JPS6146037B2 - - Google Patents
Info
- Publication number
- JPS6146037B2 JPS6146037B2 JP7267879A JP7267879A JPS6146037B2 JP S6146037 B2 JPS6146037 B2 JP S6146037B2 JP 7267879 A JP7267879 A JP 7267879A JP 7267879 A JP7267879 A JP 7267879A JP S6146037 B2 JPS6146037 B2 JP S6146037B2
- Authority
- JP
- Japan
- Prior art keywords
- fatty acid
- acid ester
- sorbitan fatty
- sludge
- petroleum
- 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
Links
- 239000010802 sludge Substances 0.000 claims description 26
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 16
- 229930195729 fatty acid Natural products 0.000 claims description 16
- 239000000194 fatty acid Substances 0.000 claims description 16
- -1 sorbitan fatty acid ester Chemical class 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 13
- 239000003208 petroleum Substances 0.000 claims description 12
- 238000009825 accumulation Methods 0.000 claims description 9
- 230000008021 deposition Effects 0.000 claims description 5
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims description 4
- 125000002947 alkylene group Chemical group 0.000 claims description 3
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 229920006395 saturated elastomer Polymers 0.000 claims description 2
- 150000004671 saturated fatty acids Chemical class 0.000 claims description 2
- 150000004670 unsaturated fatty acids Chemical class 0.000 claims description 2
- 235000021122 unsaturated fatty acids Nutrition 0.000 claims description 2
- 125000004185 ester group Chemical group 0.000 claims 1
- 239000010779 crude oil Substances 0.000 description 12
- 239000003921 oil Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 239000012188 paraffin wax Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 239000013078 crystal Substances 0.000 description 3
- 239000003112 inhibitor Substances 0.000 description 3
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical compound OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 description 2
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 2
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 239000000600 sorbitol Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 150000005690 diesters Chemical class 0.000 description 1
- 150000004665 fatty acids Chemical group 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- MOYKHGMNXAOIAT-JGWLITMVSA-N isosorbide dinitrate Chemical compound [O-][N+](=O)O[C@H]1CO[C@@H]2[C@H](O[N+](=O)[O-])CO[C@@H]21 MOYKHGMNXAOIAT-JGWLITMVSA-N 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000005691 triesters Chemical class 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Description
本発明は石油スラツジの堆積防止方法に関し、
とくに原油スラツジの堆積防止方法に関する。
現在わが国で最も多く使用されているエネルギ
ー源である石油はほとんどすべて海外から輸入さ
れ、巨大なタンクに貯蔵される。このタンクの大
きさをみると1基10万Kl以上の超大型タンクが全
体の4割弱を占め、平均約6万Klである。
一方、エネルギー供給の安定化を計る目的で石
油の長期備蓄計画が進められているが、この計画
に用いられるタンクはさらに巨大なものになると
考えられる。
石油、とくに原油を貯蔵する場合に大きな問題
となつているのは、各種の安全対策とともにタン
ク底部に堆積するスラツジの問題である。容量10
万Klのタンクの場合、タンク底から数mの高さま
でスラツジが堆積しているタンクもあり、そのス
ラツジ量は1万Kl以上に達する。
スラツジの堆積はタンクの実質的な貯蔵能力を
低下させるばかりでなく、タンクに付属する送油
管やポンプ等を閉塞する原因ともなる。
このスラツジは分子量の大きなパラフイン類が
主成分となり、これに芳香族高分子化合物、アス
フアルテン、レジン等が混合した複雑な組成をと
るもので、流動点が非常に高いためにその除去に
は多大な経費を必要とする。
このようなことは原油に限らず重油タンクでも
起こり、石油を大量消費する発電所等の事業所で
も重要な問題となつている。
このスラツジの堆積を防止する方法として現在
わが国で行なわれているのはもつぱら機械的な方
法である。すなわち、タンクの側面につけた撹拌
機によつてタンク内の原油を強制的に対流させ、
スラツジが沈降するのを防ぐ方法である。しか
し、巨大なタンクではタンク内の一部に流れが生
じるだけで充分な撹拌効果が得られない。また撹
拌機の運転に要する電力も無視できず、とくに長
期備蓄計画用のタンクでは経済的に不利である。
これらの理由から、微量の化学物質を添加して
スラツジの堆積を防止する方法が検討されるよう
になり、米国ではかなり以前から検討されてき
た。
その方法は、スラツジの成分であるパラフイン
等の結晶が析出するのを防止することを目的とし
ている。
しかしこの方法を単にわが国の場合にあてはめ
ることはできない。わが国に輸入される石油は、
気温のかなり高い中東等の遠隔地から長期間かけ
て比較的冷涼なわが国まで運ばれてくるため、輸
入原油中にはすでに充分に析出し、かつ成長した
パラフイン等の結晶が存在しているからである。
以上の理由から、本発明者らはわが国の石油事
情に合致したスラツジの堆積防止方法として、す
でに最大限に近く発生しているスラツジを界面活
性物質によつて石油中に安定に分散させ、タンク
底に沈降させないようにする目的で検討を積み重
ねた結果、石油にポリオキシアルキレンソルビタ
ン脂肪酸エステルを添加することによりスラツジ
の堆積が有効に防止されることを見い出した。
本発明で使用するポリオキシアルキレンソルビ
タン脂肪酸エステルはソルビタンまたはソルビト
ールと炭素数4〜22の直鎖または分枝鎖の、飽和
または不飽和の脂肪酸とを加熱脱水することによ
つて得られるエステルより誘導されるが、この原
料エステル中にはソルビトール、ソルビタン、ソ
ルバイド等のモノ、ジ、トリエステルが複雑な組
成比で混在するため、以下の説明では原料エステ
ル中の主成分名で表わすことにする。
このようなエステルにエチレンオキシドを5モ
ル以上付加するか、あるいはエチレンオキシドと
プロピレンオキシド、ブチレンオキシド等の他の
アルキレンオキシドとを合計5モル以上ブロツク
状またはランダム状に付加することによつて本発
明で使用するポリオキシアルキレンソルビタン脂
肪酸エステルが得られる。
本発明で使用するポリオキシアルキレンソルビ
タン脂肪酸エステルは、原料である脂肪酸の種
類、組成、アルキレンオキシドの種類、付加量、
組成等によつて石油スラツジの堆積防止効果に差
があるが、石油の種類に応じてこれらの条件を適
切に選ぶことにより、スラツジの堆積量を非常に
少くすることができる。
これらのポリオキシアルキレンソルビタン脂肪
酸エステルの添加量は石油に対して2〜
500ppm、好ましくは5〜150ppmである。2ppm
未満では効果が小さく、500ppmをこえてもそれ
ほど効果が向上しないために経済的に不利であ
る。
一方、パラフイン析出防止剤である分枝ポリエ
チレン(米国特許第3640824号)やナフタレン
(米国特許第3276519号)を用いた場合には堆積ス
ラツジ量はほとんど減少せず、何も添加しない場
合との差はほとんど認められなかつた。
しかし、原油を長期にわたつて備蓄する場合、
徐々に新たなパラフイン等の結晶が析出するとき
にはこれらのパラフイン析出防止剤と本発明のポ
リオキシアルキレンソルビタン脂肪酸エステルと
を併用すると効果的であろう。
つぎに本発明を実施例および比較例によつて説
明するが、試験はつぎの方法で行なつた。
試験容器として100ml遠沈管(JIS K−2603−
1971 遠心分離用型目盛試験管)を使用し、こ
れに原油を100mlとり、つぎに添加剤を加えたの
ち、密栓して振とう混合したものを所定温度の恒
温室中に静置した。所定期間経過したのち、この
遠沈管を逆さにして原油を流し出し、逆さにした
ままさらに1時間同じ恒温室中に静置した。この
状態でまだ底部に残つている堆積スラツジ量を遠
沈管目盛で読み取り、堆積防止効果を判断した。
表−1はバスラライト原油を用い、20℃で100
日間静置した場合の試験結果であるが、本発明の
ポリオキシアルキレンソルビタン脂肪酸エステル
を添加した実施例1〜10は堆積スラツジ量が少な
いことが明らかである。比較例1は添加剤を加え
ない場合、比較例2〜3は前記米国特許のパラフ
イン析出防止剤を加えた場合、比較例4〜10は他
の界面活性剤を用いた場合である。
The present invention relates to a method for preventing the accumulation of petroleum sludge,
In particular, it relates to a method for preventing accumulation of crude oil sludge. Oil, the most commonly used energy source in Japan today, is almost entirely imported from overseas and stored in huge tanks. Looking at the size of these tanks, just under 40% of them are ultra-large tanks with a capacity of 100,000 Kl or more each, and the average capacity is approximately 60,000 KL. Meanwhile, a long-term oil stockpiling plan is underway to stabilize energy supplies, but the tanks used in this plan are likely to be even larger. A major problem when storing oil, especially crude oil, is the problem of sludge accumulating at the bottom of tanks, as well as various safety measures. capacity 10
In the case of 10,000Kl tanks, sludge may accumulate several meters from the bottom of the tank, and the amount of sludge can reach over 10,000KL. The accumulation of sludge not only reduces the actual storage capacity of the tank, but also causes clogging of oil pipes, pumps, etc. attached to the tank. This sludge has a complex composition consisting mainly of paraffins with large molecular weights, mixed with aromatic polymer compounds, asphaltene, resin, etc. Because it has a very high pour point, it takes a lot of effort to remove it. Requires expenses. This kind of thing occurs not only in crude oil tanks but also in heavy oil tanks, and has become an important problem in business establishments such as power plants that consume large amounts of oil. The only methods currently used in Japan to prevent the accumulation of sludge are mechanical methods. In other words, a stirrer attached to the side of the tank forces convection of the crude oil in the tank.
This is a method to prevent sludge from settling. However, in a huge tank, the flow only occurs in a part of the tank, and a sufficient stirring effect cannot be obtained. Furthermore, the electric power required to operate the stirrer cannot be ignored, which is economically disadvantageous, especially in tanks for long-term stockpiling projects. For these reasons, methods of adding small amounts of chemicals to prevent sludge buildup have been studied in the United States for quite some time. The purpose of this method is to prevent the precipitation of crystals such as paraffin, which is a component of the sludge. However, this method cannot simply be applied to the case of Japan. Oil imported into our country is
Imported crude oil is transported over a long period of time from remote areas such as the Middle East, where temperatures are quite high, to Japan, where it is relatively cool, so there are already plenty of precipitated and grown crystals such as paraffin in imported crude oil. It is. For the above reasons, the present inventors have developed a method for preventing the accumulation of sludge that is consistent with Japan's petroleum situation by stably dispersing the sludge, which has already been generated close to the maximum, into oil using a surfactant. As a result of repeated studies aimed at preventing sludge from settling to the bottom, it was discovered that adding polyoxyalkylene sorbitan fatty acid ester to petroleum can effectively prevent the accumulation of sludge. The polyoxyalkylene sorbitan fatty acid ester used in the present invention is derived from an ester obtained by heating and dehydrating sorbitan or sorbitol and a linear or branched, saturated or unsaturated fatty acid having 4 to 22 carbon atoms. However, in this raw ester, mono-, di-, and triesters such as sorbitol, sorbitan, and sorbide are mixed in a complicated composition ratio, so in the following explanation, the names of the main components in the raw ester will be used. These esters can be used in the present invention by adding 5 moles or more of ethylene oxide, or by adding 5 moles or more of ethylene oxide and other alkylene oxides such as propylene oxide or butylene oxide in a block or random pattern. A polyoxyalkylene sorbitan fatty acid ester is obtained. The polyoxyalkylene sorbitan fatty acid ester used in the present invention includes the type and composition of the fatty acid as a raw material, the type and amount of alkylene oxide added,
Although the effect of preventing petroleum sludge from accumulating varies depending on the composition, etc., by appropriately selecting these conditions depending on the type of petroleum, the amount of sludge accumulation can be extremely reduced. The amount of these polyoxyalkylene sorbitan fatty acid esters added is 2 to
500 ppm, preferably 5 to 150 ppm. 2ppm
If it is less than 500 ppm, the effect will be small, and if it exceeds 500 ppm, the effect will not improve much, which is economically disadvantageous. On the other hand, when branched polyethylene (U.S. Pat. No. 3,640,824) or naphthalene (U.S. Pat. No. 3,276,519), which are paraffin precipitation inhibitors, are used, the amount of deposited sludge hardly decreases, and there is no difference from the case where nothing is added. was hardly recognized. However, when storing crude oil for a long period of time,
When new crystals such as paraffin are gradually precipitated, it may be effective to use these paraffin precipitation inhibitors in combination with the polyoxyalkylene sorbitan fatty acid ester of the present invention. Next, the present invention will be explained with reference to Examples and Comparative Examples, and tests were conducted in the following manner. A 100ml centrifuge tube (JIS K-2603-
Using a 1971 centrifugal graduated test tube, 100 ml of crude oil was added to the tube, additives were added, the mixture was tightly capped, shaken, and the mixture was allowed to stand in a thermostatic chamber at a predetermined temperature. After a predetermined period of time had elapsed, the centrifuge tube was turned upside down, the crude oil was poured out, and the tube was left standing upside down in the same constant temperature room for another hour. In this state, the amount of accumulated sludge still remaining at the bottom was read on a centrifuge tube scale to judge the effect of preventing accumulation. Table 1 uses basralite crude oil at 100°C at 20°C.
The test results obtained when the samples were allowed to stand for one day showed that Examples 1 to 10 in which the polyoxyalkylene sorbitan fatty acid ester of the present invention was added had a small amount of deposited sludge. Comparative Example 1 is a case in which no additive is added, Comparative Examples 2 to 3 are cases in which the above-mentioned US patent paraffin precipitation inhibitor is added, and Comparative Examples 4 to 10 are cases in which another surfactant is used.
【表】【table】
【表】
表−2にウムシヤイフ原油を用い、20℃で100
日間静置した場合を示すが、本発明のポリオキシ
アルキレンソルビタン脂肪酸エステルを使用した
実施例11〜17はいずれも堆積スラツジ量が著しく
少ない。[Table] In Table-2, Umm-Syaif crude oil is used, and 100% at 20℃
The case where the samples were allowed to stand for one day is shown, but in all Examples 11 to 17 in which the polyoxyalkylene sorbitan fatty acid ester of the present invention was used, the amount of deposited sludge was extremely small.
【表】【table】
【表】
表−3に大慶原油を用い、40℃で80日間静置し
た場合を示すが、本発明の実施例18〜24はいずれ
も非常に良好な堆積防止効果を示した。[Table] Table 3 shows the case where Daqing crude oil was used and allowed to stand at 40°C for 80 days, and Examples 18 to 24 of the present invention all showed very good deposition prevention effects.
