JPS6124463B2 - - Google Patents
Info
- Publication number
- JPS6124463B2 JPS6124463B2 JP4959278A JP4959278A JPS6124463B2 JP S6124463 B2 JPS6124463 B2 JP S6124463B2 JP 4959278 A JP4959278 A JP 4959278A JP 4959278 A JP4959278 A JP 4959278A JP S6124463 B2 JPS6124463 B2 JP S6124463B2
- Authority
- JP
- Japan
- Prior art keywords
- container
- wall
- treating
- treated
- 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 56
- 238000000034 method Methods 0.000 claims description 36
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 24
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 18
- 238000011282 treatment Methods 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 13
- 229910052742 iron Inorganic materials 0.000 claims description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 9
- 230000001590 oxidative effect Effects 0.000 claims description 9
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 7
- 238000005554 pickling Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 claims description 2
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 2
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 238000007664 blowing Methods 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 16
- 238000000576 coating method Methods 0.000 description 6
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 5
- 229960003753 nitric oxide Drugs 0.000 description 5
- 239000004809 Teflon Substances 0.000 description 4
- 229920006362 Teflon® Polymers 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 4
- 229910052737 gold Inorganic materials 0.000 description 4
- 239000010931 gold Substances 0.000 description 4
- 238000007747 plating Methods 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 238000009489 vacuum treatment Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 229910000617 Mangalloy Inorganic materials 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000013020 steam cleaning Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Cleaning In General (AREA)
- Furnace Housings, Linings, Walls, And Ceilings (AREA)
Description
本発明は鉄製容器特に反応性標準ガスを貯蔵す
る高圧ガス容器の内壁処理方法に関する。
近時公害防止のため関連法規制が強まり、分析
計の校正用等に用いられる酸化窒素、一酸化炭
素、亜硫酸ガス等の反応性標準ガスが多量に製造
されるようになつた。特に酸化窒素標準ガスにつ
いては自動車排ガス測定用として低濃度の標準ガ
スの需要が多い。これらの標準ガスは長期にわた
りその組成値が変化してはならず、安定性が必要
であるが低濃度標準ガスは長期間の貯蔵に於てそ
の組成値に経時変化が生ずる場合があつた。この
組成変化の主な原因は成分ガスが、容器内に存
在する錆に吸着される、容器内に残存する水分
に溶解またはこれと反応する、容器内壁と反応
する容器内壁へ吸脱着する、等であると考えら
れる。従つてこれらの原因をとり除き、低濃度標
準ガスを長期間にわたり安定して貯蔵するため
に、従来その高圧ガス容器の内壁に各種の処理を
施す等の対策が行なわれて来た。即ちテフロンコ
ーテイング、金メツキ処理、容器内壁の酸洗滌を
行つた容器を多量につくり良品を選択する等であ
る。
テフロンコーテイング法は容器内面に弗素樹脂
を塗布し、また金メツキ法は容器内壁全面に金メ
ツキを施して内壁の鉄と成分ガスの接触を断つこ
とにより組成の安定を保たせる方法である。酸洗
滌は酸によつて錆をとかし容器内面を清浄にする
方法である。しかし低濃度反応性標準ガス用容器
については特にその処理が難かしく均質で良いも
のが得られずまた得られても高価である。即ちテ
フロンコーテイング法は鉄壁と樹脂の密着性に問
題があり価格も高い。金メツキを施した容器は低
濃度標準ガスの安定性には優れた効果を示し、財
団法人化学品検査協会による公的標準ガス(基準
標準ガス)用容器として認められているが、価格
が非常に高く一般市販標準ガス用として用いるこ
とが出来ない。またメツキ処理の結果にバラツキ
がある等の欠点がある。酸処理を行う方法は廉価
に出来るが処理結果にバラツキが多く、また一般
的に高品質のものが得がたい。
本発明はこれら従来法の不都合を解消するた
め、上記低濃度反応性標準ガスの経時組成変化の
起こる原因を究明し、数多くの実験を重ねた結果
得られたものである。即ち酸洗滌、加熱真空処理
については従来行なわれていた方法についてその
処理条件を検討し実験により最適範囲を求め、更
に従来行なわれなかつた酸化性ガスの封入を行う
ことにより容器内壁面に安定な酸化被膜を形成さ
せるようにししたもので、被処理容器を酸洗滌工
程、スチームまたはスチーム温湯洗滌工程、乾燥
工程、加熱真空排気工程の各処理を行なつた後、
該容器内に酸化性ガスを封入し放置して酸化被膜
を形成する工程を行なうことを特徴とする鉄製容
器の内壁処理方法である。そして、この処理方法
によつて容器内に於ける成分ガスの内壁面の吸脱
着を最小におさえ、容器内に於ける反応を防止す
ることが出来るようになり、低濃度反応性標準ガ
スの組成を長期間安定に保たせることを可能にし
たものである。
以下本発明方法を実施例によつて詳細説明す
る。
通常用いられているマンガン鋼製高圧ガス容器
のバルブを取り去り、その取り付け口より約6規
定の塩酸を注入し、容器開口部附近まで塩酸が入
つたまま約12時間放置する。この場合の塩酸濃度
は5〜7規定であればよくまた放置時間は12時間
に限らず容器内の錆の発生状態、塩酸の濃度等に
より更に長時間にする。塩酸による処理が終了し
たならば被処理容器より塩酸を排出してスチーム
クリーナーにより容器内部を1分間以上洗滌す
る。スチームクリーナーより噴出するスチームま
たはスチームと温湯の混合物により容器内に残存
する塩酸および剥離した錆等を完全に洗い出した
後、該容器内に乾燥した窒素ガスを1分間以上吹
き込んで容器内を乾燥する。この後容器弁をとり
つけ加熱真空引きを行なう。
即ち容器弁をとりつけた容器を加熱炉内に置
き、真空ポンプに接続し真空引きを行ないながら
加熱を行なう。この場合容器温度140℃以上に保
つて3時間以上真空引きを行ない到達真空度が2
