JPH0454628B2 - - Google Patents
Info
- Publication number
- JPH0454628B2 JPH0454628B2 JP7715685A JP7715685A JPH0454628B2 JP H0454628 B2 JPH0454628 B2 JP H0454628B2 JP 7715685 A JP7715685 A JP 7715685A JP 7715685 A JP7715685 A JP 7715685A JP H0454628 B2 JPH0454628 B2 JP H0454628B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- glass
- amount
- sulfur dioxide
- dioxide gas
- 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
Links
- 239000007789 gas Substances 0.000 claims description 61
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims description 44
- 239000011521 glass Substances 0.000 claims description 31
- 239000004215 Carbon black (E152) Substances 0.000 claims description 16
- 229930195733 hydrocarbon Natural products 0.000 claims description 16
- 150000002430 hydrocarbons Chemical class 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 9
- 238000004381 surface treatment Methods 0.000 claims description 6
- 238000000465 moulding Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims 1
- 238000011282 treatment Methods 0.000 description 14
- 239000000126 substance Substances 0.000 description 11
- 239000000047 product Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- -1 Freon Gas 152-A Chemical compound 0.000 description 5
- 229910052731 fluorine Inorganic materials 0.000 description 5
- 239000011737 fluorine Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000010583 slow cooling Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 3
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000000523 sample Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001990 intravenous administration Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000012488 sample solution Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 238000011481 absorbance measurement Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000001479 atomic absorption spectroscopy Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- WMIYKQLTONQJES-UHFFFAOYSA-N hexafluoroethane Chemical compound FC(F)(F)C(F)(F)F WMIYKQLTONQJES-UHFFFAOYSA-N 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 239000005361 soda-lime glass Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C23/00—Other surface treatment of glass not in the form of fibres or filaments
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Surface Treatment Of Glass (AREA)
Description
本発明は新規なガラスの表面処理法に関するも
のである。
ガラスの表面処理には破壊強度等物理的強度向
上に関するもの、装飾性を高める等付加価値向上
に関するものの外に化学的耐久性を高めるものが
ある。たとえば輪液用、点滴用など医薬用に用い
られるびんにあつてはガラスが内容液によつて侵
されてガラス中のナトリウムやカルシウム等が内
容液中に溶出することなきよう、或はそれを最低
にするよう高度な化学的耐久性が要求される。
このようなガラスの表面を処理して化学的耐久
性を高める方法に従来から種々あり、亜硫酸ガス
を用いる処理が一般的である。この場合はガラス
びんを成形後徐冷炉に入る直前又は徐冷炉内で亜
硫酸ガスを投入するのであるが、反応速度が遅い
為ガス投入量が比較的多量必要であるという事に
起因して、徐冷炉構造物の錆による製品の汚れ、
作業環境の悪化等が問題となる。またフロンガ
ス、フレオンガス(商品名)等のフツ化炭化水素
ガスによる処理によつてもガラスの化学的耐久性
の向上をはかかることができる。この場合は投入
ガス量が微量で良く、反応速度も速い為、作業環
境悪化等を来す事はないが、処理後の製品が透明
(反応生成物が付着していない)の為、管理が難
かしい、またガス量が多くなると水洗いでも除去
できない白濁が生ずる等の問題がある。
本発明者等ははからずもガラス製品に対して亜
硫酸ガスとフツ化炭化水素ガスによる処理を併用
するときは、夫々単独の処理ではえられない程高
度な化学的耐久性を有するガラス製品を得ること
ができることを見出したのであり、本発明はかか
る知見にもとずいてなされたものである。
かくて本発明は、550〜750℃の範囲の温度に保
持された成形直後の容器状のガラス製品内部に、
容器の内容積500ml当たり、0.5〜2.5mlのフツ化
炭化水素ガスと2〜20mlの亜硫酸ガスを注入し、
えられた両ガスの混合雰囲気を前記ガラス製品に
作用させ、次いで漸次徐冷することを特徴とす
る、ガラスの表面処理法を提供するものである。
本発明について更に詳しく説明すれば、本発明
では成形直後の薬用瓶などのガラス容器の表面を
亜硫酸ガス及びフツ化炭化水素ガスで処理するの
であるが、成形機にて成形してからマシンコンベ
アに載せられて徐冷炉に送られる数十秒の間にこ
の処理が施される。処理は注入ガスを一定圧力、
容量の下にノズルからガラス容器内部に噴入する
ことによつて行なわれる。順序は亜硫酸ガス、フ
ツ化炭化水素ガスの順でもよく、その逆でもよ
く、又は同時に噴入してもよく任意であるが、容
器状のガラス製品内部で両ガスが混合されて混合
雰囲気が形成されるようにする。成形してからコ
ンベアにより徐冷炉に至る間で処理するときのガ
ラス容器の温度は550〜750℃の範囲に保つのが好
ましい。この温度以上になると水洗によつても除
去できない白濁を生ずるおそれがあり、またこの
温度以下では適切な処理効果が得られず実用的で
ない。
フツ化炭化水素ガスとしては一般にフロン12
(CCl2F2)、フロン14(CF4)、フロン116(CF3−
CH3)、フロン152A(CH3CHF2)等の商品名で市
販されているものがあるが、本発明では塩素を含
まないガス、例えばフロンガス152−Aが好まし
い。
投入する亜硫酸ガス、フツ化炭化水素ガスの量
はガラス容器の容積、形状或は表面積てよつて又
はガラス材料によつて異なるがフツ化炭化水素ガ
スの量は多くすると、白濁を生ずるに至るため通
常の内容積500mlのガラス瓶1本当り0.5〜2.5ml
程度の微量でよく、又このフツ化炭化水素ガスの
併用により従来単独で用いられていた亜硫酸ガス
の量を1/4程度にすなわち2〜20mlに減少させて
も亜硫酸ガス単独処理とと同程度の化学的耐久性
を得ることができる。また、夫々のガス量を調節
する事によつて単独使用のときに較べ4倍も耐久
性をあげる事ができる。ガラス容器の満量容量に
対するフツ化炭化水素ガスの比率では2×10-3〜
5×10-3が外観を損ねるような白濁を生ずること
なく耐久性を向上させうる範囲である。
以下に試験例を示して本発明を更に説明するこ
ととする。
ソーダ石灰ガラスからつくられる内容積500ml
のリンゲルびん(通常400mlのリンゲル液充填)
を成形後徐冷炉へ搬送するマシンコンベア上にて
採取し、これを予め準備した断熱ボード上に静置
し、フロン152−Aを注射器にて一定量注入する。
この時のびん内表面温度は約700℃である。約1
秒間放置後次いで亜硫酸ガスを注射器にてびん内
に一定条件下に注入する。びんをレアー(徐冷
炉)ネツト上左端に静置し、レアーエンドにて採
取して試料とした。
ここでは注入する二つのガスの量を種々調整
し、組合わせてそのときの化学的耐久性をテスト
した。即ち、亜硫酸ガスの量を0,2,5,10,
20,40ml、一方フツ化炭化水素ガスの量を0,
0.5,1.0,2.5,5.0,10.0mlと変化させ組合わせて
テストする。
本発明では次の如き方法により化学的耐久性の
テストを行なつた。
(1) 試料のびんを水道水にて3回清浄し純水にて
3回リンスする。ついで0.02N塩化カリウム溶
液1mlを含む0.9%NaCl水溶液100mlを入れる。
リンゲルびん使用ゴムキヤツプ+アルミシエル
にてキヤツピングした後121℃、1時間でオー
トクレーブ処理する。えられた試料溶液に指示
薬を加えたのち、1/50規定の塩酸で滴定して
中和に要した塩酸の量を測定する。
(2) 前記(1)のテスト法は比較的過酷であり、試料
間の差が明確に表われるが、本発明ではこれと
は別に吸光分析によつて、溶出するフツ素イオ
ン等を定量する。即ち前記のように水道水で3
回洗浄し、純水にて3回リンスしたのち満量容
量の90%の純水を充填し、キヤツピングしたの
ち同様なオートクレーブ処理して試料溶液を得
る。これを分けて一つは必要な処理をした後
620nmの吸光度測定により溶出フツ素イオンを
定量し、一つは原子吸光分析により溶出Na2O
の量を定量する。
第(1)の方法によるテストの結果を第1表に、第
(2)の方法によるテストの結果を第2〜3表に示
す。いずれも各試料8本についてえられた結果の
平均値で示されており、第1表にては滴定した
1/50N塩酸の量(ml)によつて表わされ第2〜
3表においては夫々1本当りの量mgで示されてい
る。いずれの場合もこの値が小さいときは溶出す
るアルカリ或はフツ素の量が少なく化学的耐久性
が大ということができる。
The present invention relates to a novel glass surface treatment method. Glass surface treatments include those that improve physical strength such as breaking strength, those that improve added value such as decorativeness, and those that increase chemical durability. For example, in the case of bottles used for medical purposes such as for intravenous fluids and intravenous drips, the glass should be protected from being eroded by the liquid inside and sodium, calcium, etc. in the glass would not be eluted into the liquid, or A high degree of chemical durability is required to minimize the There have been various methods of treating the surface of such glass to improve its chemical durability, and treatment using sulfur dioxide gas is common. In this case, sulfur dioxide gas is injected into the lehr immediately after the glass bottle is molded or inside the lehr, but because the reaction rate is slow, a relatively large amount of gas is required. product stains due to rust,
Problems include deterioration of the working environment. Furthermore, the chemical durability of glass can also be improved by treatment with fluorinated hydrocarbon gas such as chlorofluorocarbon gas and Freon gas (trade name). In this case, only a small amount of gas is required and the reaction speed is fast, so the working environment will not be degraded, but since the product after treatment is transparent (no reaction products adhered to it), it is difficult to manage it. Moreover, when the amount of gas increases, there are problems such as the formation of a cloudy cloud that cannot be removed even by washing with water. The present inventors discovered that when treating glass products with sulfur dioxide gas and fluorinated hydrocarbon gas in combination, it was possible to obtain glass products with a high level of chemical durability that could not be obtained by either treatment alone. The present invention has been made based on this finding. Thus, the present invention provides a container-shaped glass product immediately after molding that is maintained at a temperature in the range of 550 to 750°C.
Inject 0.5 to 2.5 ml of fluorinated hydrocarbon gas and 2 to 20 ml of sulfur dioxide gas per 500 ml of internal volume of the container,
The present invention provides a method for surface treatment of glass, which is characterized in that the obtained mixed atmosphere of both gases is applied to the glass product, and then the glass product is gradually cooled. To explain the present invention in more detail, in the present invention, the surface of a glass container such as a medicine bottle immediately after being formed is treated with sulfur dioxide gas and fluorinated hydrocarbon gas. This treatment is performed during the several tens of seconds that the material is loaded and sent to the slow cooling furnace. Processing is done by keeping the injection gas at a constant pressure.
This is done by injecting the inside of the glass container from a nozzle under the volume. Sulfur dioxide gas and fluorinated hydrocarbon gas may be injected in that order, vice versa, or at the same time, but both gases are mixed inside the container-shaped glass product to form a mixed atmosphere. to be done. It is preferable that the temperature of the glass container be maintained in the range of 550 to 750° C. during the processing after molding and before being transferred to the slow cooling furnace via a conveyor. If the temperature exceeds this temperature, there is a risk of clouding that cannot be removed even by washing with water, and if the temperature is below this temperature, an appropriate treatment effect cannot be obtained and it is not practical. Freon-12 is generally used as a fluorinated hydrocarbon gas.
(CCl 2 F 2 ), Freon 14 (CF 4 ), Freon 116 (CF 3 −
Although some products are commercially available under trade names such as CH 3 ) and Freon 152A (CH 3 CHF 2 ), in the present invention, a gas that does not contain chlorine, such as Freon Gas 152-A, is preferred. The amount of sulfur dioxide gas or fluorinated hydrocarbon gas to be introduced varies depending on the volume, shape, or surface area of the glass container, or depending on the glass material, but if the amount of fluorinated hydrocarbon gas is too large, it will lead to clouding. 0.5-2.5ml per glass bottle with normal internal volume of 500ml
Even if the amount of sulfur dioxide gas used in combination with fluorinated hydrocarbon gas is reduced to about 1/4, that is, 2 to 20 ml, the amount is the same as that of sulfur dioxide gas treatment alone. chemical durability can be obtained. Furthermore, by adjusting the amount of each gas, durability can be increased four times compared to when used alone. The ratio of fluorinated hydrocarbon gas to the full capacity of the glass container is 2×10 -3 ~
5×10 -3 is a range in which durability can be improved without causing cloudiness that impairs the appearance. The present invention will be further explained by showing test examples below. Internal volume 500ml made from soda lime glass
Ringer bottle (usually filled with 400ml Ringer's solution)
After molding, the sample is collected on a machine conveyor that transports it to a slow cooling furnace, placed on a heat insulating board prepared in advance, and a fixed amount of Freon 152-A is injected with a syringe.
The inner surface temperature of the bottle at this time is approximately 700°C. Approximately 1
After allowing the bottle to stand for a second, sulfur dioxide gas is injected into the bottle using a syringe under certain conditions. The bottle was placed on the upper left end of the net of a lehr (slow cooling furnace), and a sample was taken at the leir end. Here, the amounts of the two gases injected were adjusted in various ways, and the chemical durability of the combinations was tested. That is, the amount of sulfur dioxide gas is 0, 2, 5, 10,
20, 40ml, while the amount of fluorinated hydrocarbon gas is 0,
Test by changing the combinations to 0.5, 1.0, 2.5, 5.0, and 10.0ml. In the present invention, chemical durability was tested by the following method. (1) Clean the sample bottle three times with tap water and rinse it three times with pure water. Next, add 100 ml of 0.9% NaCl aqueous solution containing 1 ml of 0.02N potassium chloride solution.
After capping with a Ringer bottle rubber cap + aluminum shell, autoclave at 121°C for 1 hour. After adding an indicator to the resulting sample solution, titrate with 1/50 normal hydrochloric acid to measure the amount of hydrochloric acid required for neutralization. (2) The test method in (1) above is relatively harsh and clearly shows differences between samples, but in the present invention, apart from this, eluted fluorine ions, etc. are quantified by absorption analysis. . That is, as mentioned above, 3 times with tap water.
After washing twice and rinsing with pure water three times, it is filled with pure water to 90% of its full capacity, capped, and subjected to the same autoclave treatment to obtain a sample solution. After dividing this, one is after doing the necessary processing.
The eluted fluorine ions were quantified by absorbance measurement at 620 nm, and the eluted Na 2 O was determined by atomic absorption spectrometry.
Quantify the amount of The results of the test using method (1) are shown in Table 1.
The results of the test using method (2) are shown in Tables 2 and 3. All are shown as the average value of the results obtained for each 8 samples, and in Table 1, they are expressed by the amount (ml) of titrated 1/50N hydrochloric acid,
In Table 3, the amounts are shown in mg per bottle. In any case, when this value is small, the amount of alkali or fluorine eluted is small and it can be said that the chemical durability is high.
【表】【table】
【表】【table】
【表】
これらの表から次のことが考察される。
(A) 第1表について言えば
() 通常の亜硫酸ガスによる処理の場合現行
では、0.200mlであるのに対し、併用すれば、
例えば亜硫酸ガス2ml、フロンガス2.5mlによ
り0.055mlの値がえられこの併用処理によつて
約4倍の耐久性がえられたことが明らかであ
る。
() また同様に亜硫酸ガスのみのときは40ml
用いると0.175mlの値がえられていたが、この
値は併用の場合フロンガスをわずか0.5ml用い
ることによつて亜硫酸ガスは前記単独のときの
1/4である10mlの少量で得ることができる。
() フロンガス投入量が多くなるに従つて耐
久性は極大値を示す。これはフロンガスについ
で投入される亜硫酸ガス投入量の多少にかかわ
らず同じ傾向にある。即ちフロンガス量が2.5
mlまでその量に従つて耐久性は急増するが、そ
れ以上の量では耐久性が徐々に低下する傾向が
ある。
(B) 第2、3表についていえば
() フツ素イオンは処理によつて白濁の生ず
るフロン5ml以上の処理で検出されるが、それ
以外の試料では検出限界(0.04mg/本)以下で
あり、フツ化炭化水素ガスの処理によつてもガ
ラス表面へのフツ素イオンの残留はなく安全で
あることが明らかである。
() Na2Oの溶出も、フロンガスと亜硫酸ガ
スを組合わせた処理で白濁を生じないものであ
れば、亜硫酸ガス単独処理時より少ないNa2O
しか検出せず併用処理の有効なことが明らかで
ある。
この外、若干外観について言及すれば、フロン
ガス投入量が5ml以上になると水洗によつても落
ちない白濁が生ずることが認められる。これは亜
硫酸ガスを投入しないフロンガス単独処理の場合
も同様であつた。しかしながらフロンガス投入量
が2.5ml以下の場合は水洗後には外観的には何の
異常も認められなかつた。
以上の試験例からも明らかなように本発明によ
り、亜硫酸ガスとフツ化炭化水素ガスの両者を併
用してガラスの表面処理を行なえば、夫々単独で
処理するときに比べてごく少ない量で高い化学的
耐久性を得ることができ、輪液びん、点滴びん等
の医薬用びん或はアルコール用びん等として好適
に用いうる良好なガラス製品を得ることができ
る。
かくて本発明はまことに有効なガラスの表面処
理法を提供するものである。
尚此の処理に用いられたフツ化炭化水素ガスと
亜硫酸ガスの動きについては十分把握されてはい
ないが、本発明で規定された温度下、微量の投入
ではガラス表面の分子とガスとの熱反応によりガ
スの分子はガラス内部に含有されて化学的耐久性
の向上に貢献し、外部に溶出したり噴出したりす
ることはないものと考えられる。[Table] The following can be considered from these tables. (A) Regarding Table 1, () Current treatment with normal sulfur dioxide gas is 0.200ml, but if used together,
For example, a value of 0.055 ml was obtained with 2 ml of sulfur dioxide gas and 2.5 ml of chlorofluorocarbon gas, and it is clear that the durability was approximately four times greater by this combined treatment. () Similarly, when using only sulfur dioxide gas, 40ml
When used together, a value of 0.175 ml was obtained, but by using only 0.5 ml of fluorocarbon gas in combination, sulfur dioxide gas can be obtained in a small amount of 10 ml, which is 1/4 of the amount when using it alone. . () As the amount of Freon gas input increases, the durability reaches its maximum value. This trend is the same regardless of the amount of sulfur dioxide gas added next to the fluorocarbon gas. In other words, the amount of fluorocarbon gas is 2.5
Durability increases rapidly as the amount increases up to ml, but as the amount exceeds that amount, durability tends to gradually decrease. (B) Regarding Tables 2 and 3, () Fluorine ions are detected when 5 ml or more of Freon is treated, which causes white turbidity, but in other samples, it is below the detection limit (0.04 mg/piece). It is clear that the treatment of fluorinated hydrocarbon gas does not leave any fluorine ions on the glass surface and is safe. () The elution of Na 2 O will also be less than when treating with sulfur dioxide gas alone, provided that the treatment does not result in white turbidity.
It is clear that the combined treatment is effective. In addition, to mention a few things about the appearance, it is observed that when the amount of Freon gas added is 5 ml or more, a white turbidity occurs that does not come off even when washed with water. This was also true in the case of treatment with chlorofluorocarbon gas alone without adding sulfur dioxide gas. However, when the amount of Freon gas input was 2.5 ml or less, no abnormality was observed in appearance after washing with water. As is clear from the above test examples, if glass surface treatment is carried out using both sulfur dioxide gas and fluorinated hydrocarbon gas in combination according to the present invention, a very small amount of sulfur dioxide gas and a fluorinated hydrocarbon gas can be used to treat the surface of the glass. It is possible to obtain a good glass product which has chemical durability and can be suitably used as a medical bottle such as a liquid-ring bottle or an infusion bottle, or a bottle for alcohol. Thus, the present invention provides a truly effective glass surface treatment method. The movement of the fluorinated hydrocarbon gas and sulfur dioxide gas used in this process is not fully understood, but when a small amount is added at the temperature specified in the present invention, the heat between the molecules on the glass surface and the gas It is thought that gas molecules are contained inside the glass due to the reaction, contributing to improved chemical durability, and are not eluted or spouted to the outside.
Claims (1)
後の容器状のガラス製品内部に、容器の内容積
500ml当たり、0.5〜2.5mlのフツ化炭化水素ガス
と2〜20mlの亜硫酸ガスを注入し、えられた両ガ
スの混合雰囲気を前記ガラス製品に作用させ、次
いで漸次徐冷することを特徴とする、ガラスの表
面処理法。1 Inside the container-shaped glass product immediately after molding, which is maintained at a temperature in the range of 550 to 750℃, the inner volume of the container is
It is characterized by injecting 0.5 to 2.5 ml of fluorinated hydrocarbon gas and 2 to 20 ml of sulfur dioxide gas per 500 ml, allowing the resulting mixed atmosphere of both gases to act on the glass product, and then gradually cooling it slowly. , glass surface treatment method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7715685A JPS61236635A (en) | 1985-04-11 | 1985-04-11 | Surface treating method for glass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7715685A JPS61236635A (en) | 1985-04-11 | 1985-04-11 | Surface treating method for glass |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61236635A JPS61236635A (en) | 1986-10-21 |
| JPH0454628B2 true JPH0454628B2 (en) | 1992-08-31 |
Family
ID=13625928
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7715685A Granted JPS61236635A (en) | 1985-04-11 | 1985-04-11 | Surface treating method for glass |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61236635A (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0678181B2 (en) * | 1988-10-27 | 1994-10-05 | セントラル硝子株式会社 | Glass surface treatment method |
| JP2949846B2 (en) * | 1990-11-30 | 1999-09-20 | 吉富製薬株式会社 | How to store albumin preparations |
| WO2002051767A1 (en) * | 2000-12-26 | 2002-07-04 | Nippon Sheet Glass Co.,Ltd. | Plate glass with protective film and method of manufacturing the plate glass |
| JP2005170736A (en) * | 2003-12-11 | 2005-06-30 | Ishizuka Glass Co Ltd | Oxidation reaction-suppressing glass material and oxidation reaction-suppressing glass container |
| KR20120104972A (en) * | 2009-12-04 | 2012-09-24 | 아사히 가라스 가부시키가이샤 | Glass plate and process for production thereof |
| WO2011121811A1 (en) * | 2010-03-30 | 2011-10-06 | 東洋ガラス株式会社 | Glass container and method for treating inner face of glass container |
| US8389052B2 (en) | 2010-03-30 | 2013-03-05 | Toyo Glass Co., Ltd. | Method for treating inside surface of glass container and glass container |
| JP5970166B2 (en) * | 2011-08-29 | 2016-08-17 | 石塚硝子株式会社 | Method for producing glass container for liquor with reduced calcium ion elution |
| CN104884398B (en) * | 2012-12-27 | 2017-05-31 | 旭硝子株式会社 | Float glass for chemical strengthening |
-
1985
- 1985-04-11 JP JP7715685A patent/JPS61236635A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61236635A (en) | 1986-10-21 |
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