JPH0691300A - Apparatus for separating gas from material in transport pipe - Google Patents

Apparatus for separating gas from material in transport pipe

Info

Publication number
JPH0691300A
JPH0691300A JP30408991A JP30408991A JPH0691300A JP H0691300 A JPH0691300 A JP H0691300A JP 30408991 A JP30408991 A JP 30408991A JP 30408991 A JP30408991 A JP 30408991A JP H0691300 A JPH0691300 A JP H0691300A
Authority
JP
Japan
Prior art keywords
pipe
gas
sludge
gas body
separation chamber
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
JP30408991A
Other languages
Japanese (ja)
Inventor
Takashi Yamamoto
孝 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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP30408991A priority Critical patent/JPH0691300A/en
Publication of JPH0691300A publication Critical patent/JPH0691300A/en
Pending legal-status Critical Current

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  • Jet Pumps And Other Pumps (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To improve the biological treatment of sludge by removing or burning harmful gas such as methane separated from dredged sludge. CONSTITUTION:A sludge transport pressure pipe 1, 6 with a required diameter is divided in an optional position into an upstream pipe and a downstream pipe. The two pipes 1, 6 are placed coaxially at required interval. A tapered outer pipe 3 is installed on the periphery of the facing ends of the pressure pipes 1, 6 to connect them. Gas contained in sludge running in the upstream pipe is led to a gas separation chamber 2 in the outer pipe 3 through slits or holes to separate the gas from sludge. An ignition cock 9 and an air introduction pipe 10 are attached on the outer pipe 3 as necessity requires. Combustible gas such as methane introduced in the gas separation chamber 2, after being mixed with air, is burned, and the combustion gas is discharged into the downstream pipe.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は管内流送物のガス体分離
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 body separating apparatus for a pipe flow product.

【0002】[0002]

【従来の技術】港湾の海底や河川、湖沼、ダム等の底部
には有機物が含有した汚泥が多量に沈澱堆積して所謂ヘ
ドロとなって公害の問題となっている。そこでこの堆積
汚泥(ヘドロ)を浚渫する方法が提案されている。この
ヘドロの浚渫は汚泥掻揚用ポンプを用いたり、ジェット
ポンプを用いて行っている。
2. Description of the Related Art A large amount of sludge containing organic substances is deposited and accumulated on the sea bottom of a port, the bottom of rivers, lakes, dams, etc., forming so-called sludge, which is a pollution problem. Therefore, a method of dredging this sludge (sludge) has been proposed. The sludge dredging is performed by using a sludge lift pump or a jet pump.

【0003】[0003]

【発明が解決しようとする課題】海底、湖底等の底部に
沈澱堆積した汚泥に有機物が含有されるとこれが嫌気発
酵をしてメタンガス等の可燃性有害ガスが発生する。こ
の種ガス体は沈澱汚泥より比重が極めて軽いので、気泡
となって浮上し、大気中へ放出される。しかし汚泥等の
重量によって気泡とならず微細なる状態でヘドロ中に含
有されると、この状態でヘドロの浚渫を行うと、この有
害ガスがヘドロと分離して大気へ一時に多量が放出され
二次公害の問題の起因ともなる。
When organic matter is contained in sludge settled at the bottom of the seabed, lake bottom, etc., it undergoes anaerobic fermentation and combustible harmful gas such as methane gas is generated. Since this seed gas has an extremely lighter specific gravity than the settled sludge, it floats as bubbles and is released into the atmosphere. However, if the sludge is contained in the sludge in a fine state without forming bubbles due to the weight of the sludge, when the sludge is dredged in this state, this harmful gas is separated from the sludge and a large amount is temporarily released to the atmosphere. It also causes the next pollution problem.

【0004】本発明では浚渫されるヘドロ中の気体、メ
タンガス等の有害ガスをヘドロより分離して除去または
燃焼させて除去することを目的とする。
An object of the present invention is to remove the gas in the dredged sludge and harmful gas such as methane gas by separating them from the sludge or by burning them.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、所要径をしたヘドロ圧送管を
その途中の任意箇所で上流側と下流側に分割するととも
に両ヘドロ圧送管を同一軸心上で、かつ所要間隔を開け
て対設し、この両ヘドロ圧送管の分離箇所外周にテーパ
形をした外管を一体に配設し、上流側ヘドロ圧送管の内
周面にそって流送されるガス体を前記隙間もしくは小孔
を経て外管内のガス体分離室内へ導入してヘドロと気体
とを分離するようになしたことを要旨とする。
SUMMARY OF THE INVENTION The present invention has been made to achieve the above object, and divides a sludge pressurizing pipe having a required diameter into an upstream side and a downstream side at an arbitrary position on the way, and pressurizing both sludge pressurizing pipes. The pipes are arranged opposite each other on the same axial center with a required gap, and the tapered outer pipes are integrally arranged on the outer circumferences of the separation points of both sludge pumping pipes, and the inner peripheral surface of the upstream sludge pumping pipes. The gist of the present invention is that the gas body flown along with the gas is introduced into the gas body separation chamber in the outer tube through the gap or the small hole to separate the sludge from the gas.

【0006】[0006]

【作用】ジェットポンプその他のポンプにて浚渫したヘ
ドロを圧送管内を流送する際、この圧送管の途中に圧送
管外周に外管を配設して圧送管外周部にガス体分離室を
設けているので、圧送管の内周面にそってヘドロととも
に流送されるメタンガス等のガス体は管内周面より容易
に分離してガス体分離室へ導かれる。ヘドロ等はそのま
ま次位の圧送管内へ流送される。ヘドロより分離され、
ガス体分離室内へ導かれたメタンガス等はそのまま外管
より外部へ導き出して処理するか、またはガス体分離し
つないで空気と混合して燃焼させた後、燃焼ガスを再び
次位の圧送管内へ排出し、ヘドロと一緒に流送せしめ
る。これにより浚渫ヘドロ中のメタンガス等の有害ガス
は除去または無害化されるので、後工程でのヘドロの処
理が容易に行える。
[Function] When sludge dredged by a jet pump or other pump is sent through the pressure-feeding pipe, an outer pipe is arranged on the outer periphery of the pressure-feeding pipe in the middle of the pressure-feeding pipe, and a gas body separation chamber is provided on the outer periphery of the pressure-feeding pipe Therefore, the gas body such as methane gas sent along with the sludge along the inner peripheral surface of the pressure feed pipe is easily separated from the inner peripheral surface of the pipe and is introduced into the gas body separation chamber. Sludge and the like are sent as they are into the next pressure feed pipe. Separated from sludge,
The methane gas, etc. introduced into the gas body separation chamber is directly led to the outside through an outer tube for treatment, or after the gas body is separated, it is mixed with air and burned, and then the combustion gas is again fed into the next pressure feed tube. Discharge and send with sludge. As a result, harmful gas such as methane gas in the dredging sludge is removed or rendered harmless, so that the sludge can be easily treated in the subsequent step.

【0007】[0007]

【実施例】以下本発明管内流送物のガス体分離装置を図
示の実施例にもとづいて説明する。図において1は海底
等に堆積したヘドロを浚渫するヘドロ圧送管または浚渫
したヘドロを大気に触れることなく目的地へ搬送する搬
送管で、所要の径を有する。そしてこのヘドロ圧送管1
の途中を図1に示すように少し外周方向へ膨出させてガ
ス体分離室2を一体に形成する。これはヘドロ圧送管1
の外周に円錐形をした外管3を嵌合して構成することも
可能である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A gas body separating apparatus for in-line flow products of the present invention will be described below with reference to the illustrated embodiments. In the figure, reference numeral 1 denotes a sludge pressurizing pipe for dredging sludge accumulated on the seabed or a conveying pipe for conveying the dredged sludge to a destination without touching the atmosphere, and has a required diameter. And this sludge pressure feed pipe 1
As shown in FIG. 1, the gas body separation chamber 2 is integrally formed by slightly bulging in the middle of the process. This is a sludge pumping tube 1
It is also possible to fit the outer tube 3 having a conical shape to the outer periphery of the above.

【0008】このガス体分離室2は円錐形をした外管2
を前記ヘドロ圧送管1の後端部外周に嵌合し、外管2内
に少し突入した状態とし、この突入部1Aの外周に多数
の小孔Hを穿孔するとともにガス体分離室2に至る直前
のヘドロ圧送管1内に、これより小径短管状のガス誘導
管4を配設し、少し捻れた取付板5を介してヘドロ圧送
管1に固定し、これによりヘドロ圧送管内を流送される
ヘドロの管内周面部に旋回流を与えるようになす。
The gas body separation chamber 2 is a conical outer tube 2
Is fitted to the outer periphery of the rear end portion of the sludge pressurizing pipe 1 and slightly protrudes into the outer pipe 2. A large number of small holes H are formed in the outer periphery of the protruding portion 1A and the gas body separation chamber 2 is reached. A gas guide pipe 4 having a smaller diameter and a shorter tubular shape is arranged in the immediately preceding sludge pressurizing pipe 1, and is fixed to the sludge pressurizing pipe 1 via a slightly twisted mounting plate 5, whereby the sludge pressurizing pipe 1 is flowed. A swirl flow is applied to the inner surface of the sludge pipe.

【0009】ヘドロ圧送管1の突入部1Aと所要の隙間
Oをあけて同径のヘドロ圧送管6を同一軸心上に配列
し、このヘドロ圧送管6の先端を外管3の後端縁とを接
合せしめる。
A sludge pressurizing tube 6 having the same diameter is arranged on the same axis center with a required gap O provided between the plunge part 1A of the sludge pressurizing tube 1 and the tip of the sludge pressurizing tube 6 is the rear end edge of the outer tube 3. Join and.

【0010】またヘドロ圧送管1の先端内周面で、かつ
小孔Hの下流側に集ガス板7を突設し、これによりヘド
ロ圧送管1の内周面にそって流送されるヘドロ中のガス
体を集め、小孔Hを経て確実にガス体分離室へ導入され
るようにする。
Further, a gas collecting plate 7 is provided so as to project on the inner peripheral surface of the tip of the sludge pumping pipe 1 and on the downstream side of the small hole H, whereby sludge is flowed along the inner peripheral surface of the sludge pumping pipe 1. The gas body inside is collected and surely introduced into the gas body separation chamber through the small hole H.

【0011】外管3にはガス体分離室2内を覗くように
なした点検窓8と点火栓9及び弁11を備えた空気導入
管10を設ける。
The outer tube 3 is provided with an inspection window 8 through which the inside of the gas body separation chamber 2 is seen, an air introduction tube 10 having an ignition plug 9 and a valve 11.

【0012】従って上述の如く構成したる装置を浚渫さ
れたヘドロを圧送する管路の一部に挿入する。そして浚
渫されたヘドロが該管内を流送されるとき、特に空気を
吹き込み空気流とともにヘドロを圧送する場合、空気や
ヘドロ中のガス体は流体力学的作用により比重の重いヘ
ドロの固形物と分離され、ヘドロはヘドロ圧送管の中心
部を、比重の軽いガス体は内周面にそって圧流送され
る。そしてガス体がヘドロ圧送管の突入部1Aに達する
とこれに穿孔された小孔Hより該管外周部に設けたガス
体分離室2内へ導入される。この際、ガス体分離室直前
のヘドロ圧送管内には管内周面にそうガス体にガス誘導
管4及び取付板5にて旋回流が与えられているので、ガ
ス体は小孔Hを経て円滑にガス体分離室2内へ導かれ
る。該室内には点火栓9と空気導入管10が備えられて
いるので、該室内のメタン等の可燃性ガス濃度を測定
し、これを完全燃焼させるに必要な空気を弁11の操作
にて空気供給管10を経て供給する。そしてこのガス分
離室内の点火栓9の点火により可燃性ガス体は燃焼せし
められる。
Therefore, the device constructed as described above is inserted into a part of the pipe line for feeding the dredged sludge under pressure. When the dredged sludge is sent through the pipe, especially when air is blown and the sludge is pumped together with the air flow, the air and the gas bodies in the sludge are separated from the solid matter of the heavy sludge having a large specific gravity by the hydrodynamic action. The sludge is pressure-fed along the central portion of the sludge pressure-feeding pipe, and the gas body having a low specific gravity is pressure-fed along the inner peripheral surface. Then, when the gas body reaches the plunge portion 1A of the sludge pumping pipe, it is introduced into the gas body separation chamber 2 provided at the outer peripheral portion of the pipe through the small hole H bored in this. At this time, since the swirl flow is given to the gas body by the gas guide pipe 4 and the mounting plate 5 in the sludge pressurization pipe immediately before the gas body separation chamber, the gas body smoothly passes through the small hole H. To the gas body separation chamber 2. Since the interior of the chamber is equipped with a spark plug 9 and an air introduction pipe 10, the concentration of combustible gas such as methane in the chamber is measured, and the air necessary for completely burning it is operated by operating the valve 11. It is supplied via the supply pipe 10. The flammable gas body is burned by the ignition of the spark plug 9 in the gas separation chamber.

【0013】ヘドロ圧送管1内を圧流送されるヘドロ中
の気体は窒素ガス、酸素ガスとメタンガスを比較する
と、その各分子量は28:32:16である。このため
比重の比率はN2:O2:CH4=7:8:4となりメ
タンガスの比重が最も小さい。従ってメタンガスはヘド
ロ圧送管1の内周面の最も外側に集中し、最も濃度が高
くなる。この高濃度のメタンガスが上述の如く小孔Hよ
りガス体分離室に導入され適度に空気と混合されて点火
栓にて点火燃焼させた後、この燃焼ガスは空隙Oより次
のヘドロ圧送管6内へ噴出される。この噴出する高温、
高速の燃焼ガスにて管内の流送物に加速力を与えるとと
もに加熱し、圧送ヘドロ中の水分を蒸発させて含水率を
低下せしめる。これによりメタンガス等の有害な可燃性
ガスを効率的に燃焼するので、無害な炭酸ガスと水とに
変換できる。
The gas in the sludge pressure-fed through the sludge pressure-feeding pipe 1 has a molecular weight of 28:32:16 when comparing nitrogen gas, oxygen gas and methane gas. Therefore, the specific gravity ratio is N2: O2: CH4 = 7: 8: 4, and the specific gravity of methane gas is the smallest. Therefore, the methane gas is concentrated on the outermost side of the inner peripheral surface of the sludge pumping pipe 1 and has the highest concentration. As described above, this high-concentration methane gas is introduced into the gas body separation chamber through the small holes H, is mixed with air appropriately, and is ignited and burned by the spark plug. Erupted into the interior. This high temperature,
The high-speed combustion gas gives an accelerating force to the flowed material in the pipe and heats it to evaporate the water content in the pressure-fed sludge to reduce the water content. As a result, harmful combustible gas such as methane gas is efficiently burned, so that it can be converted into harmless carbon dioxide gas and water.

【0014】ガス体分離室2内で燃焼したガス体は突入
部内を圧送されるヘドロと再び合流して次位のヘドロ圧
送管6内を圧送されるが、この時上述の如く燃焼ガス圧
による加速と加熱が行われる。そして該管6にて所定位
置まで圧送された後、該管端に固気分離装置を設け、こ
れによりヘドロの固体分と気体とを分離する。
The gas body burned in the gas body separation chamber 2 merges again with the sludge that is pressure-fed in the rush portion and is pressure-fed in the next sludge-pressure feed pipe 6. At this time, as described above, the combustion gas pressure is applied. Acceleration and heating takes place. Then, after being pressure-fed to a predetermined position through the pipe 6, a solid-gas separation device is provided at the end of the pipe, whereby the solid content of sludge and the gas are separated.

【0015】また図2は異なりたる実施例で、内部にガ
ス誘導管4を取付板5を介して取り付けた上流側のヘド
ロ圧送管1端に、末広状のテーパ形をした外管3を接続
するとともにこの上流側のヘドロ圧送管1の端部と所要
の隙間Oを開けて、下流側のヘドロ圧送管6を対設し、
この下流側圧送管6の先端は前記テーパ形の外管3内へ
進入させ一体とする。従って、この外管内に挿入した下
流側ヘドロ圧送管6の外周面と外管3との間に気体分離
室2が形成される。
FIG. 2 shows a different embodiment, in which an outer pipe 3 having a divergent taper shape is connected to the end of the upstream sludge pumping pipe 1 in which a gas guide pipe 4 is mounted via a mounting plate 5. At the same time, a required gap O is formed between the upstream end of the sludge pressurizing pipe 1 and the downstream sludge pressurizing pipe 6, which is provided oppositely.
The tip end of the downstream side pressure feeding pipe 6 is inserted into the tapered outer pipe 3 to be integrated. Therefore, the gas separation chamber 2 is formed between the outer pipe 3 and the outer peripheral surface of the downstream sludge pressurizing pipe 6 inserted into the outer pipe.

【0016】従って上流側のヘドロ圧送管1内を流送さ
れるヘドロ中のガス体は該管内周面にそっている。この
ためヘドロ圧送管1の端部に達するとこれに接続され、
次第に下流側に広がる外管3の内周面にそって流れ、ガ
ス体分離室2内へ導かれ、ヘドロは対向した次位のヘド
ロ圧送管6内へ流送されるのでメタンガス等の気体は確
実に分離される。そしてこのガス体分離室2の外管3の
端部は閉鎖され、かつこれにガス体排出管12が接続さ
れているので、分離されたガス体は自然に外管3外へ導
き出され、該管12に接続したタンクまたはガス燃焼装
置へ供給されるものである。
Therefore, the gas body in the sludge flowed in the sludge pressurizing pipe 1 on the upstream side is along the inner peripheral surface of the pipe. Therefore, when it reaches the end of the sludge pumping pipe 1, it is connected to it,
The sludge flows gradually along the inner peripheral surface of the outer pipe 3 that spreads to the downstream side, is guided into the gas body separation chamber 2, and the sludge is sent into the sledro pressure feed pipe 6 facing the next, so that gas such as methane gas Definitely separated. The end of the outer tube 3 of the gas body separation chamber 2 is closed, and the gas body discharge pipe 12 is connected to the end portion, so that the separated gas body is naturally guided to the outside of the outer tube 3, It is supplied to a tank or a gas combustion device connected to the pipe 12.

【0017】なお分離されたガス体中にはヘドロの嫌気
発酵にて発生したメタンガス等の可燃性有害ガスの他に
空気中の酸素ガス、窒素ガス等も含有されている。この
混合されたガス体を分離するには前記ガス体排出管12
を図3に示す如き気体分離装置20に接続し、ここでそ
の比重差を利用して種別毎に気体を分離除去する。
The separated gas body contains oxygen gas and nitrogen gas in the air in addition to combustible harmful gas such as methane gas generated by anaerobic fermentation of sludge. To separate the mixed gas body, the gas body discharge pipe 12 is used.
Is connected to a gas separating device 20 as shown in FIG. 3, where the difference in specific gravity is used to separate and remove gas for each type.

【0018】前記気体分離装置20はその一例を図3に
示す。これは所要の容積を有する本体容器内にそのほぼ
中央に接線方向に管12を接続して、ガス体を旋回流を
与えるようにして容器内へ供給するとともにこの容器内
は仕切板24を千鳥状に配列し、導入された気体の流路
を長くするようになし、かつガス体の比重比により分離
し、種別毎に取り出すように排出管21,22,23が
接続される。この容器の上部には一番比重の軽いメタン
ガスを排出する排出管21を、下端部には凝集された水
を排出するための排出管23を、また容器の下部で、か
つ凝集水と分離されるような位置に空気を取り出す排出
管22が夫々接続されるものである。
An example of the gas separator 20 is shown in FIG. In this, a pipe 12 is tangentially connected to the center of a main body container having a required volume to supply a gas body into the container so as to give a swirling flow, and a partition plate 24 is staggered in the container. The exhaust pipes 21, 22 and 23 are connected so that the flow paths of the introduced gas are lengthened and separated according to the specific gravity ratio of the gas bodies and taken out for each type. A discharge pipe 21 for discharging methane gas having the lightest specific gravity is provided at the upper part of the container, a discharge pipe 23 for discharging condensed water at the lower end, and a lower part of the container and separated from condensed water. The exhaust pipes 22 for taking out the air are connected to such positions.

【発明の効果】本発明によるときは圧送管内周面にそっ
て気体が流送される性質を利用して圧送管の途中に一部
を膨出させてガス体分離室を形成しているので、このヘ
ドロ中のガス体のみはヘドロより自然に分離され、ガス
体分離室内へ導入される。このため、浚渫時ヘドロ中に
メタンガス等が含有していても、ヘドロ吐出口では有害
ガスが除去されているのでヘドロの処理が容易に行われ
る。またヘドロより気体を分離するのに他の動力を用い
ないので、構造も簡易となる等の利点を有する。
According to the present invention, the gas body separation chamber is formed by bulging a part of the gas in the middle of the pressure feeding pipe by utilizing the property that the gas is flown along the inner peripheral surface of the pressure feeding pipe. Only the gas body in this sludge is naturally separated from the sludge and introduced into the gas body separation chamber. Therefore, even if methane gas or the like is contained in the sludge during dredging, since the harmful gas is removed from the sludge discharge port, the sludge can be easily treated. Further, since no other power is used to separate the gas from the sludge, there is an advantage that the structure is simple.

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

【図1】本発明管内流送物のガス体分離装置の一実施例
を示す断面図である。
FIG. 1 is a cross-sectional view showing an embodiment of a gas body separating apparatus for in-pipe flow product of the present invention.

【図2】同異なりたる実施例の断面図である。FIG. 2 is a sectional view of the different embodiment.

【図3】気体分離装置の断面図である。FIG. 3 is a cross-sectional view of a gas separation device.

【符号の説明】[Explanation of symbols]

1 ヘドロ圧送管 2 ガス体分離室 3 外管 6 ヘドロ圧送管 9 点火栓 10 空気導入管 H 小孔 1 Sludge pressure feed pipe 2 Gas separation chamber 3 Outer pipe 6 Sludge pressure feed pipe 9 Spark plug 10 Air introduction pipe H Small hole

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 所要径をしたヘドロ圧送管をその途中の
任意箇所で上流側と下流側に分割するとともに両ヘドロ
圧送管を同一軸心上で、かつ所要間隔を開けて対設し、
この両ヘドロ圧送管の分離箇所外周にテーパ形をした外
管を一体に配設し、上流側ヘドロ圧送管の内周面にそっ
て流送されるガス体を前記隙間もしくは小孔を経て外管
内のガス体分離室内へ導入してヘドロと気体とを分離す
るようになしたことを特徴とする管内流送物のガス体分
離装置。
1. A sludge pressurizing pipe having a required diameter is divided into an upstream side and a downstream side at an arbitrary point on the way, and both sludge pressurizing pipes are arranged opposite to each other on the same axial center and at a required interval.
A tapered outer pipe is integrally provided on the outer periphery of the separation points of both sludge pressure feeding pipes, and the gas body fed along the inner peripheral surface of the upstream sludge pressure feeding pipe is discharged through the gap or the small hole. A gas body separation device for a flow object in a pipe, characterized by being introduced into a gas body separation chamber in a pipe to separate sludge and gas.
【請求項2】 上流側、下流側の両ヘドロ圧送管の接続
部に一体に設けたテーパ形の外管に点火栓と空気導入管
とを配設し、ガス体分離室内へ導入されたメタン等の可
燃性ガスを空気と適当に混合して燃焼させ、その燃焼ガ
スを下流側ヘドロ圧送管へ吐出するようになしたことを
特徴とする管内流送物のガス体分離装置。
2. Methane introduced into a gas body separation chamber by arranging a spark plug and an air introduction pipe in a tapered outer pipe integrally provided at a connection portion of both upstream and downstream sludge pressure feeding pipes. A combustible gas such as a gas is appropriately mixed with air and burned, and the burned gas is discharged to a downstream sludge pressure feeding pipe.
【請求項3】 上流側、下流側の両ヘドロ圧送管の接続
部に一体に設けたテーパ形の外管にガス体排出管を接続
し、ヘドロより分離してガス体分離室内に導いたガス体
を外管外へ導き出して処理するようになした請求項1ま
たは請求項2記載の管内流送物のガス体分離装置。
3. A gas body discharge pipe is connected to a tapered outer pipe integrally provided at a connecting portion of both upstream and downstream sludge pressure feeding pipes, and the gas is separated from the sludge and introduced into a gas body separation chamber. The gas body separating device for the in-pipe flowed article according to claim 1 or 2, wherein the body is led out of the outer pipe for processing.
JP30408991A 1991-10-22 1991-10-22 Apparatus for separating gas from material in transport pipe Pending JPH0691300A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30408991A JPH0691300A (en) 1991-10-22 1991-10-22 Apparatus for separating gas from material in transport pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30408991A JPH0691300A (en) 1991-10-22 1991-10-22 Apparatus for separating gas from material in transport pipe

Publications (1)

Publication Number Publication Date
JPH0691300A true JPH0691300A (en) 1994-04-05

Family

ID=17928894

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30408991A Pending JPH0691300A (en) 1991-10-22 1991-10-22 Apparatus for separating gas from material in transport pipe

Country Status (1)

Country Link
JP (1) JPH0691300A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5633986B1 (en) * 2013-08-25 2014-12-03 啓至 増田 Combustion refrigerant leakage detection structure
CN109654071A (en) * 2019-01-18 2019-04-19 安徽佳明环保科技股份有限公司 A kind of airtight discharge pressure storehouse of high pressure for the conveying of high concentration slurries

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5633986B1 (en) * 2013-08-25 2014-12-03 啓至 増田 Combustion refrigerant leakage detection structure
CN109654071A (en) * 2019-01-18 2019-04-19 安徽佳明环保科技股份有限公司 A kind of airtight discharge pressure storehouse of high pressure for the conveying of high concentration slurries

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