JP2014161823A5 - - Google Patents
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- JP2014161823A5 JP2014161823A5 JP2013036664A JP2013036664A JP2014161823A5 JP 2014161823 A5 JP2014161823 A5 JP 2014161823A5 JP 2013036664 A JP2013036664 A JP 2013036664A JP 2013036664 A JP2013036664 A JP 2013036664A JP 2014161823 A5 JP2014161823 A5 JP 2014161823A5
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- tank
- raw water
- precipitation filtration
- precipitated
- 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.)
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- 239000010802 sludge Substances 0.000 claims description 18
- 238000001914 filtration Methods 0.000 claims description 9
- 238000001556 precipitation Methods 0.000 claims description 7
- 238000000746 purification Methods 0.000 claims description 4
- 238000004062 sedimentation Methods 0.000 claims description 2
- 239000002244 precipitate Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 238000005192 partition Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Description
<浄化装置200の全体構成>
図1は、本発明の実施形態における浄化装置200の全体構成図である。浄化装置200は、原水を貯留する原水池300の原水中の汚泥を除去することにより原水池300の浄化を行う浄化装置であって、ゼオライト系の凝集剤粉末を連続的に投入可能な凝集剤投入機10、凝集剤粉末が投下された原水を渦流で攪拌する第1の攪拌機20、内壁への衝突による再攪拌を行う第2の攪拌機30、第1の攪拌機20による攪拌後の原水を一時貯留する揚水タンク40、2段階の沈殿濾過を行う第1の沈殿濾過槽50及び第2の沈殿濾過槽60を含む。
<Overall configuration of purification device 200>
Figure 1 is an overall configuration diagram of a purifying apparatus 200 according to an embodiment of the present invention. The purification device 200 is a purification device that purifies the raw water pond 300 by removing sludge in the raw water of the raw water pond 300 that stores the raw water, and is a flocculant capable of continuously adding zeolite-based flocculant powder. The feeder 10, the first stirrer 20 that stirs the raw water on which the flocculant powder has been dropped by vortex, the second stirrer 30 that performs re-stirring by collision with the inner wall, and the raw water that has been stirred by the first stirrer 20 temporarily A pumping tank 40 to be stored, a first precipitation filtration tank 50 that performs two-stage precipitation filtration, and a second precipitation filtration tank 60 are included.
第1の沈殿濾過槽50は、その上壁から底部の上方まで延びた隔壁51によって仕切られており、第2の攪拌機30から第1の沈殿濾過槽50内に落下した水は隔壁51を回り込んで、隔壁51の左側の空間に設けられた濾過層52を下から上に通過するようになっている。これにより、原水は、濾過層52で濾過されるとともに、原水に含まれた汚泥53が第1の沈殿濾過槽50の底部に沈殿する。沈殿した汚泥53は第1の沈殿濾過槽50の底に接続された汚泥管54を通して汚泥タンク70に送られる。汚泥タンク70の底部71には汚泥53が貯まるが、上澄み水は配管72を通して揚水タンク40に戻される。 The first precipitation filtration tank 50 is partitioned by a partition wall 51 extending from the upper wall to the upper part of the bottom, and the water that has fallen into the first precipitation filtration tank 50 from the second stirrer 30 passes around the partition wall 51. The filter layer 52 provided in the space on the left side of the partition wall 51 is passed from the bottom to the top. As a result, the raw water is filtered by the filtration layer 52 and the sludge 53 contained in the raw water is precipitated at the bottom of the first precipitation filtration tank 50. The sedimented sludge 53 is sent to the sludge tank 70 through a sludge pipe 54 connected to the bottom of the first sedimentation filtration tank 50. Sludge 53 is stored in the bottom 71 of the sludge tank 70, but the supernatant water is returned to the pumped tank 40 through the pipe 72.
そして、脱水筒98内に汚泥コンベア80から汚泥53が搬入されて、基台97の上動により脱水蓋94で汚泥が垂直方向に圧縮されることにより、汚泥53の水分が排水管96から排出されるように構成されている。排水管96から排出された水は、排水管96を通して原水池300に戻されることが好ましい。脱水されて粉末化した汚泥53は小形軽量化されていることから袋などに詰め込んだ状態で運搬するのに適しており、脱水筒98から取り出され、廃棄場所や仮置き場に運搬される。 Then, the sludge 53 is carried into the dewatering cylinder 98 from the sludge conveyor 80, and the sludge is vertically compressed by the dewatering lid 94 by the upward movement of the base 97 , whereby the moisture of the sludge 53 is discharged from the drain pipe 96. It is configured to be. The water discharged from the drain pipe 96 is preferably returned to the raw water basin 300 through the drain pipe 96. The dewatered and powdered sludge 53 is suitable for transporting in a state of being packed in a bag or the like because it is reduced in size and weight, and is taken out from the dewatering cylinder 98 and transported to a disposal place or a temporary storage place.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2013036664A JP6083737B2 (en) | 2013-02-27 | 2013-02-27 | Purification device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2013036664A JP6083737B2 (en) | 2013-02-27 | 2013-02-27 | Purification device |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2014161823A JP2014161823A (en) | 2014-09-08 |
JP2014161823A5 true JP2014161823A5 (en) | 2016-04-21 |
JP6083737B2 JP6083737B2 (en) | 2017-02-22 |
Family
ID=51612973
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2013036664A Expired - Fee Related JP6083737B2 (en) | 2013-02-27 | 2013-02-27 | Purification device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP6083737B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104787926B (en) * | 2015-03-30 | 2017-02-08 | 盛大环境工程有限公司 | Sewage treatment system and sewage treatment method |
CN106390538A (en) * | 2016-09-27 | 2017-02-15 | 符放中 | Livestock farm liquid manure treatment method and device |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5316047Y2 (en) * | 1974-04-25 | 1978-04-27 | ||
JPS539043A (en) * | 1976-07-14 | 1978-01-27 | Kurita Water Ind Ltd | Process for dissolving and supplying powder medicine |
JPS6028524B2 (en) * | 1977-11-18 | 1985-07-05 | 日本錬水株式会社 | water treatment equipment |
JPS5738908A (en) * | 1980-08-18 | 1982-03-03 | Gadelius Kk | Treating device for waste water from iron making |
JPS60156537A (en) * | 1984-01-27 | 1985-08-16 | Mitsui Toatsu Chem Inc | Stirring method of liquid in tank |
JPH0335363Y2 (en) * | 1985-07-22 | 1991-07-26 | ||
JPH11253705A (en) * | 1998-03-06 | 1999-09-21 | Kotobuki Giken Kogyo Kk | Solid-liquid separation method and apparatus for watercontaining solid matter |
JP2001026650A (en) * | 1999-07-15 | 2001-01-30 | Kobayashi Eng Works Ltd | Continuous dissolving apparatus for polymer |
JP2001224907A (en) * | 2000-02-18 | 2001-08-21 | Toshikazu Shimodaira | Advanced treatment-correspondent flocculating, settling and rapid filtering device |
JP3859074B2 (en) * | 2002-07-18 | 2006-12-20 | 株式会社真和溶接 | Purification device |
JP2004050014A (en) * | 2002-07-18 | 2004-02-19 | Shinwa Yosetsu:Kk | Flocculant feeder and stirrer |
JP2004243256A (en) * | 2003-02-17 | 2004-09-02 | Hitachi Plant Eng & Constr Co Ltd | Water purification processing method |
JP2005095867A (en) * | 2003-08-20 | 2005-04-14 | Suzuki Sangyo Kk | Water purifying treatment system |
JP4651052B2 (en) * | 2008-01-29 | 2011-03-16 | アタカ大機株式会社 | Sludge separation apparatus and sludge separation method |
-
2013
- 2013-02-27 JP JP2013036664A patent/JP6083737B2/en not_active Expired - Fee Related
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