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JPS60345B2 - Method for recovering active ingredients from methionine synthesis exhaust gas - Google Patents
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JPS60345B2 - Method for recovering active ingredients from methionine synthesis exhaust gas - Google Patents

Method for recovering active ingredients from methionine synthesis exhaust gas

Info

Publication number
JPS60345B2
JPS60345B2 JP994679A JP994679A JPS60345B2 JP S60345 B2 JPS60345 B2 JP S60345B2 JP 994679 A JP994679 A JP 994679A JP 994679 A JP994679 A JP 994679A JP S60345 B2 JPS60345 B2 JP S60345B2
Authority
JP
Japan
Prior art keywords
synthesis
hydrocyanic acid
hydantoin
exhaust gas
active ingredients
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
Application number
JP994679A
Other languages
Japanese (ja)
Other versions
JPS55102557A (en
Inventor
俊夫 川端
茂樹 仲田
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP994679A priority Critical patent/JPS60345B2/en
Priority to DE19803001806 priority patent/DE3001806A1/en
Priority to FR8001451A priority patent/FR2447367A1/en
Priority to IT47681/80A priority patent/IT1143010B/en
Priority to BE0/199089A priority patent/BE881325A/en
Priority to MX180942A priority patent/MX154099A/en
Publication of JPS55102557A publication Critical patent/JPS55102557A/en
Priority to MY8400278A priority patent/MY8400278A/en
Publication of JPS60345B2 publication Critical patent/JPS60345B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 本発明はヒダントィン反応を工程に含むメチオニン合成
法においてヒダントィン合成反応器より発生する青酸含
有ガスをヒダントィン合成原料である実質的にアンモニ
アと炭酸ガスからなる化合物の水溶液あるいはメチオニ
ンのヒダントィン(以下MHと略示する)含有反応液に
て洗浄し、該洗浄液をMH合成反応器系内にもどすこと
により青酸を有効に回収することを目的とする。
DETAILED DESCRIPTION OF THE INVENTION The present invention uses hydrocyanic acid-containing gas generated from a hydantoin synthesis reactor in a methionine synthesis method that includes a hydantoin reaction as a raw material for hydantoin synthesis, such as an aqueous solution of a compound consisting essentially of ammonia and carbon dioxide gas or methionine. The objective is to effectively recover hydrocyanic acid by washing with a reaction solution containing hydantoin (hereinafter abbreviated as MH) and returning the washing solution to the MH synthesis reactor system.

MHを合成する方法として、メチルメルカプタン(以下
MMと略示する)とアクロレィンを適当な触媒の存在下
で反応させて得られるメチルメルカプトプロピオンアル
デヒド(以下MAと略示する)と青酸および炭酸アンモ
ニウムまたは重炭酸アンモニウムなどの実質的にアンモ
ニアと炭酸ガスからなる化合物を原料として合成する方
法とMM、アクロレィン、青酸および炭酸アンモニウム
または重炭酸アンモニウム等の実質的にアンモニアと炭
酸ガスからなる化合物を原料として適当な触媒存在下で
一段にて合成する方法とが公知であるが、いずれの反応
においても反応を完結させる為に添加されるMAあるい
はアクロレインまたはMMのモル数に対し、通常青酸は
過剰に加えられる。この過剰の青酸は一部MH溶液中に
溶解するが、大部分は青酸ガスとして遊離する。この青
酸ガスの処理方法として塩素または次亜塩素酸塩等の酸
化剤による酸化分解法、アルミナ、シリカ等担体に担持
したアルカリ金属水酸化物による接触加水分解法(特関
昭49−59074号公報)等が既に提案されているが
、MH合成反応器より発生するガスをそのまま処理した
場合、いずれの方法においても多量の酸化剤または触媒
を必要とし、青酸が高価であることからも工業的に経剤
的なプロセスとはいえない。
As a method for synthesizing MH, methyl mercaptopropionaldehyde (hereinafter abbreviated as MA) obtained by reacting methyl mercaptan (hereinafter abbreviated as MM) and acrolein in the presence of an appropriate catalyst, hydrocyanic acid and ammonium carbonate or A method of synthesis using a compound consisting essentially of ammonia and carbon dioxide gas such as ammonium bicarbonate as a raw material, and a method suitable for synthesizing a compound consisting essentially of ammonia and carbon dioxide gas such as MM, acrolein, hydrocyanic acid, and ammonium carbonate or ammonium bicarbonate as a raw material. However, in either reaction, hydrocyanic acid is usually added in excess of the number of moles of MA, acrolein, or MM added to complete the reaction. . A portion of this excess hydrocyanic acid is dissolved in the MH solution, but most of it is liberated as hydrocyanic acid gas. Methods for treating this cyanide gas include an oxidative decomposition method using an oxidizing agent such as chlorine or hypochlorite, and a catalytic hydrolysis method using an alkali metal hydroxide supported on a carrier such as alumina or silica. ) have already been proposed, but if the gas generated from the MH synthesis reactor is treated directly, either method requires a large amount of oxidizing agent or catalyst, and because hydrocyanic acid is expensive, it is not suitable for industrial use. It cannot be said that it is a medicinal process.

そこで本発明者等は種々検討した結果、青酸と同様にM
H合成原料である実質的にアンモニアと炭酸ガスから成
る化合物の水溶液およびMH含有反応液が青酸を選択的
かつ安定に吸収するという知見に基づき、本発明を成す
に至った。
Therefore, as a result of various studies, the present inventors found that M
The present invention was accomplished based on the finding that an aqueous solution of a compound consisting essentially of ammonia and carbon dioxide gas, which is a raw material for H synthesis, and a reaction solution containing MH selectively and stably absorb hydrocyanic acid.

本発明方法によれば吸収された青酸は系内に回収される
為、青酸の使用量が削減されることおよびこれを無害化
する為の処理剤が大幅に削減されることにより、従来法
と比べて工業的に非常に有利となる。
According to the method of the present invention, the absorbed hydrocyanic acid is recovered within the system, so the amount of hydrocyanic acid used is reduced, and the processing agent used to make it harmless is significantly reduced, making it different from the conventional method. It is industrially very advantageous.

本発明の態様の例を図面により説明する。Examples of aspects of the present invention will be explained with reference to the drawings.

まずMH合成反応器1に配管2より青酸、配管5より重
炭酸アンモニウム水溶液、配管3よりMAあるいはァク
ロレィンとMMおよび触媒が添加される。
First, hydrocyanic acid is added to the MH synthesis reactor 1 through the pipe 2, an ammonium bicarbonate aqueous solution is added through the pipe 5, and MA or acrolein, MM, and a catalyst are added through the pipe 3.

通常この反応は温度30〜100つ0、圧力lk9′の
○以下で行われる。この反応器1より発生するガスは主
として炭酸ガス、青酸、MMより成り、配管9を経て吸
収塔7に送られ、この塔内で重炭酸アンモニウム水溶液
あるいはMH含有反応液と河流接触し、ほとんどの青酸
が吸収除去される。
This reaction is usually carried out at a temperature of 30 to 100 degrees and a pressure of less than 9'. The gas generated from this reactor 1 mainly consists of carbon dioxide gas, hydrocyanic acid, and MM, and is sent to the absorption tower 7 through the pipe 9, where it comes into contact with the aqueous ammonium bicarbonate solution or the MH-containing reaction solution, and most of the gas is Hydrocyanic acid is absorbed and removed.

重炭酸アンモニウム水溶液は配管6を、MH含有反応液
は配管11を使用して吸収塔に供給される。いずれの場
合も吸収液は配管12を通り反応器1にもどる。重炭酸
アンモニウム水溶液は図面に示すようにMH合成原料に
用いる量の一部を吸収剤として使用してもよいし、また
全量を吸収剤として使用してもよい。
The aqueous ammonium bicarbonate solution is supplied to the absorption tower through piping 6, and the MH-containing reaction liquid is supplied through piping 11. In either case, the absorption liquid returns to the reactor 1 through the pipe 12. As shown in the drawing, a portion of the ammonium bicarbonate aqueous solution used for the MH synthesis raw material may be used as an absorbent, or the entire amount may be used as an absorbent.

次に実施例をあげて説明するが本発明はこれのみに限定
されるものではない。
Next, the present invention will be described with reference to examples, but the present invention is not limited thereto.

実施例 1 MAIモルに対し、青酸1.2モルおよび重炭酸アンモ
ニウム系水溶液(N止HC033モル)を連続的に添加
し、MH合成を行うことにより得られた排ガスは青酸4
容量%、メチルメルカプタン2.弦容量%ならびに炭酸
ガス93.4容量%という組成であつた。
Example 1 1.2 moles of hydrocyanic acid and an aqueous ammonium bicarbonate solution (33 moles of N-hydrocarbonate) were continuously added to mol of MAI, and the exhaust gas obtained by performing MH synthesis was
Volume %, methyl mercaptan2. The composition was 93.4% by volume of string volume and 93.4% by volume of carbon dioxide.

この排ガス30N〆′Hrを3000、大気圧、液ガス
比(1箱重量%の重炭酸アンモニウム水溶液夕/排ガス
タ)10の条件で吸収塔にて連続向流接触させることに
より得られたガスは青酸10倣pm、メチルメルカプタ
ン2.接容量%、アンモニア20蛇pmを含んでいた。
The gas obtained by contacting this exhaust gas 30N〆'Hr continuously in an absorption tower under the conditions of 3000N, atmospheric pressure, and liquid-gas ratio (1 box weight % ammonium bicarbonate aqueous solution / exhaust gas star) in an absorption tower is Hydrocyanic acid 10 pm, methyl mercaptan 2. It contained % contact capacity and 20 pm of ammonia.

上記のようにして吸収塔で排ガスより青酸を吸収した重
炭酸アンモニウム水溶液と当該吸収された青酸量および
当該吸収用に使用した重炭酸アンモニウム水溶液量だけ
減じた量の青酸と重炭酸アンモニウム水溶液とMAとを
使用して再度MH合成を行った。先の合成液と吸収液使
用の合成液を可性ソーダで加水分解し、硫酸で中和して
得たメチオニンの収量は双方共90%であった。実施例
2 実施例1と同様の排ガスをMHIの重量%含有の反応液
と40oo、大気圧、液ガス比10の条件で向流接触さ
せた。
An aqueous ammonium bicarbonate solution that has absorbed hydrocyanic acid from the exhaust gas in the absorption tower as described above, an amount of hydrocyanic acid reduced by the amount of hydrocyanic acid absorbed, and an amount of the aqueous ammonium bicarbonate solution used for absorption, an aqueous ammonium bicarbonate solution, and MA. MH synthesis was performed again using The yield of methionine obtained by hydrolyzing the above synthetic liquid and the synthetic liquid using the absorption liquid with sodium chloride and neutralizing with sulfuric acid was 90% for both. Example 2 The same exhaust gas as in Example 1 was brought into countercurrent contact with a reaction solution containing % by weight of MHI under conditions of 40 oo, atmospheric pressure, and liquid-gas ratio of 10.

得られたガスは青酸200ppm、メチルメルカプタン
2.筋容量%、アンモニア10岬pmを含んでいた。
The obtained gas contained 200 ppm of hydrocyanic acid and 2.0 ppm of methyl mercaptan. Muscle volume %, ammonia 10 cape pm included.

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

第1図は本発明の実施の一態様を示すフローシートであ
り、1はMH合成反応器、7は吸収塔、2〜6および8
〜11は配管を示す。 次1図
FIG. 1 is a flow sheet showing one embodiment of the present invention, in which 1 is an MH synthesis reactor, 7 is an absorption tower, 2 to 6 and 8
-11 indicate piping. Next figure 1

Claims (1)

【特許請求の範囲】[Claims] 1 ヒダントイン反応を工程に含むメチオニン合成法に
おいてヒダントイン合成反応器より発生する青酸含有ガ
スをヒダントイン合成原料である実質的にアンモニアと
炭酸ガスから成る化合物の水溶液あるいはメチオニンの
ヒダントイン含有反応液にて洗浄し、該洗浄液をヒダン
トイン合成反応器系内にもどすことを特徴とするメチオ
ニン合成排ガスから有効成分の回収法。
1. In a methionine synthesis method that includes a hydantoin reaction, the hydrocyanic acid-containing gas generated from the hydantoin synthesis reactor is washed with an aqueous solution of a compound consisting essentially of ammonia and carbon dioxide gas, which is a raw material for hydantoin synthesis, or with a hydantoin-containing reaction solution of methionine. . A method for recovering active ingredients from methionine synthesis exhaust gas, characterized in that the cleaning liquid is returned into the hydantoin synthesis reactor system.
JP994679A 1979-01-25 1979-01-30 Method for recovering active ingredients from methionine synthesis exhaust gas Expired JPS60345B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP994679A JPS60345B2 (en) 1979-01-30 1979-01-30 Method for recovering active ingredients from methionine synthesis exhaust gas
DE19803001806 DE3001806A1 (en) 1979-01-25 1980-01-18 METHOD FOR OBTAINING USEFUL COMPOUNDS FROM METAL EXHAUST GASES
FR8001451A FR2447367A1 (en) 1979-01-25 1980-01-23 PROCESS FOR RECOVERING CYANHYDRIC ACID AND METHYLMERCAPTAN FROM WASTE GASES OF METHIONINE SYNTHESIS
IT47681/80A IT1143010B (en) 1979-01-25 1980-01-23 PROCEDURE FOR THE RECOVERY OF USEFUL COMPONENTS FROM THE EXHAUST GASES OF THE METHIONINE SYNTHESIS
BE0/199089A BE881325A (en) 1979-01-25 1980-01-24 PROCESS FOR RECOVERING CYANHYDRIC ACID AND METHYLMERCAPTAN FROM WASTE GASES OF METHIONINE SYNTHESIS
MX180942A MX154099A (en) 1979-01-25 1980-01-24 IMPROVED PROCEDURE FOR RECOVERING USEFUL COMPONENTS OF RESIDUAL GAS FROM THE METIONINE SYSTEM
MY8400278A MY8400278A (en) 1979-01-30 1984-12-31 Constant velocity universal joints

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP994679A JPS60345B2 (en) 1979-01-30 1979-01-30 Method for recovering active ingredients from methionine synthesis exhaust gas

Publications (2)

Publication Number Publication Date
JPS55102557A JPS55102557A (en) 1980-08-05
JPS60345B2 true JPS60345B2 (en) 1985-01-07

Family

ID=11734147

Family Applications (1)

Application Number Title Priority Date Filing Date
JP994679A Expired JPS60345B2 (en) 1979-01-25 1979-01-30 Method for recovering active ingredients from methionine synthesis exhaust gas

Country Status (2)

Country Link
JP (1) JPS60345B2 (en)
MY (1) MY8400278A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004035465A1 (en) * 2004-07-22 2006-02-16 Degussa Ag Process for the purification of CO2 gas streams
CN106661571B (en) 2014-07-11 2019-12-20 住友化学株式会社 Oxidase, polynucleotide encoding the same, and use thereof
SG11201700099PA (en) 2014-07-11 2017-02-27 Sumitomo Chemical Co Oxidase, polynucleotide encoding same, and use thereof
CN115650890A (en) * 2022-04-28 2023-01-31 宁夏紫光天化蛋氨酸有限责任公司 Method for treating tail gas generated in production of 2-hydroxy-4-methylthiobutyronitrile

Also Published As

Publication number Publication date
JPS55102557A (en) 1980-08-05
MY8400278A (en) 1984-12-31

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