KR20080059860A - A production method of drinking water from a mineral water - Google Patents

A production method of drinking water from a mineral water Download PDF

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KR20080059860A
KR20080059860A KR1020060133706A KR20060133706A KR20080059860A KR 20080059860 A KR20080059860 A KR 20080059860A KR 1020060133706 A KR1020060133706 A KR 1020060133706A KR 20060133706 A KR20060133706 A KR 20060133706A KR 20080059860 A KR20080059860 A KR 20080059860A
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water
sterilization
filtration
sending
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KR100863896B1 (en
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서희동
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/38Other non-alcoholic beverages
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/70Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
    • A23L2/72Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by filtration
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/70Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
    • A23L2/80Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by adsorption

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
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  • Polymers & Plastics (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

A method for preparing a beverage from mineral water is provided to produce a sanitarily-safe and healthful beverage from magnetized magnetite or anion-generating mine water. A method for preparing a beverage from mineral water comprises the steps of: (i) collecting mineral water from the underground base rock of a zone in which the FWHM(full width at half maximum) of 17O-NMR(nuclear magnetic resonance) is 90Hz or below, and sending the mineral water to a raw water storage tank; (ii) sending the water stored in the raw water storage tank to a sand filtration tower to remove SS, and sending the sand-filtered water to an activated carbon filtration process; (iii) sending the sand-filtered water to an activated carbon tower to remove organic matters, and then sending the water filtered through activated carbon to a microfiltration process; (iv) performing ultrafiltration or microfiltration to treat the water for its fouling index to be in a range of 2~4, and sending the microfiltered water to an electrolysis process; (v) electrolyzing the microfiltered water for its ORP(oxidation-reduction potential) value to be in a range of +200 to -200mV, sending the electrolyzed alkaline reduced water to an alkaline reduced water storage tank, and sending the water to a sterilization process by a transfer pump; (vi) sterilizing the electrolyzed water through one process selected from heat sterilization, UV sterilization, and high-pressure/high-frequency sterilization, and sending the sterilized water to a clean water storage tank; (vii) sending the water stored in the clean water storage tank to a container filling process, and filling a container such as a bottle with the clean water; and (viii) inspecting the water in the container, and packing.

Description

광천수로부터 음료수를 제조하는 방법{A production method of drinking water from a mineral water}A production method of drinking water from a mineral water}

도 1 은 광천수 생산공정도1 is a mineral water production process diagram

도 2는 전기분해공정도2 is an electrolysis process chart

〈도면의 주요부분에 대한 부호의 설명〉<Explanation of symbols for main parts of drawing>

1; 전기분해장치 2; 양극실One; Electrolysis device 2; Anode chamber

3; 음극실 4; 양극3; Cathode chamber 4; anode

5; 음극 6; 격막5; Cathode 6; Diaphragm

7; 정류기 8; 알칼리환원수 저장조7; Rectifier 8; Alkaline Reduced Water Storage Tank

9; 알칼리환원수 이송펌프9; Alkaline Reduced Water Transfer Pump

FI; 유량 지시계(Flow indicator) ⓢ; 솔레노이드밸브(Solenoid valve) FI; Flow indicator ⓢ; Solenoid Valve

pHI; pH 지시계(pH indicator)pHI; pH indicator

pHIS; 수소 이온농도지시제어기(pH indicating switch)pHIS; PH indicating switch

ORPI; 산화환원전위 지시계(Oxidation Reduction Potential indicator)ORPI; Oxidation Reduction Potential Indicator

ORPIS; 산화환원전위지시제어기(Oxidation reduction potential indicating switch)ORPIS; Oxidation reduction potential indicating switch

본 발명은 음료수를 제조하는 방법에 관한 것으로, 더욱 상세하게는 지하 암반으로부터 암반수를 취수하여 모래여과공정, 활성탄여과공정, 전기분해공정, 살균공정을 순차적으로 처리하여 음료수를 제조하는 방법에 관한 것이다.The present invention relates to a method for producing a beverage, and more particularly, to a method for producing a beverage by taking the rock water from the underground bedrock and sequentially treating the sand filtration process, activated carbon filtration process, electrolysis process, sterilization process. .

수돗물의 경우 핵자기공명 17O-NMR 반치폭(半値幅)의 값은 130∼150㎐ 범위인 데 반하여, 국내 포천시 관인면 고남산 자화된 자철광 광산의 광구에서 배출되는 암반수의 경우는 먹는 물 기준에 적합하면서 핵자기공명 17O-NMR 반치폭의 값이 90㎐ 전후로 물맛이 수돗물이나 일반 광천수에 비해서 월등히 우수한 특징이 있다.For tap water, the value of nuclear magnetic resonance 17 O-NMR half-width ranges from 130 to 150㎐, while the rock water discharged from the mining area of Gonamsan magnetized magnetite mine in Pocheon-myeon, Pocheon-si, Korea, meets the drinking water standard. Nuclear Magnetic Resonance 17 O-NMR half-width is around 90㎐ and water taste is much better than tap water or general mineral water.

물 분자는 상호 수소결합(水素結合)에 의해서 집단체(Cluster)를 형성하고 있으며, 이와 같은 물 분자의 집단수(集團數)의 측정은 핵자기공명(Nuclear magnetic resonance)17O-NMR 반치폭의 값으로 간접측정하는 데, 17O-NMR 반치폭의 값(㎐)의 1/10의 값이 물 분자의 집단수로 밝혀져 있다. 수돗물과 같이 17O-NMR 반치폭의 값이 130∼150㎐인 물의 집단수는 약 13∼15개의 물 분자가 집단을 이루고 있다.The water molecules form clusters by mutual hydrogen bonding, and the measurement of the number of these water molecules is carried out using the nuclear magnetic resonance 17 O-NMR half-width. Indirect measurement by value reveals that 1/10 of the value of the 17 O-NMR half-width is indicated by the number of populations of water molecules. Like tap water, about 13 to 15 molecules of water have a population of water with a value of 130-150 kPa of 17 O-NMR half width.

일반적으로 먹는 물은 수돗물이나 우물(Well)을 이용하고 있는 실정에 있으며, 수돗물의 경우는 유리염소, THM(Trihalomethanes)과 같은 인체에 유해한 물질이 함유되어 있는 문제점이 있으며, 우물의 경우는 세균 및 여러 유해물질이 오염 될 수 있는 문제점이 있다. In general, drinking water is in the situation of using tap water or wells, and in case of tap water, there is a problem in which harmful substances such as free chlorine and THM (Trihalomethanes) are contained, and in the case of wells, bacteria and There is a problem that various harmful substances can be contaminated.

또한, 이들 물의 대부분은 염소소독으로 산화환원전위(酸化還元電位; Oxidation-reduction potential, ORP) 값이 +500㎷ 이상 되는 산화성의 음료로 건강에 좋지 않은 문제점이 있다.In addition, most of these waters are chlorine disinfection, and the oxidation-reduction potential (ORP) value of +500 kPa or more is an oxidizing beverage having a problem that is not good for health.

물의 수소는 산화환원전위(ORP) 값은 -420㎷이며, 산소의 산화환원전위(ORP) 값은 +815㎷으로, 중간값인 +200㎷ 이하인 물을 환원수라 하며, +200㎷ 이상 되는 물을 산화수라 한다. The hydrogen has a redox potential (ORP) of -420 kW and the oxygen reduction potential (ORP) of oxygen is +815 kW, the water having a median of +200 kW or less is called reduced water. Is called oxidized water.

본 발명은 상기와 같은 문제점을 해소하기 위해 광천수를 취수하여 위생적으로 안전하면서 건강에 좋은 환원성 음료수를 제조하는 방법을 제공하는 데 본 발명의 목적이 있다.The present invention has an object of the present invention to provide a method for producing a reducing beverage that is hygienic and safe and healthy by taking mineral water in order to solve the above problems.

이와 같은 목적을 달성하기 위한 본 발명은, 자화된 자철광과 음이온을 발생하는 광산의 광구나 이들 지하 암반에서 광천수를 취수하는 공정, 모래여과공정, 활성탄여과공정, 정밀여과공정, 살균공정, 용기충전공정, 검사 및 포장공정으로 이루어진 것에 특징이 있다.In order to achieve the above object, the present invention provides a process for collecting mineral water from mines or magnetites that generate magnetized magnetite and anions, sand filtration process, activated carbon filtration process, precision filtration process, sterilization process, and container filling. It is characterized by a process, an inspection and a packaging process.

본 발명은, 지하 암반으로부터 광천수를 취수하는 공정, 모래여과공정, 활성탄여과공정, 정밀여과공정, 살균공정, 용기충전공정, 검사 및 포장공정이 순차적으로 이루어지는 음료수를 제조하는 방법으로, 이하 첨부된 도면에 의해 상세히 설명하면 다음과 같다.The present invention is a method for producing a beverage in which mineral water is taken from an underground rock, sand filtration, activated carbon filtration, precision filtration, sterilization, container filling, and inspection and packaging are sequentially performed. When described in detail by the drawings as follows.

1. 지하 암반으로부터 광천수를 취수하는 공정1. The process of taking mineral water from underground rock

본 발명에서 취수지역은, 자철광의 암반에서 핵자기공명(核磁氣共鳴; Nuclear magnetic resonance, NMR) 17O-NMR 반치폭의 값이 90㎐ 이하인 지역의 지하 암반으로부터 광천수(鑛泉水)를 취수하는 취수공의 굴착은 충적층 부위는 250∼300㎜φ구경의 외부 케이싱(Casing)을 설치한 후에 견고한 암반선 까지 더 굴착하여 200∼300㎜φ구경의 내부 케이싱을 확보하며, 이때 최초 지층 굴착구경은 최초 그라우팅(Grouting) 두께를 확보할 수 있도록 외부 케이싱 구경보다 최소한 100㎜φ이상 크게 굴착한다.In the intake zone in the present invention, intake of mineral water from the underground rock in an area where the value of the Nuclear magnetic resonance (NMR) 17 O-NMR half-width of the magnetite ore is 90 kPa or less. In the excavation of the ball, the alluvial layer is installed with an outer casing with a diameter of 250 to 300 mmφ, and then excavated to a solid rock line to secure an inner casing with a diameter of 200 to 300 mmφ. Excavate at least 100mmφ larger than outer casing bore to secure grouting thickness.

그라우팅은 상부구간 착정(鑿井) 종료 후에 상부로부터 오염된 물의 유입을 방지하기 위해서 케이싱과 착정경(鑿井徑) 사이의 공간에 착정경 저부(低部)에서부터 역 순환식 압력 시멘트 그라우팅을 하며, 이때 그라우팅은 주입제가 지표로 역류할 때까지 시행하며, 그라우팅 주입제는 벤토나이트가 2∼4Vol% 함유한 시멘트(Cement) 혼합물을 사용한다.Grouting is a reverse-circulating pressure cement grouting from the bottom of the lens top to the space between the casing and the lens to prevent the inflow of contaminated water from the top after the end of the upper section. In this case, grouting is performed until the injection back to the surface, and the grouting injection agent uses a cement mixture containing 2-4 vol% of bentonite.

취수정은 그라우팅이 완전히 고결된 후에 150∼250㎜φ범위의 구경으로 하부 대수층까지 굴착한 후에 공 내 TV-카메라 검증을 하여 그라우팅 시공상태, 케이싱 설치상태, 대수층 상태 등을 확인하여 이상이 없으면 수중모터펌프를 설치하고, 취수 량을 자동으로 측정할 수 있는 계측기 및 보호장치를 설치한다.After the grouting is completely solidified, excavate to the lower aquifer with a diameter of 150 ~ 250mmφ, and then verify the grouting construction, casing installation, aquifer, etc. Install a pump and install a meter and protection device that can automatically measure the amount of water intake.

그리고 취수정에는 감시정(監視井)과 연속 자동계측장치(원수의 수위, 전기 진도도, 온도, pH 등)를 설치한다.In addition, water wells are equipped with monitoring wells and continuous automatic measuring devices (water level, electrical intensity, temperature, pH, etc.).

취수정에서 취수된 물은 원수 저장조로 이송하며, 원수 저장조는 2개조 이상으로 하고, 밀폐된 뚜껑을 설치하고 살균장치와 에어 필터(Air filter)를 설치한다.The water collected from the intake well is transferred to the raw water storage tank, and the raw water storage tank is two or more tanks, and a sealed lid is installed and a sterilizer and an air filter are installed.

2. 모래여과공정2. Sand filtration process

원수 저장조에 저장된 물은 모래를 충전(充塡)한 여과 탑으로 보내어 수중의 고형물질(SS; Suspended solids)을 제거한다.The water stored in the raw water reservoir is sent to a sand-filled filtration tower to remove suspended solids (SS) from the water.

여과 탑에 충전된 모래는 유효경(Effective size)이 0.45∼0.7㎜, 균등계수(Uniformity coefficient)는 1.7 이하로 하고, 최대경은 2.0㎜를 넘지 못하게 하고, 최소경은 0.3㎜ 이하가 되지 않게 하며, 부득이한 경우에도 최대경을 초과하는 것과 최소경 이하인 것을 1% 이하가 되도록 한다.The sand packed in the filtration tower has an effective size of 0.45 to 0.7 mm, a uniformity coefficient of 1.7 or less, a maximum diameter of not more than 2.0 mm, and a minimum diameter of 0.3 mm or less. In this case, the maximum diameter and the minimum diameter are 1% or less.

여과 탑은 급속여과나 완속여과를 하며, 수중의 고형물질의 양에 따라서 둘 중에서 하나를 선택하며, 급속여과의 경우에는 여과속도를 120∼200m/일, 여층의 두께는 60∼70㎝로 설계하며, 급속여과의 경우에는 여과속도를 4∼5m/일, 여층의 두께는 70∼90㎝로 설계한다.The filtration tower performs either rapid filtration or slow filtration and selects one of the two depending on the amount of solids in the water.In the case of rapid filtration, the filtration speed is designed to be 120 ~ 200m / day and the thickness of the filtrate is 60 ~ 70㎝. In the case of rapid filtration, the filtration rate is 4-5 m / day and the thickness of the filtrate is 70-90 cm.

원수 중에 유기물의 농도가 CODMn의 값이 3㎎/ℓ이상 존재하는 경우에는 모래여과를 한 다음에 활성탄여과공정으로 보낸다.If the concentration of organic matter in raw water is more than 3mg / l of COD Mn , sand filtration is followed by activated carbon filtration.

그리고 원수 중에 유기물의 농도가 CODMn의 값이 3㎎/ℓ이하인 경우에는 모 래여과공정에서 수중의 고형물질을 제거한 다음에는 정밀여과공정으로 보낸다.And the concentration of the organic substance greater than the value of the COD Mn 3㎎ / ℓ in the raw water is followed by removal of the solid matter in the water in that sand filtration process are sent to the microfiltration step.

3. 활성탄여과공정3. Activated Carbon Filtration Process

원수 중에 유기물질의 성분이 존재하는 경우에는 모래여과에서 고형물질을 제거한 물을 활성탄여과공정의 활성탄 충전탑(充塡塔)으로 보내어 수중의 유기물질을 흡착 제거한 다음에 정밀여과공정으로 보낸다.If organic matter is present in the raw water, the water from which the solid matter is removed from sand filtration is sent to the activated carbon packed column of activated carbon filtration to remove the organic matter from the water and then sent to the microfiltration process.

활성탄 충전탑(充塡塔)은 선속도 4∼10m/시간으로 하고, 체류시간은 1시간 이상이 되도록 설계를 한다.The activated carbon packed column is designed to have a linear speed of 4 to 10 m / hour and a residence time of at least 1 hour.

4. 정밀여과공정4. Precision filtration process

정밀여과공정에서는 한외여과(Ultrafiltration)나 마이크로 여과(Micro-filtration) 중에서 한 종류를 선정하여 물의 FI(Fouling index)값을 2∼4 범위로 처리하여 전기분해공정으로 보낸다.In the microfiltration process, one type of ultrafiltration or micro-filtration is selected and the FI (Fouling index) value of water is treated in the range of 2 to 4 and sent to the electrolysis process.

그러나 원수의 산화환원전위(酸化還元電位; Oxidation-reduction potential, ORP)의 값이 +200㎷ 이하인 경우는 정밀여과된 물을 살균공정으로 보낸다.However, when the oxidation-reduction potential (ORP) value of raw water is less than + 200㎷, microfiltration water is sent to the sterilization process.

FI값은 대상 수중의 미세한 탁질농도를 나타내는 수치로 다음 ①식으로 표현된다.The FI value is a numerical value representing the fine turbidity concentration in the target water and is expressed by the following equation.

FI = (1-T0/T15)×100/15 …………………………①FI = (1-T 0 / T 15 ) x 100/15... … … … … … … … … … ①

여기서 T0는 0.45㎛의 정밀여과 막을 이용해 시료수를 0.2㎫로 가압 여과했 을 때에 최초의 500㎖의 시료수의 여과에 필요로 한 시간이며, T15는 T0와 동일한 상태에서 15분간 여과한 후에 500㎖의 시료수의 여과에 필요로 한 시간이다.Where T 0 is the time required for filtration of the first 500 mL of sample water when the sample water was filtered under pressure of 0.2 MPa using a 0.45 μm microfiltration membrane, and T 15 was filtered for 15 minutes in the same state as T 0. After that, it is time required for filtration of 500 ml of sample water.

5. 전기분해공정5. Electrolysis Process

정밀여과공정에서 여과된 여과 수를 양극실(2)과 음극실(3) 사이에 격막(6)으로 격리된 전기분해장치(1)의 음극실(3)로 공급하고, 양극실(2)로는 전해질로 3∼4wt%염수나 해수를 공급하고, 정류기(7)로부터 4∼20볼트(Volt)의 직류전기를 인가(印加)하여 음극실(3)의 산화환원전위(酸化還元電位, Oxidation-reduction potential, ORP) 값이 +200∼-200㎷ 범위가 되게 산화환원전위지시제어기(Oxidation reduction potential indicating switch, ORPIS)로 정류기(7)로부터 인가되는 전류를 조정하여 생산된 전해환원수인 알칼리환원수는 알칼리환원수 저장조(8)로 보내었다가, 알칼리환원수 이송펌프(9)에 의해서 살균공정으로 보낸다.The filtered water filtered in the microfiltration process is supplied to the cathode chamber 3 of the electrolysis device 1 separated by the diaphragm 6 between the anode chamber 2 and the cathode chamber 3, and the anode chamber 2 The furnace supplies 3 to 4 wt% brine or seawater to the electrolyte, and a redox potential of the cathode chamber 3 is applied by applying a DC electric current of 4 to 20 volts from the rectifier 7. Alkali-reduced water, an electrolytic reduced water produced by adjusting the current applied from the rectifier (7) with an oxidation reduction potential indicating switch (ORPIS) so that the value of -reduction potential (ORP) ranges from +200 to -200-. Is sent to the alkaline reduced water storage tank (8), and then sent to the sterilization process by the alkaline reduced water transfer pump (9).

양극실(2)에 공급하는 양극실 용수는 수소 이온농도지시제어기(pH indicating switch, pHIS)로 pH가 1.5∼3.0 범위가 되게 유입 측의 솔레노이드밸브(Solenoid valve, ⓢ)를 조정하면서 양극실 용수를 공급하며, 이때 산화환원전위지시계(Oxidation reduction potential indicator, ORPI)에 나타나는 산화환원전위 값은 +850∼+1,100㎷ 범위의 전해산화수가 생성된다.The anode chamber water supplied to the anode chamber 2 is a pH indicating switch (pHIS), and the anode chamber water is adjusted by adjusting the solenoid valve (ⓢ) at the inflow side so that the pH is in the range of 1.5 to 3.0. At this time, the redox potential value displayed on the oxidation reduction potential indicator (ORPI) generates electrolytic oxidation water in the range of +850 to +1,100 ㎷.

상술한 전기분해장치(1)에서 일어나는 전기화학반응의 메커니즘(Mechanism)은 다음과 같다.Mechanism of the electrochemical reaction occurring in the above-described electrolysis device 1 is as follows.

물은 전해질 용액에서 다음 ②의 반응식에서와 같이 해리한다.Water dissociates in electrolyte solution as in the following reaction ②.

H2O ↔ 2H+ + OH- …………………………………………………… ② H 2 O ↔ 2H + + OH - ... … … … … … … … … … … … … … … … … … … … ②

양극실(3)에서 반응Reaction in anode chamber 3

2OH- → H2O + [O] + 2e- → H2O + 1/2O2 (g)↑ + 2e- ………………③ 2OH - → H 2 O + [ O] + 2e - → H 2 O + 1 / 2O 2 (g) ↑ + 2e - ... … … … … … ③

2Cl- ( aq ) → Cl2 ( aq ) + 2e- → Cl2 (g)↑ + 2e …………………………④ 2Cl - (aq) → Cl 2 (aq) + 2e - → Cl 2 (g) ↑ + 2e ... … … … … … … … … … ④

양극실(3) 용액반응Anode Chamber (3) Solution Reaction

Cl2 ( aq ) + [O] → HClO( aq ) ………………………………………………⑤Cl 2 ( aq ) + [O]-&gt; HClO ( aq ) . … … … … … … … … … … … … … … … … … ⑤

여기서 [O]는 물에 용해되어 있는 활성산소 상태를 의미하며, O2 (g)↑는 가스상태로 대기 중으로 배출되는 상태의 산소를 의미한다.Here, [O] means active oxygen dissolved in water, and O 2 (g) ↑ means oxygen in a state of being discharged to the atmosphere in a gaseous state.

그리고 Cl2 ( aq )는 수중에 용해되어 있는 염소를 의미하며, Cl2 (g)↑는 가스상태로 대기 중으로 배출되는 상태의 염소를 의미한다.And Cl 2 ( aq ) refers to chlorine dissolved in water, and Cl 2 (g) ↑ refers to chlorine in a gaseous state.

음극실(2) 반응Cathode Chamber (2) Reaction

2H2O + 2e- → 2OH- + 2[H] → 2OH- + 2H2 (g)↑ ……………………⑥ 2H 2 O + 2e - → 2OH - + 2 [H] → 2OH - + 2H 2 (g) ↑ ... … … … … … … … ⑥

여기서 [H]는 수중에 용해되어 있는 활성수소 상태를 의미하며, H2 (g)↑는 가스상태로 대기 중으로 배출되는 상태의 수소를 의미한다.Here, [H] means active hydrogen dissolved in water, and H 2 (g) ↑ means hydrogen in a state of being discharged to the atmosphere.

전기분해장치(1)의 재질은 절연체인 아크릴수지(Acrylic resin), PP(Polypropylene), ABS(Acrylonitrile butadiene styrene copolymer), PE(Polyethylene), PVC(Polyvinylechloride), FRP(Fiber glass reinforced plastic), 베이클라이트(Bakelite), 에보나이트(Ebonite)나 강판이나 콘크리트 구조물에 FRP, 에폭시수지(Epoxy resin), 고무를 코팅(Coating) 또는 라이닝(Lining) 한 것을 사용한다.The material of the electrolysis device 1 is acrylic resin, polypropylene (PP), acrylonitrile butadiene styrene copolymer (PE), polyethylene (PE), polyvinylechloride (PVC), fiber glass reinforced plastic (FRP), and bakelite. (Bakelite), Ebonite or FRP, Epoxy resin, rubber coated or lining on steel or concrete structures.

양극실(2)에 설치된 양극(4)은 내식성(耐蝕性) 재질이면서 산소와 염소발생 과전압(Overvoltage)이 높은 티타늄 판(Titanium plate)에 TiO2-RuO2-SnO2를 소부 코딩한 DSA(Dimensionally stable anode)전극을 사용하며, 음극(5)은 수소발생 과전압이 높은 강판(鋼板)에 레이니 니켈(Raney nickel)을 코팅 또는 라이닝 한 전극을 사용한다.An anode chamber (2), the anode (4) is installed in a corrosion resistance (耐蝕性) material while oxygen and chlorine overvoltage occurs (Overvoltage) high plate titanium (Titanium plate) 2, TiO 2 -SnO 2 -RuO seizures coding to DSA ( A dimensionally stable anode electrode is used, and the cathode 5 uses an electrode coated or lined with Raney nickel on a steel sheet having high hydrogen generating overvoltage.

격막(6)은 직포(織布), 부직포(不織布), 폴리프로필렌, 폴리에틸렌, 폴리오레핀(polyolefin), 퍼플루오로술폰산(Perfluorosulfonic acid)계 수지 등에서 한 종류를 사용하며, 물리적인 공극(空隙) 또는 공공(空孔)을 갖추고 있으면서 전하를 투과시켜 이동시킬 수 있는 기능을 갖추고 있는 것으로서 고체 전해질 막과 같이 전하를 투과시켜 이동시킬 수 있는 기능을 갖추고 있는 것이 이용된다.The diaphragm 6 uses one kind of woven fabric, nonwoven fabric, polypropylene, polyethylene, polyolefin, and perfluorosulfonic acid resin, and has a physical void. Alternatively, one having a void and having a function capable of transmitting and transporting charges is used as a solid electrolyte membrane and has a function capable of transmitting and transporting charges.

6. 살균공정6. Sterilization Process

살균처리방법은 가온 살균, 자외선살균, 고전압고주파살균처리 중에서 한 종류를 적용하며, 살균공정은 2개 라인(Line) 이상으로 한다.The sterilization method is one of heating sterilization, ultraviolet sterilization and high voltage high frequency sterilization treatment. The sterilization process is two lines or more.

살균처리된 물은 정수 저장조로 보내며, 정수 저장조는 밀폐된 구조로 하며, 공기유통이 필요한 경우에는 에어 필터(Air filter) 및 살균설비를 설치한다.The sterilized water is sent to a purified water storage tank, and the purified water storage tank is sealed. If air circulation is required, an air filter and a sterilization facility are installed.

7. 용기충전공정7. Container Filling Process

정수 저장조에 저장된 물은 용기 충전공정으로 보내어 병과 같은 용기에 충전한다.The water stored in the purified water storage tank is sent to a container filling process and filled in a container such as a bottle.

용기 충전공정의 충전실(充塡室)은 청정실(Clean room)로 하며, 자외선공기살균설비를 설치한다.The filling room of the container filling process is a clean room, and an ultraviolet air sterilization facility is installed.

7. 검사 및 포장공정7. Inspection and Packaging Process

용기에 충전된 물은 검사한 후에 포장하여 음료수를 제조한다.The water filled in the container is inspected and then packaged to produce a beverage.

검사실은 제조시설과 격리하여 설치하고, 법적으로 필요한 장비와 검사에 필요한 급수시설 및 환기시설을 갖춘다.The laboratory shall be installed in isolation from the manufacturing facility and shall have legally necessary equipment, water supply and ventilation for inspection.

이상에서 상술한 바와 같이 본 발명은, 수돗물이나 일반 광천수에 비해서 자화된 자철광과 음이온을 발생하는 광물의 지하 암반에서 용출되는 암반수를 처리한 물 분자의 집단이 소집단화된 광천수는 물맛이 좋으면서 다양한 특성이 있기 때문에 먹는 물 시장에 널리 보급될 것으로 기대된다.As described above, the present invention is characterized in that the mineral water in which the group of water molecules treated with the magnetized magnetite and the rock water eluted from the underground rock of the anion-generating minerals is better than the tap water or the general mineral water. Because of its characteristics, it is expected to be widely used in the drinking water market.

Claims (3)

지하 암반으로부터 광천수를 취수하는 공정, 모래여과공정, 활성탄여과공정, 정밀여과공정, 살균공정, 용기충전공정, 검사 및 포장공정이 순차적으로 이루어지는 음료수를 제조하는 방법.A method for producing a beverage in which mineral water is taken from an underground rock, sand filtration, activated carbon filtration, precision filtration, sterilization, container filling, inspection and packaging. 1. 지하 암반으로부터 광천수를 취수하는 공정1. The process of taking mineral water from underground rock 자철광의 암반에서 핵자기공명(核磁氣共鳴; Nuclear magnetic resonance, NMR) 17O-NMR 반치폭의 값이 90㎐ 이하인 지역의 지하 암반으로부터 광천수(鑛泉水)를 취수하여 원수 저장조로 보내었다가 모래여과공정으로 보낸다.Nuclear magnetic resonance (NMR) 17 In the rock of magnetite, mineral water was collected from underground rock in areas with a half-width of 90 ㎐ or less and sent to a raw water storage tank, followed by sand filtration. Send to fair 2. 모래여과공정2. Sand filtration process 원수 저장조에 저장된 물은 모래를 충전(充塡)한 여과 탑으로 보내어 수중의 고형물질(SS; Suspended solids)을 제거하여 활성탄여과공정으로 보낸다.The water stored in the raw water storage tank is sent to a sand-filled filtration tower to remove suspended solids (SS) from the water and sent to activated carbon filtration. 3. 활성탄여과공정3. Activated Carbon Filtration Process 원수 중에 유기물질의 성분이 존재하는 경우에는 모래여과에서 고형물질을 제거한 물을 활성탄여과공정의 활성탄 충전탑(充塡塔)으로 보내어 수중의 유기물질을 흡착 제거한 다음에 정밀여과공정으로 보낸다.If organic matter is present in the raw water, the water from which the solid matter is removed from sand filtration is sent to the activated carbon packed column of activated carbon filtration to remove the organic matter from the water and then sent to the microfiltration process. 4. 정밀여과공정4. Precision filtration process 정밀여과공정에서는 한외여과(Ultrafiltration)나 마이크로 여과(Micro-filtration) 중에서 한 종류를 선정하여 물의 FI(Fouling index)값을 2∼4 범위로 처리하여 전기분해공정으로 보낸다.In the microfiltration process, one type of ultrafiltration or micro-filtration is selected and the FI (Fouling index) value of water is treated in the range of 2 to 4 and sent to the electrolysis process. 5. 전기분해공정5. Electrolysis Process 정밀여과공정에서 여과된 여과 수를 양극실(2)과 음극실(3) 사이에 격막(6)으로 격리된 전기분해장치(1)의 음극실(3)로 공급하고, 양극실(2)로는 전해질로 3∼4wt%염수나 해수를 공급하고, 정류기(7)로부터 4∼20볼트(Volt)의 직류전기를 인가(印加)하여 음극실(3)의 산화환원전위(酸化還元電位, Oxidation-reduction potential, ORP) 값이 +200∼-200㎷ 범위가 되게 산화환원전위지시제어기(Oxidation reduction potential indicating switch, ORPIS)로 정류기(7)로부터 인가되는 전류를 조정하여 생산된 전해환원수인 알칼리환원수는 알칼리환원수 저장조(8)로 보내었다가, 알칼리환원수 이송펌프(9)에 의해서 살균공정으로 보낸다.The filtered water filtered in the microfiltration process is supplied to the cathode chamber 3 of the electrolysis device 1 separated by the diaphragm 6 between the anode chamber 2 and the cathode chamber 3, and the anode chamber 2 The furnace supplies 3 to 4 wt% brine or seawater to the electrolyte, and a redox potential of the cathode chamber 3 is applied by applying a DC electric current of 4 to 20 volts from the rectifier 7. Alkali-reduced water, an electrolytic reduced water produced by adjusting the current applied from the rectifier (7) with an oxidation reduction potential indicating switch (ORPIS) so that the value of -reduction potential (ORP) ranges from +200 to -200-. Is sent to the alkaline reduced water storage tank (8), and then sent to the sterilization process by the alkaline reduced water transfer pump (9). 6. 살균공정6. Sterilization Process 살균처리방법은 가온 살균, 자외선살균, 고전압고주파살균처리 중에서 한 종류로 살균하여 정수 저장조로 보낸다.The sterilization method is one of warm sterilization, ultraviolet sterilization and high voltage high frequency sterilization and sent to a purified water storage tank. 7. 용기충전공정7. Container Filling Process 정수 저장조에 저장된 물은 용기 충전공정으로 보내어 병과 같은 용기에 충전한다.The water stored in the purified water storage tank is sent to a container filling process and filled in a container such as a bottle. 7. 검사 및 포장공정7. Inspection and Packaging Process 용기에 충전된 물은 검사한 후에 포장하여 음료수를 제조한다.The water filled in the container is inspected and then packaged to produce a beverage. 청구항 1에 있어서, 그리고 원수 중에 유기물의 농도가 CODMn의 값이 3㎎/ℓ이하인 경우에는 모래여과공정에서 수중의 고형물질을 제거한 다음에는 정밀여과공정으로 보내어 음료수를 제조하는 방법.The method according to claim 1, and a method for the concentration of organic matter, the value of COD Mn less 3㎎ / ℓ in the raw water is fed to the microfiltration step is followed by removal of the solid matter in the water in the sand filtration process producing a beverage. 청구항 1에 있어서, 원수의 산화환원전위(酸化還元電位; Oxidation-reduction potential, ORP)의 값이 +200㎷ 이하인 경우는 정밀여과된 물을 살균공정으로 보내어 음료수를 제조하는 방법.The method according to claim 1, wherein when the value of the oxidation-reduction potential (ORP) of the raw water is +200 Pa or less, the microfiltered water is sent to a sterilization process to prepare a beverage.
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RU2658419C1 (en) * 2017-03-17 2018-06-21 Федеральное государственное бюджетное образовательное учреждение высшего образования "Забайкальский государственный университет" (ФГБОУ ВО "ЗабГУ") Method of underground water treatment

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KR200315071Y1 (en) * 2003-01-07 2003-06-09 서희동 Production equipment for magnetized mineral water
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CN102583851A (en) * 2012-03-20 2012-07-18 濮阳中石集团有限公司 Mobile water treatment device and using method thereof
US9801396B2 (en) * 2013-03-14 2017-10-31 Tech Corporation Co., Ltd. Production method for natural-extract beverage
RU2658419C1 (en) * 2017-03-17 2018-06-21 Федеральное государственное бюджетное образовательное учреждение высшего образования "Забайкальский государственный университет" (ФГБОУ ВО "ЗабГУ") Method of underground water treatment

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