JPH0526113U - Continuous solid-liquid separator equipped with spiral rotating plate - Google Patents
Continuous solid-liquid separator equipped with spiral rotating plateInfo
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- JPH0526113U JPH0526113U JP8368991U JP8368991U JPH0526113U JP H0526113 U JPH0526113 U JP H0526113U JP 8368991 U JP8368991 U JP 8368991U JP 8368991 U JP8368991 U JP 8368991U JP H0526113 U JPH0526113 U JP H0526113U
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Abstract
(57)【要約】
【目的】 螺旋状分離体の分離間隙を適宜設定、調節し
て固液分離の容量、精度を高め、螺旋状分離体を振動さ
せ固体の剥離、除去を促進して固体による目詰まりを防
止し、分離装置の運転を中断することなく、液体より固
体を連続分離して固液分離処理効率を向上させる。
【構成】 金属線等を螺旋状に巻いた分離間隙を有する
螺旋状分離体を分離装置内に設置し、螺旋状分離体の分
離液の流出口を分離装置の分離液流出管と接続し、スパ
イラル状回転板を螺旋状分離体の外側面に近接させて回
転可能に挿着し、そして原液を原液流入管より分離装置
内に加圧供給し、固体を螺旋状分離体の各分離間隙等に
捕捉し、振動で落下させた固体をスパイラル状回転板で
分離装置の固体流出管へ搬出し、分離液を螺旋状分離体
の各分離間隙より内部に流入させ、螺旋状分離体の流出
口を経て分離装置の分離液流出管に集液する。
(57) [Abstract] [Purpose] The separation gap of the spiral separator is appropriately set and adjusted to enhance the capacity and accuracy of solid-liquid separation, and the spiral separator is vibrated to promote solid separation and removal. The solid-liquid separation treatment efficiency is improved by preventing the clogging due to the above and continuously separating the solid from the liquid without interrupting the operation of the separation device. [Structure] A spiral separator having a separation gap formed by spirally winding a metal wire or the like is installed in a separation device, and an outlet of the separation liquid of the spiral separator is connected to a separation liquid outflow pipe of the separation device, A spiral rotary plate is rotatably inserted close to the outer surface of the spiral separator, and the stock solution is pressure-supplied from the stock solution inflow pipe into the separation device to separate solids into each separation gap of the spiral separator. The solids trapped in the solid and dropped by vibration are carried out to the solid outflow pipe of the separation device by the spiral rotating plate, the separated liquid is made to flow into each of the separation gaps of the spiral separator, and the outlet of the spiral separator is provided. After that, the liquid is collected in the separated liquid outflow pipe of the separation device.
Description
【0001】[0001]
本考案は、工作機械等より排出する切粉、金属粉等の懸濁物と切削物、破砕物 等の粒状物を含むクーラント等の液体より、または水処理装置等の処理対象であ る砂、泥等の懸濁物と砂利、石等の粒状物を含む上下水や廃水等の液体より、あ るいは金属加工装置において発生する金、プラチナ等の貴金属の粉体等の懸濁物 と切削物、破砕物等の粒状物を含む洗浄液等の液体より、これらの懸濁物と粒状 物(以下固体という)を分離する装置に関するものである。 INDUSTRIAL APPLICABILITY The present invention uses a liquid such as a coolant discharged from a machine tool or the like, a suspension such as cutting powder or metal powder and a particulate matter such as a cutting material or a crushed material, or sand to be treated by a water treatment device or the like , Suspended solids such as mud and liquids such as sewage and wastewater containing particulates such as gravel and stones, or suspended powders of precious metals such as gold and platinum generated in metal working equipment. The present invention relates to an apparatus for separating a suspension and a particulate matter (hereinafter referred to as a solid) from a liquid such as a cleaning liquid containing a particulate matter such as a cut product or a crushed product.
【0002】[0002]
従来、固液分離するには、分離装置にスクリーンや多孔板等を付設し、これに よって原液中の懸濁物の分離を行っていたが、スクリーンや多孔板等の一度設定 したスリットや孔径を簡単に調節できるものはなく、またスクリーンや多孔板等 に固体が付着、蓄積して目詰まりをする結果、分離処理が不可能になることが多 く、その度に分離処理を中断してスクリーンや多孔板等の洗浄を行う必要が生じ 、場合によると装置の解体を伴い手間がかかり、またスクリーンや多孔板等の洗 浄が繁雑で、時間を要する等、分離処理効率が悪くなるという欠点があった。 Conventionally, in order to perform solid-liquid separation, a screen or a perforated plate was attached to the separation device to separate the suspension in the stock solution. There is nothing that can be easily adjusted, and as a result of solids adhering to and accumulating on screens, perforated plates, etc., resulting in clogging, the separation process is often impossible. It is necessary to clean the screen and the perforated plate.In some cases, the dismantling of the equipment is time-consuming, and the cleaning of the screen and the perforated plate is complicated, and it takes time. There was a flaw.
【0003】 また、分離装置に螺旋状分離体を挿填し、螺旋状分離体の外側面に原液を加圧 供給し、固体を螺旋状分離体の外側面に捕捉して分離するとともに、分離液を螺 旋状分離体の外側面の分離間隙より内部に流入させ、螺旋状分離体の外部に集液 することによって、原液中の固体の分離を行っていたが、螺旋状分離体の外側面 や分離間隙に固体が付着、蓄積して目詰まりをする結果、分離処理が不可能にな り、前述した場合と同様の欠点を有することには変わりなかった。In addition, the spiral separator is inserted into the separation device, the stock solution is pressurized and supplied to the outer surface of the spiral separator, and the solid is captured and separated on the outer surface of the spiral separator. The solid in the stock solution was separated by flowing the liquid into the inside of the spiral separator from the separation gap on the outer surface and collecting the liquid outside the spiral separator. As a result of solids adhering to and accumulating on the side surfaces and separation gaps, resulting in clogging, the separation process became impossible, and it had the same drawbacks as in the case described above.
【0004】[0004]
本考案は、分離体の分離間隙を簡単に設定、調節して固液分離の分離容量、分 離精度を高め、また螺旋状分離体を振動させることによって固体の剥離、除去を 促進して固体による目詰まりを防止し、さらに分離装置の運転を中断して螺旋状 分離体の洗浄をすることなく、液体より固体を連続して分離して固液分離処理効 率を向上させることにある。 The present invention easily sets and adjusts the separation gap of the separator to enhance the separation capacity and separation accuracy of solid-liquid separation, and vibrates the spiral separator to accelerate the separation and removal of solids and to promote solid separation. This is to prevent clogging due to the above, and to further improve the solid-liquid separation treatment efficiency by continuously separating the solid from the liquid without interrupting the operation of the separation device and cleaning the spiral separator.
【0005】[0005]
本考案は、弾力性のある金属線または合成樹脂線等を螺旋状に巻いて巻線の間 に分離間隙を有する螺旋状分離体とし、この螺旋状分離体を、上部に固体流出管 を、また下部に原液流入管を設けた分離装置内に、その両端を閉鎖するように、 分離装置の内側面と間隔をおいて設置し、この螺旋状分離体の下端の分離液の流 出口を、分離装置の下部に設けた分離液流出管と接続し、さらに螺旋状分離体に 振動を与えるスパイラル状回転板を、螺旋状分離体の外側面に近接させて回転可 能に螺旋状分離体に挿着し、そして固体を含む原液を分離装置の内側面と螺旋状 分離体の外側面の間に加圧供給し、固体を螺旋状分離体の各分離間隙および外側 面に捕捉、分離し、スパイラル状回転板によって固体を分離装置に設けた固体流 出管へ搬出するするとともに、分離液を螺旋状分離体の各分離間隙より螺旋状分 離体の内部に流入させ、螺旋状分離体の流出口を経由して分離装置に設けた分離 液流出管に集液するスパイラル状回転板を設けた連続固液分離装置に関するもの である。 In the present invention, an elastic metal wire or synthetic resin wire is spirally wound to form a spiral separator having a separation gap between windings, and this spiral separator is provided with a solid outflow pipe at the top. In addition, it is installed in the separation device with a stock solution inflow pipe at the bottom so as to close both ends of the separation device, spaced apart from the inner surface of the separation device, and the separation liquid outlet at the lower end of this spiral separator is A spiral rotary plate that connects to the separated liquid outflow pipe provided at the bottom of the separation device and that vibrates the spiral separator is placed close to the outer surface of the spiral separator so that the spiral separator can rotate. The solid solution containing the solids is inserted and pressurized between the inner surface of the separation device and the outer surface of the spiral separator, and the solid is captured and separated in each separation gap and the outer surface of the spiral separator. The solid is carried out to the solid outflow pipe provided in the separation device by the spiral rotating plate. At the same time, the separated liquid is made to flow into the inside of the spiral separator through each separation gap of the spiral separator, and is collected in the separation liquid outflow pipe provided in the separation device via the outlet of the spiral separator. The present invention relates to a continuous solid-liquid separation device provided with a spiral rotary plate.
【0006】 また本考案は、前述したスパイラル状回転板を、螺旋状分離体に対して偏心さ せ、かつ螺旋状分離体の外側面に近接させて、螺旋状分離体に回転可能に挿填す ることにのよって、螺旋状分離体に大きな振動を与えるとともに、分離した固体 を分離装置に設けた固体流出管へ搬出するスパイラル状回転板を設けた連続固液 分離装置に関するものである。 さらに本考案は、前述した螺旋状分離体に、加圧した原液、分離液または加圧 空気あるいは両者を吹き付け、旋状分離体の各分離間隙および外側面に付着、蓄 積する固体を短時間に剥離するスパイラル状回転板を設けた連続固液分離装置に 関するものである。Further, according to the present invention, the spiral rotating plate described above is eccentrically arranged with respect to the spiral separator, and is placed close to the outer surface of the spiral separator so as to be rotatably inserted into the spiral separator. Therefore, the present invention relates to a continuous solid-liquid separation device provided with a spiral rotary plate which gives a large vibration to the spiral separator and carries the separated solid to a solid outflow pipe provided in the separation device. Furthermore, the present invention sprays pressurized stock solution, separation liquid, or pressurized air, or both, onto the above-mentioned spiral separator so that solids that adhere to and accumulate in each separation gap and outer surface of the spiral separator in a short time. The present invention relates to a continuous solid-liquid separation device provided with a spiral-shaped rotating plate that is peeled off.
