JPS6026926B2 - Atomization method for liquid fuel, etc. - Google Patents
Atomization method for liquid fuel, etc.Info
- Publication number
- JPS6026926B2 JPS6026926B2 JP4479880A JP4479880A JPS6026926B2 JP S6026926 B2 JPS6026926 B2 JP S6026926B2 JP 4479880 A JP4479880 A JP 4479880A JP 4479880 A JP4479880 A JP 4479880A JP S6026926 B2 JPS6026926 B2 JP S6026926B2
- Authority
- JP
- Japan
- Prior art keywords
- additive
- emulsion
- liquid fuel
- oil
- carbon dioxide
- 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
Links
- 239000007788 liquid Substances 0.000 title claims description 11
- 239000000446 fuel Substances 0.000 title claims description 10
- 238000000889 atomisation Methods 0.000 title description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 18
- 239000000654 additive Substances 0.000 claims description 18
- 239000000839 emulsion Substances 0.000 claims description 16
- 230000000996 additive effect Effects 0.000 claims description 15
- 238000009835 boiling Methods 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 10
- 238000002485 combustion reaction Methods 0.000 claims description 9
- 239000001569 carbon dioxide Substances 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- 239000010419 fine particle Substances 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000010802 sludge Substances 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 2
- 230000001737 promoting effect Effects 0.000 claims description 2
- 239000003921 oil Substances 0.000 description 13
- 239000002245 particle Substances 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 239000000428 dust Substances 0.000 description 5
- 239000000295 fuel oil Substances 0.000 description 3
- 239000000571 coke Substances 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 230000005514 two-phase flow Effects 0.000 description 1
Landscapes
- Spray-Type Burners (AREA)
Description
【発明の詳細な説明】
この発明は重質油その他の液体燃料や可燃性スラッジ等
の微粒化方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for atomizing heavy oil, other liquid fuels, combustible sludge, and the like.
燃焼油の微粒化技術としては、油を高圧渦巻により噂霧
する方法、蒸気等の階霧媒体を用いて油を頃霧する方法
、その他が知られている。As techniques for atomizing combustion oil, there are known methods such as a method of atomizing the oil using a high-pressure swirl, a method of atomizing the oil using an atomizing medium such as steam, and others.
しかしこれらの方法を重質油の微粒化に適用した場合、
前者の方法では粘度が高くなると微粒化効率が著しく低
下し、また後者の方法では噂霧媒体と高粘度油の混合が
十分なされていないために、多量の媒体を使用しても所
期の粒径にまで微粒化することができず、そのためエネ
ルギーコスト的に不利となるばかりか、かえって多量媒
体のため燃焼が不安定なものとなった。この発明は、上
記のような点に鑑みてなされたものであって、童質油を
所期の粒径に効率よく微粒化し得る方法を提供すること
を目的とする。However, when these methods are applied to atomization of heavy oil,
In the former method, the atomization efficiency decreases significantly as the viscosity increases, and in the latter method, the atomizing medium and high viscosity oil are not mixed sufficiently, so even if a large amount of medium is used, the desired granulation cannot be achieved. It was not possible to atomize the particles to a small diameter, which not only resulted in a disadvantage in terms of energy cost, but also made combustion unstable due to the large amount of medium. This invention has been made in view of the above-mentioned points, and an object of the present invention is to provide a method that can efficiently atomize child oil to a desired particle size.
すなわち、この発明は、液体燃料や可燃性スラツジ等の
被燃焼物に、水やアルコール等の低沸点液体からなる添
加物を混入してェマルジョンを形成し、生じたェマルジ
ョンを加圧し、さらに噴射しようとする炉の内部圧力に
おける添加物の沸点以上の温度にヱマルジョンを加熱し
、しかる後加圧加熱ェマルジョンを燃焼炉内に噴射供給
して、添加物の減圧沸騰現象により、被燃焼物を微粒化
する方法であって、添加物に燃焼排ガスを接触させて、
排ガス中の炭酸ガスを添加物に吸収し、得られた炭酸ガ
ス含有添加物を用いることにより減圧沸騰現象を促進す
ることを要旨とする液体燃料等の微粒化方法である。上
記において、添加物の添加量は、被燃焼物の10〜5の
重量%がよい。That is, the present invention involves mixing an additive made of a low-boiling point liquid such as water or alcohol with a substance to be combusted such as liquid fuel or combustible sludge to form an emulsion, pressurizing the resulting emulsion, and then injecting it. The emulsion is heated to a temperature higher than the boiling point of the additive at the internal pressure of the furnace, and then the pressurized heated emulsion is injected into the combustion furnace to atomize the material to be combusted by the reduced pressure boiling phenomenon of the additive. A method of bringing combustion exhaust gas into contact with additives,
This is a method of atomizing liquid fuel, etc., in which carbon dioxide gas in exhaust gas is absorbed into an additive, and the obtained carbon dioxide-containing additive is used to promote a boiling phenomenon under reduced pressure. In the above, the amount of the additive added is preferably 10 to 5% by weight of the material to be burned.
添加後ラインミキサーで両者をよく混合する。なお、生
じたェマルジョンは、前述した高圧渦巻頃霧法や、媒体
を用いて贋髪する方法による微粒化では、十分に微粒化
されない。ただしェマルジョン燃料を燃焼すると、燃料
液滴内に含まれる水分が沸騰し、燃料液滴が再微粒化さ
れる効果がある。そのため燃焼性が向上し、煤塵濃度が
減少する。なお、重貿油をェマルジョン化してなるェマ
ルジョン燃料は、省エネルギー化および低公害化を企図
して開発されたものである。炭酸ガスは、水に対する溶
解性の高い物質であり、たとえば空気の約6M音(00
0)の溶解度を有する。After addition, mix both well with a line mixer. It should be noted that the resulting emulsion cannot be sufficiently atomized by the above-mentioned high-pressure swirling atomization method or by the method of falsifying hair using a medium. However, when the emulsion fuel is burned, the water contained in the fuel droplets boils, and the fuel droplets have the effect of being re-atomized. Therefore, combustibility is improved and soot and dust concentration is reduced. Note that emulsion fuel, which is made by emulsifying heavy trade oil, was developed with the aim of saving energy and reducing pollution. Carbon dioxide gas is a substance that is highly soluble in water, and for example, it has a high solubility in air of about 6M sound (00
It has a solubility of 0).
添加物中の炭酸ガスの含有量は多いほどよいが、排ガス
を使用するのでおのずと制限される。減圧沸騰現象は、
液体を加圧するとともに系外圧下における添加物の沸点
以上の温度に加熱し、ついで加圧加熱液体を系外に放出
することにより生じる。The higher the content of carbon dioxide gas in the additive, the better, but since exhaust gas is used, it is naturally limited. The reduced pressure boiling phenomenon is
It is produced by pressurizing the liquid and heating it to a temperature higher than the boiling point of the additive under pressure outside the system, and then releasing the pressurized and heated liquid to the outside of the system.
重質油の微粒化に減圧沸騰現象だけを適用しても、所期
の目的は達成されない。その理由は、この場合高圧高熱
が必要であって、そのため童質油の一部が熱分解して加
熱器内でコークス化したり、分解生成ガスのために気液
2相流が生じ、頃霧量の制御が困難になるためである。
ェマルジョン用添加物として水を使用する場合には、加
熱温度は120〜180qoが適当である。この発明に
よる微粒化方法は、以上のとおりで、水やアルコール等
の添加物による被燃焼物のェマルジョン化と減圧沸騰現
象とを組合わせてなるものであるので、被燃焼物はそれ
自体の沸点よりも低い温度において微粒化される。その
ため油の熱分解を生じたり、加熱器内での油がコークス
化するといった問題を生じることなく、効率よく微粒化
を達成することができる。また蒸気や空気等の頃霧媒体
を使用する必要がないので、エネルギーコストの点でも
有利であり、燃焼性も安定する。さらに添加物は炭酸ガ
スを含有しているので、減圧沸騰現象を一層促進するこ
とにより、生成微粒子の粒径を著しく小さくできるとと
もに、燃焼による媒塵の生成を極力抑えることができる
。実施例
図面に示すように、粘度13比p(150℃)の童質油
とこれの2の重量%の量の水とを、それぞれ油タンクー
および水タンク2からポンプ3,4を介して加圧下にラ
インミキサー5に供給し、ここでこれらを混合してェマ
ルジョンを形成する。Even if only the vacuum boiling phenomenon is applied to atomize heavy oil, the intended purpose will not be achieved. The reason for this is that high pressure and high heat are required in this case, which causes some of the young oil to thermally decompose and turn into coke in the heater, and gas-liquid two-phase flow to occur due to the gas produced by decomposition, causing fog. This is because it becomes difficult to control the amount.
When water is used as an additive for emulsion, a suitable heating temperature is 120 to 180 qo. As described above, the atomization method according to the present invention combines emulsion of the combustible material with additives such as water and alcohol, and reduced pressure boiling phenomenon, so that the combustible material has its own boiling point. It is atomized at temperatures lower than . Therefore, atomization can be efficiently achieved without causing problems such as thermal decomposition of the oil or coke formation of the oil within the heater. Furthermore, since there is no need to use a mist medium such as steam or air, it is advantageous in terms of energy cost and combustibility is stable. Furthermore, since the additive contains carbon dioxide gas, by further promoting the reduced pressure boiling phenomenon, the particle size of the generated fine particles can be significantly reduced, and the generation of dust due to combustion can be suppressed as much as possible. Example As shown in the drawings, virgin oil with a viscosity of 13 p (150° C.) and water in an amount of 2% by weight thereof are added from an oil tank and a water tank 2 through pumps 3 and 4, respectively. They are fed under pressure to a line mixer 5 where they are mixed to form an emulsion.
