JPS62167391A - Fuel additive - Google Patents

Fuel additive

Info

Publication number
JPS62167391A
JPS62167391A JP61008919A JP891986A JPS62167391A JP S62167391 A JPS62167391 A JP S62167391A JP 61008919 A JP61008919 A JP 61008919A JP 891986 A JP891986 A JP 891986A JP S62167391 A JPS62167391 A JP S62167391A
Authority
JP
Japan
Prior art keywords
water
acid
fuel
parts
added
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.)
Granted
Application number
JP61008919A
Other languages
Japanese (ja)
Other versions
JPH0560516B2 (en
Inventor
Takeshi Morita
武 森田
Hirosuke Okura
大蔵 宏祐
Shigeru Nakai
滋 中井
Takamasa Ishioka
石岡 高昌
Takashi Matsuo
隆 松尾
Mitsuo Onozawa
光雄 小野沢
Masaki Shoji
正樹 東海林
Akinori Yagawa
矢川 明徳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Taiho Kogyo Co Ltd
Original Assignee
Taiho Kogyo Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Taiho Kogyo Co Ltd filed Critical Taiho Kogyo Co Ltd
Priority to JP61008919A priority Critical patent/JPS62167391A/en
Priority to KR1019860009378A priority patent/KR930011927B1/en
Publication of JPS62167391A publication Critical patent/JPS62167391A/en
Publication of JPH0560516B2 publication Critical patent/JPH0560516B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:An additive having an inorganic substance such as a metallic compound, etc., in high concentration and improved compatibility with fuel oil, comprising a composition as an active ingredient obtained by dispersing a bivalent - tetravalent metallic oxide(hydroxide) subjected to adsorption treatment with a specific compound into water by the use of a water-soluble surface active agent. CONSTITUTION:The aimed fuel additive comprising a composition as an active ingredient obtained by dispersing fine particles of one or more oxides(hydroxides) of bivalent - tetravalent metals selected from Mg, Ca, Al, Ba, Mn, Cu, Zn, Fe, Cr, Ti, Sn, Mo and Co having 100-600Angstrom particle diameters subjected to adsorption treatment with one or more of naphthenic acid, tall oil fatty acid, alkylphosphoric acid ester, oleic acid and lauric acid into water by the use of a water-soluble surface active agent.

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は、金属化合物を高濃度に含有し、しかもデー
ゼルエンシン、ボイラ、加熱炉、ガスタービン等の燃焼
機関に使用される原油、重油、石油コークス、石油ピッ
チ、灯軽油、ガソリン等の燃料油との混合性が良好な燃
料添加剤に関するものである。
Detailed Description of the Invention (Field of Industrial Application) This invention is directed to crude oil, heavy oil, etc., which contain a high concentration of metal compounds and are used in combustion engines such as diesel engines, boilers, heating furnaces, and gas turbines. The present invention relates to a fuel additive that has good miscibility with fuel oils such as petroleum coke, petroleum pitch, kerosene, and gasoline.

(従来の技術) 従来燃料添加剤は使用目的に応じて硫黄酸化物、窒素酸
化物等の有害成分の発生抑制、スラ・ンジ分散剤、エマ
ルジョン破壊剤、腐食防止剤、燃料灰類の堆積防止剤、
燃焼促進剤、煤煙防止剤、着火促進剤、セタン価向上剤
、凝固点降下剤等として知られているが、これ等の燃料
添加剤の形態は無機金属、金属酸化物、金属水酸化物、
炭酸塩等の微粉末を界面活性剤を主成分とする分散剤と
共に水に混合してスラリー状にしだものである。
(Prior art) Conventional fuel additives are used to suppress the generation of harmful components such as sulfur oxides and nitrogen oxides, to suppress the generation of harmful components such as sulfur oxides and nitrogen oxides, to suppress the generation of harmful components such as sulfur oxides and nitrogen oxides, to suppress the generation of sludge dispersants, emulsion breakers, corrosion inhibitors, and to prevent the accumulation of fuel ash. agent,
It is known as a combustion accelerator, soot inhibitor, ignition accelerator, cetane number improver, freezing point depressant, etc., but these fuel additives are in the form of inorganic metals, metal oxides, metal hydroxides,
It is made into a slurry by mixing fine powder such as carbonate with water together with a dispersant whose main component is a surfactant.

(発明か解決しようとする問題点) しかし、このような形態の燃料添加剤においては組成中
に含まれる無a物か保存中に沈殿、分離したり、或は燃
料油に添加した時、配管部分やバーナ部分で沈殿して閉
塞させたり、バーナノズル部分を摩耗することかある。
(Problem to be solved by the invention) However, in this type of fuel additive, the aluminium contained in the composition may precipitate or separate during storage, or when added to fuel oil, it may leak into piping. It may precipitate and block the burner or the burner, or it may wear out the burner nozzle.

更に、このような燃料添加剤においては組成中に含まれ
る無機物の粒径か大きく、しかも分散性か悪いため、燃
焼火炎中、排りス中その他に存在する有害物質との接触
効果が不十分て、添加剤としての十分な効果が期待でき
ない。
Furthermore, in such fuel additives, the particle size of the inorganic substances contained in the composition is large and the dispersibility is poor, so the contact effect with harmful substances present in combustion flames, exhaust gas, etc. is insufficient. Therefore, sufficient effects as an additive cannot be expected.

一方、従来から油溶性の金属化合物を石油系溶剤等に溶
解した燃料添加剤も知られている。
On the other hand, fuel additives in which oil-soluble metal compounds are dissolved in petroleum-based solvents have also been known.

これ等の燃料添加剤は燃料油と均一に混合溶解し、それ
故安定性も良好であり、燃焼中排ガス中その他に存在す
る有害成分との接触効率も良好であるが、油溶性金属化
合物中の有効成分である金属成分である金属成分の含有
量か少なく、高価格であるという欠点がある。
These fuel additives uniformly mix and dissolve with fuel oil, and therefore have good stability and good contact efficiency with harmful components present in exhaust gas and other substances during combustion. The drawback is that the content of the metal component, which is the active ingredient of the methane, is low and the price is high.

そこで、この発明は金属化合物等の無機物を高濃度に含
有し、しかもデーゼルエンジン、ボイラ、加熱炉、ガス
タービン等の燃焼機関に使用される原油、重油、石油コ
ークス、石油ピッチ、灯軽油、ガソリン等の燃料油との
混合性が良好な燃料添加剤を開発することを目的とする
Therefore, this invention aims to provide crude oil, heavy oil, petroleum coke, petroleum pitch, kerosene, and gasoline that contain high concentrations of inorganic substances such as metal compounds and are used in combustion engines such as diesel engines, boilers, heating furnaces, and gas turbines. The aim is to develop fuel additives that have good miscibility with fuel oils such as

(問題点を解決するための手段) 以上の問題点を解決するために、この発明ではナフテン
酸、トール油脂肪酸、石油スルフォン酸、アルキルリン
酸エステル、オレイン酸、ラウリン酸の1種又は2種以
上で吸着処理したその粒径か100〜600人の微細粒
子からなるlag、 Ca。
(Means for Solving the Problems) In order to solve the above problems, in this invention, one or two types of naphthenic acid, tall oil fatty acid, petroleum sulfonic acid, alkyl phosphoric acid ester, oleic acid, and lauric acid are used. Ca, which is made up of fine particles with a particle size of 100 to 600, was subjected to the adsorption treatment as described above.

AI%Ba、  Mn、  Cu、  Zn%Fe、 
Cr、  Ti%Sn、  Mo%Goで表される2〜
4価金属の酸化物又は水酸化物の1種又は2種以上を、
水溶性界面活性剤を用いて水に分散させてなる組成物を
有効成分とする燃料添加剤を提案するものである。
AI%Ba, Mn, Cu, Zn%Fe,
2~ represented by Cr, Ti%Sn, Mo%Go
One or more types of oxides or hydroxides of tetravalent metals,
The present invention proposes a fuel additive whose active ingredient is a composition obtained by dispersing a water-soluble surfactant in water.

即ち、この発明てはナフテン酸等で吸着処理した粒径が
100〜600人の微細粒子からなる上記2〜4価金属
の酸化物又は水酸化物の1種又は2種以上を、水溶性界
面活性剤を用いて水に分散させてなる組成物を燃料添加
剤として使用するものであるが、この燃料添加剤は例え
ば次のようにして作成される。
That is, in this invention, one or more of the above-mentioned oxides or hydroxides of di- to tetravalent metals, which are made of fine particles having a particle size of 100 to 600 and have been adsorbed with naphthenic acid or the like, are added to a water-soluble interface. A composition prepared by dispersing an activator in water is used as a fuel additive, and this fuel additive is prepared, for example, as follows.

上記2〜4価の金属水溶性塩、例えば塩化物、硝酸塩、
硫酸塩、酢酸塩等の水溶液にNaOH1に0HSN11
.01+、Ca(OH)、  等のアルカリ剤を加え、
液のpHを9〜11に上昇させた後、ナフテン酸、トー
ル油脂肪酸、石油スルフォン酸、アルキルリン酸エステ
ル、オレイン酸、ラウリン酸の1種又は2種以上を添加
して生成した油溶性の凝集物を濾過し、更に脱塩の目的
で水洗し、脱水して微細粒子からなる粉体を得る。
The above di- to tetravalent metal water-soluble salts, such as chlorides, nitrates,
0HSN11 to NaOH1 to aqueous solution of sulfate, acetate, etc.
.. Add an alkaline agent such as 01+, Ca(OH), etc.
After raising the pH of the liquid to 9 to 11, an oil-soluble oil produced by adding one or more of naphthenic acid, tall oil fatty acid, petroleum sulfonic acid, alkyl phosphate, oleic acid, and lauric acid. The aggregates are filtered, further washed with water for the purpose of desalting, and dehydrated to obtain a powder consisting of fine particles.

得られた粉体組成物を、水溶性界面活性剤及び水に加え
て、モーター、ディスパー、ホモジナイザー等を使用し
て安定な、水を溶媒とした燃料添加剤か作成される。
The obtained powder composition is added to a water-soluble surfactant and water, and a stable fuel additive using water as a solvent is prepared using a motor, a disperser, a homogenizer, etc.

この場合、得られた粉体は脱水乾燥を行なわす含水ケー
キ(水分30〜4oz)とし、これに水溶性界面活性剤
を添加し攪拌することにより安定な水を溶媒とする燃料
添加剤を作成することもできる。
In this case, the obtained powder is dehydrated and dried to form a water-containing cake (30 to 4 oz of moisture), and a water-soluble surfactant is added to this and stirred to create a stable fuel additive that uses water as a solvent. You can also.

上記粉体の製法についてマグネシウムを例に採り、更に
詳しく説明すると、一般にマグネシウム化合物の水溶液
にアルカリ剤を添加してpHを上げると水酸化マグネシ
ウムが生成する。生成したMg(Oll)、はその粒子
か集合して粗大粒子となって存在している。
To explain in more detail the method for producing the above powder using magnesium as an example, generally, when an alkali agent is added to an aqueous solution of a magnesium compound to raise the pH, magnesium hydroxide is produced. The generated Mg(Oll) particles are aggregated and exist as coarse particles.

この発明ではMg(01+)2の微粒子−が集合粗大化
する前に、ナフテン酸、トール油脂肪酸、石油スルフォ
ン酸、アルキルリン酸エステル、オレイン酸、ラウリン
酸等て表面コーティングして粒子の粗大化を防止すると
ともに粒子を親油性(油溶性)に変化させる。
In this invention, before the fine particles of Mg(01+)2 aggregate and become coarse, the surface is coated with naphthenic acid, tall oil fatty acid, petroleum sulfonic acid, alkyl phosphate, oleic acid, lauric acid, etc. to coarsen the particles. At the same time, it changes the particles to be lipophilic (oil-soluble).

即ち、水中に懸濁したMg(Otl)zの微粒子はプラ
スに帯電しており、これにナフテン酸、石油スルフォン
酸、トール油脂肪酸、オレイン酸、ラウリル酸等の水に
不溶性のマイナス電荷を有する有機物を添加すると、プ
ラスとマイナスの電荷による吸着反応により前記のよう
な油溶性の凝集物か生成する。
That is, fine particles of Mg(Otl)z suspended in water are positively charged, and in addition to this, water-insoluble negatively charged substances such as naphthenic acid, petroleum sulfonic acid, tall oil fatty acid, oleic acid, lauric acid, etc. When an organic substance is added, an adsorption reaction due to positive and negative charges generates oil-soluble aggregates as described above.

具体的には、前記のようにマグネシウム化合物の水溶液
にアルカリ剤を加えてPl+を9〜11に上昇させ、M
g(OH) 2の微粒子を生成させた後、液温を80〜
85℃に上昇させ、上記ナフテン酸を添加して七分加熱
、W1拌してMg(011)2微粒子表面に吸着させ、
この結果微粒子表面か親油性(水不溶性)となり、凝集
する。
Specifically, as described above, an alkali agent is added to an aqueous solution of a magnesium compound to increase Pl+ to 9 to 11, and M
After generating fine particles of g(OH) 2, the liquid temperature is lowered to 80~
Raise the temperature to 85°C, add the above naphthenic acid, heat for 7 minutes, stir W1 to make it adsorbed on the surface of Mg(011)2 fine particles,
As a result, the surface of the fine particles becomes lipophilic (water-insoluble) and aggregates.

なお、この場合、ナフテン酸、トール油脂肪酸1右抽ス
ルフォン酸、アルキルリン酸エステル、オレイン酸など
をそのまま添加しても良く。
In this case, naphthenic acid, tall oil fatty acid, sulfonic acid, alkyl phosphoric acid ester, oleic acid, etc. may be added as they are.

また上記有4!!物をNa塩、に塩、N114塩等の塩
類とし添加して良く、更に上記有機物をケロシン、ノル
マルパラフィン、イソパラフィン、流動パラフィン、動
植物油等に溶解させたものを添加しても良く、この場合
特に水溶性界面活性剤を含有した水に対して分散性が非
常に良いO/W型エマルジョンの均一なコロイド溶液に
なり、その安定性も良好となる。
There are also 4 of the above! ! The substance may be added as a salt such as Na salt, Ni salt, N114 salt, etc. Furthermore, the above organic substance may be added dissolved in kerosene, normal paraffin, isoparaffin, liquid paraffin, animal or vegetable oil, etc. In this case, In particular, a uniform colloidal solution of an O/W type emulsion with very good dispersibility in water containing a water-soluble surfactant is obtained, and its stability is also good.

この場合、上記有機物と溶剤の溶解割合はl:0.5〜
l:3の範囲が適当である。
In this case, the dissolution ratio of the organic substance and solvent is 1:0.5~
A range of l:3 is suitable.

以上のように生成した油溶性の凝集物は濾過し、脱塩の
目的で水洗し、更に脱水することにより油溶性のマグネ
シウム含有の粉体を得ることができる。
The oil-soluble aggregates generated as described above are filtered, washed with water for the purpose of desalting, and further dehydrated to obtain an oil-soluble magnesium-containing powder.

この粉体を水溶性界面活性剤を含む水中に加え、ディス
パー等で混合攪拌すると、水を媒体として上記2〜4価
の金属酸化物又は水酸化物の微粒子が安定して分散した
燃料添加剤が作成される。 なお、この発明で使用する
水溶性界面活性剤としてはアルキルスルフォン酸塩、脂
肪酸右端、ジアルキルスルフォン琥珀酸塩、高級アルキ
ルリン酸塩、高級脂肪酸エステルの硫酸エステル塩、硫
酸化油、ポリオキシエチレンアルキルリン酸エステル塩
、ポリオキシエチレンアルキルエーテルタルボン酸塩、
ポリオキシエチレンアルキル硫酸エステル塩等のアニオ
ン界面活性剤、ポリオキシエチレンアルキルアリルエー
テル、ポリオキシエチレンアルコールエーテル、ポリオ
キシエチレン脂肪酸エステル、ポリオキシエチレンアル
キルフェノールフォルマリン縮合物、ポリオキシエチレ
ンアルキルアマイド、ポリオキシエチレンアルキルアミ
ン、ポリオキシエチレンソルビトール脂肪酸エステル、
プルロニックタイプ、テトロニックタイプ等のIILB
II〜15の非イオン界面活性剤があり、これ等の界面
活性剤は単独でも、また28以上を組み合わせて使用し
てもよい。
When this powder is added to water containing a water-soluble surfactant and mixed and stirred with a disper etc., the fine particles of the above-mentioned di- to tetravalent metal oxide or hydroxide are stably dispersed using water as a medium. is created. In addition, the water-soluble surfactants used in this invention include alkyl sulfonates, right end fatty acids, dialkyl sulfone succinates, higher alkyl phosphates, sulfate ester salts of higher fatty acid esters, sulfated oils, and polyoxyethylene alkyls. Phosphate ester salt, polyoxyethylene alkyl ether tarboxate,
Anionic surfactants such as polyoxyethylene alkyl sulfate salts, polyoxyethylene alkyl allyl ether, polyoxyethylene alcohol ether, polyoxyethylene fatty acid ester, polyoxyethylene alkylphenol formalin condensate, polyoxyethylene alkyl amide, polyoxy Ethylene alkylamine, polyoxyethylene sorbitol fatty acid ester,
IILB such as Pluronic type and Tetronic type
There are II to 15 nonionic surfactants, and these surfactants may be used alone or in combinations of 28 or more.

これ等水溶性界面活性剤の添加量は少なくとも1%必要
であり、1%以下ではあると、燃料添加剤の安定性に聞
届がある。
The amount of these water-soluble surfactants added must be at least 1%, and if it is less than 1%, the stability of the fuel additive will be affected.

なお、この発明に係る燃料添加剤はそのまま、或はこれ
を適当な溶剤に分散させた溶液を燃料油に添加して使用
することができる。
The fuel additive according to the present invention can be used as it is, or a solution obtained by dispersing it in a suitable solvent can be added to fuel oil.

(発明の効果) この発明に係る燃料添加剤は、100〜600人粒径の
上記2〜4価金属酸化物又は水酸化物がその粒子表面に
ナフテン酸、トール油脂肪酸、石油スルフすン酸、アル
キルリン酸エステル、オレイン酸、ラウリン酸の1種又
は2種以上を吸着し、更にその表面に水溶性界面活性剤
の親油基を吸着した状態て水媒体に分散された構造であ
り、このため極めて安定であり、長期間保存しても凝集
したり、沈降することがない。
(Effects of the Invention) The fuel additive according to the present invention has naphthenic acid, tall oil fatty acid, petroleum sulfuric acid, etc. , a structure in which one or more of alkyl phosphate esters, oleic acid, and lauric acid are adsorbed, and a lipophilic group of a water-soluble surfactant is adsorbed on the surface and dispersed in an aqueous medium, Therefore, it is extremely stable and does not aggregate or settle even when stored for a long period of time.

また、燃料添加剤も水を媒体としであるため、従来の石
油系溶媒を使用した添加剤に比べて安価て、かつ取扱い
易い等の利点があり、更に燃料添加剤中に含まれる水溶
性界面活性剤の作用により燃料油中に均一に分散され、
したかって析出することかなく、燃料油の配管やバーナ
を閉塞したり、摩耗させることかないなどの利点かある
In addition, since fuel additives use water as a medium, they have the advantage of being cheaper and easier to handle than additives that use conventional petroleum-based solvents. Uniformly dispersed in the fuel oil by the action of the activator,
This has the advantage that it does not precipitate and does not clog or wear out fuel oil piping or burners.

また、この発明に係る燃料添加剤は上記2〜4価の金1
i!酸化物又は水酸化物を高濃度に含有している。例え
ばマグネシウムについてみると、石油スルフオン酸マグ
ネシウム、ナフテン酸マグネシウム、オレイン酸マグネ
シウム、オクチル酸マグネシウム等の一般の有機マグネ
シウム化合物に比べてマグネシウムの含有率が高く、M
gOとして5oz存在する。しかも、上記金属酸化物又
は水酸化物は100〜600人粒径の微細粒子から構成
されているため、表面積が大きく、物理的、化学的活性
か大てあり、有害成分との接触効果が良好である。
Further, the fuel additive according to the present invention has the above-mentioned di- to tetravalent gold 1.
i! Contains high concentrations of oxides or hydroxides. For example, regarding magnesium, it has a higher magnesium content than general organic magnesium compounds such as magnesium petroleum sulfonate, magnesium naphthenate, magnesium oleate, and magnesium octylate.
5oz exists as gO. Moreover, since the above metal oxides or hydroxides are composed of fine particles with a particle size of 100 to 600, they have a large surface area, are highly physically and chemically active, and have good contact effects with harmful components. It is.

このため、この発明に係る燃料添加剤は燃料油中に少量
添加しても十分な効果か期待できる。例えば大気汚染源
であるSOx、NOxを多く含有する煤煙の発生を抑制
することができるばかりでなく、V、 Na、 Sによ
るスーパーヒーター等の高温腐食、 SO2,SOiの
発生によるボイラの低温部腐食を抑制することができる
Therefore, it can be expected that the fuel additive according to the present invention will have sufficient effects even if added in small amounts to fuel oil. For example, it not only suppresses the generation of soot containing a large amount of SOx and NOx, which are sources of air pollution, but also prevents high-temperature corrosion of super heaters due to V, Na, and S, and corrosion of low-temperature parts of boilers due to the generation of SO2 and SOi. Can be suppressed.

(実施例) 以下、この発明の実施例を示す。(Example) Examples of this invention will be shown below.

製造例1 A液・・・15%MgCl 2水溶液  620部B液
−−−20$NaOH水溶液  375部C液・・・ナ
フテン酸10部、イソパラフィン13部の混合溶解液 A液にB液を添°加してPHを9.5〜10に上昇させ
る。 Mg(OH)*の微粒子が生成した後、液温な8
0℃に上昇させ、C液を加え、80〜85℃で十分加熱
攪拌を行うとマグネシウム含有の油溶性粉体か凝集して
液が透明になってくる。
Production Example 1 Solution A... 15% MgCl 2 aqueous solution 620 parts Solution B --- 20$ NaOH aqueous solution 375 parts Solution C... Added solution B to solution A of a mixed solution of 10 parts of naphthenic acid and 13 parts of isoparaffin. ° to raise the pH to 9.5-10. After the fine particles of Mg(OH)* are generated, the liquid temperature is 8.
When the temperature is raised to 0°C, liquid C is added, and the temperature is sufficiently heated and stirred at 80 to 85°C, the magnesium-containing oil-soluble powder aggregates and the liquid becomes transparent.

次いで濾過水洗を行い含有されている無機塩の除去を行
う、!過水洗後得られた粉体は水分を50$程度含んだ
状態にあるが、これをφ10s園の球状ベレットにして
200メツシユの金網上に広げ風速約3 m1sec 
95℃て40分間熱風乾燥を行い含水率を2.1%に下
げる。
Next, filter and wash with water to remove the contained inorganic salts! The powder obtained after washing with water contains about 50 dollars of water, but it is made into spherical pellets of φ10s and spread on a wire mesh of 200 mesh at a wind speed of about 3 m1sec.
Dry with hot air at 95° C. for 40 minutes to reduce the moisture content to 2.1%.

乾燥後の粉体50部、ドデシルベンゼンスルフオン酸ナ
トリウム7部、ポリオキシエチレンノニルフェノールエ
ーテル(IILB l:1.0) 5部、水道水38部
を混合ディスパーで30分間攪拌し、均一な分散液を得
た。
50 parts of the dried powder, 7 parts of sodium dodecylbenzenesulfonate, 5 parts of polyoxyethylene nonylphenol ether (IILB l:1.0), and 38 parts of tap water were stirred with a mixing disper for 30 minutes to form a uniform dispersion. I got it.

なお、製造した分散液中のMgO含有量は26%であっ
た。
Note that the MgO content in the produced dispersion was 26%.

製造例2 A液・・・l5zFeC13水溶液  300部B液−
−−20!KOH水溶液   150部C液・・・トー
ル油脂肪酸4部、ケロシン8部の混合溶解液 A液にB液を添加し、 PHを9.5〜10に上昇させ
てFe(Oll)zの微粒子が生成した後、液温を80
℃に上昇させてC液を加え、80〜85℃で十分加熱攪
拌を行うとバリウム含有の油溶性粉体が來果して透明と
なってくる。
Production Example 2 Solution A...15zFeC13 aqueous solution 300 parts Solution B
--20! KOH aqueous solution 150 parts Solution C: Mixed solution of 4 parts tall oil fatty acid and 8 parts kerosene Solution B was added to Solution A, and the pH was raised to 9.5-10 to form fine particles of Fe(Oll)z. After generating, reduce the liquid temperature to 80
When the temperature is raised to 80 DEG C., liquid C is added thereto, and the temperature is sufficiently heated and stirred at 80 to 85 DEG C., the barium-containing oil-soluble powder eventually becomes transparent.

次いて濾過水洗を行う、&!過過水後後採取た粉体は水
分40%含有されているが、この含水粉体(水分40駕
含有)を80部、ジオクチルスルフォン琥珀酸ナトリウ
ム5部、ポリオキシエチレンポリオキシプロピレンブロ
ックボリマー(プルロニック)5部水道水lO部を混合
し、ディスパー30分間攪拌し安定な分散液を得た。
Next, perform filtration and washing with water, &! The powder collected after perhydration contains 40% water, and 80 parts of this water-containing powder (containing 40 parts water), 5 parts of dioctyl sulfone sodium succinate, and polyoxyethylene polyoxypropylene block polymer. (Pluronic) 5 parts and 10 parts of tap water were mixed and stirred for 30 minutes using a dispersion device to obtain a stable dispersion.

なお、製造した分散液中のFe、03含有率は23%て
あった。
Note that the content of Fe, 03 in the produced dispersion was 23%.

製造例3 A液・・・15zCaC1□水溶液  350部B液・
・・NIl、OH水溶液   200部C液・・・石油
スルフオン酸8部、ケロシン8部の混合溶解液 A液にB液を添加してpHを9.5〜IOに上昇させて
Ca(O)l)、の微粒子が生成した後、液温を80°
CにE昇させ、C液を加え、80〜85°Cて十分加熱
攪拌を行うとカルシウム含有の油溶性粉体が凝集して液
か透明になってくる。
Production example 3 A liquid...15zCaC1□ aqueous solution 350 parts B liquid...
... NIl, OH aqueous solution 200 parts Solution C... Mixed solution of 8 parts of petroleum sulfonic acid and 8 parts of kerosene Add Solution B to Solution A to raise the pH to 9.5-IO to make Ca(O) l) After the fine particles are generated, the liquid temperature is increased to 80°.
When the temperature is raised to E, C is raised to E, liquid C is added, and the temperature is sufficiently heated and stirred at 80 to 85°C, the calcium-containing oil-soluble powder aggregates and the liquid becomes transparent.

次いで濾過水洗を行い含有されている無a塩の除去を行
う。癌過水洗後得られた粉体は水分を60$程度含んだ
状態にあるが、これをφ10s−の球状ベレットにして
200メツシユの金網上に広げ風速1 m1sec 9
0℃て1時間熱風乾燥を行い、含水率2zの粉体な得た
Next, filtering and washing with water are performed to remove the a-free salts contained therein. The powder obtained after washing the cancer with water contains about 60 dollars of water, but it is made into a spherical pellet of φ10s- and spread on a wire mesh of 200 mesh at a wind speed of 1 ml sec 9
Hot air drying was performed at 0° C. for 1 hour to obtain a powder with a moisture content of 2z.

乾燥後の粉体45部、オレイン酸ナトリウム2部、ポリ
オキシエチレンドデシル硫酸ナトリウム塩3部、ポリオ
キシエチレンソルビタン脂肪酸エステル(HLB 10
.5) 3部、水道水47部を混合ディスパーで攪拌し
、均一な分散液を得た。製造した分散液中のCaO含有
量は22%てあった。
45 parts of dried powder, 2 parts of sodium oleate, 3 parts of polyoxyethylene dodecyl sulfate sodium salt, polyoxyethylene sorbitan fatty acid ester (HLB 10
.. 5) 3 parts and 47 parts of tap water were stirred with a mixing disper to obtain a uniform dispersion. The CaO content in the produced dispersion was 22%.

使用例 製造例1.2.3で得られた6液をプランジャーポンプ
を使用して燃料の1000分の1の;1合てボイラの燃
料配管に強制的に混入して燃料とともにボイラの火炎中
に噴射させ、ボイラのエアヒータ出口て発生するチッ:
X酸化物、S02、媒塵の量を測定し、エコノマイザ−
出口で803を測定し、またスーパーヒーター(JIS
 G:1462材質5TBA−24)及びエアヒータに
てテストピース(JIS G:1101材質5S−41
)をつりさげ、腐食量を測定してそれぞれ無添加と比較
した。その結果を下表に示す。
Usage Example Using a plunger pump, the 6 liquid obtained in Production Example 1.2.3 is mixed into 1/1000th of the fuel and forced into the boiler's fuel piping, causing the boiler's flame to flow together with the fuel. Chipping occurs at the boiler air heater outlet.
Measure the amount of X oxide, S02, and dust, and use the economizer.
803 was measured at the exit, and the super heater (JIS
G:1462 material 5TBA-24) and test piece with air heater (JIS G:1101 material 5S-41)
) was suspended, the amount of corrosion was measured, and each was compared with that without additives. The results are shown in the table below.

なお、使用したボイラは三菱CE自然循環型で最大連続
蒸発量か1507/11、最大使用圧力か125にg/
cI12最大使用温度か540℃、燃料使用料が211
Kg/IIである。
The boiler used was a Mitsubishi CE natural circulation type with a maximum continuous evaporation rate of 1507/11 and a maximum working pressure of 125 g/
cI12 maximum operating temperature is 540℃, fuel usage fee is 211
Kg/II.

手続補正書(自発) 昭和61年9月26日Procedural amendment (voluntary) September 26, 1986

Claims (1)

【特許請求の範囲】[Claims] ナフテン酸、トール油脂肪酸、石油スルフォン酸、アル
キルリン酸エステル、オレイン酸、ラウリン酸の1種又
は2種以上で吸着処理したその粒径が100〜600Å
の微細粒子からなるMg、Ca、Al、Ba、Mn、C
u、Zn、Fe、Cr、Ti、Sn、Mo、Coで表さ
れる2〜4価金属の酸化物又は水酸化物の1種又は2種
以上を、水溶性界面活性剤を用いて水に分散させてなる
組成物を有効成分とすることを特徴とする燃料添加剤。
Adsorption treatment with one or more of naphthenic acid, tall oil fatty acid, petroleum sulfonic acid, alkyl phosphate ester, oleic acid, and lauric acid has a particle size of 100 to 600 Å.
Mg, Ca, Al, Ba, Mn, C consisting of fine particles of
One or more oxides or hydroxides of di- to tetravalent metals represented by u, Zn, Fe, Cr, Ti, Sn, Mo, and Co are added to water using a water-soluble surfactant. A fuel additive characterized by containing a dispersed composition as an active ingredient.
JP61008919A 1986-01-21 1986-01-21 Fuel additive Granted JPS62167391A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP61008919A JPS62167391A (en) 1986-01-21 1986-01-21 Fuel additive
KR1019860009378A KR930011927B1 (en) 1986-01-21 1986-11-06 Fuel additives

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61008919A JPS62167391A (en) 1986-01-21 1986-01-21 Fuel additive

Publications (2)

Publication Number Publication Date
JPS62167391A true JPS62167391A (en) 1987-07-23
JPH0560516B2 JPH0560516B2 (en) 1993-09-02

Family

ID=11706062

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61008919A Granted JPS62167391A (en) 1986-01-21 1986-01-21 Fuel additive

Country Status (1)

Country Link
JP (1) JPS62167391A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6312691A (en) * 1986-07-04 1988-01-20 Taiho Ind Co Ltd Method for preventing combustion disturbance in combustion apparatus
JPH02225594A (en) * 1989-02-27 1990-09-07 Mitsubishi Heavy Ind Ltd Additive for fuel oil
FR2672820A1 (en) * 1991-02-19 1992-08-21 Intevep Sa PROCESS FOR THE IN SITU PRODUCTION OF A SORPTION AGENT OXIDE AEROSOL USED TO REMOVE EFFLUENTS FROM A GASEOUS COMBUSTION CURRENT
US6310430B1 (en) 1998-03-18 2001-10-30 Ngk Spark Plug Co., Ltd. Spark plug having a metallic terminal within a through-hole
WO2002077132A1 (en) * 2001-03-23 2002-10-03 Taiho Industries Co., Ltd. Fuel additive for preventing slagging and method for burning fuel
WO2012039429A1 (en) * 2010-09-24 2012-03-29 株式会社マリネックス Water-mixed fuel and method for producing same
US9527030B2 (en) 2014-02-12 2016-12-27 Kurita Water Industries Ltd. Method for preventing fouling of exhaust gas flow path of burning equipment and method for removing ammonium hydrogen sulfate contained in exhaust gas of burning equipment

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6312691A (en) * 1986-07-04 1988-01-20 Taiho Ind Co Ltd Method for preventing combustion disturbance in combustion apparatus
JPH02225594A (en) * 1989-02-27 1990-09-07 Mitsubishi Heavy Ind Ltd Additive for fuel oil
FR2672820A1 (en) * 1991-02-19 1992-08-21 Intevep Sa PROCESS FOR THE IN SITU PRODUCTION OF A SORPTION AGENT OXIDE AEROSOL USED TO REMOVE EFFLUENTS FROM A GASEOUS COMBUSTION CURRENT
US6310430B1 (en) 1998-03-18 2001-10-30 Ngk Spark Plug Co., Ltd. Spark plug having a metallic terminal within a through-hole
WO2002077132A1 (en) * 2001-03-23 2002-10-03 Taiho Industries Co., Ltd. Fuel additive for preventing slagging and method for burning fuel
WO2012039429A1 (en) * 2010-09-24 2012-03-29 株式会社マリネックス Water-mixed fuel and method for producing same
JP2012067188A (en) * 2010-09-24 2012-04-05 Marinekkus:Kk Water-mixed fuel and method for producing the same
US9527030B2 (en) 2014-02-12 2016-12-27 Kurita Water Industries Ltd. Method for preventing fouling of exhaust gas flow path of burning equipment and method for removing ammonium hydrogen sulfate contained in exhaust gas of burning equipment

Also Published As

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