CN1070675A - Regenerative liquid fuel and processing method - Google Patents
Regenerative liquid fuel and processing method Download PDFInfo
- Publication number
- CN1070675A CN1070675A CN 92104485 CN92104485A CN1070675A CN 1070675 A CN1070675 A CN 1070675A CN 92104485 CN92104485 CN 92104485 CN 92104485 A CN92104485 A CN 92104485A CN 1070675 A CN1070675 A CN 1070675A
- Authority
- CN
- China
- Prior art keywords
- liquid fuel
- catalyzer
- regenerative liquid
- water
- clean
- 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
- 239000000446 fuel Substances 0.000 title claims abstract description 26
- 239000007788 liquid Substances 0.000 title claims abstract description 19
- 230000001172 regenerating effect Effects 0.000 title claims abstract description 13
- 238000003672 processing method Methods 0.000 title claims abstract description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 11
- 230000001737 promoting effect Effects 0.000 claims abstract description 10
- 150000001875 compounds Chemical class 0.000 claims abstract description 7
- 239000002304 perfume Substances 0.000 claims abstract description 7
- 239000002904 solvent Substances 0.000 claims abstract description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 14
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- -1 clean-out system Substances 0.000 claims description 10
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- 239000003054 catalyst Substances 0.000 claims description 7
- 239000004323 potassium nitrate Substances 0.000 claims description 7
- 235000010333 potassium nitrate Nutrition 0.000 claims description 7
- 229960000935 dehydrated alcohol Drugs 0.000 claims description 6
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 claims description 4
- 239000004317 sodium nitrate Substances 0.000 claims description 4
- 235000010344 sodium nitrate Nutrition 0.000 claims description 4
- 229940001516 sodium nitrate Drugs 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 3
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 3
- 239000001273 butane Substances 0.000 claims description 3
- 239000003995 emulsifying agent Substances 0.000 claims description 3
- 150000002191 fatty alcohols Chemical class 0.000 claims description 3
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 3
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 claims description 3
- 235000011118 potassium hydroxide Nutrition 0.000 claims description 3
- 239000012286 potassium permanganate Substances 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims description 3
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 3
- 239000013543 active substance Substances 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 235000019439 ethyl acetate Nutrition 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 6
- 239000003502 gasoline Substances 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 5
- 150000001298 alcohols Chemical class 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 125000001997 phenyl group Chemical class [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 abstract 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 4
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 4
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 229960000583 acetic acid Drugs 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000012362 glacial acetic acid Substances 0.000 description 2
- MUMZUERVLWJKNR-UHFFFAOYSA-N oxoplatinum Chemical compound [Pt]=O MUMZUERVLWJKNR-UHFFFAOYSA-N 0.000 description 2
- 229910003446 platinum oxide Inorganic materials 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Images
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
Regenerative liquid fuel and processing method.The present invention relates to prepare the method for regenerative liquid fuel, it mainly solves the problem that adopts benzene class material and relatively large gasoline in the existing liquid fuel, the purpose of this invention is to provide a kind of is the domestic fuel of carrier with water and alcohols material, effect by catalyzer and promoting agent, make water molecules be decomposed a part, and under the effect of mutual solvent, strengthen water and pure mutual solubility, to reach the raising calorific value, reduce cost, produce the regenerative liquid fuel that does not have pollution.The thick methyl alcohol of the present invention accounts for 55-75%, and water accounts for 23-40%, and catalyzer accounts for 2-5% and promoting agent, clean-out system, mutual solvent, and perfume compound accounts for 0.1%, and its calorific value is at 8000 kilocalorie/kilograms.
Description
The present invention relates to prepare the method for regenerative liquid fuel, more specifically saying so a kind of is the method that main body is produced liquid fuel with water and alcohol matter.
Before the present invention carries, Chinese patent on March 29th, 89 disclosed a kind of civil liquid fuel (number of patent application 87103037.3), this invention provides the mixture of being made up of toluene, gasoline, alcohols and additive, alcohols material wherein, accounted for suitable proportion as thick methyl alcohol, added about 20% gasoline simultaneously and made vaporization agent, to improve its scintillation degree.However, this mixed fluid fuel is the civilian following deficiency that has, the one, and technology is complicated, and the cost height; The 2nd, owing to the gasoline that adds about 20%, the user in use has unsafe factor to exist; The 3rd, benzene class material discharges obnoxious flavour in combustion processes, influence the healthy of people.
