JPS62503173A - Additive for liquid fuel - Google Patents

Additive for liquid fuel

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Publication number
JPS62503173A
JPS62503173A JP61503293A JP50329386A JPS62503173A JP S62503173 A JPS62503173 A JP S62503173A JP 61503293 A JP61503293 A JP 61503293A JP 50329386 A JP50329386 A JP 50329386A JP S62503173 A JPS62503173 A JP S62503173A
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additive
oil
component
fuel
additives
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ヤコブセン,ニールズ・ナツド・エリク
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スパロル・インテルナシオナル・ア−・ペ−・エス
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/02Use of additives to fuels or fires for particular purposes for reducing smoke development
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/06Use of additives to fuels or fires for particular purposes for facilitating soot removal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1225Inorganic compounds halogen containing compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1608Well defined compounds, e.g. hexane, benzene
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1616Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • C10L1/1886Carboxylic acids; metal salts thereof naphthenic acid

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 液体燃料 添加剤 東スユmル乱1 本発明は、液体燃料例えば燃料油、ガス油やモーターディーゼルを含めたディー ゼル油用添加剤に関する。[Detailed description of the invention] Liquid fuel additive East Suyu Muru Ran 1 The present invention applies to liquid fuels including fuel oil, gas oil and motor diesel. Regarding additives for gel oil.

従来の技術 燃焼性を改良し、腐蝕損害(corrosion damages)を抑えかつ システム中の不純物蓄積aを少なくする目的で液体燃料に添加される適当な添加 剤をめて、長年開発が行なわれている。Conventional technology Improves flammability, reduces corrosion damage and A suitable additive added to a liquid fuel for the purpose of reducing the accumulation of impurities in the system. The drug has been under development for many years.

また、数多くの液体燃料用添加剤が今までに市販、使用されているが、残念なが ら満足すべきものはない。成る種の金属を用いるとすすやオイルコークスが減少 する効果が得られる。In addition, many liquid fuel additives have been commercially available and in use, but unfortunately There is nothing to be satisfied with. Soot and oil coke are reduced when using different metals. The effect of

硫酸の生成を抑え、従って腐蝕を抑制するために、僅かに過剰「の空気を使用す ると有利である。油を僅かに過剰量の空気の存在下で燃焼させると、効率がかな り改良される。しかしながら、過剰量の空気によってすすやオイルコークスが大 量に生成される欠点も生ずる。A slight excess of air is used to reduce the formation of sulfuric acid and therefore corrosion. It is advantageous if Burning oil in the presence of a slight excess of air is less efficient. improved. However, the excessive amount of air creates a large amount of soot and oil coke. There are also disadvantages created in quantity.

発明の開示 本発明の目的は、従来公知の添加剤よりも優れており、使用者に経済的利益を与 えるだけでなく、燃焼性、即ち効率を高め、特表昭62−503173 (2) 燃焼システム中に蓄積もしくは堆積する不純物の串を少なくし、環境放出物の量 を少なくすると共に酸成分例えば硫酸による腐蝕損害を抑える新規な添加剤を提 供することにある。Disclosure of invention The purpose of the present invention is to provide additives that are superior to previously known additives and provide economic benefits to the user. It not only improves fuel efficiency, but also improves combustibility, i.e. efficiency. Reduces the amount of impurities that accumulate or deposit in the combustion system and reduces the amount of environmental emissions. We propose a new additive that reduces corrosion damage caused by acid components such as sulfuric acid. It is about providing.

上記目的は、 1)脂肪酸のマンガン塩と 2)高沸点タール油と 3) ナフタレンと を含み、所望により下記追加成分 4)ナフテン酸鉄。The above purpose is 1) Fatty acid manganese salt and 2) High boiling point tar oil and 3) Naphthalene and Contains the following additional ingredients if desired: 4) Iron naphthenate.

5)塩化第二鉄及び 6)脂肪酸のカルシウム塩。5) Ferric chloride and 6) Calcium salts of fatty acids.

の1種以上を含むことを特徴とする本発明の液体燃料用添加剤により達成される 。This is achieved by the liquid fuel additive of the present invention, which is characterized by containing one or more of the following: .

使用可能なマンガン塩としては、炭素数8−9の分岐鎖脂肪酸ノマンカン塩例え ばAkzo Chemieより市販のt+anganeseSiccatol  [M n約10%、非揮発性物質61−67%、ミネラルスピリット(ホワイト スピリット)35%含有]及びNLIOdeX”口ryer Han(lane se″が例示される。Examples of manganese salts that can be used include nomankane salts of branched chain fatty acids having 8 to 9 carbon atoms. t+anganese Siccator commercially available from Akzo Chemie [Mn about 10%, non-volatile substances 61-67%, mineral spirit (white Spirit) 35% content] and NLIOdeX” mouth ryer Han (lane ``se'' is exemplified.

“NuOdeX Dryer Iron”は適当なナフテン酸鉄の一つとして例 示される。“NuOdeX Dryer Iron” is an example of a suitable iron naphthenate. shown.

適当な高沸点タール油としては、ポリ芳香族炭化水素を含有する油、例えばアン トラセン油が例示される。アントラセン油を加熱すると、その40%が330− 400℃の温度で留出する。アントラセン油の引火点は密閉容器内で180℃で ある。1適当な脂肪酸のカルシウム塩として、炭素数8−9の分岐鎖脂肪酸のカ ルシウム塩、例えばAkzo Chemieより市販のCalcium 5ic catol CCa約5%、非揮発性成分47−52%、残部ミネラルスヒリッ ト含有]或いは’Nuodex Dryer Calcium”が例示される。Suitable high-boiling tar oils include oils containing polyaromatic hydrocarbons, such as An example is tracene oil. When anthracene oil is heated, 40% of it becomes 330- Distill at a temperature of 400°C. The flash point of anthracene oil is 180℃ in a closed container. be. 1. As calcium salts of suitable fatty acids, calcium salts of branched chain fatty acids with 8-9 carbon atoms are used. Lucium salts, such as Calcium 5ic, commercially available from Akzo Chemie catol CCa approximately 5%, non-volatile components 47-52%, balance mineral salt or 'Nuodex Dryer Calcium'.

本発明の添加剤は、上記した3種の必須成分から製造される。The additive of the present invention is manufactured from the three essential components described above.

即ち、タール油を液体となるまで加熱し、連続加熱中にナフタレンを添加して均 質な液体混合物を形成後マンガン塩製剤を混合して製造される。That is, tar oil is heated until it becomes a liquid, and naphthalene is added during continuous heating to homogenize it. The manganese salt formulation is then mixed to form a quality liquid mixture.

上記した6成分を含む本発明の添加剤は、カルシウム塩製剤。The additive of the present invention containing the above six components is a calcium salt preparation.

マンガン塩製剤及びナフテン酸鉄製剤を撹拌混合して得られた混合1物、に、別 個に製造したタール油、塩化第二鉄及びナフタレンの溶融混合物を配合(添加) して製造される。A mixture obtained by stirring and mixing a manganese salt preparation and an iron naphthenate preparation; Blend (addition) of a molten mixture of separately prepared tar oil, ferric chloride and naphthalene Manufactured by

添加剤を製品として市販する前に、通常より容易に燃料と相客しうる安定な混合 物を得るために灯油が添加される。Before additives are commercialized as products, they must be mixed stably so that they can be more easily mixed with fuels. Kerosene is added to get things.

各成分の混合比率は通常状の範囲内である1)脂肪酸のマンガン塩含有製剤 1 0〜1oop”2)高沸点タール油 1〜3g 5)塩化第二鉄 0〜5 KH 2)脂肪酸のカルシウム塩含有製剤 0〜80f!燃料中の活性成分含量に是い て計算すると、混合比率Iま以下のように仮定される。しかしながら、轟を算4 1分イζ確定なものであり、以下の値は1つの例と考えるべきである。The mixing ratio of each component is within the normal range 1) Fatty acid manganese salt-containing preparation 1 0~1oop”2) High boiling point tar oil 1~3g 5) Ferric chloride 0-5 KH 2) Fatty acid calcium salt-containing preparation 0-80f! The content of active ingredients in the fuel When calculated, the mixing ratio I is assumed to be as follows. However, Todoroki calculated 4 1 minute iζ is certain, and the following values should be considered as an example.

1)脂肪酸のマンガン塩 (Mn換算) 0.008−0.08Kff / を燃料2)高沸点タール油  0.009−0.09に5 / を燃料3) ナフタレン 0.04−0.12 89/を燃料4)ナフテン酸鉄製剤 (Fe換算) O−0,05K9 / を燃料4)塩化第二鉄 0−0.048 g/を燃料6)脂肪酸のカルシウム塩 (Ca換算) O−0,03Kg/ を燃料上記6成分の混合物は通常燃料油の 燃焼用に使用される。1) Manganese salts of fatty acids (Mn conversion) 0.008-0.08Kff / Fuel 2) High boiling point tar oil 0.009-0.09 to 5/fuel 3) Naphthalene 0.04-0.12 89/ as fuel 4) Iron naphthenate preparation (Fe conversion) O-0.05K9 / Fuel 4) Ferric chloride 0-0.048 g/fuel 6) Calcium salts of fatty acids (Calculated as Ca) O-0.03Kg/ The mixture of the above six components is normally used as fuel oil. Used for combustion.

