[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JPH07118259A - Method for purifying lactide and method for polymerizing the same - Google Patents

Method for purifying lactide and method for polymerizing the same

Info

Publication number
JPH07118259A
JPH07118259A JP29129693A JP29129693A JPH07118259A JP H07118259 A JPH07118259 A JP H07118259A JP 29129693 A JP29129693 A JP 29129693A JP 29129693 A JP29129693 A JP 29129693A JP H07118259 A JPH07118259 A JP H07118259A
Authority
JP
Japan
Prior art keywords
lactide
benzene
isopropyl alcohol
crystal
molecular weight
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.)
Granted
Application number
JP29129693A
Other languages
Japanese (ja)
Other versions
JP2809069B2 (en
Inventor
Makoto Oguchi
誠 大垣内
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.)
Shimadzu Corp
Original Assignee
Shimadzu Corp
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 Shimadzu Corp filed Critical Shimadzu Corp
Priority to JP5291296A priority Critical patent/JP2809069B2/en
Publication of JPH07118259A publication Critical patent/JPH07118259A/en
Application granted granted Critical
Publication of JP2809069B2 publication Critical patent/JP2809069B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Heterocyclic Compounds That Contain Two Or More Ring Oxygen Atoms (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To obtain a refined lactide having a high purity, readily polymerizing, easily providing a polylactic acid having an extremely high molecular weight, by recrystallizing a lactide with a lower alcohol, then with benzene or an alkyl- substituted group-containing benzene. CONSTITUTION:An unpurified lactide is added to a lower alcohol (e.g. isopropyl alcohol), heated to 70 deg.C and completely dissolved. When the solution is cooled to 30 deg.C, a crystal is precipitated and filtered. The prepared crystal is washed with water or isopropyl alcohol. The prepared lactide is added to benzene or an alkyl-substituted benzene (e.g. toluene) and heated to 70 deg.C to completely dissolve the lactide. The solution is cooled to 30 deg.C, a crystal is precipitated and filtered. The prepared crystal is washed with a solvent and dried under reduced pressure to give the high-purity refined lactide providing a polylactic acid having an extremely high molecular weight.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はラクチドの精製法および
その重合法に関する。ラクチドは特にポリ乳酸の製造原
料などとして有用である。
FIELD OF THE INVENTION The present invention relates to a method for purifying lactide and a method for polymerizing the same. Lactide is particularly useful as a raw material for producing polylactic acid.

【0002】[0002]

【従来の技術および課題】ラクチドの精製法としてはイ
ソプロピルアルコールなど溶解度の温度依存性が高く、
不純物が溶けやすい溶媒を用いた再結晶法が知られてい
る。例えば、特開昭63−101378号には炭素数1〜6個の
アルコール、好ましくはイソプロピルアルコールからの
再結晶、あるいは溶液から非溶媒を用いて沈殿させるこ
とが記載されている。しかしながら、このような方法で
精製されたラクチドを用いて重合すると、得られるポリ
乳酸の分子量は1000〜5000程度であり、分子量
10万以上の高分子量ポリ乳酸を得ることは困難であ
る。
2. Description of the Related Art As a method for purifying lactide, solubility of isopropyl alcohol or the like has a high temperature dependence of solubility,
A recrystallization method using a solvent in which impurities are easily dissolved is known. For example, JP-A-63-101378 describes recrystallization from an alcohol having 1 to 6 carbon atoms, preferably isopropyl alcohol, or precipitation from a solution using a non-solvent. However, when the lactide purified by such a method is used for polymerization, the resulting polylactic acid has a molecular weight of about 1000 to 5000, and it is difficult to obtain a high molecular weight polylactic acid having a molecular weight of 100,000 or more.

【0003】本発明の目的は純度が高く、分子量の非常
に大きなポリ乳酸が容易に得られるラクチドおよびその
重合法を提供することにある。
An object of the present invention is to provide a lactide and a method for polymerizing the same, which makes it possible to easily obtain polylactic acid having a high purity and a very large molecular weight.

【0004】[0004]

【課題を解決するための手段】本発明はラクチドを低級
アルコールにて再結晶し、ついでベンゼンまたはアルキ
ル置換基ベンゼンにて再結晶することを特徴とするラク
チドの精製法を提供するものである。また、本発明は前
記の精製法により得られたラクチドを重合することを特
徴とするラクチドの重合法を提供するものである。
The present invention provides a method for purifying lactide, which comprises recrystallizing lactide with a lower alcohol and then recrystallizing with benzene or an alkyl-substituted benzene. The present invention also provides a method for polymerizing lactide, which comprises polymerizing the lactide obtained by the above-mentioned purification method.

【0005】本発明の精製法は従来公知の方法にて得ら
れたラクチドに適用できる。ラクチドはまず低級アルコ
ールにて再結晶される。このような低級アルコールとし
ては、メタノール、エタノール、n−プロピルアルコー
ル、イソプロピルアルコール(2−プロパノール)、ブ
タノール、ペンタノールなどが挙げられ、特にイソプロ
ピルアルコールが好ましい。
The purification method of the present invention can be applied to lactide obtained by a conventionally known method. Lactide is first recrystallized in lower alcohol. Examples of such lower alcohols include methanol, ethanol, n-propyl alcohol, isopropyl alcohol (2-propanol), butanol, pentanol and the like, and isopropyl alcohol is particularly preferable.

【0006】これらの低級アルコールによる再結晶は、
例えば粗ラクチドに対して1〜4倍(重量比)の溶媒を
用いて60〜70℃程度まで昇温して結晶を全て溶解さ
せた後、30℃以下まで冷却して結晶を得る。得られた
ラクチドの結晶は、ついで水、イソプロピルアルコー
ル、あるいはこれらの混合溶媒で洗浄する。洗浄は等量
以上の溶媒を用い20〜40℃にて行う。
Recrystallization with these lower alcohols
For example, a solvent is added to the crude lactide in an amount of 1 to 4 times (weight ratio) up to about 60 to 70 ° C. to dissolve all the crystals, and then cooled to 30 ° C. or less to obtain crystals. The obtained lactide crystal is then washed with water, isopropyl alcohol, or a mixed solvent thereof. Washing is performed at 20 to 40 ° C. using an equal amount or more of solvent.

【0007】さらにラクチドの結晶をベンゼンまたはア
ルキル置換基ベンゼンを再結晶溶媒として再結晶する。
このような溶媒としては、ベンゼン、トルエン、キシレ
ン、エチルベンゼン、イソプロピルベンゼンなどが挙げ
られるが、特にトルエンが好ましい。これら芳香族系の
溶媒を用いた再結晶は前記低級アルコールによる再結晶
と同様に行う。すなわち、粗ラクチドに対して1〜4倍
(重量比)以上の溶媒を用いて、室温から60〜70℃
程度まで昇温して結晶を全て溶解させた後、30℃以下
まで冷却して結晶を得る。ついで、得られたラクチドの
結晶を前記芳香族系溶媒の1種又は2種以上で洗浄す
る。洗浄は等量以上の溶媒を用い20〜40℃にて行
う。
Further, the lactide crystal is recrystallized using benzene or an alkyl-substituted benzene as a recrystallization solvent.
Examples of such a solvent include benzene, toluene, xylene, ethylbenzene and isopropylbenzene, with toluene being particularly preferred. Recrystallization using these aromatic solvents is performed in the same manner as the recrystallization using the lower alcohol. That is, using 1 to 4 times (weight ratio) or more solvent to the crude lactide, from room temperature to 60 to 70 ° C.
After raising the temperature to a certain degree to dissolve all the crystals, the crystals are obtained by cooling to 30 ° C. or lower. Then, the obtained lactide crystals are washed with one or more of the aromatic solvents. Washing is performed at 20 to 40 ° C. using an equal amount or more of solvent.

【0008】このようにして得られたラクチドはイソプ
ロピルアルコールの濃度が非常に低く、検出限界以下で
ある。
The lactide thus obtained has a very low concentration of isopropyl alcohol, which is below the detection limit.

【0009】本発明の精製法にて得られたラクチドは従
来と同様にして重合することができる。例えばベント付
き二軸混練押出機などの撹拌および送り機能を有する装
置を用い、撹拌、混合、移動、脱気を行いつつ反応させ
た後、連続的にポリマーを取り出す。重合触媒としては
錫末、ハロゲン化錫または炭素数20以下のカルボン酸
から誘導された有機錫化合物、あるいは亜鉛末、ハロゲ
ン化亜鉛または炭素数20以下のカルボン酸から誘導さ
れた有機亜鉛化合物が用いられ、特にオクチル酸錫が好
ましい。触媒の使用量はラクチドに対して0.1〜1.0
重量%程度であり、温度130〜230℃、好ましくは
160〜200℃にて混練機に連続的に供給しながら重
合を行う。
The lactide obtained by the purification method of the present invention can be polymerized in a conventional manner. For example, using a device having a stirring and feeding function such as a twin-screw kneading extruder with a vent, the reaction is carried out while stirring, mixing, moving and degassing, and then the polymer is continuously taken out. As the polymerization catalyst, tin powder, tin halide or an organotin compound derived from a carboxylic acid having 20 or less carbon atoms, or zinc powder, zinc halide or an organozinc compound derived from a carboxylic acid having 20 or less carbon atoms is used. However, tin octylate is particularly preferable. The amount of catalyst used is 0.1 to 1.0 with respect to lactide.
Polymerization is carried out at a temperature of 130 to 230 ° C., preferably 160 to 200 ° C. while continuously supplying to the kneader.

【0010】このようにして得られたポリ乳酸は分子量
が10万以上と極めて分子量が高い。すなわち、従来の
精製法によるラクチドには残留イソプロピルアルコール
があり、これが重合反応を阻害していると推定される。
これに対して、本発明にて得られたラクチドは残留イソ
プロピルアルコールが少なく重合が容易と考えられる。
The polylactic acid thus obtained has a very high molecular weight of 100,000 or more. That is, it is presumed that lactide produced by the conventional purification method has residual isopropyl alcohol, which inhibits the polymerization reaction.
On the other hand, the lactide obtained in the present invention has less residual isopropyl alcohol and is considered to be easily polymerized.

【0011】[0011]

【実施例】つぎに本発明を実施例にもとづきさらに具体
的に説明する。
EXAMPLES Next, the present invention will be described more specifically based on examples.

【0012】[実施例1]未精製のラクチド3kgに対
し、イソプロピルアルコール3kgを加え、70℃まで
加熱してラクチドを完全に溶解した。ついで、この溶液
を30℃まで冷却し、結晶を析出させて濾過した。さら
に約10kgの水および3kgのイソプロピルアルコー
ルを用いて洗浄を行った。
Example 1 To 3 kg of unpurified lactide, 3 kg of isopropyl alcohol was added and heated to 70 ° C. to completely dissolve the lactide. Then, the solution was cooled to 30 ° C., and crystals were precipitated and filtered. Further, cleaning was performed using about 10 kg of water and 3 kg of isopropyl alcohol.

【0013】このようにして得られたラクチドをさらに
精製した。すなわち、トルエン約3.5kgを加え、7
0℃まで加熱してラクチドを完全に溶解した。ついで、
このトルエン溶液を30℃まで冷却し、結晶を析出させ
濾過した。さらに約6kgのトルエンで洗浄した。得ら
れたラクチドの結晶を減圧下にて乾燥した(収量約1.9
kg)。
The lactide thus obtained was further purified. That is, add about 3.5 kg of toluene, and add 7
The lactide was completely dissolved by heating to 0 ° C. Then,
This toluene solution was cooled to 30 ° C., crystals were deposited and filtered. Further, it was washed with about 6 kg of toluene. The obtained lactide crystals were dried under reduced pressure (yield about 1.9).
kg).

