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JPS6242659B2 - - Google Patents
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JPS6242659B2 - - Google Patents

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Publication number
JPS6242659B2
JPS6242659B2 JP55110784A JP11078480A JPS6242659B2 JP S6242659 B2 JPS6242659 B2 JP S6242659B2 JP 55110784 A JP55110784 A JP 55110784A JP 11078480 A JP11078480 A JP 11078480A JP S6242659 B2 JPS6242659 B2 JP S6242659B2
Authority
JP
Japan
Prior art keywords
solution
rie
exchange resin
anion exchange
regenerating
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
JP55110784A
Other languages
Japanese (ja)
Other versions
JPS5735942A (en
Inventor
Koichi Moryama
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.)
Mitsubishi Chemical Aqua Solutions Co Ltd
Original Assignee
Nippon Rensui Co
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 Nippon Rensui Co filed Critical Nippon Rensui Co
Priority to JP11078480A priority Critical patent/JPS5735942A/en
Publication of JPS5735942A publication Critical patent/JPS5735942A/en
Publication of JPS6242659B2 publication Critical patent/JPS6242659B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Treatment Of Water By Ion Exchange (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、糖液の脱色精製に使用した塩素型強
塩基性陰イオン交換樹脂(以下単にCl−RIEと記
す)の再生方法に係るものである。 従来から、蔗糖水溶液、甜菜糖水溶液、ブドー
糖水溶液、果糖水溶液あるいは、これ等の糖の混
合糖水溶液(以下単に糖液と記す)、グリセリン
水溶液等の脱色精製にCl−RIEが使用されてお
り、この脱色精製に使用したCl−RIEの再生方法
としては、塩化ナトリウム水溶液で処理して吸着
した着色物質や有機酸等を溶離すると同時に強塩
基性陰イオン交換樹脂(以下単にRIEと記す)を
塩素型とする方法が採用されている。この方法で
は、RIEに吸着された着色物質が完全に溶離され
ず、しだいに吸着能力が低下する現象が見られ
る。吸着能力がこのように低下したRIEは、塩化
ナトリウムと水酸化ナトリウムとの混合水溶液で
再生する方法、一旦水酸化ナトリウム水溶液で処
理した後塩化ナトリウムで処理する方法等によつ
て再生する方法が採用されるが未だ吸着された着
色物質を完全に溶離する技術は完成されていな
い。 上記のような処理方法によつても、吸着能力が
回復しないRIEについては、次亜塩素酸ナトリウ
ム等による酸化処理により、着色物質を分解し吸
着能力を回復させる、いわゆる回生方法が採用さ
れるが、この次亜塩素酸ナトリウムによる酸化処
理は着色物質ばかりでなくRIE本体をも酸化する
ためRIEの寿命を短くする欠点がある。 本発明者は、次亜塩素酸ナトリウム等の酸化剤
をできるだけ使用せずに、長期間に亘つて糖液中
の着色物質を吸着および溶離することができる
Cl−RIEの再生方法を検討し本発明を完成した。 すなわち本発明は、糖液を塩素型強塩基性陰イ
オン交換樹脂に通液し、該糖液中の着色物質を吸
着させ、着色物質を吸着する能力が減退した上記
陰イオン交換樹脂に、塩化カルシウム水溶液を通
液することにより再生することを特徴とする強塩
基性陰イオン交換樹脂の再生方法をその要旨とす
るものである。 以下に本発明を詳細に説明する。 本発明で再生剤として用いられる塩化カルシウ
ム水溶液の濃度及び使用量は、着色物質の性質や
量によつて異なるが、該塩化カルシウム水溶液の
濃度は、1重量%程度の低濃度から有効であり、
濃度の上昇とともに効力が増大する。しかし、脱
色精製する糖液中に硫酸イオンが存在する場合
は、硫酸カルシウムの沈澱が生ずることになるの
で、硫酸カルシウムの沈澱をおさえるために5〜
10重量%程度の塩化カルシウム水溶液で再生すれ
ばよい。 また、再生時の温度は、高ければ高い程着色物
質の溶離効果が良いが、通常、RIEの耐熱温度で
ある70℃前後の再生剤温度で再生するとその効果
が大きい。 本発明方法は、Cl−RIEに糖液を通液し、着色
物質を吸着する能力が減退した上記RIEに塩化カ
ルシウム水溶液を通液し着色物質の溶離を行うと
ともに、RIEの塩素化を行いCl−RIEとして再生
する発明であるが、着色物質を吸着したRIEの再
生に際し、毎回塩化カルシウム水溶液による再生
を行つてもよく、また通常の再生を塩化ナトリウ
ム水溶液で行ない、塩化ナトリウムで再生して、
能力が完全に回復しなくなつたRIEについて本発
明の方法すなわち塩化カルシウム水溶液による再
生を行つてもよい。 また、本発明の再生を行う場合にも、塩化カル
シウムと水酸化ナトリウムとの混合水溶液による
再生を行つてもよい。 塩化カルシウム水溶液が糖液の脱色精製に使用
したイオン交換樹脂の再生に効果的である理由に
ついては明らかではないが、本発明方法によれば
従来より使用されている塩化ナトリウム水溶液や
塩化ナトリウムと水酸化ナトリウムの混合溶液に
よる再生にくらべて、樹脂細孔部に吸着した色素
物質やその他の有機物等の夾雑物の溶離も効果的
に行なわれるので、次亜塩素酸ナトリウムによる
処理の併用を必要とせず、運転管理が非常に容易
になる。 次に本発明を実施例により具体的に説明する。 実施例 1 内径20mm、高さ1000mmのジヤケツト付ガラス製
カラムに強塩基性陰イオン交換樹脂ダイヤイオン
SA11A(三菱化成工業株式会社製造販売)を
150ml充填し、7%塩化カルシウム溶液200mlを通
液し樹脂をCl型にした。 このCl−RIE塔に炭酸飽充処理後の蔗糖水溶液
(固形分、Brix70)7を65℃に保ちながら通液
し、脱塩水750mlで水洗後、再生剤として70℃の
7%塩化カルシウム溶液を200mlを用いSV5hr-1
で通液し、該RIE塔を再生した。次いでまた蔗糖
液の通液及び再生を行う操作を30サイクル行い、
31サイクル目の再生廃液の脱離色素量を測定し
た。 再生剤として塩化ナトリウムを用いた場合につ
いても、上記と同じ条件で同様の実験を行なつ
た。 結果を第1表に示す。
The present invention relates to a method for regenerating a chlorine-type strongly basic anion exchange resin (hereinafter simply referred to as Cl-RIE) used for decolorizing and purifying a sugar solution. Conventionally, Cl-RIE has been used to decolorize and purify sucrose aqueous solutions, beet sugar aqueous solutions, glucose aqueous solutions, fructose aqueous solutions, mixed sugar solutions of these sugars (hereinafter simply referred to as sugar solutions), glycerin aqueous solutions, etc. The method for regenerating the Cl-RIE used for this decolorization and purification is to elute the adsorbed colored substances and organic acids by treating it with an aqueous sodium chloride solution, and at the same time to elute it with a strong basic anion exchange resin (hereinafter simply referred to as RIE). A chlorine type method is adopted. In this method, the colored substance adsorbed on RIE is not completely eluted, and the adsorption capacity gradually decreases. For RIE whose adsorption capacity has decreased in this way, methods of regenerating it with a mixed aqueous solution of sodium chloride and sodium hydroxide, a method of first treating it with an aqueous sodium hydroxide solution and then treating it with sodium chloride, etc. are adopted. However, the technology to completely elute the adsorbed colored substances has not yet been perfected. For RIE whose adsorption capacity cannot be recovered even with the treatment methods described above, a so-called regeneration method is adopted in which the adsorption capacity is restored by decomposing the colored substance through oxidation treatment using sodium hypochlorite, etc. This oxidation treatment with sodium hypochlorite oxidizes not only the colored substance but also the RIE itself, which has the disadvantage of shortening the life of the RIE. The present inventor is able to adsorb and elute colored substances in sugar solution over a long period of time without using oxidizing agents such as sodium hypochlorite as much as possible.
