JPS6055094A - Preparation of basic magnesium sulfonate - Google Patents
Preparation of basic magnesium sulfonateInfo
- Publication number
- JPS6055094A JPS6055094A JP16335783A JP16335783A JPS6055094A JP S6055094 A JPS6055094 A JP S6055094A JP 16335783 A JP16335783 A JP 16335783A JP 16335783 A JP16335783 A JP 16335783A JP S6055094 A JPS6055094 A JP S6055094A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- acid
- reaction
- hydroxyacetic acid
- basic magnesium
- 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.)
- Pending
Links
- 239000011777 magnesium Substances 0.000 title claims abstract description 27
- 229910052749 magnesium Inorganic materials 0.000 title claims abstract description 21
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 20
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 title claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims abstract description 10
- 150000003839 salts Chemical class 0.000 claims abstract description 10
- 239000002253 acid Substances 0.000 claims abstract description 9
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 8
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 8
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 8
- 239000000347 magnesium hydroxide Substances 0.000 claims abstract description 7
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims abstract description 7
- 239000002904 solvent Substances 0.000 claims abstract description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 24
- 239000000203 mixture Substances 0.000 claims description 15
- 239000001569 carbon dioxide Substances 0.000 claims description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 12
- 239000000395 magnesium oxide Substances 0.000 claims description 11
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 11
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- AEMRFAOFKBGASW-UHFFFAOYSA-N Glycolic acid Chemical compound OCC(O)=O AEMRFAOFKBGASW-UHFFFAOYSA-N 0.000 abstract description 22
- 229960004275 glycolic acid Drugs 0.000 abstract description 11
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 abstract description 5
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 abstract description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 4
- 150000002576 ketones Chemical class 0.000 abstract description 4
- 238000007796 conventional method Methods 0.000 abstract description 2
- 235000012254 magnesium hydroxide Nutrition 0.000 abstract 2
- 238000000034 method Methods 0.000 description 9
- 239000000126 substance Substances 0.000 description 7
- 239000003921 oil Substances 0.000 description 6
- 239000002585 base Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000003208 petroleum Substances 0.000 description 5
- 150000001412 amines Chemical class 0.000 description 4
- 239000002480 mineral oil Substances 0.000 description 4
- 235000010446 mineral oil Nutrition 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000008096 xylene Substances 0.000 description 3
- 150000001342 alkaline earth metals Chemical class 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- -1 magnesium sulfonates Chemical class 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 125000000020 sulfo group Chemical group O=S(=O)([*])O[H] 0.000 description 2
- 150000003460 sulfonic acids Chemical class 0.000 description 2
- XFNJVJPLKCPIBV-UHFFFAOYSA-N trimethylenediamine Chemical compound NCCCN XFNJVJPLKCPIBV-UHFFFAOYSA-N 0.000 description 2
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001341 alkaline earth metal compounds Chemical class 0.000 description 1
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 1
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- GHWVXCQZPNWFRO-UHFFFAOYSA-N butane-2,3-diamine Chemical compound CC(N)C(C)N GHWVXCQZPNWFRO-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000003747 fuel oil additive Substances 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 239000002198 insoluble material Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 150000002681 magnesium compounds Chemical class 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- ZNZJJSYHZBXQSM-UHFFFAOYSA-N propane-2,2-diamine Chemical compound CC(C)(N)N ZNZJJSYHZBXQSM-UHFFFAOYSA-N 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000000341 volatile oil Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
本発明は潤滑油あるいは燃料油の添加剤として有用な塩
基性マグネシウムスルホネートの製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a process for producing basic magnesium sulfonates useful as lubricating or fuel oil additives.
本発明においていう塩基性マグネシウムスルホネートと
は、スルホン酸を中和するのに必要表置と比較して、化
学量論必要量より過剰にマグネシウムを含む化合物を意
味する。The basic magnesium sulfonate as used in the present invention means a compound containing magnesium in excess of the stoichiometric amount required to neutralize the sulfonic acid.