【0014】得られたラクチドに、オクチル酸錫を0.
24%加え、190℃で混練機で連続的に重合したとこ
ろ、重量平均分子量15万のポリ乳酸が得られた。
To the obtained lactide, tin octylate was added in an amount of 0.1.
When 24% was added and the mixture was continuously polymerized at 190 ° C. with a kneader, polylactic acid having a weight average molecular weight of 150,000 was obtained.

【0015】[実施例2]未精製のラクチド1.9kg
に対し、イソプロピルアルコール2.8kgを加え、7
0℃まで加熱してラクチドを完全に溶解した。ついで、
この溶液を30℃まで冷却し、結晶を析出させて濾過し
た。さらに約8.4kgのイソプロピルアルコールを用
いて洗浄を行った。
Example 2 1.9 kg of unpurified lactide
2.8kg of isopropyl alcohol was added to
The lactide was completely dissolved by heating to 0 ° C. Then,
The solution was cooled to 30 ° C., crystals were deposited and filtered. Further, cleaning was performed using about 8.4 kg of isopropyl alcohol.

【0016】このようにして得られたラクチドをさらに
精製した。すなわち、トルエン2.8kgを加え、70
℃まで加熱してラクチドを完全に溶解した。ついで、こ
のトルエン溶液を30℃まで冷却し、結晶を析出させ濾
過した。さらに約5.6kgのトルエンで洗浄した。得
られたラクチドの結晶を減圧下にて乾燥した(収量約0.
95kg)。
The lactide thus obtained was further purified. That is, add 2.8 kg of toluene, and add 70
The lactide was completely dissolved by heating to ℃. Then, this toluene solution was cooled to 30 ° C., crystals were deposited and filtered. It was further washed with about 5.6 kg of toluene. The crystals of lactide obtained were dried under reduced pressure (yield approx.
95 kg).

【0017】得られたラクチドに、オクチル酸錫を0.
24%加え、190℃で混練機で連続的に重合したとこ
ろ、重量平均分子量15万のポリ乳酸が得られた。
To the obtained lactide, tin octylate was added in an amount of 0.1.
When 24% was added and the mixture was continuously polymerized at 190 ° C. with a kneader, polylactic acid having a weight average molecular weight of 150,000 was obtained.

【0018】[比較例1]未精製のラクチド1.0kg
に対し、イソプロピルアルコール1.0kgを加え、7
0℃まで加熱してラクチドを完全に溶解した。ついで、
この溶液を30℃まで冷却し、結晶を析出させて濾過し
た。さらに約9.0kgの水、1.0kgのイソプロピル
アルコールを用いて洗浄を行った。同様の操作をさらに
2回、計3回行い、得られたラクチドの結晶を減圧下に
て乾燥した(収量約0.52kg)。得られたラクチド
に、オクチル酸錫を0.24%加え、190℃で混練機
で連続的に重合したところ、重合はほとんど進まなかっ
た。
Comparative Example 1 1.0 kg of unpurified lactide
To 1.0 isopropyl alcohol, add 7
The lactide was completely dissolved by heating to 0 ° C. Then,
The solution was cooled to 30 ° C., crystals were deposited and filtered. Further, cleaning was performed using about 9.0 kg of water and 1.0 kg of isopropyl alcohol. The same operation was further repeated twice, a total of three times, and the obtained lactide crystals were dried under reduced pressure (yield about 0.52 kg). When 0.24% of tin octylate was added to the obtained lactide and the mixture was continuously polymerized at 190 ° C. with a kneader, the polymerization hardly proceeded.

【0019】[0019]

【発明の効果】本発明の精製法にて得られたラクチドは
純度が高く、重合が進みやすいため、分子量の非常に大
きなポリ乳酸が容易に得られる。
EFFECTS OF THE INVENTION The lactide obtained by the purification method of the present invention has a high purity and is apt to undergo polymerization, so that polylactic acid having a very large molecular weight can be easily obtained.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ラクチドを低級アルコールにて再結晶
し、ついでベンゼンまたはアルキル置換基ベンゼンにて
再結晶することを特徴とするラクチドの精製法。
1. A method for purifying lactide, which comprises recrystallizing lactide with a lower alcohol and then recrystallizing with benzene or an alkyl-substituted benzene.
【請求項2】 ラクチドを低級アルコールにて再結晶
し、ついでベンゼンまたはアルキル置換基ベンゼンにて
再結晶し、得られたラクチドを重合することを特徴とす
るラクチドの重合法。
2. A method for polymerizing lactide, which comprises recrystallizing lactide with a lower alcohol and then recrystallizing with benzene or an alkyl-substituted benzene to polymerize the obtained lactide.
JP5291296A 1993-10-26 1993-10-26 Lactide purification and polymerization Expired - Fee Related JP2809069B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5291296A JP2809069B2 (en) 1993-10-26 1993-10-26 Lactide purification and polymerization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5291296A JP2809069B2 (en) 1993-10-26 1993-10-26 Lactide purification and polymerization

Publications (2)

Publication Number Publication Date
JPH07118259A true JPH07118259A (en) 1995-05-09
JP2809069B2 JP2809069B2 (en) 1998-10-08

Family

ID=17767055

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5291296A Expired - Fee Related JP2809069B2 (en) 1993-10-26 1993-10-26 Lactide purification and polymerization

Country Status (1)

Country Link
JP (1) JP2809069B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000018756A1 (en) * 1998-09-25 2000-04-06 Shimadzu Corporation Process for purifying lactide and lactide used as food additive
US6313319B1 (en) 1998-09-25 2001-11-06 Shimadzu Corporation Method for purifying lactide and lactide for food additives
CN100343247C (en) * 2005-10-17 2007-10-17 南京工业大学 Method for recrystallizing lactide by using ethanol
JP2007538132A (en) * 2004-05-20 2007-12-27 リライアンス ライフ サイエンシーズ ピーヴィーティー エルティーディー Process for the production of polylactic acid (PLA) from renewable feedstock
JP2011074084A (en) * 1999-03-22 2011-04-14 Purac Biochem Bv Method of industrial-scale purification of lactic acid
JP2013536285A (en) * 2010-08-20 2013-09-19 コンパニア レフィナドラ ダ アマゾニア Method for producing polylactic acid and reactor used in the method
RU2699801C1 (en) * 2018-11-20 2019-09-11 Федеральное государственное автономное образовательное учреждение высшего образования "Национальный исследовательский Томский государственный университет" (ТГУ, НИ ТГУ) Lactide purification method
CN113292531A (en) * 2021-05-20 2021-08-24 重庆大学 Method for purifying mixed lactide of meso-lactide and D, L-lactide

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06279435A (en) * 1993-03-31 1994-10-04 Dainippon Ink & Chem Inc Purification of lactide

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06279435A (en) * 1993-03-31 1994-10-04 Dainippon Ink & Chem Inc Purification of lactide

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000018756A1 (en) * 1998-09-25 2000-04-06 Shimadzu Corporation Process for purifying lactide and lactide used as food additive
EP1048665A1 (en) * 1998-09-25 2000-11-02 Shimadzu Corporation Method for purifying lactide and lactide for food additives
US6313319B1 (en) 1998-09-25 2001-11-06 Shimadzu Corporation Method for purifying lactide and lactide for food additives
EP1048665A4 (en) * 1998-09-25 2002-11-20 Shimadzu Corp Method for purifying lactide and lactide for food additives
JP2011074084A (en) * 1999-03-22 2011-04-14 Purac Biochem Bv Method of industrial-scale purification of lactic acid
JP2007538132A (en) * 2004-05-20 2007-12-27 リライアンス ライフ サイエンシーズ ピーヴィーティー エルティーディー Process for the production of polylactic acid (PLA) from renewable feedstock
JP2011103903A (en) * 2004-05-20 2011-06-02 Reliance Life Sciences Pvt Ltd Process for production of polylactic acid (pla) from renewable feedstocks
CN100343247C (en) * 2005-10-17 2007-10-17 南京工业大学 Method for recrystallizing lactide by using ethanol
JP2013536285A (en) * 2010-08-20 2013-09-19 コンパニア レフィナドラ ダ アマゾニア Method for producing polylactic acid and reactor used in the method
RU2699801C1 (en) * 2018-11-20 2019-09-11 Федеральное государственное автономное образовательное учреждение высшего образования "Национальный исследовательский Томский государственный университет" (ТГУ, НИ ТГУ) Lactide purification method
CN113292531A (en) * 2021-05-20 2021-08-24 重庆大学 Method for purifying mixed lactide of meso-lactide and D, L-lactide
CN113292531B (en) * 2021-05-20 2023-09-26 重庆大学 Purification method of mixed lactide of meso-lactide and D, L-lactide

Also Published As

Publication number Publication date
JP2809069B2 (en) 1998-10-08

Similar Documents

Publication Publication Date Title
JP2809069B2 (en) Lactide purification and polymerization
US4316004A (en) Process for producing oxybenzoyl copolyesters
JP3988195B2 (en) Lactide purification and polymerization
JP2959375B2 (en) Lactide purification and polymerization
JPS62225558A (en) Solid high-molecular stabilizer compound and its production
JPH0539267A (en) Flame retardant composition containing halogenated imide
JP2009019123A (en) 6-position-highly acetylated cellulose acetate and method for producing the same
JPH10279577A (en) Lactide for food additive and purification of lactide
JP4698421B2 (en) Process for producing 2,3,6,7,10,11-hexahydroxytriphenylene
JP3625504B2 (en) High purity biphenyltetracarboxylic dianhydride and process for producing the same
EP0508147B1 (en) Process for producing carboxylic acid chloride
WO2008060107A1 (en) Method for purifying terephthalaldehyde
US4720570A (en) Rate of crystallizing diphenylisophthalate/diphenylterephthalate monomer
KR20160052437A (en) Production method of poly(alkylene carbonate) particles
WO2001040178A1 (en) Process for the preparation of a carboxylic acid derivative
JPH0825943B2 (en) Method for producing high melting point dibromopropyl ether compound
JPH08302061A (en) Recovery of aromatic dicarboxylic acid from waste aromatic polyester
JPH06321836A (en) Method for purifying 9,9-bis(4-hydroxyphenyl)fluorene
JPH06256262A (en) Purification of 2,6-naphthalene dicarboxylic acid dimethyl ester
JP2010185049A (en) Method for producing polylactic acid block copolymer
KR940005323B1 (en) Process for preparing glycolide
US3670003A (en) Preparation of phenylene diisocyanate by thermal decomposition of corresponding dinitrile sulfite
JPH06279435A (en) Purification of lactide
JPS61251644A (en) Production of high-purity aromatic diamine
JPS6395231A (en) Separation and recovery of aromatic polyether polymer

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20080731

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20080731

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 11

Free format text: PAYMENT UNTIL: 20090731

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090731

Year of fee payment: 11

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 12

Free format text: PAYMENT UNTIL: 20100731

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 13

Free format text: PAYMENT UNTIL: 20110731

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110731

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120731

Year of fee payment: 14

LAPS Cancellation because of no payment of annual fees