JPS5848548B2 - Method for producing 4,4'-diaminostilbene-2,2'-disulfonic acid or its salts - Google Patents

Method for producing 4,4'-diaminostilbene-2,2'-disulfonic acid or its salts

Info

Publication number
JPS5848548B2
JPS5848548B2 JP1056377A JP1056377A JPS5848548B2 JP S5848548 B2 JPS5848548 B2 JP S5848548B2 JP 1056377 A JP1056377 A JP 1056377A JP 1056377 A JP1056377 A JP 1056377A JP S5848548 B2 JPS5848548 B2 JP S5848548B2
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JP
Japan
Prior art keywords
dns
catalyst
autoclave
temperature
reaction
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
JP1056377A
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Japanese (ja)
Other versions
JPS5395952A (en
Inventor
孝治 磯部
政友 藤瀬
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Nippon Kayaku Co Ltd
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Nippon Kayaku Co Ltd
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Priority to JP1056377A priority Critical patent/JPS5848548B2/en
Publication of JPS5395952A publication Critical patent/JPS5395952A/en
Publication of JPS5848548B2 publication Critical patent/JPS5848548B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は4・l−ジニトロスチルベン−2・2′ジスル
ホン酸又はその塩(以下これをDNSと略記する)を酸
性亜硫酸塩で被毒処理をしたラネーニッケル触媒の存在
下、水素加圧下で接触還元を行なわせることによる4・
4′−ジアミノスチルベン−2・グージスルホン酸又は
その塩(以下これをDASと略記する)の製造法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is based on the presence of a Raney nickel catalyst in which 4,l-dinitrostilbene-2,2'disulfonic acid or its salt (hereinafter abbreviated as DNS) is poisoned with an acidic sulfite. 4. by performing catalytic reduction under hydrogen pressure.
The present invention relates to a method for producing 4'-diaminostilbene-2 goudisulfonic acid or a salt thereof (hereinafter abbreviated as DAS).

DNS及びDASのうち塩とはナトリウム塩、カリウム
塩、或はアンモニウム塩を指すものである。
Among DNS and DAS, salt refers to sodium salt, potassium salt, or ammonium salt.

DASは染料、特に螢光増白染料を製造するた?の中間
体として重要な化合物であり、高純度の品質が要求され
る。
DAS manufactures dyes, especially fluorescent whitening dyes. It is an important compound as an intermediate for , and requires high purity.

従来DASの製造にはDNSを鉄粉と酸で還元する方法
が=般に行われてきていたが、還元後のDASと還元に
使用された鉄粉との分離操作の繁雑さや鉄粉残渣を処理
することの困難性等に問題があった。
Conventionally, DAS has been produced by reducing DNS with iron powder and acid, but the process of separating the reduced DAS from the iron powder used for reduction is complicated and the iron powder residue is There were problems such as difficulty in processing.

これらの欠点がなく、連続操業大量生産に適している方
法として接触還元法が知られているが、DNSの接触還
元におし・ては、ニトロ基のアミノ基への還元と共にエ
チレン結合も水素化された4・4′−ジアノジベンジル
−2・2−ジスルホン酸又はその塩(以下これをDAB
Sと略記する。
Catalytic reduction is known as a method that does not have these drawbacks and is suitable for continuous mass production. However, in DNS catalytic reduction, nitro groups are reduced to amino groups, and ethylene bonds are also converted to hydrogen. 4,4'-dianodibenzyl-2,2-disulfonic acid or its salt (hereinafter referred to as DAB)
It is abbreviated as S.

)が副生し、又着色生成物ができて低純度のDASとな
りやすいという問題がある。
) is produced as a by-product, and colored products are produced, which tends to result in low-purity DAS.

これまで、DASの接触還元による製造法としては (1)特公昭48−815号に記載された吸油率50〜
190のカーボンブラック上にセ持されたパラジウム若
しくは白金触媒を使用してDNSを接触還元する方法。
Up until now, the methods for producing DAS by catalytic reduction have been as follows: (1) Oil absorption rate of 50~
A method for catalytic reduction of DNS using a palladium or platinum catalyst supported on 190 carbon black.

(2)特開昭49−127955号に記載された、DN
Sをパラジウム系触媒とヨウ素、臭素又はこれらのイオ
ンを共存させて接触還元する方法。
(2) DN described in JP-A-49-127955
A method of catalytically reducing S in the presence of a palladium-based catalyst and iodine, bromine, or these ions.

(3)特開昭50−12059号に記載された、DNS
を元素の周期律表第8族の金属の存在で一定の範囲の反
応温度、液のPH値、および水素圧力下で水素化してD
ASを得る方法。
(3) DNS described in JP-A-50-12059
is hydrogenated in the presence of a metal from group 8 of the periodic table of elements under a certain range of reaction temperature, pH value of the liquid, and hydrogen pressure to obtain D.
How to get AS.

(4)特開昭50−84551号に記載された、DNS
をニッケル触媒下にPH5〜10の水溶液中で接触還元
する方法。
(4) DNS described in Japanese Patent Application Laid-Open No. 50-84551
A method in which catalytic reduction is carried out in an aqueous solution with a pH of 5 to 10 under a nickel catalyst.

(5)特開昭50−84550号に記載された、DNS
をアルコール溶媒中、ニッケル触媒で接触還元する際、
反応開始時の系の含水量を3%以下とする方法。
(5) DNS described in Japanese Patent Application Laid-Open No. 50-84550
When catalytically reduced with a nickel catalyst in an alcohol solvent,
A method in which the water content of the system at the start of the reaction is 3% or less.

(6)特開昭50−93927号に記載されているC−
C多重結合をも有する芳香族二トロ化合物を、触媒とし
て、式MeSx(式中Xは1〜4の数であり、そしてM
eは元素周期律表第8族の金属原子を表わすか、または
レニウムを表わす。
(6) C- described in JP-A No. 50-93927
An aromatic nitro compound also having a C multiple bond was used as a catalyst with the formula MeSx (wherein X is a number from 1 to 4, and M
e represents a metal atom of Group 8 of the Periodic Table of Elements or rhenium.

)の硫化金属の存在下で接触還元する方法。) in the presence of metal sulfide.

(7)特開昭50−93953号に記載された、DNS
をコバルト触媒で接触還元する方法等がある。
(7) DNS described in Japanese Patent Application Laid-Open No. 50-93953
There are methods such as catalytic reduction of the cobalt using a cobalt catalyst.

しかし、特公昭48−815号、特開昭4912795
5号、特開昭50−93952号などの方法はいずれも
貴金属触媒を使用していて、本発明で使用しているラネ
ーニッケル触媒よりはるかに高価であり、また回収操作
を効率よく行ない再使用することが困難であり、不経済
である。
However, Japanese Patent Publication No. 48-815, Japanese Patent Publication No. 4912795
No. 5, JP-A-50-93952, and other methods all use precious metal catalysts, which are much more expensive than the Raney nickel catalyst used in the present invention, and require efficient recovery operations and reuse. It is difficult and uneconomical to do so.

これに比し本発明で使用するラネーニッケルは安価であ
り、しかも回収、再使用が容易にできるので工業的に使
用する場合は貴金属触媒と比較して非常に有利である。
In comparison, Raney nickel used in the present invention is inexpensive and can be easily recovered and reused, so it is very advantageous compared to noble metal catalysts when used industrially.

特開昭50−12059号には周期律表第8族の金属の
存在下で接触還元してDASを得る方法が示されている
が、ラネーニッケルは触媒の具体的例に示されていない
ばかりか実施例19(比較のため)におち・て、ラネー
ニッケルを使用した場合は、DNSの接触還元におL・
てDABSが副生して好ましくないと記述してある。
JP-A-50-12059 discloses a method for obtaining DAS by catalytic reduction in the presence of a metal from group 8 of the periodic table, but Raney nickel is not listed as a specific example of a catalyst. In Example 19 (for comparison), when Raney nickel was used, L.
It is stated that DABS is produced as a by-product and is not desirable.

特開昭50−84550及び50−84551号の方法
ではいずれもニッケル触媒を使用してDNSを接触還元
し、DASを得ているが、前者は含水率3%以下のアル
コール類を溶媒として使用していて、反応後アルコール
類の回収操作を必要とし、後者の場合は、反応液のPH
を5〜10に保持するために、緩衝剤の添加を行ってい
て、DASを析出させ採取する際に緩衝剤が混入し、D
ASの純度を低《するという問題がある。
In the methods of JP-A-50-84550 and JP-A-50-84551, DAS is obtained by catalytic reduction of DNS using a nickel catalyst, but the former uses alcohols with a water content of 3% or less as a solvent. In the latter case, the PH of the reaction solution needs to be recovered after the reaction.
In order to keep the DAS between 5 and 10, a buffer is added, and when DAS is precipitated and collected, the buffer is mixed in and the DAS is collected.
There is a problem of lowering the purity of AS.

また沢液にも緩衝剤がゆき排水を汚染することになる。In addition, buffering agents will also be present in the sap, contaminating the wastewater.

特開昭50−93927号の実施例15には硫化ニッケ
ル触媒の使用が記載されているが、150バールもの高
圧をもって反応を行っている。
Example 15 of JP-A-50-93927 describes the use of a nickel sulfide catalyst, but the reaction is carried out at a pressure as high as 150 bar.

これは高圧の反応装置を必要として不利である。This is disadvantageous as it requires a high pressure reactor.

これに対して本発明者等は、被毒処理したラネ 4一ニ
ッケルを使用してDNSの接触還元を行なえば、DAB
Sの副生が著しく抑制されて、品質の優れたDASが容
易に得られることを見出した。
On the other hand, the present inventors have found that if catalytic reduction of DNS is performed using poisoned Rane 41 nickel, DAB
It has been found that the by-product of S is significantly suppressed and DAS of excellent quality can be easily obtained.

本発明を遂行する為に用いられる被毒処理したラネーニ
ッケルは次の様な方法で得ることが出来る。
The poisoned Raney nickel used to carry out the present invention can be obtained by the following method.

展開されたラネーニッケルの水性ペーストの所定量を秤
量し、所定量の蒸留水(有害な重金属イオンや硫化物を
含まない水であればイオン交換水でもよい)中に懸濁し
、攪拌しながら所定量の酸性亜硫酸塩を少量ずつ加えて
所定の温度で所定の時間処理する。
Weigh a predetermined amount of the developed Raney nickel aqueous paste, suspend it in a predetermined amount of distilled water (ion-exchanged water may be used as long as it does not contain harmful heavy metal ions or sulfides), and add the predetermined amount while stirring. Acidic sulfite is added little by little and treated at a predetermined temperature for a predetermined time.

処理後上澄液を除き新らしい蒸留水(上と同じ)を加え
て攪拌し洗浄する。
After treatment, remove the supernatant, add fresh distilled water (same as above), stir and wash.

この洗浄操作を数回行ない、傾斜して上澄液を除き、ゞ
被毒された“ラネーニッケル水性ペーストを得る。
This washing operation is repeated several times and the supernatant liquid is removed by decanting to obtain a poisoned "Raney nickel aqueous paste".

この様にして製造した被毒されたラネーニッケル水性ペ
ーストを使用して水素加圧下でDNSを接触還元する。
The poisoned Raney nickel aqueous paste thus prepared is used to catalytically reduce DNS under hydrogen pressure.

