CN101067094B - Preparation method of microemulsion diesel oil - Google Patents
Preparation method of microemulsion diesel oil Download PDFInfo
- Publication number
- CN101067094B CN101067094B CN2007100285345A CN200710028534A CN101067094B CN 101067094 B CN101067094 B CN 101067094B CN 2007100285345 A CN2007100285345 A CN 2007100285345A CN 200710028534 A CN200710028534 A CN 200710028534A CN 101067094 B CN101067094 B CN 101067094B
- Authority
- CN
- China
- Prior art keywords
- diesel oil
- speed
- rpm
- stir
- time
- 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
- 239000002283 diesel fuel Substances 0.000 title claims abstract description 47
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 239000004530 micro-emulsion Substances 0.000 title abstract description 7
- 238000003756 stirring Methods 0.000 claims abstract description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 claims abstract description 18
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims abstract description 9
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims abstract description 9
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims abstract description 9
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000005642 Oleic acid Substances 0.000 claims abstract description 9
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims abstract description 9
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims abstract description 9
- 239000002904 solvent Substances 0.000 claims abstract description 9
- 239000000839 emulsion Substances 0.000 claims abstract description 6
- 239000011259 mixed solution Substances 0.000 claims abstract description 6
- 238000002485 combustion reaction Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 239000000446 fuel Substances 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 238000013517 stratification Methods 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 230000005923 long-lasting effect Effects 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
- Colloid Chemistry (AREA)
Abstract
本发明涉及了一种微乳化柴油的制备方法,该制备方法是将0号柴油与油酸混合,在水浴中中速搅拌一段时间,充分溶解后均速滴加水,搅拌一段时间后缓慢滴加乙醇胺并继续搅拌使混合液充分乳化,待乳化液变清澈后再加入200号溶剂油搅拌一段时间后得到微乳化柴油,本制备方法工艺简单,所制备的微乳化柴油表观均匀,光亮透明,稳定性高,具有成本低等优点。The invention relates to a preparation method of micro-emulsified diesel oil. The preparation method is to mix No. 0 diesel oil and oleic acid, stir in a water bath at a medium speed for a period of time, and after fully dissolving, add water dropwise at an even speed, and then slowly add in drops after stirring for a period of time Ethanolamine and continue stirring to fully emulsify the mixed solution. After the emulsion becomes clear, add No. 200 solvent oil and stir for a period of time to obtain micro-emulsion diesel oil. The preparation method is simple, and the prepared micro-emulsion diesel oil is uniform in appearance, bright and transparent, High stability, low cost and other advantages.
Description
技术领域technical field
本发明涉及一种微乳化柴油的制备方法。The invention relates to a preparation method of microemulsion diesel oil.
背景技术Background technique
进入新世纪以来,世界上很多的国家受到全球化的影响,已经进入了一个高速增长的新时期。在这种情况下,全世界对能源的需求量日益增大,能源的供给可持续性以及环境问题成为当今全球最关注的问题。Since the beginning of the new century, many countries in the world have been affected by globalization and have entered a new period of rapid growth. Under such circumstances, the world's demand for energy is increasing day by day, and the sustainability of energy supply and environmental issues have become the most concerned issues in the world today.
因此解决能源短缺的难题在现阶段就必须“开源”和“节能”并举。目前世界各国虽在“开源”上做出重大努力,但与上世纪石油开采的盛景大相径庭了,所以近年来特别着力于“节能”方面的工作:一是从技术上对内燃机加以改进,提高效率:其二是改善燃油品质,提高燃烧效率。在柴油中加入与其成分相匹配的添加剂以改善其燃烧状况,则是一种简便易行且行之有效的节能措施。乳化柴油作为一种代用燃料技术,既可以减少燃料消耗又可以控制排放,在节油和改善环境污染中已显示出其优越性,而被普遍重视和竟相探索,并获得很大的发展。虽然目前很多科研部门和科技工作者在柴油掺水的领域取得了显著的成绩,柴油掺水的技术也已发展到相当水平,然而,至今乳化柴油并没有得到广泛的推广和应用,其原因主要有:Therefore, to solve the problem of energy shortage at this stage, "open source" and "energy saving" must be developed simultaneously. Although all countries in the world have made great efforts in "open source" at present, they are quite different from the grand scene of oil exploitation in the last century. Therefore, in recent years, they have focused on the work of "energy saving": one is to improve the internal combustion engine technically. Efficiency: The second is to improve fuel quality and combustion efficiency. It is a simple and effective energy-saving measure to add additives matching its composition to diesel to improve its combustion conditions. As an alternative fuel technology, emulsified diesel oil can reduce fuel consumption and control emissions. It has shown its superiority in saving fuel and improving environmental pollution. It has been widely valued and explored, and has achieved great development. Although many scientific research departments and scientific and technological workers have made remarkable achievements in the field of diesel oil mixed with water, and the technology of diesel oil mixed with water has also developed to a considerable level, however, emulsified diesel oil has not been widely promoted and applied so far. The main reasons are have:
1、乳化柴油的研究还没有完全深入,形成机理还没有完全清楚,如今也还没有找到一套完整清晰的理论和标准来评价乳化柴油的质量优劣。1. The research on emulsified diesel has not been fully in-depth, the formation mechanism has not been fully understood, and a complete and clear set of theories and standards to evaluate the quality of emulsified diesel has not yet been found.
