JPH05111698A - Rice washing waste water disposal equipment - Google Patents

Rice washing waste water disposal equipment

Info

Publication number
JPH05111698A
JPH05111698A JP3305395A JP30539591A JPH05111698A JP H05111698 A JPH05111698 A JP H05111698A JP 3305395 A JP3305395 A JP 3305395A JP 30539591 A JP30539591 A JP 30539591A JP H05111698 A JPH05111698 A JP H05111698A
Authority
JP
Japan
Prior art keywords
tank
water
sludge
rice
rice washing
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
JP3305395A
Other languages
Japanese (ja)
Inventor
Toshihiko Satake
利彦 佐竹
Satoru Satake
覚 佐竹
Katsuyuki Kumamoto
勝行 熊本
Yuichi Ozaki
雄一 尾崎
Kou Shimodera
香 下寺
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.)
Satake Engineering Co Ltd
Original Assignee
Satake Engineering Co 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 Satake Engineering Co Ltd filed Critical Satake Engineering Co Ltd
Priority to JP3305395A priority Critical patent/JPH05111698A/en
Publication of JPH05111698A publication Critical patent/JPH05111698A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Fodder In General (AREA)
  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

PURPOSE:To dry dehydrated sludge and to reutilize it for feed and manure. CONSTITUTION:A sludge drier 104 for drying dehydrated sludge by dry wind is provided in the rear stage of a dehydrator 96 in a rice washing waste water disposal equipment 67 which is constituted of a precipitation device 75, biological treatment devices 83, 84 and the dehydrator 96.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、米粒を洗米することに
より発生する廃水を処理する洗米廃水処理装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a rice washing wastewater treatment apparatus for treating wastewater generated by washing rice grains.

【0002】[0002]

【従来の技術】大規模炊飯工場または酒造工場で生じる
洗米廃水には大量の糖類、蛋白質などが含まれており、
そのまま放流すると河川が高栄養化により汚染されてし
まう。そこで、活性汚泥菌や酵母菌を利用して洗米廃水
処理を行う方法が知られており、その廃水処理におい
て、発生する沈殿物は脱水機により脱水されて脱水ケー
キが形成される。
2. Description of the Related Art A large amount of sugars, proteins, etc. are contained in rice washing wastewater generated in a large-scale rice cooking factory or a brewing factory,
If it is discharged as it is, the river will be polluted due to high nutrition. Therefore, a method is known in which activated sludge fungus or yeast is used to perform a washing wastewater treatment. In the wastewater treatment, a precipitate generated is dehydrated by a dehydrator to form a dehydrated cake.

【0003】[0003]

【発明が解決しようとする課題】脱水機で形成された脱
水汚泥は、焼却されるか産業廃棄物として処理されて、
ほとんど再利用されていなかった。この発明は、従来、
再利用されていなかった洗米廃水処理装置で形成される
脱水汚泥を、効率的に乾燥処理を行うことにより飼料や
肥料に再利用可能とする洗米廃水処理装置を提供するこ
とを目的とする。
The dehydrated sludge formed by the dehydrator is incinerated or treated as industrial waste,
It was hardly reused. This invention is
It is an object of the present invention to provide a rice washing wastewater treatment device that can reuse dehydrated sludge formed in a rice washing wastewater treatment device that has not been reused as feed or fertilizer by efficiently performing a drying process.

【0004】[0004]

【課題を解決するための手段】洗米廃水を沈殿物と液体
とに分離する沈殿装置と、前記液体を活性汚泥菌または
酵母菌により生物処理する生物処理装置と、前記沈殿物
を脱水して脱水汚泥に形成する脱水装置とからなる洗米
廃水処理装置において、前記脱水汚泥を乾燥風により乾
燥する汚泥乾燥装置を、前記脱水装置の後工程に設け
る。
[Means for Solving the Problems] A settling device for separating washed rice sewage into a precipitate and a liquid, a biological treatment device for biologically treating the liquid with activated sludge fungus or yeast, and dehydration by dehydrating the precipitate. In a rice washing wastewater treatment device comprising a dehydrator for forming sludge, a sludge drying device for drying the dehydrated sludge with a drying air is provided in a subsequent step of the dehydrator.

【0005】[0005]

【作用】洗米廃水は沈殿装置により沈殿物と液体とに分
離され、液体は生物処理装置に送られて活性汚泥菌また
は酵母菌により生物処理され、沈殿物は脱水装置に送ら
れて脱水汚泥に形成されり、脱水汚泥は汚泥乾燥装置に
おくられ、乾燥風により乾燥されて所定水分の汚泥に処
理される。
[Function] The rice rinsing wastewater is separated into a sediment and a liquid by a sedimentation device, the liquid is sent to a biological treatment device for biological treatment by activated sludge fungus or yeast, and the sediment is sent to a dehydrator to be dehydrated sludge. The formed and dehydrated sludge is placed in a sludge drying device, dried by a drying air, and processed into sludge having a predetermined water content.

【0006】[0006]

【実施例】本発明の実施例を図面を参照しながら説明す
る。図1は本発明を実施した洗米廃水処理装置のフロー
チャート、図2は洗米加工装置のフローチャート、図3
は撹拌乾燥機の部分側断面図、図4は汚泥乾燥機の側面
図である。
Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a flow chart of a rice washing wastewater treatment apparatus according to the present invention, FIG. 2 is a flow chart of a rice washing processing apparatus, and FIG.
Is a partial side sectional view of the agitation dryer, and FIG. 4 is a side view of the sludge dryer.

【0007】洗米加工装置1の供給ホッパ2をロータリ
ーバルブ3を介して混合タンク4に連絡し、5は混合タ
ンク4内の水を常に一定レベルに保つレベル計である。
混合タンク4はポンプ6,7,8及び切換弁9,10か
らなる洗米機11を介して洗米脱水機12の供給管13
に連絡している。なお、洗米機は本実施例のものに限ら
れず、撹拌作用により洗米を行う等種々のものでよい。
A supply hopper 2 of the rice washing processing apparatus 1 is connected to a mixing tank 4 via a rotary valve 3, and 5 is a level meter for keeping the water in the mixing tank 4 at a constant level.
The mixing tank 4 is provided with a supply pipe 13 of a rice washer / dewaterer 12 via a rice washer 11 including pumps 6, 7, 8 and switching valves 9, 10.
Have been contacted. The rice washing machine is not limited to the one used in this embodiment, and may be any of various types such as washing rice by stirring.

【0008】次に洗米脱水機12を図3を参照しながら
説明する。洗米脱水機12の架台14の一側壁にモータ
15を取付け、モータ15に軸装したプーリ16はベル
ト17を介して、主軸18に軸装したプーリ19に連結
する。プーリ20はベルト21を介して中空状の回転軸
22のプーリ23に連結し、24はテンションプーリで
ある。主軸18は連結軸25を介して撹拌体26に連結
し、撹拌体26に取付けた連結体27は洗米筒28に連
結する。29は洗米室であり、洗米筒28の外周に揚送
用の螺旋翼30を取付け、洗米筒28と螺旋翼29を包
囲する多孔壁筒31とで脱水室32を形成する。多孔壁
筒31は回転台33を介して回転軸22に連結し、螺旋
翼30の上端は排出口34を介して排出樋35に連絡す
る。洗米筒28に設けたノズル36を脱水室32に臨ま
せ、ノズル36は貯水室37、通口38、給水路39を
介して給水管40に連絡し、また41は供給管13と洗
米室29とを連絡する供給路である。42は脱水した水
を集めて排出する排出口であり、排出口42は、排出筒
43、電磁弁44を介してポンプ45に連絡している。
排出樋35に連結した排出筒46にエアーシャッタ47
を設け、排出筒46の下部を水滴が落下する程度の多孔
壁に形成する。
Next, the rice washing and dehydrating machine 12 will be described with reference to FIG. A motor 15 is attached to one side wall of a pedestal 14 of the rice washer / dewaterer 12, and a pulley 16 mounted on the motor 15 is connected to a pulley 19 mounted on a main shaft 18 via a belt 17. The pulley 20 is connected to a pulley 23 of a hollow rotary shaft 22 via a belt 21, and 24 is a tension pulley. The main shaft 18 is connected to a stirring body 26 via a connecting shaft 25, and a connecting body 27 attached to the stirring body 26 is connected to a rice washing cylinder 28. 29 is a rice washing chamber. A spiral blade 30 for lifting is attached to the outer periphery of the rice washing cylinder 28, and a dehydration chamber 32 is formed by the rice washing cylinder 28 and a perforated wall cylinder 31 surrounding the spiral blade 29. The perforated wall cylinder 31 is connected to the rotary shaft 22 via a rotary table 33, and the upper end of the spiral blade 30 communicates with a discharge gutter 35 via a discharge port 34. A nozzle 36 provided on the rice washing cylinder 28 faces the dehydration chamber 32, the nozzle 36 communicates with a water supply pipe 40 through a water storage chamber 37, a through hole 38, and a water supply passage 39, and 41 indicates a supply pipe 13 and a rice washing chamber 29. It is a supply route to communicate with. 42 is a discharge port for collecting and discharging dehydrated water, and the discharge port 42 communicates with a pump 45 via a discharge cylinder 43 and a solenoid valve 44.
An air shutter 47 is attached to a discharge tube 46 connected to the discharge gutter 35.
Is provided, and the lower portion of the discharge tube 46 is formed as a porous wall to which water droplets fall.

【0009】洗米脱水機12の排出筒46を、撹拌乾燥
機58の供給タンク48に連絡する。撹拌乾燥機58の
横設した多孔壁筒49内に回転自在に設けた主軸50に
撹拌転子51を軸装し、主軸50に複数個の通風口52
を撹拌転子51に噴風口53をそれぞれ設ける。撹拌転
子51と多孔壁筒49とで乾燥室54を形成し、主軸5
0の一端は、送風管55、送風機56を介して熱風発生
機57に連絡し、また、撹拌乾燥機58の排出樋59を
揚穀機60に連絡する。
The discharge cylinder 46 of the rice washing / drying machine 12 is connected to the supply tank 48 of the stirring / drying machine 58. A stirring rotator 51 is rotatably mounted on a main shaft 50 rotatably provided in a perforated wall cylinder 49 provided side by side in a stirring dryer 58, and the main shaft 50 has a plurality of ventilation ports 52.
The stirrer 51 is provided with a jet port 53. The stirring chamber 51 and the perforated wall cylinder 49 form a drying chamber 54, and the main shaft 5
One end of 0 connects to the hot air generator 57 via the blower pipe 55 and the blower 56, and also connects the discharge gutter 59 of the stirring dryer 58 to the grain elevator 60.

【0010】61,62は貯水タンクであり、タンク6
1,62は切換弁63を介して水の供給装置(図示せ
ず)に連絡するとともに、切換弁64を介して洗米脱水
機12に連絡し、切換弁65,66は一方を混合タンク
4に、他方を洗米廃水処理装置67の原水槽68に連絡
している。また、69は水の濃度を測定する濃度測定装
置である。
Reference numerals 61 and 62 are water storage tanks, and the tank 6
1, 62 are connected to a water supply device (not shown) via a switching valve 63, and are connected to the washing and dehydrating machine 12 via a switching valve 64, and one of the switching valves 65 and 66 is connected to the mixing tank 4. The other is connected to the raw water tank 68 of the rice washing wastewater treatment device 67. Further, 69 is a concentration measuring device for measuring the concentration of water.

【0011】次に、洗米水処理装置67を図2を参照し
て説明する。なお、図2に示す洗米廃水処理装置67
は、洗米廃水を活性汚泥処理して、清浄水を下水道へ放
流する方式である。原水槽68は一定濃度に達した洗米
廃水を一時的に貯留する槽であり、原水槽68は原水計
量槽70を介して凝集反応槽71,72に連絡してい
る。凝集反応槽71は凝集剤槽73に、凝集反応槽72
は凝集剤槽74にそれぞれ連絡し、凝集剤槽73には5
%濃度の塩化カルシウムが貯留され、凝集剤槽74には
0.05%濃度のアルギン酸ナトリウムが貯留されてい
る。
Next, the rice washing water treatment device 67 will be described with reference to FIG. In addition, the rice washing wastewater treatment device 67 shown in FIG.
Is a method in which the waste water from washing rice is treated with activated sludge and the clean water is discharged to the sewer. The raw water tank 68 is a tank for temporarily storing the washing water having a certain concentration, and the raw water tank 68 communicates with the aggregating reaction tanks 71 and 72 via a raw water measuring tank 70. The flocculation reaction tank 71 is a flocculation agent tank 73, and the flocculation reaction tank 72 is
Contact the flocculant tank 74, and
% Calcium chloride is stored, and coagulant bath 74 stores 0.05% sodium alginate.

【0012】凝集反応槽71,72は凝集沈殿槽75を
介して原水調整槽76に連絡し、77は原水調整槽76
の原水(一次処理水)をPH調整槽78へ揚送するポン
プであり、79,80は原水調整槽76の水位を検知す
る水位計である。PH調整槽78はカセイソーダを貯留
した中和剤槽81に連絡し、PH調整槽78は計量槽8
2を介して曝気槽83に連絡している。曝気槽83と曝
気槽84とは開口85を設けた仕切壁86により仕切ら
れ、原水調整槽76、曝気槽83,84内に設けた散気
管87,88,89は送風機90に連絡し、曝気槽8
3,84にヒータ91を設ける。
The coagulation reaction tanks 71 and 72 are connected to a raw water adjusting tank 76 via a coagulating sedimentation tank 75, and 77 is a raw water adjusting tank 76.
Is a pump for pumping the raw water (primary treated water) to the PH adjusting tank 78, and 79 and 80 are water level gauges for detecting the water level of the raw water adjusting tank 76. The pH adjusting tank 78 communicates with the neutralizing agent tank 81 storing caustic soda, and the PH adjusting tank 78 is the measuring tank 8
It communicates with the aeration tank 83 via 2. The aeration tank 83 and the aeration tank 84 are partitioned by a partition wall 86 having an opening 85, and the raw water adjusting tank 76 and the air diffusers 87, 88, 89 provided in the aeration tanks 83, 84 communicate with the blower 90 to perform aeration. Tank 8
A heater 91 is provided at 3, 84.

【0013】曝気槽84は、曝気水を固液分離する沈殿
槽92に連絡し、沈殿槽75,92はポンプ93を介し
て、活性汚泥の余剰汚泥を一時貯留する汚泥調整槽94
に連絡している。活性汚泥槽94は凝集反応槽95を介
して脱水機96に連絡し、凝集反応槽95に凝集剤(ケ
イ藻土)を貯留した凝集剤槽97を連絡する。脱水機9
6は回転自在に装設した塗布98と、汚泥を脱水ケーキ
に圧縮するローラ99とからなる。100は沈殿槽92
からの処理水(清浄水)を一時貯留する処理水槽であ
り、この処理水は脱水機96の濾布98の洗浄水として
使用され、洗浄水は濾液槽101に一時貯留されてから
原水調整槽76に戻される。
The aeration tank 84 communicates with a settling tank 92 for solid-liquid separation of the aerated water, and the settling tanks 75 and 92, via a pump 93, temporarily store excess sludge of activated sludge.
Have been contacted. The activated sludge tank 94 communicates with the dehydrator 96 via the coagulation reaction tank 95, and connects with the coagulation agent tank 97 in which the coagulant (diatomaceous earth) is stored. Dehydrator 9
Reference numeral 6 includes a coating 98 that is rotatably mounted and a roller 99 that compresses sludge into dehydrated cake. 100 is a settling tank 92
Is a treated water tank for temporarily storing treated water (clean water) from the above, this treated water is used as washing water for the filter cloth 98 of the dehydrator 96, and the washing water is temporarily stored in the filtrate tank 101 and then the raw water adjusting tank Returned to 76.

【0014】脱水機96のローラ99を汚泥乾燥機10
4の供給樋105に連絡し、汚泥乾燥機104はケーシ
ング106内に多孔壁回転筒107を回転自在に装架
し、多孔壁回転筒107の内壁に螺旋翼108を周設す
る。多孔壁回転筒107内に、下方を給気口109に開
口した給気装置110を臨ませ、給気筒111は灯油ま
たはガスの燃焼機(図示せず)に連絡している。多孔壁
回転筒107の排出端を排出樋112に臨ませ、ケーシ
ング106下部に取付けた排気筒113を吸引機(図示
せず)に連絡する。
The roller 99 of the dehydrator 96 is replaced by the sludge dryer 10.
The sludge dryer 104 rotatably mounts the perforated wall rotary cylinder 107 in the casing 106, and the spiral blade 108 is provided around the inner wall of the perforated wall rotary cylinder 107. An air supply device 110 whose lower side is opened to an air supply port 109 is faced in the multi-walled rotary cylinder 107, and a supply cylinder 111 is connected to a kerosene or gas combustor (not shown). The discharge end of the perforated wall rotary cylinder 107 faces the discharge gutter 112, and the exhaust cylinder 113 attached to the lower portion of the casing 106 is connected to a suction device (not shown).

【0015】次に上記構成における作用を説明する。水
の供給装置(図示せず)から切換弁63を介して貯水タ
ンク61に水が供給され、貯水タンク61の水は切換弁
65を介して混合タンク4に注水される。混合タンク4
内に一定のレベルの水が貯留されると、供給ホッパ2内
の白米がロータリバルブ3により間歇排出され、混合タ
ンク4内に投入されて水と混合される。白米は洗米機1
1のポンプ6,7,8により予備洗米されるが、白米の
種類に対応して制御装置(図示せず)の調節によりポン
プの通過回数を変更する。つまり、新米のように比較的
洗米の容易な白米はポンプ6のみを通過させ、切換弁9
を切換えて洗米脱水機12に供給する。また古米のよう
に洗米のしずらい白米は、ポンプ6,7を通過させ、切
換弁10を切換えて洗米脱水機12に供給するか、古々
米のようにさらに洗米のしずらい白米は、ポンプ6,
7,8すべてを通過させて洗米脱水機12に供給する。
Next, the operation of the above configuration will be described. Water is supplied from a water supply device (not shown) to the water storage tank 61 via the switching valve 63, and the water in the water storage tank 61 is poured into the mixing tank 4 via the switching valve 65. Mixing tank 4
When a certain level of water is stored therein, the white rice in the supply hopper 2 is intermittently discharged by the rotary valve 3 and put into the mixing tank 4 to be mixed with water. White rice is a rice washing machine 1
Although the rice is pre-washed by the pumps 6, 7, and 8 of No. 1, the number of passages of the pump is changed by adjusting the control device (not shown) according to the type of white rice. In other words, white rice, which is relatively easy to wash like fresh rice, passes only the pump 6 and the switching valve 9
Is switched to supply to the washing and dehydrating machine 12. In addition, if it is difficult to wash rice like old rice, pass pumps 6 and 7 and switch the switching valve 10 to supply it to the rice washing dehydrator 12. , Pump 6,
All of them are passed through and supplied to the washing and dehydrating machine 12.

