JPH0773797B2 - Solid-liquid separation device - Google Patents
Solid-liquid separation deviceInfo
- Publication number
- JPH0773797B2 JPH0773797B2 JP4080761A JP8076192A JPH0773797B2 JP H0773797 B2 JPH0773797 B2 JP H0773797B2 JP 4080761 A JP4080761 A JP 4080761A JP 8076192 A JP8076192 A JP 8076192A JP H0773797 B2 JPH0773797 B2 JP H0773797B2
- Authority
- JP
- Japan
- Prior art keywords
- solid
- screw
- liquid
- filter
- filtration
- 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 - Lifetime
Links
- 239000007788 liquid Substances 0.000 title claims description 60
- 238000000926 separation method Methods 0.000 title claims description 19
- 238000001914 filtration Methods 0.000 claims description 45
- 239000000126 substance Substances 0.000 claims description 43
- 230000002093 peripheral effect Effects 0.000 claims description 22
- 239000000706 filtrate Substances 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 8
- 238000004804 winding Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 238000000354 decomposition reaction Methods 0.000 claims 2
- 239000007787 solid Substances 0.000 description 8
- 239000000428 dust Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009751 slip forming Methods 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
- B30B9/14—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with only one screw or worm
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】Detailed Description of the Invention
【0001】[0001]
【産業上の利用分野】この発明は、固液混合物質を連続
的にスクリューによって供給し固形物質と液状物質とを
連続的に分離排出する固液分離装置に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid-liquid separating device for continuously supplying a solid-liquid mixed substance by a screw and continuously separating and discharging a solid substance and a liquid substance.
【0002】[0002]
【従来の技術】この種の固液分離装置の先行技術とし
て、本発明者の出願に係るスクレーパ濾過装置(特開平
2−290208号)と筒型固液分離装置(特開平3−
86204号)が提案されている。このスクレーパ濾過
装置の要部構成側断面図とA部拡大斜視図を図5に示
す。2. Description of the Related Art As a prior art of this type of solid-liquid separation device, a scraper filtration device (Japanese Patent Application Laid-Open No. 2-290208) and a cylindrical solid-liquid separation device (Japanese Patent Application Laid-Open No. 3-290208) filed by the present inventor.
No. 86204) has been proposed. FIG. 5 shows a sectional side view and an enlarged perspective view of a portion A of the essential parts of this scraper filtration device.
【0003】図5において、1は濾過周面を有する筒体
であり、穴あき多孔円筒体などで加工形成されて多数の
液体流通孔1aが設けられている。In FIG. 5, reference numeral 1 denotes a cylindrical body having a filtration peripheral surface, which is formed by processing a perforated porous cylindrical body or the like and is provided with a large number of liquid circulation holes 1a.
【0004】この筒体1の内周面に所定のピッチでら旋
状に係止溝1bが刻設され、この係止溝1bに頂端部を
係合して断面二等辺三角形状の線材2がスパイラル状に
巻装されて係止固着され、線材2同士の中間に所定の幅
寸法を有する濾過孔であるスリットsが連続してら旋状
に形成されている。A locking groove 1b is formed in a spiral shape on the inner peripheral surface of the cylindrical body 1 at a predetermined pitch, and a top end portion is engaged with the locking groove 1b to form a wire rod 2 having an isosceles triangular cross section. Is wound in a spiral shape and locked and fixed, and slits s, which are filtration holes having a predetermined width dimension, are continuously formed in a spiral shape between the wire rods 2.
