JPS58134856A - Vessel made of plastic - Google Patents
Vessel made of plasticInfo
- Publication number
- JPS58134856A JPS58134856A JP1088482A JP1088482A JPS58134856A JP S58134856 A JPS58134856 A JP S58134856A JP 1088482 A JP1088482 A JP 1088482A JP 1088482 A JP1088482 A JP 1088482A JP S58134856 A JPS58134856 A JP S58134856A
- Authority
- JP
- Japan
- Prior art keywords
- container
- treatment
- gasoline
- gas
- permeation
- 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
Links
Landscapes
- Details Of Rigid Or Semi-Rigid Containers (AREA)
- Treatments Of Macromolecular Shaped Articles (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明はプラスチック製容器に関する。、−更に詳しく
は特にアルコール混合炭化水素類の透過防止能に秀れた
プラスチック製容器に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to plastic containers. More specifically, the present invention relates to a plastic container that is particularly excellent in preventing permeation of alcohol-mixed hydrocarbons.
炭化水素類を保存する為の容器素材として種々のプラス
チックが多くの分野で利用されているが、容器の一例に
自動車のガソリンタンク(以下GTと略する)があり、
プラスチックとして、ポリエチレン、特に超高分子量の
高密度ポリエチレンが経済性、成形加工性、強度面で最
も期待されているが、保存されたガソリンの気体又は液
体がポリエチレン壁を通して大気中に飛散し、やすい即
ち透過防止能に於いて劣るという欠点を有することが知
られている。Various plastics are used as container materials for storing hydrocarbons in many fields, and one example of a container is an automobile gasoline tank (hereinafter abbreviated as GT).
As a plastic, polyethylene, especially ultra-high molecular weight high-density polyethylene, is the most promising in terms of economy, moldability, and strength, but stored gasoline gas or liquid easily scatters into the atmosphere through the polyethylene wall. That is, it is known to have a drawback of being inferior in permeation prevention ability.
そこでか\る欠点を解消する為、ポリエチレン、ポリプ
ロピレンからなる容器を三酸化イオウ(803)を約0
.1〜20容量チ含む乾燥不活性ガス、例えばN2、C
O2、SO2及び空気等で処理するか、或いは塩化メチ
レン、四塩化炭素のような液状多塩素化脂肪族炭化水素
中のS03の溶液等で処理後、ガス状アンモニア及びメ
チルアミンの様な気相中和剤或いは、アルカリ金属又は
アルカリ土類金属の水酸化物または対応する弱酸の塩等
により中和し洗滌乾燥する方法や、該容器を吹き込み成
形法にて成形する際、容積で約0.1〜20チの弗素と
共にSO2、C01CO2,02、O12友びBr2か
ら成る群よシ選ばれた1種以上の反応性ガスを吹き込み
気体として使用する事によシ容器内面を弗素化する方法
等が提案されている。In order to eliminate this drawback, we created containers made of polyethylene and polypropylene containing approximately 0 sulfur trioxide (803).
.. 1 to 20 volumes of dry inert gas, such as N2, C
After treatment with O2, SO2 and air, etc., or with a solution of S03 in a liquid polychlorinated aliphatic hydrocarbon such as methylene chloride, carbon tetrachloride, etc., the gaseous phase such as gaseous ammonia and methylamine is removed. When using a neutralizing agent, a hydroxide of an alkali metal or an alkaline earth metal, or a salt of a corresponding weak acid, washing and drying the container, or molding the container using a blow molding method, the volume is about 0. A method of fluorinating the inner surface of a container by blowing one or more reactive gases selected from the group consisting of SO2, CO1CO2,02, O12 friends and Br2 together with 1 to 20 fluorine, etc. is proposed.
