JPS6279860A - Separation of solid matter from hardly separable liquid - Google Patents

Separation of solid matter from hardly separable liquid

Info

Publication number
JPS6279860A
JPS6279860A JP60220410A JP22041085A JPS6279860A JP S6279860 A JPS6279860 A JP S6279860A JP 60220410 A JP60220410 A JP 60220410A JP 22041085 A JP22041085 A JP 22041085A JP S6279860 A JPS6279860 A JP S6279860A
Authority
JP
Japan
Prior art keywords
liquid
angle
inclination angle
solid
inclination
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.)
Pending
Application number
JP60220410A
Other languages
Japanese (ja)
Inventor
Masaaki Sakurai
桜井 雅章
Shoroku Suzuki
鈴木 荘六
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KOTOBUKI TEKKOSHO KK
Mitsui Toatsu Chemicals Inc
Original Assignee
KOTOBUKI TEKKOSHO KK
Mitsui Toatsu Chemicals Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by KOTOBUKI TEKKOSHO KK, Mitsui Toatsu Chemicals Inc filed Critical KOTOBUKI TEKKOSHO KK
Priority to JP60220410A priority Critical patent/JPS6279860A/en
Publication of JPS6279860A publication Critical patent/JPS6279860A/en
Pending legal-status Critical Current

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  • Non-Alcoholic Beverages (AREA)
  • Centrifugal Separators (AREA)
  • Beans For Foods Or Fodder (AREA)
  • Tea And Coffee (AREA)

Abstract

PURPOSE:To economically separate solid matter from liquid with high accuracy by using a double cant type decanter for solid-liquid sepn. in a food producing stage and specifying the degree of inclination for discharging settled solid particles. CONSTITUTION:The initial angle X of inclination of a sloped part 1a for discharging the settled solid particles is set larger than the angle Y of inclination of the terminal and the angle of inclination of the liquid surface part is set same as the angle Y or larger than said angle but smaller than the angle X in a method for separating the solid matter from the hardly separable liquid such as concd. coffee, fruit juice or soybean milk. The double cant type decanter is adopted for the solid-liquid sepn. in the food producing stage in the above- mentioned manner, by which the fine particles are separated and removed with good accuracy and the yield of the product is improved.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は濃縮コーヒー中に存在する固型物およびタール
状物質の除去、果汁からのバルブ物質の除去、q乳から
のおからの除去などを行うための改良された方法に関す
る。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is applicable to the removal of solids and tar-like substances present in concentrated coffee, the removal of valve substances from fruit juice, the removal of okara from milk, etc. Concerning an improved method for performing.

〔従来の技術〕[Conventional technology]

スーパーデカンタやスクリューデカンタ等と呼ばれてい
るスクリュー式連続遠心沈降装置は、沈降固体粒Y−を
連続的に外部に排出する機構をもっている。この種の装
置は、円すい形または円筒−円すい形の高速回転するボ
ウルと、このボウルとわずかの間隙をもって回転して、
ボウルの内面に付着した固体粒子をボウル外へ排出する
スクリューとを備えている。ところが、実際の操業にあ
たっては、このボウルの形状か問題となる。
A screw-type continuous centrifugal sedimentation device called a super decanter, screw decanter, etc. has a mechanism for continuously discharging settled solid particles Y- to the outside. This type of device includes a conical or cylindrical-conical bowl that rotates at high speed, and a bowl that rotates with a small gap between the bowl and the bowl.
The bowl is equipped with a screw that discharges solid particles attached to the inner surface of the bowl to the outside of the bowl. However, in actual operation, the shape of this bowl becomes a problem.

固体粒Y〜を排出する部分は面述のように円すい形にな
っているが、排出を効果的にするには、ボウルの円すい
部(傾斜部分)の傾斜角を非常に小さくしなければなら
ない。ところが、このように傾斜角を小さくすると、回
転体およびスクリューの長さを著しく大きくとらなけれ
ばならない。したがって所要の性能を得るためには、装
置の大型化が避けられない。これは、装置の設備空間が
大きくなることを意味し、実際ト、コスト高を招くばか
りでなく、操業に非常な不便をもたらすことになる。ま
た、操業の効率も悪くなる。
The part that discharges the solid particles Y~ has a conical shape as described above, but in order to make the discharge effective, the angle of inclination of the conical part (slanted part) of the bowl must be made very small. . However, if the inclination angle is made small in this way, the length of the rotating body and the screw must be significantly increased. Therefore, in order to obtain the required performance, it is inevitable to increase the size of the device. This means that the installation space of the apparatus becomes large, which not only causes an increase in costs but also brings great inconvenience to the operation. In addition, the efficiency of operation also deteriorates.

また、ボウル円すい部の傾斜角を小さくすると、ボウル
中の液深を浅くしなければならないので、被処理懸濁液
中の固体と液体との比重差が小さい場合には固体の分離
が十分に行なわれないこととなる。
In addition, if the inclination angle of the bowl cone is made smaller, the depth of the liquid in the bowl must be made shallower, so if the difference in specific gravity between the solid and liquid in the suspension to be treated is small, the separation of the solids will be insufficient. It will not be done.

このような欠点の解消のために本発明者らの一人は特開
昭50−54961 号に開示されたダブルカント型ス
クリュー式連続遠心沈降装置を提案した。
In order to eliminate these drawbacks, one of the present inventors proposed a double cant type screw type continuous centrifugal sedimentation device disclosed in Japanese Patent Application Laid-open No. 54961/1983.

このダブルカント型スクリュー式連続遠心沈降装置にお
いては、ボウルの沈降固体粒子排出用の傾斜部分の初期
傾斜角が終端傾斜角より大きく設定され、かつ液面のと
ころの傾斜角は終端傾斜角と同一か、またはそれよりも
大きいが初期傾斜角よりも小さく設定され、懸濁液から
分離された固体は液面向Fのところから緩かな傾斜面に
沿って液面北に搬送される。この装置により固液の分離
を行なう場合、沈降した固体粒子は液面下では液体と固
体粒子”との比重差により遠心力の作用を受け、液面上
では固体粒子の比重に比例して遠心力の作用を受ける。
In this double-cant screw type continuous centrifugal sedimentation device, the initial inclination angle of the inclined part of the bowl for discharging settled solid particles is set larger than the final inclination angle, and the inclination angle at the liquid level is the same as the final inclination angle. or larger but smaller than the initial inclination angle, and the solids separated from the suspension are transported from the liquid surface direction F along a gentle slope to the north of the liquid surface. When separating solid and liquid using this device, the settled solid particles are subjected to centrifugal force under the liquid surface due to the difference in specific gravity between the liquid and the solid particles, and above the liquid surface, they are centrifuged in proportion to the specific gravity of the solid particles. subjected to the action of force.

したかって液面下にある固体粒7− jJト出川用傾斜
部分の傾斜角を大きくとっても、液中での固体粒りの搬
送は可能であるが、液面上では固体粒子の受りる遠心力
効果が比較的大きいので傾斜角を小さくして搬送を容易
にできるようにしたのである。
Therefore, even if the angle of inclination of the slope section for solid particles below the liquid level is large, it is possible to transport the solid particles in the liquid. Since the force effect is relatively large, the angle of inclination was made small to facilitate transportation.

上記のダブルカント型の装置によって沈降固体粒子の排
出能力を高く保持しながら装置の小型化が可能となり、
活性汚泥のように比重が1.02〜1.04程度で水と
の比重差が小さく、微細な粒子である上に、脱水される
とプリン状またはペースト状であフて極めて塑性変形を
受けやすいケーキとなる物質の懸濁液を固液に分離する
場合にも満足すべき結果を得ることができるようになっ
た。
The above-mentioned double cant type device makes it possible to downsize the device while maintaining a high discharge capacity for settled solid particles.
Like activated sludge, it has a specific gravity of about 1.02 to 1.04, with a small difference in specific gravity from water, and is fine particles, and when dehydrated, it becomes pudding-like or paste-like and is extremely susceptible to plastic deformation. Satisfactory results can now be obtained even when a suspension of a substance that easily forms a cake is separated into solid and liquid.

インスタントコーヒーの製造において、濃縮設備出口の
濃縮コーヒー中には分離設備をリークした来た固型物お
よび濃縮設備中で生成した固型物およびタール状物質の
存在が知られているが、濃縮コーヒーが約10,000
センチボイズと極めて高粘度であるために、有効な経済
的な分離方法がなく、これらの物質は製品中に混入し、
飲用の際にカップの底に残留し、品質に与える印象が問
題となっていた。
In the production of instant coffee, it is known that the concentrated coffee at the outlet of the concentration equipment contains solid substances that have leaked from the separation equipment and solid substances and tar-like substances that have been generated in the concentration equipment. is approximately 10,000
Due to their centiboids and extremely high viscosity, there are no effective and economical separation methods, and these substances end up in the product.
When drinking, it remains at the bottom of the cup, giving an impression of quality, which has become a problem.

また、果汁はその溶質として糖分、打機酸を合有し、液
比型は1よりも大きく、また固型物として植物セルロー
ス(パルプ質)を含むので、従来遠心分離が困難でスク
リュープレスなどの濾過機が搾汁機として多用されて来
た。しかし、搾汁機において果汁の清澄性を高めようと
して濾過精度を上げると濾過面がパルプ質で目詰りを起
す。
In addition, fruit juice contains sugar and persimmon acid as its solutes, has a liquid ratio greater than 1, and contains plant cellulose (pulp) as a solid, so it is difficult to centrifuge it, so it is difficult to use a screw press. filtration machines have been widely used as juice extraction machines. However, if the filtration accuracy is increased in an attempt to improve the clarity of fruit juice in a juice extractor, the filtration surface becomes clogged with pulp.

従って、多くの工場では搾汁機の′ti過目を大きくし
て目詰りを防いで操業しているので、搾汁中にはパルプ
質が2〜5fflff1%リークし、後の工程でディス
ク型(デラバル型またはウエストファリア型とも呼ばれ
る)デカンタ−によりパルプ質を分離する必要がある。
Therefore, in many factories, the extraction machine is operated with a large opening to prevent clogging, so 2 to 5% of the pulp leaks out during the extraction process, and in the later process the disc-shaped It is necessary to separate the pulp using a decanter (also called DeLaval type or Westfalia type).

しかし、このようなデカンタ−は構造上、内部において
目詰りを起し易く、またパルプ質の濃縮スラリーとして
排出されるので果汁の損失か問題であった。
However, due to the structure of such a decanter, the inside of the decanter is easily clogged, and the decanter is discharged as a pulpy concentrated slurry, resulting in a loss of fruit juice.

さらに、豆腐の製造においても豆乳からおからを分離す
るに宵1って、高精度ておからを分離することにより、
固型物を含まない豆乳が得られ、これから得られる豆腐
は品質の優れたものとなり得るが、このように高精度で
豆乳からおからを分離するための手段は知られていなか
った。
Furthermore, in the production of tofu, by separating okara from soy milk with high precision,
Although soybean milk containing no solids can be obtained, and the tofu obtained from this can be of excellent quality, there has been no known means for separating okara from soymilk with such high precision.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明は上記のような食品製造工程における液体から固
を物の分離を高精度に、かつ経済的に行なう方法を提供
しようとするものである。
The present invention aims to provide a method for accurately and economically separating solids from liquids in the food manufacturing process as described above.

c問題点を解決するための手段〕 本発明の難分#液体から固型物の分離方法は濃縮コーヒ
ーからの固型物およびタール状物質の除去、搾果汁から
のバルブ状物質の除去、またはσ乳からおからの除去を
行うに当って、ボウルの沈降固体粒Y・排出用の傾斜部
分の初期傾斜角が終端傾斜角より大きく設定され、かつ
液面のところの傾斜角は終端傾斜角と同一・か、または
それより大きいが初期傾斜角よりも小さく設定されたス
クリュー型遠心沈降機を用いて前記除去を行うことを特
徴とするものである。
[Means for Solving Problems] Difficulties #The method of separating solids from liquid of the present invention is the removal of solids and tar-like substances from concentrated coffee, the removal of bulb-like substances from squeezed fruit juice, or When removing okara from σ milk, the initial inclination angle of the inclined part for settling solid particles Y and discharge of the bowl is set to be larger than the final inclination angle, and the inclination angle at the liquid level is set to be equal to the final inclination angle. The method is characterized in that the removal is carried out using a screw type centrifugal sedimentation machine set to be the same as or larger than the initial inclination angle but smaller than the initial inclination angle.