従来、塩基性アルカリ土類スルホネートの一般的な製法
としては、油溶性スルホ/酸とアルカリ土類金属酸化物
または水酸化物との混合物中へ二酸化炭素を通ずる方法
であった。しかし、塩基性マグネシウムスルホネートの
場合は、他のアルカリ土類金属例えばバリウム、カルシ
ウムの場合と比較【7て、長い反応時間を必要とし、ま
た反応終了後のf過分熱が困難であるという点で異って
いる0
従来この問題点を克服する方法として種々な方法が提案
されている。その代表的な方法として、1)、石油媒体
中に油溶性中性マグネシウムスルホネート、酸化マグネ
シウムと、低級アルカノール、水及びエチレンジアミン
を含ませた反応混合物に二酸化炭素を通ずる方法。すな
わち、低級アルカノール、水及びエチレンジアミンを混
合物に含ませて、反応を促進すると共に濾過性をよくす
る方法。(特公昭49−13782号公報参照)
2)、油溶性スルホネートまたはスルホン酸、過剰のマ
グネシウム化合物に、炭化水素溶剤とアルコールまたは
ケトン、水及び反応促進剤を含ませだ混合物に特定条件
下で二酸化炭素を供給する方法。すなわち、アルコール
またはケトン、水及び反応促進剤を含ませて、反応を促
進すると共にf過性をよくする方法。(特開昭56−1
09821号公報参照)
しかしながら、これらの方法では十分に満足し得る程度
に改善されていない。Traditionally, a common method for making basic alkaline earth sulfonates has been to pass carbon dioxide through a mixture of an oil-soluble sulfo/acid and an alkaline earth metal oxide or hydroxide. However, in the case of basic magnesium sulfonate, compared to the case of other alkaline earth metals such as barium and calcium [7], it requires a long reaction time and it is difficult to carry out overheating after the reaction is completed. Different 0 Various methods have been proposed to overcome this problem. Typical methods include 1) passing carbon dioxide through a reaction mixture containing oil-soluble neutral magnesium sulfonate, magnesium oxide, lower alkanol, water and ethylenediamine in a petroleum medium; That is, a method in which lower alkanol, water, and ethylenediamine are included in the mixture to accelerate the reaction and improve filterability. (Refer to Japanese Patent Publication No. 49-13782) 2) A mixture containing an oil-soluble sulfonate or sulfonic acid, an excess of magnesium compound, a hydrocarbon solvent, an alcohol or ketone, water, and a reaction accelerator is subjected to oxidation under specific conditions. How to supply carbon. That is, a method in which alcohol or ketone, water, and a reaction accelerator are included to accelerate the reaction and improve the f-transactivity. (Unexamined Japanese Patent Publication No. 56-1
(See Publication No. 09821) However, these methods do not provide a sufficiently satisfactory improvement.
本発明の目的は、反応生成混合物の炭化水素溶解部と主
として無機物質から不溶物との分離が速やかでr過が容
易であり、かつ反応も迅速で、マグネシウム含有率が高
く、また全塩基価の高い塩基性マグネシウムスルホネー
トの製造法を提供するにある。It is an object of the present invention to quickly separate the hydrocarbon-dissolved portion of the reaction product mixture from insoluble materials mainly from inorganic substances, to facilitate filtration, to have a rapid reaction, to have a high magnesium content, and to have a total base number. The present invention provides a method for producing highly basic magnesium sulfonate.
本発明者らは、前記目的を達成すべく鋭意研究の結果、
従来法における、アルコール、またはケトンに代え、ヒ
ドロキシ酢酸を使用すると、前記目的が達成し得られる
ことを究明し得た。この知見に基いて本発明を完成した
。As a result of intensive research to achieve the above object, the present inventors found that
It has been found that the above object can be achieved by using hydroxyacetic acid instead of alcohol or ketone in conventional methods. The present invention was completed based on this knowledge.
本発明の要旨は、油溶性スルホ/酸またはその塩、これ
と反応する化学量論量より過剰の酸化マグネシウムまた
は水酸化マグネシウム、炭化水素溶剤、ヒドロキシ酢酸
、水及び反応促進剤を含む混合物に、二酸化炭素を通ず
ることを特徴とする塩基性マグネシウムスルホネートの
製造法にある。The gist of the invention is to provide a mixture comprising an oil-soluble sulfo/acid or its salt, a substoichiometric excess of magnesium oxide or hydroxide to be reacted with, a hydrocarbon solvent, hydroxyacetic acid, water and a reaction promoter. A method for producing basic magnesium sulfonate characterized by passing carbon dioxide therethrough.
