351 A CN201610701351 A CN 201610701351A CN 106221787 A CN106221787 A CN 106221787A
- Authority
- CN
- China
- Prior art keywords
- coal tar
- preparation
- fuel oil
- addition
- reactor
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G53/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
- C10G53/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only
-
- 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
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
-
- 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
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
- C10G2300/802—Diluents
-
- 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
- C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
- C10L2230/04—Catalyst added to fuel stream to improve a reaction
-
- 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
- C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
- C10L2230/14—Function and purpose of a components of a fuel or the composition as a whole for improving storage or transport of the fuel
-
- 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
- C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
- C10L2230/22—Function and purpose of a components of a fuel or the composition as a whole for improving fuel economy or fuel efficiency
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The present invention relates to the preparation method of a kind of fuel oil, including: coal tar, diluent and catalyst mixing, through natural subsidence and filtration, remove the impurity in heavy oil, it is subsequently adding in reactor and airtight, temperature of reactor is heated to 220 600 DEG C, constant temperature 10 20 minutes, product being taken out from reactor after being down to room temperature, add solvent naphtha and additive, the addition of described solvent naphtha is the 10% of coal tar quality, the addition of described additive is the 10% of coal tar quality, carry out separated again, take the fraction of 80 280 DEG C, obtain fuel oil.Fuel oil prepared by the present invention have energy-efficient, calorific value is high, environmental protection, safe and nontoxic, smokeless, corrosion-free, do not stay residual liquid, sanitation and hygiene, easily transport, easily store and low price feature.
Description
Technical field
The present invention relates to the preparation method of a kind of fuel oil, belong to chemistry new energy field.
Background technology
Existing situation is that energy crisis is on the rise and consumption of petroleum amount is continuously increased, the cost of high-grade fuel oil and price
Escalating, people more wish to replace high-quality fuel oil with reduced fuel oil.This makes various fuel oil all to heaviness side
To development.
Summary of the invention
The technical problem to be solved is to provide the preparation method of a kind of fuel oil, fuel oil prepared by the present invention
Have energy-efficient, calorific value is high, environmental protection, safe and nontoxic, smokeless, corrosion-free, do not stay residual liquid, sanitation and hygiene, easily transport, easily store up
Deposit and low price feature.
The technical scheme is that the preparation method of a kind of fuel oil, including:
Coal tar, diluent and catalyst mixing, through natural subsidence and filtration, remove the impurity in heavy oil, then add
Enter in reactor and airtight, temperature of reactor is heated to 220-600 DEG C, constant temperature 10-20 minute, produces reaction after being down to room temperature
Thing takes out from reactor, adds solvent naphtha and additive, and the addition of described solvent naphtha is the 10% of coal tar quality, described
The addition of additive is the 10% of coal tar quality, then carries out separated, takes the fraction of 80-280 DEG C, obtains fuel oil.
On the basis of technique scheme, the present invention can also do following improvement.
Further, the addition of described diluent is the 1%-2% of coal tar quality, and described diluent is gasoline, described
The addition of catalyst is the 5%-12% of coal tar quality, and described catalyst is aluminium oxide.
Further, the one during described additive is combustion adjuvant, propellant, anticorrosive.
Further, described combustion adjuvant is black shale, potassium chlorate and Linesless charcoal 5:2:1 in mass ratio composition.
Further, described propellant is that Barium monoxide forms with ethanol 3:2 in mass ratio.
Further, described anticorrosive is sorbic acid.
The invention has the beneficial effects as follows:
Fuel oil prepared by the present invention have energy-efficient, calorific value is high, environmental protection, safe and nontoxic, smokeless, corrosion-free, do not stay
Residual liquid, sanitation and hygiene, easily transport, easily storage and low price feature.
Detailed description of the invention
Principle and feature to the present invention are described below, and example is served only for explaining the present invention, is not intended to limit
Determine the scope of the present invention.
Embodiment 1
A kind of preparation method of fuel oil, including:
Coal tar, diluent and catalyst mixing, through natural subsidence and filtration, remove the impurity in heavy oil, then add
Enter in reactor and airtight, temperature of reactor is heated to 220-600 DEG C, constant temperature 10-20 minute, produces reaction after being down to room temperature
Thing takes out from reactor, adds solvent naphtha and additive, and the addition of described solvent naphtha is the 10% of coal tar quality, described
The addition of additive is the 10% of coal tar quality, then carries out separated, takes the fraction of 80-280 DEG C, obtains fuel oil,
Wherein, the addition of described diluent is the 1%-2% of coal tar quality, and described diluent is gasoline, adding of described catalyst
Entering the 5%-12% that amount is coal tar quality, described catalyst is aluminium oxide.Described additive is combustion adjuvant.Described combustion adjuvant is
Black shale, potassium chlorate and Linesless charcoal 5:2:1 in mass ratio forms.
Embodiment 2
A kind of preparation method of fuel oil, including:
Coal tar, diluent and catalyst mixing, through natural subsidence and filtration, remove the impurity in heavy oil, then add
Enter in reactor and airtight, temperature of reactor is heated to 220-600 DEG C, constant temperature 10-20 minute, produces reaction after being down to room temperature
Thing takes out from reactor, adds solvent naphtha and additive, and the addition of described solvent naphtha is the 10% of coal tar quality, described
The addition of additive is the 10% of coal tar quality, then carries out separated, takes the fraction of 80-280 DEG C, obtains fuel oil,
Wherein, the addition of described diluent is the 1%-2% of coal tar quality, and described diluent is gasoline, adding of described catalyst
Entering the 5%-12% that amount is coal tar quality, described catalyst is aluminium oxide.Described additive is propellant.Described propellant is
Barium monoxide forms with ethanol 3:2 in mass ratio.
Embodiment 3
A kind of preparation method of fuel oil, including:
Coal tar, diluent and catalyst mixing, through natural subsidence and filtration, remove the impurity in heavy oil, then add
Enter in reactor and airtight, temperature of reactor is heated to 220-600 DEG C, constant temperature 10-20 minute, produces reaction after being down to room temperature
Thing takes out from reactor, adds solvent naphtha and additive, and the addition of described solvent naphtha is the 10% of coal tar quality, described
The addition of additive is the 10% of coal tar quality, then carries out separated, takes the fraction of 80-280 DEG C, obtains fuel oil,
Wherein, the addition of described diluent is the 1%-2% of coal tar quality, and described diluent is gasoline, adding of described catalyst
Entering the 5%-12% that amount is coal tar quality, described catalyst is aluminium oxide.Described additive is anticorrosive.Described anticorrosion
Agent is sorbic acid.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all spirit in the present invention and
Within principle, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (6)
1. the preparation method of a fuel oil, it is characterised in that including:
Coal tar, diluent and catalyst mixing, through natural subsidence and filtration, remove the impurity in heavy oil, is subsequently adding anti-
Answer in device and airtight, temperature of reactor be heated to 220-600 DEG C, constant temperature 10-20 minute, be down to after room temperature by product from
Taking out in reactor, add solvent naphtha and additive, the addition of described solvent naphtha is the 10% of coal tar quality, described interpolation
The addition of agent is the 10% of coal tar quality, then carries out separated, takes the fraction of 80-280 DEG C, obtains fuel oil.
Preparation method the most according to claim 1, it is characterised in that the addition of described diluent is coal tar quality
1%-2%, described diluent is gasoline, and the addition of described catalyst is the 5%-12% of coal tar quality, described catalyst
For aluminium oxide.
Preparation method the most according to claim 1, it is characterised in that described additive is combustion adjuvant, propellant, anticorrosion
One in agent.
Preparation method the most according to claim 3, it is characterised in that described combustion adjuvant is black shale, potassium chlorate and wood
Charcoal 5:2:1 in mass ratio forms.
Preparation method the most according to claim 3, it is characterised in that described propellant is Barium monoxide with ethanol in mass ratio
3:2 forms.
Preparation method the most according to claim 3, it is characterised in that described anticorrosive is sorbic acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610701351.4A CN106221787A (en) | 2016-08-19 | 2016-08-19 | A kind of preparation method of fuel oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610701351.4A CN106221787A (en) | 2016-08-19 | 2016-08-19 | A kind of preparation method of fuel oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106221787A true CN106221787A (en) | 2016-12-14 |
Family
ID=57553662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610701351.4A Pending CN106221787A (en) | 2016-08-19 | 2016-08-19 | A kind of preparation method of fuel oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106221787A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101733132A (en) * | 2008-11-12 | 2010-06-16 | 北京清研利华石油化学技术有限公司 | Catalyst system for producing diesel oil and method for producing diesel oil by using system |
| CN102776020A (en) * | 2012-08-08 | 2012-11-14 | 赵世洲 | Safe and environment-friendly oil refining process and device |
-
2016
- 2016-08-19 CN CN201610701351.4A patent/CN106221787A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101733132A (en) * | 2008-11-12 | 2010-06-16 | 北京清研利华石油化学技术有限公司 | Catalyst system for producing diesel oil and method for producing diesel oil by using system |
| CN102776020A (en) * | 2012-08-08 | 2012-11-14 | 赵世洲 | Safe and environment-friendly oil refining process and device |
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| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161214 |
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| RJ01 | Rejection of invention patent application after publication |