JP2782484B2 - Oil sludge dispersion method - Google Patents
Oil sludge dispersion methodInfo
- Publication number
- JP2782484B2 JP2782484B2 JP4058787A JP5878792A JP2782484B2 JP 2782484 B2 JP2782484 B2 JP 2782484B2 JP 4058787 A JP4058787 A JP 4058787A JP 5878792 A JP5878792 A JP 5878792A JP 2782484 B2 JP2782484 B2 JP 2782484B2
- Authority
- JP
- Japan
- Prior art keywords
- test
- group
- sludge
- carbon atoms
- aliphatic hydrocarbon
- 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 - Fee Related
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、石油スラッジ、特に原
油の貯蔵中に発生するスラッジの分散方法に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for dispersing petroleum sludge, particularly sludge generated during storage of crude oil.
【0002】[0002]
【従来の技術】日本国内で使用される原油は一般に一基
数万〜10万キロリットル規模のストレージタンクに長
期間保存された後に使用されるが、近年エネルギーの安
定供給を図るために原油の国家備蓄量は増加し、ストレ
ージタンクの容量は巨大化し、貯蔵期間も長期に渉るよ
うになってきている。このような状況の中で問題となる
ことはストレージタンクの底部に徐々に堆積するスラッ
ジである。2. Description of the Related Art Crude oil used in Japan is generally used after being stored for a long time in a storage tank of several tens of thousands to 100,000 kiloliters. National reserves are increasing, storage tanks are getting bigger and storage periods are long. In this situation, a problem is sludge that gradually accumulates at the bottom of the storage tank.
【0003】このスラッジは一般には原油中のワック
ス、樹脂分、アスファルテン等の高分子物質が複雑に混
合したもので、タンクの貯蔵能力を低下させたり、送油
パイプやポンプを詰まらせる原因にもなり、原油貯蔵時
の大きな問題となっている。このスラッジの堆積を防止
する方法としては一般に撹拌機等による機械的な方法で
液を撹拌しスラッジの沈降、沈殿を防ぐ方法が行われて
いる。[0003] This sludge is generally a complex mixture of wax, resin, asphaltenes, and other high-molecular substances in crude oil, and may reduce the storage capacity of a tank or clog oil feed pipes and pumps. This is a major problem when storing crude oil. As a method for preventing the sludge from accumulating, generally, a method is employed in which the liquid is stirred by a mechanical method using a stirrer or the like to prevent sedimentation and sedimentation of the sludge.
【0004】[0004]
【発明が解決しようとする課題】しかながら、これらの
巨大タンク内にある原油のスラッジを撹拌により分散さ
せることは非常に困難であり、経済的にも得策ではな
い。そのため少量の油溶性分散剤を添加することにより
スラッジを安定的に分散させる方法が検討されてきた
(特公昭62−1435号公報)。しかしながら、世界各
地で生産される多種類の原油に対して幅広く効果を示す
薬剤は見出されていない。更に近年は原油関係のストレ
ージタンクには法定点検が必要となっている。However, it is very difficult to disperse the crude oil sludge in these huge tanks by stirring, and it is not economically advantageous. Therefore, a method of stably dispersing sludge by adding a small amount of an oil-soluble dispersant has been studied.
(Japanese Patent Publication No. 62-1435). However, no drug has been found that has a wide range of effects on various types of crude oil produced around the world. Furthermore, in recent years, legal inspections of crude oil storage tanks have become necessary.
【0005】[0005]
【課題を解決するための手段】本発明者等は多くの油溶
性分散剤について鋭意研究を重ねた結果、特定の構造を
有するポリアミドが多くの原油種に対して幅広くスラッ
ジ分散効果を示し、原油の流動性をも改良することを見
出した。The present inventors have conducted intensive studies on many oil-soluble dispersants, and as a result, a polyamide having a specific structure has a wide sludge dispersing effect on many types of crude oils. Has also been found to improve the flowability of
【0006】即ち本発明は原油に一般式(1)で示される
ポリアミドを10〜5000ppm添加する事により原
油中に存在するスラッジを有効に分散する方法である。 [式中のR1、R2はその一方が水素原子であるときは他
の一方は炭素数6〜30の飽和脂肪族炭化水素基であ
り、R1、R2の両方が飽和脂肪族炭化水素基であるとき
はR1、R2の炭素数の合計が6〜30であり、X1、X2
は一方は−NY1Y2基(Y1、Y2は炭素数10〜28の
脂肪族炭化水素基を示す)、他の一方は−OM基(Mは水
素、アルカリ金属、アミンを示す)、nは2〜30の正
数を示す]。本発明に係るポリアミドの製造方法に関し
ては特公昭56−54037号公報、特公昭56−54
038号公報に詳細に述べられている通りである。That is, the present invention is a method for effectively dispersing sludge present in crude oil by adding 10 to 5000 ppm of a polyamide represented by the general formula (1) to crude oil. [In the formula, when one of R 1 and R 2 is a hydrogen atom, the other is a saturated aliphatic hydrocarbon group having 6 to 30 carbon atoms, and both R 1 and R 2 are saturated aliphatic hydrocarbon groups. When it is a hydrogen group, the total number of carbon atoms of R 1 and R 2 is 6 to 30, and X 1 and X 2
One is a -NY 1 Y 2 group (Y 1 and Y 2 each represent an aliphatic hydrocarbon group having 10 to 28 carbon atoms), and the other is a -OM group (M represents hydrogen, an alkali metal, or an amine) , N represents a positive number of 2 to 30]. Regarding the method for producing the polyamide according to the present invention, JP-B-56-54037 and JP-B-56-54.