成分6)を含まない添加剤は通常ガス油の燃焼用に使用される。Additives that do not contain component 6) are usually used for gas oil combustion.

成分6)を含まない添加剤は通常ディーゼル油(モーターディーゼル油を含む) の燃焼用に使用される。しかしながら、脂肪酸のカルシウム塩を少迅添加するの が好ましい場合もある。こうすると、機械類に堆積した(硬質の)堆積物(de posits)が解きほぐれる。Additives that do not contain component 6) are usually diesel oil (including motor diesel oil) used for combustion. However, adding calcium salts of fatty acids slowly may be preferable. This will remove the (hard) deposits that have accumulated on the machinery. positions) are unraveled.

本発明の添加剤は、燃料の表面張力を低下させ、その結果より細かく微粒化(a tomization)され、中断回数の少ない優れた作業効率が得られるよう に作用すると考えられる。The additives of the present invention reduce the surface tension of the fuel, resulting in finer atomization (a tomization) to achieve excellent work efficiency with fewer interruptions. It is thought that it acts on

液体燃料の燃焼に伴ってすすが形成される原因は、憤霧された燃料液滴(dro ps)が余りに大きいことにある。そのために不完全にしか燃焼せず、部分的に 非燃焼状態でボイラーを通過し、管内や他の加熱表面上にすすの形態で堆積する のである。オイルコークスが形成される原因も燃料液滴が余りに大ぎいことにあ る。液滴中のオイルがある温度に加熱されたとき、液滴が燃え尽きる前にコーク ス化してしまうからである。形成されたオイルコークス粒子は普通の条件下では 燃焼し得ず、従って排気ガスと一緒に同伴される。本発明の添加剤を使用するこ とによって燃料をより細かく微粒化することができ、燃料をより大きな液滴の形 態で燃焼させたときに比べてはるかに完全な燃焼が確保されうる。より細かい液 滴を微粒化することによって、形成された小さな液滴内の温度がより容易に高温 に維持され完全燃焼が確保される。大きな液滴の中心部が燃焼中なお低温のまま であることが避けられる。完全に燃焼されると未燃焼の不純物がシステムに導入 されることはなくなり、従って堆積物や汚染放出物が防止される。燃料が十分に 微粒化されると、完全燃焼を妨げることなく少ない空気の供給量で作動させるこ とができる。空気の供給量が少なくなると、排気ガス中のCO2含但が高くなり 、最適の燃焼性と効率が得られる。The formation of soot with the combustion of liquid fuels is caused by atomized fuel droplets. ps) is too large. Therefore, it burns only incompletely, and only partially Passes through the boiler in an unburned state and is deposited in the form of soot in pipes and on other heated surfaces It is. Oil coke is also formed because the fuel droplets are too large. Ru. When the oil in a droplet is heated to a certain temperature, coke will form before the droplet burns out. This is because it becomes a social network. The formed oil coke particles under normal conditions It cannot be combusted and is therefore entrained with the exhaust gas. Using the additive of the invention The fuel can be atomized into finer particles by Much more complete combustion can be ensured than when combustion is carried out in the same state. finer liquid By atomizing the droplets, the temperature within the small droplets formed can more easily be raised to high temperatures. is maintained to ensure complete combustion. The center of the large droplet remains cool during combustion This can be avoided. Complete combustion introduces unburned impurities into the system This eliminates the possibility of contamination, thus preventing deposits and polluting emissions. enough fuel Once atomized, it can be operated with less air supply without interfering with complete combustion. I can do it. When the air supply decreases, the CO2 content in the exhaust gas increases. , resulting in optimal flammability and efficiency.

本発明の燃料油用添加剤と一緒に、通常燃料油1tに対して11の灯油含有添加 剤が添加される。後者の添加剤を添加すると、通常燃焼前に行なわれる油の予備 加熱温度を下げることができる。予備加熱は通常電気を使用して行なわれ、費用 がかさむ。こうして得られるエネルギー節約は添加剤のコスト以上であろう。Together with the fuel oil additive of the present invention, 11 kerosene-containing additions per 1 ton of normal fuel oil agent is added. The addition of the latter additive improves the oil reserve that is normally done before combustion. Heating temperature can be lowered. Preheating is usually done using electricity and is less expensive. It gets heavy. The energy savings thus obtained may exceed the cost of the additive.

