[go: up one dir, main page]

KR101533978B1 - Combined CDI and EDI System for Liquid Radioactive Waste Treatment - Google Patents

Combined CDI and EDI System for Liquid Radioactive Waste Treatment Download PDF

Info

Publication number
KR101533978B1
KR101533978B1 KR1020130156542A KR20130156542A KR101533978B1 KR 101533978 B1 KR101533978 B1 KR 101533978B1 KR 1020130156542 A KR1020130156542 A KR 1020130156542A KR 20130156542 A KR20130156542 A KR 20130156542A KR 101533978 B1 KR101533978 B1 KR 101533978B1
Authority
KR
South Korea
Prior art keywords
radioactive waste
unit
radioactive
waste liquid
desalination
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.)
Active
Application number
KR1020130156542A
Other languages
Korean (ko)
Other versions
KR20150069878A (en
Inventor
박승철
양호연
이지훈
조항래
Original Assignee
한국수력원자력 주식회사
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 한국수력원자력 주식회사 filed Critical 한국수력원자력 주식회사
Priority to KR1020130156542A priority Critical patent/KR101533978B1/en
Publication of KR20150069878A publication Critical patent/KR20150069878A/en
Application granted granted Critical
Publication of KR101533978B1 publication Critical patent/KR101533978B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04Treating liquids
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Molecular Biology (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • General Engineering & Computer Science (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

본 발명은 이온교환수지를 교체할 필요 없이 방사성 폐액에 함유된 방사성 핵종을 용이하게 제거 처리할 수 있도록 한 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템을 제공하는데 그 목적이 있다.
상기한 목적을 달성하기 위한 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 폐액이 역삼투막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 역삼투장치부와; 상기 역삼투장치부에서 이송된 방사성 폐액이 축전식탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 축전식탈염장치로 흡착되는 축전식탈염장치부와; 상기 축전식탈염장치부에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 핵종을 포함한 이온성 물질이 완벽하게 제거되어 배출되는 삼방밸브가 구비된 전기탈염장치부로 구성됨을 특징으로 한다.
An object of the present invention is to provide a combined radioactive waste liquid treatment system and a system for removing radioactive nuclides contained in a radioactive waste liquid, without the necessity of replacing the ion exchange resin.
According to an aspect of the present invention, there is provided a combined radioactive waste liquid treatment system comprising: a reverse osmosis membrane unit for passing radioactive waste solution through a reverse osmosis membrane to remove radioactive material contained in a radioactive waste solution; A radioactive waste solution transported from the reverse osmosis membrane unit is passed through a storage desalination unit and the radioactive waste contained in the radioactive waste solution is adsorbed by a storage desalination unit; And an electrolytic desalination unit provided with a three-way valve through which the radioactive waste liquid transferred from the electrolytic saline solution unit is passed through the electrodeposition unit to completely remove the ionic substance including the radionuclide contained in the radioactive waste liquid, do.

Description

축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템{Combined CDI and EDI System for Liquid Radioactive Waste Treatment}Technical Field [0001] The present invention relates to a combined radioactive waste treatment system and a radioactive waste treatment system,

본 발명은 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템에 관한 것으로, 특히 액체 방사성 폐기물에 함유된 희박한 방사성 핵종을 완전히 제거하여 순수 수준으로 처리할 수 있는 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템에 관한 것이다.[0001] The present invention relates to a combined radioactive waste liquid treatment system of a storage desalination apparatus and an electrodemetation apparatus, and more particularly to a storage desalination apparatus and an electrolytic desalination apparatus which can completely remove rare radioactive nuclides contained in liquid radioactive waste, The present invention relates to a combined radioactive waste liquid treating system of an apparatus.

원전의 수처리 시스템 운영, 오염된 장치의 제염, 방사선 작업복의 세탁 등 활동 중에 필연적으로 액체 방사성 폐기물이 발생된다.Liquid radioactive waste is inevitably generated during operation such as operation of water treatment system of nuclear power plants, decontamination of contaminated equipment, and washing of radioactive clothes.

일반적으로 상기한 액체 방사성 폐기물은 포함된 이온상태의 방사성 물질을 선택적 혹은 비선택적으로 제거하여 처리하며 보통 일정한 전처리 과정에서 이물질 등을 제거한 후에 증발농축, 선택적 이온교환, 역삼투 분리 등의 주요처리 공정을 이용하여 대부분의 전도도 유발물질 및 방사성 핵종을 제거 처리한다. Generally, the above-mentioned liquid radioactive waste selectively or non-selectively removes the radioactive material contained in the ionic state. In general, the radioactive waste is subjected to a main treatment process such as evaporation concentration, selective ion exchange, reverse osmosis separation To remove most of the conductivity-causing substances and radionuclides.

그러나 이러한 주요 처리공정으로 처리한 폐액에 매우 희박한 염분 및 핵종이 잔류할 수 있으며, 이 경우 보통 이온교환수지를 사용하여 추가 처리를 하게 되는데 원자력급 이온교환수지는 고가이고, 1회용이므로 많은 비용이 소요되며, 사용한 이온교환수지를 다시 2차 폐기물로 발생시키는 문제점이 있다.However, very rare salt and nuclear species can remain in the waste solution treated with this main treatment process. In this case, the additional treatment is usually performed using ion exchange resin. The ion exchange resin of nuclear grade is expensive and disposable, And the used ion exchange resin is again generated as secondary waste.

따라서, 상술한 문제점을 해결하기 위한 방사성 폐액 처리 시스템의 개발이 절실히 필요한 실정이다.Therefore, there is an urgent need to develop a radioactive waste liquid treatment system for solving the above-mentioned problems.

이와 관련된 특허로는 한국공개특허 제2000-0073685호의 역삼투막과 유브이/과산화수소 광산화법을 이용한 방사성 세탁폐액 처리방법 및 장치가 제시되어 있다.As a related patent, a method and an apparatus for treating a radioactive waste solution using a reverse osmosis membrane and a UV / hydrogen peroxide photooxidation method of Korean Patent Publication No. 2000-0073685 have been proposed.

한국공개특허 제2000-0073685호(2000.12.05)Korean Patent Publication No. 2000-0073685 (December 2000)

이에, 본 발명은 상기한 바와 같은 제문제점을 해결하기 위해 안출된 것으로, 이온교환수지를 교체할 필요 없이 방사성 폐액에 잔류하는 희박한 방사성 핵종을 용이하게 제거 처리할 수 있도록 한 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템을 제공하는데 그 목적이 있다.SUMMARY OF THE INVENTION Accordingly, the present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to provide an apparatus for removing radioactive nuclides from a radioactive waste solution, And to provide a combined radioactive waste liquid treatment system of a desalination apparatus.

