JP2000033250A - Method and apparatus for producing salts-containing water - Google Patents
Method and apparatus for producing salts-containing waterInfo
- Publication number
- JP2000033250A JP2000033250A JP10199965A JP19996598A JP2000033250A JP 2000033250 A JP2000033250 A JP 2000033250A JP 10199965 A JP10199965 A JP 10199965A JP 19996598 A JP19996598 A JP 19996598A JP 2000033250 A JP2000033250 A JP 2000033250A
- Authority
- JP
- Japan
- Prior art keywords
- water
- salt
- concentration
- pure water
- containing water
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 275
- 150000003839 salts Chemical class 0.000 title claims abstract description 136
- 238000000034 method Methods 0.000 title claims description 4
- 238000002156 mixing Methods 0.000 claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 claims description 26
- 238000001914 filtration Methods 0.000 claims description 10
- 239000003651 drinking water Substances 0.000 claims description 3
- 235000020188 drinking water Nutrition 0.000 claims description 3
- 238000003860 storage Methods 0.000 abstract description 16
- 238000002360 preparation method Methods 0.000 abstract description 15
- 239000000706 filtrate Substances 0.000 abstract description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 10
- 150000002500 ions Chemical class 0.000 description 10
- 235000013361 beverage Nutrition 0.000 description 7
- 238000001514 detection method Methods 0.000 description 5
- 239000012528 membrane Substances 0.000 description 4
- 238000005374 membrane filtration Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000011033 desalting Methods 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 241001122767 Theaceae Species 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 235000016213 coffee Nutrition 0.000 description 1
- 235000013353 coffee beverage Nutrition 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000013616 tea Nutrition 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/05—Conductivity or salinity
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/043—Treatment of partial or bypass streams
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
- Accessories For Mixers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、通常の濾過水より
も低い塩類濃度の塩類含有水を製造する装置および方法
に関し、とくに目標濃度の塩類含有水を自動調製可能な
塩類含有水の製造装置および製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for producing salt-containing water having a salt concentration lower than that of ordinary filtered water, and particularly to an apparatus for producing salt-containing water capable of automatically preparing a target concentration of salt-containing water. And a manufacturing method.
【0002】[0002]
【従来の技術】たとえば炭酸飲料やコーヒー、紅茶、あ
るいはジュース等の各種飲料製造分野においては、飲料
製造用の水として、濾過水、たとえば市水を膜濾過装置
や活性炭フィルタ等を用いて濾過した水や、純水製造装
置によって製造した純水を用いることが多い。このうち
濾過水では、濾過により懸濁物質等の不純物は除去され
るものの、塩類(たとえば、陽イオン成分としてのナト
リウムイオンやカルシウムイオン、マグネシウムイオン
等、陰イオン成分としての塩化物イオンや硫化物イオン
等)の濃度は濾過前の原水と略同じであり、純水では、
通常イオン交換体や逆浸透膜等の脱塩手段で塩類が除去
されるので、極めて低い塩類濃度となっている。2. Description of the Related Art In the field of producing various beverages such as carbonated beverages, coffee, tea, and juices, filtered water, for example, city water, is filtered as a water for producing beverages using a membrane filtration device or an activated carbon filter. Water or pure water produced by a pure water producing apparatus is often used. In the filtered water, although impurities such as suspended substances are removed by filtration, salts (for example, sodium ions, calcium ions, magnesium ions, etc. as cation components, chloride ions and sulfides as anion components, etc.) Ion etc.) concentration is almost the same as raw water before filtration.
Usually, salts are removed by a desalting means such as an ion exchanger or a reverse osmosis membrane, so that the salt concentration is extremely low.
【0003】ところが最近、製造すべき飲料によって
は、原水の含有イオンのバランスを略そのまま保ちつ
つ、全体として低塩類濃度とした(つまり、濾過水の塩
類濃度よりは低いが純水の塩類濃度よりは高い)低塩類
含有水が、製造される飲料の味や風味に微妙に望ましい
影響力をもつことが判り始め、ビーカースケールでのテ
ストが試み始められている。ビーカースケールでのテス
トでは、濾過水と純水との割合を変えて両者を混合する
ことにより、各種低塩類含有水を調製することはできる
が、工業的な規模でこのような要求を満たすことのでき
る装置は、未だ見当たらない。However, recently, depending on the beverage to be produced, the salt concentration of raw water is kept low while maintaining the balance of the ions contained in the raw water substantially (that is, the salt concentration is lower than that of filtered water but lower than that of pure water). It has been found that water with a low salt content has a subtly desirable effect on the taste and flavor of the beverages produced, and testing on a beaker scale has begun. In tests at the beaker scale, various low-salt content waters can be prepared by changing the ratio of filtered water and pure water and mixing both, but satisfying such requirements on an industrial scale There is no device that can do this.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上記のよう
な最近の新しい要求に応えるべく鋭意検討した結果完成
に至ったものである。SUMMARY OF THE INVENTION The present invention has been completed as a result of intensive studies to meet the recent new demands as described above.
【0005】すなわち、単に濾過水と純水を手動で混合
する低塩類含有水の製造では、手間がかかるとともに、
製造量にも限界があり、工業的な規模での利用は困難で
ある。また、目標濃度の塩類含有水の自動調製も困難で
ある。That is, the production of low-salt content water in which pure water is simply mixed with filtered water is time-consuming,
The production volume is limited, and it is difficult to use it on an industrial scale. In addition, it is difficult to automatically prepare salt-containing water having a target concentration.
【0006】また、純水製造装置によって製造した純水
にNaCl等の塩類を添加して所望濃度の塩類含有水を
製造することも考えられるが、一旦純水製造装置で塩類
を取り除いた後に塩類を加えるというシステム上の無駄
があるとともに、原水がもっていたイオンバランスが崩
れてしまい飲料用水としての望ましいイオンバランスを
達成できなくなるおそれがある。つまり、原水の成分を
略そのまま残して塩類濃度のみ低くしたいという要求に
応えることができない。It is also conceivable to add salts such as NaCl to pure water produced by a pure water producing apparatus to produce salt-containing water at a desired concentration. However, once the salts are removed by a pure water producing apparatus, the salt is removed. In addition to the waste in the system of adding water, there is a possibility that the ion balance of the raw water may be lost and the desired ion balance as drinking water may not be achieved. That is, it is not possible to meet the demand for lowering only the salt concentration while leaving the raw water component substantially as it is.
【0007】そこで本発明の課題は、前述の如き低塩類
含有水の新しい要求に応えるべく、原水の望ましいイオ
ン成分のバランスを残しつつ、塩類濃度のみを目標とす
る低い濃度に調整可能な塩類含有水の製造装置および製
造方法を提供することにある。[0007] Accordingly, an object of the present invention is to meet the above-mentioned new requirements for low-salt content water, while maintaining a desirable balance of ionic components in the raw water and adjusting the salt content to a target low concentration only for the salt concentration. An object of the present invention is to provide an apparatus and a method for producing water.
【0008】また本発明の課題は、併せて、所望の低塩
類含有水を容易に自動調製できる塩類含有水の製造装置
および製造方法を提供することにある。Another object of the present invention is to provide an apparatus and a method for producing salt-containing water that can easily and automatically prepare desired low salt-containing water.
【0009】[0009]
【課題を解決するための手段】上記課題を解決するため
に、本発明の塩類含有水の製造装置は、濾過水製造装置
からの濾過水と純水製造装置からの純水とを混合して目
標濃度の塩類含有水を調製する手段を有することを特徴
とするものからなる。In order to solve the above-mentioned problems, an apparatus for producing salt-containing water according to the present invention mixes filtered water from a filtered water producing apparatus and pure water from a pure water producing apparatus. It is characterized by having means for preparing salt-containing water at a target concentration.
【0010】ここで、上記濾過水と純水は、同じ原水か
ら製造してもよく、異なる原水から製造してもよい。同
じ原水から製造する場合には、たとえば、純水製造用の
原水として、濾過水を使用するシステムとしてもよい。Here, the filtered water and the pure water may be produced from the same raw water or different raw waters. When producing from the same raw water, for example, a system using filtered water may be used as raw water for producing pure water.
【0011】上記濾過水製造装置としてはとくに限定さ
れるものではないが、たとえば砂濾過装置や活性炭濾過
装置、あるいは精密濾過膜(MF)や限外濾過膜(U
F)等の膜を用いた膜濾過装置を挙げることができ、ま
た、上記純水製造装置としては、たとえばイオン交換樹
脂や逆浸透膜等の脱塩手段を用いた公知の純水製造装置
を挙げることができる。The filtration water producing apparatus is not particularly limited. For example, a sand filtration apparatus or an activated carbon filtration apparatus, or a microfiltration membrane (MF) or an ultrafiltration membrane (U
Examples of the pure water production apparatus include a known pure water production apparatus using a desalting unit such as an ion exchange resin or a reverse osmosis membrane. Can be mentioned.
【0012】上記塩類含有水の調製手段には、濾過水と
純水との混合水の塩類の濃度を実質的に検知可能な手段
が設けられていることが好ましく、該検知手段からの情
報が、濾過水供給系および純水供給系の少なくとも一方
にフィードバックされていることが好ましい。また、濾
過水供給系にも、同時に濾過水の塩類の濃度を実質的に
検知可能な手段が設けられていることが好ましい。この
ような検知手段からの情報をフィードバックすることに
より、目標塩類濃度の混合水を調製するに際し、容易に
自動化することが可能になる。Preferably, the means for preparing salt-containing water is provided with means capable of substantially detecting the concentration of salts in the mixed water of filtered water and pure water, and information from the detecting means is provided. It is preferable that feedback is provided to at least one of the filtered water supply system and the pure water supply system. Further, it is preferable that the filtrate water supply system is also provided with means capable of substantially detecting the concentration of salts of the filtrate water at the same time. By feeding back information from such a detecting means, it becomes possible to easily automate the preparation of the mixed water having the target salt concentration.
【0013】塩類の濃度は、各種のイオンが含まれてい
るため直接的に測定することは難しいが、塩類濃度と電
気伝導度とはある濃度範囲で略一対一に対応することが
知られているから、上記実質的に塩類濃度を検知する手
段として、電気伝導度検知手段を用いることができる。Although it is difficult to measure the salt concentration directly because it contains various ions, it is known that the salt concentration and the electric conductivity correspond substantially one to one in a certain concentration range. Therefore, an electric conductivity detecting means can be used as the means for detecting the salt concentration substantially.
【0014】また、塩類含有水の調製手段としては、バ
ッチ式、連続式のいずれのシステムにも構成可能であ
る。バッチ式の場合には、濾過水と純水とのバッチ式混
合槽を設ければよく、連続式の場合には、ライン構成と
して、濾過水と純水との連続式混合系を形成すればよ
い。The means for preparing the salt-containing water can be constituted by either a batch system or a continuous system. In the case of a batch type, a batch type mixing tank of filtered water and pure water may be provided.In the case of a continuous type, a continuous mixing system of filtered water and pure water may be formed as a line configuration. Good.
【0015】このような塩類含有水の製造装置は、とく
に飲料用の水として、目標濃度の塩類含有水を工業的に
製造する場合に用いて好適なものである。Such an apparatus for producing salt-containing water is suitable for use in industrial production of salt-containing water having a target concentration, particularly as drinking water.
【0016】本発明に係る塩類含有水の製造方法は、濾
過水製造装置により濾過水を製造し、純水製造装置によ
り純水を製造し、濾過水と純水を所定の割合で混合して
濾過水の塩類濃度と純水の塩類濃度の中間の目標塩類濃
度の塩類含有水を調製することを特徴とする方法からな
る。In the method for producing salt-containing water according to the present invention, filtered water is produced by a filtered water producing device, pure water is produced by a pure water producing device, and the filtered water and pure water are mixed at a predetermined ratio. The method comprises preparing salt-containing water having a target salt concentration intermediate between the salt concentration of filtered water and the salt concentration of pure water.
【0017】このような本発明に係る塩類含有水の製造
装置および製造方法においては、濾過水と純水とを混合
して所望塩類濃度の塩類含有水を製造するので、とくに
濾過水が有する元の原水の成分バランスやイオンバラン
スが実質的にそのまま活かされ、混合水にあっては実質
的に塩類濃度のみが目標とする濃度まで低減されること
になる。したがって、飲料用等に要求される望ましいイ
オンバランスが残されたまま、目標濃度の塩類含有水が
容易に製造される。In the apparatus and method for producing salt-containing water according to the present invention, since filtered water and pure water are mixed to produce salt-containing water having a desired salt concentration, the source of the filtered water is particularly high. The component balance and ion balance of the raw water are utilized substantially as it is, and in the mixed water, substantially only the salt concentration is reduced to the target concentration. Therefore, the desired concentration of salt-containing water can be easily produced while the desired ion balance required for beverages and the like is left.
【0018】また、電気伝導度等の検知により混合水、
さらには混合すべき濾過水の塩類濃度を検知し、濾過水
と純水との混合割合を制御できるようにすれば、目標濃
度の塩類含有水を自動的に、かつ濃度のばらつきを小さ
くして精度よく調製できるようになり、工業的に容易に
利用できるようになる。Further, by detecting electric conductivity or the like, mixed water,
Furthermore, if the salt concentration of the filtered water to be mixed is detected and the mixing ratio between the filtered water and the pure water can be controlled, the salt-containing water at the target concentration is automatically reduced and the variation in the concentration is reduced. It can be prepared with high precision and can be easily used industrially.
【0019】[0019]
【発明の実施の形態】以下に、本発明の望ましい実施の
形態を図面を参照して説明する。図1は、本発明の一実
施態様に係る塩類含有水の製造装置および製造方法の基
本構成を示している。図1において、1は塩類含有水の
製造装置全体を示しており、たとえば市水を用いた原水
が濾過水製造装置2によって処理されて濾過水とされ、
該濾過水が濾過水貯槽3に一旦蓄えられる。また、濾過
水の一部は純水製造装置4に供給され、純水が製造され
て純水貯槽5に一旦蓄えられる。純水製造装置4には、
たとえば、陽イオン交換樹脂と陰イオン交換樹脂とを用
いた混床式の純水製造装置が用いられる。純水製造装置
4の原水としては、上記のように濾過水を用いる他、市
水等を直接用いてもよい。Preferred embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows a basic configuration of an apparatus and a method for producing salt-containing water according to an embodiment of the present invention. In FIG. 1, reference numeral 1 denotes an entire apparatus for producing salt-containing water.
The filtered water is temporarily stored in the filtered water storage tank 3. Further, a part of the filtered water is supplied to the pure water producing device 4, where pure water is produced and temporarily stored in the pure water storage tank 5. The pure water production device 4 includes:
For example, a mixed bed type pure water production apparatus using a cation exchange resin and an anion exchange resin is used. As the raw water of the pure water production apparatus 4, in addition to using the filtered water as described above, city water or the like may be directly used.
【0020】濾過水貯槽3からの濾過水と、純水貯槽5
からの純水とが、塩類含有水調製手段6により所定の割
合で混合され、塩類の濃度が目標濃度に調整された低塩
類含有水が調製される。The filtered water from the filtered water storage tank 3 and the pure water storage tank 5
Is mixed at a predetermined ratio by the salt-containing water preparing means 6 to prepare low salt-containing water in which the salt concentration is adjusted to the target concentration.
【0021】塩類濃度の制御には、たとえば電気伝導度
(電気伝導率とも言う。)の検出を利用できる。すなわ
ち、水中に溶存している塩類の濃度と電気伝導度との間
には、ある濃度範囲内において比例関係があることが知
られている。したがって、調製すべき塩類含有水の塩類
濃度の目標値、つまり電気伝導度の目標値が設定されれ
ば、調製に使用する濾過水の電気伝導度と、純水の電気
伝導度とから、両者をいかなる比率で混合すればよいか
が計算できる。たとえば濾過水の電気伝導度が240μ
S/cm、純水のそれが1μS/cm、である場合、こ
れらを等量混合すると、(240+1)/2≒120μ
S/cmの水が得られ、濾過水に対し約半分の塩類濃度
の低塩類含有水が得られることになる。本発明において
は、塩類含有水の調製に際して、この電気伝導度の検
出、およびその検出値に基づいたフィードバック制御を
極めて有効に活用できる。For controlling the salt concentration, for example, detection of electric conductivity (also referred to as electric conductivity) can be used. That is, it is known that there is a proportional relationship between the concentration of salts dissolved in water and the electric conductivity within a certain concentration range. Therefore, if the target value of the salt concentration of the salt-containing water to be prepared, that is, the target value of the electric conductivity is set, the electric conductivity of the filtered water used for the preparation and the electric conductivity of the pure water are used. Can be calculated in what ratio should be mixed. For example, the electrical conductivity of the filtered water is 240μ
If S / cm and that of pure water are 1 μS / cm, when they are mixed in equal amounts, (240 + 1) / 2 ≒ 120 μ
S / cm of water is obtained, and low salt-containing water having a salt concentration about half that of the filtered water is obtained. In the present invention, the detection of the electric conductivity and the feedback control based on the detected value can be utilized very effectively when preparing the salt-containing water.
【0022】図2は、塩類含有水をバッチ式で調製する
場合のより具体的な態様を示している。図2に示す塩類
含有水の製造装置においては、市水等からなる原水が、
膜濾過装置11、活性炭フィルタ12からなる濾過水製
造装置13によって濾過され、濾過水が生成される。生
成された濾過水は、一旦濾過水貯槽14に蓄えられる。
また、生成された濾過水の一部は、混床式等の純水製造
装置15に送られ、イオン交換処理により純水が生成さ
れる。生成された純水は、一旦純水貯槽16に蓄えられ
る。FIG. 2 shows a more specific embodiment in which salt-containing water is prepared in a batch system. In the apparatus for producing salt-containing water shown in FIG.
Filtration is performed by a filtration water production device 13 including a membrane filtration device 11 and an activated carbon filter 12 to generate filtered water. The generated filtered water is temporarily stored in the filtered water storage tank 14.
In addition, a part of the generated filtered water is sent to a mixed-bed type pure water producing apparatus 15 or the like, and pure water is generated by an ion exchange treatment. The generated pure water is temporarily stored in the pure water storage tank 16.
【0023】濾過水貯槽14からの濾過水と、純水貯槽
16からの純水が所定割合でバッチ式混合槽からなる塩
類含有水調製槽17で混合され、所定塩類濃度の塩類含
有水に調製される。このときの濃度調整の制御には各種
方式を用いることができるが、以下にその一例を示す。The filtered water from the filtered water storage tank 14 and the pure water from the pure water storage tank 16 are mixed at a predetermined ratio in a salt-containing water preparation tank 17 composed of a batch type mixing tank to prepare salt-containing water having a predetermined salt concentration. Is done. Various methods can be used for controlling the density adjustment at this time, examples of which are described below.
【0024】本実施態様では、まず、純水貯槽16か
ら、予め定められた一定量の純水が塩類含有水調製槽1
7に供給される。このとき、純水の供給量は液面計18
で制御され、正確に所定の一定量の純水が供給される。
なお、19は塩類含有水調製槽に付設されたエアフィル
タを示している。In this embodiment, first, a predetermined fixed amount of pure water is supplied from the pure water storage tank 16 to the salt-containing water preparation tank 1.
7 is supplied. At this time, the supply amount of pure water is
, And a predetermined fixed amount of pure water is supplied accurately.
Reference numeral 19 denotes an air filter attached to the salt-containing water preparation tank.
【0025】次いで、付設のポンプ20を駆動して調製
槽17内の水を循環ライン21および29を介して循環
させ、純水供給前に調製槽17内および循環ライン21
および29内に残留していた前回の調製水と新たに供給
された純水とがよく混合され、この混合水の電気伝導度
が、循環ライン21に設けられた電気伝導率計22(C
I)によって検知される。Next, the water in the preparation tank 17 is circulated through the circulation lines 21 and 29 by driving the attached pump 20, and before the pure water is supplied, the water in the preparation tank 17 and the circulation line 21 are circulated.
And the newly prepared water remaining in the pipe 29 and the newly supplied pure water are mixed well, and the electric conductivity of the mixed water is measured by the electric conductivity meter 22 (C) provided in the circulation line 21.
I).
【0026】一方、濾過水貯槽14内の濾過水は、ポン
プ23によって循環ライン24を介して循環され、循環
ラインに付設された電気伝導率計25(CI)により濾
過水の電気伝導度が検知、測定される。この濾過水は、
ポンプ23によって所定量塩類含有水調製槽17に供給
されるが、この供給量が演算・制御装置26を用いて次
のように制御される。On the other hand, the filtered water in the filtered water storage tank 14 is circulated through a circulation line 24 by a pump 23, and the electric conductivity of the filtered water is detected by an electric conductivity meter 25 (CI) attached to the circulation line. Measured. This filtered water is
A predetermined amount is supplied to the salt-containing water preparation tank 17 by the pump 23, and the supply amount is controlled as follows using the arithmetic and control unit 26.
【0027】電気伝導率計22によって測定された、調
製槽17内に貯留された純水の電気伝導度の信号と、電
気伝導率計25によって測定された濾過水の電気伝導度
の信号が演算・制御装置26に送られ、これらの電気伝
導度と、予め把握されている塩類含有水調製槽17内の
純水量(循環ライン21および29中に存在する水量も
含む)とから、目標塩類濃度に調整するために混合すべ
き濾過水の量が演算される。この演算された量の濾過水
が供給されるよう、(積算)流量計27からの検出信号
が入力されながらポンプ23の駆動が制御される。The signal of the electric conductivity of the pure water stored in the preparation tank 17 measured by the electric conductivity meter 22 and the signal of the electric conductivity of the filtered water measured by the electric conductivity meter 25 are calculated. A target salt concentration based on the electric conductivity sent to the controller 26 and the amount of pure water in the salt-containing water preparation tank 17 (including the amount of water present in the circulation lines 21 and 29), which is grasped in advance; In order to adjust the amount of filtered water, the amount of filtered water to be mixed is calculated. The drive of the pump 23 is controlled while the detection signal from the (integrated) flow meter 27 is input so that the calculated amount of filtered water is supplied.
【0028】その結果、調製される塩類含有水が目標電
気伝導度となるように、濾過水と純水が所定の割合で精
度よく混合される。前述した如く電気伝導度と塩類の濃
度は比例関係にあるから、目標とする塩類濃度の塩類含
有水が精度よく調製される。As a result, filtered water and pure water are accurately mixed at a predetermined ratio so that the prepared salt-containing water has the target electric conductivity. As described above, since the electrical conductivity and the salt concentration are in a proportional relationship, the salt-containing water having the target salt concentration is accurately prepared.
【0029】調製された塩類含有水は、必要に応じて、
ポンプ20によりユースポイントへと供給される。本実
施態様では、この塩類含有水供給系に紫外線殺菌装置2
8が設けられているが、このような付設機器は要求に応
じて設ければよい。また本実施態様では、常時少量づつ
循環させて菌の繁殖を防止できるように循環ライン29
が設けられている。The prepared salt-containing water may be used, if necessary,
It is supplied to the point of use by the pump 20. In this embodiment, an ultraviolet sterilizer 2 is installed in this salt-containing water supply system.
8 are provided, but such attached devices may be provided as required. Further, in this embodiment, the circulation line 29 is circulated so as to always circulate in small amounts to prevent the growth of bacteria.
Is provided.
【0030】上記のような塩類含有水の製造装置および
製造方法においては、濾過水と純水を混合して目標とす
る塩類濃度の低塩類含有水を調製するので、濾過水が有
する元の原水の成分バランスやイオンバランスが実質的
にそのまま残され、飲料用等にとって望ましいイオンバ
ランスを有する水が製造される。In the above-described apparatus and method for producing salt-containing water, since filtered water and pure water are mixed to prepare low salt-containing water having a target salt concentration, the original raw water contained in the filtered water is removed. Is substantially left as it is, and water having an ion balance desirable for beverages and the like is produced.
【0031】したがって、たとえば純水を用い、該純水
に塩類を添加して所望塩類濃度の塩類含有水を調製する
場合に比べ、原水や濾過水が有するイオンバランスを実
質的にそのまま残すことができ、飲料用等に望ましい塩
類含有水が容易に調製される。また、純水のみから塩類
含有水を製造する場合には、塩類を一旦除去してから再
度塩類を加えるというシステム上の無駄があるが、本発
明ではこのような無駄は全くなく、塩類含有水製造コス
トの低減をはかることもできる。Therefore, as compared with a case where pure water is used and salts are added to the pure water to prepare salt-containing water having a desired salt concentration, the ion balance of the raw water or the filtered water can be substantially left as it is. It is possible to easily prepare salt-containing water which is desirable for drinking and the like. Further, when producing salt-containing water from pure water alone, there is a waste in the system of removing the salt once and then adding the salt again. In the present invention, there is no such waste, and the salt-containing water is not present. Manufacturing costs can also be reduced.
【0032】また、塩類の濃度調整に電気伝導度の検知
を利用することにより、各種の塩類が含まれている場合
にあっても、電気伝導度という一つの指標に基づいて制
御することが可能になり、精度の良い濃度制御を容易に
行うことができる。さらに、演算・制御装置26を用い
て濾過水と純水との混合割合を演算、制御することによ
り、自動化も容易に達成でき、さらに濃度制御の向上を
はかることもできる。Further, by utilizing the detection of electric conductivity for adjusting the concentration of salts, even when various salts are contained, it is possible to control based on one index of electric conductivity. , And accurate density control can be easily performed. Furthermore, by calculating and controlling the mixing ratio of the filtered water and the pure water using the calculation / control device 26, automation can be easily achieved, and the concentration control can be further improved.
【0033】ちなみに、図2に示した装置を用いて、上
記電気伝導度に基づいた混合、調製による濃度制御の精
度を確認するテストを行ったところ、次のような優れた
結果が得られた。By the way, using the apparatus shown in FIG. 2, a test was conducted to confirm the accuracy of the concentration control by mixing and preparation based on the above-mentioned electric conductivity, and the following excellent results were obtained. .
【0034】市水を膜濾過装置11、活性炭フィルタ1
2に通水して得られた、塩類を多く含んだ濾過水(電気
伝導度:200〜300μS/cm)と、その濾過水を
純水製造装置15に通水して得られた、塩類を殆ど含ま
ない純水(電気伝導度:1μS/cm程度)を各々貯留
しておき、塩類含有水調製槽17で、電気伝導度が各目
標値(20μS/cmおよび2μS/cm)になるよう
に所定割合で混合して低塩類含有水を調製した結果、表
1に示すように、極めて精度よく目標塩類濃度に調整で
きた。The city water is passed through the membrane filtration device 11 and the activated carbon filter 1
2 and filtered water containing a large amount of salts (electric conductivity: 200 to 300 μS / cm), and the filtered water passed through a pure water production device 15 to obtain salts. Pure water (electric conductivity: about 1 μS / cm) containing almost no water is stored, and in the salt-containing water preparation tank 17, the electric conductivity becomes each target value (20 μS / cm and 2 μS / cm). As a result of preparing low-salt content water by mixing at a predetermined ratio, as shown in Table 1, it was possible to adjust the target salt concentration extremely accurately.
【0035】[0035]
【表1】 [Table 1]
【0036】上記実施態様では、バッチ式で塩類含有水
を調製する場合について説明したが、本発明においては
塩類含有水を連続式に調製することもできる。In the above embodiment, the case where the salt-containing water is prepared in a batch manner has been described. However, in the present invention, the salt-containing water can be prepared in a continuous manner.
【0037】たとえば図3に塩類含有水の製造装置の要
部を示すように、濾過水貯槽31の循環ライン32で前
記実施態様と同様電気伝導率計33で濾過水の電気伝導
度を検知し、その濾過水を流量制御弁34で流量制御し
ながらポンプ35で送給し、この濾過水と、純水貯槽3
6から流量制御弁37で流量制御しながらポンプ38で
送給する純水とを、混合ライン39中で直接混合し、混
合された低塩類含有水の塩類の濃度を電気伝導率計40
で検出する。電気伝導率計40で測定される塩類濃度が
目標値となるように、電気伝導率計33からの測定値を
用いて濾過水と純水との混合割合を演算・制御装置41
で演算し、その演算に基づいて流量制御弁34、あるい
は両流量制御弁34、37を制御する。For example, as shown in FIG. 3 showing the main part of the apparatus for producing salt-containing water, the electric conductivity of the filtered water is detected by the electric conductivity meter 33 in the circulation line 32 of the filtered water storage tank 31 as in the above embodiment. The filtered water is supplied by a pump 35 while controlling the flow rate of the filtered water by a flow control valve 34, and the filtered water is supplied to a pure water storage tank 3.
6 and pure water supplied by a pump 38 while controlling the flow rate by a flow control valve 37, are directly mixed in a mixing line 39, and the salt concentration of the mixed low salt content water is measured by an electric conductivity meter 40.
To detect. The calculating and controlling device 41 calculates the mixing ratio of the filtered water and the pure water using the measured value from the electric conductivity meter 33 so that the salt concentration measured by the electric conductivity meter 40 becomes the target value.
And the flow control valve 34 or both flow control valves 34 and 37 are controlled based on the calculation.
【0038】このような連続式の混合調製系に構成して
も、所望塩類濃度の塩類含有水が精度よく製造され、し
かも自動的にかつ連続的に製造される。Even with such a continuous mixing / preparing system, salt-containing water having a desired salt concentration is produced with high precision, and is produced automatically and continuously.
【0039】なお、純水側の電気伝導度は通常極めて低
い値であるため、図3に示したように塩類含有水調製後
の電気伝導度を測定するだけで十分に高い濃度制御が可
能であるが、さらに制御精度を高めるために、混合前の
純水の電気伝導度を測定し、その情報もフィードバック
するようにしてもよい。Since the electric conductivity on the pure water side is usually a very low value, a sufficiently high concentration control can be performed only by measuring the electric conductivity after preparing the salt-containing water as shown in FIG. However, in order to further increase the control accuracy, the electric conductivity of pure water before mixing may be measured, and the information may be fed back.
【0040】[0040]
【発明の効果】以上説明したように、本発明に係る塩類
含有水の製造装置および製造方法によれば、所望の塩類
濃度の塩類含有水を容易にかつ大量に製造することがで
き、飲料用等に使用する水として新しい要求に応えるこ
とのできる低塩類含有水を工業的規模で効率よくしかも
安価に製造できる。As described above, according to the apparatus and method for producing salt-containing water of the present invention, salt-containing water having a desired salt concentration can be produced easily and in large quantities, and can be used for beverages. Low salt content water which can meet new requirements can be efficiently and inexpensively produced on an industrial scale.
【0041】また、電気伝導度検知に基づいた制御を行
うことにより、所望の塩類含有水の製造を容易に自動化
できる。Further, by performing control based on the detection of electric conductivity, the production of desired salt-containing water can be easily automated.
【図1】本発明の塩類含有水の製造装置の基本構成例を
示す概略構成図である。FIG. 1 is a schematic configuration diagram showing a basic configuration example of an apparatus for producing salt-containing water of the present invention.
【図2】本発明の一実施態様に係る塩類含有水の製造装
置の概略機器系統図である。FIG. 2 is a schematic system diagram of an apparatus for producing salt-containing water according to an embodiment of the present invention.
【図3】本発明の別の実施態様に係る塩類含有水の製造
装置の要部の概略機器系統図である。FIG. 3 is a schematic system diagram of a main part of an apparatus for producing salt-containing water according to another embodiment of the present invention.
1 塩類含有水の製造装置 2、13 濾過水製造装置 3、14、31 濾過水貯槽 4、15 純水製造装置 5、16、36 純水貯槽 6 塩類含有水調製手段 11 膜濾過装置 12 活性炭フィルタ 17 塩類含有水調製槽 18 液面計 19 エアフィルタ 20、23、35、38 ポンプ 21、24、29、32 循環ライン 22、25、33、40 電気伝導率計 26、41 演算・制御装置 27 (積算)流量計 28 紫外線殺菌装置 34、37 流量制御弁 39 混合ライン DESCRIPTION OF SYMBOLS 1 Production apparatus of salt-containing water 2,13 Filtration water production apparatus 3,14,31 Filtration water storage tank 4,15 Pure water production apparatus 5,16,36 Pure water storage tank 6 Salt-containing water preparation means 11 Membrane filtration apparatus 12 Activated carbon filter 17 Salt-containing water preparation tank 18 Liquid level gauge 19 Air filter 20, 23, 35, 38 Pump 21, 24, 29, 32 Circulation line 22, 25, 33, 40 Electric conductivity meter 26, 41 Operation / control device 27 ( Integration) flow meter 28 UV sterilizer 34, 37 flow control valve 39 mixing line
Claims (9)
装置からの純水とを混合して目標濃度の塩類含有水を調
製する手段を有することを特徴とする塩類含有水の製造
装置。An apparatus for producing salt-containing water, comprising means for mixing filtered water from a filtered water producing apparatus with pure water from a pure water producing apparatus to prepare salt-containing water having a target concentration. .
れたものである、請求項1の塩類含有水の製造装置。2. The apparatus for producing salt-containing water according to claim 1, wherein said filtered water and pure water are produced from the same raw water.
純水との混合水の塩類の濃度を実質的に検知可能な手段
が設けられ、該検知手段からの情報が、濾過水供給系お
よび純水供給系の少なくとも一方にフィードバックされ
ている、請求項1または2の塩類含有水の製造装置。3. The means for preparing salt-containing water is provided with means capable of substantially detecting the concentration of salts in a mixed water of filtered water and pure water, and the information from the detecting means is used to supply filtered water. The apparatus for producing salt-containing water according to claim 1 or 2, wherein the apparatus is fed back to at least one of the system and the pure water supply system.
を実質的に検知可能な手段が設けられている、請求項3
の塩類含有水の製造装置。4. The filtered water supply system is also provided with means capable of substantially detecting the concentration of salts of the filtered water.
For producing salt-containing water.
電気伝導度を検知する手段からなる、請求項3または4
の塩類含有水の製造装置。5. The method according to claim 3, wherein the means capable of substantially detecting the concentration of salts comprises a means for detecting electric conductivity.
For producing salt-containing water.
純水とのバッチ式混合槽を有する、請求項1ないし5の
いずれかに記載の塩類含有水の製造装置。6. The apparatus for producing salt-containing water according to claim 1, wherein said means for preparing salt-containing water has a batch type mixing tank of filtered water and pure water.
純水との連続式混合系を有する、請求項1ないし5のい
ずれかに記載の塩類含有水の製造装置。7. The apparatus for producing salt-containing water according to claim 1, wherein said means for preparing salt-containing water has a continuous mixing system of filtered water and pure water.
る、請求項1ないし7のいずれかに記載の塩類含有水の
製造装置。8. The apparatus for producing salt-containing water according to claim 1, wherein the target concentration of salt-containing water is drinking water.
純水製造装置により純水を製造し、濾過水と純水を所定
の割合で混合して濾過水の塩類濃度と純水の塩類濃度の
中間の目標塩類濃度の塩類含有水を調製することを特徴
とする、塩類含有水の製造方法。9. Filtration water is produced by a filtration water production device,
Pure water is produced by a pure water production apparatus, and filtered water and pure water are mixed at a predetermined ratio to prepare salt-containing water having a target salt concentration intermediate between the salt concentration of the filtered water and the salt concentration of the pure water. A method for producing salt-containing water.
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JP2002153867A (en) * | 2000-11-16 | 2002-05-28 | Kurita Water Ind Ltd | Producing apparatus for resistivity controlled water, and apparus for producing water for inspection of can |
JP2011078914A (en) * | 2009-10-07 | 2011-04-21 | Nano Science:Kk | Method of manufacturing water for living body containing stabilized ozone-nanobubble nucleus and water for living body |
WO2015090366A1 (en) * | 2013-12-17 | 2015-06-25 | Judo Wasseraufbereitung Gmbh | Blending control method with determination of untreated water hardness via the conductivity of the soft water and blended water |
CN105829249A (en) * | 2013-12-17 | 2016-08-03 | 居道水再生有限公司 | Blending control method with determination of untreated water hardness via the conductivity of the soft water and blended water |
RU2643554C2 (en) * | 2013-12-17 | 2018-02-02 | Юдо Вассерауфберайтунг Гмбх | Dilution regulation with determination of raw water rigidity in conductivity of soft and mixed water |
AU2013407918B2 (en) * | 2013-12-17 | 2018-04-12 | Judo Wasseraufbereitung Gmbh | Blending control method with determination of untreated water hardness via the conductivity of the soft water and blended water |
US10577260B2 (en) | 2013-12-17 | 2020-03-03 | Judo Wasseraufereitung Gmbh | Blending control method with determination of untreated water hardness via the conductivity of the soft water and blended water |
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