JPH0784410B2 - Method for producing granulated product of sodium benzoate - Google Patents

Method for producing granulated product of sodium benzoate

Info

Publication number
JPH0784410B2
JPH0784410B2 JP62237505A JP23750587A JPH0784410B2 JP H0784410 B2 JPH0784410 B2 JP H0784410B2 JP 62237505 A JP62237505 A JP 62237505A JP 23750587 A JP23750587 A JP 23750587A JP H0784410 B2 JPH0784410 B2 JP H0784410B2
Authority
JP
Japan
Prior art keywords
sodium benzoate
weight
neutralization reaction
granulated product
aqueous solution
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
JP62237505A
Other languages
Japanese (ja)
Other versions
JPS6483045A (en
Inventor
正弘 木村
照雄 吉田
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.)
Toagosei Co Ltd
Original Assignee
Toagosei 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 Toagosei Co Ltd filed Critical Toagosei Co Ltd
Priority to JP62237505A priority Critical patent/JPH0784410B2/en
Publication of JPS6483045A publication Critical patent/JPS6483045A/en
Publication of JPH0784410B2 publication Critical patent/JPH0784410B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Medicinal Preparation (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Formation And Processing Of Food Products (AREA)

Description

【発明の詳細な説明】 (イ)発明の目的 〔産業上の利用分野〕 本発明は、キャビア、清涼飲料、醤油等の食品及びタバ
コの防腐剤、解熱剤、膀胱炎、扁桃腺炎等の医薬、過酸
化ベンゾイル等の合成原料として、各種分野で巾広く使
用されている安息香酸ソーダ造粒品の製造方法に関する
ものであり、食品、医薬、有機合成化学工業等において
広く用いられるものである。
DETAILED DESCRIPTION OF THE INVENTION (a) Purpose of the invention [Industrial field of application] The present invention relates to foods such as caviar, soft drinks, soy sauce and preservatives for tobacco, antipyretics, cystitis, tonsillitis, and other pharmaceuticals. The present invention relates to a method for producing a granulated product of sodium benzoate, which is widely used in various fields as a synthetic raw material such as benzoyl peroxide, and is widely used in food, medicine, organic synthetic chemical industry and the like.

〔従来の技術〕[Conventional technology]

安息香酸ソーダは、カセイソーダ水溶液又は炭酸ソーダ
水溶液に安息香酸を加えて中和した液(以下中和反応液
という)を濃縮晶析又は蒸発乾固して製造される(第3
版食品添加物公定書注解66頁,食品添加物公定書注解編
集委員会編 金原出版(株)1974年発行)。
Sodium benzoate is produced by concentrating crystallization or evaporation to dryness of a solution neutralized by adding benzoic acid to an aqueous solution of caustic soda or an aqueous solution of sodium carbonate (hereinafter referred to as neutralization reaction solution) (third part).
Edition, 66 pages, commentary on Food Additives, edited by Editorial Committee on Food Additives, Kanehara Shuppan Co., Ltd., 1974).

しかしながら、安息香酸ソーダは微細な針状結晶である
ため、結晶間の空隙に多量の水が含まれ易く、濃縮晶析
により生成した結晶を遠心分離又は吸引濾過等、通常の
分離又は濾過方法で分離することを試みても、結晶は水
分50〜60%と含水量の多いスラリー又はケーキ状として
しか得られず、安息香酸ソーダ結晶粉末とするためには
過剰の水分をさらに除去する必要がある、さらに分離又
は濾過のために長時間を要する等、濃縮晶析品を分離す
る方法では安息香酸ソーダを効率良く得ることが困難で
ある(E.C.Clarke,Can.J.Chem.,1974,52,3281)。この
為、一般的に安息香酸ソーダの結晶を得る方法としては
中和反応液を蒸発乾固する方法が用いられている。
However, since sodium benzoate is fine needle-shaped crystals, a large amount of water is likely to be contained in the voids between the crystals, and the crystals produced by concentrated crystallization can be separated by ordinary separation or filtration methods such as centrifugation or suction filtration. Even if it is tried to separate, crystals can be obtained only as a slurry or cake with a high water content of 50 to 60%, and it is necessary to further remove excess water in order to obtain sodium benzoate crystal powder. , It is difficult to efficiently obtain sodium benzoate by a method for separating a concentrated crystallization product, such as requiring a long time for further separation or filtration (ECClarke, Can.J.Chem., 1974, 52 , 3281). ). Therefore, a method of evaporating the neutralization reaction solution to dryness is generally used as a method of obtaining crystals of sodium benzoate.

このような方法で得られた安息香酸ソーダは乾燥した20
0メッシュ(70μ)以下の微細な結晶であり、取り扱い
時に粉立ちしたり粉塵爆発を起こすことがあったりする
という問題があった(H.G.Dorsett Jr.,UNITED STATES
DEPARTMENT OF THE INTERIOR OF BUREAU OF MINES,repo
rt of investigations 7132)。
Sodium benzoate obtained in this way was dried 20
It is a fine crystal of 0 mesh (70μ) or less, and there is a problem that it may stand up during handling or cause a dust explosion (HGDorsett Jr., UNITED STATES
DEPARTMENT OF THE INTERIOR OF BUREAU OF MINES, repo
rt of investigations 7132).

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

安息香酸ソーダの微細結晶が取扱時に粉立ちしたり、粉
塵爆発を起こすことを防止するためには、微細な結晶か
らなる粉末を少なくとも100μ以上の造粒物とする必要
がある。本発明者等は、安息香酸ソーダを取り扱う作業
の危険を軽減し、かつ衛生上の問題を解決するため、安
息香酸ソーダ造粒品を製造する優れた方法を確立するこ
とを図った。
In order to prevent the fine crystals of sodium benzoate from becoming dusty during handling or causing a dust explosion, it is necessary to make the powder of fine crystals into granules of at least 100 μ or more. The present inventors have established an excellent method for producing a granulated product of sodium benzoate in order to reduce the risk of working with sodium benzoate and solve the problem of hygiene.

(ロ)発明の構成 〔問題点を解決するための手段〕 本発明者等は、安息香酸ソーダの粉晶粉末を造粒するに
際し、安息香酸ソーダ粉末中の水分を調節することが重
要なことであり、その手段として安息香酸とカセイソー
ダ水溶液又は炭酸ソーダ水溶液から得られた中和反応液
を使用するという手段を採用することにより適正な粒度
に、かつ容易に安息香酸ソーダの結晶粉末を造粒し得る
ことを見出し、かくして上記粉塵爆発及び粉立ちの問題
を解決し得たのである。
(B) Configuration of the Invention [Means for Solving the Problems] It is important for the present inventors to control the water content in the sodium benzoate powder when granulating the powder crystal powder of sodium benzoate. By adopting a means of using a neutralization reaction solution obtained from benzoic acid and a caustic soda aqueous solution or a sodium carbonate aqueous solution as the means, an appropriate particle size can be easily obtained, and the crystal powder of sodium benzoate can be easily granulated. It was possible to solve the above problems of dust explosion and dusting.

即ち、本発明はカセイソーダ水溶液又は炭酸ソーダ水溶
液と安息香酸との中和反応液から得られる安息香酸ソー
ダ結晶粉末に、前記中和反応液を安息香酸ソーダ100重
量部に対して、水が25〜42重量部となる量添加すること
により調湿して造粒することを特徴とする安息香酸ソー
ダ造粒品の製造方法に関するものである。
That is, the present invention is a sodium benzoate crystal powder obtained from a neutralization reaction solution of an aqueous solution of caustic soda or an aqueous solution of sodium carbonate and benzoic acid, the neutralization reaction solution to 100 parts by weight of sodium benzoate, water is 25 ~. The present invention relates to a method for producing a granulated product of sodium benzoate, which comprises adding 42 parts by weight to adjust the humidity and granulate.

本発明に於いて使用する安息香酸としてはトルエンの酸
化反応等により得られる一般的に使用されている安息香
酸を用いることができる。
As the benzoic acid used in the present invention, a generally used benzoic acid obtained by an oxidation reaction of toluene or the like can be used.

また、カセイソーダ水溶液は通常の食塩の電気分解で得
られるカセイソーダ水溶液を用いることができる。炭酸
ソーダも工業的規模で広く用いられている純度のものが
使用可能である。
Further, as the caustic soda aqueous solution, a caustic soda aqueous solution obtained by electrolysis of ordinary sodium chloride can be used. Sodium carbonate having a purity widely used on an industrial scale can also be used.

中和反応は、カセイソーダ又は炭酸ソーダと安息香酸の
量を、一般的には化学当量比となるようにして行い、安
息香酸ソーダが結晶として析出しないような濃度に調整
したカセイソーダ水溶液又は炭酸ソーダ水溶液を用いて
行う。安息香酸ソーダの水への溶解度は室温から60℃付
近までは約38重量%であるので、例えばカセイソーダ水
溶液を使用する場合には15重量%以下のカセイソーダ水
溶液を使用することが望ましい。また、安息香酸の水へ
の溶解度は20℃で3g/、40℃で6g/、60℃で12g/、
80℃で28g/と温度とともに上昇する為、予めカセイソ
ーダ水溶液を40〜60℃に加熱して安息香酸を添加するこ
とが反応を促進するためには望ましい。
The neutralization reaction is carried out so that the amount of caustic soda or sodium carbonate and benzoic acid is generally in a chemical equivalent ratio, and the caustic soda aqueous solution or sodium carbonate aqueous solution is adjusted to a concentration such that sodium benzoate does not precipitate as crystals. Using. Since the solubility of sodium benzoate in water is about 38% by weight from room temperature to around 60 ° C., when using an aqueous caustic soda solution, it is desirable to use an aqueous caustic soda solution of 15% by weight or less. The solubility of benzoic acid in water is 3g / at 20 ° C, 6g / at 40 ° C, 12g / at 60 ° C,
Since the temperature rises to 28 g / at 80 ° C, it is desirable to preheat the caustic soda aqueous solution to 40-60 ° C and add benzoic acid to promote the reaction.

この様にして得られた中和反応液は、造粒工程で処理さ
れる安息香酸ソーダ結晶粉末を得るための原料として用
いられる原料用と、造粒工程での水分の調整に用いられ
る調湿用に分けられる。中和反応液の使用方法として
は、1バッチを原料用と調湿用の2種に適当に分けて使
用してもよいし、バッチ毎に原料用と調湿用の2種に区
分して使用してもよく、特に限定されない。
The neutralization reaction liquid thus obtained is used as a raw material for obtaining a sodium benzoate crystal powder to be treated in the granulation step, and as a humidity control used for adjusting the water content in the granulation step. Divided for. As a method of using the neutralization reaction liquid, one batch may be appropriately divided into two types, one for raw material and one for humidity control, or it may be divided into two types for raw material and humidity control for each batch. It may be used and is not particularly limited.

前記した様に一般的には安息香酸ソーダ結晶の粉末は、
得られた中和反応液を蒸発乾固することにより得ること
ができる。蒸発乾固する方法としては、例えば通常の減
圧濃縮法、スプレードライ法、ドラムドライ法等が用い
られる。通常の濃縮蒸発法にて得られる安息香酸ソーダ
結晶中の水分は1%前後である。
As described above, the powder of sodium benzoate crystals is generally
It can be obtained by evaporating the obtained neutralization reaction liquid to dryness. As a method of evaporating to dryness, for example, a usual vacuum concentration method, a spray drying method, a drum drying method and the like are used. The water content in the sodium benzoate crystal obtained by the usual concentrated evaporation method is about 1%.

本発明においては、中和反応液の蒸発乾固、濃縮蒸発な
どにより得られる結晶に中和反応液を加えて造粒用原料
とするが、中和反応液は、造粒用原料中の安息香酸ソー
ダ100重量部に対して、好ましくは水が25〜42重量部、
更に30〜40重量部となる量添加される。例えば30重量%
の安息香酸ソーダ中和反応液の場合では40〜73重量部、
更に好ましくは49〜69重量部加える。
In the present invention, the neutralization reaction liquid is added to the crystals obtained by evaporating the neutralization reaction liquid to dryness, concentration, and the like to be used as the raw material for granulation. The neutralization reaction liquid is benzoin in the raw material for granulation. With respect to 100 parts by weight of acid soda, preferably 25 to 42 parts by weight of water,
Further, 30 to 40 parts by weight is added. For example, 30% by weight
In the case of the sodium benzoate neutralization reaction solution of 40-73 parts by weight,
More preferably, 49 to 69 parts by weight are added.

水が25重量部より少ないと、水による安息香酸ソーダ粉
末粒子相互の結合が不十分なため、造粒工程での未造粒
品が多くなる。未造粒品が多いということは、造粒工程
から混合又は混練工程に再循環しないければならないも
のが多くなることを意味し、混合又は混練のための造粒
設備が大きくしたり、混合又は混練に長時間を必要とす
るという問題が発生する。
If the amount of water is less than 25 parts by weight, the mutual binding of the sodium benzoate powder particles with water is insufficient, and the amount of ungranulated products in the granulation process increases. The fact that there are many ungranulated products means that many things must be recirculated from the granulation process to the mixing or kneading process, and the granulation equipment for mixing or kneading becomes large, or There is a problem that it takes a long time for kneading.

又、水が42重量部より多くなると、造粒時に混合又は混
練設備及び造粒設備の内壁等に、結晶粉末が付着する量
が多く、かつ得られた造粒品の相互付着も激しくなり、
実質的に造粒は困難となる。
Further, when the amount of water is more than 42 parts by weight, the amount of the crystal powder adhered to the inner wall of the mixing or kneading equipment and the granulation equipment during granulation is large, and the mutual adhesion of the obtained granulated product becomes severe,
Granulation becomes practically difficult.

安息香酸ソーダ結晶粉末と中和反応液の混合又は混練方
法としては、一般的な混合方法又は混練方法が採用で
き、特別な制限はない。安息香酸ソーダ結晶粉末と中和
反応液の添加順序は何れでも良く、安息香酸ソーダ結晶
粉末に中和反応液を加えても良く、又その逆でも良い。
As a method for mixing or kneading the sodium benzoate crystal powder and the neutralization reaction liquid, a general mixing method or a kneading method can be adopted and there is no particular limitation. The sodium benzoate crystal powder and the neutralization reaction solution may be added in any order, and the neutralization reaction solution may be added to the sodium benzoate crystal powder or vice versa.

混合又は混練方法はその設備として容器回転型又は容器
固定型の混合又は混練設備の何れでも使用可能である。
一般的には安息香酸ソーダ結晶粉末に中和反応液を添加
し、リボン型混合機で混合する。
As the mixing or kneading method, any of a container rotating type or a container fixed type mixing or kneading apparatus can be used as the equipment.
In general, a neutralization reaction solution is added to sodium benzoate crystal powder and mixed with a ribbon mixer.

安息香酸ソーダ結晶粉末と中和反応液を混合又は混練し
た後、当該混合品又は混練品を造粒機にて造粒するが、
造粒機としては転動型、振動型、圧縮型、押し出し型の
何れの造粒機でも使用可能である。これらの一般的な造
粒成形法のなかでは、所望する造粒品品質にもよるが、
押し出し成形して造粒する方法が望ましい。このとき、
造粒品の大きさは、押し出し機の目皿の粗さにより調整
され、直径0.2〜1.2mm、長さ数mm〜数cmの丸みを帯びた
棒状品として得られる。
After mixing or kneading the sodium benzoate crystal powder and the neutralization reaction solution, the mixture or the kneaded product is granulated by a granulator,
As the granulator, any of a rolling type, a vibration type, a compression type and an extrusion type can be used. Among these general granulation molding methods, depending on the desired granulated product quality,
A method of extruding and granulating is desirable. At this time,
The size of the granulated product is adjusted by the roughness of the perforated plate of the extruder, and is obtained as a round bar-shaped product having a diameter of 0.2 to 1.2 mm and a length of several mm to several cm.

造粒した安息香酸ソーダは所望により、例えば水分1重
量%以下になるように乾燥する。ここで用いる乾燥方法
としてはバスケット型、気流法、流動法の何れでも、又
回分式、連続式何れでも適用可能であるが、一般的には
連続式流動乾燥法にて乾燥する。乾燥した安息香酸ソー
ダ造粒品は、篩により粒度を調節した後、容器等へ収納
される。収納に際し、安息香酸ソーダは吸湿性を有する
ため、湿気に注意した収納する。又、貯蔵保管に際して
も同様に、湿気に注意して貯蔵保管することが望まし
い。
If desired, the granulated sodium benzoate is dried to have a water content of 1% by weight or less. As the drying method used here, any of a basket type, an air flow method, a fluidizing method, a batch type and a continuous type can be applied, but in general, a continuous type fluidizing drying method is used. The dried sodium benzoate granulation product is stored in a container or the like after adjusting the particle size with a sieve. When storing, soda benzoate has hygroscopicity, so store it paying attention to moisture. Similarly, when storing and storing the same, it is desirable that the storage and storage should be performed while paying attention to moisture.

〔作用〕[Action]

安息香酸とカセイソーダ水溶液を濃縮して得られた結晶
を105℃で乾燥し、示差熱分析を行って結果では、結晶
水は認められず、すべて付着水であった。これらの結晶
表面の付着水は結晶相互の結合剤として作用し、造粒時
に安息香酸ソーダ結晶粉末中に含まれるべき水分を中和
反応液中の水分で賭うことによって、前記した様に造粒
を安定的に且つ良好になし得るという優れた作用を示
す。
The crystals obtained by concentrating the benzoic acid and caustic soda aqueous solution were dried at 105 ° C. and subjected to differential thermal analysis. As a result, no water of crystallization was observed and all the water was attached water. The water adhering to the surface of these crystals acts as a binding agent for the crystals, and the water to be contained in the sodium benzoate crystal powder at the time of granulation is betted with the water in the neutralization reaction solution to produce the water as described above. It exhibits an excellent effect that the grains can be formed stably and satisfactorily.

〔実施例〕〔Example〕

以下実施例を示して本発明をより具体的に説明する。 Hereinafter, the present invention will be described more specifically with reference to examples.

実施例1 10重量%のカセイソーダ水溶液100重量部を50℃に加熱
し、撹拌下、安息香酸30.5重量部を2時間で加え、更に
1時間撹拌しPH9の安息香酸ソーダ水溶液を得た。この
水溶液100重量部を蒸発乾固して水分1%の安息香酸ソ
ーダ結晶27.4重量部を得た。得られた安息香酸ソーダ結
晶に上記中和反応液11.4重量部を加え、ニーダーで1時
間混練して造粒用安息香酸ソーダ混練品を得、直径0.8m
mの目皿を有する横型押し出し造粒機により造粒後、110
℃の熱風乾燥機にて乾燥し、水分0.5%の安息香酸ソー
ダ造粒品28.8重量部を得た。得られた安息香酸ソーダ造
粒品は、A型硬度計により硬度を測定した結果、平均13
の表面が滑らかなかつ相互付着のない造粒品であり、直
径0.8mm、長さ数mm〜数cmの丸みを帯びた棒状品であっ
た。又特殊型粉塵爆発試験装置KPK−II型で粉塵爆発性
を検討したが濃度2000mg/でも粉塵爆発は起こらなか
った。
Example 1 100 parts by weight of a 10 wt% caustic soda aqueous solution was heated to 50 ° C., 30.5 parts by weight of benzoic acid was added with stirring for 2 hours, and the mixture was further stirred for 1 hour to obtain an aqueous sodium benzoate solution of PH9. 100 parts by weight of this aqueous solution was evaporated to dryness to obtain 27.4 parts by weight of sodium benzoate crystals having a water content of 1%. 11.4 parts by weight of the above neutralization reaction solution was added to the obtained sodium benzoate crystals, and the mixture was kneaded with a kneader for 1 hour to obtain a kneaded product of sodium benzoate for granulation.
After granulating with a horizontal extrusion granulator with m
It was dried with a hot air dryer at ℃ to obtain 28.8 parts by weight of a granulated product of sodium benzoate having a water content of 0.5%. The obtained sodium benzoate granulated product had an average hardness of 13 as a result of measuring the hardness with an A type hardness meter.
It was a granulated product with a smooth surface and no mutual adhesion, and was a round bar product with a diameter of 0.8 mm and a length of several mm to several cm. In addition, we examined the dust explosiveness with the special type dust explosion tester KPK-II type, but no dust explosion occurred even at a concentration of 2000 mg /.

実施例2 実施例1に於いて10重量%カセイソーダ水溶液の代わり
に13.3重量%炭酸ソーダ水溶液を使用し、以下実施例1
と同様の操作を行い、A型硬度計による硬度12の、かつ
濃度2000mg/でも粉塵爆発性を有しない安息香酸ソー
ダ造粒品28.2重量部を得た。
Example 2 In Example 1, a 13.3 wt% sodium carbonate aqueous solution was used instead of the 10 wt% caustic soda aqueous solution.
28.2 parts by weight of a sodium benzoate granulated product having a hardness of 12 by an A type hardness meter and having no dust explosive property even at a concentration of 2000 mg / was obtained.

(ハ)発明の効果 本発明によれば、安息香酸ソーダ結晶粉末を効率良く造
粒でき、微細結晶の有する粉立ち現象及び粉塵爆発性の
問題を解決することができ、安息香酸ソーダ取扱時の作
業環境及び安全性の大幅な改良が可能となり、本発明は
安息香酸ソーダ造粒品を経済的に製造することを可能と
し、安息香酸ソーダを使用する食品、医薬、有機合成化
学業界に寄与するものである。
(C) Effect of the Invention According to the present invention, it is possible to efficiently granulate sodium benzoate crystal powder, solve the problems of dusting and dust explosiveness that fine crystals have, and handle sodium soda benzoate. The working environment and safety can be greatly improved, and the present invention makes it possible to economically produce a sodium benzoate granulated product, and contributes to the food, pharmaceutical and organic synthetic chemistry industries using the sodium benzoate. It is a thing.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 A61K 31/19 9454−4C ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display area A61K 31/19 9454-4C

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】カセイソーダ水溶液又は炭酸ソーダ水溶液
と安息香酸との中和反応液から得られた安息香酸ソーダ
結晶粉末に、前記中和反応液を、安息香酸ソーダ100重
量部に対して、水が25〜42重量部となる量添加すること
により調湿して造粒することを特徴とする安息香酸ソー
ダ造粒品の製造方法。
1. A sodium benzoate crystal powder obtained from a neutralization reaction solution of an aqueous solution of caustic soda or an aqueous solution of sodium carbonate and benzoic acid is added to the neutralization reaction solution, and water is added to 100 parts by weight of sodium benzoate. A method for producing a granulated product of sodium benzoate, which comprises granulating by adjusting the humidity by adding 25 to 42 parts by weight.
JP62237505A 1987-09-24 1987-09-24 Method for producing granulated product of sodium benzoate Expired - Fee Related JPH0784410B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62237505A JPH0784410B2 (en) 1987-09-24 1987-09-24 Method for producing granulated product of sodium benzoate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62237505A JPH0784410B2 (en) 1987-09-24 1987-09-24 Method for producing granulated product of sodium benzoate

Publications (2)

Publication Number Publication Date
JPS6483045A JPS6483045A (en) 1989-03-28
JPH0784410B2 true JPH0784410B2 (en) 1995-09-13

Family

ID=17016313

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62237505A Expired - Fee Related JPH0784410B2 (en) 1987-09-24 1987-09-24 Method for producing granulated product of sodium benzoate

Country Status (1)

Country Link
JP (1) JPH0784410B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111943834A (en) * 2020-07-02 2020-11-17 江苏顺丰化工有限公司 Granular sodium benzoate and production method thereof

Also Published As

Publication number Publication date
JPS6483045A (en) 1989-03-28

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