KR100938606B1 - Mineral extraction method and extracted mineral from composite clay mineral - Google Patents

Mineral extraction method and extracted mineral from composite clay mineral Download PDF

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KR100938606B1
KR100938606B1 KR1020080034832A KR20080034832A KR100938606B1 KR 100938606 B1 KR100938606 B1 KR 100938606B1 KR 1020080034832 A KR1020080034832 A KR 1020080034832A KR 20080034832 A KR20080034832 A KR 20080034832A KR 100938606 B1 KR100938606 B1 KR 100938606B1
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mineral
clay mineral
sulfuric acid
minerals
acid solution
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남정우
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    • 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
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • 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
    • C02F1/26Treatment of water, waste water, or sewage by extraction
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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Abstract

본 발명은 복합점토광물로부터 미네랄을 추출하는 방법 및 그 방법을 이용해 추출된 미네랄에 관한 것으로, 보다 자세하게는 미네랄을 추출하는 방법으로 복합점토광물을 파쇄하는 점토광물파쇄단계, 전술한 점토광물파쇄단계를 거쳐 형성된 점토광물 분말이 전기분해장치를 통과하는 전기분해처리단계, 전술한 전기분해처리단계를 거친 점토광물 분말을 황산용액과 교반하는 황산용액처리단계 및 전술한 황산용액처리단계를 거쳐 형성된 혼합물을 유압필터에서 1차 여과하고 멤브레인필터에서 2차로 여과하는 필터여과단계를 포함하여 이루어진다.The present invention relates to a method for extracting minerals from complex clay minerals and to minerals extracted by using the method, and more specifically, to a method of extracting minerals, the method of extracting minerals from clay mineral crushing step, the above-mentioned clay mineral crushing step The mixture formed through the electrolytic treatment step in which the clay mineral powder formed through the electrolysis device passes through the electrolysis device, the sulfuric acid solution treatment step of stirring the clay mineral powder through the above-described electrolysis treatment step with sulfuric acid solution, and the sulfuric acid solution treatment step described above. It comprises a filter filtration step of primary filtration in the hydraulic filter and secondary filtration in the membrane filter.

또한, 전술한 복합점토광물로부터 미네랄을 추출하는 방법을 이용하여 추출된 미네랄을 포함한다.In addition, it includes a mineral extracted using the method of extracting the mineral from the above-mentioned complex clay mineral.

점토, 광물, 미네랄, 추출, 전기분해, 교반, 필터 Clay, mineral, mineral, extraction, electrolysis, stirring, filter

Description

복합점토광물로부터 미네랄을 추출하는 방법 및 그 방법을 이용해 추출된 미네랄{MINERAL EXTRACTION METHOD AND EXTRACTED MINERAL FROM COMPOSITE CLAY MINERAL}Method of extracting minerals from complex clay minerals and minerals extracted using the method {MINERAL EXTRACTION METHOD AND EXTRACTED MINERAL FROM COMPOSITE CLAY MINERAL}

본 발명은 복합점토광물로부터 미네랄을 추출하는 방법 및 그 방법을 이용해 추출된 미네랄에 관한 것으로, 점토광물파쇄단계, 전기분해처리단계, 황산용액처리단계 및 필터여과단계를 포함하여 이루어진다.The present invention relates to a method for extracting minerals from complex clay minerals and to minerals extracted using the method, comprising a clay mineral crushing step, an electrolysis treatment step, a sulfuric acid solution treatment step and a filter filtration step.

본 발명은 복합점토광물로부터 미네랄을 추출하는 방법 및 그 방법을 이용해 추출된 미네랄에 관한 것으로, 생명체 유지에 꼭 필요한 필수미네랄과 일반미네랄을 포함하고 있는 복합점토광물 내에 존재하는 미네랄을 추출하는 방법 및 그 방법을 이용해 추출된 미네랄에 관한 것이다.The present invention relates to a method for extracting minerals from complex clay minerals and to minerals extracted by using the method, and a method for extracting minerals present in complex clay minerals containing essential minerals and general minerals necessary for life support, and It relates to minerals extracted using the method.

종래에는 단순히 복합점토광물을 파쇄 및 분체하여 미네랄 조성물을 얻는 방법 내지는 인위적으로 미네랄 조성물을 만들어 내는 방법이 이용되었는데, 그 사용법과 효과가 동의보감 문헌에도 기록되어 있을 만큼 오래전부터 이용되어 왔다.Conventionally, a method of obtaining a mineral composition by artificially crushing and powdering a composite clay mineral or a method of artificially producing a mineral composition has been used, and its use and effect have been used for a long time as it is recorded in the consent book.

그러나 이러한 방법으로 제조된 미네랄 조성물은 조성물에 미네랄 함량이 미미하거나 화학적으로 불안정하여 미네랄의 균형이 쉽게 깨어지는 문제점이 있었다.However, the mineral composition prepared by this method has a problem in that the balance of minerals is easily broken because the mineral content is insignificant or chemically unstable in the composition.

또한, 인위적으로 제조된 미네랄 조성물의 경우는 조성물에 미네랄 함량이 과하거나 부족하여 생명체에 부작용이 발생하는 문제점이 있었다.In addition, in the case of artificially prepared mineral composition, there is a problem that side effects occur in living beings due to excessive or insufficient mineral content in the composition.

본 발명은 전술한 문제점을 해결하기 위한 것으로, 점토광물파쇄단계, 전기분해처리단계, 황산용액처리단계 및 필터여과단계를 포함하는 복합점토광물로부터 미네랄을 추출하는 방법을 이용하여 용출원소수와 용출량이 많은 미네랄 추출방법을 제공하는 것이다.The present invention is to solve the above problems, using the method of extracting minerals from complex clay minerals, including clay mineral crushing step, electrolysis treatment step, sulfuric acid solution treatment step and filter filtration step, elution element water and elution amount It is to provide many mineral extraction methods.

전술한 본 발명의 목적은 복합점토광물을 파쇄하는 점토광물파쇄단계, 전술한 점토광물파쇄단계를 거쳐 형성된 점토광물 분말이 전기분해장치를 통과하는 전기분해처리단계, 전술한 전기분해처리단계를 거친 점토광물 분말을 황산용액과 교반하는 황산용액처리단계 및 전술한 황산용액처리단계를 거쳐 형성된 혼합물을 유압필터에서 1차 여과하고 멤브레인필터에서 2차로 여과하는 필터여과단계를 포함하여 이루어지는 것을 특징으로 하는 복합점토광물로부터 미네랄을 추출하는 방법을 제공함에 의해 달성된다.An object of the present invention described above is a clay mineral crushing step of crushing a complex clay mineral, the clay mineral powder formed through the above-mentioned clay mineral crushing step is subjected to an electrolysis step of passing through an electrolysis device, the electrolytic treatment step described above A sulfuric acid solution treatment step of stirring clay mineral powder with sulfuric acid solution and a filter filtration step of firstly filtering the mixture formed through the above-mentioned sulfuric acid solution treatment step in a hydraulic filter and secondly in a membrane filter. By providing a method for extracting minerals from complex clay minerals.

본 발명의 바람직한 특징에 따르면, 전술한 황산용액처리단계는 황산 20 내지 80 중량%와 정제수 20 내지 80 중량%를 혼합하여 제조된 황산용액 100 내지 500 중량부를 전술한 복합점토광물에 혼합하여 2 내지 24시간 교반한 후에, 고형분을 제거하는 과정을 포함하여 이루어진다.According to a preferred feature of the present invention, the above-described sulfuric acid solution treatment step 2 to 20 to 80% by weight of sulfuric acid solution prepared by mixing 20 to 80% by weight of sulfuric acid and purified water mixed with the above-mentioned complex clay mineral 2 to After stirring for 24 hours, the process includes removing the solids.

본 발명의 더 바람직한 특징에 따르면, 전술한 복합점토광물은 일라이트, 뮤 스코바이트, 클로라이트, 버미큘라이트 및 할로이사이트로 이루어진 그룹으로부터 선택된 하나 이상을 포함하여 이루어진다.According to a further preferred feature of the invention, the above-mentioned complex clay mineral comprises at least one selected from the group consisting of illite, muscobite, chlorite, vermiculite and halosite.

또한, 본 발명은 전술한 복합점토광물로부터 미네랄을 추출하는 방법을 이용하여 추출되는 것을 특징으로 하는 복합점토광물로부터 미네랄을 추출하는 방법을 이용하여 추출된 미네랄을 제공함에 의해 달성된다.In addition, the present invention is achieved by providing a mineral extracted using the method of extracting minerals from the composite clay mineral, characterized in that the extraction using the method of extracting minerals from the above-mentioned complex clay mineral.

본 발명의 더 바람직한 특징에 따르면 전술한 미네랄은 나트륨, 철, 칼륨, 마그네슘, 알루미늄, 망간, 규소, 칼슘, 아연 및 티타늄으로 이루어진 그룹으로부터 선택되는 하나 이상으로 이루어진다.According to a further preferred feature of the invention the above-mentioned minerals consist of one or more selected from the group consisting of sodium, iron, potassium, magnesium, aluminum, manganese, silicon, calcium, zinc and titanium.

본 발명에 의한 복합점토광물로부터 미네랄을 추출하는 방법 및 그 방법을 이용하여 추출된 미네랄은 효율적인 추출방법을 적용하여 다양한 용출원소수와 많은 미네랄 용출량을 제공할 수 있다.The method of extracting minerals from the composite clay mineral according to the present invention and the minerals extracted using the method can provide various extraction element numbers and a large amount of mineral leaching amount by applying an efficient extraction method.

또한, 환경친화적인 추출방법을 이용하기 때문에 환경오염이 발생하지 않는다는 장점이 있다.In addition, there is an advantage that environmental pollution does not occur because of using an environmentally friendly extraction method.

또한, 본 발명에 의해 제조된 미네랄은 악취제거, 정균, 수처리 등 다양한 분야에 이용될 수 있다.In addition, the mineral produced by the present invention can be used in various fields, such as odor removal, bacteriostatic, water treatment.

또한, 본 발명에 의해 제조된 미네랄은 농작물에 적용하여 생산성을 높이고, 축산물에 적용하여 축산환경을 개선할 수 있다.In addition, the minerals prepared by the present invention can be applied to crops to increase productivity, and can be applied to livestock products to improve the livestock environment.

이하에는, 본 발명의 바람직한 실시예와 각 성분의 물성을 상세하게 설명하되, 이는 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자가 발명을 용이하게 실시할 수 있을 정도로 상세하게 설명하기 위한 것이지, 이로 인해 본 발명의 기술적인 사상 및 범주가 한정되는 것을 의미하지는 않는다.In the following, preferred embodiments of the present invention and the physical properties of each component will be described in detail, which is intended to explain in detail enough to be able to easily carry out the invention by one of ordinary skill in the art, This does not mean that the technical spirit and scope of the present invention is limited.

본 발명에 따른 복합점토광물로부터 미네랄을 추출하는 방법 및 그 방법을 이용하여 추출된 미네랄은 복합점토광물을 파쇄하는 점토광물파쇄단계(S101), 전술한 점토광물파쇄단계(S101)를 거쳐 형성된 점토광물 분말이 전기분해장치를 통과하는 전기분해처리단계(S103), 전술한 전기분해처리단계(S103)를 거친 점토광물 분말을 황산용액과 교반하는 황산용액처리단계(S105) 및 전술한 황산용액처리단계(S105)를 거쳐 형성된 혼합물을 유압필터에서 1차 여과하고 멤브레인필터에서 2차로 여과하는 필터여과단계(S107)를 포함하여 이루어진다.Method for extracting minerals from the composite clay mineral according to the present invention and the minerals extracted by using the method is a clay mineral crushing step (S101) for crushing the complex clay minerals, clay formed through the above-described clay mineral crushing step (S101) Sulfuric acid solution treatment step (S105) and the above-mentioned sulfuric acid solution treatment in which the mineral powder passes through an electrolysis apparatus (S103), the clay mineral powder passed through the electrolytic treatment step (S103) with sulfuric acid solution The filter formed through the step (S105) and the primary filter in the hydraulic filter and a filter filtration step (S107) for filtration secondly in the membrane filter is made.

전술한 점토광물파쇄단계(S101)는 일라이트, 뮤스코바이트, 클로라이트, 버미큘라이트 및 할로이사이트로 등으로 이루어진 복합점토광물을 볼밀링 장치를 이용하여 파쇄하는 단계로, 이러한 볼밀링 장치를 통과한 복합점토광물은 물과 혼합하기 전에 10 내지 500 메시 크기의 분말로 파쇄된다.The above-mentioned clay mineral crushing step (S101) is a step of crushing a complex clay mineral made of illite, muscobite, chlorite, vermiculite and halosite using a ball milling device, and passed through the ball milling device. The composite clay mineral is crushed into powder of 10 to 500 mesh size before mixing with water.

전술한 전기분해처리단계(S103)는 전술한 복합점토광물을 파쇄하여 형성된 점토광물 분말 20 중량부와 물 80 중량부를 혼합하여 형성된 혼합물을 교반한 후 에, 전극봉에 5 내지 8 볼트의 전극을 1 내지 6 시간 동안 걸어주게 되면 전술한 복합점토광물에 이온층이 파괴되어 결합력이 약해지기 때문에 미네랄 추출작업시에 미네랄 용출량을 증가시키게 된다.In the aforementioned electrolytic treatment step (S103), after stirring the mixture formed by mixing 20 parts by weight of clay mineral powder and 80 parts by weight of water formed by crushing the complex clay mineral described above, an electrode of 5 to 8 volts is added to the electrode. If you walk for 6 hours to increase the mineral leaching amount during the mineral extraction operation because the binding layer is weakened by breaking the ionic layer to the above-mentioned complex clay minerals.

전술한 시간 동안 전극을 걸어주고 난 후에는 물을 제거하고 24 내지 48 시간 동안 건조하는데, 건조가 완료되면 볼밀링 장치를 이용하여 다시 파쇄한다.After the electrode is hung for the above-mentioned time, the water is removed and dried for 24 to 48 hours. When the drying is completed, it is crushed again using a ball milling device.

전술한 황산용액처리단계(S105)는 황산 20 내지 80중량%와 정제수 20 내지 80중량%를 혼합하여 제조된 황산용액 100 내지 500 중량부를 전술한 점토광물 분말에 혼합하여 2 내지 24시간 교반한 후에, 고형분을 제거하는 과정을 포함하여 이루어진다.In the aforementioned sulfuric acid solution treatment step (S105), 100 to 500 parts by weight of the sulfuric acid solution prepared by mixing 20 to 80% by weight of sulfuric acid and 20 to 80% by weight of purified water is mixed with the aforementioned clay mineral powder and stirred for 2 to 24 hours. And removing the solids.

전술한 필터여과단계(S107)는 전술한 황산용액처리단계(S105)를 거쳐 형성된 혼합물을 필터를 이용하여 여과하는 단계로, 먼저 유압필터를 이용하여 1차로 여과하는데, 유압필터를 이용한 여과가 완료되면 고형분은 교반탱크에서 따로 분리한다.The above-described filter filtration step (S107) is a step of filtering the mixture formed through the above-described sulfuric acid solution treatment step (S105) by using a filter, first filtering using a hydraulic filter, filtration using a hydraulic filter is completed Solids are separated from the agitation tank.

전술한 유압필터를 이용한 여과가 완료되면 여과액을 멤브레인필터로 이송하여 미세여과하는 2차 여과 과정이 이루어진다.When the filtration using the above-described hydraulic filter is completed, the secondary filtration process is carried out by transferring the filtrate to the membrane filter and microfiltration.

전술한 단계로 이루어지는 복합점토광물로부터 미네랄을 추출하는 방법을 이용하여 추출되는 것을 특징으로 하는 복합점토광물로부터 미네랄을 추출하는 방법 을 이용하여 추출된 미네랄은 나트륨, 철, 칼륨, 마그네슘, 알루미늄, 망간, 규소, 칼슘, 아연 및 티타늄으로 이루어진 그룹으로부터 선택된 하나 이상으로 이루어진다.Minerals extracted using the method of extracting minerals from the composite clay mineral, characterized in that the extraction is carried out using a method of extracting minerals from the composite clay mineral consisting of the above-mentioned steps are sodium, iron, potassium, magnesium, aluminum, manganese , At least one selected from the group consisting of silicon, calcium, zinc and titanium.

이하에서는 본 발명에 따른 복합점토광물로부터 미네랄을 추출하는 방법에 따른 실시예를 들어 설명한다.Hereinafter, an embodiment according to the method for extracting minerals from the composite clay mineral according to the present invention will be described.

실시예 1>Example 1

일라이트, 버미큘라이트 및 뮤스코바이트로 이루어진 복합점토광물을 볼밀링 장치를 이용하여 100 메시 크기의 분말로 파쇄하여 형성된 점토광물 분말 20 중량부와 물 80 중량부를 혼합하여 혼합물을 형성한다.A composite clay mineral composed of elite, vermiculite and muscobite is crushed into powder of 100 mesh size using a ball milling device to form a mixture by mixing 20 parts by weight of clay mineral powder and 80 parts by weight of water.

전술한 혼합물에 전극봉을 설치하여 6 볼트의 전극을 5 시간 동안 걸어준 후에 물을 제거하면서 36시간 동안 건조하고, 볼밀링 장치를 이용하여 다시 파쇄한다.The electrode was installed in the mixture described above, and the electrode of 6 volts was hung for 5 hours, dried for 36 hours while removing water, and crushed again using a ball milling device.

파쇄된 점토광물 분말 130 중량부를 황산 80 중량%와 정제수 20 중량%를 혼합하여 제조된 황산용액 300 중량부와 혼합하여 교반한 후에, 고형분을 제거하고 유압필터를 이용하여 1차로 여과하는데, 유압필터를 이용한 여과가 완료되면 고형분은 교반탱크에서 따로 분리한다.130 parts by weight of crushed clay mineral powder was mixed with 300 parts by weight of sulfuric acid solution prepared by mixing 80% by weight of sulfuric acid and 20% by weight of purified water, and then the solids were removed and filtered first using a hydraulic filter. After filtration is completed, the solids are separated from the stirring tank separately.

전술한 유압필터를 이용한 여과가 완료되면 여과액을 멤브레인필터로 이송하여 미세여과하는 2차 여과과정이 이루어진다.When the filtration using the above-mentioned hydraulic filter is completed, a secondary filtration process of transferring the filtrate to the membrane filter and microfiltration is performed.

전술한 과정을 통해 진행하되 교반시간을 2, 12, 24, 48 시간으로 실시했을 경우 추출되는 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.Proceed through the above process, but when the stirring time was carried out for 2, 12, 24, 48 hours, the amount of extraction by type of minerals extracted was measured using ICP-Mass.

실시예 2>Example 2

일라이트, 클로라이트 및 할로이사이트로 이루어진 복합점토광물을 이용하고 나머지 과정은 실시예 1과 동일하게 진행하여 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.The complex clay mineral consisting of elite, chlorite and halosite was used, and the rest of the procedure was carried out in the same manner as in Example 1, and the extraction amount of each mineral was measured using ICP-Mass.

실시예 3>Example 3

일라이트 및 버미큘라이트로 이루어진 복합점토광물을 이용하고 나머지 과정은 실시예 1과 동일하게 진행하여 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.The composite clay mineral consisting of elite and vermiculite was used, and the rest of the procedure was performed in the same manner as in Example 1, and the extraction amount of each mineral was measured using ICP-Mass.

실시예 4>Example 4

일라이트 및 뮤스코바이트로 이루어진 복합점토광물을 이용하고 나머지 과정은 실시예 1과 동일하게 진행하여 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.The composite clay mineral consisting of illite and muscobite was used, and the rest of the procedure was carried out in the same manner as in Example 1, and the extraction amount of each mineral was measured using ICP-Mass.

실시예 5>Example 5

일라이트로 이루어진 복합점토광물을 이용하고 나머지 과정은 실시예 1과 동 일하게 진행하여 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.측정하였다.The composite clay mineral made of elite was used, and the rest of the procedure was performed in the same manner as in Example 1, and the extraction amount of each type of mineral was measured using ICP-Mass.

실시예 6>Example 6

일라이트, 버미큘라이트 및 뮤스코바이트로 이루어진 복합점토광물을 볼밀링 장치를 이용하여 100 메시 크기의 분말로 파쇄하여 형성된 점토광물 분말 20 중량부와 물 80 중량부를 혼합하여 혼합물을 형성한다.A composite clay mineral composed of elite, vermiculite and muscobite is crushed into powder of 100 mesh size using a ball milling device to form a mixture by mixing 20 parts by weight of clay mineral powder and 80 parts by weight of water.

전술한 혼합물에 전극봉을 설치하고 6 볼트의 전극을 5 시간 동안 걸어준 후에 물을 제거하면서 36시간 동안 건조하고, 볼밀링 장치를 이용하여 다시 파쇄한다.The electrode was installed in the above mixture, the electrode of 6 volts was hung for 5 hours, dried for 36 hours while removing water, and crushed again using a ball milling device.

파쇄된 점토광물 분말 130 중량부를 황산과 정제수를 혼합하여 제조된 황산용액 300 중량부와 혼합하여 24시간 동안 교반한 후에, 고형분을 제거하고 유압필터를 이용하여 1차로 여과하는데, 유압필터를 이용한 여과가 완료되면 고형분은 교반탱크에서 따로 분리한다.130 parts by weight of crushed clay mineral powder was mixed with 300 parts by weight of sulfuric acid solution prepared by mixing sulfuric acid and purified water, and stirred for 24 hours, and then the solids were removed and filtered first using a hydraulic filter. When complete, the solids are separated from the agitation tank.