×10-2Torr以下であることを確認する。この真
空度に達していない時にには更に加熱真空引きを
継続する。この処理によつて容器内壁に吸着して
いたガス、水分が完全に脱着され容器外へ排出さ
れ、容器内が完全に清浄になる。次いでこの内部
が完全に清浄になつた容器内に酸素または酸素含
有ガス等の酸化性ガスを封入し、一定期間放置す
ることにより該容器内壁に酸化被膜を形成させ
る。封入ガスは酸素、窒素等の不活性ガス中に酸
素を任意量混合した酸素含有ガス、乾燥空気、オ
ゾン、オゾン含有ガスあるいは二酸化窒素等の酸
化性のガスならばいづれでも良く、酸素含有ガス
の酸素含有量は100ppm程度以上であれば各種濃
度で処理が可能である。またオゾン含有ガスにつ
いても同様である。封入期間は1日以上であるこ
とが必要である。以上の処理により容器内は完全
に清浄にされた上内壁面に吸着されていたガス、
水分を脱着し、更に内壁表面は安定な酸化被膜が
形成されるため、この容器に酸化窒素等の反応性
の低濃度標準ガスを貯蔵した場合、その組成変化
を生じさせることがなく極めて安定に保たせるこ
とが出来る。
上記方法によつて処理した容器に各種の低濃度
反応性標準ガスを充填して、このガスの組成の経
時変化を調べた例を次に示す。即ち内容積10の
マンガン鋼製高圧ガス容器に上記処理を施し封入
ガスを真空排気した後、窒素中に酸化窒素を混合
した標準ガスを150Kg/cm2G充填し、その後この
標準ガスを定期的に抜き出して窒素酸化物分析計
により測定した。約1年間にわたり組成の経時変
化を調べた所、第1表の如くその変化は分析誤差
内であつた。また窒素中に一酸化炭素を混合しし
た標準ガスについても同様の実験を行つた結果は
第2表の通りである。これらの表によれば本発明
方法による処理を行つつた容器に充填した低濃度
反応性標準ガスは長期間にわたり極めて安定した
組成を保つていることが明らかである。
The present invention relates to a method for treating the inner wall of an iron container, particularly a high-pressure gas container for storing a reactive standard gas. In recent years, related laws and regulations have been strengthened to prevent pollution, and reactive standard gases such as nitrogen oxide, carbon monoxide, and sulfur dioxide gas, which are used for calibrating analyzers, have come to be produced in large quantities. In particular, there is a high demand for low-concentration nitrogen oxide standard gases for measuring automobile exhaust gas. These standard gases must be stable so that their composition values do not change over a long period of time, but when low concentration standard gases are stored for a long period of time, their composition values may change over time. The main causes of this compositional change are that the component gases are adsorbed by rust existing in the container, dissolved in or reacted with moisture remaining in the container, adsorbed and desorbed to the inner wall of the container and reacting with the inner wall of the container, etc. It is thought that. Therefore, in order to eliminate these causes and to store low-concentration standard gas stably for a long period of time, conventional measures have been taken such as applying various treatments to the inner walls of the high-pressure gas containers. That is, a large quantity of containers with Teflon coating, gold plating, and pickling of the inner walls of the containers are manufactured and quality products are selected. In the Teflon coating method, a fluororesin is applied to the inner surface of the container, and in the gold plating method, the entire inner wall of the container is plated with gold to prevent contact between the iron on the inner wall and the component gases, thereby maintaining the stability of the composition. Acid washing is a method of cleaning the inner surface of a container by removing rust using acid. However, containers for low-concentration reactive standard gases are particularly difficult to process, making it difficult to obtain homogeneous products, and even if they are obtained, they are expensive. That is, the Teflon coating method has problems with the adhesion between the iron wall and the resin and is expensive. Gold-plated containers have an excellent effect on the stability of low-concentration standard gases, and are recognized as containers for official standard gases (reference standard gases) by the Chemical Inspection Association, but they are very expensive. It cannot be used for general commercially available standard gases. Further, there are drawbacks such as variations in the results of the plating process. Although the acid treatment method is inexpensive, the treatment results vary widely and it is generally difficult to obtain high quality products. In order to overcome these disadvantages of the conventional methods, the present invention was achieved by investigating the cause of the change in composition over time of the above-mentioned low concentration reactive standard gas and by conducting numerous experiments. In other words, for pickling and heating and vacuum treatment, we examined the treatment conditions of conventional methods and determined the optimal range through experiments. Furthermore, by filling in oxidizing gas, which had not been done in the past, we created a stable coating on the inner wall surface of the container. It is designed to form an oxide film, and after the container to be treated is subjected to the following treatments: pickling process, steam or steam hot water washing process, drying process, heating vacuum evacuation process,
This is a method for treating the inner wall of an iron container, characterized by performing a step of sealing an oxidizing gas in the container and leaving it to form an oxide film. This treatment method makes it possible to minimize adsorption and desorption of component gases on the inner wall surface of the container and prevent reactions within the container, thereby reducing the composition of the low-concentration reactive standard gas. This makes it possible to maintain stability for a long period of time. The method of the present invention will be explained in detail below using examples. Remove the valve of a commonly used manganese steel high-pressure gas container, inject approximately 6N of hydrochloric acid through its installation port, and leave the container with hydrochloric acid near the opening for approximately 12 hours. In this case, the concentration of hydrochloric acid may be 5 to 7N, and the standing time is not limited to 12 hours, but may be longer depending on the state of rust in the container, the concentration of hydrochloric acid, etc. When the treatment with hydrochloric acid is completed, the hydrochloric acid is discharged from the container to be treated, and the inside of the container is washed with a steam cleaner for at least 1 minute. After the hydrochloric acid and peeled rust remaining in the container are completely washed away with the steam or a mixture of steam and hot water ejected from the steam cleaner, dry nitrogen gas is blown into the container for at least 1 minute to dry the inside of the container. . After this, attach the container valve and perform heating and evacuation. That is, a container fitted with a container valve is placed in a heating furnace, connected to a vacuum pump, and heated while being evacuated. In this case, maintain the container temperature at 140°C or higher and evacuate it for more than 3 hours until the final vacuum level reaches 2.
Check that it is below ×10 -2 Torr. When this degree of vacuum has not been reached, heating and evacuation are further continued. Through this process, the gas and moisture adsorbed on the inner wall of the container are completely desorbed and discharged to the outside of the container, making the inside of the container completely clean. Next, an oxidizing gas such as oxygen or an oxygen-containing gas is sealed in the container whose interior has been completely cleaned, and an oxidized film is formed on the inner wall of the container by leaving it for a certain period of time. The sealed gas may be any oxygen-containing gas such as oxygen, an oxygen-containing gas mixed with an arbitrary amount of oxygen in an inert gas such as nitrogen, dry air, ozone, an ozone-containing gas, or an oxidizing gas such as nitrogen dioxide. As long as the oxygen content is about 100 ppm or more, treatment can be performed at various concentrations. The same applies to ozone-containing gas. The enclosure period must be one day or more. Through the above treatment, the inside of the container was completely cleaned, and the gas that had been adsorbed on the upper inner wall surface was removed.
Moisture is desorbed and a stable oxide film is formed on the inner wall surface, so when a reactive low concentration standard gas such as nitrogen oxide is stored in this container, its composition will not change and it will be extremely stable. It can be kept. The following is an example in which a container treated by the above method was filled with various low-concentration reactive standard gases, and changes in the composition of the gases over time were investigated. That is, a high-pressure gas container made of manganese steel with an internal volume of 10 is subjected to the above treatment and the sealed gas is evacuated, then it is filled with 150 kg/cm 2 G of a standard gas containing nitrogen oxide mixed with nitrogen, and then this standard gas is periodically pumped. It was extracted and measured using a nitrogen oxide analyzer. When the changes in composition over time were investigated over a period of about one year, the changes were within the analytical error as shown in Table 1. Table 2 shows the results of a similar experiment using a standard gas containing nitrogen and carbon monoxide. According to these tables, it is clear that the low-concentration reactive standard gas filled in the container undergoing treatment according to the method of the present invention maintains an extremely stable composition over a long period of time.
【表】【table】
【表】
本発明は以上の如く、低濃度反応性標準ガスの
経時組成変化の原因を究明してこれを除く処理法
を数多くの実験の結果得られたもので、酸洗滌、
スチーム洗滌により容器内の錆を完全に除去し、
窒素乾燥、加熱真空処理により、容器内壁の水
分、吸着ガスを完全に取り去つて清浄にした後、
酸化性ガスの封入を行うことによい安定な酸化被
膜を形成させるようにしたものである。これらの
処理をすることによつて容器内に於ける成分ガス
の内壁面への吸脱着を最小におさえ、容器内に於
ける反応を防止することが出来るようになり、低
濃度反応性標準ガスの組成を長期間安定に保たせ
ることが可能になつた。しかも本発明方法は酸処
理、加熱真空引処理等は従来用いられていた設備
を利用出来るため本発明方法実施のために新たな
設備の増設が必要なく、酸化性ガスの封入工程も
比較的容易に出来るため価格的に安く、実施も容
易である。テフロンコーテイング法、金メツキ法
が夫々このための処理設備を必要とし、且つ被膜
自体が高価であるのに比較して極めて優れた特徴
である。更に本発明方法によれば処理結果にバラ
ツキがなく均質の容器を容易大量に得ることが出
来、一般市販標準ガス用高圧ガス容器の処理方法
として望ましい条件を備えている。[Table] As described above, the present invention is the result of numerous experiments in which the causes of changes in the composition of low-concentration reactive standard gases over time have been investigated, and treatment methods for eliminating them have been obtained.
Steam cleaning completely removes rust inside the container.
After completely removing moisture and adsorbed gas from the inner wall of the container by nitrogen drying and heating vacuum treatment,
It is designed to form a stable oxide film that is suitable for enclosing oxidizing gas. By performing these treatments, it becomes possible to minimize adsorption and desorption of component gases to the inner wall surface of the container and prevent reactions within the container. It became possible to keep the composition stable for a long period of time. Moreover, since the method of the present invention can use conventionally used equipment for acid treatment, heating vacuum treatment, etc., there is no need to add new equipment to carry out the method of the present invention, and the process of filling the oxidizing gas is relatively easy. It is inexpensive and easy to implement. This is an extremely advantageous feature compared to the Teflon coating method and the gold plating method, which each require processing equipment and the coating itself is expensive. Further, according to the method of the present invention, homogeneous containers with uniform treatment results can be easily obtained in large quantities, and the method has desirable conditions as a method for treating high-pressure gas containers for general commercially available standard gases.
