JP3151538B2 - Method and apparatus for producing deodorizing granules - Google Patents

Method and apparatus for producing deodorizing granules

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Publication number
JP3151538B2
JP3151538B2 JP31536291A JP31536291A JP3151538B2 JP 3151538 B2 JP3151538 B2 JP 3151538B2 JP 31536291 A JP31536291 A JP 31536291A JP 31536291 A JP31536291 A JP 31536291A JP 3151538 B2 JP3151538 B2 JP 3151538B2
Authority
JP
Japan
Prior art keywords
dispersion
particle holding
liquid
deodorizing
chamber
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 - Fee Related
Application number
JP31536291A
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Japanese (ja)
Other versions
JPH05123570A (en
Inventor
幹育 中西
Original Assignee
鈴木総業株式会社
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Application filed by 鈴木総業株式会社 filed Critical 鈴木総業株式会社
Priority to JP31536291A priority Critical patent/JP3151538B2/en
Publication of JPH05123570A publication Critical patent/JPH05123570A/en
Application granted granted Critical
Publication of JP3151538B2 publication Critical patent/JP3151538B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の目的】[Object of the invention]

【産業上の利用分野】本発明はアンモニア、硫化水素等
の悪臭ガスの臭気を除去する脱臭微粉末剤を更に使用し
やすい形態に加工した脱臭粒剤の製造方法並びにその製
造装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a deodorizing granule obtained by further processing a deodorizing fine powder for removing an odor of an odorous gas such as ammonia and hydrogen sulfide into a form which can be more easily used, and an apparatus for producing the same. .

【0002】[0002]

【発明の背景】近年、酸化亜鉛と二酸化チタンとを脱臭
成分として含む脱臭剤(特開昭63−54935号参
照)や酸化亜鉛と酸化アルミニウムおよび酸化珪素とを
脱臭成分として含む脱臭剤(特開昭63−246167
号参照)が、その強力な脱臭性能が評価されて種々の分
野において使用されている。このような脱臭剤に代表さ
れるような脱臭微粉末剤は、ミクロンないしサブミクロ
ンオーダーの微粒子であるため、そのままの状態で使用
すると飛散してしまう。
BACKGROUND OF THE INVENTION In recent years, deodorants containing zinc oxide and titanium dioxide as deodorizing components (see JP-A-63-54935) and deodorants containing zinc oxide, aluminum oxide and silicon oxide as deodorizing components (see JP-A-63-54935). 63-246167
Has been used in various fields because of its strong deodorizing performance. The deodorized fine powder typified by such a deodorant is a fine particle on the order of microns or submicrons, and is scattered when used as it is.

【0003】そこでこのものを使用するに際しては、P
VA等のバインダーを用いて紙、繊維、発泡体等に担持
させて使用していたが、このような方法で使用する場合
には、バインダーの粘性等のため造粒しにくく、またP
VA膜のガス透過性の悪さから脱臭機能が低下するとい
う問題点があった。
[0003] Therefore, when this is used, P
It has been used by supporting it on paper, fiber, foam, etc. using a binder such as VA. However, when used in such a method, granulation is difficult due to the viscosity of the binder and the like.
There is a problem that the deodorizing function is reduced due to the poor gas permeability of the VA membrane.

【0004】また脱臭微粉末剤をシート状のものに担持
させた後、これを活性種存在雰囲気下に晒してその表面
を荒らす方法や、脱臭微粉末剤を分散させて高粘度水溶
液とし、このものから造粒する方法なども提案されてい
るが、前者の方法はシート状にする過程で多くの脱臭微
粉末剤を含有することができず、また後者の方法は水が
分散媒であるためバインダー機能が得られず造粒物は指
で潰すと粉々になってしまうというものであった。
[0004] Further, after the deodorized fine powder is carried on a sheet, it is exposed to an atmosphere containing active species to roughen the surface, or the deodorized fine powder is dispersed to form a high-viscosity aqueous solution. Although a method of granulating from things has also been proposed, the former method cannot contain many deodorized fine powders in the process of forming into a sheet, and the latter method is because water is a dispersion medium. The binder function was not obtained, and the granulated product was shattered when crushed with a finger.

【0005】そこで本発明者は、いわゆる人工いくらの
製法にヒントを得て、脱臭微粉末剤を水溶性アルギン酸
塩水溶液に混合したものを、ある種の金属塩水溶液や酸
あるいはアルコール中に滴下させて液滴の表面をゲル化
させ、これを乾燥して粒剤化するという技術を開発する
とともに(特開平2−298346号参照)、このよう
な造粒に使用するのに適するノズルとして、管体端部よ
り線体を延長形成した滴下部を有するものを開発した
(特開平3−202138号参照)。
Therefore, the inventor of the present invention inspired the so-called artificial production method and dropped a mixture of the deodorized fine powder in a water-soluble alginate aqueous solution into a certain metal salt aqueous solution, an acid or alcohol. In addition to developing a technique of gelling the surface of the droplets by drying and granulating the droplets by drying (see JP-A-2-298346), a nozzle suitable for use in such granulation is a tube. A device having a drip portion formed by extending a linear body from the body end has been developed (see JP-A-3-202138).

【0006】しかし、このようなノズルを使用しても滴
下という一種の自然現象を利用するものであるため、単
位時間当たりの製造量には自ずから限界があり、工業的
生産に見合うだけの効率の良い製造が行なえない。また
このノズルは、粒径の大きさをある程度調節することは
できるものの、その範囲は狭く、多様なニーズに対応し
てもっと幅広く自由に粒径調節を行なえるものが望まれ
ていた。更にまたノズルが詰まることもあり、その修復
にも時間と労力が掛かる。このように幾つかの課題をか
かえていた。
However, even if such a nozzle is used, since a kind of natural phenomenon called dripping is used, the production amount per unit time is naturally limited, and the efficiency of the production is high enough to meet industrial production. Good manufacturing cannot be performed. Further, although the size of the particle size can be adjusted to some extent, the nozzle has a narrow range, and it is desired that the nozzle can be adjusted more widely and freely to meet various needs. Further, the nozzle may be clogged, and repairing the nozzle takes time and effort. In this way, we had some issues.

【0007】[0007]

【開発を試みた技術的事項】本発明はこのような背景に
鑑みなされたものであって、脱臭粒剤を製造するにあた
り、より効率的に製造でき且つ広域な粒径調節可能な脱
臭粒剤の製造方法並びにその装置の開発を試みたもので
ある。
[Technical matters attempted to be developed] The present invention has been made in view of such a background, and in producing a deodorizing granule, a deodorizing granule which can be produced more efficiently and whose particle diameter can be adjusted over a wide range. An attempt was made to develop a manufacturing method and an apparatus therefor.

【0008】[0008]

【発明の構成】Configuration of the Invention

【目的達成の手段】即ち本出願の第一の発明たる脱臭粒
剤の製造方法は、分散粒保持室と分散原液供給室との間
を多孔性隔壁で仕切り、分散原液供給室には脱臭微粉末
を水溶性アルギン酸塩水溶液に分散させた分散原液を前
記分散粒保持室よりも加圧状態で供給し、この分散原液
を前記多孔性隔壁を介して分散粒保持室側へ滴化状態で
押し出し、この液滴を分散粒保持液と反応させて液滴の
少なくとも表面をゲル化させて中間生成物とし、これを
乾燥して粒体化させることを特徴として成るものであ
る。
Means for Achieving the Object In a first aspect of the present invention, a method for producing a deodorant granule comprises a partition wall between a dispersion particle holding chamber and a dispersion stock solution supply chamber, and a fine deodorization fine dispersion chamber. A stock dispersion obtained by dispersing the powder in a water-soluble alginate aqueous solution is supplied in a pressurized state from the dispersion particle holding chamber, and this dispersion stock solution is extruded in a droplet state to the dispersion particle holding chamber side through the porous partition wall. The droplets are reacted with a dispersed particle holding liquid to gel at least the surface of the droplets to form an intermediate product, which is dried and granulated.

【0009】また本出願の第二の発明たる脱臭粒剤の製
造方法は、前記要件に加えて前記分散原液供給室の加圧
は、周期的に加圧と非加圧を繰り返す方法で行うことを
特徴として成るものである。
Further, in the method for producing a deodorizing granule according to the second invention of the present application, in addition to the above-mentioned requirements, the pressurizing of the dispersion stock solution supply chamber is performed by a method of periodically repeating pressurizing and non-pressurizing. It is characterized by the following.

【0010】更に本出願の第三の発明たる脱臭粒剤の製
造方法は、分散粒保持室と分散原液供給室との間を多孔
性隔壁で仕切り、分散粒保持室には分散粒保持液を一定
方向に流動させ、一方分散原液供給室には脱臭微粉末を
水溶性アルギン酸塩水溶液に分散させた分散原液を分散
粒保持室よりも加圧状態で供給し、この分散原液が前記
多孔性隔壁を介して分散粒保持室側へ流れ出たものを分
散粒保持液の流動により剪断して液滴化させるととも
に、この液滴と分散粒保持液との反応により液滴の少な
くとも表面をゲル化させて中間生成物とし、これを乾燥
して粒体化させることを特徴として成るものである。
Further, in the method for producing a deodorizing granule according to the third invention of the present application, the dispersion particle holding chamber and the dispersion liquid supply chamber are partitioned by a porous partition, and the dispersion particle holding liquid is filled in the dispersion particle holding chamber. The dispersion liquid is supplied in a certain direction, and the dispersion liquid supply chamber is supplied with a dispersion liquid in which deodorized fine powder is dispersed in a water-soluble alginate aqueous solution under a higher pressure than the dispersion particle holding chamber. The liquid that has flowed out to the dispersed particle holding chamber through is sheared by the flow of the dispersed particle holding liquid to form droplets, and at least the surface of the droplets is gelled by the reaction between the droplets and the dispersed particle holding liquid. To produce an intermediate product, which is dried and granulated.

【0011】更にまた本出願の第四の発明たる脱臭粒剤
の製造方法は、前記要件に加えて前記分散粒保持液は多
価金属イオンとなり得る金属塩水溶液であることを特徴
として成るものである。
Further, the method for producing a deodorizing granule according to the fourth invention of the present application is characterized in that, in addition to the above requirements, the dispersion particle holding liquid is an aqueous solution of a metal salt which can be a polyvalent metal ion. is there.

【0012】更にまた本出願の第五の発明たる脱臭粒剤
の製造方法は、前記要件に加えて前記分散粒保持液は酸
であることを特徴として成るものである。
Further, the method for producing a deodorizing granule according to the fifth invention of the present application is characterized in that, in addition to the above requirements, the dispersion particle holding liquid is an acid.

【0013】更にまた本出願の第六の発明たる脱臭粒剤
の製造方法は、前記要件に加えて前記分散粒保持液はア
ルコールであることを特徴として成るものである。
Further, the method for producing a deodorizing granule according to the sixth invention of the present application is characterized in that, in addition to the above requirements, the dispersion particle holding liquid is alcohol.

【0014】更にまた本出願の第七の発明たる脱臭粒剤
の製造方法は、前記要件に加えて前記脱臭微粉末は酸化
物系白色脱臭剤であることを特徴として成るものであ
る。
Further, the method for producing a deodorizing granule according to the seventh invention of the present application is characterized in that, in addition to the above requirements, the deodorizing fine powder is an oxide-based white deodorizing agent.

【0015】更にまた本出願の第八の発明たる脱臭粒剤
の製造装置は、分散粒保持液を静止または一定方向に流
動状態で注入した分散粒保持室と、脱臭微粉末を含む分
散原液を分散粒保持室よりも加圧状態で注入した分散原
液供給室とが多孔性隔壁で仕切られており、分散原液供
給室側から多孔性隔壁を介して分散粒保持室側へ分散原
液を滴化状態で押し出し、あるいは分散原液供給室側か
ら多孔性隔壁を介して分散粒保持室側へ流れた分散原液
を分散粒保持液の流動により剪断して液滴化させるよう
にしたことを特徴としてなるものである。これら発明に
より前記目的を達成せんとするものである。
Further, an apparatus for producing a deodorizing granule according to an eighth aspect of the present invention comprises a dispersion particle holding chamber into which a dispersion particle holding liquid is injected in a stationary or flowing state in a fixed direction, and a dispersion stock solution containing deodorized fine powder. The dispersion stock solution supply chamber injected under pressure from the dispersion grain holding chamber is separated by a porous partition, and the dispersion stock solution is dropped from the dispersion stock solution supply chamber side to the dispersion grain holding chamber side via the porous partition wall. The dispersion stock solution extruded in the state or flowing from the dispersion stock solution supply chamber side to the dispersion grain holding chamber side via the porous partition wall is sheared by the flow of the dispersion grain holding liquid to form droplets. Things. It is an object of the present invention to achieve the above object.

【0016】[0016]

【発明の作用】本発明では、分散原液が分散原液供給室
から多孔性隔壁に形成された複数の小孔を介して分散粒
保持室側へ押し出され、表面張力により液滴化されて複
数の液滴が一度に製造できる。
According to the present invention, the undiluted dispersion liquid is extruded from the undiluted dispersion supply chamber to the dispersed particle holding chamber through a plurality of small holes formed in the porous partition wall, and is formed into droplets by surface tension. Droplets can be manufactured at once.

【0017】また分散粒保持液を流動させる場合には、
各小孔から分散粒保持室側へ流れ出した分散原液がこの
流動によって剪断されて分散原液の液滴化がなされるた
め、短時間に多くの液滴を作ることができるとともに、
分散原液供給室の圧力、分散粒保持液の流速等のパラメ
ータを変えることで幅広い粒径寸法の脱臭粒剤を製造す
ることができる。
When the dispersed particle holding liquid is caused to flow,
Since the undiluted dispersion flowing out from each small hole to the dispersed particle holding chamber side is sheared by this flow to form droplets of the undiluted dispersion, many droplets can be made in a short time,
Deodorizing granules having a wide range of particle sizes can be manufactured by changing parameters such as the pressure of the dispersion stock solution supply chamber and the flow rate of the dispersed particle holding solution.

【0018】[0018]

【実施例】以下本発明を図示の実施例に基づいて説明す
る。図中符号1は、本発明たる脱臭粒剤の製造方法を実
施するための一例たる粒剤製造装置であって、このもの
は一例として一端を閉塞した内パイプ2の一部回りに上
下に蓋部3aと底部3bとを有する筒状であって、その
断面が内パイプ2と同心円となるように外パイプ3が設
けられて成る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on the illustrated embodiment. In the figure, reference numeral 1 denotes a granule production apparatus as an example for carrying out the method for producing a deodorized granule according to the present invention, which is, as an example, a top and bottom cover around a part of an inner pipe 2 having one end closed. It has a cylindrical shape having a portion 3a and a bottom portion 3b, and is provided with an outer pipe 3 so that its cross section is concentric with the inner pipe 2.

【0019】そして内パイプ2の内部には分散原液供給
室4が形成され、外パイプ3の内面と内パイプ2の外面
とによって囲まれた部分には分散粒保持室5が形成され
る。また内パイプ2のうち外パイプ3によって囲まれた
筒状部分には、全体に亘って多数の小孔6が形成され、
これによって分散原液供給室4と分散粒保持室5とが連
絡されている。尚このように小孔6が多数形成された内
パイプ2の部分を多孔性隔壁7と定義する。
A raw dispersion liquid supply chamber 4 is formed inside the inner pipe 2, and a dispersed particle holding chamber 5 is formed at a portion surrounded by the inner surface of the outer pipe 3 and the outer surface of the inner pipe 2. Also, a large number of small holes 6 are formed in the entire cylindrical portion of the inner pipe 2 surrounded by the outer pipe 3,
Thereby, the dispersion liquid supply chamber 4 and the dispersion particle holding chamber 5 are connected to each other. The portion of the inner pipe 2 in which many small holes 6 are formed is defined as a porous partition 7.

【0020】因みに本実施例では内パイプ2と外パイプ
3との二重円筒構造を採るため内パイプ2の一部が多孔
性隔壁7を構成するが、粒剤製造装置が他の形態を採る
場合にも、要は分散原液供給室4と分散粒保持室5とが
隣接し、その境界部に多孔性隔壁7が形成される構造で
あればよいのである。
In this embodiment, a part of the inner pipe 2 constitutes the porous partition wall 7 in order to adopt a double cylindrical structure of the inner pipe 2 and the outer pipe 3, but the granule manufacturing apparatus takes another form. In this case, what is essential is that the dispersion liquid supply chamber 4 and the dispersed particle holding chamber 5 are adjacent to each other, and the porous partition wall 7 is formed at the boundary.

【0021】尚、多孔性隔壁7の形態としては、パンチ
ングメタルや金網または金属繊維等の金属多孔体を適宜
適用したもの、また例えば重油バーナーのノズルフィル
ターにおける金属焼結体のようなものが挙げられる他、
例えば脱臭粒剤に防虫、誘虫、嫌虫あるいは芳香といっ
た他の機能をもたせる場合には、一例として図4に示す
ような多重のノズル10を分散原液供給室4と分散粒保
持室5との境界部に複数設け、これに対応して内パイプ
2を適宜図4のように変更してこれを多孔性隔壁7とし
てもよい。
As the form of the porous partition wall 7, a metal porous body such as a punching metal, a wire mesh or a metal fiber is appropriately applied, or a metal sintered body in a nozzle filter of a heavy oil burner, for example. Besides
For example, when the deodorizing granule is provided with other functions such as insect repellent, insect attractant, insect repellent or fragrance, multiple nozzles 10 as shown in FIG. The inner pipe 2 may be appropriately changed as shown in FIG.

【0022】ここで粒剤製造装置1の他の実施例につい
て簡単に説明すると、まず前記図1、2に示す粒剤製造
装置1において、分散原液Aと分散粒保持液Bとの位置
関係を逆にすることができる。即ち図示はしないが外パ
イプ3の一端を閉塞状態として分散原液Aを加圧状態で
供給し、一方内パイプ2に分散粒保持液Bを注入して、
中央にあるパイプから中間生成物Sを回収するようにし
てもよいのである。
Here, another embodiment of the granule manufacturing apparatus 1 will be briefly described. First, in the granule manufacturing apparatus 1 shown in FIGS. Can be reversed. That is, although not shown, one end of the outer pipe 3 is closed and the dispersion stock solution A is supplied in a pressurized state, while the dispersion particle holding liquid B is injected into the inner pipe 2,
The intermediate product S may be recovered from the central pipe.

【0023】要は粒剤製造装置は、分散粒保持室と、こ
れよりも加圧状態にある分散原液供給室とを具え、その
間に多孔性隔壁を有していれば、その形態及び各部の位
置関係は問わない。
The essential point is that the granule manufacturing apparatus includes a dispersion particle holding chamber and a dispersion liquid supply chamber which is more pressurized than this, and if a porous partition is provided between the chamber, the form and the parts The positional relationship does not matter.

【0024】粒剤製造装置1は以上のような構造を有す
るものであり、以下このものを用いて脱臭粒剤を製造す
る方法について説明するが、その前にそれぞれ分散原液
供給室4と分散粒保持室5とに供給される分散原液Aと
分散粒保持液Bとについてここで説明する。
The granule manufacturing apparatus 1 has the above-described structure. A method for manufacturing a deodorizing granule using the granule manufacturing apparatus will be described below. Here, the dispersion stock solution A and the dispersion particle holding solution B supplied to the holding chamber 5 will be described.

【0025】まず分散原液Aに含まれる脱臭微粉末は、
粒径がミクロンないしサブミクロンオーダーの微粉末状
の脱臭剤であり、一例として酸化亜鉛と二酸化チタンと
水分子とが緊密に結合した粒子の集合体(特開昭63−
54935号参照)や、酸化亜鉛と酸化アルミニウムお
よび/または酸化珪素との緊密結合体粒子の集合体(特
開昭63−246167号)が挙げられる。尚、この粒
子の集合体は白色であるため、白色の脱臭粒剤を製造す
る場合に使用できる。また脱臭微粉末剤はこのほかに
も、酸化チタン、酸化亜鉛、酸化マグネシウム、酸化カ
ルシウム、酸化アルミニウム、酸化珪素等の吸着性のあ
る酸化物の一部または全部を主体とした白色系のものや
その他従来公知のものを使用することもできる。
First, the deodorized fine powder contained in the dispersion liquid A is
A fine powder type deodorant having a particle diameter of the order of microns or submicrons. As an example, an aggregate of particles in which zinc oxide, titanium dioxide and water molecules are tightly bound (Japanese Patent Application Laid-Open No.
54935) and an aggregate of tightly-bound particles of zinc oxide and aluminum oxide and / or silicon oxide (JP-A-63-246167). Since the aggregate of these particles is white, it can be used for producing a white deodorizing granule. In addition, the deodorized fine powder may also be a white powder mainly containing a part or all of adsorbable oxides such as titanium oxide, zinc oxide, magnesium oxide, calcium oxide, aluminum oxide and silicon oxide. Other conventionally known materials can also be used.

【0026】次に分散原液Aの分散媒となっている水溶
性アルギン酸塩水溶液について説明する。このものは具
体的にはアルギン酸ナトリウムに代表されるものの水溶
液であり、ほかにもアルギン酸アンモニウムなどを使用
することができる。ここでは代表してアルギン酸ナトリ
ウムについて説明する。
Next, an aqueous solution of a water-soluble alginate serving as a dispersion medium for the dispersion stock solution A will be described. This is, specifically, an aqueous solution of sodium alginate, and ammonium alginate and the like can also be used. Here, sodium alginate will be described as a representative.

【0027】このアルギン酸ナトリウムは、コンブ、カ
ジメ、アラメなどの褐藻類の細胞膜を形成する物質であ
り、乳化安定剤、粘強剤、型剥離剤などとして用いられ
る。この物質は極めて高粘性のコロイド物質で親水性が
強く、冷水、温水、いずれにも良く溶解し、非常に粘稠
均一な溶液となる性質を有する。また、この溶液にアル
ミニウム、バリウム、カルシウム、銅、鉄、鉛、亜鉛、
ニッケルなどの金属塩を加えると、水に不溶性のアルギ
ン酸塩となる。因みに、請求項4に記載した発明はアル
ギン酸ナトリウムのこのような性質を利用するものであ
る。
This sodium alginate is a substance that forms a cell membrane of brown algae such as kelp, scallop, and alame, and is used as an emulsion stabilizer, a thickener, a mold release agent, and the like. This substance is an extremely high-viscosity colloidal substance, has a strong hydrophilicity, and is well soluble in cold water and hot water, and has the property of being a very viscous and uniform solution. In addition, aluminum, barium, calcium, copper, iron, lead, zinc,
Addition of a metal salt such as nickel results in a water-insoluble alginate. Incidentally, the invention described in claim 4 utilizes such properties of sodium alginate.

【0028】またアルギン酸ナトリウムに酸を加える
と、ゲル状で水に不溶のアルギン酸となる。因みに請求
項5に記載した発明は、アルギン酸ナトリウムのこのよ
うな性質を利用するものである。
When an acid is added to sodium alginate, it becomes a gel-like water-insoluble alginic acid. Incidentally, the invention described in claim 5 utilizes such properties of sodium alginate.

【0029】次に分散粒保持液Bとしては請求項4、
5、6にそれぞれ記載したように多価金属イオンとなり
得る金属塩水溶液、酸またはアルコールが適用できる。
まず請求項4記載の発明における多価金属イオンとなり
得る金属塩水溶液は、具体的にはアルミニウム、バリウ
ム、カルシウム、銅、鉄、鉛、亜鉛、ニッケルなどの塩
の水溶液がある。即ち、要はアルギン酸と結合したとき
に水に不溶ないしは難溶となるような金属を選定する。
尚、色付きの脱臭粒剤を得る一つの方法として多価金属
イオンの色を発色させることができるが、その例として
は鉄イオンの赤褐色、銅イオンの黄青色、金イオンの青
紫色、ニッケルイオンの淡黄緑色などがある。
Next, the dispersed particle holding liquid B is described in claim 4,
As described in 5 and 6, an aqueous solution of a metal salt which can become a polyvalent metal ion, an acid or an alcohol can be applied.
First, the aqueous solution of a metal salt that can be a polyvalent metal ion in the invention of claim 4 specifically includes an aqueous solution of a salt of aluminum, barium, calcium, copper, iron, lead, zinc, nickel, or the like. That is, a metal that is insoluble or hardly soluble in water when combined with alginic acid is selected.
Incidentally, as one method of obtaining colored deodorizing granules, the color of a polyvalent metal ion can be developed, and examples thereof include reddish brown of iron ion, yellow blue of copper ion, blue purple of gold ion, and nickel ion. And pale yellow-green.

【0030】また請求項5記載の発明における酸は、塩
酸、硫酸、硝酸などに代表される強酸のほか、アルギン
酸よりも強い醋酸等の弱酸を含むものである。
The acid in the invention according to claim 5 includes a strong acid represented by hydrochloric acid, sulfuric acid, nitric acid and the like, and a weak acid such as acetic acid which is stronger than alginic acid.

【0031】更に請求項6記載の発明におけるアルコー
ルとは、鎖式または脂環式炭化水素の水素原子、または
芳香族炭化水素の側鎖の水素原子を水酸基で置換した構
造をもつ化合物を言い、例えばメタノール、エタノール
などがある。
The alcohol in the invention according to claim 6 is a compound having a structure in which a hydrogen atom of a chain or alicyclic hydrocarbon or a hydrogen atom of a side chain of an aromatic hydrocarbon is substituted with a hydroxyl group. For example, there are methanol, ethanol and the like.

【0032】分散原液A及び分散粒保持液Bは以上のよ
うな構成のものであり、脱臭粒剤の製造にあたっては、
まず分散原液Aを分散原液供給室4に一定の加圧状態で
供給するとともに、分散粒保持室5には取入口8から分
散粒保持液Bを供給し、これを排出口9から流し出すよ
うにして分散粒保持室5の上方から下方への定常的な流
動を維持するようにする。尚、分散粒保持液Bの流動形
態は、多孔性隔壁7の回りを旋回するように流したり、
多孔性隔壁7の周辺で局部的にヘリカル流等の剪断能力
の高い渦を生じさせるように流動させてもよい。
The dispersion stock solution A and the dispersion particle holding solution B are configured as described above.
First, the dispersion stock solution A is supplied to the dispersion stock solution supply chamber 4 under a constant pressurized state, and the dispersion grain holding liquid B is supplied to the dispersion grain holding chamber 5 from the intake port 8 and flows out from the discharge port 9. Thus, a steady flow from the upper side to the lower side of the dispersed particle holding chamber 5 is maintained. In addition, the flow form of the dispersed particle holding liquid B is such that the liquid is swirled around the porous partition wall 7,
The fluid may be caused to locally generate a vortex having a high shearing capability such as a helical flow around the porous partition wall 7.

【0033】このようにすれば分散原液供給室4と分散
粒保持室5との圧力差により分散原液Aが分散粒保持室
5側へ流れ出ようとするが、分散粒保持液Bの流れによ
って分散粒保持室5側へ流れ出ようとする分散原液Aは
図3に示すように剪断されて液滴aとなり、分散粒保持
液Bの流れにのって下方へ移送される。この液滴aは分
散粒保持液B中で浮遊している間に分散粒保持液Bの種
類に応じてそれぞれ次のような反応を生じて液滴aの表
面ないし液滴中央にかけてゲル化する。
In this way, the dispersion liquid A tends to flow toward the dispersion particle holding chamber 5 due to the pressure difference between the dispersion liquid supply chamber 4 and the dispersion particle holding chamber 5. The undiluted dispersion A that is going to flow out to the particle holding chamber 5 is sheared into droplets a as shown in FIG. While the droplet a is floating in the dispersion particle holding liquid B, the following reaction occurs depending on the type of the dispersion particle holding liquid B, and the droplet a is gelled from the surface of the droplet a to the center of the droplet. .

【0034】即ち多価金属イオンとなり得る金属塩水溶
液を分散粒保持液Bとする場合には、アルギン酸ナトリ
ウムのナトリウムイオンが多価金属イオンたる例えばカ
ルシウムイオンに置換して、水に不溶なゲル状のアルギ
ン酸カルシウムの層を少なくとも表面に形成した中間生
成物を生ずる。
That is, when an aqueous solution of a metal salt that can become a polyvalent metal ion is used as the dispersion particle holding liquid B, the sodium ion of sodium alginate is replaced by a polyvalent metal ion such as calcium ion to form a water-insoluble gel. To form an intermediate product having a layer of calcium alginate formed on at least the surface.

【0035】また酸を分散粒保持液Bとする場合には、
アルギン酸ナトリウムのナトリウムイオンが水素イオン
に置換して、水に不溶なゲル状のアルギン酸の層を少な
くとも表面に形成した中間生成物を生ずる。
When the acid is used as the dispersion particle holding liquid B,
The sodium ions of the sodium alginate are replaced by hydrogen ions, resulting in an intermediate product having a water-insoluble, gel-like layer of alginic acid formed on at least the surface.

【0036】更にまたアルコールを分散粒保持液Bとす
る場合には、水溶性アルギン酸塩と水和状態にある水分
子がアルコールの脱水作用により脱水されるため、水溶
性アルギン酸塩自体が水に不溶となって少なくとも表面
がゲル状の中間生成物を生ずる。
Further, when alcohol is used as the dispersion particle holding liquid B, the water molecules in the hydrated state with the water-soluble alginate are dehydrated by the dehydration of the alcohol, so that the water-soluble alginate itself is insoluble in water. To form an intermediate product having at least a gel surface.

【0037】表面ないし液滴中央にかけてゲル化した中
間生成物Sは、分散粒保持液Bと共に外パイプ3の底部
3bから排出され、網等により中間生成物Sだけが回収
される。このように回収された中間生成物Sは熱風乾燥
炉等を用いて外部加熱して乾燥する方法の他、誘電加熱
により自己発熱させる内部加熱を単独であるいは外部加
熱と併用して乾燥させてもよい。尚、分散原液Aにかけ
る圧力、分散粒保持液Bの流速を変えることで中間生成
物Sの大きさを種々変えることができる。
The intermediate product S that has gelled from the surface to the center of the droplet is discharged from the bottom 3b of the outer pipe 3 together with the dispersed particle holding liquid B, and only the intermediate product S is recovered by a net or the like. The intermediate product S thus recovered may be dried by external heating using a hot-air drying furnace or the like, or may be dried alone or in combination with external heating by self-heating by dielectric heating. Good. The size of the intermediate product S can be variously changed by changing the pressure applied to the dispersion stock solution A and the flow rate of the dispersion particle holding solution B.

【0038】ここで誘電加熱とは、高周波数帯域の電界
内に誘電体たる加熱物を置き、その誘電体の分子が印加
電界の方向に一致しようとして、常に回転を繰り返して
隣接分子と摩擦を起こし、この摩擦熱で内部から発熱す
る原理を応用する加熱方式であり、食品、木材等、水分
を含むものの加熱、乾燥、更には樹脂シート、プラスチ
ック等の接着等の加工に利用されている技術である。一
般に誘電加熱の特徴としては加熱に要する時間が短い、
熱効率が高い、加熱電力の制御が容易で応答が速い、複
雑な形状のものでも比較的均一に加熱できるなどが挙げ
られるが、中間生成物を誘電加熱して乾燥させれば、気
化した内部水分が膨張し、外部に放出され、若干なりと
も発泡作用を起こして膨化した脱臭粒剤が得られる。
Here, the dielectric heating is to place a heated object as a dielectric in an electric field in a high frequency band, and to constantly rotate the dielectric material in such a way that the dielectric molecules try to match the direction of the applied electric field, thereby causing friction with adjacent molecules. This is a heating method that applies the principle of generating heat from the inside due to this frictional heat, and is used for heating and drying foods, wood, etc. that contain moisture, and also for processing resin sheets, plastics, etc. It is. Generally, the characteristic of dielectric heating is that the time required for heating is short,
High heat efficiency, easy control of heating power, quick response, and relatively uniform heating of complex shapes are possible.If the intermediate product is dried by dielectric heating, the vaporized internal moisture Are swollen and released to the outside, and a foaming action is caused to some extent to obtain a swollen deodorized granule.

【0039】因みにこのように膨化した脱臭粒剤は表面
積が大きくなるため、脱臭能力の高いものとなる。尚、
膨化した脱臭粒剤を製造するには、中間生成物を真空凍
結乾燥法で乾燥してもよい。また尚、脱臭微粉末剤とし
て酸化亜鉛と二酸化チタンと水分子とが緊密に結合した
粒子の集合体を使用した場合には、乾燥時に100℃を
超えると変色するため、これ以下の温度で乾燥するよう
にする。また乾燥した脱臭粒剤を焼成して脱臭粒剤中に
金属酸化物(例えば酸化カルシウム)を生じさせ、水、
一酸化炭素、二酸化炭素の吸着能をも発揮できるように
してもよい。
Incidentally, the expanded deodorizing granules have a large surface area, and therefore have a high deodorizing ability. still,
In order to produce a swollen deodorant granule, the intermediate product may be dried by a vacuum freeze-drying method. In addition, when an aggregate of particles in which zinc oxide, titanium dioxide, and water molecules are tightly bound is used as a deodorizing fine powder, the color changes when the temperature exceeds 100 ° C. during drying. To do it. Further, the dried deodorizing granules are fired to generate metal oxides (eg, calcium oxide) in the deodorizing granules, and water,
You may make it also exhibit the adsorption capability of carbon monoxide and carbon dioxide.

【0040】更に前述したように分散粒保持液Bとして
酸を適用した場合には、アルギン酸ナトリウムの液滴a
との接触によりアルギン酸のゲルとなるが、更にこのア
ルギン酸のゲルの水素をアルカリ金属以外の金属(例え
ばアルミニウム、バリウム等)に置換することで、脱臭
機能に併せて、置換した金属の触媒機能を得ることもで
きる(特開平1−343543号公報参照)。
Further, as described above, when an acid is applied as the dispersion particle holding liquid B, a droplet a of sodium alginate is used.
Although the gel of alginic acid is formed by contact with hydrogen, the hydrogen of the gel of alginic acid is further substituted with a metal other than an alkali metal (for example, aluminum, barium, etc.), so that the catalyst function of the substituted metal can be performed in addition to the deodorizing function. Can also be obtained (see JP-A-1-343543).

【0041】また更には乾燥した脱臭粒剤あるいは乾燥
前の中間生成物Sを例えば不織布内に入れてシート状に
することもできる。因みにこのような方法の一例として
特願平2−24015号、特願平2−24016号など
がある。
Further, the dried deodorizing granules or the intermediate product S before drying can be put into, for example, a nonwoven fabric to form a sheet. Incidentally, as an example of such a method, there are Japanese Patent Application No. 2-24015 and Japanese Patent Application No. 2-24016.

【0042】次に上記粒剤製造装置1を用いた分散原液
Aの他の液滴化方法について説明する。上記方法では分
散粒保持液Bを流動させて分散原液Aを剪断し液滴aを
製造するものであるが、分散粒保持液Bは必ずしも流動
させる必要はなく、分散原液供給室4の圧力によって多
孔性隔壁7の小孔6から押し出された分散原液Aを、そ
の表面張力により自然に液滴化させる方法を採ってもよ
いし、分散原液供給室4内の分散原液Aにかける加圧状
態を周期的に加圧と非加圧を繰り返すようにすること
で、分散原液Aが多孔性隔壁7の小孔6から瞬間的に飛
び出して液滴化する方法を採用することもできる。尚勿
論このような方法を採用する場合であっても、分散粒保
持液Bを流動させるようにしてもよい。
Next, another method of forming droplets of the dispersion stock solution A using the granule manufacturing apparatus 1 will be described. In the above-described method, the dispersion particle holding liquid B is caused to flow to shear the dispersion liquid A to produce the droplets a. However, the dispersion particle holding liquid B does not necessarily need to flow, and the pressure of the dispersion liquid supply chamber 4 depends on the pressure. The dispersion stock solution A extruded from the small holes 6 of the porous partition wall 7 may be naturally formed into droplets by its surface tension, or a pressurized state applied to the dispersion stock solution A in the dispersion stock solution supply chamber 4. By periodically repeating pressurization and non-pressurization, a method in which the dispersion stock solution A instantaneously jumps out of the small holes 6 of the porous partition wall 7 to form droplets can be adopted. Of course, even when such a method is adopted, the dispersed particle holding liquid B may be caused to flow.

【0043】[0043]

【発明の効果】本発明では分散粒保持室5と分散原液供
給室4との間を多孔性隔壁7で仕切り、前記分散粒保持
室5には分散粒保持液Bを一定方向に流動させ、一方分
散原液供給室4には脱臭微粉末を水溶性アルギン酸塩水
溶液に分散させた分散原液Aを分散粒保持室5よりも加
圧状態で供給し、この分散原液Aが前記多孔性隔壁7を
介して分散粒保持室5側へ流れ出たものを分散粒保持液
Bの流動により剪断して液滴化させるとともに、この液
滴aと分散粒保持液Bとの反応により液滴の少なくとも
表面をゲル化させて中間生成物Sとし、これを乾燥して
粒体化させるから、多孔性隔壁7の小孔6の数に応じて
一度に多くの中間生成物Sを造ることができ、効率のよ
い脱臭粒剤の製造を行なうことができる。また分散原液
供給室の圧力や分散粒保持液の流速を種々変えること
で、種々の粒径の脱臭粒剤を簡単に容易に製造すること
ができる。
According to the present invention, the dispersion particle holding chamber 5 and the undiluted liquid supply chamber 4 are partitioned by the porous partition walls 7, and the dispersed particle holding liquid B flows in the dispersion particle holding chamber 5 in a certain direction. On the other hand, a dispersion stock solution A in which deodorized fine powder is dispersed in a water-soluble alginate aqueous solution is supplied to the dispersion stock solution supply chamber 4 under a higher pressure than the dispersion particle holding chamber 5. What has flowed out to the dispersed particle holding chamber 5 through the flow of the dispersed particle holding liquid B is sheared into droplets, and at least the surface of the droplets is reacted by the droplet a and the dispersed particle holding liquid B. Since the intermediate product S is gelled to be dried and granulated, a large number of intermediate products S can be produced at one time according to the number of the small holes 6 of the porous partition wall 7, and the efficiency is improved. Good deodorizing granules can be produced. By changing the pressure of the dispersion liquid supply chamber and the flow rate of the dispersion particle holding liquid in various ways, deodorizing granules having various particle diameters can be easily and easily produced.

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

【図1】本発明の脱臭粒剤の製造装置を示す透視斜視図
である。
FIG. 1 is a perspective view showing an apparatus for producing a deodorizing granule of the present invention.

【図2】同上縦断面図である。FIG. 2 is a longitudinal sectional view of the same.

【図3】同上多孔性隔壁部分を拡大して示す縦断面図で
ある。
FIG. 3 is an enlarged longitudinal sectional view showing a porous partition wall portion of the same.

【図4】多孔性隔壁の他の実施例を示す縦断面図であ
る。
FIG. 4 is a longitudinal sectional view showing another embodiment of the porous partition.

【符号の説明】[Explanation of symbols]

1 粒剤製造装置 2 内パイプ 3 外パイプ 3a 蓋部 3b 底部 4 分散原液供給室 5 分散粒保持室 6 小孔 7 多孔性隔壁 8 取入口 9 排出口 10 ノズル A 分散原液 a 液滴 B 分散粒保持液 S 中間生成物 DESCRIPTION OF SYMBOLS 1 Granule manufacturing apparatus 2 Inner pipe 3 Outer pipe 3a Lid 3b Bottom 4 Dispersion liquid supply chamber 5 Dispersion particle holding chamber 6 Small hole 7 Porous partition wall 8 Inlet 9 Discharge port 10 Nozzle A Dispersion liquid a Droplet B Dispersion particles Retentate S Intermediate product

Claims (8)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 分散粒保持室と分散原液供給室との間を
多孔性隔壁で仕切り、分散原液供給室には脱臭微粉末を
水溶性アルギン酸塩水溶液に分散させた分散原液を前記
分散粒保持室よりも加圧状態で供給し、この分散原液を
前記多孔性隔壁を介して分散粒保持室側へ滴化状態で押
し出し、この液滴を分散粒保持液と反応させて液滴の少
なくとも表面をゲル化させて中間生成物とし、これを乾
燥して粒体化させることを特徴とする脱臭粒剤の製造方
法。
A porous partition wall separates a dispersion particle holding chamber and a dispersion stock solution supply chamber, and a dispersion stock solution in which deodorized fine powder is dispersed in a water-soluble alginate aqueous solution is stored in the dispersion stock solution supply chamber. The dispersion source solution is supplied in a pressurized state from the chamber, and this dispersion stock solution is extruded in the form of droplets through the porous partition wall toward the dispersion particle holding chamber, and the droplets are reacted with the dispersion particle holding solution to form at least the surface of the droplets. A method for producing a deodorizing granule, which comprises gelling an intermediate product, drying the granulated product and granulating the intermediate product.
【請求項2】 前記分散原液供給室の加圧は、周期的に
加圧と非加圧を繰り返す方法で行うことを特徴とする請
求項1記載の脱臭粒剤の製造方法。
2. The method for producing a deodorizing granule according to claim 1, wherein the pressurization of the dispersion liquid supply chamber is performed by a method of periodically repeating pressurization and non-pressurization.
【請求項3】 分散粒保持室と分散原液供給室との間を
多孔性隔壁で仕切り、分散粒保持室には分散粒保持液を
一定方向に流動させ、一方分散原液供給室には脱臭微粉
末を水溶性アルギン酸塩水溶液に分散させた分散原液を
分散粒保持室よりも加圧状態で供給し、この分散原液が
前記多孔性隔壁を介して分散粒保持室側へ流れ出たもの
を分散粒保持液の流動により剪断して液滴化させるとと
もに、この液滴と分散粒保持液との反応により液滴の少
なくとも表面をゲル化させて中間生成物とし、これを乾
燥して粒体化させることを特徴とする脱臭粒剤の製造方
法。
3. The dispersion particle holding chamber and the raw dispersion liquid supply chamber are partitioned by a porous partition wall, and the dispersed particle holding liquid is caused to flow in a fixed direction in the dispersed particle holding chamber, while the deodorized fine liquid is supplied to the raw dispersion liquid supply chamber. An undiluted dispersion obtained by dispersing the powder in an aqueous solution of a water-soluble alginate is supplied under pressure from the dispersion particle holding chamber, and the undiluted dispersion liquid flowing out to the dispersed particle holding chamber through the porous partition wall is dispersed particles. The liquid is sheared by the flow of the retentate to form droplets, and at least the surface of the droplets is gelled by the reaction between the droplets and the dispersed particle retentate to form an intermediate product, which is dried and granulated. A method for producing a deodorizing granule, comprising:
【請求項4】 前記分散粒保持液は多価金属イオンとな
り得る金属塩水溶液であることを特徴とする請求項1、
2または3記載の脱臭粒剤の製造方法。
4. The method according to claim 1, wherein the dispersed particle holding liquid is an aqueous solution of a metal salt that can be a polyvalent metal ion.
4. The method for producing a deodorizing granule according to 2 or 3.
【請求項5】 前記分散粒保持液は酸であることを特徴
とする請求項1、2または3記載の脱臭粒剤の製造方
法。
5. The method for producing a deodorizing granule according to claim 1, wherein the dispersion particle holding liquid is an acid.
【請求項6】 前記分散粒保持液はアルコールであるこ
とを特徴とする請求項1、2または3記載の脱臭粒剤の
製造方法。
6. The method for producing a deodorizing granule according to claim 1, wherein the dispersion particle holding liquid is alcohol.
【請求項7】 前記脱臭微粉末は酸化物系白色脱臭剤で
あることを特徴とする請求項1、2、3、4、5または
6記載の脱臭粒剤の製造方法。
7. The method for producing deodorizing granules according to claim 1, wherein said deodorizing fine powder is an oxide-based white deodorizing agent.
【請求項8】 分散粒保持液を静止または一定方向に流
動状態で注入した分散粒保持室と、脱臭微粉末を含む分
散原液を分散粒保持室よりも加圧状態で注入した分散原
液供給室とが多孔性隔壁で仕切られており、分散原液供
給室側から多孔性隔壁を介して分散粒保持室側へ分散原
液を滴化状態で押し出し、あるいは分散原液供給室側か
ら多孔性隔壁を介して分散粒保持室側へ流れた分散原液
を分散粒保持液の流動により剪断して液滴化させるよう
にしたことを特徴とする脱臭粒剤の製造装置。
8. A dispersion particle holding chamber into which the dispersion particle holding liquid is injected in a stationary or flowing state in a fixed direction, and a dispersion source liquid supply chamber into which a dispersion raw liquid containing deodorized fine powder is injected under a higher pressure than the dispersion particle holding chamber. Are separated by a porous partition wall, and the dispersion raw liquid is extruded in a droplet state from the dispersion raw liquid supply chamber side to the dispersed particle holding chamber side through the porous partition wall, or through the porous raw liquid supply chamber side through the porous partition wall. An apparatus for producing a deodorizing granule, characterized in that the undiluted dispersion flowing to the side of the dispersed particle holding chamber is sheared by the flow of the dispersed particle holding liquid to form droplets.
JP31536291A 1991-11-01 1991-11-01 Method and apparatus for producing deodorizing granules Expired - Fee Related JP3151538B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31536291A JP3151538B2 (en) 1991-11-01 1991-11-01 Method and apparatus for producing deodorizing granules

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31536291A JP3151538B2 (en) 1991-11-01 1991-11-01 Method and apparatus for producing deodorizing granules

Publications (2)

Publication Number Publication Date
JPH05123570A JPH05123570A (en) 1993-05-21
JP3151538B2 true JP3151538B2 (en) 2001-04-03

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Country Link
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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4803508B2 (en) 2009-12-04 2011-10-26 国立大学法人九州大学 Method and apparatus for producing a composition in which a dispersed phase is finely dispersed in a continuous phase
WO2012133736A1 (en) * 2011-03-31 2012-10-04 国立大学法人九州大学 Method and device for producing composition having dispersed phase finely dispersed in continuous phase

Also Published As

Publication number Publication date
JPH05123570A (en) 1993-05-21

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