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JP3535191B2 - Suction type recovery method and device - Google Patents
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JP3535191B2 - Suction type recovery method and device - Google Patents

Suction type recovery method and device

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Publication number
JP3535191B2
JP3535191B2 JP18920593A JP18920593A JP3535191B2 JP 3535191 B2 JP3535191 B2 JP 3535191B2 JP 18920593 A JP18920593 A JP 18920593A JP 18920593 A JP18920593 A JP 18920593A JP 3535191 B2 JP3535191 B2 JP 3535191B2
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JP
Japan
Prior art keywords
pressure
storage chamber
chamber
solid
liquid
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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
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JP18920593A
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Japanese (ja)
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JPH0719199A (en
Inventor
武幸 西村
登 工岡
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Tsurumi Manufacturing Co Ltd
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Tsurumi Manufacturing Co Ltd
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Priority to JP18920593A priority Critical patent/JP3535191B2/en
Publication of JPH0719199A publication Critical patent/JPH0719199A/en
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Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は、真空ポンプ、排気ブロ
ワー等の減圧装置を用いた吸引式の回収方法および装置
に関し、例えば、シールド工事における竪坑からの排水
排土や、ポンプ沈砂池の土砂など、含水比の低い固液混
合体を回収対象とするものである。 【0002】 【従来技術とその問題点】従来から、固液混合体の回収
を行わせるについて、真空ポンプ、排気ブロワー等の減
圧装置を用いるという技術的思想は公知である。そして
バキューム車に代表されるよう、回収タンク内が満杯と
なったときに減圧装置の駆動を停止し、タンクハッチを
開けて回収物を取り出すという方式のものが主流となっ
ている。 【0003】しかしながら、この方式では回収物の連続
吸引ができず、回収物排出の際にも人為的操作が必要と
なり、また、吸引作業の中断中に回収物が管路に滞溜
し、吸引作業再開時に屡々管路閉塞を来すことがある。 【0004】このような欠点を解消する手段として図1
1ないし図14に示されるよう、回収タンク2′を上下
二室に区画して上室を第1貯溜室2′aとし、下室を第
2貯溜室2′bとし、両室の下底部には常閉型のハッチ
12′a,12′bをそれぞれ装着し、両室2′a,
2′b間を連通管14′で連通させ、該連通管14′に
両室間の連通を開閉させる第1のバルブ17′aを附設
すると共に、第2貯溜室2′b内とを外気との導通路1
5′を開閉する第2のバルブ17′bを附設した吸引式
回収装置により、吸引作業を継続させながら回収物を断
続的に排出するという方法が提案されている。 【0005】この装置における上室ハッチ12′aおよ
び下室ハッチ12′bは、減圧装置が駆動していない間
は、いずれも軽く閉合した状態に保たれている。つまり
常閉型のものであり、上室ハッチ12′aは第1貯溜室
2′a内が負圧で第2貯溜室2′b内が正圧のときに密
閉し、第2貯溜室2′b内が第1貯溜室2′a内と同様
負圧状態となったときは貯溜物の重量により開放され
る。貯溜物の重量を受けて初めて開放されるのであっ
て、両室2′a,2′b内の圧力が均衡しただけでは開
放せられない構造である。また、下室ハッチ12′bは
第2貯溜室2′b内が第1貯溜室2′a内と同様負圧と
なったときに密閉し、第2貯溜室2′b内が正圧となっ
たときは貯溜物の重量により開放される。このハッチ1
2′bも貯溜物の重量を受けて初めて開放されるのであ
って、第2貯溜室2′b内が大気圧と均衡しただけでは
開放せられない構造である。 【0006】そして第1のバルブ17′aを閉操作して
第2のバルブ17′bを開操作した状態で減圧装置を駆
動させると、第1貯溜室2′a内は負圧となって第2貯
溜室2′b内と圧力差が生じるため、上室ハッチ12′
aは上方に吸引されて密閉状態となり、貯溜物の荷重に
耐え得る体制となる。そして図12に見られるよう負圧
となった第1貯溜室2′a内には吸込管5′を介して流
入する回収物が貯溜されることになり、その貯溜量が所
定値になった時点で第2バルブ17′bを閉操作し第1
バルブ17′aを開操作すると、連通管14′を通じて
第2貯溜室2′b内も負圧となり、外気との圧力差によ
り下室ハッチ12′bは密閉し、他方、第1貯溜室2′
a内と第2貯溜室2′b内の圧力差が減少して上室ハッ
チ12′aの密閉性が失われるため、第1貯溜室2′a
内の貯溜物はその重量により上室ハッチ12′aを下傾
状に開放させつつ図13に見られるよう第2貯溜室2′
b内へ落下する。次に第1バルブ17′aを閉操作し第
2バルブ17′bを開操作すれば、第2貯溜室2′b内
は導通路15′を介して外気と導通することで正圧とな
るが、第1貯溜室2′a内は引き続き負圧状態とされる
ため第2貯溜室2′b内の貯溜物はその重量により下室
ハッチ12′bを開放させつつ図14に見られるよう外
部へ排出せられることになる。 【0007】しかし上記図11ないし図14の回収装置
には、実用上において重大な欠陥が存在する。すなわ
ち、図13の状態において第1貯溜室2′a内の気体は
吸引管8′により直接吸引されるが、第2貯溜室2′b
内の気体は連通管14′および第1貯溜室2′aを経由
して吸引管8′により吸引されるため圧損が大きく、従
って第2貯溜室2′b内の圧力は第1貯溜室2′a内の
圧力よりも若干高い状態にあり、上室ハッチ12′aの
開作動に好適な条件が満たされているとはいえず、しか
もこの上室ハッチ12′aは貯溜物の重量により開放さ
れる常閉型のものであるから、回収物が比重の大きいも
の、流動性のよいものである場合は問題はないが、比重
の小さいもの、流動性の悪い不定形な固形物を含んだ固
液混合体であれば第2貯溜室2′b内へ円滑に移動し得
ないことになる。また、第2貯溜室2′b内からの気体
の吸引に圧損が大きいということは、下室ハッチ12′
bの密閉力を弱化させる要因にもなり、第2貯溜室2′
b内の貯溜物が所定量に達しないうちに外部へ漏出し
て、定量間欠排出作業の確実性が損なわれることにな
る。 【0008】更にまた、従来の吸排装置により回収され
た固液混合体は、そのままの濃度で排出されるので、別
途固液分離装置により後処理しなければならないという
不便さがある。 【0009】 【発明の目的】本発明の目的は、回収物の連続吸引と定
量間欠排出作業が確実に行われ、しかも回収された固液
混合体を回収タンク内で含水比の低い固分として排出し
得る吸引式回収方法およびその装置を提供することにあ
る。 【0010】 【発明の構成】本発明に係る吸引式回収方法では、流通
室から導出される吸込管を固液混合体の供給源へ向けて
開口させ、流通室から液分回収タンクを経て減圧装置に
至る第1の減圧管路を開通させて流通室内を負圧とな
し、貯溜室から液分回収タンクを経て減圧装置に至る第
2の減圧管路を開通させて貯溜室内を負圧とすることに
より、流通室の下底部から貯溜室内へ通ずるよう装着さ
れた第1の常開型リップ弁を自らの弾力により開放状態
に保持させると共に貯溜室の下底部から大気中へ通ずる
よう装着された第2の常開型リップ弁を大気圧との差圧
により閉合させ、上記大気圧との差圧により吸込管から
吸い込まれる固液混合体を第1常開型リップ弁の開口面
から貯溜室内へ流下させ、上方部に若干の空気溜りを残
して貯溜室内がほぼ満杯状態となったのち流通室内に残
存する固液混合体中の固分のみを固液の比重差を利用し
て貯溜室内へ流下させるのと入れ替えに上記固分の体積
と同体積の液分を貯溜室から流通室内へ上昇させ、減圧
装置の駆動を中断することなく流通室内の負圧状態を保
持しつつ第2減圧管路を閉塞すると共に貯溜室から負圧
解除手段に通ずる増圧路を開通させて貯溜室内を正圧と
することにより、第1常開型リップ弁を上記2室間の差
圧により閉合させると共に第2常開型リップ弁を自らの
弾力により開放復帰させ、貯溜室内において含水比の低
くなった固液混合体を第2常開型リップ弁の開口面から
外部へ排出させる。 【0011】また、本発明に係る吸引式回収装置では、
減圧装置の駆動により吸込管を介して固液混合体を回収
タンク内へ吸引させる吸引式回収装置において、回収タ
ンクを上下2室構造としてその上方室を流通室に形成す
ると共に下方室を貯溜室に形成し、固液混合体の供給源
へ向けて開口させる吸込管を流通室から導出し、流通室
と液分回収タンクとを第1の吸引管により導通させ且つ
減圧装置の吸込側を液分回収タンクに導通させて第1の
減圧管路を構成し、貯溜室と液分回収タンクとを第2の
吸引管により導通させ且つ減圧装置の吸込側を液分回収
タンクに導通させて第2の減圧管路を構成し、貯溜室を
負圧解除手段に導通させる増圧路を開設し、上記第2減
圧管路の開通時には増圧路を閉止させ該増圧路の開通時
には上記第2減圧管路を閉止させるためのバルブ機構を
装備し、流通室の下底部には流通室内および貯溜室内が
負圧状態にあるときに自らの弾力により開放状態を保持
し且つ貯溜室内の圧力が流通室内の圧力よりも高圧とな
ったときはその差圧によって閉合状態とされる第1の常
開型リップ弁を附設し、貯溜室の下底部には流通室内お
よび貯溜室内が負圧状態となったときに大気圧との差圧
により閉合状態とされ且つ貯溜室内が正圧となったとき
は自らの弾力により開放状態に復元される第2の常開型
リップ弁を附設し、貯溜室内の上方部に若干の空気溜り
の形成スペースを存置して固液混合体の収容上限を規制
するよう構成した。 【0012】 【実施例】以下実施例の図面により説明をする。 【0013】図1ないし図4において、1は水封式の真
空ポンプ或いは排気ブロワー等を用いた減圧装置、2は
減圧装置1の作動によって負圧とされる回収タンクであ
って、上方に位置する流通室2aと、下方に位置する貯
溜室2bの2室で構成せられ、各室2a,2bはその下
方部がそれぞれ漏斗状の傾斜面3a,3bに形成されて
その底部には矩形孔4,4がそれぞれ開設されている。
5は流通室2aより導下された吸込管であって、その導
下先端部5eを固液混合体の供給源6へ向けて開口す
る。5vは吸込管5に附設された開閉バルブ、7は流通
室2aの上方部と減圧装置1の吸引側1aとを第1の吸
引管8により導通させて構成される第1の減圧管路、9
は減圧装置1の吸引側1aと第1吸気管8との間に介装
された液分回収タンク、10は第1吸引管8に附設され
たフローコントロールバルブ、11は貯溜室2bの壁面
上方部において後記第1常開型リップ弁12aの開放下
縁部12eよりも上方に位置するよう開設された気孔、
11sは気孔11に附設された固液分離スクリーン、1
3は気孔11と減圧装置1の吸引側1aとを第2の吸引
管14により導通させて構成される第2の減圧管路であ
って、減圧装置1の吸引側1aと第2吸引管14との間
には液分回収タンク9が介装されている。15は上記第
2吸引管14から分岐状に導出されて何らかの負圧解除
手段16に導通される増圧路、17は第2減圧管路13
を開閉すると共にその閉止時には貯溜室2bを上記負圧
解除手段16に開通させたり閉止させたりするためのバ
ルブ機構であって、例えば第2減圧管路13の閉止と同
時に増圧路15を大気中へ開放させ、或いは送気管18
を介して減圧装置1の排気側1bへ開通させ、或いは別
設の送気装置(図示せず)へ開通させる等により貯溜室
2b内へ正圧を供給し、或いは第2減圧管路13の閉止
と共に増圧路15をも閉止するのである。従って上記バ
ルブ機構17は、貯溜室2bを第2の減圧管路13また
は増圧路15のいずれかと開通させることになり、貯溜
室2bが第2減圧管路13と開通するときは貯溜室2b
と増圧路15との開通は断たれ、貯溜室2bが増圧路1
5と開通するときは貯溜室2bと第2減圧管路13との
開通は断たれるように開閉作動する。しかし必要によっ
ては貯溜室2bを第2減圧管路13および増圧路15の
いずれとも閉止状態とすることもある。実施例の図面に
おいては第2減圧管路13と増圧路15との分岐点に1
個の3方切換バルブを介装して第2減圧管路13の開閉
用と増圧路15の開閉用とに兼用させた態様となってい
るが、3個の切換バルブを使用して第2減圧管路13の
開閉と増圧路15の開閉とをそれぞれ別個の切換バルブ
により行わせるという態様としてもよい。このようにし
て減圧装置1の作動時に貯溜室2b内の圧力を、流通室
2a内の圧力と同圧に減圧する機能、および大気圧と同
圧に昇圧する機能を併有した圧力変換機構が構成される
のである。 【0014】流通室2aの下底部から貯溜室2b内へ通
ずるよう装着された第1の常開型リップ弁12aは、流
通室2a内および貯溜室2b内が負圧状態にあるときに
自らの弾力により開放状態を保持し、且つ貯溜室2b内
の圧力が流通室2a内の圧力よりも高圧となったときは
その差圧により閉合状態とされる。また、貯溜室2bの
下底部から大気中へ通ずるよう装着された第2の常開型
リップ弁12bは、流通室2a内および貯溜室2b内が
負圧状態となったときに大気圧との差圧により閉合状態
とされ、且つ貯溜室2b内が正圧となったときは自らの
弾力により開放状態に復元される。これら両リップ弁1
2a,12bの具体的構造例としては、図5および図6
に見られるような角筒状弁体の上縁周辺部に締着板19
を当接して取付部となし、図7および図8に示すような
弁座12fを介して前記矩形孔3の孔縁部に装着する。
そして上記取付部の下方で前後から相対する回動壁2
0,20に補強板21,21および巻込防止材21s,
21sを添設して剛性を保有させ、上記回動壁20,2
0の側端部と連接する屈伸壁22,22には可撓性を存
置させ、上記回動壁20,20の下縁を弾褥性の離接面
23,23に形成し、外部圧力の作用により屈伸壁2
2,22が撓屈し両回動壁20,20は互いに接近方向
に回動して離接面23,23が閉合することで、矩形孔
4は閉塞状態とされる。また、外部圧力の解除により屈
伸壁22,22は伸展し両回動壁20,20は離隔方向
へ回動して離接面23,23が分離することで、矩形孔
4は開放状態とされる。 【0015】再び図1ないし図4において、24は貯溜
室2b内における固分の堆積状態を検出するためのサン
ドセンサー、25は流通室2a内に装備される固液分離
スクリーンであって、流通室2aの周壁内面における吸
込管入口5hよりも上方に定着された支持材26によ
り、遊嵌状に横設されて上下方向に微震し得る態様とな
っている。27は液分回収タンク9内に設置された水中
ポンプ、28は水中ポンプ27の吐出口から導出された
液分返送管であって、その導出先端部28eは固液混合
体の供給源6内の下方部へ導入開口されている。なお、
流通室2aの底部矩形孔4に装着されて貯溜槽2b内へ
導下された第1の常開型リップ弁12aは、開放時に回
収物の流下路となるばかりでなく、後述のように貯溜室
2b内からの液分上昇路にもなるものであり、その開放
下縁部12eは前記気孔11の開口位置よりも下方に達
していることを必要とする。 【0016】 【作用】減圧装置1が駆動していないときには、流通室
2a内の圧力と貯溜室2b内の圧力が均衡して大気圧と
同圧であるため、図1に示すよう第1の常開型リップ弁
12aおよび第2の常開型リップ弁12bは共に開放状
態を保っている。 【0017】図1の管路構成により吸込管5の導下先端
部5eを固液混合体の供給源6へ向けて減圧装置1を駆
動し、バルブ機構17の作動で第1減圧管路7および第
2減圧管路13が開通状態となると共に増圧路15が閉
止状態となれば、大気圧下に接する貯溜室2bの底部矩
形孔4より外気を吸引してその吸引作用により図2に示
すよう第2の常開型リップ弁12bは閉合し、減圧装置
1の駆動を続けることにより流通室2a内は第1減圧管
路7を経由して抽気され、貯溜室2b内は第2減圧管路
7を経由して抽気され両室2a,2b共ども負圧となる
ため、吸込管5から若干の空気と共に揚送された固液混
合体は、流通室2a内の漏斗状傾斜面3aに沿って流下
し開放状態の矩形孔4から貯溜室2b内へ貯溜される
が、このとき貯溜室2b内の圧力は降下しているため第
2常開型リップ弁12bには大気圧との差圧分の圧力が
作用し下底部矩形孔4を強固に閉塞して貯溜室2b内か
らの固液混合体の流出を阻止されると共に気密性も保持
されることになる。本発明の実施において、第1減圧管
路7と第2減圧管路13の管路抵抗を完全に均しくする
ことにより、図2の状態における両室2a,2b内の圧
力比は完全に同一となり、完全な真空状態を形成するま
でもなく或程度まで負圧が進めば第1常開型リップ弁1
2aは100%開作動する。また、例えば第1吸引管8
の管径を小さくしたり、管長を長くしたり或いはフロー
コントロールバルブ10を操作するなどにより、第1減
圧管路7の管路抵抗を第2減圧管路13の管路抵抗より
も若干大きくしておけば、貯溜室2b内の負圧度が流通
室2a内の負圧度よりも若干大きくなり、第1常開型リ
ップ弁12aの開作動を更に確実に行わせると共に第2
常開型リップ弁12bの閉作動をも確実なものとするこ
とができる。 【0018】減圧装置1の駆動中は吸込管5を通って継
続的に固液混合体が送り込まれ、流通室2aから貯溜室
2bへ流下する固液混合体の貯溜量は次第に増大して、
第1常開型リップ弁12aの開放下縁部12eよりも上
方まで上昇し、図3に示すよう貯溜室2bの上方周辺に
若干の空気溜り29を形成した状態で上昇は規制され、
それ以上には液分は貯溜室2b内へ流下し得ずに流通室
2a内に残留し、比重の大きい固分のみが流下して貯溜
室2b内の液面を更に押し上げようとするが、その作用
は液面状に形成された空気溜り29により抑止されるた
め、貯溜室2b内の液分が逆に開放状態の矩形孔4を遡
って流通室2aへ移動させられることになる。このよう
な固液の入れ替え作用によって時間の経過と共に次第に
含水比の低い固分が貯溜室2b内に堆積することにな
る。 【0019】第2の常開型リップ弁12bが閉作動して
から所定の時間が経過すれば、バルブ機構17の切り換
わり作動で第2減圧管路13は閉止状態となり増圧路1
5は開通状態となって貯溜室2b内の負圧状態が解消さ
れるため、図4に示すよう第1の常開型リップ弁12a
が閉作動すると共に第2の常開型リップ弁12bは開状
態に復帰して貯溜室2b内における含水比の低い固分が
矩形孔4から外部へ排出される。この間も流通室2a内
は負圧状態に保たれて吸込管5からは連続的に固液混合
体が送り込まれる。上記貯溜室2b内の負圧解除手段1
6としては、第2減圧路13の閉止と同時に増圧路15
を大気中へ開放して貯溜室2b内を大気圧と均衡させる
ほか、増圧路15を減圧装置1の排気側1bへ開通し或
いは別設の送気装置へ開通するなどにより貯溜室2b内
を大気圧よりも高圧とすることも可能であり、後者の方
式を採り入れることにより第2常開型リップ弁12bの
開作動を一層確実に行わせ得ると共に第1常開型リップ
弁12aの閉合状態を強化させることができる。上述の
ようにして貯溜室2b内に貯溜されていた固液混合体の
排出が終わると、バルブ機構17の切り換わり作動で第
2減圧管路13は開通状態となり増圧路15は閉止状態
となって貯溜室2b内は負圧状態となるため、第2の常
開型リップ弁12bが閉作動すると共に第1の常開型リ
ップ弁12aは開放状態に復帰し、図2に示すよう吸込
管5から揚送される固液混合体は流通室2a内の漏斗状
傾斜面3aに沿って流下し開放状態の矩形孔4から貯溜
室2b内へ貯溜される。そして第1の常開型リップ弁1
2aおよび第2の常開型リップ弁12bの閉作動は、弾
褥性の離接面23,23同士が互いに面接触して閉合す
るという態様で行われるため、砂粒等の異物が閉合面に
噛み込んでも、その異物は弾褥性の離接面23,23間
に包み込まれた状態となり、閉合面の気密性は保持され
ることになる。 【0020】前述のバルブ機構17の切り換え作動は、
タイマーの時間設定により所定時間毎に自動的に行わせ
てもよく、或いはサンドセンサー24等により固分の堆
積状態を検出してその検出信号に基づき電気的に行わせ
てもよい。このようなバルブ機構17の切り換え作動に
伴う第1常開型リップ弁12aおよび第2常開型リップ
弁12bの交互開閉作用の反復により、吸込管5を通っ
て連続的に吸い込まれる固液混合体を含水比の低い固分
として貯溜室2b内から間欠的に排出させるという作業
が行われるのである。 【0021】流通室2a内の液分は固液分離スクリーン
25により更に固分を取り除かれて、液分回収タンク9
内へ移送されるのであるが、上記スクリーン25の通水
断面積は大きく流速が遅いこと、および支持部材26に
より遊嵌されて上下に微振動を生じることにより、スク
リーンの目詰まりは殆ど生じることがない。 【0022】回収物の吸排過程において回収タンク2内
から液分回収タンク9内に至る通気中に混入する液分は
液分回収タンク9内へ回収せられ、水中ポンプ27の作
動により液分返送管28を通って元の供給源6内へ還元
させるのであるが、導出先端部28eから液分が流出す
る際、供給源6内における混合攪拌作用を生じさせて吸
込管先端部5eからの固分の吸い込みを容易ならしめる
のである。 【0023】 【発明の効果】本発明よれば、回収物の連続吸引と定量
間欠排出作業が確実に行われ、しかも回収された固液混
合体を回収タンク内で含水比の低い固分として排出する
ことができるので、別途固液分離装置による後処理は不
要となるという利点がある。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a suction type recovery method and apparatus using a decompression device such as a vacuum pump and an exhaust blower. It is intended to collect solid-liquid mixtures with low water content, such as drainage and earth from pump sedimentation basins. 2. Description of the Related Art Conventionally, the technical idea of using a pressure reducing device such as a vacuum pump or an exhaust blower for recovering a solid-liquid mixture has been known. As typified by a vacuum vehicle, a system in which the drive of the pressure reducing device is stopped when the inside of the collection tank is full, and the tank hatch is opened to take out the collected material has become mainstream. However, in this method, it is not possible to continuously suck the collected material, and it is necessary to perform an artificial operation when the collected material is discharged. At the time of resuming work, there is often a case where a line is blocked. [0004] As means for solving such a disadvantage, FIG.
As shown in FIGS. 1 to 14, the recovery tank 2 'is divided into two upper and lower chambers, the upper chamber being a first storage chamber 2'a, the lower chamber being a second storage chamber 2'b, and the lower bottom of both chambers. Are equipped with normally-closed hatches 12'a and 12'b, respectively.
A communication pipe 14 'connects between the 2'b and a first valve 17'a for opening and closing the communication between the two chambers, and the inside of the second storage chamber 2'b is connected to the outside air. Conduction path 1 with
A method has been proposed in which a suction-type collection device provided with a second valve 17'b that opens and closes 5 'intermittently discharges the collection while continuing the suction operation. [0005] The upper chamber hatch 12'a and the lower chamber hatch 12'b in this apparatus are both kept lightly closed while the pressure reducing device is not driven. That is, the upper chamber hatch 12'a is closed when the pressure in the first storage chamber 2'a is negative and the pressure in the second storage chamber 2'b is positive, and the upper chamber hatch 12'a is closed. When the inside of the storage chamber 'b becomes a negative pressure state like the inside of the first storage chamber 2'a, the storage chamber is opened by the weight of the storage material. It is opened only after receiving the weight of the stored material, and cannot be opened only when the pressure in both chambers 2'a and 2'b is balanced. Also, the lower chamber hatch 12'b is closed when the inside of the second storage chamber 2'b becomes a negative pressure like the inside of the first storage chamber 2'a, and the inside of the second storage chamber 2'b becomes positive pressure. When it does, it is released by the weight of the stored material. This hatch 1
The second storage chamber 2'b is also opened only after receiving the weight of the storage material, and cannot be opened only when the inside of the second storage chamber 2'b is balanced with the atmospheric pressure. When the pressure reducing device is driven in a state where the first valve 17'a is closed and the second valve 17'b is opened, a negative pressure is generated in the first storage chamber 2'a. Due to the pressure difference between the second storage chamber 2'b and the upper chamber hatch 12 '
a is sucked upward to be in a sealed state, and a system capable of withstanding the load of the stored material is established. Then, as shown in FIG. 12, the recovered material flowing through the suction pipe 5 'is stored in the first storage chamber 2'a having a negative pressure, and the stored amount has reached a predetermined value. At this point, the second valve 17'b is closed and the first valve
When the valve 17'a is opened, the pressure in the second storage chamber 2'b also becomes negative through the communication pipe 14 ', and the lower chamber hatch 12'b is closed by the pressure difference with the outside air. ′
a, and the pressure difference between the second storage chamber 2′b and the upper chamber hatch 12′a loses the hermeticity, so that the first storage chamber 2′a
As shown in FIG. 13, the storage material in the second storage chamber 2 'is opened while the upper chamber hatch 12'a is opened downward by its weight.
Drops into b. Next, if the first valve 17'a is closed and the second valve 17'b is opened, the inside of the second storage chamber 2'b communicates with the outside air via the conduction path 15 ', so that the pressure becomes positive. However, since the inside of the first storage chamber 2'a is kept in a negative pressure state, the stored material in the second storage chamber 2'b opens the lower chamber hatch 12'b by its weight, as shown in FIG. It will be discharged outside. However, the recovery apparatus shown in FIGS. 11 to 14 has a serious defect in practical use. That is, in the state of FIG. 13, the gas in the first storage chamber 2'a is directly sucked by the suction pipe 8 ', but the second storage chamber 2'b
The gas inside is sucked by the suction pipe 8 'via the communication pipe 14' and the first storage chamber 2'a, so that the pressure loss is large. Therefore, the pressure in the second storage chamber 2'b is reduced to the first storage chamber 2 '. ′ A, which is slightly higher than the pressure in the upper chamber hatch 12′a, which does not satisfy the conditions suitable for opening the upper chamber hatch 12′a. Since it is a normally closed type that is opened, there is no problem if the collected material is large in specific gravity or good in flowability, but it contains low specific gravity or amorphous solid with poor fluidity. If the solid-liquid mixture is used, it cannot be smoothly moved into the second storage chamber 2'b. In addition, the fact that a large pressure loss occurs in the suction of gas from the second storage chamber 2'b means that the lower chamber hatch 12 '
b also weakens the sealing force of the second storage chamber 2 '.
The stored matter in b leaks out before reaching the predetermined amount, and the reliability of the quantitative intermittent discharge operation is impaired. Further, since the solid-liquid mixture recovered by the conventional suction / discharge device is discharged at the same concentration, there is the inconvenience that the post-treatment must be separately performed by a solid-liquid separation device. SUMMARY OF THE INVENTION It is an object of the present invention to ensure that the continuous suction of the collected material and the intermittent discharge operation of the fixed amount are reliably performed, and that the recovered solid-liquid mixture is converted into a solid having a low water content in the recovery tank. An object of the present invention is to provide a suction-type recovery method and a device capable of discharging the same. In the suction type recovery method according to the present invention, the suction pipe led out of the flow chamber is opened toward the supply source of the solid-liquid mixture, and the pressure is reduced from the flow chamber through the liquid recovery tank. A first decompression line leading to the device is opened to make the distribution chamber a negative pressure, and a second decompression line leading from the storage chamber to the decompression device through the liquid recovery tank is opened to create a negative pressure in the storage room. By doing so, the first normally-open lip valve mounted to communicate from the lower bottom of the flow chamber into the storage chamber is held open by its own elasticity, and is mounted to communicate from the lower bottom of the storage chamber to the atmosphere. The second normally-open type lip valve is closed by a differential pressure from the atmospheric pressure, and the solid-liquid mixture sucked from the suction pipe by the differential pressure from the atmospheric pressure is stored from an opening surface of the first normally-open type lip valve. Allow the air to flow down into the room, leaving a small air pocket in the upper part. After the storage chamber is almost full, only the solids in the solid-liquid mixture remaining in the distribution chamber are allowed to flow down into the storage chamber using the specific gravity difference between the solids and liquids. A volume of liquid is raised from the storage chamber into the distribution chamber, and the second decompression line is closed while the negative pressure state in the distribution chamber is maintained without interrupting the operation of the decompression device, and the negative pressure is released from the storage chamber to the negative pressure release means. By opening the communicating pressure increasing passage to make the storage chamber a positive pressure, the first normally open lip valve is closed by the differential pressure between the two chambers, and the second normally open lip valve is opened by its own elasticity. The lip valve is returned and the solid-liquid mixture having a low water content in the storage chamber is discharged to the outside from the opening surface of the second normally-open lip valve. Further, in the suction type recovery device according to the present invention,
In a suction-type recovery device that draws a solid-liquid mixture into a recovery tank through a suction pipe by driving a decompression device, a recovery tank has a two-chamber structure, an upper chamber is formed as a flow chamber, and a lower chamber is formed as a storage chamber. And a suction pipe for opening toward the supply source of the solid-liquid mixture is drawn out of the flow chamber, the flow chamber and the liquid collection tank are connected to each other by the first suction pipe, and the suction side of the pressure reducing device is connected to the liquid. A first pressure-reducing pipe line by conducting to the liquid collecting tank, the reservoir and the liquid collecting tank are connected by the second suction pipe, and the suction side of the pressure reducing device is connected to the liquid collecting tank by the second collecting pipe. 2, a pressure-intensifying path for connecting the storage chamber to the negative pressure releasing means is opened, the pressure-increasing path is closed when the second pressure-reducing pipe is opened, and the pressure-increasing path is opened when the pressure-increasing path is opened. 2 Equipped with a valve mechanism for closing the decompression line, At the bottom, when the distribution chamber and the storage chamber are in a negative pressure state, they maintain the open state by their own elasticity, and when the pressure in the storage chamber becomes higher than the pressure in the distribution chamber, the closed state is established by the differential pressure. A first normally-open lip valve is provided, and the lower bottom portion of the storage chamber is closed by a pressure difference from the atmospheric pressure when the circulation chamber and the storage chamber are in a negative pressure state, and the storage chamber is closed. A second normally-open lip valve which is restored to an open state by its own elasticity when the pressure becomes positive is attached, and a solid-liquid mixture is provided with a space for forming a small air reservoir in the upper part of the storage chamber. It is configured to regulate the upper limit of accommodation. Embodiments will be described below with reference to the drawings of the embodiments. 1 to 4, reference numeral 1 denotes a pressure reducing device using a water ring type vacuum pump or an exhaust blower, and 2 denotes a recovery tank which is made to have a negative pressure by the operation of the pressure reducing device 1. And two lower chambers 2a and 2b. Each of the lower chambers 2a and 2b has a funnel-shaped inclined surface 3a and 3b, respectively, and has a rectangular hole at the bottom. 4 and 4 are established respectively.
Reference numeral 5 denotes a suction pipe led down from the flow chamber 2a, and the leading end 5e of the suction pipe opens toward the supply source 6 of the solid-liquid mixture. 5 v is an open / close valve attached to the suction pipe 5, 7 is a first decompression pipe line configured by connecting the upper part of the flow chamber 2 a and the suction side 1 a of the decompression device 1 by the first suction pipe 8, 9
Is a liquid recovery tank interposed between the suction side 1a of the pressure reducing device 1 and the first suction pipe 8, 10 is a flow control valve attached to the first suction pipe 8, and 11 is above the wall surface of the storage chamber 2b. Pores opened in the upper portion than the open lower edge portion 12e of the first normally open lip valve 12a described below,
11s is a solid-liquid separation screen attached to the pore 11;
Reference numeral 3 denotes a second decompression pipe formed by connecting the pores 11 and the suction side 1a of the decompression device 1 with a second suction pipe 14, and the second decompression pipe line includes the suction side 1a of the decompression device 1 and the second suction pipe 14. A liquid component recovery tank 9 is interposed between the tanks. Reference numeral 15 denotes a pressure-increasing passage which is led out of the second suction pipe 14 in a branched manner and is conducted to some negative pressure releasing means 16.
And a valve mechanism for opening and closing the storage chamber 2b to and from the negative pressure releasing means 16 when the valve is closed. For example, when the second pressure reducing pipe 13 is closed, Open to the inside or the air line 18
A positive pressure is supplied into the storage chamber 2b by opening the exhaust side 1b of the decompression device 1 through the air passage, or by opening a separate air supply device (not shown), or the like. The pressure increasing path 15 is also closed together with the closing. Therefore, the valve mechanism 17 opens the storage chamber 2b with either the second pressure reducing pipe 13 or the pressure increasing path 15, and when the storage chamber 2b opens with the second pressure reducing pipe 13, the storage chamber 2b is opened.
And the pressure increasing passage 15 is disconnected, and the storage chamber 2b is connected to the pressure increasing passage 1
5, the opening and closing operation is performed so that the opening between the storage chamber 2b and the second pressure reducing conduit 13 is cut off. However, if necessary, the storage chamber 2b may be closed with both the second pressure reducing pipe 13 and the pressure increasing path 15. In the drawings of the embodiment, the branch point between the second pressure reducing line 13 and the pressure increasing line 15 is
