JPH0747663B2 - Foam pellets of chlorinated polyolefin - Google Patents
Foam pellets of chlorinated polyolefinInfo
- Publication number
- JPH0747663B2 JPH0747663B2 JP1205017A JP20501789A JPH0747663B2 JP H0747663 B2 JPH0747663 B2 JP H0747663B2 JP 1205017 A JP1205017 A JP 1205017A JP 20501789 A JP20501789 A JP 20501789A JP H0747663 B2 JPH0747663 B2 JP H0747663B2
- Authority
- JP
- Japan
- Prior art keywords
- solvent
- chlorinated polyolefin
- production
- foamed
- chlorinated
- 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 - Fee Related
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はトルエン、キシレン単独又はトルエン又はキシ
レンと他の有機溶剤(これらを前記したように使用溶剤
と略称する。)に溶解して使用に供するための原料とな
る、発泡剤を含有するか又は含有しない塩素化ポリオレ
フインの発泡ペレツトに関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention can be used by dissolving toluene, xylene alone, or toluene or xylene and another organic solvent (these are abbreviated as a use solvent as described above). The present invention relates to a foamed pellet of chlorinated polyolefin containing or not containing a foaming agent, which is a raw material to be supplied.
従来塩素化ポリオレフインは接着性が強大であるため、
通常ペレツト状にしてトルエン、キシレン等の芳香族炭
化水素溶剤単独又はケトン類、エステル類等の他の有機
溶剤との混合溶剤(以下単に混合溶剤という。)に溶解
して接着剤用、インキ用、塗料用、コーテイング用、ポ
リプロピレン成型品等のプライマー用としての用途に広
く使用されている。Conventional chlorinated polyolefin has strong adhesiveness,
It is usually made into pellets and dissolved in an aromatic hydrocarbon solvent such as toluene or xylene alone or in a mixed solvent with other organic solvents such as ketones and esters (hereinafter simply referred to as mixed solvent) for adhesives and inks. It is widely used for paints, coatings, and as a primer for polypropylene moldings.
塩素化ポリオレフインのペレツトを撹拌機付溶解槽を使
用して使用溶剤例えばトルエン、キシレン又はその他混
合溶剤に溶解する場合、従来の塩素化ポリオレフインペ
レツトは溶解槽に沈澱し、表面のみが溶剤によつて部分
的に溶解されてポリオレフインペレツト同志が互に結合
し合つて柔かい餅状となり、溶解槽下部に粘着し、撹拌
機の効果が発揮されず、溶解に長時間と著しい動力を必
要とし、尚かつ均一に溶解せしめることが困難な問題点
があつた。When the chlorinated polyolefin pellets are dissolved in the solvent used, for example, toluene, xylene or other mixed solvent using a dissolution tank equipped with a stirrer, the conventional chlorinated polyolefin pellets are precipitated in the dissolution tank and only the surface is dissolved by the solvent. Then, the polyolefin pellets were partially dissolved and bonded together to form a soft rice cake-like, sticking to the bottom of the dissolution tank, the effect of the stirrer was not exerted, and it took a long time and significant power to dissolve, In addition, there was a problem that it was difficult to dissolve it uniformly.
これらの問題点を解決するために、本発明者等は塩素化
ポリオレフインペレツトを使用溶剤に溶解する場合、溶
解槽中で沈澱せず、浮遊して撹拌によつて容易に溶解す
るような塩素化ポリオレフインの発泡ペレツトを製造
し、使用することによつて該発泡ペレツトを使用溶剤中
に浮遊せしめることができて、撹拌がスムースになり、
該発泡ペレツトを容易に溶剤に溶解せしめ得ることを確
認して本発明を完成するに至つたもので、本発明は使用
溶剤に溶解して使用するために、溶解時、それらの使用
溶剤に浮遊する塩素化ポリオレフインの発泡ペレツトを
提供することを目的とするものである。In order to solve these problems, the present inventors have found that when chlorinated polyolefin pellets are dissolved in a solvent used, they do not precipitate in a dissolution tank and are floated so that they are easily dissolved by stirring. By producing a foamed pellet of modified polyolefin and by using it, the foamed pellet can be suspended in the solvent used, and the stirring becomes smooth,
The present invention has been completed by confirming that the foamed pellets can be easily dissolved in a solvent, and the present invention is to be dissolved in a solvent to be used. It is an object of the present invention to provide a foamed pellet of chlorinated polyolefin.
本発明は溶液状塩素化ポリオレフインからその製造時に
使用された溶剤即ち上記の製造溶剤例えば四塩化炭素溶
剤等を離脱せしめた固形の塩素化ポリオレフインに不活
性ガス、炭酸ガス又は空気を圧入するか、又は固体状塩
素化ポリオレフインに残留した製造溶剤を減圧下で加熱
して離脱せしめて発泡せしめるか、又は製造された塩素
化ポリオレフインに使用溶剤及び/又は製造溶剤を添加
して減圧下で加熱して離脱せしめて発泡せしめた塩素化
ポリオレフインの発泡ペレツトに関するものである。The present invention is to inject an inert gas, carbon dioxide gas or air into a solid chlorinated polyolefin obtained by removing the solvent used in the production thereof from a solution chlorinated polyolefin, that is, the above-mentioned production solvent such as a carbon tetrachloride solvent. Alternatively, the production solvent remaining in the solid chlorinated polyolefin is heated under reduced pressure to separate and foam, or the production solvent and / or the production solvent is added to the produced chlorinated polyolefin and heated under reduced pressure. The present invention relates to a foamed pellet of chlorinated polyolefin which is released and foamed.
本発明の不活性ガス、炭酸ガス又は空気を圧入するか、
又は固体状塩素化ポリオレフインに残留した製造溶剤を
減圧下で加熱して離脱せしめて発泡せしめるか、又は製
造された塩素化ポリオレフインに使用溶剤及び/又は製
造溶剤を添加して減圧下で加熱して離脱せしめて発泡せ
しめた塩素化ポリオレフインの発泡ペレツトは使用溶剤
に浮遊する程度の見掛けの比重(本発明では残留ガス、
製造溶剤及び/又は使用溶剤を部分的に含有する発泡ペ
レツトの比重を見掛けの比重と定義する。)を有し、使
用溶剤に溶解時、溶解槽中で、使用溶剤中に浮遊するが
故に容易に溶解槽の撹拌機によつて撹拌溶解される。Injecting an inert gas, carbon dioxide gas or air of the present invention,
Alternatively, the production solvent remaining in the solid chlorinated polyolefin is heated under reduced pressure to separate and foam, or the production solvent and / or the production solvent is added to the produced chlorinated polyolefin and heated under reduced pressure. The foamed pellet of chlorinated polyolefin that has been separated and foamed has an apparent specific gravity (residual gas in the present invention, such that it floats in the solvent used,
The specific gravity of the foamed pellet partially containing the production solvent and / or the used solvent is defined as the apparent specific gravity. ) And is dissolved in the solvent used, it is easily stirred and dissolved by the stirrer in the dissolution tank because it floats in the solvent used.
本発明の塩素化ポリオレフインとしては通常塩素化ポリ
エチレン、塩素化ポリプロピレンが使用されるが、これ
らのみに限定されるものではない。As the chlorinated polyolefin of the present invention, chlorinated polyethylene and chlorinated polypropylene are usually used, but the chlorinated polyolefin is not limited thereto.
また塩素化ポリオレフインの発泡ペレツトの使用溶剤と
しての主なるものを、比重とともに第1表に示した。比
重は20℃において測定した値で示した。Table 1 shows the main solvents used as the solvent for the foamed pellets of chlorinated polyolefin together with the specific gravity. The specific gravity is indicated by the value measured at 20 ° C.
第一表の溶剤のうち前記したようにトルエン、キシレン
は単独で使用されるが、その他の溶剤はトルエン又はキ
シレンと混合して混合溶剤として使用される。 Of the solvents in Table 1, toluene and xylene are used alone as described above, but other solvents are used as a mixed solvent by mixing with toluene or xylene.
塩素化ポリプロピレンの発泡ペレツトが使用溶剤に溶解
する場合については、塩素化ポリプロピレンの発泡ペレ
ツトの前記した見掛けの比重と溶剤の真比重とに関係が
ある。When the foamed pellet of chlorinated polypropylene is dissolved in the solvent used, there is a relationship between the apparent specific gravity of the foamed pellet of chlorinated polypropylene and the true specific gravity of the solvent.
塩素化ポリプロピレンの真比重は塩素含有量、塩素化ポ
リプロピレンに残存する製造溶剤の量によつて異るが1.
08〜1.17程度であり、平均は1.1程度である。The true specific gravity of chlorinated polypropylene depends on the chlorine content and the amount of manufacturing solvent remaining in the chlorinated polypropylene, but 1.
It is about 08 to 1.17, and the average is about 1.1.
上記塩素化ポリプロピレンの発泡ペレツトを使用溶剤中
に浮遊しめるためには、下記に記載するように容積膨脹
率程度未満にする必要があり、上記ガス類、製造溶剤及
び/又は使用溶剤を部分的に残存した塩素化ポリプロピ
レンの発泡ペレツトの見掛けの比重を少くとも使用溶剤
の真比重未満にまで低下せしめる必要がある。In order to float the chlorinated polypropylene foam pellets in the solvent used, it is necessary to make the volume expansion coefficient less than approximately as described below, and the gas, the production solvent and / or the used solvent are partially contained. It is necessary to reduce the apparent specific gravity of the residual chlorinated polypropylene foam pellets to at least less than the true specific gravity of the solvent used.
例えば第一表の使用溶剤であるトルエンに塩素化ポリプ
ロピレンの発泡ペレツトが浮遊するためには となり発泡率は26.9%以上が必要である。For example, in order for the chlorinated polypropylene foam pellets to float in toluene, which is the solvent used in Table 1, Therefore, the foaming rate must be 26.9% or more.
同様にしてキシレン溶剤に浮遊するためには となり、発泡率は27.9%以上が必要である。Similarly, to float in xylene solvent, Therefore, the foaming rate must be 27.9% or more.
その他の混合溶剤についても、トルエン又はキシレンと
他の有機溶剤との混合割合によつて異るが、それぞれの
比重が混合割合によつて定まるが故に上記トルエン、キ
シレンの場合と同様に塩素化ポリプロピレンの発泡ペレ
ツトを浮遊せしめる発泡率が決定される。Other mixed solvents also differ depending on the mixing ratio of toluene or xylene and other organic solvent, but since the specific gravity of each is determined by the mixing ratio, the same chlorinated polypropylene as in the case of toluene and xylene. The rate of foaming that causes the foam pellets to be suspended is determined.
即ち窒素ガス、炭酸ガス、空気又は製造溶剤及び/又は
使用溶剤を残存した塩素化ポリプロピレンの発泡ペレツ
トをトルエン、キシレン、混合溶剤等の使用溶剤に浮遊
させるためには少くとも上記の発泡率以上にする必要が
ある。That is, in order to suspend the foaming pellets of chlorinated polypropylene in which nitrogen gas, carbon dioxide gas, air or the manufacturing solvent and / or the used solvent remain in the used solvent such as toluene, xylene and mixed solvent, at least the above foaming ratio or more is required. There is a need to.
固形の塩素化ポリプロピレンを加熱して圧入される場合
に使用される不活性ガスとしては、主として窒素ガスが
使用される。また窒素ガスの代りに炭酸ガス又は炭酸ガ
スを発生する物質も使用可能である。Nitrogen gas is mainly used as the inert gas used when the solid chlorinated polypropylene is heated and press-fitted. Instead of nitrogen gas, carbon dioxide gas or a substance that generates carbon dioxide gas can also be used.
次に図面によつて本発明を説明する。 The present invention will now be described with reference to the drawings.
第1図は上部に開口を有する溶液状塩素化ポリプロピレ
ンから四塩化炭素溶剤を高温減圧下で離脱せしめ、つい
で窒素ガスを高温で圧入して塩素化ポリプロピレンの発
泡ペレツトを製造するシリンダー型押出装置の概略断面
図を示すもので、第1図の装置を使用して塩素化ポリプ
ロピレンの四塩化炭素溶液から、加熱減圧下で四塩化炭
素を離脱せしめ、ついで加圧下、窒素ガスを圧入し、最
終的に切断して塩素化ポリプロピレンの発泡ペレツトが
得られる。測定結果を第2表に示した。第2表の条件で
測定した結果、塩素化ポリプロピレンの発泡ペレツトの
窒素含有量はNo.2,4が34.02%、No.3が33.03%、No.7が
38.15%であつた。第2表中◎は該発泡ペレツトがトル
エン溶剤に浮く場合、△は浮いたり、沈んだりする場
合、×はNo.1のブランクテストの結果で沈む場合であ
る。FIG. 1 shows a cylinder type extruder for producing a foamed pellet of chlorinated polypropylene by releasing a carbon tetrachloride solvent from a solution chlorinated polypropylene having an opening at the top under a high temperature and reduced pressure and then injecting nitrogen gas at a high temperature. A schematic cross-sectional view is shown, in which carbon tetrachloride is released from the carbon tetrachloride solution of chlorinated polypropylene under heating and reduced pressure by using the apparatus shown in FIG. A chlorinated polypropylene foam pellet is obtained by cutting into pieces. The measurement results are shown in Table 2. As a result of measurement under the conditions shown in Table 2, the nitrogen content of the foamed pellets of chlorinated polypropylene was 34.02% for No.2,4, 33.03% for No.3 and No.7.
It was 38.15%. In Table 2, ⊚ indicates that the foam pellet floats in the toluene solvent, Δ indicates that it floats or sinks, and x indicates that it sinks as a result of the No. 1 blank test.
第2図は本発明の窒素ガス含有塩素化ポリプロピレンの
発泡ペレツトと従来の塩素化ポリプロピレンペレツト及
び後記の空気含有該発泡ペレツトのトルエン溶剤に溶解
する場合の種々な溶解温度における溶解温度と溶解時間
との関係を示した。溶解温度が常用の30℃程度では溶解
時間に著しい差のあることがわかる。 FIG. 2 shows the melting temperature and the melting time at various melting temperatures when the foamed pellets of the nitrogen gas-containing chlorinated polypropylene of the present invention, the conventional chlorinated polypropylene pellets and the air-containing foamed pellets described below are dissolved in a toluene solvent. The relationship with It can be seen that there is a marked difference in the dissolution time when the dissolution temperature is around 30 ° C, which is the usual condition.
更に空気混入塩素化ポリプロピレンの発泡ペレツトの場
合は、製造溶剤である四塩化炭素に溶解した塩素化ポリ
プロピレン溶液をドラムドライヤ方式で四塩化炭素を吸
引して回収しながら乾燥し、溶剤を離脱せしめてテープ
状に集束して空気を含有せしめ、発泡ペレツトを製造す
ることが可能である。Furthermore, in the case of foamed pellets of aerated chlorinated polypropylene, the chlorinated polypropylene solution dissolved in carbon tetrachloride, which is the manufacturing solvent, is dried by sucking carbon tetrachloride with a drum dryer and collecting it to remove the solvent. It is possible to produce a foamed pellet by bundling it into a tape and allowing it to contain air.
この場合の発泡ペレツトの空気含有量の一例は42.66%
であつた。そのため使用溶剤として使用されるトルエン
に浮遊する発泡ペレツトが製造され、第2図(6),
(6)′の曲線で示すような優秀な溶解性を示すことが
わかる。An example of the air content of foam pellets in this case is 42.66%
It was. Therefore, foamed pellets floating in toluene, which is used as a solvent, are produced, as shown in Fig. 2 (6),
It can be seen that it exhibits excellent solubility as shown by the curve (6) '.
更に第1図のシリンダー型押出装置を使用する場合又は
ドラムドライヤー方式を使用する場合にしても、塩素化
ポリプロピレン溶液から四塩化炭素を離脱せしめる場
合、四塩化炭素を残存せしめるか、又は四塩化炭素の残
存した固体状塩素化ポリプロピレンに使用溶剤例えばト
ルエンを添加して加圧下で塩素化ポリプロピレンに含有
せしめた後、脱溶剤することによつて前記と同様にして
塩素化ポリプロピレンの発泡ペレツトを製造することが
可能である。Further, even when the cylinder type extruder shown in FIG. 1 is used or the drum dryer method is used, when carbon tetrachloride is released from the chlorinated polypropylene solution, carbon tetrachloride is left behind or carbon tetrachloride is left. A solvent such as toluene is added to the remaining solid chlorinated polypropylene to make it contained in the chlorinated polypropylene under pressure, and then the solvent is removed to produce a foamed pellet of chlorinated polypropylene in the same manner as described above. It is possible.
本発明の発泡ペレツトは上記実施例のみによる製造に限
定されるものではない。The foam pellets of the present invention are not limited to the production according to the above embodiment alone.
第2図に示したように本発明によつて製造された不活性
ガス、炭酸ガス又は空気を包含したポリプロピレンの発
泡ペレツトはトルエン、キシレンその他の混合溶剤等の
使用溶剤に浮遊し、従来の塩素化ポリオレフイン粒子よ
りも30〜40℃における溶解時間が著しく早く、しかも低
温になるに従つて溶解時間の差が大となる。これに反し
て通常の塩素化ポリオレフインは溶解に著しく長時間を
要し、それだけ動力を必要とすることになる。As shown in FIG. 2, a polypropylene foam pellet containing inert gas, carbon dioxide gas or air produced according to the present invention floats in a solvent such as toluene, xylene or other mixed solvent, and the conventional chlorine The dissolution time at 30-40 ° C is significantly faster than that of the modified polyolefin particles, and the difference in the dissolution time becomes larger as the temperature becomes lower. In contrast, conventional chlorinated polyolefins take a significantly longer time to dissolve and thus require more power.
更に本発明の塩素化ポリオレフインの発泡ペレツトは塩
素化ポリオレフインの製造時に使用される溶解例えば四
塩化炭素を離脱せしめて固形の塩素化ポリオレフインの
製造工程に連結して不活性ガス、炭酸ガス、空気更には
製造溶剤の四塩化炭素及び/又は使用溶剤のトルエンを
添加して加熱減圧下でそれらの溶剤を離脱せしめ、ある
いは部分的に包含せしめて本発明の目的が達成される利
点がある。Further, the foamed pellets of chlorinated polyolefin of the present invention are used in the production of chlorinated polyolefin, for example, by dissolving carbon tetrachloride to remove the solid chlorinated polyolefin, and the solid chlorinated polyolefin is linked to the production process to prepare an inert gas, carbon dioxide gas, air and Has the advantage that the object of the present invention can be achieved by adding carbon tetrachloride as a production solvent and / or toluene as a solvent to be used to remove these solvents under heating and reduced pressure, or partially including them.
第1図は本発明の四塩化炭素溶液に溶解した塩素化ポリ
オレフインを固形化し、かつ不活性ガスを圧入し、切断
して塩素化ポリオレフインの発泡ペレツトを製造する押
出型製造装置の概略断面図、第2図は本発明の塩素化ポ
リオレフインの発泡ペレツトのトルエン溶剤への溶解時
間と溶解温度との関係を示す図である。 1.塩素化ポリピロピレン四塩化炭素溶液の投入口 2.真空吸引口 3.窒素ボンベ 4.ストランドカツター装置 5.窒素ガス含有塩素化ポリプロピレン発泡ペレツトのト
ルエン溶剤への溶解時間、温度曲線 6,6′.空気含有塩素化ポリプロピレン発泡ペレツトの
同上溶解時間、温度曲線 7.従来の塩素化ポリプロピレンの同上溶解時間、温度曲
線FIG. 1 is a schematic cross-sectional view of an extrusion-type manufacturing apparatus for solidifying a chlorinated polyolefin dissolved in a carbon tetrachloride solution of the present invention, and injecting an inert gas under pressure to cut the chlorinated polyolefin to produce a foamed pellet of chlorinated polyolefin. FIG. 2 is a diagram showing the relationship between the dissolution time and the dissolution temperature of the chlorinated polyolefin of the present invention in the foamed pellet of toluene. 1. Charging port for chlorinated polypyrrolene carbon tetrachloride solution 2. Vacuum suction port 3. Nitrogen cylinder 4. Strand cutter device 5. Dissolution time of chlorinated polypropylene foam pellets containing nitrogen gas in toluene solvent, temperature curve 6,6 ′. Dissolving time and temperature curve of chlorinated polypropylene foam pellets containing air 7. Dissolving time and temperature curve of conventional chlorinated polypropylene
Claims (2)
時に使用された溶剤(以下製造溶剤という。)を離脱せ
しめた固体状塩素化ポリオレフインに不活性ガス、炭酸
ガス又は空気を圧入又は含有せしめるか、又は固体状塩
素化ポリオレフインに残留した製造溶剤を減圧下で加熱
して離脱し、発泡せしめるか、又は製造された塩素化ポ
リオレフインに使用時の可溶性溶剤(以下使用溶剤とい
う。)及び/又は製造溶剤を添加して減圧下で加熱して
離脱し、発泡せしめてなる塩素化ポリオレフインの発泡
ペレツト。1. A solid chlorinated polyolefin obtained by releasing a solvent (hereinafter referred to as a production solvent) used at the time of its production from a solution chlorinated polyolefin, by injecting or containing an inert gas, carbon dioxide gas or air, or Alternatively, the production solvent remaining in the solid chlorinated polyolefin is heated and released under reduced pressure to cause foaming, or the produced chlorinated polyolefin is a soluble solvent at the time of use (hereinafter referred to as a used solvent) and / or a production solvent. A foamed pellet of chlorinated polyolefin in which is added and heated under reduced pressure to release the foam.
炭酸ガス又は空気を圧入するか、又は固体状塩素化ポリ
オレフインに残留した製造溶剤を減圧下で加熱発泡せし
めるか、又は製造された塩素化ポリオレフインに使用溶
剤及び/又は製造溶剤を添加して減圧下で加熱して離脱
し、発泡せしめて製造された塩素化ポリオレフインの発
泡ペレツトの見掛けの比重を該塩素化ポリオレフインの
発泡ペレツトの使用溶剤の真比重未満にしてなる請求項
1記載の塩素化ポリオレフインの発泡ペレツト。2. Solid chlorinated polyolefin with nitrogen gas,
Carbon dioxide gas or air is injected under pressure, or the production solvent remaining in the solid chlorinated polyolefin is heated and foamed under reduced pressure, or the produced solvent is added to the produced chlorinated polyolefin and the production solvent is added under reduced pressure. 2. The chlorinated polyolefin of claim 1, wherein the apparent specific gravity of the foamed pellet of the chlorinated polyolefin produced by foaming is reduced to less than the true specific gravity of the solvent used for the foamed pellet of the chlorinated polyolefin. Foam pellets.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1205017A JPH0747663B2 (en) | 1989-08-07 | 1989-08-07 | Foam pellets of chlorinated polyolefin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1205017A JPH0747663B2 (en) | 1989-08-07 | 1989-08-07 | Foam pellets of chlorinated polyolefin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0368637A JPH0368637A (en) | 1991-03-25 |
| JPH0747663B2 true JPH0747663B2 (en) | 1995-05-24 |
Family
ID=16500065
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1205017A Expired - Fee Related JPH0747663B2 (en) | 1989-08-07 | 1989-08-07 | Foam pellets of chlorinated polyolefin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0747663B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6020388A (en) * | 1997-03-04 | 2000-02-01 | Tri-Technologies, Inc. | Methods for impregnating polymer beads |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6059322A (en) * | 1983-09-12 | 1985-04-05 | Seiko Epson Corp | Liquid-crystal display panel |
-
1989
- 1989-08-07 JP JP1205017A patent/JPH0747663B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0368637A (en) | 1991-03-25 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |