CN101538496B - Technology for preparing intermediate-temperature industrial fuel from loose heavy oil - Google Patents
Technology for preparing intermediate-temperature industrial fuel from loose heavy oil Download PDFInfo
- Publication number
- CN101538496B CN101538496B CN2009100370493A CN200910037049A CN101538496B CN 101538496 B CN101538496 B CN 101538496B CN 2009100370493 A CN2009100370493 A CN 2009100370493A CN 200910037049 A CN200910037049 A CN 200910037049A CN 101538496 B CN101538496 B CN 101538496B
- Authority
- CN
- China
- Prior art keywords
- industrial fuel
- oil
- heavy oil
- temperature
- fuel
- 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.)
- Expired - Fee Related
Links
- 239000000295 fuel oil Substances 0.000 title claims abstract description 20
- 239000000446 fuel Substances 0.000 title claims abstract description 19
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000000839 emulsion Substances 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract description 3
- 239000003921 oil Substances 0.000 claims description 10
- 238000003756 stirring Methods 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000000967 suction filtration Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 2
- 239000011259 mixed solution Substances 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 abstract description 4
- 238000009833 condensation Methods 0.000 abstract description 3
- 230000005494 condensation Effects 0.000 abstract description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 abstract 2
- 239000002893 slag Substances 0.000 description 3
- 239000004816 latex Substances 0.000 description 2
- 229920000126 latex Polymers 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 1
- 235000011613 Pinus brutia Nutrition 0.000 description 1
- 241000018646 Pinus brutia Species 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
The invention discloses a technology for preparing intermediate-temperature industrial fuel by using loose heavy oil, which adopts the main technical scheme that: the loose heavy oil is fully mixed with methanol, ethanol and petroleum ether in a blending tank according to a certain proportion, and finally, the uniform emulsion is the intermediate-temperature industrial fuel oil. The invention not only reduces the cost of industrial fuel oil, but also improves the condensation point of the fuel oil so that the fuel oil can be used at low temperature.
Description
Technical field:
The invention belongs to a kind of preparation method of industrial fuel, especially a kind of middle temperature industrial fuel technology with the loose heavy oil preparation.
Technical background:
Current, industrial fuel is main with petroleum slag mainly, and this residual oil exists the cost height, heavy-polluted drawback, and also the also low low temperature of condensation point can not use with regard to being easy to solidify.The birth of pine product and use and to have increased new life to industrial fuel, it not only low the but also fuel value of production cost also be not less than petroleum slag.And, pollute also during burning and reduce relatively, use flowability also good than petroleum slag, be regarded as all well and good industrial fuel.This high-temperature industrial fuel maximum combustion temperature can reach 1000 degree, and total heat can reach 6000 kilocalories.
Summary of the invention:
The object of the present invention is to provide a kind of middle temperature industrial fuel technology with the loose heavy oil preparation, adopting said method has effectively reduced the use cost of industrial fuel, has also reduced the atmospheric pollution that flue dust brings.Improved the flowability that the fuel condensation point is brought simultaneously, made the microthermal climate use of burning normally.This high-temperature industrial fuel maximum combustion temperature can reach 1000 degree, and total heat can reach 6000 kilocalories.This temperature and heat are fit to glass and fire with automotive lacquer etc.
For reaching above-mentioned requirement, technical scheme of the present invention is:
Heavy oil and organic solvent that the distillation of crow oil process proposes behind the light ends organically are combined to form a kind of new middle temperature industrial oil product again.Its process step is:
Heavy oil behind the black oil distillate (3) and 90% above methyl alcohol (4) are mixed in airtight Mixer pot (1) lining by mass ratio 1: 0.2-04 at normal temperature, fully stir back formation latex A; Mix by mass ratio 1: 0.1-0.3 with ethanol (4) more than 85% again and add through stirring into uniform emulsion B; Last and sherwood oil (4) adds airtight Mixer pot back warp according to mass ratio 1: 0.1-0.3 and stirs the uniform emulsion of back formation, and suction filtration (2) obtains middle temperature industrial fuel, gets into fuel oil drum (5) at last and prepares to use.
Description of drawings:
This figure is a process flow sheet of the present invention, and its major equipment constitutes:
1---Mixer pot, 2---suction filter pump, 3---heavy oil oil supply line, 4---solvent is given stockline, and 5---the finished product jar.
Concrete embodiment:
Embodiment one: (heavy oil and the ratio that adds organic solvent)
Heavy oil (3) behind the 100kg crow oil distillate and methyl alcohol (4) more than 90% are mixed in airtight Mixer pot (1) lining by mass ratio 1: 0.3 at normal temperature; Obtain 130kg after fully stirring and get mixed solution; Mix at 1: 0.2 by mass ratio with ethanol (4) more than 85% again and add the uniform mixing liquid that obtains 150kg through stirring; Last and sherwood oil (4) adds airtight Mixer pot back warp according to mass ratio and stirs back formation homogeneous latex emulsion 170kg at 1: 0.2; Suction filtration (2) obtains middle temperature industrial fuel, gets into fuel oil drum (5) at last.
Claims (1)
1. method with temperature industrial fuel in the loose heavy oil preparation is that the heavy oil behind the 100kg crow oil distillate and methyl alcohol more than 90% are mixed in airtight Mixer pot (1) lining by mass ratio 1: 0.3 at normal temperature, fully obtains the 130kg mixed solution after the stirring; Mix at 1: 0.2 by mass ratio with ethanol more than 85% again and add the uniform mixing liquid that obtains 150kg through stirring; Last and sherwood oil adds airtight Mixer pot back warp according to mass ratio and stirs the uniform emulsion 170kg of back formation at 1: 0.2, and suction filtration obtains middle temperature industrial fuel, gets into fuel oil product jar (5) at last and prepares to use;
Temperature industrial fuel maximum combustion temperature reaches 1000 degree in said, and total heat reaches 6000 kilocalories.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100370493A CN101538496B (en) | 2009-02-02 | 2009-02-02 | Technology for preparing intermediate-temperature industrial fuel from loose heavy oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100370493A CN101538496B (en) | 2009-02-02 | 2009-02-02 | Technology for preparing intermediate-temperature industrial fuel from loose heavy oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101538496A CN101538496A (en) | 2009-09-23 |
| CN101538496B true CN101538496B (en) | 2012-04-25 |
Family
ID=41121888
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009100370493A Expired - Fee Related CN101538496B (en) | 2009-02-02 | 2009-02-02 | Technology for preparing intermediate-temperature industrial fuel from loose heavy oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101538496B (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101220301A (en) * | 2008-01-31 | 2008-07-16 | 浙江赛孚能源科技有限公司 | Methanol gasoline fuel and process for fuel production |
| CN101338226A (en) * | 2008-08-08 | 2009-01-07 | 高三林 | Environment protection type liquid fuel and method for preparing same |
-
2009
- 2009-02-02 CN CN2009100370493A patent/CN101538496B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101220301A (en) * | 2008-01-31 | 2008-07-16 | 浙江赛孚能源科技有限公司 | Methanol gasoline fuel and process for fuel production |
| CN101338226A (en) * | 2008-08-08 | 2009-01-07 | 高三林 | Environment protection type liquid fuel and method for preparing same |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101538496A (en) | 2009-09-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1916130A (en) | Clean gasoline and prepartion method | |
| CN104449894A (en) | Methanol gasoline air-lock inhibitor | |
| CN1931972A (en) | Process of producing natural gas substitute with dimethyl ether as material | |
| CN101538496B (en) | Technology for preparing intermediate-temperature industrial fuel from loose heavy oil | |
| CN101538495B (en) | Technology for preparing high-temperature industrial fuel from loose heavy oil | |
| CN101619249B (en) | Alcohol-based fuel modifier, enhancer, alcohol-based liquid fuel after modification and enhancement and production process thereof | |
| CN102268305A (en) | Environmentally-friendly methanol diesel oil for automobile and preparation method thereof | |
| CN105779035A (en) | Clean and environment-friendly diesel oil | |
| CN102127477B (en) | Petrochemical additive and preparation method thereof | |
| CN101538494B (en) | Technology for preparing low-temperature industrial fuel by using loose heavy oil | |
| CN101580745B (en) | Technology for preparing high-temperature clean industrial fuel from pine-stump light oil | |
| CN102876403A (en) | Alcohol ether diesel fuel for new-energy-resource vehicle | |
| CN101580746B (en) | Intermediate temperate cleaning industrial fuel technology prepared from pine-stump light oil | |
| CN106520218B (en) | Ecological fuel oil and preparation method thereof | |
| CN101570705B (en) | Technology for preparing low temperature clean industrial fuel from pine-stump light oil | |
| CN103571547A (en) | Method for preparing ethanol-diesel oil mixed fuel | |
| CN108148640A (en) | A kind of alcohol-based fuel formula and its preparation process | |
| CN102719284A (en) | Renewable swill-cooked dirty fuel oil | |
| CN101144038A (en) | Nano composite gasoline | |
| CN104263431A (en) | Automobile fuel composition | |
| CN100393855C (en) | Composite fuel for automobile engine | |
| CN103627444A (en) | Novel industrial fuel and preparation method therefor | |
| CN103074128A (en) | Water/hydrocarbon emulsion fuel | |
| CN106635192A (en) | Preparation method of alcohol-based fuel | |
| CN101705123A (en) | Environment friendly and energy-saving heavy oil additive |
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 | ||
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 523000, room five, building 508, Jinhai building, Dongcheng District Tong Road, Dongguan, Guangdong Patentee after: Wang Jiaxing Address before: Wushi Village Primary School in Dongguan city of Dongcheng District province Guangdong road 523000 Lane 1 No. 6 main mountain Patentee before: Wang Jiaxing |
|
| ASS | Succession or assignment of patent right |
Owner name: NANTONG HUASHAN INDUSTRY CO., LTD. Free format text: FORMER OWNER: WANG JIAXING Effective date: 20130813 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 523000 DONGGUAN, GUANGDONG PROVINCE TO: 226300 NANTONG, JIANGSU PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130813 Address after: 226300 No. 14, Tong Hai Road, Tongzhou District Development Zone, Jiangsu, Nantong Patentee after: Huashan Nantong Industrial Co., Ltd. Address before: 523000, room five, building 508, Jinhai building, Dongcheng District Tong Road, Dongguan, Guangdong Patentee before: Wang Jiaxing |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20170509 Address after: 24 Nantong province high tech Zone, Tongzhou District Province, the village of the bridge group of the group of 226300, Patentee after: Liwang Chemical (Nantong) Co., Ltd. Address before: 226300 No. 14, Tong Hai Road, Tongzhou District Development Zone, Jiangsu, Nantong Patentee before: Huashan Nantong Industrial Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120425 Termination date: 20180202 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |