JPH0515334Y2 - - Google Patents
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- Publication number
- JPH0515334Y2 JPH0515334Y2 JP10444786U JP10444786U JPH0515334Y2 JP H0515334 Y2 JPH0515334 Y2 JP H0515334Y2 JP 10444786 U JP10444786 U JP 10444786U JP 10444786 U JP10444786 U JP 10444786U JP H0515334 Y2 JPH0515334 Y2 JP H0515334Y2
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- Japan
- Prior art keywords
- pressure
- chemical liquid
- pump
- flow rate
- regulating valve
- Prior art date
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- Fire-Extinguishing By Fire Departments, And Fire-Extinguishing Equipment And Control Thereof (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
本考案は消防ポンプからの放水中に消火用泡剤
を均一割合で混合するための装置に関する。[Detailed Description of the Invention] (Industrial Field of Application) The present invention relates to a device for mixing fire extinguishing foam in a uniform proportion in water discharged from a fire pump.
(従来の技術)
火災の種類にもよるが、消防ポンプから消火用
水に消火泡剤を混入して放水する場合、泡剤(薬
液)を均等な割合で混合すべく、従来第2図に示
すような混合装置を用いていた。(Prior art) Although it depends on the type of fire, when a fire pump mixes fire extinguishing foam with fire extinguishing water and sprays it, the conventional technique shown in Figure 2 is to mix the foam (chemical solution) in an even ratio. A similar mixing device was used.
これは圧送自動比例混合方式と呼ばれるもの
で、図中1は消防ポンプ、2は放水用ターレツ
ト、3は泡剤となる薬液を収容する薬液槽、4は
薬液ポンプである。消防ポンプ1の駆動によりメ
イン配管5から消火用水が放水用ターレツト2に
圧送される。 This is called a pressure feed automatic proportional mixing system, and in the figure, 1 is a fire pump, 2 is a water turret, 3 is a chemical tank containing a chemical solution to be used as a foaming agent, and 4 is a chemical pump. By driving the fire pump 1, fire extinguishing water is pumped from the main pipe 5 to the water turret 2.
また薬液ポンプ4の駆動により薬液槽3からの
薬液が配管6により、高圧の消火用水が流れる前
記メイン配管5の途中に混合器7を介して圧送さ
れる。 Further, by driving the chemical liquid pump 4, the chemical liquid from the chemical liquid tank 3 is pumped through the pipe 6 through the mixer 7 into the main pipe 5 through which high-pressure fire extinguishing water flows.
両者の混合割合を一定にするために、混合器7
の各入口にオリフイスが設けられ、これら各オリ
フイスの上流側圧力が、パイロツト圧力として管
路9と10により、等圧弁(定差圧弁)11のダ
イヤフラムで画成された両室に導かれ、等圧弁1
1はこれらの圧力が等しくなるように配管6の薬
液圧力を調整する。 In order to keep the mixing ratio of both constant, mixer 7
An orifice is provided at each inlet of the orifice, and the upstream pressure of each orifice is guided as pilot pressure through pipes 9 and 10 to both chambers defined by the diaphragm of an equal pressure valve (constant differential pressure valve) 11, etc. Pressure valve 1
1 adjusts the chemical pressure in the pipe 6 so that these pressures become equal.
なお、実際の薬液混入時は弁12Aを閉じて弁
12Bを開き、配管6の薬液が等圧弁11の部分
を通過するようにする。 Note that when the chemical liquid is actually mixed, the valve 12A is closed and the valve 12B is opened so that the chemical liquid in the pipe 6 passes through the equal pressure valve 11.
混合器7に流入する消火用水と薬液の流量は、
各オリフイスの開口面積とその上流側圧力に比例
して変化し、オリフイス開度が一定ならば圧力が
高くなる程流量が増大する。したがつて両オリフ
イスの上流圧力を同一に維持すれば、流量比率は
オリフイス開度にのみ比例し、常に一定の混合割
合となる。 The flow rates of fire extinguishing water and chemical solution flowing into the mixer 7 are:
It changes in proportion to the opening area of each orifice and its upstream pressure, and if the orifice opening is constant, the flow rate increases as the pressure increases. Therefore, if the upstream pressures of both orifices are maintained the same, the flow rate ratio is proportional only to the opening degree of the orifices, and a constant mixing ratio is always maintained.
等圧弁11は各オリフイス上流の圧力を検出し
て、例えば薬液側の圧力が高いときはダイヤフラ
ムに連動して薬液配管6の開度を減少して圧力を
下げ、逆に低いときは開度を拡大して圧力を上げ
るのであり、このようにして両圧力を常に一致さ
せるように制御する。この結果、消火用水に対す
る薬液(泡剤)の混合割合が常に一定に調整され
る。 The equal pressure valve 11 detects the pressure upstream of each orifice, and for example, when the pressure on the chemical side is high, it operates in conjunction with the diaphragm to reduce the opening of the chemical liquid piping 6 to lower the pressure, and conversely, when the pressure is low, it reduces the opening. It expands and increases the pressure, and in this way it is controlled so that both pressures always match. As a result, the mixing ratio of the chemical solution (foam) to the fire extinguishing water is always adjusted to be constant.
なお、等圧弁11により常に一定の差圧を保つ
ように制御して、混合割合を一定に調整すること
もできる。 Note that the mixture ratio can also be adjusted to a constant value by controlling the equal pressure valve 11 to always maintain a constant differential pressure.
(考案が解決しようとする問題点)
しかしながらこの装置では、薬液配管6を消防
ポンプ1の吐出側、つまり二次側に接続している
ために、薬液の供給圧力を消防ポンプ1の吐出圧
力と一致するまで高める必要があつた。そのため
に薬液ポンプ4として高圧ポンプが必要となり、
薬液ポンプが非常に高価になつてしまう問題があ
つた。(Problem to be solved by the invention) However, in this device, since the chemical liquid piping 6 is connected to the discharge side of the fire pump 1, that is, the secondary side, the supply pressure of the chemical liquid is equal to the discharge pressure of the fire pump 1. I needed to increase it until it matched. Therefore, a high-pressure pump is required as the chemical pump 4.
There was a problem that chemical pumps became very expensive.
また混合器7にオリフイスを設けて流路を絞つ
ているため、圧力損失が大きく、ポンプ効率も低
下するという問題もあつた。 Further, since the mixer 7 is provided with an orifice to restrict the flow path, there is a problem in that the pressure loss is large and the pump efficiency is also reduced.
本考案はこのような問題を解決するために提案
されたもので、消防ポンプの吸込側に薬液を正確
に混入できるようにした装置を提供することを目
的とする。 The present invention was proposed in order to solve such problems, and its purpose is to provide a device that can accurately mix chemical liquid into the suction side of a fire pump.
(問題点を解決するための手段)
そこで本考案は、消防ポンプの吸込配管の途中
に薬液ポンプからの薬液配管を接続し、この薬液
配管の途中に圧力調整弁と可変オリフイスを直列
に介装し、前記圧力調整弁を消防ポンプの吐出配
管に設けた流量検出部の検出圧力と可変オリフイ
ス上流の圧力に応動する部材及びこの圧力応動部
材に連結した弁体とから構成し、前記ポンプ吐出
流量に比例して薬液混合量を制御するようにし
た。(Means for solving the problem) Therefore, the present invention connects the chemical liquid piping from the chemical liquid pump in the middle of the suction piping of the fire pump, and inserts a pressure regulating valve and a variable orifice in series in the middle of this chemical liquid piping. The pressure regulating valve is composed of a member that responds to the detected pressure of a flow rate detection section provided in the discharge piping of the fire pump and the pressure upstream of the variable orifice, and a valve body connected to this pressure responsive member, and the pressure regulating valve is configured to adjust the pump discharge flow rate. The amount of chemical liquid mixed is controlled in proportion to.
(作用)
したがつて消防ポンプの吸込側に薬液が混入さ
れるので、薬液の要求供給圧力が低く、また圧力
調整弁により通路圧力が変動しても、正確に混合
割合を制御することができる。(Function) Therefore, since the chemical liquid is mixed into the suction side of the fire pump, the required supply pressure of the chemical liquid is low, and even if the passage pressure fluctuates using the pressure regulating valve, the mixing ratio can be accurately controlled. .
(実施例)
以下本考案の実施例を第1図に従つて説明す
る。消火用水を圧送する消防ポンプ1の吸込配管
5Aの途中に薬液槽3からの薬液配管6が接続す
る。(Example) An example of the present invention will be described below with reference to FIG. A chemical liquid pipe 6 from a chemical liquid tank 3 is connected to the middle of a suction pipe 5A of a fire pump 1 that pumps fire extinguishing water.
消防ポンプ1に吐出配管5Bには放水用ターレ
ツト2が接続され、消火用水を放出する。 A water discharge turret 2 is connected to the discharge pipe 5B of the fire pump 1, and discharges fire extinguishing water.
前記薬液配管6の途中には増幅型の圧力調整弁
(バランスレギユレータ)15と、薬液の種類に
応じて混合割合を調整するための可変オリフイス
16が介装される。 An amplification type pressure regulating valve (balance regulator) 15 and a variable orifice 16 for adjusting the mixing ratio according to the type of chemical liquid are interposed in the middle of the chemical liquid piping 6.
圧力調整弁15は大小受圧面積の異なる2つの
第1、第2ダイヤフラム装置17,18を備えて
おり、両ダイヤフラム17Aと18Aとを連結す
るロツド19の途中に調整弁体20が一体に取付
けられ、ロツド19の変位に伴つて弁開度が増減
変化するようになつている。 The pressure regulating valve 15 is equipped with two first and second diaphragm devices 17 and 18 having different sizes and pressure receiving areas, and a regulating valve body 20 is integrally attached in the middle of a rod 19 that connects both diaphragms 17A and 18A. , the valve opening degree increases or decreases as the rod 19 is displaced.
消防ポンプ1の吐出配管5Bの途中には流量検
出部21が設けられ、この流量検出部21はピト
ー管による動圧検出部22と静圧検出部23から
なり、それぞれ検出圧力は管路22Aと23Aを
介して第1のダイヤフラム装置17のダイヤフラ
ム17Aの両面に導かれる。したがつてダイヤフ
ラム17Aはこれらの差圧、つまり吐出配管5B
を流れる流量に比例して変位する。なお、24は
圧力計を示す。 A flow rate detection section 21 is provided in the middle of the discharge piping 5B of the fire pump 1, and this flow rate detection section 21 consists of a dynamic pressure detection section 22 and a static pressure detection section 23 using pitot tubes, and the detected pressure is determined by the pipe line 22A and the static pressure detection section 23, respectively. 23A to both sides of the diaphragm 17A of the first diaphragm device 17. Therefore, the diaphragm 17A handles these differential pressures, that is, the discharge pipe 5B.
displacement in proportion to the flow rate. Note that 24 indicates a pressure gauge.
次ぎに第2のダイヤフラム装置18のダイヤフ
ラム18Aには、圧力調整弁15の下流でかつ可
変オリフイス16の上流の薬液圧力が導かれ、こ
の圧力に応じてダイヤフラム18Aが変位する。 Next, the chemical pressure downstream of the pressure regulating valve 15 and upstream of the variable orifice 16 is introduced to the diaphragm 18A of the second diaphragm device 18, and the diaphragm 18A is displaced in accordance with this pressure.
したがつて前記ロツド19は、これらダイヤフ
ラム17Aと18Aとがバランスする位置まで上
下に移動し、これに応じて圧力調整弁15の開度
が変化する。 Therefore, the rod 19 moves up and down to a position where these diaphragms 17A and 18A are balanced, and the opening degree of the pressure regulating valve 15 changes accordingly.
なお、25は圧力調整用のスプリング、26は
圧力計である。 In addition, 25 is a spring for pressure adjustment, and 26 is a pressure gauge.
前記可変オリフイス16の下流には、逆止弁2
7が介装され、消防ポンプ1の駆動停止時に吸込
配管5Aを自然落下していく消火用水により生じ
る負圧で、薬液が吸引されるのを防止する(した
がつて、この逆止弁27のクラツキング圧力は最
大でも大気圧に相当する1Kg/cm2)。 A check valve 2 is provided downstream of the variable orifice 16.
7 is interposed to prevent the chemical liquid from being sucked in by the negative pressure generated by the fire extinguishing water that naturally falls down the suction pipe 5A when the fire pump 1 stops driving (therefore, this check valve 27 The maximum cracking pressure is 1Kg/cm 2 , which is equivalent to atmospheric pressure.
以上のように構成されており、次ぎに作用につ
いて説明する。 The structure is as described above, and the operation will be explained next.
消防ポンプ1の駆動に伴い図示しない貯水槽な
どから消火用水が吸込配管5Aに汲み上げられ、
吐出配管5Bから放水用ターレツト(放水銃)2
へと圧送される。 As the fire pump 1 is driven, fire extinguishing water is pumped up from a water tank (not shown) to the suction pipe 5A,
Water turret (water cannon) 2 from discharge pipe 5B
be pumped to.
一方薬液ポンプ4の駆動により圧力調整弁15
から可変オリフイス16を経由して薬液が低圧
(負圧)の吸込配管5Aに送り込まれる。 On the other hand, the pressure regulating valve 15 is driven by the chemical pump 4.
From there, the chemical liquid is fed into the low pressure (negative pressure) suction pipe 5A via the variable orifice 16.
したがつて消火用水と共に薬液(泡剤)が消防
ポンプ1に吸い込まれ、互いに混合しながら前記
放水用ターレツト2に圧送される。 Therefore, a chemical solution (foam) is sucked into the fire pump 1 together with the fire extinguishing water, and is pumped to the water discharge turret 2 while being mixed with each other.
消火用水に混合される薬液の割合は、圧力調整
弁15によつて決まる圧力と、可変オリフイス1
6の開度に応じて変化する。 The ratio of the chemical solution mixed into the fire extinguishing water is determined by the pressure determined by the pressure regulating valve 15 and the variable orifice 1.
It changes depending on the opening degree of 6.
そこで混入する薬液の種類に応じて可変オリフ
イス16の開度を設定し、圧力調整弁15の初期
圧力をスプリング25に調整することにより、消
火用水に対する混合割合を設定する。 The opening degree of the variable orifice 16 is set according to the type of chemical liquid to be mixed, and the initial pressure of the pressure regulating valve 15 is adjusted by the spring 25, thereby setting the mixing ratio for the fire extinguishing water.
放水用ターレツト2からの放水量は、例えば消
防ポンプ1の回転数等により必要に応じて適切な
値に設定される。 The amount of water discharged from the water discharge turret 2 is set to an appropriate value as necessary, for example, depending on the rotational speed of the fire pump 1 and the like.
このようにして一定の流量が放水用ターレツト
2に供給されているとすると、流量検出部21に
より検出部22と23との差圧は一定になるた
め、第1のダイヤフラム17Aはその位置に静止
し、したがつてロツド19も動かず、圧力調整弁
15の開度は一定値を維持しようとする。このた
め、薬液ポンプ4から送り込まれる薬液圧力が変
化しない限り、可変オリフイス16を通過する薬
液流量も変わらず、消火用水に対する薬液の混合
割合もオリフイス開度に応じて一定に制御され
る。 Assuming that a constant flow rate is supplied to the water turret 2 in this way, the flow rate detection unit 21 makes the differential pressure between the detection units 22 and 23 constant, so the first diaphragm 17A remains stationary at that position. However, the rod 19 also does not move, and the opening degree of the pressure regulating valve 15 attempts to maintain a constant value. Therefore, as long as the pressure of the chemical liquid sent from the chemical pump 4 does not change, the flow rate of the chemical liquid passing through the variable orifice 16 does not change, and the mixing ratio of the chemical liquid to the fire extinguishing water is also controlled to be constant according to the opening degree of the orifice.
これに対して、放水流量が変化しないのに、例
えば薬液ポンプ4の吐出圧力が低下したとする
と、可変オリフイス16の手前の圧力も相対的に
下がり、通過流量が減少して薬液の混合割合が低
下しようとする。 On the other hand, if, for example, the discharge pressure of the chemical liquid pump 4 decreases even though the discharge flow rate does not change, the pressure in front of the variable orifice 16 will also decrease relatively, the passing flow rate will decrease, and the mixing ratio of the chemical liquid will decrease. Trying to go down.
しかし、この薬液吐出圧力の低下に伴い第2の
ダイヤフラム18Aに作用する圧力が低下し、こ
のため第1のダイヤフラム17Aとのバランスが
崩れて、ダイヤフラムは上方につり合いが取れる
位置まで上昇する。したがつて圧力調整弁15の
開度が増大し、圧力調整弁15での圧力降下分を
少なくするため、可変オリフイス16の上流圧力
が回復する。 However, as the chemical liquid discharge pressure decreases, the pressure acting on the second diaphragm 18A decreases, and as a result, the balance with the first diaphragm 17A is lost, and the diaphragm rises upward to a balanced position. Therefore, the opening degree of the pressure regulating valve 15 increases, and in order to reduce the pressure drop at the pressure regulating valve 15, the upstream pressure of the variable orifice 16 is restored.
この結果、薬液の混合割合の減少が防止され、
可変オリフイス16によつて設定された所定の混
合割合を維持することができる。 As a result, a decrease in the mixing ratio of the chemical solution is prevented,
A predetermined mixing ratio set by variable orifice 16 can be maintained.
また、これとは逆に薬液ポンプ4の吐出圧力が
上昇したときは、圧力調整弁15の開度が小さく
なり、薬液の混合割合が増大するのを防止する。 Conversely, when the discharge pressure of the chemical liquid pump 4 increases, the opening degree of the pressure regulating valve 15 becomes smaller, thereby preventing the mixing ratio of the chemical liquid from increasing.
一方、放水流量を増加させる場合、消防ポンプ
1から吐出流量(消火用水と薬液との混合液)が
増加すると、流量検出部21の検出差圧が大きく
なり、第1のダイヤフラム17Aが図中上方に変
位しようとする。 On the other hand, when increasing the water discharge flow rate, when the discharge flow rate (mixture of fire extinguishing water and chemical solution) from the fire pump 1 increases, the differential pressure detected by the flow rate detection unit 21 increases, and the first diaphragm 17A moves upward in the figure. attempt to displace it.
ダイヤフラム17Aの上方への移動に伴いロツ
ド19を介して弁体20も引き上げられ、圧力調
整弁15の開度が増加する。このため可変オリフ
イス16の上流側の圧力が高まり、可変オリフイ
ス16を通過する薬液流量も増加する。 As the diaphragm 17A moves upward, the valve body 20 is also pulled up via the rod 19, and the opening degree of the pressure regulating valve 15 increases. Therefore, the pressure on the upstream side of the variable orifice 16 increases, and the flow rate of the chemical solution passing through the variable orifice 16 also increases.
ただし、この圧力は第2のダイヤフラム18A
にも作用し、圧力の上昇に応じてダイヤフラム1
8Aを下方に移動、つまり増加した圧力調整弁1
5の開度を元の方向、つまり減少方向に変位させ
ようとするため、ダイヤフラム17Aと18Aに
は、それぞれに作用する圧力とダイヤフラム面積
比に比例した駆動力が働き、両者がバランスする
位置へと変位し、結局、両ダイヤフラム17Aと
18Aとに作用する圧力比が一定になるように、
圧力調整弁15の開度を制御する。 However, this pressure is applied to the second diaphragm 18A.
diaphragm 1 as the pressure increases.
8A moved downward, that is, increased pressure regulating valve 1
5 in the original direction, that is, in the decreasing direction, a driving force proportional to the pressure acting on each diaphragm and the diaphragm area ratio acts on the diaphragms 17A and 18A, and the two move to a balanced position. so that the pressure ratio acting on both diaphragms 17A and 18A becomes constant.
The opening degree of the pressure regulating valve 15 is controlled.
この結果、全体流量が増加すると、これに対応
して薬液流量も増えるのであるが、増加割合が全
体流量に比例するため、結局消火用水に対する薬
液の割合は最初に設定した一定の値を維持する。 As a result, when the overall flow rate increases, the chemical solution flow rate also increases, but since the rate of increase is proportional to the overall flow rate, the ratio of chemical solution to fire extinguishing water remains at the initially set value. .
このようにして常に薬液の混合割合を正確に目
標値に維持することができるのである。 In this way, the mixing ratio of the chemical solution can always be maintained accurately at the target value.
他方、薬液の混入は消防ポンプ1の吸込側、つ
まり低圧側で行なわれるために、薬液ポンプ4は
高圧ポンプとする必要がなく、逆止弁27のクラ
ツキング圧力(1Kg/cm2)に打ち勝つだけの吐出
圧力を発生すればよく、小型で安価なもので済
む。 On the other hand, since the chemical liquid is mixed in on the suction side, that is, the low pressure side, of the fire pump 1, the chemical liquid pump 4 does not need to be a high pressure pump, and only needs to overcome the cracking pressure (1 Kg/cm 2 ) of the check valve 27. It is sufficient to generate a discharge pressure of
また消防ポンプ1の吐出側の流量検出部21に
は、従来のようなオリフイスが必要なく、したが
つて圧力損失も少ない。 Further, the flow rate detection section 21 on the discharge side of the fire pump 1 does not require an orifice like the conventional one, and therefore there is little pressure loss.
(考案の効果)
以上のように本考案によれば、消防ポンプの吸
込配管の途中に薬液ポンプからの薬液配管を接続
し、この薬液配管の途中に圧力調整弁と可変オリ
フイスを直列に介装し、消防ポンプの吸込側に薬
液を混入するようにしたので、薬液の要求供給圧
力が低く、薬液ポンプを低圧型の安価なものとす
ることができ、また圧力調整弁は消防ポンプの吐
出配管に設けた流量検出部の検出圧力と可変オリ
フイス上流の圧力に応動してポンプ吐出流量に比
例して薬液混合量を制御するようにしたため、薬
液供給圧力や消防ポンプの吐出量が変動しても、
正確に混合割合を制御することができる。(Effect of the invention) As described above, according to the invention, the chemical liquid piping from the chemical liquid pump is connected in the middle of the suction piping of the fire pump, and the pressure regulating valve and the variable orifice are interposed in series in the middle of this chemical liquid piping. However, since the chemical liquid is mixed into the suction side of the fire pump, the required supply pressure of the chemical liquid is low, and the chemical liquid pump can be made into a low-pressure, inexpensive type. Since the chemical liquid mixture amount is controlled in proportion to the pump discharge flow rate in response to the detected pressure of the flow rate detection unit installed at ,
The mixing ratio can be precisely controlled.
第1図は本考案の実施例を示す回路構成図、第
2図は従来例の回路構成図である。
1……消防ポンプ、2……放水用ターレツト、
3……薬液槽、4……薬液ポンプ、5A……吸込
配管、5B……吐出配管、6……薬液配管、15
……圧力調整弁、16……可変オリフイス、1
7,18……ダイヤフラム装置、19……ロツ
ド、21……流量検出部。
FIG. 1 is a circuit configuration diagram showing an embodiment of the present invention, and FIG. 2 is a circuit configuration diagram of a conventional example. 1...Fire pump, 2...Water turret,
3... Chemical liquid tank, 4... Chemical liquid pump, 5A... Suction piping, 5B... Discharge piping, 6... Chemical liquid piping, 15
...Pressure regulating valve, 16...Variable orifice, 1
7, 18...Diaphragm device, 19...Rod, 21...Flow rate detection section.
Claims (1)
の薬液配管を接続し、この薬液配管の途中に圧力
調整弁と可変オリフイスを直列に介装し、前記圧
力調整弁を消防ポンプの吐出配管に設けた流量検
出部の検出圧力と可変オリフイス上流の圧力に応
動する部材及びこの圧力応動部材に連結した弁体
とから構成し、前記ポンプ吐出流量に比例して薬
液混合量を制御するようにしたことを特徴とする
消防用泡剤混合装置。 A chemical liquid pipe from a chemical liquid pump is connected in the middle of the suction pipe of the fire pump, a pressure regulating valve and a variable orifice are interposed in series in the middle of this chemical liquid piping, and the pressure regulating valve is provided in the discharge pipe of the fire pump. It is composed of a member that responds to the detected pressure of the flow rate detection unit and the pressure upstream of the variable orifice, and a valve body connected to this pressure responsive member, and controls the amount of mixed chemical liquid in proportion to the pump discharge flow rate. Characteristic firefighting foam mixing device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10444786U JPH0515334Y2 (en) | 1986-07-08 | 1986-07-08 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10444786U JPH0515334Y2 (en) | 1986-07-08 | 1986-07-08 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6311056U JPS6311056U (en) | 1988-01-25 |
JPH0515334Y2 true JPH0515334Y2 (en) | 1993-04-22 |
Family
ID=30977953
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10444786U Expired - Lifetime JPH0515334Y2 (en) | 1986-07-08 | 1986-07-08 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0515334Y2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020035938A (en) * | 2000-11-07 | 2002-05-16 | 배득희 | super chemical fire engine water and foam system |
KR100437074B1 (en) * | 2001-10-19 | 2004-06-23 | 홍영기 | foam injection apparatus for fire fighting |
KR100436698B1 (en) * | 2001-10-19 | 2004-06-22 | 주식회사 우리특장 | Form proportioning apparatus of a fire engine |
-
1986
- 1986-07-08 JP JP10444786U patent/JPH0515334Y2/ja not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS6311056U (en) | 1988-01-25 |
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