JPH0483589A - Purification of sewage - Google Patents
Purification of sewageInfo
- Publication number
- JPH0483589A JPH0483589A JP2199730A JP19973090A JPH0483589A JP H0483589 A JPH0483589 A JP H0483589A JP 2199730 A JP2199730 A JP 2199730A JP 19973090 A JP19973090 A JP 19973090A JP H0483589 A JPH0483589 A JP H0483589A
- Authority
- JP
- Japan
- Prior art keywords
- water
- pulp
- contaminant
- pulp fiber
- fixed
- 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
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 12
- 238000000746 purification Methods 0.000 title claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 239000000835 fiber Substances 0.000 claims abstract description 27
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 19
- 239000001301 oxygen Substances 0.000 claims abstract description 19
- 238000010009 beating Methods 0.000 claims abstract description 18
- 239000000356 contaminant Substances 0.000 claims abstract description 16
- 239000002351 wastewater Substances 0.000 claims abstract description 16
- 229920001131 Pulp (paper) Polymers 0.000 claims abstract description 15
- 239000011230 binding agent Substances 0.000 claims abstract description 7
- 239000000919 ceramic Substances 0.000 claims abstract description 7
- 239000006228 supernatant Substances 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 23
- 239000010893 paper waste Substances 0.000 claims description 19
- 239000003344 environmental pollutant Substances 0.000 claims description 12
- 231100000719 pollutant Toxicity 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 11
- 230000004913 activation Effects 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 238000005119 centrifugation Methods 0.000 claims description 3
- 229920000126 latex Polymers 0.000 abstract description 5
- 239000000843 powder Substances 0.000 abstract description 5
- 150000003839 salts Chemical class 0.000 abstract description 5
- 229910052751 metal Inorganic materials 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract description 3
- 239000010797 grey water Substances 0.000 description 6
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 5
- 239000011574 phosphorus Substances 0.000 description 5
- 229910052698 phosphorus Inorganic materials 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 3
- 239000013505 freshwater Substances 0.000 description 3
- 241000251468 Actinopterygii Species 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- 230000003749 cleanliness Effects 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 235000015170 shellfish Nutrition 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は汚水浄化方法に関するものであり、詳細には、
汚水中に含まれている汚染物質を、故紙パルプの繊維表
面に凝集状態で付着させて除去する資源再利用型の汚水
浄化方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for purifying sewage, and in detail,
The present invention relates to a resource reuse type wastewater purification method in which pollutants contained in wastewater are removed by being attached to the fiber surface of waste paper pulp in an agglomerated state.
河川や湖沼、あるいは、海域の汚染防止手段として各種
の物理的、あるは、物理化学的汚水処理方法、または、
好気性処理法、嫌気性処理法を始めとする生物化学的汚
水処理方法等が知られている。Various physical or physicochemical sewage treatment methods as a means of preventing pollution of rivers, lakes, or sea areas, or
Biochemical wastewater treatment methods such as aerobic treatment methods and anaerobic treatment methods are known.
例えば、一般家庭から排出される生活雑排水は、河川水
や湖沼水の生物化学的酸素要求量(BOD)に悪影響を
与える油脂類や燐を可成り多量に含んでいるため、吸着
や固形化等の分離回収手段を利用したり、無燐洗剤や石
鹸を使用する等の汚染防止策が実施されている。For example, gray water discharged from households contains considerable amounts of fats and oils and phosphorus, which have a negative effect on the biochemical oxygen demand (BOD) of river water, lake water, and marshes, so they are absorbed and solidified. Measures to prevent contamination are being implemented, such as using separation and recovery methods such as phosphorus-free detergents and soaps.
水質汚染の指標の一つである上記生物化学的酸素要求量
(BOD)は、好気性微生物が、好気的条件下で一定時
間内に水中の有機物を分解するのに消費する溶存酸素量
(DO)として定義されており、河川、あるいは、淡水
性湖沼水中の生物分解性有機物量に対応するものである
。例えば、BOD I PPm以下であれば、そのまま
飲用可能な極めて清浄な水質基準が維持されていること
を意味し、また、BOD 3 PPm以下であれば、淡
水魚の大部分が生棲可能な中程度の水質基準が維持され
ていることを意味する。一般的には、BOD 5 PP
+nが水質管理上汚濁の限界値とさている。尚、水中に
塩、類が含まれていると2、塩類によって微生物の増殖
が阻害されるだめBODの測定:よ不可能となる。The biochemical oxygen demand (BOD), which is one of the indicators of water pollution, is the amount of dissolved oxygen consumed by aerobic microorganisms to decompose organic matter in water within a certain period of time under aerobic conditions. DO), which corresponds to the amount of biodegradable organic matter in rivers or freshwater lakes and marshes. For example, if BOD I PPm or less, it means that the water quality standards are extremely clean and can be drunk as is, and if BOD 3 PPm or less, it means that the water quality is moderate enough for most freshwater fish to live in. water quality standards are maintained. Generally, BOD 5 PP
+n is said to be the limit value for pollution in water quality management. Note that if the water contains salts, the growth of microorganisms will be inhibited by the salts, making BOD measurement impossible.
一方、化学的酸素要求1(COD>は、港湾等の海域、
河川水、あるいは、湖沼水中の有機物含有量の指標の一
つで、水中の還元性有機物を一定の酸化条件(100℃
、30分間)下で反応させ、そ、れに要する酸化剤(過
マンガン酸カリウム)の量を当量酸素量(Oz mg/
l )に換算して表示したものである。CODは測定
が容島なため港湾等の海域、河川、あるいは、汽水性湖
沼の環境基準値として広く用いられているが、有機物の
種類によって酸化分解の程度が異なり、また、有機性の
還元物質が測定に開与するので、COD値の示す内容は
必ずしも明確ではない。On the other hand, chemical oxygen demand 1 (COD>) is
One of the indicators of the organic matter content in river water or lake water.
, for 30 minutes), and the amount of oxidizing agent (potassium permanganate) required for this was adjusted to the equivalent amount of oxygen (Oz mg/
1). COD is widely used as an environmental standard value for sea areas such as ports, rivers, and brackish water lakes because COD can be measured only on a regular basis. However, the degree of oxidative decomposition varies depending on the type of organic matter, and the is involved in the measurement, so what the COD value indicates is not necessarily clear.
これらの事情を考慮して、生活雑排水が流入する河川あ
るいは湖沼の水質基準値としては一般にBODが使用さ
れている。Taking these circumstances into consideration, BOD is generally used as the water quality standard value for rivers or lakes into which domestic wastewater flows.
[発明が解決しようとする課題〕
一般家庭の厨房等から放出される生活雑排水中にはチン
素や燐のような生物の栄t#!となる物質が可成り多量
に含まれているから、これらの汚濁物質を分離回収しな
いまま河川や湖沼に放流すると、植物プランクトンの増
殖が加速され、淡水赤潮を発生させる。更に詳しく説明
すると、増殖後、死亡した植物プランクトンの死骸や魚
介類、あるいは、貝類のの糞が湖沼の底に沈積し、分解
されることによってチン素や燐が溶出し、栄養塩類とし
て蓄積される悪循環を繰返すことによって河川水や湖沼
水の富栄養化現象が進行する。植物プランクトンは、水
中にチン素、燐のほか、水銀、カドミウム、鉛等の毒性
の高い有機化合物が含有されている場合には、これを吸
着する性質も持っている。このため、チン素、あるいは
、燐および上記有毒物質を摂り入れた植物プランクトン
の死骸が大愛に沈積すると、河川水や湖沼水がヘドロ化
し水質を悪化させるだけでなく、この河川や湖沼を水源
として使用している流域の住民に、例えば、イタビイタ
イ病等の公害病を発生させる原因となる。一方、紙資源
の有効利用策の一環として故紙パルプの再生利用が提唱
されている。しかしながら、これ迄の方法は再生紙とし
ての利用に累られており、汚水浄化技術への転用は全く
検討されておらなかった。[Problem to be solved by the invention] Gray water discharged from kitchens in ordinary homes contains living organisms such as chlorine and phosphorus! If these pollutants are discharged into rivers or lakes without being separated and collected, the proliferation of phytoplankton will be accelerated, causing freshwater red tide. To explain in more detail, after multiplication, dead phytoplankton carcasses, fish and shellfish, or shellfish feces are deposited on the bottom of the lake, and as they decompose, tin and phosphorus are leached out and accumulated as nutrients. By repeating this vicious cycle, the phenomenon of eutrophication of river water and lake water progresses. Phytoplankton also has the property of adsorbing highly toxic organic compounds such as mercury, cadmium, and lead, in addition to tinnic acid and phosphorus, if the water contains them. For this reason, when dead phytoplankton that have ingested tin, phosphorus, and the above toxic substances are deposited in Odaiai, river water and lake water not only turn into sludge and deteriorate water quality, but also turn these rivers and lakes into water sources. For example, it can cause pollution-related diseases such as Itabi-itai disease to occur in the residents of the basin where they are used as water. On the other hand, recycling of waste paper pulp has been proposed as part of measures to effectively utilize paper resources. However, the methods used so far have been used only for recycled paper, and no consideration has been given to its application to wastewater purification technology.
上記課題の解決手段として本発明は、汚水の11に対し
て約3重量部以上の故紙パルプを混入した状態で上記故
紙パルプを叩解し、パルプ繊細の表面積を増大させる工
程と、上記叩解中、あるいは、叩解後の故紙のパルプ含
有汚水にバインダを添加し、パルプ繊維の表面に上記汚
水中に含有されている汚染物質を定着させる工程と、上
記工程中、あるいは、上記工程終了後、汚染物質の定着
によって生成されたスラリー状の被処理水に凝集剤を添
加し、汚染物質を定着させたパルプ繊維を沈降させて、
上澄液を抽出する工程と、汚染物質を定着させて沈降し
た含水状態のバルブ繊維を遠心分離作用を利用して水分
と汚染物質が定着したパルプ繊維とに分離し、水分を抽
出する工程とからなる汚水浄化方法、および上記上澄液
と遠心分離により抽出した水分との混合液に酸素を与え
て溶存酸素量を増大させ、かつ、上記混合液に遠赤外線
放射セラミックスを接触させることによって上記被処理
水に励起反応を起こさせ、上記被処理水に活性化エネル
ギーを付与する汚水浄化方法を提供するものである。As a means for solving the above problems, the present invention provides a step of beating the waste paper pulp in a state in which about 3 parts by weight or more of the waste paper pulp is mixed with 11 parts of waste water to increase the surface area of the pulp, and during the beating, Alternatively, a process of adding a binder to the pulp-containing wastewater of waste paper after beating and fixing the pollutants contained in the wastewater on the surface of the pulp fibers, and a process of fixing the pollutants contained in the wastewater during the above process or after the completion of the above process. A flocculant is added to the slurry-like treated water generated by the fixation of the pollutants, and the pulp fibers with the contaminants fixed thereon are sedimented.
A step of extracting the supernatant liquid, and a step of separating the water-containing valve fibers, which have fixed contaminants and settled, into pulp fibers with fixed contaminants using centrifugal separation, and extract the moisture. A sewage purification method comprising: increasing the amount of dissolved oxygen by adding oxygen to a mixture of the supernatant liquid and water extracted by centrifugation; and bringing a far-infrared emitting ceramic into contact with the mixture; The present invention provides a wastewater purification method that causes an excited reaction in the water to be treated and imparts activation energy to the water to be treated.
使用済みの紙材に脱墨処理を施し、インクやビニール等
のコーティング屓を除去した故紙パルプの繊維を汚水の
浄化媒体として使用する。汚水、例えば、生活雑排水1
1に対して約3重量部以上の故紙パルプを混入した状態
で上記故紙パルプを叩解し、パルプ繊維の表面積を増大
させる。叩解中、あるいは、叩解を終了した段階で、故
紙バルブ含有汚水にゴムラテックスからなるバインダと
凝集剤として三価の金属塩、例えば、Af2(S04
) aを添加し、パルプ繊維の表面に汚水中に含有され
ている汚染物質を定着させると共に、汚染物質を付着さ
せたパルプ繊維を叩解機の底部に沈降させる。汚染物質
を定着させて沈降したパルプ繊維は、遠心分離機に供給
し、遠心分離作用を利用して水分を分離する。汚染物質
を定着させたパルプ繊維は、この後、焼却することによ
って残灰となるが、この残灰は、例えば、プラスチック
やセメント等に混入し、建築物の素材として再利用する
。Used paper materials are deinked to remove ink, vinyl coatings, etc., and the waste paper pulp fibers are used as a wastewater purification medium. Sewage, e.g. gray water 1
The above-mentioned waste paper pulp is beaten in a state in which about 3 parts by weight or more of waste paper pulp is mixed into the waste paper pulp to increase the surface area of the pulp fibers. During beating or at the end of beating, a binder consisting of rubber latex and a trivalent metal salt, such as Af2 (S04
) A is added to fix the contaminants contained in the wastewater on the surface of the pulp fibers, and the pulp fibers with the contaminants attached are allowed to settle at the bottom of the beating machine. The pulp fibers, on which contaminants have settled and settled, are fed to a centrifuge, and water is separated using centrifugal action. The pulp fibers with pollutants fixed thereon are then incinerated to become residual ash, which is mixed into, for example, plastics, cement, etc., and reused as building materials.
一方、叩解機内に貯溜された上澄液と遠心分離によって
パルプ繊維から抽出された水分との混合液からなる一次
処理水中に酸素を導入することによって溶存酸素量(D
o)を増大させる。また、上記−次処理水に、遠赤外線
放射セラミックスの微粉末を接触させることによって、
励起反応を起こさせ、活性化エネルギーを増大させる。On the other hand, the amount of dissolved oxygen (D
o) increase. In addition, by bringing fine powder of far-infrared emitting ceramics into contact with the above-mentioned secondary treated water,
Causes an excited reaction and increases activation energy.
この被処理水は、環境基準に適合した二次処理水として
河川や湖沼に放流される。This treated water is discharged into rivers and lakes as secondary treated water that meets environmental standards.
第1図は本発明方法の実施に使用される汚水浄化装置の
破断正面図である。同図において(1)は故紙パルプ繊
維の叩解機、(2)は遠心分離機(3)被処理液の貯槽
を示す。FIG. 1 is a cutaway front view of a sewage purification apparatus used for carrying out the method of the present invention. In the figure, (1) shows a waste paper pulp fiber beating machine, (2) a centrifugal separator, and (3) a storage tank for a liquid to be treated.
厨房から排出されたBOD 8 PPmを有する生活雑
排水11に対して、故紙パルプの混合量を第1表に示す
ように2段階に変化させた2種類の試料水(4)を準備
する。Two types of sample water (4) are prepared in which the mixed amount of waste paper pulp is changed in two stages as shown in Table 1 for gray water 11 having BOD 8 PPm discharged from a kitchen.
上記2種類の試料水(4)をそれぞれ叩解機(1)に供
給し、故紙パルプを約5kg/−の圧縮空気の導入下に
叩解することによってパルプ繊維の表面積を増大させる
。叩解中、それぞれの試料水(4)にゴムラテックスか
らなるバインダと、三価の金属塩、例えば、Aj!2
[504)aの10%溶液からなる凝集剤とを添加する
。上記バインダ、および凝集剤の添加量は、第1表に示
すように故紙パルプの混合量に応じて調節する。The above two types of sample water (4) are respectively supplied to the beating machine (1), and the waste paper pulp is beaten while introducing about 5 kg/- of compressed air to increase the surface area of the pulp fibers. During beating, a binder consisting of rubber latex and a trivalent metal salt, for example Aj!, are added to each sample water (4). 2
[504) A flocculant consisting of a 10% solution of a is added. The amounts of the binder and flocculant added are adjusted according to the amount of waste paper pulp mixed, as shown in Table 1.
(第1表)
凝集剤を添加する以前のバインダはOOのイオンが平衡
した乳化状態に保持されている。試料液(4)中に凝集
剤を投入すると、上記のイオン的平衡状態が破れ、ゴム
ラテックスは試料水(4)の汚染物質と共に叩解によっ
て表面積を増大させたパルプ繊維の表面に定着する。汚
染物質を定着させたパルプ繊維は、叩解機(1)の底部
に沈降し、その上部には一次処理水として上澄液(4A
)が溜まる。汚染物質を定着させて叩解機(1)の底部
に沈降した含水状態のパルプ繊維(5)は遠心分離!8
(2)に投入し、遠心分離作用を利用して水分(6)と
、汚染物質を定着させたパルプ繊維(5A)とに分離す
る。このパルプ繊維(5A)は、その後、遠心分離機(
2)から取出し、焼却することによって灰化させ、例え
ば、建築物の素材等に再利用する。(Table 1) Before adding the flocculant, the binder is maintained in an emulsified state in which OO ions are balanced. When a flocculant is introduced into the sample liquid (4), the above ionic equilibrium state is broken, and the rubber latex, together with the contaminants in the sample water (4), settles on the surface of the pulp fibers whose surface area has been increased by beating. The pulp fibers with the contaminants fixed on them settle at the bottom of the beating machine (1), and the supernatant liquid (4A
) accumulates. The pulp fibers (5) in a water-containing state that settle on contaminants and settle at the bottom of the beating machine (1) are centrifuged! 8
(2) and separated into water (6) and pulp fibers (5A) on which contaminants have been fixed using centrifugal separation. This pulp fiber (5A) is then subjected to a centrifugal separator (
2) and incinerate it to ashes and reuse it, for example, as a building material.
一方、叩解機(1)の内部に貯溜された上澄液(4A)
は、遠心分離機(2)から抽出された水分(6)と混合
し、−次処理水(8)として貯槽(3)内に導入する。On the other hand, the supernatant liquid (4A) stored inside the crusher (1)
is mixed with the water (6) extracted from the centrifuge (2) and introduced into the storage tank (3) as second treated water (8).
この段階で一次処理液(8)中に酸素を吹き込み、溶存
酸素量(DO)を増大させると共に、遠赤外線放射セラ
ミ−/クスの微粉末と接触させることによって、励起反
応を生起させ、活性化エネルギーを増大させる。貯槽(
3)内の処理を終了した被処理液(9)は、汚染物質の
殆どすべてを除去された清澄な二次処理水(9)として
河川や湖沼に放流する。試料1、および、試料2のCO
Dを叩解機(1)からの液流路および貯槽(3)からの
放流路で採取した被処理水について測定した結果を第2
表に示す。At this stage, oxygen is blown into the primary treatment liquid (8) to increase the amount of dissolved oxygen (DO), and at the same time, by bringing it into contact with the fine powder of far-infrared emitting ceramic/cus, an excited reaction is caused and the activation is activated. Increase energy. Storage tank (
The treated liquid (9) that has undergone the treatment in step 3) is discharged into rivers or lakes as clear secondary treated water (9) from which almost all pollutants have been removed. CO of sample 1 and sample 2
The results of measuring D on the water to be treated collected in the liquid flow path from the beater (1) and the discharge path from the storage tank (3) are shown in the second table.
