JPS6033870B2 - Low temperature fluidity improver for fuel oil - Google Patents

Low temperature fluidity improver for fuel oil

Info

Publication number
JPS6033870B2
JPS6033870B2 JP9002183A JP9002183A JPS6033870B2 JP S6033870 B2 JPS6033870 B2 JP S6033870B2 JP 9002183 A JP9002183 A JP 9002183A JP 9002183 A JP9002183 A JP 9002183A JP S6033870 B2 JPS6033870 B2 JP S6033870B2
Authority
JP
Japan
Prior art keywords
fuel oil
fluidity improver
weight
hydrogen
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP9002183A
Other languages
Japanese (ja)
Other versions
JPS59215390A (en
Inventor
健 日原
敏道 清水
壌太郎 永井
隆史 山内
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.)
TOHO KAGAKU KOGYO KK
Original Assignee
TOHO KAGAKU KOGYO KK
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 TOHO KAGAKU KOGYO KK filed Critical TOHO KAGAKU KOGYO KK
Priority to JP9002183A priority Critical patent/JPS6033870B2/en
Publication of JPS59215390A publication Critical patent/JPS59215390A/en
Publication of JPS6033870B2 publication Critical patent/JPS6033870B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は塩素化されたエチレンとエチレン性不飽和単量
体より成ることを特徴とする燃料油用流動性改良剤及び
本流動’性改良剤に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluidity improver for fuel oil characterized by comprising chlorinated ethylene and an ethylenically unsaturated monomer, and the present fluidity improver.

石油留出残酒油を含む燃料油、例えば船舶用ディーゼル
燃料油、加熱油等の使用に際しは、これらの油の低温流
動性にかかわる問題が多く発生する。
When using fuel oils containing petroleum distillate residues, such as marine diesel fuel oils, heating oils, etc., many problems arise regarding the low-temperature fluidity of these oils.

すなわち、低温度に於て半固体、又はゲル状になった燃
料油は送油パイプやストレーナ−を詰らせたり、内燃機
関への燃料油の供給を不能にしたりする。この問題を解
決するために現在迄に多くの研究が行われた結果多くの
低温流動性改良剤が開発され商業的に使用されている。
That is, fuel oil that becomes semi-solid or gelatinous at low temperatures can clog oil pipes and strainers, or make it impossible to supply fuel oil to an internal combustion engine. In order to solve this problem, much research has been carried out to date, and as a result many cold flow improvers have been developed and are in commercial use.

この種の添加物は燃料油中のワックスとの作用によりそ
の結晶成長をコントロールし、微細な状態に保つ事によ
り低温に於ける燃料油の流動性を改善する。特に石油留
出残澄油を含有する燃料油に関しては、従来比較的高分
子量のエチレンとエチレン性不飽和単量体との共重合物
が多く用いられるが、これらは残澄油中に存在するレジ
ン、アスフアルデン等の高分子物質とワックスとが互い
に影響しあうため生じる油の経時変化により薬剤の効果
が減少してしまう様な現象が多く認められる欠点がある
This type of additive controls the crystal growth of the wax in the fuel oil by controlling its crystal growth and improves the fluidity of the fuel oil at low temperatures by keeping it in a fine state. In particular, for fuel oil containing petroleum distillate residue oil, copolymers of relatively high molecular weight ethylene and ethylenically unsaturated monomers are often used, but these copolymers are present in the residue oil. There are many disadvantages in which the effectiveness of the drug is often reduced due to changes in the oil over time due to the interaction between wax and polymeric substances such as resins and asphaldenes.

又、共重合物の平均分子量が比較的大きいため流動性改
良剤濃厚物の流動点や粘度が高くなり、ハンドリング上
問題となる場合も多くある。
Furthermore, since the average molecular weight of the copolymer is relatively large, the pour point and viscosity of the fluidity improver concentrate become high, which often causes handling problems.

本発明者らは特に石油留出残笹を含む燃料油用の流動性
改良剤のこれらの欠点を解決するための研究を行った結
果、下記の如き発明に致つた。すなわち、エチレンとエ
チレン性不飽和単量体との共重合物をハロゲン化(特に
塩素化)する事により英重合物の油に対する溶解性が増
大し比較的低温に於ても容易に油への混合が可能になる
と共に、薬剤効果の経時安定性も著しく向上することを
見出した。さらに塩素化によって流動点降下剤濃厚物の
流動点や粘度が低下する事によってハンドリングが改善
される。これらの特性は多分以下に限定する範囲内にハ
ロゲン化されたエチレンとエチレン性不飽和単量体との
共重合物の燃料油への溶解性の変化がワックスとの相互
作用を容易にし、より安定した細かなワックス結晶を生
成させるものと考えられる。
The present inventors conducted research to solve these drawbacks of fluidity improvers for fuel oils containing petroleum distillate residues, and as a result, they came up with the following invention. In other words, by halogenating (particularly chlorinating) a copolymer of ethylene and an ethylenically unsaturated monomer, the solubility of the polymer in oil increases, making it easy to dissolve in oil even at relatively low temperatures. It has been found that mixing becomes possible and the stability of drug effects over time is also significantly improved. Additionally, chlorination improves handling by lowering the pour point and viscosity of pour point depressant concentrates. These properties are likely to be less limited to the extent that changes in the solubility of copolymers of halogenated ethylene and ethylenically unsaturated monomers in fuel oil facilitate their interaction with waxes and more It is thought that stable fine wax crystals are generated.

本発明に使用する塩素化されたエチレンとエチレン性不
飽和単量体との共重合物は数平均分子量10000〜6
0000で60〜85重量%のエチレンと15〜40重
量%のエチレン性不飽和単量体より成る共重合体であっ
てその塩素化率は約1〜1の重量%である。エチレンと
共重合されるエチレン性不飽和単量体は下記一般式〔式
中、R,は水素またはメチル基であり、R2は−OCO
R4、または一COOR4基(式中、R4は水素または
、C,〜4の直鎖又は分枝アルキル基である。
The copolymer of chlorinated ethylene and ethylenically unsaturated monomer used in the present invention has a number average molecular weight of 10,000 to 6.
0000 is a copolymer consisting of 60-85% by weight of ethylene and 15-40% by weight of ethylenically unsaturated monomer, and its chlorination rate is about 1-1% by weight. The ethylenically unsaturated monomer to be copolymerized with ethylene has the following general formula [wherein, R is hydrogen or a methyl group, and R2 is -OCO
R4, or a COOR4 group, where R4 is hydrogen or a C, to 4 straight-chain or branched alkyl group.

)でありR3は水素または−COORである。〕で表さ
れる不飽和モノ及び(あるいは)ジェチルである。こ)
で一般式中R,及びR3が水素でR2が−OCOR4で
表されるェステルの例としては酢酸ビニル、ィソ藤酸ビ
ニルなどがある。また、R2が−COOR4で表される
ェステル類としてはアクリル酸メチル、メタクリル酸メ
チル及びアクリル酸ィソブチルなどが該当する。これら
の化合物とエチレンとの共重合反応は一般に高圧下での
ラジカル反応により商業的に合成されているものなので
、ここでは詳細な説明は行わない。又、これらの共重合
物の塩素化は一般にハロアルカン等を溶媒として80〜
150℃の温度で紫外線又は、可視光線を触媒として反
応系中に塩素ガスを吹き込む事により通常のアルカン類
ろ塩素化と同様容易に行う事ができる。
) and R3 is hydrogen or -COOR. ] are unsaturated mono and/or ethyl. child)
Examples of esters in which R and R3 are hydrogen and R2 is -OCOR4 include vinyl acetate and vinyl isoforthate. Examples of esters in which R2 is -COOR4 include methyl acrylate, methyl methacrylate, and isobutyl acrylate. Since the copolymerization reaction between these compounds and ethylene is generally synthesized commercially by radical reaction under high pressure, a detailed explanation will not be given here. In addition, chlorination of these copolymers is generally carried out using a haloalkane or the like as a solvent.
By blowing chlorine gas into the reaction system at a temperature of 150° C. using ultraviolet rays or visible light as a catalyst, it can be easily carried out in the same way as ordinary alkanes filtration chlorination.

本発明の流動性改良剤は取り扱いを容易にするため、一
般に炭化水素系溶剤例えば、軽油、ケロシン、滋油など
と混合して純分15〜4の重量%の濃厚溶液として使用
される。
In order to facilitate handling, the fluidity improver of the present invention is generally mixed with a hydrocarbon solvent such as light oil, kerosene, natural oil, etc., and used as a concentrated solution with a purity of 15 to 4% by weight.

次に代表的な実施例によって本発明を更に説明する。The present invention will now be further explained by means of representative examples.

実施例 1 実施例にて使用する燃料油の性状は表1に示すように石
油蟹出残澄油を含む2種類の燃料油である。
Example 1 As shown in Table 1, the properties of the fuel oils used in the examples are two types of fuel oils including petroleum cannibal residue oil.

表−1 表2に本発明で得られる共重合物及び塩素化共重合物の
濃厚溶液(30%ケロシン溶液)の性状を示す。
Table 1 Table 2 shows the properties of the concentrated solution (30% kerosene solution) of the copolymer and chlorinated copolymer obtained in the present invention.