The object of the present invention is to provide a kind of is the civil liquid fuel of carrier with water and alcohols material, effect by catalyzer and promoting agent, make water molecules be decomposed a part, and can strengthen water and pure mutual solubility, to reach the raising calorific value, reduce cost, produce the reproducibility new forms of energy that do not have pollution.
Realizing that concrete scheme of the present invention is, as main raw material, is main add composition with water with thick methyl alcohol, is equipped with little amount of catalyst and trace active agent, clean-out system, and perfume compound and mutual solvent are mixed and made into.Its proportioning of composition in the liquid fuel of the present invention: be thick methyl alcohol by weight percentage: 55～75%, water: 23～40%; Catalyzer: 2～5%; Promoting agent, clean-out system, perfume compound and mutual solubility total amount account for 0.1%, wherein, catalyzer is mixed by SODIUMNITRATE, saltpetre, potassium hydroxide, sodium hydroxide, ethyl acetate, dehydrated alcohol to be produced, also ethyl acetate wherein can be removed, replace, also saltpetre can be removed by formicester acetate and micro-light benzine, by nitrocalcite, Vanadium Pentoxide, glacial acetic acid and platinum oxide trace replace.Promoting agent of the present invention is polyoxyethylene groups, polyoxyethylene Fatty Alcohol(C12-C14 and C12-C18) and butane, and perfume compound is aromatic alcohol, and clean-out system is the automobile oil pipe clean-out system, and mutual solvent is potassium permanganate, potassium bichromate and emulsifier BP.
Its technology of regenerative liquid fuel of the present invention is methyl alcohol and promoting agent to be stirred produce ignition dope, catalyst mix is added entry again, then ignition dope and the catalyzer of producing added aqueous solution, add mutual solubility again and stir, promptly get regenerative liquid fuel.Wherein churning time is 5 minutes, 500 rev/mins of stirring velocitys, and stirred pot can adopt gold-plating formula jar, slurry formula jar and air-flowing type jar.
Superiority of the present invention is:
1, the present invention directly makes water as deputy combustion fluid component, greatly reduces cost, and objectionable impurities is significantly less than national standard in the waste gas of burning back;
2, the present invention is a main raw material with thick methyl alcohol, and the exploitation of thick methyl alcohol is used, and has alleviated the pressure of supply and demand of petroleum products greatly;
3, catalyzer of the present invention proportion in fuel is very little, and the source is abundant, and is cheap, can not involve introducing to the market of fuel because of its supply restriction;
4, the present invention guides domestic cooking fuel into, can replenish coal gas, the deficiency in short supply of liquefied gas supply the market, and it is smokelessly nontoxic, does not explode, canned convenience, safety.
5, production technique of the present invention is simple, less investment, and instant effect is very easily introduced to the market;
6, to 10000 kilocalorie/kilograms, as adopting the vortex burner kitchen range, the calorie utilization ratio can reach 86% to calorie of the present invention at 7500 kilocalorie/kilograms, and temperature exceeds about 150 ℃, has strengthened the decomposition amount of water.
7, the present invention and Xu Rongsheng slip-stick artist's patented invention " separator " is used, and can become diesel oil on behalf of fuel and the secondary fuel of automobile, saves gasoline 30%, has a extensive future.
Accompanying drawing of the present invention is a process flow sheet, provides several groups of embodiment provided by the invention according to technical process.
Example one:
Thick methyl alcohol: 75%(self moisture 10%)
Water: 23%;
Catalyst formulation: 2% wherein,
Sell ammonium 0.2% saltpetre 0.2% potassium hydroxide 0.2%
Sodium hydroxide 0.2% ethyl acetate 0.4% dehydrated alcohol 0.8%
Potassium permanganate: micro solution 300CC
Promoting agent: polyoxyethylene groups 1000: 0.5
Total water content: 30.5%
Calorie: 7500 kilocalorie/kilograms
Example two:
Thick methyl alcohol: 60%(comprise self moisture 10%)
Water: 37%
Catalyst formulation: 3% wherein,
SODIUMNITRATE 0.3%, saltpetre 0.3%, potassium hydroxide 0.3%
Sodium hydroxide 0.3% formicester acetate 0.4% light benzine 0.4%
Dehydrated alcohol 1%
In proportion: aromatic alcohol 1000: 0.5
Automobile oil pipe clean-out system (commodity) 1000: 1
Polyoxyethylene Fatty Alcohol(C12-C14 and C12-C18) 1000: 0.5
Potassium bichromate micro solution 300CC
Calorific value: 8500 kilocalorie/kilograms
Total water content: 43%
Example three
Thick methyl alcohol: 55%(comprise self moisture 10%)
Water: 40%
Catalyst formulation: 5%
Saltpetre 0.5% nitrocalcite 0.5% potassium hydroxide 0.5%
Sodium hydroxide 0.5% Vanadium Pentoxide 0.5% glacial acetic acid 1%
Dehydrated alcohol 1.5% platinum oxide trace
Automobile oil pipe clean-out system (commodity) 1000: 1
Aromatic alcohol 1000: 0.5
Butane 1000: 1
Emulsifier BP 1000: 0.5
Caloic 10000 kilocalorie/kilograms
Contain water inventory: 45.5%
Claims (5)
1, the thick methyl alcohol of a kind of usefulness is as main raw material, with water is the main composition that adds, be equipped with little amount of catalyst and trace active agent, clean-out system, perfume compound and mutual solvent mix the regenerative liquid fuel of producing, and it is characterized in that its proportioning of composition in the described liquid fuel, be by weight percentage, thick methyl alcohol: 55-75%, water: 23-40%, catalyzer: 2-5%, promoting agent, clean-out system, perfume compound and mutual solvent total amount account for 0.1%.
2, a kind of processing method of producing regenerative liquid fuel, it is characterized in that methyl alcohol mixed with promoting agent to stir producing ignition dope, catalyst mix is added entry again, then ignition dope and the catalyzer of producing added aqueous solution, add mutual solvent again and stir.
3, regenerative liquid fuel according to claim 1 is characterized in that catalyzer by SODIUMNITRATE, saltpetre, and potassium hydroxide, sodium hydroxide, ethyl acetate, dehydrated alcohol mix to be produced.
4, regenerative liquid fuel according to claim 1 is characterized in that promoting agent is a polyoxyethylene groups, polyoxyethylene Fatty Alcohol(C12-C14 and C12-C18) and butane, perfume compound is aromatic alcohol, clean-out system is the automobile oil pipe clean-out system, and mutual solubility is potassium permanganate, potassium bichromate and emulsifier BP.
5, according to claim 1,3 described regenerative liquid fuel, it is characterized in that catalyzer can be by SODIUMNITRATE, saltpetre, potassium hydroxide, sodium hydroxide, formicester acetate, micro-light benzine and dehydrated alcohol are produced.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92104485 CN1070675A (en) | 1992-06-12 | 1992-06-12 | Regenerative liquid fuel and processing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92104485 CN1070675A (en) | 1992-06-12 | 1992-06-12 | Regenerative liquid fuel and processing method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1070675A true CN1070675A (en) | 1993-04-07 |
Family
ID=4940828
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92104485 Pending CN1070675A (en) | 1992-06-12 | 1992-06-12 | Regenerative liquid fuel and processing method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1070675A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003064923A1 (en) * | 2002-02-01 | 2003-08-07 | Pan, Weibiao | Fuel with the decomposition and combination of water and combustor using the fuel |
| CN102358853A (en) * | 2011-09-16 | 2012-02-22 | 邓群英 | Novel environmental protection and energy saving biological alcohol oil |
| CN102408924A (en) * | 2011-10-12 | 2012-04-11 | 陈金城 | Double-base liquid fuel and preparation method thereof |
| CN102504888A (en) * | 2011-11-14 | 2012-06-20 | 殷孟波 | Composite clean liquid fuel and production method thereof |
| CN102625825A (en) * | 2009-08-13 | 2012-08-01 | 穆哈默·法礼·宾·撒亚 | Methanol-based liquid fuel |
| CN102660334A (en) * | 2012-05-14 | 2012-09-12 | 王国平 | Biological alcohol oil and preparation method thereof |
| CN103403130A (en) * | 2010-11-25 | 2013-11-20 | 甘恩能源有限公司 | Method and fuel for powering a compression ignition engine |
| CN104764004A (en) * | 2015-04-09 | 2015-07-08 | 郎君羊 | Seawater decomposition and combustion device |
-
1992
- 1992-06-12 CN CN 92104485 patent/CN1070675A/en active Pending
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003064923A1 (en) * | 2002-02-01 | 2003-08-07 | Pan, Weibiao | Fuel with the decomposition and combination of water and combustor using the fuel |
| CN102625825A (en) * | 2009-08-13 | 2012-08-01 | 穆哈默·法礼·宾·撒亚 | Methanol-based liquid fuel |
| US9447724B2 (en) | 2010-11-25 | 2016-09-20 | Gane Energy & Resources Pty Ltd. | Fuel and process for powering a compression ignition engine |
| US10815441B2 (en) | 2010-11-25 | 2020-10-27 | Gane Energy & Resources Pty Ltd. | Fuel and process for powering a compression ignition engine |
| CN103403130A (en) * | 2010-11-25 | 2013-11-20 | 甘恩能源有限公司 | Method and fuel for powering a compression ignition engine |
| US10023818B2 (en) | 2010-11-25 | 2018-07-17 | Gane Energy & Resources Pty Ltd. | Process for powering a compression ignition engine and fuel therefor |
| CN102358853A (en) * | 2011-09-16 | 2012-02-22 | 邓群英 | Novel environmental protection and energy saving biological alcohol oil |
| CN102408924A (en) * | 2011-10-12 | 2012-04-11 | 陈金城 | Double-base liquid fuel and preparation method thereof |
| CN102408924B (en) * | 2011-10-12 | 2014-05-07 | 陈金城 | Double-base liquid fuel and preparation method thereof |
| CN102504888A (en) * | 2011-11-14 | 2012-06-20 | 殷孟波 | Composite clean liquid fuel and production method thereof |
| CN102504888B (en) * | 2011-11-14 | 2014-02-19 | 殷孟波 | Production method of composite clean liquid fuel |
| CN102660334A (en) * | 2012-05-14 | 2012-09-12 | 王国平 | Biological alcohol oil and preparation method thereof |
| CN104764004A (en) * | 2015-04-09 | 2015-07-08 | 郎君羊 | Seawater decomposition and combustion device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102260554B (en) | Microemulsified biodiesel and preparation technique thereof | |
| CN1070675A (en) | Regenerative liquid fuel and processing method | |
| CN102373101B (en) | High-cleaning aged fuel | |
| CN102827654A (en) | Cleaning fuel for vehicle | |
| CN1281724C (en) | Highly efficient fuel accelerant and method for preparing the same | |
| CN102643686B (en) | Compound-type environmentally-friendly fuel oil solution and preparation method thereof | |
| CN107892961B (en) | Preparation method of environment-friendly gasoline additive | |
| CN1167773C (en) | Environmental protection energy saving methanol gasoline | |
| CN1446886A (en) | Light hydrocarbon emulsion fuel and its manufacturing method | |
| EP0265850B1 (en) | Combustion aids | |
| CN101302451A (en) | Environment-protecting clean diesel | |
| CN108913232B (en) | Alcohol-based fuel and preparation method thereof | |
| CN1101661A (en) | Compound gasoline | |
| CN1087934A (en) | Civil liquid fuel | |
| AU2021104095A4 (en) | Hydrogen-oxygen liquid used for fuel catalysis | |
| CN111621343A (en) | Environment-friendly renewable fuel oil formula | |
| CN103450950B (en) | A kind of high-efficiency environment-friendly fuel oil and preparation method thereof | |
| CN1206329C (en) | Metal welding and cutting ether-hydrocarbon gas | |
| CN1931970A (en) | Additive for gasoline and diesel oil and its prepn process | |
| CN110835559A (en) | New energy composite diesel oil | |
| CN1288042A (en) | Catalyst for heavy oil mixed with water | |
| CN113322108A (en) | Micro-emulsified diesel oil | |
| CN1243086C (en) | Environmental protection gasoline additive | |
| CN108658773B (en) | Method for preparing cetane number improver by using nano oxide in auxiliary manner | |
| CN115161082A (en) | Environment-friendly alcohol-based fuel and preparation method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C01 | Deemed withdrawal of patent application (patent law 1993) | ||
| WD01 | Invention patent application deemed withdrawn after publication |