一方、現在及び将来に於いて石油供給不足が懸念されて
おシ特にガソリン事情の先行きは深刻な問題が大きくク
ローズアップされ社会問題となつてきている。これに対
して、ガフ11ンの消費節約を担うべくアルコールをガ
ソリンに混入したいわゆるガスオール(Gasol)が
新しい燃料として登場し、既に石油不足に悩むブラジル
等では、政府指導の下で実用化されておシ、又つい最近
我が国に於いても通産省、資源エネルギー庁が、ガスオ
ールの実用化の検討を開始している。On the other hand, there are concerns about oil supply shortages now and in the future, and the future of the gasoline situation in particular is becoming a serious problem that has become a social issue. In response to this, so-called Gasol, which is a mixture of alcohol and gasoline, has appeared as a new fuel in order to reduce consumption, and in countries such as Brazil, which are already suffering from oil shortages, it has been put into practical use under government guidance. Also, just recently in Japan, the Ministry of International Trade and Industry and the Agency for Natural Resources and Energy have begun considering the practical application of Gas All.
既述の透過防止手段の中では、ポリエチレンの(以下P
Eと称する)の内面をSO3処理後NH3ガスで中和し
てなるGTが最も実用的でかつ既に米国等で一部実車搭
載されている。ところが゛本発明らが前記処理の容器に
ついてガソリン及びガスオールで種々の透過試験を行な
ったところ、ガソリン単体では確かに、未処理品に比べ
て透過量は1/10〜1/40と非常に秀れた透過防止
能を有する事が確認されたもの、ガスオール例えばガソ
リン/メタノール−90/10(容量比)では、透過量
は(以下余白)
1/’3〜1/10となり透過防止能は低下してしまう
事が判明した。Among the permeation prevention means mentioned above, polyethylene (hereinafter referred to as P
The most practical type of GT is the one in which the inner surface of the gas (referred to as E) is neutralized with NH3 gas after SO3 treatment, and is already installed in some vehicles in the United States and other countries. However, when the present inventors conducted various permeation tests using gasoline and gas all on the above-mentioned treated containers, it was found that the permeation amount of gasoline alone was 1/10 to 1/40 of that of untreated containers. For gas all that has been confirmed to have excellent permeation prevention ability, for example, gasoline/methanol - 90/10 (volume ratio), the amount of permeation will be 1/3 to 1/10 (see the margin below), and the permeation prevention ability will be was found to decrease.
この低下の理由については、鋭意究明中であるが、親水
性化されたPEの表面(PE−803NH,)がアルコ
ールとは非常に親和性が良い為、透過しゃすくなったも
のと推定される。従ってガスオールの透過性を改良する
為には、PE表面は疎水性及び親水性、即ちガソリン及
びアルコールの両方に対して透過防止能を有する必要を
認め、発明者らは、この点の改良に鋭意検討を重ねてき
た。The reason for this decrease is currently under investigation, but it is presumed that the hydrophilic PE surface (PE-803NH) has a very good affinity for alcohol, making it less permeable. . Therefore, in order to improve the permeability of gas all, the PE surface needs to be hydrophobic and hydrophilic, that is, to have the ability to prevent the permeation of both gasoline and alcohol, and the inventors have attempted to improve this point. We have been carefully considering this.
その結果、プラスチック容器をS03処理後すH3ガス
等で中和処理したものについてさらにBaCl2、Ba
(OH)2・8H20の如きアルカリ土類金属化合物
を含む溶液にて該表面を処理すると、ガソリン単体では
言うに及ばずガスオールでも透過防止能は一段と秀れ、
透過量は、未処理品(スルホン化処理無し)に比べて1
/40〜L/6 o又S03処理/NH,中和処理品の
115〜l/10にも改良できるという警異的な効果が
ある事を見出し発明の完成に至った。As a result, for plastic containers that had been neutralized with H3 gas after S03 treatment, BaCl2, Ba
When the surface is treated with a solution containing an alkaline earth metal compound such as (OH)2.8H20, the permeation prevention ability is even better not only for gasoline alone but also for all gases.
The amount of permeation is 1 compared to the untreated product (no sulfonation treatment).
/40~L/6o or S03 treated /NH, neutralized products were found to have the alarming effect of being able to be improved to 115~L/10, leading to the completion of the invention.
即ち本発明の要旨は、内部表面及び/又は外部表面をス
ルホン酸化処理し次いで中和処理を施した後1さらに該
表面をアルカリ土類金属を含む溶液で処理してなるプラ
スチック容器、である。That is, the gist of the present invention is a plastic container whose inner and/or outer surfaces are subjected to sulfonation treatment, followed by neutralization treatment, and then the surfaces are further treated with a solution containing an alkaline earth metal.
本発明に使用されてプラスチック容器の基材としては特
に限定はないが、エチレン、プロピレン、イソブチレン
、ブテン−14−メチルペンテン−1等の如きα−オレ
フィンのホモポリマー或いは、これらα−オレフィン同
志のコポリマー、塩素化ポリエチレン、アイオノマー、
上記α−オ゛レフインと少量の例えばアクリル酸、メタ
クリル酸或いはこれらのアルキルエステルの如きモノマ
ーノ共重合体、これらの混合物等、いわゆるオレフィン
系ポリマーが挙げられる。The base material of the plastic container used in the present invention is not particularly limited, but homopolymers of α-olefins such as ethylene, propylene, isobutylene, butene-14-methylpentene-1, etc., or combinations of these α-olefins are used. Copolymers, chlorinated polyethylene, ionomers,
So-called olefin polymers such as the above α-olefin and a small amount of monomer copolymers such as acrylic acid, methacrylic acid or alkyl esters thereof, and mixtures thereof may be mentioned.
上記の様なオレフィン系ポリマーを素材として、プロー
成形などにより成形して得られた容器は、内部表面及び
又は外部表面がスルホン酸化処理される。このスルホン
酸化処理め方法は、SO3を約15〜18容量チを含む
乾燥不活性ガス例えばN2、CO2、SO3或いは空気
で処理するか、或いは塩化メチレン、四塩化炭素のよう
な液体多塩素化脂肪族炭化水素中のSO3の溶液で処理
すれば良い。こうしたスルホン酸化処理では例えばポリ
エチレンの場合単位表面積当シS03が0.001〜2
0 my/cA導入される0
こうしてスルホン酸化処理された面は次いで中和処理が
施こされる。この中和処理は、アルカリ金属の水酸化物
または対応する弱酸の塩、アルカリ土類金属の水酸化物
または対応する弱酸の塩、重金属塩化物または硫酸塩、
第1、第2または第3アミン、水酸化アンモニウム、こ
れらの混合物等の稀釈水性溶液で処理するか、或いはガ
ス状アンモニア、メチルアミン等のような気相中和剤で
処理すれば良い。通常経済的観点等からガス状アンモニ
アを用い1〜数分間の処理が好んで用いられる。この中
和処理により、表面のスルホン酸基はスルホン酸の塩例
えばアンモニアガス中和では[PE−8o、NH,]
に変換される。A container obtained by molding the olefin polymer as described above by blow molding or the like is subjected to sulfonation treatment on the inner and/or outer surface. This sulfonation treatment method involves treating SO3 with a dry inert gas containing about 15-18 volumes of hydrogen, such as N2, CO2, SO3, or air, or with a liquid polychlorinated fat such as methylene chloride, carbon tetrachloride, etc. It may be treated with a solution of SO3 in group hydrocarbons. In such sulfonation treatment, for example, in the case of polyethylene, the S03 per unit surface area is 0.001 to 2.
0 my/cA introduced 0 The surface thus sulfonated is then subjected to a neutralization treatment. This neutralization treatment consists of alkali metal hydroxides or corresponding weak acid salts, alkaline earth metal hydroxides or corresponding weak acid salts, heavy metal chlorides or sulfates,
Treatment may be with dilute aqueous solutions of primary, secondary or tertiary amines, ammonium hydroxide, mixtures thereof, or with gas phase neutralizing agents such as gaseous ammonia, methylamine and the like. Usually, from an economic point of view etc., treatment using gaseous ammonia for 1 to several minutes is preferably used. By this neutralization treatment, the sulfonic acid groups on the surface are converted into sulfonic acid salts such as [PE-8o, NH,] in the case of ammonia gas neutralization.
is converted to
本発明に於いてはこのようにしてスルホン酸化(以下余
白)
後中和処理した処理面は、さらにアルカリ土類金属化合
物を含む溶液通常は水溶液にて処理される。In the present invention, the treated surface that has been subjected to the sulfonation (hereinafter referred to as blank space) and then neutralization treatment is further treated with a solution containing an alkaline earth metal compound, usually an aqueous solution.
アルカリ土類金属としては周期律表第1Ia族金属でB
e、 Mg%Ca%Sv、 Ba、 Rcなどが挙げら
れるが、そのうちで入手しやすい金属としてMg%Ca
、Baが好ましい。Alkaline earth metals include B in Group Ia of the periodic table.
e, Mg%Ca%Sv, Ba, Rc, etc. Among them, Mg%Ca is the most easily available metal.
, Ba are preferred.
該金属化合物としては、塩化物、臭化物、沃化物、弗化
物、水酸化物、次亜塩素酸塩、重クロム酸塩、炭酸塩、
硝酸塩、硫酸塩、酢酸塩、蟻酸塩、吉草酸塩、グリコン
酸塩、ケイ皮酸塩、男すチル酸、酪酸塩等が挙げられる
が、本発明では取り扱い性、経済性の点等からこれらの
化合物或いは塩の中で水に対して溶解性のある塩化物、
水酸化物、酢酸塩等が好ましい。具体的に挙げれば、塩
化マグネシウム、塩化カルシウム、塩化バリウム、水酸
化バリウム、酢酸マグネシウム、酢酸カルシウム、酢酸
バリウム等が好ましい。水溶液中の濃度に特に制限はな
いが、凡そ0.1q6〜飽和濃飽和量で選ばれ凡そ05
〜5チ濃度で充分である。The metal compounds include chloride, bromide, iodide, fluoride, hydroxide, hypochlorite, dichromate, carbonate,
Examples include nitrates, sulfates, acetates, formates, valerates, glyconates, cinnamates, androthylic acid, and butyrates, but in the present invention, these salts are used from the viewpoint of ease of handling and economical efficiency. chloride which is soluble in water among the compounds or salts of
Hydroxides, acetates and the like are preferred. Specifically, preferred are magnesium chloride, calcium chloride, barium chloride, barium hydroxide, magnesium acetate, calcium acetate, barium acetate, and the like. There is no particular limit to the concentration in the aqueous solution, but it is selected from approximately 0.1q6 to saturated concentration and approximately 0.5
A concentration of ~5% is sufficient.
処理温度についても特に制限はないが凡そ室温〜水の沸
点(100’(:りであり、又処理時間についてはスル
ホン酸化処理同様所望のバリヤ性との関連で決まってく
るが凡そ、数10秒〜数10分通常は1〜10分処理で
充分である。処理の方法は、例えば該金族化合物の水溶
液を容器に導入し一定温度で一定時間保持する方法や、
多孔のノズルを設けたパイプを用いシャワー状に該溶液
を容器面に一定時間噴出させる方法が挙げられる。この
ようにして処理された面は必要に応じ充分な水洗が施こ
され最後に乾・燥される。このアルカリ土類金属化合物
の水溶液処理によって、処理面単位面積当シ凡そ0.0
001〜0.05 m97cutのアルカリ土類金属が
導入される。There are no particular restrictions on the treatment temperature, but it ranges from room temperature to the boiling point of water (100'), and the treatment time, like the sulfonation treatment, is determined in relation to the desired barrier properties, but is approximately several tens of seconds. ~ several tens of minutes Usually, a treatment of 1 to 10 minutes is sufficient. Examples of treatment methods include, for example, introducing an aqueous solution of the metal compound into a container and holding it at a constant temperature for a certain period of time;
An example of this method is to use a pipe equipped with a porous nozzle to spray the solution in a shower-like manner onto the surface of the container for a certain period of time. The surface treated in this way is washed thoroughly with water if necessary, and finally dried. By this aqueous solution treatment of the alkaline earth metal compound, approximately 0.0
001-0.05 m97 cut of alkaline earth metal is introduced.
このようにして得られた容器はガソリン単体のみならず
ガソリン/メタノール、ガソリン/エタノール等のアル
コール混合炭化水素類の透過防止能に秀れ、かつ含水ガ
ソリンについてもアルコール混合ガソリン(ガスオール
)同様透過防止能に秀れている。又、このバリヤー膜の
耐久性については現在検討中であるが、少くともスルホ
ン酸化処理後アンモニア中和処理膜に比較して耐久性に
秀れ実用化レベルの高い処理方法である。The container obtained in this way has excellent permeation prevention ability not only for gasoline alone but also for alcohol mixed hydrocarbons such as gasoline/methanol and gasoline/ethanol, and is permeable for water-containing gasoline as well as alcohol mixed gasoline (Gas All) Excellent prevention ability. Although the durability of this barrier film is currently under investigation, it is a treatment method that is superior in durability and has a high level of practical application, at least compared to a membrane treated with ammonia neutralization after sulfonation treatment.
以下、本発明を具体的に実施例を挙げて詳細に説明する
。Hereinafter, the present invention will be specifically explained in detail by giving examples.
実施例r〜8、比較例1
ポリエチレンとして高密度ポリエチレン()−イロード
メルトインデックス−5,0g/10=i= 、密度=
0.9459Arl )を使用しカーボンブラック2
チを混合して、ブロー成形により平均肉厚2−1内容積
約1000crI11内部表面積約650crAの円筒
型容器を得た。この容器の内部を乾燥窒素ガスで置換し
た後、籾温70℃で約13容量係のS03を含む窒素ガ
スを約21/−i=の流速で120秒伺該容器内に導入
同雰囲気下に8分間保持した。Examples r to 8, Comparative Example 1 High density polyethylene () as polyethylene - Erode melt index - 5,0 g/10 = i =, Density =
0.9459Arl) using carbon black 2
A cylindrical container having an average wall thickness of 2-1, an internal volume of about 1000 crI, and an internal surface area of about 650 crA was obtained by blow molding. After replacing the inside of this container with dry nitrogen gas, nitrogen gas containing about 13 volumes of S03 at a rice grain temperature of 70°C was introduced into the container at a flow rate of about 21/-i for 120 seconds under the same atmosphere. It was held for 8 minutes.
次いで室温で5分間窒素ガスを517mの流速で導入し
未反応S03ガスをパージし、NH3ガスを室温にて2
分間21j/mの流速で該容器に導入し表面をNH3中
和を行なった後、充分な水洗を施こし乾燥した(比較例
1)。こうして処理された容器の内部に、表1に示す各
種金属の塩化物の3wt%水溶液を充填し、表1に示す
各温度、各時間で保持した後充分な水洗を施こし乾燥し
た。Next, nitrogen gas was introduced at a flow rate of 517 m for 5 minutes at room temperature to purge unreacted S03 gas, and NH3 gas was introduced at room temperature for 2
The material was introduced into the container at a flow rate of 21 j/m per minute to neutralize the surface with NH3, and then thoroughly washed with water and dried (Comparative Example 1). The interior of the thus treated container was filled with a 3 wt % aqueous solution of the chlorides of various metals shown in Table 1, held at each temperature and for each time shown in Table 1, thoroughly washed with water, and dried.
これ等の容器にレギュラーガソリン或いはこれに容量で
メタノール10%、20%、エタノール10%を混入し
た混合ガソリンを500CC充填し、40℃で7日間状
態調節をした後内容液を全て廃棄し、新らたに状態調節
に用いたと同じ液を500cc充填し40℃の防爆型恒
温等品室に放置し、この容器の重量を随時測定して重量
損失を追跡し1日当シの透過量を求めた。なお比較例1
としてNH3中和処理迄の容器及びブランク品としてプ
ロー成形した後に無処理の容器についても同様にして透
過量を求めた。表1の透過量から明らかなように本発明
の容器はブランクは勿論比較例1の容器より透過防止能
がはるかに秀れている。Fill these containers with 500 cc of regular gasoline or mixed gasoline mixed with methanol 10%, 20%, and ethanol 10% by volume, and condition the container at 40°C for 7 days, then discard all the contents and make a new one. Fill the container with 500 cc of the same liquid used for conditioning, leave it in an explosion-proof constant temperature room at 40°C, measure the weight of this container at any time, track the weight loss, and calculate the permeation amount per day. Ta. Furthermore, comparative example 1
The amount of permeation was determined in the same manner for containers that had not been subjected to NH3 neutralization treatment and containers that had been blow molded as blanks and were not treated. As is clear from the amount of permeation in Table 1, the container of the present invention has much better permeation prevention ability than the blank as well as the container of Comparative Example 1.
実施例1〜8で用いた塩化物の代りに、表2に示す各種
金属の水酸化物、酢酸塩を用いた他は実施例1〜8と同
様に行なった。但し内容物はガソリン/メタノール90
/10(容量比)で検討した。Examples 1 to 8 were carried out in the same manner as in Examples 1 to 8, except that hydroxides and acetates of various metals shown in Table 2 were used instead of the chlorides used in Examples 1 to 8. However, the contents are gasoline/methanol 90
/10 (capacity ratio).
表2の透過量から明らかなように本発明の容器は透過防
止能が秀れている。As is clear from the amount of permeation in Table 2, the container of the present invention has excellent permeation prevention ability.
表 2Table 2
Claims (1)
で中和処理を施した後、さらに該表面をアルカリ土類金
属を含む溶液で処理してなるプラスチック製容器。A plastic container whose inner and/or outer surfaces are subjected to sulfonation treatment, followed by neutralization treatment, and then the surfaces are further treated with a solution containing an alkaline earth metal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1088482A JPS58134856A (en) | 1982-01-28 | 1982-01-28 | Vessel made of plastic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1088482A JPS58134856A (en) | 1982-01-28 | 1982-01-28 | Vessel made of plastic |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58134856A true JPS58134856A (en) | 1983-08-11 |
JPH0260577B2 JPH0260577B2 (en) | 1990-12-17 |
Family
ID=11762736
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1088482A Granted JPS58134856A (en) | 1982-01-28 | 1982-01-28 | Vessel made of plastic |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58134856A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0221591A2 (en) * | 1985-10-07 | 1987-05-13 | The Dow Chemical Company | Method of sulfonating the interior surface of a plastics enclosure member |
US5605718A (en) * | 1994-07-20 | 1997-02-25 | Solvay (Soci et e Anonyme) | Process for the surface treatment of an article by sulphonation and neutralization |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5955165A (en) * | 1997-04-22 | 1999-09-21 | The Proctor & Gamble Company | Apparatus for handling viscous materials, composition for making such apparatus, method of making such apparatus |
-
1982
- 1982-01-28 JP JP1088482A patent/JPS58134856A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0221591A2 (en) * | 1985-10-07 | 1987-05-13 | The Dow Chemical Company | Method of sulfonating the interior surface of a plastics enclosure member |
US5605718A (en) * | 1994-07-20 | 1997-02-25 | Solvay (Soci et e Anonyme) | Process for the surface treatment of an article by sulphonation and neutralization |
Also Published As
Publication number | Publication date |
---|---|
JPH0260577B2 (en) | 1990-12-17 |
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