予備加熱温度を下げてはならない場合もある。その代り完全に燃焼され、″゛ボ イラー中より優れた結果”が得られる。In some cases, the preheating temperature must not be lowered. Instead, it is completely burned and better results than during the error.

本発明の添加剤を燃料油用の燃焼用システムに使用すると、スス、オイルコーク ス、クリンカー及び硫酸の生成量が減少する。従って、ボイラー中に断熱性コー ティングが形成されずに高い効率が得られる。また排気ガスサイドが腐蝕を受け にくくなり、水が存在していても水は油中に乳化される。その結果、ボイラーは クリーンでドライな状態にあり、その寿命が長くなる。システムはより安定して 作動し、その補修回数は少なくて済む。When the additive of the present invention is used in combustion systems for fuel oil, soot, oil coke, etc. The amount of carbon dioxide, clinker and sulfuric acid produced is reduced. Therefore, an insulating coat in the boiler High efficiency is achieved without the formation of ringing. In addition, the exhaust gas side suffered from corrosion. If water is present, it will be emulsified into the oil. As a result, the boiler It stays clean and dry, extending its lifespan. the system is more stable It works and requires fewer repairs.

本発明の添加剤をガス油に添加するときにも、油1tに対して11の灯油含有添 加剤が使用される。添加剤はパラフィン・ワックスの発生を防止、タンク、チュ ーブ及びフィルターをクリーンに保持し、油中に存在する水もしくは凝縮により 形成された水を乳化させ、かつ腐蝕を防止する。添加剤により一18℃までの温 度でも保護される。より細く微粒化され、従ってより完全な燃焼が確保され、ス スやコークスの[積が防止される。When adding the additive of the present invention to gas oil, 11 kerosene-containing additives are added to 1 ton of oil. Additives are used. Additives prevent the formation of paraffin wax, tanks and tubes. Keep the pipes and filters clean and free from water or condensation present in the oil. Emulsifies the water formed and prevents corrosion. Temperatures up to -18℃ with additives protected at any time. finer atomization, thus ensuring more complete combustion and Accumulation of gas and coke is prevented.

よりクリーンに燃焼されるため燃料消費量が少なくなり、ディーゼルエンジンに 使用した際の摩耗や破損が抑制される。Cleaner combustion reduces fuel consumption, making it suitable for diesel engines Wear and damage during use are suppressed.

本発明の添加剤は、定置式もくしは移動式ディーゼルエンジン例えば船用エンジ ンに使用されるディーゼル油の添加用に適している。通常、ディーゼル油1tに 対して1pの灯油含有添加剤が添加される。添加剤に、より、パラフィン・ワッ クスの生成量が少なくなり、エンジンをよりクリーンに保つことができ、かつ始 動が促進される。添加剤により、−18℃までの温度に対する保護が与えられる 。タンク、チューブ及びフィルターがクリーンに維持される。添加剤により、デ ィーゼル油中に存在する水も凝縮により形成された水も乳化される。従って、タ ンク。The additive of the present invention can be used in stationary or mobile diesel engines such as marine engines. Suitable for addition to diesel oil used in engines. Usually, 1 ton of diesel oil 1 p of kerosene-containing additive is added. Due to additives, paraffin wax This reduces the amount of fuel produced, which helps keep the engine cleaner and starts faster. movement is promoted. Additives provide protection against temperatures down to -18°C . Tanks, tubes and filters are kept clean. With additives, de Both the water present in the diesel oil and the water formed by condensation is emulsified. Therefore, Nku.

チューブ、ポンプやバルブの腐蝕が防止される。微粒化が改良される結果、より 完全な燃焼が達成され、ススとコークスの堆積が避けられる。燃料消費量が少な くなり、ディーゼルエンジンの摩耗が少なくなる。Corrosion of tubes, pumps and valves is prevented. As a result of improved atomization, more Complete combustion is achieved and soot and coke deposits are avoided. low fuel consumption This reduces diesel engine wear.

実 売 例 本発明を、下記実施例及びテストを参照しながら更に詳細に説明する。Actual sales example The invention will be explained in more detail with reference to the following examples and tests.

割血豆−ユ 燃料油用添加剤の製造 Calcium 5iccatol 401 (約36.8に4F) (約1. 825 KyCa含有)。Split blood bean yu Manufacture of fuel oil additives Calcium 5iccatol 401 (approximately 36.8 to 4F) (approximately 1. 825 KyCa containing).

