JPH0557008B2 - - Google Patents
Info
- Publication number
- JPH0557008B2 JPH0557008B2 JP60146700A JP14670085A JPH0557008B2 JP H0557008 B2 JPH0557008 B2 JP H0557008B2 JP 60146700 A JP60146700 A JP 60146700A JP 14670085 A JP14670085 A JP 14670085A JP H0557008 B2 JPH0557008 B2 JP H0557008B2
- Authority
- JP
- Japan
- Prior art keywords
- section
- filtration
- drying
- container
- solids
- 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
Links
- 238000001914 filtration Methods 0.000 claims description 52
- 238000001035 drying Methods 0.000 claims description 51
- 239000007787 solid Substances 0.000 claims description 29
- 239000000463 material Substances 0.000 claims description 13
- 238000005192 partition Methods 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 8
- 230000002093 peripheral effect Effects 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 6
- 239000000706 filtrate Substances 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 description 5
- 239000011343 solid material Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 238000011109 contamination Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000010981 drying operation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は固形物を含んだスラリー等の濾過乾
燥装置に関するものある。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an apparatus for filtering and drying slurry containing solids.
スラリー等の固形物および液体を含む被処理物
から乾燥固形物を得るために、脱水濾過操作と、
乾燥操作を別の装置で行うものが広く知られてい
る。
In order to obtain dry solids from a processed material containing solids and liquids such as slurry, a dehydration filtration operation;
It is widely known that the drying operation is performed using a separate device.
また脱水濾過終了後、容器自体を反転または傾
斜させて、濾過された固形物をジヤツトの付いた
乾燥部に落下させたり、あるいは回転を継続して
て乾燥させる装置が知ている(例えば特公昭52−
17898号)。 Furthermore, there are known devices in which after dehydration filtration is completed, the container itself is inverted or tilted, and the filtered solids are dropped into a drying section with a jacket, or the container is dried by continuing rotation. 52−
No. 17898).
しかしながら、上記の別の装置で濾過と乾燥を
行うものでは、濾過された固形物を乾燥装置に移
送する必要があり、その際ゴミ等の異物の混入、
空気との接触による変質、有害物による人体およ
び環境への悪影響が発生し、繁雑な手間を要する
という問題点があつた。
However, in the above-mentioned devices that perform filtration and drying using separate devices, it is necessary to transfer the filtered solids to a drying device, which may cause contamination of foreign matter such as dust.
There were problems such as deterioration due to contact with the air, adverse effects on the human body and environment due to harmful substances, and the need for complicated labor.
また容器を反転または傾斜させて濾過および乾
燥を行う装置では、1回の濾過操作によつて得ら
れる固形物を1回の乾燥操作で処理するため、濾
過性が悪い多くの場合、乾燥装置の容積効率が著
しく劣り、かつ反転、傾斜、回転に危険を伴い、
被処理物の供給と乾燥物の排出がライン−自動化
できないなどの問題点があつた。 In addition, in devices that perform filtration and drying by inverting or tilting the container, the solids obtained in one filtration operation are processed in one drying operation, so in many cases, the drying device has poor filtration performance. The volumetric efficiency is extremely poor, and it is dangerous to flip, tilt, or rotate.
There were problems such as the inability to automate the supply of materials to be processed and the discharge of dried materials on a line.
この発明は上記問題点を解決するためのもの
で、1つの装置で濾過と乾燥を行うことができ、
これにより被処理物を中間工程で外部と接触させ
るとがなく、濾過、乾燥の容積効率が高く、かつ
危険が少ない濾過乾燥装置を提供することを目的
としている。 This invention is intended to solve the above problems, and it is possible to perform filtration and drying with one device.
The object of the present invention is to provide a filtration/drying apparatus that does not bring the material to be processed into contact with the outside during intermediate steps, has high volumetric efficiency in filtration and drying, and is less dangerous.
