JPS6116480Y2 - - Google Patents

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Publication number
JPS6116480Y2
JPS6116480Y2 JP11981477U JP11981477U JPS6116480Y2 JP S6116480 Y2 JPS6116480 Y2 JP S6116480Y2 JP 11981477 U JP11981477 U JP 11981477U JP 11981477 U JP11981477 U JP 11981477U JP S6116480 Y2 JPS6116480 Y2 JP S6116480Y2
Authority
JP
Japan
Prior art keywords
gas
holder
outer tank
gas holder
water
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
Application number
JP11981477U
Other languages
Japanese (ja)
Other versions
JPS5445412U (en
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 filed Critical
Priority to JP11981477U priority Critical patent/JPS6116480Y2/ja
Publication of JPS5445412U publication Critical patent/JPS5445412U/ja
Application granted granted Critical
Publication of JPS6116480Y2 publication Critical patent/JPS6116480Y2/ja
Expired legal-status Critical Current

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  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Description

【考案の詳細な説明】 本考案は、有水式ガスホルダに対して適正収容
量を超えた貯蔵ガスが供給される場合に、余分の
ガスをホルダ外部へ安全に放散させるための装置
に関するものである。
[Detailed description of the invention] The present invention relates to a device for safely dissipating excess gas to the outside of a water-filled gas holder when stored gas exceeding the appropriate capacity is supplied to the holder. be.

転炉や高炉において発生するガスは、通常底面
を水封した有水式ガスホルダへ連続的に送られて
収容されており、一定の収容量を超えてもなおガ
スホルダへ送り込まれる場合は、余分の供給ガス
を外部へ放散させるようにしている。有水式ガス
ホルダの構成を第1図によつて説明すれば、ガス
ホルダ1は内槽11、中槽12、外槽13の3つ
の槽を組合せて成る伸縮可能の収容のタンクであ
つて、水槽2内に底部を開口して設けられ、底面
は水封されて内部にガスを収容するようになつて
いる。外槽の側面にはガイドローラ14が一体に
突設しており、これが水槽の縁部に沿つて垂設し
たガイド支柱3に係合され、これによつて前記ガ
スホルダ1が収容ガス量に対応して円滑に伸縮す
るようになつている。ガスホルダ1には、転炉4
などから送られるガスをホルダ内に導く供給パイ
プ5を設けてあるが、所定量以上のガスをホルダ
内へ供給すると外槽13の下部からガスが噴き出
したり、または水封部やホルダの天井部に多大の
トラブルを発生させることとなるので、余分なガ
スの供給を中止して外部へ放散させる必要があ
る。このため従来は第1図に示すように供給パイ
プ5の一部に分岐路51を設けると共に、これを
放散塔52に導いておき、内槽11が一定高さに
達したとき、レベル計がこれを検出して弁53,
54を同時に切換えて、余分のガスを放散させる
ようにしていた。このような従来装置において
は、内槽の最高高さは安全率を考慮して使用限界
の90%に設定していたため、利用効率が悪く、し
かも放散経路の設備装置が複雑となつてコスト高
となる欠点があつた。
The gas generated in converters and blast furnaces is normally continuously sent to and stored in a water-filled gas holder whose bottom is sealed with water.If the gas is still sent to the gas holder even after exceeding a certain capacity, excess The supplied gas is dissipated to the outside. The structure of the water-filled gas holder will be explained with reference to FIG. 1. The gas holder 1 is an expandable storage tank consisting of a combination of three tanks: an inner tank 11, a middle tank 12, and an outer tank 13. 2 with an open bottom, and the bottom is sealed with water to accommodate gas inside. A guide roller 14 is integrally protruded from the side surface of the outer tank, and is engaged with a guide column 3 vertically installed along the edge of the tank, whereby the gas holder 1 corresponds to the amount of gas accommodated. It is designed to expand and contract smoothly. The gas holder 1 has a converter 4
A supply pipe 5 is provided to guide gas into the holder, but if more than a predetermined amount of gas is supplied into the holder, the gas may blow out from the bottom of the outer tank 13, or from the water seal or the ceiling of the holder. Therefore, it is necessary to stop the supply of excess gas and dissipate it to the outside. For this reason, in the past, as shown in FIG. 1, a branch passage 51 was provided in a part of the supply pipe 5, and this was led to a diffusion tower 52, and when the inner tank 11 reached a certain height, a level meter was installed. Detecting this, the valve 53,
54 at the same time to dissipate excess gas. In such conventional equipment, the maximum height of the inner tank was set at 90% of the usage limit in consideration of the safety factor, which resulted in poor usage efficiency and complicated equipment for the emission path, resulting in high costs. There was a drawback.

本考案の目的は、これら従来の欠点を排除し、
ガスホルダを高効率で使用しうるようにした非常
放散装置を提供することにある。
The purpose of this invention is to eliminate these conventional drawbacks,
An object of the present invention is to provide an emergency dissipation device that allows a gas holder to be used with high efficiency.

本考案の非常放散装置は、ガスホルダ外槽下部
の浸水部分に該外槽の下端縁より上方であつて正
常貯蔵時における外槽内水位より下方の位置に穿
設した開口部と、前記開口部に対して下端が連通
接続してなる案内筒と、ガスホルダのガイド支柱
等に垂立固定され前記案内筒の上部を入子式に嵌
合連結するガス放散筒とで構成されている。
The emergency dissipation device of the present invention has an opening formed in the flooded part of the lower part of the outer tank of the gas holder at a position above the lower edge of the outer tank and below the water level in the outer tank during normal storage; The gas dissipation tube is composed of a guide tube whose lower end is connected in communication with the gas holder, and a gas dissipation tube which is vertically fixed to the guide column of the gas holder and connects the upper part of the guide tube in a telescopic manner.

本実施例の装置は、第2図に示すように供給パ
イプ5には特別の構成を設けることなく、ホルダ
1に対して設けてある。すなわち、ホルダ1の最
下段となる外槽13の下部浸水部分に、第4図に
示すような比較的穿設範囲の広いガス放出用の開
口6を設ける。この開口は外槽13の下端縁より
上方であつて正常貯蔵時における外槽13内の水
位より下方の位置、すなわちガスホルダ1に導入
されるガス量が例えば使用限界の98%に達したと
きに該ホルダ内に送り込まれる余分のガスをホル
ダ外部へ放出できるような位置に設けてあり、そ
の時の水面から開口までの距離dを算出して穿設
してある。
In the apparatus of this embodiment, as shown in FIG. 2, the supply pipe 5 is provided with respect to the holder 1 without any special structure. That is, in the lower submerged portion of the outer tank 13, which is the lowest stage of the holder 1, a gas discharge opening 6 having a relatively wide opening range is provided as shown in FIG. This opening is located above the lower edge of the outer tank 13 and below the water level in the outer tank 13 during normal storage, that is, when the amount of gas introduced into the gas holder 1 reaches, for example, 98% of the usage limit. It is provided at a position where excess gas fed into the holder can be discharged to the outside of the holder, and the hole is bored by calculating the distance d from the water surface to the opening.

前記開口6を設けた部分には案内筒61が連通
接続してあつて、該開口6から放出されるガスを
水槽2の上方へ導くようにしてあり、案内筒61
の上端は、ガイド支柱3に垂設固定された放散筒
62に対して入子式に嵌合させてある。案内筒6
1の嵌合部分はホルダ1の昇降変位に伴つてスラ
イドできるように係合されており、第3図に示す
ように、嵌合部分の長さHは、外槽13が最も高
い位置にある場合に、放散筒62と案内筒61を
ガスを外に噴出しない程度に嵌合代を確保させて
ある。
A guide tube 61 is connected in communication with the portion where the opening 6 is provided, and is configured to guide the gas released from the opening 6 to the upper side of the water tank 2.
The upper end of the guide column 3 is telescopically fitted into a radiation tube 62 which is vertically fixed to the guide column 3. Guide tube 6
The fitting portion 1 is engaged so as to be slidable as the holder 1 moves up and down, and as shown in FIG. 3, the length H of the fitting portion is such that the outer tank 13 is at the highest position In this case, the fitting allowance between the diffusion tube 62 and the guide tube 61 is ensured to the extent that the gas is not ejected to the outside.

放散筒62の先端には配管またはダクトを接続
し、安全な高所に導いて大気中へ放散させる。案
内筒及び放散筒の設置数は、発生するガス量やホ
ルダの容量等によつて異るものであり、そのケー
スに応じて算出決定する。放散量の算出側につい
ては次に示す。
A pipe or duct is connected to the distal end of the dissipation tube 62, and the dissipation tube is guided to a safe high place and dissipated into the atmosphere. The number of guide tubes and diffusion tubes to be installed varies depending on the amount of gas generated, the capacity of the holder, etc., and is calculated and determined depending on the case. The calculation side of the emission amount is explained below.

ホルダ容量 50.000m3 ホルダ内圧 300mmAq ガス密度 1.362Kg/Nm3 放出管断面積0.2m2の場合の圧力損失について
みれば、 1 外槽より流入の圧損 △P1=γ/2g(Q/A) =0.87×1.362/2×9.8×(Q/0.2)
=1.574Q2 2 吐出管の圧損(500φの直管として)
500φ=0.196m2 △P2=λ1/αγ/2g(Q/A) =0.02×30/0.5×1.362/2×9.8×
(Q/0.2) =2.085Q2 3 吐出部の圧損 △P3=γ/2g(Q/A) =1.362/2×9.8×(Q/0.2)=1.
737Q2 4 合計 △P=△P1+△P2+△P3=5.396Q2 =300mmAq したがつて設置本数は ガス発生量/放散量=120000m3/H/26.90
0m/N本=4.46となり5本の設 置が必要となる。
Holder capacity 50.000m 3Holder internal pressure 300mmAq Gas density 1.362Kg/Nm 3If we look at the pressure loss when the cross-sectional area of the discharge pipe is 0.2m2 , we have: 1 Pressure drop from the outer tank to the inflow △P 1 = γ/2g (Q/A) 2 = 0.87×1.362/2×9.8×(Q/0.2)
2 = 1.574Q 2 2 Pressure loss of discharge pipe (as a 500φ straight pipe)
500φ=0.196m 2 △P 2 = λ1/αγ/2g (Q/A) 2 = 0.02×30/0.5×1.362/2×9.8×
(Q/0.2) 2 = 2.085Q 2 3 Pressure loss at the discharge part △P 3 = γ/2g (Q/A) 2 = 1.362/2 x 9.8 x (Q/0.2) 2 = 1.
737Q 2 4 Total △P=△P 1 +△P 2 +△P 3 =5.396Q 2 =300mmAq Therefore, the number of installed gas generation amount/dissipation amount = 120000m 3 /H/26.90
0m/N lines = 4.46, so 5 lines need to be installed.

本考案による非常放散装置の設置により、ガス
噴出による中毒や火災の発生を防止できることは
当然であるが、ホルダの使用上限を98%にまで引
上げることが可能となつたため、ガスの回収量が
増加して利用効率が良好となつた。また装置自体
は簡単な構成であるので、多くの設備費用を必要
とせず、誤作動も生じにくいなど多くの利点を具
えている。
It goes without saying that by installing the emergency dissipation device of this invention, it is possible to prevent poisoning and fires caused by gas ejections, but since it has become possible to raise the upper limit of use of the holder to 98%, the amount of gas recovered can be reduced. This increased the utilization efficiency. Furthermore, since the device itself has a simple configuration, it does not require much equipment cost and has many advantages, such as being less likely to malfunction.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の非常放散手段を具えた有水式ガ
スホルダの側面視図。第2図は本考案の非常放散
装置を具えたガスホルダの側面視図。第3図は本
考案装置の構成を拡大して示す要部の断面図。第
4図は第3図の−方向からみた正面図。 1:ガスホルダ、11:内槽、12:中槽、1
3:外槽、2:水槽3:ガイド支柱、4:転炉、
5:供給パイプ、6:開口、61:案内筒、6
2:放散筒。
FIG. 1 is a side view of a water-type gas holder equipped with a conventional emergency dissipation means. FIG. 2 is a side view of a gas holder equipped with the emergency dissipation device of the present invention. FIG. 3 is an enlarged cross-sectional view of the main parts of the device according to the present invention. FIG. 4 is a front view seen from the - direction of FIG. 3. 1: Gas holder, 11: Inner tank, 12: Middle tank, 1
3: Outer tank, 2: Water tank 3: Guide support, 4: Converter,
5: Supply pipe, 6: Opening, 61: Guide tube, 6
2: Diffusion tube.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] ガスホルダ外槽下部の浸水部分に該外槽の下端
縁より上方であつて正常貯蔵時における外槽内水
位より下方の位置に穿設した開口部と、前記開口
部に対して下端が連通接続してなる案内筒と、ガ
スホルダのガイド支柱等に垂立固定され前記案内
筒の上部を入子式に嵌合連結するガス放散筒とか
ら成る有水式ガスホルダの非常放散装置。
An opening is formed in the flooded part of the lower part of the outer tank of the gas holder at a position above the lower edge of the outer tank and below the water level in the outer tank during normal storage, and the lower end is connected in communication with the opening. An emergency dissipation device for a water-type gas holder, which comprises a guide tube formed of a gas holder, and a gas dissipation tube that is vertically fixed to a guide column or the like of the gas holder and that fits and connects the upper part of the guide tube in a telescopic manner.
JP11981477U 1977-09-06 1977-09-06 Expired JPS6116480Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11981477U JPS6116480Y2 (en) 1977-09-06 1977-09-06

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11981477U JPS6116480Y2 (en) 1977-09-06 1977-09-06

Publications (2)

Publication Number Publication Date
JPS5445412U JPS5445412U (en) 1979-03-29
JPS6116480Y2 true JPS6116480Y2 (en) 1986-05-21

Family

ID=29075430

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11981477U Expired JPS6116480Y2 (en) 1977-09-06 1977-09-06

Country Status (1)

Country Link
JP (1) JPS6116480Y2 (en)

Also Published As

Publication number Publication date
JPS5445412U (en) 1979-03-29

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