【0007】[0007]
図1は、分離装置1内に、スパイラル状回転板3を螺旋状分離体2に回転可能 に挿填した状態を示す断面図で、螺旋状分離体2は、例えばサブゼロ硬化処理を して弾力性に富んだステンレス鋼線を螺旋状、すなわちコイルスプリング状に巻 き、巻線の間に分離間隙7を形成したものである。 この分離間隙7は、その儘あるいは引っ張ったり、押し付けたりして、任意の幅 に簡単、容易に設定、調整できるのであるので、種々の固液分離目的に応じて適 宜決定する。 螺旋状分離体2は、原液より固体を分離するもので、原液を螺旋状分離体2の 外側面6に加圧供給し、固体を螺旋状分離体2の分離間隙7、外側面8で分離す るとともに、分離液を螺旋状分離体2の分離間隙7より螺旋状分離体2の内部に 流入させて集液するものである。 FIG. 1 is a cross-sectional view showing a state in which a spiral rotary plate 3 is rotatably inserted in a spiral separator 2 in a separator 1, and the spiral separator 2 is elastically subjected to, for example, a sub-zero curing treatment. A stainless steel wire having excellent properties is wound in a spiral shape, that is, a coil spring shape, and a separation gap 7 is formed between the windings. The separation gap 7 can be easily and easily set and adjusted to an arbitrary width by pulling it, pulling it, or pressing it. Therefore, the separation gap 7 is appropriately determined according to various solid-liquid separation purposes. The spiral separator 2 separates a solid from a stock solution. The stock solution is pressurized and supplied to the outer side surface 6 of the spiral separator 2, and the solid is separated at the separation gap 7 and the outer surface 8 of the spiral separator 2. In addition, the separated liquid is made to flow into the inside of the spiral separator 2 through the separation gap 7 of the spiral separator 2 to collect the liquid.
【0008】 螺旋状分離体2の種類としては、引っ張って巻線の分離間隙7を一定の幅に設 定する引きばねタイプ(間隔の保持性は高い)、押し付けて巻線の分離間隙7を 一定の幅に設定する押しばねタイプ(放すと分離間隙が広がるので逆洗を行うと きに便利)、引っ張ったり、押し付けたりせずに、ねじって巻線の分離間隙7を 一定の幅に設定するねじりばねタイプ(装置内への取付性がよい)の三種類があ り、いずれの螺旋状分離体2も弾力性(振動性)があるが、特に、ねじりばねタ イプのものが、自然体であるので弾力性に富んでいる。 また螺旋状分離体2の巻線の巻方には、右巻と左巻の二種類がある。The type of the spiral separator 2 is a pulling spring type in which the separation gap 7 of the winding is set to a constant width by pulling (the space retention is high), and the separation gap 7 of the winding is pressed. A push spring type that sets a constant width (useful for backwashing because the separation gap widens when released), set the width of the winding separation gap 7 to a constant width by twisting without pulling or pressing There are three types of torsion springs (having good mountability in the device), and all of the spiral separators 2 have elasticity (vibration). Especially, the torsion spring type is a natural body. Therefore, it is highly elastic. In addition, there are two types of winding methods for the winding of the spiral separator 2; right winding and left winding.