この発明は、隔壁により上部に濾過部および下
部に乾燥部が区画された容器と、
この容器の中央部の乾燥部の底部から濾過部ま
で伸びるセンターポールと、
前記濾過部の隔壁より上部に設けられた濾材
と、
前記濾過部の濾材より上部に設けられた被処理
物導入部、および濾材より下部に設けられた濾液
排出部と、
前記濾過部から乾燥部へ固形物を落下させるよ
うに、隔壁および濾材を通して形成された通路
と、
この通路を開閉するシヤツタと、
前記乾燥部の周囲に設けられたジヤケツトと、
このジヤケツトに熱媒を導入および排出する熱
媒入口および熱媒出口と、
前記乾燥部に設けられた蒸気排出部および乾燥
物排出部と、
前記濾過部で得られた固形物を前記通路を通し
て乾燥部へ移送しかつ乾燥部における固形物を撹
拌するように前記容器に設けられた振動発生装置
と
を備えた濾過乾燥装置である。
This invention provides a container having a filtration section at the top and a drying section at the bottom divided by a partition, a center pole extending from the bottom of the drying section in the center of the container to the filtration section, and a center pole provided above the partition of the filtration section. a filter medium provided in the filtration section; a material introduction section provided above the filter medium of the filtration section; and a filtrate discharge section provided below the filter medium; a passage formed through a partition wall and a filter medium; a shutter for opening and closing this passage; a jacket provided around the drying section; a heat medium inlet and a heat medium outlet for introducing and discharging a heat medium into the jacket; a steam discharge section and a dry matter discharge section provided in the drying section; and a steam discharge section and a dry matter discharge section provided in the container so as to transfer the solids obtained in the filtration section to the drying section through the passage and to stir the solids in the drying section. This is a filtration drying device equipped with a vibration generator.
本発明の濾過乾燥装置においては、被処理物導
入部から容器内の濾過部にスラリー等の被処理物
を導入し、濾材を通して濾過を行い、濾液を外部
に排出するとともに、固形物を濾材により捕捉す
る。濾過終了後、振動発生装置により容器に振動
を与えることによつて、濾過により得られた固形
物を濾材上を移動させ、シヤツタを開くことによ
り通路を通して乾燥部に落下させる。これらの操
作は必要により複数回行うことができる。その後
熱媒入口からジヤケツトに熱媒を導入して乾燥部
を加熱するとともに、振動発生装置により容器を
振動させて固形物を撹拌し乾燥を行う。
In the filtration drying apparatus of the present invention, a material to be treated such as a slurry is introduced from a material introduction part into a filtration part in a container, filtered through a filter medium, and the filtrate is discharged to the outside, while solids are removed by the filter medium. Capture. After the filtration is completed, the solids obtained by filtration are moved on the filter medium by applying vibrations to the container using a vibration generator, and the solids obtained by the filtration are caused to fall through the passage into the drying section by opening the shutter. These operations can be performed multiple times if necessary. Thereafter, a heating medium is introduced into the jacket from the heating medium inlet to heat the drying section, and the container is vibrated by a vibration generator to agitate and dry the solids.
振動発生装置により容器が振動すると、濾過部
の固形物および乾燥部の固形物はそれぞれ容器の
周壁に沿つて移動し撹拌されるが、センターポー
ルがあるため、中心部における滞留や短絡は防止
され移送および撹拌効果は高くなる。乾燥部で発
生する蒸気は蒸気排出部から排出され、乾燥した
固形物は乾燥物排出部から排出される。 When the container is vibrated by the vibration generator, the solids in the filtration section and the solids in the drying section move along the peripheral wall of the container and are agitated, but because of the center pole, stagnation and short circuits in the center are prevented. The transfer and stirring effect will be high. The steam generated in the drying section is discharged from the steam discharge section, and the dried solids are discharged from the dry matter discharge section.
{実施例〕
以下、この発明を実施例により説明する。第1
図は実施例の垂直断面図、第2図はそのA−A断
面図、第3図および第4図は別の状態を示すB−
B断面図である。{Examples] The present invention will be explained below using examples. 1st
The figure is a vertical sectional view of the embodiment, FIG. 2 is a sectional view taken along line A-A, and FIGS.
It is a sectional view of B.
図において、1は本体容器で、竪型円筒状に形
成され、上部に濾過部2および下部に乾燥部3が
隔壁4によつて区画されている。容器1の中央部
には乾燥部3の底部から中空のセンターポール5
が立上がり、濾過部2の途中まで伸びている。 In the figure, reference numeral 1 denotes a main body container, which is formed into a vertical cylindrical shape, and is partitioned by a partition wall 4 into a filtration section 2 at the upper part and a drying section 3 at the lower part. A hollow center pole 5 is inserted into the center of the container 1 from the bottom of the drying section 3.
rises and extends halfway through the filter section 2.
濾過部2には隔壁4の上に濾材としての濾板6
が設けられ、フランジ7によつて固定されてい
る。隔壁4および濾板6の一部には通路8が設け
られている。通路8にはシヤツタ9が設けられレ
バー10により開閉可能になつている。濾過部2
の上部には供給バルブ11を有する供給ノズル1
2および圧空入口13が設けられている。隔壁4
の最低部から排液管14がフレキシブルチユーブ
15を介して排液ノズル16に続し、真空ポンプ
17で吸引されるようになつている。 In the filtration section 2, a filter plate 6 as a filter medium is provided on the partition wall 4.
is provided and fixed by a flange 7. A passage 8 is provided in a portion of the partition wall 4 and the filter plate 6. A shutter 9 is provided in the passage 8 and can be opened and closed by a lever 10. Filtration section 2
A supply nozzle 1 with a supply valve 11 is located in the upper part of the
2 and a compressed air inlet 13 are provided. Partition wall 4
A drain pipe 14 is connected to a drain nozzle 16 from the lowest part through a flexible tube 15, and is suctioned by a vacuum pump 17.
乾燥部3の側壁および底壁にはジヤケツト18
が設けられ、熱媒入口19および熱媒出口20に
接続している。乾燥部3の上部には排気ノズル2
1が設けられ、下部には排出弁22を有する排出
ノズル23が設けられている。容器1は防振ゴム
24を介して支柱25に支持されている。 A jacket 18 is installed on the side wall and bottom wall of the drying section 3.
is provided and connected to the heat medium inlet 19 and the heat medium outlet 20. An exhaust nozzle 2 is installed at the top of the drying section 3.
1 is provided, and a discharge nozzle 23 having a discharge valve 22 is provided at the bottom. The container 1 is supported by a column 25 via a vibration-proof rubber 24.
容器1の下部両側には、容器1のの周壁に沿つ
て傾斜方向に振動を与えるように、2個の振動発
生装置26,27が交差する方向に設けられてい
る。振動発生装置26,27は容器1の下部両側
に交差する方向に傾斜して取付けられた2個のモ
ータの回転軸の両端に重錘を取付けて、水平方向
の分力を打消し合うように回転させ、それぞれの
重錘により容器1にその周壁に沿つた傾斜方向の
直線振動を与えるようになつている。 Two vibration generators 26 and 27 are provided on both sides of the lower part of the container 1 in an intersecting direction so as to apply vibrations in an inclined direction along the peripheral wall of the container 1. The vibration generators 26 and 27 are constructed by attaching weights to both ends of the rotating shafts of two motors installed at both sides of the lower part of the container 1 so as to be inclined in the intersecting direction, so as to cancel out the horizontal component forces. The containers 1 are rotated, and the respective weights apply linear vibrations to the container 1 in the direction of inclination along its peripheral wall.
上記の構成において、第3図のようにシヤツタ
9を閉じて供給ノズル12からスラリー等の被処
理物を容器1の濾過部2に供給し、供給バルブ1
1を閉じて排液ノズ16より真空ポンプ17にて
吸引し、濾過を行う。このとき圧空入口13から
圧縮空気を送つて加圧法により濾過を行つてもよ
い。濾過により被処理物は濾板6にて濾液と固形
物に分離され、濾液は排液ノズル16より外部に
排出され、固形物は濾板6に捕捉される。濾過は
複数回行つてもよく、また連続濾過を行つてもよ
い。 In the above configuration, the shutter 9 is closed as shown in FIG.
1 is closed and suction is performed from the drain nozzle 16 using the vacuum pump 17 to perform filtration. At this time, compressed air may be sent from the compressed air inlet 13 to perform filtration by a pressurization method. By filtration, the material to be treated is separated into a filtrate and solid matter by the filter plate 6, the filtrate is discharged to the outside from the drain nozzle 16, and the solid matter is captured by the filter plate 6. Filtration may be performed multiple times, or continuous filtration may be performed.
濾過終了後、振動発生装置26,27を駆動し
て容器1に振動を与え、第4図のようにシヤツタ
9を開くと、濾板6上の固形物は振動により容器
1の周壁に沿つて斜上方向に持上つて濾板6上を
環状に移動し、通路8から乾燥部3に落下する。
このときノズル28より圧縮空気または洗浄水等
を導入して剥離を促進したり、濾板6を洗浄する
こともできる。固形物落下後、乾燥部3の乾燥能
力に余裕があるときは、上記濾過および固形物の
移送を複数回繰返えす。 After filtration, the vibration generators 26 and 27 are driven to give vibration to the container 1, and when the shutter 9 is opened as shown in FIG. 4, the solids on the filter plate 6 are vibrated along the peripheral wall of the container 1. It is lifted obliquely upward, moves in a circular manner on the filter plate 6, and falls into the drying section 3 through the passage 8.
At this time, compressed air, washing water, or the like may be introduced through the nozzle 28 to promote peeling or to wash the filter plate 6. After the solid matter has fallen, if the drying capacity of the drying section 3 is sufficient, the above-mentioned filtration and solid matter transfer are repeated several times.
こうして乾燥部3に適当量の固形物が移送され
るると、ジヤケツト18に熱媒を導入して乾燥部
3内の固形物を加熱するとともに、振動発生装置
26,27を駆動して固形形物を撹拌する。この
とき容器1の振動により固形物は周壁に沿つた傾
斜方向の振動を与えられ、容器1とのの接触面積
の大きい側壁部に固形物が側壁に沿つて斜上方向
に持上がり、固形物層の上面に沿つて内側に移動
し、容器1の中央部をセンターポール5に沿つて
下降する渦巻運動を行いながら、周壁に沿つて環
状に移動する。このとき固形物は水平方向の移動
および上下方向の跳躍移動となり、効率よく撹拌
が行われる。この場合乾燥部3にバツフルを設け
て撹拌効率を上げることも可能である。 When an appropriate amount of solid material is transferred to the drying section 3 in this way, a heating medium is introduced into the jacket 18 to heat the solid material in the drying section 3, and the vibration generators 26 and 27 are driven to remove the solid material. Stir. At this time, the vibration of the container 1 causes the solid material to vibrate in an oblique direction along the peripheral wall, and the solid material is lifted obliquely upward along the side wall to the side wall part where the contact area with the container 1 is large. It moves inward along the upper surface of the layer, and moves in a circular manner along the peripheral wall while performing a spiral movement in which the central portion of the container 1 descends along the center pole 5. At this time, the solids move in the horizontal direction and jump in the vertical direction, and are efficiently stirred. In this case, it is also possible to increase the stirring efficiency by providing a buffer in the drying section 3.
こうして乾燥部3において固形物は乾燥され、
発生する蒸気は排気ノズル21から排出される。
このとき排気ノズル21から吸引すると乾燥が促
進される。吸引の具体的な方法としては、真空ポ
ンプ17またはブロア等の吸引手段に接続するコ
ンデンサ(図示せず)に排気ノズル21を導き、
上記コンデンサに冷却水を供給して冷却しながら
真空引きし、真空乾燥を行う。乾燥物は振動を続
けながら排出弁22を開くことにより、排出ノズ
ル23から排出される。 In this way, the solid matter is dried in the drying section 3,
The generated steam is exhausted from the exhaust nozzle 21.
At this time, suction from the exhaust nozzle 21 accelerates drying. As a specific method of suction, the exhaust nozzle 21 is guided to a condenser (not shown) connected to a suction means such as a vacuum pump 17 or a blower.
Cooling water is supplied to the condenser and the condenser is evacuated while being cooled to perform vacuum drying. The dried material is discharged from the discharge nozzle 23 by opening the discharge valve 22 while continuing to vibrate.
上記の装置では、濾過と乾燥を1機種の装置で
行うことができ、被処理物は中間工程で外部と接
触することなく、このため異物の混入や変質等の
おそれがない。また数回の濾過および固形物の移
送の繰返しにより、単位容積当りの乾燥張込量が
従来のものより大きくなり、このため供給、排出
の所要時間が減り、結果的に単位時間当りの処理
量(生産量)が増大する。また容器1は反転、傾
斜等の必要がないため、危険性はない。 In the above-mentioned apparatus, filtration and drying can be performed in one type of apparatus, and the material to be treated does not come into contact with the outside during intermediate steps, so there is no risk of contamination with foreign substances or deterioration of quality. In addition, by repeating filtration and transferring solids several times, the dry loading amount per unit volume is larger than that of conventional methods, which reduces the time required for supply and discharge, resulting in a reduction in the throughput per unit time. (production volume) increases. Further, since the container 1 does not need to be turned over or tilted, there is no danger.
なお、以上の説明において、容器1、濾過部
2、乾燥部3、通路8、シヤツタ9、振動発生装
置26,27、濾材等の構造、配置等は実施例の
ものに限定されず、変更可能である。また被処理
物もスラリーに限らず、固形物および液体を含む
ものであればよい。 In addition, in the above description, the structure, arrangement, etc. of the container 1, filtration part 2, drying part 3, passage 8, shutter 9, vibration generators 26, 27, filter media, etc. are not limited to those in the example and can be changed. It is. Furthermore, the object to be treated is not limited to slurry, but may be anything containing solids and liquids.
この発明によれば、容器に濾過部および乾燥部
を上下に区画する隔壁に、開閉可能なシヤツタを
有する通路を設け、濾過部から固形物を振動によ
り乾燥物を落下させ、乾燥部では振動により固形
物を撹拌しながら、ジヤケツトにより加熱し、セ
ンターポートにより移送、戰拌効果を高めるよう
にしたので、1つの装置でシヤツタ開閉により固
形物を移動させて、濾過と撹拌をを継続または並
行して効率よく行うことができ、被処理物を途中
で外部と接触させることがなく、濾過、乾燥の容
積効率を高くできるとともに、容器を反転または
傾斜させる必要がないため、危険性が少ないなど
の効果がある。
According to this invention, a passage having a shutter that can be opened and closed is provided in the partition wall that divides the filtration part and the drying part into upper and lower parts of the container, and the dried material is dropped from the filtration part by vibration, and in the drying part by vibration. While stirring the solid matter, it is heated by the jacket and transferred through the center port to enhance the stirring effect, so the solid matter can be moved by opening and closing the shutter in one device, and filtration and stirring can be carried out continuously or in parallel. The process can be carried out efficiently, and the material to be processed does not come into contact with the outside during the process, increasing the volumetric efficiency of filtration and drying, and there is no need to invert or tilt the container, so there is less danger. effective.
第1図は実施例の垂直断面図、第2図はそのA
−A断面図、第3図および第4図は別の状態を示
すB−B断面図である。
各図中、同一符号は同一部分を示し、1は本体
容器、2は濾過部、3は乾燥部、4は隔壁、5は
センターポール、6は濾板、8は通路、9はシヤ
ツタ、12は供給ノズル、16は排液ノズル、1
8はジヤケツト、21は排気ノズル、23は排出
ノズル、26,27は振動発生装置である。
Figure 1 is a vertical sectional view of the embodiment, and Figure 2 is its A.
-A sectional view, FIGS. 3 and 4 are BB sectional views showing other states. In each figure, the same reference numerals indicate the same parts, 1 is the main container, 2 is the filtration part, 3 is the drying part, 4 is the partition wall, 5 is the center pole, 6 is the filter plate, 8 is the passage, 9 is the shutter, 12 is a supply nozzle, 16 is a drain nozzle, 1
8 is a jacket, 21 is an exhaust nozzle, 23 is an exhaust nozzle, and 26 and 27 are vibration generators.
Claims (1)
が区画された容器と、 この容器の中央部の乾燥部の底部から濾過部ま
で伸びるセンターポールと、 前記濾過部の隔壁より上部に設けられた濾材
と、 前記濾過部の濾材より上部に設けられた被処理
物導入部、および濾材より下部に設けられた濾液
排出部と、 前記濾過部から乾燥部へ固形物を落下させるよ
うに、隔壁および濾材を通して形成された通路
と、 この通路を開閉するシヤツタと、 前記乾燥部の周囲に設けられたジヤケツトと、 このジヤケツトに熱媒を導入および排出する熱
媒入口および熱媒出口と、 前記乾燥部に設けられた蒸気排出部および乾燥
物排出部と、 前記濾過部で得られた固形物を前記通路を通し
て乾燥部へ移送しかつ乾燥部における固形物を撹
拌するように前記容器に設けられた振動発生装置
と を備えた濾過乾燥装置。 2 容器が上部に濾過部、下部に乾燥部を有する
竪型円筒状容器である特許請求の範囲第1項記載
の濾過乾燥装置。 3 振動発生装置が容器の周壁に沿つて傾斜方向
の振動を与えるものである特許請求の範囲第1項
または第2項記載の濾過乾燥装置。[Scope of Claims] 1. A container having a filtration section at the top and a drying section at the bottom divided by partition walls, a center pole extending from the bottom of the drying section in the center of the container to the filtration section, and a center pole extending from the partition wall of the filtration section. a filter medium provided at the top; a material introduction section provided above the filter medium of the filtration section; and a filtrate discharge section provided below the filter medium; solids are dropped from the filtration section to the drying section. a passage formed through a partition wall and a filter medium; a shutter for opening and closing this passage; a jacket provided around the drying section; a heating medium inlet and a heating medium outlet for introducing and discharging a heating medium into the jacket. a steam exhaust section and a dry matter discharge section provided in the drying section; and the container configured to transfer the solids obtained in the filtration section to the drying section through the passage and to stir the solids in the drying section. A filtration drying device equipped with a vibration generator installed in the filtration drying device. 2. The filtration and drying device according to claim 1, wherein the container is a vertical cylindrical container having a filtration section at the top and a drying section at the bottom. 3. The filtration drying device according to claim 1 or 2, wherein the vibration generator applies vibration in an oblique direction along the peripheral wall of the container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60146700A JPS629172A (en) | 1985-07-05 | 1985-07-05 | Filtering drier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60146700A JPS629172A (en) | 1985-07-05 | 1985-07-05 | Filtering drier |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS629172A JPS629172A (en) | 1987-01-17 |
JPH0557008B2 true JPH0557008B2 (en) | 1993-08-23 |
Family
ID=15413575
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60146700A Granted JPS629172A (en) | 1985-07-05 | 1985-07-05 | Filtering drier |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS629172A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5217898A (en) * | 1975-07-02 | 1977-02-10 | Eastman Kodak Co | Spotting tool |
JPS5236363A (en) * | 1975-09-18 | 1977-03-19 | Mitsubishi Rayon Co | Method of separating solid matter by using filter net and its device |
-
1985
- 1985-07-05 JP JP60146700A patent/JPS629172A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5217898A (en) * | 1975-07-02 | 1977-02-10 | Eastman Kodak Co | Spotting tool |
JPS5236363A (en) * | 1975-09-18 | 1977-03-19 | Mitsubishi Rayon Co | Method of separating solid matter by using filter net and its device |
Also Published As
Publication number | Publication date |
---|---|
JPS629172A (en) | 1987-01-17 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |