JPS5932910A - Apparatus for conveying out precipitated solid substance - Google Patents
Apparatus for conveying out precipitated solid substanceInfo
- Publication number
- JPS5932910A JPS5932910A JP14226182A JP14226182A JPS5932910A JP S5932910 A JPS5932910 A JP S5932910A JP 14226182 A JP14226182 A JP 14226182A JP 14226182 A JP14226182 A JP 14226182A JP S5932910 A JPS5932910 A JP S5932910A
- Authority
- JP
- Japan
- Prior art keywords
- solid
- solid substance
- liquid
- spiral blade
- liquid component
- 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.)
- Granted
Links
- 239000007787 solid Substances 0.000 title claims abstract description 56
- 239000000126 substance Substances 0.000 title abstract 11
- 239000007788 liquid Substances 0.000 claims abstract description 38
- 238000000926 separation method Methods 0.000 claims abstract description 14
- 239000011343 solid material Substances 0.000 claims description 9
- 239000010419 fine particle Substances 0.000 abstract description 7
- 238000007599 discharging Methods 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 abstract 1
- 239000002245 particle Substances 0.000 description 8
- 241001474791 Proboscis Species 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000004576 sand Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 241000931705 Cicada Species 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 210000003746 feather Anatomy 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 241000102542 Kara Species 0.000 description 1
- 101000905241 Mus musculus Heart- and neural crest derivatives-expressed protein 1 Proteins 0.000 description 1
- 235000021170 buffet Nutrition 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 235000021055 solid food Nutrition 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 230000035922 thirst Effects 0.000 description 1
Abstract
Description
本発明は水処理装置において沈澱lh」彫物と液分とを
分離し、固形物のみを系外に(ンノ出する装置11′に
関づる。
固液分離装置uVtには神々あるか、車力式固液分離装
置には、分肉iFされた固形物の搬出に併械的方法が最
も多く用いられている。本発明は1、その機械的(el
il装出において、固形物搬出筒内((固転自在に収容
した、立型螺旋羽根と、この螺旋羽根に形成した返送用
孔[1−れ、よび固形物搬出筒側向に形成した返送用排
出孔により、同形物の−・部を固液分離装置1を内と固
液分離層を循環させることにより、有轡性微粒子智の1
;W粒子剥離効率を高めて、固液分離を行なわせるよう
に1〜たもので、4る。
沈澱固形物の搬出装置ジの一例を第1図に示1゛、1は
重力式同液分離槽である。被処理液は、流入ゞ1へ・2
より流入し、液中の固形物は固液分離槽1にて固液分離
され、液分は流出口るより放出される。
固形物層は、沈澱固形物として槽下部にイL潰され、索
条4に懇垂された多数のバフツ5にてl蚤寄搬出される
。バフツ5によって搬出された沈澱固形物は、固液外1
ii11: 4’、I!l 1 、 l一部に設置?!
されたベルトコンベヤ6にて糸外に持出される。なお、
1N・Jl装出uの索条4の駆動は、伝達歯車7にて行
い、七“の索条4の案内が8の滑i[である。また9か
駆動装置である。
上記従来の沈澱固形物の1す)H−1−’; iij’
lτおい−11、装置のe’7 i?’l上、ハケッ
5目沈ボよ固形物層ど液5〕の分離が不可能なこと、ま
た沈り慢1+’a11ヒト7・1に附着した有機性微粒
子をもその上i: qq:y +i1t、、(豊〃)に
おいて別途微粒子剥pr*操作後、固形物を糸外に((
“ン出−(−イ)という二重の操作?−j稈を心火と′
(イ・欠I+、′jかあ<s nさらに搬出装置庁の必
要hII)力は、?J’7”r、Q国彫物C〜掻さ′に
)′せ1・よび、搬出用の動力/工らひK ’fl檀性
イ1”・ν(・ンそ剥離1・■・作に必安な動力である
か、ぞV)殆んどが搬出タニ1i!¥およびj)々心シ
子+’(J離操11′・に消イアされて、ら・ll、特
にバフツ5による固形物σ−■、1′:L1脣(,1キ
[−7、液分もいっしょに搬出セさるをイ(トないの卵
l力t 、I Clスか大きい。
不発明は上呂ピ従来の沈びρ同形物c〕月′5I、・出
装置白“の欠点を除去し、単一の装置に′て沈(ZS固
tl” !l>りの搬INと固形9ククに附尤した粒子
のl’!+’g去とし・52つの機能苓・愕(すことを
目的としてなさ才tだもの−C11期形1勿卦1ン出市
内に蝉旋羽する回転自在に収′ど≠し、この螺Mij羽
根に孔(返送用孔IEI )を形fjV L、かつ固形
物搬出筒の111117rnに孔(返送用排出(−1)
を肘成l〜、す・メ旋羽根を回転車diノI」−ること
1C11、す、tlり分1・1.1、ひ固形I吻に附着
した微粒子を、j−心分離!−て分1iillシトれた
液体を返送用、几[−1オ・うよO−コ1ン必用排出「
1ろ・11111.、= ’で[The present invention relates to a device 11' that separates precipitated objects and liquid components in a water treatment device, and discharges only the solids out of the system. In solid-liquid separators, a mechanical method is most often used for transporting solids that have been divided into particles.
In the solid material unloading, a vertical spiral blade is housed in the solid material discharge cylinder ((a vertical spiral blade is housed in a rotatable manner, a return hole is formed in the spiral blade, and a return hole is formed in the side of the solid material discharge cylinder). By circulating the same-shaped particles through the solid-liquid separator 1 and the solid-liquid separation layer through the discharge hole, one part of the wasteful particulate matter is removed.
; 1 to 4 to increase W particle separation efficiency and perform solid-liquid separation. An example of a device for discharging the precipitated solids is shown in FIG. 1. 1 is a gravity-type liquid separation tank. The liquid to be treated flows into 1 and 2.
The solid matter in the liquid is separated into solid and liquid in the solid-liquid separation tank 1, and the liquid is discharged from the outlet. The solid layer is crushed in the lower part of the tank as precipitated solids, and is carried out by a large number of buffs 5 suspended from cables 4. The precipitated solids carried out by the buffet 5 are
ii11: 4', I! l 1, l installed in some parts? !
The yarn is carried out by the belt conveyor 6. In addition,
The cable 4 of the 1N/Jl loading u is driven by the transmission gear 7, and the guide of the cable 4 of 7" is the slide i of 8. Also, the drive device 9 is used. Solid matter 1) H-1-';iij'
lτ hey-11, device e'7 i? In addition, it is impossible to separate the solid matter layer and liquid 5], and also the organic fine particles attached to the human body 7.1. After a separate fine particle peeling pr* operation at y + i1t,, (Yutaka), the solid matter was removed from the thread ((
“Double operation called “N-de-(-i)”?
(I・lack I+,'jkaa<s nfurthermore, the necessary hII of the unloading equipment agency) What is the force? J'7"r, Is it an indispensable power source?V) Most of them are carried out with the 1i! ¥ and j) The solid matter σ-■, 1':L1脣(,1ki[-7, The liquid content is also carried out together. Eliminates defects and removes the particles attached to the solid 9 kg with a single device. (It was not intended to be used as a gift.) Place the cicada in a rotatable manner so that the cicada's whirling wings can be freely rotated in the C11th period form 1, and make a hole (return hole IEI) in this threaded blade. fjV L, and a hole (return discharge (-1)
The particulate matter attached to the solid I proboscis is separated from the j-center! - For returning the spilled liquid, it is necessary to discharge the liquid.
1ro・11111. ,=' with [
【−1計分1)jjF
(1,10内に、14ジし、固形物10ツメ、を糸夕
(に1ハJ flJ−イるようK t、ている。また1
iil [i=rに、1.’、I形σ) −、、、FI
Bイヒ鈷り込部IJJrtlj [1カラ固’Af分子
fi:i槽K y L、 ティ1lli Bl 8 )
!−7,)、)−トにより、固)ヒ物の附R’; シた
他・粒子の4E Puffり1j2・ト(4・面めてい
る。
以下本ジ?、明4・2442図とハλ3図にントず′人
カバ14例について’6[’ #tllに贋明l−る。
24ル2図にyi<ず実か11しIIにおいては車力式
固?イ’<分離槽11は槽下↑11Xを円錐形とし、沈
澱固形物層12の沈設固形物を伯のθぼ中央に白[−置
した本発明にかかる搬出装置i<1’、 J(1((i
lより人出するものであイ)。
飯出装f市)10は、同液分離槽1】内において被処理
液の畝面にほぼ垂的力向に設置r(さtした円筒ルの立
、jqJl固ハ゛ジ物11q出筒1;3を1.li+i
え、この固J1イ物1)、、出ii’1)13は一ト嬬
か沈澱固形物層12に接する開放V;1! I3Aとさ
れ、子端1λISにおいて固形物伴出C11/4に伸’
:1Jil L−ていイ〕。
図示の実施(’、/II においてこの固形物口:=
I11筒1;3に1.1:3a〜13dで示す各部分で
4Hu成さねてし・イ、。この実施1<中で6オ、こね
ら名iW、 1’J a 〜I’、((1’7+、□
6J虞1F If’ 、+i、’jと、L、゛で継ぎ合
ぜて+f17成し7ているが、−・A、の′1llll
’肯で構成し7゛Cもよいことは勿a=である。固バ
ー′物几出摘H1’iにはけばその全艮にわたって4j
、宰旋羽枦111をIj、V (・1し1“回転liす
1117が配設され−Cいる。螺1n+・羽根1(+は
沈澱固j1ユ9勿の′向性に背7合羽根角な41すイ)
ようV・−止ツlノψされている。
ところで、1句形j1..’441撮出筒13t’Cお
いて、いも(・1ん下の[:3aで示した部分は開放7
i、i l:i Aか”)+’、’t、 i8’2固力
・物枦上方に込り込も、固jt’; !It/月y、述
部−ひ渇・イ)。また1:(Cは固形物の固液分画操作
により’yje)lされた微粒子を含む液分な固/fk
分l(1ハ11に戸“I J、4送用+II出イ1]5
を具えた返送部である。こθ)返送部II Cにオ(く
ける4累旋羽根16には、第3図に51.1ように孔(
返送用1(L[」) t(i aかル成されてオいり、
固ire分p:lIl某作中、固形物の一部をこの、比
1(i a J3−、iJ+(して吊−1さ一1↓返送
用排出孔15を通して固液分離)111にPされるよう
にt7ていイ)。固形物搬出筒13(、・・1.’(d
”C゛糸し2/、−1t;1分は固沿分曲トされた固
形物を螺旋羽根にで搬j/、[7固形′吻((f) L
1口114から1+’y−;出すイ)固ノする物搬′出
部である。また、同形物J送込部1:(aと六送部13
cとの間に狭まれたjt(分1:3bは、螺旋羽根1G
の回111.% 1141117の11itt受18を
イll′持する部分でル)イ・。回転11η1;1フイ
、・)+ス。1は適宜の伝達枦jfl 191x介して
駆1Jjj+装fi’i 20区]1・it1’iされ
ている。なお21は流入管、22は流出口、23はベル
トコンベヤである。
次に、相゛・作付(1イについて着叫1イ)。中力r(
固l(り分会[目・、l′j11のt(叙li1吋4′
臣げ籾・)下部力叶1省jj Jに N)たi)槽下名
l)中央に11す、液分?ともに固形物11ゞ)□・出
前13の固ノ1<、物J2込81・、J3 a K休り
込ま才1ろ。区り込まわたit“、数置彫物とlIl、
分(工、■弊711y羽根16の1111上において、
)!Ij心分l’Jされブ、(からpu; +r;r方
向K /l’を動11〕。、−の遠心外1+4i+!I
tノ1作の間に1・・いて、沈(>、;固形42・1に
ト11循しているイ]槻件做杓子熔、の微粒子は剥離さ
才1イ)1、分t’ilfされた成分はjlr−’11
q力向移勤行程中、ゾ・く送j41ζ1;3Cに:jt
りいて某七h;V平1根]、(5に6丈けられた返1本
月1化11]t)aよりそのドのヒ゛ツナの曵υifu
羽)1艮16ににf古[し、1・111コ−遠心外1”
+iトi+Hh作を有り。Illら返送fall 1.
’(C内にオ・Sけイ)固形乍ノIの油時間は増加−f
イ)こととなりイーれだし)イ;□1■粒子の剥綜さi
る111合が増大−するう次に返送7i口:3与下部(
C設けQ旬)た7J・4込用1j18出孔15より、返
送部Is cにおいて固液外1’J o′″−噌また液
分と<y−uλ〔された微オ゛党−子および固Jヒ′(
切タトの一7〜1NtHをし占」液分m(t i・hl
lに排出する。4″だ、固)13物送込部1;3の返送
j+1XI30 K送込まれるμ′赦固形物の一部量も
排出する。このとき近、r% RB 13cに4・9い
ても、固jヒq勿は遠心分N4 h、’I作が締返えさ
れ、返き部1.3cνCおけるμm]着微粒子411μ
ljtの補助操作とf、(−)て(・る。
以上のようにして沈鮫固Jするt吻中(〕、4做釈!子
とak分を115)、去した固形′吻1亜ノ1;ヒ羽根
10で上刃に運はitて固形q勿1般出口14から排さ
れ7、ベルトコア・ベヤーハで[N;l i夜分膿僧]
1の/A4・・−トfち出される2、本発明における操
4′)、実験の一1旬を都市ト水について使用した結!
A^をン背四1−イ)。
1i4+、知のごとく、1−水の処理装置は1、下水の
3止れる固形物除去操作同形物心7 <a、 0.2p
”−以上の^(11砂分およびそれ以外の粒子外に分類
し、これ等の固]1.z。
物除去処理を一次処理行程と呼んで℃・4)。
上記の処■4−1!イ’Tbのうち、除砂操作に、tt
iいて、砂に耐着した有機rト倣iN′?子が末広1i
ly 1.ti後にp1敗をおこI7、処P■1装さ+
の大きな弊害となっている。よって本実験処おいては、
号?旋羽根16の羽根角および回転x9はI(1″X砂
物の内部Ir察保叔を1!’+−251与の範囲の関数
と(7て取扱い、また、返テ2′ζ川穴目1(i aを
各ビツヂごとに螺;J年羽横lGの:’HFj’(j方
向込1.1−のJ)係前後の返送範囲に設定し、かつ返
送部14Ji帛穴」5の排出に庵もそのh・1囲どI−
ゴニ。
J’−1十の条作に! /、l、チル^・結果は、1^
」ノド9勿4ノIIL+ +114より搬出さAまた0
中の有機グ1倣粒子の含4U’−1tlは殆んどプエく
、0.2+vI+僅以下の固形物h1も殆んど無視でき
る結果で1・・つた。
以上の結果から、本発明による固液分ll;IF装凶に
jこれは往来法のものに比較し、単−装(6,にて汀、
内円彫物1i1着倣粒子の;t 1+ pr++除去か
13−i能とな4)はかりか、適切なる羽根角および羽
根回転数の条件下において、立型螺JM羽根の固j19
物返送川孔[jのqネに羽根半径方向の位1山を変える
ことにより、(眼出固ノヒ物の限シ“f−峯)賀争、即
ち、固形物の分級を任、意に設定できることとなる。ま
た、士、d郁rt 、’d:r ri割粉粒子剥除効率
(土、固形′吻置送孔1−4の大小どイ151数および
1j4送川4JI出孔の大小シimよる返送固形IV7
)1の各槽pj、、量によって可能となイ)。次に、第
1M1、よひ自42図から明らかなごとく、lt:g出
・)・°i置の備逓1゛白+−i格−1、・榛1〆4の
設置il′ti 11?か小さく、が−) )IL−!
ji’j旨体がカ1)鴫什−c゛き、設備iI′φの
低減がvノ+侍tllJ来るとともに、その簡ト1;〜
化の結果、総i−?、jlIIl ti[ti力のハ/
jλは11旧)がでに1べ)。
1ノl i+iiのli’i J4”先な糾明ja+
] ly、目1、t&l ?fk分闘1(乃セ”φ
作Cハイ1來θ、(〕)〕重カ式1−61iT+分1セ
]1槽の−pHをボ″3図で乞ハる。第2[月はこの一
部(明(り一実施例を7f−″す[1、(o:3図は第
20の装置tバー↑)1(拡大れ岨1tI?i自1トI
、ン7’、 4 「図は第:(l””、) +i+i
VJ丁1菫し]でA・)る。
10・・・同液分離見IKt 、 II・・・固成り月
−、′[山。
13・・1市i形物1に、□;出山部1・1・・・固形
物1・i!1101゜J5・・・返送用91出孔、16
・・・Nu: jk小羽根lt、i a −A送用孔、
1r−=−回E fall 、 21− ?11+、
人口。
22・・・3ii 出口、:ハ・・・ベルトコンベヤ第
4しA
第3図[-1 total 1) jjF
(In 1,10, 14 times, 10 pieces of solid food, 1 ha J flJ-K t, 1,1
iil [i=r, 1. ', I-form σ) −,,,FI
B Ihi Forward Part IJJrtlj [1 Kara solid 'Af molecule fi: i tank K y L, T 1lli Bl 8)
! -7,),)-t, attached R'; Regarding the 14 cases of human cover in Figure 3, '6[' is false in #tll. 24 Figure 2 shows yi<'11, and in II, it is a car-powered solid?'<separation tank. 11 is an unloading device i<1', J(1((i
(There are more people than I). The cylindrical tube 10 is installed in the same liquid separation tank 1 in an almost perpendicular force direction to the ridge surface of the liquid to be treated. 3 to 1.li+i
Eh, this solid J1 thing 1),, out ii'1) 13 is an open V in contact with the precipitated solid layer 12; 1! I3A, and the solid matter entrainment C11/4 is extended at the terminal 1λIS.
:1 Jil L-Tii]. In the illustrated implementation (', /II this solids port:=
4Hu was formed in each part of I11 cylinder 1:3 shown by 1.1:3a to 13d. 6 o in this implementation 1
6J 1F If', +i, 'j and L, ゛ are combined to form +f17, but -・A,'1llll
Of course, a= is also good if it is composed of ``affirmative'' and 7゛C. If the solid bar's material is extracted H1'i, it will be 4j over its entire length.
, Ij, V (・1 and 1" rotation li 1117 is arranged -C. Screw 1n+・Blade 1 (+ is the direction of sedimentation hardness J1 Yu9 course) Blade angle 41 sui)
The V-stop is set as follows. By the way, 1 phrase form j1. .. '441 Shooting tube 13t'C
i, i l: i A?") +', 't, i8'2 solidity/crowding in the upper part of the object is also solid jt'; !It/month y, predicate - thirst/i). In addition, 1: (C is a liquid solid/fk containing fine particles separated by a solid-liquid fractionation operation)
Minute l (1 ha 11 door "I J, 4 sending + II output A 1] 5
It is a return section equipped with θ) The four spiral blades 16 that go into the return section IIC are provided with holes (51.1 in FIG.
For return 1 (L ['') t (i a has been completed,
Solid ire fraction p: lIlDuring a certain operation, a part of the solid matter is transferred to this ratio 1 (i a J3-, iJ+ (solid-liquid separation through the return discharge hole 15) 111. t7 so that it is done). Solid material delivery cylinder 13 (...1.'(d
``C゛ Threading 2/, -1t; 1 minute is solid paralleling The bent solid is conveyed to the spiral blade j/, [7 solid' proboscis ((f) L
1+'y-;1+'y-; A) This is an ejection part for carrying out solidified goods from the opening 114. In addition, same-shaped product J feeding section 1: (a and six feeding section 13
jt (minute 1:3b is the spiral blade 1G
Episode 111. % 1141117 in the part that holds 11itt receiver 18. Rotation 11η1; 1 phi, ・) + s. 1 is transmitted through an appropriate transmission mechanism 191x. Note that 21 is an inflow pipe, 22 is an outlet, and 23 is a belt conveyor. Next, phase ゛・planting (shouting 1 ii for 1 ii). Zhongriki r (
solid l(ribranch [me・, l'j11 no t(written li1 吋4'
Omige paddy・) Lower force 1 min jj J N) t i) Tank lower name l) 11 in the center, liquid content? Both solids are 11ゞ) □・Delivery 13 solids 1<, things J2 are included 81・, J3 a K rest is 1ro. ``It's a kuikomiwata it'', number ornament carvings and lIl,
Min.
)! Ij heart minute l'J and b (from pu; +r; moving r direction K/l' 11]., - centrifugal outside 1+4i+!I
During the t no 1 production, the fine particles are exfoliated and settled (>,; solid 42.1 is circulated to 11 times). The ilfed component is jlr-'11
During the q force direction transfer process, zo.
Rite a certain seven h;
feather) 1 barb 16 years old
There are works by +i and i+Hh. I'll return it fall 1.
'(O・Skei in C) The oil time of solid 乍ノI increases -f
A) This is the beginning) A; □1■ Particle peeling i
111 go increases - then return 7i mouth: 3 give lower part (
From the 1j18 outlet hole 15 for 7J and 4 provided in C, the solid-liquid outside 1'J o''' - also the liquid and <yu-uλ and solid Jhi′(
Add 17 to 1NtH of liquid and calculate the amount of liquid m (ti・hl).
Discharge to l. 4", solid) 13 material feeding section 1; 3 return j + 1 j Hiq Of course, the centrifugal minute N4 h, 'I work is tightened and the returned part 1.3cνC μm] Adhering fine particles 411μ
The auxiliary operation of ljt and f, (-)te(・ru. As above, the solid proboscis is 115), and the solid proboscis is removed. No. 1: With the feather 10, the luck is on the upper blade, and it is discharged from the solid q course 1 general exit 14, and at the belt core Beyaha [N;
1/A4...-To be launched 2, operation 4' in the present invention), the conclusion of using the first part of the experiment on urban water!
A^ を ん 4 1-i). 1i4+, as you know, 1-Water treatment equipment is 1, sewage 3 is stopped, solids removal operation isomorphic material center 7 <a, 0.2p
” - above ^ (classified into 11 sand and other particles, these solids) 1.z. The material removal process is called the primary treatment process and is ℃ 4). The above process ■ 4-1 !In Tb, for sand removal operation, tt
Is it possible to imitate organic materials that adhere to sand? Child is Suehiro 1i
ly 1. P1 loss after ti I7, place P■1 set+
It has become a major disadvantage. Therefore, in this experimental procedure,
issue? The blade angle and rotation x9 of the whirl blade 16 are treated as I(1'' Eye 1 (screw i a for each bit; set the return range before and after the 'HFj' (j direction included 1.1-J) of J year wing side lG, and return part 14Ji hole'5 In the discharge of the hermitage, the h.1 enclosure I-
Goni. J'-10 row crops! /, l, chill ^・Result is 1^
” Throat 9 No 4 no IIL + +114 to carry out A and 0
The content of 4U'-1tl of the organic group 1 imitation particles in the sample was almost 0.2 + vI + solid h1 of less than 0.2 + vI + 1... with almost negligible results. From the above results, it can be seen that the solid-liquid separation according to the present invention;
t 1 + pr ++ removal of inner circular engraving 1i1 imprinted particles;
By changing the position of the radial direction of the blade in the direction of the q-ne of the material, it is possible to classify the solid material at will. In addition, it is possible to set Return solid IV7 depending on size and size im
) Possible depending on the amount of each tank pj, 1). Next, as is clear from Fig. 42 of 1st M1, lt:g exit. ? or small, ga-) )IL-!
ji'j body becomes 1) 髫绀-c゛, the reduction of equipment iI′φ comes to vノ+samurai tllJ, and its simplicity 1;~
As a result of , the total i-? , jlIIl ti [ti power ha/
jλ is 11 old) and 1 be). 1 nol i+ii's li'i J4" first investigation ja+
] ly, eye 1, t&l? fk battle 1 (nose"φ
The -pH of the 1st tank is determined by the 3rd figure.The 2nd month is a part of this Example 7f-''
, N7', 4 "The figure is number: (l"",) +i+i
A.). 10...Separation of the same liquid IKt, II...Solidification month-,'[Mountain. 13...1 city i-shaped object 1, □; Deyama section 1.1... solid object 1.i! 1101゜J5... 91 holes for return, 16
...Nu: jk small blade lt, ia-A feeding hole,
1r-=-times E fall, 21-? 11+,
population. 22...3ii Exit: C...Belt conveyor No. 4 A Figure 3
Claims (1)
、上端に固形物搬出口を一’rj7 tlぞれ有する固
形物搬出筒を被処理??vの液1hW*ぼ化11方向に
設f〆イし、この固形物搬出筒内に上端を!=’14s
ili#装置i’7に連結した螺旋羽根を配設し2、
過賞の高さにおけるriit記螺旋羽根に返送用孔口を
形成1く)とともに、その近傍の固形物搬出筒側面に返
送J旧:I+111r、+を形成したことを特徴とする
沈澱固形!1(月〔出ツ、; liI。[Scope of Claims] A solid material discharge cylinder having an open end in contact with a precipitated solid layer in a solid-liquid separation tank at the lower end and a solid material discharge port at the upper end thereof is treated. ? Place the liquid 1hW*in the 11 direction, and place the upper end inside this solid material delivery cylinder! ='14s
A spiral blade connected to the ili# device i'7 is arranged 2,
A precipitated solid characterized by forming a return hole in the helical blade at the height of the upper limit (1) and forming a return hole on the side of the solid material delivery tube near the hole! 1 (month [out,; liI.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14226182A JPS5932910A (en) | 1982-08-17 | 1982-08-17 | Apparatus for conveying out precipitated solid substance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14226182A JPS5932910A (en) | 1982-08-17 | 1982-08-17 | Apparatus for conveying out precipitated solid substance |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5932910A true JPS5932910A (en) | 1984-02-22 |
| JPS6130604B2 JPS6130604B2 (en) | 1986-07-15 |
Family
ID=15311216
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14226182A Granted JPS5932910A (en) | 1982-08-17 | 1982-08-17 | Apparatus for conveying out precipitated solid substance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5932910A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61111107A (en) * | 1984-11-05 | 1986-05-29 | Fujii Shizuo | Device for discharging solid deposit |
| JPS63194704A (en) * | 1987-02-05 | 1988-08-11 | Meiwa Kogyo Kk | Separator for solid-liquid mixture |
-
1982
- 1982-08-17 JP JP14226182A patent/JPS5932910A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61111107A (en) * | 1984-11-05 | 1986-05-29 | Fujii Shizuo | Device for discharging solid deposit |
| JPS63194704A (en) * | 1987-02-05 | 1988-08-11 | Meiwa Kogyo Kk | Separator for solid-liquid mixture |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6130604B2 (en) | 1986-07-15 |
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