JPS6171888A - Treatment of water with ozone - Google Patents
Treatment of water with ozoneInfo
- Publication number
- JPS6171888A JPS6171888A JP19147584A JP19147584A JPS6171888A JP S6171888 A JPS6171888 A JP S6171888A JP 19147584 A JP19147584 A JP 19147584A JP 19147584 A JP19147584 A JP 19147584A JP S6171888 A JPS6171888 A JP S6171888A
- Authority
- JP
- Japan
- Prior art keywords
- air
- oxygen
- ozone
- ozonized
- water
- 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
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 26
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 37
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 37
- 239000001301 oxygen Substances 0.000 claims abstract description 37
- 239000012528 membrane Substances 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 3
- 239000004793 Polystyrene Substances 0.000 abstract description 2
- 229920001296 polysiloxane Polymers 0.000 abstract description 2
- 229920002223 polystyrene Polymers 0.000 abstract description 2
- 229910001882 dioxygen Inorganic materials 0.000 abstract 1
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 230000029142 excretion Effects 0.000 abstract 1
- 239000004417 polycarbonate Substances 0.000 abstract 1
- 229920000515 polycarbonate Polymers 0.000 abstract 1
- 238000010521 absorption reaction Methods 0.000 description 8
- 239000010800 human waste Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229920005549 butyl rubber Polymers 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、安価に製造されたオゾンを利用する上水、用
水、下水、し尿、工場廃水等の水処理方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a water treatment method for clean water, commercial water, sewage, human waste, industrial wastewater, etc., using inexpensively produced ozone.
現在使用されている工業用オゾン発生機は、無声放電方
式によるもので、一般的には空気を原料としている。Industrial ozone generators currently in use use a silent discharge method, and generally use air as a raw material.
特殊なケースとして酸素を原料とすることもあり、この
場合、オゾン生成に要する電力はA−Aになる。また、
酸素供給手段としては、液体酸素を利用する場合と、モ
レキュラーシープ等の吸着剤を利用した吸着法(以下「
PSA法」と略す)が一般的である。In a special case, oxygen may be used as a raw material, and in this case, the power required to generate ozone will be A-A. Also,
Oxygen supply methods include the use of liquid oxygen and the adsorption method using adsorbents such as molecular sheep (hereinafter referred to as "
PSA method (abbreviated as “PSA method”) is common.
従来のオゾンを利用した水処理におけるオゾン生成シス
テムは、
(il 空気を原料としたオゾン生成システムでは、
設備費は安いが、生成オゾン一度が低く(通常10〜1
2J/Nぜで使用)、水処理#C右けるオゾン吸収効率
が低い。The conventional ozone generation system for water treatment using ozone is (il).
The equipment cost is low, but the ozone produced is low (usually 10 to 1
(Used at 2J/N), water treatment #C has low ozone absorption efficiency.
(11) 酸素を利用したオゾン生成システムでは、
空気を利用した場合と比較し、単位オゾン生成量当りの
放電々力は%以下となり、生成オゾン鑓度が高いために
水処理におけるオゾン吸収効率も高く維持できるが、酸
素発生装置がきわめて高価で、酸素発生に要するエネル
ギーも大きい。(11) In an ozone generation system using oxygen,
Compared to when air is used, the discharge force per unit of ozone generation is less than %, and the ozone absorption efficiency in water treatment can be maintained at a high level due to the high degree of generated ozone, but the oxygen generator is extremely expensive. , the energy required to generate oxygen is also large.
例えば、PSA法の場合、設備費はオゾン発生機とほぼ
同等であり、消費電力もオゾン発生時と同等かそれ以上
となる。For example, in the case of the PSA method, the equipment cost is almost the same as that of an ozone generator, and the power consumption is also the same or more than when generating ozone.
また、酸素源として液体は素を使用する方式は、水処理
のようにオゾンを大量に使用する場合には、適用困難で
ある。Furthermore, the method of using a liquid element as an oxygen source is difficult to apply when a large amount of ozone is used, such as in water treatment.
本発明は、前記従来の問題点を解決し、水処理に好適な
オゾン生成方法を採用し、水処理におけるオゾン吸収効
率を高く維持し、水処理設備全体の設備費、ランニング
コスト等を大幅に低減しようとするものである。The present invention solves the above conventional problems, adopts an ozone generation method suitable for water treatment, maintains high ozone absorption efficiency in water treatment, and significantly reduces equipment costs, running costs, etc. of the entire water treatment facility. This is what we are trying to reduce.
本発明は、高分子酸素富化膜によって空気中の酸素濃度
を高め、得られた酸素富化空気を原料として高鐘度のオ
ゾン化空気を生成し、該オゾン化空気を用いて水処理を
行うことを特徴とするものである。The present invention increases the oxygen concentration in the air using a polymeric oxygen-enriching membrane, uses the obtained oxygen-enriched air as a raw material to generate highly ozonized air, and uses the ozonized air to perform water treatment. It is characterized by the fact that
〔実施例〕
本発明の一実施例を、し尿高度処理の例につき、図面を
参照しつつ説明すれば、第1図において、1はし尿3次
処理水2を導入して、底部よりオゾンを吹き込んで反応
を行わしめる反応槽で、3は処理水、4は排オゾンを示
す。そして、反応槽1の底部に連なるオゾン発生機器は
、除湿、冷却等の前処理装置6及び空気源プロワ−7が
付属され、空気源プロワーフの吸引側には、酸素に対す
る高い選択透過性を持った高分子素材の酸素富化膜を具
備した酸素富化装置8を設置しである。[Embodiment] An embodiment of the present invention will be described with reference to the drawings as an example of advanced human waste treatment. In FIG. This is a reaction tank in which the reaction is carried out by blowing in water. 3 indicates treated water and 4 indicates exhausted ozone. The ozone generating equipment connected to the bottom of the reaction tank 1 is equipped with a pre-treatment device 6 for dehumidification, cooling, etc. and an air source blower 7, and the suction side of the air source blower has a high permselectivity for oxygen. An oxygen enrichment device 8 equipped with an oxygen enrichment membrane made of a polymeric material is installed.
したがって、空気源プロワ−7で吸い込まれる空気は、
まず酸素富化装置8を経由することによって、空気を酸
素富化空気となし、前処理装置6を経てオゾン発生機6
にて高濃度のオゾン化空気を生成し、これを反応槽lに
吹き込むことによってし尿3次処理水2のオゾン吸収効
率が高まり、効果的な処理が行われる。Therefore, the air sucked in by the air source blower 7 is
First, the air is made into oxygen-enriched air by passing through an oxygen enrichment device 8, and then passes through a pretreatment device 6 to an ozone generator 6.
By generating highly concentrated ozonized air and blowing it into the reaction tank 1, the ozone absorption efficiency of the tertiary human waste water 2 is increased, and effective treatment is performed.
このときの酸素富化装置8で得られる酸素富化空気は、
実用的には酸素濃度25〜60%程度にするのが好まし
く、オゾン発生機Sでは10〜40 II/ Nu’の
高謎度オゾン化空気が生成される。The oxygen-enriched air obtained by the oxygen enrichment device 8 at this time is
Practically, it is preferable to set the oxygen concentration to about 25 to 60%, and the ozone generator S generates ozonized air with a high degree of mystery of 10 to 40 II/Nu'.
前記酸素富化装置8に使用される酸素に対する高い選択
透過性を持った高分子素材の酸素富化膜としては、シリ
コン系、Iリカーボネイト系、ポリスチレン系、ポリエ
チレン系、ナイロン系、セルロースアセテート系、エチ
ルセルロース系、メチルゴム系、ブチルゴム系等があり
、主として平膜で用いる吸引型(第1図示例、のように
空気源プロワ−7の吸引側に設りと、主として中空糸膜
で用いる加圧型(空気源プロワ−7の吐出側に設置)が
ある。The oxygen enrichment membrane made of a polymeric material with high permselectivity for oxygen used in the oxygen enrichment device 8 may be silicone-based, I-recarbonate-based, polystyrene-based, polyethylene-based, nylon-based, or cellulose acetate-based. , ethyl cellulose-based, methyl rubber-based, butyl rubber-based, etc., and there are suction type mainly used for flat membranes (as shown in the first example shown in the figure, there is a pressurized type installed on the suction side of the air source blower 7) and pressurized type mainly used for hollow fiber membranes. (installed on the discharge side of the air source blower 7).
これらの選択透過性膜を利用した酸素富化膜法では、酸
素濃度25〜60%の酸素富化空気を大量に安価に製造
することができ、PSA法に比較し、設備費の面で数分
の一以下に、電力費では、第2図に示すようtこ、例え
ば30%酸素富化空気を得るのに塊前後に低減できる。The oxygen-enriched membrane method using these permselective membranes can produce large amounts of oxygen-enriched air with an oxygen concentration of 25 to 60% at low cost, and compared to the PSA method, it is several times cheaper in terms of equipment costs. As shown in FIG. 2, the power cost can be reduced by more than a factor of 1, for example, to obtain 30% oxygen-enriched air.
また、酸素富化膜は、原料空気中の酸素分圧を高くする
ことができるため、オゾン発生機で生成されるオゾン−
厩が高くなる。例えば、原料空気の酸素濃度を25〜6
0%にすることにより、10〜409/Ntrlの高オ
ゾン濃度のオゾン化空気をつくることが可能である。こ
のように、供給オゾン一度を高くすれば、水処理に右け
るオゾン吸収効率を高くすることができる。すなわち、
第3図は上水処理の例(オゾン注入率3′II9/l)
であり、供給オゾン濃度を1(1/N□1から30ji
/H,lに上げることにより、オゾン吸収効率は75%
程度から90%近くまで上昇する。In addition, since the oxygen enrichment membrane can increase the oxygen partial pressure in the raw air, the ozone generated by the ozone generator
Stables get taller. For example, if the oxygen concentration of the raw air is 25 to 6
By setting it to 0%, it is possible to create ozonized air with a high ozone concentration of 10 to 409/Ntrl. In this way, by increasing the amount of ozone supplied, the ozone absorption efficiency, which affects water treatment, can be increased. That is,
Figure 3 is an example of water treatment (ozone injection rate 3'II9/l)
and the supply ozone concentration is 1 (1/N□1 to 30ji
/H,l, the ozone absorption efficiency is 75%.
It increases from about 90% to almost 90%.
さらに、次表は、第1図に示した本発明の実施例におい
て、酸素富化膜による酸素富化空気の酸素濃度を35%
とし、従来法と同等の処理効果を得た場合のコスト比較
を行ったもので、本発明がいかに有利であるかが分る。Furthermore, the following table shows that in the embodiment of the present invention shown in FIG.
This figure shows how advantageous the present invention is by comparing costs when the same treatment effect as that of the conventional method is obtained.
以下余白
〔発明の効果〕
以上述べたようlζ、本発明は、オゾン発生機に供給す
る原料空気を、安価な高分子酸素富化膜によって酸素富
化空気とし、これを原料としてオゾンを生成せしめ水処
理に利用するものであるから、従来の空気原料オゾン生
成システムに比較して生成オゾン濃度、オゾン吸収効率
の向上のみならず、オゾン発生設備ひいては水処理設備
全体の設備費やランニングコストの大幅低減ができる等
多くの有益なる効果を生ずるものである。Margins below [Effects of the Invention] As stated above, the present invention converts the raw material air supplied to the ozone generator into oxygen-enriched air using an inexpensive polymeric oxygen-enriched membrane, and uses this as the raw material to generate ozone. Since it is used for water treatment, it not only improves the generated ozone concentration and ozone absorption efficiency compared to conventional air-based ozone generation systems, but also significantly reduces the equipment costs and running costs of the ozone generation equipment and the water treatment equipment as a whole. This has many beneficial effects, such as reducing the amount of water used.
第1図は本発明の一実施例を示す系統説明図であり、第
2図は酸素富化空気量と製造電力との関係を示す線図、
第3図は供給オゾン濃度とオゾン吸収効率との関係を示
す線図である。
l・・・・・・反応種、2・・・・・・し尿3次処理水
、3・・・・・・処理水、4・・・・・・排オゾン、5
・・・・・・オゾン発生機、6・・・・・・前処理装置
、7・・団・空気源プロワ−18・・・・・・酸素富化
装置。FIG. 1 is a system explanatory diagram showing one embodiment of the present invention, and FIG. 2 is a diagram showing the relationship between the amount of oxygen-enriched air and the produced power.
FIG. 3 is a diagram showing the relationship between supplied ozone concentration and ozone absorption efficiency. l... Reactive species, 2... Human waste tertiary treated water, 3... Treated water, 4... Exhaust ozone, 5
. . . Ozone generator, 6 . . . Pretreatment device, 7. Air source blower 18 . . . Oxygen enrichment device.
Claims (1)
、得られた酸素富化空気を原料として高濃度のオゾン化
空気を生成し、該オゾン化空気を用いて水処理を行うこ
とを特徴とするオゾンによる水処理方法。 2、前記酸素富化空気の酸素濃度を25〜60%にする
ものである特許請求の範囲第1項記載のオゾンによる水
処理方法。[Claims] 1. Increase the oxygen concentration in the air with a polymeric oxygen-enriching membrane, use the obtained oxygen-enriched air as a raw material to generate highly concentrated ozonized air, and use the ozonized air as a raw material. A water treatment method using ozone. 2. The water treatment method using ozone according to claim 1, wherein the oxygen concentration of the oxygen-enriched air is adjusted to 25 to 60%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19147584A JPS6171888A (en) | 1984-09-14 | 1984-09-14 | Treatment of water with ozone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19147584A JPS6171888A (en) | 1984-09-14 | 1984-09-14 | Treatment of water with ozone |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6171888A true JPS6171888A (en) | 1986-04-12 |
Family
ID=16275271
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19147584A Pending JPS6171888A (en) | 1984-09-14 | 1984-09-14 | Treatment of water with ozone |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6171888A (en) |
-
1984
- 1984-09-14 JP JP19147584A patent/JPS6171888A/en active Pending
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