このェマルジョンをヒータ6で130〜150qoに加
熱し、バーナ7から炉8内に頃霧する。こうして微粒化
した童質油を炉8内で燃焼する。また、炉8の後方にC
02吸収塔9を配設して、これにダンパの操作により燃
焼排ガスを通過させる。そして水タンク2からポンプ1
0を介してきた水をC02吸収塔9に通して、ポンプ2
に導く。こうして形成したC02含有水を用いて、以下
上記と同様に操作し、軍質油の燃焼を行う。そしてC0
2吸収時と非吸収時について、異なるェマルジョン温度
における生成微粒子の平均粒径と燃焼時の媒塵濃度とを
測定する。結果をそれぞれ表1および表2に示す。表
1 (平均粒径)
表 2 (煤塵濃度)
上記各表からわかるように、C02吸収により、特に低
加熱度領域において、生成微粒子の粒径を著しく4・さ
くでき、また媒塵量を大量に低減することができる。This emulsion is heated to 130 to 150 qo with a heater 6 and atomized into a furnace 8 from a burner 7. The virgin oil thus atomized is burned in the furnace 8. Also, there is a C at the rear of the furnace 8.
A 02 absorption tower 9 is provided, and combustion exhaust gas is passed through this by operating a damper. And from water tank 2 to pump 1
The water that has passed through the C02 absorption tower 9 is passed through the pump 2.
lead to. Using the CO2-containing water thus formed, military oil is combusted in the same manner as described above. and C0
2. Measure the average particle size of the generated fine particles at different emulsion temperatures and the dust concentration during combustion during absorption and non-absorption. The results are shown in Tables 1 and 2, respectively. table
1 (Average particle size) Table 2 (Soot and dust concentration) As can be seen from the above tables, CO2 absorption can significantly reduce the particle size of generated fine particles by 4.0 mm, especially in the low heating degree region, and also increase the amount of dust. can be reduced.
図面はこの発明の実施例を示す系統図である。 The drawing is a system diagram showing an embodiment of the present invention.
Claims (1)
ルコール等の低沸点液体からなる添加物を混入してエマ
ルジヨンを形成し、生じたエマルジヨンを加圧し、さら
に噴射しようとする炉の内部圧力における添加物の沸点
以上の温度にエマルジヨンを加熱し、しかる後加圧加熱
エマルジヨンを燃焼炉内に噴射供給して、添加物の減圧
沸騰現象により、被燃焼物を微粒化する方法であつて、
添加物に燃焼排ガスを接触させて、排ガス中の炭酸ガス
を添加物に吸収し、得られた炭酸ガス含有添加物を用い
ることにより減圧沸騰現象を促進することを特徴とする
液体燃料等の微粒化方法。1 The inside of a furnace where an emulsion is formed by mixing additives made of low boiling point liquids such as water and alcohol with materials to be combusted such as liquid fuel and combustible sludge, and the resulting emulsion is pressurized and then injected. A method of heating the emulsion to a temperature higher than the boiling point of the additive under pressure, and then injecting the heated emulsion under pressure into a combustion furnace to atomize the material to be combusted by the boiling phenomenon of the additive under reduced pressure. ,
Fine particles of liquid fuel, etc. characterized by bringing combustion exhaust gas into contact with an additive, absorbing carbon dioxide gas in the exhaust gas into the additive, and promoting a reduced pressure boiling phenomenon by using the obtained carbon dioxide gas-containing additive. method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4479880A JPS6026926B2 (en) | 1980-04-04 | 1980-04-04 | Atomization method for liquid fuel, etc. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4479880A JPS6026926B2 (en) | 1980-04-04 | 1980-04-04 | Atomization method for liquid fuel, etc. |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56142320A JPS56142320A (en) | 1981-11-06 |
| JPS6026926B2 true JPS6026926B2 (en) | 1985-06-26 |
Family
ID=12701436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4479880A Expired JPS6026926B2 (en) | 1980-04-04 | 1980-04-04 | Atomization method for liquid fuel, etc. |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6026926B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20030066093A (en) * | 2002-02-04 | 2003-08-09 | 주식회사 기가씨앤이 | system and method for burning emulsion oil of water-in-oil type |
| CN109163324B (en) * | 2018-09-12 | 2020-08-07 | 广东电网有限责任公司 | Evaluation method, device, equipment and storage medium for sludge-mixed combustion boiler |
-
1980
- 1980-04-04 JP JP4479880A patent/JPS6026926B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56142320A (en) | 1981-11-06 |
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