In this embodiment, three three-way switching valves are interposed to open and close the second pressure reducing pipe 13 and open and close the pressure increasing path 15, but the three switching valves are used. (2) The opening and closing of the pressure reducing line 13 and the opening and closing of the pressure increasing passage 15 may be performed by separate switching valves. Thus, when the pressure reducing device 1 is operated, the pressure conversion mechanism having both the function of reducing the pressure in the storage chamber 2b to the same pressure as the pressure in the flow chamber 2a and the function of raising the pressure to the same pressure as the atmospheric pressure is provided. It is composed. The first normally-open lip valve 12a, which is mounted so as to communicate from the lower bottom of the flow chamber 2a into the storage chamber 2b, operates when the flow chamber 2a and the storage chamber 2b are in a negative pressure state. When the open state is maintained by the elasticity and the pressure in the storage chamber 2b becomes higher than the pressure in the flow chamber 2a, the closed state is established by the differential pressure. The second normally-open lip valve 12b mounted to communicate with the atmosphere from the lower bottom of the storage chamber 2b is connected to the atmospheric pressure when the flow chamber 2a and the storage chamber 2b are in a negative pressure state. When the closed state is established by the differential pressure and the pressure in the storage chamber 2b becomes positive, the state is restored to the open state by its own elasticity. These two lip valves 1
FIGS. 5 and 6 show specific structural examples of 2a and 12b.
A fastening plate 19 is provided around the upper edge of the square tubular valve element as seen in FIG.
To form an attachment portion, and is attached to the edge of the rectangular hole 3 via a valve seat 12f as shown in FIGS.
And a rotating wall 2 facing the front and rear below the mounting portion.
0 and 20, reinforcing plates 21 and 21 and a roll-up preventing material 21s,
21s to provide rigidity to the rotating walls 20, 2
The flexing and extending walls 22, 22 connected to the side end of the elastic member 0 have flexibility, and the lower edges of the rotating walls 20, 20 are formed on the depressing and separating surfaces 23, 23, respectively, so that external pressure can be reduced. Bending wall 2 by action
The rectangular holes 4 are closed by the bending walls 2 and 22 being bent and the rotating walls 20 and 20 rotating in the direction of approach to each other to close the separating and contacting surfaces 23 and 23. When the external pressure is released, the bending / extending walls 22, 22 are extended, and the turning walls 20, 20 are turned in the separating direction to separate the contact surfaces 23, 23, so that the rectangular hole 4 is opened. You. Referring again to FIGS. 1 to 4, reference numeral 24 denotes a sand sensor for detecting the state of solids accumulation in the storage chamber 2b, and reference numeral 25 denotes a solid-liquid separation screen provided in the flow chamber 2a. The support member 26 fixed above the suction pipe inlet 5h on the inner surface of the peripheral wall of the chamber 2a has a mode in which the support member 26 is laterally installed in a loose fit state and can be vertically shaken. Reference numeral 27 denotes a submersible pump installed in the liquid collection tank 9, reference numeral 28 denotes a liquid return pipe derived from a discharge port of the submersible pump 27, and a leading end portion 28 e of which is provided in the supply source 6 of the solid-liquid mixture. Is introduced into the lower part of the opening. In addition,
The first normally-open lip valve 12a, which is mounted in the rectangular hole 4 at the bottom of the flow chamber 2a and guided into the storage tank 2b, not only serves as a flow path for the collected material when opened, but also as a storage path as described later. It also serves as a liquid rise path from inside the chamber 2b, and its open lower edge 12e needs to reach below the opening position of the pore 11. When the pressure reducing device 1 is not driven, the pressure in the circulation chamber 2a and the pressure in the storage chamber 2b are balanced and equal to the atmospheric pressure, so that the first pressure as shown in FIG. The normally open lip valve 12a and the second normally open lip valve 12b are both kept open. The pressure reducing device 1 is driven by the pipe configuration shown in FIG. 1 with the leading end 5 e of the suction pipe 5 directed toward the solid-liquid mixture supply source 6, and the first pressure reducing pipe 7 is operated by the operation of the valve mechanism 17. When the second pressure reducing pipe 13 is opened and the pressure increasing path 15 is closed, the outside air is sucked from the bottom rectangular hole 4 of the storage chamber 2b which is in contact with the atmospheric pressure, and the suction action is performed as shown in FIG. As shown, the second normally-open lip valve 12b is closed, and by continuing to drive the pressure reducing device 1, the inside of the flow chamber 2a is bled via the first pressure reducing line 7, and the inside of the storage chamber 2b is subjected to the second pressure reduction. Since the air is extracted through the pipe 7 and both chambers 2a and 2b have a negative pressure, the solid-liquid mixture pumped up with some air from the suction pipe 5 has a funnel-shaped inclined surface 3a in the flow chamber 2a. Flows down and is stored in the storage chamber 2b from the open rectangular hole 4 at this time. The pressure in the second lower lip valve 12b acts on the second normally-open type lip valve 12b, and the lower bottom rectangular hole 4 is firmly closed, so that the pressure in the storage chamber 2b is reduced. The outflow of the liquid mixture is prevented and the airtightness is maintained. In the embodiment of the present invention, the pressure ratio between the two chambers 2a and 2b in the state shown in FIG. 2 is completely the same by completely equalizing the pipe resistance of the first pressure reducing pipe 7 and the second pressure reducing pipe 13. When the negative pressure is advanced to some extent without forming a complete vacuum state, the first normally-open lip valve 1
2a opens 100%. Also, for example, the first suction pipe 8
The pipe resistance of the first pressure reducing pipe 7 is made slightly larger than the pipe resistance of the second pressure reducing pipe 13 by reducing the pipe diameter, increasing the pipe length, or operating the flow control valve 10. In this case, the degree of negative pressure in the storage chamber 2b is slightly larger than the degree of negative pressure in the flow chamber 2a, so that the opening operation of the first normally-open lip valve 12a is performed more reliably and the second
The closing operation of the normally-open lip valve 12b can be ensured. During the operation of the pressure reducing device 1, the solid-liquid mixture is continuously fed through the suction pipe 5, and the storage amount of the solid-liquid mixture flowing down from the flow chamber 2a to the storage chamber 2b gradually increases.
Rises to the open lower edge 12 e by remote above the first normally open lip valve 12a, elevated while forming a slight air reservoir 29 to the upper periphery of the O cormorants savings reservoir 2b shown in FIG. 3 is regulated And
Above that, the liquid component cannot flow down into the storage chamber 2b and remains in the flow chamber 2a, and only solids having a large specific gravity flow down to further push up the liquid surface in the storage chamber 2b. Since the effect is suppressed by the air reservoir 29 formed in a liquid surface form, the liquid in the storage chamber 2b is conversely moved back to the open rectangular hole 4 to the circulation chamber 2a. Due to such a solid-liquid exchange action, solids having a low water content gradually accumulate in the storage chamber 2b with the passage of time. When a predetermined time has elapsed since the second normally-open lip valve 12b was closed, the second pressure reducing line 13 was closed by the switching operation of the valve mechanism 17, and the pressure increasing line 1 was turned on.
5 is opened to release the negative pressure state in the storage chamber 2b, so that the first normally open lip valve 12a as shown in FIG.
Is closed and the second normally-open lip valve 12b returns to the open state, and solids having a low water content in the storage chamber 2b are discharged from the rectangular holes 4 to the outside. During this time, the inside of the flow chamber 2a is maintained in a negative pressure state, and the solid-liquid mixture is continuously fed from the suction pipe 5. Negative pressure release means 1 in storage chamber 2b
6, the second pressure reducing passage 13 is closed and the pressure increasing passage 15
Is opened to the atmosphere to equilibrate the inside of the storage chamber 2b with the atmospheric pressure, and the pressure increase path 15 is opened to the exhaust side 1b of the pressure reducing device 1 or to a separate air supply device to open the storage chamber 2b. Can be set to a pressure higher than the atmospheric pressure. By adopting the latter method, the opening operation of the second normally-open type lip valve 12b can be performed more reliably and the first normally-open type lip valve 12a can be closed. The condition can be strengthened. When the solid-liquid mixture stored in the storage chamber 2b is discharged as described above, the switching operation of the valve mechanism 17 causes the second pressure reducing pipe 13 to be in the open state, and the pressure increasing path 15 to be in the closed state. As a result, the inside of the storage chamber 2b is in a negative pressure state, so that the second normally-open lip valve 12b closes and the first normally-open lip valve 12a returns to the open state, as shown in FIG. The solid-liquid mixture discharged from the pipe 5 flows down along the funnel-shaped inclined surface 3a in the flow chamber 2a and is stored in the storage chamber 2b from the open rectangular hole 4. And the first normally open lip valve 1
The closing operation of the 2a and the second normally-open type lip valve 12b is performed in such a manner that the depressing and separating surfaces 23, 23 are brought into surface contact with each other and closed, so that foreign matters such as sand particles are closed on the closing surface. Even if it is bitten, the foreign matter is wrapped between the depressing and separating surfaces 23, 23, and the airtightness of the closing surface is maintained. The switching operation of the valve mechanism 17 is performed as follows.
The operation may be automatically performed at predetermined time intervals by setting a timer, or may be electrically performed based on a detection signal obtained by detecting a solid deposition state using a sand sensor 24 or the like. By the repetition of the alternate opening and closing operation of the first normally open lip valve 12a and the second normally open lip valve 12b accompanying the switching operation of the valve mechanism 17, solid-liquid mixing continuously sucked through the suction pipe 5 is performed. An operation of intermittently discharging the body as a solid having a low water content from the storage chamber 2b is performed. The liquid content in the flow chamber 2a is further removed by a solid-liquid separation screen 25, and the liquid recovery tank 9
The screen 25 has a large cross-sectional area of water flow and a low flow velocity. Also, the screen 25 is loosely fitted by the support member 26 and slightly vibrates up and down. There is no. In the process of sucking and discharging the collected material, the liquid mixed during the ventilation from the collection tank 2 to the liquid collection tank 9 is collected into the liquid collection tank 9 and returned by the operation of the submersible pump 27. The liquid is reduced into the original supply source 6 through the pipe 28. However, when the liquid component flows out from the leading end 28e, a mixing and stirring action occurs in the supply source 6 to solidify the liquid from the suction pipe distal end 5e. It makes it easy to inhale the minute. According to the present invention, the continuous suction and quantitative intermittent discharge operation of the collected material are reliably performed, and the collected solid-liquid mixture is discharged as a solid having a low water content in the collection tank. Therefore, there is an advantage that a separate post-treatment by a solid-liquid separation device becomes unnecessary.

【図面の簡単な説明】 【図1】本発明装置における作動態様の説明図であっ
て、減圧装置未駆動時の状態を示す。 【図2】本発明装置における作動態様の説明図であっ
て、吸込管により揚送されて来る固液混合体が流通室内
の漏斗状傾斜面に沿って貯溜室内へ流下する状態を示
す。 【図3】本発明装置における作動態様の説明図であっ
て、固液混合体が貯溜室内に貯溜されてその上方部に空
気溜まりを形成した状態を示す。 【図4】本発明装置における作動態様の説明図であっ
て、貯溜室内に堆積した固分が下底部から排出される状
態を示す。 【図5】本発明装置に装着される常開型リップ弁の開状
態における斜視図である。 【図6】本発明装置に装着される常開型リップ弁の開状
態における縦断側面図である。 【図7】本発明装置における常開型リップ弁装着用弁座
の斜視図である。 【図8】本発明装置における常開型リップ弁装着用弁座
の縦断側面図である。 【図9】本発明装置に装着された常開型リップ弁の開状
態における側面図である。 【図10】本発明装置に装着された常開型リップ弁の閉
状態における側面図である。 【図11】従来の装置における作動態様の説明図であっ
て、減圧装置未駆動時の状態を示す。 【図12】従来の装置における作動態様の説明図であっ
て、吸込管により揚送されて来る回収物が第1貯溜室内
に貯溜された状態を示す。 【図13】従来の装置における作動態様の説明図であっ
て、第1貯溜室内の貯溜物がその重量により上室ハッチ
を下傾状に開放させつつ第2貯溜室内へ落下する状態を
示す。 【図14】従来の装置における作動態様の説明図であっ
て、第2貯溜室内の貯溜物がその重量により下室ハッチ
を下傾状に開放させつつ外部へ排出される状態を示す。 【符号の説明】 1 減圧装置 1a 吸込側 2 回収タンク 2a 流通室 2b 貯溜室 5 吸込管 6 固液混合体の供給源 7 第1の減圧管路 8 第1の吸引管 9 液分回収タンク 12a 第1の常開型リップ弁 12b 第2の常開型リップ弁 13 第2の減圧管路 14 第2の吸引管 15 増圧路 16 負圧解除手段 17 バルブ機構 29 空気溜り
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an explanatory view of an operation mode in the device of the present invention, showing a state when a pressure reducing device is not driven. FIG. 2 is an explanatory view of an operation mode in the apparatus of the present invention, and shows a state in which a solid-liquid mixture discharged by a suction pipe flows down into a storage chamber along a funnel-shaped inclined surface in a flow chamber. FIG. 3 is an explanatory view of an operation mode in the device of the present invention, showing a state where a solid-liquid mixture is stored in a storage chamber and an air reservoir is formed above the storage chamber. FIG. 4 is an explanatory view of an operation mode in the device of the present invention, showing a state where solids accumulated in a storage chamber are discharged from a lower bottom portion. FIG. 5 is a perspective view of a normally-open lip valve mounted on the device of the present invention in an open state. FIG. 6 is a vertical side view of the normally open lip valve mounted on the apparatus of the present invention in an open state. FIG. 7 is a perspective view of a valve seat for mounting a normally open lip valve in the device of the present invention. FIG. 8 is a vertical sectional side view of a valve seat for mounting a normally open lip valve in the device of the present invention. FIG. 9 is a side view of the normally open lip valve mounted on the apparatus of the present invention in an open state. FIG. 10 is a side view of the normally-open lip valve mounted on the device of the present invention in a closed state. FIG. 11 is an explanatory view of an operation mode of the conventional device, and shows a state when the pressure reducing device is not driven. FIG. 12 is an explanatory view of an operation mode in the conventional device, and shows a state in which a recovered material pumped up by a suction pipe is stored in a first storage chamber. FIG. 13 is an explanatory view of an operation mode in the conventional device, and shows a state in which the stored matter in the first storage chamber falls into the second storage chamber while opening the upper chamber hatch downwardly by its weight. FIG. 14 is an explanatory view of an operation mode of the conventional device, and shows a state in which the stored material in the second storage chamber is discharged to the outside while opening the lower chamber hatch downwardly by its weight. [Description of Signs] 1 Decompression device 1a Suction side 2 Recovery tank 2a Distribution chamber 2b Storage chamber 5 Suction pipe 6 Solid-liquid mixture supply source 7 First decompression pipe line 8 First suction pipe 9 Liquid collection tank 12a 1st normally open type lip valve 12b 2nd normally open type lip valve 13 2nd decompression pipe line 14 2nd suction pipe 15 booster path 16 negative pressure release means 17 valve mechanism 29 air pool

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−50292(JP,A) 特開 平6−50296(JP,A) 特開 平3−230000(JP,A) 実開 昭54−183702(JP,U) (58)調査した分野(Int.Cl.7,DB名) F04F 1/02,1/06 F04F 3/00 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-6-50292 (JP, A) JP-A-6-50296 (JP, A) JP-A-3-230000 (JP, A) 183702 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) F04F 1 / 02,1 / 06 F04F 3/00

Claims (1)

(57)【特許請求の範囲】 【請求項1】 流通室(2a)から導出される吸込管
(5)を固液混合体の供給源(6)へ向けて開口させ、
流通室(2a)から液分回収タンク(9)を経て減圧装
置(1)に至る第1の減圧管路(7)を開通させて流通
室(2a)内を負圧となし、貯溜室(2b)から液分回
収タンク(9)を経て減圧装置(1)に至る第2の減圧
管路(13)を開通させて貯溜室(2b)内を負圧とす
ることにより、流通室(2a)の下底部から貯溜室(2
b)内へ通ずるよう装着された第1の常開型リップ弁
(12a)を自らの弾力により開放状態に保持させると
共に貯溜室(2b)の下底部から大気中へ通ずるよう装
着された第2の常開型リップ弁(12b)を大気圧との
差圧により閉合させ、上記大気圧との差圧により吸込管
(5)から吸い込まれる固液混合体を第1常開型リップ
弁(12a)の開口面から貯溜室(2b)内へ流下さ
せ、上方部に若干の空気溜り(29)を残して貯溜室
(2b)内がほぼ満杯状態となったのち流通室(2a)
内に残存する固液混合体中の固分のみを固液の比重差を
利用して貯溜室(2b)内へ流下させるのと入れ替えに
上記固分の体積と同体積の液分を貯溜室(2b)から流
通室(2a)内へ上昇させ、減圧装置(1)の駆動を中
断することなく流通室(2a)内の負圧状態を保持しつ
つ第2減圧管路(13)を閉塞すると共に貯溜室(2
b)から負圧解除手段(16)に通ずる増圧路(15)
を開通させて貯溜室(2b)内を正圧とすることによ
り、第1常開型リップ弁(12a)を上記2室(2a)
(2b)間の差圧により閉合させると共に第2常開型リ
ップ弁(12b)を自らの弾力により開放復帰させ、貯
溜室(2b)内において含水比の低くなった固液混合体
を第2常開型リップ弁(12b)の開口面から外部へ排
出させることを特徴とする吸引式回収方法。
(57) Claims 1. A suction pipe (5) led out from the flow chamber (2a) is opened toward a solid-liquid mixture supply source (6),
A first decompression line (7) from the flow chamber (2a) to the decompression device (1) through the liquid recovery tank (9) is opened to make the inside of the flow chamber (2a) a negative pressure, and the storage chamber ( By opening a second decompression pipe (13) from the liquid decompression device (1) to the decompression device (1) through the liquid recovery tank (9) to make the inside of the storage chamber (2b) a negative pressure, the flow chamber (2a) is opened. ) From the bottom of the storage chamber (2
b) The first normally open lip valve (12a) mounted to communicate with the inside is held open by its own elasticity, and the second normally mounted lip valve (12a) is mounted to communicate from the lower bottom of the storage chamber (2b) to the atmosphere. The normally open lip valve (12b) is closed by a differential pressure from the atmospheric pressure, and the solid-liquid mixture sucked from the suction pipe (5) by the differential pressure from the atmospheric pressure is supplied to the first normally open lip valve (12a). reservoir from the opening surface of) (passed down into 2b) within reservoir leaving some air pockets (29) in the upper part (after 2b) in becomes nearly full state flow chamber (2a)
Instead of letting only the solids in the solid-liquid mixture remaining inside the solid-liquid mixture flow down into the storage chamber (2b) by utilizing the specific gravity difference between the solids and liquids, a liquid having the same volume as that of the solids is stored in the storage chamber. (2b) is raised into the flow chamber (2a), and the second pressure reducing pipe (13) is closed while maintaining the negative pressure state in the flow chamber (2a) without interrupting the operation of the pressure reducing device (1). And the storage room (2
Pressure intensifier (15) leading from b) to negative pressure release means (16)
Is opened to make the inside of the storage chamber (2b) a positive pressure, so that the first normally open lip valve (12a) is connected to the two chambers (2a).
(2b) and the second normally-open lip valve (12b) is opened and returned by its own elasticity, and the solid-liquid mixture having a low water content in the storage chamber (2b) is closed by a second pressure. A suction type recovery method comprising discharging the normally open lip valve (12b) to the outside through an opening surface thereof.
JP18920593A 1993-06-30 1993-06-30 Suction type recovery method and device Expired - Lifetime JP3535191B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18920593A JP3535191B2 (en) 1993-06-30 1993-06-30 Suction type recovery method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18920593A JP3535191B2 (en) 1993-06-30 1993-06-30 Suction type recovery method and device

Publications (2)

Publication Number Publication Date
JPH0719199A JPH0719199A (en) 1995-01-20
JP3535191B2 true JP3535191B2 (en) 2004-06-07

Family

ID=16237297

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18920593A Expired - Lifetime JP3535191B2 (en) 1993-06-30 1993-06-30 Suction type recovery method and device

Country Status (1)

Country Link
JP (1) JP3535191B2 (en)

Also Published As

Publication number Publication date
JPH0719199A (en) 1995-01-20

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