DNSの接触還元は4・4l−ジニトロスチルベン−2
−2’−シスルホン酸又ハソの塩を、酸性亜硫酸塩及び
ラネーニッケル触媒の存在下、水素加圧下で接触還元す
ることによっても行うことができる。
Catalytic reduction of DNS is 4,4l-dinitrostilbene-2
It can also be carried out by catalytic reduction of a salt of -2'-cissulfonic acid or haso under pressure of hydrogen in the presence of an acidic sulfite and a Raney nickel catalyst.

即ち展開したラネーニッケル水性ペーストを所定量秤量
し、これと還元反応に使用する水の一部を反応器中に移
し入れ、所定量の酸性亜硫酸塩を添加し、攪拌し、水素
加圧下DNSを接触還元することによっても同様な効果
が得られる。
That is, a predetermined amount of the developed Raney nickel aqueous paste was weighed, this and a portion of the water used for the reduction reaction were transferred into a reactor, a predetermined amount of acidic sulfite was added, stirred, and DNS was contacted under hydrogen pressure. A similar effect can be obtained by reduction.

本発明に使用される酸性亜硫酸塩としては、工業的に入
手し易い塩でよく、例えば酸性亜硫酸ソーダ、酸性亜硫
酸アンモニウム、酸性亜硫酸カリウムなどを挙げること
が出来る。
The acidic sulfite used in the present invention may be any industrially easily available salt, such as acidic sodium sulfite, acidic ammonium sulfite, acidic potassium sulfite, and the like.

1被毒“させる酸性亜硫酸塩の量は、ラネーニッケルの
ニッケル金属1モルに対して100分の1モル乃至3分
の1モル即ちニッケル金属1001に対し酸性亜硫酸ソ
ーダの場合、22〜50Pの範囲で選ぶことが出来る。
1. The amount of acidic sulfite that causes poisoning ranges from 1/100 mole to 1/3 mole per 1 mole of nickel metal in Raney nickel. You can choose.

どの程度の条件で被毒した触媒を使用するのが適当であ
るかは、DNSを還元する時の反応条件(反応温度、反
応圧力、触媒帯留量等)によって、工業的に有利になる
様な範囲で選択して決定することが出来る。
The appropriate conditions under which to use a poisoned catalyst depend on the reaction conditions (reaction temperature, reaction pressure, amount of catalyst banded, etc.) when reducing DNS, depending on the conditions that are industrially advantageous. You can select and decide within the range.

展開したラネーニッケルの被毒処理の方法に関しては、
被毒の際に使用する水の量、酸性亜硫酸塩の添加方法、
処理温度、処理時間、処理後の洗浄回数等を一定にすれ
ば被毒効果に顕著な違いは生じないので被毒効果の再現
性は高い。
Regarding the method of poisoning developed Raney nickel,
The amount of water used during poisoning, the method of adding acidic sulfites,
If the treatment temperature, treatment time, number of times of washing after treatment, etc. are kept constant, there will be no noticeable difference in the poisoning effect, so the reproducibility of the poisoning effect is high.

被毒の際の処理条件と被毒の程度との関係は次の通りで
ある。
The relationship between the treatment conditions during poisoning and the degree of poisoning is as follows.

先ず使用する水の量であるが、これは被毒剤である酸性
亜硫酸塩の触媒金属に対する濃度に関係するが、水の使
用量を少なくし、換言すれば酸性亜硫酸塩の濃度を高く
した方が被毒効果は太き《なる。
First, the amount of water used is related to the concentration of acidic sulfite, which is a poisoning agent, relative to the catalyst metal. However, the poisoning effect becomes thicker.

工業的には操作出来る範囲で、本発明の目的に適する様
に任意の水の量を決定することが出来る。
Any amount of water can be determined to suit the purpose of the present invention within an industrially manageable range.

酸性亜硫酸塩の添加方法は酸性亜硫酸塩をそのまま少量
ずつ又はその濃厚な水溶液を攪拌下に触媒の水懸濁液に
添加するが、それらに限定されない。
The method of adding the acidic sulfite is, but is not limited to, adding the acidic sulfite as it is little by little or adding its concentrated aqueous solution to the aqueous suspension of the catalyst while stirring.

被毒する温度は通常常温または弱い加温下例えば10℃
〜40℃で行なうが必ずしもそれに限定されない。
The temperature at which poisoning occurs is usually room temperature or under mild heating, e.g. 10°C.
Although it is carried out at a temperature of ~40°C, it is not necessarily limited thereto.

被毒処理後の水洗は反応器の中で酸性亜硫酸塩によって
被毒する時には行なわない。
Washing with water after poisoning treatment is not performed when the reactor is poisoned by acidic sulfites.

被毒処理した触媒は、驚《べきことには伺回水で洗浄し
てもその被毒効果は事実上全く減じないし、同じ触媒に
よって水素化反応を繰り返し行なっても、被毒効果が少
なくとも十数回以上は持続されることが実験の結果明ら
かになった。
Surprisingly, the poisoning effect of the poisoned catalyst does not actually decrease at all even after washing with recycled water, and even if the hydrogenation reaction is repeated with the same catalyst, the poisoning effect remains at least sufficient. Experiments have shown that it lasts for more than a few times.

本発明方法で被毒した触媒を使用してDNSを接触還元
する操作法としては次の様な方法で行なうが、この操作
法に本発明方法が制限されるものではない。
The method of catalytically reducing DNS using a poisoned catalyst in the method of the present invention is as follows, but the method of the present invention is not limited to this method.

攪拌機付のオートクレープに所定量の被毒処理したラネ
ーニッケル触媒の水性ペースト及び水を入れ蓋を閉じ、
内部を水素置換する。
Pour the specified amount of poisoned Raney nickel catalyst aqueous paste and water into an autoclave equipped with a stirrer, close the lid, and
Replace the inside with hydrogen.

あるいはオートクレープに所定量の展開したラネーニッ
ケルペースト、還元反応に使用する水の一部、所定量の
酸性亜硫酸を入れ内部を水素置換してもよい。
Alternatively, a predetermined amount of expanded Raney nickel paste, a portion of the water used for the reduction reaction, and a predetermined amount of acidic sulfite may be placed in an autoclave and the interior may be replaced with hydrogen.

つL・で昇圧、昇温し、例えば10kg/rstゲージ
圧80℃とする。
The pressure and temperature are increased by 1 L· to, for example, 10 kg/rst and a gauge pressure of 80°C.

次にこの圧力温度を保ちながらDNSの水溶液を定量ポ
ンプを用いて徐々にオートクレープに圧入しながら接触
還元を行なう。
Next, while maintaining this pressure and temperature, catalytic reduction is performed while gradually pressurizing the DNS aqueous solution into the autoclave using a metering pump.

この様にすれば反応は容易に進行する。In this way, the reaction will proceed easily.

併しDNSのDASへの転換速度よりDNS仕込速度が
速く、反応液中にDNSが多量に残在してくる場合は、
きびしい条件を与えないと反応が進行しにくいのでどう
しても反応を進行させたければ、きびしい条件下で反応
を行なわせなげればならない。
However, if the rate of DNS preparation is faster than the rate of conversion of DNS to DAS and a large amount of DNS remains in the reaction solution,
It is difficult for the reaction to proceed unless strict conditions are provided, so if you really want the reaction to proceed, you must conduct the reaction under strict conditions.

その様な条件下で反応を行なわせればスチルベンのエチ
レン結合にも水素添加が起こる割合が増大し望ましい結
果が得られない。
If the reaction is carried out under such conditions, the proportion of hydrogenation occurring in the ethylene bonds of stilbene will increase, making it impossible to obtain desired results.

(例えば特開昭5012059実施例19によれば15
0℃から180℃で水素圧150バールで水素化してい
る)本還元に於で水素は常時補充され、圧力は一定に保
たれる。
(For example, according to Example 19 of JP-A-5012059, 15
During the main reduction, hydrogen is constantly replenished and the pressure is kept constant.

DNSの圧入が終了すると間もな《水素の吸収は停止す
る。
Immediately after DNS injection is completed, hydrogen absorption stops.

その後オートクレープを冷却し、内容物の温度が約45
℃に下がった時に攪拌を停止し、減圧する。
The autoclave is then cooled until the temperature of the contents is approximately 45.
When the temperature drops to ℃, stop stirring and reduce the pressure.

触媒は沈降分離および沢過により回収し、次回の還元に
使用する。
The catalyst is recovered by sedimentation and filtration and used for the next reduction.

触媒を回収分離した液はDASを原料とする螢光増白染
料などの製造にそのまま使用することができる。
The liquid from which the catalyst has been recovered and separated can be used as it is in the production of fluorescent whitening dyes using DAS as a raw material.

また酸性にしてDASの結晶を析出させて沢過すればプ
レスケーキを得ることができ、これも同様に螢光増白染
料などの製造に使用することができる。
Further, by acidifying the mixture to precipitate DAS crystals and filtering it, a press cake can be obtained, which can also be used in the production of fluorescent whitening dyes and the like.

被毒処理しないラネーニッケル触媒を使用して同様な条
件で接触還元を行なっても反応は進行する。
Even if catalytic reduction is carried out under similar conditions using an unpoisoned Raney nickel catalyst, the reaction proceeds.

しかしこの場合はDABSが多量に副生ずるし、また赤
色の生或物力墳1]生する。
However, in this case, a large amount of DABS is produced as a by-product, and a red color is also produced.

以下実施例をあげて本発明の詳細につき説明するが、本
発明はそれらに限定されるものではない。
The details of the present invention will be explained below with reference to Examples, but the present invention is not limited thereto.

実施例 1 ラネーニッケル4.Of(金属)と蒸留水100ml.
を計量し、攪拌子を入れたビーカーに入れ、攪拌しなが
ら酸性亜硫酸ナトリウム(関東化学株式会社製) 5
0 0/Qを少量ずつ投入し、室温にて30分間攪拌し
た。
Example 1 Raney nickel4. Of (metal) and 100 ml of distilled water.
Weigh the amount of sodium sulfite (manufactured by Kanto Kagaku Co., Ltd.) and add it to a beaker with a stirring bar, while stirring.
00/Q was added little by little and stirred at room temperature for 30 minutes.

その後、傾斜して上澄みの水を捨て1001r1lの新
しい水を加えて5分間攪拌した。
Thereafter, the supernatant water was discarded by tilting, 1001 liters of fresh water was added, and the mixture was stirred for 5 minutes.

再び傾斜して水を捨てた。この操作を3回繰返した。I tilted it again and dumped the water. This operation was repeated three times.

最後に攪拌子に付着している触媒を洗い落し、傾斜して
十分に水を切って攪拌機付の500mlステンレス製の
オートクレープに100771lの水と共に入れ、蓋を
閉じ、水素置換し、2kg/crriゲージに加圧しゆ
っくり攪拌しながら76℃まで昇温した。
Finally, wash off the catalyst attached to the stirrer, drain the water thoroughly by tilting it, put it in a 500ml stainless steel autoclave with a stirrer together with 100,771L of water, close the lid, replace it with hydrogen, and produce 2kg/crri. Pressure was applied to the gauge and the temperature was raised to 76° C. while stirring slowly.

76℃に達した時攪拌速度をあげ内圧を10kg/cr
riゲージとし、11.2%DNS(4・4’−シニト
ロスチルベン2・2′シスルホン酸ジナトリウム塩)水
溶液941を定量ポンプを用L・て一定の流速で65分
を費してオートクレープに圧入しながら接触還元を行な
った。
When the temperature reached 76℃, increase the stirring speed and increase the internal pressure to 10kg/cr.
Using an RI gauge, autoclave 11.2% DNS (4,4'-sinitrostilbene 2,2' cisulfonic acid disodium salt) aqueous solution 941 using a metering pump at a constant flow rate for 65 minutes. Catalytic reduction was carried out while press-fitting the material.

反応中は、温度を76℃乃至80℃に保ち、圧力を水素
吸収に応じて水素を補充しなから9乃至1 0 kg/
c♂ゲージに保った。
During the reaction, the temperature was maintained at 76°C to 80°C, and the pressure was maintained at 9 to 10 kg/h while replenishing hydrogen according to hydrogen absorption.
I kept it at c♂ gauge.

DNSの圧入が終了した後l2分間反応温度と同じ温度
に保った後攪拌を停止し、オートクレープを外部から冷
却した。
After the injection of DNS was completed, the autoclave was kept at the same temperature as the reaction temperature for 12 minutes, then stirring was stopped, and the autoclave was cooled from the outside.

減圧して蓋を開き内容物を抜き出し触媒をf別した。The pressure was reduced, the lid was opened, the contents were extracted, and the catalyst was separated.

こうして得られた生成液を液体クロマトグラフ法によつ
て分析した結果、DABSの含有率は0.13%であり
、その他はDASであった。
As a result of analyzing the product liquid thus obtained by liquid chromatography, the content of DABS was 0.13%, and the rest was DAS.

生成液を酸析して得られたDASの収率はジアゾ化分析
によると98.0%対理論であった。
According to diazotization analysis, the yield of DAS obtained by acid precipitation of the product solution was 98.0% versus theory.

実施例 2 ラネーニッケル4.0′i!(金属)、蒸留水100M
、酸性亜硫酸ナトリウム250In9の割合で実施例1
と同様の方法で被毒した触媒を1001llの水と共に
実施例1で使用したオートクレープに入れ、蓋を閉じ、
水素置換し2kg/crrtに加圧し攪拌を開始し、7
7℃まで昇温した。
Example 2 Raney Nickel 4.0'i! (metal), distilled water 100M
, sodium acid sulfite 250In9 proportions Example 1
The catalyst poisoned in the same manner as above was placed in the autoclave used in Example 1 along with 1001 liters of water, and the lid was closed.
After purging with hydrogen and pressurizing to 2 kg/crrt, stirring was started.
The temperature was raised to 7°C.

DNSの11.2%水溶液を104Pを定量ポンプを用
(・て一定の流速で174分間を費してオートクレープ
に圧入しながら接触還元を行なった。
Catalytic reduction was performed while an 11.2% aqueous solution of DNS was injected into an autoclave using a metering pump (174 minutes) at a constant flow rate.

反応中は温度77℃乃至79℃に保ち、圧力を水素吸収
に応じて水素を補充しながら9乃至1 0 ky/c4
ゲージに保った。
During the reaction, the temperature was maintained at 77°C to 79°C, and the pressure was increased to 9 to 10 ky/c4 while replenishing hydrogen according to hydrogen absorption.
I kept it on the gauge.

DNSの圧人が終了した後同温度で10分間攪拌を続げ
た後オートクレープを外部から冷却し内容物を45℃と
した。
After the DNS pressure was completed, stirring was continued for 10 minutes at the same temperature, and then the autoclave was cooled from the outside to bring the contents to 45°C.

減圧後蓋を開き内容物を抜き出し触媒を沢別した。After reducing the pressure, the lid was opened, the contents were taken out, and the catalyst was separated.

こうして得られた生或液を液体クロマトグラフ法によっ
て分析した結果DABSの含有率は0.83%で他はD
ASであった。
Analysis of the raw liquid thus obtained by liquid chromatography revealed that the content of DABS was 0.83%, and the rest was D.
It was AS.

実施例 3 ラネーニッケル4.0?(金属)、蒸留水100ml、
酸性亜硫酸ナトリウム500■の割合で実施例1と同様
の方法で被毒した触媒をlQQmlの水と共にオートク
レープに入れ、実施例1と同様にしてDNSの15.0
%水溶液1512を128分間費して仕込みながら接触
還元を行なった。
Example 3 Raney Nickel 4.0? (metal), distilled water 100ml,
A catalyst poisoned in the same manner as in Example 1 at a ratio of 500 μl of sodium acid sulfite was placed in an autoclave together with 1 QQ ml of water, and a DNS of 15.0 μl was added in the same manner as in Example 1.
Catalytic reduction was carried out while charging a 1512% aqueous solution for 128 minutes.

反応中は温度78乃至82℃に保ち、圧力を水素吸収に
応じて水素を補充しなから6乃至7 kg/crAゲー
ジに保った。
During the reaction, the temperature was maintained at 78 to 82° C., and the pressure was maintained at 6 to 7 kg/crA gauge without replenishing hydrogen according to hydrogen absorption.

仕込終了後10分間攪拌を続げた後、オートクレープを
冷却した。
After the completion of the preparation, stirring was continued for 10 minutes, and then the autoclave was cooled.

生成液の分析結果はDABS0.73%で他はDASで
あった。
The analysis result of the produced liquid was 0.73% DABS and the rest was DAS.

実施例 4 ラネーニッケル4.OS’(金属)、蒸留水100ml
、酸性亜硫酸ナ} IJウム1000■の割合で実施例
1と同様の方法で被毒した触媒を100771lの水と
共にオートクレープに入れ実施例1と同様にして、DN
Sの11.2%水溶液1041を90分間費して仕込み
ながら接触還元を行なった。
Example 4 Raney nickel4. OS' (metal), distilled water 100ml
, acidic sodium sulfite} A catalyst poisoned in the same manner as in Example 1 at a ratio of 1,000 μl of sodium sulfite was placed in an autoclave with 100,771 liters of water and treated in the same manner as in Example 1.
Catalytic reduction was carried out while charging an 11.2% S aqueous solution 1041 for 90 minutes.

反応中は温度96乃至100℃に保ち、圧力を水素吸収
に応じて水素を補充しなから9乃至1 0kg/cwt
ゲージに保った。
During the reaction, the temperature was maintained at 96 to 100°C, and the pressure was maintained at 9 to 10 kg/cw, with hydrogen being replenished according to hydrogen absorption.
I kept it on the gauge.

仕込終了後10分間攪拌を続げた後、オートクレープを
冷却した。
After the completion of the preparation, stirring was continued for 10 minutes, and then the autoclave was cooled.

生成液の分析結果はDAB80.55%で他はDASで
あった。
The analysis result of the produced liquid was 80.55% DAB and the rest was DAS.

実施例 5 ラネーニッケル2.0P(金属)、蒸留水100ml、
酸性亜硫酸ナトリウム500Ivの割合で実施例1と同
様の方法で被毒した触媒を100rfLlの水と共にオ
ートクレープに入れ、実施例1と同様にしてDNSの1
1.2%水溶液1041を85分間費して仕込みながら
接触還元を行なった。
Example 5 Raney nickel 2.0P (metal), distilled water 100ml,
A catalyst poisoned in the same manner as in Example 1 with a proportion of 500 Iv of sodium acid sulfite was placed in an autoclave together with 100 rfLl of water, and 1v of DNS was added in the same manner as in Example 1.
Catalytic reduction was carried out while charging a 1.2% aqueous solution 1041 for 85 minutes.

反応中は温度119℃乃至120℃に保ち、圧力を水素
吸収に応じて水素を補充しながら9乃至IOkg/cr
Aゲージに保った。
During the reaction, the temperature was maintained at 119°C to 120°C, and the pressure was increased from 9 to IO kg/cr while replenishing hydrogen according to hydrogen absorption.
I kept it in A gauge.

仕込終了後、10分間攪拌を続げた後オートクレープを
冷却した。
After the preparation was completed, stirring was continued for 10 minutes, and then the autoclave was cooled.

生或液の分析結果はDAB80.61%で、他はDAS
であった。
The analysis result of raw liquid is DAB80.61%, the rest is DAS
Met.

実施例 6 ラネーニッケル4.Of(金属)、蒸留水100−、酸
性亜硫酸ナトリウム500Ivの割合で実施例1と同様
の方法で被毒した触媒を10OrI′llの水と共にオ
ートクレープに入れ実施例1と同様にしてDNSの11
.2%水溶液1 04Pを7■分間費して仕込みながら
接触還元を行なった。
Example 6 Raney nickel4. A catalyst poisoned in the same manner as in Example 1 with the proportions of Of (metal), distilled water 100 -, and acidic sodium sulfite 500 Iv was placed in an autoclave with 10 OrI'll of water and treated with DNS 11 in the same manner as in Example 1.
.. Catalytic reduction was carried out while charging a 2% aqueous solution of 104P for 7 minutes.

反応中は温度48℃乃至52℃に保ち、圧力を水素吸収
に応じて水素を補充しなから2乃至3 kg/crAゲ
ージに保った。
During the reaction, the temperature was maintained at 48° C. to 52° C., and the pressure was maintained at 2 to 3 kg/crA gauge without replenishing hydrogen according to hydrogen absorption.

仕込終了後10分間攪拌を続げた後オートクレープを冷
却した。
After the completion of the preparation, stirring was continued for 10 minutes, and then the autoclave was cooled.

生成液の分析結果はDABS0.60%で他はDASで
あった。
The analysis result of the product liquid was 0.60% DABS and the rest was DAS.

実施例 7 ラネーニッケル2.Of(金属)、蒸留水100TLl
、酸性亜硫酸ナトリウム500■の割合で実施例1と同
様の方法で被毒した触媒を100mlの水と共にオート
クレープに入れ実施例1と同様にしてDNSの11.2
%水溶液104.Pを73分間費して仕込みながら接触
還元を行なった。
Example 7 Raney Nickel2. Of (metal), distilled water 100TLl
A catalyst poisoned in the same manner as in Example 1 at a ratio of 500 μl of sodium acid sulfite was placed in an autoclave with 100 ml of water, and the same method as in Example 1 was used to prepare 11.2 μl of DNS.
% aqueous solution 104. Catalytic reduction was carried out while charging P for 73 minutes.

反応中は温度78乃至80℃に保ち、圧力を水素吸収に
応じて9乃至1 0 kg/crAゲージに保った。
During the reaction, the temperature was maintained at 78-80° C. and the pressure was maintained at 9-10 kg/crA gauge depending on hydrogen absorption.

仕込終了後10分間攪拌を続げた後、オートクレープを
冷却した。
After the completion of the preparation, stirring was continued for 10 minutes, and then the autoclave was cooled.

生戒液の分析結果はDABS0.11%で他はDASで
あった。
The analysis results of the raw liquid were 0.11% DABS and the rest was DAS.

実施例 8 ラネーニッケル4.0P(金属)、蒸留水100継、酸
性亜硫酸ナトリウム2000m9の割合で実施例1と同
様の方法で被毒した触媒を100771lの水と共にオ
ートクレープに入れ、実施例■と同様にしてDNSの1
1.2%水溶液102iを62分間費して仕込みながら
接触還元を行なった。
Example 8 A catalyst poisoned in the same manner as in Example 1 with 4.0P (metal) of Raney nickel, 100 parts of distilled water, and 2000 m of sodium acid sulfite was placed in an autoclave together with 100,771 liters of water, and the same method as in Example 2 was carried out. and DNS 1
Catalytic reduction was carried out while charging a 1.2% aqueous solution 102i for 62 minutes.

反応中は温度97乃至100℃に保ち、圧力を水素吸収
に応じて水素を補充しなから9乃至1 0 kg/cr
Aゲージに保った。
During the reaction, the temperature was maintained at 97 to 100°C, and the pressure was maintained at 9 to 10 kg/cr while replenishing hydrogen according to hydrogen absorption.
I kept it in A gauge.

仕込終了後10分間攪拌を続げた後オートクレープを冷
却した。
After the completion of the preparation, stirring was continued for 10 minutes, and then the autoclave was cooled.

生成液の分析結果はDAB80.01%で他はDASで
あった。
The analysis result of the produced liquid was 80.01% DAB and the rest was DAS.

実施例 9 ラネーニッケル4.(1(金属)、蒸留水100ml、
酸性亜硫酸アンモニウム1000In9の割合で実施例
1と同様の方法で被毒した触媒を100mlの水と共に
オートクレープに入れ、実施例1と同様にしてDNSの
11.2%水溶液1021を62分間費して仕込みなが
ら接触還元を行なった。
Example 9 Raney Nickel4. (1 (metal), 100ml of distilled water,
A catalyst poisoned in the same manner as in Example 1 with a proportion of 1000 In9 acidic ammonium sulfite was placed in an autoclave with 100 ml of water, and a 11.2% aqueous solution of DNS 1021 in the same manner as in Example 1 was added for 62 minutes. Contact reduction was performed during preparation.

反応中は温度79℃乃至80℃に保ち、圧力を水素吸収
に応じて水素を補充しなから9乃至10kg/c4ゲー
ジに保った。
During the reaction, the temperature was maintained at 79° C. to 80° C., and the pressure was maintained at 9 to 10 kg/c4 gauge without replenishing hydrogen according to hydrogen absorption.

仕込終了後10分間攪拌を続げた後、オートクレープを
冷却した。
After the completion of the preparation, stirring was continued for 10 minutes, and then the autoclave was cooled.

生戒液の分析結果はDAB80.26%で他はDASで
あった。
The analysis result of the raw liquid was 80.26% DAB and the rest was DAS.

実施例 10 攪拌機付5001rLlオートクレープにラネーニッケ
ル触媒水性ペースト4P(金属)と水100mlと酸性
亜硫酸ソーダ1500■とを入れ蓋を閉じ水素置換し非
常にゆっくり攪拌しながら76℃に昇温し次いで水素圧
を1 0 kg/cmゲージとし攪拌を速くし4・4′
−ジニトロスチルベン−2・2′一ジスルホン酸の11
.2%の水溶液96tを60分間費して仕込みながら接
触還元を行なった。
Example 10 Put Raney nickel catalyst aqueous paste 4P (metal), 100 ml of water, and 1500 μl of acidic sodium sulfite into a 5001 rL autoclave equipped with a stirrer, close the lid, replace the hydrogen with hydrogen, raise the temperature to 76°C while stirring very slowly, and then reduce the hydrogen pressure. Use a 10 kg/cm gauge and speed up the stirring to 4.4'.
-Dinitrostilbene-2.2'-monodisulfonic acid 11
.. Catalytic reduction was carried out while charging 96 tons of a 2% aqueous solution over 60 minutes.

反応中温度を95乃至1. 0 0℃に保ち、圧力を水
素吸収に応じて水素を補充しなから9乃至1 0 kg
/crttゲージに保った。
The temperature during the reaction was kept at 95-1. Maintain the temperature at 0.0°C and replenish the pressure according to the hydrogen absorption.9 to 10 kg.
/crtt gauge.

DNSの圧入が終了した後同温度で10分間攪拌し、オ
ートクレープを冷却し減圧後蓋を開き内容物を抜き出し
触媒をP別した。
After the injection of DNS was completed, the autoclave was stirred at the same temperature for 10 minutes, the autoclave was cooled, the pressure was reduced, the lid was opened, the contents were extracted, and the catalyst was separated.

こうして得られた生成液を液体クロマトグラフ法で分析
した結果DABSの含有率は0.25%で他はDASで
あった。
Analysis of the product liquid thus obtained by liquid chromatography revealed that the content of DABS was 0.25% and the rest was DAS.

比較例 1 ラネーニッケル0.5P(金属)を100m#)水と共
に攪拌機付のステンレス製5 0 0 1111オート
クレープに入れ蓋を閉じ水素置換し、2kg/cviゲ
ージに加圧しゆっくり攪拌しながら、77℃まで昇温し
た。
Comparative Example 1 Raney nickel 0.5P (metal) was placed in a stainless steel 500 1111 autoclave equipped with a stirrer with 100 m#) water, the lid was closed, hydrogen was replaced, the pressure was increased to 2 kg/cvi gauge, and the temperature was heated to 77°C while stirring slowly. The temperature rose to .

76゜Cに達した時、攪拌速度をあげ、内圧を■Okg
/crAゲージとし、11.2%DNS水溶液102f
?を定量ポンプを用し・て一定の流速で90分を費して
オートクレープに圧入しながら接触還元を行なった。
When the temperature reaches 76°C, increase the stirring speed and reduce the internal pressure to OK.
/crA gauge, 11.2% DNS aqueous solution 102f
? Catalytic reduction was performed while pressurizing the sample into an autoclave using a metering pump at a constant flow rate for 90 minutes.

反応中は温度76℃乃至78℃に保ち、圧力を水素吸収
に応じて水素を補充しなから9乃至1 0 kg/cr
j.ゲージに保った。
During the reaction, the temperature was maintained at 76°C to 78°C, and the pressure was maintained at 9 to 10 kg/cr while replenishing hydrogen according to hydrogen absorption.
j. I kept it on the gauge.

仕込終了後10分間攪拌を続げた後、オートクレープを
冷却した。
After the completion of the preparation, stirring was continued for 10 minutes, and then the autoclave was cooled.

生成液の分析結果は、DAB83.13%で他はDAS
であった。
The analysis result of the produced liquid was 83.13% DAB and the rest was DAS.
Met.

比較例 2 ラネーニッケル4.o?(金属)を100mlの水と共
に比較例1で使用したオートクレープに入れ比較例1と
同様にしてDNSの11.2%水溶液1 5Clを10
0分間費して仕込みながら接触還元を行なった。
Comparative example 2 Raney nickel 4. o? (metal) with 100 ml of water into the autoclave used in Comparative Example 1, and in the same manner as Comparative Example 1, add 1 5 Cl of 11.2% aqueous solution of DNS to 10
Catalytic reduction was carried out during preparation for 0 minutes.

反応中は反応温度76℃乃至82℃に保ち、圧力を水素
吸収に応じて水素を補充しなから9乃至1 0 kg/
crAゲージに保った。
During the reaction, the reaction temperature was maintained at 76°C to 82°C, and the pressure was maintained at 9 to 10 kg/h while replenishing hydrogen according to hydrogen absorption.
The crA gauge was maintained.

仕込終了後16分間攪拌を続けた後オートクレープを冷
却した。
After the completion of the preparation, stirring was continued for 16 minutes, and then the autoclave was cooled.

生成液の分析結果はDAB864.03%で他はDAS
であった。
The analysis result of the produced liquid is DAB864.03% and the rest is DAS.
Met.

比較例 3 ラネーニッケル0.6r(金属)を100mlの水と共
に比較例1で使用したオートクレープに入れ、比較例1
と同様にしてDNSの11.2%水溶液15M’を90
分間費して仕込みながら接触還元を行なった。
Comparative Example 3 Raney nickel 0.6r (metal) was placed in the autoclave used in Comparative Example 1 with 100 ml of water.
In the same manner as above, add 15M' of 11.2% aqueous solution of DNS to 90%
The catalytic reduction was carried out during preparation, which took several minutes.

反応中は反応温度55℃乃至61℃に保ち、圧力を水素
吸収に応じて水素を補充しなから4乃至5 kg/cy
ylゲージに保った。
During the reaction, the reaction temperature was maintained at 55°C to 61°C, and the pressure was maintained at 4 to 5 kg/cy depending on hydrogen absorption.
I kept it at yl gauge.

仕込終了後16分間攪拌を続げた後、オートクレープを
冷却した。
After the completion of the preparation, stirring was continued for 16 minutes, and then the autoclave was cooled.

生或液の分析結果はDAB32.10%で他はDASで
あった。
The analysis result of the raw liquid was 32.10% DAB and the rest was DAS.

以上の様にラネーニッケル触媒を酸性亜硫酸塩で処理し
ないでDNSの接触還元に使用した場合はDABSの副
生が多く殊に触媒の使用量が多い場合には半分以上がD
ABSになった。
As mentioned above, when Raney nickel catalyst is used for catalytic reduction of DNS without treatment with acidic sulfite, more than half of DABS is produced as a by-product, especially when a large amount of catalyst is used.
It became ABS.

Claims (1)

【特許請求の範囲】[Claims] 1 4・4′−ジニトロスチルベン−2・2′−シスル
ホン酸又はその塩を酸性亜硫酸塩で被毒処理をしたラネ
ーニッケル触媒又は酸性亜硫酸塩及びラネーニッケル触
媒の存在下、水素加圧下で接触還元することを特徴とす
る4・4′−ジアミノスチルベン−2・2′−ジスルホ
ン酸又はその塩の製造方法。
1 Catalytic reduction of 4,4'-dinitrostilbene-2,2'-cisulfonic acid or its salt under hydrogen pressure in the presence of a Raney nickel catalyst poisoned with an acidic sulfite or an acidic sulfite and a Raney nickel catalyst. A method for producing 4,4'-diaminostilbene-2,2'-disulfonic acid or a salt thereof, characterized by:
JP1056377A 1977-02-02 1977-02-02 Method for producing 4,4'-diaminostilbene-2,2'-disulfonic acid or its salts Expired JPS5848548B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1056377A JPS5848548B2 (en) 1977-02-02 1977-02-02 Method for producing 4,4'-diaminostilbene-2,2'-disulfonic acid or its salts

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1056377A JPS5848548B2 (en) 1977-02-02 1977-02-02 Method for producing 4,4'-diaminostilbene-2,2'-disulfonic acid or its salts

Publications (2)

Publication Number Publication Date
JPS5395952A JPS5395952A (en) 1978-08-22
JPS5848548B2 true JPS5848548B2 (en) 1983-10-28

Family

ID=11753700

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1056377A Expired JPS5848548B2 (en) 1977-02-02 1977-02-02 Method for producing 4,4'-diaminostilbene-2,2'-disulfonic acid or its salts

Country Status (1)

Country Link
JP (1) JPS5848548B2 (en)

Also Published As

Publication number Publication date
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