JPH0683759U - Fine powder separator for miscella in oil extractor - Google Patents

Fine powder separator for miscella in oil extractor

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Publication number
JPH0683759U
JPH0683759U JP2449193U JP2449193U JPH0683759U JP H0683759 U JPH0683759 U JP H0683759U JP 2449193 U JP2449193 U JP 2449193U JP 2449193 U JP2449193 U JP 2449193U JP H0683759 U JPH0683759 U JP H0683759U
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JP
Japan
Prior art keywords
miscella
oil
hopper
fine powder
raw material
Prior art date
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JP2449193U
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Japanese (ja)
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JP2595161Y2 (en
Inventor
忍 鈴木
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Showa Sangyo Co Ltd
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Showa Sangyo Co Ltd
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Priority to JP1993024491U priority Critical patent/JP2595161Y2/en
Publication of JPH0683759U publication Critical patent/JPH0683759U/en
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Publication of JP2595161Y2 publication Critical patent/JP2595161Y2/en
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Abstract

(57)【要約】 〔目的〕 米ぬか等の油脂原料使用で生じ易い微粉を除
去する油抽出機におけるミセラ用微粉分離装置を提供す
る。 〔構成〕 原料ホッパー2から投入する油脂原料を受け
る平滑搬送面4上に摺動走行のスクレーパー9を配設
し、このスクレーパー9で適宜層高として移動する油脂
原料を、筐体1の天井部に配管した溶剤パイプ8より散
布する溶剤を浸透させて油分を抽出し、この油分と溶剤
の混ざったミセラを平滑搬送面4を経て下方の複数個の
ミセラ用ホッパー7で受け、各ホッパー7のミセラを手
前位置の溶剤使用とし、手前側のミセラ用ホッパー7を
順次濃厚なミセラとする油抽出機において、終端のミセ
ラ用ホッパー7′に微粉分離装置となる内部中央に円弧
状スクリーン15を縦装着し前後2室に区画した縦型ケ
ーシング12上のフィードヘッダー17を接続し、フィ
ードヘッダー17に流入の濃厚ミセラを案内チューブ1
8からノズル16をもって前記円弧状スクリーン15の
スクリーン面14aに噴射し、液体のみを通過させ、微
粉の通過を阻止し下方へ落下させ分離する。
(57) [Summary] [Purpose] To provide a fine powder separating device for a miscella in an oil extractor that removes fine powder that tends to be generated by using an oil and fat raw material such as rice bran. [Structure] A scraper 9 for sliding traveling is arranged on a smooth conveying surface 4 for receiving the oil / fat raw material fed from the raw material hopper 2, and the oil / fat raw material that moves at an appropriate layer height by this scraper 9 is used for the ceiling portion of the casing 1. The solvent to be sprayed is permeated through the solvent pipe 8 which is piped to the oil pipe to extract the oil, and the miscella in which the oil and the solvent are mixed is received by the plurality of miscella hoppers 7 below through the smooth transport surface 4, and the hoppers 7 of In an oil extractor in which the miscella is used as a solvent at the near side and the near side miscella hopper 7 is made into a dense miscella, an arc-shaped screen 15 is vertically provided at the inner center of the end miscella hopper 7'becomes a fine powder separating device. The feed header 17 on the vertical casing 12 which is installed and divided into two chambers, front and rear, is connected, and the rich miscella flowing into the feed header 17 is connected to the guide tube 1
The liquid is sprayed from 8 through the nozzle 16 onto the screen surface 14a of the arcuate screen 15 to allow only liquid to pass therethrough, block fine powder from passing through, and drop downward to separate.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

この考案は大豆,菜種,その他の植物種子、特に米ぬかの油脂原料から油分を 抽出するための油抽出機におけるミセラ用微粉分離装置に関するもである。 The present invention also relates to a fine powder separator for miscella in an oil extractor for extracting oil from soybeans, rapeseed, and other plant seeds, particularly rice bran oil and fat raw materials.

