JPH0688936B2 - Method for producing granular sodium benzoate - Google Patents

Method for producing granular sodium benzoate

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Publication number
JPH0688936B2
JPH0688936B2 JP23750487A JP23750487A JPH0688936B2 JP H0688936 B2 JPH0688936 B2 JP H0688936B2 JP 23750487 A JP23750487 A JP 23750487A JP 23750487 A JP23750487 A JP 23750487A JP H0688936 B2 JPH0688936 B2 JP H0688936B2
Authority
JP
Japan
Prior art keywords
sodium benzoate
water
weight
granulated
granulation
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
JP23750487A
Other languages
Japanese (ja)
Other versions
JPS6483044A (en
Inventor
正弘 木村
照雄 吉田
Original Assignee
東亞合成化学工業株式会社
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
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Application filed by 東亞合成化学工業株式会社 filed Critical 東亞合成化学工業株式会社
Priority to JP23750487A priority Critical patent/JPH0688936B2/en
Publication of JPS6483044A publication Critical patent/JPS6483044A/en
Publication of JPH0688936B2 publication Critical patent/JPH0688936B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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の造粒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 granulation method of sodium benzoate, which is widely used in various fields as a synthetic raw material for benzoyl peroxide and the like, 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または炭酸ソー
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) 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。
Sodium benzoate is produced by concentrating crystallization or evaporation to dryness of a liquid obtained by adding benzoic acid to an aqueous solution of caustic soda or an aqueous solution of sodium carbonate (hereinafter referred to as a neutralization reaction liquid) (third edition food additive). 66 pages of the compendial document, published by the editorial committee of the compendial document of food additives, published by Kanehara Publishing Co., Ltd. in 1974) However, since sodium benzoate is a fine needle crystal, a large amount of water is contained in the voids between the crystals. Even if an attempt is made to separate the crystals produced by the concentrated crystallization by an ordinary separation or filtration method such as centrifugation or suction filtration, the crystals are formed into a slurry or cake with a water content of 50 to 60% and a high water content. In order to obtain only sodium benzoate crystal powder, it is necessary to further remove excess water, and it takes a long time for further separation or filtration. Works with soda It is difficult to obtain good (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.

この様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という問題があった。(H.G.
Dorsett Jr.,UNITED STATES DEPARTMENT OF THE INTERI
OR OF BUREAU OF MINES,report of investigations 713
2) 〔発明が解決しようとする問題点〕 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
から成る粉末を少なくとも100μ以上の造粒物とする必
要があるため、本発明者等は安息香酸ソーダを効率よく
造粒する方法を確立し、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ことにつ
いて種々検討した。
Sodium benzoate obtained in this way was dried
It was a fine crystal of 0 mesh or less, and there was a problem that it powdered when handling and caused a dust explosion. (HG
Dorsett Jr., UNITED STATES DEPARTMENT OF THE INTERI
OR OF BUREAU OF MINES, report of investigations 713
2) [Problems to be solved by the invention] Fine crystals of sodium benzoate may become powdery during handling,
In order to prevent the dust explosion from occurring, it is necessary to make the powder consisting of fine crystals into a granule having a particle size of at least 100 μ, so the present inventors established a method for efficiently granulating sodium benzoate. However, various studies were conducted to reduce the danger of working with sodium benzoate and to 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、安息香酸ソーダを造粒するに際し、安息
香酸ソーダ中の水分の割合を適切な範囲に調整すること
により、容易に、かつ、経済的に安息香酸ソーダ造粒品
を得ることを見出し、上記粉塵爆発及び粉立ちの問題を
解決し本発明に至った。
(B) Configuration of the invention [Means for solving the problems] The present inventors can easily prepare a granulated sodium benzoate by adjusting the proportion of water in the sodium benzoate to an appropriate range. In addition, they have found that a sodium benzoate granulated product can be obtained economically and have solved the problems of dust explosion and dusting, resulting in the present invention.

即ち、本発明は20〜30重量%の水分を含有する安息香酸
ソーダを造粒することを特徴とする粒状安息香酸ソーダ
の製造方法に関するものである。
That is, the present invention relates to a method for producing granular sodium benzoate, which comprises granulating sodium benzoate containing 20 to 30% by weight of water.

本発明に於いては、中和反応液を蒸発乾固又は蒸発濃縮
して得られる安息香酸ソーダを用いることができる。中
和反応液を蒸発乾固又は蒸発濃縮する方法としては、通
常の方法例えば減圧濃縮法、スプレードライ法、ドラム
ドライ法等が用いられる。
In the present invention, sodium benzoate obtained by evaporating the neutralization reaction solution to dryness or evaporation can be used. As a method for evaporating the neutralization reaction solution to dryness by evaporation or concentration, an ordinary method such as a vacuum concentration method, a spray dry method, a drum dry method or the like is used.

10μ以下の針状結晶として得られた安息香酸ソーダの水
分は結晶取得方法により異なるが、例えば蒸発乾固して
得た結晶の場合には通常1%未満である。
The water content of sodium benzoate obtained as needle-shaped crystals of 10 μm or less depends on the crystal acquisition method, but is usually less than 1% in the case of crystals obtained by evaporation to dryness.

この様にして得られた安息香酸ソーダを効率良く造粒す
るためには、当該安息香酸ソーダ中に水分を20〜30重量
%含有させる必要があり、特に水分が23〜29重量%の場
合、より良く造粒することができる。安息香酸ソーダ中
に含有させる水分は、必ずしも外部から添加する水分で
ある必要はなく、中和反応液の蒸発濃縮を、残留水分が
造粒に適した水分(20〜30重量%)となったときに停止
するなどの手段により、外部から全く水分を添加せず、
そのまま造粒用原料とすることもできる。
In order to efficiently granulate the sodium benzoate obtained in this way, it is necessary to contain 20 to 30% by weight of water in the sodium benzoate, particularly when the water content is 23 to 29% by weight, Better granulation. The water contained in sodium benzoate does not necessarily have to be the water added from the outside, and the evaporation of the neutralization reaction solution caused the residual water to become suitable for granulation (20 to 30% by weight). By means such as sometimes stopping, no water is added from the outside,
It can also be used as it is as a raw material for granulation.

水分の含有量が20重量%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ければ
ならないものが多くなる事を意味し、混合又は混練のた
めの造粒設備を大きくしたり、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。
When the content of water is less than 20% by weight, the mutual binding of the sodium benzoate powder particles with water is insufficient, and the number of ungranulated products in the granulation process increases. The fact that there are many ungranulated products means that many things must be recycled from the granulation process to the mixing or kneading process, and the granulating equipment for mixing or kneading is enlarged, or There is a problem that it takes a long time for kneading.

又、水分の含有量が30重量%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, if the water content is more than 30% by weight, the amount of the crystal powder adhered to the inner wall of the mixing or kneading equipment and the granulation equipment at the time of granulation is large, and the mutual adhesion of the obtained granulated product is also caused. It becomes violent and practically difficult to granulate.

安息香酸ソーダ結晶粉末と水と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水の添加順序は
何れでも良く、安息香酸ソーダ粉末に水を加えても良
く、又その逆でも良い。
As a method for mixing or kneading the sodium benzoate crystal powder and water, a general mixing method or a kneading method can be adopted, and there is no particular limitation. The sodium benzoate crystal powder and water may be added in any order, and water may be added to the sodium benzoate powder or vice versa.

混合又は混練を行うには容器回転型又は容器固定型の何
れの設備でも使用可能である。一般的には中和反応液を
蒸発乾固して得られた安息香酸ソーダ粉末に水を添加
し、リボン型混合機で混合する。
For mixing or kneading, any equipment of container rotation type or container fixed type can be used. Generally, water is added to the sodium benzoate powder obtained by evaporating the neutralization reaction solution to dryness, and mixed with a ribbon mixer.

適量の水分を含有する安息香酸ソーダを造粒機にて造粒
するが、造粒機としては転動型、振動型、圧縮型、押し
出し成形型の何れのものでも使用することができる。こ
れらの一般的な造粒法のなかでは、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。
Although sodium benzoate containing an appropriate amount of water is granulated by a granulator, any of a rolling type, a vibration type, a compression type and an extrusion type can be used as the granulating device. Among these general granulation methods, the method of granulating by extrusion molding is desirable, depending on the desired quality of the granulated product. At this time, the size of the granulated product is adjusted by the roughness of the perforated plate of the extruder to obtain 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、容器等に収納す
る。収納に際し、安息香酸ソーダは吸湿性を有するた
め、湿気に注意して収納する。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, sodium benzoate has hygroscopic properties, 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又は炭酸ソーダ水溶液か
ら安息香酸ソーダ水溶液を得、これ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た結果では、結
晶水は認められず、すべて付着水であった。これらの結
晶表面の付着水が結晶相互の結合剤として作用し、特に
特定量の水分が安息香酸ソーダの造粒を定常化し且つ良
好にするという優れた作用を示す。
An aqueous solution of sodium benzoate was obtained from an aqueous solution of benzoic acid and caustic soda or an aqueous solution of sodium carbonate, and the crystals obtained by concentrating this were dried at 105 ° C and the results of differential thermal analysis showed that no water of crystallization was observed and all the water was attached. It was water. The water adhering to the surface of these crystals acts as a binder for the mutual crystals, and in particular, a specific amount of water has an excellent effect that the granulation of sodium benzoate is stabilized and good.

〔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.

10重量%のカセイソーダ水溶液100重量部を50℃に加熱
し、攪拌下、これに安息香酸を化学理論量加え(30.5重
量部)、更に1時間攪拌して安息香酸ソーダ水溶液を得
た。この水溶液を濃縮蒸発乾固して水分0.5%で10μ以
下の針状結晶の安息香酸ソーダ粉末35.3重量部を得た。
この安息香酸ソーダ粉末に表1に示した各割合で水を添
加後、ニーダーで混合し、造粒用混合品を得た。得られ
た造粒用混合品を直径1.0mm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、水分含有造粒品を得、その外観を観察した。
100 parts by weight of a 10 wt% caustic soda aqueous solution was heated to 50 ° C., a stoichiometric amount of benzoic acid was added to this under stirring (30.5 parts by weight), and the mixture was further stirred for 1 hour to obtain an aqueous sodium benzoate solution. This aqueous solution was concentrated and evaporated to dryness to obtain 35.3 parts by weight of needle-shaped crystalline sodium benzoate powder having a water content of 0.5% and 10 μm or less.
Water was added to the sodium benzoate powder at the ratios shown in Table 1 and mixed with a kneader to obtain a granulated mixture. The obtained mixture for granulation is granulated by a horizontal extrusion granulator having a 1.0 mm diameter plate and then dried by a hot air dryer at 110 ° C to obtain a water-containing granulated product, and its appearance is observed. did.

実施例1〜3に示した様に、安息香酸ソーダが含有する
水分を20〜30重量%に調整して造粒すると、未造粒品は
殆どなく、造粒品の表面が滑らかで、大きさが揃い、流
動性に富むものが得られた。ほとんど(99重量%以上)
の造粒品は、その直径が1.0mm、長さ数mm〜数cmの丸み
を帯びた棒状品であった。
As shown in Examples 1 to 3, when the water content of sodium benzoate is adjusted to 20 to 30% by weight and granulated, there is almost no ungranulated product and the surface of the granulated product is smooth and large. A product with uniform liquidity and high liquidity was obtained. Most (99% by weight or more)
The granulated product of was a round bar-shaped product having a diameter of 1.0 mm and a length of several mm to several cm.

一方、安息香酸ソーダに含まれる水分が20重量%より小
さい比較例1では、未造粒品が多く、造粒品の表面がザ
ラザラしていた。
On the other hand, in Comparative Example 1 in which the water content of sodium benzoate was less than 20% by weight, there were many ungranulated products and the surface of the granulated products was rough.

また、安息香酸ソーダに含まれる水分が30重量%より多
い比較例2では、造粒品が互いに付着し大きな塊状とな
り、造粒品表面の凹凸が大きく、流動性のある造粒品が
得られなかった。
Further, in Comparative Example 2 in which the water content of sodium benzoate was more than 30% by weight, the granulated products adhered to each other to form a large lump, and the granulated product surface had large irregularities and a fluidized granulated product was obtained. There wasn't.

(ハ)発明の効果 本発明の方法によれば、安息香酸ソーダを効率良く造粒
でき、結晶が微細な為に起こる粉立ち及び粉塵爆発を防
止することができ、その結果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 method of the present invention, sodium benzoate can be efficiently granulated, and it is possible to prevent dusting and dust explosion that occur due to fine crystals, and as a result, when handling sodium benzoate. The present invention can greatly improve the working environment and safety, and the present invention contributes to the food, pharmaceutical and organic synthetic chemistry industries using sodium benzoate.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】20〜30重量%の水分を含有する安息香酸ソ
ーダを造粒することを特徴とする粒状安息香酸ソーダの
製造方法。
1. A method for producing granular sodium benzoate, which comprises granulating sodium benzoate containing 20 to 30% by weight of water.
JP23750487A 1987-09-24 1987-09-24 Method for producing granular sodium benzoate Expired - Fee Related JPH0688936B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23750487A JPH0688936B2 (en) 1987-09-24 1987-09-24 Method for producing granular sodium benzoate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23750487A JPH0688936B2 (en) 1987-09-24 1987-09-24 Method for producing granular sodium benzoate

Publications (2)

Publication Number Publication Date
JPS6483044A JPS6483044A (en) 1989-03-28
JPH0688936B2 true JPH0688936B2 (en) 1994-11-09

Family

ID=17016297

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23750487A Expired - Fee Related JPH0688936B2 (en) 1987-09-24 1987-09-24 Method for producing granular sodium benzoate

Country Status (1)

Country Link
JP (1) JPH0688936B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1011307C1 (en) * 1999-02-15 2000-08-17 Dsm Nv Method for shaping (earth) alkali metal benzoate particles.
CN100463895C (en) * 2006-07-27 2009-02-25 天津市东大化工有限公司 Granular sodium benzoate and its production process
KR20160036559A (en) 2013-07-26 2016-04-04 디에스엠 아이피 어셋츠 비.브이. Improved powderous formulations of organic acids or esters having an aromatic ring system
JP2015189900A (en) * 2014-03-28 2015-11-02 出光興産株式会社 Methylene chloride solution of 3-pentadecylphenol, method for producing the same, and method for producing polycarbonate resin using the solution

Also Published As

Publication number Publication date
JPS6483044A (en) 1989-03-28

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