JPS60104190A - Water-incorporated fuel oil and its manufacture - Google Patents

Water-incorporated fuel oil and its manufacture

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Publication number
JPS60104190A
JPS60104190A JP58209960A JP20996083A JPS60104190A JP S60104190 A JPS60104190 A JP S60104190A JP 58209960 A JP58209960 A JP 58209960A JP 20996083 A JP20996083 A JP 20996083A JP S60104190 A JPS60104190 A JP S60104190A
Authority
JP
Japan
Prior art keywords
oil
water
fuel oil
heavy
hydrated
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
JP58209960A
Other languages
Japanese (ja)
Other versions
JPH027353B2 (en
Inventor
Koji Shigemitsu
重光 孝治
Ko Jo
徐 綱
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP58209960A priority Critical patent/JPS60104190A/en
Priority to KR1019840002539A priority patent/KR850003564A/en
Publication of JPS60104190A publication Critical patent/JPS60104190A/en
Publication of JPH027353B2 publication Critical patent/JPH027353B2/ja
Granted legal-status Critical Current

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Classifications

    • 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

Abstract

PURPOSE:To obtain the titled oil of good dispersion stability and high combustion efficiency with little environmental pollution, by incorporating heavy fuel oil with water and aqueous solution containing nonylphenyl polyethylene glycol ether and PVA. CONSTITUTION:The objective fuel oil can be obtained by incorporating (A) 7- 10t of heavy fuel oil with (B) 1-5t of water and (C) 20-80l of an aqueous solution containing (i) 0.01wt% of nonylphenyl polyethylene glycol ether [pref. of formula I (n is 1,500-2,500)] and (ii) 4wt% of PVA [pref. of formula II (n is 500-2,500)].