本発明の方法で製りする塩基性マグネシウムスルホネー
トは、マグネシウムスルホネートの油溶液であり、それ
自身が、過剰のコロイド状アルカリ土類金属化合物を分
散する界面活性剤として働くものであるから、原料のス
ルホン酸またはその塩は油に可溶のものであることが必
要である。油溶性スルホン酸またはその塩としては、例
えば油I性石油スルホン酸、アルキルスルホン酸、アリ
ールスルホン酸、アルキルアリールスルホン酸、及びこ
れらの塩が挙げられる。塩としてはマグネシウム塩が最
も好ましいが、他のアルカリ、アルカリ土類金ll1l
塩あるいはアンモニウム塩であってもよい。The basic magnesium sulfonate produced by the method of the present invention is an oil solution of magnesium sulfonate, which itself acts as a surfactant to disperse excess colloidal alkaline earth metal compound. It is necessary that the sulfonic acid or its salt be soluble in oil. Examples of oil-soluble sulfonic acids or salts thereof include oil-based petroleum sulfonic acids, alkylsulfonic acids, arylsulfonic acids, alkylarylsulfonic acids, and salts thereof. Magnesium salts are most preferred as salts, but other alkali and alkaline earth metals may also be used.
It may be a salt or an ammonium salt.
酸化マグネシウムまたは水酸化マグネシウムの使用量は
、油溶性スルホン酸またはその塩と反応する化学量論量
より過剰であることが必要である。The amount of magnesium oxide or magnesium hydroxide used must be in excess of the stoichiometric amount for reaction with the oil-soluble sulfonic acid or its salt.
それはこの過剰のこれらをマグネシウムスルホネートに
分散保有させるためである。好ましい範囲は、油溶性ス
ルホン酸の当量に対し、2〜20当量であることが好ま
しい。炭化水素溶剤は、混合物中に二酸化炭素を供給す
る際、混合物を流動状態に保持させるためのものである
から、混合物を流動状態に保つ十分な量使用する。炭化
水素溶剤としては、例えば、トルエン、キシレン、鉱物
油あるいはヘキサン等が挙げられる。しかしこれに限定
されるものではない。This is because this excess of these substances is dispersed and retained in the magnesium sulfonate. The preferred range is 2 to 20 equivalents relative to the equivalent of the oil-soluble sulfonic acid. Since the hydrocarbon solvent is used to maintain the mixture in a fluid state when carbon dioxide is supplied into the mixture, an amount sufficient to maintain the mixture in a fluid state is used. Examples of the hydrocarbon solvent include toluene, xylene, mineral oil, and hexane. However, it is not limited to this.
ヒドロキシ酢酸は主として無機物質からなる固型沈殿物
を硬く、大きくする作用を有している。Hydroxyacetic acid has the effect of hardening and increasing the size of solid precipitates mainly composed of inorganic substances.
そのため反応生成物中の炭化水素溶解部と固型沈殿物と
の分離が速やかとなり、その分離も極めて容易となる。Therefore, the hydrocarbon dissolved portion in the reaction product and the solid precipitate can be quickly separated, and the separation is also extremely easy.
また、更に得られる塩基性マグネシウムスルホネートの
マグネシウム含有率を7.5%にも高めると共に全塩基
価(強酸で滴定した時の試料1を当量のKOHのキ当量
数)も380と高いものとなし得る。その使用量は酸化
マグネシウム1重量部に対し、0.2〜2.5重量部で
あることが好(5)
ましい。Furthermore, the magnesium content of the basic magnesium sulfonate obtained was increased to 7.5%, and the total base number (the number of KOH equivalents equivalent to sample 1 when titrated with a strong acid) was as high as 380. obtain. The amount used is preferably 0.2 to 2.5 parts by weight per 1 part by weight of magnesium oxide (5).
水は反応物の接触をよくし、反応を円滑にする作用をし
、その使用量は酸化マグネシウムまたは水酸化マグネシ
ウムの使用量に対し変化させ、酸化マグネシウムにおい
てはその1重量部に対し0.5〜1.5重量部であるこ
とが好ましい。Water has the effect of improving the contact between the reactants and smoothing the reaction, and the amount of water used is changed depending on the amount of magnesium oxide or magnesium hydroxide used, and in the case of magnesium oxide, it is 0.5% per 1 part by weight. It is preferable that it is 1.5 parts by weight.
反応促進剤社反応を促進すると共にマグネシウムの含有
率を高める作用をし、その代表例はアミン類、04〜0
6ジケトン類、油溶性カルボン酸等があるが、アミン類
が好ましい。アミン類としては、例えばエチレンジアミ
ン、ジアミノプロパン。Reaction accelerator acts to accelerate the reaction and increase the magnesium content, typical examples of which are amines, 04-0
Examples include 6-diketones and oil-soluble carboxylic acids, but amines are preferred. Examples of amines include ethylenediamine and diaminopropane.
ジアミノブタン、トリエチレンテトラミン等が挙げられ
る。しかし、それに限定されるものではない。その使用
量は、使用する酸化マグネシウムに1重量部に対し、0
.1〜1重量部であることが好ましい。Examples include diaminobutane and triethylenetetramine. However, it is not limited thereto. The amount used is 0 to 1 part by weight of the magnesium oxide used.
.. It is preferably 1 to 1 part by weight.
以上の混合物を加熱して50〜60℃になった時、二酸
化炭素を導入し初める。その温度を徐々に100℃まで
上昇させる。二酸化炭素の導入量は、酸化マグネシウム
の1当量に対し、1〜3当量が(6)
よい。二酸化炭素導入終了後、静置して放冷すると、固
型沈殿物が速やかに沈降する。これを遠心濾過等でP別
する。P液から炭化水素溶剤等の揮発性物質を溜去する
と、塩基性マグネシウムスルホネートの油溶液が得られ
る。When the above mixture is heated to 50 to 60°C, carbon dioxide begins to be introduced. The temperature is gradually increased to 100°C. The amount of carbon dioxide introduced is preferably 1 to 3 equivalents per equivalent of magnesium oxide (6). After the introduction of carbon dioxide, the solid precipitate quickly settles when left to cool. This is separated by P by centrifugal filtration or the like. When volatile substances such as hydrocarbon solvents are distilled off from the P liquid, an oil solution of basic magnesium sulfonate is obtained.
実施例1〜4
石油スルホン酸(分子量500 ) 50 Fと鉱油3
22との混合物に、酸化マグネシウム352、キシレン
174F、ヒドロキシ酢酸、水及びアミン反応促進剤を
下記の量づつ順次加えた。この反応混合物を加温し、5
0〜60℃に々つ九時二酸化炭素の導入を開始した。二
酸化炭素は60 l/3時間の割合で導入した。この間
反応混合物の温度、 を徐々に上昇させ、90〜100
℃にした。導入終了後放冷静置し、遠心濾過した。f液
を減圧下、150℃まで加熱して揮発性物質を5留去し
た。残液は塩基性マグネシウムスルホネート油溶液であ
り、その性状は下記の通りであった。Examples 1-4 Petroleum sulfonic acid (molecular weight 500) 50F and mineral oil 3
To the mixture with No. 22, magnesium oxide 352, xylene 174F, hydroxyacetic acid, water, and an amine reaction accelerator were added in the following amounts in order. The reaction mixture was warmed and
Introduction of carbon dioxide was started at 9 o'clock at a temperature of 0 to 60°C. Carbon dioxide was introduced at a rate of 60 l/3 h. During this time, the temperature of the reaction mixture was gradually increased to 90-100.
It was set to ℃. After the introduction was completed, the mixture was allowed to stand and centrifugally filtered. Liquid f was heated to 150° C. under reduced pressure to remove 5 volatile substances. The residual liquid was a basic magnesium sulfonate oil solution, and its properties were as follows.
なお、比較のため、ヒドロキシ酢酸を混合しない場合を
列記する。For comparison, the case where hydroxyacetic acid is not mixed is listed.
この結果が示すように、ヒドロキシ酢酸の混合によシ、
濾過性がよくな漫、また、生成物の量1Mg含有率も向
上し、1つ全塩基価の高いものが得られる。As this result shows, mixing hydroxyacetic acid
The filterability is improved, the Mg content of the product is also improved, and a product with a high total base number is obtained.
実施例5
油溶性石油スルホン酸ナトリウム(平均分子量500)
油含有率60%の鉱油溶液821、重油170 t、
Mg0j2・6H2011,2f及び水25fを、45
℃で3時間攪拌した後水層を除去した。これに酸化マグ
ネシウム35f1ヒドロキシ酢酸10f1水312及び
エチレンジアミン3.52を加えた。この混合物を50
〜100℃の温度上昇操作中に二酸化炭素60ノを3時
間で導入した。その後放冷、静置し、遠心濾過しだ。r
液を減圧下で1501:まで加熱して揮発油物質を追出
し、残液295fを得た。Example 5 Oil-soluble sodium petroleum sulfonate (average molecular weight 500)
Mineral oil solution with oil content of 60% 821, heavy oil 170 t,
Mg0j2・6H2011, 2f and water 25f, 45
After stirring at ℃ for 3 hours, the aqueous layer was removed. To this were added 35 f1 of magnesium oxide, 10 f1 of hydroxyacetic acid, 312 g of water, and 3.52 g of ethylenediamine. 50% of this mixture
During the temperature raising operation to ~100°C, 60 kg of carbon dioxide were introduced over 3 hours. After that, it was left to cool, left to stand, and centrifugally filtered. r
The liquid was heated to 1501:1 under reduced pressure to drive off volatile oil substances, yielding 295f of residual liquid.
濾過性は良好で、Mg含有率6%、全塩基価は300で
あった。The filterability was good, the Mg content was 6%, and the total base number was 300.
゛ 実施例6
石油スルホン酸(分子量570 ) 50 rと鉱油(
9)
32fとの混合物に、水酸化マグネシウム511i?、
キシレン114y、じドロキシ酢酸10 f、 水31
F及び1.3−ジアミノプロパン4.3 f ′(i7
順次に加えた。反応混合物を50〜60℃に加渇し二酸
化炭素の導入を開始し、40473時間の割合で導入l
−だ。その間混合物の温度を90〜100′cまで徐々
に上昇させ反応を完了し、放冷・静置した後、遠心濾過
した。P液を減圧下、150℃まで加熱して揮発性物質
を除去し、塩基性マグネクラムスルホネート103r′
fc得たo Mg含有率は5.3%、全塩基価は250
であった。また濾過性は良好であった。゛ Example 6 Petroleum sulfonic acid (molecular weight 570) 50 r and mineral oil (
9) Magnesium hydroxide 511i in the mixture with 32f? ,
114y of xylene, 10f of didroxyacetic acid, 31g of water
F and 1,3-diaminopropane 4.3 f′(i7
Added sequentially. The reaction mixture was cooled to 50-60°C and the introduction of carbon dioxide was started at a rate of 40,473 hours.
-It is. During this time, the temperature of the mixture was gradually raised to 90-100'C to complete the reaction, allowed to cool and stand, and then centrifugally filtered. The P solution was heated to 150°C under reduced pressure to remove volatile substances, and basic magnesium sulfonate 103r'
fc obtained o Mg content is 5.3%, total base number is 250
Met. Moreover, the filterability was good.
以上のように、本発明の方法によると、r過性が極めて
良好となり、また、得られる塩基性マグネシウムスルホ
ネートの収率、そのMg含有率、全#i&価の高いもの
が容易に得られる優れた効果な秦し得られる。As described above, according to the method of the present invention, the r-permeability is extremely good, and the yield of the basic magnesium sulfonate obtained, its Mg content, and the high total #i & value are easily obtained. The effective Qin Dynasty was obtained.
特許出願人 錦海化学株式会社 (10)Patent applicant Kinkai Chemical Co., Ltd. (10)
Claims (1)
化学量論量より過剰の酸化マグネシウムまたは水酸化マ
グネシウム、炭化水素溶剤、とドロキシ酢酸、水及び反
応促進剤を含む混合物に、二酸化炭素を通ずることを特
徴とする塩基性マグネシウムスルホネートの製造法。1. Passing carbon dioxide through a mixture containing an oil-soluble sulfonic acid or its salt, a stoichiometric excess of magnesium oxide or hydroxide to be reacted with, a hydrocarbon solvent, droxyacetic acid, water, and a reaction promoter. A method for producing basic magnesium sulfonate, characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16335783A JPS6055094A (en) | 1983-09-07 | 1983-09-07 | Preparation of basic magnesium sulfonate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16335783A JPS6055094A (en) | 1983-09-07 | 1983-09-07 | Preparation of basic magnesium sulfonate |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6055094A true JPS6055094A (en) | 1985-03-29 |
Family
ID=15772343
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16335783A Pending JPS6055094A (en) | 1983-09-07 | 1983-09-07 | Preparation of basic magnesium sulfonate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6055094A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008196796A (en) * | 2007-02-14 | 2008-08-28 | Matsushita Electric Ind Co Ltd | Heat storage device |
JP2009097746A (en) * | 2007-10-15 | 2009-05-07 | Panasonic Corp | Heat storage device |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5573653A (en) * | 1978-11-30 | 1980-06-03 | Saapasu Chem Ltd | Basified magnesium sulfonate |
-
1983
- 1983-09-07 JP JP16335783A patent/JPS6055094A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5573653A (en) * | 1978-11-30 | 1980-06-03 | Saapasu Chem Ltd | Basified magnesium sulfonate |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008196796A (en) * | 2007-02-14 | 2008-08-28 | Matsushita Electric Ind Co Ltd | Heat storage device |
JP2009097746A (en) * | 2007-10-15 | 2009-05-07 | Panasonic Corp | Heat storage device |
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