No. 038, as described in detail.
【0007】以下に本発明の内容を実施例及び比較例に
よって説明するが、本発明はこれらの実施例に限定され
るものではない。本発明の実施例に使用した試料スラッ
ジの性状は表−1の通りである。 Hereinafter, the contents of the present invention will be described with reference to examples and comparative examples, but the present invention is not limited to these examples. Table 1 shows the properties of the sample sludge used in the examples of the present invention.
【0008】[0008]
【実施例 1】 分散浸透試験 試験方法 本重油添加剤(以下添加剤と略称する)を10〜5,0
00ppm濃度迄の試験溶液(1リットル)を調整し、そ
れぞれに二種類の違う試料A、Bを1grづつ添加し
た。3000rpmで10分間撹拌(スターラー撹拌)し
たのち、試料溶液5Aメッシュの濾紙を用いて濾過し、
その濾紙の状況を目視確認した。但し、ブランクは試験
用溶媒(1リットル)のみとした。試験結果を表−2に示
す。Example 1 Dispersion Penetration Test Test Method The present heavy oil additive (hereinafter abbreviated as additive) was added to 10 to 5.0
A test solution (1 liter) was prepared to a concentration of 00 ppm, and two different samples A and B were added to each of them in an amount of 1 gr. After stirring at 3000 rpm for 10 minutes (stirrer stirring), the sample solution was filtered using a 5A mesh filter paper,
The condition of the filter paper was visually checked. However, the blank was only a test solvent (1 liter). Table 2 shows the test results.
【0009】 註1: ± 変化なし + 残留大 ++ 残留小 +++ 残留無し 註2:添加剤 C16〜18オレフィンと無水マレイン酸との共重合物
の水添ジタローポリアミド、分子量6000[0009] Note 1: ± No change + Large residue ++ Small residue ++++ No residue Note 2: Additive C16-18 Hydrogenated ditallow polyamide of copolymer of olefin and maleic anhydride, molecular weight 6,000
【0010】[0010]
【実施例 2】 剥離試験 試験方法:添加剤を10〜5,000ppm濃度まで
の試験溶媒水(1リットル)を調整する。試験片(ステン
レス鋼)に試料A、Bを塗布し1夜間放置し、試験水中
に試験片を浸漬し、室温にて60分放置し、剥離(浸透)
状況を目視確認する。但し、ブランクは試験溶媒(1リ
ットル)のみとした。試験結果を表−3に示した。Example 2 Peeling Test Test Method: The additive is prepared in a test solvent water (1 liter) to a concentration of 10 to 5,000 ppm. Samples A and B are applied to a test piece (stainless steel), left for one night, immersed in test water, left at room temperature for 60 minutes, and peeled (penetrated)
Check the situation visually. However, the blank was only the test solvent (1 liter). The test results are shown in Table-3.
【0011】 註1: − 剥がれなし + 剥離1/2未満 ++ 剥離1/2以上 +++ 全て剥離 註2:添加剤:C12,14,16,18のオレフィ
ンと無水マレイン酸との共重合物のジステアリルポリア
ミド、MW:4500[0011] Note 1:-No peeling + Less than 1/2 peeling ++ More than 1/2 peeling +++ All peeled Note 2: Additive: distearyl polyamide, a copolymer of C12,14,16,18 olefin and maleic anhydride MW: 4500
【0012】[0012]
【実施例 3】 除去試験 試験方法:添加剤を10〜5,000ppm濃度まで
含有させた試験溶媒水(1リットル)を調整した。有機溶
媒に試料A、Bを5g溶解した(この時多少の沈澱物の
発生が見られた)。ポリエステル製試験布に溶解したス
ラッジ溶液を各0.25ミリリットルづつ滴下しスポッ
トを作った。スポットのついた試験布を試験水中に室温
で1時間浸漬した後のスポットの状態を観察した。但
し、ブランクは試験用溶媒(1リットル)に浸漬した試験
布とした。試験結果を表−4に示した。Example 3 Removal test Test method: Test solvent water (1 liter) containing additives to a concentration of 10 to 5,000 ppm was prepared. 5 g of Samples A and B were dissolved in the organic solvent (at this time, some generation of a precipitate was observed). A sludge solution dissolved in a polyester test cloth was dropped by 0.25 ml each to form a spot. After the test cloth with the spot was immersed in test water at room temperature for 1 hour, the state of the spot was observed. The blank was a test cloth immersed in a test solvent (1 liter). The test results are shown in Table-4.
【0013】 註1: − 変化なし + 面積1/2以上 ++ 面積1/2未満 +++ 全て除去 註2:添加剤は添加剤のn−ブチルアミン塩[0013] Note 1:-No change + More than 1/2 area ++ Less than 1/2 area +++ All removed Note 2: Additive is n-butylamine salt of additive
【0014】[0014]
【発明の効果】実施例1〜3の分散浸透試験、剥離試
験、除去試験の結果が示すように、原油に本発明の添加
剤を加えることによって、原油中のスラッジが分離、沈
降してタンク壁面に固着したり、底部に沈殿堆積せず、
タンク内原油全体の流動性が維持できることが明らかで
ある。As shown in the results of the dispersion penetration test, the peel test and the removal test in Examples 1 to 3, by adding the additive of the present invention to the crude oil, the sludge in the crude oil is separated and settled to form a tank. It does not stick to the wall or settle down on the bottom,
It is clear that the flowability of the whole crude oil in the tank can be maintained.
フロントページの続き (72)発明者 本坊 一浩 東京都文京区本郷5丁目5番16号オルガ ノ株式会社内 審査官 船岡 嘉彦 (56)参考文献 特開 昭54−86505(JP,A) 特開 昭54−81307(JP,A) 特開 平1−101394(JP,A) (58)調査した分野(Int.Cl.6,DB名) C10L 1/22 C08L 35/00Continuation of the front page (72) Inventor Kazuhiro Honbo Examiner Yoshihiko Funaoka, Organo Co., Ltd. 5-5-16-1 Hongo, Bunkyo-ku, Tokyo (56) References JP-A-54-86505 (JP, A) 54-81307 (JP, A) JP-A-1-101394 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C10L 1/22 C08L 35/00
Claims (1)
イン酸の共重合体のポリアミドを石油に対して10〜5
000ppm添加することを特徴とする石油スラッジの
分散方法。 [式中のR1、R2はその一方が水素原子であるときは他
の一方は炭素数6〜30の飽和脂肪族炭化水素基であ
り、R1、R2の両方が飽和脂肪族炭化水素基であるとき
はR1、R2の炭素数の合計が6〜30であり、X1、X2
は一方は−NY1Y2基(Y1、Y2は炭素数10〜28の
脂肪族炭化水素基を示す)、他の一方は−OM基(Mは水
素又はアルカリ金属又はアミンを示す)、nは2〜30
の正数を示す。](1) A polyamide of a copolymer of an olefin and maleic acid represented by the following formula (1):
A method for dispersing petroleum sludge, comprising adding 000 ppm. [In the formula, when one of R 1 and R 2 is a hydrogen atom, the other is a saturated aliphatic hydrocarbon group having 6 to 30 carbon atoms, and both R 1 and R 2 are saturated aliphatic hydrocarbon groups. When it is a hydrogen group, the total number of carbon atoms of R 1 and R 2 is 6 to 30, and X 1 and X 2
One is a -NY 1 Y 2 group (Y 1 , Y 2 represents an aliphatic hydrocarbon group having 10 to 28 carbon atoms), and the other is a -OM group (M represents hydrogen or an alkali metal or an amine) , N is 2 to 30
Indicates a positive number. ]
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4058787A JP2782484B2 (en) | 1992-02-13 | 1992-02-13 | Oil sludge dispersion method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4058787A JP2782484B2 (en) | 1992-02-13 | 1992-02-13 | Oil sludge dispersion method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0641554A JPH0641554A (en) | 1994-02-15 |
JP2782484B2 true JP2782484B2 (en) | 1998-07-30 |
Family
ID=13094288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4058787A Expired - Fee Related JP2782484B2 (en) | 1992-02-13 | 1992-02-13 | Oil sludge dispersion method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2782484B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0826213B2 (en) * | 1987-03-10 | 1996-03-13 | ダイセル・ヒユルス株式会社 | Resin composition |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5481307A (en) * | 1977-12-13 | 1979-06-28 | Toho Kagaku Kougiyou Kk | Liquid fuel composition |
JPS5486505A (en) * | 1977-12-22 | 1979-07-10 | Toho Kagaku Kougiyou Kk | Fuel oil composition |
ATE74620T1 (en) * | 1987-09-15 | 1992-04-15 | Basf Ag | FUELS FOR GASOLINE ENGINES. |
-
1992
- 1992-02-13 JP JP4058787A patent/JP2782484B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0641554A (en) | 1994-02-15 |
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