JPS6061038A - Reaction process - Google Patents

Reaction process

Info

Publication number
JPS6061038A
JPS6061038A JP58170069A JP17006983A JPS6061038A JP S6061038 A JPS6061038 A JP S6061038A JP 58170069 A JP58170069 A JP 58170069A JP 17006983 A JP17006983 A JP 17006983A JP S6061038 A JPS6061038 A JP S6061038A
Authority
JP
Japan
Prior art keywords
reaction
tank
catalyst
filter
small
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP58170069A
Other languages
Japanese (ja)
Inventor
Kenji Mizuno
健二 水野
Yasushi Hibino
靖 日比野
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP58170069A priority Critical patent/JPS6061038A/en
Publication of JPS6061038A publication Critical patent/JPS6061038A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/42Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed subjected to electric current or to radiations this sub-group includes the fluidised bed subjected to electric or magnetic fields
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/005Pretreatment specially adapted for magnetic separation
    • B03C1/01Pretreatment specially adapted for magnetic separation by addition of magnetic adjuvants

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

PURPOSE:To separate catalyst magnetically with high efficiency after reaction by using small body of magnetic catalyst in a reaction system. CONSTITUTION:Reaction liquid is introduced into an intermediary tank 3 from a storage tank 1 of the reaction liquid, and small bodies of magnetic catalyst are added to the tank 3 to perform stirring. Then, the reaction liquid is introduced into a reaction tower 6. For an oxidation reaction, air is added by a blower 7, and the reaction liquid is introduced into a separation tank 10 after the reaction. A magnetic filter 9 comprising filter medium 9A and an exciting coil 9B for magnetizing the filter medium 9a is provided in the separation tank 10, and small catalyst body 4 is separated effectively and completely by the filter 9 in the tank 10. Produced reaction liquid is discharged through a discharge line 11. Furhter, when specified amt. of small catalyst body 4 is collected by th filter 9, the introduction of the produced liquid into the tank 10 is intermitted for a while, and back washing water is introduced from a waste water line 11 into the tank 10. Small catalyst 4 body collected by the filter 9 is back-washed and returned to the tank 3 through a returning line 12 and reutilized.

Description

【発明の詳細な説明】 本発明は反応方法に関するものである。触媒を用いる反
応には周知のように液体もしくは気体の反応系を触媒時
に送通して反応せしめる固定床方式、該反応系に触媒小
体を分散して反応せしめる流動床方式があるが、後者は
前者に比して触媒接触効率が高く、更には触媒を再生、
更新するために操業を停止する必要もなく望ましいもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a reaction method. As is well known, reactions using catalysts include a fixed bed method in which a liquid or gaseous reaction system is passed through the catalyst to cause a reaction, and a fluidized bed method in which a catalyst is dispersed in the reaction system to cause a reaction. Compared to the former, the catalyst contact efficiency is higher, and it is also possible to regenerate the catalyst.
It is also desirable that the update does not require stopping operations.

しかし反応系から触媒を効率よ(分離しにくい点に問題
がある。
However, there is a problem in that it is difficult to efficiently separate the catalyst from the reaction system.

本発明は上記流動床方式における問題点を解決すること
を目的とし、触媒を磁性体として磁気的に反応系から分
離することを骨子とする。
The present invention aims to solve the above-mentioned problems in the fluidized bed system, and its main feature is to magnetically separate the catalyst from the reaction system as a magnetic substance.

本発明を以下に詳細に説明する。The present invention will be explained in detail below.

本発明においては触媒を磁性体とする。触媒を磁性体と
する一般的な方法は金属である触媒をフェライFに取入
れることである。フェライトは周知のようにMO・Fe
2O3なる型の2価金属の塩でらりフェリ磁性を示し、
特に逆スピネル型(14造を有するものは強磁性を示す
。Mは触媒となる金属であり例えば酸化触媒や還元触媒
の場合にはFe、Co。
In the present invention, the catalyst is a magnetic material. A common method of making the catalyst magnetic is to incorporate a metal catalyst into Ferai-F. As is well known, ferrite is MO/Fe
It is a divalent metal salt of type 2O3 and exhibits ferrimagnetism.
In particular, those having an inverse spinel type (14 structure) exhibit ferromagnetism. M is a metal that serves as a catalyst, such as Fe or Co in the case of an oxidation catalyst or a reduction catalyst.

Ni 、 Rh、 T’d、 Pt ’$σ皿族もしく
はCu、 Ag、 Au等のIb族の金属である。上記
金属はフェライトに取入れられることにより上記したよ
うに磁性を有するようになるが、史にそれによって反応
系が水溶液の場合に溶出が防止されると言う予期せざる
効果も発現される。上記〕□ウライト触媒は例えばMの
塩の水溶液にFe2O3粉末を投入して加熱攪拌し、そ
の後詰Fe2O3を取出して還元焼成する方法によって
製造せられ、粉状1粒状9片状等のいわゆる小体に形成
される。、更に本発明の触媒はポリエチレン、ポリプロ
ピレン、ポリ塩化ビニル、ポリアミド等のプラスチック
、シリカ、アルミナ等のセラミック等を担体としてその
上に担持されてもよい。上記担体に本発明の触媒を担持
するには例えばボールミルにて混練するメカノケミカル
法が用りられる。
These are Ni, Rh, T'd, Pt'$σ disk group metals or Ib group metals such as Cu, Ag, and Au. When the metal is incorporated into ferrite, it becomes magnetic as described above, but it also has the unexpected effect of preventing elution when the reaction system is an aqueous solution. [Above] □ Urite catalyst is produced by, for example, adding Fe2O3 powder to an aqueous solution of the salt of M, heating and stirring, and then taking out the packed Fe2O3 and reducing and calcining it. is formed. Further, the catalyst of the present invention may be supported on a carrier such as a plastic such as polyethylene, polypropylene, polyvinyl chloride, or polyamide, or a ceramic such as silica or alumina. In order to support the catalyst of the present invention on the above-mentioned carrier, a mechanochemical method of kneading in a ball mill, for example, is used.

本発明の触媒は反応系に容易に分散せしめるためには比
重を反応系の比重に近似させることが望ましい。
In order to easily disperse the catalyst of the present invention in the reaction system, it is desirable that the specific gravity approximates the specific gravity of the reaction system.

第1図に本発明の一実施例を示す。図において(1)は
反応液の貯溜槽であり反応液はポンプ(2)Aの介在す
る導入径路(2)Kよって中継槽(3)に導入せられ、
該中継槽(3)において本発明の触媒(4ン汐;添加せ
られ纜拌機(3)Aによって攪拌分散せらhる。該反応
液は触媒(4)が分散せられた後連絡径路(5)Kよっ
て反応塔(6)に導入されるが、酸化反応の場合にはそ
の前にブロア(7)によって空気、その他の酸素含有ガ
ス、酵素ガス、オゾン、!尚酸化水素等の酸化剤等が添
加される。反応塔(6)において反応せられた反応液は
反応生成液となり連絡径路(8)を介して分・ヤ槽(I
Qに導入される。分離槽aQ内には磁気フィルター(9
)が設置される。磁気フィルター(9)はi両媒体(9
)Aと該濾過媒体を磁化する励磁コイル(9)Bとから
なる。かくして分離槽OI内では磁気フィルター(9)
によって触媒(4)は効高よく実質的に完全1C分帰さ
れ、反応生成液は排出径路aTJから排出される。触1
f!(4)力;所定の全磁気フィル*−rg)に捕集さ
れたら反応生成液の分離槽OIへの導入を一時中断して
排出径m(11Jから分離槽01へ逆洗水を注入し、磁
気フィルター(9)に捕集されている触[(4)を逆洗
して返送径路Q3から触媒(4)を中継f* C3)に
返送して再使用を行う。
FIG. 1 shows an embodiment of the present invention. In the figure, (1) is a storage tank for the reaction liquid, and the reaction liquid is introduced into the relay tank (3) through the introduction path (2) K interposed by the pump (2) A.
In the relay tank (3), the catalyst of the present invention (4 ml) is added and stirred and dispersed by the stirrer (3) A. After the catalyst (4) is dispersed, the reaction liquid is passed through the communication path ( 5) In the case of an oxidation reaction, air, other oxygen-containing gases, enzyme gases, ozone, and oxidizing agents such as hydrogen oxide are introduced into the reaction column (6) by K. The reaction liquid reacted in the reaction tower (6) becomes a reaction product liquid and is sent to the separation tank (I) via the communication path (8).
Introduced in Q. A magnetic filter (9
) will be installed. The magnetic filter (9) is
)A and an excitation coil (9)B that magnetizes the filtration medium. Thus, in the separation tank OI, the magnetic filter (9)
As a result, the catalyst (4) is efficiently and substantially completely returned to 1C, and the reaction product liquid is discharged from the discharge path aTJ. Touch 1
f! (4) When the force is collected by the predetermined total magnetic filter *-rg, the introduction of the reaction product liquid to the separation tank OI is temporarily stopped and backwash water is injected from the discharge diameter m (11J to the separation tank 01). , the catalyst (4) collected on the magnetic filter (9) is backwashed, and the catalyst (4) is returned to the relay f* C3) from the return path Q3 for reuse.

本発明は上記実施例によって限宇せられるものではなく
、例えば反応系は気体であってもよい。
The present invention is not limited to the above embodiments; for example, the reaction system may be a gas.

一本発明は上記したように流動床触媒として磁性触媒小
体を用いるから反応俵核触媒は磁気的に効高よく分離さ
れろ。
First, since the present invention uses magnetic catalyst bodies as the fluidized bed catalyst as described above, the reaction bale core catalyst can be effectively separated magnetically.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例の系統図である。 図中、(4)・・・・触媒、(6)・・・・反応塔、(
9)・・・・磁気フィルター、00・・・・分陛槽
FIG. 1 is a system diagram of an embodiment of the present invention. In the figure, (4)...catalyst, (6)...reaction tower, (
9)...magnetic filter, 00...bunkyo tank

Claims (1)

【特許請求の範囲】[Claims] 磁性触媒小体を流動床方式によって反応系に適用し、反
応後は磁気的に該磁性触媒小体を反応系から分離するこ
とを特徴とする反応方法
A reaction method characterized by applying magnetic catalyst bodies to a reaction system using a fluidized bed method, and magnetically separating the magnetic catalyst bodies from the reaction system after the reaction.
JP58170069A 1983-09-14 1983-09-14 Reaction process Pending JPS6061038A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58170069A JPS6061038A (en) 1983-09-14 1983-09-14 Reaction process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58170069A JPS6061038A (en) 1983-09-14 1983-09-14 Reaction process

Publications (1)

Publication Number Publication Date
JPS6061038A true JPS6061038A (en) 1985-04-08

Family

ID=15898054

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58170069A Pending JPS6061038A (en) 1983-09-14 1983-09-14 Reaction process

Country Status (1)

Country Link
JP (1) JPS6061038A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003001243A (en) * 2001-06-04 2003-01-07 Japan Science & Technology Corp System for removing environmental hormone
WO2012137936A1 (en) * 2011-04-08 2012-10-11 新日鉄エンジニアリング株式会社 Catalytic reaction device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003001243A (en) * 2001-06-04 2003-01-07 Japan Science & Technology Corp System for removing environmental hormone
WO2012137936A1 (en) * 2011-04-08 2012-10-11 新日鉄エンジニアリング株式会社 Catalytic reaction device

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