【0016】洗米脱水機12へ送られた白米は、供給管
13から供給路41を経て洗米室29に供給される。モ
ーター15の起動により洗米筒28は毎分約1,500 〜2,
000回転に回転しており、その回転により撹拌体26が
回転して、洗米室29に供給された白米は洗米作用を受
ける。その洗米作用により白米に残存する糠層が分離し
て溶出し、洗米された白米は螺旋翼30により脱水室3
3内を揚送される。そのとき、洗米筒28より約100 回
転遅く回転する多孔壁筒31により脱水作用が行なわ
れ、白米より溶出した糠を含む水は多孔壁筒31の孔よ
り排出される。脱水室32において、まずその下部で初
期脱水が行われ、次に、脱水室32に臨ませたノズル3
6からの注水により白米は再洗米されて、白米表面に残
存する糠等の付着物が除去され、再洗米された白米は揚
送されて再脱水される。そして排出された洗米排水は排
出口42に集められ、排出筒43を流下して電磁弁44
の開成とポンプ45の作動により機外へ排出される。そ
して、その洗米排水は切換弁79を経て貯水タンク76
へ送られ、切換弁80を経て再び混合タンク4に供給さ
れて循環される。また、洗米終了後、洗米脱水機12を
洗浄するときは、エアーシャッタ47を閉成して後工程
に水が流れないようにしてから水を供給して行う。
The white rice sent to the rice washing and dehydrating machine 12 is supplied from the supply pipe 13 to the rice washing chamber 29 through the supply passage 41. When the motor 15 is activated, the rice washing cylinder 28 is about 1,500 to 2,
It rotates at 000 rotations, and the stirring body 26 rotates by the rotation, and the white rice supplied to the rice washing chamber 29 receives the rice washing action. By the washing action, the bran layer remaining in the white rice is separated and eluted, and the washed white rice is removed by the spiral blade 30 in the dehydration chamber 3
3 is pumped. At that time, the perforated wall cylinder 31 rotating about 100 rotations slower than the rice washing cylinder 28 performs a dehydration action, and the water containing the bran eluted from the white rice is discharged from the hole of the perforated wall cylinder 31. In the dehydration chamber 32, the initial dehydration is first performed in the lower part thereof, and then the nozzle 3 facing the dehydration chamber 32.
The white rice is rewashed by pouring water from No. 6, the adhering substances such as bran remaining on the surface of the white rice are removed, and the rewashed white rice is pumped and re-dehydrated. Then, the discharged waste water of washed rice is collected in the discharge port 42, flows down the discharge cylinder 43, and flows through the solenoid valve 44.
Is discharged and the pump 45 is operated to discharge it to the outside of the machine. Then, the drainage of the washed rice passes through the switching valve 79 and the water storage tank 76.
Is sent to the mixing tank 4 again via the switching valve 80 and circulated. After washing the rice, when washing the rice washing dehydrator 12, the air shutter 47 is closed to prevent the water from flowing to the subsequent steps, and then the water is supplied.

【0017】脱水された白米は螺旋翼30により揚送さ
れて排出口35から排出され、排出樋35から排出筒4
6を流下して撹拌乾燥機58の供給タンク48に投入さ
れる。供給タンク48に投入された白米は、乾燥室54
において、撹拌転子51の回転(周速度 100〜 300m/
分)による撹拌作用により、白米は粒々摩擦されて米粒
表面が滑面化される。
The dewatered white rice is pumped by the spiral blade 30 and discharged from the discharge port 35, and from the discharge gutter 35 to the discharge cylinder 4.
6 is made to flow down and is put into the supply tank 48 of the stirring dryer 58. The white rice put in the supply tank 48 is stored in the drying chamber 54.
Rotation of the stirring rotator 51 (peripheral speed 100 to 300 m /
By the stirring action of (minute), the polished rice is rubbed into particles and the surface of the rice grains is made smooth.

【0018】外気は熱風発生機57により加熱されて熱
風(60℃以下)となり、送風機56により送風管55,
53を経て中空状の主軸50に送られる。熱風は主軸5
0の通風口52を経て噴風口53から乾燥室54へ噴出
し、乾燥室54内を撹拌流動されながら横送される白米
(滞留時間は 5〜10秒)に付着する水分を乾燥する。乾
燥の終了した白米は、排出樋59から揚穀機60を経て
次工程へ送られる。
The outside air is heated by the hot air generator 57 to become hot air (60 ° C. or less), and the air blower 56 blows air into the blow pipes 55,
It is sent to the hollow main shaft 50 via 53. Hot air is the main shaft 5
The water adhering to the white rice (residence time is 5 to 10 seconds) jetted from the air outlet 53 to the drying chamber 54 through the 0 ventilation port 52 and agitated and flowed in the drying chamber 54 is dried. The dried white rice is sent from the discharge gutter 59 through the grain elevator 60 to the next step.

【0019】洗米脱水機12での洗米に使用された水
は、貯水タンク61に戻されて再循環されるが、BOD
(生物化学的酸素要求量)が約8,000PPM程度に達
すると(それは、濃度測定装置69により水の濃度を測
定することにより判断される。)、切換弁65を切換え
て洗米廃水処理装置67の原水槽68へ送られる。その
とき、切換弁63が切換えられて水の供給装置(図示せ
ず)から貯水タンク62に水が供給され、切換弁66を
介して混合タンク4へ送られて、同様にBODが約8,
000PPM に達するまで循環される。BODが約8,0
00PPM に達すると切換弁66が切換えられて、水は原
水槽68へ送られ、そのとき切換弁63の切換えによ
り、貯水タンク61に洗米用の水が供給される。
The water used for washing rice in the rice washing and dehydrating machine 12 is returned to the water storage tank 61 and is recirculated.
When the (biochemical oxygen demand) reaches about 8,000 PPM (which is judged by measuring the concentration of water by the concentration measuring device 69), the changeover valve 65 is changed over to the rice washing wastewater treatment device 67. Sent to the raw water tank 68. At that time, the switching valve 63 is switched, water is supplied from the water supply device (not shown) to the water storage tank 62, and the water is sent to the mixing tank 4 through the switching valve 66. Similarly, the BOD is about 8,
It is circulated until it reaches 000PPM. BOD is about 8.0
When the pressure reaches 00 PPM, the switching valve 66 is switched and the water is sent to the raw water tank 68. At this time, by switching the switching valve 63, water for washing rice is supplied to the water storage tank 61.

【0020】原水槽68の洗米廃水は原水計量槽70へ
送られ、原水計量槽70で計量(流量1.25m3 /
時)されてから凝集反応槽71へ供給され、余分な洗米
廃水は原水槽68へ戻される。凝集反応槽71内の洗米
廃水に、凝集剤槽73から塩化カルシウムが供給されて
凝集反応が行われる。塩化カルシウム(300PPM 以
上)の添加により、フロックの凝集が促進されてフロッ
ク回収率が向上される。洗米廃水は凝集反応槽71から
凝集反応槽72へ送られ、凝集剤槽74から供給される
アルギン酸ナトリウム(3PPM )により同様に凝集反応
が行われる。なお、凝集反応槽71,72における洗米
廃水の滞留時間は約10〜15分間である。凝集反応が
行われた洗米廃水は、凝集沈殿槽75へ送られて沈降分
離され、沈殿物(スラッジ=汚泥)はタイマーにより定
期的にポンプ93により汚泥調整槽94に送られ、上澄
水(BODは約2,000PPM 以下)は凝集沈殿槽75
からオーバーフローして原水調整槽76へ送られる。な
お、凝集沈殿槽85における洗米廃水の滞留時間は約
2.5〜3時間程度であり、タイマーの設定時間以上に
沈殿物が堆積すると、スラッジセンサ111の検知によ
りポンプ93が作動して、沈殿物が汚泥調整槽94へ送
られる。
Waste rice washing water in the raw water tank 68 is sent to the raw water measuring tank 70, and is measured in the raw water measuring tank 70 (flow rate 1.25 m3 /
After that, it is supplied to the flocculation reaction tank 71, and excess waste water for washing rice is returned to the raw water tank 68. Calcium chloride is supplied from the flocculant tank 73 to the rice washing wastewater in the flocculation reaction tank 71 to cause the flocculation reaction. Addition of calcium chloride (300 PPM or more) promotes floc aggregation and improves floc recovery rate. The rice washing wastewater is sent from the flocculation reaction tank 71 to the flocculation reaction tank 72, and the flocculation reaction is similarly performed with sodium alginate (3 PPM) supplied from the flocculation agent tank 74. In addition, the residence time of the rice rinsing wastewater in the flocculation reaction tanks 71 and 72 is about 10 to 15 minutes. The rice rinsing wastewater that has undergone the flocculation reaction is sent to a flocculation sedimentation tank 75 for sedimentation and separation, and the sediment (sludge = sludge) is periodically sent by a timer to a sludge adjusting tank 94 by a pump 93 and the supernatant water (BOD). Is about 2,000 PPM or less) is a coagulating sedimentation tank 75
Overflows and is sent to the raw water adjusting tank 76. In addition, the residence time of the rice washing wastewater in the coagulation sedimentation tank 85 is approximately 2.5 to 3 hours, and when the sediment is accumulated for a time longer than the set time of the timer, the pump 93 is activated by the detection of the sludge sensor 111 to cause the sedimentation. The product is sent to the sludge adjusting tank 94.

【0021】原水調整槽76(容量7.5m3 )は、
曝気槽88,89での活性汚泥菌の処理能力が低下する
のを防止するための中間調整槽であり、送風機90から
散気管87へ送られる空気(空気量50m3 /時)に
より曝気撹拌を行い、水質の均一化をはかっている。原
水調整槽76内の水位計79が原水を検知すると、原水
調整槽76以降の二次処理工程(凝集沈殿槽75以前を
一次処理工程とする)が作動し、水位計80が原水を検
知すると一次処理工程の停止及び異常警報が発せられ
る。水位計79の検知によりポンプ77が作動して所定
水量の原水(一次処理水)がPH調整槽78へ送られ、
PH調整槽78において曝気槽88,89へ供給される
一次処理水のPH値を所定範囲(6.8〜7.5)内に
自動調節される。つまり、PH計101で一次処理水の
PH値が常に測定され、PH指示調整計(図示せず)に
おける設定値(例えば設定値を7とする)以下となる
と、中和剤槽81内のカセイソータがPH調整槽78へ
供給されてPH値が所定範囲に修正される。
The raw water adjusting tank 76 (capacity 7.5 m3) is
It is an intermediate adjustment tank to prevent the treatment capacity of activated sludge bacteria in the aeration tanks 88 and 89 from decreasing, and aeration and stirring is performed by the air (air amount 50 m3 / hour) sent from the blower 90 to the air diffuser 87. , We are trying to make the water quality uniform. When the water level meter 79 in the raw water adjusting tank 76 detects the raw water, the secondary treatment process after the raw water adjusting tank 76 (the pre-aggregation sedimentation tank 75 is the primary treatment process) is activated, and the water level indicator 80 detects the raw water. The primary processing process is stopped and an alarm is issued. The pump 77 is activated by the detection of the water level indicator 79, and a predetermined amount of raw water (primary treated water) is sent to the PH adjusting tank 78,
In the pH adjusting tank 78, the PH value of the primary treated water supplied to the aeration tanks 88 and 89 is automatically adjusted within a predetermined range (6.8 to 7.5). That is, when the PH value of the primary treated water is constantly measured by the PH meter 101 and becomes less than or equal to the set value (for example, the set value is 7) in the PH indicator adjuster (not shown), the caustic sorter in the neutralizer tank 81. Is supplied to the pH adjusting tank 78, and the PH value is corrected within a predetermined range.

【0022】一次処理水は所定範囲のPH値に調整され
てから計量槽82を経て曝気槽88へ供給され、曝気槽
88に供給された活性汚泥菌と流入原水(一次処理水)
とが、送風機90から散気管88へ送られる空気(空気
量50m3 /時)により曝気混合される。原水中の有
機物は活性汚泥菌により消化され、一次処理水が浄水化
されるとともに沈降性のよい安定した汚泥に処理され
る。曝気槽88の一次処理水は曝気槽89に送られて、
送風機90から散気管89におくられる空気により曝気
混合され、また、曝気槽88曝気槽89とに送風される
空気量の比率は6:4程度である。ヒータ91は生物処
理が安定して行われるように水温を維持するものであ
り、冬場においては例えば15℃程度に保持する(水温
10℃以下では活性汚泥菌は不活動となる)。
The primary treated water is supplied to the aeration tank 88 through the measuring tank 82 after being adjusted to a PH value within a predetermined range, and the activated sludge bacteria and the inflow raw water (primary treated water) supplied to the aeration tank 88.
Are aerated and mixed by the air (air amount 50 m3 / hour) sent from the blower 90 to the air diffuser 88. Organic matter in the raw water is digested by the activated sludge bacteria, and the primary treated water is purified and treated into stable sludge with good sedimentation. The primary treated water of the aeration tank 88 is sent to the aeration tank 89,
The ratio of the amount of air that is aerated and mixed by the air sent from the blower 90 to the air diffuser 89 and is sent to the aeration tank 88 and the aeration tank 89 is about 6: 4. The heater 91 maintains the water temperature so that biological treatment can be stably performed, and in the winter, the heater 91 maintains the water temperature at about 15 ° C. (when the water temperature is 10 ° C. or less, the activated sludge bacteria are inactive).

【0023】曝気槽84からの曝気水は沈殿槽92(容
量2.5m3 )に送られ、浄化されたものは上澄水と
して槽上部に、汚泥は槽底部に沈殿されて分離される。
分離された汚泥(ほぼ全量)は送風機90からの送風に
より計量槽82を経て曝気槽83へ送られて活性汚泥処
理に使用され、定期的(約一年)に堆積した余剰汚泥を
ポンプ93により沈殿槽92から汚泥調整槽94へ送
る。
The aerated water from the aeration tank 84 is sent to the settling tank 92 (capacity 2.5 m3), and the purified water is separated as supernatant water at the top of the tank and sludge at the bottom of the tank.
The separated sludge (almost all amount) is sent to the aeration tank 83 through the metering tank 82 by the air blow from the blower 90 and used for the activated sludge treatment, and the excess sludge accumulated periodically (about one year) is pumped by the pump 93. It is sent from the settling tank 92 to the sludge adjusting tank 94.

【0024】凝集沈殿槽75からの沈殿物および沈殿槽
92からの活性汚泥は、汚泥調整槽94において一時貯
留されてから定量(流量300l/時)ごとに凝集反応
槽95へ送られる。凝集剤槽97の凝集剤が凝集反応槽
95の汚泥に添加されて凝集処理され、凝集反応槽95
よりオーバーフローした汚泥(水分約99%)は、脱水
機96の濾布98上に供給される。汚泥は脱水機96に
おいて吸引機(図示せず)により吸引され、ローラ99
により圧縮されて脱水ケーキとして排出される。沈殿槽
92の上澄水は処理水槽100へ送られ、一部は脱水機
99の濾布98の洗浄水として使用され、他は下水道へ
放流される。放流水のBODは600PPM 以下であり、
SSは600PPM 以下である。濾布98を洗浄した洗浄
水は、濾液槽101に送られてから原水調整槽76に戻
される。
The precipitate from the coagulation-sedimentation tank 75 and the activated sludge from the sedimentation tank 92 are temporarily stored in the sludge adjusting tank 94 and then sent to the coagulation reaction tank 95 at a fixed amount (a flow rate of 300 l / hour). The coagulant in the coagulant tank 97 is added to the sludge in the coagulation reaction tank 95 to be coagulated, and the coagulation reaction tank 95
The more overflowed sludge (water content: about 99%) is supplied onto the filter cloth 98 of the dehydrator 96. The sludge is sucked by a suction device (not shown) in the dehydrator 96, and the sludge is removed.
Is compressed and discharged as a dehydrated cake. The supernatant water of the settling tank 92 is sent to the treated water tank 100, part of which is used as washing water for the filter cloth 98 of the dehydrator 99, and the other is discharged to the sewer. BOD of discharged water is 600PPM or less,
SS is 600PPM or less. The washing water that has washed the filter cloth 98 is sent to the filtrate tank 101 and then returned to the raw water adjusting tank 76.

【0025】次に、汚泥乾燥機104の作用を述べる。
脱水機96により脱水ケーキに形成された汚泥114
(長さ200mm,幅20mm,厚さ5mm,水分約65〜7
0%)は、供給樋105を流下して多孔壁回転筒107
に投入される。多孔壁回転筒107は2分間隔で回転と
停止とが繰り返えされ、多孔壁回転筒107が停止状状
態のときに汚泥114は投入され、乾燥風によりまず汚
泥114表面が固められる。これは、汚泥114が軟か
いときに多孔壁回転筒107が回転すると、汚泥114
が球状になり、内部の乾燥が進まなくなって乾燥時間が
長くなるとともに、内部が高水分であるため腐敗しやす
くなるためである。そして、汚泥114は多孔壁回転筒
107内を螺旋翼108により撹拌されながら間歇的に
搬送され、燃焼機(図示せず)から給気筒111、給気
口109を介して供給される乾燥風(熱風温度105℃
〜135℃、風量15m3/時)により乾燥され、湿気
を含んだ乾燥風は排気筒113から機外へ排出される。
汚泥114は多孔壁回転筒107内の滞留時間は約30
分間(流量20kg/時)であり、汚泥114は水分約
15%に乾燥される。
Next, the operation of the sludge dryer 104 will be described.
Sludge 114 formed on the dehydrated cake by the dehydrator 96
(Length 200mm, width 20mm, thickness 5mm, moisture about 65-7
0%) flows down the supply gutter 105 and the perforated wall rotating cylinder 107
Be thrown into. The perforated wall rotary cylinder 107 is repeatedly rotated and stopped at intervals of 2 minutes, and when the perforated wall rotary cylinder 107 is in a stopped state, the sludge 114 is introduced and the surface of the sludge 114 is first solidified by the dry air. This is because when the perforated wall rotary cylinder 107 rotates when the sludge 114 is soft, the sludge 114
This is because the particles become spherical, the internal drying does not proceed and the drying time becomes long, and the high internal water content facilitates the decomposition. Then, the sludge 114 is intermittently conveyed in the perforated wall rotary cylinder 107 while being agitated by the spiral blades 108, and the dry air supplied from the combustor (not shown) through the cylinders 111 and 109. Hot air temperature 105 ℃
The drying air containing the moisture is discharged from the exhaust pipe 113 to the outside of the machine.
The sludge 114 has a residence time of about 30 in the perforated wall rotary cylinder 107.
The flow rate is 20 kg / hour, and the sludge 114 is dried to a water content of about 15%.

【0026】図5は本発明の別実施例であり、ケーシン
グ106の下記に、ローラ115,115間に有孔のベ
ルト116を張設したベルトコンベア117を設ける。
その作用を述べると、供給樋105を流下してベルト1
16上に供給された汚泥114は、ベルト116上を搬
送されながら給気装置110から給気される乾燥風によ
り乾燥され、乾燥された汚泥114は排出樋112から
機外へ排出される。
FIG. 5 shows another embodiment of the present invention. Below the casing 106, a belt conveyor 117 in which a belt 116 having a hole is stretched between rollers 115 is provided.
The operation is as follows.
The sludge 114 supplied onto 16 is dried by the dry air supplied from the air supply device 110 while being conveyed on the belt 116, and the dried sludge 114 is discharged from the discharge gutter 112 to the outside of the machine.

【0027】なお、本実施例においては、洗米廃水の生
物処理を活性汚泥菌により処理したが、洗米廃水を多糖
類資化性酵母等の酵母菌により生物処理してもよい。ま
た、汚泥乾燥機は本実施例に限られず、汚泥を乾燥する
装置であればよい。
In the present embodiment, the biological treatment of the rice washing wastewater was treated with activated sludge bacteria, but the rice washing wastewater may be biologically treated with yeast such as polysaccharide-assimilating yeast. The sludge dryer is not limited to this embodiment, and may be any device that dries sludge.

【0028】[0028]

【発明の効果】本発明における洗米廃水処理装置によれ
ば、脱水汚泥を乾燥風により乾燥する汚泥乾燥装置を、
脱水装置の後工程に設ける構成により、従来、焼却され
るかまたは産業廃棄物として処理されていた脱水汚泥
を、乾燥風により効率的に乾燥することができ、飼料や
肥料等に再利用することができる。
According to the rice washing wastewater treatment apparatus of the present invention, a sludge drying apparatus for drying dehydrated sludge by dry air is provided.
Due to the configuration provided in the subsequent process of the dehydrator, the dehydrated sludge that was conventionally incinerated or treated as industrial waste can be efficiently dried by the drying air and can be reused for feed, fertilizer, etc. You can

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

【図1】図1は洗米廃水処理装置のフローチャートであ
る。
FIG. 1 is a flow chart of a rice washing wastewater treatment device.

【図2】図2は本発明を実施した洗米加工装置のフロー
チャートである。
FIG. 2 is a flow chart of a rice washing processing apparatus embodying the present invention.

【図3】図3は撹拌乾燥機の部分側断面図である。FIG. 3 is a partial side cross-sectional view of a stirring dryer.

【図4】図4は汚泥乾燥機の側面図である。FIG. 4 is a side view of a sludge dryer.

【図5】図5は他の汚泥乾燥機の側面図である。FIG. 5 is a side view of another sludge dryer.

【符号の説明】[Explanation of symbols]

1 洗米加工装置 2 供給ホッパ 3 ロータリーバルブ 4 混合タンク 5 レベル計 6 ポンプ 7 ポンプ 8 ポンプ 9 切換弁 10 切換弁 11 洗米機 12 洗米脱水機 13 供給筒 14 架台 15 モータ 16 プーリ 17 ベルト 18 主軸 19 プーリ 20 プーリ 21 ベルト 22 回転軸 23 プーリ 24 テンションプーリ 25 連結軸 26 撹拌体 27 連結体 28 洗米筒 29 洗米室 30 螺旋翼 31 多孔壁筒 32 脱水室 33 回転台 34 排出口 35 排出樋 36 ノズル 37 貯水室 38 通口 39 給水路 40 給水管 41 供給路 42 排出口 43 排出筒 44 電磁弁 45 ポンプ 46 排出筒 47 エアーシャッタ 48 供給タンク 49 多孔壁筒 50 主軸 51 撹拌転子 52 通風口 53 噴風口 54 乾燥室 55 送風管 56 送風機 57 熱風発生機 58 撹拌乾燥機 59 排出樋 60 揚穀機 61 貯水タンク 62 貯水タンク 63 切換弁 64 切換弁 65 切換弁 66 切換弁 67 洗米廃水処理装置 68 原水槽 69 濃度測定装置 70 原水計量槽 71 凝集反応槽 72 凝集反応槽 73 凝集剤槽 74 凝集剤槽 75 凝集沈殿槽 76 原水調整槽 77 ポンプ 78 PH調整槽 79 水位計 80 水位計 81 中和剤槽 82 計量槽 83 曝気槽 84 曝気槽 85 開口 86 仕切壁 87 散気管 88 散気管 89 散気管 90 送風機 91 ヒータ 92 沈殿槽 93 ポンプ 94 汚泥調整槽 95 凝集反応槽 96 脱水機 97 凝集剤槽 98 濾布 99 ローラ 100 処理水槽 101 濾液槽 102 PH計 103 スラッジセンサ 104 汚泥乾燥機 105 供給樋 106 ケーシング 107 多孔壁回転筒 108 螺旋翼 109 給気口 110 給気装置 111 給気筒 112 排出樋 113 排気筒 114 汚泥 115 ローラ 116 ベルト 117 ベルトコンベア 1 Rice Washing Processing Equipment 2 Supply Hopper 3 Rotary Valve 4 Mixing Tank 5 Level Meter 6 Pump 7 Pump 8 Pump 9 Switching Valve 10 Switching Valve 11 Rice Washing Machine 12 Rice Washing Dewatering Machine 13 Supply Cylinder 14 Frame 15 Motor 16 Pulley 17 Belt 18 Spindle 19 Pulley 20 pulley 21 belt 22 rotary shaft 23 pulley 24 tension pulley 25 connecting shaft 26 stirring body 27 connecting body 28 rice washing cylinder 29 rice washing chamber 30 spiral blade 31 perforated wall cylinder 32 dehydration chamber 33 turntable 34 discharge port 35 discharge gutter 36 nozzle 37 water storage Chamber 38 Passage 39 Water supply channel 40 Water supply pipe 41 Supply path 42 Discharge port 43 Discharge cylinder 44 Solenoid valve 45 Pump 46 Discharge cylinder 47 Air shutter 48 Supply tank 49 Perforated wall cylinder 50 Main spindle 51 Stirring rotor 52 Vent hole 53 Jet port 54 Drying room 55 Blower tube 56 Blower 57 Hot air generator 58 Stirring drier 59 Discharge gutter 60 Grain lifter 61 Water storage tank 62 Water storage tank 63 Switching valve 64 Switching valve 65 Switching valve 66 Switching valve 67 Rice washing wastewater treatment device 68 Raw water tank 69 Concentration measuring device 70 Raw water measuring tank 71 Coagulation reaction tank 72 Coagulation reaction tank 73 Coagulant tank 74 Coagulant tank 75 Coagulation sedimentation tank 76 Raw water adjusting tank 77 Pump 78 PH adjusting tank 79 Water level meter 80 Water level meter 81 Neutralizer tank 82 Metering tank 83 Aeration tank 84 Aeration tank 85 Opening 86 Partition wall 87 Diffuser tube 88 Diffuser tube 89 Diffuser tube 90 Blower 91 Heater 92 Settling tank 93 Pump 94 Sludge adjusting tank 95 Coagulation reaction tank 96 Dewatering machine 97 Coagulant tank 98 Filter cloth 99 Roller 100 Treated water tank 101 Filtration tank 102 PH Total 103 Sludge sensor 104 Sludge dryer 105 Supply gutter 106 Casing 107 Perforated Wall Rotating Cylinder 108 Spiral Blade 109 Air Supply Port 110 Air Supply Device 111 Supply Cylinder 112 Exhaust Gutter 113 Exhaust Cylinder 114 Sludge 115 Roller 116 Belt 117 Belt Conveyor

フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C02F 11/12 D 7824−4D C05F 7/00 301 Z 7057−4H (72)発明者 下寺 香 広島県東広島市西条西本町2番30号佐竹製 作所内Continuation of front page (51) Int.Cl. 5 Identification number Office reference number FI technical display location C02F 11/12 D 7824-4D C05F 7/00 301 Z 7057-4H (72) Inventor Shikadera Azuma Hiroshima Prefecture 2-30, Saijo Nishihonmachi, Hiroshima City Satake Factory

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 洗米廃水を沈殿物と液体とに分離する沈
殿装置と、前記液体を活性汚泥菌または酵母菌により生
物処理する生物処理装置と、前記沈殿物を脱水して脱水
汚泥に形成する脱水装置とからなる洗米排水処理装置に
おいて、前記脱水汚泥を乾燥風により乾燥する汚泥乾燥
装置を、前記脱水装置の後工程に設けたことを特徴とす
る洗米廃水処理装置。
1. A settling device for separating the rice rinsing wastewater into a precipitate and a liquid, a biological treatment device for biologically treating the liquid with activated sludge fungus or yeast, and dehydrating the precipitate to form dehydrated sludge. A rice washing wastewater treatment device comprising a dewatering device and a sludge drying device for drying the dewatered sludge with a drying air in a subsequent step of the dewatering device.
JP3305395A 1991-10-23 1991-10-23 Rice washing waste water disposal equipment Pending JPH05111698A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3305395A JPH05111698A (en) 1991-10-23 1991-10-23 Rice washing waste water disposal equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3305395A JPH05111698A (en) 1991-10-23 1991-10-23 Rice washing waste water disposal equipment

Publications (1)

Publication Number Publication Date
JPH05111698A true JPH05111698A (en) 1993-05-07

Family

ID=17944608

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3305395A Pending JPH05111698A (en) 1991-10-23 1991-10-23 Rice washing waste water disposal equipment

Country Status (1)

Country Link
JP (1) JPH05111698A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011194373A (en) * 2010-03-23 2011-10-06 Mayekawa Mfg Co Ltd Treatment method and apparatus of rice processing wastewater
JP2016113357A (en) * 2014-12-10 2016-06-23 株式会社前川製作所 Producing method of phosphoric acid fertilizer and producing device of phosphoric acid fertilizer
CN110387306A (en) * 2018-04-23 2019-10-29 吴海洋 A method of peculiar smell in the condensed water that removal agricultural byproducts processing generates
CN113087100A (en) * 2021-04-16 2021-07-09 西昌市蓝鼎环保科技有限公司 Sedimentation tank for wastewater treatment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011194373A (en) * 2010-03-23 2011-10-06 Mayekawa Mfg Co Ltd Treatment method and apparatus of rice processing wastewater
JP2016113357A (en) * 2014-12-10 2016-06-23 株式会社前川製作所 Producing method of phosphoric acid fertilizer and producing device of phosphoric acid fertilizer
CN110387306A (en) * 2018-04-23 2019-10-29 吴海洋 A method of peculiar smell in the condensed water that removal agricultural byproducts processing generates
CN113087100A (en) * 2021-04-16 2021-07-09 西昌市蓝鼎环保科技有限公司 Sedimentation tank for wastewater treatment

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