상기한 목적을 달성하기 위한 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 폐액에 포함된 고농도의 염 및 방사성 물질을 1차로 제거하는 역삼투장치부와; 상기 역삼투장치부에서 이송된 방사성 폐액이 축전식탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 축전식탈염장치로 흡착되는 축전식탈염장치부와; 상기 축전식탈염장치부에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질을 제거하여 순수 수준으로 처리 배출되는 삼방밸브가 구비된 전기탈염장치부로 구성됨을 특징으로 한다.According to an aspect of the present invention, there is provided a combined radioactive waste liquid treatment system comprising: a reverse osmosis treatment unit for primarily removing salt and radioactive substances contained in a radioactive waste solution; A radioactive waste solution transported from the reverse osmosis membrane unit is passed through a storage desalination unit and the radioactive waste contained in the radioactive waste solution is adsorbed by a storage desalination unit; And an electrically desalter unit provided with a three-way valve which is passed through the electrolytic desalination unit to transfer the radioactive waste liquid transferred from the electrolytic electrolytic saline unit and the radioactive waste contained in the radioactive waste liquid is removed and discharged to a pure water level.

이상에서 설명한 바와 같이, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 다음과 같은 효과가 있다.INDUSTRIAL APPLICABILITY As described above, the combined radioactive waste solution treatment system of the present invention for separating desalination apparatus and desalination apparatus has the following effects.

첫째, 본 발명은 이온교환수지를 교체할 필요 없이 축전식탈염장치와 전기탈염장치를 이용하여 방사성 폐액에 함유된 방사성 물질을 저렴하고 용이하게 제거할 수 있다.First, the present invention can inexpensively and easily remove the radioactive material contained in the radioactive waste solution by using a storage desalination device and an electrodemetation device without the need to replace the ion exchange resin.

둘째, 본 발명은 기존에 적용한 이온교환수지 대신에 전기를 사용하는 축전식탈염장치와 전기탈염장치를 사용함으로써 고체 폐기물의 발생량을 감소시킬 수 있다.Second, the present invention can reduce the amount of solid waste generated by using a depolarizing apparatus and an electrodepositing apparatus that use electricity instead of the ion exchange resin that has been conventionally applied.

도 1은 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제1실시예를 나타낸 개략도,
도 2는 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제2실시예를 나타낸 개략도,
도 3은 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제3실시예를 나타낸 개략도,
도 4는 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제4실시예를 나타낸 개략도,
도 5는 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제5실시예를 나타낸 개략도.
1 is a schematic view showing a first embodiment of a combined radioactive waste liquid treatment system of a depolarizing apparatus and a desalination apparatus according to the present invention,
FIG. 2 is a schematic view showing a second embodiment of a combined radioactive waste liquid treating system of a depolarizing apparatus and an electrodepositing apparatus according to the present invention,
3 is a schematic view showing a third embodiment of the combined radioactive waste liquid treatment system of the electrothermal desalination apparatus and the electrothermal desalination apparatus according to the present invention,
4 is a schematic view showing a fourth embodiment of the combined radioactive waste liquid treatment system of the electrothermal desalination apparatus and the electrothermal desalination apparatus according to the present invention,
FIG. 5 is a schematic view showing a fifth embodiment of a combined radioactive waste liquid treatment system of a depolarizing apparatus and a desalination apparatus according to the present invention. FIG.

이하, 본 발명을 첨부한 예시도면 및 다양한 실시예를 예로 들어 상세히 설명한다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings and various embodiments.

[제1실시예][First Embodiment]

도 1은 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제1실시예를 나타낸 개략도이다.1 is a schematic view showing a first embodiment of a combined radioactive waste liquid treatment system of a depolarization apparatus and an electrodeposition apparatus according to the present invention.

이 도면에 도시된 바와 같이, 본 발명에 따른 축전식탈염장치와 전기탈염장치 결합형 방사성 폐액 처리시스템은 방사성 폐액이 주요처리공정인 다단의 역삼투막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 일부 역삼투장치부(100)와; 상기 역삼투장치부(100)에서 처리된 방사성 폐액이 축전식탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 축전식탈염장치로 흡착되는 축전식탈염장치부(200)와; 상기 축전식탈염장치부(200)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 모두 제거된 처리수가 배출되는 삼방밸브(310)가 구비된 전기탈염장치부(300)로 구성된다.As shown in this figure, the radioactive waste liquid treatment system combined with the electrothermal desalination apparatus according to the present invention is characterized in that the radioactive waste solution is passed through a multi-stage reverse osmosis membrane as a main treatment process, A reverse osmosis membrane part (100); A radioactive waste disposal unit 200 in which the radioactive waste liquid treated in the reverse osmosis unit 100 is passed through a storage desalination unit and the radioactive material contained in the radioactive waste liquid is adsorbed by a storage desalination unit; (300) provided with a three-way valve (310) through which the radioactive waste liquid transferred from the electrolytic saline storage unit (200) is passed through the electrodeposition unit to discharge the treated water from which the radioactive material contained in the radioactive waste liquid ).

즉, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 역삼투장치부(100)와 축전식탈염장치부(200) 및 전기탈염장치부(300)가 유기적으로 결합되어 이루어진 시스템이다.That is, the combined radioactive waste solution processing system of the present invention comprises a reverse osmosis membrane element (100), an electrolytic electrolytic saline solution unit (200) and an electrolytic desalination unit (300) System.

여기서, 상기 역삼투장치부(100)는 펌프(10)에 의해 일정 압력이 가해진 방사성 폐액이 다단의 반투막에 통과되어 그 방사성 폐액에 포함된 방사성 물질이 일부 제거된다.Here, in the reverse osmosis membrane unit 100, the radioactive waste solution to which the predetermined pressure is applied by the pump 10 is passed through the semipermeable membrane of the multi-stage, and the radioactive material contained in the radioactive waste solution is partially removed.

상기 축전식탈염장치부(200)는 역삼투장치부(100)에서 이송된 방사성 폐액이 축전식탈염장치로 통과되어, 상기 방사성 폐액에 포함된 방사성 물질의 90% 이상을 제거한다.The radioactive waste solution sent from the reverse osmosis membrane element (100) is passed through the storage desalination device to remove more than 90% of the radioactive waste contained in the radioactive waste solution.

또한, 상기 축전식탈염장치부(200)는 역삼투장치부(100)에서 이송된 방사성 폐액이 다수개의 전기탈염장치로 통과된다.In addition, the radioactive waste liquid transferred from the reverse osmosis membrane element (100) is passed through the electrochemical desalination unit (200).

여기서, 상기 축전식탈염장치는 다공성 탄소전극으로 이루어지는 이중전극 사이에 구비되는 스페이서로 구성되며, 상기 이중전극에 약 1~2V의 전극 전위를 인가하여, 이중전극 표면에서 발생하는 흡착반응을 이용하여 방사성 폐액에 포함된 방사성 물질을 흡착하여 제거하는 역할을 한다.Here, the storage desalination apparatus is composed of a spacer provided between double electrodes made of a porous carbon electrode, and an electrode potential of about 1 to 2 V is applied to the double electrode, and an adsorption reaction And absorbs and removes the radioactive material contained in the radioactive waste liquid.

