JPH0381395A - Tetrafluoroethane composition for refrigerating machine - Google Patents

Tetrafluoroethane composition for refrigerating machine

Info

Publication number
JPH0381395A
JPH0381395A JP1217551A JP21755189A JPH0381395A JP H0381395 A JPH0381395 A JP H0381395A JP 1217551 A JP1217551 A JP 1217551A JP 21755189 A JP21755189 A JP 21755189A JP H0381395 A JPH0381395 A JP H0381395A
Authority
JP
Japan
Prior art keywords
residue
group
tetrafluoroethane
compound
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.)
Pending
Application number
JP1217551A
Other languages
Japanese (ja)
Inventor
Iwahiro Otsuka
大塚 厳弘
Hiroki Fukuda
博樹 福田
Kiyoshi Tanabe
田辺 清士
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.)
AGC Inc
Original Assignee
Asahi Glass 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 Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP1217551A priority Critical patent/JPH0381395A/en
Priority to AU45087/89A priority patent/AU616073B2/en
Priority to EP89912503A priority patent/EP0406433B9/en
Priority to PCT/JP1989/001150 priority patent/WO1990005172A1/en
Priority to DE68927858T priority patent/DE68927858T3/en
Priority to CA002002693A priority patent/CA2002693C/en
Priority to KR1019900701488A priority patent/KR960007698B1/en
Publication of JPH0381395A publication Critical patent/JPH0381395A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the title composition excellent in functions such as abrasion, friction and anti-seizing properties at a sliding part of a compressor, etc., and having low moisture absorption properties by mixing a specific polyether with tetrafluoroethane. CONSTITUTION:The title composition is obtained by mixing one or more ethers selected from the group consisting of ethers of formulae I-III [wherein R<1> is alkylene; R<2-4> are each alkanesulfonyl, arenesulfonyl or H provided that 2 or more of R<2-4> are not H atoms at the same time; l, m and n are each a positive number such that the kinematic viscosity may be 5-300cst (40 deg.C); X<1> is R<1> or the residue of a monohydroxy compound from which the hydroxyl group is removed provided that X<1> and R<1> are not H atoms at the same time: R<2> is the residue of a dihydroxy compound from which the hydroxyl groups are removed; and X<3> is the residue of a trihydroxy compound from which the hydroxyl groups are removed] with the tetrafluoroethane.

Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は、冷媒であるテトラフルオロエタン、好ましく
は1,1,1.2−テトラフルオロエタン(R−134
a)に対し、−20℃ないしはそれ以下の温度から、+
40℃ないしはそれ以上の温度で、自由な比率で相溶性
を有し、かつ吸湿性が低いポリエーテルとテトラフルオ
ロエタンからなる冷凍機用組成物に関するものである。
[Industrial Application Field] The present invention is directed to the refrigerant tetrafluoroethane, preferably 1,1,1,2-tetrafluoroethane (R-134
For a), from -20℃ or lower, +
The present invention relates to a composition for a refrigerator consisting of polyether and tetrafluoroethane, which are compatible in any ratio at temperatures of 40° C. or higher and have low hygroscopicity.

【従来の技術】[Conventional technology]

冷蔵庫やカーエアコンなどの冷凍サイクルにおいて、R
−12(ジクロロジフルオロメタン)が良好な冷媒とし
て使用されている。しかしR−12は成層圏のオゾン層
を破壊し、生体系に悪影響を与える可能性があり、代替
物質の検討がなされている。R−12の代替物質として
は、R−134aが最も有力と考えられているが、R−
12用の一般的な冷凍機油であるナフテン系鉱油、パラ
フィン系鉱油はR−134aと相溶しない。したがって
、R−134a用の冷凍機油として、ナフテン系鉱油、
パラフィン系鉱油は使用することができない。 R−134aと比較的よく相溶する物質として、表1の
ような構造のポリエーテル油が知られている。 (ア)については、例えばDu PontのRe5ea
rchDisclosure(174830ct、19
78)に記載されている。(イ)については、例えばU
、 S、 Pat、 4.755゜316号に記載され
ている。 [発明が解決しようとする課題〕 しかし表1のようなポリエーテルには、次のような問題
点があった。 ・R−134aとの相溶性が十分でない一冷凍機油の最
も重要な役割である潤滑性を発揮するためには、R−1
34aと相溶し、R−134aと共に系内を循環する必
要がある。(7) 、 C45の冷凍機油は、例えば4
0℃における動粘度が100cstの場合、高温臨界温
度(表1備考覧参照)は、表1に示すとおりである。相
溶性が十分とは言えない。 ・吸湿性が高い−(7) 、 C4)の冷凍機油は、吸
湿性が高く、水分を吸収しやすい。水分の混入により絶
縁抵抗の低下、金属に対する腐食性の増大といった悪影
響をもたらす。 表1 従来のポリエーテル油と、 高温臨界温度 (*)高温臨界温度 :油とR−134aを重量比15:85で混合、密閉す
る。温度を上 昇していき、にごりまたは2 層分離が始まった温度を、高 温臨界温度と称する。相溶性 の良いものほど、高温臨界温 度は高くなる。 [課題を解決するための手段] 本発明者らは、前述の問題を解決するにあたり、ポリエ
ーテル油の吸湿性が高いのは末端ヒドロキシル基に原因
があると推定した。そこで、末端ヒドロキシル基の数が
1〜3の範囲のポリ−エーテルを用い、各末端ヒドロキ
シル基の全て、または一部をスルホン酸エステル化した
化合物を用いて、R−134a用冷凍機油としての評価
をは実施した。その結果、吸湿性の向上だけでなく、R
−134aとの相溶性、粘度指数についても向上してい
ることを見い出し、本発明を完成した。 すなわち、本発明は下記一般式 %式%) [式中、R1はアルキレン基、R”、 R”、 R’は
アルカンスルホニル、アレーンスルホニル又は水素、R
R,R1,R4は同一でも異なっていてもよい、(但し
、R”、 R”、 R’から選ばれる2個以上が同時に
水素となることはない。)β。 m、nは上記化合物■〜■の動粘度が5〜300cst
(40℃)となる正数であり、同一でも異なっていても
よい。 XIは水素、アルカンスルホニル、アレーンスルホニル
又はモノヒドロキシ化合物の水酸基を除いた残基。(但
し、XlとR1′は同時に水素となることはない、) X2はジヒドロキシ化合物の水酸基を除いた残基。 x3はトリヒドロキシ化合物の水酸基を除いた残基。] から選ばれるポリエーテルの少なくとも1種及びテトラ
フルオロエタンからなるテトラフルオロエタン系冷凍機
用組成物に関するものである。 一般式■におけるXIとしては、水素、スルホニル基又
はモノヒドロキシ化合物の水酸基を除いた残基である。 スルホニル基を−SQ、−Aと表わせば、Aとして例え
ばメチル基、エチル基、プロピル基、ブチル基等のアル
キル基やフェニル基等のアリール基が好ましい。モノヒ
ドロキシ化合物の水酸基を除いた残基としては、メチル
基、エチル基、プロピル基、ブチル基、2−エチルヘキ
シル基、ノニル基等のアルキル基やフェニル基等のアリ
ール基が好ましい。 一般式■におけるx3としては、エチレングリコール残
基、プロピレングリコール残基等のジヒドロキシ化合物
の水酸基を除いた残基が好ましく、一般式■におけるX
3としては、グリセリン残基、トリメチロールプロパン
残基等のトリヒドロキシ化合物の水酸基を除いた残基が
好ましい。 一般式Φ〜■におけるR1としては、エチレン基、プロ
ピレン基、ブチレン基、テトラメチレン基等のアルキレ
ン基であり、これらの単独あるいはこれらがランダム又
はブロック状に併存していてもよく、併存する場合はプ
ロピレン基を主成分とすることが好ましい。一般式■〜
■におけるR′は同一でも異なっていても良い。 一般式Φ〜■におけるRx、Rs、R4は前記と同様ア
ルカンスルホニル、アレーンスルホニル又は水素であり
、これらは同一でも異なっていてもよい。但し、XIと
R3は同時に水素となることはない。又、Rm、Rm、
f<4から選ばれる2個以上が同時に水素となることは
ない。 通常、一般式■、■、■で表わされる化合物を合成する
時、対応する開始剤は、それぞれ活性水素基の数はそれ
ぞれ1,2.3である。 活性水素基の数が4以上の開始剤を用いて、カーエアコ
ン用や冷蔵庫用の冷凍機油の一般的動粘度である12c
st (40℃)〜200cst (40℃)の範囲の
化合物を得ようとすると、12. m、 nの数すなわ
ち、アルキレンオキシドの付加モル数は少なくなり過ぎ
、潤滑性能が低下してしまうため、好ましくない。 前記一般式Φ〜■で表わされる化合物としては、冷凍機
油として圧縮機等の摺動部における摩擦、摩耗及び焼き
付き防止等の機能を充分に達成するために、その動粘度
として5〜300cst (40℃)、好ましくは12
〜200 cst(40℃)となるようなものが望まし
く、一般式Φ〜■における分子量あるいは(1,m、n
の値はこのような粘度範囲となるような値を選択するこ
とが好ましい。12.m、nの値はおよそ3〜60、好
ましくは6〜30であり、同一でも異なっていてもよい
。 前記一般式■〜■で表わされる化合物とR134aの重
量比はl/99〜99/1、好ましくは5/95〜60
/40である。R134aには、1,1,2.2−テト
ラフルオロエタン(R134)が少量含まれていてもよ
い。一般式Φ〜■の化合物は単独で、又はこれらの混合
物として使用することができる。 本発明の組成物は、低温〜高温分野の冷凍、冷蔵及び空
調を目的とした冷凍サイクルの応用の場合に特に有効で
あるが、ランキンサイクル等のその他各種の熱回収技術
用としても使用可能である。 本発明の組成物は、熱安定性が優れており、通常の使用
条件においては安定剤を必要としないが、過酷な使用条
件のため熱安定性の向上が必要な場合には、ジメチルホ
スファイト、ジイソプロピルホスファイト、ジフェニル
ホスファイト等のホスファイト系化合物、トリフエノキ
シホスフィンサルファイド、トリメチルホスフィンサル
ファイド等のホスフィンサルファイド系化合物その他グ
リシジルエーテル類等の安定剤を0.01−10重量%
程度添加すれば良い。 又、本発明の一般式Φ〜■で表わされる化合物と従来使
用されているナフテン系鉱物油、パラフィン系鉱物油、
アルキルベンゼン系合成油、ポリ−α−オレフィン系合
成油、フッ素系潤滑油であるパーフルオロポリエーテル
油、含フッ素シリコーン油あるいは本発明のポリエーテ
ル油以外のポリエーテル油等と混合使用することが可能
である。 又、フェノール系やアミン系の酸化防止剤、イオウやリ
ン系の極圧添加剤、シリコーン系の消泡剤、あるいはベ
ンゾトリアゾール等の金属不活性剤等の各種添加剤を本