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は加水燃料油に関シフ、より詳しくは分散相持性
のよい加水燃料油及びその製法に関する。 現在、我が国では石油系燃料の殆んど90係以上を外国
から輸入し、貴重な外貨を消費しているが、その石油資
源は有限のもので、しかもその価格は年々上昇し、供給
欲は減少の順向を示している為、石油を効率よく燃焼せ
しめ、大気汚染等の公害を減少させる必要があることは
周知の事実である。 此の必要性を満たす為に、今日寸で世界各国で多くの研
究者等が種々の努力を重ねて来ておシ、れている「油に
水を加えることにより燃焼効果が上る」という原理を応
用して、油に最適訃の水を加えてエマルジョン燃料をつ
くる試みがなされて米た。 しかしながらその殆んどが経済的に価値が低いか、又は
不安定なものが多く、本来の目的を達せしめるに値いす
るものが見当らないのが現状である。 発明者等は、20年前にソ連の科学者が発表した「水の
粒子の周シを油が囲んだとき、外側の油が未燃焼乃至未
完全燃焼の状態において、水の粒子は熱の伝導作用によ
って気化し、この気化した水蒸気は急激にその体積を増
大して(約5800倍になる)、外側の油を拡散させ、
これを粉々にう微傷理論に着目し、水の粒子の周りに油
の粒子を均一に囲1せ、しかも半永久的に水と油の結合
が持続し、完全燃焼が行われる為原料重油よりも効率が
高く、加えて排出ガスの一酸化炭素が低い燃料を得る事
を研究し、それを可能ならしめたものである。 一般に水素(H2)の化学連鎖反応過程において、適当
なH2OはH2の迅速な反応に有利である事が知られて
いるが、同時にCOの化学連鎖反応過程において適当な
H2OはCOの迅速な反応に有利だという事も知られて
いる。 如(a■なる燃料油もその反応過程において必らずH2
とCOの発生過程があり、燃料油の中に適当なIJ20
を加えると、II2とCOの迅速な反応に効果があって
、燃料油自身の迅速な燃焼にも効果がある事が知られて
いる。 寸だ、H2Oを含1ないCOは燃焼中たくさんの0□を
必要とするが、H2Oを含んだCO′/i燃焼に必訝な
02のilがかなり少くてすむ、即ち含水燃料油は不含
水燃付油より燃焼過程において過剰酸素が比較的少ない
。 同一条件下では含水燃pF混合気は非含水・燃料混合気
より燃焼時間が短かくてすむし、同じ燃焼時間と同じ燃
料混合気の条件下では含水燃料がよりよく完全に燃焼す
るものである。 従ってボイラーの中で燃焼する適当な含水燃料油は不含
水燃1′−1油に比し、より多く、より完全燃焼するも
のである。即ちボイラーの中ですべての燃料油は一定燃
焼条件下においてより良くより完全に燃焼効果を」二げ
るためには燃料混合気中に適当な含水量を与えなければ
なら力い。 此の目的を達成する為に色々な試みはあるが、先述の1
10 <従来のエマルジョン燃料は界面活性剤や乳化剤
の力によってエマルジョンを形成してはいるが、完全な
結合ではないだめ、要求される保存期間に達しなかった
り、経済効果の低いものが殆んどであった。 本発明は、省エネルギーと環境汚染防止のだめに役立つ
加水重油をつくる為に水と重油を完全に結合せしめ、水
と油が分離せずに永く保存され貯蔵運搬にも而1え、燃
焼効率が良く環境汚染のないjJ1気ガスを排出する新
しい加水燃料油及びその製法を提供するものである。 本発明による加水燃料油は、重質燃料油と水とをポリビ
ニルアルコールおよびノニルフェニルポリエチレンダリ
コールエーテルの存在下に分散結合せしめたものであり
、所望により前記加水燃料油はさらに少量のアルカリ金
属塩素酸塩、ディーゼル油又はへ重油からなる群から選
ばれる添加剤を含有することができる。本発明の加水燃
料油は水の一部をエチレングリコール又はエチレングリ
コールと飽和食塩水に換え凍結防止形態にすることがで
きる。 本発明に使用する重質燃料油はB= C重油である。添
加する水の量は重質燃料油7〜10を当り1〜5tであ
る。使用されるポリビニルアルコールは式: %式%] (式中nは500〜2500である) で表わされ、nが約1700であるものが好ましい。ノ
ニルフェニルポリエチレンクリコールニーで表わされ、
nが約2000のものが好ましい。 乳化分散剤のノニルフェニルポリエチレングリコールエ
ーテル(以下NPEGEと表わす)及びポリビニルアル
コール(以下PvAと表わす)はNPEGEo、01%
及びPVA4係を含む水溶液(以下4%P液と称する)
に調製して使用することが好壕しく、重質燃料油7〜1
0tにつき4チP液20〜80を使用される。 アルカリ金属塩素酸塩としては通常塩素酸カリウムが使
用され、これは助燃剤として煤や沈澱物の発生を防止し
、所望により重質窓4目1117〜1゜を当り40〜2
007使用され、予め4重量%の水溶液として添加する
ことが好ましい。 ディーゼル油又はA重油を添加するときは重質燃イ′−
[油7・〜10tにつき1〜251tg使用され、重質
窓4F油がC重油であるときゃ加水用、の多い場合に初
期へ火を助け、舶用等の大きい内燃機関に用いる場合に
必要である。 本発明の加水燃料油の配合例は次の如くである。 A) B重油9〜11t、例えば10tに対し水1〜5
t、例えば2t、と4%P液3o〜4ot、例えば40
 t。 B) C重油9〜lit、例えば10tに対し水2.5
〜3.5t、例えば3t24%P液25〜35t、例え
ば30を及び4%KCtO3水溶液4kg。 c) C重油6.5〜7.5t、例えば7tに対し水2
.5〜3.5t、例えば3L14係P液25〜35t、
例えば30t、4%KCl−03水溶液2J31tg及
びディーゼル油10〜131cg、例えば13/cg。 D) C重油7.5〜8.5t、例えば7tに対し水1
.8〜2.2t、例えば2t、4%P液25〜35t1
例えば30t、4チKCtO3水溶液2.81tg及び
へ重油10〜12kg1例えば111tg。 E) C重油9.5〜10.5t、例えば10tに対し
71(3,5〜4.5L、例えば4t14チP液25〜
35t、例えば3′0ム4係KCt03水溶液4kg及
びディーゼル油又はA重油18〜221cg、例、えば
201tg。 上記配合例において、Bi油の場合に、A) B [f
i油10tに対し水2を及び4%P液4゜ム C重油の場合に。 B) C重油Lotに対し水3t、4%P液30t、4
%KC6O3水溶液4 kg及びA重油又はディーゼル
油201tg、 とすることができる。 本発明の前記加水燃料油の冬季の凍結を防止するだめ、
前記配合において添IIIする水の2〜15係をエチレ
ングリコールで置換することができる。 この場合エチレングリコールで置換する水の量は気温に
より次のように変えることができる。 気 温 置換量 0〜−10℃ 2〜5% −10〜−20℃ 5〜10係 −20℃以下 10〜15係 さらに上記エチレングリコールを8量に減じ仕上った加
水重油の11−ンにつき40〜400 ccの飽和食塩
水を添加する事により天候気温に左右されない安定した
製品を得ることができる。 本発明の加水燃料油は次のように製造される。 攪拌機を設けたジャケット付容器中で加温した水にポリ
ビニルアルコールを溶解し、これにノニルフェニルポリ
エチレングリコールエーテルヲ添加してノニルノエニル
ポリエチレンクリコール0.01%を介有する4係ポリ
ビニルアルコール溶液を調製する。このm液の所定肘を
40〜50℃に加温した別容器の水に攪拌しながら加え
、これを、又別な攪拌機付容器で40〜50℃に加温1
−だ所定鼠の重質油に添加し、約20分間攪拌混合して
製品を得る。必要に応じ4%KCto3浴液やディーゼ
ル油を加えて混合する。重質燃料油への前記4%P液を
゛添加した水の添’、IJlは噴霧化して行なうのが好
ましい。 本発明の加水燃料油は次表に示すような性質を有する。 表 実際の損失 11〜17% 2〜せいぜい5%バーナ一
温度 約1,120’C約1o6o〜1o8o℃点火容
易性 低い 高い 従来の水と油の混合物、例えば燃料油にアルコールや水
を混合したもの、米国詩作A4158551のように、
せいぜい22係の水と陰イオンのethoxylate
dalkylphenol (エトキシアルキルフェノ
ール)とからなる乳化剤を使用する方法が公表されてい
るが、これらは能率乃至効率の犠牲が伴い、その混合物
は濁っていて結合が破れて分離する。今迄に知られる限
りでは、水の粒子と油の粒子が完全に結合し、それがタ
ンクに貯蔵された時あるいは道路上で運搬された時を問
わず、分離しないという特性を得るに至らず、又燃焼に
おいて断火不完全燃焼のために効率と性能に損失を力え
ないものは完成されていな゛い。 これに反し、本発明の加水燃料油は実施例にみられる」
:うに、極めて安定で長期間の保存にも耐え、運搬する
際にも(それが道路上、パイプ中を問わず)水と油が分
離するという事がなく、燃焼に除しては完全燃焼をする
ため、エネルギー損失の原因であるススやタールの発生
がなく、逆に炉壁に沈着する本来なら当然エネルギーに
なるべきもの迄燃焼させて取り除く事が百丁能である。 又そのυV出ガスの一酸化炭素量は水による重油の部分
的な代用のだめ低下されるばかシでなく、排出ガスの中
のSO3窒素酸化物、不燃炭山水素等は低下され、エネ
ルギー節約の有利性をもたらす外、環境保全にも役立つ
ものである。又析出物や腐蝕をバーナーや炉壁におこさ
せない有利性もある。 即ち従来の重油よりも本発明の加水重油は完全燃焼によ
る゛エネルギーの高利用の池、燃焼装置の寿命を延ず効
果もあり、本質的にエネルギーコストのう1き下げを可
能とする。 本発明に使用する添JJO剤、は添加剤の歌が液受でし
かも極めて価格が安く、我が国において大量に生産し、
廉価に輸出されているものであるばかりでなく、此の方
法によって製出された新しい加水燃料油は、使用さ扛る
燃焼製置に限界を要求しないし、熱エネルギーを必要と
するあらゆる分野に従来の重油と同様に使用出来るもの
である。 しかも運殿中と貯蔵中を問わず、水と油の粒子の結合が
均一安定で分離しないものである。 本発明の加水燃料油の製造方法並びにそれにか\る雑加
剤は、従来の無加水重油のみにては期待出来ない完全燃
焼と、それに伴う100係に近い熱効率が期待され、し
かも環境保全l1好ましいクリーンな排気ガスを排出し
、燃焼機器の寿命をのばす効果があり、すくなくとも燃
vi費の20%以上を節約出来る。本発明は70年も前
に知られた油に水を加えれば燃焼効果が上る原理と、こ
れを最も効果的に水の動きを引き出すだめの微傷理論を
実際に最も安い経費と簡単な方法で実現し解決したもの
で、これが実施により社会的国家的に多大な経済効果を
挙げるであろう。 実施例に 重構造になって内壁と外壁の間に蒸気を通じて間接的に
加熱出来る攪拌機f;」の釜に水10tを入れ、これを
90〜100℃にυ1」鰭しながら、攪拌翼を80〜1
00 r 、p、rnの速度で回転させなからPVA(
重合度1700のポリビニールアルコール)粉末400
yを除々に投入し、完全に溶解させ、これに二人i4の
ノ二一ルフエニールポリエチレンクリコールエーテルを
加fてノニルフェニルポリエチレングリコール0.01
%を含む4チP液をつくる。次に加温用の水蒸気パイプ
(蛇管)を装置した大きな容器に10 tonのB重油
を入れ、40〜50℃に温めてから、又別な容器にて4
0〜50℃に温めだ水2 tonに対し3otの4ZP
液を投入して充分混合せる水プラス41P液を除々に出
来れば噴霧状にして添加し、500〜120Or;’p
、rnの゛速度で約20分間攪拌混合して新しい加水燃
制油約12 tonを得た。此の加水燃料油は燃焼に頓
し無加水重油よりもその燃焼に多くの酸素を必要とせず
、南九州公害研究所の計量1直で示す通り(表2)、そ
の排出ガスのCO2値が高く、残存02量は少い。又無
加水重油よりも1を当シの蒸発計が大きく、排ガス温度
が低い事はボイラー(燃焼機関)の熱効率が犬なること
を示した。また表(1)の福岡県工業試験場の試験によ
れば、20係の水が加えられているにもがかわらず、そ
の熱量は無加水−重油が10470 catであるのに
対し、20係加水燃料油は、1019 oeatである
ことは如何に省エネ効果をもたらすががうががえる。 表1 (福岡県福岡工業試験場委託試験結果)B重油 
本発明の加水燃料油 カロリー(cat)1 0470 1 01 90表2
 排気ガスの比較(南九州公害分析センター委託試、験
結果) 加水燃4F油 A重油 JJ1出Jjス量(湿’) )、N% 210 300
〃 (乾き)、y’iH1so 280排気ガス温度、
℃ 157 211 排出ガス組成、係 CO21−2,68,4 o23.9 11.4 C〇 − 表3 排気ガスの比較(何升動力技研委託試験結果)A
重油 本発明の加水燃料油 制用ガス CO210% 13% 温度 230℃ 210℃ ボイラー効率 87% 90.5係 表4 ボ、イラ燃焼による蒸発量試験 (何升動力技研委託試験結果) ■を当りの蒸発水量 A重油 11.28I−(昭585/′i8〜5/23
)■3重油 11.25t(昭586/1〜6/4)本
発明の加水燃料油 11.95t(昭585/24〜F
y29)(同一条件 同一 ボイラーによる試験)実施
例2 実/Ii!1例1と同様の装置及び方法で、C重油1゜
tonに対し、水3 ton、4ZP液(0,01%ノ
ニルフェニルポリエチレンクリコールエーテルヲ含む)
25t、4 kgの4 % KClO3水溶液、201
cgのA重油を加えて新しい加水重油約13 tonを
得た。 此の加水C重油の燃焼効果も実施例1で得た加水燃料油
と同様のすばらしい結果を得る事が出来た。 実施例3 実施例1の配合において使用した水2t、onの内、4
0Lをエチレングリコールで置換し以下同様の操作工程
を経てつくった加水燃料油1d−15℃の冷凍能力のあ
る庫内にその一部を容器に取って一昼夜放置しても尚凍
結現象が見られなかった。 実施例4 又実施例3において水と置換するエチレングリコールを
17/2にへらし、代りに飽和食塩水480 ccを加
え攪拌混合して得た製品は同法の冷凍試験において凍結
が免かれ実施例1で得だ製品と何等変らぬ好結果が得ら
れた。 上記各実施例、からとった放置試料は現在1で成分の分
離がみられない。 手続性0正書(自発) 昭和58年11月 15日 特許庁長官 若杉 和犬 殴 1 事件の表示 −・ 1.2′〆・)′ 〆′ / 
・ 昭和58年11月10日提出の特許願 2 発明の名称 加水燃料油およびそのIIl法 3 補正をする者 事件との関係 特許出願人 熊本県熊本市神水1の14の50 重 光 孝 治 4代理人 東京都千代田区五番町2番地4 5 補正命令の日付 tIJ細書の発明の詳細な説明の欄 ′7 補正の内容 本願明細書の記載事項の一部を下記のとおり補正する。 記 (1) 明細書第11頁第11行の「ノニルフェニルポ
リエチレングリコール」とあるのをrノニルフェニルポ
リエチレングリコ−ル工−テル」と補正する。 (2)同書第13頁第12行の「縮少」とあるのを、「
僅少」と補正する。 (3) 同書第15頁第1行および第2行の[ノニルフ
ェニルポリエチレングリコールJとあるのを、「ノニル
フェニルポリエチレングリフールエーテル」と補正ずろ
。 なお、補正の対象の欄に記載した事項以外は内容に変更
はない。 一′r−糸プdネ市1−1ミー書 (自発)昭和59年
3月21[] 特、t′1庁長官 若杉 和犬 殿 1 °1−件の表示 昭和58年特許願第209960号 2 11の名称 加水燃料油およびその製法 3 補11:をする者 ・II性との関係 特許出願人 l′fヒ本県能本山神水lの14の50小 光 孝 R
j 4 代理人 東4;(都T代111(メIL番町2番11!!45 
補11命令の11付 1」発補;1− 6 祁i +Eの対象 明M11 NSの特許請求の範囲および発明の詳細な説
明の各欄。 7 補lFの内容 本願発明に(Aし、別紙のとおり明細書の全文を補正す
る・ なお、Ni +[−の対象の欄に記載したl’4以外は
、内容に変更はない。 明 細 書 1、発明の名称 加水燃料油おJ、びイの製法 特許請求の範囲 (1)手賀ブ然オ’l f+17へ・1()」につさ、
水1へ、 5i Lどボリビニルフlルー1−ルー1%
からなる水溶液20〜80琵とを含む加水燃111油。 (2)前記ポリビニルノ/ル:」−ルが式1式%) @1問第1項記載の加水燃料油。 (3)前記の水の約2〜15%の吊を同♀の土ヂレング
リ]−ルC1iff 1条し!、二、l:I !llフ
ン1七範囲第114’週又は第2項記載の加水燃料油。 (4)前記土fレングリ」−ルの川を最大1/2ωまで
減じ、製品1L当り40・〜400ccの飽和食塩水ぐ
置換しでなる、特許請求の範囲第3項記載の加水燃料油
。 (5)所定量のポリビニルアルコールを水μ溶解しCポ
リビニルアル]−ル4%水溶液を調製し、すj゛イーゼ
ル油はへ重油からなる群がら選は゛れる添加剤どどもに
あらかじめ加ン品された重質燃料油に加え(均一に分散
結合さけることを14徴とJる加水燃料油の製法。 3、発明の詳細な説明 木兄明は加水燃料油に関し、より詳しくは分散結合の安
定な、燃焼効率がよくかつ環境汚染の少41′い燃11
特性のJ、い加水燃料油Jj J、びイの製法に関りる
。 規イ1、我が[Uぐは石油系燃料の殆んど9式%以上4
外田から輸入し、肖重な外C1を消費ししいるが、−f
のイ1油資源4.LイJ限のもので、しかもその価格は
イI//1シ1し、供給量は減少の傾向を示し−Cいる
為、イi油を効率J、く燃焼Iしめ、人気汚染着の公害
を減少させる必要があることGユ周知の事実である。 此の必要性を満だ一4為に、今日まで世界各国で多くの
(ill究者等が種々の努力を重ねて来ており、その/
1F)Aどして燃焼効率を高めるための装置の数色、燃
料油供給法の改良とか、70年も前から知られ(いる[
油に水を加えることにより燃焼効果が]−る」という原
理を応用し−(、油に最適量の水を加えて■マルジjン
燃石をつくる試みがなされて来/j。 しかしながらイの殆んどが杼演的に価値がII(いか、
又tよ不安定<t bのが多く、本来の[」的を達lし
めるにM、iいりるしのが見当ら4jいのが現状Cある
。 弁明者等は、2()1萌にソ連の科学者が弁表した1水
の粒子の周りを油が囲lυだとさ、外側の油が未燃焼乃
至未完全燃焼の状fぷにおいて、水のδ゛1子
The present invention relates to a hydrated fuel oil, and more particularly to a hydrated fuel oil having good dispersion compatibility and a method for producing the same. Currently, our country imports more than 90% of its petroleum-based fuels from foreign countries, consuming valuable foreign currency, but its petroleum resources are limited, and the price is rising year by year, and the appetite for supply is decreasing. It is a well-known fact that there is a need to burn oil more efficiently and reduce air pollution and other pollution, as it is showing signs of decreasing. In order to meet this need, many researchers around the world are currently making various efforts to develop the principle that ``adding water to oil increases the combustion effect.'' Attempts have been made to create emulsion fuel by applying this method and adding water from dead bodies to oil. However, most of them have low economic value or are unstable, and the current situation is that we cannot find anything worthy of achieving the original purpose. The inventors are based on a statement made by Soviet scientists 20 years ago: ``When a water particle is surrounded by oil, and the oil on the outside is unburned or incompletely combusted, the water particle loses heat. It is vaporized by conduction, and this vaporized water vapor rapidly increases its volume (approximately 5800 times) and diffuses the oil on the outside.
Focusing on the theory of fine scratches, oil particles are evenly surrounded around water particles, and the combination of water and oil continues semi-permanently, resulting in complete combustion, which is better than raw heavy oil. This research has made it possible to obtain a fuel with high efficiency and low carbon monoxide emissions. It is generally known that in the chemical chain reaction process of hydrogen (H2), an appropriate amount of H2O is advantageous for the rapid reaction of H2, but at the same time, in the chemical chain reaction process of CO, an appropriate amount of H2O is advantageous for the rapid reaction of CO. It is also known that it is beneficial for In the reaction process, fuel oil such as
There is a process of generating CO and IJ20 in fuel oil.
It is known that the addition of fuel oil has an effect on the rapid reaction between II2 and CO, and is also effective on the rapid combustion of the fuel oil itself. In fact, CO that does not contain H2O requires a lot of 0□ during combustion, but the amount of 02 that is required for combustion of CO'/i that contains H2O is considerably smaller. There is relatively less excess oxygen in the combustion process than with hydrous fuel oil. Under the same conditions, a hydrous fuel pF mixture takes less time to burn than a non-hydrous fuel mixture, and for the same combustion time and the same fuel mixture, a hydrous fuel burns better and more completely. . Therefore, a suitable hydrous fuel oil for burning in a boiler will be more abundant and burn more completely than a non-hydrous fuel 1'-1 oil. That is, all fuel oils in a boiler must have an appropriate moisture content in the fuel mixture to achieve better and more complete combustion under certain combustion conditions. There are various attempts to achieve this goal, but the first one mentioned above
10 <Conventional emulsion fuels form emulsions using the power of surfactants and emulsifiers, but most of them do not have a complete bond and do not reach the required shelf life or have low economic efficiency. Met. The present invention completely combines water and heavy oil to create hydrated heavy oil, which is useful for energy saving and prevention of environmental pollution.The water and oil can be stored for a long time without separating, can be stored and transported, and has good combustion efficiency. The present invention provides a new hydrated fuel oil that emits JJ1 gas without environmental pollution and a method for producing the same. The hydrated fuel oil according to the present invention is obtained by dispersion bonding heavy fuel oil and water in the presence of polyvinyl alcohol and nonylphenyl polyethylene dalicol ether, and if desired, the hydrated fuel oil further contains a small amount of alkali metal chlorine. It may contain additives selected from the group consisting of acid salts, diesel oil or heavy fuel oil. The hydrated fuel oil of the present invention can be made into an antifreeze form by replacing part of the water with ethylene glycol or ethylene glycol and saturated saline. The heavy fuel oil used in the present invention is B=C heavy oil. The amount of water added is 1 to 5 tons per 7 to 10 tons of heavy fuel oil. The polyvinyl alcohol used is represented by the formula: %Formula %] where n is from 500 to 2,500, preferably about 1,700. Represented by nonylphenyl polyethylene glycolny,
Preferably, n is about 2000. Nonylphenyl polyethylene glycol ether (hereinafter referred to as NPEG) and polyvinyl alcohol (hereinafter referred to as PvA) as emulsifying and dispersing agents are NPEGEo, 01%.
and an aqueous solution containing PVA4 (hereinafter referred to as 4% P solution)
It is preferable to prepare and use heavy fuel oil 7 to 1.
20-80 g of 4-chi P liquid is used per 0 t. Potassium chlorate is usually used as the alkali metal chlorate, and it acts as a combustion improver to prevent the generation of soot and sediment.
007 is used and is preferably added in advance as a 4% by weight aqueous solution. When adding diesel oil or A heavy oil, use heavy fuel
[1 to 251 tg is used per 7 to 10 t of oil, and if the heavy window 4F oil is C heavy oil, it is used for adding water. It helps the initial stage of fire when there is a lot of oil, and is necessary when used in large internal combustion engines such as ships. . A blending example of the hydrated fuel oil of the present invention is as follows. A) 9 to 11 tons of B heavy oil, for example 1 to 5 tons of water to 10 tons
t, e.g. 2t, and 4% P solution 3o-4ot, e.g. 40
t. B) C heavy oil 9 to liter, for example 10 tons to 2.5 liters of water
~3.5t, e.g. 3t24% P liquid 25-35t, e.g. 30 and 4kg of 4% KCtO3 aqueous solution. c) 6.5 to 7.5 t of C heavy oil, e.g. 7 t to 2 t of water
.. 5-3.5t, for example 3L14 P liquid 25-35t,
For example, 30t, 4% KCl-03 aqueous solution 2J31tg and diesel oil 10-131cg, for example 13/cg. D) 7.5 to 8.5 t of C heavy oil, for example 1 ton of water to 7 t
.. 8-2.2t, e.g. 2t, 4% P liquid 25-35t1
For example, 30 tons, 2.81 tg of 4-chi KCtO3 aqueous solution and 10 to 12 kg of heavy oil, for example 111 tg. E) C heavy oil 9.5-10.5t, for example 10t, 71 (3.5-4.5L, for example 4t14chi P liquid 25-
35t, e.g. 4kg of 3'0m4 KCt03 aqueous solution and 18-221cg of diesel oil or A heavy oil, e.g. 201tg. In the above formulation example, in the case of Bi oil, A) B [f
In the case of 10 tons of I oil, 2 parts water, 4% P liquid, 4°m C heavy oil. B) 3 tons of water, 30 tons of 4% P liquid for C heavy oil lot, 4
%KC6O3 aqueous solution 4 kg and A heavy oil or diesel oil 201 tg. To prevent the hydrated fuel oil of the present invention from freezing in winter,
In the above formulation, 2 to 15 portions of the added water can be replaced with ethylene glycol. In this case, the amount of water replaced with ethylene glycol can be changed depending on the temperature as follows. Temperature Replacement amount 0 to -10°C 2 to 5% -10 to -20°C 5 to 10 ratio -20°C or less 10 to 15 ratio The amount of ethylene glycol was further reduced to 8, and the amount of ethylene glycol was reduced to 8. By adding ~400 cc of saturated saline, a stable product that is not affected by weather and temperature can be obtained. The hydrated fuel oil of the present invention is produced as follows. Polyvinyl alcohol was dissolved in heated water in a jacketed container equipped with a stirrer, and nonylphenyl polyethylene glycol ether was added thereto to obtain a 4-functional polyvinyl alcohol solution containing 0.01% of nonylnoenyl polyethylene glycol. Prepare. A predetermined amount of this M solution was added to water in a separate container heated to 40-50℃ with stirring, and this was heated to 40-50℃ in another container with a stirrer.
- Add to the specified heavy oil and stir and mix for about 20 minutes to obtain the product. If necessary, add 4% KCto3 bath liquid or diesel oil and mix. It is preferable that the ``addition of water containing the 4% P liquid'' to heavy fuel oil, IJl, be carried out by atomization. The hydrated fuel oil of the present invention has properties as shown in the following table. Table Actual Losses 11-17% 2-5% at most Burner Temperature Approx. 1,120'C Approx. Something like American Poetry A4158551,
At most 22 units of water and anion ethoxylate
Methods using emulsifiers consisting of dalkylphenol (ethoxyalkylphenol) have been published, but these come at the cost of efficiency and the mixture is cloudy and separates due to bond rupture. As far as is known so far, it has not been possible to obtain the property that water particles and oil particles combine completely and do not separate, whether they are stored in tanks or transported on the road. Furthermore, no combustion engine has been perfected that does not suffer losses in efficiency and performance due to incomplete combustion due to intermittent combustion. On the contrary, the hydrated fuel oil of the present invention is shown in the Examples.
: Sea urchin is extremely stable and can withstand long-term storage.Water and oil do not separate when transported (whether on the road or in pipes), and when compared to combustion, it burns completely. Therefore, there is no generation of soot or tar, which causes energy loss, and on the contrary, it is possible to burn and remove even the substances deposited on the furnace wall that should naturally be used as energy. In addition, the amount of carbon monoxide in the υV output gas is not only reduced due to partial substitution of heavy oil with water, but also the amount of SO3 nitrogen oxides, unburnt coal mine hydrogen, etc. in the exhaust gas is reduced, which is advantageous for energy saving. In addition to providing sex, it is also useful for environmental conservation. It also has the advantage of not causing deposits or corrosion on the burner or furnace walls. That is, compared to conventional heavy oil, the hydrated heavy oil of the present invention has the effect of achieving high utilization of energy through complete combustion, extending the life of combustion equipment, and essentially making it possible to lower energy costs. The additive JJO agent used in the present invention is a liquid receiver and is extremely inexpensive, and is produced in large quantities in Japan.
