JPS6317878B2 - - Google Patents
Info
- Publication number
- JPS6317878B2 JPS6317878B2 JP59088834A JP8883484A JPS6317878B2 JP S6317878 B2 JPS6317878 B2 JP S6317878B2 JP 59088834 A JP59088834 A JP 59088834A JP 8883484 A JP8883484 A JP 8883484A JP S6317878 B2 JPS6317878 B2 JP S6317878B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ozone
- tank
- heavy oil
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 14
- 239000000446 fuel Substances 0.000 claims description 7
- 238000000889 atomisation Methods 0.000 claims description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 4
- 229910001882 dioxygen Inorganic materials 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 238000002715 modification method Methods 0.000 claims 1
- 239000000295 fuel oil Substances 0.000 description 11
- 238000002407 reforming Methods 0.000 description 5
- 239000011882 ultra-fine particle Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
- C10L1/328—Oil emulsions containing water or any other hydrophilic phase
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Feeding And Controlling Fuel (AREA)
- Colloid Chemistry (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
【発明の詳細な説明】
「産業上の利用分野」
本発明は低質燃油所謂Ｃ重油を船舶用デイーゼ
ル機関並びに陸上発電機用デイーゼル機関等へ有
効に利用するため改質する分野に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to the field of reforming low-quality fuel, so-called C heavy oil, in order to effectively utilize it in diesel engines for ships, diesel engines for land-based power generators, and the like.
「従来の技術」
従来の改質法は加温Ｃ重油を過してスラツ
ジ、タール等の粒子を残渣として排出するもので
あつた。"Prior Art" Conventional reforming methods pass through heated C heavy oil and discharge particles such as sludge and tar as a residue.
「発明が解決しようとする問題点」
本発明は上記残渣を排出することなく燃焼性良
好な燃料として利用し媒煙の発生を防止し完全に
燃焼させることを目的とする。"Problems to be Solved by the Invention" An object of the present invention is to use the above-mentioned residue as a fuel with good combustibility without emitting it, thereby preventing the generation of smoke and completely burning it.
「問題を解決するための手順」
本発明は水にオゾンを混合又は溶解して酸素ガ
スを水に飽和させ、これを低質燃油の超微粒化槽
内に投入して懸濁又は乳化し、これを液体燃料と
することを特徴とする低質油改質法を特徴とす
る。``Procedures for solving the problem'' The present invention involves mixing or dissolving ozone in water to saturate the water with oxygen gas, and placing this in a low-quality fuel ultra-atomization tank to suspend or emulsify it. The present invention is characterized by a method for reforming low quality oil, which is characterized by using it as a liquid fuel.
「作用」
酸素含有量の多いオゾン（O3）をオゾン発生
機によつて水槽内の水に注入拡散させ撹拌機で撹
拌することによつて水とオゾンは混合又は溶解し
て該オゾンは発生機の酸素及び酸素ガスが該水に
飽和状態に溶解する。これを加温流動性Ｃ重油用
超微粒化槽内に投入すると超微粒化用超音波クラ
ツシヤーの作用によつて同Ｃ重油と上記混合液又
は溶液は微細化して上記Ｃ重油と懸濁液又は乳液
を形成するこのような液内のスラツジやタール等
は懸濁液又は乳液の水・オゾン微粒子に表面張力
によつてくつついて沈降することなくポンプで燃
料タンクに送られ、さらに内燃機関内に供給され
燃焼して同機関を動作するものである。"Operation" Ozone with a high oxygen content (O 3 ) is injected into the water in the aquarium using an ozone generator, diffused, and stirred with a stirrer.The water and ozone are mixed or dissolved, and the ozone is generated. The oxygen and oxygen gas of the machine are dissolved in the water in a saturated state. When this is put into an ultra-atomization tank for heated fluid C heavy oil, the C heavy oil and the above mixed liquid or solution are finely divided by the action of the ultrasonic crusher for ultra atomization, and the above C heavy oil and the suspension or solution are finely divided. The sludge, tar, etc. in the liquid that forms the emulsion cling to the water and ozone particles in the suspension or emulsion due to surface tension and are sent to the fuel tank by a pump without settling, and are further pumped into the internal combustion engine. It is supplied and burned to operate the engine.
「実施例」
図面に基いて説明すると水槽１内に一定水位に
水を収容し、その水位はフロート弁２によつて保
持され、底部にオゾン注入拡散管３を水平方向に
配設する。水位附近には水面４の上下に亘つて回
転する撹拌回転羽根５を設け、同水槽１は気密に
構成される。上記拡散管３はオゾン発生器６に接
続し、上記回転羽根５の回転軸７は原動機８によ
つて高速回転させ水面４上のオゾンを水面下に搬
入する役目を果し発生機の酸素及び酸素ガスは水
に飽和し、飽和水はポンプ１１及び配管１２によ
つて送られ加温流動Ｃ重油の超微粒化槽９（第１
図）の手前で同Ｃ重油と混合器１０によつて混合
して同槽９内に収容され、同槽９内の超音波クラ
ツシヤー１０によつて上記混合物は超微粒子に破
砕され水・オゾンは超微粒子となつて懸濁又は乳
化するばかりでなく硬いスラツジやタール等も超
微粒子に破砕され水・イオンの超微粒子と表面張
力によつてくつついて沈降しない。この状態のＣ
重油はポンプ１３でタンク１４に送られさらに内
燃機関に供給されてこれを動作するものである。
尚図中１５で示すものはＣ重油配管、１６は電磁
弁である。Ａ、Ｂ重油には水・オゾンに代えて
水・水素を用いることがある。``Embodiment'' To explain based on the drawings, water is stored in a water tank 1 at a constant water level, the water level is maintained by a float valve 2, and an ozone injection diffusion tube 3 is arranged horizontally at the bottom. A stirring rotary blade 5 that rotates above and below the water surface 4 is provided near the water level, and the water tank 1 is constructed to be airtight. The diffusion tube 3 is connected to an ozone generator 6, and the rotary shaft 7 of the rotary blade 5 is rotated at high speed by a prime mover 8 to carry the ozone on the water surface 4 to below the water surface. The oxygen gas is saturated with water, and the saturated water is sent by the pump 11 and piping 12 to the heated fluid C heavy oil ultra-atomization tank 9 (first
(Figure), the mixture is mixed with C heavy oil in a mixer 10 and stored in the same tank 9, and the above mixture is crushed into ultrafine particles by an ultrasonic crusher 10 in the same tank 9, and water and ozone are Not only are they suspended or emulsified as ultrafine particles, but hard sludge, tar, etc. are also crushed into ultrafine particles and do not settle due to the surface tension of the ultrafine particles of water and ions. C in this state
The heavy oil is sent to a tank 14 by a pump 13 and further supplied to the internal combustion engine to operate it.
In the figure, 15 indicates C heavy oil piping, and 16 indicates a solenoid valve. For A and B heavy oils, water and hydrogen may be used instead of water and ozone.
「効果」
上記Ｃ重油は上記超微粒化槽（第１図）内でタ
ールやスラツジが沈降することなく超微粒となつ
て水・オゾン超微粒子に伴つて内燃機関内で燃焼
するため水中の飽和酸素や発生機の酸素のために
完全に燃焼し、媒煙を生じることなくクリーンエ
ネルギーとして利用し得るばかりでなく熱効率を
著しく向上することができる。``Effects'' The C heavy oil becomes ultrafine particles in the ultraatomization tank (Figure 1) without sedimentation of tar or sludge, and is combusted in the internal combustion engine along with water and ultrafine ozone particles, so it becomes saturated in water. It is completely combusted due to the presence of oxygen and the oxygen in the generator, and can be used as clean energy without producing smoke, as well as significantly improving thermal efficiency.
第１図は本発明の低質油改質法を示す図、第２
図は水槽の正面図、第３図は第２図Ａ−Ａ線によ
る平面図、第４図は第１図の側面図である。
１……水・オゾン混合水槽、９……超微粒化
槽。
Figure 1 is a diagram showing the low quality oil reforming method of the present invention, Figure 2 is a diagram showing the low quality oil reforming method of the present invention.
The figure is a front view of the aquarium, FIG. 3 is a plan view taken along line A--A in FIG. 2, and FIG. 4 is a side view of FIG. 1. 1...Water/ozone mixing tank, 9...Ultra atomization tank.
Claims (1)
に飽和させ、これを低質燃油の超微粒化槽内に投
入して懸濁又は乳化し、これを液体燃料とするこ
とを特徴とする低質油改質法。1 A low-quality fuel that is characterized by mixing or dissolving ozone in water to saturate the water with oxygen gas, and then putting this into a low-quality fuel ultra-atomization tank to suspend or emulsify it and make it into a liquid fuel. Oil modification method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8883484A JPS60231794A (en) | 1984-05-02 | 1984-05-02 | Improving quality of low-grade oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8883484A JPS60231794A (en) | 1984-05-02 | 1984-05-02 | Improving quality of low-grade oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60231794A JPS60231794A (en) | 1985-11-18 |
| JPS6317878B2 true JPS6317878B2 (en) | 1988-04-15 |
Family
ID=13953972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8883484A Granted JPS60231794A (en) | 1984-05-02 | 1984-05-02 | Improving quality of low-grade oil |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60231794A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6330593A (en) * | 1986-07-24 | 1988-02-09 | Kotobuki Senpaku Shoji:Kk | Method of reforming fuel oil |
| CA2093861A1 (en) * | 1992-04-14 | 1993-10-15 | Carlos Jorge Guinart Jaritz | Combustion process: the use of ozone as a supporter of combustion |
| JPH0753974A (en) * | 1993-08-06 | 1995-02-28 | Tadashi Mochihata | Production of emulsion fuel |
| JP2000219886A (en) * | 1999-02-01 | 2000-08-08 | Masatoshi Matsumura | Method and apparatus for conversion of vegetable oil (virgin) or waste vegetable oil to fuel for diesel engine |
| JP2008019359A (en) * | 2006-07-13 | 2008-01-31 | Shinkawa Yoshiro | Manufacturing method of emulsion composition and apparatus for emulsification |
| WO2011137378A2 (en) | 2010-04-30 | 2011-11-03 | University Of Utah Research Foundation | Ozonation conversion of heavy hydrocarbons for resource recovery |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60232231A (en) * | 1984-04-28 | 1985-11-18 | Daido Steel Co Ltd | Removal of bad smell and oil fume in scrap preheating apparatus |
-
1984
- 1984-05-02 JP JP8883484A patent/JPS60231794A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60232231A (en) * | 1984-04-28 | 1985-11-18 | Daido Steel Co Ltd | Removal of bad smell and oil fume in scrap preheating apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60231794A (en) | 1985-11-18 |
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