【0009】 螺旋状分離体2の材質としては、前述したサブゼロ硬化処理をたステンレス鋼 線が弾力性に富んでる点で最適であるが、これ以外にも通常のステンレス鋼線、 合成樹脂の線、または鉄線に合成樹脂を被覆したもの等の弾力性があって、物理 的強度のあるものであれば、どんなものでもよい。 螺旋状分離体2の直径と長さは、液体中の固体の種類、固体濃度、分離目的、 分離精度等の処理条件に応じて適宜決定するが、通常の場合は、直径としては1 〜50cm、長さとして10〜500cmの範囲のものを用いるとよい。 螺旋状分離体2を形成する巻線の線径は1〜8mm程度が適当であり、また固 体を分離する螺旋状分離体2の巻線の間隔は0.5〜5mm程度が適当であり、 螺旋状分離体2の長さが同じであれば,巻線の線径と間隔が小さいぼど分離面積 が大きくなり、分離精度もよくなるが、通液抵抗の増加による分離流量の低下、 目詰りの増加による分離容量の低下、分離時間の短縮等の問題もあり、また巻線 の線径と間隔が大きいぼど、前述の場合と反対になるので、従って、螺旋状分離 体2の巻線の線径と間隔は、液体中の固体の種類、固体濃度、分離目的、分離精 度等の処理条件を考慮して最適な範囲を決定することになる。As a material for the spiral separator 2, the above-mentioned sub-zero-hardened stainless steel wire is most suitable because it is highly elastic, but in addition to this, ordinary stainless steel wire and synthetic resin wire are also available. , Or an iron wire coated with a synthetic resin, as long as it has elasticity and physical strength, any material may be used. The diameter and length of the spiral separator 2 are appropriately determined according to the processing conditions such as the type of solid in the liquid, the solid concentration, the purpose of separation, the accuracy of separation, etc., but in the usual case, the diameter is 1 to 50 cm. It is advisable to use one having a length in the range of 10 to 500 cm. The wire diameter of the winding forming the spiral separating body 2 is preferably about 1 to 8 mm, and the interval between the windings of the spiral separating body 2 separating the solid body is about 0.5 to 5 mm. , If the length of the spiral separator 2 is the same, the wire diameter and the interval of the winding are small, and the separation area is large and the separation accuracy is good, but the separation flow rate decreases due to the increase in the liquid flow resistance. There are also problems such as a decrease in separation capacity due to increased clogging, a reduction in separation time, and the like, which is the opposite of the above case when the winding wire diameter and spacing are large. The wire diameter and spacing will be determined in the optimum range by considering the processing conditions such as the type of solid in the liquid, the solid concentration, the purpose of separation, and the separation accuracy.
【図1】[Figure 1]
【0010】 さらに、図2に示すように、分離装置1の上部に固体流出管4を設けるととも に、同装置1の下側部に原液流入管5を設け、この分離装置1内に、螺旋状分離 体2をその両端を閉鎖して、固定軸12を介して分離装置の内側面と間隔をおい て設置し、また螺旋状分離体2の下端の分離液の流出口を、分離装置1の下部に 設けた分離液流出管6に接続する。 そして、螺旋状分離体2にはスパイラル状回転板3を、その内端が螺旋状分離体 2の外側面8に近接させて回転可能に挿着するが、このスパイラル状回転板3は 、螺旋状分離体2に振動を与えて固体を剥離するとともに、分離装置1内に落下 して蓄積した固体を固体流出管4に搬出するものである。 スパイラル状回転板3は、分離装置1に設けたモーター9の回転軸10に取り 付けた固定板11に接続するが、モーター9以外の他の回転手段を用いてもさし つかえない。Further, as shown in FIG. 2, a solid outflow pipe 4 is provided at the upper part of the separation device 1, and a stock solution inflow pipe 5 is provided at a lower side part of the separation device 1, and inside the separation device 1, Both ends of the spiral separator 2 are closed, and the spiral separator 2 is installed with a space between the spiral separator 2 and the inner side surface of the separator, and the outlet of the separation liquid at the lower end of the spiral separator 2 is connected to the separator. 1 is connected to the separated liquid outflow pipe 6 provided at the lower part. Then, the spiral rotary plate 3 is rotatably attached to the spiral separator 2 such that the inner end of the spiral rotary plate 3 is close to the outer surface 8 of the spiral separator 2, and the spiral rotary plate 3 has a spiral shape. The solid separator 2 is vibrated to separate solids, and the solids that have fallen into the separator 1 and accumulated therein are carried out to the solid outflow pipe 4. The spiral rotary plate 3 is connected to the fixed plate 11 attached to the rotary shaft 10 of the motor 9 provided in the separating device 1, but other rotating means other than the motor 9 may be used.
【0011】 そして原液(クーラント廃液)を流入管5より分離装置1の内側面と螺旋状分 離体2の外側面の間に圧入させると同時に、モーター9を駆動してスパイラル状 回転板3を回転させ、螺旋状分離体2の分離間隙7を均等に調整し、この螺旋状 分離体2の分離間隙7と外側面8で原液中の固体を分離する。 一方、螺旋状分離体2の分離間隙7より螺旋状分離体2の内部に流入して集液 した分離液は、螺旋状分離体2の下端の流出口よに分離装置1に設けた分離液流 出管6を経て分離装置1の外部に流出させ、分離液(クーラント)として貯留槽 に貯えて、必要に応じて再利用に供する。 また螺旋状分離体2の分離間隙7と外側面8側面に捕捉、付着した固体は、ス パイラル状回転板3による螺旋状分離体の振動のために、螺旋状分離体2の分離 間隙7と外側面8より剥離して分離装置1の底部に落下、蓄積して行くが、固体 の蓄積量がある程度になると、スパイラル状回転板3の回転によって生ずる掻き 上げ作用、サイクロン作用により固体を効率よく固体流出管4へ搬出し、固体( スラッジ)として分離装置1の外部に排出させる。Then, the undiluted solution (coolant waste solution) is pressed into the space between the inner surface of the separation device 1 and the outer surface of the spiral separating member 2 through the inflow pipe 5, and at the same time, the motor 9 is driven to move the spiral rotating plate 3 By rotating, the separation gap 7 of the spiral separator 2 is evenly adjusted, and the separation gap 7 of the spiral separator 2 and the outer surface 8 separate the solid in the stock solution. On the other hand, the separated liquid that flows into the inside of the spiral separator 2 through the separation gap 7 of the spiral separator 2 and collects the separated liquid is provided in the separation device 1 from the outlet at the lower end of the spiral separator 2. It flows out of the separation device 1 through the outflow pipe 6, is stored as a separated liquid (coolant) in a storage tank, and is reused as necessary. Further, the solids trapped and attached to the separation gap 7 and the side surface of the outer side surface 8 of the spiral separator 2 are separated from the separation gap 7 of the spiral separator 2 due to the vibration of the spiral separator by the spiral rotary plate 3. Although it separates from the outer surface 8 and falls to the bottom of the separator 1 and accumulates, when the amount of accumulated solids reaches a certain level, the scraping action and cyclone action caused by the rotation of the spiral rotary plate 3 efficiently removes the solids. It is carried out to the solid outflow pipe 4, and discharged as solid (sludge) to the outside of the separator 1.
【図2】[Fig. 2]
【0012】 なお螺旋状分離体2をスパイラル状回転板3で振動させる理由の一つは、螺旋 状分離体2は、それ自体、固体を分離する分離間隙7を有しているが、原液の通 液圧等によって分離間隙7が不均等になって偏り、狭くなったり、広くなったり して固体の分離に悪影響が生ずるすることがあるので、螺旋状分離体2に振動を 与えることにより、偏りを解して全側面に均等な分離間隙7を確保することにあ る。 また螺旋状分離体を振動させる理由の他の一つは、螺旋状分離体2に付着、蓄 積した固体を、螺旋状分離体2を振動させることにより剥離、落下させることに ある。 スパイラル状回転板3の材質も、前述した螺旋状分離体2の材質と同じものを用 い、そのスパイラルの間隔は、原液の固体の含有量が多く、螺旋状分離体2に付 着し易い固体が含まれている原液の場合には、間隔が狭く、また原液の固体の含 有量が少なく、螺旋状分離体2に付着し難い固体が含まれている原液の場合には 広くなるが、通常の場合は、3〜10cmの間隔にすることになる。 スパイラル状回転板3の回転数は、10〜100 r.p.m であることが望ましく、時に はスパイラル状回転板3の回転を間欠的に行ったり、または一定期間ごとに逆回 転させてもよい。One of the reasons why the spiral separator 2 is vibrated by the spiral rotary plate 3 is that the spiral separator 2 itself has a separation gap 7 for separating solids. The separation gap 7 may become uneven and uneven due to liquid pressure or the like, and may be narrowed or widened to adversely affect the separation of solids. Therefore, by applying vibration to the spiral separator 2, This is to eliminate the bias and ensure a uniform separation gap 7 on all sides. Another reason for vibrating the spiral separator is that the solids attached to and accumulated on the spiral separator 2 are separated and dropped by vibrating the spiral separator 2. The material of the spiral rotary plate 3 is also the same as that of the spiral separator 2 described above. The spiral interval is large in the solid content of the stock solution, and is easily attached to the spiral separator 2. In the case of an undiluted solution containing solids, the interval is narrow, and the content of undiluted solids is small, but it is wide in the case of undiluted solution containing solids that are difficult to adhere to the spiral separator 2. Normally, the distance will be 3 to 10 cm. The rotation speed of the spiral rotary plate 3 is preferably 10 to 100 r.p.m, and sometimes the spiral rotary plate 3 may be intermittently rotated, or may be reversely rotated at regular intervals.
【0013】 なおスパイラル状回転板3は、図3に示すように、螺旋状分離体2に挿填する スパイラル状回転板3の挿入口を中心に設けずに多少遍心させ、かつスパイラル 状回転板3の各羽根の挿入口の遍心位置を多少ずらせると、螺旋状分離体2との 接触度合いが大きくなり、螺旋状分離体2が全体として波打つような強力な振動 を与えることができる。As shown in FIG. 3, the spiral rotating plate 3 is slightly eccentric to the spiral separating plate 2 without inserting the insertion port of the spiral rotating plate 3 into the center, and the spiral rotating plate 3 is rotated. By slightly shifting the eccentric position of the insertion opening of each blade of the plate 3, the degree of contact with the spiral separator 2 becomes large, and the spiral separator 2 can be given strong vibrations that wavy as a whole. .
