JPS6033524B2 - peristaltic separator - Google Patents
peristaltic separatorInfo
- Publication number
- JPS6033524B2 JPS6033524B2 JP57068053A JP6805382A JPS6033524B2 JP S6033524 B2 JPS6033524 B2 JP S6033524B2 JP 57068053 A JP57068053 A JP 57068053A JP 6805382 A JP6805382 A JP 6805382A JP S6033524 B2 JPS6033524 B2 JP S6033524B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- peristaltic
- wall
- dehydrated cake
- liquid
- 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.)
- Expired
Links
- 230000002572 peristaltic effect Effects 0.000 title claims 6
- 239000007788 liquid Substances 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- 230000033001 locomotion Effects 0.000 claims description 16
- 239000008213 purified water Substances 0.000 claims description 13
- 238000004140 cleaning Methods 0.000 claims description 10
- 230000018044 dehydration Effects 0.000 claims description 10
- 238000006297 dehydration reaction Methods 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 2
- 239000011295 pitch Substances 0.000 claims 2
- 238000000926 separation method Methods 0.000 claims 1
- 241000282693 Cercopithecidae Species 0.000 description 24
- 239000010802 sludge Substances 0.000 description 11
- 208000005156 Dehydration Diseases 0.000 description 7
- 239000010419 fine particle Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 241000269821 Scombridae Species 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000020640 mackerel Nutrition 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 241000124033 Salix Species 0.000 description 1
- 241000277331 Salmonidae Species 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 235000000396 iron Nutrition 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 210000000278 spinal cord Anatomy 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】 本発明に鯖動分離機に関する。[Detailed description of the invention] The present invention relates to a machining separator.
−般に、汚泥処理は、第1図のブロック図に示すような
手法が採用されている。-Generally, a method as shown in the block diagram of Fig. 1 is adopted for sludge treatment.
すなわち、この手法は、汚泥貯留槽の原汚泥をフロック
調整槽へ送り込むとともに、原汚泥の種類、濃度によっ
て薬液タンクから、たとえば可性ソーダパック、高分子
凝集剤等の薬液をフロック調整槽に添加し、汚泥を良好
なフロックに成長調整した後、フロツク調整槽からフロ
ックを自然落下によって脱水機に送り、この脱水機によ
って、脱水ケーキと脱水水分(浄化水)とに分離する方
法である。また、脱水ケーキは場外へ搬出し、埋立ても
しくは再利用を図るとともに、脱水水分は原水槽に返送
している。ところで、このような汚泥処理に用いる従来
の脱水機は、微粒子の目詰りにより稼動率が低下する難
点がある。In other words, in this method, the raw sludge from the sludge storage tank is sent to the floc adjustment tank, and depending on the type and concentration of the raw sludge, chemicals such as soluble soda pack and polymer flocculant are added to the floc adjustment tank from the chemical tank. After adjusting the growth of the sludge into good flocs, the flocs are sent from the floc adjustment tank to a dehydrator by gravity, and the dehydrator separates them into dehydrated cake and dehydrated water (purified water). In addition, the dehydrated cake is transported off-site and either landfilled or reused, and the dehydrated water is returned to the raw water tank. By the way, conventional dehydrators used for such sludge treatment have the disadvantage that the operating rate decreases due to clogging with fine particles.
したがって、本発明の目的は微粒子による目詰りが起き
難い蟻勤分離機を提供することにある。以下、実施例に
より本発明を説明する。第2図〜第9図は本発明の一実
施例による蟻勤分離機を示す図であって、第2図は外観
を示す正面図、第3図は正面断面図、第4図は一部の側
面断面図、第5図は平面断面図、第6図は回転軸回転機
構を示す側面断面図、第7図は猿片の斜視図、第8図は
櫨片の敬付状態を示す断面図、第9図は洗浄液流入路系
を示す一部の側面図である。Therefore, an object of the present invention is to provide an ant separator that is less likely to be clogged with fine particles. The present invention will be explained below with reference to Examples. Figures 2 to 9 are views showing an ant separator according to an embodiment of the present invention, in which Figure 2 is a front view showing the external appearance, Figure 3 is a front sectional view, and Figure 4 is a partial view. 5 is a plan sectional view, FIG. 6 is a side sectional view showing the rotary shaft rotation mechanism, FIG. 7 is a perspective view of the monkey piece, and FIG. 8 is a cross-sectional view showing the state in which the oak piece is attached. FIG. 9 is a side view of a part of the cleaning liquid inflow path system.
この鯖動分離機は第3図および第5図に示すように、右
側上部に猿槽1を、右側下部に駆動源となるモータ2を
、左側に櫨槽1に取り付けられる3a〜3hおよび3s
〜3zなる16本の回転軸31にモータ2の回転を伝達
する伝達機構4をそれぞれ配した構造となっている。そ
して、全体の枠組は山形鋼5や隔壁6、カバー7等で構
成されている。櫨槽1は周囲および底は内壁8と外壁9
からなる二重構造となるとともに、一枚の天井板1川こ
はフロックを含む汚泥液である被処理液11を供給する
供給口12を有し、かつ、中央に向かうにしたがって低
くなる底の内壁中央には浄化水を排出する排出管13が
取り付けられている。As shown in Figs. 3 and 5, this mackerel separator has a monkey tank 1 on the upper right side, a motor 2 serving as a drive source on the lower right side, and 3a to 3h and 3s attached to the sand tank 1 on the left side.
It has a structure in which a transmission mechanism 4 for transmitting the rotation of the motor 2 is arranged to each of 16 rotating shafts 31 named .about.3z. The entire framework is composed of angle irons 5, partition walls 6, covers 7, and the like. The periphery and bottom of the oak tank 1 are an inner wall 8 and an outer wall 9.
It has a double structure consisting of a single ceiling plate 1, and has a supply port 12 for supplying the treated liquid 11, which is a sludge liquid containing flocs, and a bottom plate that becomes lower toward the center. A discharge pipe 13 for discharging purified water is attached to the center of the inner wall.
この排出管13は脱水機外に迄延在している。また、略
平行となって延在する一対の内側壁14間には16本の
回転軸3か回動自在に貫通固定されている。脱水機の外
壁をも構成する一方の側壁15にあっては、回転軸3は
その外側壁16を貫通しないが、前記隔壁6の略延長上
に位置しかつカバー7内に位置する他方の側壁17にあ
っては、回転軸3はそれぞれ貫通し、その先端に18a
〜18h、18s〜18zのスプロケツト18を有して
いる。回転軸3は内側壁14と外側壁16との間に配設
される第9図で示すようなそれぞれ独立した受部19に
ベアリング20を介して回転可能に取り付けられている
。また、16本の回転髄3のうち、半分は上段に、残り
の半分は下段にそれぞれ略水平方向に沿って列を作って
配設されている。そして、上列と下列の回転軸3は上下
相対位置がずれていて相互に逆方向(上列は左回転、下
列は右回転)に回転するようになっている。この回転は
第3図,第5図,第6図に示すような伝達機構4によっ
て伝達している。すなわち、モータ2の回転はモー夕2
に固定された駆動歯車21に噛み合う第1スプロケット
22を有する第1歯車23に伝達されるとともに、その
逆方向の回転は第1歯車23に噛み合う第2スプロケッ
ト24を有する第2歯車25に伝達される。第1歯車2
3および第2歯車25の回転は第1・第2スプロケツト
22,24およびタイミングベルト26等を介してそれ
ぞれ第5,第6および第7,第8のスプロケット27,
28,29,30、をそれぞれ有する第3,第4のスプ
ロケット31,32に回転され、かつ第5,第6および
第7,第8のスプロケット27〜30およびタイミング
ベルト33等を介して、上列および下列のスプロケット
18a〜18h,18s〜18zに伝達される。なお、
各列のスプロケット18a〜18h,18s〜18zは
相互に干渉しないように、第3図に示すように、回転軸
3の長さは異なっている。一方、各列の回転軸3のピッ
チはaなるピッチとなっている。This discharge pipe 13 extends to the outside of the dehydrator. Further, 16 rotating shafts 3 are rotatably fixed through a pair of inner walls 14 extending substantially parallel to each other. The rotating shaft 3 does not pass through the outer wall 16 of one side wall 15 that also constitutes the outer wall of the dehydrator, but the rotating shaft 3 does not pass through the outer wall 16 of the other side wall that is located substantially on the extension of the partition wall 6 and within the cover 7. 17, the rotating shafts 3 pass through each other, and a 18a is provided at the tip thereof.
It has sprockets 18 of ~18h and 18s~18z. The rotating shaft 3 is rotatably attached via a bearing 20 to independent receiving portions 19, as shown in FIG. 9, which are disposed between an inner wall 14 and an outer wall 16. Further, among the 16 rotating spinal cords 3, half are arranged in the upper stage and the remaining half in the lower stage, forming a row along the substantially horizontal direction. The rotation shafts 3 in the upper row and the lower row are vertically shifted relative to each other, and rotate in opposite directions (the upper row rotates to the left, and the lower row rotates to the right). This rotation is transmitted by a transmission mechanism 4 as shown in FIGS. 3, 5, and 6. In other words, the rotation of motor 2 is
Rotation in the opposite direction is transmitted to a first gear 23 having a first sprocket 22 meshing with a drive gear 21 fixed to the drive gear 21, and rotation in the opposite direction is transmitted to a second gear 25 having a second sprocket 24 meshing with the first gear 23. Ru. 1st gear 2
The rotation of the third and second gears 25 is transmitted to the fifth, sixth, seventh, and eighth sprockets 27 and 25, respectively, via the first and second sprockets 22 and 24, the timing belt 26, etc.
28, 29, and 30, respectively, and via the fifth, sixth, seventh, and eighth sprockets 27 to 30, the timing belt 33, etc. It is transmitted to sprockets 18a to 18h, 18s to 18z in the row and lower row. In addition,
As shown in FIG. 3, the lengths of the rotating shafts 3 of the sprockets 18a to 18h and 18s to 18z in each row are different so that they do not interfere with each other. On the other hand, the pitch of the rotating shafts 3 in each row is a pitch.
また、各回転軸3には第7図に示すような段付ドーナツ
状の櫨片34が同一の方向性(形態)で1対の内側壁間
一杯に亘つて重ねて固定されている。渡片34は一面の
中央部が円板状に厚い厚肉部35と、この厚肉部35の
周辺に拡がる厚肉部35の厚さ2cの半分の厚さの円板
状の薄肉部36とからなるとともに、薄肉部36の幅b
の中央の1/2bの軌跡を円周とする円上には定間隔、
ここでは90度間隔にdなる径の櫨孔37を有している
。この猿片34の輝孔37を設ける前記円の直径は前記
回転軸3間のピッチaと一致させる。また、櫨片34は
被処理液に腐食されずかつ摩耗し‘こくい金属、樹脂あ
るいはセラミック等によって形成される。また、特に図
示はしないが、各様片34はキー等を用いて回転軸3に
対して回動しないように固定される。また、重なり合う
櫨片34の各嬢孔37は第8図に示すように、同一直線
上に位置するように固定される。なお、渡片34の具体
的要部の寸法、たとえば、aこ70肌,b=30側,c
=0.2肋,d=10肋である。なお、渡片34の形状
は、図示のように中央部を厚肉部35とせずに、この部
分を別体のスベーサとしてもよいし、中央部の厚肉部3
5を薄肉部の片方のみに突出させずに、厚肉部の中央部
に薄肉部36が続くようにしてもよい。回転軸3と、こ
の回転軸3に一定の形態で固定される櫨片34と、から
なる単位猿体38は、隣り合う単位櫨体間では、第8図
に示すように、猿片34の向き、すなわち、表裏面が相
互に逆となつている。In addition, stepped donut-shaped oak pieces 34 as shown in FIG. 7 are fixed to each rotating shaft 3 in the same direction (shape) in an overlapping manner extending completely between the pair of inner walls. The crossing piece 34 has a thick part 35 in the shape of a disk at the center of one side, and a thin part 36 in the form of a disk with a thickness half the thickness 2c of the thick part 35 that spreads around the thick part 35. and the width b of the thin portion 36
On a circle whose circumference is the locus of 1/2b in the center of , there are regular intervals,
Here, holes 37 having a diameter of d are provided at 90 degree intervals. The diameter of the circle in which the bright holes 37 of this monkey piece 34 are provided is made to match the pitch a between the rotating shafts 3. Further, the oak piece 34 is made of metal, resin, ceramic, or the like, which is not corroded by the liquid to be treated and is hard to wear. Further, although not particularly shown in the drawings, each piece 34 is fixed using a key or the like so as not to rotate with respect to the rotating shaft 3. Further, the respective holes 37 of the overlapping pieces 34 are fixed so as to be located on the same straight line, as shown in FIG. 8. In addition, the specific dimensions of the main parts of the crossing piece 34, for example, a is 70 skin, b is 30, and c is
=0.2 ribs, d=10 ribs. Note that the shape of the crossing piece 34 may be such that instead of having the thick wall portion 35 at the center as shown in the figure, this portion may be a separate smoother, or the thick wall portion 35 at the center may
5 may not protrude from only one side of the thin-walled portion, but the thin-walled portion 36 may continue in the center of the thick-walled portion. As shown in FIG. 8, the unit monkey body 38 is made up of a rotating shaft 3 and a wooden piece 34 fixed to the rotating shaft 3 in a fixed form. The orientation, that is, the front and back sides are opposite to each other.
この結果、隣り合う単位渡体38の猿片34の薄肉部は
その窪み側が相互に重なり合い、櫨体群全体では隙間は
生じなくなる。なお、被処理液と直接接触する猿槽各部
は耐食性の材質で形成されている。他方、上列と下列の
櫨体間ではその間に被処理液11が入り込むように、そ
の間隔が広くなっている。As a result, the recessed sides of the thin walled portions of the pieces 34 of adjacent unit crossing bodies 38 overlap with each other, and no gaps are formed in the entire rod group. Note that each part of the monkey tank that comes into direct contact with the liquid to be treated is made of a corrosion-resistant material. On the other hand, the interval between the upper and lower rows of rods is wide so that the liquid to be treated 11 can enter between them.
また、回転軸3を支持する1対の内側壁14面には各単
位櫨体38の最外側の櫨片34外面が接触し、この部分
では被処理液11が下方に洩れないようになっている。
また、下列の櫨体群の両端の単位猿体38の猿片34外
周面はそれぞれ猿槽1の内端壁39の表面に接触してい
る。したがって、両端の単位櫨体38の外周部の櫨片3
4の薄肉部36間の隙間c部分からしか被処理液(実際
には隙間が0.2柳と極めて狭いことから、猿過された
浄化水〉は下方の浄化水集荷室40に入らない。この場
合、前記スリット状の隙間からの洩れを防止するために
、このスリツ−ト(隙間)に噛み合う洩れ防止片群を内
端壁39に設けてもよい。また、上列の櫨体群の一端は
内端壁39との間に広い流路空間41が設けられている
。このため、上列の単位櫨体38の回転によって運ばれ
る彼処理液11はこの流路空間41を通って下方に落ち
、下列の猿体群上に移る。また、一方、1対の内側壁1
4と上下列の櫨体群によって取り囲まれる細長の端動空
間42の端末には脱水ケーキ43を櫨槽1外に排出する
開閉蓋44を有する排出口45が設けられている。Further, the outer surface of the outermost oak piece 34 of each unit oak body 38 comes into contact with the surface of the pair of inner walls 14 that support the rotating shaft 3, and the liquid to be treated 11 is prevented from leaking downward in this part. There is.
Further, the outer peripheral surfaces of the monkey pieces 34 of the unit monkey bodies 38 at both ends of the lower row of rod groups are in contact with the surface of the inner end wall 39 of the monkey tank 1, respectively. Therefore, the oak piece 3 on the outer periphery of the unit oak body 38 at both ends
The liquid to be treated (actually, since the gap is extremely narrow at 0.2 willow, the filtered purified water) enters the purified water collection chamber 40 below only through the gap c between the thin walled portions 36 of 4. In this case, in order to prevent leakage from the slit-shaped gap, a group of leakage prevention pieces that engage with the slit (gap) may be provided on the inner end wall 39. A wide channel space 41 is provided between one end and the inner end wall 39. Therefore, the processing liquid 11 carried by the rotation of the unit rods 38 in the upper row passes through this channel space 41 and downwards. and move onto the lower row of monkey bodies.On the other hand, a pair of inner walls 1
A discharge port 45 having an opening/closing lid 44 for discharging the dehydrated cake 43 to the outside of the canister tank 1 is provided at the end of the elongated end-moving space 42 surrounded by the upper and lower rows of cane bodies.
開閉蓋44は開閉ハンドル46の歯車47にラック部が
噛み合い、開閉ハンドル46の正逆回転操作によって開
閉する。また、筒状の排出口45の内部には、排出口4
5の天井部を中心に上下に揺回動する調整蓋48が設け
られている。この調整蓋48は調整ハンドル49の正逆
回動によって排出口45の流路径を調整するようになる
。この調整ハンドル49の操作によって、排出口45を
移動する脱水ケーキ43の移動抵抗を変えることができ
るため、脱水ケーキ43の硬さの調整が可能となる。な
お、この実施例では、排出口45側の上・下列のそれぞ
れ2つの単位櫨体38はeだけ他のものより高くし、前
記同様に脱水ケーキ43の移動抵抗を増大するようにな
っている。さらに、隣り合う単位猿体38のそれぞれの
猿片34は回転軸3間に位置した猿孔37が、第3図〜
第5図および第8図に示すように、同一線上に位置して
相互に運通状態となるようになっている。The opening/closing lid 44 has a rack portion that meshes with a gear 47 of the opening/closing handle 46, and is opened/closed by rotating the opening/closing handle 46 in forward and reverse directions. Further, inside the cylindrical discharge port 45, the discharge port 4
An adjustment lid 48 is provided that swings up and down about the ceiling of 5. The adjusting lid 48 adjusts the flow path diameter of the discharge port 45 by rotating the adjusting handle 49 in the forward and reverse directions. By operating this adjustment handle 49, the movement resistance of the dehydrated cake 43 moving through the discharge port 45 can be changed, so that the hardness of the dehydrated cake 43 can be adjusted. In this embodiment, the two unit rods 38 in the upper and lower rows on the side of the discharge port 45 are made higher than the others by e, so as to increase the movement resistance of the dehydrated cake 43 as described above. . Further, each monkey piece 34 of the adjacent unit monkey bodies 38 has a monkey hole 37 located between the rotating shafts 3, as shown in FIGS.
As shown in FIG. 5 and FIG. 8, they are located on the same line and are in mutual communication.
また、この蓮適状態の櫨孔37に対応する1対の内側壁
14には脱水孔50が設けられている(第9図参照)。
また、脱水孔50‘ま達適状藤下の渡孔37の各位層に
対応して内側壁14に設けられる。他方の側壁17にあ
っては、脱水孔50から他方の側壁17間に入った浄化
水は第3図で実線矢印で示すように、他方の側壁17の
内側壁14の下部に設けた導孔51を通って浄化水集荷
室401こ入り、排出管13から排出される。一方、一
方の側壁15にあっては、内側壁14と外側壁16に第
9図に示すように、枠体52を設け、脱水孔50を枠体
内のバッファ室53に密閉状態で運速させる。また、こ
のバッファ室53に蓮適する洗浄液供給管(供給口)5
4が外側壁16に取り付けられている。この洗浄液供給
管54は猿片34等の洗浄時に洗浄液をバッファ室53
に送り込む際用いる。バッファ室53に圧送された洗浄
液は第9図および第3図の二点鎖線に示すように、脱水
孔50から櫨片34の櫨孔37に入り、この渡孔37か
ら逆に猿槽1に逆流して、櫨片34および猿槽1を洗う
ようになる。また、この際、一部は櫨孔37を介して、
他の脱水孔5川こ入り、他方の側壁17内を通って浄化
水集荷室40内にも入る。この結果、流路系全体の洗浄
が行なえるようになる。なお、排出口側の上・下列の単
位櫨体における猿片には脱水ケーキに水分を供給しない
ようにするため、猿孔は設けないことが望ましい。この
ような分離機にあってはフロックを有する被処理液11
は供給口12から順次櫨槽1内に供給される。Further, a dehydration hole 50 is provided in a pair of inner walls 14 corresponding to the hole 37 in the lotus state (see FIG. 9).