Claims (1)
酸エステルを添加することを特徴とする石油スラ
ツジの堆積防止方法。 2 ポリオキシアルキレンソルビタン脂肪酸エス
テルが炭素数4〜22の直鎖または分枝鎖の、飽和
または不飽和の脂肪酸のエステルである特許請求
の範囲第1項記載の石油スラツジの堆積防止方
法。 3 ポリオキシアルキレンソルビタン脂肪酸エス
テルがソルビタン脂肪酸エステルのエチレンオキ
シド5モル以上の付加物である特許請求の範囲第
1項または第2項記載の石油スラツジの堆積防止
方法。 4 ポリオキシアルキレンソルビタン脂肪酸エス
テルがソルビタン脂肪酸エステルにエチレンオキ
シドと炭素数3または4のアルキレンオキシドと
を合計5モル以上ブロツク状またはランダム状に
付加したものである特許請求の範囲第1項または
第2項記載の石油スラツジの堆積防止方法。 5 ポリオキシアルキレンソルビタン脂肪酸エス
テルの添加量が石油に対して2〜500ppmである
特許請求の範囲第1項、第2項、第3項または第
4項記載の石油スラツジの堆積防止方法。[Claims] 1. A method for preventing deposition of petroleum sludge, which comprises adding polyoxyalkylene sorbitan fatty acid ester to petroleum. 2. The method for preventing deposition of petroleum sludge according to claim 1, wherein the polyoxyalkylene sorbitan fatty acid ester is an ester of a linear or branched, saturated or unsaturated fatty acid having 4 to 22 carbon atoms. 3. The method for preventing deposition of petroleum sludge according to claim 1 or 2, wherein the polyoxyalkylene sorbitan fatty acid ester is an adduct of sorbitan fatty acid ester with 5 moles or more of ethylene oxide. 4. Claims 1 or 2, wherein the polyoxyalkylene sorbitan fatty acid ester is obtained by adding ethylene oxide and an alkylene oxide having 3 or 4 carbon atoms to a sorbitan fatty acid ester in a block or random manner of 5 moles or more in total. The described method for preventing the accumulation of petroleum sludge. 5. The method for preventing deposition of petroleum sludge according to claim 1, 2, 3, or 4, wherein the amount of polyoxyalkylene sorbitan fatty acid ester added is 2 to 500 ppm based on petroleum.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7267879A JPS55164295A (en) | 1979-06-09 | 1979-06-09 | Deposit prevention of petroleum sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7267879A JPS55164295A (en) | 1979-06-09 | 1979-06-09 | Deposit prevention of petroleum sludge |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS55164295A JPS55164295A (en) | 1980-12-20 |
JPS6146037B2 true JPS6146037B2 (en) | 1986-10-11 |
Family
ID=13496261
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7267879A Granted JPS55164295A (en) | 1979-06-09 | 1979-06-09 | Deposit prevention of petroleum sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS55164295A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60127392A (en) * | 1983-12-12 | 1985-07-08 | Sanyo Chem Ind Ltd | Addition agent for improving flow property for fuel oil |
JPS60260691A (en) * | 1984-06-08 | 1985-12-23 | Mitsubishi Oil Co Ltd | Dehydrating agent for diesel gas oil |
-
1979
- 1979-06-09 JP JP7267879A patent/JPS55164295A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS55164295A (en) | 1980-12-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES2352963T3 (en) | ADDITIVES FOR OILS. | |
JPH0251478B2 (en) | ||
CA1277974C (en) | Oil and fuel oil compositions | |
EP0004195A2 (en) | Aqueous fuel oil emulsions | |
US4416796A (en) | Emulsion-breaking composition | |
FI91776C (en) | fuel Mixtures | |
NO309729B1 (en) | Petroleum intermediate distillate mixture containing nitrogenous additives and a method for regulating the sedimentation of paraffins | |
KR20070075310A (en) | Additives for low-sulfur mineral oil distillates, comprising graft copolymers based on ethylene-vinyl ester copolymers | |
US3251664A (en) | Fuel compositions containing branched polyalkylenepolyamines and derivatives thereof | |
EP0649456A1 (en) | Oil additives and compositions | |
US5494967A (en) | Oil additives and compositions | |
US2632694A (en) | Petroleum distillates containing ammonium mahogany sulfonates and oil soluble carboxylic acids to prevent corrosion | |
KR100306334B1 (en) | Oil Additives and Compositions | |
JPS6146037B2 (en) | ||
US5423890A (en) | Fuel oil additive and compositions | |
JPH02300292A (en) | Additive for fuel or lubricating oil | |
JP2005179674A (en) | Low temperature flowability-improving agent composition for fuel | |
KR101027884B1 (en) | A fuel oil composition | |
US4444567A (en) | Motor fuel composition containing an ashless antiknock agent | |
JP4754773B2 (en) | Oily liquids stabilized against oxidation based on vegetable or animal oils | |
RU2771022C2 (en) | Cold-resistant additives lowering freezing point | |
JPS621433B2 (en) | ||
JPS621435B2 (en) | ||
JPS6310197B2 (en) | ||
US3838990A (en) | Middle distillate fuel oil compositions having improved pumpability |