CN1786115A - Catalyst for producing light fuel oil using oily rock as raw material and its method - Google Patents
Catalyst for producing light fuel oil using oily rock as raw material and its method Download PDFInfo
- Publication number
- CN1786115A CN1786115A CN 200510126073 CN200510126073A CN1786115A CN 1786115 A CN1786115 A CN 1786115A CN 200510126073 CN200510126073 CN 200510126073 CN 200510126073 A CN200510126073 A CN 200510126073A CN 1786115 A CN1786115 A CN 1786115A
- Authority
- CN
- China
- Prior art keywords
- oil
- clorafin
- raw material
- fuel oil
- catalyzer
- 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)
- Catalysts (AREA)
Abstract
The present invention relates to a catalyst for producing light fuel oil by using oil-bearing rock and its method. Said catalyst raw material composition includes (by wt%) 20-35% of cobalt naphthenate, 30-40% of ethylene glycol monomethyl ether, 3-5% of acidified active clay, 10-20% of stearin and 20-37% of chlorinated paraffin. The described chlorinated paraffin is industrial chlorinated paraffin 70. Said invention also provides the concrete method and steps of utilizing said catalyst to produce light fuel oil.
Description
Technical field
The invention belongs to the petroleum refining technology field, relating in particular to a kind of is the Catalyst And Method of raw material production light-weight fuel oil with the oil-bearing rock.
Background technology
Oil-bearing rock is that scabland forms naturally, and it is a kind of organic rock that bituminous matter and inorganic ore form by volcanic explosion, and reserves are abundant.Oil-bearing rock is different from oil, is difficult to its large batch of light-weight fuel oil that is processed into traditional petroleum refining technology, and its product can only be as road and structure material, and utility value is low.China is consumption of petroleum big country, and how utilizing oil-bearing rock processing to obtain light-weight fuel oil, to replace diesel oil be the major issue of comprehensive utilization petroleum resources.
At present, enterprise adopts the method for hydrogenation under the high-temperature and high-pressure conditions both at home and abroad, distills out light-weight fuel oil from the powdery oil-bearing rock, not only has the production safety problem but also increase production cost.
Summary of the invention
The purpose of this invention is to provide a kind of is raw material with the oil-bearing rock, and normal pressure distills the Catalyst And Method that obtains light-weight fuel oil down, does not need hydrogenation technique, and the light-weight fuel oil that obtains can substitute 0# diesel oil, reduces production costs greatly simultaneously.
The technical solution used in the present invention is as follows:
A kind of is the catalyzer of raw material production light-weight fuel oil with the oil-bearing rock, the weight percent that it is characterized in that this catalyzer raw material consists of: cobalt naphthenate 20～35%, ethylene glycol monomethyl ether 30～40%, acid activated bentonite 3～5%, stearin 10～20%, clorafin 20～37%, described clorafin are technical grade clorafin 70.
The weight percent of this catalyzer raw material is formed can be cobalt naphthenate 25%, ethylene glycol monomethyl ether 40%, and acid activated bentonite 5%, stearin 10%, clorafin 20%, described clorafin are technical grade clorafin 70.
Described acid activated bentonite is commercially available industrial raw material, and its preparation method is to be 98% sulfuric acid and carclazyte by weight 98% sulfuric acid with concentration: carclazyte=physical mixed obtained in 1: 49.
A kind of is the method for raw material production light-weight fuel oil with the oil-bearing rock, it is characterized in that comprising being prepared as follows step:
(1) oil-bearing rock is processed into powdery, with catalyzer by weight oil-bearing rock: catalyzer=95～97: 3～5 mix and obtain mixture, described catalyzer is to be mixed by following materials of weight proportions to obtain: cobalt naphthenate 20～35%, ethylene glycol monomethyl ether 30～40%, acid activated bentonite 3～5%, stearin 10～20%, clorafin 20～37%, clorafin wherein are technical grade clorafin 70;
(2) mixture that step (1) is obtained is sent into water distilling apparatus, and under normal pressure, be warmed up to 550 ℃ in 3 hours and distill, output dry gas above water distilling apparatus, the middle part obtains light-weight fuel oil.
Cobalt naphthenate, ethylene glycol monomethyl ether, acid activated bentonite, stearin and clorafin raw material that this catalyzer uses are the commercially available prod.For example there is Changfeng Chemical Plant, Shanghai in the manufacturer of described cobalt naphthenate, the Shenyang Application Technology Experiment Factory, imperial chemical plant is avenged in Changzhou, Shenyang ship board chemical industry company limited, there is Fushun oil factory in the manufacturer of described ethylene glycol monomethyl ether, Shenyang Petroleum-Chemial Plant, Shanghai reagent three factories, there is Huangshan Baiyue Activated Clay Co., Ltd. in the manufacturer of described atlapulgite, Beipiao City Red Hill carclazyte factory, second chemical plant, Tiandong County, Guangxi, Yang County, Shaanxi atlapulgite factory, there is Guangzhou Long Sha company limited in the manufacturer of described glyceryl stearate, Hangzhou Jin Cheng auxiliary agent company limited, Henan Zhengtong Chemical Co., Ltd., there are gold dollar chemical plant, Gongyi City in Zhangjiagang oil and fat chemical two factories, the manufacturer of described clorafin 70, Foochow chemical company limited, Nanjing rosy clouds waffle worker company limited, Jingjiang great river, Jiangsu chemical industry company limited.
Five kinds of raw materials of this catalyzer can obtain through physical mixed, catalyzer and be processed into the powdered oil-bearing rock and mix in proportion after, at normal pressure with do not add under the condition of hydrogen, in 3 hours, the mixture in the water distilling apparatus is heated to 550 ℃ gradually, the initial boiling point of light-weight fuel oil is 200 ℃, and final boiling point is 550 ℃.The collection temperature of dry gas is 450～480 ℃, can be used as reusing of energy source, at water distilling apparatus bottom output coke.
Of the present invention is the catalyzer of raw material production light-weight fuel oil with the oil-bearing rock, at normal pressure with do not add that the super large molecular chain disconnects and reorganization between 13～22 in the following oil-bearing rock of condition of hydrogen, decolour simultaneously, the light-weight fuel oil long storage physical and chemical index of producing is not rebounded.Cobalt naphthenate in the catalyzer can shorten the reaction times when catalytic distillation, improve product output, ethylene glycol monomethyl ether can improve the mutual solubility and the long term storage stability of its product light-weight fuel oil, reach the service requirements of diesel oil, acid activated bentonite can be the light Fuel oil decolorization, take off flavor, deodorization, the light-weight fuel oil acid number that makes not to be gone up, color reversion not, limpid transparent, stay in grade, long quality-guarantee period, glyceryl stearate has froth breaking, disperse, thickening power, make the light-weight fuel oil exquisiteness, lubricated, satisfy diesel oil viscosity, density, the requirement of lubricity, the solid clorafin is a fire retardant, makes the light Fuel oil flash that distills out reach the diesel oil safety index.
Beneficial effect of the present invention is, this catalyzer is a raw material with chemical industry product commonly used, can effectively reduce with the oil-bearing rock is the cost of raw material production light-weight fuel oil and the every performance index that improve the light Fuel oil production, is that raw material uses the method for this Catalyst Production light-weight fuel oil to break traditions to need under the condition of high pressure, hydrogenation technique the method for distillation light-weight fuel oil from oil-bearing rock with the oil-bearing rock.Employing with oil-bearing rock and catalyst mix after at normal pressure, do not add under the condition of hydrogen and distill out light-weight fuel oil, its product performance are good, alternative 0# diesel oil, and production process does not have waste gas, waste water, waste residue generation, and production safety coefficient height, production cost reduces greatly.
Embodiment
The present invention is further illustrated below in conjunction with embodiment, and the percentage ratio among the following embodiment is weight percentage except that specifying.
Embodiment 1 gets the 25kg cobalt naphthenate, the 40kg ethylene glycol monomethyl ether, and the 5kg acid activated bentonite, 10kg glyceryl stearate and 20kg clorafin 70, above-mentioned raw materials is commercially available industrial raw material.Above-mentioned raw materials mixed obtain this catalyzer.
Embodiment 2 gets commercially available cobalt naphthenate 20kg, and ethylene glycol monomethyl ether 30kg, acid activated bentonite 3kg, the glyceryl stearate 20kg and the trade mark are 70 clorafin 27kg.Wherein acid activated bentonite is to be 98% sulfuric acid and carclazyte by weight 98% sulfuric acid with concentration: carclazyte=physical mixed obtained in 1: 49.Above-mentioned five kinds of raw materials are mixed obtain this catalyzer.
Embodiment 3 gets the 20kg cobalt naphthenate, the 30kg ethylene glycol monomethyl ether, and the 3kg acid activated bentonite, 10kg glyceryl stearate and 37kg clorafin 70, above-mentioned raw materials is commercially available industrial raw material.Above-mentioned raw materials mixed obtain this catalyzer.
Embodiment 4 gets commercially available cobalt naphthenate 35kg, and ethylene glycol monomethyl ether 30kg, acid activated bentonite 5kg, the glyceryl stearate 10kg and the trade mark are 70 clorafin 20kg.Wherein acid activated bentonite is to be 98% sulfuric acid and carclazyte by weight 98% sulfuric acid with commercially available concentration: carclazyte=physical mixed obtained in 1: 49.Above-mentioned five kinds of raw materials are mixed obtain this catalyzer.
It is the feedstock production light-weight fuel oil that embodiment 5 produces oil-bearing rock with Sichuan.95kg oil-bearing rock pulverizing back is even with the catalyst mix that 5kg embodiment 1 provides, mixture is sent into and is carried out the normal pressure catalytic distillation in the distillation tower, in 3 hours, the mixture in the distillation tower is heated to 510 ℃ gradually, the initial boiling point of light-weight fuel oil is 200 ℃, final boiling point is 550 ℃, and the collection temperature of dry gas is 450～480 ℃.Obtain dry gas above water distilling apparatus, the middle part obtains light-weight fuel oil, obtains coke in the water distilling apparatus bottom.
Used oil-bearing rock is the oil-bearing rock that produce in Sichuan in this experiment, and its technical indicator sees Table 1.
The every technical indicator of table 1 Sichuan oil-bearing rock
| Project name | Technical indicator |
| Density g/cm 3 | 1.7～2.6 |
| Colourity | ≤5 |
| Hardness (Mohs) | 4 |
| Oil length (butt) % | 26.0～34.0 |
The weight output capacity of light-weight fuel oil is about 30% in this experiment, and dry gas yied is about 16%, and the weight of coke productive rate is 54%.Every technical indicator of this light Fuel oil production and 0# diesel oil standard comparative result see Table 2.
The light-weight fuel oil of table 2 output of the present invention and the contrast of 0# diesel oil technical indicator
| Project name | The lightweight combustion that embodiment 5 obtains | 0# diesel oil |
| Density (20 ℃) g/cm 3 | 0.84～0.85 | 0.84～0.86 |
| Kinematic viscosity (20 ℃) mm 2/s | 4 | 3～8 |
| Condensation point ℃ | -3 | 0 |
| Colourity (being not deeper than) | 4 | 3.5 |
| Mechanical impurity % | Do not have | Do not have |
| Water soluble acid or alkali | Do not have | Do not have |
| Copper corrosion (50 ℃, 3 hours) | 1 | 1 |
| Ash % | ＜0.01 | ＜0.01 |
| Moisture % | Vestige | Vestige |
As can be seen from the above table, the every technical indicator that adopts catalyzer provided by the invention and prepare the light-weight fuel oil that the method for light-weight fuel oil obtains all reaches or meets the standard of 0# diesel oil, can substitute the use of 0# diesel oil fully.Its safe preparation process, simple, production cost is well below existing High Temperature High Pressure catalytic distillation method.
