JPS5947402B2 - Method for refining orthophosphate ester oil for electrical insulation - Google Patents

Method for refining orthophosphate ester oil for electrical insulation

Info

Publication number
JPS5947402B2
JPS5947402B2 JP8995376A JP8995376A JPS5947402B2 JP S5947402 B2 JPS5947402 B2 JP S5947402B2 JP 8995376 A JP8995376 A JP 8995376A JP 8995376 A JP8995376 A JP 8995376A JP S5947402 B2 JPS5947402 B2 JP S5947402B2
Authority
JP
Japan
Prior art keywords
orthophosphoric
triester
orthophosphoric acid
acid
refining
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
JP8995376A
Other languages
Japanese (ja)
Other versions
JPS5315596A (en
Inventor
貞喜 向井
修 山口
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.)
Nissin Electric Co Ltd
Original Assignee
Nissin Electric Co Ltd
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 Nissin Electric Co Ltd filed Critical Nissin Electric Co Ltd
Priority to JP8995376A priority Critical patent/JPS5947402B2/en
Publication of JPS5315596A publication Critical patent/JPS5315596A/en
Publication of JPS5947402B2 publication Critical patent/JPS5947402B2/en
Expired legal-status Critical Current

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  • Fixed Capacitors And Capacitor Manufacturing Machines (AREA)
  • Organic Insulating Materials (AREA)

Description

【発明の詳細な説明】 この発明は電気絶縁油用正リン酸トリエステルの精製法
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying orthophosphoric acid triester for electrical insulating oil.

周知のように、正リン酸トリエステルは、鉱物油とは異
なつて難燃性であり、又誘電率が大きいと言つた有利な
特性を備えているが、誘電正接、体積固有抵抗の点にお
いて劣つており、市販のままでは電気絶縁用としては利
用できない。
As is well known, orthophosphoric acid triester has advantageous properties such as being flame retardant and having a large dielectric constant, unlike mineral oil, but it is inferior in terms of dielectric loss tangent and volume resistivity. It is inferior and cannot be used for electrical insulation as it is commercially available.

このような不利な特性を呈する原因としては、正リン酸
トリエステルの合成の過程で正リン酸ジエステル、正リ
ン酸モノエステル(以下ハーフエステルと称す)又はリ
ン酸が生成され、これが油中に混在し5 ていることに
基因するものと考えられる。従来においても、これらの
分離のため、酸性白土による吸着処理或いは脱水処理が
行なわれているが、たとえばトリクレジルホスフエイト
について言えば市販のままではtanδが100%以上
、ρが1.0j0×1010オームCm(いずれも80
℃における値。以下同じ。)、破壊電圧48KV/ 2
.5−であるのに対し、酸性白土処理(1o0℃、1時
間)をほどこしたとしても、tanδが70Cfll、
ρが4.5×1010オームm、破壊電圧が52KV/
2.5wr!n程度’5 であり、この酸性白土処理
をほどこしたものを更に減圧脱水処理(100℃、10
−2−Hg)したとしてもtanδが50%、ρが8.
0×1010オームm、破壊電圧が52KV/ 2.5
−程度に改善されるにすぎず、これではなお電気絶縁油
として利用20できるものではない。粗製正リン酸トリ
エステルを分留することも考えられるが、ハーフエステ
ル、リン酸は沸点が高いため分留が極めて困難であるた
め従来のような常法の分留法では粗製正リン酸トリエス
テルからハーフエステル、リン酸を分離25することは
困難とされていた。この発明は、粗製正リン酸トリエス
テルからのハーフエステル、リン酸の分留を容易にし、
もつて電気絶縁油として使用可能な特性を満足するに足
る精製法を提供することにある。
The reason for these disadvantageous properties is that orthophosphoric acid diester, orthophosphoric acid monoester (hereinafter referred to as half ester), or phosphoric acid is produced during the synthesis of orthophosphoric acid triester, and this is produced in the oil. This is thought to be due to the fact that they are mixed. In the past, adsorption treatment with acid clay or dehydration treatment has been carried out to separate these substances, but for example, in the case of tricresyl phosphate, as it is commercially available, tan δ is 100% or more and ρ is 1.0j0× 1010 ohm Cm (both 80
Value in °C. same as below. ), breakdown voltage 48KV/2
.. 5-, but even with acid clay treatment (1o0℃, 1 hour), tan δ is 70Cfl,
ρ is 4.5×1010 ohmm, breakdown voltage is 52KV/
2.5wr! This acid clay treated material is further subjected to vacuum dehydration treatment (100℃, 100℃).
-2-Hg), tan δ is 50% and ρ is 8.
0x1010 ohm m, breakdown voltage 52KV/2.5
The improvement is only to a certain degree, and it is still not possible to use it as an electrical insulating oil. It is possible to fractionally distill the crude orthophosphoric acid triester, but since half esters and phosphoric acid have high boiling points, fractional distillation is extremely difficult. It has been considered difficult to separate half ester and phosphoric acid from ester. This invention facilitates the fractional distillation of half ester and phosphoric acid from crude orthophosphoric triester,
The object of the present invention is to provide a refining method that satisfies the characteristics necessary for use as an electrical insulating oil.

30この発明は、粗製正リン酸トリエステルを塩基性金
属酸化物の1種又は2種をもつて吸着処理をほどこし、
正リン酸トリエステル中のハーフエステル、リン酸を分
離除去し、ついで真空蒸留法によつて残余のハーフエス
テル、リン酸を正リン酸あ トリエステルから分留する
ことを特徴とする。
30 This invention subjects crude orthophosphoric acid triester to adsorption treatment with one or two types of basic metal oxides,
The method is characterized in that the half ester and phosphoric acid in the orthophosphoric acid triester are separated and removed, and then the remaining half ester and phosphoric acid are fractionated from the orthophosphoric acid triester using a vacuum distillation method.

ここに吸着処理のための化学吸着剤として鉄、亜鉛、カ
ルシウム、マグネシウム、バリウム、アルミニユウム、
クロム、鉛、カドミウムなどの塩基性金属酸化物のなか
から選択する。その金属酸化物の粉末を塔に充填し、こ
こに流通させるか或いは粉末を粗製正リン酸トリエステ
ルに混入し、かくはんするなどして化学吸着処理する。
前記粉末に粗製正リン酸トリエステル中のハーフエステ
ル、リン酸、その他の不純物が触れると反応して吸着さ
れ、不溶性又は難溶性の塩となる。このようにして、ハ
ーフエステル等の不純物の大半を分離除去したのち、正
リン酸トリエステルを高真空の下で蒸留すれば、残余の
ハーフエステル等の不純物を正リン酸トリエステルから
分留することができる。この場合、ハーフエステル、リ
ン酸等は正リン酸トリエステルよ)も沸点が高いので蒸
留後の正リン酸トリエステルは気相として取う出され、
ハーフエステル等は液相のままで残存する。高真空下で
行なうので蒸留温度を、大気圧時よりも低くすることが
できて都合がよい。つぎに、この発明の実施例を説明す
る。
Here iron, zinc, calcium, magnesium, barium, aluminum, as chemical adsorbents for adsorption treatment.
Select from basic metal oxides such as chromium, lead, and cadmium. The metal oxide powder is packed into a tower and distributed there, or the powder is mixed with crude orthophosphoric acid triester and stirred to perform chemisorption treatment.
When the half ester, phosphoric acid, and other impurities in the crude orthophosphoric acid triester come into contact with the powder, they react and are adsorbed, forming an insoluble or poorly soluble salt. After separating and removing most of the impurities such as half esters in this way, if the orthophosphoric triester is distilled under high vacuum, the remaining half esters and other impurities can be fractionated from the orthophosphoric triester. be able to. In this case, half esters, phosphoric acid, etc. (orthophosphoric triesters) also have high boiling points, so the orthophosphoric triesters after distillation are taken out as a gas phase.
Half esters and the like remain in the liquid phase. Since the distillation is carried out under high vacuum, the distillation temperature can be conveniently lowered than at atmospheric pressure. Next, embodiments of the invention will be described.

下記の表は、この発明にしたがつて精製処理した各リン
酸トリエステル油の電気特性を示すものである。な卦、
下記の表においてTCPはトリクレジホスフエート、C
DPはクレジルフエニールホスフエート、TXPはトリ
キシレニルホスフエート、MIPPはモノイソプロピル
フエノールの正リン酸トリエステル、0PP(1)はオ
ルソフエニルフエノール1モルとクレゾール2モルを含
む正リン酸トリエステル、0PP(2)はオルソフエニ
ルフエノール2モルとクレゾール1モルを含む正リン酸
トリエステルをそれぞれ示す。比較のためにTCPにつ
き化学吸着処理をせず真空蒸留のみを行なつた場合の特
性を最後の欄に併記した。なお、Tanδは%、ρはオ
ームm、破壊電圧はKV/2.5TWf1で表わしてあ
る。又化学吸着処理は室温で行なつた。蒸留装置として
薄膜蒸留装置(フイルムエバポレータ)を用いた。上記
の表から理解されるように、各種正リン酸トリエステル
はいずれも、Tanδが1.5〜1.9以下に、ρも8
.3〜8.7×1012以上に、又破壊電圧も60KV
/2.5wn程度となシ、未処理のもの、酸性白土処理
のみ或いはこれに減圧脱水処理を行なつたもの、更には
真空蒸留のみを行なつたものに比較すれば、いずれも顕
著に改善されていることが理解される。
The table below shows the electrical properties of each phosphotriester oil purified according to the present invention. A trigram,
In the table below, TCP is tricrediphosphate, C
DP is cresyl phenyl phosphate, TXP is tricylenyl phosphate, MIPP is orthophosphoric triester of monoisopropylphenol, and 0PP (1) is orthophosphoric triester containing 1 mole of orthophenylphenol and 2 moles of cresol. The ester, 0PP (2), each represents an orthophosphoric acid triester containing 2 moles of orthophenylphenol and 1 mole of cresol. For comparison, the characteristics of TCP when only vacuum distillation was performed without chemical adsorption treatment are also listed in the last column. Note that Tan δ is expressed in %, ρ is expressed in ohms m, and breakdown voltage is expressed in KV/2.5TWf1. The chemisorption treatment was also carried out at room temperature. A thin film distillation device (film evaporator) was used as the distillation device. As can be understood from the above table, all of the various orthophosphoric triesters have a Tan δ of 1.5 to 1.9 or less and a ρ of 8.
.. 3~8.7×1012 or more, and the breakdown voltage is 60KV
/2.5wn, which is a significant improvement when compared to untreated products, those treated only with acid clay treatment, those treated with vacuum dehydration, and those treated only with vacuum distillation. It is understood that what is being done.

これらの数値はいずれも電気絶縁油として充分使用可能
な範囲にあること言うまでもない。以上のように、この
発明による精製法によれば粗製正リン酸トリエステル中
のハーフエステル、リン酸、その他の不純物を充分除去
し、難燃性を損なわずその電気特性を、電気絶縁油とし
て充分使用に耐え得る範囲まで改善できる効果がある。
Needless to say, all of these values are within a range that allows sufficient use as electrical insulating oil. As described above, the refining method of the present invention sufficiently removes half ester, phosphoric acid, and other impurities from crude orthophosphoric acid triester, and maintains its electrical properties as an electrical insulating oil without impairing its flame retardancy. It has the effect of improving it to the extent that it can be used satisfactorily.

Claims (1)

【特許請求の範囲】[Claims] 1 粗製正リン酸トリエステルを塩基性金属酸化物で処
理して正リン酸トリエステル中の正リン酸ジエステル、
正リン酸モノエステル及びリン酸を分離除去し、ついで
真空蒸留法によつて残余の正リン酸ジエステル、正リン
酸モノエステル及びリン酸を正リン酸トリエステルから
分留することを特徴とする電気絶縁油用正リン酸トリエ
ステルの精製法。
1. Orthophosphoric acid diester in orthophosphoric triester by treating crude orthophosphoric acid triester with a basic metal oxide,
It is characterized by separating and removing the orthophosphoric acid monoester and phosphoric acid, and then fractionating the remaining orthophosphoric acid diester, orthophosphoric acid monoester, and phosphoric acid from the orthophosphoric acid triester by a vacuum distillation method. A method for purifying orthophosphoric acid triester for electrical insulating oil.
JP8995376A 1976-07-28 1976-07-28 Method for refining orthophosphate ester oil for electrical insulation Expired JPS5947402B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8995376A JPS5947402B2 (en) 1976-07-28 1976-07-28 Method for refining orthophosphate ester oil for electrical insulation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8995376A JPS5947402B2 (en) 1976-07-28 1976-07-28 Method for refining orthophosphate ester oil for electrical insulation

Publications (2)

Publication Number Publication Date
JPS5315596A JPS5315596A (en) 1978-02-13
JPS5947402B2 true JPS5947402B2 (en) 1984-11-19

Family

ID=13985052

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8995376A Expired JPS5947402B2 (en) 1976-07-28 1976-07-28 Method for refining orthophosphate ester oil for electrical insulation

Country Status (1)

Country Link
JP (1) JPS5947402B2 (en)

Also Published As

Publication number Publication date
JPS5315596A (en) 1978-02-13

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