本発明方法の実施に用いるスクリュー式遠心沈降機は、
いわゆるダブルカント型と呼ばれるもので、そのボウル
とスクリュー部分の代表的な例を第1図に示す。第1図
において、1はボウル、2はスクリューを示し、3は液
面を示す。1aは沈降固体粒子排出用の傾斜部分であり
、Xはこの傾斜部の初jυ1傾斜角を、Yは終端傾斜角
を示す。Zはこれら2段の傾斜部分の合致点であり、液
面3よりも少しドに位置する。角XはIO°〜80°、
角Yは2°〜15°であるのが好ましい。また、傾斜部
分を3段以上の多段または曲面としてもよいし、さらに
液面直下の傾斜部分に、液面−ヒに搬送される沈降固体
粒子が液中へ逆流するのを防止するための滞留部を設け
てもよい。
The screw type centrifugal sedimentation machine used to carry out the method of the present invention is
This is the so-called double cant type, and a typical example of its bowl and screw portion is shown in Figure 1. In FIG. 1, 1 indicates a bowl, 2 indicates a screw, and 3 indicates a liquid level. 1a is a sloped part for discharging settled solid particles, X shows the initial jυ1 inclination angle of this sloped part, and Y shows the final inclination angle. Z is the matching point of these two tiered inclined portions, and is located slightly below the liquid level 3. Angle X is IO° ~ 80°,
Preferably, the angle Y is between 2° and 15°. Further, the sloped portion may be multi-staged with three or more stages or a curved surface, and further, the sloped portion directly below the liquid surface is provided with a retention area to prevent the settled solid particles conveyed to the liquid surface from flowing back into the liquid. A section may be provided.

以下に本発明の液体からの固型物の分離を濃縮コーヒー
、搾果汁、豆乳の場合につき、第2図〜第4図を参照し
て具体的に説明する。
The separation of solids from liquids according to the present invention will be specifically explained below in the case of concentrated coffee, squeezed fruit juice, and soybean milk with reference to FIGS. 2 to 4.

縮コーヒー の古升り お びタール゛  の部 第2図はインスタントコーヒー製造工程の一例を示すフ
ローシートである。原料コーヒーは抽出装置2Iにおい
て熱湯で抽出され、コーヒーかすは底部から排出される
。抽出7&(コーヒー液)は固液分離装置22で随伴さ
れる固型物を分離除去されたのち、濃縮装置23で濃縮
される。濃縮装置からの濃縮コーヒーは濃縮過程で生成
した固型物を随伴し、粘度は10,000センチボイズ
と極めて高い。
Fig. 2 is a flow sheet showing an example of the instant coffee manufacturing process. The raw coffee is extracted with hot water in the extraction device 2I, and the coffee grounds are discharged from the bottom. Extract 7 & (coffee liquid) is subjected to separation and removal of accompanying solid matter in a solid-liquid separator 22, and then concentrated in a concentrator 23. Concentrated coffee from a concentrator is accompanied by solid matter produced during the concentration process, and has an extremely high viscosity of 10,000 centivoids.

この濃縮コーヒーを第1図に示したボウル形状をもつダ
ブルカント型スクリュー式遠心沈降機(以下ダブルカン
ト型デカンタ−という)24供給し、固型物およびター
ル状物質を分離除去する。このダブルカント型デカンタ
−における分離操作により10〜20ミクロンの微粒子
までほぼ100%の精度で除去される。
This concentrated coffee is fed to a double cant type screw type centrifugal sedimentation machine (hereinafter referred to as a double cant type decanter) 24 having a bowl shape as shown in FIG. 1, and solids and tar-like substances are separated and removed. This separation operation in the double cant decanter removes fine particles down to 10 to 20 microns with almost 100% accuracy.

このようにして得られた濃縮コーヒーを乾燥装置25で
乾燥して得られたインスタントコーヒーの製品26は飲
用の際カップの底には残留物がなかった。
The instant coffee product 26 obtained by drying the concentrated coffee thus obtained in the drying device 25 had no residue on the bottom of the cup when drinking.

二1〜′か のバルブ9のノ 第3図は果汁製造工程の一例を示すフローシートである
。原料果実はベルトコンベヤーにより破砕機31に供給
されて破砕され、得られた破砕物は搾汁機32に送られ
、ここで搾果汁がらバルブ質が分離される。この搾汁機
として従来用いられたスクリューブレス32°などに代
えて本発明では第1図に示したようなダブルカント型デ
カンタ−32を用いる。ダブルカント型デカンタ−32
を出た果汁は殺菌器33を経て包装設備35.殺菌設備
36を経て製、漬37となる。従来は搾汁機32°から
の果汁中には2〜5%のバルブ質が随伴されていたので
、殺菌器33の後にバルブ質分離機34を設ける必要が
あったが、本発明に、よれば搾汁機32を出る果汁中に
含むバルブ室は必要濃度、例えば混濁りんごジュースで
は0.3〜0.6重量%になるように運転が可能である
から、バルブ質分離機34は省略することができる。
FIG. 3 of the valve 9 in items 21-' is a flow sheet showing an example of the fruit juice manufacturing process. The raw fruit is supplied to a crusher 31 by a belt conveyor and crushed, and the resulting crushed product is sent to a juicer 32, where the pulp is separated from the squeezed fruit juice. In the present invention, a double cant type decanter 32 as shown in FIG. 1 is used in place of the 32° screw press or the like conventionally used as the juice extracting machine. Double cant type decanter 32
The juice that comes out passes through a sterilizer 33 and is sent to packaging equipment 35. After going through sterilization equipment 36, it is made into pickles 37. Conventionally, the fruit juice from the juice extractor 32° contained 2 to 5% bulb quality, so it was necessary to install a bulb quality separator 34 after the sterilizer 33. Since the valve chamber contained in the juice exiting the juice extractor 32 can be operated to maintain the required concentration, for example, 0.3 to 0.6% by weight for cloudy apple juice, the valve quality separator 34 is omitted. be able to.

本発明によれば、搾汁機32を出るバルブ質は濃縮スラ
リーではなく、ケーキとして果汁を実質的に完全に搾っ
た状態で回収されるので、果汁の損失がなく、従って原
料果実に対するジュースの収率が向北する。
According to the present invention, the pulp exiting the juice extractor 32 is not recovered as a concentrated slurry, but as a cake with substantially all the juice squeezed out, so that there is no loss of juice and, therefore, a reduction in juice relative to the raw fruit. Yield is heading north.

−か のおかCの′ 第4図は大豆からの豆乳の製造工程の一例を示すフロー
シートである。原料大豆は浸積器41中で水中に約1晩
浸積され、磨砕しやすくし、磨砕機42に供給される。
-Kanooka C' Figure 4 is a flow sheet showing an example of the process for producing soymilk from soybeans. The raw soybeans are soaked in water for about one night in a soaker 41 to make them easier to grind, and then fed to a grinder 42 .

磨砕機42で充分になめらかに磨砕されて磨砕生汁とさ
れる。この生汁は加熱器43中で加熱されて脂肪、植物
性蛋白質を液中に抽出される。加熱器43からのおから
を含む豆乳は第1図に示したダブルカント型デカンタ−
44に供給され豆乳をおからから分層する。こうして得
られた豆乳は固型物を実質的に含まず、これから製造さ
れた豆腐はなめらかで美味であった。
It is sufficiently and smoothly ground by a grinder 42 to obtain ground raw juice. This raw juice is heated in a heater 43 to extract fat and vegetable protein into the liquid. The soybean milk containing okara from the heater 43 is transferred to the double cant decanter shown in FIG.
44 to separate the soy milk from okara. The soymilk thus obtained was substantially free of solid matter, and the tofu produced therefrom was smooth and delicious.

また、分離されたおからは充分に豆乳が分離されている
ので原料大豆に対する豆乳の収率を2〜4%高めること
が可能である。
Furthermore, since the soybean milk is sufficiently separated from the separated okara, it is possible to increase the yield of soymilk by 2 to 4% based on the raw soybeans.

〔発明の効果〕〔Effect of the invention〕

以上述べたように、本発明によれば、上記食品製造工程
の固液分離にダブルカント型デカンタ−を採用すること
により、従来不可能ないし困難であった微細粒子を精度
よく分離除去することができ、また製品収率を改善し、
さらに工程の簡略化をも行なうことができるなど品質の
改善、製造コストの低下に顕著な効果が得られる。
As described above, according to the present invention, by employing a double cant decanter for solid-liquid separation in the food manufacturing process, it is possible to accurately separate and remove fine particles, which was previously impossible or difficult. can also improve product yield,
Furthermore, the process can be simplified, resulting in significant improvements in quality and reduction in manufacturing costs.

なお、本発明は上記の3例の食品製造工程につき具体的
に説明されたが、これ以外の種々の食品製造工程におけ
る固液分離にも有利に採用することができるのは、いう
までもないことである。
Although the present invention has been specifically explained with respect to the three food manufacturing processes mentioned above, it goes without saying that it can be advantageously applied to solid-liquid separation in various other food manufacturing processes. That's true.

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

第1図は本発明の実施に用いられるダブルカント型スク
リュー式遠心沈降機のボウルとスクリュー部分を示す説
明図、第2図はインスタントコーヒー製造工程の一例を
示すフローシート、第・ 3図は果汁製造工程の一例を
示すフローシート、第4図は大豆からの豆乳製造工程の
一例を示すフローシートである。 1・・・ボウル、     2・−スクリュー、3・・
・液面、21・−抽出装置、 22・・・固W、分離装置、 23−・・濃縮装置、2
4−・・ダブルカント型デカンタ−125・・・乾燥装
置、   26・・・製品。 31・・・破砕機、 32・・・搾汁機(ダブルカント型デカンタ−)、32
°・・・スクリュープレス、 33−・・殺菌器、    34・・・パルプ買分離機
、35・・・包装設備、   36・・・殺菌設備、4
1・・・浸積器、    42−・・磨砕機、イ3・・
・加熱器、 44・・・ダブルカント型デカンタ−0特許出願人 三
井東圧化学株式会社 株式会社 壽鐵工所
Figure 1 is an explanatory diagram showing the bowl and screw portion of the double-cant screw type centrifugal sedimentation machine used in the implementation of the present invention, Figure 2 is a flow sheet showing an example of the instant coffee manufacturing process, and Figures 3 and 3 are illustrations of the bowl and screw portion of the double-cant screw type centrifugal sedimentation machine used in the implementation of the present invention. Flowsheet showing an example of the manufacturing process. FIG. 4 is a flowsheet showing an example of the process of manufacturing soybean milk from soybeans. 1... Bowl, 2... Screw, 3...
-Liquid level, 21--Extraction device, 22--Solid W, separation device, 23--Concentration device, 2
4-...Double cant type decanter-125...Drying device, 26...Product. 31... Crusher, 32... Juicing machine (double cant decanter), 32
°... Screw press, 33-... Sterilizer, 34... Pulp buying separator, 35... Packaging equipment, 36... Sterilization equipment, 4
1... soaker, 42-... grinder, i3...
・Heater, 44...Double cant type decanter - 0 Patent applicant: Mitsui Toatsu Chemical Co., Ltd., Ju Iron Works Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 濃縮コーヒーからの固型物およびタール状物質の除去、
搾果汁からのパルプ状物質の除去、または豆乳からおか
らの除去を行うに当って、ボウルの沈降固体粒子排出用
の傾斜部分の初期傾斜角が終端傾斜角より大きく設定さ
れ、かつ液面のところの傾斜角は終端傾斜角と同一か、
またはそれより大きいが初期傾斜角よりも小さく設定さ
れたスクリュー式遠心沈降機を用いて前記除去を行うこ
とを特徴とする難分離液体から固形物の分離方法。
Removal of solids and tarry substances from concentrated coffee,
When removing pulpy substances from squeezed fruit juice or removing okara from soy milk, the initial inclination angle of the inclined part of the bowl for discharging settled solid particles is set larger than the final inclination angle, and the liquid level is However, is the inclination angle the same as the terminal inclination angle?
Or a method for separating solids from a difficult-to-separate liquid, characterized in that the removal is carried out using a screw-type centrifugal sedimentation machine set to be larger than the initial inclination angle but smaller than the initial inclination angle.
JP60220410A 1985-10-04 1985-10-04 Separation of solid matter from hardly separable liquid Pending JPS6279860A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60220410A JPS6279860A (en) 1985-10-04 1985-10-04 Separation of solid matter from hardly separable liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60220410A JPS6279860A (en) 1985-10-04 1985-10-04 Separation of solid matter from hardly separable liquid

Publications (1)

Publication Number Publication Date
JPS6279860A true JPS6279860A (en) 1987-04-13

Family

ID=16750679

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60220410A Pending JPS6279860A (en) 1985-10-04 1985-10-04 Separation of solid matter from hardly separable liquid

Country Status (1)

Country Link
JP (1) JPS6279860A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007102385A1 (en) * 2006-03-08 2007-09-13 Ehime Beverage Inc. Carotenoid-rich material, method of producing the same and product comprising the same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS542409A (en) * 1977-06-01 1979-01-10 Dainippon Ink & Chemicals Composition for paper coating

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS542409A (en) * 1977-06-01 1979-01-10 Dainippon Ink & Chemicals Composition for paper coating

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007102385A1 (en) * 2006-03-08 2007-09-13 Ehime Beverage Inc. Carotenoid-rich material, method of producing the same and product comprising the same
JP2007236285A (en) * 2006-03-08 2007-09-20 Ehime Inryo:Kk Carotinoid highly containing-material, production method for the same, and product of the material

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