JPS61254204A - Apparatus for separating liquid - Google Patents
Apparatus for separating liquidInfo
- Publication number
- JPS61254204A JPS61254204A JP9761985A JP9761985A JPS61254204A JP S61254204 A JPS61254204 A JP S61254204A JP 9761985 A JP9761985 A JP 9761985A JP 9761985 A JP9761985 A JP 9761985A JP S61254204 A JPS61254204 A JP S61254204A
- Authority
- JP
- Japan
- Prior art keywords
- stock solution
- holes
- solution
- raw solution
- flat plate
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は各種の液体を半透過性のセラミック板により限
外濾過あるいは精密濾過する液体分離装置に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a liquid separation device that performs ultrafiltration or precision filtration of various liquids using a semi-permeable ceramic plate.
(従来の技術)
従来から食品、医薬、化学等の分野において液体を限外
濾過あるいは精密濾過するためには、高分子膜のような
膜モジュールや多孔質金属管、セラミック管のような管
状モジュールを濾過体として用いた液体分離装置が用い
られている。ところが、例えば特公昭52−10113
号公報、特公昭53−35552号公報に示されるよう
な高分子膜を用いた従来の液体分離装置は高分子の特性
上から耐熱性、耐薬品性、耐酸及び耐アルカリ性に劣る
うえに高分子膜が微生物に侵食されたり液中の粒子によ
って削られて損傷し易い欠点があり、120〜130℃
の蒸気殺菌が必要とされる食品、医薬等の分野には用い
ることができない場合があった。また、管状モジュール
を用いたもののうち特公昭58−30305号公報に示
されるように原液を外側から供給する外圧型のものは液
が均一に流れないため、使用中に有効濾過面積が減少し
たり微生物汚染を生ずることがある欠点があり、逆に原
液を内側から供給する内圧型のものは膜性能を維持する
ためには原液流量がたくさんいるので動力費が大となる
うえ、管の内径によって規定される有効濾過面積を大き
く取ることができない欠点があった。(Prior art) Conventionally, in order to perform ultrafiltration or precision filtration of liquids in the fields of food, medicine, chemistry, etc., membrane modules such as polymer membranes and tubular modules such as porous metal tubes and ceramic tubes have been used. A liquid separation device using a filter as a filter is used. However, for example,
Conventional liquid separation devices using polymer membranes, such as those shown in Japanese Patent Publication No. 53-35552, have poor heat resistance, chemical resistance, acid resistance, and alkali resistance due to the characteristics of polymers. The disadvantage is that the membrane is easily damaged by being eroded by microorganisms or scraped by particles in the liquid.
In some cases, it could not be used in fields such as food and medicine that require steam sterilization. In addition, among those using tubular modules, in the external pressure type that supplies the stock solution from the outside as shown in Japanese Patent Publication No. 58-30305, the liquid does not flow uniformly, so the effective filtration area may decrease during use. The drawback is that it may cause microbial contamination, and on the other hand, internal pressure types that supply the stock solution from the inside require a large flow rate of stock solution to maintain membrane performance, resulting in high power costs, and depending on the inner diameter of the tube. There was a drawback that the specified effective filtration area could not be set large.
(発明が解決しようとする問題点)
本発明はこのような従来の問題点を解決して、耐熱性、
耐薬品性等に優れ、液の停滞による微生物の繁殖や有効
濾過面積の減少がなく、圧力損失が小で動力費が安い液
体分離装置を目的として完成されたものである。(Problems to be solved by the invention) The present invention solves these conventional problems and improves heat resistance,
It was developed for the purpose of being a liquid separation device that has excellent chemical resistance, no growth of microorganisms due to liquid stagnation, no reduction in effective filtration area, low pressure loss, and low power costs.
(問題点を解決するための手段)
本発明は原液供給孔及び原液流出孔を備えた多孔質のセ
ラミック平板と、該セラミック平板の一側面に位置する
原液側スペーサと、該セラミック平板の反対側の側面に
位置し透過液排出手段を備えた透過液側スペーサとを、
多数枚積層して一体化したことを特徴とするものである
。(Means for Solving the Problems) The present invention includes a porous ceramic flat plate having a stock solution supply hole and a stock solution outflow hole, a stock solution side spacer located on one side of the ceramic plate, and a spacer on the opposite side of the ceramic plate. a permeate-side spacer located on the side surface and equipped with a permeate discharge means;
It is characterized by having multiple layers laminated and integrated.