The present invention was completed after studying a method for regenerating Cl-RIE. That is, in the present invention, a sugar solution is passed through a chlorine-type strongly basic anion exchange resin, colored substances in the sugar solution are adsorbed, and the anion exchange resin, which has a reduced ability to adsorb colored substances, is chlorinated. The gist of this invention is a method for regenerating a strongly basic anion exchange resin, which is characterized by regenerating it by passing an aqueous calcium solution through it. The present invention will be explained in detail below. The concentration and amount of the calcium chloride aqueous solution used as a regenerating agent in the present invention vary depending on the nature and amount of the coloring substance, but the concentration of the calcium chloride aqueous solution is effective from a concentration as low as about 1% by weight.
Potency increases with increasing concentration. However, if sulfate ions are present in the sugar solution to be decolorized and purified, calcium sulfate will precipitate.
It can be regenerated with a calcium chloride aqueous solution of about 10% by weight. Furthermore, the higher the temperature during regeneration, the better the elution effect of the colored substance, but the effect is usually greater when the regenerant temperature is around 70° C., which is the heat-resistant temperature of RIE. In the method of the present invention, a sugar solution is passed through Cl-RIE, and a calcium chloride aqueous solution is passed through the RIE whose ability to adsorb colored substances has decreased to elute colored substances, and the RIE is chlorinated to Cl-RIE. - Although the invention is for regeneration as RIE, each time RIE that has adsorbed a colored substance is regenerated, regeneration with a calcium chloride aqueous solution may be performed, or normal regeneration is performed with a sodium chloride aqueous solution, and regeneration is performed with sodium chloride.
RIEs whose capacity has not been completely restored may be regenerated by the method of the present invention, that is, by using an aqueous calcium chloride solution. Also, when performing the regeneration of the present invention, regeneration may be performed using a mixed aqueous solution of calcium chloride and sodium hydroxide. Although it is not clear why an aqueous calcium chloride solution is effective in regenerating the ion exchange resin used for decolorizing and purifying sugar solutions, the method of the present invention enables the use of aqueous sodium chloride solutions or sodium chloride and water that have been used in the past. Compared to regeneration using a mixed solution of sodium oxide, impurities such as pigments and other organic substances adsorbed in the resin pores can be eluted more effectively, so treatment with sodium hypochlorite is not necessary. Therefore, operation management becomes very easy. Next, the present invention will be specifically explained using examples. Example 1 A glass column with a jacket of 20 mm inner diameter and 1000 mm height was coated with a strong basic anion exchange resin Diaion.
SA11A (manufactured and sold by Mitsubishi Chemical Industries, Ltd.)
It was filled with 150 ml and 200 ml of 7% calcium chloride solution was passed through it to convert the resin into Cl type. Aqueous sucrose solution (solid content, Brix 70) 7 after carbonation treatment was passed through this Cl-RIE tower while maintaining the temperature at 65°C, and after washing with 750ml of demineralized water, a 7% calcium chloride solution at 70°C was added as a regenerating agent. SV5hr -1 using 200ml
The RIE tower was regenerated. Next, 30 cycles of passing the sucrose solution and regenerating were performed.
The amount of dye released from the regenerated waste liquid at the 31st cycle was measured. Similar experiments were conducted under the same conditions as above when sodium chloride was used as the regenerant. The results are shown in Table 1.

【表】 第1表において脱離色素量は塩化ナトリウムに
おける脱離色素量を基準としこれを100として比
較表示した。 実施例 2 内径20mm、高さ1000mmのジヤケツト付ガラス製
カラムに強塩基性陰イオン交換樹脂ダイヤイオン
SA11A(三菱化成工業株式会社製造販売)を
150ml充填し、10%食塩水溶液200c.c.を通液し充填
樹脂をCl型にした。 このCl−RIE塔に、炭酸飽充処理後の蔗糖水溶
液(固形分、Brix70)7を65℃に保ちながら通
液した後水洗し、70℃の10%塩化ナトリウム水溶
液200mlを用いて再生し、水洗した。この操作を
30サイクルくり返した後、31サイクル目は7の
糖液を通液し水洗した状態で終了した。 なお、塩化ナトリウム水溶液及び蔗糖液の通液
はSV=5hr-1の速度で行なつた。 次にこの樹脂をカラムから取り出しカラム上下
部の樹脂をよく混合した後、上記で使用したガラ
ス製カラムと同様のカラム6本に充填した。この
樹脂に、第2表記載の各温度に保持しつつ、各濃
度の塩化カルシウム水溶液をSV=5hr-1で、20ml
通液し、流出液中の溶離色素量を測定した。同様
のテストを第2表記載の各温度及び各濃度の塩化
ナトリウム水溶液20mlと、第2表記載の各温度及
び濃度の塩化ナトリウム水溶液10mlと10%水酸化
ナトリウム水溶液10mlとの混合溶液について行な
つた。
[Table] In Table 1, the amount of dye released is compared with the amount of dye released in sodium chloride as 100. Example 2 Strongly basic anion exchange resin Diaion was placed in a jacketed glass column with an inner diameter of 20 mm and a height of 1000 mm.
SA11A (manufactured and sold by Mitsubishi Chemical Industries, Ltd.)
It was filled with 150 ml and 200 c.c. of 10% saline solution was passed through it to make the filled resin into Cl type. A sucrose aqueous solution (solid content, Brix 70) 7 after carbonation saturation treatment was passed through this Cl-RIE tower while maintaining it at 65°C, washed with water, and regenerated using 200 ml of a 10% sodium chloride aqueous solution at 70°C. Washed with water. This operation
After repeating 30 cycles, the 31st cycle was completed with the sugar solution in step 7 passed through and washed with water. Note that the sodium chloride aqueous solution and the sucrose solution were passed at a rate of SV=5 hr -1 . Next, this resin was taken out from the column, and after thoroughly mixing the resins in the upper and lower parts of the column, the resin was packed into six columns similar to the glass columns used above. To this resin, 20 ml of calcium chloride aqueous solution of various concentrations was added at SV = 5 hr -1 while maintaining each temperature listed in Table 2.
The amount of eluted dye in the effluent was measured. A similar test was conducted on 20 ml of sodium chloride aqueous solution at each temperature and concentration listed in Table 2, and a mixed solution of 10 ml of sodium chloride aqueous solution at each temperature and concentration listed in Table 2 and 10 ml of 10% sodium hydroxide aqueous solution. Ta.

【表】 第2表において溶離色素量は10%塩化ナトリウ
ム水溶液で20℃における溶離色素量を基準とし、
これを100として比較表示した。これらから明ら
かなように本発明の塩化カルシウムを再生剤とし
て使用すれば色素の溶離効果が著しく良好である
ことが理解される。さらに再生剤の温度をあげる
ことによりより一段とその効果が向上することが
理解される。
[Table] In Table 2, the amount of eluted dye is based on the amount of eluted dye at 20°C in a 10% sodium chloride aqueous solution.
This was set as 100 and displayed for comparison. As is clear from these results, it is understood that when the calcium chloride of the present invention is used as a regenerating agent, the dye elution effect is extremely good. Furthermore, it is understood that the effect is further improved by increasing the temperature of the regenerant.

Claims (1)

【特許請求の範囲】 1 糖液を塩素型強塩基性陰イオン交換樹脂に通
液し、該糖液中の着色物質を吸着させ、着色物質
を吸着する能力が減退した上記陰イオン交換樹脂
に、塩化カルシウム水溶液を通液することにより
再生することを特徴とする強塩基性陰イオン交換
樹脂の再生方法。 2 特許請求の範囲第1項記載の強塩基性陰イオ
ン交換樹脂の再生方法において、塩化カルシウム
水溶液が5〜10重量%の塩化カルシウムを含む水
溶液である方法。
[Scope of Claims] 1. A sugar solution is passed through a chlorine-type strongly basic anion exchange resin to adsorb colored substances in the sugar solution, and the anion exchange resin has a reduced ability to adsorb colored substances. A method for regenerating a strongly basic anion exchange resin, the method comprising regenerating a strongly basic anion exchange resin by passing an aqueous calcium chloride solution through the resin. 2. The method for regenerating a strongly basic anion exchange resin according to claim 1, wherein the calcium chloride aqueous solution is an aqueous solution containing 5 to 10% by weight of calcium chloride.
JP11078480A 1980-08-12 1980-08-12 Regeneration of strongly basic anionic exchange resin Granted JPS5735942A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11078480A JPS5735942A (en) 1980-08-12 1980-08-12 Regeneration of strongly basic anionic exchange resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11078480A JPS5735942A (en) 1980-08-12 1980-08-12 Regeneration of strongly basic anionic exchange resin

Publications (2)

Publication Number Publication Date
JPS5735942A JPS5735942A (en) 1982-02-26
JPS6242659B2 true JPS6242659B2 (en) 1987-09-09

Family

ID=14544528

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11078480A Granted JPS5735942A (en) 1980-08-12 1980-08-12 Regeneration of strongly basic anionic exchange resin

Country Status (1)

Country Link
JP (1) JPS5735942A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63148222U (en) * 1987-03-20 1988-09-29

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63148222U (en) * 1987-03-20 1988-09-29

Also Published As

Publication number Publication date
JPS5735942A (en) 1982-02-26

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