It is the feedstock production light-weight fuel oil that embodiment 6 produces oil-bearing rock with Xinjiang autonomous region.The catalyst mix that 97kg oil-bearing rock and 3kg embodiment 2 are provided is even, mixed material is sent into and is carried out the normal pressure catalytic distillation in the distillation tower, in 3 hours, the mixture in the distillation tower is warming up to 550 ℃ gradually, the initial boiling point of light-weight fuel oil is 200 ℃, final boiling point is 550 ℃, and the collection temperature of dry gas is 450～480 ℃.Obtain dry gas above water distilling apparatus, the middle part obtains light-weight fuel oil, obtains coke in the water distilling apparatus bottom.
The weight output capacity of light-weight fuel oil is about 25% in this experiment, and dry gas yied is about 15%, and the weight of coke productive rate is 60%.After testing, every technical indicator of this light Fuel oil production all can reach or satisfy the 0# diesel oil standard.
Claims (4)
1. one kind is the catalyzer of raw material production light-weight fuel oil with the oil-bearing rock, the raw material weight per-cent that it is characterized in that this catalyzer consists of: cobalt naphthenate 20～35%, ethylene glycol monomethyl ether 30～40%, acid activated bentonite 3～5%, stearin 10～20%, clorafin 20～37%, described clorafin are technical grade clorafin 70.
2. according to claim 1 is the catalyzer of raw material production light-weight fuel oil with the oil-bearing rock, the raw material weight per-cent that it is characterized in that this catalyzer consists of: cobalt naphthenate 25%, ethylene glycol monomethyl ether 40%, acid activated bentonite 5%, stearin 10%, clorafin 20%, described clorafin are technical grade clorafin 70.
According to claim 1 and 2 described be the catalyzer of raw material production light-weight fuel oil with the oil-bearing rock, it is characterized in that described acid activated bentonite is commercially available industrial raw material, its preparation method is to be 98% sulfuric acid and carclazyte by weight 98% sulfuric acid with concentration: carclazyte=physical mixed obtained in 1: 49.
4. one kind is the method for raw material production light-weight fuel oil with the oil-bearing rock, it is characterized in that comprising being prepared as follows step:
(1) oil-bearing rock is processed into powdery, with catalyzer by weight oil-bearing rock: catalyzer=95～97: 3～5 mix and obtain mixture, described catalyzer is to be mixed by following materials of weight proportions to obtain: cobalt naphthenate 20～35%, ethylene glycol monomethyl ether 30～40%, acid activated bentonite 3～5%, stearin 10～20%, clorafin 20～37%, clorafin wherein are technical grade clorafin 70;
(2) mixture that step (1) is obtained is sent into water distilling apparatus, and under normal pressure, be warmed up to 550 ℃ in 3 hours and distill, output dry gas above water distilling apparatus, the middle part obtains light-weight fuel oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101260736A CN1326974C (en) | 2005-11-30 | 2005-11-30 | Catalyst for producing light fuel oil using oily rock as raw material and its method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101260736A CN1326974C (en) | 2005-11-30 | 2005-11-30 | Catalyst for producing light fuel oil using oily rock as raw material and its method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1786115A true CN1786115A (en) | 2006-06-14 |
| CN1326974C CN1326974C (en) | 2007-07-18 |
Family
ID=36783729
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005101260736A Expired - Fee Related CN1326974C (en) | 2005-11-30 | 2005-11-30 | Catalyst for producing light fuel oil using oily rock as raw material and its method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1326974C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101962559A (en) * | 2010-11-05 | 2011-02-02 | 曹志德 | Method for preparing light fuel oil by using oil shale ore |
| CN103464179A (en) * | 2013-09-24 | 2013-12-25 | 吉林大学 | Catalyst used for extracting shale oil from oil shale and application method of catalyst |
| WO2016000456A1 (en) * | 2014-06-30 | 2016-01-07 | 湖南万通科技有限公司 | Method for preparing light oil |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1178823A (en) * | 1996-10-08 | 1998-04-15 | 伍伟国 | Process for oil refinery from waste material of used petroleum product |
| US6835861B2 (en) * | 2000-08-10 | 2004-12-28 | Rj Lee Group, Inc. | Low energy method of pyrolysis of hydrocarbon materials such as rubber |
| AU2001283221A1 (en) * | 2000-08-10 | 2002-02-25 | Rj Leegroup, Inc. | Low energy method of pyrolysis of hydrocarbon materials such as rubber |
| CN1261545C (en) * | 2003-12-09 | 2006-06-28 | 中国石油化工集团公司 | Combined process for heavy oil upgrading |
-
2005
- 2005-11-30 CN CNB2005101260736A patent/CN1326974C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101962559A (en) * | 2010-11-05 | 2011-02-02 | 曹志德 | Method for preparing light fuel oil by using oil shale ore |
| CN103464179A (en) * | 2013-09-24 | 2013-12-25 | 吉林大学 | Catalyst used for extracting shale oil from oil shale and application method of catalyst |
| CN103464179B (en) * | 2013-09-24 | 2015-04-15 | 吉林大学 | Catalyst used for extracting shale oil from oil shale and application method of catalyst |
| WO2016000456A1 (en) * | 2014-06-30 | 2016-01-07 | 湖南万通科技有限公司 | Method for preparing light oil |
| CN105273749A (en) * | 2014-06-30 | 2016-01-27 | 湖南万通科技有限公司 | Preparation method for light oil |
| RU2662218C1 (en) * | 2014-06-30 | 2018-07-25 | Хунань Ваньтун Текнолоджи Ко., Лтд. | Method of light oil producing |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1326974C (en) | 2007-07-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105778987B (en) | A kind of production method of biodiesel and bunker fuel oil | |
| CN102796547B (en) | Biological asphalt, biological asphalt composition and preparation method | |
| CN1473907A (en) | Process for producing biological diesel oil | |
| CN1326974C (en) | Catalyst for producing light fuel oil using oily rock as raw material and its method | |
| CN101967412B (en) | Compound additive and vehicle alcohol-ether compound gasoline | |
| CN1260325C (en) | Catalyst and method for producing light fuel oil | |
| CN101215481A (en) | Liquid fuel for boiler and preparation method thereof | |
| CN102408905B (en) | Method for producing petroleum product from waste plastics | |
| CN1318551C (en) | Additive for producing high-grade gasoline using 90# gasoline and the high grade gasoline | |
| CN101157868A (en) | Method for producing low freezing point biodiesel by employing waste animal and vegetable oil coupling and special device | |
| CN100386282C (en) | Preparation method of concrete high efficiency water reducer | |
| CN101074391A (en) | Method and catalyst for producing biological diesel oil by high-acid value grease | |
| CN1401743A (en) | Ethanol and mixed alcohol gasoline | |
| CN1315995C (en) | Additive for producing high-grade gasoline using naphtha and the high grade gasoline | |
| CN102079990B (en) | Processing method of shale oil | |
| CN112725012A (en) | Production method of etherified oxygenated deep-processing waste plastic oil | |
| CN101050376B (en) | Additive for producing biologic diesel oil directly from grease of animals and plants, and biologic diesel oil prepared by the additive | |
| CN1821349A (en) | Method for producing biological diesel oil from leftover of edible oil process | |
| CN214881301U (en) | Device for producing gasoline and kerosene additive raw material by using dephenolized phenol oil | |
| CN1283765C (en) | Method for producing biological clean fuel | |
| CN102242016A (en) | Method for producing biodiesel with palm fatty acid | |
| CN101225331A (en) | Environment-protection energy-saving methanol/ethanol gasoline modifier | |
| CN100371427C (en) | Bio-fuel-oil and process for making same | |
| CN107043544A (en) | A kind of biomass pitch and preparation method | |
| CN103756791A (en) | Synthetic method of biodiesel |
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 | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Easy clean energy technology development Co Ltd Assignor: Cao Zhide Contract fulfillment period: 2009.5.21 to 2025.11.29 contract change Contract record no.: 2009990000685 Denomination of invention: Catalyst for producing light fuel oil using oily rock as raw material and its method Granted publication date: 20070718 License type: exclusive license Record date: 2009.6.23 |
|
| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.5.21 TO 2025.11.29; CHANGE OF CONTRACT Name of requester: YIGAO CLEAN ENERGY TECHNOLOGY DEVELOPMENT CO., LTD Effective date: 20090623 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070718 Termination date: 20161130 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |