KR102389951B1 - Method for concentration of sea water - Google Patents

Method for concentration of sea water Download PDF

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KR102389951B1
KR102389951B1 KR1020210113619A KR20210113619A KR102389951B1 KR 102389951 B1 KR102389951 B1 KR 102389951B1 KR 1020210113619 A KR1020210113619 A KR 1020210113619A KR 20210113619 A KR20210113619 A KR 20210113619A KR 102389951 B1 KR102389951 B1 KR 102389951B1
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seawater
concentrated
salinity
absorbent member
sea water
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KR1020210113619A
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Korean (ko)
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박규식
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박규식
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Priority to KR1020210113619A priority Critical patent/KR102389951B1/en
Priority to PCT/KR2021/012351 priority patent/WO2023027231A1/en
Priority to GBGB2313120.4A priority patent/GB202313120D0/en
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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
    • A23L27/00Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/40Table salts; Dietetic salt substitutes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/30Accessories for evaporators ; Constructional details thereof
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D3/00Halides of sodium, potassium or alkali metals in general
    • C01D3/04Chlorides
    • C01D3/06Preparation by working up brines; seawater or spent lyes
    • 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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • 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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/043Details
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2300/00Processes
    • A23V2300/10Drying, dehydrating
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2300/00Processes
    • A23V2300/50Concentrating, enriching or enhancing in functional factors
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Abstract

The present invention relates to an evaporation field structure of a novel configuration capable of concentrating sea water to a desired salinity level in a relatively short time, thereby producing concentrated sea water in an economical manner, and to a sea water concentration method of a novel type using the same. According to the present invention, provided is an evaporation field structure and a sea water concentration method using the same, wherein in an evaporation field for concentrating sea water by natural evaporation, an absorbent member (12) is installed on the bottom of the evaporation field (10). Accordingly, when sea water supplied to the evaporation field (10) is naturally evaporated and concentrated, the absorbent member (12) is salted in the concentrated sea water. As such, when concentrated sea water is discharged to the outside and sea water is newly supplied to the evaporation field (10), the salinity of the newly supplied sea water is increased by the salted absorbent member (12).

Description

해수 농축방법{Method for concentration of sea water}Method for concentration of sea water

본 발명은 증발지 구조 및 이를 이용한 해수 농축방법에 관한 것으로서, 보다 상세하게는 상대적으로 단 시간에 해수를 원하는 수준의 염도로 농축할 수 있는 새로운 구성의 증발지 구조 및 이를 이용한 해수 농축방법에 관한 것이다. The present invention relates to an evaporator structure and a seawater concentration method using the same, and more particularly, to a new evaporator structure capable of concentrating seawater to a desired level of salinity in a relatively short time, and a seawater concentration method using the same will be.

일반적으로 천일염을 생산하는 염전은 해수를 저장하는 저수지와, 저수지로부터 해수를 공급받아 해수를 자연증발시켜서 농축시키는 증발지와, 증발지에서 농축된 해수를 추가로 증발시켜서 소금결정을 만드는 결정지로 구성된다.In general, salt fields that produce sea salt are composed of a reservoir that stores seawater, an evaporator that receives seawater from the reservoir and naturally evaporates the seawater to concentrate it, and a crystalline pond that additionally evaporates the concentrated seawater in the evaporator to make salt crystals. do.

천일염은 해수를 이러한 염전에서 점차적으로 농축시켜서 생산되는데, 통상적으로 해수가 염도 23~25% 정도로 농축되었을 때부터 소금이 결정화되며, 해수를 염도 23~25% 정도로 농축시키기 위해서는 22~23일 정도의 상당히 긴 시간이 소요되고, 최종적으로 천일염을 얻기 까지는 대략 25일 정도가 소요된다. Sea salt is produced by gradually concentrating seawater in these salt fields. Usually, salt crystallizes when seawater is concentrated to about 23-25% salinity. It takes quite a long time, and it takes about 25 days to finally obtain sea salt.

이와 같이 해수를 농축시키는데, 상당히 긴 시간이 소요되므로 천일염의 생산성이 상당히 낮으며, 천일염의 생산성을 높이기 위해서는 상대적으로 넓은 면적의 증발지가 요구되는데, 이러한 요소들로 인해 천일염의 경제성은 상당히 낮은 수준이다. As such, it takes a very long time to concentrate seawater, so the productivity of sea salt is quite low. .

대한민국 등록특허 제10-1704179호(2017. 02. 01)Republic of Korea Patent Registration No. 10-1704179 (2017. 02. 01) 대한민국 등록특허 제10-1319835호(2013. 10. 07)Republic of Korea Patent Registration No. 10-1319835 (2013. 10. 07) 대한민국 공개특허 제10-2020-0120141호(2020. 10. 21)Republic of Korea Patent Publication No. 10-2020-0120141 (2020. 10. 21) 대한민국 공개특허 제10-2020-0049634호(2020. 05. 08)Republic of Korea Patent Publication No. 10-2020-0049634 (2020. 05. 08) 대한민국 등록특허 제10-1253500호(2013. 04. 05)Republic of Korea Patent Registration No. 10-1253500 (2013. 04. 05)

본 발명은 상기와 같은 점에 착안하여 제안된 것으로서, 상대적으로 단 시간에 해수를 원하는 수준의 염도로 농축할 수 있어서 농축 해수를 경제적으로 생산할 수 있는 새로운 구성의 증발지 구조 및 이를 이용한 새로운 방식의 해수 농축방법을 제공하는 것이다.The present invention has been proposed in view of the above points, and it is possible to concentrate seawater to a desired level of salinity in a relatively short time, so that it is possible to economically produce concentrated seawater with a new structure of an evaporator structure and a new method using the same. It is to provide a method of concentrating seawater.

본 발명의 특징에 따르면, 해수를 자연증발시켜서 농축시키는 증발지에 있어서, 상기 증발지(10)의 바닥에는 흡수성 부재(12)가 설치되어, 상기 증발지(10)로 급수된 해수가 자연증발되어 농축되면 상기 흡수성 부재(12)가 농축된 해수에 염장되어, 농축된 해수를 외부로 배출시킨 다음 증발지(10)에 해수를 새로 급수시키면 새로 급수된 해수의 염도가 상기 염장된 흡수성 부재(12)에 의해 상승되는 것을 특징으로 하는 증발지 구조가 제공된다.According to a feature of the present invention, in an evaporator for naturally evaporating and concentrating seawater, an absorbent member 12 is installed at the bottom of the evaporator 10 so that the seawater supplied to the evaporator 10 is naturally evaporated. When concentrated, the absorbent member 12 is salted in the concentrated seawater, and after discharging the concentrated seawater to the outside, when seawater is newly supplied to the evaporator 10, the salinity of the freshly supplied seawater is changed to the salted absorbent member 12 ) is provided with an evaporator structure characterized in that it is raised by.

본 발명의 다른 특징에 따르면, 상기 흡수성 부재(12)는 천, 부직포, 스펀지, 로프, 직조매트 중에서 어느 하나로 이루어진다. According to another feature of the present invention, the absorbent member 12 is made of any one of a cloth, a non-woven fabric, a sponge, a rope, and a woven mat.

본 발명의 또 다른 특징에 따르면, 상기 흡수성 부재(12)는 코어매트(coir mat), 황마매트, 아바카매트(abaca mat) 중에서 어느 하나로 이루어진다.According to another feature of the present invention, the absorbent member 12 is made of any one of a core mat (coir mat), jute mat, abaca mat (abaca mat).

본 발명의 또 다른 특징에 따르면, 바닥에 흡수성 부재가 깔린 증발지에 해수를 급수하는 제1단계; 상기 증발지에 급수된 해수를 자연증발시켜서 소요되는 수준으로 농축시키고, 상기 흡수성 부재가 농축된 해수에 염장되도록 하는 제2단계;According to another feature of the present invention, the first step of supplying seawater to the evaporator with an absorbent member on the bottom; a second step of concentrating the seawater supplied to the evaporator to a required level by natural evaporation, and allowing the absorbent member to be salted in the concentrated seawater;

상기 제2단계에서 농축된 해수를 외부로 배출시키는 제3단계; 해수를 상기 증발지에 새로 급수하는 제4단계; 상기 제4단계에서 새로 급수된 해수를 자연증발시켜서 소요되는 수준으로 농축시키는 제5단계; 및 상기 제5단계에서 농축된 해수를 외부로 배출시키는 제6단계;를 포함하며, 상기 제4단계에서는 새로 급수된 해수의 염도가 상기 제2단계에서 농축된 해수에 염장된 흡수성 부재에 의해 상승되는 것을 특징으로 하는 해수 농축방법이 제공된다. a third step of discharging the seawater concentrated in the second step to the outside; a fourth step of newly supplying seawater to the evaporator; a fifth step of naturally evaporating the freshly supplied seawater in the fourth step and concentrating it to a required level; and a sixth step of discharging the seawater concentrated in the fifth step to the outside; in the fourth step, the salinity of the freshly supplied seawater is increased by the absorbent member salted in the seawater concentrated in the second step There is provided a seawater concentration method, characterized in that it becomes.

이상과 같은 구성을 가지는 본 발명은 증발지에 흡수성 부재를 깔고, 일차적으로 해수를 농축시켜서 흡수성 부재를 농축 해수로 염장시킨 다음, 증발지에 해수를 급수함으로써 증발지에 급수된 해수의 염도가 농축 해수로 염장된 흡수성 부재에 의해 상승된다. 이와 같이 증발지로 급수된 해수의 염도가 별도의 자연증발과정을 거치지 않고 자동적으로 상승되므로 해수를 상대적으로 빨리 농축시킬 수 있다.In the present invention having the above configuration, an absorbent member is laid on an evaporator, seawater is first concentrated, and the absorbent member is salted with concentrated seawater, and then the salinity of the seawater supplied to the evaporator is salted with concentrated seawater by supplying seawater to the evaporator. It is raised by an absorbent member. As described above, the salinity of the seawater supplied to the evaporation site is automatically increased without going through a separate natural evaporation process, so that the seawater can be concentrated relatively quickly.

따라서 상대적으로 단시간에 해수를 소요되는 수준의 염도로 농축시킬 수 있으므로 좀 더 경제적으로 농축 해수를 제조할 수 있다.Therefore, since seawater can be concentrated to a required level of salinity in a relatively short time, concentrated seawater can be manufactured more economically.

도 1은 본 발명의 바람직한 실시예에 따른 증발지의 사진
도 2는 상기 실시예에서 사용된 흡수성 부재 사진
1 is a photograph of an evaporator according to a preferred embodiment of the present invention;
2 is a photograph of the absorbent member used in the above embodiment;

먼저, 본 발명의 장점 및 특징, 그리고 그것들을 달성하는 방법은 첨부되는 도면과 함께 상세하게 후술되어지는 실시예들을 참조하면 명확해질 것이다. 여기에서, 본 발명은 이하에서 개시되는 실시예들에 한정되는 것이 아니라 서로 다른 다양한 형태로 구현될 수 있으며, 단지 본 실시예들은 본 발명의 개시가 완전하도록 하고, 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자가 발명의 범주를 명확하게 이해할 수 있도록 하기 위해 예시적으로 제공되는 것이므로, 본 발명의 기술적 범위는 청구항들에 의해 정의되어야 할 것이다.First, the advantages and features of the present invention, and a method for achieving them will become clear with reference to the embodiments described below in detail in conjunction with the accompanying drawings. Here, the present invention is not limited to the embodiments disclosed below, but may be implemented in a variety of different forms, and only these embodiments allow the disclosure of the present invention to be complete, and are common in the technical field to which the present invention pertains. Since it is provided by way of example so that those with knowledge of the present invention can clearly understand the scope of the invention, the technical scope of the present invention should be defined by the claims.

아울러, 아래의 본 발명을 설명함에 있어서 공지 기능 또는 구성 등에 대한 구체적인 설명이 본 발명의 요지를 불필요하게 흐릴 수 있다고 판단되는 경우에는 그 상세한 설명을 생략할 것이다. 그리고, 후술되는 용어들은 본 발명에서의 기능을 고려하여 정의된 용어들인 것으로, 이는 사용자, 운용자 등의 의도 또는 관례 등에 따라 달라질 수 있음은 물론이다. 그러므로, 그 정의는 본 발명의 설명 전반에 걸쳐 기술되는 기술사상을 토대로 이루어져야 할 것이다.In addition, in the following description of the present invention, if it is determined that a detailed description of a well-known function or configuration may unnecessarily obscure the gist of the present invention, the detailed description thereof will be omitted. And, the terms to be described later are terms defined in consideration of functions in the present invention, which may vary depending on the intentions or customs of users, operators, etc., of course. Therefore, the definition should be made based on the technical idea described throughout the description of the present invention.

이하, 첨부된 도면을 참조하여 본 발명의 바람직한 실시예에 대하여 상세하게 설명한다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도 1, 2는 본 발명의 바람직한 실시예의 사진이다. 본 발명은 해수를 농축시키기 위한 증발지에 관한 것으로서, 도시된 바와 같이, 증발지(10)에는 흡수성 부재(12)가 설치된다. 통상적으로 증발지는 바닥에 비닐장판이나 타일 등이 깔리는데, 본 발명에 의한 증발지(10)는 이러한 통상의 증발지에 흡수성 부재(12)가 추가로 설치되는 것이다.1 and 2 are photographs of a preferred embodiment of the present invention. The present invention relates to an evaporator for concentrating seawater, and as shown, an absorbent member 12 is installed in the evaporator 10 . In general, the evaporator is covered with a vinyl sheet or tiles on the floor, and in the evaporator 10 according to the present invention, the absorbent member 12 is additionally installed in the conventional evaporator.

상기 흡수성 부재(12)는 증발지에 급수된 해수를 흡수할 수 있는 소재로 이루어지는데, 흡수성 부재(12)는 소재 자체가 흡수성을 가지거나 또는 조직에 형성된 기공을 통해 흡수성을 가지는 다양한 종류의 소재로 이루어진다. 이러한 흡수성 부재(12)는 사용가능한 종류가 특별히 한정되지 않으나, 사용이 바람직한 몇 가지를 예시하면, 천, 부직포, 스펀지, 로프(rope), 직조매트 등을 예로 들 수 있다. 상기 로프는 볏짚, 코코넛 껍질, 마, 바나나껍질. 옥수수대, 보릿대 등의 식물성 섬유나 합성섬유로 이루어진 것이고, 직조매트로는 상기와 같은 로프나 천이나 부직포 등으로 직조된 것이다. The absorbent member 12 is made of a material capable of absorbing seawater supplied to the evaporator, and the absorbent member 12 is made of various types of materials that either have absorbency in themselves or have absorbency through pores formed in the tissue. is done The type of the absorbent member 12 that can be used is not particularly limited, but examples of some preferable examples include cloth, nonwoven fabric, sponge, rope, woven mat, and the like. The rope is rice straw, coconut shells, hemp, banana peels. It is made of vegetable fibers or synthetic fibers such as corn stalks and barley stalks, and the woven mat is woven with the same rope, cloth, or non-woven fabric as described above.

이러한 흡수성 부재(12)는 증발지(10) 바닥에 깔리는데, 흡수성 부재(12)가 천이나 부직포 등의 비교적 얇은 시트로 이루어지는 경우에는 천이나 부직포를 편편하게 펼쳐서 깔기 보다는 여러 겹으로 접거나 주름지게 깔아서 후술하는 바와 같이, 천이나 부직포가 해수를 상대적으로 많이 흡수하여 염장될 수 있도록 한다. 그리고 흡수성 부재(12)로 로프가 사용되는 경우에는 로프를 말거나 구부려서 로프가 증발지(10) 바닥을 전체적으로 덮을 수 있도록 한다. The absorbent member 12 is spread on the bottom of the evaporation paper 10, and when the absorbent member 12 is made of a relatively thin sheet such as cloth or nonwoven fabric, it is folded or wrinkled in several layers rather than spread out flat. As described later, the cloth or nonwoven fabric absorbs a relatively large amount of seawater so that it can be salted. And when a rope is used as the absorbent member 12, the rope is rolled or bent so that the rope can cover the entire bottom of the evaporation paper 10.

전술한 바와 같이, 흡수성 부재(12)로 사용가능한 종류가 특별히 한정되지는 않으나, 바람직하게는 흡수성 부재(12)로 직조매트가 사용된다. 흡수성 부재(12)로 직조매트를 사용하면 흡수성 부재(12)를 증발지(10)에 설치하기도 용이할 뿐만 아니라, 매트의 두께가 상당히 두툼하여 농축된 해수를 충분히 흡수하여 효과적으로 염장되기 때문이다. As described above, the types that can be used as the absorbent member 12 are not particularly limited, but a woven mat is preferably used as the absorbent member 12 . When the woven mat is used as the absorbent member 12, it is not only easy to install the absorbent member 12 in the evaporator 10, but also because the thickness of the mat is quite thick enough to absorb the concentrated seawater and effectively salt it.

흡수성 부재(12)로 특히 사용이 바람직한 직조매트로는 코코넛껍질로 만든 코어매트(coir mat), 황마((jute))로 만든 황마매트, 마닐라삼으로 만든 아바카매트(abaca mat) 등을 예로 들 수 있다. 이러한 종류의 흡수성 매트들은 인체에 무해하고 환경오염을 일으키지 않으므로 환경친화적이며, 흡습성 및 강도가 강하며, 침수하여도 잘 부패되지 않는 장점을 가진다. As a woven mat particularly preferable to be used as the absorbent member 12, for example, a core mat made of coconut shell, a jute mat made of jute, an abaca mat made of manila hemp, etc. can This type of absorbent mat is harmless to the human body and does not cause environmental pollution, so it is environmentally friendly, has strong hygroscopicity and strength, and is not easily corrupted even when submerged.

본 발명에 의한 증발지(10)는 바닥에 이러한 흡수성 부재(12)가 깔려 있기 때문에 이러한 증발지(10)에서 해수를 자연증발시켜서 농축시키면, 농축된 해수가 흡수성 부재(12)에 흡수되어 흡수성 부재(12)가 염장된다. Since the evaporator 10 according to the present invention has such an absorbent member 12 on the bottom, when the seawater is naturally evaporated and concentrated in the evaporator 10, the concentrated seawater is absorbed by the absorbent member 12 to absorb The member 12 is salted.

이와 같이 흡수성 부재(12)가 염장된 상태이므로 농축된 해수를 외부로 배출시키고, 증발지(10)에 새로 해수를 급수하면, 새로 급수된 해수와 농축된 해수로 염장된 흡수성 부재(12) 사이에 일종의 삼투현상이 발생되어 새로 급수된 해수와 흡수성 부재(12) 사이에 염도의 균일화가 진행되어 흡수성 부재(12)의 염도는 낮아지는 대신에 해수의 염도는 상승된다. In this way, since the absorbent member 12 is in a salted state, the concentrated seawater is discharged to the outside, and when seawater is newly supplied to the evaporator 10, between the absorbent member 12 salted with the newly supplied seawater and the concentrated seawater. A kind of osmosis phenomenon occurs in the salinity between the freshly supplied seawater and the absorbent member 12, so that the salinity of the absorbent member 12 is lowered, but the salinity of the seawater is increased.

이와 같이 농축된 해수로 염장된 흡수성 부재(12)에 의해 새로 급수된 해수 염도가 자연증발에 의하지 않고 자동적으로 상승되므로 해수를 소요되는 수준의 염도로 농축시키는데 걸리는 시간이 단축된다. 즉, 해수를 좀 더 신속하게 농축시킬 수 있는 것이다. Since the salinity of the freshly supplied seawater is automatically increased by the absorbent member 12 salted with the concentrated seawater as described above, the time taken for concentrating the seawater to a required level of salinity is shortened. That is, seawater can be concentrated more quickly.

이하에서, 이러한 구성의 증발지를 이용하여 해수를 농축하는 방법에 대해 살펴본다.Hereinafter, a method of concentrating seawater using an evaporator having such a configuration will be described.

1) 제1단계1) Step 1

저수지에 저장된 해수를 양수하여 흡수성 부재(12)가 깔린 증발지(10)에 급수한다. 이때 도 1 및 도 2에 게시된 바와 같이, 증발지(10)에 깔린 흡수성 부재(12)의 상단부가 조금 노출될 정도로 해수를 급수한다. 본 실시예에서는 흡수성 부재(12)가 코어매트로 이루어진 것으로 예시되었다.The seawater stored in the reservoir is pumped and water is supplied to the evaporator 10 on which the absorbent member 12 is laid. At this time, as shown in FIGS. 1 and 2 , seawater is supplied to such an extent that the upper end of the absorbent member 12 laid on the evaporator 10 is slightly exposed. In this embodiment, the absorbent member 12 is exemplified as being made of a core mat.

2) 제2단계2) Step 2

증발지(10)로 급수된 해수를 자연증발시켜서 농축시킨다. 해수가 농축됨에 따라 흡수성 부재(12)는 농축된 해수에 염장된다. 농축된 해수로 천일염을 제조하는 경우에는 20일 정도 자연증발시켜서 해수를 염도 24~25%로 농축시킨다. The seawater supplied to the evaporator 10 is naturally evaporated and concentrated. As the seawater is concentrated, the absorbent member 12 is salted in the concentrated seawater. In the case of producing sea salt with concentrated seawater, it is evaporated naturally for about 20 days to concentrate the seawater to a salinity of 24 to 25%.

3) 제3단계 3) Step 3

증발지(10)의 농축된 해수를 외부로 배출시킨다. 증발지(10)의 농축된 해수가 배출시키더라도 흡수성 부재(12)는 농축된 해수에 염장된 상태가 유지된다. Concentrated seawater in the evaporator 10 is discharged to the outside. Even if the concentrated seawater of the evaporator 10 is discharged, the absorbent member 12 is maintained in a salted state in the concentrated seawater.

4) 제4단계4) Step 4

증발지(10)에 해수를 새로 급수한다. 본 단계에서도 흡수성 부재(12)의 상단부가 조금 노출될 정도로 해수를 급수한다. Seawater is newly supplied to the evaporator 10 . Even in this step, seawater is supplied to such an extent that the upper end of the absorbent member 12 is slightly exposed.

증발지(10)에 해수를 새로 급수하면 앞에서도 언급한 바와 같이, 새로 급수된 해수와 농축된 해수로 염장된 흡수성 부재(12) 사이에 일종의 삼투현상이 발생되어 염장된 흡수성 부재(12)의 염도가 낮아지는 대신에 해수의 염도가 상승된다. 실험에 의하면, 흡수성 부재(12)가 24~25% 염도로 농축된 해수로 염장된 경우에 염도 2~2.3%의 해수를 급수하면 해수의 염도가 18~22% 정도로 자동적으로 상승된다. When seawater is newly supplied to the evaporator 10, a kind of osmosis occurs between the freshly supplied seawater and the absorbent member 12 salted with concentrated seawater, as mentioned above, Instead of decreasing the salinity, the salinity of seawater increases. According to the experiment, when the absorbent member 12 is salted with seawater concentrated to a salinity of 24 to 25%, when seawater having a salinity of 2 to 2.3% is supplied, the salinity of the seawater is automatically increased to about 18 to 22%.

5) 제5단계5) Step 5

증발지(10)로 급수된 해수를 자연증발시켜서 원하는 염도로 농축시킨다. 천일염 또는 천일식제조소금을 생산하는 경우에는 해수를 24~25%의 염도를 가지도록 농축시킨다. The seawater supplied to the evaporator 10 is naturally evaporated and concentrated to a desired salinity. In the case of producing sea salt or sea salt, the seawater is concentrated to have a salinity of 24 to 25%.

제4단계에서 새로 급수된 해수의 염도가 염장된 흡수성 부재(12)에 의해 상승된 상태이므로 상대적으로 짧은 시간에 해수를 원하는 염도로 농축시킬 수 있다.Since the salinity of the freshly supplied seawater in the fourth step is elevated by the salted absorbent member 12, the seawater can be concentrated to a desired salinity in a relatively short time.

상기 제1단계에서는 해수를 염도 24~25%로 농축시킬 때 20일 정도 소요되었으나, 제4단계에서는 해수가 증발지(10)로 급수되면서 염도가 자동적으로 18~22%로 높아진 상태이므로 20일 보다 상당히 짧은 시간에 해수를 염도 24~25%로 농축시킬 수 있는 것이다. 실험에 의하면 염도 18~22%의 해수를 2~5일 정도 자연증발시키면 해수를 염도 24~25%로 농축시킬 수 있다. In the first step, it took about 20 days to concentrate the seawater to a salinity of 24 to 25%, but in the fourth step, the salinity is automatically increased to 18 to 22% as the seawater is supplied to the evaporation pond 10, so 20 days It is possible to concentrate seawater to a salinity of 24 to 25% in a significantly shorter time. According to the experiment, if seawater with a salinity of 18 to 22% is evaporated naturally for 2 to 5 days, the seawater can be concentrated to a salinity of 24 to 25%.

6) 제6단계6) Step 6

상기 제5단계에서 농축된 해수를 외부로 배출시킨다.The seawater concentrated in the fifth step is discharged to the outside.

한편, 증발지(10)에서 배출된 농축 해수는 천일염 또는 천일식제조소금, 액상 소금의 원료 또는 수소제조용 전해질 등 다양한 용도로 사용되는데, 사용되는 용도에 따라 적절한 방법으로 후처리된다.On the other hand, the concentrated seawater discharged from the evaporator 10 is used for various purposes, such as sea salt or sea salt, a raw material for liquid salt, or an electrolyte for hydrogen production, and is post-treated in an appropriate way according to the use.

예를 들어 농축 해수로 천일염 또는 천일식제조소금을 만드는 경우에는 농축 해수를 추가적으로 자연증발시켜서 소금을 석출시킨다. 그리고 농축 해수의 불순물을 여과하여 제거시켜서 액상 소금의 원료로 사용하거나 또는 수소제조용 전해질로 사용한다. For example, in the case of making sea salt or salt produced by sea salt with concentrated seawater, the concentrated seawater is additionally evaporated to precipitate salt. Then, impurities in the concentrated seawater are filtered out and used as a raw material for liquid salt or as an electrolyte for hydrogen production.

7) 제4단계~제6단계 반복7) Repeat steps 4 to 6

상기 제4단계~제6단계를 반복하여 농축 해수를 반복적으로 생산한다. Repeat steps 4 to 6 to repeatedly produce concentrated seawater.

실험예 1Experimental Example 1

6m×1m 면적의 증발지 바닥에 코어매트를 깔고, 염도 2%의 해수 200ℓ를 급수하여 자연증발시켜서 해수를 농축시키되, 매일 해수를 50~100ℓ씩 보충하면서20일 동알 해수를 농축시켰다. 남은 농축 해수는 100ℓ 였으며, 염도는 24% 이였다.A core mat was laid on the bottom of the 6m × 1m evaporator, and 200 liters of seawater with a salinity of 2% was supplied, and the seawater was concentrated by natural evaporation. The remaining concentrated seawater was 100ℓ, and the salinity was 24%.

농축 해수를 외부로 배출시키고, 증발지에 염도 2%의 해수 200ℓ를 새로 급수하였다. 증발지에 급수된 해수의 염도를 측정한 결과 해수의 염도는 20% 이였다. 이와 같이 새로 급수된 해수의 염도가 20%로 상승된 것은 농축 해수로 염장된 코어매트에 의한 것임을 짐작할 수 있다. Concentrated seawater was discharged to the outside, and 200 liters of seawater having a salinity of 2% was newly supplied to the evaporation pond. As a result of measuring the salinity of the seawater supplied to the evaporator, the salinity of the seawater was 20%. It can be inferred that the increase in the salinity of the freshly supplied seawater to 20% is due to the core mat salted with the concentrated seawater.

이어서 해수를 3일 동안 자연증발시켜서 농축시킨 다음, 농축 해수의 염도를 측정하였다. 농축 해수의 염도는 24% 이였다. 농축 해수를 결정지로 보내서 3일 동안 추가로 자연증발시켜서 천일염을 수확하였다. Then, the seawater was concentrated by natural evaporation for 3 days, and then the salinity of the concentrated seawater was measured. The salinity of the concentrated seawater was 24%. Seawater was harvested by sending concentrated seawater to the crystallizer and allowing it to evaporate naturally for 3 days.

이와 같이 실험예 1에서는 해수를 3일 동안 자연증발시켜서 염도 24%의 농축 해수를 제조하였으며, 농축 해수를 추가로 3일 더 자연증발시켜서 최종적으로 6일 만에 천일염을 수확하였다. 본 실험예와 같이 3일 간격으로 해수 농축과 소금 결정이 반복적으로 이루어 질 경우 3일 간격으로 소금이 생산이 가능하게 된다. As such, in Experimental Example 1, seawater was naturally evaporated for 3 days to produce concentrated seawater having a salinity of 24%, and the concentrated seawater was naturally evaporated for an additional 3 days to finally harvest sea salt in 6 days. As in this experimental example, when seawater concentration and salt crystallization are repeatedly performed at intervals of 3 days, salt production is possible at intervals of 3 days.

본 발명을 이용하면 평균적으로 3~5일 정도면 천일염을 수확할 수 있는데, 통상적으로 천일염 수확에 25일 정도 소요된다는 점을 고려할 때 본 발명을 이용하면 상당히 짧은 시간에 천일염을 수확할 수 있다. Sea salt can be harvested on average in about 3 to 5 days using the present invention. Considering that it usually takes about 25 days to harvest sea salt, using the present invention, sea salt can be harvested in a fairly short time.

이상의 설명은 본 발명의 기술사상을 예시적으로 설명한 것에 불과한 것으로서, 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자라면 본 발명의 본질적인 특성에서 벗어나지 않는 범위 내에서 여러 가지 치환, 변형 및 변경 등이 가능함을 쉽게 알 수 있을 것이다. 즉, 본 발명에 개시된 실시 예들은 본 발명의 기술 사상을 한정하기 위한 것이 아니라 설명하기 위한 것으로서, 이러한 실시 예에 의하여 본 발명의 기술 사상의 범위가 한정되는 것은 아니다.The above description is merely illustrative of the technical idea of the present invention, and those of ordinary skill in the art to which the present invention pertains may make various substitutions, modifications, and changes within the scope not departing from the essential characteristics of the present invention. It will be easy to see that this is possible. That is, the embodiments disclosed in the present invention are not intended to limit the technical spirit of the present invention but to explain, and the scope of the technical spirit of the present invention is not limited by these embodiments.

따라서, 본 발명의 보호 범위는 후술되는 청구범위에 의하여 해석되어야 하며, 그와 동등한 범위 내에 있는 모든 기술사상은 본 발명의 권리범위에 포함되는 것으로 해석되어야 할 것이다.Accordingly, the protection scope of the present invention should be interpreted by the claims described below, and all technical ideas within the scope equivalent thereto should be interpreted as being included in the scope of the present invention.

Claims (4)

삭제delete 삭제delete 삭제delete 해수를 농축시키는 방법에 있어서,
바닥에 흡수성 부재가 깔린 증발지에 해수가 급수되는 제1단계;
상기 증발지에 급수된 해수가 자연증발되어 목표 수준의 염도로 농축되고, 상기 흡수성 부재가 상기 목표 수준의 염도로 농축된 해수로 염장되는 제2단계;
상기 제2단계에서, 상기 흡수성 부재에 흡수된 염장 해수를 제외한 해수가 외부로 배출되는 제3단계;
새로운 해수가 상기 증발지에 급수된 후 삼투압 작용에 의해 상기 새로운 해수와 상기 염장 해수의 염도가 18~22%의 염도로 평형 상태를 이루는 제4단계;
상기 제4단계에서 상기 18~22%의 염도로 평형상태를 이룬 해수가 자연증발되어 24~25%의 염도로 농축되는 제5단계; 및
상기 제5단계에서 24~25%의 염도로 농축된 해수가 외부로 배출되는 제6단계;를 포함하는 것을 특징으로 하는 해수 농축방법.
In the method of concentrating seawater,
A first step of supplying seawater to an evaporator with an absorbent member on the bottom;
a second step in which the seawater supplied to the evaporator is naturally evaporated and concentrated to a target level of salinity, and the absorbent member is salted with seawater concentrated to the target level of salinity;
In the second step, a third step of discharging seawater except for the salted seawater absorbed by the absorbent member to the outside;
A fourth step of balancing the salinity of the new seawater and the salted seawater to a salinity of 18 to 22% by osmotic pressure after the new seawater is supplied to the evaporator;
a fifth step of naturally evaporating the seawater equilibrated to a salinity of 18 to 22% in the fourth step and concentrating to a salinity of 24 to 25%; and
Seawater concentration method comprising a; a sixth step in which the seawater concentrated to a salinity of 24 to 25% in the fifth step is discharged to the outside.
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