2、乳化柴油本身存在稳定性问题,乳化柴油的分散相分散程度不均匀,长期保存会出现混浊、析水、分层等现象,影响大面积的推广。2. The emulsified diesel has stability problems. The dispersion of the dispersed phase of the emulsified diesel is uneven, and long-term storage will cause turbidity, water separation, and stratification, which will affect the promotion of large areas.
3、在以往的柴油乳化过程中,为了达到乳化柴油的长期稳定而油与水不分层的目的,必须添加用量较大的乳化剂,由于现今乳化剂价格仍然较高,大量使用必然使柴油的成本提高,所以减少使用高成本的添加剂仍然需要关注的一个重要问题。3. In the previous diesel emulsification process, in order to achieve the long-term stability of the emulsified diesel oil without delamination of oil and water, it is necessary to add a large amount of emulsifier. Since the price of emulsifier is still high today, a large amount of use will inevitably make diesel oil The cost increases, so reducing the use of high-cost additives remains an important concern.
4、添加其他添加剂提高乳化柴油的燃烧值,进一步降低柴油使用带来的环境污染的问题也越来越重要。4. It is more and more important to add other additives to increase the combustion value of emulsified diesel oil and further reduce the environmental pollution caused by the use of diesel oil.
5、乳化柴油掺水燃烧方式都存在自身的弱点,无法解决低负荷工作平稳和高负荷降低排放的矛盾,含水燃烧机理还没有完全清楚,会出现点火困难等情况;影响大规模的推广使用。5. The combustion method of emulsified diesel oil mixed with water has its own weaknesses. It cannot solve the contradiction between stable operation at low load and low emission at high load.
发明内容Contents of the invention
本发明的目的:针对目前乳化柴油存在的问题,通过对其制备方法的研究,改善乳化柴油在制备过程中乳化效果,使乳化柴油的粒径趋于均匀,从而制备出具有稳定性能较高,燃烧效果好,持久保持光亮澄清,外观与普通柴油相同的实用型微乳化柴油。The purpose of the present invention: aiming at the problems existing in the current emulsified diesel oil, through the research on its preparation method, the emulsification effect of the emulsified diesel oil in the preparation process is improved, the particle size of the emulsified diesel oil tends to be uniform, thereby preparing a product with high stability, It is a practical micro-emulsion diesel oil with good combustion effect, long-lasting bright and clear appearance, and the same appearance as ordinary diesel oil.
本发明是通过以下技术方案来实现的:The present invention is achieved through the following technical solutions:
一种微乳化柴油的制备方法是将0#柴油与油酸混合,在25~45℃左右的水浴中以800~1200转/分钟的转速搅拌10~30分钟,充分溶解后均速滴入水,速度控制在每秒1~3滴,滴加完毕后保持800~1400转/分钟的转速继续搅拌10~20分钟,再以每秒1~3滴速度缓慢滴加乙醇胺,调低搅拌速度至300~800转/分钟,搅拌较长一段时间使混合液充分乳化,待乳化液变清澈后加入200#溶剂油搅拌一段时间后得到微乳化柴油。A preparation method of micro-emulsified diesel oil is to mix 0# diesel oil with oleic acid, stir in a water bath at 25-45°C at a speed of 800-1200 rpm for 10-30 minutes, and drop it into water at an even speed after fully dissolving , the speed is controlled at 1-3 drops per second. After the dropwise addition, keep the speed of 800-1400 rpm and continue stirring for 10-20 minutes, then slowly add ethanolamine dropwise at a rate of 1-3 drops per second, and reduce the stirring speed to 300-800 rev/min, stirring for a long period of time to fully emulsify the mixed solution, add 200# solvent oil after the emulsion becomes clear and stir for a period of time to obtain micro-emulsion diesel oil.
本发明的有益效果是:The beneficial effects of the present invention are:
本制备工艺所制备出的乳化柴油分散程度好,分散相微粒半径均匀,这有利于改善乳化柴油在燃烧过程中所产生的“微爆”效果和“二次雾化”效果,使乳化柴油燃烧更完全,达到提高燃烧效果的目的。The emulsified diesel oil prepared by this preparation process has a good degree of dispersion, and the particle radius of the dispersed phase is uniform, which is conducive to improving the "micro-explosion" effect and "secondary atomization" effect of the emulsified diesel oil in the combustion process, so that the emulsified diesel oil burns More complete, to achieve the purpose of improving the combustion effect.
本制备工艺方法简单,适合大型生产应用。采用该制备工艺制备出的实用型微乳化柴油具有自身不发生分层,稳定性能较高,持久保持光亮澄清不分层,外观与普通柴油相同。而且制备出来的乳化柴油燃烧性能好,具有节能减污效果。The preparation method is simple and suitable for large-scale production applications. The practical micro-emulsion diesel oil prepared by the preparation process has the characteristics of no stratification itself, high stability, long-lasting brightness, clarity and no stratification, and the same appearance as ordinary diesel oil. Moreover, the prepared emulsified diesel oil has good combustion performance and has the effect of saving energy and reducing pollution.
具体实施方式Detailed ways
下面实施例是对本发明进一步证明,本发明不限于此。The following examples further prove the present invention, and the present invention is not limited thereto.
实施例一:Embodiment one:
将0#柴油与油酸混合,在30℃左右的水浴中以900转/分钟的转速搅拌30分钟,充分溶解后均速滴入水,速度控制在每秒1~2滴,滴加完毕后保持900转/分钟的转速继续搅拌20分钟,再以每秒1~2滴速度缓慢滴加乙醇胺,调低搅拌速度至600转/分钟,搅拌较长一段时间使混合液充分乳化,待乳化液变清澈后加入200#溶剂油搅拌一段时间后得到微乳化柴油。Mix 0# diesel oil with oleic acid, stir in a water bath at about 30°C at a speed of 900 rpm for 30 minutes, and drop it into water at an even speed after fully dissolving, with the speed controlled at 1-2 drops per second. Keep stirring at a speed of 900 rpm and continue stirring for 20 minutes, then slowly add ethanolamine dropwise at a rate of 1 to 2 drops per second, reduce the stirring speed to 600 rpm, and stir for a long period of time to fully emulsify the mixture. After becoming clear, add 200# solvent naphtha and stir for a period of time to obtain micro-emulsified diesel oil.
实施例二:Embodiment two:
将0#柴油与油酸混合,在35℃左右的水浴中以1200转/分钟的转速搅拌20分钟,充分溶解后均速滴入水,速度控制在每秒1~2滴,滴加完毕后保持1200转/分钟的转速继续搅拌15分钟,再以每秒1~2滴速度缓慢滴加乙醇胺,调低搅拌速度至600转/分钟,搅拌较长一段时间使混合液充分乳化,待乳化液变清澈后加入200#溶剂油搅拌一段时间后得到微乳化柴油。Mix 0# diesel oil with oleic acid, stir in a water bath at about 35°C at a speed of 1200 rpm for 20 minutes, and drop it into water at an even speed after fully dissolving. Keep stirring at a speed of 1200 rpm and continue stirring for 15 minutes, then slowly add ethanolamine dropwise at a rate of 1-2 drops per second, reduce the stirring speed to 600 rpm, and stir for a long period of time to fully emulsify the mixture. After becoming clear, add 200# solvent naphtha and stir for a period of time to obtain micro-emulsified diesel oil.
实施例三:Embodiment three:
将0#柴油与油酸混合,在40℃左右的水浴中以1400转/分钟的转速搅拌10分钟,充分溶解后均速滴入水,速度控制在每秒2~3滴,滴加完毕后保持1400转/分钟的转速继续搅拌10分钟,再以每秒2~3滴速度缓慢滴加乙醇胺,调低搅拌速度至500转/分钟,搅拌较长一段时间使混合液充分乳化,待乳化液变清澈后加入200#溶剂油搅拌一段时间后得到微乳化柴油。Mix 0# diesel oil with oleic acid, stir in a water bath at about 40°C at a speed of 1400 rpm for 10 minutes. Keep stirring at a speed of 1400 rpm and continue stirring for 10 minutes, then slowly add ethanolamine dropwise at a rate of 2 to 3 drops per second, reduce the stirring speed to 500 rpm, and stir for a long period of time to fully emulsify the mixture. After becoming clear, add 200# solvent naphtha and stir for a period of time to obtain micro-emulsified diesel oil.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2007100285345A CN101067094B (en) | 2007-06-12 | 2007-06-12 | Preparation method of microemulsion diesel oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2007100285345A CN101067094B (en) | 2007-06-12 | 2007-06-12 | Preparation method of microemulsion diesel oil |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101067094A CN101067094A (en) | 2007-11-07 |
CN101067094B true CN101067094B (en) | 2010-06-09 |
Family
ID=38879794
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2007100285345A Expired - Fee Related CN101067094B (en) | 2007-06-12 | 2007-06-12 | Preparation method of microemulsion diesel oil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101067094B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102344838B (en) * | 2011-09-02 | 2013-12-11 | 彭千 | Preparation method for emulsified diesel oil |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1113937A (en) * | 1994-06-03 | 1995-12-27 | 关恩泽 | Hydro-diesel oil and its producing method |
US5746783A (en) * | 1994-03-30 | 1998-05-05 | Martin Marietta Energy Systems, Inc. | Low emissions diesel fuel |
CN1410514A (en) * | 2002-09-29 | 2003-04-16 | 季忠 | Production technology and formulation of microemulsion fuel oil |