전술한 유압필터를 이용한 여과가 완료되면 여과액을 멤브레인필터로 이송하여 미세여과하는 2차 여과과정이 이루어진다.When the filtration using the above-mentioned hydraulic filter is completed, a secondary filtration process of transferring the filtrate to the membrane filter and microfiltration is performed.

전술한 과정을 통해 진행하되 전술한 정제수와 전술한 황산의 혼합비율이 8:2, 6:4, 5:5, 4:6, 2:8, 0:10으로 정해졌을 때 추출되는 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.Proceed through the process described above, when the mixing ratio of the above-mentioned purified water and the aforementioned sulfuric acid is set to 8: 2, 6: 4, 5: 5, 4: 6, 2: 8, 0:10 The extraction amount was measured using ICP-Mass.

실시예 7>Example 7

일라이트, 버미큘라이트 및 뮤스코바이트로 이루어진 복합점토광물을 볼밀링 장치를 이용하여 100 메시 크기의 분말로 파쇄하여 형성된 점토광물 분말 20 중량부와 물 80 중량부를 혼합하여 형성된 혼합물에 전극봉을 설치하고 6 볼트의 전극을 5 시간 동안 걸어준 후에 물을 제거하면서 36시간 동안 건조하고, 볼밀링 장치를 이용하여 다시 파쇄한다.Electrode rod was installed in the mixture formed by mixing 20 parts by weight of clay mineral powder and 80 parts by weight of water formed by crushing the composite clay mineral composed of elite, vermiculite and muscobite into powder of 100 mesh size using a ball milling device. The electrode of the bolt was walked for 5 hours, dried for 36 hours while removing water, and crushed again using a ball milling device.

파쇄된 점토광물 분말을 황산 20 중량%와 정제수 80 중량%를 혼합하여 제조된 황산용액과 혼합하여 24시간 동안 교반한 후에, 고형분을 제거하고 유압필터를 이용하여 1차로 여과하는데, 유압필터를 이용한 여과가 완료되면 고형분은 교반탱크에서 따로 분리한다.The crushed clay mineral powder was mixed with a sulfuric acid solution prepared by mixing 20% by weight of sulfuric acid and 80% by weight of purified water, stirred for 24 hours, and then the solids were removed and filtered first using a hydraulic filter. Once the filtration is complete, the solids are separated from the stirring tank separately.

전술한 유압필터를 이용한 여과가 완료되면 여과액을 멤브레인필터로 이송하여 미세여과하는 2차 여과과정이 이루어진다.When the filtration using the above-mentioned hydraulic filter is completed, a secondary filtration process of transferring the filtrate to the membrane filter and microfiltration is performed.

전술한 과정을 통해 진행하되 전술한 점토광물 분말과 전술한 황산용액의 혼합비율이 3:7, 5:5, 7:3, 8:2, 9:1로 정해졌을 때 추출되는 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.Proceed through the process described above, when the mixing ratio of the above-mentioned clay mineral powder and the above-mentioned sulfuric acid solution is set to 3: 7, 5: 5, 7: 3, 8: 2, 9: 1 Was measured using ICP-Mass.

실시예 8>Example 8

일라이트, 버미큘라이트 및 뮤스코바이트로 이루어진 복합점토광물을 볼밀링 장치를 이용하여 100 메시 크기의 분말로 파쇄하여 형성된 점토광물 분말 20 중량부와 물 80 중량부를 혼합하여 형성된 혼합물에 전극봉을 설치하고 6 볼트의 전극 을 걸어준 후에 물을 제거하면서 36시간 동안 건조하고, 볼밀링 장치를 이용하여 다시 파쇄한다.Electrode rod was installed in the mixture formed by mixing 20 parts by weight of clay mineral powder and 80 parts by weight of water formed by crushing the composite clay mineral composed of elite, vermiculite and muscobite into powder of 100 mesh size using a ball milling device. Hang the bolt electrode, dry for 36 hours while removing water, and crush again using a ball milling device.

파쇄된 점토광물 분말 130 중량부를 황산 20 중량%와 정제수 80 중량%를 혼합하여 제조된 황산용액 300 중량부와 혼합하여 24 시간동안 교반한 후에, 고형분을 제거하고 유압필터를 이용하여 1차로 여과하는데, 유압필터를 이용한 여과가 완료되면 고형분은 교반탱크에서 따로 분리한다.130 parts by weight of the crushed clay mineral powder was mixed with 300 parts by weight of sulfuric acid solution prepared by mixing 20% by weight of sulfuric acid and 80% by weight of purified water, and then stirred for 24 hours, and then the solids were removed and filtered first using a hydraulic filter. When the filtration using the hydraulic filter is completed, the solids are separated from the stirring tank.

전술한 유압필터를 이용한 여과가 완료되면 여과액을 멤브레인필터로 이송하여 미세여과하는 2차 여과과정이 이루어진다.When the filtration using the above-mentioned hydraulic filter is completed, a secondary filtration process of transferring the filtrate to the membrane filter and microfiltration is performed.

전술한 과정을 통해 진행하되 전술한 6볼트의 전극을 걸어주는 시간이 0(미자극), 1, 3, 5시간으로 정해졌을 때 추출되는 미네랄의 종류별 추출량을 ICP-Mass를 이용하여 측정하였다.Proceed through the process described above, when the time for applying the 6-volt electrode is set to 0 (unstimulated), 1, 3, 5 hours, the extraction amount of each type of mineral to be extracted was measured using ICP-Mass.

전술한 실시예 1 내지 실시예 5의 과정으로 추출된 미네랄의 추출량을 표 1에 정리하였다.Table 1 summarizes the extraction amounts of the minerals extracted by the above-described Examples 1 to 5.

표 1>Table 1>

Figure 112008026834713-pat00001
Figure 112008026834713-pat00001

표 1에 나타낸 종류별 미네랄 추출량을 보면 일라이트, 버미큘라이트 및 뮤스코바이트로 이루어진 복합점토광물을 사용했을 경우에 가장 많은 미네랄 추출되었으며, 교반시간으로는 24시간을 교반했을 경우에 가장 많은 미네랄이 추출됐다.According to the amount of mineral extraction by type shown in Table 1, the most minerals were extracted when the complex clay minerals consisting of illite, vermiculite and muscobite were used, and the most minerals were extracted when stirring for 24 hours. .

전술한 실시예 6의 과정으로 추출된 미네랄의 추출량을 표 2에 정리하였다.Table 2 summarizes the extraction amounts of the minerals extracted by the above-described Example 6.

표 2>Table 2>

Figure 112008026834713-pat00002
Figure 112008026834713-pat00002

표 2에 나타낸 것처럼 정제수와 황산용액의 혼합비가 2:8일때 가장 많은 미네랄이 추출됐다.As shown in Table 2, the most minerals were extracted when the mixing ratio of purified water and sulfuric acid solution is 2: 8.

전술한 실시예 7의 과정으로 추출된 미네랄의 추출량을 표 3에 정리하였다.Table 3 summarizes the extraction amounts of the minerals extracted by the above-described Example 7.

표 3>Table 3>

Figure 112008026834713-pat00003
Figure 112008026834713-pat00003

표 3에 나타낸 것처럼 황산용액과 점토광물 분말의 혼합비율이 7:3일때 가장 많은 미네랄이 추출됐다.As shown in Table 3, the most minerals were extracted when the mixing ratio of sulfuric acid solution and clay mineral powder was 7: 3.

전술한 실시예 8의 과정으로 추출된 미네랄의 추출량을 표 4에 정리하였다.Table 4 summarizes the extraction amounts of the minerals extracted by the above-described Example 8.

표 4>Table 4>

Figure 112008026834713-pat00004
Figure 112008026834713-pat00004

표 4에 나타낸 것처럼 전극을 걸어주는 시간이 5시간일때 가장 많은 미네랄이 추출됐다.As shown in Table 4, the most minerals were extracted when the electrode was applied for 5 hours.

도 1은 본 발명의 따른 복합점토광물로부터 미네랄을 추출하는 방법을 도시한 순서도.1 is a flow chart illustrating a method for extracting minerals from the composite clay mineral according to the present invention.

Claims (5)

복합점토광물로부터 미네랄을 추출하는 방법에 있어서,In the method of extracting minerals from complex clay minerals, 일라이트, 뮤스코바이트, 클로라이트, 버미큘라이트 및 할로이사이트로 이루어진 그룹으로부터 선택된 하나 이상을 포함하여 이루어지는 복합점토광물을 파쇄하는 점토광물파쇄단계;A clay mineral crushing step of crushing a complex clay mineral including at least one selected from the group consisting of illite, muscobite, chlorite, vermiculite, and halosite; 상기 점토광물파쇄단계를 거쳐 형성된 점토광물 분말이 전기분해장치를 통과하는 전기분해처리단계;An electrolytic treatment step in which the clay mineral powder formed through the clay mineral crushing step passes through an electrolysis device; 상기 전기분해처리단계를 거친 점토광물 분말을 황산용액과 교반하는 황산용액처리단계; 및 Sulfuric acid solution treatment step of stirring the clay mineral powder after the electrolytic treatment step with sulfuric acid solution; And 상기 황산용액처리단계를 거쳐 형성된 혼합물을 유압필터에서 1차 여과하고 멤브레인필터에서 2차로 여과하는 필터여과단계;를 포함하여 이루어지며,And a filter filtration step of first filtering the mixture formed through the sulfuric acid solution treatment step in a hydraulic filter and secondly in a membrane filter. 상기 미네랄은 나트륨, 철, 칼륨, 마그네슘, 알루미늄, 망간, 규소, 칼슘, 아연 및 티타늄으로 이루어진 그룹으로부터 선택된 하나 이상으로 이루어지는 것을 특징으로 하는 복합점토광물로부터 미네랄을 추출하는 방법.Wherein said mineral is at least one selected from the group consisting of sodium, iron, potassium, magnesium, aluminum, manganese, silicon, calcium, zinc and titanium. 청구항 1에 있어서,The method according to claim 1, 상기 황산용액처리단계는 황산 20 내지 80중량%와 정제수 20 내지 80중량%를 혼합하여 제조된 황산용액 100 내지 500 중량부를 상기 점토광물 분말에 혼합하여 2 내지 24시간 교반한 후에, 고형분을 제거하는 과정을 포함하여 이루어지는 것을 특징으로 하는 복합점토광물로부터 미네랄을 추출하는 방법.The sulfuric acid solution treatment step is to mix 100 to 500 parts by weight of sulfuric acid solution prepared by mixing 20 to 80% by weight of sulfuric acid and 20 to 80% by weight of purified water to the clay mineral powder and stirred for 2 to 24 hours, to remove the solid content Method of extracting minerals from the composite clay mineral, characterized in that comprises a process. 삭제delete 삭제delete 삭제delete
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200047210A (en) 2018-10-26 2020-05-07 안형일 Liquid mineral feed additives and manufacturing method of thereof
KR102140217B1 (en) * 2020-01-30 2020-07-31 구동찬 Preparation method of activated mineral solution

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102625331B1 (en) * 2021-03-18 2024-01-18 주식회사 더말코리아 Composite for antibacterial and deodorant agent using ionized minerals and persimmon leaf extract and other natural materials

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992007796A1 (en) * 1990-10-30 1992-05-14 Takagi Keiji Method of fractionizing water molecule cluster, water-soluble mineral containing solution used for this fractionizing method and method of producing the mineral containing solution
KR100197168B1 (en) 1995-05-11 1999-06-15 황도성 Method for extracting poisonous character from a material
KR20030008746A (en) * 2001-07-19 2003-01-29 최연수 Manufacturing method of water treatment agent using mineral
JP2008062218A (en) 2006-09-11 2008-03-21 Ikeda Mago Sekizai:Kk Method and apparatus for extracting mineral water and clay particle from porous basaltic andesite

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992007796A1 (en) * 1990-10-30 1992-05-14 Takagi Keiji Method of fractionizing water molecule cluster, water-soluble mineral containing solution used for this fractionizing method and method of producing the mineral containing solution
KR100197168B1 (en) 1995-05-11 1999-06-15 황도성 Method for extracting poisonous character from a material
KR20030008746A (en) * 2001-07-19 2003-01-29 최연수 Manufacturing method of water treatment agent using mineral
JP2008062218A (en) 2006-09-11 2008-03-21 Ikeda Mago Sekizai:Kk Method and apparatus for extracting mineral water and clay particle from porous basaltic andesite

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200047210A (en) 2018-10-26 2020-05-07 안형일 Liquid mineral feed additives and manufacturing method of thereof
KR102140217B1 (en) * 2020-01-30 2020-07-31 구동찬 Preparation method of activated mineral solution
JP2021120339A (en) * 2020-01-30 2021-08-19 ク,ドンチャン Production method of activated mineral solution
JP7076597B2 (en) 2020-01-30 2022-05-27 ク,ドンチャン Manufacturing method of activated mineral solution
US11897824B2 (en) 2020-01-30 2024-02-13 Dong Chan Koo Method of preparing activated mineral solution

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