In addition to being exported at a low price, the new hydrated fuel oil produced by this method does not require any limitations on the combustion equipment in which it is used and is suitable for all fields requiring thermal energy. It can be used in the same way as conventional heavy oil. In addition, the bond between water and oil particles is uniform and stable and does not separate, regardless of whether it is in the container or during storage. The method for producing hydrated fuel oil of the present invention and its miscellaneous additives are expected to achieve complete combustion, which cannot be expected with conventional non-hydrated heavy oil alone, and associated thermal efficiency close to 100%, and are environmentally friendly. It has the effect of emitting preferable clean exhaust gas, extending the life of combustion equipment, and saving at least 20% or more of fuel consumption. The present invention is based on the principle known 70 years ago that adding water to oil improves the combustion effect, and the theory of slight scratches to bring out the movement of water in the most effective way. This has been realized and resolved, and its implementation will have a huge economic effect socially and nationally. In an example, 10 tons of water was put into a pot of a multi-layered stirrer that could be indirectly heated by passing steam between the inner and outer walls, and heated to 90 to 100 degrees Celsius with stirring blades of 80℃. ~1
PVA (
Polyvinyl alcohol (polymerization degree 1700) powder 400
Gradually add y and dissolve it completely, add 4 y of nonylphenyl polyethylene glycol ether to make 0.01 of nonylphenyl polyethylene glycol.
Make a 4-chiP solution containing %. Next, put 10 tons of heavy oil B into a large container equipped with a heating steam pipe (serpentine pipe), warm it to 40-50℃, and then transfer it to another container for 4 hours.
3 tons of 4ZP for 2 tons of water warmed to 0-50℃
Pour in the liquid and mix thoroughly. Add the water plus the 41P liquid gradually, preferably in the form of a spray, and add 500 to 120 Or;'p.
, rn for about 20 minutes to obtain about 12 tons of new hydrostatic fuel oil. This hydrated fuel oil requires less oxygen to burn than unhydrated heavy oil, and as shown in the first measurement at the Minamikyushu Pollution Research Institute (Table 2), the CO2 value of its exhaust gas is lower. The amount of remaining 02 is small. In addition, the evaporometer of this type was larger than that of unhydrated heavy oil, and the exhaust gas temperature was lower, indicating that the thermal efficiency of the boiler (combustion engine) was lower. Furthermore, according to the test conducted by the Fukuoka Prefectural Industrial Research Institute in Table (1), even though 20 parts of water is added, the calorific value is 10,470 cat for unhydrated heavy oil, whereas the calorific value of heavy oil with 20 parts of water is 10,470 cat. The fact that the fuel oil is 1019 oeat is a great way to save energy. Table 1 (Fukuoka Prefecture Fukuoka Industrial Testing Station commissioned test results) B heavy oil
Hydrogenated fuel oil calories (cat) of the present invention 1 0470 1 01 90 Table 2
Comparison of exhaust gas (Test commissioned by Minami Kyushu Pollution Analysis Center, test results) Hydrogenated fuel 4F oil A heavy oil JJ1 output amount (humid)), N% 210 300
〃 (dry), y'iH1so 280 exhaust gas temperature,
℃ 157 211 Exhaust gas composition, CO21-2,68,4 o23.9 11.4 C〇 - Table 3 Comparison of exhaust gas (results of tests commissioned by Power Engineering Research Institute) A
Heavy oil Hydrated fuel oil gas of the present invention CO2 10% 13% Temperature 230°C 210°C Boiler efficiency 87% 90.5 Table 4 Evaporation test by Bo and Ira combustion (results of test commissioned by Power Engineering Research Institute) Evaporated water amount A heavy oil 11.28I- (1985/'i8 to 5/23
) Triple heavy oil 11.25t (1986/1-6/4) Hydrogenated fuel oil of the present invention 11.95t (1986/24-F
y29) (Test using the same boiler under the same conditions) Example 2 Actual/Ii! 1 Using the same equipment and method as in Example 1, 1 ton of heavy oil C, 3 ton of water, and 4ZP liquid (containing 0.01% nonylphenyl polyethylene glycol ether).
25t, 4 kg of 4% KClO3 aqueous solution, 201
cg of A heavy oil was added to obtain about 13 tons of new hydrated heavy oil. The combustion effect of this hydrated C heavy oil was also excellent, similar to that of the hydrated fuel oil obtained in Example 1. Example 3 Of the 2 tons of water used in the formulation of Example 1, 4
Even if a portion of the hydrated fuel oil 1d, which was prepared by replacing 0L with ethylene glycol and following the same steps, was placed in a container with a freezing capacity of -15°C and left overnight, no freezing phenomenon was observed. There wasn't. Example 4 Also, in Example 3, the ethylene glycol to be replaced with water was reduced to 17/2, and 480 cc of saturated saline was added instead and mixed with stirring.The product obtained did not freeze in the freezing test of the same method, and was evaluated as an example. Good results were obtained that were no different from the products obtained with 1. As for the samples taken from each of the above-mentioned Examples, no separation of components was observed in sample 1. Procedurality 0 official document (spontaneous) November 15, 1981 Commissioner of the Japan Patent Office Wakasugi Wanu Hitting 1 Display of the incident −・ 1.2′〆・)′ 〆′ /
・Patent application 2 filed on November 10, 1988 Name of the invention Hydrated fuel oil and its relation to the case of the person making the amendment 3 Patent applicant Takaharu Shigemitsu, 1-14-50, Shinsui, Kumamoto City, Kumamoto Prefecture 4 Agent 2-4 Goban-cho, Chiyoda-ku, Tokyo 5 Date of amendment order t Column for detailed explanation of the invention in IJ specification '7 Contents of amendment Part of the matters stated in the specification of the present application will be amended as follows. (1) On page 11, line 11 of the specification, the phrase "nonylphenyl polyethylene glycol" is amended to read "r-nonylphenyl polyethylene glycol". (2) The word “reduction” on page 13, line 12 of the same book was replaced with “
I am corrected by saying, ``Minor.'' (3) In the same book, page 15, lines 1 and 2, [nonylphenyl polyethylene glycol J] was corrected to "nonylphenyl polyethylene glycol ether." There are no changes to the content other than the matters stated in the column subject to amendment. 1'r-Ito Pdne City 1-1 Me (Spontaneous) March 21, 1980[] Special, t'1 Agency Director Wakasugi Wainu 1 ° 1- Display of 1988 Patent Application No. 209960 No. 2 Name of 11 Hydrated fuel oil and its manufacturing method 3 Supplement 11: Relationship with the person who does it and the II nature Patent applicant l'f Himoto Prefecture Nohmoto Yamashinsui l 14-50 Ko Mitsutaka R
j 4 Agent Higashi 4;
Supplement 11 of Instruction 11 Appendix 1; 1-6 Qi +E subject matter M11 NS Claims and Detailed Description of the Invention columns. 7. Contents of Supplement 1F (A) The entire text of the specification is amended as shown in the attached sheet. There is no change in the content except l'4 written in the column of subject of Ni + [-.Details Book 1, Name of the invention Process for manufacturing hydrated fuel oil Claims (1) Tega Buzeno'l f+17 to 1()''
To water 1, 5i L polyvinylfluor 1-1%
Hydrogenated fuel 111 oil containing 20 to 80 liters of an aqueous solution consisting of. (2) The polyvinyl resin: 1%) @1 The hydrated fuel oil described in item 1. (3) Add about 2 to 15% of the above water to the same soil. ,2,l:I! 17 Range 114' week or the hydrated fuel oil according to paragraph 2. (4) The hydrated fuel oil according to claim 3, wherein the water content of the soil is reduced to a maximum of 1/2 ω and replaced with 40 to 400 cc of saturated saline per liter of product. (5) A predetermined amount of polyvinyl alcohol was dissolved in water to prepare a 4% aqueous solution of polyvinyl alcohol, and additives selected from the group consisting of easel oil and heavy oil were added in advance. In addition to heavy fuel oil, a method for producing hydrated fuel oil (which includes uniformly avoiding dispersion bonds). 3. Detailed description of the invention 41' Burning fuel with high combustion efficiency and low environmental pollution11
It is concerned with the production method of hydrated fuel oil Jj J, which has the characteristics. Rule 1: Most of the petroleum-based fuels contain 9% or more.
It is imported from Sotoda and consumes the heavy Soto C1, but -f
1. Oil resources 4. Since it is limited to L and J, and its price is I//1, and the supply is showing a decreasing trend, it burns the oil more efficiently and makes it a popular pollutant. It is a well-known fact that pollution needs to be reduced. In order to satisfy this need, many ill researchers have been making various efforts in various countries around the world to date.
1F) A Several types of devices to increase combustion efficiency and improvements to fuel oil supply methods have been known for 70 years.
Attempts have been made to create margin fuel by adding an optimal amount of water to oil by applying the principle that adding water to oil produces a combustion effect. Most of them are worth II (squid,
In addition, there are many situations where t<t b is unstable, and the current situation is that C cannot find a sign that requires M or i to achieve the original target. The apologists argue that oil surrounds a particle of water, as described by a Soviet scientist in 2010, and in a state where the outer oil is unburned or incompletely combusted, δ゛1 child of water

