JP2003144881A - Gas-liquid mixing apparatus - Google Patents

Gas-liquid mixing apparatus

Info

Publication number
JP2003144881A
JP2003144881A JP2001344399A JP2001344399A JP2003144881A JP 2003144881 A JP2003144881 A JP 2003144881A JP 2001344399 A JP2001344399 A JP 2001344399A JP 2001344399 A JP2001344399 A JP 2001344399A JP 2003144881 A JP2003144881 A JP 2003144881A
Authority
JP
Japan
Prior art keywords
air
gas
liquid mixing
pressure
sewage
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.)
Pending
Application number
JP2001344399A
Other languages
Japanese (ja)
Inventor
Yukihiro Yamamoto
幸広 山本
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP2001344399A priority Critical patent/JP2003144881A/en
Publication of JP2003144881A publication Critical patent/JP2003144881A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a gas-liquid mixing apparatus which can inject air into, for example, the sewage pressure-feeding pipeline of an air injection type sewage pressure-feeding system while reducing running cost. SOLUTION: The primary side 4A outlet of the sewage pressure-feeding pipeline 4 is connected to the one end side in the direction of the axis line C of a gas-liquid mixing rotation tank 14 by making to have a tangential direction or a direction near a tangent line, and the secondary side 4B inlet of the pipeline 4 is connected to the other end part side. An air suction pipe 15 provided with a plurality of air discharge ports 15A is airtightly inserted into the axial center part of the tank 14, and the outside edge opening part 15C of the pipe 15 is opened to air. A direct advance flow of sewage introduced into the tank 14 is converted into a circular flow S along the inner surface of the peripheral wall 14C of the tank 14, and is discharged to the secondary side 4B. Thereby, a negative pressure part is formed at the outer peripheral part of an air suction pipe 15, the air is injected into the tank 14 by using a pressure difference between atmospheric pressure and the negative pressure part, and the air is mixed with the sewage.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、液体流に空気を混
合する気液混合装置に係り、たとえば、空気注入式汚水
圧送システムに好適な気液混合装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas-liquid mixing device for mixing air into a liquid stream, and more particularly to a gas-liquid mixing device suitable for an air injection type sewage pumping system.

【0002】[0002]

【従来の技術】従来より、図4に示す汚水圧送システム
が知られている。このシステムは、ポンプ井1内の汚水
2を圧送する汚水圧送ポンプ3と、汚水圧送管路4とを
備えている。
2. Description of the Related Art Conventionally, a sewage pumping system shown in FIG. 4 has been known. This system is provided with a sewage pump 3 for pumping sewage 2 in a pump well 1 and a sewage pumping line 4.

【0003】ところが、前記構成の汚水圧送システムに
よれば、汚水圧送管路4で汚水が長時間滞留すると、管
内が嫌気状態になって硫化物が生成され、悪臭の発生や
汚水圧送管路4を腐食させる原因になる。
However, according to the sewage pumping system having the above structure, when sewage stays in the sewage pumping line 4 for a long time, the inside of the pipe becomes anaerobic and sulfides are generated, and a bad odor is generated and the sewage pumping line 4 is generated. Cause corrosion.

【0004】このような、悪臭の発生や汚水圧送管路4
を腐食させる原因になる硫化物の生成を抑える汚水圧送
システムとして、たとえば、図5に示す空気注入式汚水
圧送システムが提供されている。このシステムは、ポン
プ井1内の汚水2を圧送する汚水圧送ポンプ3と、汚水
圧送管路4と、空気注入系5とを備え、汚水圧送管路4
は、その上流側に逆止弁6や流量計7などを直列で介設
して汚水圧送ポンプ3の吐出口に接続され、空気注入系
5は、エアーコンプレッサー8と、蓄圧タンク9、減圧
弁10、流量計11、流量調整弁12、逆止弁12Aな
どを直列に介設して、エアーコンプレッサー8を汚水圧
送管路4に接続した空気注入管5Aとを備えている。
[0004] Such an offensive odor and sewage pressure feeding pipeline 4
As a sewage pumping system that suppresses the formation of sulfides that cause corrosion of water, for example, an air injection type sewage pumping system shown in FIG. 5 is provided. This system is provided with a sewage pump 3 for pumping sewage 2 in a pump well 1, a sewage pumping line 4, and an air injection system 5, and has a sewage pumping line 4
Is connected to the discharge port of the sewage pump 3 through a check valve 6 and a flow meter 7 connected in series on the upstream side thereof. The air injection system 5 includes an air compressor 8, a pressure accumulator tank 9, and a pressure reducing valve. An air injection pipe 5A in which an air compressor 8 is connected to the sewage pressure feed pipe line 4 is provided with 10, a flow meter 11, a flow rate adjusting valve 12, a check valve 12A, and the like interposed in series.

【0005】前記構成の空気注入式汚水圧送システムに
よれば、空気注入系5によって汚水圧送管路4内に空気
を注入して曝気することにより、管内を好気状態にして
硫化物の生成を抑えて、悪臭の発生や汚水圧送管路4の
腐食を防止することができる。
According to the air-injection type sewage pumping system having the above-mentioned structure, by injecting air into the sewage pumping line 4 by the air injection system 5 to aerate the pipe, the inside of the pipe is aerobicized to generate sulfide. It is possible to suppress the generation of a bad odor and the corrosion of the sewage pressure-feeding pipeline 4 by suppressing.

【0006】[0006]

【発明が解決しようとする課題】ところが、この前記従
来の空気注入式汚水圧送システムでは、空気注入系5か
ら高圧の空気を汚水圧送管路4に導入する必要があるの
で、通常は、エアーコンプレッサー8の高出力連続運転
で汚水圧送管路4内に空気を注入している。このため、
エアーコンプレッサー8の消費電力が大きくなって、ラ
ンニングコストが高くなる欠点を有している。
However, in this conventional air-injection type sewage pumping system, since it is necessary to introduce high-pressure air from the air injection system 5 into the sewage pumping line 4, normally, an air compressor is used. In the high-power continuous operation of No. 8, air is injected into the wastewater pressure-feeding pipeline 4. For this reason,
The air compressor 8 consumes a large amount of power and has a drawback of increasing running costs.

【0007】本発明は、このような事情に鑑みてなされ
たもので、ランニングコストを削減して、たとえば、空
気注入式汚水圧送システムの汚水圧送管路に対して空気
を注入することができる気液混合装置を提供することを
目的としている。
The present invention has been made in view of the above circumstances, and it is possible to reduce the running cost and inject air into, for example, the sewage pumping line of the air injection type sewage pumping system. An object is to provide a liquid mixing device.

【0008】[0008]

【課題を解決するための手段】前記目的を達成するため
に、請求項1に記載の発明に係る気液混合装置は、液体
圧送管路内を圧送される液体に空気を混合させる気液混
合装置であって、前記液体圧送管路の一次側から導入し
た液体の直進流を周壁内面に沿う旋回流に変換して前記
液体圧送管路の二次側に吐出する筒状の気液混合旋回槽
と、この気液混合旋回槽の軸線方向にのびて該気液混合
旋回槽の軸心部に挿入されているとともに、外端開口部
を気液混合旋回槽の外部で大気に開放した空気吸入管と
を備え、この空気吸入管の管壁に複数個の空気吐出口が
設けられていることを特徴としている。
In order to achieve the above object, the gas-liquid mixing device according to the invention of claim 1 is a gas-liquid mixing device in which air is mixed with the liquid pumped in the liquid pumping line. In the device, a cylindrical gas-liquid mixing swirl for converting a straight flow of the liquid introduced from the primary side of the liquid pressure feeding pipeline into a swirling flow along the inner surface of the peripheral wall and discharging the swirling flow to the secondary side of the liquid pressure feeding pipeline. A tank and air which extends in the axial direction of the gas-liquid mixing swirl tank and is inserted into the axial center of the gas-liquid mixing swirl tank, and whose outer end opening is open to the atmosphere outside the gas-liquid mixing swirl tank. The air suction pipe is provided with a plurality of air discharge ports on the wall of the air suction pipe.

【0009】また、請求項2に記載の発明のように、空
気吸入管に空気注入系を接続してもよい。
Further, as in the second aspect of the invention, an air injection system may be connected to the air suction pipe.

【0010】請求項1に記載の発明によれば、液体圧送
管路の一次側から気液混合旋回槽に導入された液体の直
進流は、気液混合旋回槽の壁内面に沿う旋回流に変換し
て液体圧送管路の二次側に吐出されることで、気液混合
旋回槽の軸心部およびその外周付近に負圧部が形成され
る。空気吸入管は気液混合旋回槽の軸心部に挿入されて
いるので、前記負圧部は空気吸入管の管壁に設けた複数
個の空気吐出口と空気吸入管の外端開口部を介して大気
に連通する。したがって、大気圧と負圧部との圧力差に
より空気吸入管を通して空気を気液混合旋回槽内に吸込
み、気液混合旋回槽内で気液混合して液体圧送管路の二
次側に気液混合流体として吐出することができる。
According to the first aspect of the invention, the straight flow of the liquid introduced into the gas-liquid mixing swirl tank from the primary side of the liquid pressure-feeding conduit becomes a swirl flow along the inner surface of the wall of the gas-liquid mixing swirl tank. By converting and discharging the liquid to the secondary side of the liquid pressure feeding conduit, a negative pressure portion is formed in the vicinity of the axial center of the gas-liquid mixing swirl tank and its outer periphery. Since the air suction pipe is inserted into the axial center of the gas-liquid mixing swirl tank, the negative pressure portion has a plurality of air discharge ports provided on the pipe wall of the air suction pipe and an outer end opening of the air suction pipe. Through the atmosphere. Therefore, due to the pressure difference between the atmospheric pressure and the negative pressure portion, air is sucked into the gas-liquid mixing swirl tank through the air suction pipe, the gas-liquid is mixed in the gas-liquid mixing swirl tank, and the air is sucked to the secondary side of the liquid pressure feeding pipeline. It can be discharged as a liquid mixed fluid.

【0011】空気吸入管に空気注入系を接続すること
で、空気注入系の空気注入能力を低く抑えることができ
る。
By connecting the air injection system to the air suction pipe, the air injection capacity of the air injection system can be suppressed low.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1は本発明の第1実施の形態を
示す構成図である。なお、前記図4および図5で説明し
た従来例と同一もしくは相当部分には、同一符号を付し
て、これらの重複した構造の説明および作用の説明は省
略する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram showing a first embodiment of the present invention. The same or corresponding parts as those of the conventional example described with reference to FIGS. 4 and 5 are designated by the same reference numerals, and the description of the overlapping structure and the description of the operation will be omitted.

【0013】図1および図2において、気液混合装置1
3は、気液混合旋回槽14と、空気吸入管15とを備え
ている。気液混合旋回槽14は、軸線C方向の両端部を
閉塞板14A,14Bによって気密に閉塞した円筒状の
もで、その周壁部14Cにおける軸線C方向一端部側の
閉塞板14Aに付近に、接線方向または接線に近い方向
を有して、汚水圧送管路4における一次側4Aの出口を
接続するとともに、周壁部14Cにおける軸線C方向他
端部側の閉塞板14Bに付近に、接線方向または接線に
近い方向を有して、汚水圧送管路4における二次側4B
の入口を接続してある。なお、汚水圧送管路4における
一次側4Aの上流端部は、図5に示すように、汚水圧送
ポンプ3の吐出口に接続され、汚水圧送ポンプ3の吸込
口は汚水2を貯留したポンプ井2に接続される。
In FIGS. 1 and 2, a gas-liquid mixing device 1
3 includes a gas-liquid mixing swirl tank 14 and an air suction pipe 15. The gas-liquid mixing swirl tank 14 has a cylindrical shape in which both end portions in the axis C direction are airtightly closed by the closing plates 14A and 14B, and the peripheral wall portion 14C is provided near the closing plate 14A on the one end side in the axis C direction. It has a tangential direction or a direction close to the tangential line, connects the outlet of the primary side 4A in the wastewater pressure-feeding pipeline 4, and near the closing plate 14B on the other end side in the axial line C direction of the peripheral wall portion 14C, in the tangential direction or Secondary side 4B in the sewage pumping pipeline 4 having a direction close to the tangent line
The entrance of is connected. In addition, the upstream end of the primary side 4A in the sewage pumping pipeline 4 is connected to the discharge port of the sewage pump 3 as shown in FIG. 5, and the suction port of the sewage pump 3 is a pump well that stores the sewage 2. Connected to 2.

【0014】一方、空気吸入管15には、その管壁を貫
通して複数個の空気吐出口15A,15A…が設けら
れ、軸線C方向の内端部が閉塞板15Bによって気密に
閉塞されている。この空気吸入管15は、液混合旋回槽
14の閉塞板14Aを気密に貫通して該気液混合旋回槽
14の軸心部に挿入され、その外端開口部15Cは気液
混合旋回槽14の外部で大気に開放されているととも
に、外端開口部15Bの直下流位置に矢印Aで示す空気
の吸入流れを許容し、かつ反矢印A方向の流れを遮断す
る逆止弁16が介設されている。
On the other hand, the air suction pipe 15 is provided with a plurality of air discharge ports 15A, 15A ... Penetrating the pipe wall, and the inner end portion in the direction of the axis C is airtightly closed by a closing plate 15B. There is. The air suction pipe 15 penetrates the closing plate 14A of the liquid mixing swirl tank 14 in an airtight manner and is inserted into the axial center part of the gas liquid mixing swirl tank 14, and the outer end opening 15C is provided in the gas liquid mixing swirl tank 14. A check valve 16 that is open to the outside of the air and that allows the intake flow of air indicated by the arrow A and blocks the flow in the direction opposite to the arrow A is provided directly downstream of the outer end opening 15B. Has been done.

【0015】このような構成であれば、汚水圧送管路4
の一次側4Aから気液混合旋回槽14に導入された汚水
2の直進流は、気液混合旋回槽14における周壁14C
の内面に沿う旋回流Sに変換して液体圧送管路4の二次
側4Bに吐出される。このように、汚水が周壁14Cの
内面に沿って旋回することで、気液混合旋回槽14の軸
心部およびその外周付近の圧力、つまり気液混合旋回槽
14に挿入されている空気吸入管15の外周部の圧力が
気液混合旋回槽14の周壁14C側の圧力よりも低くな
って、空気吸入管15の外周部に負圧部が形成される。
With such a structure, the sewage pumping line 4
The straight flow of the sewage 2 introduced into the gas-liquid mixing swirl tank 14 from the primary side 4A is the peripheral wall 14C in the gas-liquid mixing swirl tank 14.
Is converted into a swirling flow S along the inner surface of the liquid and is discharged to the secondary side 4B of the liquid pressure-feeding conduit 4. In this way, the sewage swirls along the inner surface of the peripheral wall 14C, so that the pressure near the axial center of the gas-liquid mixing swirl tank 14 and its outer periphery, that is, the air suction pipe inserted into the gas-liquid mixing swirl tank 14 The pressure of the outer peripheral part of 15 becomes lower than the pressure of the peripheral wall 14C side of the gas-liquid mixing swirl tank 14, and a negative pressure part is formed in the outer peripheral part of the air suction pipe 15.

【0016】空気吸入管15は気液混合旋回槽14の軸
心部に挿入されているので、前記負圧部は、空気吸入管
15の管壁に設けた複数個の空気吐出口15A,15A
…と、逆止弁16および空気吸入管15の外端開口部1
5Cを介して大気に連通する。したがって、大気圧と前
記負圧部との圧力差により空気吸入管15に空気を吸い
込んで、複数個の空気吐出口15A,15A…から気液
混合旋回槽14内に空気を吐出して、空気と汚水を混合
した気液混合流体として汚水圧送管路4の二次側4Bに
吐出することができる。
Since the air suction pipe 15 is inserted into the axial center of the gas-liquid mixing swirl tank 14, the negative pressure portion has a plurality of air discharge ports 15A, 15A provided on the wall of the air suction pipe 15.
... and the outer end opening 1 of the check valve 16 and the air suction pipe 15.
It communicates with the atmosphere through 5C. Therefore, air is sucked into the air suction pipe 15 due to the pressure difference between the atmospheric pressure and the negative pressure portion, and the air is discharged from the plurality of air discharge ports 15A, 15A ... It can be discharged to the secondary side 4B of the sewage pressure-feeding pipeline 4 as a gas-liquid mixed fluid in which sewage and

【0017】このように、大気圧と負圧部との圧力差を
利用して気液混合旋回槽14内に空気を注入することが
できるので、従来の空気注入式汚水圧送システムにおい
て必要とされていた空気注入系5が不要になる。このた
め、設備費を削減できるばかりか、ランニングコストを
削減することができる。
As described above, since the air can be injected into the gas-liquid mixing swirl tank 14 by utilizing the pressure difference between the atmospheric pressure and the negative pressure portion, it is required in the conventional air injection type sewage pumping system. The air injection system 5 that has been used is no longer necessary. Therefore, not only the equipment cost can be reduced, but also the running cost can be reduced.

【0018】一方、図3に示すように、空気吸入管15
の外端開口部15Cに空気注入系5の空気注入管5Aを
接続してもよい。なお、図3において、図1、図2で説
明した実施の形態および図5で説明した従来例と同一も
しくは相当部分には、同一符号を付して重複した構造と
作用の説明は省略する。このように、空気吸入管15の
外端開口部15Cに空気注入系5の空気注入管5Aを接
続することで、空気注入系5から空気吸入管15の外周
部に形成した前述の負圧部に空気が注入されることにな
るので、空気注入系5の空気注入能力を低く抑えること
ができる。すなわち、空気注入系5の注入空気圧力を低
く抑えても容易に空気を注入することができるから、エ
アーコンプレッサー8の消費電力を小さくして、ランニ
ングコストを削減することができる。
On the other hand, as shown in FIG.
The air injection pipe 5A of the air injection system 5 may be connected to the outer end opening 15C of the. In FIG. 3, the same or corresponding parts as those of the embodiment described with reference to FIGS. 1 and 2 and the conventional example described with reference to FIG. In this way, by connecting the air injection pipe 5A of the air injection system 5 to the outer end opening 15C of the air intake pipe 15, the above-mentioned negative pressure portion formed from the air injection system 5 to the outer peripheral portion of the air intake pipe 15 is connected. Since air is injected into the air, the air injection capacity of the air injection system 5 can be suppressed to a low level. That is, since the air can be easily injected even if the injection air pressure of the air injection system 5 is kept low, the power consumption of the air compressor 8 can be reduced and the running cost can be reduced.

【0019】なお、前記実施の形態では、本発明に係る
気液混合装置13を汚水圧送管路4内の汚水に空気を注
入する空気注入式汚水圧送システムに適用して説明して
いるが、この気液混合装置13の適用は、前記実施の形
態のみに限定されるものではなく、管路内を流れる液体
に空気を混合させる他の空気注入式液体圧送システムに
も適用することができる。
In the above embodiment, the gas-liquid mixing device 13 according to the present invention is applied to an air injection type sewage pumping system for injecting air into the sewage in the sewage pumping line 4. The application of the gas-liquid mixing device 13 is not limited to the above-described embodiment, but can be applied to other air-injection liquid pressure-feeding systems that mix air with the liquid flowing in the pipeline.

【0020】[0020]

【発明の効果】以上説明したように、本発明の気液混合
装置は構成されているので、以下のような格別の効果を
奏する。
As described above, since the gas-liquid mixing device of the present invention is constructed, the following special effects are obtained.

【0021】請求項1に記載の発明によれば、気液混合
旋回槽に導入した液体の直進流を気液混合旋回槽の壁内
面に沿う旋回流に変換して、気液混合旋回槽の軸心部お
よびその外周付近に負圧部を形成し、この負圧部を空気
吸入管の管壁に設けた複数個の空気吐出口と空気吸入管
の外端開口部を介して大気に連通させることで、大気圧
と負圧部との圧力差を利用して空気を注入して気液を混
合することができるので空気注入系が不要になる。この
ため、ランニングコストを削減することができる。
According to the first aspect of the invention, the straight flow of the liquid introduced into the gas-liquid mixing swirl tank is converted into a swirl flow along the inner surface of the wall of the gas-liquid mixing swirl tank, and the gas-liquid mixing swirl tank A negative pressure portion is formed near the shaft center portion and its outer periphery, and the negative pressure portion communicates with the atmosphere through a plurality of air discharge ports provided on the wall of the air suction pipe and an outer end opening of the air suction pipe. By doing so, air can be injected by utilizing the pressure difference between the atmospheric pressure and the negative pressure portion to mix the gas and liquid, so that the air injection system is not required. Therefore, the running cost can be reduced.

【0022】請求項2に記載の発明のように、空気吸入
管に空気注入系を接続することにより、空気注入系から
空気吸入管の外周部に形成した負圧部に空気が注入され
ることになるので、空気注入系の空気注入能力を低く抑
えても容易に空気を注入することができるから、ランニ
ングコストを削減することができる。
According to the second aspect of the invention, by connecting the air injection system to the air intake pipe, the air is injected from the air injection system to the negative pressure portion formed on the outer peripheral portion of the air intake pipe. Therefore, even if the air injection capacity of the air injection system is suppressed to a low level, the air can be easily injected, so that the running cost can be reduced.

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

【図1】本発明の第1実施の形態を示す側面図である。FIG. 1 is a side view showing a first embodiment of the present invention.

【図2】図1のB−B線に沿う断面図である。FIG. 2 is a sectional view taken along line BB of FIG.

【図3】本発明の第2実施の形態を示す図2相当図であ
る。
FIG. 3 is a view corresponding to FIG. 2 showing a second embodiment of the present invention.

【図4】従来の汚水圧送システムの構成図である。FIG. 4 is a configuration diagram of a conventional sewage pumping system.

【図5】従来の空気注入式汚水圧送システムの構成図で
ある。
FIG. 5 is a configuration diagram of a conventional air-injection type sewage pumping system.

【符号の説明】[Explanation of symbols]

2 汚水 4 汚水圧送管路(液体圧送管路) 4A 一次側 4B 二次側 5 空気注入系 13 気液混合装置 14 気液混合旋回槽 14C 気液混合旋回槽の周壁部(気液混合旋回槽の周
壁) 15 空気吸入管 15A 空気吐出口 15C 空気吸入管の外端開口部 C 軸線 S 旋回流
2 sewage 4 sewage pressure feed pipe line (liquid pressure feed pipe line) 4A primary side 4B secondary side 5 air injection system 13 gas-liquid mixing device 14 gas-liquid mixing swirl tank 14C gas-liquid mixing swirl tank peripheral wall (gas-liquid mixing swirl tank 15) Air suction pipe 15A Air discharge port 15C Outer end opening C of air suction pipe C Axis S Swirling flow

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 液体圧送管路内を圧送される液体に空気
を混合させる気液混合装置であって、前記液体圧送管路
の一次側から導入した液体の直進流を周壁内面に沿う旋
回流に変換して前記液体圧送管路の二次側に吐出する筒
状の気液混合旋回槽と、この気液混合旋回槽の軸線方向
にのびて該気液混合旋回槽の軸心部に挿入されていると
ともに、外端開口部を気液混合旋回槽の外部で大気に開
放した空気吸入管とを備え、この空気吸入管の管壁に複
数個の空気吐出口が設けられていることを特徴とする気
液混合装置。
1. A gas-liquid mixing device for mixing air with a liquid to be pressure-fed in a liquid pressure-feeding conduit, wherein a straight flow of the liquid introduced from the primary side of the liquid pressure-feeding conduit is swirling along an inner surface of a peripheral wall. And a cylindrical gas-liquid mixing swirl tank which is converted into and is discharged to the secondary side of the liquid pressure-feeding pipeline, and extends in the axial direction of the gas-liquid mixing swirl tank and is inserted into the axial center portion of the gas-liquid mixing swirl tank. And an air intake pipe having an outer end opening opened to the atmosphere outside the gas-liquid mixing swirl tank, and a plurality of air discharge ports are provided on the wall of the air intake pipe. Characteristic gas-liquid mixing device.
【請求項2】 前記空気吸入管に空気注入系が接続され
ている請求項1に記載の気液混合装置。
2. The gas-liquid mixing device according to claim 1, wherein an air injection system is connected to the air suction pipe.
JP2001344399A 2001-11-09 2001-11-09 Gas-liquid mixing apparatus Pending JP2003144881A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001344399A JP2003144881A (en) 2001-11-09 2001-11-09 Gas-liquid mixing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001344399A JP2003144881A (en) 2001-11-09 2001-11-09 Gas-liquid mixing apparatus

Publications (1)

Publication Number Publication Date
JP2003144881A true JP2003144881A (en) 2003-05-20

Family

ID=19157936

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001344399A Pending JP2003144881A (en) 2001-11-09 2001-11-09 Gas-liquid mixing apparatus

Country Status (1)

Country Link
JP (1) JP2003144881A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004226371A (en) * 2003-01-27 2004-08-12 Dkk Toa Corp Sample water analyzing unit and sample water analyzing device
JP2013081880A (en) * 2011-10-06 2013-05-09 Clean Tech Service:Kk Gas dissolving apparatus
RU2622414C1 (en) * 2016-09-06 2017-06-15 Владимир Иванович Савичев Liquid and gas mixing device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004226371A (en) * 2003-01-27 2004-08-12 Dkk Toa Corp Sample water analyzing unit and sample water analyzing device
JP2013081880A (en) * 2011-10-06 2013-05-09 Clean Tech Service:Kk Gas dissolving apparatus
RU2622414C1 (en) * 2016-09-06 2017-06-15 Владимир Иванович Савичев Liquid and gas mixing device

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