JPS6216383A - Storage tank for suspension - Google Patents

Storage tank for suspension

Info

Publication number
JPS6216383A
JPS6216383A JP60148186A JP14818685A JPS6216383A JP S6216383 A JPS6216383 A JP S6216383A JP 60148186 A JP60148186 A JP 60148186A JP 14818685 A JP14818685 A JP 14818685A JP S6216383 A JPS6216383 A JP S6216383A
Authority
JP
Japan
Prior art keywords
suspension
concentration
storage tank
pipe
dispensing
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
JP60148186A
Other languages
Japanese (ja)
Inventor
晴仁 岡本
福原 二一
浜田 謙二郎
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP60148186A priority Critical patent/JPS6216383A/en
Publication of JPS6216383A publication Critical patent/JPS6216383A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分計〕 この発明は、懸濁液の貯槽に関する。[Detailed description of the invention] [Industrial usage total] The present invention relates to a suspension storage tank.

〔従来の技術〕[Conventional technology]

従来懸濁液を貯蔵する設備として貯槽が使われているが
、貯槽している懸濁液を目的のプロセスに供給するため
に、受入れ時と同じ濃度の懸濁液を払い出す必要がある
。しかし懸濁液は貯槽に貯蔵すると、その固体粒子が沈
降分離して貯槽内の懸濁液の下方の濃度が高くなり、そ
のままでは高濃度の懸濁液を払い出すことになる。その
ため払い出した懸濁液の輸送に支障を生じるばかりでな
く、懸濁液が供給されるプロセスの操作範囲から外れる
ことになる。
Conventionally, storage tanks have been used as equipment to store suspensions, but in order to supply the stored suspensions to the intended process, it is necessary to discharge the suspensions at the same concentration as when they were received. However, when the suspension is stored in a storage tank, the solid particles settle and separate, increasing the concentration of the suspension in the lower part of the storage tank. This not only causes problems in transporting the dispensed suspension, but also causes the suspension to be out of the operating range of the process to which it is supplied.

そこで従来の懸濁液の貯槽では、貯槽の下部から高濃度
の懸濁液を抜き出して貯槽上部にポンプにより循環し、
貯槽内の懸濁液を均一するようにしている。
Therefore, in conventional suspension storage tanks, a highly concentrated suspension is extracted from the bottom of the storage tank and circulated to the top of the storage tank using a pump.
The suspension in the storage tank is kept uniform.

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

上記のような従来の懸濁液の貯槽では、単に貯槽下部の
高濃度の懸濁液を貯槽の上部に循環しているだけである
から、貯槽内の懸濁液がどの程度に混合され、濃度の均
一が行われているか不明であり、かつ懸濁液の循環では
濃度の均一化が行われないという問題がある。
In the conventional suspension storage tank as described above, the highly concentrated suspension at the bottom of the tank is simply circulated to the top of the tank, so it is difficult to determine how well the suspension in the storage tank is mixed. There is a problem in that it is unclear whether the concentration is uniform, and that the concentration is not uniform when the suspension is circulated.

また、濃度の均一化が不十分で高濃度の懸濁液を払い出
すと、貯槽内には低濃度の懸濁液が残留し、それらの減
少が繰り返されると、払い出す懸濁液の濃度が不均一に
なる問題がある。
In addition, if the concentration is not sufficiently homogenized and high concentration suspension is discharged, low concentration suspension remains in the storage tank, and if these decreases repeatedly, the concentration of the discharged suspension will increase. There is a problem with unevenness.

〔問題点を解決するための手段〕[Means for solving problems]

