JPS6329993B2 - - Google Patents
Info
- Publication number
- JPS6329993B2 JPS6329993B2 JP60094201A JP9420185A JPS6329993B2 JP S6329993 B2 JPS6329993 B2 JP S6329993B2 JP 60094201 A JP60094201 A JP 60094201A JP 9420185 A JP9420185 A JP 9420185A JP S6329993 B2 JPS6329993 B2 JP S6329993B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- fruit juice
- water
- regeneration
- treatment
- 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
Links
- 239000011347 resin Substances 0.000 claims description 29
- 229920005989 resin Polymers 0.000 claims description 29
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000000126 substance Substances 0.000 claims description 11
- 238000011001 backwashing Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 7
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 7
- 238000013019 agitation Methods 0.000 claims description 6
- 235000020971 citrus fruits Nutrition 0.000 claims description 6
- 238000001125 extrusion Methods 0.000 claims description 6
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims description 6
- 230000001172 regenerating effect Effects 0.000 claims description 6
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims description 2
- 239000003957 anion exchange resin Substances 0.000 claims 1
- 238000011069 regeneration method Methods 0.000 description 12
- 230000008929 regeneration Effects 0.000 description 11
- 239000000243 solution Substances 0.000 description 7
- 238000002347 injection Methods 0.000 description 6
- 239000007924 injection Substances 0.000 description 6
- 235000019658 bitter taste Nutrition 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 235000015203 fruit juice Nutrition 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000011345 viscous material Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000005349 anion exchange Methods 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
Landscapes
- Non-Alcoholic Beverages (AREA)
Description
本発明は柑橘類果汁の脱苦味または減酸処理に
使用した樹脂の再生方法の改良に関する。
従来、これら樹脂の再生方法は次のような工程
がとられるのが一般的である。例えば脱苦味処理
の合成吸着樹脂の場合は、通液→液押出→水抜→
空気撹拌→水逆洗→水抜→空気撹拌→水逆洗→沈
静→苛性ソーダ(薬品)注入→押出→水抜→塩酸
液張(中和処理)→空気撹拌→水抜→水逆洗→洗
浄→水抜→果汁液張→通液。
ところが、果汁原液中にはパイプ質や粘性物質
が含まれていて通液中に樹脂に絡まり、圧損の原
因となるため、通常のイオン交換装置の再生方法
のように水逆洗だけでは復元し得ず、前述のよう
に空気撹拌を行い水逆洗を行う工程を2度繰返し
ても樹脂の絡まりは容易にほぐれず、マツドボー
ルとなり易い。樹脂層にマツドボールが生ずると
薬液の流れが不均等になり、再生が不十分とな
り、性能低下を誘発する。このような傾向は脱苦
味塔および減酸塔を別個に直列に連結した精製装
置にあつては、最初の塔の樹脂再生時に著しく現
われる。
本発明は柑橘類果汁の精製樹脂の再生に際して
従来の再生方法において生ずる上述の通液による
樹脂の絡まりを完全にほぐして均質な樹脂層を復
元し、薬液の注入、押出しによる再生効率を良好
にする再生方法を提供することを目的とするもの
である。
すなわち本発明の再生方法は、柑橘類果汁の合
成吸着樹脂による脱苦味処理または陰イオン交換
装置による減酸処理に用いた樹脂の再生方法にお
いて、前記樹脂への薬品の注入、押出による処理
工程前に、前記樹脂を苛性ソーダ液に浸潤した
後、空気撹拌、水逆洗処理を行うことを特徴とす
るものである。
本発明は柑橘類果汁中に含まれ、樹脂の絡りの
原因となるパイプ質や粘性物質が苛性ソーダ液に
比較的容易に溶解することを利用するものであつ
て、通液終了後、液の押出を行い、空気撹拌の前
に約3〜10%NaOHを樹脂層表面より約100mm程
上部まで注入して浸潤させた後、空気撹拌を行つ
て水逆洗を行うと樹脂が良くほぐれて、汚染も速
やかに洗浄されて、均質な樹脂層を作ることがで
きるものである。その後、空気撹拌、水逆洗を再
度繰返すと、NaOH浸潤を行わない場合に比べ
て非常に速やかに清澄し、樹脂層が均質となつて
薬注以下の再生操作がスムーズに行われるように
なる。
以下に実施例を示す。
実施例
果汁原液の脱苦味処理を行つた合成吸着樹脂の
再生を本発明方法によつた実施例と前述した従来
方法によつた比較例につき実施した。脱苦味塔と
しては塔径200mm、高さ700mmのものを用い、この
塔内に高さ350mmに合成吸着樹脂を充填した。そ
の結果は次表のようになつた。
The present invention relates to an improvement in a method for regenerating resin used for removing bitterness or reducing acidity from citrus fruit juice. Conventionally, methods for recycling these resins generally involve the following steps. For example, in the case of synthetic adsorption resin for bitterness removal treatment, liquid passing → liquid extrusion → water removal →
Air stirring → water backwashing → water removal → air stirring → water backwashing → settling → caustic soda (chemical) injection → extrusion → water removal → hydrochloric acid solution (neutralization treatment) → air stirring → water removal → water backwashing → washing → water removal → Fruit juice liquid tension → liquid passage. However, the raw fruit juice contains pipes and viscous substances that get entangled with the resin during liquid passage and cause pressure loss, so it cannot be restored by simply backwashing with water, which is the usual method for regenerating ion exchange equipment. Even if the above-described steps of air agitation and water backwashing are repeated twice, the tangles of the resin cannot be easily loosened, and matted balls tend to form. When mud balls occur in the resin layer, the flow of the chemical solution becomes uneven, leading to insufficient regeneration and deterioration of performance. In the case of a purification apparatus in which a bitterening tower and an acid reducing tower are separately connected in series, this tendency becomes noticeable during resin regeneration in the first tower. The present invention completely loosens the tangles of the resin caused by the above-mentioned liquid passage when regenerating the purified resin of citrus fruit juice, restores a homogeneous resin layer, and improves the regeneration efficiency by injection and extrusion of chemical solutions. The purpose is to provide a reproduction method. That is, the regeneration method of the present invention is a method for regenerating a resin used for the bitterness removal treatment of citrus fruit juice using a synthetic adsorption resin or the acid reduction treatment using an anion exchange device, in which the resin is injected with chemicals into the resin before the treatment step by extrusion. The method is characterized in that after the resin is infiltrated into a caustic soda solution, air agitation and water backwashing are performed. The present invention takes advantage of the fact that pipes and viscous substances contained in citrus fruit juice that cause resin entanglement are relatively easily dissolved in a caustic soda solution. Before air agitation, approximately 3 to 10% NaOH is injected to about 100 mm above the surface of the resin layer to infiltrate it, and then air agitation and backwashing with water will loosen the resin and eliminate contamination. It can also be quickly washed to create a homogeneous resin layer. After that, when air agitation and water backwashing are repeated again, the clarification becomes much faster than when NaOH infiltration is not performed, and the resin layer becomes homogeneous, allowing regeneration operations beyond chemical injection to be performed smoothly. . Examples are shown below. Examples The regeneration of synthetic adsorption resins obtained by removing bitterness from fruit juice stock solutions was carried out in Examples using the method of the present invention and Comparative Examples using the conventional method described above. The bitterness removal tower used was one with a tower diameter of 200 mm and a height of 700 mm, and the inside of this tower was filled with synthetic adsorption resin to a height of 350 mm. The results were as shown in the table below.
【表】【table】
【表】
このように本発明実施例によつた場合、樹脂層
が均等に沈積するため、以下の薬注→押出→水抜
→塩酸液張→空気撹拌→水抜→水逆洗→洗浄→水
抜の再生操作がスムーズに、効率よく行うことが
できたのに反し、比較例、すなわち通常の従来方
法によつた場合には樹脂の底部に若干の固まりが
残存し、これが以下の再生工程において薬液の流
れを不均等にし、再生が不十分となつた。
以上のような本発明による効果を例挙すれば次
のようである。
○イ 均等な薬注により安定した再生ができる。
○ロ 再生前処理の逆洗水量を30%程度節約でき
る。
○ハ 前添加する苛性ソーダは薬注用の苛性ソーダ
をあてることができるので、薬品量を増さなく
てもよく、設備費もほとんど増えない。
○ニ 逆洗水量を節減することにより、再生時間も
若干短くできる。[Table] In the case of the embodiment of the present invention, the resin layer is deposited evenly, so the following steps: chemical injection → extrusion → water removal → hydrochloric acid solution → air stirring → water removal → water backwashing → washing → water removal. While the regeneration operation was able to be carried out smoothly and efficiently, in the comparative example, that is, when the normal conventional method was used, some lumps remained at the bottom of the resin, and this caused difficulty in applying the chemical solution in the following regeneration process. This resulted in uneven flow and insufficient regeneration. Examples of the effects of the present invention as described above are as follows. ○B Stable regeneration can be achieved by uniform chemical injection. ○B The amount of backwash water used for pre-regeneration treatment can be saved by approximately 30%. ○C The pre-added caustic soda can be used for chemical injection, so there is no need to increase the amount of chemicals and there is almost no increase in equipment costs. ○D By reducing the amount of backwash water, the regeneration time can be slightly shortened.
Claims (1)
または陰イオン交換樹脂による減酸処理に用いた
樹脂の再生方法において、前記樹脂への薬品の注
入、押出による処理工程の前に、前記樹脂を苛性
ソーダ液に浸潤した後、空気撹拌、水逆洗処理を
行うことを特徴とする柑橘類果汁精製樹脂の再生
方法。1. In a method for regenerating a resin used for de-bitterness treatment of citrus fruit juice with a synthetic adsorption resin or acid reduction treatment with an anion exchange resin, the resin is treated with a caustic soda solution before the treatment step of injecting chemicals into the resin and extrusion. A method for regenerating citrus fruit juice purification resin, which comprises infiltrating it into a liquid, followed by air agitation and water backwashing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60094201A JPS61254166A (en) | 1985-05-01 | 1985-05-01 | Regeneration of resin for purifying citrus fruit juice |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60094201A JPS61254166A (en) | 1985-05-01 | 1985-05-01 | Regeneration of resin for purifying citrus fruit juice |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61254166A JPS61254166A (en) | 1986-11-11 |
JPS6329993B2 true JPS6329993B2 (en) | 1988-06-16 |
Family
ID=14103683
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60094201A Granted JPS61254166A (en) | 1985-05-01 | 1985-05-01 | Regeneration of resin for purifying citrus fruit juice |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61254166A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6437073A (en) * | 1987-08-03 | 1989-02-07 | Sony Corp | Printed board |
JPH04115758U (en) * | 1991-03-25 | 1992-10-14 | 富士通株式会社 | Circuit board grounding structure |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5141611A (en) * | 1985-05-16 | 1992-08-25 | Memtec Limited | Removing and recovering plant polyphenols |
US5368832A (en) * | 1991-06-07 | 1994-11-29 | Occidental Chemical Corporation | Zero discharge process for manufacturing of phosphorous acid and hypophosphorous acid |
-
1985
- 1985-05-01 JP JP60094201A patent/JPS61254166A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6437073A (en) * | 1987-08-03 | 1989-02-07 | Sony Corp | Printed board |
JPH04115758U (en) * | 1991-03-25 | 1992-10-14 | 富士通株式会社 | Circuit board grounding structure |
Also Published As
Publication number | Publication date |
---|---|
JPS61254166A (en) | 1986-11-11 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |