CN1884441A - Method for promoting light oil yield of atmospheric and vacuum distillation of petroleum oil - Google Patents
Method for promoting light oil yield of atmospheric and vacuum distillation of petroleum oil Download PDFInfo
- Publication number
- CN1884441A CN1884441A CN 200610026856 CN200610026856A CN1884441A CN 1884441 A CN1884441 A CN 1884441A CN 200610026856 CN200610026856 CN 200610026856 CN 200610026856 A CN200610026856 A CN 200610026856A CN 1884441 A CN1884441 A CN 1884441A
- Authority
- CN
- China
- Prior art keywords
- oil
- atmospheric
- vacuum distillation
- yield
- petroleum
- 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
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention relates the method for improving atmospheric and vacuum distillation light oil productivity. The method comprises the following step: adding the 0.001-0.1wt% addition agent with colophony into crude oil in atmospheric and vacuum distillation tower. The addition agent comprises 50-80% colophony and 50-20% organic solvent. The pH is 7.0-7.5. The organic solvent comprises ethanol or cellosolve or ethyl propyl acetone or acetate cellosolve. The method can be used in oil-extraction plant, and the light oil productivity is improved by 1.5-2.3wt%.
Description
Technical field
The present invention relates to a kind of method that improves light oil yield of atmospheric and vacuum distillation of petroleum oil, is a kind of improvement technology in the refining of petroleum, can improve in the atmospheric and vacuum distillation of petroleum process productive rate than light constituent effectively.Belong to fuel and energy technology field.
Background technology
Therefore oil will face exhaustion in first half in this century, how improve its cut and go out rate and more and more seem important and urgent.Oil fuel processing at first is that crude oil is distilled time processing through ordinary decompression column, lighting end gasoline, kerosene, diesel oil in the crude oil are isolated, then more residual residual oil branch at the bottom of last running and the tower is entered devices such as catalytic cracking and coking and carry out secondary processing, it is converted into light-end products.In a word, every possible means, make the maximum benefit of crude oil performance the taking-up as much as possible of the light ends in the crude oil.
Chinese patent CN1030250A is with containing the petroleum catalytic cracking recycle stock of aromatic hydrocarbon or catalytic slurry as additive, the weight ratio of pressing 0.5-10% adds, can improve the vacuum distillate yield, but its addition is bigger, and be catalytic cracking recycle oil and catalytic slurry, these all are valuable petrochemical materials.In addition, this invention can only be used to have the refinery of catalytic cracking unit, and only limits to vacuum distillation range.
Summary of the invention
The objective of the invention is at the deficiencies in the prior art, a kind of method that improves light oil yield of atmospheric and vacuum distillation of petroleum oil is provided, the light oil yield in the time of can effectively improving crude distillation, and the cost that drops into is very low.
For realizing this purpose, the present invention has adopted a kind of additive that contains the rosin natural organic matter, is added to carry out normal reduced crude distillation in the crude oil when oil refining, can increase than the light constituent productive rate.
Components of additives of the present invention and weight percent are: the rosin natural organic matter of 50-80%, and the organic solvent of 50-20%, the pH value is 7.0~7.5.Wherein said organic solvent can be ethanol, ethylene glycol diethyl ether, ethyl propyl ketone, ethylene glycol ether etc.
Additive of the present invention is added in the crude oil of atmospheric and vacuum distillation of petroleum tower, and the add-on of additive is 0.001~0.1% of a crude oil feeding amount weight, is preferably 0.003~0.08%.In 0.001~0.1% add-on scope, the physical and chemical index of the normal vacuum distillate of gained does not have considerable change.
Additive of the present invention mainly contains the rosin natural organic matter, is natural organic nontoxic product, belongs to Green Product, poison exponent LD50 〉=950mg/kg (mouse).
The present invention adds additive in crude oil, the light oil yield in the time of can effectively improving crude distillation, and the cost that drops into is very low.Need not change simultaneously the structure of existing oil refining apparatus, a need add a pipeline in the process furnace ingress and gauge gets final product.
Method of the present invention can be used for all refinerys, comprises on normal pressure, the vacuum distillation apparatus.The weight percent of the light oil yield the when additive that the present invention adopts can make normal reduced crude distill increases by 1.5~2.3%, has significant substantial effect.
Embodiment
Below by specific embodiment technical scheme of the present invention is further described.