Furthermore, dewatering holes 50' are provided on the inner wall 14 corresponding to each layer of the water passage hole 37 of the Fujishita. In the other side wall 17, the purified water that has entered between the dehydration hole 50 and the other side wall 17 flows through a guide hole provided at the lower part of the inner wall 14 of the other side wall 17, as shown by the solid arrow in FIG. The purified water enters the purified water collection chamber 401 through 51 and is discharged from the discharge pipe 13. On the other hand, in one side wall 15, a frame 52 is provided on the inner wall 14 and the outer wall 16, as shown in FIG. . Also, a cleaning liquid supply pipe (supply port) 5 suitable for this buffer chamber 53 is provided.
4 is attached to the outer wall 16. This cleaning liquid supply pipe 54 supplies the cleaning liquid to the buffer chamber 53 when cleaning the monkey pieces 34, etc.
Used when sending to. As shown by the two-dot chain line in FIGS. 9 and 3, the cleaning liquid pumped into the buffer chamber 53 enters the hole 37 of the oak piece 34 through the dehydration hole 50, and conversely flows into the monkey tank 1 through the passage hole 37. The water flows back and washes the oak piece 34 and the monkey tank 1. In addition, at this time, some of the parts pass through the hole 37,
The other dewatering hole 5 also enters the purified water collecting chamber 40 through the other side wall 17. As a result, the entire channel system can be cleaned. In addition, in order to prevent water from being supplied to the dehydrated cake, it is preferable that no holes are provided in the holes in the upper and lower rows of unit rods on the discharge port side. In such a separator, the liquid to be treated 11 having flocs
are sequentially supplied into the oak tank 1 from the supply port 12.
フロック等は回転する上列の櫨体群上を第4図中左方向
に順次移動し、左端から外れて流路空間41を通って下
列櫨体群上に移る。また、猿体群の上部には幅が0.2
側と極めて狭い扇形状の窪みが多数形成されるため、粒
子の大きなフロック等はこの窪み中には入らない。した
がって、これらの窪みは櫨布と同様に被処理液11を猿
過するようになり、窪みに入った被処理液11は渡過さ
れた浄化水となる。この浄化水は猿孔37を通って他方
の側壁17の脱水孔50内に入り、他方の側壁17内お
よび導孔51、浄化水集荷室40、排出管13を経て外
部に排出される。また、嫌動空間42に入った被処理液
11には、相互関係位置を上下で少しずらして設けられ
てある上・下列の櫨体群の同一移送方向への回転によっ
て、その上下間隔が拡がったり狭まったりする空間を圧
縮,膨張を繰り返しながら移送されるという鴫動運動が
生じる。なお、上下相互関係位置をずらさなくても端動
運動は生ずるので、この状態でも使用できるが、前記の
ようにした方が鱒勤運動は細かく行われ効率はよい。こ
の結果、大イ・,種々の粒状の物質が混在している櫨過
対象物である被処理液11はスロースピードで圧縮,膨
張を繰返されることにより、粒子の大きなものが中央部
へ、小なるものが外側へと集り、最も小なるものである
水分が最外端へと押し出され、渡片34によって猿過分
離される。なお、この際、猿片34の間にも微粒子の層
が出来ることにより、この層が櫨材の役割を果し、櫨過
性能をより向上させる。しかし、逆にこの微粒子の層が
目詰まりの原因になるわけであるが猿片が回転する際に
1分間に4回程度除去されることにより、解消される。
そこで、処理に先立って、開閉ハンドル46を操作して
開閉蓋44を閉じておく。The flocs and the like sequentially move to the left in FIG. 4 on the rotating upper row of rods, leave the left end, pass through the channel space 41, and move onto the lower row of rods. In addition, the width of the upper part of the monkey body group is 0.2
Since many fan-shaped depressions with extremely narrow sides are formed, large flocs and the like do not fit into these depressions. Therefore, these depressions allow the liquid to be treated 11 to pass therethrough in the same way as a wicker cloth, and the liquid to be treated 11 that has entered the depressions becomes purified water. This purified water enters the dehydration hole 50 of the other side wall 17 through the monkey hole 37, and is discharged to the outside through the other side wall 17, the guide hole 51, the purified water collection chamber 40, and the discharge pipe 13. In addition, the liquid to be treated 11 that has entered the reluctance space 42 has its upper and lower rows of rods, whose relative positions are slightly shifted vertically, rotated in the same transfer direction, thereby increasing the vertical distance between them. A drooping movement occurs in which the material is repeatedly compressed and expanded through a space that is gradually becoming smaller or smaller. Incidentally, since end-motion movement occurs even without shifting the vertical relative position, it can be used in this state, but the above-mentioned method allows the trout movement to be performed more precisely and is more efficient. As a result, the liquid to be processed 11, which is the object to be filtered and which contains a mixture of large particles and various granular substances, is repeatedly compressed and expanded at a slow speed, so that the large particles are transferred to the center and the small particles are transferred to the center. The water, which is the smallest, is pushed out to the outermost edge and separated by the crosspiece 34. At this time, a layer of fine particles is also formed between the pieces 34, so that this layer plays the role of a oak material and further improves the oak passing performance. However, on the contrary, this layer of fine particles causes clogging, which is eliminated by being removed about four times per minute when the pieces rotate.