【図3】[Figure 3]
【0014】 なお原液の固体の含有量が多かったり、螺旋状分離体2に付着し易い固体が含 まれてい等の処理条件においては、螺旋状分離体2の分離間隙7、外側面8に付 着、蓄積した固体をスパイラル状回転板3の回転だけでは剥離することができな いこともあるので、このような時は、螺旋状分離体2の外側面8に加圧した原液 または加圧空気あるいは両者によってを吹き付け、スパイラル状回転板3の振動 とともに固体を剥離すると、固体の剥離性が格段によくなる。 また固体の洗浄については、螺旋状分離体2の内部より外側面8に向けて、加 圧した分離液または加圧空気あるいは両者を逆流状態で吹き付け、螺旋状分離体 2の分離間隙7、外側面8に付着、蓄積した固体をスパイラル状回転板3よる振 動とともに剥離すると、最も固体の剥離性がよい。Under the processing conditions such that the undiluted solution contains a large amount of solids or contains solids that easily adhere to the spiral separator 2, the separation gap 7 and the outer surface 8 of the spiral separator 2 are attached. In some cases, the solids deposited and accumulated cannot be separated only by rotating the spiral rotary plate 3. Therefore, in such a case, the stock solution or the pressurized liquid applied to the outer surface 8 of the spiral separator 2 is pressed. When air or both are blown and the solid is peeled off with the vibration of the spiral rotary plate 3, the solid peeling property is remarkably improved. For washing solids, the pressurized separation liquid, pressurized air, or both are blown in a reverse flow direction from the inside of the spiral separator 2 toward the outer surface 8 to remove the separation gap 7 of the spiral separator 2 and the outside. When the solid attached and accumulated on the side surface 8 is peeled off together with the vibration by the spiral rotary plate 3, the peeling property of the solid is the best.
【0015】 なお、固体の洗浄は、分離装置1と原液の貯槽(図示せず)をポンプを付設し た配管によって連通し、貯槽に貯えた原液の一部をポンプによって螺旋状分離体 2に噴射すればよく、また空気の吹き付けは、加圧空気の貯槽(図示せず)をバ ルブを付設した配管によって連通し、貯槽に貯えた加圧空気の一部をバルブを開 いて螺旋状分離体2に空気を噴射すればよい。 また原液と空気とを同時に吹き付ける場合は、配管にエジェクターを付設し、エ ジェクターより吸引した空気を原液とともに螺旋状分離体2に吹き付けてもかま わない。 さらに分離液を螺旋状分離体2に吹き付ける場合は、分離液の分離液流出管6よ り加圧した分離液を螺旋状分離体2内に逆流状態で吹き付け、螺旋状分離体2の 分離間隙7より逆噴射させればよい。 これらの洗浄液の吹き付け速度は 1〜15m/秒の範囲であれば十分であり、空気 の吹き付け速度は 30 〜 100m/秒の範囲でかまわない。In order to wash solids, the separation device 1 and a stock solution storage tank (not shown) are connected to each other through a pipe provided with a pump, and a part of the stock solution stored in the storage tank is pumped into a spiral separator 2. Air may be blown, and a pressurized air storage tank (not shown) is connected by a pipe with a valve, and a portion of the pressurized air stored in the storage tank is opened by a valve to form a spiral separation. Air may be jetted onto the body 2. When spraying the stock solution and air at the same time, an ejector may be attached to the pipe and the air sucked from the ejector may be sprayed together with the stock solution onto the spiral separator 2. Further, when the separated liquid is sprayed onto the spiral separator 2, the separated liquid pressurized by the separated liquid outflow pipe 6 is sprayed into the spiral separator 2 in a reverse flow state to separate the separated gap of the spiral separator 2. Reverse injection from 7 is sufficient. It is sufficient that the spraying speed of these cleaning liquids is in the range of 1 to 15 m / sec, and the spraying speed of air may be in the range of 30 to 100 m / sec.
【0016】[0016]
本考案によると、種々の固液分離の目的に適合させて螺旋状分離体2の分離間 隙7を、任意の幅に簡単に設定、調整をきるので、分離容量、分離精度を格段に 向上させることが可能であり、また螺旋状分離体2に付着、蓄積する固体を、螺 旋状分離体2の振動により、あるいは加圧した原液、分離液、空気等の併用によ り、螺旋状分離体2に付着、蓄積した固体を容易に剥離、除去できるため、螺旋 状分離体2の固体による目詰りがなく、固液分離を連続して長時間行うことが可 能となるという利点もある。 また、螺旋状分離体2に固体が付着、蓄積することがないために、従来、固体 による目詰まりが発生した場合に、分離処理を中断して行っていた、装置の解体 、螺旋状分離体2よりの固体の剥離、洗浄等の時間と手間がかかる繁雑な洗浄作 業が一切不要となり、分離処理効率が飛躍的に向上し、装置のランニングコスト が安価になるメリットもある。 さらに本考案は、スパイラル状回転板3の回転によって生ずる掻き上げ作用、 サイクロン作用により、分離装置1の下部に落下、蓄積した固体を効率よく固体 流出管4へ搬出することができる。 本考案の分離装置によると、工作機械等より排出する切粉、金属粉等の懸濁物 と切削物、破砕物等の粒状物とを含むクーラント廃液よりクーラントを、また鉄 粉等の懸濁物と破砕物等の粒状物を含むエンジンオイル廃液よりエンジンオイル を、有価物として回収して再利用でき、また金属加工装置において発生する金、 プラチナ等の貴金属粉体の懸濁物と貴金属切削物、破砕物等の粒状物を含む洗浄 液より金、プラチナ等の貴金属を有価物として回収して再利用できるほか、水処 理装置の処理対象である砂、泥等の懸濁物と砂利、石等の粒状物とを含む上下水 や廃水より懸濁物、粒状物を除去して清浄な処理水を得ることができる等、その 他種々の固体と種々の液体との分離を行うことができる。 According to the present invention, the separation gap 7 of the spiral separator 2 can be easily set and adjusted to an arbitrary width in accordance with various solid-liquid separation purposes, so that the separation capacity and the separation accuracy are significantly improved. The solid that adheres to and accumulates on the spiral separator 2 can be spirally formed by the vibration of the spiral separator 2 or the combined use of pressurized stock solution, separation liquid, air and the like. Since solids that have adhered to and accumulated on the separator 2 can be easily peeled off and removed, there is also no merit that the spiral separator 2 is clogged with solids, and solid-liquid separation can be continuously performed for a long time. is there. In addition, since solids do not adhere to and accumulate on the spiral separator 2, disassembly of the apparatus and spiral separators that have been conventionally performed by interrupting the separation process when clogging by solids occurs. It eliminates the need for time-consuming and labor-intensive cleaning operations such as peeling off solids, cleaning, etc., and has the advantage of dramatically improving separation processing efficiency and lowering the running cost of the equipment. Further, according to the present invention, the solids dropped and accumulated in the lower part of the separation device 1 can be efficiently carried out to the solid outflow pipe 4 by the scraping action and the cyclone action caused by the rotation of the spiral rotary plate 3. According to the separation device of the present invention, the coolant and the iron powder etc. are suspended from the coolant waste liquid containing the suspension of cutting chips, metal powder etc. discharged from machine tools etc. and the particulate matter such as cutting materials, crushed materials etc. Engine oil can be collected as a valuable resource and reused from engine oil waste liquid containing particulate matter such as crushed material and crushed material, and a suspension of precious metal powder such as gold and platinum generated in metal processing equipment and precious metal cutting. Noble metals such as gold and platinum can be recovered as valuables from the cleaning liquid that contains particulate matter such as debris and crushed material, and can also be reused, as well as suspensions and gravel such as sand and mud that are subject to treatment by water treatment equipment. Separation of various other solids and various liquids, such as the removal of suspended solids and particulates from sewage and wastewater containing granular materials such as stones, etc. to obtain clean treated water. You can
【図1】本考案の螺旋状分離体にスパイラル状回転板を
回転可能に取り付けた状態を示す断面図である。FIG. 1 is a cross-sectional view showing a state in which a spiral rotary plate is rotatably attached to a spiral separator of the present invention.
【図2】本考案のスパイラル状回転板を回転可能に挿填
した螺旋状分離体を分離装置に設置した状態を示す断面
図である。FIG. 2 is a cross-sectional view showing a state where a spiral separator having a spiral rotary plate of the present invention rotatably inserted therein is installed in a separator.
【図3】本考案の螺旋状分離体に挿填するスパイラル状
回転板の挿入口を遍心させた状態を示す断面図である。FIG. 3 is a cross-sectional view showing a state in which an insertion opening of a spiral rotary plate to be inserted into the spiral separator of the present invention is eccentric.
1 分離装置 2 螺旋状分離体 3 スパイラル状回転板 4 固体流出管 5 原液流入管 6 固体流出管 7 分離間隙 8 外側面 1 Separation Device 2 Spiral Separator 3 Spiral Rotating Plate 4 Solid Outflow Pipe 5 Undiluted Liquid Inflow Pipe 6 Solid Outflow Pipe 7 Separation Gap 8 Outer Side
Claims (3)
を螺旋状に巻いて巻線の間に分離間隙を有する螺旋状分
離体を、上部に固体流出管を設けるとともに側部に原液
流入管を設けた分離装置の内側面と間隔をおいて設置
し、また螺旋状分離体の下端の分離液の流出口を、分離
装置の下部に設けた分離液流出管と接続し、さらに螺旋
状分離体に振動を与えるスパイラル状回転板を、螺旋状
分離体の外側面に近接させて回転可能に挿着し、固体を
含む原液を分離装置の内側面と螺旋状分離体の外側面の
間に加圧供給し、固体を螺旋状分離体の各分離間隙およ
び外側面に捕捉、分離し、スパイラル状回転板によって
固体を分離装置に設けた固体流出管へ搬出するするとと
もに、分離液を螺旋状分離体の各分離間隙より螺旋状分
離体の内部に流入させ、螺旋状分離体の流出口を経由し
て分離装置に設けた分離液流出管に集液するスパイラル
状回転板を設けた連続固液分離装置。1. A spiral separator having spirally wound elastic metal wire or synthetic resin wire or the like and having a separation gap between windings, a solid outflow pipe being provided on the upper side, and a stock solution flowing into a side part. It is installed at a distance from the inner surface of the separation device provided with a pipe, and the outlet of the separation liquid at the lower end of the spiral separator is connected to the separation liquid outflow pipe provided at the bottom of the separation device, and further spiral A spiral rotary plate that gives vibration to the separator is rotatably inserted close to the outer surface of the spiral separator so that the stock solution containing solids is between the inner surface of the separator and the outer surface of the spiral separator. The solid is trapped in each separation gap and the outer surface of the spiral separator and separated, and the solid is carried out to the solid outflow pipe provided in the separator by the spiral rotating plate, and the separated liquid is spiraled. Flow into each spiral separator through each separation gap. A continuous solid-liquid separation device provided with a spiral rotary plate that collects liquid into a separation liquid outflow pipe provided in the separation device via an outlet of the spiral separator.
状分離体に対して偏心させて螺旋状分離体に回転可能に
装填することによって、螺旋状分離体に大きな振動を与
えるスパイラル状回転板を設けた連続固液分離装置。2. The spiral rotation plate which gives a large vibration to the spiral separator by eccentrically mounting the spiral rotary plate of claim 1 on the spiral separator and rotatably loading the spiral separator. A continuous solid-liquid separator equipped with a plate.
に、加圧した原液、分離液または加圧空気あるいは両者
を吹き付け、旋状分離体の各分離間隙および外側面に付
着、蓄積する固体を短時間に剥離するスパイラル状回転
板を設けた連続固液分離装置。3. The spiral stock according to claim 1 or 2 is sprayed with a pressurized stock solution, a separation liquid, or pressurized air, or both, and adheres and accumulates in each separation gap and the outer surface of the spiral separation body. A continuous solid-liquid separation device equipped with a spiral rotating plate that separates solids in a short time.
Priority Applications (1)
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JP8368991U JP2562392Y2 (en) | 1991-09-19 | 1991-09-19 | Continuous solid-liquid separator with spiral rotating plate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP8368991U JP2562392Y2 (en) | 1991-09-19 | 1991-09-19 | Continuous solid-liquid separator with spiral rotating plate |
Publications (2)
Publication Number | Publication Date |
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JPH0526113U true JPH0526113U (en) | 1993-04-06 |
JP2562392Y2 JP2562392Y2 (en) | 1998-02-10 |
Family
ID=13809462
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JP8368991U Expired - Lifetime JP2562392Y2 (en) | 1991-09-19 | 1991-09-19 | Continuous solid-liquid separator with spiral rotating plate |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012150625A1 (en) * | 2011-05-02 | 2012-11-08 | 日本オイルポンプ株式会社 | Filter mechanism |
CN114602239A (en) * | 2022-03-31 | 2022-06-10 | 上海格氏流体设备科技有限公司 | Tangential flow intelligent filtering device for biological pharmacy |
-
1991
- 1991-09-19 JP JP8368991U patent/JP2562392Y2/en not_active Expired - Lifetime
Cited By (10)
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---|---|---|---|---|
WO2012150625A1 (en) * | 2011-05-02 | 2012-11-08 | 日本オイルポンプ株式会社 | Filter mechanism |
CN103619436A (en) * | 2011-05-02 | 2014-03-05 | 日本油泵株式会社 | Filter mechanism |
EP2705886A1 (en) * | 2011-05-02 | 2014-03-12 | Nippon Oil Pump Co., Ltd. | Filter mechanism |
EP2705886A4 (en) * | 2011-05-02 | 2014-10-22 | Nippon Oil Pump Co Ltd | Filter mechanism |
JP5757997B2 (en) * | 2011-05-02 | 2015-08-05 | 日本オイルポンプ株式会社 | Filter mechanism |
CN103619436B (en) * | 2011-05-02 | 2015-08-19 | 日本油泵株式会社 | Filter mechanism |
US10040013B2 (en) | 2011-05-02 | 2018-08-07 | Nippon Oil Pump Co., Ltd. | Filter mechanism |
US10525393B2 (en) | 2011-05-02 | 2020-01-07 | Nippon Oil Pump Co., Ltd. | Filter mechanism |
CN114602239A (en) * | 2022-03-31 | 2022-06-10 | 上海格氏流体设备科技有限公司 | Tangential flow intelligent filtering device for biological pharmacy |
CN114602239B (en) * | 2022-03-31 | 2023-12-05 | 上海格氏流体设备科技有限公司 | Tangential flow intelligent filtering device for bio-pharmaceuticals |
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JP2562392Y2 (en) | 1998-02-10 |
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