この発明に係る懸濁液の貯槽は、貯槽本体の底部に貯溜
を設け、この貯溜に開口を有する払出し管と貯槽内の懸
濁液の液面のフロートサクションに連通ずる払出し管と
、それらの払出し管から抜き出した高濃度と低濃度の懸
濁液の混合手段と混合された懸濁液の濃度の計測装置を
設け、かつ混合された懸濁液の貯槽内への循環配管と外
部へ払い出す払出し管とを設け、計測装置での測定値に
より高濃度および/または低濃度の懸濁液の払出し量を
調節して混合された懸濁液の濃度が既知の受入れ時の濃
度になるようにして外部へ払い出すか、または貯槽内へ
循環するようにしたものである。
The suspension storage tank according to the present invention includes a storage tank provided at the bottom of the storage tank body, a delivery pipe having an opening in the storage tank, a delivery pipe communicating with a float suction on the liquid surface of the suspension in the storage tank, and a delivery pipe having an opening in the storage tank. A means for mixing high-concentration and low-concentration suspensions extracted from a dispensing pipe and a device for measuring the concentration of the mixed suspension are provided, and a circulation pipe for circulating the mixed suspension into the storage tank and discharging it to the outside are provided. A dispensing pipe is provided, and the dispensing amount of the high concentration and/or low concentration suspension is adjusted based on the measured value with the measuring device so that the concentration of the mixed suspension becomes the known concentration at the time of receiving. The water is then discharged to the outside or circulated into a storage tank.

〔作用〕[Effect]

この発明においては、貯槽に貯蔵する%S ’fA 液
(D固体粒子が分離しても、量も濃度の高い懸濁液と、
最も濃度の低い懸濁液を払出して混合し、この混合され
懸濁液の濃度を計測して払出し量を調節し、受入れ時の
濃度と同じにするから、受入れ時とほぼ同じ濃度懸濁液
を循環するか、または外部へ払い出すことができろ。
In this invention, the %S'fA liquid stored in the storage tank (D Even if the solid particles are separated, the suspension is high in volume and concentration,
The suspension with the lowest concentration is discharged and mixed, and the concentration of this mixed suspension is measured and the discharge amount is adjusted to make it the same as the concentration at the time of reception, so the suspension has almost the same concentration as at the time of reception. be able to circulate it or send it out.

〔実施例〕〔Example〕

第1図は乙の発明の一実施例の説明図である。 FIG. 1 is an explanatory diagram of an embodiment of the invention of B.

図において、(1)は貯槽、(2)は貯槽(1)の底部
であり、底部を傾斜させて断面が逆三角の底部貯槽(2
a)。
In the figure, (1) is the storage tank, and (2) is the bottom of the storage tank (1).
a).

(2b) 、 (2e)を形成している。(3)は貯槽
(1)の底部近傍に水平方向に配設された高濃度懸濁液
用の払出し管、(3m) 、 (3b) 、 (3c)
は払出し管に連通し、底部貯溜(2a) 、 (2b、
 (2c)に開口を有する垂直方向の払出し管、(4)
は貯槽(1)から外へ延びた払出し管(3)に設けたバ
ルブ、(5)は払出し管(3)に設けたラインミキシン
グ装置、(6)は高濃度懸濁液の払出しポンプ、(8)
はサービスタンク(8)に取付けられた混合装置、(8
b)はサービスタンク(8)に設けられた濃度計測袋′
   置である。
(2b) and (2e) are formed. (3) is a dispensing pipe for high concentration suspension arranged horizontally near the bottom of the storage tank (1), (3m), (3b), (3c)
are connected to the dispensing pipe, and the bottom reservoirs (2a), (2b,
(2c) a vertical dispensing pipe having an opening at (4);
(5) is a line mixing device installed in the dispensing pipe (3), (6) is a dispensing pump for high concentration suspension, ( 8)
is a mixing device attached to the service tank (8), (8
b) is the concentration measurement bag installed in the service tank (8)
It is a place.

(10)ば貯槽(1)内の懸fA液の液面(33)に浮
遊させであるフロートサクション、(11)はフロート
サクシフンに接続されているフレキシブルな払出し管で
、貯槽(1)から外へ伸びる払出し管(11)はサービ
スタンク(8)に連通しており、途中にバルブ(12)
(10) is a float suction that suspends the suspended fA liquid on the liquid surface (33) in the storage tank (1), and (11) is a flexible delivery pipe connected to the float suction pump from the storage tank (1). The discharge pipe (11) extending outside communicates with the service tank (8), and there is a valve (12) on the way.
.

(14)とポンプ(13)が設けられている。(14) and a pump (13) are provided.

(20)はサービスタンク(8)から’ay!A液を抜
き出す払出し管で、これは循環用配管(20a)と払出
し管(2Qb)に分岐され、循環用配管(20m)は先
端が貯槽(11の内の懸濁液の液面の付近に開口してお
り、払出し管(20b)は懸濁液を供給する目的のプロ
セスへノ配管に連通している。(21)は循環用配管(
20a)に設けた循環用のポンプ、(22)は払出し用
ポンプで、(23) 、 (24)はポンプ(21) 
、 (22)の前に設けたバルブである。
(20) says 'ay!' from the service tank (8). This is a dispensing pipe for withdrawing liquid A. This is branched into a circulation pipe (20a) and a discharging pipe (2Qb), and the tip of the circulation pipe (20m) is near the liquid level of the suspension in the storage tank (11). The discharge pipe (20b) is open and communicates with the pipe to the process for supplying the suspension.(21) is connected to the circulation pipe (20b).
20a) is the circulation pump, (22) is the dispensing pump, and (23) and (24) are the pumps (21).
, (22) is a valve provided before.

第2図は乙の発明の貯槽(1)に貯蔵された懸濁液の濃
度分布の経時変化の実験結果を示す線図であり、縦軸は
懸濁液の液面の高さ方向、横軸は懸濁液の濃度を示して
いる。図において、(30)は懸濁液の濃度分布曲線、
(31)は貯槽(1)に懸濁液を受は入れた時点での濃
度分布曲線(30)上の位置を表示している。また(3
2)は懸濁液を受入れた時点から日数が経過した払出し
時の懸濁液の濃度分布曲線(30)上の位置、(33)
は懸濁液の液面である。
Figure 2 is a diagram showing the experimental results of changes over time in the concentration distribution of the suspension stored in the storage tank (1) of B's invention, where the vertical axis is the height direction of the suspension liquid level, and the horizontal axis is The axis shows the concentration of the suspension. In the figure, (30) is the concentration distribution curve of the suspension;
(31) indicates the position on the concentration distribution curve (30) at the time when the suspension is received in the storage tank (1). Also (3
2) is the position on the concentration distribution curve (30) of the suspension at the time of dispensing after the number of days has passed since the suspension was received; (33)
is the liquid level of the suspension.

この濃度分布曲線(30)から、懸濁液の受入れ時にお
いては貯槽(1)内の懸濁液の液面(30)までの高さ
方向の濃度はほぼ均一であるが懸濁液の払出し時では、
懸濁液の液面高さ方向の底部に近い位置での濃度が太き
(なり、液面(33)に近い位置での濃度は著しく小さ
くなっている。
From this concentration distribution curve (30), it can be seen that when the suspension is received, the concentration in the height direction up to the liquid level (30) of the suspension in the storage tank (1) is almost uniform; At times,
The concentration at a position near the bottom of the suspension in the liquid level height direction is thick (becomes), and the concentration at a position close to the liquid level (33) is significantly small.

上記第1図に示すように構成された懸濁液の貯槽(1)
に、第2図に示すように濃度分布曲線(30)が経時変
化する懸濁液を受は入れた後払い出すには、以下の操作
をする。貯槽(1)の底部貯溜(2a) j (2b)
 。
Suspension storage tank (1) configured as shown in Figure 1 above
In order to receive and then discharge a suspension whose concentration distribution curve (30) changes over time as shown in FIG. 2, the following operation is performed. Bottom storage of storage tank (1) (2a) j (2b)
.

(2c)に貯蔵された高濃度懸濁液は、払出し管(3a
) 。
The high concentration suspension stored in (2c) is transferred to the dispensing pipe (3a).
).

(3b) 、 (3e)および(3)を通じてポンプ(
6)により抜き出され、ラインミキシング装置(5)で
混合してサービスタンク(8)に入れる。また貯槽(1
)内の懸濁液の液面(33)の低濃度懸濁液は、フロー
トサクシ9ンにより取り入れられて払出し管(11)を
通じてポンプ(13)により払出し、サービスタンク(
8)に入れる。
(3b), (3e) and (3) through the pump (
6), mixed by a line mixing device (5), and put into a service tank (8). Also storage tank (1
The low-concentration suspension at the liquid level (33) in the tank () is taken in by the float pump 9, discharged by the pump (13) through the discharge pipe (11), and then transferred to the service tank (
8).

このようにして、サービスタンク(8)に入れられた高
濃度および低濃度およびの懸濁液は、混合装置(8a)
で混合しながら濃度を均一化し、計測装置(8b)によ
り濃度を計測する。そしてその計測結果により、サービ
スタンク(8)内の濃度が受入れ時の既知の懸濁液の濃
度になるようにバルブ(4) 、 (71。
In this way, the high concentration and low concentration suspensions placed in the service tank (8) are transferred to the mixing device (8a).
The concentration is made uniform while mixing with a measuring device (8b), and the concentration is measured with a measuring device (8b). Based on the measurement results, the valves (4) and (71) are set so that the concentration in the service tank (8) becomes the known suspension concentration at the time of reception.

(12) 、 (14)の開度を調整する等して、サー
ビスタンク(8)に入れる高濃度の懸濁液の量を調整す
る。
(12) Adjust the opening degree of (14) to adjust the amount of highly concentrated suspension to be put into the service tank (8).

次いで、バルブ(23) 、 (24)を開いて、ポン
プ(22)によりサービスタンク(8)の懸濁液が払出
し管(20) 、 (20b)を通じて目的のプロセス
へ圧送される。
Then, the valves (23) and (24) are opened, and the suspension in the service tank (8) is pumped by the pump (22) to the target process through the discharge pipes (20) and (20b).

なお、上記したようにサービスタンク(8)で混合して
濃度を計測し、サービスタンク(8)の懸濁液の濃度が
貯槽(1)への受入れ時の濃度になるように、高濃度お
よび低濃度懸濁液へのサービスタンク(8)への払出し
量の関係を決めると、その条件を維持すれば、サービス
タンク(8)で混合しながら連続して貯槽(1)内の懸
濁液を受入れ時と同じ濃度で目的のプロセスに圧送する
ことができる。
As mentioned above, the mixture is mixed in the service tank (8) and the concentration is measured, and high concentration and Once the relationship between the amount of low-concentration suspension and the amount dispensed to the service tank (8) is determined, if the conditions are maintained, the suspension in the storage tank (1) will be continuously mixed while being mixed in the service tank (8). can be pumped to the desired process at the same concentration as when received.

また貯槽(1)内の懸濁液の濃度を均一化するには、受
入れ時とほぼ同じ濃度となった懸濁液を、バルブ(23
)を開きポンプ(21)によけサービスタンク(8)貯
槽(1)内の液面に循環させる操作を連続して行う。
In addition, in order to equalize the concentration of the suspension in the storage tank (1), the suspension that has almost the same concentration as when it was received must be pumped through the valve (23).
) is opened and the pump (21) is opened to circulate the liquid to the liquid level in the service tank (8) and storage tank (1).

その結果懸濁液を長時間貯蔵する場合にも、貯槽(1)
内の懸濁液濃度が均一化されるので、貯槽(1)底部の
高濃度懸濁液中の固体粒子が分離沈降して圧縮され、流
動不能になることがない。
As a result, even if the suspension is stored for a long time, the storage tank (1)
Since the concentration of the suspension in the storage tank (1) is made uniform, the solid particles in the highly concentrated suspension at the bottom of the storage tank (1) will not be separated and settled, compressed, and become unable to flow.

第3図はこの発明の他の実施例の説明図である。FIG. 3 is an explanatory diagram of another embodiment of the invention.

図において、(1)〜(5)、(8)〜(8a)、(1
0)〜(14) 、 (33)は第1図の実施例と同一
のものである。図において、(40)は払出し用のポン
プ(41)が設けられたサービスタンク(8)の払出し
管であり、先端は払出し管(3)に連通ずると共に、途
中にも分岐配管(42)が連通されている。(43)は
払出し管(3)に連通させた払出し管(40)と分岐管
(42)との間に設けられたポンプ、(44) 、 (
45)は払出し管(40)および分岐管(42)に取り
付けられたバルブ、(4B)は払出し管(3)に設けた
濃度計測装置である。貯槽(1)の外へ伸びた払出し管
(3)の先端は循環用配管(47)と払出し用配管(4
7a)に分岐され、循環用配管(47)は、先端開放口
が貯槽(1)内の懸濁液の液面(33)の付近に位置す
るようにして配管される。(48) 、 (49)は循
環用配管(47)および払出し用配管(47a)に取り
付けられたバルブである。
In the figure, (1) to (5), (8) to (8a), (1
0) to (14) and (33) are the same as the embodiment shown in FIG. In the figure, (40) is a discharge pipe of the service tank (8) equipped with a discharge pump (41), and the tip communicates with the discharge pipe (3), and there is also a branch pipe (42) in the middle. It is communicated. (43) is a pump provided between the dispensing pipe (40) and the branch pipe (42) which are communicated with the dispensing pipe (3);
45) is a valve attached to the dispensing pipe (40) and the branch pipe (42), and (4B) is a concentration measuring device provided in the dispensing pipe (3). The dispensing pipe (3) extending outside the storage tank (1) has a circulation pipe (47) and a dispensing pipe (4) at its tip.
7a), and the circulation pipe (47) is arranged so that the open end thereof is located near the liquid level (33) of the suspension in the storage tank (1). (48) and (49) are valves attached to the circulation pipe (47) and the discharge pipe (47a).

この実施例において、受入れ時の濃度とほぼ同じ濃度の
懸濁液を払い出すには次の操作をする。
In this example, the following operation is performed to dispense a suspension having approximately the same concentration as when received.

先ず底部貯溜(2m) 、 (2b) 、 (2e)か
ら払出し! (3a)(3b) 、 (3e)および(
3)を通じてポンプ(43)により高濃度懸濁液が抜き
出される。また低濃度懸濁液もフロートサクシリン(l
O)から払出し管(11)を通じてポンプ(13)より
抜き出してサービスタンク(81に入れ、混合装置(8
m)により混合して濃度を均一にする。そしてこの濃度
を均一にした低濃度懸濁液は、濃度計測装置で濃度を計
測され、ポンプ(41)により払出し管(40)から払
出し管(3)に流入して払出し管(3)内で高濃度と低
濃度の懸濁液が混合され、その濃度計測N(46)によ
り計測し、混合された懸濁液の濃度が受入れ時の濃度と
ほぼ同じになるように、高濃度および/または低濃度の
懸濁液の量をバルブ(4) 、 (44) 、 (42
)の開度により調整し、払出し管(47m)により目的
のプロセスに払い出される。
First, pay out from the bottom storage (2m), (2b), (2e)! (3a) (3b), (3e) and (
3) through which the highly concentrated suspension is extracted by a pump (43). In addition, low concentration suspensions can also be prepared using float succilin (l
It is extracted from the pump (13) through the discharge pipe (11) and put into the service tank (81).
m) to make the concentration uniform. The concentration of this uniformly concentrated low-concentration suspension is measured by a concentration measuring device, and the pump (41) flows from the dispensing pipe (40) into the dispensing pipe (3). The high and/or low concentration suspensions are mixed and measured by the concentration meter N (46), so that the concentration of the mixed suspension is approximately the same as the concentration at the time of reception. The amount of low concentration suspension is controlled by valves (4), (44), (42).
) is adjusted by the opening degree of the pipe (47m), and is delivered to the target process through the delivery pipe (47m).

また、貯槽(1)内の懸濁液の濃度を均一化するには、
上記の高濃度と低濃度の懸濁液を混合したものを循環用
パイプ(47)を通じて貯槽(1)内に戻す。
In addition, in order to equalize the concentration of the suspension in the storage tank (1),
The mixture of the above-mentioned high concentration and low concentration suspensions is returned to the storage tank (1) through the circulation pipe (47).

〔発明の効果〕〔Effect of the invention〕

この発明は以上説明したように、貯槽内で分離沈降する
固体粒子を含む懸濁液であっても、貯槽に受入れ時と同
じ濃度の懸濁液を払い出すことができ、しかも貯槽内り
と貯蔵する懸濁液の濃度を均一化することができるので
、長期貯蔵が可能となる効果がある。
As explained above, even if the suspension contains solid particles that separate and settle in the storage tank, the present invention can dispense the suspension at the same concentration as when it was received into the storage tank, and moreover, Since the concentration of the suspension to be stored can be made uniform, it has the effect of enabling long-term storage.

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

第1図はこの発明の一実施例の説明図、第2図は懸濁液
の濃度分布曲線の線図、第3図はこの発明の他の実施例
の説明図である。 図において、(1)は貯槽、(2)は貯槽の底部、(3
1゜(3a)、 (3b)、 (3c)、 (11)、
 (20)、 (20a)、 (40)、 (47m)
は払出し管、14)、 (7)、 (12)、 (14
)、 (23)、 (44)、 (45)。 (48) (49Jはバルブ、(5)はラインミキシン
グ装置、(61、(13) 、 (21) 、 (22
) 、 (41) 、 (43)はポンプ、(8)はサ
ービスタンク、(8a) 、 (46)は濃度計測装置
、(10)はフロートサクシコンである。 代理人 弁理士 佐 藤 正 年 第2図 4m(イ←高) 第3 図
FIG. 1 is an explanatory diagram of one embodiment of this invention, FIG. 2 is a diagram of a concentration distribution curve of a suspension, and FIG. 3 is an explanatory diagram of another embodiment of this invention. In the figure, (1) is the storage tank, (2) is the bottom of the storage tank, and (3) is the bottom of the storage tank.
1゜(3a), (3b), (3c), (11),
(20), (20a), (40), (47m)
is the discharge pipe, 14), (7), (12), (14
), (23), (44), (45). (48) (49J is a valve, (5) is a line mixing device, (61, (13), (21), (22)
), (41), and (43) are pumps, (8) is a service tank, (8a), (46) are concentration measuring devices, and (10) is a float succincon. Agent Patent Attorney Tadashi Sato Figure 2 4m (A ← High) Figure 3

Claims (1)

【特許請求の範囲】 (a)底部に貯溜を設けた懸濁液を貯蔵する貯槽と、 (b)上記貯溜に開口部を有する払出し管と、(c)上
記貯槽に貯蔵した懸濁液の液面のフロートサクションお
よびこれに連通する払出し管と、(d)上記(B)およ
び(C)の払出し管で払い出したそれぞれの懸濁液を混
合する手段と、(e)上記(d)で混合した懸濁液の濃
度計測装置と、 (f)上記(d)で混合した懸濁液を上記貯槽へ循環す
る配管外部へ払い出す配管と、 からなり上記(e)で計測された濃度から、上記(d)
で混合された懸濁液の濃度が貯槽に受入れ時の懸濁液の
濃度になるように上記(B)および(C)で払い出す懸
濁液の量を調整して、上記貯槽に受入れ時とほぼ同じ濃
度の懸濁液を外部へ払い出すか、または、上記貯槽内へ
循環するようにした懸濁液の貯槽。
[Scope of Claims] (a) A storage tank with a reservoir at the bottom for storing the suspension; (b) a dispensing pipe having an opening in the reservoir; (c) a discharge pipe for storing the suspension stored in the storage tank; A float suction on the liquid surface and a dispensing pipe communicating therewith; (d) means for mixing each of the suspensions discharged by the dispensing pipes in (B) and (C) above; (e) in (d) above; A device for measuring the concentration of the mixed suspension; (f) a pipe for discharging the mixed suspension in (d) above to the outside of the pipe circulating to the storage tank, and measuring the concentration measured in (e) above. , above (d)
Adjust the amount of the suspension to be dispensed in (B) and (C) above so that the concentration of the mixed suspension is the same as the concentration of the suspension when received into the storage tank. A suspension storage tank in which a suspension having approximately the same concentration as the liquid is discharged to the outside or circulated into the storage tank.
JP60148186A 1985-07-08 1985-07-08 Storage tank for suspension Pending JPS6216383A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60148186A JPS6216383A (en) 1985-07-08 1985-07-08 Storage tank for suspension

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60148186A JPS6216383A (en) 1985-07-08 1985-07-08 Storage tank for suspension

Publications (1)

Publication Number Publication Date
JPS6216383A true JPS6216383A (en) 1987-01-24

Family

ID=15447164

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60148186A Pending JPS6216383A (en) 1985-07-08 1985-07-08 Storage tank for suspension

Country Status (1)

Country Link
JP (1) JPS6216383A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003512212A (en) * 1999-10-29 2003-04-02 ヴィデオジェット テクノロジーズ インコーポレイテッド Circulation system and method for mixing inkjet inks
JP2021531879A (en) * 2018-07-25 2021-11-25 アプライド ライフサイエンシズ アンド システムズ エルエルシー Circulation system and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003512212A (en) * 1999-10-29 2003-04-02 ヴィデオジェット テクノロジーズ インコーポレイテッド Circulation system and method for mixing inkjet inks
JP2021531879A (en) * 2018-07-25 2021-11-25 アプライド ライフサイエンシズ アンド システムズ エルエルシー Circulation system and method

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