Therefore, prior to processing, the opening/closing handle 46 is operated to close the opening/closing lid 44.
この結果、開閉蓋44に塞がれた排出口45部分には開
閉蓋44に接する領域から順次粒子の大きい物質が堆積
し、脱水ケーキ43が形成され始める。この脱水ケーキ
43は処理時間が増大すればする程その量が多くなると
ともに、下層あるいは開閉蓋側での含水率は低くなる。
つぎに、ある程度脱水ケーキ43が形成された時点で、
開閉蓋44を開いて排出口45を開口する。As a result, substances with larger particles are accumulated in the discharge port 45 portion blocked by the openable lid 44 starting from the region in contact with the openable lid 44, and a dehydrated cake 43 begins to be formed. As the processing time increases, the amount of this dehydrated cake 43 increases, and the moisture content of the lower layer or the opening/closing lid side decreases.
Next, when the dehydrated cake 43 has been formed to some extent,
The opening/closing lid 44 is opened to open the discharge port 45.
すると、脱水ケーキ43は、蟻勤運動によって徐々に押
し出される。そこで、この押し出された脱水ケーキ43
を所定の場所に運ぶ。なお、この実施例では、排出口4
5側の上下列の単位猿体38の位置を他のものよりも高
くしていることから、脱水ケーキの移動抵抗が高くなり
、脱水ケーキは比較的硬いものとなる。また、移動抵抗
増大機構として、調整ハンドル49による調整蓋48が
配設されていることから、脱水ケーキを硬くする場合に
は、排出口45の流路内に調整蓋48を多く突出させる
。また、逆に脱水ケーキを敏くする場合には、調整蓋4
8の突出量を少〈し、脱水ケーキの移動抵抗の軽減を図
る、この結果、所望の硬さの脱水ケーキを作ることがで
きる。このような実施例によれば、特殊形状の猿片34
およびその組み合せによる猿体によって、篭め細粒子の
櫨週が行なえるとともに、供給口12より投入される彼
処理液の上列の猿体群上における水分落下による糟過、
及び上下列の櫨体群間における圧縮、膨張を繰返しなが
らの鯖勤運動による猿過作業と、この蟻動運動によって
生じる脱水ケーキの硬度調整機構によって、所望の硬さ
の脱水ケーキが効率的に形成できる。Then, the dehydrated cake 43 is gradually pushed out by the dovetail movement. Therefore, this extruded dehydrated cake 43
carry it to the designated location. In addition, in this embodiment, the discharge port 4
Since the unit monkey bodies 38 in the upper and lower rows on the 5th side are positioned higher than the others, the movement resistance of the dehydrated cake becomes high and the dehydrated cake becomes relatively hard. Further, since the adjustment lid 48 by the adjustment handle 49 is provided as a movement resistance increasing mechanism, the adjustment lid 48 is made to protrude more into the flow path of the discharge port 45 when the dehydrated cake is to be hardened. On the other hand, if you want to make the dehydrated cake faster, use the adjustment lid 4.
By reducing the amount of protrusion 8, the movement resistance of the dehydrated cake is reduced, and as a result, a dehydrated cake of desired hardness can be produced. According to such an embodiment, the specially shaped monkey piece 34
In addition, by using a monkey body with a combination thereof, it is possible to carry out filtration of fine particles, and also to filtrate the treated liquid by dropping moisture on the monkey body group in the upper row, which is injected from the supply port 12.
The dehydrated cake of the desired hardness can be efficiently produced by the sarcophagus work by the mackerel movement that repeats compression and expansion between the upper and lower rows of rod groups, and by the hardness adjustment mechanism of the dehydrated cake generated by this dovetail movement. Can be formed.
また、この実施例の脱水ケーキは、鯖動運動によって形
成されることから、脱水ケーキの最外層は微粒子のノロ
状体となる。このノロ状態は外気に触れると一瞬のうち
に固化するため、脱水ケーキをオブラートで包んだ形態
となり、脱水ケーキの臭気を外部に出さないような働き
をする。一般に、脱水処理を行なう場合の条件として、
汚泥含水率職%、脱水ケーキ含水率80%以上のものを
使うが、本発明によるこの実施例装置では目詰りが発生
し難いことから、脱水ケ−キ含水率は60〜75%のも
のでも充分適用できる。Further, since the dehydrated cake of this example is formed by the sloughing motion, the outermost layer of the dehydrated cake becomes a slag-like body of fine particles. This slag solidifies instantly when exposed to outside air, so the dehydrated cake is wrapped in wafer, which works to prevent the odor of the dehydrated cake from coming out. Generally, the conditions for dehydration treatment are as follows:
A sludge with a moisture content of at least 80% and a dehydrated cake with a moisture content of 80% or more are used, but since clogging is unlikely to occur in this embodiment of the apparatus according to the present invention, a dehydrated cake with a moisture content of 60 to 75% is also used. Fully applicable.
この実施例の具体的な例として、汚泥舎水率98%、脱
水ケーキ含水率70%、出口低減率70%、櫨片直径1
00側、贋片回転数IRPM、脱水ケーキ厚さ45柳と
した場合、時間当り約300kgの脱水ケーキを製造し
、汚泥も時間当り約4.5トン処理できることになる。As a specific example of this embodiment, the sludge water rate is 98%, the dehydrated cake water content is 70%, the outlet reduction rate is 70%, and the diameter of the oak piece is 1.
00 side, counterfeit rotation speed IRPM, and dehydrated cake thickness 45 Yanagi, approximately 300 kg of dehydrated cake can be produced per hour and approximately 4.5 tons of sludge can be processed per hour.
また、この実施例の分離機は猿片等の洗浄が容易である
ことから、メインテナンスが容易である。なお、本発明
は前記実施例に限定されるものでなく、本発明の技術思
想に塞く変形は可能である。Furthermore, the separator of this embodiment is easy to maintain since it is easy to clean the pieces of the separator. It should be noted that the present invention is not limited to the above-mentioned embodiments, and modifications can be made without departing from the technical idea of the present invention.
以上のように、本発明によれば、目詰りが起き難くかつ
脱水能力が高い蟻動分離機を提供することができる。As described above, according to the present invention, it is possible to provide an ant separator that is less likely to be clogged and has a high dewatering ability.
第1図は汚泥処理フ。
。セスを示すブロック図、第2図〜第9図は本発明の−
実施例による端動分離機を示す図であって、第2図は外
観を示す正面図、第3図は正面断面図、第4図は一部の
側面断面図、第5図は平面断面図、第6図は回転軸回転
機構を示す側面断面図、第7図は頬片の斜視図、第8図
は櫨片の取付状態を示す断面図、第9図は洗浄液流入路
系を示す一部の側面図である。1…猿槽、3・・・回転
軸、4・・・伝達機構、8・・・内壁、9・・・外壁、
11・・・彼処理液、12・・・供給口、13・・・排
出管、14・・・内側壁、15・・・一方の側壁、16
・・・外側壁、17・・・他方の側壁、18・・・スプ
ロケツト、34・・・櫨片、35・・・厚肉部、36・
・・薄肉部、37・・・猿孔、38・・・単位猿体、3
9・・・内端整、40・・・浄化水集荷室、41・・・
流路空間、42・・・鯖動空間、43・・・脱水ケーキ
、44・・・開閉蓋、45…排出口、48・・・調整蓋
、50・・・脱水孔、54・・・洗浄液供給管。
第1図
第2図
第3図
第4図
第5図
第8図
第7図
第6図
第9図Figure 1 shows the sludge treatment facility. . The block diagrams of FIGS. 2 to 9 show the process of the present invention.
FIG. 2 is a front view showing the external appearance, FIG. 3 is a front sectional view, FIG. 4 is a partial side sectional view, and FIG. 5 is a plan sectional view showing an end motion separator according to an embodiment. , FIG. 6 is a side cross-sectional view showing the rotary shaft rotation mechanism, FIG. 7 is a perspective view of the cheek piece, FIG. 8 is a cross-sectional view showing the mounting state of the tooth piece, and FIG. 9 is a side view showing the cleaning liquid inlet system. FIG. DESCRIPTION OF SYMBOLS 1... Monkey tank, 3... Rotating shaft, 4... Transmission mechanism, 8... Inner wall, 9... Outer wall,
DESCRIPTION OF SYMBOLS 11... Processing liquid, 12... Supply port, 13... Discharge pipe, 14... Inner wall, 15... One side wall, 16
. . . Outer wall, 17. Other side wall, 18. Sprocket, 34. Oak piece, 35. Thick wall portion, 36.
...Thin wall part, 37... Monkey foramen, 38... Unit monkey body, 3
9... Internal arrangement, 40... Purified water collection room, 41...
Channel space, 42... Slip movement space, 43... Dehydration cake, 44... Open/close lid, 45... Discharge port, 48... Adjustment lid, 50... Dehydration hole, 54... Washing liquid supply pipe. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 8 Figure 7 Figure 6 Figure 9
Claims (1)
前記濾槽の1対の内側壁に亘つて略水平方向に平行にか
つ上下2列にそれぞれピツチaで取り付けられ、さらに
上列と下列では相互上下関係位置がずれていてしかも回
転方向が相互に逆となる複数の回転軸と、前記回転軸に
それぞれ重ねて嵌合固定されるとともに、内側壁間全体
に亘つて取り付けられ、かつ同列の隣り合う回転軸間で
は嵌合時の表裏面が逆となるように取り付けられるとこ
ろの、一面の中央部が盛り上がるとともに周辺部に中央
部の半分の厚さの薄肉部を有し、かつ薄肉部の中央であ
る直径が前記ピツチaと同一のaなる円上に定間隔に濾
孔を有する段付ドーナツ状の複数の濾片と、前記回転軸
とこれに固定される濾片とからなる単位濾体の濾体群と
前記1対の内側壁とによつて形成される蠕動空間端末に
連通して設けられる脱水ケーキを排出する開閉蓋を有す
る排出口と、を備え、前記隣接する単位濾体にあつては
その回転によつて隣接する単位濾体の中間に位置した相
互の濾孔が総て連通するように構成され、かつ内側壁の
少なくとも一方には連通状態の濾孔群に対面して濾槽外
に浄化水を案内する脱水孔が設けられ、さらに前記被処
理液は上列の濾体群の回転方向端から下列の濾体群上に
移動するように構成されることを特徴とする蠕動分離機
。 2 前記排出口部分には脱水ケーキの移動抵抗を増大あ
るいは調整できる移動抵抗増大機構が設けられているこ
とを特徴とする特許請求の範囲第1項記載の蠕動分離機
。 3 前記内側壁に設ける脱水孔のうち、一側壁は脱水孔
に、他側壁は濾片洗浄用の洗浄液を供給する洗浄液供給
口とする特許請求の範囲第1項ないし第2項記載の蠕動
分離機。[Claims] 1. A filter tank having a supply port for supplying a liquid to be treated upward;
They are mounted in two rows, upper and lower, with pitches a over the pair of inner walls of the filter tank, approximately horizontally parallel to each other, and furthermore, the upper and lower rows are vertically deviated from each other, and their rotational directions are mutually different. A plurality of rotating shafts that are opposite to each other are fitted and fixed onto the respective rotating shafts, and are attached across the entire inner wall, and the front and back surfaces of adjacent rotating shafts in the same row are reversed when fitted. The central part of one side is raised and has a thin part half the thickness of the central part on the periphery, and the diameter at the center of the thin part is a, which is the same as the pitch a. A filter body group of a unit filter body consisting of a plurality of stepped donut-shaped filter pieces having filter holes at regular intervals on a circle, the rotation shaft and the filter pieces fixed thereto, and the pair of inner walls. a discharge port having an opening/closing lid for discharging the dehydrated cake, which is provided in communication with the end of the peristaltic space formed by the peristaltic space; All of the mutual filter holes located in the middle of the body are configured to communicate with each other, and at least one of the inner walls has a dehydration hole facing the communicating filter hole group and guiding purified water to the outside of the filter tank. A peristaltic separator, wherein the liquid to be treated is further configured to move from an end in the rotational direction of the upper row of filter bodies onto the lower row of filter bodies. 2. The peristaltic separator according to claim 1, wherein the discharge port portion is provided with a movement resistance increasing mechanism that can increase or adjust the movement resistance of the dehydrated cake. 3. The peristaltic separation according to claim 1 or 2, wherein one side wall of the dehydration holes provided in the inner wall is a dehydration hole, and the other side wall is a cleaning liquid supply port for supplying a cleaning liquid for cleaning filter pieces. Machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57068053A JPS6033524B2 (en) | 1982-04-24 | 1982-04-24 | peristaltic separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57068053A JPS6033524B2 (en) | 1982-04-24 | 1982-04-24 | peristaltic separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58186408A JPS58186408A (en) | 1983-10-31 |
| JPS6033524B2 true JPS6033524B2 (en) | 1985-08-03 |
Family
ID=13362647
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57068053A Expired JPS6033524B2 (en) | 1982-04-24 | 1982-04-24 | peristaltic separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6033524B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0257117U (en) * | 1988-10-18 | 1990-04-25 | ||
| JPH0257116U (en) * | 1988-10-18 | 1990-04-25 | ||
| JP2007000808A (en) * | 2005-06-24 | 2007-01-11 | Ishikawajima Harima Heavy Ind Co Ltd | Multiple disk dehydrator |
| JP2007000805A (en) * | 2005-06-24 | 2007-01-11 | Ishikawajima Harima Heavy Ind Co Ltd | Multiple circular disc dehydration apparatus |
| JP6401356B2 (en) * | 2017-09-05 | 2018-10-10 | 株式会社鶴見製作所 | Solid-liquid separator |
| CN113232192A (en) * | 2021-04-14 | 2021-08-10 | 王荣 | Creeping type anti-blocking filter screen for regenerated ABS plastic granulator |
-
1982
- 1982-04-24 JP JP57068053A patent/JPS6033524B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58186408A (en) | 1983-10-31 |
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