Hanganese 5iccatol 20j! (約20Kg>(約2N9 )In含有)及びナフテン酸鉄製剤”Nuodex Dryer Iron”2 01(約24Kg)と、別個に調製した“アントラセン油”(40%が330〜 400℃で沸II)21 (約2゜32に9>、塩化第二鉄IN9及びナフタレ ン12に3を含有する溶融混合物とを撹拌しながら混合した。得られた混合物を 冷却し、灯油20Ilを混合した。この混合物を添加剤として燃料1tあたり  11の割合で配合した。この添加剤に対するデーターは次の通りである。Hanganese 5iccatol 20j! (Approx. 20Kg>(Approx. 2N9 ) In-containing) and iron naphthenate preparation "Nuodex Dryer Iron" 2 01 (approximately 24 kg) and separately prepared “anthracene oil” (40% of which is 330 ~ boiling at 400°C II) 21 (approx. The molten mixture containing 12 and 3 was mixed with stirring. the resulting mixture It was cooled and mixed with 20 Il of kerosene. per 1 ton of fuel using this mixture as an additive It was blended at a ratio of 11:1. The data for this additive are as follows.

密 度: 0.9G 外 観:褐色の液体 引 火 点:58℃ 貯蔵耐久性:無限 実施例 2 ガス油層添加剤の製造 ■ Manganese 5iccatol 401 (約40&y)及びブフテン 酸鉄製剤“t4uodex Dryer Iron″401(約48Ky)と、 別個に調製した゛″アントラセン油(40%が330〜400℃で沸騰) 21  (2,32Ky>、塩化第二鉄IKg及びナフタレン12幻を含有する溶融混 合物とを撹拌しながら混合した。得られた混合物を冷却し、灯油201を混合し た。この混合物を添加剤として燃F11tあたり 111の割合で配合した。こ の添加剤に対するデーターは次の通りである。Density: 0.9G Appearance: brown liquid Flash point: 58℃ Storage durability: infinite Example 2 Production of gas oil reservoir additives ■ Manganese 5iccatol 401 (about 40&y) and Buchten Acid iron preparation "t4uodex Dryer Iron" 401 (approximately 48Ky), Separately prepared anthracene oil (40% boiling at 330-400°C) 21 (2,32Ky>, molten mixture containing IKg of ferric chloride and 12Ky of naphthalene) The mixture was mixed with stirring. The resulting mixture was cooled and kerosene 201 was mixed with it. Ta. This mixture was blended as an additive at a ratio of 111 parts per 11 tons of fuel F. child The data for the additives are as follows.

密 度: 0.9Q 外 観:褐色の液体 引 火 点 :55℃ 貯蔵耐久性:無限 友i五−ユ ディーゼル油用添加剤のfJ i HanganeSe 5iccatol 701 (約70に3 )及びナフテ ン酸鉄製剤“NLIOdeX Dryer Iron”101(約12Fs>と 、別個にmWした“アントラセン油”(40%が330〜400℃で沸W1)  2j! (2,32に3)、塩化第二鉄189及びナフタレン12 K9を含有 する溶融混合物とを撹拌しながら混合した。得られた混合物を冷却し、灯油20 1を混合した。この混合物を添加剤として燃料1tあたり 11の割合で配合し た。この添加剤に対するデーターは次の通りである。Density: 0.9Q Appearance: brown liquid Flash point: 55℃ Storage durability: infinite Tomo Igo-Yu diesel oil additive fJi HanganeSe 5iccatol 701 (approximately 3 in 70) and naphte iron phosphate preparation “NLIOdeX Dryer Iron” 101 (approximately 12Fs> , separately mW “anthracene oil” (40% boiling W1 at 330-400°C) 2j! (2,32 to 3), contains ferric chloride 189 and naphthalene 12 K9 The molten mixture was mixed with stirring. The resulting mixture is cooled and heated with kerosene 20 1 was mixed. This mixture is added as an additive at a ratio of 11 parts per ton of fuel. Ta. The data for this additive are as follows.

密 度: 0.85 外 観:褐色の液体 引 火 点 : 55℃ 貯R耐久性:無限 本発明の添加剤により驚くべき作用効果が得られることは、次のテストから明ら かである。Density: 0.85 Appearance: brown liquid Flash point: 55℃ Storage R durability: Infinite It is clear from the following tests that the additive of the present invention provides surprising effects. That's it.