Shown in the table.
(第2表)
上記第2表から汚水IE当りの故紙バルブ混入量を3重
量部以上に設定した試料1が良好な清浄度を維持してい
ることが理解される。一方、汚水11当たりの故紙バル
ブの混入量が3重量部に満たない試料2では清浄度が試
料1より劣ることが理解される。(Table 2) From Table 2 above, it is understood that Sample 1, in which the amount of waste paper valve mixed per wastewater IE was set to 3 parts by weight or more, maintained good cleanliness. On the other hand, it is understood that sample 2, in which the amount of waste paper valves mixed in per sewage 11 was less than 3 parts by weight, was inferior to sample 1 in cleanliness.
貯槽(3)内に酸素を導入する方法としては、−次処理
水(8)中に直接酸素を吹き込む方法の他、例えば、0
.4〜10%の固形状酸素発生剤を添加する方法も採用
することができる。上記酸素の供給量、ならびに、遠赤
外線放射セラミックス微粉末の添加量は、叩解機(1)
、ならびに、遠心分離!a (2)から取出される一次
処理水(8)と、貯槽(3)から取出される二次処理水
(9)のCOD値、ならびに、用途によって調整するが
、一般的には、未処理の生活雑排水1000ccに付き
4乃至10ccの酸素と、10乃至15gのセラミック
ス微粉末を添加することが好ましい。Methods for introducing oxygen into the storage tank (3) include a method of directly blowing oxygen into the secondary treated water (8), and a method of introducing oxygen into the storage tank (3).
.. A method of adding 4 to 10% of a solid oxygen generating agent can also be adopted. The amount of oxygen supplied and the amount of far-infrared emitting ceramic fine powder added are determined by the beating machine (1).
, as well as centrifugation! The COD values of the primary treated water (8) taken out from a (2) and the secondary treated water (9) taken out from the storage tank (3) are adjusted depending on the use, but in general, untreated water It is preferable to add 4 to 10 cc of oxygen and 10 to 15 g of fine ceramic powder per 1000 cc of gray water.
本発明方法によれば、生活雑排水中の汚染物質が略完全
に除去される。また、汚染物質の定着除去媒体として故
紙バルブを再利用しているため、環境破壊の防止及び省
資源対策の促進に対しても特筆すべき効果が発揮される
。According to the method of the present invention, pollutants in gray water are almost completely removed. In addition, since waste paper valves are reused as a medium for fixing and removing pollutants, it has a remarkable effect on preventing environmental destruction and promoting resource conservation measures.
【図面の簡単な説明】
第1図は汚水浄化装置の破断正面図である。
(1) −叩解機、 (2)−遠心分N機、(3)
−貯槽。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cutaway front view of the sewage purification device. (1) - Beating machine, (2) - Centrifugal N machine, (3)
-Storage tank.
Claims (2)
を混入した状態で上記故紙パルプを叩解し、パルプ繊細
の表面積を増大させる工程と、上記叩解中、あるいは、
叩解後の故紙のパルプ含有汚水にバインダを添加し、パ
ルプ繊維の表面に上記汚水中に含有されている汚染物質
を定着させる工程と、 上記工程中、あるいは、上記工程終了後、汚染物質の定
着によって生成されたスラリー状の被処理水に凝集剤を
添加し、汚染物質を定着させたパルプ繊維を沈降させて
、上澄液を抽出する工程と、汚染物質を定着させて沈降
した含水状態のパルプ繊維を遠心分離作用を利用して水
分と汚染物質が定着したパルプ繊維とに分離し、水分を
抽出する工程とからなる汚水浄化方法。(1) Beating the waste paper pulp in a state where about 3 parts by weight or more of waste paper pulp is mixed with 1 liter of wastewater to increase the surface area of the pulp, and during the beating, or
A step of adding a binder to the pulp-containing wastewater of waste paper after beating and fixing the pollutants contained in the wastewater on the surface of the pulp fibers, and fixing the pollutants during or after the above step. A process of adding a flocculant to the slurry-like treated water generated by the process, sedimenting the pulp fibers with pollutants fixed thereon, and extracting the supernatant liquid; A sewage purification method that consists of the steps of separating pulp fibers into pulp fibers with moisture and contaminants fixed thereon using centrifugal separation, and extracting the moisture.
合液に酸素を与えて溶存酸素量を増大させ、かつ、上記
混合液に遠赤外線放射セラミックスを接触させることに
よって上記被処理水に励起反応を起こさせ、上記被処理
水に活性化エネルギーを付与することを特徴とする請求
項1記載の汚水浄化方法。(2) Oxygen is added to the mixture of the supernatant liquid and the water extracted by centrifugation to increase the amount of dissolved oxygen, and the mixture is brought into contact with far-infrared emitting ceramics, thereby increasing the amount of water to be treated. 2. The method for purifying waste water according to claim 1, wherein activation energy is imparted to the water to be treated by causing an excited reaction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2199730A JPH0483589A (en) | 1990-07-26 | 1990-07-26 | Purification of sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2199730A JPH0483589A (en) | 1990-07-26 | 1990-07-26 | Purification of sewage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0483589A true JPH0483589A (en) | 1992-03-17 |
Family
ID=16412668
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2199730A Pending JPH0483589A (en) | 1990-07-26 | 1990-07-26 | Purification of sewage |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0483589A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002113305A (en) * | 2000-10-11 | 2002-04-16 | Neos Co Ltd | Paint mist treatment agent |
-
1990
- 1990-07-26 JP JP2199730A patent/JPH0483589A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002113305A (en) * | 2000-10-11 | 2002-04-16 | Neos Co Ltd | Paint mist treatment agent |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4173532A (en) | Method for treating plant effluent | |
| JPH01502650A (en) | How to treat contaminants | |
| SE525083C2 (en) | Way to treat mucus | |
| US11807565B2 (en) | Remediation of per- and poly-fluoroalkyl substances in wastewater | |
| JP6611480B2 (en) | Sewage treatment method, phosphorus resource production method | |
| EP0062543A1 (en) | Improved physical-chemical waste treatment method and apparatus | |
| CN105967496B (en) | A kind of harmless treatment method of high-salt sludge | |
| RU2361823C1 (en) | Sewage treatment plant for solid domestic wastes | |
| JPH0483589A (en) | Purification of sewage | |
| WO2007053110A1 (en) | Treatment of wastewater | |
| KR20080051863A (en) | Food Wastewater Treatment System and Wastewater Treatment Method Using the Same | |
| CN116065985B (en) | Harmless advanced treatment method for solid-liquid waste of water-based drilling fluid | |
| CN116395897A (en) | A high-efficiency sewage treatment system for slaughterhouses | |
| Wang et al. | Treatment of Food Ingredients Manufacturing Effluent by Physicochemical–Biological Two-Stage Wastewater Treatment System | |
| US8497406B2 (en) | Preparation and conditioning of sedimentary materials | |
| RU1834859C (en) | Method for purification of sewage water at cattle-breeding farms "ekotechproekt" | |
| CN106493149B (en) | A kind of paper mill waste preprocessing technology | |
| JP3267948B2 (en) | Treatment method for oil-containing waste liquid | |
| CN205241465U (en) | Processing system of printing and dyeing sewage | |
| CN1331769C (en) | Method for processing saponified sewage | |
| Ash et al. | Operators Need to Know Wastewater Treatment Processes. | |
| KR200173545Y1 (en) | Device for reclaiming waste water | |
| CN214299770U (en) | Pretreatment system of fresh leachate | |
| US20230014479A1 (en) | Compositions for the remediation of per- and poly-fluoroalkyl substances in wastewater | |
| JP2011183305A (en) | Method of treating incineration ash |