発明の組成物にさらに添加しても良い。 〔作 用] 本発明において、末端のヒドロキシル基をスルホン酸エ
ステル化することにより、親水性が低下し、吸湿性が低
下するものと考えられる。 又、本発明の油と、冷媒であるテトラフルオロエタンと
の相溶化の機構は必ずしも明確ではないが、スルホン酸
エステル基のスルホン基と、テトラフルオロエタンとの
ある種の相互作用が関与しているものと考えられる。 【実施例] 実施例1〜5、比較例1〜5 実施例1〜5及び比較例1〜5に用いた油の構造、R−
134aとの相溶性、吸湿性、40℃における動粘度の
結果を表2に示す。 吸湿性テスト方法 直径150mmのシャーレに、水分0.03%以下であ
ることを確認した油を15g入れる。 シャーレを開放したまま、室温20℃、湿度50%の恒
温、恒温室に静置する。30時間後の油の重量なYgと
した時、重量増加率を次式[発明の効果]
In refrigeration cycles such as refrigerators and car air conditioners, R
-12 (dichlorodifluoromethane) has been used as a good refrigerant. However, R-12 can destroy the ozone layer in the stratosphere and have a negative impact on biological systems, so alternatives are being considered. R-134a is considered to be the most promising substitute for R-12;
Naphthenic mineral oil and paraffinic mineral oil, which are common refrigeration oils for R-12, are not compatible with R-134a. Therefore, naphthenic mineral oil,
Paraffinic mineral oil cannot be used. Polyether oils having the structures shown in Table 1 are known as substances that are relatively compatible with R-134a. Regarding (a), for example, Du Pont's Re5ea
rchDisclosure(174830ct, 19
78). Regarding (b), for example, U
, S. Pat, No. 4.755°316. [Problems to be Solved by the Invention] However, the polyethers shown in Table 1 had the following problems.・Insufficient compatibility with R-134a - In order to demonstrate lubricity, which is the most important role of refrigeration oil, R-1
It is necessary to be compatible with R-134a and circulate within the system together with R-134a. (7), C45 refrigerating machine oil is, for example, 4
When the kinematic viscosity at 0° C. is 100 cst, the high temperature critical temperature (see notes in Table 1) is as shown in Table 1. The compatibility cannot be said to be sufficient. - Highly hygroscopic - Refrigerating machine oil (7), C4) has high hygroscopicity and easily absorbs moisture. Contamination with moisture causes negative effects such as a decrease in insulation resistance and an increase in corrosiveness to metals. Table 1 Conventional polyether oil and High temperature critical temperature (*) High temperature critical temperature: Oil and R-134a are mixed at a weight ratio of 15:85 and sealed. As the temperature is increased, the temperature at which turbidity or two-layer separation begins is called the high temperature critical temperature. The better the compatibility, the higher the high-temperature critical temperature. [Means for Solving the Problems] In solving the above-mentioned problems, the present inventors presumed that the high hygroscopicity of polyether oil is caused by the terminal hydroxyl groups. Therefore, using a polyether with a number of terminal hydroxyl groups in the range of 1 to 3, and using a compound in which all or part of each terminal hydroxyl group was converted into a sulfonic acid ester, we evaluated it as a refrigerating machine oil for R-134a. was carried out. As a result, not only hygroscopicity is improved, but R
It was discovered that the compatibility with -134a and the viscosity index were also improved, and the present invention was completed. That is, the present invention is based on the following general formula (%) [wherein R1 is an alkylene group, R'', R'', R' is alkanesulfonyl, arenesulfonyl or hydrogen, R
R, R1, and R4 may be the same or different (however, two or more selected from R'', R'', and R' may not be hydrogen at the same time) β. m and n are the kinematic viscosity of the above compounds (■ to ■) of 5 to 300 cst
(40°C), and may be the same or different. XI is hydrogen, alkanesulfonyl, arenesulfonyl, or a residue of a monohydroxy compound from which the hydroxyl group has been removed. (However, Xl and R1' do not become hydrogen at the same time.) X2 is the residue of a dihydroxy compound from which the hydroxyl group has been removed. x3 is the residue of the trihydroxy compound from which the hydroxyl group has been removed. The present invention relates to a tetrafluoroethane-based refrigerator composition comprising at least one polyether selected from the following and tetrafluoroethane. XI in the general formula (2) is hydrogen, a sulfonyl group, or a residue of a monohydroxy compound from which the hydroxyl group has been removed. When a sulfonyl group is represented by -SQ or -A, A is preferably an alkyl group such as a methyl group, an ethyl group, a propyl group, a butyl group, or an aryl group such as a phenyl group. The residue of the monohydroxy compound excluding the hydroxyl group is preferably an alkyl group such as a methyl group, an ethyl group, a propyl group, a butyl group, a 2-ethylhexyl group, a nonyl group, or an aryl group such as a phenyl group. As x3 in the general formula (■), a residue from which the hydroxyl group of a dihydroxy compound such as an ethylene glycol residue or a propylene glycol residue has been removed is preferable;
3 is preferably a residue from which the hydroxyl group of a trihydroxy compound has been removed, such as a glycerin residue or a trimethylolpropane residue. R1 in the general formulas Φ~■ is an alkylene group such as an ethylene group, a propylene group, a butylene group, a tetramethylene group, etc., and these may be used alone or together in a random or block form, and when they exist together, It is preferable that the main component is a propylene group. General formula■~
R' in (2) may be the same or different. Rx, Rs, and R4 in the general formulas Φ to 2 are alkanesulfonyl, arenesulfonyl, or hydrogen as described above, and these may be the same or different. However, XI and R3 do not become hydrogen at the same time. Also, Rm, Rm,
Two or more elements selected from f<4 do not become hydrogen at the same time. Usually, when synthesizing the compounds represented by the general formulas (1), (2), and (2), the number of active hydrogen groups in the corresponding initiators is 1 and 2.3, respectively. Using an initiator with the number of active hydrogen groups of 4 or more, the kinematic viscosity is 12c, which is the general kinematic viscosity of refrigeration oil for car air conditioners and refrigerators.
st (40°C) to 200cst (40°C), 12. The number of m and n, that is, the number of moles of alkylene oxide added, becomes too small, which is undesirable because the lubricating performance deteriorates. The compounds represented by the general formulas Φ to ■ have a kinematic viscosity of 5 to 300 cst (40 °C), preferably 12