テスト 1 実施例1で製造した灯油含有添加剤を燃料油1tあたり11含む燃料油と添加剤 を含まない燃料油とを比較した。Test 1 Fuel oil and additive containing 11 kerosene-containing additives produced in Example 1 per 1 ton of fuel oil compared with fuel oil that does not contain

ボイラーを80%負荷率(load)で作動させ、テスト中ボイラーの調整は行 なわなかった。The boiler was operated at 80% load and no adjustments were made to the boiler during the test. I didn't jump.

添加剤を含まない2例(テストa及びb)及び添加剤を含む2例(テストC及び d)についてテストを行った。得られた結果を第1表に示す。Two cases without additives (tests a and b) and two cases with additives (tests C and d) was tested. The results obtained are shown in Table 1.

テスト1を繰返した。但し、Calcium 5iccatol 2Qj!と灯 油50!を含む添加剤を使用した。得られた結果を第2表に示す。Test 1 was repeated. However, Calcium 5iccatol 2Qj! and light Oil 50! Additives containing were used. The results obtained are shown in Table 2.

第 2 表 第1表及び第2表から明らかな通り、固体物質の放出量が少なくなる結果、すす 数(soot number)が少なくなり、ボイラーシステムをより経済的に 作動させうる。テストの結〜ゴ添加斉1の放出量抑制に対する効果を調べるため に!<−ナーの調整を行なわずに行った結果である。Table 2 As is clear from Tables 1 and 2, as a result of the reduction in the amount of solid substances released, soot The soot number is reduced, making the boiler system more economical. It can be activated. Conclusion of the test - To investigate the effect of Go addition Qi 1 on suppressing the release amount To! This is the result obtained without adjusting the <-ner.

添加剤を使用したときの放出量は、環境省(Department ofthe  Environment )が指導している限界値(2,597に9油)以下 であり・バーナーを再調整することによって通常の毎日の作動中により高い経済 性(より高いCo2パーセンテージ)が得られうる。The amount of emissions when using additives is determined by the Ministry of the Environment (Department of the Environment). Below the limit value (2,597 to 9 oil) prescribed by the Environmental Protection Agency - Higher economy during normal daily operation by readjusting the burner (higher Co2 percentage).

上記した如く、ボイラーはテスト中調整しなかった。得られたCO2−数は殆ん ど未変化のようである。ボイラーを適当に調整することによりCO2含聞合量適 にすることができる。As mentioned above, the boiler was not adjusted during the test. The CO2- number obtained is almost It seems like nothing has changed. By adjusting the boiler appropriately, the CO2 content can be adjusted appropriately. It can be done.

テスト 3 添加剤を使用せずに3種の燃料油用システムをテストした。排気ガス中のCo2 含量は約12.5%であり、すす数(Bacharach )は約5であった。Test 3 Three fuel oil systems were tested without additives. Co2 in exhaust gas The content was approximately 12.5% and the soot number (Bacharach) was approximately 5.

同じシステムについて8%の水を添加してテストした。結果は次の通りであった 。CO2含有率13.5%、すす数3〜4゜実施例1の添加剤(油1tあたり灯 油含有添加剤11’)を添加して得られた結果は次の通りである。CO2−含有 率14.5%。The same system was tested with 8% water added. The results were as follows . CO2 content 13.5%, soot number 3-4° Additive of Example 1 (light per ton of oil) The results obtained with the addition of oil-containing additive 11') are as follows. CO2-containing Rate 14.5%.

すす数2〜3゜ 上記テスト中もボイラーの調整は行なわなかった。Soot number 2~3° No adjustments were made to the boiler during the above test.

水を液体燃料中に乳化させることによってCO2含有率が高められることは公知 である。本発明の添加剤によりCO2含有率をより高めることができる。It is known that CO2 content can be increased by emulsifying water in liquid fuel. It is. The additive of the present invention can further increase the CO2 content.

水を使用しないと石灰質の堆積呈が少なくなり、補修回数も少なくて済む。If water is not used, there will be less calcareous deposits and fewer repairs will be required.

本発明の添加剤を使用すると、添加剤だけでタンクに注入したり他の簡単な方法 で分配することができるので、従来水と一緒に使用されていた高価な乳化システ ムが不必要となる。With the additive of the present invention, the additive can be simply injected into the tank or by other easy methods. can be dispensed with water, eliminating the need for expensive emulsification systems traditionally used with water. is no longer necessary.

本発明の添加剤を使用することにより、従来頻繁に行なわれていた洗浄が実際的 に不必要となる。もし洗浄を行いたいときには、システムが別の理由で停止した ときに行えばよい。By using the additive of the present invention, cleaning that was previously frequently performed is now practical. becomes unnecessary. If the system has stopped for another reason and you want to perform a flush, You can do it from time to time.

上記テストでは、本発明の添加剤を使用後但しテスト開始前にボイラーをクリー ンにした。In the above test, the boiler was cleaned after using the additive of the present invention but before starting the test. I turned it on.

テスト 4 慣用のガス油システムを従来通り作動させた場合、排気ガス中のCO2含有率は 約13%、すす数は1〜2であった。Test 4 When a conventional gas-oil system is operated as usual, the CO2 content in the exhaust gas is Approximately 13%, soot number was 1-2.

実施例2の添加剤(ガス油1tにつき111)を使用してシステムを作動させた 場合、Co2含量は約14.5%、すす数はO〜1であった。The system was operated using the additive of Example 2 (111 per ton of gas oil). In this case, the Co2 content was about 14.5% and the soot number was O~1.

添加剤を使用したことを知らない煙突掃除夫が添加剤を使用後初めて掃除したと きには、煙突が驚(はど完全に乾いており、煙突の底にたまった除去すべき固体 物質の量が極めて僅かであることに驚いた。A chimney sweep who did not know that the additive had been used was cleaning it for the first time after using the additive. When the chimney is dry (completely dry, there is no solids that have accumulated at the bottom of the chimney to remove). I was surprised at how small the amount of the substance was.

従来添加剤を使用しなかったときに比べてボイラーの作動中のノイズや臭いがな いことも知見された。There is less noise and odor during boiler operation compared to when no additives were used. It was also discovered that

テスト 5 古いディーゼル駆動トラックの場合には従来始動の問題があり、通常排気ガスが 生じた。Test 5 Older diesel-powered trucks have traditionally had starting problems and exhaust emissions are typically occured.

実施例3の添加剤をディーゼル油1tにつき1!!添加した場合、8時間駆動後 始動の問題がなくなり、排気ガスの発生もなかった。トラックはより優れた牽引 性(traction)を示した。Add the additive of Example 3 at 1 ton per ton of diesel oil! ! If added, after 8 hours of operation There were no starting problems and no exhaust fumes. Trucks have better traction traction.

国際調査報告international search report

Claims (1)

【特許請求の範囲】 1.1)脂肪酸のマンガン塩, 2)高沸点タール油, 3)ナフタレンと、 所望により下記の追加成分 4)ナフテン酸鉄, 5)塩化第二鉄, 6)脂肪酸のカルシウム塩 の少なくとも1種とを含むことを特徴とする液体燃料用添加剤。 2.脂肪酸のマンガン塩1)が炭素数8〜9の分岐鎖脂肪酸のマンガン塩であり 、高沸点タール油2)がポリ芳香族炭化水素を含む高沸点タール油であってその タール油の35〜50%、好ましくは約40%が400℃の温度までに留出する ことを特徴とする請求の範囲1に記載の添加剤。 3.6成分全てを含むことを特徴とする請求の範囲1または2に記載の燃料油用 添加剤。 4.成分1)〜5)を含むことを特徴とする請求の範囲1または2に記載のガス 油用添加剤。 5.成分1)〜5)を含むことを特徴とする請求の範囲1または2に記載のディ ーゼル油用添加剤。 6.6成分全てを含むことを特徴とする請求の範囲1または2に記載のディーゼ ル油用添加剤。 7.成分6)として炭素数8〜9の分岐鎖脂肪酸のカルシウム塩を含む請求の範 囲1,2,3または6に記載の添加剤。 8.燃料に添加後の燃料1tあたりの活性成分の含量が、成分1)0.008〜 0.08kg(Mn換算),成分2)0.009〜0.09kg, 成分3)0.04〜0.12kg, 成分4)0〜0.05kg(Fe換算),成分5)0〜0.04kg,及び 成分6)0〜0.03kg(Ca換算)であることを特徴する請求の範囲1に記 載の添加剤。 9.成分1)としてHanganese Siccatol(R)を含むことを 特徴とする請求の範囲1〜8のいずれかに記載の添加剤。 10.成分4)として“Nuodex(R)Dryer Iron”及び/又は 成分6)としてCalcium Siccatol(R)を含むことを特徴とす る請求の範囲1〜3,6〜8,9のいずれかに記載の添加剤。[Claims] 1.1) Manganese salts of fatty acids, 2) High boiling point tar oil, 3) Naphthalene and Additional ingredients below as desired 4) Iron naphthenate, 5) Ferric chloride, 6) Calcium salts of fatty acids An additive for liquid fuel characterized by containing at least one kind of. 2. Manganese salt of fatty acid 1) is a manganese salt of branched chain fatty acid having 8 to 9 carbon atoms. , the high-boiling point tar oil 2) is a high-boiling point tar oil containing polyaromatic hydrocarbons; 35-50%, preferably about 40% of the tar oil distills up to a temperature of 400°C The additive according to claim 1, characterized in that: 3.For fuel oil according to claim 1 or 2, characterized in that it contains all of the six components. Additive. 4. The gas according to claim 1 or 2, characterized in that it contains components 1) to 5). Additive for oil. 5. The dill according to claim 1 or 2, characterized in that it contains components 1) to 5). Additive for diesel oil. 6. Diesel according to claim 1 or 2, characterized in that it contains all six components. Additive for oil. 7. Claims containing a calcium salt of a branched chain fatty acid having 8 to 9 carbon atoms as component 6) Additives according to boxes 1, 2, 3 or 6. 8. The content of the active ingredient per 1 ton of fuel after being added to the fuel is 0.008~ 0.08kg (Mn equivalent), component 2) 0.009-0.09kg, Component 3) 0.04-0.12kg, Component 4) 0 to 0.05 kg (Fe equivalent), Component 5) 0 to 0.04 kg, and Component 6) According to claim 1, the amount is 0 to 0.03 kg (calculated as Ca). Additives listed. 9. Contains Hanganese Siccatol (R) as component 1) The additive according to any one of claims 1 to 8, characterized in that: 10. "Nuodex (R) Dryer Iron" and/or as component 4) It is characterized by containing Calcium Siccatol (R) as component 6) The additive according to any one of claims 1 to 3, 6 to 8, and 9.
JP61503293A 1985-06-28 1986-06-11 Additive for liquid fuel Pending JPS62503173A (en)

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DK294485A DK152925C (en) 1985-06-28 1985-06-28 ADDITIVE TO LIQUID FUEL
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105331403A (en) * 2015-10-30 2016-02-17 无棣华信石油技术服务有限公司 Fuel-oil composite energy-saving additive and preparing method thereof

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0763079A1 (en) * 1994-05-31 1997-03-19 ORR, William C. Vapor phase combustion methods and compositions
FR2751662B1 (en) * 1996-07-29 1998-10-23 Total Raffinage Distribution MIXED ORGANOMETALLIC COMPOSITION COMPRISING AT LEAST THREE METALS AND THEIR APPLICATIONS AS ADDITIVES FOR FUELS OR FUELS
DE69907138T2 (en) * 1998-01-15 2004-02-19 The Associated Octel Co. Ltd. FUEL ADDITIVES
JP2001354979A (en) * 2000-06-14 2001-12-25 Ibe:Kk Fuel modifier
US20040074230A1 (en) * 2002-10-16 2004-04-22 Guinther Gregory H. Method of oxidizing soot and reducing soot accumulation in a diesel fuel combustion after treatment system
US8257450B2 (en) 2002-12-18 2012-09-04 Afton Chemical Intangibles Llc Manganese compounds to inhibit both low-and high-temperature corrosion in utility and industrial furnace systems
US7300477B2 (en) 2003-08-14 2007-11-27 Afton Chemical Corporation Method and fuel additive including iron naphthenate
US7332001B2 (en) * 2003-10-02 2008-02-19 Afton Chemical Corporation Method of enhancing the operation of diesel fuel combustion systems
US8177865B2 (en) 2009-03-18 2012-05-15 Shell Oil Company High power diesel fuel compositions comprising metal carboxylate and method for increasing maximum power output of diesel engines using metal carboxylate

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1092461A (en) * 1912-06-05 1914-04-07 Arthur W Swanberg Process of increasing the efficiency of hydrocarbon liquids and the material for effecting such results.
DE3044907C2 (en) * 1980-11-28 1983-07-14 Ruhrchemie Ag, 4200 Oberhausen Use of iron and / or manganese salts of aliphatic carboxylic acids as combustion aids for liquid fuels
AT373274B (en) * 1981-10-12 1984-01-10 Lang Chem Tech Prod ADDITION WITH COMBUSTION-PROTECTING AND SOOT-RESISTING EFFECT OF FUEL OILS, DIESEL FUELS AND OTHER LIQUID FUELS AND LIQUIDS, AND LIQUID FUEL AND FUELS WITH THIS ADDITION

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105331403A (en) * 2015-10-30 2016-02-17 无棣华信石油技术服务有限公司 Fuel-oil composite energy-saving additive and preparing method thereof
CN105331403B (en) * 2015-10-30 2017-07-28 无棣华信石油技术服务有限公司 Fuel oil composite energy-saving additive and preparation method thereof

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