JPH0739572B2 - Evaporation suppressant and evaporation suppression method using the same - Google Patents

Evaporation suppressant and evaporation suppression method using the same

Info

Publication number
JPH0739572B2
JPH0739572B2 JP2206003A JP20600390A JPH0739572B2 JP H0739572 B2 JPH0739572 B2 JP H0739572B2 JP 2206003 A JP2206003 A JP 2206003A JP 20600390 A JP20600390 A JP 20600390A JP H0739572 B2 JPH0739572 B2 JP H0739572B2
Authority
JP
Japan
Prior art keywords
evaporation
gas
liquid
ammonia
gas evaporation
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 - Lifetime
Application number
JP2206003A
Other languages
Japanese (ja)
Other versions
JPH0489882A (en
Inventor
宏幸 高橋
純平 鳥海
悟允 江藤
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.)
Miyata Industry Co Ltd
Original Assignee
Miyata Industry Co Ltd
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 Miyata Industry Co Ltd filed Critical Miyata Industry Co Ltd
Priority to JP2206003A priority Critical patent/JPH0739572B2/en
Publication of JPH0489882A publication Critical patent/JPH0489882A/en
Publication of JPH0739572B2 publication Critical patent/JPH0739572B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Fire-Extinguishing Compositions (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、アンモニア水とか酢酸等の毒性及び刺激性ガ
スを発生する液化ガスが、地震その他不測の事故等によ
り貯蔵中の密閉容器から漏洩した場合に、毒性及び刺激
性ガスの蒸発を緊急に抑制するため、漏洩した蒸発性液
の表面を覆うガス蒸発抑制剤とこれを用いたガス蒸発抑
制方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention discloses that liquefied gas that produces toxic and irritating gases such as ammonia water and acetic acid leaks from a closed container during storage due to an earthquake or other unexpected accident. In this case, the present invention relates to a gas evaporation inhibitor that covers the surface of the leaked evaporative liquid and a gas evaporation suppression method using the same in order to urgently suppress the evaporation of toxic and irritating gases.

〔従来の技術〕[Conventional technology]

例えば貯蔵中の高濃度アンモニア水が漏洩した場合、大
量に大気中に蒸発した刺激性ガスが拡散して大きな被害
を与えるおそれがある。
For example, if the high-concentration aqueous ammonia leaks during storage, a large amount of the stimulating gas evaporated in the atmosphere may diffuse to cause serious damage.

そこで貯蔵タンクの周囲を防液堤で囲んで流出液の拡散
を阻止すると共に、大量に注水し希釈する方法が一般に
行われている。また、特公昭61-17768号には流出した液
体アンモニアの表面を気泡で覆って蒸発を防止する方法
が提案されている。これは、例えば気泡剤であるアニオ
ン界面活性と泡安定剤であるグリコールエーテルとから
なる水溶性気泡形成剤の水溶液を、防液堤内に漏洩して
いる液体アンモニアの液面に広く散布し、アンモニアガ
スを内包する気泡を発生させて液面を該気泡で覆うこと
により、アンモニアの蒸発拡散を抑制するものである。
Therefore, a method is generally used in which the storage tank is surrounded by a dike to prevent the effluent from diffusing and a large amount of water is injected to dilute it. Also, Japanese Patent Publication No. 61-17768 proposes a method of covering the surface of liquid ammonia that has flowed out with bubbles to prevent evaporation. This is because, for example, an aqueous solution of a water-soluble bubble forming agent consisting of an anionic surface active agent which is a foaming agent and glycol ether which is a foaming stabilizer is widely sprayed on the liquid surface of liquid ammonia leaking in the dike, By generating bubbles containing gas and covering the liquid surface with the bubbles, the evaporation and diffusion of ammonia is suppressed.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかしながら、従来の注水による希釈方法では極めて大
量の水を使用しなければいけないし、且つ−30〜−40℃
の低温である漏洩アンモニアに常温の水を注入すると、
漏洩アンモニアは注水当初爆発的に蒸発が進行する。し
たがってその後の大量の水の二次処理が困難となる欠点
があった。
However, in the conventional dilution method using water injection, an extremely large amount of water must be used, and -30 to -40 ° C.
Injecting room temperature water into the leaking ammonia, which is the low temperature of
The leaked ammonia explosively evaporates at the beginning of water injection. Therefore, there is a drawback that the subsequent secondary treatment of a large amount of water becomes difficult.

一方、泡で液面を被覆して蒸発を抑制する方法の場合
は、以下のような問題点があった。
On the other hand, the method of covering the liquid surface with bubbles to suppress evaporation has the following problems.

泡の保持時間30分程度と短く、その持続時間内に防液
堤内の漏洩液化ガスをバキュームカー等により汲み出さ
なければならない。
The retention time of bubbles is as short as about 30 minutes, and the leaked liquefied gas in the dike must be pumped out by a vacuum car etc. within the duration.

泡が風で吹き飛ばされて漏洩液化ガスの液面が露出し
易い。しかも、一端泡が飛ばされると、新たに気泡形成
剤の追加をし発泡させなければいけない。
The bubbles are easily blown off and the liquid surface of the leaked liquefied gas is easily exposed. Moreover, once the bubbles are blown off, it is necessary to newly add a bubble-forming agent to foam the bubbles.

気泡形成剤は水溶液として用いられるから、鉄製の容
器、配管等の内部が錆び易く、防錆処置に費用がかか
る。
Since the bubble forming agent is used as an aqueous solution, the inside of iron containers, pipes and the like are easily rusted, and rust preventive measures are expensive.

気泡形成剤は6%程度の水溶液で散布されるから、面
積の大きい防液堤内に滞留する漏洩液化ガスに対して
は、気泡形成剤の貯蔵タンクと共に大容量の貯水槽が必
要で、設備費が高価になる。
Since the bubble forming agent is sprayed with an aqueous solution of about 6%, a large-capacity water storage tank along with a storage tank for the bubble forming agent is required for leaked liquefied gas that stays in a large levee. Becomes expensive.

防液堤内に漏洩した液体アンモニアの液面全体に平均
して気泡形成剤の水溶液を散布するためには、延長距離
の長い配管に多数の散布用ノズルを配設して液面全体に
対する散布設備が必要となり、設備費、保守費が高価に
なる。
In order to spray the aqueous solution of the air bubble forming agent on average over the entire liquid surface of the liquid ammonia leaked into the levee, install a large number of spray nozzles in the pipe with a long extension distance and spray equipment over the entire liquid surface. Is required, and the equipment cost and maintenance cost are high.

そこで本発明は、上記従来の問題点に着目してなされた
ものであり、その目的とするところは持続時間が極めて
長い非水溶性の液体で被処理液の液面を被覆して毒性ガ
ス、刺激臭ガスの蒸発を緊急に抑制する蒸発性液化ガス
の蒸発抑制剤と蒸発抑制方法を提供して従来の問題点を
解決することにある。
Therefore, the present invention has been made by paying attention to the above-mentioned conventional problems, and the purpose thereof is to cover the liquid surface of the liquid to be treated with a non-water-soluble liquid having an extremely long duration and a toxic gas, An object of the present invention is to solve the problems of the prior art by providing an evaporation inhibitor and a method for suppressing evaporation of liquefied liquefied gas that urgently suppresses evaporation of irritating odorous gas.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記目的を達成するため、本発明の蒸発液化ガスの蒸発
抑制方法は、主成分が飽和炭化水素からなる液体で蒸発
性液化ガスの液面を覆うことを特徴とする。
In order to achieve the above object, the method for suppressing evaporation of an evaporated liquefied gas according to the present invention is characterized in that the liquid surface of the evaporated liquefied gas is covered with a liquid whose main component is a saturated hydrocarbon.

また、本発明のガス蒸発抑制剤は一般式CnH2n+2で表さ
れ且つnが10〜46のパラフィン系炭化水素と、一般式 で表され且つnが10〜46のナフテン系炭化水素とを混合
してなる。
Further, the gas evaporation inhibitor of the present invention is represented by the general formula C n H 2n + 2 and n is 10 to 46, and a paraffinic hydrocarbon And a naphthene-based hydrocarbon having n of 10 to 46 are mixed.

更に蒸発抑制効果を向上させるために上記ガス蒸発抑制
剤に、末端基にカルボキシル基COOH、水酸基OH、アミノ
基NH2、スルフォン酸基SO3の如く親水基を持つ有機化合
物、例えば、 等を混合したものである。
In order to further improve the evaporation suppressing effect, the gas evaporation suppressing agent, an organic compound having a hydrophilic group such as carboxyl group COOH, hydroxyl group OH, amino group NH 2 and sulfonic acid group SO 3 at the end group, for example, Etc. are mixed.

〔作用〕[Action]

例えば高濃度アンモニア水溶液が防液堤内に漏洩したと
き、飽和炭化水素の混合物を主成分とするガス蒸発抑制
剤を漏洩液の液面に散布すると、拡がって液面を被覆
し、刺激性のあるアンモニアガスの蒸発揮散を長時間に
わたって抑制する事が出来る。
For example, when a high-concentration aqueous ammonia solution leaks into the dike, if a gas evaporation inhibitor containing a mixture of saturated hydrocarbons as the main component is sprayed on the liquid surface of the leaked liquid, it spreads and covers the liquid surface, which is irritating. It is possible to suppress evaporation of ammonia gas over a long period of time.

パラフィン炭化水素とナフテン系炭化水素との混合物の
物性は熱、光、酸・アルカリ等の化学薬品に対し不活性
で長期安定性が優れており、且つ金属に対する腐食性も
なく容器、配管等に錆を生じるおそれもない。
The physical properties of a mixture of paraffin hydrocarbons and naphthenic hydrocarbons are inert to heat, light, chemicals such as acids and alkalis, and have excellent long-term stability, and they are not corrosive to metals and are suitable for containers, piping, etc. There is no risk of rusting.

また、ある程度の厚みを持った層として液面を被覆出来
るため、泡のように風に吹き飛ばされることもなく、長
時間安定したガス蒸発抑制効果を示す。
Further, since the liquid surface can be covered with a layer having a certain thickness, it is not blown away by the wind like bubbles, and exhibits a stable gas evaporation suppressing effect for a long time.

したがって、時間をかけて漏洩液を処理することが可能
である。また、漏洩液の回収の際も、ガス抑制剤の被覆
が破れることがないから、ガス蒸発が完全に阻止され
る。且つガス抑制剤自身の毒性がないから極めて安全に
作業することができる。
Therefore, it is possible to process the leaked liquid over time. Further, even when the leaked liquid is collected, the gas inhibitor coating does not break, and gas evaporation is completely prevented. Moreover, since the gas suppressor itself is not toxic, it is possible to work extremely safely.

ガス蒸発抑制剤中に混合されたメタクリル酸ポリマーの
如くの末端基に親水基を持つ有機化合物は、被処理液面
への飽和炭化水素の拡散を促進し、液面全体に流動展開
する。
An organic compound having a hydrophilic group at the terminal group, such as a methacrylic acid polymer mixed in a gas evaporation inhibitor, promotes diffusion of saturated hydrocarbons to the liquid surface to be treated, and fluidly spreads over the entire liquid surface.

又、ガス蒸発抑制装置には、ガス蒸発抑制剤の貯蔵タン
ク以外に貯水槽を設ける必要はなく設備費用、設置スペ
ースが僅かで済む。
Further, in the gas evaporation suppressing device, it is not necessary to provide a water storage tank other than the storage tank for the gas evaporation suppressing agent, and the equipment cost and installation space are small.

以下さらに詳細に説明する。This will be described in more detail below.

本発明のガス蒸発抑制剤は、一般式CnH2n+2で表され且
つnが10〜46のパラフィン系炭化水素と、一般式 で表され且つnが10〜46のナフテン系炭化水素との混合
物が望ましく、nが10未満ではガス状であるか、もしく
は液状であっても引火点が低下することになり好ましく
ない。一方、nが46を越えると流動性が不足する。
The gas evaporation inhibitor of the present invention comprises a paraffinic hydrocarbon represented by the general formula C n H 2n + 2 and n is 10 to 46, and a general formula And a mixture with a naphthene-based hydrocarbon having n of 10 to 46 is preferable, and when n is less than 10, it is not preferable because the flash point is lowered even if it is gaseous or liquid. On the other hand, when n exceeds 46, the liquidity is insufficient.

パラフィン系炭化水素:ナフテン系炭化水素の混合比
は、6:4〜8:2の範囲が適当で、特に7:3のものが最適で
ある。
The mixing ratio of paraffinic hydrocarbon to naphthenic hydrocarbon is appropriately in the range of 6: 4 to 8: 2, and particularly 7: 3.

パラフィン系炭化水素の割合が6未満になると粘度が低
くなりすぎ、一方8を越えると流動性が低下するため使
い勝手が悪くなる。
If the ratio of the paraffinic hydrocarbon is less than 6, the viscosity becomes too low, while if it exceeds 8, the fluidity is lowered and the usability becomes poor.

n=15〜34、パラフィン系炭化水素:ナフテン系炭化水
素=7:3の流動パラフィン等は引火点が220℃程度、20℃
での比重が0.82ないし0.89g/ccであり、好適に使用出来
る。
Liquid paraffin with n = 15-34 and paraffin hydrocarbon: naphthene hydrocarbon = 7: 3 has a flash point of about 220 ℃, 20 ℃.
It has a specific gravity of 0.82 to 0.89 g / cc and can be suitably used.

上記流動パラフィンは、そのままアンモニア水等被処理
液面に散布して用いてよいが、前記各炭化水素と相溶性
がよく且つ親水性を有するポリマーである 等を混合することにより、被処理面における展開性を向
上せしめ、特に防液堤のコンクリート表面との親和性が
富むことから、流動パラフィンとコンクリート表面のメ
ニスカスは凹となり、より効果を上げる事が出来る。
The liquid paraffin may be used as it is by spraying it onto the surface of the liquid to be treated such as ammonia water, but it is a polymer that has good compatibility with the above hydrocarbons and is hydrophilic. It improves the spreadability on the surface to be treated, especially because it has a good affinity with the concrete surface of the levee, so the liquid paraffin and the meniscus on the concrete surface become concave, and the effect can be further improved. I can.

又上記ポリマーの添加量は、0.01〜10W/V%の範囲が好
適であることが実験により確認された。
It was confirmed by experiments that the amount of the above polymer added is preferably in the range of 0.01 to 10 W / V%.

本発明のガス蒸発抑制剤を適用できる被処理液は、例え
ば高濃度アンモニア水、酢酸、モノメチルアミン、ジメ
チルアミン、トリメチルアミン等のアミン類及びシアン
化水素など、有毒性ガスを発生する液体またはその高濃
度水溶液で、且つ飽和炭化水素より比重が大きいもので
ある。
The liquid to be treated to which the gas evaporation inhibitor of the present invention can be applied is, for example, high-concentration aqueous ammonia, acetic acid, amines such as monomethylamine, dimethylamine, trimethylamine, and hydrogen cyanide. And has a larger specific gravity than saturated hydrocarbons.

〔実施例〕〔Example〕

以下、本発明の実施例について説明する。 Examples of the present invention will be described below.

(第1実施例) 一辺の長さ1m、深さ20cmの開放容器内に被処理液として
29%アンモニア水を入れ、ガス蒸発抑制剤として、具体
的にはCnH2n+2(n=15〜34)のパラフィン系炭化水
素: (n=15〜34)のナフテン系炭化水素=7:3の流動パラ
フィンを投入した場合のアンモニア水の重量減少量の時
間変化をガス蒸発抑制剤を投入しない場合(ブランク)
と比較する。
(First Example) As a liquid to be treated in an open container having a side length of 1 m and a depth of 20 cm.
29% ammonia water was added, and as a gas evaporation inhibitor, specifically, C n H 2n + 2 (n = 15 to 34) paraffinic hydrocarbon: (N = 15 to 34) naphthenic hydrocarbons = 7: 3 liquid paraffin was added to the ammonia water weight loss with time without gas evaporation inhibitor (blank)
Compare with.

アンモニアガスの蒸発による重量減少量は、容器をプラ
ットホーム型ロードセル(共和電業製、LCL−F)上に
載置して歪量を動歪測定器(同、DPM-611A)で計測し、
レコーダーに記録する。
The amount of weight loss due to the evaporation of ammonia gas is placed on a platform type load cell (Kyowa Dengyo Co., LCL-F), and the strain amount is measured with a dynamic strain measuring instrument (the same as DPM-611A).
Record on the recorder.

試験条件 平均気温:約25℃ アンモニア水量:25.78kg 投入前アンモニア水温度:23℃ 投入前アンモニア水濃度:29% ガス蒸発抑制剤投入量:8.42kg 投入抑制剤の被覆層厚:1cm 第1図は、上記試験で求めたアンモニアガス蒸発量線図
である。
Test conditions Average temperature: Approx. 25 ℃ Ammonia water amount: 25.78kg Ammonia water temperature before injection: 23 ℃ Ammonia water concentration before injection: 29% Gas evaporation inhibitor injection amount: 8.42kg Coating layer thickness of injection inhibitor: 1cm Fig. 1 [Fig. 3] is an ammonia gas evaporation amount diagram obtained in the above test.

この図から、本発明のガス蒸発抑制剤によるガス蒸発抑
制効果は明白である。
From this figure, the gas evaporation suppressing effect of the gas evaporation suppressing agent of the present invention is clear.

(第2実施例) 第1実施例と同じ流動パラフィンに末端基にカルボキシ
ル基の親水基を有するメタアクリル酸ポリマーを混合し
た場合の展開性の変化とメニスカスの変化をみる。
(Second Example) A change in developability and a change in meniscus when a methacrylic acid polymer having a carboxyl group as a hydrophilic group in a terminal group are mixed with the same liquid paraffin as in the first example will be examined.

容器に入れた29%アンモニア水の液面中央部に、流動パ
ラフィンに所定量のメタクリル酸ポリマーを混合してな
るガス蒸発抑制剤50mlをゆっくり流し込む。ガス蒸発抑
制剤はアンモニア水面上ほぼ真円を描いて浮遊するか
ら、その直径及び厚さをスケールで測定する。結果を表
1に示す。
Into the center of the liquid surface of 29% ammonia water in a container, slowly pour 50 ml of a gas evaporation inhibitor, which is a mixture of liquid paraffin and a predetermined amount of methacrylic acid polymer. Since the gas evaporation inhibitor floats in a nearly perfect circle on the surface of ammonia water, its diameter and thickness are measured on a scale. The results are shown in Table 1.

次いで、ガス蒸発抑制剤を50ml追加すると、アンモニア
水面のガス蒸発抑制剤は完全に容器壁に到達して、アン
モニア水面を密閉化してしまう。第2図は、この時のコ
ンクリート容器1と、アンモニア水2を覆ったガス蒸発
抑制剤3とのメニスカスの状態を示すもので、図中のA
はコンクリート壁に接しない場所の蒸発抑制剤の厚さを
表し、Bはコンクリート壁に接する場所の蒸発抑制剤の
厚さを表している。これらAとBとの寸法の変化をスケ
ールで測定する。その結果を表2に示す。
Next, when 50 ml of the gas evaporation inhibitor is added, the gas evaporation inhibitor on the ammonia water surface completely reaches the container wall and seals the ammonia water surface. FIG. 2 shows the state of the meniscus between the concrete container 1 and the gas evaporation inhibitor 3 covering the ammonia water 2 at this time.
Represents the thickness of the evaporation suppressor in a place not in contact with the concrete wall, and B represents the thickness of the evaporation suppressor in a place in contact with the concrete wall. The changes in the dimensions of A and B are measured on a scale. The results are shown in Table 2.

メタクリル酸ポリマーを僅かな量添加する事により、ガ
ス蒸発抑制剤の展開性が大きく向上している。これは、
親水性で且つガス蒸発抑制の主成分である流動パラフィ
ンとの相溶性を有するメタクリル酸ポリマーの作用で、
流動パラフィンとアンモニア水の間の界面張力が低下す
るためである。又コンクリートと蒸発抑制剤のメニスカ
スが改善されるのは、コンクリート側にある親水基(水
酸基)と親水基(カルボキシル基)を有するメタクリル
酸ポリマーとの親和性が良いことに起因するものであ
り、この添加で蒸発ガス密封性能が向上してガス蒸発抑
制剤の使用量を低減させることが出来る。
By adding a small amount of methacrylic acid polymer, the developability of the gas evaporation inhibitor is greatly improved. this is,
By the action of the methacrylic acid polymer, which is hydrophilic and compatible with liquid paraffin, which is the main component for suppressing gas evaporation,
This is because the interfacial tension between liquid paraffin and ammonia water is reduced. Further, the reason why the meniscus of the concrete and the evaporation inhibitor is improved is that the affinity of the methacrylic acid polymer having the hydrophilic group (hydroxyl group) and the hydrophilic group (carboxyl group) on the concrete side is good, With this addition, the evaporative gas sealing performance is improved and the amount of the gas evaporation inhibitor used can be reduced.

なお、その他の末端基に親水基を有した有機化合物も流
動性の展開性とメニスカスの変化が同様にみられた。
In addition, other organic compounds having a hydrophilic group at the terminal group also exhibited the same developability of fluidity and change of meniscus.

〔発明の効果〕 以上説明したように、本発明によれば、主成分が飽和炭
化水素からなるガス蒸発抑制剤で蒸発性液化ガスの液面
を覆うものであり、次の様な顕著な効果を得ることが出
来る。
[Effects of the Invention] As described above, according to the present invention, the liquid level of the evaporative liquefied gas is covered with the gas evaporation inhibitor whose main component is saturated hydrocarbon, and the following remarkable effects are obtained. Can be obtained.

漏洩した液の液面を完全に被覆し、長時間にわたって
ガス蒸発を抑制できる。しかも風で吹き飛ばされにく
く、且つ一端吹き寄せられても復元する。
The surface of the leaked liquid can be completely covered, and gas evaporation can be suppressed for a long time. Moreover, it is difficult to be blown away by the wind, and even if blown away, it will be restored.

飽和炭化水素は熱、光、化学薬品に不活性で長期間貯
蔵できる。
Saturated hydrocarbons are inert to heat, light and chemicals and can be stored for long periods.

又、金属に対する腐食性もなく保守、取扱が容易であ
る。
In addition, it is not corrosive to metals and is easy to maintain and handle.

漏洩した被処理液を時間をかけて処理する事が可能
で、安全に作業できる。
It is possible to process the leaked liquid to be processed over time and work safely.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明のガス蒸発抑制剤の効果を説明するアン
モニアガス蒸発量線図、第2図はコンクリートとガス蒸
発抑制剤とのメニスカスの変化を測定する方法を説明す
る図である。
FIG. 1 is an ammonia gas evaporation amount diagram for explaining the effect of the gas evaporation inhibitor of the present invention, and FIG. 2 is a diagram for explaining a method for measuring a change in meniscus between concrete and the gas evaporation inhibitor.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】一般式CnH2n+2で表され且つnが10〜46の
パラフィン系炭化水素と、一般式 で表され且つnが10〜46のナフテン系炭化水素とを混合
してなる流動パラフィンに、メタクリル酸ポリマー,ア
クリル酸ポリマー,ポリビニルアルコール,ポリアクリ
ルアミド,ポリエチレンイミン,ポリエチレンスルホン
酸の中から選ばれた一種又は二種以上の物質を混合して
なるガス蒸発抑制剤。
1. A paraffinic hydrocarbon represented by the general formula C n H 2n + 2 , where n is 10 to 46, and a general formula Which is selected from the group consisting of methacrylic acid polymer, acrylic acid polymer, polyvinyl alcohol, polyacrylamide, polyethyleneimine, and polyethylenesulfonic acid, in the liquid paraffin mixed with a naphthenic hydrocarbon represented by A gas evaporation inhibitor formed by mixing one or more substances.
【請求項2】請求項(1)記載のガス蒸発抑制剤で蒸発
性液化ガスの液面を覆うことを特徴とする蒸発性液化ガ
スの蒸発抑制方法。
2. A method for suppressing evaporation of liquefied volatile gas, which comprises covering the liquid surface of the liquefied volatile gas with the gas evaporation inhibitor according to claim 1.
JP2206003A 1990-08-03 1990-08-03 Evaporation suppressant and evaporation suppression method using the same Expired - Lifetime JPH0739572B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2206003A JPH0739572B2 (en) 1990-08-03 1990-08-03 Evaporation suppressant and evaporation suppression method using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2206003A JPH0739572B2 (en) 1990-08-03 1990-08-03 Evaporation suppressant and evaporation suppression method using the same

Publications (2)

Publication Number Publication Date
JPH0489882A JPH0489882A (en) 1992-03-24
JPH0739572B2 true JPH0739572B2 (en) 1995-05-01

Family

ID=16516300

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2206003A Expired - Lifetime JPH0739572B2 (en) 1990-08-03 1990-08-03 Evaporation suppressant and evaporation suppression method using the same

Country Status (1)

Country Link
JP (1) JPH0739572B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5948182B2 (en) * 2012-08-06 2016-07-06 藤倉化成株式会社 Pollutant scattering prevention material and pollutant scattering prevention method using the same
JP6831758B2 (en) * 2017-06-28 2021-02-17 株式会社豊田中央研究所 Smell sustained release agent and odor sustained release member

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5557272A (en) * 1978-10-25 1980-04-26 Shin Kobe Electric Mach Co Ltd Lead battery
JPS6117768A (en) * 1984-06-30 1986-01-25 Fuji Heavy Ind Ltd Lubricating device of four-wheel driving device for vehicle

Also Published As

Publication number Publication date
JPH0489882A (en) 1992-03-24

Similar Documents

Publication Publication Date Title
ES2140363T3 (en) METHOD FOR REHABILITATING AND / OR PROTECTIVE INHIBITION OF CORROSION OF REINFORCEMENT STEEL INCREASED IN A CONCRETE STRUCTURE HARDENED BY MEANS OF CORROSION INHIBITING COMPOSITIONS APPLIED ON THE SURFACE.
RU2643006C2 (en) Water-soluble inhibitor of corrosion for protection of operating pipes and pipelines for natural gas and also method of its obtaining
KR20040068144A (en) Fluorosurfactant-free foam fire-extinguisher
US2373570A (en) Noncorrosive liquids
EP1287855A1 (en) Fire-extinguishing chemical
Wachter Sodium Nitrite as Corrosion Inhibitor for Water.
JPH0739572B2 (en) Evaporation suppressant and evaporation suppression method using the same
CN102732894A (en) Low-temperature corrosion inhibitor
WO2005047402A1 (en) Method of corrosion prevention and anticorrosion material
UA117131C2 (en) Corrosion inhibitor for protection of crude oil extraction equipment, crude oil pipelines, and crude oil tanks as well as the method of its production
JP5789916B2 (en) Pitting corrosion inhibitor and pitting corrosion suppression method
JP2019077947A (en) Composition of vapor phase corrosion inhibitor, and use of the same and method for manufacturing the same
KR102200670B1 (en) Manufacturing method of Desiccant which has volatile corrosion inhibiting effect
KR100871532B1 (en) Volatile corrosion inhibitor liquid manufacturing method
US5853620A (en) Compositions and compounds to minimize hydrogen charging and hydrogen induced cracking of steels
JP7168176B1 (en) Method for removing chlorides from surface-conditioned steel structures
JP2002256466A (en) Corrosion inhibitor
US2768955A (en) Permanent anti-freeze liquid containing an anti-foam phase of a silicone in a mineral lubricating oil
JPS62116697A (en) Neutral detergent
JP7325040B2 (en) Method for producing volatile rust inhibitor and volatile rust inhibitor
JP3336087B2 (en) Absorption liquid composition for absorption refrigerator
JP2002256462A (en) Corrosion inhibitor
CN115029037A (en) Water-based anticorrosive paint and preparation method and application thereof
Miller et al. Corrosion mechanism of high lead solder and correlation to dissolved oxygen
CN115926569A (en) Coating and preparation method and application thereof

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

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

Free format text: PAYMENT UNTIL: 20090501

Year of fee payment: 14

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

Free format text: PAYMENT UNTIL: 20100501

Year of fee payment: 15

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

Free format text: PAYMENT UNTIL: 20110501

Year of fee payment: 16

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110501

Year of fee payment: 16