이때, 상기 이중전극 표면에는 방사성 폐액에 포함된 방사성 물질 중 양이온 또는 음이온 상태의 방사성 핵종이 흡착되며, 이중전극은 양극과 음극으로 구성된다.At this time, the surface of the double electrode is adsorbed with a radioactive nuclide in the form of cation or anion among the radioactive materials contained in the radioactive waste liquid, and the double electrode is composed of the anode and the cathode.

또한, 상기 축전식탈염장치는 이중전극에 흡착된 방사성 물질의 흡착한도를 초과한 경우, 이중전극에 전극 전위를 인가하는 것을 중지하여 이중전극에 흡착된 방사성 물질들을 탈착하여 재생한다. In addition, when the storage desalination apparatus exceeds the adsorption limit of the radioactive material adsorbed on the double electrode, application of the electrode potential to the double electrode is stopped, and the radioactive materials adsorbed on the double electrode are desorbed and regenerated.

이때, 상기 이중전극에서 탈착된 방사성 물질이 포함된 농축수는 내부적으로 연결 결합된 전기탈염장치부(300)로 이송된다.At this time, the concentrated water containing the radioactive material desorbed from the double electrode is transferred to the electrically coupled desalination unit 300 internally.

그리고 상기 전기탈염장치부(300)는 축전식탈염장치부(200)에서 내부적으로 이송된 방사성 폐액을 3개의 유로로 분산시키는 삼방밸브(310)를 구비하며, 상기 삼방밸브(310)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 모두 제거된 처리수, 전기탈염장치에서 사용된 전해수, 및 축전식탈염장치부(200)에서 축전식탈염장치에 흡착된 방사성 물질이 포함된 농축수가 각각 배출된다.The electric desalination unit 300 includes a three-way valve 310 for dispersing the radioactive waste liquid internally transferred from the electrolytic electrolytic solution unit 200 into three channels, and the radioactive waste discharged from the three- The electrolytic water used in the electrolytic desalination apparatus and the radioactive material adsorbed in the electrolytic desalination unit in the electrolytic electrolytic dissolving apparatus 200 Each contained concentrated water is discharged.

여기서, 상기 전기탈염장치는 수만 V의 전극 전위가 인가되는 양이온교환막과 음이온교환막, 상기 양이온교환막과 음이온교환막 사이에 혼합이온교환수지가 충전되는 탈염실이 구성될 수 있다.Here, the electrodeposition system may include a cation exchange membrane and an anion exchange membrane to which electrode potentials of tens of thousands of volts are applied, and a desalination chamber to which a mixed ion exchange resin is charged between the cation exchange membrane and the anion exchange membrane.

상기한 바와 같은 구성으로 이루어진 본 발명에 따른 방사성 폐액 처리 시스템은 방사성 폐액이 다단의 반투막에 통과되어 방사성 폐액에 포함된 방사성 물질이 일부 제거되는 역삼투장치부(100)와; 상기 역삼투장치부(100)에서 이송된 방사성 폐액이 축전식탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 축전식탈염장치로 흡착되는 축전식탈염장치부(200)와; 상기 축전식탈염장치부(200)에서 내부적으로 이송된 방사성 폐액이 전기탈염장치로 통과되어 방사성 폐액에 포함된 방사성 물질이 모두 제거된 처리수가 배출되는 전기탈염장치부(300)로 구성됨으로써, 이온교환수지를 교체할 필요 없이 축전식탈염장치와 전기탈염장치를 이용하여 방사성 폐액에 함유된 방사성 물질을 용이하게 제거할 수 있는 작용효과가 있다.The system for treating radioactive waste solution according to the present invention having the above-described structure comprises a reverse osmosis membrane unit 100 in which a radioactive waste solution is passed through a multi-stage semipermeable membrane to partially remove radioactive material contained in the radioactive waste solution; An electrification device 200 for passing the radioactive waste liquid transferred from the reverse osmosis device 100 to a storage desalination device and for adsorbing the radioactive material contained in the radioactive waste liquid by a storage desalination device; And an electrolytic desalination unit 300 through which the radioactive waste liquid internally transferred from the electrolytic saline solution unit 200 is passed through the electrodeposition unit and the radioactive material contained in the radioactive waste liquid is completely removed, It is possible to easily remove the radioactive material contained in the radioactive waste liquid by using the electrostatic demineralization apparatus and the electrodeposition apparatus without the necessity of replacing the resin.

한편, 상기 전기탈염장치부(300)의 전기탈염장치에 유입되는 방사성 폐액의 수질은 1~10㎲/㎝(Electric Conductivity)가 권장되지만, 역삼투장치부(100)를 통과한 방사성 폐액의 수질은 10~500㎲/cm까지 다양한 수질이 나타날 수 있다.On the other hand, it is recommended that the radioactive waste solution flowing into the electrodecommitant unit 300 has a water quality of 1 to 10 μs / cm (Electric Conductivity), but the quality of the radioactive waste solution passing through the reverse osmosis membrane unit 100 Various water quality can be shown from 10 to 500 μs / cm.

이때, 상기 역삼투장치부(100)와 전기탈염장치부(300) 사이에 축전식탈염장치부(200)를 설치하여, 방사성 폐액을 처리할 경우, 상기 축전식탈염장치부(200)의 축전식탈염장치를 통과한 방사성 폐액의 수질이 1~5㎲/cm가 유지될 수 있으므로, 상기 역삼투장치부(100)를 통과한 방사성 폐액의 수질에 관계없이 방사성 폐액에 포함된 방사성 물질을 모두 제거할 수 있다.When the radioactive waste solution is treated, the electrolytic desalination unit (200) of the electrolytic desalination unit (200) is installed between the reverse osmosis unit (100) and the electrical desalination unit It is possible to remove the radioactive material contained in the radioactive waste liquid regardless of the quality of the radioactive waste liquid passing through the reverse osmosis unit 100 .

또한, 상기 축전식탈염장치부(200)의 축전식탈염장치는 약 0.05~0.2 kWh/㎥의 에너지가 소모되므로 매우 작은 양의 에너지가 소모되므로 매우 경제적이다.In addition, the storage type desalination apparatus of the electrolytic saline storage unit 200 consumes energy of about 0.05 to 0.2 kWh / m3, so that a very small amount of energy is consumed, which is very economical.

그리고 상기 축전식탈염장치부(200)는 축전식탈염장치를 통과한 방사성 폐액에 포함된 방사성 물질의 90% 이상이 축전식탈염장치에서 전기적으로 흡착 제거된다. In the electrocatalytic desalination unit 200, at least 90% of the radioactive material contained in the radioactive waste liquid passing through the electrothermal desalination unit is electrically adsorbed and removed in the electric desalination unit.

이때, 상기 축전식탈염장치부(200)는 축전식탈염장치를 통과한 방사성 폐액에 포함된 방사성 물질의 제거율이 90%가 되지 않으면 방사성 폐액을 축전식탈염장치로 재순환시킬 수 있다.At this time, if the removal rate of the radioactive material contained in the radioactive waste liquid passing through the electrolytic desalination unit is not 90%, the radioactive waste solution unit 200 can recycle the radioactive waste liquid to the electrolytic desalination unit.

또한, 상기 축전식탈염장치부(200)는 방사성 폐액에 포함된 방사성 물질을 좀 더 제거시킬 수 있도록 상기 역삼투장치부(100)에서 이송된 방사성 폐액이 다수개의 전기탈염장치로 통과되도록 구성될 수도 있음을 밝혀둔다.
In addition, the storage electrolytic saline solution unit 200 may be configured such that the radioactive waste solution transferred from the reverse osmosis membrane unit 100 is passed through a plurality of electrical desalination apparatuses so that the radioactive substance contained in the radioactive waste solution can be more removed. .

[제2실시예][Second Embodiment]

도 2는 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제2실시예를 나타낸 개략도이다.FIG. 2 is a schematic view showing a second embodiment of a combined radioactive waste liquid treatment system of a depolarizing apparatus and a desalination apparatus according to the present invention.

이 도면에 도시된 바와 같이, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 폐액이 역삼투막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 역삼투장치부(100)와; 상기 역삼투장치부(100)에서 이송된 방사성 폐액이 축전식탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 축전식탈염장치로 흡착되는 축전식탈염장치부(200)와; 상기 축전식탈염장치부(200)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되어 처리수가 배출되는 삼방밸브(310)가 구비된 전기탈염장치부(300)로 구성된다.As shown in this figure, the combined radioactive waste liquid treatment system of the present invention is characterized in that the radioactive waste solution is passed through a reverse osmosis membrane, and the radioactive waste contained in the radioactive waste solution is removed, 100); An electrification device 200 for passing the radioactive waste liquid transferred from the reverse osmosis device 100 to a storage desalination device and for adsorbing the radioactive material contained in the radioactive waste liquid by a storage desalination device; An electric desalination unit 300 having a three-way valve 310 through which the radioactive waste liquid transferred from the electrolytic saline solution unit 200 is passed to the electrodeposition unit and the radioactive material contained in the radioactive waste liquid is removed, .

여기서, 상기 역삼투장치부(100)에서 이송된 방사성 폐액이 밸브(20) 또는 펌프(30)를 이용하여 방사성 폐액의 일정량이 축전식탈염장치부(200)을 거쳐 방사성 물질이 제거되고, 나머지 일정량의 방사성 폐액이 전기탈염장치부(300)를 거쳐 방사성 물질이 제거되도록 구성된다.Here, the radioactive waste liquid transferred from the reverse osmosis membrane unit 100 is removed from the radioactive waste liquid by a predetermined amount of the radioactive waste solution by the valve 20 or the pump 30, The radioactive waste solution is configured to remove the radioactive material through the electrodeposition unit 300.

즉, 상기 역삼투장치부(100)과 전기탈염장치부(300)가 서로 밸브(20)를 통해 연결될 경우에는 상기 역삼투장치부(100)과 밸브(20) 사이에 축전식탈염장치부(200)를 설치할 수 있다.
That is, when the reverse osmosis membrane unit 100 and the electrical desalination unit 300 are connected to each other through the valve 20, the electrolytic filtration unit 200 is provided between the reverse osmosis membrane unit 100 and the valve 20 Can be installed.

[제3실시예][Third Embodiment]

도 3은 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제3실시예를 나타낸 개략도이다.3 is a schematic view showing a third embodiment of the combined radioactive waste liquid treatment system of the electrothermal demineralization apparatus and the electrothermal desalination apparatus according to the present invention.

이 도면에 도시된 바와 같이, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 폐액이 역삼투막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 역삼투장치부(100)와; 상기 역삼투장치부(100)에서 이송된 방사성 폐액이 축전식탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 축전식탈염장치로 흡착되는 축전식탈염장치부(200)와; 상기 축전식탈염장치부(200)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되어 처리수가 배출되는 삼방밸브(310)가 구비된 전기탈염장치부(300)로 구성된다.As shown in this figure, the combined radioactive waste liquid treatment system of the present invention is characterized in that the radioactive waste solution is passed through a reverse osmosis membrane, and the radioactive waste contained in the radioactive waste solution is removed, 100); An electrification device 200 for passing the radioactive waste liquid transferred from the reverse osmosis device 100 to a storage desalination device and for adsorbing the radioactive material contained in the radioactive waste liquid by a storage desalination device; An electric desalination unit 300 having a three-way valve 310 through which the radioactive waste liquid transferred from the electrolytic saline solution unit 200 is passed to the electrodeposition unit and the radioactive material contained in the radioactive waste liquid is removed, .

여기서, 상기 전기탈염장치부(300)에서 발생된 농축수를 축전식탈염장치부(200)로 이송시키는 이송수단(410)이 구성된다.Here, the conveying means 410 for conveying the concentrated water generated in the electrodeposition unit 300 to the electrothermal filtering unit 200 is formed.

즉, 상기 이송수단(410)은 전기탈염장치부(300)에서 이송된 농축수를 다시 축전식탈염장치부(200)로 이송시키는 역할을 한다.In other words, the conveying means 410 serves to convey the concentrated water conveyed from the electrodeposition unit 300 to the electrostatic precipitator 200 again.

또한, 상기 축전식탈염장치부(200)로 이송된 농축수는 축전탈염장치를 통과하여 농축수에 포함된 방사성 물질이 축전식탈염장치로 흡착된다.In addition, the concentrated water transferred to the electrolytic saline storage unit 200 is passed through the condensate desalination unit, and the radioactive material contained in the concentrated water is adsorbed by the accumulative desalination unit.

상기한 바와 같은 구성으로 이루어진 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 축전식탈염장치부(200)에서 축전식탈염장치에 흡착된 방사성 물질이 포함된 농축수를 재처리함을 특징으로 한다.
In the combined radioactive waste liquid treatment system of the present invention having the above-described configuration, the concentrated desalination apparatus includes a concentrated water containing radioactive material adsorbed by a storage desalination apparatus And reprocessing.

[제4실시예][Fourth Embodiment]

도 4는 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제4실시예를 나타낸 개략도이다.4 is a schematic view showing a fourth embodiment of the combined radioactive waste solution treatment system of the electrothermal desalination apparatus and the electrothermal desalination apparatus according to the present invention.

이 도면에 도시된 바와 같이, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 폐액이 역삼투압막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 역삼투장치부(500)와; 상기 역삼투장치부(500)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거된 처리수와 방사성 폐액에 포함된 방사성 물질이 제거된 농축수가 각각 배출되는 전기탈염장치부(600)와; 상기 전기탈염장치부(600)에서 이송된 농축수가 축전식탈염장치로 통과되어, 농축수에 포함된 방사성 물질이 축전식탈염장치에 흡착되는 축전식탈염장치부(700)로 구성된다.As shown in this figure, in the combined radioactive waste liquid treatment system of the present invention, the radioactive waste solution is passed through the reverse osmotic membrane, and the radioactive waste contained in the radioactive waste solution is removed, A tooth 500; The radioactive waste liquid transferred from the reverse osmosis membrane unit 500 is passed through the electrodeposition unit to remove the radioactive material contained in the radioactive waste liquid and the electrolytic desalination A device unit 600; And a condensing electrolytic saline solution unit 700 through which the concentrated water transferred from the electrodemetation unit 600 is passed through the electrolytic desalination unit and the radioactive substance contained in the concentrated water is adsorbed by the electrolytic desalination unit.

즉, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 역삼투장치부(500)와 전기탈염장치부(600) 및 축전식탈염장치부(700)가 유기적으로 결합되어 이루어진 시스템이다.That is, the combined radioactive waste solution treatment system of the present invention comprises a reverse osmosis membrane unit 500, an electrodemetation unit 600, and an electrolytic electrolytic solution unit 700, System.

여기서, 상기 역삼투장치부(500)는 펌프(10)에 의해 일정 압력이 가해진 방사성 폐액이 다단의 반투막에 통과되어 그 방사성 폐액에 포함된 방사성 물질이 일부 제거된다.Here, the radioactive waste liquid, to which the constant pressure is applied by the pump 10, is passed through the semi-permeable membrane of the reverse osmosis membrane unit 500, and the radioactive material contained in the radioactive waste liquid is partially removed.

특히, 상기 역삼투장치부(500)는 반투막을 사이에 둔 고농도 용액과 저농도 용액에 있어서, 고농도 용액에 삼투압 이상의 압력을 가하면 고농도 용액의 물이 저농도 용액으로 이동되는 역삼투현상을 이용하여, 방사성 물질이 일부 제거된 방사성 폐액을 회수한다.Particularly, in the reverse osmosis membrane part 500, when a pressure higher than the osmotic pressure is applied to the high concentration solution in the high concentration solution and the low concentration solution having the semipermeable membrane interposed therebetween, the water of the high concentration solution is moved to the low concentration solution, The partially removed radioactive waste solution is recovered.

여기서, 상기 반투막은 셀룰로우즈막과 TFC(Thin Film Composite)막으로 구성될 수 있다.Here, the semipermeable membrane may be composed of a cellulose membrane and a TFC (Thin Film Composite) membrane.

전자인 셀룰로우즈막은 이온제거율이 보통 95% 이상이고, 염소소독약 성분에는 강하지만 막표면에 세균이 증식하는 경우에는 막에 큰 구멍이 생겨 이온제거기능이 떨어져 불순물까지도 거를 능력을 상실한다.The cellulosic membrane, which is an electron, has an ion removal rate of more than 95% and is strong against the chlorine disinfectant component. However, when the bacteria grow on the membrane surface, large holes are formed in the membrane and the ion removal function is lost to the impurities.

후자인 TFC막은 이온제거율이 약 98% 이상이고 세균에는 강하지만 반대로 염소성분에는 매우 약하여 막표면에 염소성분이 묻을 때에는 이 또한 막면에 큰 구멍이 생겨 이온제거능력이 거의 없어지기 때문에 TFC막은 반드시 활성탄에 의한 완벽한 염소 전처리가 필수적이다.The latter TFC membrane has an ion removal rate of about 98% or more and is strong against bacteria, but on the contrary, it is very weak against chlorine components. When a chlorine component is present on the membrane surface, a large hole is formed on the membrane surface, A complete chlorine pretreatment is essential.

또한, 상기 방사성 폐액은 반투막을 통과하기 전에 마이크로필터나 활성탄필터를 포함하는 전처리장치를 통과하여 방사성 폐액에 포함된 미립자와 유기물이 제거될 수 있다.The radioactive waste solution may be passed through a pretreatment device including a microfilter or an activated carbon filter before passing through the semipermeable membrane to remove particulates and organic matter contained in the radioactive waste solution.

한편, 상기 역삼투장치부(500)는 다단의 반투막이 방사성 폐액에 포함된 방사성 물질이 90% 이상 제거될 수 있는 개수로 구성하는 것이 바람직하다.Meanwhile, it is preferable that the reverse osmosis membrane unit 500 is formed of a number of multi-stage semipermeable membranes capable of removing 90% or more of the radioactive material contained in the radioactive waste solution.

그리고 상기 전기탈염장치부(600)는 역삼투장치부(500)에서 이송된 방사성 폐액을 3개의 유로로 분산시키는 삼방밸브(610)로 구성되며, 상기 역삼투장치부(500)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 물질이 모두 제거된 처리수와, 전기탈염장치에서 사용된 전해수, 방사성 폐액에 포함된 방사성 물질이 일부 제거된 처리수가 각각 배출된다.The desalination unit 600 includes a three-way valve 610 for dispersing the radioactive waste discharged from the reverse osmosis unit 500 into three flow paths. The radioactive waste solution transferred from the reverse osmosis unit 500 The electrolytic water used in the electrolytic desalination unit and the treated water in which the radioactive material contained in the radioactive waste liquid is partially removed are discharged.

여기서, 상기 전기탈염장치는 수만 V의 전극 전위가 인가되는 양이온교환막과 음이온교환막, 상기 양이온교환막과 음이온교환막 사이에 혼합이온교환수지가 충전되는 탈염실로 구성될 수 있다.Here, the electrodeposition system may include a cation exchange membrane and an anion exchange membrane to which an electrode potential of tens of thousands of volts is applied, and a desalination chamber to which a mixed ion exchange resin is charged between the cation exchange membrane and the anion exchange membrane.

또한, 상기 축전식탈염장치부(700)는 전기탈염장치부(600)에서 이송된 처리수가 축전식탈염장치로 통과되어, 처리수에 포함된 방사성 물질이 축전식탈염장치에 흡착된다.In addition, in the electrocatalytic desalination unit 700, the treated water transferred from the electrodemetative unit 600 is passed through a storage type desalination unit, and the radioactive material contained in the treated water is adsorbed to the electrolytic desalination unit.

특히, 상기 축전식탈염장치는 다공성 탄소 전극으로 이루어지는 이중전극 사이에 구비되는 스페이서로 구성되며, 상기 이중전극에 약 1~2V의 전극 전위를 인가하여, 이중전극 표면에서 발생하는 흡착반응을 이용하여, 처리수에 포함된 방사성 물질을 흡착하여 제거하는 역할을 한다.Particularly, the storage desalination apparatus is composed of a spacer provided between double electrodes made of a porous carbon electrode, and an electrode potential of about 1 to 2 V is applied to the double electrode to use an adsorption reaction occurring on the surface of the double electrode , And adsorbs and removes the radioactive material contained in the treated water.

이때, 상기 이중전극 표면에는 방사성 폐액에 포함된 방사성 물질 중 방사성 핵종, 양이온, 음이온이 흡착되며, 이중전극은 양극과 음극으로 구성된다.At this time, radionuclides, cations, and anions among the radioactive materials contained in the radioactive waste solution are adsorbed on the surface of the double electrode, and the double electrode is composed of an anode and a cathode.

또한, 상기 축전식탈염장치는 이중전극에 흡착된 방사성 물질의 흡착한도를 초과한 경우, 상기 이중전극에 전극 전위를 인가하는 것을 중지하여 이중전극에 흡착된 방사성 물질들을 탈착하여 재생한다.In addition, when the storage desalination apparatus exceeds the adsorption limit of the radioactive material adsorbed on the double electrode, application of the electrode potential to the double electrode is stopped, and the radioactive materials adsorbed on the double electrode are desorbed and regenerated.

상기한 바와 같은 구성으로 이루어진 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 폐액이 역삼투압막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 역삼투장치부(500)와; 상기 역삼투장치부(500)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거된 처리수와 방사성 폐액에 포함된 방사성 물질이 제거된 농축수가 각각 배출되는 전기탈염장치부(600)와; 상기 전기탈염장치부(600)에서 이송된 농축수가 축전식탈염장치로 통과되어, 농축수에 포함된 방사성 물질이 축전식탈염장치에 흡착되는 축전식탈염장치부(700)로 구성됨으로써, 방사성 물질이 배출되지 않는 작용효과가 있다.
In the combined radioactive waste liquid treatment system of the present invention having the above-described configuration, the radioactive waste solution is passed through the reverse osmosis membrane to remove the radioactive material contained in the radioactive waste solution, (500); The radioactive waste liquid transferred from the reverse osmosis membrane unit 500 is passed through the electrodeposition unit to remove the radioactive material contained in the radioactive waste liquid and the electrolytic desalination A device unit 600; The condensate water transferred from the electrodemetation unit 600 is passed through a storage desalination unit and the radioactive substance contained in the concentrated water is adsorbed by the storage desalination unit. There is an action effect not to be discharged.

[제5실시예][Fifth Embodiment]

도 5는 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 제5실시예를 나타낸 개략도이다.5 is a schematic view showing a fifth embodiment of the combined radioactive waste liquid treatment system of the electrothermal demineralization apparatus and the electrothermal desalination apparatus according to the present invention.

이 도면에 도시된 바와 같이, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 폐액이 역삼투압막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 역삼투장치부(500)와; 상기 역삼투장치부(500)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거된 처리수와 방사성 폐액에 포함된 방사성 물질이 제거된 농축수가 각각 배출되는 전기탈염장치부(600)와; 상기 전기탈염장치부(600)에서 이송된 농축수가 축전식탈염장치로 통과되어, 농축수에 포함된 방사성 물질이 축전식탈염장치에 흡착되는 축전식탈염장치부(700)로 구성된다.As shown in this figure, in the combined radioactive waste liquid treatment system of the present invention, the radioactive waste solution is passed through the reverse osmotic membrane, and the radioactive waste contained in the radioactive waste solution is removed, A tooth 500; The radioactive waste liquid transferred from the reverse osmosis membrane unit 500 is passed through the electrodeposition unit to remove the radioactive material contained in the radioactive waste liquid and the electrolytic desalination A device unit 600; And a condensing electrolytic saline solution unit 700 through which the concentrated water transferred from the electrodemetation unit 600 is passed through the electrolytic desalination unit and the radioactive substance contained in the concentrated water is adsorbed by the electrolytic desalination unit.

여기서, 상기 축전식탈염장치부(700)에서 이송된 처리수를 전기탈염장치부(600)로 이송시키는 이송수단(810)이 구성된다.Here, a conveying means 810 for conveying the treated water conveyed from the electrolytic dissolving unit 700 to the electrodeposition unit 600 is formed.

즉, 상기 이송수단(810)은 축전식탈염장치부(700)에서 이송된 처리수를 전기탈염장치부(600)로 이송시키는 역할을 한다.That is, the transfer means 810 transfers the treated water transferred from the electrolytic dissolution apparatus 700 to the desalination apparatus 600.

특히, 상기 이송수단(810)은 방사성 물질이 일부 함유된 처리수를 전기탈염장치부(600)에서 재처리함을 특징으로 한다.Particularly, the conveying unit 810 is characterized in that the treated water containing a part of the radioactive material is reprocessed in the electrodeposition unit 600.

상기한 바와 같은 구성으로 이루어진 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템은 방사성 물질이 배출되지 않는 작용효과가 있다.The combined radioactive waste liquid treatment system of the present invention having the above-described configuration of the storage desalination device and electrodeposition device has the action and effect that the radioactive material is not discharged.

이하, 본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 실험에 대해 설명한다.Hereinafter, an experiment of the combined radioactive waste liquid treatment system of the electrothermal desalination apparatus and the electrothermal desalination apparatus according to the present invention will be described.

<실험예><Experimental Example>

본 발명에 따른 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템의 실시예를 이용하여, 실험을 수행하였다.Experiments were conducted using an embodiment of the combined radioactive waste liquid treatment system of the electrothermal desalination unit and the electrothermal desalination unit according to the present invention.

상기 방사성 폐액에 포함된 방사성 물질의 농도에 따른 영향을 살펴보기 위하여, 20, 50, 100㎲/㎝(Electric Conductivity) NaCl 수용액을 제조하여 탈염실험에 사용하였다.In order to investigate the influence of the concentration of the radioactive material contained in the radioactive waste solution, aqueous solutions of 20, 50 and 100 μs / cm (Electric Conductivity) NaCl were prepared and used for desalting experiments.

상기 20, 50, 100㎲/㎝ NaCl 수용액을 각각 역삼투장치부의 역삼투장치로 주입하여 전처리 한 다음, 축전식탈염장치부의 축전식탈염장치로 주입하였다.The 20, 50, and 100 μs / cm NaCl aqueous solutions were respectively injected into the reverse osmosis unit of the reverse osmosis tube and pretreated, and then injected into the depolarization apparatus of the electrolytic saline.

상기 축전식탈염장치부의 축전식탈염장치에 0.8 내지 1.5 V의 전극 전위를 15분 동안 인가하여 상기 20, 50, 100㎲/㎝ NaCl 수용액의 흡착 반응을 유도한 후, 전극 전위를 인가하는 것을 중지시켜 3분 동안 탈착 반응을 유도하였다.An electrode potential of 0.8 to 1.5 V was applied to the electrothermal desalination apparatus of the electrolytic electrolytic saline solution unit for 15 minutes to induce the adsorption reaction of the aqueous solution of 20, 50, and 100 / / ㎝ NaCl, And the desorption reaction was induced for 3 minutes.

상기 20㎲/㎝ NaCl 수용액의 흡착 반응 유도 결과, 축전식탈염장치를 통과한 후, 전기전도도(Electric Conductivity)를 측정한 결과 0.5㎲/㎝까지 감소하는 것을 확인할 수 있었다.As a result of the adsorption reaction induction of the aqueous solution of 20 μs / cm 2 NaCl, it was confirmed that the electric conductivities were reduced to 0.5 μs / ㎝ after passing through the storage desalination device.

상기 축전식탈염장치를 통과한 20㎲/㎝ NaCl 수용액을 전기탈염장치부의 전기탈염장치로 통과시킨 후, 전기저항을 측정한 결과 18.2MΩㆍ㎝로 방사성 핵종을 포함 대부분의 이온성 물질이 제거된 것을 확인할 수 있다.The aqueous solution of 20 μs / cm NaCl passed through the above described electrochemical desalination unit was passed through an electrodemetation unit of the electrodemetation unit, and the electrical resistance was measured. As a result, 18.2 MΩ · cm was found to be the most ionic substance including radionuclide .

이상의 실험 결과로부터 축전식탈염장치부는 역삼투장치부를 통과한 유출수의 수질이 다소 흔들림에도 전기탈염장치의 권장 유입수질 조건을 충족시킬 수 있으므로 반도체 등급의 처리수를 얻을 수 있을 만큼 모든 핵종을 완벽하게 제거할 수 있는 시스템임을 알 수 있었다.From the above experimental results, it can be seen that even though the water quality of the effluent passing through the reverse osmosis unit is somewhat fluctuated, the storage desalination unit can satisfy the recommended inlet water quality conditions of the electrical desalination unit. It is clear that the system can be removed.

10: 펌프 20: 밸브
30: 펌프 100: 역삼투장치부
200: 축전식탈염장치부 300: 전기탈염장치부
310: 삼방밸브 410: 이송수단
500: 역삼투장치부 600: 전기탈염장치부
610: 삼방밸브 700: 축전식탈염장치부
810: 이송수단
10: Pump 20: Valve
30: Pump 100: Reverse osmosis pump
200: electrolytic desalting unit 300: electric desalination unit
310: Three-way valve 410: Feeding means
500: reverse osmosis unit 600: electric desalination unit
610: Three-way valve 700:
810:

Claims (5)

방사성 폐액이 주요처리공정인 다단의 역삼투막에 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거되는 역삼투장치부(100)와; 상기 역삼투장치부(100)에서 처리된 방사성 폐액이 축전식탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 축전식탈염장치로 흡착되는 축전식탈염장치부(200)와; 상기 축전식탈염장치부(200)에서 이송된 방사성 폐액이 전기탈염장치로 통과되어, 방사성 폐액에 포함된 방사성 물질이 제거된 처리수가 배출되는 삼방밸브(310)가 구비된 전기탈염장치부(300)로 구성되고, 상기 역삼투장치부(100)에서 이송된 방사성 폐액이 밸브(20) 또는 펌프(30)를 이용하여 방사성 폐액의 일정량이 축전식탈염장치부(200)을 거쳐 방사성 물질이 제거되고, 나머지 일정량의 방사성 폐액이 전기탈염장치부(300)를 거쳐 방사성 물질이 제거되도록 구성되며, 상기 전기탈염장치부(300)에서 발생된 농축수를 축전식탈염장치부(200)로 이송시키는 이송수단(410)이 구성되며, 상기 축전식탈염장치는 다공성 탄소전극으로 이루어지는 이중전극 사이에 구비되는 스페이서로 구성되며, 상기 이중전극에 1∼2V의 전극 전위를 인가하여, 이중전극 표면에서 발생하는 흡착반응을 이용하여 방사성 폐액에 포함된 방사성 물질을 흡착하여 제거하되, 상기 이중전극 표면에는 방사성 폐액에 포함된 방사성 물질 중 양이온 또는 음이온 상태의 방사성 핵종이 흡착되며, 이중전극은 양극과 음극으로 구분됨을 특징으로 하는 축전식탈염장치와 전기탈염장치의 결합형 방사성 폐액 처리시스템.
A reverse osmosis membrane unit (100) through which a radioactive waste solution is passed through a multi-stage reverse osmosis membrane as a main treatment process to remove radioactive material contained in a radioactive waste solution; A radioactive waste disposal unit 200 in which the radioactive waste liquid treated in the reverse osmosis unit 100 is passed through a storage desalination unit and the radioactive material contained in the radioactive waste liquid is adsorbed by a storage desalination unit; An electric desalination unit 300 having a three-way valve 310 through which the radioactive waste liquid transferred from the electrolytic salt removing unit 200 is passed through the electrodeposition unit and the treated water from which the radioactive material contained in the radioactive waste liquid is removed is discharged, And the radioactive waste liquid transferred from the reverse osmosis membrane unit 100 is removed by the valve 20 or the pump 30 through the electrifying plate 200 and the remaining A predetermined amount of radioactive waste solution is supplied to the electrodialysis device unit 300 to remove the radioactive material and the conveying device 410 for transferring the concentrated water generated in the electrodialysis device unit 300 to the electrotherapy apparatus 200 ), And the storage and desalination apparatus is composed of a spacer provided between double electrodes made of a porous carbon electrode, and an electrode potential of 1 to 2 V is applied to the double electrode, And the radioactive material contained in the radioactive waste liquid is adsorbed on the surface of the double electrode, and the radioactive material of the positive or negative ionic state contained in the radioactive waste contained in the radioactive waste liquid is adsorbed on the surface of the double electrode, Wherein the radioactive waste solution is separated into a radioactive waste solution and a radioactive waste solution.
삭제delete 삭제delete 삭제delete 삭제delete
KR1020130156542A 2013-12-16 2013-12-16 Combined CDI and EDI System for Liquid Radioactive Waste Treatment Active KR101533978B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020130156542A KR101533978B1 (en) 2013-12-16 2013-12-16 Combined CDI and EDI System for Liquid Radioactive Waste Treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020130156542A KR101533978B1 (en) 2013-12-16 2013-12-16 Combined CDI and EDI System for Liquid Radioactive Waste Treatment

Publications (2)

Publication Number Publication Date
KR20150069878A KR20150069878A (en) 2015-06-24
KR101533978B1 true KR101533978B1 (en) 2015-07-06

Family

ID=53516887

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020130156542A Active KR101533978B1 (en) 2013-12-16 2013-12-16 Combined CDI and EDI System for Liquid Radioactive Waste Treatment

Country Status (1)

Country Link
KR (1) KR101533978B1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101650137B1 (en) * 2015-12-10 2016-08-24 광주과학기술원 Capacitive deionization device and method of controlling thereof
KR101981019B1 (en) * 2018-12-03 2019-08-28 현대건설주식회사 Treating apparatus and method for concentrated waste water using ro-cdi process
KR20250118490A (en) 2024-01-30 2025-08-06 한국과학기술원 Capacitive Deionization Electrodes and Adsorption/Desorption Methods for Cesium and Strontium Ions Using the same

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB201617347D0 (en) * 2016-10-13 2016-11-30 VWS (UK) Limited Method and apparatus for providing ultrapure water
CN112340917B (en) * 2020-11-04 2023-12-22 江汉大学 Method and system for treating radioactive wastewater
KR102818749B1 (en) * 2023-06-19 2025-06-11 주식회사 이노켐텍 Apparatus and method for treating waste liquid from nuclear facilities

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010060228A (en) * 1999-11-02 2001-07-06 타케토시 카즈오 Electric deionizing apparatus and electric deionizing treatment method using the same
KR20100053571A (en) * 2007-07-30 2010-05-20 쿠리타 고교 가부시키가이샤 Pure water production apparatus and pure water production method
KR20120035531A (en) * 2010-10-06 2012-04-16 (주) 시온텍 Manufacturing apparatus of ultrapure water using capacitive deionization electrode

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010060228A (en) * 1999-11-02 2001-07-06 타케토시 카즈오 Electric deionizing apparatus and electric deionizing treatment method using the same
KR20100053571A (en) * 2007-07-30 2010-05-20 쿠리타 고교 가부시키가이샤 Pure water production apparatus and pure water production method
KR20120035531A (en) * 2010-10-06 2012-04-16 (주) 시온텍 Manufacturing apparatus of ultrapure water using capacitive deionization electrode

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101650137B1 (en) * 2015-12-10 2016-08-24 광주과학기술원 Capacitive deionization device and method of controlling thereof
KR101981019B1 (en) * 2018-12-03 2019-08-28 현대건설주식회사 Treating apparatus and method for concentrated waste water using ro-cdi process
KR20250118490A (en) 2024-01-30 2025-08-06 한국과학기술원 Capacitive Deionization Electrodes and Adsorption/Desorption Methods for Cesium and Strontium Ions Using the same

Also Published As

Publication number Publication date
KR20150069878A (en) 2015-06-24

Similar Documents

Publication Publication Date Title
KR101533978B1 (en) Combined CDI and EDI System for Liquid Radioactive Waste Treatment
Dermentzis Removal of nickel from electroplating rinse waters using electrostatic shielding electrodialysis/electrodeionization
CN103058425B (en) desalination system and method
KR102011115B1 (en) capacitive deionization system for concentrated water saving type
US20060231403A1 (en) Chambered electrodeionization apparatus with uniform current density, and method of use
US20080198531A1 (en) Capacitive deionization system for water treatment
CN105417635B (en) Device for purifying a fluid and method for purifying a fluid by means of the same
KR20120035531A (en) Manufacturing apparatus of ultrapure water using capacitive deionization electrode
WO2011065222A1 (en) Device and method for treating nitrogen compound-containing acidic solutions
NL2020640B1 (en) Deionization device and method for at least partially deionizing a feed liquid in which an electrolyte is dissolved, and apparatuses using such devices
US20150175448A1 (en) System for treating wastewater containing boron and iodine
CN105321589A (en) Method for treating radioactive wastewater through whole membrane technology
Kim et al. Effect of brine water on discharge of cations in membrane capacitive deionization and its implications on nitrogen recovery from wastewater
US8143471B2 (en) Electrochemical capacitive concentration and deactivation of actinide nuclear materials
US9932253B2 (en) Apparatus for purifying a fluid and method for purifying a fluid, in particular by means of the aforesaid apparatus
Dermentzis et al. Ammonia removal from fertilizer plant effluents by a coupled electrostatic shielding based electrodialysis/electrodeionization process
US20230149857A1 (en) Improved chlorine tolerance of continuous electrodeionization modules
US20130240362A1 (en) Flow-through condenser cell for purifying a fluid
JP6534752B1 (en) Radioactive waste liquid treatment system
Keshtkar et al. Performance evaluation of continuous electrodeionization (CEDI) for removal of strontium and cesium from aqueous solutions using Taguchi method
US20230406734A1 (en) Electrodeionization Configuration for Enhanced Boron Removal
CN203112637U (en) Preparation system for liquid dosimeter preparation water
Nagasawa et al. Boron removal from aqueous solution by bipolar electrodialysis
Zahakifar et al. Removal of cesium from radioactive wastewater using ELECTRODIALYSIS (ED)
WO2019118163A1 (en) Method for selectively removing dissolved ions from water using composite resin electrodes

Legal Events

Date Code Title Description
PA0109 Patent application

Patent event code: PA01091R01D

Comment text: Patent Application

Patent event date: 20131216

PA0201 Request for examination
PE0902 Notice of grounds for rejection

Comment text: Notification of reason for refusal

Patent event date: 20141121

Patent event code: PE09021S01D

AMND Amendment
E601 Decision to refuse application
PE0601 Decision on rejection of patent

Patent event date: 20150515

Comment text: Decision to Refuse Application

Patent event code: PE06012S01D

Patent event date: 20141121

Comment text: Notification of reason for refusal

Patent event code: PE06011S01I

AMND Amendment
PX0901 Re-examination

Patent event code: PX09011S01I

Patent event date: 20150515

Comment text: Decision to Refuse Application

Patent event code: PX09012R01I

Patent event date: 20150120

Comment text: Amendment to Specification, etc.

PG1501 Laying open of application
PX0701 Decision of registration after re-examination

Patent event date: 20150626

Comment text: Decision to Grant Registration

Patent event code: PX07013S01D

Patent event date: 20150519

Comment text: Amendment to Specification, etc.

Patent event code: PX07012R01I

Patent event date: 20150515

Comment text: Decision to Refuse Application

Patent event code: PX07011S01I

Patent event date: 20150120

Comment text: Amendment to Specification, etc.

Patent event code: PX07012R01I

X701 Decision to grant (after re-examination)
GRNT Written decision to grant
PR0701 Registration of establishment

Comment text: Registration of Establishment

Patent event date: 20150630

Patent event code: PR07011E01D

PR1002 Payment of registration fee

Payment date: 20150701

End annual number: 3

Start annual number: 1

PG1601 Publication of registration
FPAY Annual fee payment

Payment date: 20190618

Year of fee payment: 5

PR1001 Payment of annual fee

Payment date: 20190618

Start annual number: 5

End annual number: 5

PR1001 Payment of annual fee

Payment date: 20200624

Start annual number: 6

End annual number: 6

PR1001 Payment of annual fee

Payment date: 20210629

Start annual number: 7

End annual number: 7

PR1001 Payment of annual fee

Payment date: 20220628

Start annual number: 8

End annual number: 8

PR1001 Payment of annual fee

Payment date: 20230627

Start annual number: 9

End annual number: 9

PR1001 Payment of annual fee

Payment date: 20240627

Start annual number: 10

End annual number: 10