【0002】[0002]

【従来の技術】[Prior art]

一般に、大豆,菜種,その他の植物種子,米ぬか等の油脂原料にヘキサン等の 溶剤を散布し、溶剤が油脂原料に浸透し油分を抽出し油分の混ざった溶剤、所謂 ミセラを得るようにした油抽出機としては各種タイプが知られている。この場合 、構造が複雑とならず抽出機本体が比較的コンパクトに形成される連続抽出装置 とし、例えば本件出願人が先に提示した油脂の抽出装置(特公平2−53480 号公報)がある。 Generally, oils and fats such as soybeans, rapeseed, other plant seeds, and rice bran are sprayed with a solvent such as hexane, and the solvent permeates the oils and fats to extract the oils and obtain a mixture of oils, a so-called miscella oil. Various types of extractors are known. In this case, there is a continuous extraction device in which the structure of the extraction device is not complicated and the extraction device main body is relatively compact, and there is, for example, the oil and fat extraction device presented by the applicant of the present application (Japanese Patent Publication No. 2-53480).

【0003】 これは、原料ホッパーに供給した油脂原料を下方に位置する固定の平滑搬送面 で一旦受け溜めて堆積状とし、該平滑搬送面を摺動走行するスクレーパーで所定 層高として前方へ移動し、この移動中に上方の溶剤パイプから散布した溶剤を油 脂原料に浸透させて油分を抽出し、油分の混ざったミセラを平滑搬送面のスリッ トを経て滴下し、下方に配設した複数個のミセラ用ホッパーで順次受ける構成で ある。この場合、前記溶剤パイプに流入する溶剤は、ミセラ用ホッパーに溜まっ たミセラをポンプアップして手前位置の使用溶剤として循環流用方式を採る。This is because the oil / fat raw material supplied to the raw material hopper is once received and accumulated in a fixed smooth conveying surface located below, and is accumulated in a pile, and is moved forward with a predetermined height by a scraper that slides on the smooth conveying surface. Then, during this movement, the solvent sprayed from the upper solvent pipe is permeated into the oil / fat raw material to extract the oil, and the miscella mixed with the oil is dropped through the slits on the smooth transport surface, and the multiple oils are placed below. The configuration is such that the individual hoppers for the miscella will receive them one after another. In this case, for the solvent flowing into the solvent pipe, the miscella accumulated in the miscella hopper is pumped up and the circulating solvent is used as the solvent used at the front position.

【0004】[0004]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかし、ミセラ用ホッパーに溜まったミセラを使用溶剤とするには、油脂原料 が米ぬかの如く細かい原料使用ではどうしてもミセラ中の微粉(ファイン)が増 して行き、終端のミセラ用ホッパーではミセラ中の微粉の割合が多くなり次段工 程(精製工程)での精製歩留まりを下げ、工程に於けるトラブルの原因の一つと なっている。この欠陥の解決手段として、例えば各ミセラ用ホッパーを経るポン プアップ時に、その都度微粉を濾過する等の微粉分離手段を装備することも考え られているが、この様に各ホッパーごとに分離手段を取付けるには装置全体の大 型化が余儀無くされ、且つメンテナンスも極めて面倒となる等の欠点を有し、こ のため実用化までに至っていない。 However, in order to use the miscella accumulated in the miscella hopper as a solvent, the fine powder in the miscella inevitably increases when the oil and fat raw material is a fine material such as rice bran, and in the miscella hopper at the end, This is one of the causes of troubles in the process, as the proportion of fine powder increases and the refining yield in the next process (refining process) decreases. As a means for solving this defect, it is also considered to equip a fine powder separating means such as filtering fine powder each time when pumping up through each micella hopper, but in this way, a separating means is provided for each hopper. To install it, the size of the entire device is inevitable, and maintenance is extremely troublesome. For this reason, it has not been put to practical use.

【0005】 本考案は上記実情に鑑み、終端ミセラ用ホッパーの後方に別置きするケーシン グ内の円弧状スクリーン体にミセラを吹き付け強制的に液体と微粉を分離するよ うにし、上記課題を解決し微粉対策となる油抽出機におけるミセラ用微粉分離装 置を提供することを目的としたものである。In view of the above situation, the present invention solves the above problems by spraying a miscella on an arc-shaped screen body in a casing separately installed behind the hopper for the end miscella to forcibly separate the liquid and fine powder. The purpose of the present invention is to provide a fine powder separation device for a miscella in an oil extractor that is a countermeasure against fine powder.

【0006】[0006]

【課題を解決するための手段】[Means for Solving the Problems]

本考案は、気密型筐体内にあって、原料ホッパーに供給した油脂原料を下方の 固定の平滑搬送面に溜め、この油脂原料を平滑搬送面を走行するスクレーパーで 適宜層高として前方へ移動し、油脂原料の移動中に上方より散布する溶剤を浸透 させ油分を含む溶剤となるミセラを平滑搬送面のスリットを経て下方に配列の複 数個のミセラ用ホッパーで順次受け、この先方側ホッパーから手前側ホッパーに 向け濃度を上げた各ミセラを、それぞれ汲み上げその手前位置の使用溶剤とし、 平滑搬送面の最手前位置のホッパーで高濃度のミセラを得る油抽出機において、 終端のミセラ用ホッパーから導出の処理配管を縦型ケーシングの分流用フィード ヘッダーに接続し、該フィードヘッダーより分岐突設の複数本の案内チューブの 噴射ノズルを、ケーシング内の中央に縦装着した円弧状スクリーン体の上端位置 にその円弧面に沿うよう取付けし、且つ円弧状スクリーン体より下方のケーシン グを液体回収ホッパー部と微粉回収ホッパー部に区画したものである。 In the present invention, in the airtight case, the oil / fat raw material supplied to the raw material hopper is stored on the lower fixed smooth transport surface, and this oil / fat raw material is moved forward with a scraper running on the smooth transport surface at an appropriate layer height. During the movement of the oil / fat raw material, the miscella that permeates the solvent sprayed from above and becomes the solvent containing the oil is sequentially received by the multiple hoppers for miscella arranged below through the slits on the smooth transport surface. In an oil extractor that pumps each miscella whose concentration has been increased toward the front side hopper and uses it as the solvent at the front position to obtain a high concentration miscella at the frontmost hopper on the smooth transport surface, from the end miscella hopper. The discharge processing pipe is connected to the diverting feed header of the vertical casing, and the injection nozzles of the plurality of guide tubes branching and projecting from the feed header are connected to It is installed along the arc surface at the upper end position of the arc-shaped screen body vertically mounted in the center of the housing, and the casing below the arc-shaped screen body is divided into the liquid recovery hopper part and the fine powder recovery hopper part. is there.

【0007】[0007]

【作用】[Action]

上記のように、原料ホッパーに投入した油脂原料を平滑搬送面に一旦溜め、該 平滑搬送面を走行するスクレーパーで所定層高として溶剤散布工程側となる前方 へ移動し、天井側の溶剤パイプから散布の溶剤を油脂原料に注ぎ、溶剤にて油脂 原料内の油分を抽出し、この油分を含む溶剤となったミセラを平滑搬送面のスリ ットを経て複数個のミセラ用ホッパーに順次滴下し溜めて行き、各ミセラ用ホッ パーに溜まったミセラを夫々手前位置の溶剤パイプへポンプアップし使用溶剤と する。このため、原料給送側(手前位置)のミセラ用ホッパーに向かうにつれ溜 まるミセラは濃度を増し、終端のホッパーに溜まった濃厚ミセラをミセラ用微粉 分離装置に導き微粉と液体を分離する。即ち、ミセラ用ホッパーから導いた濃厚 ミセラを縦型のミセラ用微粉分離装置のフィードヘッダーに流入し、該フィード ヘッダーから噴射ノズルに流入し、該噴射ノズルから噴出するミセラを円弧状ス クリーン体のスクリーン面に噴射させれば、液体(油,溶剤)のみがネット型ス クリーン面を抜けて外側へ流下し、該スクリーン面を抜けられない微粉はこの内 側円弧に沿って滑り落ちる。即ち、液体と微粉が確実に分離する。 As described above, the oil / fat raw material charged in the raw material hopper is temporarily stored on the smooth conveying surface, and the scraper traveling on the smooth conveying surface moves to the front side which is the solvent spraying process side with a predetermined layer height and moves from the solvent pipe on the ceiling side. The spraying solvent is poured into the oil / fat raw material, the oil content in the oil / fat raw material is extracted with the solvent, and the miscella, which has become the solvent containing this oil, is dripped in sequence onto multiple hoppers for miscella through the slits on the smooth transport surface. The miscella accumulated in each miscella hopper is pumped up to the solvent pipes at the front position and used as the solvent to be used. For this reason, the concentration of the miscella that accumulates toward the miscella hopper on the raw material feeding side (front side) increases, and the concentrated miscella accumulated in the hopper at the end is guided to the miscella fine powder separator to separate fine powder and liquid. That is, the rich miscella introduced from the miscella hopper flows into the feed header of the vertical fine powder separation device for miscella, flows from the feed header into the injection nozzle, and ejects the miscella from the injection nozzle into an arc-shaped screen body. When sprayed onto the screen surface, only the liquid (oil, solvent) passes through the net-type screen surface and flows outward, and the fine powder that cannot pass through the screen surface slides down along the inner arc. That is, the liquid and the fine powder are reliably separated.

【0008】[0008]

【実施例】【Example】

以下、本考案を実施例の図面に基づいて説明すれば、次の通りである。 The present invention will be described below with reference to the drawings of the embodiments.

【0009】 1は一端上部に塔型原料ホッパー2を設け他端下部に排出ホッパー3を配設し た装置本体となる気密タンク構成の長方形状筐体であり、該筐体1の中央位置に 油脂原料搬送兼ミセラ落下用の固定型平滑搬送面4を敷設すると共に、該平滑搬 送面4上に無端の回転チェーン5で回転するスクレーパー6を走行する配設とし 、且つ平滑搬送面4の下方の長手方向に漏斗状槽構造となる複数個のミセラ用ホ ッパー7を連設し、該各ミセラ用ホッパー7の底部に有する流出口7aに接続し た汲み上げ配管9を、このミセラ用ホッパー7より一つ手前位置のミセラ用ホッ パー7の真上となる筐体天井部1aに横配管した溶剤パイプ8に順次接続する循 環配管とし、これら全体構成で油抽出機主体となる。10は前記複数個のミセラ 用ホッパー7中、濃厚なミセラを溜める終端のミセラ用ホッパー7′の流出口7 aに接続した処理配管11の先端側に配置したミセラ用微粉分離装置で、該ミセ ラ用微粉分離装置10の構成は、縦型ケーシング12の内部中央に、側面円弧を 呈する長方形カートリッジ枠13とネットスクリーン14より形成した円弧状ス クリーン体15を縦装着しケーシング内を前後2室に区画すると共に、この円弧 状スクリーン体15の上端縁部15aに複数本のミセラ噴射用ノズル16を、該 円弧状スクリーン体15の円弧端の延線上に位置し且つノズル口16aをスクリ ーン面14aの内側に臨むよう夫々取付け、また各ミセラ噴射用ノズル16のケ ーシング外に突出した基端には、ケーシング12の外頂部に横配設するミセラ流 入用フィードヘッダー17より分岐突設した複数本のフレキシブルチューブより なる案内チューブ18の弯曲先端を夫々接続し、且つケーシング12の下端部に あって円弧状スクリーン体15を堺とした前後位置に液体回収ホッパー部19と 微粉回収ホッパー部20を形成したものよりなる。21はミセラ噴射用ノズル1 6の先端部を把持するノズルセット具であり、22は案内チューブ18の基端部 に介在したボールバルブである。また、ミセラ用フィードヘッダー17の背部に 前記処理配管11の先端を接続する。Reference numeral 1 denotes a rectangular casing having an airtight tank structure, which is a main body of an apparatus, in which a tower-shaped raw material hopper 2 is provided at one end and a discharge hopper 3 is provided at a lower end of the other end. A fixed type smooth conveying surface 4 for transporting oil and fat materials and for dropping a miscella is laid, and a scraper 6 that rotates with an endless rotating chain 5 runs on the smooth conveying surface 4, and A plurality of miscella hoppers 7 having a funnel-shaped tank structure are continuously provided in the lower longitudinal direction, and a pumping pipe 9 connected to an outlet 7a at the bottom of each miscella hopper 7 is connected to the miscella hopper. 7 is a circulation pipe that is sequentially connected to a solvent pipe 8 that is laterally piped on the housing ceiling portion 1a that is located directly above the miscella hopper 7 and that is mainly composed of an oil extractor. Reference numeral 10 denotes a fine powder separation device for miscella, which is arranged at the tip end side of the processing pipe 11 connected to the outlet 7a of the misper hopper 7'of the end of the plurality of miscella hoppers 7 for accumulating rich miscella. The fine powder separating apparatus 10 for la has a structure in which an arc-shaped screen body 15 formed by a rectangular cartridge frame 13 having a side arc and a net screen 14 is vertically mounted in the center of the inside of a vertical casing 12 and two chambers in the front and rear are provided inside the casing. A plurality of miscella injection nozzles 16 are located at the upper edge 15a of the arcuate screen body 15, and are located on the extension line of the arcuate end of the arcuate screen body 15 and the nozzle port 16a is screened. Each of them is mounted so as to face the inside of the surface 14a, and the base end of each miscella injection nozzle 16 protruding outside the casing is laterally arranged on the outer top of the casing 12. Before and after the curved screen body 15 is located at the lower end of the casing 12 to which the curved tip ends of the guide tubes 18 made of a plurality of flexible tubes branchingly projecting from the miscella inlet feed header 17 are connected. A liquid recovery hopper section 19 and a fine powder recovery hopper section 20 are formed at the positions. Reference numeral 21 is a nozzle setting tool for holding the tip of the miscella injection nozzle 16 and reference numeral 22 is a ball valve interposed at the base end of the guide tube 18. Further, the tip of the processing pipe 11 is connected to the back of the miscella feed header 17.

【0010】 いまこの作用を説明すると、先ず所定の前処理を施した油脂原料(被抽出物) Aをスクリューコンベヤ23から原料ホッパー2に投入し下方の平滑搬送面4で 順次受け、原料ホッパー2内の中途位置まで堆積状態とする。ここで、平滑搬送 面4上を摺動走行のスクレーパー6で油脂原料Aを所定層高として繰出し溶剤散 布工程側となる前方へ移送する。Explaining this action, first, the oil / fat raw material (substance to be extracted) A which has been subjected to a predetermined pretreatment is put into the raw material hopper 2 from the screw conveyor 23 and sequentially received by the lower smooth conveying surface 4, and the raw material hopper 2 The deposition state is reached up to the middle position. Here, the oil / fat raw material A is fed out to a predetermined layer height by a scraper 6 that slides on the smooth conveying surface 4, and is forwarded to the solvent spraying process side.

【0011】 この様に、溶剤散布工程となる平滑搬送面4の前方へ移動した油脂原料Aに、 天井部位置の溶剤パイプ8から散布されたヘキサン等の溶剤Bが傾斜均一散布板 24を経て均等に注がれる(散布される)。この溶剤Bが油脂原料Aに浸透し油 分を抽出し、この油分と溶剤の混ざったミセラCが、平滑搬送面4を構成する多 数本の断面三角状のウエッジワイヤー4a間に形成されたスリット4bから滴下 し下方のミセラ用ホッパー7に順次溜めるものである。As described above, the solvent B such as hexane sprayed from the solvent pipe 8 at the ceiling portion passes through the inclined uniform spray plate 24 on the oil / fat raw material A that has moved to the front of the smooth transport surface 4 in the solvent spray step. Pour (sprinkle) evenly. The solvent B permeates the oil / fat raw material A to extract the oil, and the miscella C in which the oil and the solvent are mixed is formed between the plurality of wedge wires 4a having a triangular cross section which constitute the smooth transport surface 4. It is dropped from the slit 4b and is successively accumulated in the hopper 7 for the miscella below.

【0012】 この場合、ミセラ用ホッパー7に溜まったミセラCは、漏斗状底部に有する流 出口7aから汲み上げ用配管9に所定のポンプアップをし、このミセラ用ホッパ ー7より一つ手前位置のミセラ用ホッパー7の真上に位置した溶剤パイプ8に給 送し使用溶剤とする。即ち、各ミセラ用ホッパー7のミセラCを還流し隣りのミ セラ用ホッパー7の溶剤パイプ8の使用溶剤とするため、複数個のミセラ用ホッ パー7は新しい原料が繰出される平滑搬送面4の基方側に向けて濃度を順次高め て行き、終端のミセラ用ホッパー7′が最も濃厚なミセラCが溜まる。但し、こ のミセラC中には前記平滑搬送面4のスリット4bを通過してしまった微粉bの 量も順次増しているため、次段の精製工程に直接送らず所定の微粉分離作業を施 さねばならない。In this case, the miscella C accumulated in the miscella hopper 7 is pumped up from the outlet 7a provided at the funnel-shaped bottom part to the pumping pipe 9 by a predetermined amount so that the miscella hopper 7 is located in front of the miscella hopper 7. The solvent is fed to the solvent pipe 8 located directly above the micella hopper 7 and used as the solvent. That is, since the miscella C of each miscella hopper 7 is refluxed to be used as the solvent for the solvent pipe 8 of the adjacent miscella hopper 7, the plurality of miscella hoppers 7 have a smooth conveying surface 4 on which new raw materials are fed. The concentration is gradually increased toward the base side of, and the thickest miscella C is accumulated in the miscella hopper 7'for the end. However, since the amount of the fine powder b that has passed through the slit 4b of the smooth conveying surface 4 is gradually increasing in the miscella C, a predetermined fine powder separating operation is performed without directly sending the powder to the next purification step. I have to ask.

【0013】 ここにおいて、終端のミセラ用ホッパー7′に溜まった濃厚なミセラCを、処 理配管11を介してミセラ用微粉分離装置10の上部に配設のフィードヘッダー 17に導き、該フィードヘッダー17から分岐突設した複数本の案内チューブ1 8を経てミセラ噴射用ノズル16に圧送する。Here, the rich miscella C collected in the terminating miscella hopper 7 ′ is guided through a processing pipe 11 to a feed header 17 arranged above the fine powder separation device 10 for miscella, and the feed header 17 It is pressure-fed to the miscella injection nozzle 16 through a plurality of guide tubes 18 branchingly provided from 17.

【0014】 ここで、斜め下向きとなる前記ノズル16のノズル口16aが円弧状スクリー ン体15のスクリーン面14aの内側に位置するため、このノズル16を噴射し たミセラCは、液体(油,溶剤)aのみがネツトスクリーン14を通過し円弧状 スクリーン体15の外側に流出し液体回収ホッパー部19に流入する。一方、ス クリーン面14aを通過できなかったミセラC中の微粉bは、このスクリーン面 14aの内側円弧に沿って落下し下方の微分回収ホッパー20に溜まるものとな る。従って、この微粉bを分離した液体aを蒸留の精製工程に送ればよい。Here, since the nozzle opening 16a of the nozzle 16 which is directed obliquely downward is located inside the screen surface 14a of the arc-shaped screen body 15, the miscella C ejected from this nozzle 16 is a liquid (oil, oil, Only the solvent a passes through the net screen 14, flows out to the outside of the arcuate screen body 15, and flows into the liquid recovery hopper section 19. On the other hand, the fine powder b in the miscella C, which could not pass through the screen surface 14a, falls along the inner arc of the screen surface 14a and accumulates in the differential recovery hopper 20 below. Therefore, the liquid a from which the fine powder b has been separated may be sent to the purification step of distillation.

【0015】 ちなみに、米ぬか使用のミセラにおいて、スクリーン面がR760mmの円弧 形状のときノズルからの噴射圧力は1〜2kgでよい。By the way, in the miscella using rice bran, when the screen surface has an arc shape of R760 mm, the injection pressure from the nozzle may be 1 to 2 kg.

【0016】[0016]

【考案の効果】[Effect of device]

上述の様に、本考案の油抽出機におけるミセラ用微粉分離装置は終端のミセラ 用ホッパーの後部に接続する縦型ケーシング内に円弧状スクリーン体を縦装着し 内部を縦二分し、該円弧状スクリーン体のスクリーンの円弧面に沿ってミセラを ノズルをもって噴射させる構成としてなるため、ノズルから噴射したミセラ中、 液体(油,溶剤)分だけがスクリーン面を通過し、微粉はスクリーン面に接衝し 一種の濾過状態となって円弧内側に残り、該円弧に沿って滑り落ちる。即ち、ミ セラを円弧状スクリーン体に噴射するだけで、簡単,確実に液体と微粉を分離し 得る。このため、各ミセラ用ホッパーごとに微粉対策を施すことがないため、油 抽出機全体の装置の大型化が防げ、且つ精製工程の歩留まりを上げることにもな る。しかも、本考案は円弧状スクリーン体とノズルの組合わせとなる簡略構造の ため、使用中、目詰まり等の故障,誤動作などを招かず長期使用に耐え得るもの である。勿論、この円弧状スクリーン体の円弧角度は、使用する原料により適宜 選定することにより、目詰まりを招かない等の実用的効果も奏する。 As described above, the fine powder separating device for the miscella in the oil extractor of the present invention is such that the arcuate screen body is vertically mounted in the vertical casing connected to the rear part of the micella hopper at the end, and the inside is vertically divided into two parts. Since the miscella is sprayed by the nozzle along the arc surface of the screen of the screen body, only the liquid (oil, solvent) passes through the screen, and the fine powder contacts the screen. Then, it becomes a kind of filtration state and remains inside the arc, and slides down along the arc. That is, the liquid and the fine powder can be easily and reliably separated only by ejecting the miscella onto the arc-shaped screen body. For this reason, since no countermeasures against fine powder are taken for each miscella hopper, it is possible to prevent the overall size of the oil extractor from increasing in size and to increase the yield of the refining process. Moreover, since the present invention has a simple structure in which the arc-shaped screen body and the nozzle are combined, it can withstand long-term use without causing troubles such as clogging during use and malfunctions. Of course, by appropriately selecting the arc angle of the arc-shaped screen body according to the raw material used, practical effects such as not causing clogging can be obtained.

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

【図1】この考案のミセラ用微粉分離装置を備えた油抽
出機の実施例を示す側面図である。
FIG. 1 is a side view showing an embodiment of an oil extractor equipped with a fine powder separating device for a miscella according to the present invention.

【図2】同平面図である。FIG. 2 is a plan view of the same.

【図3】ミセラ用微粉分離装置の要部拡大断面図であ
る。
FIG. 3 is an enlarged cross-sectional view of a main part of a fine powder separating device for a miscella.

【図4】同ミセラ用微粉分離装置の一部切り欠き正面図
である。
FIG. 4 is a partially cutaway front view of the fine powder separating apparatus for the miscella.

【符号の説明】[Explanation of symbols]

1 筐体 2 原料ホッパー 4 平滑搬送面 6 スクレーパー 7 ミセラ用ホッパー 8 溶剤パイプ 11 処理配管 12 縦型ケーシング 15 円弧状スクリーン体 16 ミセラ噴射用ノズル 17 フィードヘッダー 18 案内チューブ 19 液体回収ホッパー部 20 微粉回収ホッパー部 1 Case 2 Raw Material Hopper 4 Smooth Transport Surface 6 Scraper 7 Hopper for Miscella 8 Solvent Pipe 11 Processing Pipe 12 Vertical Casing 15 Circular Screen Body 16 Miscella Jet Nozzle 17 Feed Header 18 Guide Tube 19 Liquid Recovery Hopper 20 Fine Powder Recovery Hopper part

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 気密型筐体内にあって、原料ホッパーに
供給した油脂原料を下方の固定の平滑搬送面に溜め、こ
の油脂原料を平滑搬送面を走行するスクレーパーで適宜
層高として前方へ移動し、油脂原料の移動中に上方より
散布する溶剤を浸透させ油分を含む溶剤となるミセラを
平滑搬送面のスリットを経て下方に配列の複数個のミセ
ラ用ホッパーで順次受け、この先方側ホッパーから手前
側ホッパーに向け濃度を上げた各ミセラを、それぞれ汲
み上げその手前位置の使用溶剤とし、平滑搬送面の最手
前位置のホッパーで高濃度のミセラを得る油抽出機にお
いて、終端のミセラ用ホッパーから導出の処理配管を縦
型ケーシングの分流用フィードヘッダーに接続し、該フ
ィードヘッダーより分岐突設の複数本の案内チューブの
噴射ノズルを、ケーシング内の中央に縦装着した円弧状
スクリーン体の上端位置にその円弧面に沿うよう取付け
し、且つ円弧状スクリーン体より下方のケーシングを液
体回収ホッパー部と微粉回収ホッパー部に区画してなる
油抽出機におけるミセラ用微粉分離装置。
1. An oil / fat raw material supplied to a raw material hopper is stored in a fixed smooth conveying surface below in an airtight casing, and the oil / fat raw material is moved forward by a scraper traveling on the smooth conveying surface to a proper layer height. Then, while moving the oil and fat raw material, the solvent sprayed from above is permeated and the miscella that becomes the solvent containing the oil is sequentially received by the multiple hoppers for miscella arranged below through the slits on the smooth transport surface, and from this side hopper. In an oil extractor that pumps each miscella whose concentration has been increased toward the front hopper and uses it as the solvent at the front position to obtain a high-concentration miscella at the frontmost hopper on the smooth transport surface, from the end miscella hopper. The discharge processing pipe is connected to the diverting feed header of the vertical casing, and the injection nozzles of the plurality of guide tubes branching from the feed header are connected to the casing. Oil that is installed along the arc surface at the upper end position of the arc-shaped screen body vertically mounted in the center of the single chamber, and divides the casing below the arc-shaped screen body into the liquid recovery hopper part and the fine powder recovery hopper part. Fine powder separator for miscella in the extractor.
JP1993024491U 1993-05-12 1993-05-12 Fine powder separator for miscella in oil extractor Expired - Lifetime JP2595161Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1993024491U JP2595161Y2 (en) 1993-05-12 1993-05-12 Fine powder separator for miscella in oil extractor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1993024491U JP2595161Y2 (en) 1993-05-12 1993-05-12 Fine powder separator for miscella in oil extractor

Publications (2)

Publication Number Publication Date
JPH0683759U true JPH0683759U (en) 1994-11-29
JP2595161Y2 JP2595161Y2 (en) 1999-05-24

Family

ID=12139657

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1993024491U Expired - Lifetime JP2595161Y2 (en) 1993-05-12 1993-05-12 Fine powder separator for miscella in oil extractor

Country Status (1)

Country Link
JP (1) JP2595161Y2 (en)

Also Published As

Publication number Publication date
JP2595161Y2 (en) 1999-05-24

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