【0005】線材2の三角断面の底辺2aによって平滑
な円筒状の内周面Rを形成し、筒体1とら旋状に巻装さ
れた線材2とで固形物質と液状物質とを濾過分離するフ
ィルタエレメントFが構成されている。3はフィルタエ
レメントFを外筒3aの内側に嵌着して形成されたシリ
ンダ、4は外筒3aの底部に配設されフィルタエレメン
トFで濾過された濾液を排出する排出管、5はシリンダ
3のフィルタエレメントFの内周面Rとの間に微少間隙
を保持して非接触に貫装保持されたフィードスクリュー
(以下スクリューという。)であり、このスクリュー5
の山のピッチは先端に行くに従って小さくなるバルアブ
ルピッチ方式かまたは、先端に向かって溝の深さを浅く
するバリアブルデプス方式などによって、供給される固
液混合物質をスクリュー5の回転によってシリンダ4の
先端方向に圧送する構成となっている。The base 2a of the triangular cross section of the wire 2 forms a smooth cylindrical inner peripheral surface R, and the solid substance and the liquid substance are separated by filtration with the cylindrical body 1 and the spirally wound wire 2. A filter element F is constructed. Reference numeral 3 is a cylinder formed by fitting the filter element F inside the outer cylinder 3a, 4 is a discharge pipe disposed at the bottom of the outer cylinder 3a for discharging the filtrate filtered by the filter element F, and 5 is the cylinder 3 Of the filter element F is a feed screw (hereinafter referred to as a screw) which is held in a non-contact manner with a small gap maintained between the inner peripheral surface R and the filter element F.
The pitch of the crests of the solid-liquid mixed substance supplied by the rotation of the screw 5 changes the supplied solid-liquid mixed substance by a variable pitch method in which the groove depth decreases toward the tip, or a variable depth method in which the depth of the groove decreases toward the tip. It is configured to be pressure-fed toward the tip of the.
【0006】6はスクリュー5の山の周端面に刻設され
た溝内に保持され、外周方向にばね弾性を付与されたス
クレーパ機構(以下スクレーパという。)であり、この
スクレーパ6がフィルタエレメントFの内周面Rと摺接
して、内周面Rに付着する固形物質を掻き落すように構
成されている。7はスクリュー5の先端を回転自在に保
持する軸受であり、この軸受7はシリンダ3の先端に取
り付けられたシリンダヘッド(以下ヘッドという。)8
によって支持されている。9はヘッド8の先端開口部の
内周縁との間隙cを調整可能に保持される絞り部材であ
り、この絞り部材9の周縁に所望の勾配で形成された絞
り面9aとヘッド8の先端内周縁に形成された絞り面8
aとの間隙cを、絞り調整ねじ10に取り付けたハンド
ル11の回転操作によって任意に調整できるようになっ
ている。12は絞り面8aと9aとの調整された間隙c
から排出される固形物質を不図示の容器に収納するため
のホッパであり、13は濾過装置のフレームである。そ
して、ヘッド8,絞り部材9Aと絞り調整ねじ10およ
びハンドル11とで濾カスの排出機構Aが構成されてい
る。Reference numeral 6 denotes a scraper mechanism (hereinafter referred to as a scraper) which is held in a groove formed on the peripheral end surface of the crest of the screw 5 and is provided with spring elasticity in the outer peripheral direction. The scraper 6 is a filter element F. It is configured to be in sliding contact with the inner peripheral surface R and scrape off the solid substance adhering to the inner peripheral surface R. Reference numeral 7 denotes a bearing that rotatably holds the tip of the screw 5, and the bearing 7 is a cylinder head (hereinafter referred to as a head) 8 attached to the tip of the cylinder 3.
Supported by. Reference numeral 9 denotes a diaphragm member that holds the gap c between the inner peripheral edge of the tip opening portion of the head 8 and the inner peripheral edge of the head member 8. Aperture surface 8 formed on the periphery
The gap c with the a can be arbitrarily adjusted by rotating the handle 11 attached to the aperture adjusting screw 10. 12 is an adjusted clearance c between the diaphragm surfaces 8a and 9a.
Reference numeral 13 denotes a hopper for storing the solid substance discharged from the container in a container (not shown), and 13 denotes a frame of the filtering device. The head 8, the diaphragm member 9A, the diaphragm adjusting screw 10 and the handle 11 constitute a filter residue discharging mechanism A.
【0007】以上の構成に基づいて動作を説明する。先
ず、不図示のモータを駆動してスクリュー5を回転させ
ると、不図示のフィードホッパからスクリュー5に供給
される固液混合物質がスクリュー5の回転に応じてシリ
ンダ3内側を前方へ向かって押し出される。この時、ス
クリュー5の溝の容積変化に伴う圧縮作用で液状物質が
フィルタエレメントFの内周面Rのスリットsから流通
孔1aを通って外筒3a内に導かれ、底部の排出管4に
よって外部に取り出される。スクリュー5の先端に進む
に従って固液混合物質は液状物質がスリットsにより濾
過されて濾カスが分離され、ヘッド8内に吐出される。
ヘッド8の絞り面8aと絞り部材9の絞り面9aとの間
隙cは、予めハンドル11の操作によって最も固液分離
に適する間隙寸法に調整されているので、ヘッドに充満
した濾カスが間隙cから排出されるとともに、絞り効果
によって濾カスの吐出圧力が高くなり、この圧力がスク
リュー5に背圧を与えるので、スクリュー5の溝内の圧
力もこれに応じて高くなり、液状物質の分離が一層効果
的に行われる。間隙cから排出された濾カスはホッパ1
2によって案内され、不図示の収納容器に分離収納され
る。The operation will be described based on the above configuration. First, when a screw (5) is rotated by driving a motor (not shown), the solid-liquid mixed substance supplied to the screw (5) from a feed hopper (not shown) is pushed forward inside the cylinder (3) according to the rotation of the screw (5). Be done. At this time, the liquid substance is guided from the slit s of the inner peripheral surface R of the filter element F through the circulation hole 1a into the outer cylinder 3a by the compression action due to the volume change of the groove of the screw 5, and by the discharge pipe 4 at the bottom. It is taken out. As it goes to the tip of the screw 5, the liquid substance of the solid-liquid mixed substance is filtered by the slit s to separate the filter residue, and the solid substance is discharged into the head 8.
The gap c between the diaphragm surface 8a of the head 8 and the diaphragm surface 9a of the diaphragm member 9 is adjusted in advance to the most suitable gap size for solid-liquid separation by the operation of the handle 11, so that the filter residue filled in the head has a gap c. The discharge pressure of the filter dust increases due to the throttling effect, and this pressure gives a back pressure to the screw 5, so that the pressure inside the groove of the screw 5 also increases accordingly, and the liquid substance is separated. More effectively done. The filter dust discharged from the gap c is in the hopper 1.
It is guided by 2 and separately stored in a storage container (not shown).
【0008】[0008]
【発明が解決しようとする課題】従来例は以上のように
して固液混合物質から固形物質と液状物質の分離が行わ
れているので、液状物質の分離濾過は殆ど完全に近い十
分な濾過が可能である。しかしながら、濾カス排出時に
更に濾カスを絞り込んで更に濾過の完全を期すというこ
とは行われていなかった。In the conventional example, the solid substance and the liquid substance are separated from the solid-liquid mixed substance as described above, and therefore, the separation and filtration of the liquid substance is almost complete and sufficient. It is possible. However, it has not been attempted to further squeeze the filter residue at the time of discharging the filter residue to further complete the filtration.
【0009】この発明は、固液混合物質からの固液分離
を従来より更に完全にするためになされたもので、スク
リューから排出された濾カスに対して、排出機構によっ
て付加される絞りによる高い圧力を利用して2次濾過を
行い、固液分離を従来より、より完全に行うことができ
る固液分離装置の提供を目的としている。The present invention has been made in order to further complete the solid-liquid separation from the solid-liquid mixed substance as compared with the prior art, and is high with respect to the filter residue discharged from the screw due to the restriction added by the discharging mechanism. It is an object of the present invention to provide a solid-liquid separation device that can perform solid-liquid separation more completely than before by performing secondary filtration using pressure.