一〇 表2から明らかな様に本発明の塩素化共重合物の濃厚溶
液は流動点の箸るしい低下が認められ、薬剤のハンドリ
ング上極めて有利な性状となる事がわかる。
As is clear from Table 2, the pour point of the concentrated solution of the chlorinated copolymer of the present invention is significantly lowered, and it can be seen that it has extremely advantageous properties in terms of drug handling.

※ 表3は表1の燃料油に表2に示す共重合物及び塩素
化共重合物を添加したものの流動点雌蓬下温度及び隆時
安定性について測定した結果を示したものである。
*Table 3 shows the results of measuring the below-pour point temperature and the stability at rising time of the fuel oils shown in Table 1 to which the copolymers and chlorinated copolymers shown in Table 2 were added.

表−m (△T℃は、各々の油のブランクの流動点からの上下)
表3からは本発明の塩素化共重合物の濃厚溶液を添加し
た燃料油は、共重合物の濃厚溶液添加時にに比べて特に
優れた経時安定性を示している事が判る。
Table-m (△T℃ is above and below the pour point of each oil blank)
From Table 3, it can be seen that the fuel oil to which the concentrated solution of the chlorinated copolymer of the present invention is added exhibits particularly excellent stability over time compared to the fuel oil when the concentrated solution of the copolymer is added.

したがって本発明における塩素化されたエチレンとエチ
レン性不飽和共重合物の濃厚溶液は優れた低温流動性改
良能を有するものである。
Therefore, the concentrated solution of chlorinated ethylene and ethylenically unsaturated copolymer according to the present invention has an excellent ability to improve low-temperature fluidity.

Claims (1)

【特許請求の範囲】 1 数平均分子量約10.000〜60.000、60
〜85重量%のエチレンと40〜15重量%の下記一般
式▲数式、化学式、表等があります▼ 〔式中、R_1
は水素またはメチル基であり、R_2は−OCOR_4
また−COOR_4基(式中、R_4は水素またはC_
1_〜_4の直鎖または分枝アルキル基である)であり
、R_3は水素または−COOR_4基である。 〕で表わされる不飽和モノ及び(あるいは)ジエステル
であるエチレン性不飽和単量体との共重合体の塩素化物
(塩素化率約1〜10重量%)より成る燃料油流動性改
良剤。
[Claims] 1. Number average molecular weight of about 10.000 to 60.000, 60
~85% by weight of ethylene and 40~15% by weight of the following general formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ [In the formula, R_1
is hydrogen or methyl group, R_2 is -OCOR_4
-COOR_4 group (in the formula, R_4 is hydrogen or C_
R_3 is hydrogen or a -COOR_4 group. ] A fuel oil fluidity improver comprising a chlorinated copolymer (chlorination rate of about 1 to 10% by weight) of an ethylenically unsaturated monomer and an unsaturated mono- and/or diester represented by the following formula.
JP9002183A 1983-05-24 1983-05-24 Low temperature fluidity improver for fuel oil Expired JPS6033870B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9002183A JPS6033870B2 (en) 1983-05-24 1983-05-24 Low temperature fluidity improver for fuel oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9002183A JPS6033870B2 (en) 1983-05-24 1983-05-24 Low temperature fluidity improver for fuel oil

Publications (2)

Publication Number Publication Date
JPS59215390A JPS59215390A (en) 1984-12-05
JPS6033870B2 true JPS6033870B2 (en) 1985-08-05

Family

ID=13987037

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9002183A Expired JPS6033870B2 (en) 1983-05-24 1983-05-24 Low temperature fluidity improver for fuel oil

Country Status (1)

Country Link
JP (1) JPS6033870B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6079957U (en) * 1983-11-05 1985-06-03 北川工業株式会社 Bait feeder for longline fishing
JPH06506590A (en) * 1991-04-19 1994-07-28 ウェブマック ノミニーズ ピーティーワイ リミテッド Branch line deployment mechanism
US8783041B2 (en) 2010-06-09 2014-07-22 Chevron U.S.A. Inc. LNG transport vessel and method for storing and managing excess boil off gas thereon

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6079957U (en) * 1983-11-05 1985-06-03 北川工業株式会社 Bait feeder for longline fishing
JPH06506590A (en) * 1991-04-19 1994-07-28 ウェブマック ノミニーズ ピーティーワイ リミテッド Branch line deployment mechanism
US8783041B2 (en) 2010-06-09 2014-07-22 Chevron U.S.A. Inc. LNG transport vessel and method for storing and managing excess boil off gas thereon

Also Published As

Publication number Publication date
JPS59215390A (en) 1984-12-05

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