~200 cst (40°C) is desirable, and the molecular weight in the general formula Φ~■ or (1, m, n
It is preferable to select a value that falls within such a viscosity range. 12. The values of m and n are approximately 3 to 60, preferably 6 to 30, and may be the same or different. The weight ratio of the compounds represented by the above general formulas (1) to (2) and R134a is 1/99 to 99/1, preferably 5/95 to 60.
/40. R134a may contain a small amount of 1,1,2,2-tetrafluoroethane (R134). Compounds of the general formulas Φ to (■) can be used alone or as a mixture thereof. The composition of the present invention is particularly effective in refrigeration cycle applications for freezing, refrigeration, and air conditioning in the low to high temperature fields, but can also be used in various other heat recovery technologies such as Rankine cycles. be. The composition of the present invention has excellent thermal stability and does not require a stabilizer under normal usage conditions, but when it is necessary to improve thermal stability due to harsh usage conditions, dimethyl phosphite , phosphite compounds such as diisopropyl phosphite and diphenyl phosphite, phosphine sulfide compounds such as triphenoxyphosphine sulfide and trimethylphosphine sulfide, and other stabilizers such as glycidyl ethers in an amount of 0.01 to 10% by weight.
It is sufficient to add a certain amount. In addition, the compounds represented by the general formulas Φ to ■ of the present invention and conventionally used naphthenic mineral oils, paraffinic mineral oils,
Can be mixed with alkylbenzene-based synthetic oil, poly-α-olefin-based synthetic oil, perfluoropolyether oil which is a fluorinated lubricating oil, fluorine-containing silicone oil, or polyether oil other than the polyether oil of the present invention. It is. Additionally, various additives such as phenol-based or amine-based antioxidants, sulfur- or phosphorus-based extreme pressure additives, silicone-based antifoaming agents, or metal deactivators such as benzotriazole may be added to the composition of the present invention. It may be further added. [Function] In the present invention, it is thought that by converting the terminal hydroxyl group into a sulfonic acid ester, hydrophilicity is reduced and hygroscopicity is reduced. Further, although the mechanism of compatibilization between the oil of the present invention and the refrigerant tetrafluoroethane is not necessarily clear, it is believed that a certain interaction between the sulfonic group of the sulfonic acid ester group and tetrafluoroethane is involved. It is thought that there are. [Example] Examples 1 to 5, Comparative Examples 1 to 5 Structure of oil used in Examples 1 to 5 and Comparative Examples 1 to 5, R-
Table 2 shows the results of compatibility with 134a, hygroscopicity, and kinematic viscosity at 40°C. Hygroscopicity test method: 15 g of oil, which has been confirmed to have a moisture content of 0.03% or less, is placed in a petri dish with a diameter of 150 mm. The petri dish is left open in a constant temperature room with a room temperature of 20°C and a humidity of 50%. When the weight of oil after 30 hours is Yg, the weight increase rate is expressed by the following formula [Effect of the invention]

Claims (1)

【特許請求の範囲】 1、下記一般式 (1)▲数式、化学式、表等があります▼ (2)▲数式、化学式、表等があります▼ (3)▲数式、化学式、表等があります▼ [式中、R^1はアルキレン基、R^2、R^3、R^
4はアルカンスルホニル、アレーンスルホニル又は水素
、R^2、R^3、R^4は同一でも異なっていてもよ
い。(但し、R^2、R^3、R^4から選ばれる2個
以上が同時に水素となることはない。)l、m、nは上
記化合物(1)〜(3)の動粘度が5〜300cst(
40℃)となる正数であり、同一でも異なっていてもよ
い。 X^1は水素、アルカンスルホニル、アレーンスルホニ
ル又はモノヒドロキシ化合物の水酸基を除いた残基。(
但し、X^1とR^2は同時に水素となることはない。 ) X^2はジヒドロキシ化合物の水酸基を除いた残基。 X^3はトリヒドロキシ化合物の水酸基を除いた残基。 ] から選ばれるポリエーテルの少なくとも1種及びテトラ
フルオロエタンからなるテトラフルオロエタン系冷凍機
用組成物。
[Claims] 1. The following general formula (1) ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (2) ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (3) ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ [In the formula, R^1 is an alkylene group, R^2, R^3, R^
4 is alkanesulfonyl, arenesulfonyl, or hydrogen, and R^2, R^3, and R^4 may be the same or different. (However, two or more selected from R^2, R^3, and R^4 will not become hydrogen at the same time.) l, m, and n represent compounds (1) to (3) whose kinematic viscosity is 5. ~300cst(
40° C.), and may be the same or different. X^1 is hydrogen, alkanesulfonyl, arenesulfonyl, or a residue of a monohydroxy compound from which the hydroxyl group has been removed. (
However, X^1 and R^2 do not become hydrogen at the same time. ) X^2 is the residue of a dihydroxy compound from which the hydroxyl group has been removed. X^3 is the residue of the trihydroxy compound from which the hydroxyl group has been removed. ] A tetrafluoroethane-based refrigerator composition comprising at least one polyether selected from the following and tetrafluoroethane.
JP1217551A 1988-11-11 1989-08-25 Tetrafluoroethane composition for refrigerating machine Pending JPH0381395A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP1217551A JPH0381395A (en) 1989-08-25 1989-08-25 Tetrafluoroethane composition for refrigerating machine
AU45087/89A AU616073B2 (en) 1988-11-11 1989-11-09 Tetrafluoroethane composition for a refrigerator
EP89912503A EP0406433B9 (en) 1988-11-11 1989-11-09 Tetrafluoroethane composition for a regrigerator
PCT/JP1989/001150 WO1990005172A1 (en) 1988-11-11 1989-11-09 Tetrafluoroethane composition for a regrigerator
DE68927858T DE68927858T3 (en) 1988-11-11 1989-11-09 TETRAFLUORETHANGEMISCH FOR A REFRIGERATOR
CA002002693A CA2002693C (en) 1988-11-11 1989-11-10 Tetrafluoroethane composition for a refrigerator
KR1019900701488A KR960007698B1 (en) 1988-11-11 1990-07-11 Tetrafluoroethane composition for a refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1217551A JPH0381395A (en) 1989-08-25 1989-08-25 Tetrafluoroethane composition for refrigerating machine

Publications (1)

Publication Number Publication Date
JPH0381395A true JPH0381395A (en) 1991-04-05

Family

ID=16706033

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1217551A Pending JPH0381395A (en) 1988-11-11 1989-08-25 Tetrafluoroethane composition for refrigerating machine

Country Status (1)

Country Link
JP (1) JPH0381395A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7987007B2 (en) 2002-03-18 2011-07-26 Creative Technology Ltd Memory module with audio playback mode

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7987007B2 (en) 2002-03-18 2011-07-26 Creative Technology Ltd Memory module with audio playback mode

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