Embodiment 1:
Carry out on-the-spot normal pressure true boiling point distillation test with Daqing crude oil, components of additives and weight percent are: rosin 60%, ethyl propyl ketone 40%.The add-on of additive is 0.003% of a former weight of oil, and the gained test-results is as described in Table 1.
Table 1
Temperature range ℃ | Blank cut yield w% | Doping 0.003% cut yield w% | The cut yield changes w% |
<200 | 2.23 | 2.66 | +0.43 |
200~300 | 3.29 | 3.77 | +0.48 |
300~365 | 3.58 | 4.20 | +0.62 |
Add up to :+1.53% |
By table 1 data as can be known, improve normal pressure light oil yield 1.53%.
Embodiment 2:
With the Nile, Middle East crude oil: the crude oil proportioning is (Wenchang: Ban Qienasi)=85: 15, the true boiling point distillation of often reducing pressure test, distillation apparatus is the semi-automatic true boiling point distillation instrument that German FISCHER company makes, and this distillation apparatus meets ASTM2892 and ASTM5236 standard specifications.Components of additives and weight percent are: rosin 50%, ethylene glycol ether 50%.The add-on of additive is 0.004% of a former weight of oil, and the gained test-results is as shown in table 2.
Table 2
Temperature range ℃ | Blank cut yield w% | Doping 0.004% cut yield w% | The cut yield changes w% |
<200 | 16.77 | 17.10 | +0.33 |
200~365 | 42.54 | 43.73 | +1.19 |
356~540 | 73.22 | 74.08 | +0.86 |
Add up to :+2.38 |
By table 2 data as can be known, improve atmospheric tower light oil yield 1.52w%; Improve vacuum distillation tower light oil yield 0.86w%; Add up to light oil yield to increase 2.38w%.
Embodiment 3:
Crude oil and test apparatus are with example 2.Components of additives and weight percent are: rosin: 70%, and ethylene glycol diethyl ether 30%.The add-on of additive is 0.003% of a former weight of oil, and the gained test-results is as shown in table 3.
Temperature range ℃ | Blank cut yield w% | Doping 0.003% cut yield w% | The cut yield changes w% |
<200 | 16.77 | 16.93 | +0.16 |
200~365 | 42.54 | 43.48 | +0.94 |
365~540 | 73.22 | 73.98 | +0.76 |
Add up to :+1.86 |
By table 3 data as can be known, improve atmospheric tower light oil yield 1.10w%, improve vacuum distillation tower light oil yield 0.76w%, add up to light oil yield to increase 1.86w%.
Claims (3)
1, a kind of method that improves light oil yield of atmospheric and vacuum distillation of petroleum oil is characterized in that the additive that will contain rosin is added in the crude oil of atmospheric and vacuum distillation of petroleum tower, and the add-on of additive is 0.001~0.1% of a crude oil feeding amount weight; Described components of additives and weight percent are: the rosin natural organic matter of 50-80%, and the organic solvent of 50-20%, the pH value is 7.0~7.5.
2, according to the method for the raising light oil yield of atmospheric and vacuum distillation of petroleum oil of claim 1, it is characterized in that described organic solvent is ethanol, ethylene glycol diethyl ether, ethyl propyl ketone or ethylene glycol ether.
3, according to the method for the raising light oil yield of atmospheric and vacuum distillation of petroleum oil of claim 1, the add-on that it is characterized in that described additive is 0.003~0.08% of a crude oil feeding amount weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2006100268561A CN100348695C (en) | 2006-05-25 | 2006-05-25 | Method for promoting light oil yield of atmospheric and vacuum distillation of petroleum oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2006100268561A CN100348695C (en) | 2006-05-25 | 2006-05-25 | Method for promoting light oil yield of atmospheric and vacuum distillation of petroleum oil |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1884441A true CN1884441A (en) | 2006-12-27 |
CN100348695C CN100348695C (en) | 2007-11-14 |
Family
ID=37582748
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2006100268561A Expired - Fee Related CN100348695C (en) | 2006-05-25 | 2006-05-25 | Method for promoting light oil yield of atmospheric and vacuum distillation of petroleum oil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN100348695C (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102041028A (en) * | 2009-10-13 | 2011-05-04 | 中国石油化工股份有限公司 | Composite for strengthening crude oil distillation and application thereof |
CN101475826B (en) * | 2008-11-21 | 2012-07-18 | 华东理工大学 | Atmospheric vacuum distillation process for light crude oil |
CN104419443A (en) * | 2013-09-09 | 2015-03-18 | 中国石油化工股份有限公司 | Hydrocarbon oil distillation method |
CN104830366A (en) * | 2015-05-13 | 2015-08-12 | 湖南长岭石化科技开发有限公司 | Method for enhancing crude oil distillation pull-out rate and improving residual oil properties |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58167683A (en) * | 1982-03-29 | 1983-10-03 | Nippon Zeon Co Ltd | Extractive distillation |
CN1005062B (en) * | 1987-03-16 | 1989-08-30 | 中国石油化工总公司洛阳石油化工工程公司 | Method for increasing yield of distillate oil of petroleum vacuum distillation |
CN1106857A (en) * | 1994-12-12 | 1995-08-16 | 上思县化工综合厂 | Process for producing machinery oil using rosin waste residue |
-
2006
- 2006-05-25 CN CNB2006100268561A patent/CN100348695C/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101475826B (en) * | 2008-11-21 | 2012-07-18 | 华东理工大学 | Atmospheric vacuum distillation process for light crude oil |
CN102041028A (en) * | 2009-10-13 | 2011-05-04 | 中国石油化工股份有限公司 | Composite for strengthening crude oil distillation and application thereof |
CN102041028B (en) * | 2009-10-13 | 2013-08-14 | 中国石油化工股份有限公司 | Composite for strengthening crude oil distillation and application thereof |
CN104419443A (en) * | 2013-09-09 | 2015-03-18 | 中国石油化工股份有限公司 | Hydrocarbon oil distillation method |
CN104419443B (en) * | 2013-09-09 | 2016-01-20 | 中国石油化工股份有限公司 | A kind of hydrocarbon ils distillating method |
CN104830366A (en) * | 2015-05-13 | 2015-08-12 | 湖南长岭石化科技开发有限公司 | Method for enhancing crude oil distillation pull-out rate and improving residual oil properties |
Also Published As
Publication number | Publication date |
---|---|
CN100348695C (en) | 2007-11-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102786981B (en) | Catalytically cracked oil utilizes novel process | |
CN101218327A (en) | Light oil fuel | |
CN100348695C (en) | Method for promoting light oil yield of atmospheric and vacuum distillation of petroleum oil | |
CN101691499A (en) | Method for producing heavy environment-friendly rubber oil | |
CN102585902B (en) | Environment-friendly rubber oil and preparation method thereof | |
CN101475826A (en) | Atmospheric vacuum distillation process for light crude oil | |
CN1974734A (en) | Vehicle gasoline for replacing petroleum fuel and its prepn process | |
US9193926B2 (en) | Fuel compositions and methods based on biomass pyrolysis | |
CN106190277A (en) | A kind of method that biomass fuel is prepared in nano material catalytic cracking | |
CN104611005B (en) | A kind of process increasing production coker gas oil | |
CN1214092C (en) | Gasoline-oxygenate blend oil | |
CN108913233A (en) | A kind of cleaning motor petrol blend component oil and its preparation method and application | |
CN111978976A (en) | Method for improving distillate oil yield of atmospheric and vacuum distillation unit | |
CN102329662A (en) | Method for blending diesel oil with high cetane number by using aviation kerosene refined from gas condensate | |
CN103320165B (en) | Method for producing environmentally-friendly rubber oil through using inferior cycloalkyl heavy wax oil, and environmentally-friendly rubber oil prepared therethrough | |
US20240034948A1 (en) | Tall diesel composition | |
Latypova et al. | Natural hydrocarbonic raw material as a source of sulphides receiving | |
CN102807891A (en) | System and method for processing condensate oil | |
CN109852465A (en) | A kind of production technology of naphthenic base lubricating oil | |
CN103320163B (en) | Method for producing environmentally-friendly rubber oil through using inferior cycloalkyl heavy wax oil, and environmentally-friendly rubber oil prepared therethrough | |
RU2039791C1 (en) | Method for production of winter-grade diesel fuel | |
CN102311781A (en) | Delayed coking unit | |
CN111647425B (en) | Diesel oil and continuous production method thereof | |
CN114106867B (en) | Method for reducing sulfur content in carbon five fraction | |
WO2019097199A1 (en) | Process for obtaining a renewable hydrocarbon stream suitable as a component of gasoline formulations, renewable hydrocarbon stream, and gasoline formulation |
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 | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071114 Termination date: 20100525 |