Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0679683B2 - Air diffuser - Google Patents
[go: Go Back, main page]

JPH0679683B2 - Air diffuser - Google Patents

Air diffuser

Info

Publication number
JPH0679683B2
JPH0679683B2 JP2030164A JP3016490A JPH0679683B2 JP H0679683 B2 JPH0679683 B2 JP H0679683B2 JP 2030164 A JP2030164 A JP 2030164A JP 3016490 A JP3016490 A JP 3016490A JP H0679683 B2 JPH0679683 B2 JP H0679683B2
Authority
JP
Japan
Prior art keywords
air
aggregate
diffuser
diffuser plate
present
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.)
Expired - Lifetime
Application number
JP2030164A
Other languages
Japanese (ja)
Other versions
JPH03232555A (en
Inventor
丈雄 加藤
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.)
NTT Inc
Original Assignee
Nippon Telegraph and Telephone Corp
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 Nippon Telegraph and Telephone Corp filed Critical Nippon Telegraph and Telephone Corp
Priority to JP2030164A priority Critical patent/JPH0679683B2/en
Publication of JPH03232555A publication Critical patent/JPH03232555A/en
Publication of JPH0679683B2 publication Critical patent/JPH0679683B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Nozzles (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は下水処理場の曝気槽等の内部に設置され、汚水
中に空気を曝気し酸素を供給するために使用される散気
板の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention is directed to a diffuser plate installed inside an aeration tank of a sewage treatment plant and used for aerating air and supplying oxygen to wastewater. It is about improvement.

(従来の技術) 曝気槽等において使用される散気板は、均一発泡性を有
するとともに水中において長期間使用できる機械的強度
および耐久性を持つこと、エアレーションに好適の適度
の大きさの気泡を散気板の各部から均一に放出できるこ
と、目詰まりしにくく圧力損失の小さいこと、仮に目詰
まりしても容易に逆洗等により再生できること等の性質
を持つことが要求される。そして従来の散気板として
は、陶磁器等を粉砕して整粒した不定形のセルベンある
いは珪砂等の骨材を水ガラス、釉薬等のガラス質のフラ
ックスにより結合したものが一般的に使用されてきた。
(Prior art) A diffuser plate used in an aeration tank, etc. has uniform foamability and mechanical strength and durability that can be used in water for a long period of time. It also has bubbles of appropriate size suitable for aeration. It is required to be able to be uniformly discharged from each part of the diffuser plate, to be less likely to be clogged with a small pressure loss, and to be easily regenerated by backwashing even if it is clogged. As a conventional air diffusing plate, it is generally used that aggregates such as irregularly shaped cerben or silica sand, which are crushed and sized by porcelain, etc., are bonded by vitreous flux such as water glass and glaze. It was

ところが従来のこのような骨材を用いた散気板は、骨材
形状が不定形であるので圧力損失が大きく所定の通気量
を確保しようとすると不定形の骨材粒子の間に存在する
フラックスの量を減少させねばならず、必然的に散気板
の機械的強度が小さくなるため、薄形化することができ
ないという問題があった。また空気を流通させて気泡を
発生させる空隙は不定形の骨材粒子の間に形成される不
定形のバラツキの大きい空隙より成るものであるから、
散気される気泡の大きさの均一性に欠けるうえ、長期間
の使用により目詰まりした場合の逆洗等による再生の効
果も必ずしも十分ではないという問題もあった。更に従
来の散気板は通気量の調整を骨材粒子の粒度を調整する
ことによって主に行っていたため、製造工程が複雑化す
るという問題もあった。
However, since the air diffuser using such a conventional aggregate has an irregular shape of the aggregate, the pressure loss is large and the flux existing between the irregular aggregate particles is large when trying to secure a predetermined air flow amount. However, since the mechanical strength of the diffuser plate is inevitably reduced, there has been a problem that it cannot be thinned. In addition, since the voids that generate air bubbles by circulating air consist of irregularly shaped large voids formed between the irregularly shaped aggregate particles,
There is also a problem in that the size of the air bubbles to be diffused is not uniform, and the effect of regeneration by backwashing etc. when it is clogged due to long-term use is not always sufficient. Further, in the conventional air diffuser plate, the air flow rate is mainly adjusted by adjusting the particle size of the aggregate particles, so that there is a problem that the manufacturing process is complicated.

(発明が解決しようとする課題) 本発明はこのような従来の問題点を解決して、圧力損失
が少なく所定の通気量を確保しつつ嵩比重及び強度の増
加を図ることができ、しかも均一な大きさの気泡を散気
板の各部から均一に発生させることができるうえ、目詰
まりが生じにくく、また圧力損失も小さく、また目詰ま
りした場合の逆洗等による再生処理が極めて容易で、再
生効率がよいうえ、製造工程において通気量の調整を粒
度調整の他にも成形圧力、ガラス質結合材の量等を変化
させることによって容易に行える散気板を提供するため
に完成されたものである。
(Problems to be Solved by the Invention) The present invention solves the above-mentioned problems of the related art, and it is possible to increase the bulk specific gravity and the strength while ensuring a predetermined air flow rate with less pressure loss, and moreover, uniform Air bubbles of various sizes can be generated uniformly from each part of the air diffuser, clogging is less likely to occur, pressure loss is also small, and regeneration processing such as backwashing when clogging is extremely easy, Completed to provide a diffuser plate that has good regeneration efficiency and that can be easily adjusted in the manufacturing process by changing the molding pressure, the amount of vitreous binder, etc. in addition to adjusting the particle size. Is.

(課題を解決するための手段) 上記の課題を解決するためになされた本発明は、セラミ
ック原料粉末を造粒して得た球状のセラミック粒子をガ
ラス質結合材により結合した表面が滑らかな球状のセラ
ミック粒子からなり、曲げ強度90kg/cm2以上でかつ通気
量1300ml/cm2・min・120mmAq以上の特性を有することを
特徴とするものである。
(Means for Solving the Problems) The present invention made to solve the above problems is a spherical surface having a smooth surface obtained by combining spherical ceramic particles obtained by granulating a ceramic raw material powder with a vitreous binder. It is characterized by having a bending strength of 90 kg / cm 2 or more and an air permeability of 1300 ml / cm 2 · min · 120 mmAq or more.

このように本発明の散気板は従来の不定形の骨材粒子に
代えて、セラミック原料粉末を造粒して得た球状のセラ
ミック粒子を使用したことにより、通気量が均一で目詰
りしにくく、また長期間の使用で仮りに目詰りしても高
圧力の空気、水等で簡単に目詰りの再生処理ができる点
に大きい特徴がある。球状のセラミック粒子は不定形の
骨材粒子に比較して充填性に優れ、また球状のセラミッ
ク粒子間に形成される空隙は大きさや分布が均一となっ
て均一な大きさの気泡を散気板の各部より均一に発生さ
せることができる。なお、セラミック原料粉末を造粒し
て得た球状のセラミック粒子の粒径は0.5〜3.0mm程度が
最適であるが、ほぼ同一粒径のもののみを用いても、粒
径の異なる複数種類の骨材を混合して使用してもよい。
As described above, the air diffuser of the present invention uses spherical ceramic particles obtained by granulating the ceramic raw material powder, instead of the conventional amorphous aggregate particles, so that the air flow rate is uniform and clogging occurs. It is difficult to use, and even if it becomes clogged even if it is used for a long period of time, the clogging can be easily regenerated with high pressure air, water or the like. Spherical ceramic particles have better packing properties than irregularly shaped aggregate particles, and the voids formed between spherical ceramic particles have a uniform size and distribution, and air bubbles of uniform size are diffused on the diffuser plate. Can be generated more uniformly from each part. It should be noted that the particle size of the spherical ceramic particles obtained by granulating the ceramic raw material powder is optimally about 0.5 to 3.0 mm. The aggregate may be mixed and used.

このような球状のセラミック粒子は、10〜20%程度のガ
ラス質結合材と混合され、プレス成形、焼成の各工程を
経て散気板とされる。得られた散気板は表面がガラス質
結合材により滑らかにコーティングされた球状のセラミ
ック粒子からなる。
Such spherical ceramic particles are mixed with about 10 to 20% of a vitreous binder, and after being subjected to steps of press molding and firing, a diffuser plate is formed. The diffuser plate obtained consists of spherical ceramic particles whose surface is smoothly coated with a glassy binder.

本発明の散気板は第1図及び第2図のグラフに示される
ように、骨材の形状差に基づき、従来の不定形骨材を用
した散気板と比較して曲げ強度と通気量との関係および
風圧と通気量との関係において、大きく異なるものであ
る。第1図に示されるように、本発明の散気板は曲げ強
度90kg/cm2以上でかつ通気量が1300ml/cm2・min・120mm
Aq以上である極めて機械的強度が高くかつ通気量の多い
散気板である。また本発明の散気板は、第2図に示され
るように圧力損失が少ないので同じ通気量を得るのに風
圧は従来品の1/2でよい。また、圧力が高くなっても従
来品ほど通気量の低下率が大きくならない。さらに、本
発明の散気板はプレス成形の圧力を変えることによって
球状のセラミック粒子の充填密度を変え、通気量をかな
り自由にコントロールすることもできる。
As shown in the graphs of FIGS. 1 and 2, the air diffusing plate of the present invention is based on the shape difference of the aggregates, and has a higher bending strength and ventilation than the air diffusing plate using the conventional irregular shaped aggregate. There is a large difference in the relationship with the amount and the relationship between the wind pressure and the air flow rate. As shown in FIG. 1, the diffuser plate of the present invention has a bending strength of 90 kg / cm 2 or more and an air flow rate of 1300 ml / cm 2 · min · 120 mm.
It is a diffuser plate with Aq or more, which has extremely high mechanical strength and a large amount of ventilation. Further, since the air diffuser of the present invention has a small pressure loss as shown in FIG. 2, the air pressure may be half that of the conventional product in order to obtain the same ventilation amount. Further, even if the pressure increases, the rate of decrease in the air flow rate does not increase as much as the conventional product. Further, the air diffuser of the present invention can change the packing density of spherical ceramic particles by changing the pressure for press molding, and the air flow rate can be controlled quite freely.

更に本発明の散気板は、セラミック粉末を造粒して得た
球状のセラミック粒子をガラス質結合材により結合した
ものであるから骨材の表面が極めて滑らかであるので、
従って、内部に形成される空隙の表面も滑らかであり、
従来の不定形の骨材粒子に比較して長期間使用しても目
詰まりを生じにくい。しかも仮りに目詰まりを生じた場
合にも、骨材および空隙の表面が滑らかであるために高
圧の空気、水等で逆洗すれば第3図に示すように容易に
目詰まり物質を除去して目詰りを回復することができ散
気板の再生が簡単にできる利点がある。
Further, since the air diffuser plate of the present invention is the one in which the spherical ceramic particles obtained by granulating the ceramic powder are bonded by the vitreous binder, the surface of the aggregate is extremely smooth,
Therefore, the surface of the void formed inside is also smooth,
Compared with conventional amorphous particles, clogging is less likely to occur even after long-term use. Moreover, even if a clogging occurs, the clogging material can be easily removed as shown in Fig. 3 by backwashing with high pressure air, water, etc. because the surface of the aggregate and the void is smooth. There is an advantage that the clogging can be recovered and the diffuser plate can be easily regenerated.

更に本発明の散気板は、造粒した球状の骨材を用いてい
るので、粒径をコントロールすることが容易で、従っ
て、気孔の大きさも均一となり、第4図に示すように気
孔のバラツキが従来の不定形の骨材を用いたものより極
めて小さい利点も有する。なお、本発明の散気板の数値
限定理由を述べれば、曲げ強度が90kg/cm2未満であると
従来品とほとんど変りなく長期間の使用により劣化が著
しいものであり、また、通気量が1300ml/cm2・min・120
mmAq以下では不定形骨材を用いた従来品と比べて優位性
がなく、大容量のブロアーを用いなければならず、本発
明はこれらの相乗効果を有する優れた散気板である。
Further, since the air diffuser of the present invention uses the granulated spherical aggregate, it is easy to control the particle size, and therefore the pore size becomes uniform, and as shown in FIG. It also has an advantage that the variation is extremely smaller than that using the conventional amorphous aggregate. The reason for limiting the numerical value of the air diffuser of the present invention is that the bending strength is less than 90 kg / cm 2, which is almost the same as the conventional product and is significantly deteriorated by long-term use. 1300 ml / cm 2・ min ・ 120
If it is less than mmAq, it is not superior to a conventional product using an irregularly shaped aggregate, and a large capacity blower must be used. The present invention is an excellent diffuser plate having these synergistic effects.

次に本発明の実施例を示す。Next, examples of the present invention will be described.

(実施例) 第1表にNo.1〜No.3として示す3種類の粒度分布を示す
球状のセラミック粒子を、表中に示されるそれぞれの量
のフラックスと混合し、10Kg/cm2の成形圧力で30cm×30
cm×3cmの寸法にプレス成形し、1280℃で2時間焼成を
行って本発明の散気板No.1〜No.3を得た。
(Examples) Spherical ceramic particles having three kinds of particle size distributions shown as No. 1 to No. 3 in Table 1 were mixed with respective amounts of flux shown in the table, and molded into 10 Kg / cm 2 . 30 cm by pressure
The air diffuser plates No. 1 to No. 3 of the present invention were obtained by press molding into a size of cm × 3 cm and firing at 1280 ° C. for 2 hours.

なお、比較の為にNo.1〜No.3と同じ粒度分布を示す従来
のセルベンよりなる不定形の骨材を用い、同量のフラッ
クスを用いて同様に従来品No.1〜No.3の3種類の比較散
気板を得た。得られた6種の散気板について曲げ強度、
通気量、製品嵩比重、気孔率等を測定した。結果を第1
表中に記載した。
In addition, for comparison, an amorphous aggregate made of conventional cerben showing the same particle size distribution as No. 1 to No. 3 was used, and the same amount of flux was used in the same manner as the conventional product No. 1 to No. 3. Three types of comparative diffuser plates were obtained. Bending strength of the obtained 6 kinds of diffuser plates,
The air flow rate, product bulk specific gravity, porosity, etc. were measured. First result
Described in the table.

第1表の結果より明らかなとおり本発明のセラミック粉
末を造粒して得た球状骨材を用いたものは、従来の不定
形骨材を用いているものに比較して、曲げ強度、通気量
ともに優れていることが確認された。また、充填性にも
優れているので嵩比重の大きな散気板が得られることも
確認された。
As is clear from the results of Table 1, the one using the spherical aggregate obtained by granulating the ceramic powder of the present invention has a higher bending strength and ventilation than the one using the conventional irregular-shaped aggregate. It was confirmed that both amounts were excellent. It was also confirmed that an air diffuser having a large bulk specific gravity can be obtained because it has excellent filling properties.

(発明の効果) 本発明は以上に説明したように、従来の陶磁器質を破砕
して整粒した不定形のセンベルあるいは珪砂等の骨材粒
子に代えて充填性に優れまた表面の滑らかな造粒成形し
た球状のセラミック粒子をガラス質結合材により結合し
た曲げ強度90Kg/cm2以上、通気量1300ml/cm2・min・120
mmAq以上の特性を有するもので、これにより所定の通気
量を確保しつつ嵩比重及び強度の増加を図ることができ
ること、均一な大きさの気泡を発生させることができる
こと、目詰まりが生じにくく圧力損失も小さく、また目
詰まりした場合でも逆洗等により再生が容易であるこ
と、通気量を成形圧力の調整により変えることができ、
製造工程において通気量の調整を容易に行えること等の
多くの利点を有するものである。
(Effects of the Invention) As described above, the present invention replaces aggregate particles such as irregular shaped sembel or silica sand obtained by crushing and sizing conventional ceramics, and has excellent filling properties and a smooth surface. Bending strength 90 Kg / cm 2 or more with air-flow rate 1300 ml / cm 2 min 120
Since it has a characteristic of mmAq or more, it is possible to increase the bulk specific gravity and strength while ensuring a predetermined ventilation volume, to generate bubbles of uniform size, and to prevent clogging and pressure. Loss is small, and even if it becomes clogged, it can be easily regenerated by backwashing, and the aeration rate can be changed by adjusting the molding pressure.
It has many advantages such as easy adjustment of the air flow rate in the manufacturing process.

よって本発明は従来の問題点を解決した散気板として、
産業の発展に寄与するところは極めて大きいものであ
る。
Therefore, the present invention, as a diffuser plate that solves the conventional problems,
The areas that contribute to the development of industry are extremely large.

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

第1図は製品の曲げ強度と通気量との関係を示すグラ
フ、第2図は製品の風圧と通気量との関係を示すグラ
フ、第3図は製品の使用時間と目詰り回復率との関係を
示すグラフ、第4図は製品の骨材平均粒径と平均気孔径
との関係を示すグラフである。
FIG. 1 is a graph showing the relationship between the bending strength of the product and the air flow rate, FIG. 2 is a graph showing the relationship between the air pressure and the air flow rate of the product, and FIG. 3 is the relationship between the product use time and the clogging recovery rate. FIG. 4 is a graph showing the relationship, and FIG. 4 is a graph showing the relationship between the average particle diameter of the aggregate of the product and the average pore diameter.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】セラミック原料粉末を造粒して得た球状の
セラミック粒子をガラス質結合材により結合した表面が
滑らかな球状のセラミック粒子からなり、曲げ強度90kg
/cm2以上でかつ通気量1300ml/cm2・min・120mmAq以上の
特性を有することを特徴とする散気板。
1. A spherical ceramic particle obtained by granulating a ceramic raw material powder, which is bonded by a vitreous binder, and has a smooth surface. The bending strength is 90 kg.
/ cm 2 or more and diffuser plate characterized by having an aeration rate 1300ml / cm 2 · min · 120mmAq or more properties.
JP2030164A 1990-02-09 1990-02-09 Air diffuser Expired - Lifetime JPH0679683B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2030164A JPH0679683B2 (en) 1990-02-09 1990-02-09 Air diffuser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2030164A JPH0679683B2 (en) 1990-02-09 1990-02-09 Air diffuser

Publications (2)

Publication Number Publication Date
JPH03232555A JPH03232555A (en) 1991-10-16
JPH0679683B2 true JPH0679683B2 (en) 1994-10-12

Family

ID=12296116

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2030164A Expired - Lifetime JPH0679683B2 (en) 1990-02-09 1990-02-09 Air diffuser

Country Status (1)

Country Link
JP (1) JPH0679683B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS632154Y2 (en) * 1981-03-14 1988-01-20
JPH01155956A (en) * 1987-12-14 1989-06-19 Nippon Seiko Kk Fluid injector and manufacture thereof
JP2556875B2 (en) * 1988-02-22 1996-11-27 本田技研工業株式会社 Method for manufacturing ceramic gas ejector

Also Published As

Publication number Publication date
JPH03232555A (en) 1991-10-16

Similar Documents

Publication Publication Date Title
JP5658136B2 (en) Porous ceramic sintered body and method for producing the same
CN102210954B (en) Solid-liquid separation composite filter board and preparation method thereof
GB2354478B (en) Ceramic membrane
JP2005523808A (en) Aerator
AU783262B2 (en) Air cleaning filter
US6528446B1 (en) Process for making clay spheroids
JPH0679683B2 (en) Air diffuser
CN101264402B (en) Preparation of tripolite filtering screen
JPS5978679A (en) Porous ceramic material useful as strain bed, etc.
JPH1121182A (en) Production of porous ceramic
CN109912295B (en) Silicate-based biological filter material and preparation method and application thereof
JP4437198B2 (en) Method for producing foam using crushed sludge and the like, and foam
JP2009227511A (en) Inorganic hydrothermally solidified body, method of manufacturing the same and material using hydrothermally solidified body
JPS58213669A (en) Manufacture of ceramic porous body
JP2800134B2 (en) Manufacturing method of porous ceramics
JPS6121961A (en) Glass coated ceramic particle
JP4666452B2 (en) Compressed activated carbon block
JPH0725683A (en) Pottery having microvoid and production thereof
KR20040068824A (en) Micro Bio-carrier for fluidizing reactor by using waste slag and fly ash
JPH0462774B2 (en)
JP2868425B2 (en) Water quality improving material and method for producing water quality improving material
JP2000128658A (en) Ceramic filter using incinerated ash, method for producing the same, and method for concentrating and dewatering using the same
JP2000119075A (en) Titanium dioxide-deposited continuous porous sintered compact and its production
JPH08323369A (en) Water quality improving material and production of the material
JPH0686995A (en) Carrier for waste water treatment