Claims (1)
チーム温湯洗滌工程、乾燥工程、加熱真空排気工
程の各処理を行なつた後、該容器内に酸化性ガス
を封入し放置して酸化被膜を形成する工程を行な
うことを特徴とする鉄製容器の内壁処理方法。 2 上記酸洗滌工程が5〜7規定の塩酸を被処理
容器中に注入して放置することを特徴とする特許
請求の範囲第1項記載の鉄製容器の内壁処理方
法。 3 上記酸洗滌工程が6規定の塩酸を被処理容器
中に注入して約12時間放置することを特徴とする
特許請求の範囲第2項記載の鉄製容器の内壁処理
方法。 4 上記スチームまたはスチーム温湯洗滌工程が
前工程において注入した酸塩を排出後スチームま
たはスチーム温湯混合物にて被処理容器内部を1
分間以上洗滌することを特徴とする特許請求の範
囲第1項記載の鉄製容器の内壁処理方法。 5 上記乾燥工程が被処理容器内に乾燥した窒素
ガスを1分間以上吹き込むことを特徴とする特許
請求の範囲第1項記載の鉄製容器の内壁処理方
法。 6 上記加熱真空排気工程が、被処理容器を140
℃以上に保ちつつ3時間以上真空排気を行なうこ
とを特徴とする特許請求の範囲第1項記載の鉄製
容器の内壁処理方法。 7 前記被処理容器内に酸化性ガスを封入し放置
する工程において、封入する酸化性ガスが酸素、
酸素含有ガス、乾燥空気、オゾン、オゾン含有ガ
ス、二酸化窒素であり、その放置時間が1日以上
であることを特徴とする特許請求の範囲第1項記
載の鉄製容器の内壁処理方法。 8 被処理容器内に封入する酸素含有ガスまたは
オゾン含有ガス中の酸素またはオゾンの濃度が
夫々100ppm以上であることを特徴とする特許請
求の範囲第7項記載の鉄製容器の内壁処理方法。[Scope of Claims] 1 After a container to be treated is subjected to each of the following treatments: pickling process, steam or steam hot water washing process, drying process, and heating vacuum evacuation process, an oxidizing gas is sealed in the container and left to stand. 1. A method for treating the inner wall of an iron container, comprising a step of forming an oxide film. 2. The method for treating the inner wall of an iron container according to claim 1, wherein the pickling step involves injecting 5 to 7N hydrochloric acid into the container to be treated and leaving the container to stand. 3. The method for treating the inner wall of an iron container according to claim 2, wherein the pickling step involves injecting 6N hydrochloric acid into the container to be treated and leaving it for about 12 hours. 4 After the steam or steam hot water cleaning process discharges the acid salt injected in the previous process, the inside of the container to be treated is washed with steam or a steam hot water mixture.
The method for treating the inner wall of an iron container according to claim 1, wherein the cleaning is performed for at least a minute. 5. The method for treating the inner wall of an iron container according to claim 1, wherein the drying step includes blowing dry nitrogen gas into the container to be treated for one minute or more. 6 The above heating vacuum evacuation process
A method for treating the inner wall of an iron container according to claim 1, characterized in that evacuation is carried out for 3 hours or more while maintaining the temperature at or above .degree. 7 In the step of sealing an oxidizing gas in the container to be treated and leaving it, the oxidizing gas to be sealed is oxygen,
2. The method for treating the inner wall of an iron container according to claim 1, wherein the method uses an oxygen-containing gas, dry air, ozone, an ozone-containing gas, or nitrogen dioxide, and is left to stand for one day or more. 8. The method for treating the inner wall of an iron container according to claim 7, wherein the concentration of oxygen or ozone in the oxygen-containing gas or ozone-containing gas sealed in the container to be treated is 100 ppm or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4959278A JPS54141347A (en) | 1978-04-26 | 1978-04-26 | Treatment of internal surface of iron container |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4959278A JPS54141347A (en) | 1978-04-26 | 1978-04-26 | Treatment of internal surface of iron container |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54141347A JPS54141347A (en) | 1979-11-02 |
| JPS6124463B2 true JPS6124463B2 (en) | 1986-06-11 |
Family
ID=12835496
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4959278A Granted JPS54141347A (en) | 1978-04-26 | 1978-04-26 | Treatment of internal surface of iron container |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS54141347A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004245249A (en) * | 2003-02-10 | 2004-09-02 | Mcc Kogyo:Kk | Container for highly purified high-pressure gas, and manufacturing method therefor |
-
1978
- 1978-04-26 JP JP4959278A patent/JPS54141347A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54141347A (en) | 1979-11-02 |
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