【0010】[0010]
【課題を解決するための手段】このため、この発明に係
る固液分離装置は、周面に所望の大きさの濾過孔を形成
した濾過周面を有する筒体内にスクレーパ機構を外周端
面に設けた固液混合物質を移送するスクリューを回転自
在に配設し、前記筒体の一方に固液混合被濾過物質の供
給口を設け他方の先端に前記スクリューによって圧縮移
送される濾カスを排出する排出機構を備え、この排出機
構に近接して、前記スクリューの押圧圧力により2次濾
過を行う2次濾過手段と、この2次濾過手段によって濾
過される濾液を外部へ取り出す濾液排出手段とを設ける
とともに、2次濾過手段に形成する濾過面は、平面板状
の孔あきベース板上に等間隔寸法で渦巻状に線材を巻装
固着し、前記線材間に所望の等しい幅寸法の渦巻状のス
リットを連続して形成し、或は、2次濾過手段に形成す
る濾過面は、円錐板形状の孔あきベース板上に間隔を変
化させて渦巻状に線材を巻装固着して形成することによ
り、前記の目的を達成しようとするものである。Therefore, in the solid-liquid separation device according to the present invention, the scraper mechanism is provided on the outer peripheral end face in the cylindrical body having the filtration peripheral surface having the filtration holes of the desired size formed on the peripheral surface. A screw for transferring the solid-liquid mixed substance is rotatably arranged, and a supply port for the solid-liquid mixed substance to be filtered is provided in one of the cylinders to discharge the filter residue compressed and transferred by the screw at the other end. A discharge mechanism is provided , and in the vicinity of this discharge mechanism, there are provided secondary filtration means for performing secondary filtration by the pressing pressure of the screw, and filtrate discharge means for taking out the filtrate filtered by this secondary filtration means to the outside. At the same time, the filtering surface formed in the secondary filtering means is formed by spirally winding and fixing the wire rods on the flat plate- shaped perforated base plate at equal intervals and spirally with a desired equal width between the wire rods. Continuous slits Form, or filtering surface to form a secondary filtering means, varying the spacing conical plate shape perforated base plate on
It is intended to achieve the above-mentioned object by winding and fixing the wire material in a spiral shape by making it into a spiral shape .
【0011】[0011]
【作用】以上のような構成としたこの発明に係る固液分
離装置は、スクリューから押し出された濾カスを排出機
構によって付加される高い排出圧力を活用して2次濾過
を行う2次濾過手段により2次絞りを十分に行って、濾
カスを更に完全に絞り出して、液状物質の分離がきわめ
て完全な状態で行われる。In the solid-liquid separation device according to the present invention having the above-described structure, the secondary filtering means for carrying out the secondary filtration by utilizing the high discharge pressure applied by the discharging mechanism to the filter residue extruded from the screw. In this way, the secondary squeezing is sufficiently performed to squeeze out the filter residue even more completely, and the separation of the liquid substance is performed in an extremely complete state.
【0012】[0012]
【実施例】以下に、この発明の一実施例を図に基づいて
説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.
【0013】(構成)図1はこの発明の一実施例を示す
固液分離装置の要部構成側断面図、図2は同じく要部拡
大側断面図である。なお、従来例と同一または相当部分
は同一符号で表わす。(Structure) FIG. 1 is a sectional side view of a main part of a solid-liquid separator showing an embodiment of the present invention, and FIG. 2 is an enlarged side sectional view of the same part. Note that the same or corresponding parts as those of the conventional example are represented by the same reference numerals.
【0014】図1および図2において、14は液状物質
の流通孔14aを有する多孔構造の孔あきベース板(以
下ベース板という。)であり、このベース板14には所
定の間隔寸法p1 で渦巻状に刻設された係止溝14bに
断面二等辺三角形状の線材2の頂端部が係合して接着剤
や溶接などにより固着され、所望の幅寸法のスリットs
1 が連続して渦巻状に形成されて、線材2の三角形断面
の底辺2aが平滑な平面状の濾過面R1 を形成してい
る。9Aは間隙cの調整により濾カスの排出圧力を制御
する絞り部材であり、この絞り部材9Aに凹穴9bが形
成され、この凹穴9bの端縁に段差9cが設けられてお
り、この段差9cにベース板14が嵌合保持されてい
る。15は凹穴9bの内周下面に開口された液状物質の
排出口9dにねじ込みなどによって取り付けられた分離
液状物質の排出管であり、16は間隙調整ねじ11の先
端に一方のレースが嵌合され、他方のレースが絞り部材
9Aに嵌合されて、ねじ11の回転に応じて間隙cの寸
法を調整するとともに、濾カスの排出圧力によるスラス
トが負荷されるスラスト軸受である。F1 はベース板1
4と線材2によって構成されるフィルタエレメントであ
り、フィルタエレメントF1 とシリンダヘッド8(以下
ヘッドという。),絞り部材9A,絞り調整ねじ10お
よびハンドル11とで2次濾過手段Bが、また、絞り部
材9Aと排出管15とで濾液排出手段Cがそれぞれ構成
されている。s,s1 は濾過孔を形成するスリットであ
る。In FIGS. 1 and 2, reference numeral 14 denotes a perforated base plate (hereinafter referred to as a base plate) having a porous structure having a liquid substance flow hole 14a, and the base plate 14 has a predetermined interval dimension p 1 . The top end portion of the wire rod 2 having an isosceles triangular cross section is engaged with the locking groove 14b formed in a spiral shape and is fixed by an adhesive agent or welding, and a slit s having a desired width dimension is formed.
1 is continuously formed in a spiral shape, and the bottom side 2a of the triangular cross section of the wire rod 2 forms a smooth planar filtration surface R 1 . Reference numeral 9A denotes a throttle member that controls the discharge pressure of the filter residue by adjusting the gap c. The throttle member 9A is formed with a recessed hole 9b, and a step 9c is provided at the edge of the recessed hole 9b. The base plate 14 is fitted and held on 9c. Reference numeral 15 is a discharge pipe for the separated liquid substance attached to the discharge port 9d for the liquid substance opened on the lower surface of the inner periphery of the recessed hole 9b by screwing or the like, and 16 is one of the races fitted to the tip of the gap adjusting screw 11. The other race is fitted to the throttle member 9A to adjust the size of the gap c according to the rotation of the screw 11, and the thrust bearing is loaded with thrust due to the discharge pressure of the filter residue. F 1 is base plate 1
4 and the wire rod 2. The filter element F 1 , the cylinder head 8 (hereinafter referred to as a head), the throttle member 9A, the throttle adjusting screw 10 and the handle 11 together form the secondary filtering means B. The throttle member 9A and the discharge pipe 15 constitute filtrate discharge means C, respectively. s and s 1 are slits that form the filtration holes.
【0015】(動作)以上の構成に基づいて動作を説明
する。固液混合物質がヘッド8に押し出されるまでは従
来例と全く同様なので詳細の説明を省略する。(Operation) An operation will be described based on the above configuration. Until the solid-liquid mixed substance is pushed out to the head 8, it is exactly the same as in the conventional example, and therefore detailed description thereof is omitted.
【0016】スクリュー5を回転させると、スクリュー
5とフィルタエレメントFとによって液状物質を殆ど完
全に分離された固形物質、即ち濾カスはヘッド8内に充
満し、予めハンドル11の操作によって調整された間隙
cからホッパ12内に吐出される。この時、間隙cによ
る絞り効果によって、ヘッド8内の濾カスの圧力は高く
なる。この高い圧力によって、ヘッド8内の濾カスはフ
ィルタエレメントF1の濾過面R1 に押圧され、濾カス
内に残留する液状物質は2次絞りにより、更に完全に絞
り出され、スリットs1 から流通穴14aを通って凹穴
9b内に導入され、排出管15から外部に取り出され
る。これによって、調整間隙cから吐出される濾カスに
は液状物質の残留分が皆無の状態となり、固液混合物質
の固液分離を完全なものにすることができる。When the screw 5 is rotated, the head 8 is filled with a solid substance, which is a liquid substance almost completely separated from the liquid substance by the screw 5 and the filter element F, that is, filter residue, which is adjusted by the operation of the handle 11 in advance. It is discharged from the gap c into the hopper 12. At this time, the pressure of the filter residue in the head 8 increases due to the throttling effect of the gap c. Due to this high pressure, the filter residue in the head 8 is pressed against the filter surface R 1 of the filter element F 1 , and the liquid substance remaining in the filter residue is further squeezed out completely by the secondary throttle, and from the slit s 1. It is introduced into the recessed hole 9b through the circulation hole 14a and taken out from the discharge pipe 15 to the outside. As a result, no residue of the liquid substance remains in the filter residue discharged from the adjustment gap c, and the solid-liquid separation of the solid-liquid mixed substance can be completed.
【0017】次に、この発明の他の実施例を図3の固液
分離装置の要部構成側断面図と、図4の要部拡大側断面
図に示す。なお、上記実施例と同一または相当部分は同
一符号で表わす。Next, another embodiment of the present invention is shown in FIG. 3 which is a sectional side view of the solid-liquid separation device, and FIG. 4 is an enlarged side sectional view of the main part. The same or corresponding parts as those in the above embodiment are designated by the same reference numerals.
【0018】図3および図4において、8Aはシリンダ
ヘッド(以下ヘッドという。)であり、ヘッド8Aの絞
り面8bは部分円錐状の広い勾配面が形成されている。
絞り部材9Aはヘッド8Aの絞り面8bに勾配をほぼ等
しくして、間隙c1 が濾カスの吐出端に近くなる程小さ
くなる所望の角度の円錐形状に形成されるフィルタエレ
メントF2 を段差9cに嵌合保持している。In FIGS. 3 and 4, 8A is a cylinder head (hereinafter referred to as a head), and the diaphragm surface 8b of the head 8A is formed with a wide conical surface having a partial cone shape.
Diaphragm member 9A is almost equal gradient stop surface 8b of the head 8A, step a filter element F 2 a gap c 1 is formed to a desired angle of the conical shape small enough to be close to the discharge end of the filtration Kas 9c Is held in place.
【0019】以上の構成において、動作は上記実施例と
同様であるが、分離された濾カスが吐出端に近づくに従
って圧縮圧力が高められてフィルタエレメントF2 に形
成される円錐形状の濾過面R2 に押しつけられ、これに
よって濾カスが更に完全に絞られるとともに、分離され
た濾カスが濾過面R2 に沿って高圧で摺動移動するため
に、フィルタエレメントF2 の目づまりが防止され、長
期間にわたって液状物質の濾過効率を完全なレベルに保
つことができる。In the above construction, the operation is the same as that of the above embodiment, but the compression pressure is increased as the separated filter residue approaches the discharge end, and the conical filtering surface R formed on the filter element F 2 is formed. The filter element F 2 is pressed against 2 , which causes the filter residue to be more completely squeezed, and the separated filter residue slides along the filter surface R 2 at a high pressure to prevent the filter element F 2 from being clogged. The filtration efficiency of the liquid substance can be kept at a perfect level over a period of time.
【0020】このため、スクリューに配設されるスクレ
ーパ機構と連携して目づまりを起こさず、固液混合物質
の固液分離に最適な、性能のきわめて優れた固液分離装
置を得ることができる。For this reason, it is possible to obtain a solid-liquid separator having excellent performance which is optimal for solid-liquid separation of a solid-liquid mixed substance without causing clogging in cooperation with a scraper mechanism arranged on the screw.
【0021】なお、上記実施例では、フィルタエレメン
トF,F1 ,F2 にいずれも断面が二等辺三角形の線材
を巻装固着する構造としたが、これに限定されず、断面
が丸形,角形,正三角形,台形形状などの線材を用いて
もよく、またメッシュ構造など適宜な構造のフィルタエ
レメントを用いてもよい。更に、線材のベース板への固
着は接着剤やスポット溶接など適宜な方法で行えばよ
い。In the above-mentioned embodiment, the wire element having an isosceles triangular cross section is wound around and fixed to each of the filter elements F, F 1 and F 2. However, the present invention is not limited to this, and the cross section is round, A wire rod having a square shape, an equilateral triangle shape, a trapezoidal shape, or the like may be used, and a filter element having an appropriate structure such as a mesh structure may be used. Further, the wire material may be fixed to the base plate by an appropriate method such as an adhesive or spot welding.
【0022】また、2次濾過手段の構成は上記実施例に
限定されずフィルタエレメントの濾過面をほぼ円筒状に
形成するなど2次濾過を有効に行える適宜な構成とすれ
ばよい。Further, the structure of the secondary filtering means is not limited to the above embodiment, and any suitable structure capable of effectively performing the secondary filtering such as forming the filtering surface of the filter element into a substantially cylindrical shape may be used.
【0023】[0023]
【発明の効果】以上説明したように、この発明によれ
ば、周面に濾過孔を有する筒体内にスクリューを非接触
で回転自在に配設しこのスクリューの外周端面にスクレ
ーパ機構を備えた濾過装置のシリンダヘッドに、スクリ
ューによって圧縮吐出される濾カスを排出機構によって
生じる高い排出圧力を利用して2次濾過を行う濾過手段
と、この濾過手段によって濾過される濾液を外部に取り
出す濾液排出手段とを設けたので、スクリューによって
絞られた濾カスを更に、高い圧力で2次濾過することに
よって、分離される固形物質に残留する液状物質が皆無
の状態で分離回収することが可能になる。As described above, according to the present invention, a screw is rotatably arranged in a non-contact manner in a cylinder having a filter hole in its peripheral surface, and a screwer mechanism is provided on the outer peripheral end surface of this screw. Filtration means for performing secondary filtration on the cylinder head of the apparatus by utilizing the high discharge pressure generated by the discharge mechanism for filter dust compressed and discharged by the screw, and filtrate discharge means for taking out the filtrate filtered by this filter means to the outside. Since the filter is provided, the filter residue squeezed by the screw is further subjected to secondary filtration at a high pressure, so that the liquid substance remaining in the separated solid substance can be separated and collected without any liquid substance.
【0024】2次濾過手段を円錐形状面に吐出端に近く
なるほど間隔を狭く線材を巻装固着して形成することに
より、濾過絞り作用は向上し、固液混合物質からの液状
物質の分離が更に充分なものとなり、固液混合物質の分
離濾過を完全な状態で行うことができる極めて高性能な
固液分離装置を提供することができる。The secondary filtering means has a conical surface close to the discharge end.
We decided to form the wire by winding and fixing the wire closely.
More, filtered throttling is improved, separation of the liquid material from the solid-liquid substance mixture becomes even more satisfactory, solid-liquid be extremely Umate high performance that can be performed in a complete state separation filtration of the mixed substance <br /> can it to provide a solid-liquid separator.
【図1】 この発明の一実施例を示す固液分離装置の要
部構成側断面図である。FIG. 1 is a side sectional view showing a configuration of a main part of a solid-liquid separator according to an embodiment of the present invention.
【図2】 上記実施例の要部拡大側断面図である。FIG. 2 is an enlarged side sectional view of a main part of the above embodiment.
【図3】 この発明の他の実施例を示す固液分離装置の
要部構成側断面図である。FIG. 3 is a side sectional view showing the configuration of the essential parts of a solid-liquid separation device according to another embodiment of the present invention.
【図4】 上記他の実施例の要部拡大側断面図である。FIG. 4 is an enlarged side sectional view of a main part of the other embodiment.
【図5】 従来例の固液分離濾過装置の要部構成側断面
図とA部拡大部分斜視図である。FIG. 5 is a cross-sectional side view and a partially enlarged perspective view of a main part of a solid-liquid separation filtration device of a conventional example.
1 筒体 1b,14b 係止溝 2 線材 5 スクリュー 6 スクレーパ機構 14 ベース板 A 排出機構 B 2次濾過手段 C 濾液排出手段 p,p1 間隔寸法 s,s1 スリット(濾過孔) なお、図中同一符号は同一または相当部分を示す。1 cylinder 1b, 14b locking groove 2 wire rod 5 screw 6 scraper mechanism 14 base plate A discharge mechanism B secondary filtration means C filtrate discharge means p, p 1 interval dimension s, s 1 slit (filter hole) In the figure The same reference numerals indicate the same or corresponding parts.
Claims (2)
濾過周面を有する筒体内にスクレーパ機構を外周端面に
設けた固液混合物質を移送するスクリューを回転自在に
配設し、前記筒体の一方に固液混合被濾過物質の供給口
を設け他方の先端に前記スクリューによって圧縮移送さ
れる濾カスを排出する排出機構を備え、この排出機構に
近接して、前記スクリューの押圧圧力により2次濾過を
行う2次濾過手段と、この2次濾過手段によって濾過さ
れる濾液を外部へ取り出す濾液排出手段とを設けて成る
固液分解装置であって、前記2次濾過手段に形成する濾
過面は、平面板状の孔あきベース板上に等間隔寸法で渦
巻状に線材を巻装固着し、前記線材間に所望の等しい幅
寸法の渦巻状のスリットが形成されていることを特徴と
する固液分離装置。1. A screw for transporting a solid-liquid mixed substance having a scraper mechanism provided on an outer peripheral end face is rotatably arranged in a cylinder having a filter peripheral face having a filter hole of a desired size formed on the peripheral face, a discharge mechanism for discharging the filtration debris is compressed transported by the screw to the other tip provided the supply port of the solid-liquid mixture to be filtered material to one of said tubular body, in proximity to the discharge mechanism, the pressing of the screw A secondary filtration means for performing secondary filtration by pressure and a filtrate discharge means for taking out the filtrate filtered by the secondary filtration means to the outside are provided.
A solid-liquid decomposition apparatus, comprising a filter formed in the secondary filtration means.
The upper surface is a flat plate-shaped perforated base plate with evenly spaced vortices.
The wire is wound and fixed in a winding shape, and a desired equal width is provided between the wire.
It is characterized by forming a spiral slit of size
Solid-liquid separator to.
濾過周面を有する筒体内にスクレーパ機構を外周端面に
設けた固液混合物質を移送するスクリューを回転自在に
配設し、前記筒体の一方に固液混合被濾過物質の供給口
を設け他方の先端に前記スクリューによって圧縮移送さ
れる濾カスを排出する排出機構を備え、この排出機構に
近接して、前記スクリューの押圧圧力により2次濾過を
行う2次濾過手段と、この2次濾過手段によって濾過さ
れる濾液を外部へ取り出す濾液排出手段とを設けて成る
固液分解装置であって、前記2次濾過手段に形成する濾
過面は、円錐板形状の孔あきベース板上に間隔を変化さ
せて渦巻状に線材を巻装固着し、前記線材間に幅寸法を
変化させた渦巻状のスリットが形成されていることを特
徴とする固液分離装置。2. A filter hole having a desired size is formed on the peripheral surface.
A scraper mechanism is attached to the outer peripheral end surface in a cylinder with a filtration peripheral surface.
Freely rotate the screw to transfer the solid-liquid mixed substance
A supply port for the solid-liquid mixed substance to be filtered is provided in one of the cylinders.
The other end is compressed and transferred by the screw.
Equipped with a discharge mechanism to discharge the filter residue
Adjacent to each other, secondary pressure is applied by pressing pressure of the screw.
The secondary filtering means to be performed and the secondary filtering means
And a means for discharging the filtrate to the outside are provided.
A solid-liquid decomposition apparatus, comprising a filter formed in the secondary filtration means.
The upper surface is a conical disc-shaped perforated base plate with a variable spacing.
Then, the wire is wound and fixed in a spiral shape, and the width dimension is set between the wires.
Specially, the changed spiral slit is formed.
Solid-liquid separation device to collect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4080761A JPH0773797B2 (en) | 1992-04-02 | 1992-04-02 | Solid-liquid separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4080761A JPH0773797B2 (en) | 1992-04-02 | 1992-04-02 | Solid-liquid separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05277794A JPH05277794A (en) | 1993-10-26 |
| JPH0773797B2 true JPH0773797B2 (en) | 1995-08-09 |
Family
ID=13727406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4080761A Expired - Lifetime JPH0773797B2 (en) | 1992-04-02 | 1992-04-02 | Solid-liquid separation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0773797B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4688333B2 (en) * | 2001-04-09 | 2011-05-25 | 株式会社荒井鉄工所 | Axial type throttle device |
| WO2011161767A1 (en) * | 2010-06-22 | 2011-12-29 | 株式会社荒井鉄工所 | Filter cake outlet structure and solid-liquid separation device provided with filter cake outlet structure |
| CN104890276B (en) * | 2014-03-06 | 2017-12-15 | 珠海格力电器股份有限公司 | Oil press |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62214898A (en) * | 1986-03-18 | 1987-09-21 | Maezawa Kogyo Kk | Screen residue dehydrator |
-
1992
- 1992-04-02 JP JP4080761A patent/JPH0773797B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05277794A (en) | 1993-10-26 |
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