CN1422934A (en) * | 2001-12-06 | 2003-06-11 | 徐涛 | Micro emulsion fuel production process and formula |
CN1422935A (en) * | 2001-12-07 | 2003-06-11 | 关恩泽 | Micro emulsion diesel fuel |
CN1542100A (en) * | 2003-11-07 | 2004-11-03 | 陆翼德 | Emulsified diesel oil and preparation method thereof |
DE10315900A1 (en) * | 2003-04-08 | 2004-11-18 | Valerij Albrandt | Fuel composition comprising diesel fuel and water includes an emulsifier containing a substance referred to as dioleate of oleic acid and monoethanolamine |
-
2007
- 2007-06-12 CN CN2007100285345A patent/CN101067094B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5746783A (en) * | 1994-03-30 | 1998-05-05 | Martin Marietta Energy Systems, Inc. | Low emissions diesel fuel |
CN1113937A (en) * | 1994-06-03 | 1995-12-27 | 关恩泽 | Hydro-diesel oil and its producing method |
CN1422934A (en) * | 2001-12-06 | 2003-06-11 | 徐涛 | Micro emulsion fuel production process and formula |
CN1422935A (en) * | 2001-12-07 | 2003-06-11 | 关恩泽 | Micro emulsion diesel fuel |
CN1410514A (en) * | 2002-09-29 | 2003-04-16 | 季忠 | Production technology and formulation of microemulsion fuel oil |
DE10315900A1 (en) * | 2003-04-08 | 2004-11-18 | Valerij Albrandt | Fuel composition comprising diesel fuel and water includes an emulsifier containing a substance referred to as dioleate of oleic acid and monoethanolamine |
CN1542100A (en) * | 2003-11-07 | 2004-11-03 | 陆翼德 | Emulsified diesel oil and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN101067094A (en) | 2007-11-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100554381C (en) | A kind of diesel oil emulsification and preparation method thereof | |
CN102399607B (en) | Practical micro-emulsified environment-friendly and energy-saving diesel oil and preparation method thereof | |
CN103320185B (en) | Bio-based methanol gasoline antiknock sending down abnormally ascending resist and preparation method thereof | |
CN102260554A (en) | Microemulsified biodiesel and preparation technique thereof | |
CN103396843B (en) | bio-based methanol gasoline component oil and preparation method thereof | |
CN101067094B (en) | Preparation method of microemulsion diesel oil | |
CN1136583A (en) | Water base ternary mixed fuel composed of coal, water and oil | |
CN108679599B (en) | A kind of oxygen-enhanced combustion method of pulverized coal blended with biomass | |
CN101619249B (en) | Alcohol-based fuel modifier, enhancer, alcohol-based liquid fuel after modification and enhancement and production process thereof | |
CN104804780B (en) | Low-proportion methanol diesel fuel and preparation method thereof | |
CN1389547A (en) | Oil-based coal slurry fuel and preparation process thereof | |
CN101837256A (en) | Method for preparing high-quality emulsified heavy oil | |
CN106190352B (en) | A kind of lignocellulosic base γ valerolactones diesel oil mediation fuel and preparation method thereof | |
CN101323801B (en) | Micro-emulsified diesel oil biomass composite additive | |
CN101914400A (en) | A kind of preparation method of emulsified diesel oil and emulsifier | |
CN108728179A (en) | A kind of high heating value hydrogen energy fuel and the preparation method and application thereof | |
CN102229821A (en) | Micro-emulsified methanol diesel and preparation method thereof | |
CN101987982A (en) | Emulsified diesel fuel and emulsifying agent preparation method | |
CN106520225A (en) | Novel fuel with energy saving and emission reducing effects and preparation method thereof | |
CN101705123B (en) | Environment friendly and energy-saving heavy oil additive | |
CN103351892B (en) | A kind of Environmentally-friebiofuel biofuel for boiler and preparation method thereof | |
CN105199789B (en) | Superpower dynamic main additive of water repellent micro emulsion diesel fuel of high temperature resistant and preparation method thereof | |
AU2020102695A4 (en) | Alcohol/ether fuel for diesel vehicles | |
CN108913234A (en) | A kind of low-carbon environment-friendly fuel and preparation method thereof based on diesel oil | |
CN102876408A (en) | Method for improving stability of coke water slurry and device |
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 | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100609 |