【、1.
熱の仏心作用にJ、つく瞬+1.’lに気化し、この気
It。 しlJ氷魚気はだ!激にその1本拍を増大して(約51
1 (l 01)−にtrる)、外側の油の粒子を−ぞ
の拡散上ネルギーによっ(更に微細にりるという霧化現
象を起し、より完全な燃焼(ごlフスになる」という微
jM理論に′?S[1し、水の拉rの周りに油の粒子を
均一・に囲よU、しかし半永久的に水とi+l+の結合
が持続し、完全燃焼が行われる為原料手簡より−し効率
が高く、加え−U 111出ガスの一酸化炭素が11(
い燃料を17る事を(il+究し、−ξれを11能なら
しめたb (J) Cある。 −・81に水XS(++2>の化学連鎖反応過程におい
−(、適当’−c H20は1−12の迅速な反応に右
利であるUlが知られているが、同+131c COの
化学連鎖反応過程にJ3いて適当なIf20t、tco
の迅速な反応にfJ刊だという事も知られている。 υ1111なる燃11i1油−bぞの反応過程にJ3い
て必らず112どCOの発生過程があり、燃lIl油の
中に適当な11,0を加えると、142とCOの迅速な
反応に効果があって、燃料油白身の迅速な燃焼にも効果
がある事が知られでいる。 また、H2OをaまないCOは燃焼中たくさんの02を
必要どりるが、l−120を含んだCOは燃焼に必要な
02の量がかなり少り−(りむ、即ち含水燃料油は不含
水燃f1油にり燃焼過程においC過剰酸素が比較的少な
い。 同−条イ71上では含水燃第1混合気は]1合水燃料混
合気より燃焼時間が短かくてりむし、同じ燃焼時間と同
じ燃料混合気の条1′[下では含水燃料がよりJ、く完
全に燃焼づるものである。 ILL−)でボイラーの中′C燃焼りる適当なa水域石
油tよ不含水L!i 1:tl油に比し、J、り多く、
より完全燃焼りるらのである。即ちボイラーの申(・リ
ベ−Cの燃料油は一定燃焼条fl Fに+3いてJ、り
良くJ、り完全に燃焼効果を−にけるためには燃i11
混合気中に適当な含水量を!jえ41(〕ればならない
。 此の目的を達成りる為に色々な試みはあるが、先述の如
く従)1この」−フルジ」ン燃オ゛:1はW面活性剤\
゛】乳1ヒ剤の力にJ:ってJ−マルジョンを形成しく
はいるが、完全41結合(はない/qめ、要求される保
(j 1111聞に達しなかったり、経済効果の低いも
のが殆んどぐあっIC1゜ 不発明番よ、省J−ネル丁−ど環境汚染防止の!こめに
役立つ加水りi al+をつくる為【、二本ど重油を完
全に結合lしめ、水ど油が分l18Il 1! 4’に
長く保存され貯蔵運搬にし耐え、燃力′d効率が良く環
境汚染のないIJI気ガスを1出りる新しい加水燃料油
及びその製;人を1足供Jるbのぐある。 本発明にJ、る加水燃料油は、i、ll!質燃オ゛」油
ど水どをポリビニルアルコールの存在下に分散結合uし
めたもの−Cあり、所望により前5d加水燃11油はさ
らに生伍のゲイ−ビル油又はへ重油からなる群から選ば
れる添加剤を含有Jることかひきる。本発明の加水量S
31油は水の一部を]−ブレングリコール又G;U ]
:ブレングリ」−ルど飽和食塩水に換え凍結防止形態に
JることがCさる。 本発明に使用りる重質燃料油は1−3、C重油で゛ある
。添加りる水のmlよ重11燃石油7〜10を当り1−
、.51て゛ある。使用されるポリビニルアル」−ルl
j j−’C: (C112・CIl (011’) −) 。 (表わされ、11が約1700であるしのが好ましい。 ポリビニルアルコール(以下P VΔと表わツー)は1
)VΔ4%を含む水溶液(」ス下4%P液と称する)に
調製し4使用することが好ましく、重質燃料油7へ・1
01につぎ4%P波20〜80文使用される。 1″イーLル油又(よΔ重油を添加りるときはΦ負燃1
31油7〜10tにつぎ1〜2!Jg使用され、重質燃
料油がC重油であるときや加水量の多い場合に初明魚火
を助り、舶用等の人さい内燃(幾関に用いる場合に必要
ひある。 本発明の加水燃I::1油の配台例は次ぎの如くである
。 △) B重油9−1111例;tl;[101,KIJ
 二水1 ”・E) t N例えば21、ど11%+〕
液3O−ho 1、Mえぽ40文。 +3 ) Ci[i油9−.111.、例工IJ、’ 
10 t ニ3J L/水25〜3.51:、例えば3
1 、l1%[〕液2;J〜:りjI焚、 Bi2え(
ま3()リ 、。 C)C重油[i、!i・〜、7.51例えば71に幻し
水2.5”−3,5t 、ltl;tlf 3 1− 
、 ’I % P 液2.’i−□351 。 例工LJ:301、及(f j’ イー t’ JLi
油10〜13++g、例えば 13ハg 。 1))C重油7.:今8.4i’t、、例えば71に対
し水1.8〜2.2t、1列えGJ’2t、、1%P液
25〜35愛、例えば30愛、及びへ重油1o−121
(び、例えば111(g。 tE)C重油!1.5= 10.5 t 、例えば+o
lJJt、水3.5〜4.5’l、例えば4L14%P
液25〜35斐、例えば30斐、及びディービル油又は
へ重油18〜22酌、例えば201(!? 上記配合1列に+7いC113重油の場合に、Δ′ )
D重油iotに対し水2[及び4%P液40fL。 C重油の1合に、 13’)C2[i油10Fに対し水3じ4%P液301
、Δ重用1又(はディーLJし)山20に9、どりるこ
とかできる。 本発明の前記加水燃料油の冬季の凍結を防止Jるlこめ
、前記配合に+3いて添加りる水の2〜15%を土ブレ
ングリコールで買換りることができる。 この場合」−ブーレンゲリコールで置換りる水のωはさ
らに上記土ブレングリー]−ルを1/2filに減じイ
」−1−った加水重油の11−ンにつき4oへ−400
ccの飽和食塩水を添加りる事にJ、り天候気)品に左
右されない安定した製品を1りることができる。 本発明の加水燃料油は次のJ、うに製造される。 1責I丁はを5すりたジ亀・クツI−(!I容器中で加
温した水にポリじニルアル−1−ルを溶解し、4%ポリ
ビールノ/ルー1−ル溶液を調製りる。この溶液の所定
量を40へ・50°C(ご加温した別容器の水に攪拌し
ながら加え、これを、又別な攪拌11(J容器C40=
5Q℃に加)品しlこ所定量の重′Ll浦に添加し、約
20分間攪打沢含し−C製品を1!lる。必要に応じア
イ−ピル油を加えC混合りる。重質燃お1油への前記4
%])油を添加した水の添加は噴霧化しC行なうのがり
fましい。 本発明の加水燃J’l油は次表に示りJ、うな竹7′1
をイj リ る 。 (以[・余白) 従来の水と油の混合物、例えば燃才v油にアルコールや
水をMu合したbの、米国1:j i+’tNL+、 
4158551のJ、・)に、けい「い22%の水ど陰
−(−14ンの(!L11(IXI/1aL(![Ia
lky11111e410I (l l−4ジアルキル
フエノール)とからなる乳化剤を使用りる方法が公表さ
れCいるが、これらは能率乃至効率の犠牲が伴い、その
混合物は濁っていて結合が破れて分離υ−る。今迄に知
られる限りでは、水の粒子と油の粒子が完全に結合し、
それがタンクに貯蔵された場合あるいは道路上で運搬さ
れl〔揚台とを問わず、5) Ilf Lないという1
!f性を1!ノるに至Iう4゛、又燃焼にa3いC断火
不完金燃焼のために効率と性能に損失を与えないしのは
完成されCいない。 これに反し、本発明の加水燃料油は実施例にみにれるJ
、うに、)ルめて安定で長期間の医存にも耐え、運搬り
る際にしくそれが道路上、パイプ中を問わず)水と油が
分離りるという事がなく、燃焼に際しては完全燃力2を
するため、エネルギー損失の1東回であるススやタール
のn1がなく、逆に炉壁に沈着りる本来なら当然−[ネ
ル1!−になるべ3ムの迄燃焼さl!c取り除く小がi
jl filである。又その1)1出ガスの一酸化炭素
吊は水にJ、る重油の部分的な代用のため低下されるば
かりでなく、排出カスの中のSO2窒i(i M化物、
不燃炭化水素等4;L (Ii上され、コーネルギー1
111約のイJ利性をもたらり外、環境保全にも役立″
つbのぐある1、又IJi出物や腐蝕をバーノーや炉ハ
!におこさμない右利性もある。 即ち従来の中油よりも本発明の加水重油は完全燃焼によ
る1ネルギーの九利用の他、燃焼装置の寿命を延り一効
果もあり、木質的にエネルギーコストの引き下げを可能
どりる。 本発明に使用りる添加剤は添加剤の量が僅少でしかも(
ルめて価格が安く、我が田にa3い°C大尾に生産し、
1Ili(lIIlに輸出されCいるしのであるばかり
でなく、此の方法によって製出された力iしい加水燃J
−31油は、使用される燃tA装訂に限界を要求しない
し、熱」ニネル−1゛−を必要とりるあらゆる分野に従
来の重油と同様に使用出来るものである。 しかb運搬中ど貯蔵中を問わり゛、水と油の粒子の結合
が均一安定で分離しない・bのCある。 本発明の加水燃料油の製造lj法並ひにそれにか)る添
加剤は、従来の無加水小油のみにては期祐出来ない完全
燃焼と、ぞれに伴う 100%に近い熱効率が期待され
、しかも環境保全1好ましいクリーンなJJI気ガスを
刊出し、燃焼KIS i(iのズを命をのぼり効果があ
り、Jくなくどb燃料費の20%以上を節約出来る。本
発明は70年も前に知られた油に水を加えれば燃焼効果
が上る原理と、これを最も効果的に水の識きを引き出す
!こめの微陣理論を実際に最も安い経費と119車な方
法で実現し解決しIこもの(・、これが実施にJ、り社
会的国家的に、多大な経済効果を挙(Jる(あろう。 実施例に 小イー1造に’(L J(内壁ど外壁の間に蒸気を通じ
C間接的に加熱出来る攪拌機(・1の釜に水10D、を
入れ、これを90・−・1 (l (l ’Cに加熱し
ながら、攪拌翼を80〜1001’ 、 l+ 、 I
llの速1.!夏’Q回転さlII:がI51つ■△(
重合1身1700のポリじニルノフル」−ル)′t!J
)未400gを徐々に投入し、完全に溶解さU、4%P
油を′)くる。次に加温用の水蒸気パイプ< ’J!i
’、管)を装置した人さくふ容器に10tの13重曲を
入れ、40・〜・!i 0 ℃に渇めCから、又別なγ
i′器に(40−・ゼ+O’Cに;品めた水2]に3.
lt、30史の4%1)液を投入して充分混合する水プ
ラス4%1〕8kを徐々に出来れぽ噴霧υ(にし−(添
加し、500〜1200 r、 p 、 mの速度で約
2(1分間攪打混合しく一新しい加水1 !3+油約1
21を得た。此の加水燃料油は燃力K1..:際し無加
水重油よりもイの燃焼に多くの酸素を必要とIず、南九
州公害研究所のiff RI+負で示づ−通り(表2)
、モの排出ガスの(/ 02値が高く、残存02mは少
い。 又無加水CF−i+IIJ、りも1斐〉!1りの黒光1
品が大きく、IJIガス温度が低い事はボイラー(燃焼
別間)の熱効率が人なることを示した。グしに表(1)
の福岡94■聚試験場の試験によれば、20%の水が加
えられCいるにbかかイつらず、イの〃(帛は無加水1
3重油が01470 Caρであるのに対し、20%加
水加水燃料ま、ioH+Ocan rあることは如何に
省」ネ効宋をもたらりかが゛)かがえる。 (以1・余白) 表2 II+気ガスの比較(南九州公害分析しンター■ 表331)1気ガスの比較 (河!l!J’ 8力抜期委託試験結果?表4 ボイラ
燃焼にJ、る蒸発量試験 (河N’)動力技ω1森託試験結果) (同一・条(’t 同一ボイラーにJ、る試験)実施例
2 実施例1ど同様の装「l及びbv1″c、C重油10t
に対し、水3し、4%P液25α、201τ3のA重油
を加えC新しい加水重油約131をIf7. /j 、
此の加水C重油の燃焼効果も実施例1(・冑lS加水燃
料油と同様のJばらしい結果を得る事が出来た。 実施例3 実施例1の配合にJ3い−(使用した水21の内、40
1を1Fレングリニ1−ルC置換し以下ル目、pの操作
]稈をl¥(つくった加水燃料油は(−)15℃の冷凍
能力のある庫内にその一部を容器に取って−IJS夜放
置し−Cも尚江IS帖現象が見られなかった。 実施例4 又実施例3において水と置換りるエチレングリ」−ルを
1/2にへらし、代りに飽和食塩水480ccを加え攪
拌混合しU i!7 /こ製品は同様の冷凍試験にL1
3い(凍結が免がれ実/il!!例1ぐvlに製品と1
11等変0ぬ好結果が冑られた。 −F記各実茄例からどった放置の試料は現在まC成分の
分離がみられない、。
[,1.
J, the moment when the Buddha mind effect of heat +1. 'l vaporized, this mind It. ShilJ Hyogo Hada! The number of beats increased dramatically (approximately 51
1 (l01) - due to the energy of diffusion of the outer oil particles, an atomization phenomenon occurs in which they become even finer, resulting in more complete combustion. According to the fine jM theory, '?S [1, the oil particles are uniformly surrounded around the water r, but since the combination of water and i+l+ continues semi-permanently and complete combustion occurs, the raw material It is more efficient than simple, and in addition, the carbon monoxide output gas is reduced by 11 (
b (J) C. In the chemical chain reaction process of water It is known that H20 is useful for the rapid reaction of 1-12, but if20t, tco is suitable for J3 in the chemical chain reaction process of +131c CO.
It is also known that it is published by fJ due to its quick response. In the reaction process of υ1111 fuel 11i1 oil-b, there is always a process of generating 112 CO, and adding an appropriate amount of 11,0 to the fuel lIl oil has an effect on the rapid reaction of 142 and CO. It is also known to be effective in quickly burning fuel oil whites. Also, CO that does not contain H2O requires a large amount of 02 during combustion, but CO that contains l-120 requires a much smaller amount of 02 during combustion. In the combustion process of hydrous fuel F1 oil, C excess oxygen is relatively small. On the same article A71, the hydrous fuel first mixture has a shorter combustion time than the [1 water-containing fuel mixture], and the combustion is the same. When the fuel mixture is the same as the time, the water-containing fuel is more completely combusted. ! i 1: Compared to tl oil, more J,
It is more complete combustion. In other words, the boiler's fuel oil (reveal C fuel oil has a constant combustion line fl F +3 and J, well J, and in order to completely reduce the combustion effect -11)
Appropriate water content in the mixture! There are various attempts to achieve this purpose, but as mentioned above, 1) This "-Full Dione" combustion gas: 1 is a W surface active agent.
゛] The power of the emulsion is to form a J-mulsion, but there is no complete 41 bond (1111 bond), the required bond (1111 bond) is not reached, or the economic effect is low. Most of the things are gas IC1゜Uninvented!In order to make a water-added material that is useful for preventing environmental pollution, two types of heavy oil are completely combined and water is added. A new hydrated fuel oil that can be stored for a long time, withstands storage and transportation, has good fuel efficiency, and emits gas without environmental pollution; and its production; The hydrated fuel oil according to the present invention includes -C, which is obtained by dispersion-bonding a high-quality fuel oil, water, etc. in the presence of polyvinyl alcohol, and optionally pre-hydrogenated fuel oil. The 5d hydrogenated fuel oil further contains an additive selected from the group consisting of raw gay-bill oil or heavy fuel oil.The amount of water added according to the present invention is
31 Oil contains a part of water]-Brene glycol or G;U]
: It is possible to change the liquid to saturated saline to prevent freezing. The heavy fuel oil used in the present invention is 1-3, C heavy oil. 1-1 ml of water added per 11 ml of fuel oil 7-10
,.. There are 51. Polyvinyl alcohol used
j j−'C: (C112・CIl (011') −). (Represented by PVΔ, and preferably 11 is about 1700. Polyvinyl alcohol (hereinafter expressed as PVΔ) is 1
) It is preferable to prepare an aqueous solution containing 4% VΔ (hereinafter referred to as 4% P liquid) and use it.
After 01, 20 to 80 sentences of 4% P waves are used. 1"E L oil or (when adding Δheavy oil, ΦNegative combustion 1
31 oil 7-10t then 1-2! When the heavy fuel oil is C heavy oil or when a large amount of water is added, it helps the hatching fish fire, and it is necessary when using it for artificial internal combustion such as ships.The water addition of the present invention An example of fuel I::1 oil arrangement is as follows. △) B heavy oil 9-1111 example; tl; [101, KIJ
2 water 1 ”・E) t N e.g. 21, 11%+]
Liquid 3 O-ho 1, M epo 40 sentences. +3) Ci[i oil 9-. 111. , Example IJ,'
10t 3J L/Water 25-3.51:, for example 3
1, l1% [] liquid 2; J~: rijI firing, Bi2e (
Ma3()ri,. C) C heavy oil [i,! i・~, 7.51 For example, 71 is phantom water 2.5"-3,5t, ltl;tlf 3 1-
, 'I % P solution 2. 'i-□351. Example LJ: 301, and (f j' E t' JLi
10-13++ g of oil, e.g. 13 hag. 1)) C heavy oil 7. : Now 8.4i't,, For example, 71 to 1.8-2.2t of water, 1 row GJ'2t, 1% P liquid 25-35a, for example 30a, and heavy oil 1o-121
(and, for example, 111 (g. tE) C heavy oil! 1.5 = 10.5 t, for example +o
lJJt, 3.5-4.5'l of water, e.g. 4L14%P
25 to 35 parts of liquid, for example 30 parts, and 18 to 22 parts of Divil oil or heavy oil, such as 201 parts (!? In the case of +7 C113 heavy oil in the above formulation 1 row, Δ')
D heavy oil iot to 2 liters of water and 40 fL of 4% P solution. 1 cup of C heavy oil, 13') C2 [i oil 10F to 3 tablespoons water 4% P liquid 301
, Δ heavy use 1 or D LJ and 9 can be returned to mountain 20. To prevent winter freezing of the hydrated fuel oil of the present invention, 2 to 15% of the water added to the formulation can be replaced with earthen glycol. In this case, the ω of the water to be replaced by Boulengericol is further reduced to 1/2 filtrate to 400 for every 11 ton of hydrated heavy oil added.
By adding cc of saturated saline, it is possible to create a stable product that is not affected by weather conditions. The hydrated fuel oil of the present invention is produced as follows. Dissolve polyvinyl alcohol in warm water in a container to prepare a 4% polyvinyl alcohol solution. Add a predetermined amount of this solution to water in a separate container heated to 40°C and 50°C (J container C40=
At 5Q°C, add a predetermined amount of the product to a predetermined amount of the product and stir for about 20 minutes. Ill. Add i-pil oil as needed and mix. Said 4 to heavy fuel 1 oil
%]) The addition of water to which oil has been added is preferably carried out by atomization. The hydrolyzed fuel J'l oil of the present invention is shown in the following table: J, Unatake 7'1
Let's do it. (Hereinafter [・margins] Conventional mixtures of water and oil, such as fuel oil mixed with alcohol and water, U.S. 1: j i+'tNL+,
J of 4158551, ・), Kei ``22% water shade - (-14 of (!L11(IXI/1aL(![Ia
A method using an emulsifying agent consisting of lky11111e410I (11111e410I) (11-4 dialkyl phenol) has been published, but these involve sacrifices in efficiency and the mixture is cloudy and bonds are broken and separated. As far as is known so far, water particles and oil particles are completely combined,
If it is stored in a tank or transported on the road (whether on a platform or on a platform, 5)
! 1 f sex! Until now, no combustion method has been completed without causing a loss in efficiency and performance due to incomplete combustion. On the contrary, the hydrated fuel oil of the present invention is
, sea urchin, ) is extremely stable and can withstand long-term survival, does not cause separation of water and oil when transported (whether on the road or in pipes), and is resistant to combustion. Because it has a complete combustion power of 2, there is no soot or tar, which causes energy loss, and on the contrary, it naturally deposits on the furnace wall - [Nel 1! - It burns until 3 times! c The small to be removed is i
jl fil. In addition, 1) the carbon monoxide level of the output gas is not only lowered due to partial substitution of heavy oil in water, but also due to the partial substitution of heavy oil with SO2 in the exhaust gas
Non-flammable hydrocarbons, etc. 4;
Not only does it bring about 111 benefits, but it also helps protect the environment.
Tsub no guru 1, also IJi material and corrosion burnout and furnace ha! There is also a right-handed person who does not have any problems. That is, compared to conventional medium oil, the hydrated heavy oil of the present invention not only utilizes one energy through complete combustion, but also has the effect of extending the life of the combustion equipment, making it possible to reduce energy costs in terms of wood quality. The amount of additives used in the present invention is very small (
The price is low, and we produce it in our farm at A3°C.
Not only is it exported to 1Ili (lIIl), but also the powerful hydrocarbons produced by this method.
-31 oil does not require any limitations on the fuel loading used, and can be used in any field requiring thermal nineel-1 in the same way as conventional heavy fuel oil. However, whether during transportation or storage, the bond between water and oil particles is uniform and stable, and they do not separate. The lj method for producing hydrated fuel oil of the present invention as well as the additives used therewith are expected to achieve complete combustion, which cannot be achieved with conventional non-hydrated small oils alone, and associated thermal efficiency close to 100%. Moreover, it publishes a clean JJI gas that is preferable for environmental conservation, and has the effect of increasing the number of lives of combustion KIS i (i), and can save more than 20% of the fuel cost. The principle that the combustion effect increases when water is added to oil, which has been known for many years, and the most effective way to bring out the knowledge of water! The theory of fine formation is actually applied at the lowest cost and in a 119-minute method. This will be implemented and solved, and it will have a great economic effect on the social and national level. A stirrer that can indirectly heat C by passing steam between the outer walls (1) Pour 10 D of water into a pot, and heat it to 90 - 1 (l'C) while turning the stirring blades to 80 - 1001'C. , l+ , I
ll speed 1. ! Summer 'Q rotated lII: is I51 ■△(
Polymerized 1700% polyvinylfluor)'t! J
) Gradually add 400 g of unused U and 4% P until completely dissolved.
Add oil. Next, the steam pipe for heating <'J! i
A 13-fold tube of 10 tons was placed in a sacrificial container equipped with a tube), and 40...! i 0 ℃ From C, another γ
Add 3.
lt, 30 minutes of 4% 1) Add the liquid and mix thoroughly. Add water plus 4% 1] 8k gradually and spray at a speed of 500 to 1200 r, p, m. 2 (stir for 1 minute and add fresh water 1 ! 3 + oil approx. 1
I got 21. This hydrated fuel oil has a fuel power of K1. .. : However, more oxygen is required for combustion than unhydrated heavy oil, as shown by Minamikyushu Pollution Research Institute's if RI + negative (Table 2).
, the exhaust gas (/02 value is high, and the remaining 02m is small. Also, non-hydrated CF-i + IIJ, Rimo 1 hi〉! 1's black light 1
The large size and low IJI gas temperature indicated that the thermal efficiency of the boiler (combustion section) was low. Table (1)
According to a test conducted at the Fukuoka 94 ■ Ju Experimental Station, 20% of water was added to C, but it did not cause any damage;
While triple fuel oil has 0.01470 Caρ, the fact that there is 20% hydrated fuel, ioH+Ocanr, can be seen as a great saving effect. (1, blank) Table 2 Comparison of II + Gas (Minami Kyushu Pollution Analysis Center ■ Table 331) Comparison of 1 Gas (Ri!l!J' 8 Power Extraction Commissioned Test Results? Table 4 J for Boiler Combustion , evaporation amount test (river N') power technique ω1 forest trust test results) (same column ('t J, test on the same boiler) Example 2 Same equipment as in Example 1 "l and bv1"c, C heavy oil 10t
To this, add 3 parts of water, add 4% P liquid 25α, 201τ3 of A heavy oil, and add about 131 of new hydrated heavy oil C to If7. /j,
The combustion effect of this hydrated C fuel oil was also similar to that of Example 1 (-1S), and excellent J results could be obtained. Of these, 40
Replace 1 with 1F Renglilin 1-L C and proceed as follows: 1) Add the culm to 1 ¥ (The prepared hydrated fuel oil is (-) Place a portion of it in a container in a refrigerator with a freezing capacity of 15℃. - IJS left overnight - No Naoe IS phenomenon was observed in -C.Example 4 Also, in Example 3, the amount of ethylene glycol used to replace water was reduced to 1/2, and 480 cc of saturated saline was added instead. Add and stir to mix.Ui!7/This product passed the same freezing test as L1.
3 (Freezing is avoided! Product and 1 in example 1)
I was impressed with the good results, with 11 mag and no change. -Currently, no separation of the C component is observed in the leftover samples taken from each of the eggplants listed in F.

Claims (1)

【特許請求の範囲】 01 重質燃料油7〜10tにつき、水1〜5tとノニ
ルフェニルポリエチレングリコールエーテルQ、01 
% 及Uポリビニルアルコール4係からなる水溶液20
〜80tとを含む加水燃料油。 (2) 前記ポリビニルアルコールカ式%式%) で表わさIt、11が500〜2500であり、ノニル
フェニルポリエチレングリコールエーテルで表わされ、
■が1500〜2500である、特許請求の範囲第1項
記載の加水燃料油。 (3) さらに、重質燃料油7〜Lot当り、アルカリ
金属塩素酸塩を40〜200fを含む特許請求の範囲第
1項又は第2項記載の加水燃料油。 (4) 前記の水の約2〜15%の量を同量のエチレン
クリコールで置換した、特許請求の範囲第1項、第2項
又は第3項記載の加水燃Vat油。 (5)前記エチレングリコールの量を最大%量1で減じ
、製品1を当り40〜400 ccの飽オ日食塩水で置
換してなる、特許請求の範囲第4項記載の加水燃料油。 (6)所定量のポリビニルアルコールを水に溶解し、C
,fLK/=ルフェニルホリエチレングリコールエーテ
ルを加えて0.01 %のノニルフェニルポリエチレン
グリコールエーテルを含むポリビニルアルコール4係水
溶液を調製し、この溶液の所定量を所定量の水に加え、
所望によりアルカリ金属塩素酸塩水溶液、ディーゼル油
又はA重油からなる群から選ばれる添加剤とともにあら
かじめ加温された重質燃料油に加えて均一に分散結合さ
ぜることを特徴とする加水燃料油の製法。
[Claims] 01 For 7 to 10 tons of heavy fuel oil, 1 to 5 tons of water and nonylphenyl polyethylene glycol ether Q, 01
Aqueous solution consisting of % and 4 parts of polyvinyl alcohol 20
~80t of hydrated fuel oil. (2) the polyvinyl alcohol is represented by the formula %, where 11 is from 500 to 2,500, and is represented by nonylphenyl polyethylene glycol ether;
The hydrated fuel oil according to claim 1, wherein (1) is 1,500 to 2,500. (3) The hydrated fuel oil according to claim 1 or 2, further comprising 40 to 200 f of alkali metal chlorate per 7 to 2 lots of heavy fuel oil. (4) Hydrogenated Vat oil according to claim 1, 2 or 3, wherein about 2 to 15% of said water is replaced with the same amount of ethylene glycol. (5) The hydrated fuel oil according to claim 4, wherein the amount of ethylene glycol is reduced by a maximum of 1% and the product 1 is replaced with 40 to 400 cc of saturated saline. (6) Dissolve a predetermined amount of polyvinyl alcohol in water,
, fLK/=ruphenyl polyethylene glycol ether to prepare a polyvinyl alcohol 4 aqueous solution containing 0.01% nonylphenyl polyethylene glycol ether, and add a predetermined amount of this solution to a predetermined amount of water,
A hydrated fuel oil characterized in that it is added to pre-warmed heavy fuel oil and uniformly dispersed and mixed with an additive selected from the group consisting of an alkali metal chlorate aqueous solution, diesel oil or A heavy oil, if desired. manufacturing method.
JP58209960A 1983-11-10 1983-11-10 Water-incorporated fuel oil and its manufacture Granted JPS60104190A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP58209960A JPS60104190A (en) 1983-11-10 1983-11-10 Water-incorporated fuel oil and its manufacture
KR1019840002539A KR850003564A (en) 1983-11-10 1984-05-11 Hydrolyzed fuel oil and its preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58209960A JPS60104190A (en) 1983-11-10 1983-11-10 Water-incorporated fuel oil and its manufacture