(実施例)
次に本発明を図示の実施例によって詳細に説明すると、
第1図及び第2図に示す第1の実施例において(1)は
平均細孔径が10人〜2μmで厚みが0.5〜5鰭のセ
ラミック微粒子の焼結体よりなる均質な多孔質のアルミ
ナ系、ジルコニア系等のセラミック平板、(2)は該セ
ラミック平板(1)の−側面に位置する原液側スペーサ
、(3)はセラミック平板fl)の反対側の側面に位置
する透過液側スペーサであって、これらの3種類の板が
固定側の端板(4)と締付用シリンダ(5)によって加
圧される可動側の端板(6)との間に多数枚積層され加
圧一体化されている。セラミック平板(11は第2図に
示されるようにその下端付近に原液供給孔(7)を備え
、またその上端付近に原液流出孔(8)を備えている。(Example) Next, the present invention will be explained in detail with reference to illustrated examples.
In the first embodiment shown in FIGS. 1 and 2, (1) is a homogeneous porous body made of a sintered body of ceramic fine particles with an average pore diameter of 10 to 2 μm and a thickness of 0.5 to 5 fins. Ceramic flat plate of alumina type, zirconia type, etc., (2) is a stock solution side spacer located on the negative side of the ceramic flat plate (1), (3) is a permeated liquid side spacer located on the opposite side of the ceramic flat plate (fl) A large number of these three types of plates are stacked between the end plate (4) on the fixed side and the end plate (6) on the movable side which is pressurized by the tightening cylinder (5). It is integrated. As shown in FIG. 2, the ceramic flat plate (11) has a stock solution supply hole (7) near its lower end, and a stock solution outflow hole (8) near its top end.
これらの原液供給孔(7)及び原液流出孔(8)の個数
は1個でも複数でもよく、またその形状は円形、長円形
等の任意の形状とすることができる。またその周辺部分
は液のしみ込みを避けるために無機材料等によりシーリ
ングしておくことが好ましい。原液側スペーサ(2)は
天然ゴム、ブチルゴム、ウレタンゴム等のゴム、テフロ
ン系、ポリエチレン系、ポリプロピレン系等の合成樹脂
のようなシール性のある材料からなるもので、例えば原
液の流れる方向、即ち前記の原液供給孔(7)から原液
流出孔(8)に向かう方向に延びるリブ(9)を備え、
リブ(9)及び周縁部側面をセラミック平板(1)の−
側面に密着させてセラミック平板(11の片側に原液供
給用空間(10)を形成するものである。一方、透過液
側スペーサ(3)も原液側スペーサ(2)と同様なゴム
、合成樹脂等のようなシール性のある材料からなるもの
で、その下端付近には前記のセラミック平板!11の原
液供給孔(ηに連通ずる透孔(11)を備え、その上端
付近には原液流出孔(8)に連通ずる透孔(12)を備
えている。また透過液側スペーサ(3)はその中央部に
セラミック平板(11に作用する偏圧を受けるためのリ
ブ(13)を備えるとともにセラミック平板(1)との
間に形成される透過液排出用空間(14)内に流出した
透過液を下方へ排出するためのバイブ状の透過液排出手
段(15)を備えている。リブ(9)及びリブ(13)
の方向は任意であるが、リブ(13)を図示のように横
リプとしたときには各リブ(13)にも透過液排出用の
透孔(16)を透設しておくものとする。なお(17)
は透過液側スペーサ(3)の透孔(12)とのみ連通ず
る連通孔(18)を備えた不透過性の中間板であり、こ
の中間板(17)を介在させつつ原液側スペーサ(2)
とセラミック平板(1)と透過液側スペーサ(3)とか
らなるユニットが多数ユニット積層されるものである。The number of these stock solution supply holes (7) and stock solution outflow holes (8) may be one or more, and the shape thereof may be any shape such as circular or oval. Further, it is preferable that the surrounding area is sealed with an inorganic material or the like to prevent liquid from seeping in. The stock solution side spacer (2) is made of a material with sealing properties such as rubber such as natural rubber, butyl rubber, or urethane rubber, or synthetic resin such as Teflon, polyethylene, or polypropylene. A rib (9) extending in a direction from the stock solution supply hole (7) to the stock solution outflow hole (8),
The rib (9) and peripheral side surface of the ceramic flat plate (1)
A space (10) for supplying the stock solution is formed on one side of the ceramic flat plate (11) by being brought into close contact with the side surface.On the other hand, the permeate side spacer (3) is also made of rubber, synthetic resin, etc. similar to the stock solution side spacer (2). It is made of a sealing material such as, and near its lower end is provided with a through hole (11) that communicates with the stock solution supply hole (η) of the ceramic flat plate 11 described above, and near its upper end is a stock solution outflow hole (11). The permeated liquid side spacer (3) is provided with a rib (13) in the center thereof for receiving the biased pressure acting on the ceramic flat plate (11). (1) is provided with a vibrator-shaped permeate discharge means (15) for discharging downward the permeate that has flowed into the permeate discharge space (14) formed between the rib (9) and the rib (9). and ribs (13)
Although the direction of the ribs (13) is arbitrary, when the ribs (13) are horizontally ribbed as shown, each rib (13) is also provided with a through hole (16) for discharging the permeated liquid. Note (17)
is an impermeable intermediate plate provided with a communication hole (18) that communicates only with the through hole (12) of the permeated liquid side spacer (3), and the undiluted liquid side spacer (2) is )
A large number of units consisting of a ceramic flat plate (1) and a permeated liquid side spacer (3) are stacked.
以上に説明した第1の実施例の液体分離装置は、一方の
端板(6)の原液供給ヘッダ(19)から濾過されるべ
き原液を1〜10kg/−程度の圧力で供給すれば、原
液は透孔(11)、原液供給孔(7)を経てセラミンク
平板(1)の−側面に位置する原液側スペーサ(2)の
原液供給用空間(10)に流入し、その一部は多孔質の
セラミック平板(1)によって濾過されて透過液のみが
反対側の透過液側スペーサ(3)の透過液排出用空間(
14)に入りその下部の透過液排出手段(15)から下
方へ排出される。図示のように原液側スペーサ(2)は
その両側にセラミック平板fi+を備えているのでこの
濾過作用は2枚のセラミック平板(1)により同時に行
われることとなる。また、原液の残部はセラミック平板
illの原液流出孔(8)、透孔(12)、中間板(1
7)の連通孔(18)を経て隣接するユニットへ入り、
同様に濾過が行われることとなる第3図、第4図に示す
第2の実施例はセラミック平板(11と原液側スペーサ
(2)とは第1の実施例と同一であるが、透過液側スペ
ー廿(3)を繊維や石綿のような多孔質の材料からなる
平板としたものである。第1の実施例においては透過液
排出用空間(14)に流出した透過液がパイプ状の透過
液排出手段(15)から外部へ排出されるに対し、本実
施例においては透過液は多孔質の透過液側スペーサ(3
)の内部の細孔を流れてその下端から下方へ滴下する。The liquid separator of the first embodiment described above can be used by supplying the undiluted liquid to be filtered from the undiluted liquid supply header (19) of one end plate (6) at a pressure of about 1 to 10 kg/-. flows through the through hole (11) and the stock solution supply hole (7) into the stock solution supply space (10) of the stock solution side spacer (2) located on the negative side of the ceramic plate (1), and a part of it is porous. Only the permeated liquid is filtered by the ceramic flat plate (1) of the permeate discharge space (
14) and is discharged downward from the permeate discharge means (15) located below. As shown in the figure, the stock solution side spacer (2) is provided with ceramic flat plates fi+ on both sides, so that this filtration action is performed simultaneously by the two ceramic flat plates (1). In addition, the remaining part of the undiluted solution is stored in the undiluted solution outflow hole (8) of the ceramic flat plate ill, the through hole (12), and the intermediate plate (1).
7) enters the adjacent unit through the communication hole (18),
In the second embodiment shown in FIGS. 3 and 4, in which filtration is performed in the same way, the ceramic flat plate (11) and the stock solution side spacer (2) are the same as in the first embodiment, but the permeated liquid is The side space (3) is a flat plate made of a porous material such as fiber or asbestos.In the first embodiment, the permeate flowing into the permeate discharge space (14) is drained into a pipe-shaped pipe. While the permeate is discharged to the outside from the permeate discharge means (15), in this embodiment the permeate is discharged from the porous permeate side spacer (3).
) and drips downward from its lower end.
このために透過液側スペーサ(3)の下端は図示のよう
にセラミック平板(11等よりも下方へ長く延長されて
この部分が通過液排出手段(15)として作用するよう
にされている。また、透過液側スペーサ(3)に透設さ
れた透孔(11)、(12)の周囲はその内部を流れる
原液が透過液と混合することを防止するためにシール材
(20)によりシーリングしておくものとする。上記の
実施例においては、セラミック平板(1)はセラミック
微粒子の焼結体よりなる均質な単層のものとしたが、平
均細孔径0.2〜20μmで厚み1〜5鶴のセラミック
粒子の焼結体よりなる中心層と、平均細孔径が10人〜
2μmで厚み1μm % I nのセラミック微粒子の
焼結体よりなる表面層とからなる複層式のものとしても
よい。For this purpose, the lower end of the permeate side spacer (3) is extended downward longer than the ceramic flat plate (11, etc.) as shown in the figure, so that this part acts as a permeate liquid discharge means (15). The surroundings of the through holes (11) and (12) provided in the permeated liquid side spacer (3) are sealed with a sealing material (20) to prevent the stock liquid flowing inside them from mixing with the permeated liquid. In the above example, the ceramic flat plate (1) was a homogeneous single layer made of a sintered body of ceramic fine particles, but the ceramic plate (1) had an average pore diameter of 0.2 to 20 μm and a thickness of 1 to 5 μm. The center layer is made of a sintered body of Tsuru ceramic particles, and the average pore diameter is 10 ~
It may also be of a multi-layer type, comprising a surface layer of 2 μm and a sintered body of ceramic fine particles having a thickness of 1 μm % In.
また、原液側スペーサ(2)と透過液側スペーサ(3)
はセラミック平板(1)の側面に接着されたものであっ
ても、またライニングやコーティング法によりセラミッ
ク平板(11の表面に一体的に形成されたちのとしでも
よい。更にまた、セラミック平板fll自体に原液供給
孔(7)や原液流出孔(8)を設ける代りに、第5図に
示すようにセラミック平板(11を合成樹脂、ゴム、金
属等からなる枠体(21)で囲われたものとして、この
枠体(21)に原液供給孔(7)や原液流出孔(8)を
透設してもよい。In addition, the stock solution side spacer (2) and the permeate side spacer (3)
may be glued to the side surface of the ceramic flat plate (1), or may be integrally formed on the surface of the ceramic flat plate (11) by lining or coating. Instead of providing an undiluted solution supply hole (7) and an undiluted solution outflow hole (8), a ceramic flat plate (11) surrounded by a frame (21) made of synthetic resin, rubber, metal, etc. as shown in Fig. 5 is used. The frame body (21) may be provided with a stock solution supply hole (7) and a stock solution outflow hole (8).
(作用)
このように構成されたものは多孔質のセラミック平板(
1)を濾過体として原液の限外濾過あるいは精密濾過を
行うものであることは前述のとおりであるが、従来の高
分子膜を用いたものとは異なり耐熱性に優れるため高温
反応系に用いることができ、また120〜130℃の蒸
気殺菌を行うこともできるので食品工業や医薬品工業に
も用いることができる。更にセラミック平板(1)は有
機溶剤等に対する耐薬品性、耐酸及び耐アルカリ性、耐
微生物性に優れる利点があり、また洗浄による目詰りの
回復が容易で長期間安定した機能を発揮できるものであ
る。また、本発明の液体分離装置は、原液は原液側スペ
ーサ(2)によってセラミック平板(11の全面に供給
されて濾過され、透過液がその反対側の側面に位置する
透過液側スペーサ(3)に流入するので外圧型の管状モ
ジュールのような偏流を生ずることがなく、常に広い有
効濾過面積を維持することができ、従って液の停滞がな
くまた透過流量に対する原液流量を少なく出来るため内
圧型の管状モジュールに比較して動力費は著しく安価な
ものとなる。なお、セラミック平板(1)は焼成品であ
るために肉厚に多少の誤差が不可避的に生じ、多数枚を
積層して締付用シリンダ(5)によって強く締付けた際
に偏圧により割れる危険性が考えられるが、本発明にお
いてはセラミック平板(1)の両側面に原液側スペーサ
(2)と透過液側スペーサ(3)とが置かれてセラミッ
ク平板(11の肉厚誤差を吸収するうえ、実施例のよう
に原液側スペーサ(2)と透過液側スベー4(3)とに
リブ(9)、(13)を設けておけば、これらのリブ(
9)、(13)がセラミック平板(1)の中央部分にも
接して締付圧力の均等分散を図り、セラミック平板(1
1が割れるおそれを防止することができるものである。(Function) The device configured in this way is a porous ceramic flat plate (
As mentioned above, 1) is used to perform ultrafiltration or precision filtration of the stock solution as a filter, but unlike those using conventional polymer membranes, it has excellent heat resistance and is therefore used in high-temperature reaction systems. It can also be used in the food industry and pharmaceutical industry because it can also be steam sterilized at 120 to 130°C. Furthermore, the ceramic flat plate (1) has the advantage of being excellent in chemical resistance to organic solvents, acid and alkali resistance, and microbial resistance, and it is also easy to recover from clogging by cleaning and can exhibit stable functionality for a long period of time. . Further, in the liquid separation device of the present invention, the stock solution is supplied to the entire surface of the ceramic flat plate (11) and filtered by the stock solution side spacer (2), and the permeate is placed on the opposite side surface of the permeate side spacer (3). Because it flows into the tube, it does not cause uneven flow unlike the external pressure type tubular module, and it is possible to always maintain a wide effective filtration area.Therefore, there is no stagnation of liquid, and the flow rate of the raw liquid can be reduced relative to the permeation flow rate, so the internal pressure type The power cost is significantly lower than that of a tubular module.Since the ceramic flat plate (1) is a fired product, there will inevitably be some variation in wall thickness, so it is necessary to stack a large number of plates and tighten them. There is a risk of cracking due to uneven pressure when strongly tightened with the cylinder (5), but in the present invention, spacers on the undiluted solution side (2) and spacers on the permeate side (3) are provided on both sides of the ceramic flat plate (1). In addition to absorbing the thickness error of the ceramic flat plate (11), ribs (9) and (13) are provided on the stock solution side spacer (2) and the permeate side spacer 4 (3) as in the example. If you keep these ribs (
9) and (13) are also in contact with the central part of the ceramic flat plate (1) to evenly distribute the tightening pressure.
1 can be prevented from breaking.
(発明の効果)
本発明は以上の説明からも明らかなように、高分子膜モ
ジュールを用いたものと比較して耐熱性、耐薬品性、耐
酸及び耐アルカリ性等に優れ、また外圧型の管状モジュ
ールを用いたものに比較して有効濾過面積の減少や液の
停滞による微生物の繁殖がなく、更に内圧型の管状モジ
ュールを用いたものに比較して単位流量に対する濾過に
使用される流量の比率が高いので原液流量を少なくする
ことができ、動力費を安価にすることができるものであ
る。よって本発明は従来の液体分離装置の問題点を一掃
したものとして、産業の発展に寄与するところは極めて
大である。(Effects of the Invention) As is clear from the above description, the present invention has excellent heat resistance, chemical resistance, acid resistance, alkali resistance, etc. compared to those using polymer membrane modules, and also has an external pressure type tubular shape. Compared to those using modules, there is no reduction in the effective filtration area and no proliferation of microorganisms due to liquid stagnation, and the ratio of flow rate used for filtration to unit flow rate is lower compared to those using internal pressure type tubular modules. Since this is high, the flow rate of the stock solution can be reduced and the power cost can be reduced. Therefore, the present invention eliminates the problems of conventional liquid separators and greatly contributes to the development of industry.
第1図は本発明の第1の実施例を示す断面図、第2図は
その分解斜視図、第3図は本発明の第2の実施例を示す
断面図、第4図はその分解斜視図、第5図は本発明の第
3の実施例のセラミック平板を示す一部切欠斜視図であ
る。
(1):セラミック平板、(2):原液側スペーサ、(
3):透過液側スペーサ、(7):原液供給孔、(8)
;原液流出孔、(9):リブ、(11)、(1,2):
透孔、(13):リブ(15) :透過液排出手段。Fig. 1 is a sectional view showing a first embodiment of the present invention, Fig. 2 is an exploded perspective view thereof, Fig. 3 is a sectional view showing a second embodiment of the invention, and Fig. 4 is an exploded perspective view thereof. FIG. 5 is a partially cutaway perspective view showing a ceramic flat plate according to a third embodiment of the present invention. (1): Ceramic flat plate, (2): Stock solution side spacer, (
3): Permeate side spacer, (7): Stock solution supply hole, (8)
; Stock solution outflow hole, (9): Rib, (11), (1,2):
Through hole (13): Rib (15): Permeated liquid discharge means.
Claims (1)
孔質のセラミック平板(1)と、該セラミック平板(1
)の一側面に位置する原液側スペーサ(2)と、該セラ
ミック平板(1)の反対側の側面に位置し透過液排出手
段(15)を備えた透過液側スペーサ(3)とを、多数
枚積層して一体化したことを特徴とする液体分離装置。 2、原液供給孔(7)がセラミック平板(1)の一端部
に設けられ、原液流出孔(8)が対向する他端部に設け
られたものである特許請求の範囲第1項記載の液体分離
装置。 3、原液側スペーサ(2)と透過液側スペーサ(3)の
いずれか一方又は双方がリブ(9)、(13)を備えた
ものである特許請求の範囲第1項又は第2項記載の液体
分離装置。 4、透過液側スペーサ(3)がセラミック平板(1)の
原液供給孔(7)及び原液流出孔(8)に連通する透孔
(11)、(12)を備えたものである特許請求の範囲
第1項又は第2項又は第3項記載の液体分離装置。 5、セラミック平板(1)が平均細孔径が比較的大きい
中心層と平均細孔径が比較的小さい表面層からなるもの
である特許請求の範囲第1項又は第2項又は第3項又は
第4項記載の液体分離装置。[Claims] 1. A porous ceramic flat plate (1) equipped with a stock solution supply hole (7) and a stock solution outflow hole (8);
), and a permeate side spacer (3) located on the opposite side of the ceramic plate (1) and provided with a permeate discharge means (15). A liquid separation device characterized by being integrated by laminating layers. 2. The liquid according to claim 1, wherein the stock solution supply hole (7) is provided at one end of the ceramic flat plate (1), and the stock solution outflow hole (8) is provided at the opposite end. Separation device. 3. According to claim 1 or 2, either one or both of the undiluted liquid side spacer (2) and the permeated liquid side spacer (3) are provided with ribs (9) and (13). Liquid separation equipment. 4. The permeate side spacer (3) is provided with through holes (11) and (12) communicating with the stock solution supply hole (7) and stock solution outflow hole (8) of the ceramic flat plate (1). A liquid separation device according to scope 1, 2, or 3. 5.Claim 1 or 2 or 3 or 4, wherein the ceramic flat plate (1) consists of a central layer with a relatively large average pore diameter and a surface layer with a relatively small average pore diameter. Liquid separation device as described in section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9761985A JPS61254204A (en) | 1985-05-07 | 1985-05-07 | Apparatus for separating liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9761985A JPS61254204A (en) | 1985-05-07 | 1985-05-07 | Apparatus for separating liquid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61254204A true JPS61254204A (en) | 1986-11-12 |
Family
ID=14197215
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9761985A Pending JPS61254204A (en) | 1985-05-07 | 1985-05-07 | Apparatus for separating liquid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61254204A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001518381A (en) * | 1997-09-26 | 2001-10-16 | バッテル・メモリアル・インスティチュート | Microchannel laminated mass exchanger and manufacturing method |
-
1985
- 1985-05-07 JP JP9761985A patent/JPS61254204A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001518381A (en) * | 1997-09-26 | 2001-10-16 | バッテル・メモリアル・インスティチュート | Microchannel laminated mass exchanger and manufacturing method |
JP2008207178A (en) * | 1997-09-26 | 2008-09-11 | Battelle Memorial Inst | Lamination layer-type microchannel device |
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