JP2744546B2 - Solid extractor - Google Patents

Solid extractor

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Publication number
JP2744546B2
JP2744546B2 JP4080038A JP8003892A JP2744546B2 JP 2744546 B2 JP2744546 B2 JP 2744546B2 JP 4080038 A JP4080038 A JP 4080038A JP 8003892 A JP8003892 A JP 8003892A JP 2744546 B2 JP2744546 B2 JP 2744546B2
Authority
JP
Japan
Prior art keywords
tank
extraction
rotary
extract
extraction tank
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
Application number
JP4080038A
Other languages
Japanese (ja)
Other versions
JPH05277303A (en
Inventor
彦重 藤井
Original Assignee
株式会社栃本天海堂
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 株式会社栃本天海堂 filed Critical 株式会社栃本天海堂
Priority to JP4080038A priority Critical patent/JP2744546B2/en
Publication of JPH05277303A publication Critical patent/JPH05277303A/en
Application granted granted Critical
Publication of JP2744546B2 publication Critical patent/JP2744546B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Medicines Containing Plant Substances (AREA)
  • Extraction Or Liquid Replacement (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】この発明は固体抽出機において、
特に桂皮、甘草等の生薬を抽出する場合に好適な固体抽
出機に関する。
The present invention relates to a solid extractor,
Particularly, the present invention relates to a solid extractor suitable for extracting crude drugs such as cinnamon and licorice.

【0002】[0002]

【従来の技術】一般に、固体中に含まれる可溶成分を抽
剤中に移動させる固体抽出機としては種々のものが提供
されている。生薬を工業的に抽出しそのエキスを得る場
合も、これらの固体抽出機が用いられているが、従来、
特に抽出槽内に攪拌用の回転翼を設置しこの回転翼の攪
拌作用により抽出する抽出機や、抽出槽の槽底より送り
揚げた抽剤を上部より散布し抽剤を繰り返し循環させて
抽出する抽出機がよく使用されている。
2. Description of the Related Art In general, various types of solid extractors for transferring a soluble component contained in a solid into an extractant have been provided. Even when crude drugs are industrially extracted and their extracts are obtained, these solid extractors are used.
In particular, an extractor that installs a rotary impeller for stirring in the extraction tank and performs extraction by the stirring action of the rotary impeller, or extracts from the top of the extractor by spraying the extractant that has been pumped from the bottom of the extractor tank and repeatedly circulating the extractant for extraction Extractors are commonly used.

【0003】[0003]

【発明が解決しようとする課題】しかしこの種の抽出機
では抽剤との接触回数が乏しく、抽出効率の点で未だ満
足できるものではない。特に裁断、粉砕等された生薬を
被抽出物とする場合、抽剤の攪拌や循環散布だけでは所
望とするエキスを短時間で得難い問題点がある。また生
薬を被抽出物とする場合、従来は上記の抽出機で抽出さ
れた液を別途濾過機で濾過し、さらにこれを濃縮してエ
キスを得る工程を必要としていた。
However, in this type of extractor, the number of times of contact with the extractant is poor, and extraction efficiency is still unsatisfactory. In particular, when a crude drug that has been cut or pulverized is used as the extract, there is a problem that it is difficult to obtain a desired extract in a short time only by stirring the extractant or circulating the extract. Further, when a crude drug is used as an extract, conventionally, a step of separately filtering a liquid extracted by the above-mentioned extractor with a filter and further concentrating the extract to obtain an extract has been required.

【0004】この発明の目的は、抽出効率がきわめてす
ぐれ、濾過と濃縮を同時にすることもでき、生薬の抽出
に好適である固体抽出機を提供する点にある。
An object of the present invention is to provide a solid extractor which is extremely excellent in extraction efficiency, can simultaneously perform filtration and concentration, and is suitable for extracting crude drugs.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に鋭意検討した結果、この発明は、抽出槽内に被抽出物
が投入される多孔構造の回転槽を取り付けた固体抽出機
を採用した。
As a result of intensive studies to achieve the above object, the present invention employs a solid extractor equipped with a rotary tank having a porous structure into which an extract is charged in an extraction tank. .

【0006】回転槽は通常は回転軸を通じて槽外の攪拌
モーターと連結し、攪拌モーターの回転駆動により回転
する構成とするが、特にその回転手段については限定さ
れない。また回転槽は例えばパンチングメタルなど多孔
構造であれば差支えないが、好ましくは被抽出物が回転
槽の回転により衝突すると同時に、抽剤がこの被抽出物
に接触しやすく、かつ良好に槽外に通過できる構造であ
ることが好適である。材質としてはステンレス鋼が好ま
しいが、この点も特に限られるものではない。なお回転
による水等の抽剤の攪拌を一層良好にするためには回転
槽の外周壁に攪拌用の羽根を設けることもできる。
[0006] The rotary tank is usually connected to a stirring motor outside the tank through a rotating shaft, and is configured to rotate by rotation of the stirring motor. However, the rotating means is not particularly limited. The rotary tank may have any porous structure such as a punched metal, but preferably, the extractables collide with the rotation of the rotary tank, and at the same time, the extractant easily comes into contact with the extractables and is preferably removed from the tank. Preferably, it is a structure that can pass through. The material is preferably stainless steel, but this is not particularly limited. In order to further improve the stirring of the extractant such as water by rotation, a stirring blade may be provided on the outer peripheral wall of the rotating tank.

【0007】濾過体は必要に応じて採用すればよいが、
採用する場合は回転槽の内壁に沿って設置するものであ
れば差支えない。例えば濾布や濾紙等を使用することが
できる。また他に被抽出物を例えば袋状の濾過体内に充
填し、これを回転槽内に直接投入することもできる。
[0007] The filter may be adopted as needed.
In the case of adoption, any structure can be used as long as it is installed along the inner wall of the rotating tank. For example, filter cloth, filter paper, or the like can be used. In addition, it is also possible to fill the extract with, for example, a bag-shaped filter body, and to directly charge this into the rotary tank.

【0008】抽出槽は減圧可能な気密構造とすることが
好ましいが、その手段については特に限定されない。減
圧手段は例えば真空ポンプを用いることができる。真空
ポンプは抽出槽に直接併設してもよいが、外部手段とし
て設置することもできる。真空ポンプに連結する場合
は、抽出槽の上部に冷却器を設置し、この冷却器を通し
て吸気させることが好適である。なお冷却器で液化した
抽剤は、帰還パイプを設置すれば抽出時に抽出槽内に帰
還させることもでき、また濃縮時は外部に排出すること
もできる。なお必要に応じて、抽出槽に加熱手段を設置
することが好ましい。
[0008] The extraction tank preferably has an air-tight structure capable of reducing pressure, but the means is not particularly limited. As the pressure reducing means, for example, a vacuum pump can be used. The vacuum pump may be directly installed in the extraction tank, or may be installed as an external means. When connecting to a vacuum pump, it is preferable to install a cooler above the extraction tank and to draw air through this cooler. The extractant liquefied by the cooler can be returned to the extraction tank at the time of extraction by installing a return pipe, and can be discharged to the outside at the time of concentration. In addition, it is preferable to install a heating means in an extraction tank as needed.

【0009】[0009]

【作用】この発明は上述の通りであるので、例えば生薬
の裁断物からエキスを抽出させる場合、回転槽内に当該
裁断物を投入し、この回転槽を攪拌モーターで回転させ
ると、回転槽の回転ととともに、抽剤である水が渦巻き
状に攪拌され、さらに回転槽の遠心力が生薬の裁断物を
回転槽の壁面に濾過体を介して衝突させる。そして渦巻
き状に攪拌された水は、生薬の裁断物と接触後、回転槽
の孔を通じて抽出槽の壁面に衝突し、衝突後は回転槽の
遠心力で抽出槽の壁面を上昇し、その後抽出槽の上部壁
に衝突して再び回転槽内に送り込まれる。これを繰り返
すことで生薬の裁断物は接触量がきわめて大きくなり、
また遠心力による搾り出し作用が発揮されて極めて効率
よく抽出することができる。また濾過体を回転槽内壁に
配置した場合は、濾過作用も同時に行なうことができ
る。なお加熱手段を設け、減圧抽出した場合は抽出効率
は一層高まり、また濃縮も同時に行なうことができる。
The present invention is as described above. For example, when extracting an extract from a crude drug cut, the cut material is put into a rotary tank, and the rotary tank is rotated by a stirring motor. With the rotation, the water as the extractant is stirred in a spiral shape, and the centrifugal force of the rotary tank causes the cut material of the crude drug to collide with the wall surface of the rotary tank via the filter. Then, the water stirred in a spiral shape comes into contact with the cut material of the crude drug, collides with the wall of the extraction tank through the hole of the rotary tank, and after the collision, rises the wall of the extraction tank by the centrifugal force of the rotary tank and then extracts. It collides with the upper wall of the tank and is sent into the rotary tank again. By repeating this, the amount of contact with the cut crude drug becomes extremely large,
In addition, squeezing action by centrifugal force is exerted, and extraction can be performed very efficiently. When the filter is disposed on the inner wall of the rotary tank, a filtering operation can be performed at the same time. When a heating means is provided and extraction is performed under reduced pressure, the extraction efficiency is further enhanced, and concentration can be performed simultaneously.

【0010】[0010]

【実施例】図1はこの発明に係る固体抽出機の一実施例
を示す一部切欠正面図、図2は同平面図である。
1 is a partially cutaway front view showing an embodiment of a solid extractor according to the present invention, and FIG. 2 is a plan view thereof.

【0011】図において、1は減圧可能な気密構造の抽
出槽、2は抽出槽内に回転可能に設置された多孔構造の
回転槽である。抽出槽1は、図示の通り、抽出槽本体1
aと抽出槽蓋体1bからなり、抽出槽蓋体1bがアーム
3を軸に開閉できる構造となっている。回転槽2は抽出
槽1の下部に設置した攪拌モータ4に回転軸5を介して
連結されており、この攪拌モータ4の駆動によって回転
槽2が回転運動をする構成となっている。なおFは回転
槽2の内面に沿って配設した濾過体である。
In the drawing, reference numeral 1 denotes an extraction tank having an airtight structure capable of reducing pressure, and reference numeral 2 denotes a rotary tank having a porous structure rotatably installed in the extraction tank. The extraction tank 1 is, as shown, an extraction tank body 1.
a and the extraction tank lid 1b, and the extraction tank lid 1b has a structure that can be opened and closed around the arm 3. The rotary tank 2 is connected via a rotary shaft 5 to a stirring motor 4 installed at the lower part of the extraction tank 1, and the rotary tank 2 rotates by driving the stirring motor 4. F is a filter disposed along the inner surface of the rotary tank 2.

【0012】6は抽出槽1の外周に配設されたヒータで
あり、保温のためこのヒータ6の外周にさらに保温部材
7が設けられている。8は抽出槽蓋体1bの上方に設置
された冷却器であり、抽出槽蓋体1bの上部から真空ポ
ンプ9に至る配管10の途中に設置され、減圧抽出時に
気化した水蒸気を液化し、同じく配管10途中に設けら
れた帰還パイプPを通じて抽出槽1内へ帰還させること
としている。なお11は抽出槽蓋体1bに設置された連
成計、12は安全弁、13は分り窓、14はエアー抜き
バルブである。15は抽出槽1の下部側壁に設置した排
出バルブ、16は圧力スイッチ、17は攪拌モータ4、
ヒータ6及び真空ポンプを制御する操作盤である。
Reference numeral 6 denotes a heater disposed on the outer periphery of the extraction tank 1, and a heat retaining member 7 is further provided on the outer periphery of the heater 6 for keeping the temperature. Reference numeral 8 denotes a cooler installed above the extraction tank lid 1b, which is installed in the middle of a pipe 10 from the upper part of the extraction tank lid 1b to the vacuum pump 9, and liquefies the vaporized vapor at the time of vacuum extraction. The water is returned to the extraction tank 1 through a return pipe P provided in the middle of the pipe 10. In addition, 11 is a compound meter installed in the extraction tank lid 1b, 12 is a safety valve, 13 is a window, and 14 is an air vent valve. 15 is a discharge valve installed on the lower side wall of the extraction tank 1, 16 is a pressure switch, 17 is a stirring motor 4,
The operation panel controls the heater 6 and the vacuum pump.

【0013】この装置を用いて生薬の裁断物からそのエ
キスを抽出する場合は、原料である当該裁断物を水と共
に回転槽2内に投入し、抽出槽蓋体1bを閉めた後、制
御盤17において内圧、内温及び時間を所定条件に設定
し、滅菌処理を行なう。滅菌処理は圧力スイッチ16に
よる圧力制御と、ヒータ6による加熱で行なわれる。滅
菌処理後はエアー抜きバルブ14を開とし、抽出槽1内
を常圧にする。
When extracting the extract from the cut crude drug using this apparatus, the cut raw material is put into the rotary tank 2 together with water, and the extraction tank lid 1b is closed. At 17, internal pressure, internal temperature and time are set to predetermined conditions, and sterilization is performed. The sterilization process is performed by pressure control by the pressure switch 16 and heating by the heater 6. After the sterilization process, the air vent valve 14 is opened, and the inside of the extraction tank 1 is set to normal pressure.

【0014】次に攪拌モータ4を回転し、同時に真空ポ
ンプ9で減圧し、ヒータ6で加熱する。図3は攪拌モー
タ4稼動前の状態を示す概略図、図4は同稼動直後の状
態を示す概略図、図5は同稼動安定時の状態を示す概略
図、図6は同概略平面図である。なお18は生薬の裁断
物である。これらの一連の図に示す通り、攪拌モータ4
によって回転槽2を回転させると、回転槽2の遠心力に
よる攪拌作用により水は渦巻き状態で周囲に送り出さ
れ、その流れに応じて生薬の裁断物18は回転槽2の内
壁に濾過体Fを介して衝突する(図4参照)。その際抽
剤である水は、生薬の裁断物18と接触しながら濾過体
Fを通じて回転槽2の孔を通過し、抽出槽1と回転槽2
の間隙19内に移行すると同時に、回転槽2の攪拌作用
によって抽出槽1の壁面に衝突しながらを壁面を伝わっ
て上方に向かってのぼり揚る(図5及び図6参照)。そ
して回転槽2の上部までのぼり揚った水は回転槽2の上
方から滝状に回転槽2内に流れ落ち、再び回転槽2内に
おいて渦巻き状態で周囲に送り出され、生薬の裁断物1
8と接触する。抽出時ではこの状態が循環して繰り返し
行なわれることにより、水と生薬の裁断物18との接触
量がきわめて大きくなり、抽出効率が大幅に向上する。
なおこの抽出は真空ポンプ9で吸気し、かつ加熱状態で
行なわれるため、水は気化するが、冷却器8で液化され
るため、配管10から帰還パイプPを通じて当該水蒸気
は抽出槽1内に帰還される。
Next, the stirring motor 4 is rotated, and at the same time, the pressure is reduced by the vacuum pump 9 and heated by the heater 6. FIG. 3 is a schematic diagram showing a state before the stirring motor 4 is operated, FIG. 4 is a schematic diagram showing a state immediately after the operation, FIG. 5 is a schematic diagram showing a state when the operation is stable, and FIG. is there. Reference numeral 18 denotes a cut product of a crude drug. As shown in these series of figures, the stirring motor 4
When the rotary tank 2 is rotated by the centrifugal force of the rotary tank 2, the water is sent out in a spiral state to the surroundings, and according to the flow, the cut material 18 of the crude drug forms the filter body F on the inner wall of the rotary tank 2. (See FIG. 4). At that time, the water as the extractant passes through the hole of the rotary tank 2 through the filter F while being in contact with the cut material 18 of the crude drug, and the extraction tank 1 and the rotary tank 2
At the same time, while being colliding with the wall surface of the extraction tank 1 due to the stirring action of the rotary tank 2, it rises upward along the wall surface (see FIGS. 5 and 6). Then, the water that has risen to the upper part of the rotary tub 2 flows down into the rotary tub 2 from above the rotary tub 2 in a waterfall manner, is again sent out in a spiral state in the rotary tub 2, and is cut into crude drugs 1.
Contact 8 At the time of extraction, this state is circulated and repeated, so that the amount of contact between water and the cut crude drug 18 becomes extremely large, and the extraction efficiency is greatly improved.
Since this extraction is carried out in a vacuum pump 9 and carried out in a heated state, the water is vaporized, but is liquefied in the cooler 8, so that the water vapor returns to the extraction tank 1 through the return pipe P from the pipe 10. Is done.

【0015】減圧抽出の終了後、濃縮する場合は、この
帰還パイプPの排出口を槽外に向けるて水蒸気を回収す
る。また場合によっては真空ポンプ9で回収してもよ
い。
After the completion of the reduced pressure extraction, in the case of concentration, the outlet of the return pipe P is directed to the outside of the tank to collect steam. In some cases, it may be collected by a vacuum pump 9.

【0016】所定濃度のエキスが得られると、排出バル
ブ15を開け、この排出バルブ15から外部に取り出
す。なお排出する場合は攪拌モータを高速回転し、生薬
の裁断物18からさらにエキスを搾り出すことが好まし
い。
When an extract having a predetermined concentration is obtained, the discharge valve 15 is opened, and the extract is taken out from the discharge valve 15. In addition, when discharging, it is preferable to rotate the stirring motor at a high speed to further extract the extract from the cut crude drug 18.

【0017】ところでこの発明は上記の実施例に限定さ
れるものではない。特にその使用方法は一例であって、
必ずしも滅菌操作から減圧抽出を経て濃縮操作をとらな
くても差支えない。例えば常圧下で抽出することもでき
る。因みに水15リットルと原料である生薬750gを
回転槽2内に投入し、内温55℃に設定して、攪拌抽出
すると、15分間の抽出ではエキス濃度27.2%とな
り、30分では33.6%のエキス溶液が得られた。そ
してさらにこの抽出後の生薬について抽出を試みてみた
が、15分では1.55%のエキス濃度の溶液しか得ら
れず、60分では1.95%であった。このことによ
り、条件設定にもよるが、加熱下での減圧抽出ではさら
に迅速かつ高効率でエキスが回収できることが確認でき
る。
The present invention is not limited to the above embodiment. In particular, the usage is an example,
There is no problem if the concentration operation is not necessarily performed through the reduced pressure extraction from the sterilization operation. For example, it can be extracted under normal pressure. By the way, 15 liters of water and 750 g of a crude drug as a raw material are put into the rotary tank 2, the internal temperature is set to 55 ° C., and the extract is stirred and extracted. When the extract is extracted for 15 minutes, the extract concentration becomes 27.2%. A 6% extract solution was obtained. Further, extraction of the crude drug after the extraction was tried, but only a solution with an extract concentration of 1.55% was obtained in 15 minutes, and 1.95% in 60 minutes. This confirms that the extract can be recovered more quickly and efficiently by reduced pressure extraction under heating, depending on the condition setting.

【0018】なお上記の実施例は固体原料として生薬を
採用したが、他の食品物や飼料、工業原料など種々の固
体原料についても使用できることはいうまでもない。
In the above embodiment, crude drugs are used as solid raw materials. However, it goes without saying that various solid raw materials such as other foods, feeds, and industrial raw materials can be used.

【0019】[0019]

【発明の効果】以上の通りこの発明は、抽出槽内に被抽
出物が投入される多孔構造の回転槽が取り付けられた固
体抽出機であるため、回転槽の回転運動により流体が攪
拌されるとともに、遠心力がさらにこれに加わるため、
被抽出物の抽剤との接触量が従来に比して格段に向上
し、抽出効率を飛躍的にアップさせることができる。
As described above, the present invention is a solid extractor in which a rotary tank having a porous structure in which an extraction target is charged is mounted in an extraction tank, so that the fluid is stirred by the rotary motion of the rotary tank. At the same time, centrifugal force is added to this,
The amount of contact between the extract and the extractant is remarkably improved as compared with the related art, and the extraction efficiency can be dramatically increased.

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

【図1】この発明に係る固体抽出機の一実施例を示す一
部切欠正面図である。
FIG. 1 is a partially cutaway front view showing an embodiment of a solid extractor 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】攪拌モータの稼動前の状態を示す概略図であ
る。
FIG. 3 is a schematic diagram showing a state before a stirring motor is operated.

【図4】同稼動直後の状態を示す概略図である。FIG. 4 is a schematic diagram showing a state immediately after the operation.

【図5】同稼動安定時の状態を示す概略図である。FIG. 5 is a schematic diagram showing a state when the operation is stable.

【図6】同概略平面図である。FIG. 6 is a schematic plan view of the same.

【符号の説明】[Explanation of symbols]

1 抽出槽 2 回転槽 1 Extraction tank 2 Rotation tank

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 被抽出物が投入される多孔構造の回転槽
が抽出槽内に取り付けられ、前記回転槽と抽出槽との間
の間隙と前記回転槽の投入口とが連通されることによ
り、抽剤の循環路が形成された固体抽出機。
1. A rotary tank having a porous structure into which an object to be extracted is charged is mounted in an extraction tank, and a rotary tank is provided between the rotary tank and the extraction tank.
Is connected to the inlet of the rotary tank.
And a solid extractor in which a circulation path for the extractant is formed .
【請求項2】回転槽の内壁に濾過体を配設した請求項1
記載の固体抽出機。
2. The filter according to claim 1, wherein a filter is provided on the inner wall of the rotary tank.
A solid extractor as described.
【請求項3】抽出槽が加熱手段を備えた請求項1又は2
記載の固体抽出機。
3. The extraction tank according to claim 1, wherein the extraction tank has a heating means.
A solid extractor as described.
【請求項4】抽出槽を減圧可能な気密構造とし、減圧手
段を備えた請求項1、2又は3記載の固体抽出機。
4. The solid extractor according to claim 1, wherein the extraction tank has an airtight structure capable of reducing pressure, and is provided with a pressure reducing means.
JP4080038A 1992-04-01 1992-04-01 Solid extractor Expired - Lifetime JP2744546B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4080038A JP2744546B2 (en) 1992-04-01 1992-04-01 Solid extractor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (2)

Publication Number Publication Date
JPH05277303A JPH05277303A (en) 1993-10-26
JP2744546B2 true JP2744546B2 (en) 1998-04-28

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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69433759T2 (en) 1993-07-30 2005-03-31 Aruba International Pty. Ltd., Rocklea PLASMADELIPIDATIONSSYSTEM
JP3752640B2 (en) * 1997-04-15 2006-03-08 秀幸 西澤 Solid-liquid countercurrent extraction continuous separator
JP3675681B2 (en) * 1999-09-02 2005-07-27 株式会社サクション瓦斯機関製作所 Container moving device and chromatograph device
PT1641421T (en) * 2003-07-03 2019-03-27 Hdl Therapeutics Inc Methods and apparatus for creating particle derivatives of hdl with reduced lipid content
JP5553325B2 (en) * 2008-01-21 2014-07-16 国立大学法人鳥取大学 Natural polymer compound extraction and purification system
CN105031309A (en) * 2015-08-13 2015-11-11 杨大妹 Traditional Chinese medicine for curing dizziness
US11027052B2 (en) 2017-11-22 2021-06-08 HDL Therapuetics, Inc. Systems and methods for priming fluid circuits of a plasma processing system
EP3731814A4 (en) 2017-12-28 2021-09-29 HDL Therapeutics, Inc. Methods for preserving and administering pre-beta high density lipoprotein extracted from human plasma
CN114307249A (en) * 2021-12-30 2022-04-12 漯河医学高等专科学校 Centrifugal extraction device with solid-liquid separation function for pharmaceutical chemistry production

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59162902A (en) * 1983-03-05 1984-09-13 Sogo Insatsu Kogei Kk Plant and crude drug concentrating extractor
JP2731186B2 (en) * 1988-11-02 1998-03-25 株式会社東芝 Beverage extractor

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