Publications (2)

Publication Number Publication Date
JPS60104190A true JPS60104190A (en) 1985-06-08
JPH027353B2 JPH027353B2 (en) 1990-02-16

Family

ID=16581517

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58209960A Granted JPS60104190A (en) 1983-11-10 1983-11-10 Water-incorporated fuel oil and its manufacture

Country Status (2)

Country Link
JP (1) JPS60104190A (en)
KR (1) KR850003564A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60206893A (en) * 1984-03-31 1985-10-18 Yoshinari Shimada Preparation of w/o type emulsion fuel oil
JPH01247492A (en) * 1988-03-30 1989-10-03 Mitsubishi Heavy Ind Ltd Heavy oil/water mixture fuel composition
JPH0247194A (en) * 1988-08-08 1990-02-16 Intevep Sa Viscous hydrocarbon/water emulsion
WO2015150971A1 (en) * 2014-04-03 2015-10-08 Fuber Limited Emulsifying additive for forming emulsions of water in heavy fuel oil (hfo)
US11015126B2 (en) 2016-12-30 2021-05-25 Eme International Limited Apparatus and method for producing biomass derived liquid, bio-fuel and bio-material
US11084004B2 (en) 2014-11-10 2021-08-10 Eme International Lux S.A. Device for mixing water and diesel oil, apparatus and process for producing a water/diesel oil micro-emulsion

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56112993A (en) * 1980-02-09 1981-09-05 Tsutomu Morita Emulsifier for emulsified heavy oil

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56112993A (en) * 1980-02-09 1981-09-05 Tsutomu Morita Emulsifier for emulsified heavy oil

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60206893A (en) * 1984-03-31 1985-10-18 Yoshinari Shimada Preparation of w/o type emulsion fuel oil
JPH01247492A (en) * 1988-03-30 1989-10-03 Mitsubishi Heavy Ind Ltd Heavy oil/water mixture fuel composition
JPH0247194A (en) * 1988-08-08 1990-02-16 Intevep Sa Viscous hydrocarbon/water emulsion
JPH0579278B2 (en) * 1988-08-08 1993-11-01 Intevep Sa
WO2015150971A1 (en) * 2014-04-03 2015-10-08 Fuber Limited Emulsifying additive for forming emulsions of water in heavy fuel oil (hfo)
US11084004B2 (en) 2014-11-10 2021-08-10 Eme International Lux S.A. Device for mixing water and diesel oil, apparatus and process for producing a water/diesel oil micro-emulsion
US11015126B2 (en) 2016-12-30 2021-05-25 Eme International Limited Apparatus and method for producing biomass derived liquid, bio-fuel and bio-material

Also Published As

Publication number Publication date
KR850003564A (en) 1985-06-20
JPH027353B2 (en) 1990-02-16

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