KR100481286B1 - Method of preparing liquid calcium chloride using shell - Google Patents

Method of preparing liquid calcium chloride using shell Download PDF

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KR100481286B1
KR100481286B1 KR10-2003-0006291A KR20030006291A KR100481286B1 KR 100481286 B1 KR100481286 B1 KR 100481286B1 KR 20030006291 A KR20030006291 A KR 20030006291A KR 100481286 B1 KR100481286 B1 KR 100481286B1
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calcium chloride
shell
hydrochloric acid
mixed solution
liquid calcium
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KR10-2003-0006291A
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KR20040069754A (en
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김덕환
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삼일화학공업 주식회사
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/20Halides
    • C01F11/24Chlorides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/10Oxidants
    • B01D2251/106Peroxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/20Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2055Carbonaceous material
    • B01D39/2058Carbonaceous material the material being particulate
    • B01D39/2062Bonded, e.g. activated carbon blocks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/80Destroying solid waste or transforming solid waste into something useful or harmless involving an extraction step
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/20Halides
    • C01F11/24Chlorides
    • C01F11/32Purification
    • 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
    • Y02W30/00Technologies for solid waste management
    • Y02W30/20Waste processing or separation

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

본 발명은 패각을 이용하여 액상 염화칼슘을 제조하는 방법에 관한 것으로서, 꼬막, 바지락, 제첩, 조개 등과 같은 패각을 이용하여 의료용, 제설용의 액상 염화칼슘을 제조하는 방법에 관한 것이다. The present invention relates to a method for producing liquid calcium chloride using a shell, and to a method for producing liquid calcium chloride for medical use and snow removal using a shell such as a cockle, a clam, a book, a shellfish, and the like.

본 발명은 패각을 이용한 액상 염화칼슘의 제조방법으로, 반응조 내에서 패각을 염산에 용해시키는 반응단계 ; 상기 반응단계에서 얻어진 염화칼슘 혼합용액(A)에 CaO 또는 CaCO3 를 첨가하는 중화단계 ; 상기 중화단계를 통과한 염화칼슘 혼합용액(B)에 과망간산칼륨(KMnO4)를 첨가하는 정제 1 단계 ; 상기 정제 1 단계를 통과한 염화칼슘 혼합용액(C)에 과산화수소(H2O2) 및 활성탄(active carbon)을 첨가하는 정제 2 단계 ; 및 상기 정제 2 단계를 통과한 염화칼슘 혼합 용액(D)을 여과시키는 단계를 포함하는 것을 특징으로 하는 염화칼슘의 제조방법을 제공한다.The present invention provides a method for producing liquid calcium chloride using the shell, the reaction step of dissolving the shell in hydrochloric acid in the reaction tank; A neutralization step of adding CaO or CaCO 3 to the calcium chloride mixture solution (A) obtained in the reaction step; A first step of purifying potassium permanganate (KMnO 4 ) to the calcium chloride mixed solution (B) passed through the neutralization step; Refining two steps of adding hydrogen peroxide (H 2 O 2 ) and activated carbon to the calcium chloride mixed solution (C) that has passed through the first refining step; And it provides a method for producing calcium chloride comprising the step of filtering the calcium chloride mixed solution (D) passed through the purification step 2.

본 발명의 제조방법은 천연 해양 자원인 패각을 활용하여 저렴하고, 고순도의 액상염화칼슘을 대량생산할 수 있는 우수한 효과가 있다.The production method of the present invention is inexpensive using a shell which is a natural marine resource, and has an excellent effect of mass-producing liquid calcium chloride of high purity.

Description

패각을 이용한 액상 염화칼슘의 제조방법 {METHOD OF PREPARING LIQUID CALCIUM CHLORIDE USING SHELL}Method for preparing liquid calcium chloride using a shell {METHOD OF PREPARING LIQUID CALCIUM CHLORIDE USING SHELL}

본 발명은 패각을 이용하여 액상 염화칼슘을 제조하는 방법에 관한 것이다. 보다 상세하게는 꼬막, 바지락, 제첩, 굴껍질 및 조개 등과 같은 패각을 염산과 반응시킨 다음 중화, 정제, 여과의 단계로 구성되는 액상 염화칼슘의 제조방법에 관한 것이다. The present invention relates to a method for producing liquid calcium chloride using a shell. More particularly, the present invention relates to a method for preparing liquid calcium chloride consisting of a step of neutralizing, purifying, and filtration by reacting a shell such as a pinnacle, clam, batter, oyster shell and shellfish with hydrochloric acid.

일반적으로 액상 염화칼슘(CaCl2)은 각종 건조제의 배합용, 제설용, 의료용, 전자재료용, 콘크리트와 혼합하여 빙결방지, 탈색탄(脫色炭)의 제조, 용제류의 탈수용, 제설용, 식품첨가제 등으로 사용된다.Generally, liquid calcium chloride (CaCl 2 ) is mixed with various drying agents, for snow removal, for medical use, for electronic materials, and with concrete, to prevent freezing, to manufacture decolored coal, for dehydration of solvents, for snow removal, and for food. It is used as an additive or the like.

종래의 염화칼슘은 플래이크타입(Flake type)으로서, 사용에 불편함과 금속에 사용시 부식된다는 문제점이 있었다. 근래에는 결빙을 방지하기 위하여 액상 명화칼슘을 도로 등에 직접 살포함으로써 상기 문제를 해결하였다. Conventional calcium chloride is a flake type (Flake type), there was a problem in that it is inconvenient to use and corroded when used in metal. In recent years, the problem has been solved by spraying liquid calcium chloride directly on the road to prevent freezing.

염화칼슘의 제조방법으로는, 암모니아-소다법(솔베이법)을 이용한 공업적 제조방법이 있었다. 이는 암모니아 증류탑의 폐액(廢液)을 농축하거나, 석회법으로 염소산나트륨을 제조함에 있어 부산물로 염화칼슘을 제조하는 등의 화학적 합성 방법에 의한 제법이었는데, 이 경우 염화칼슘은 부산물의 형태로 생산되는 것으로써 순도가 다소 떨어진다는 문제가 있었다. As a manufacturing method of calcium chloride, there existed the industrial manufacturing method using the ammonia-soda method (Solvay method). This was done by a chemical synthesis method such as concentrating the waste solution of the ammonia distillation column, or producing calcium chloride as a by-product in preparing sodium chlorate by the lime method, in which case calcium chloride is produced in the form of by-products. There was a problem that the purity was somewhat lower.

상기와 같이 공업적으로 제조하는 방법이 아닌, 자연산의 칼슘화합물을 다량으로 함유하는 패각류를 사용하려는 시도로는, 대한민국공개특허 제2001-44280호(패각류 껍질을 이용한 젖산 칼슘의 제조방법),대한민국특허 제265976호(도로 제설용 염화칼슘용액제조장치) 등이 있으며, As an attempt to use a shellfish containing a large amount of natural calcium compounds, rather than the method of industrial production as described above, Korean Patent Laid-Open No. 2001-44280 (Method for producing calcium lactate using shell shell) , Korean Patent No. 265976 (Calcium Chloride Solution Manufacturing Equipment for Road Snow Removal),

또한, 대한민국공개특허 제2002-23845호의 "패각류를 이용한 고순도 염화칼슘의 제조공정"에는 염산에 패각을 녹이고, 암모니아를 첨가하여 pH를 조절하고, 불순물은 침전을 통해 제거하는 방법이 개시되었다. 하지만, 상기 방법은 염산과 패각의 반응에 의하여 발생하는 이산화탄소에 의한 거품으로 인하여, 대량생산을 하기가 어렵다는 문제점이 있었다.In addition, Korean Patent Laid-Open Publication No. 2002-23845, "Manufacturing process of high purity calcium chloride using shellfish", discloses a method of dissolving a shell in hydrochloric acid, adding ammonia to adjust pH, and removing impurities through precipitation. However, the method has a problem that it is difficult to mass-produce due to foaming by carbon dioxide generated by the reaction of hydrochloric acid and shells.

본 발명자는 자연산의 칼슘화합물을 다량으로 함유하는 패각을 이용하여 액상 염화칼슘을 제조하기 위하여 끊임없는 연구를 거듭한 결과, 원가가 저렴하고, 순도가 높은 액상 염화칼슘의 간략화된 제조방법을 제공하는 것을 목적으로 한다.The present inventors have continually researched to produce liquid calcium chloride using shells containing a large amount of natural calcium compounds, and the object of the present invention is to provide a simplified method for producing liquid calcium chloride with low cost and high purity. It is done.

또한, 본 발명은 염산과 패각이 반응함에 따라 발생하는 이산화탄소에 의한 거품을, 염산을 스프레이에 의하여 분사하여 제거함으로써 액상 염화칼슘의 제조 공정을 단축시키고, 대량으로 생산이 가능하며, 고순도의 액상 염화칼슘의 제조방법을 제공하는 것을 목적으로 한다.In addition, the present invention shortens the manufacturing process of liquid calcium chloride by spraying hydrochloric acid by spraying to remove bubbles generated by the reaction of hydrochloric acid and shells, it is possible to produce in large quantities, the high-purity of liquid calcium chloride It is an object to provide a manufacturing method.

상기한 기술적 과제를 해결하기 위한, 액상 염화칼슘의 제조방법을 설명하면 다음과 같다.In order to solve the above technical problem, a liquid calcium chloride manufacturing method will be described.

본 발명은 폐각을 이용한 액상 염화 칼슘의 제조방법으로서, The present invention is a method for producing liquid calcium chloride using a waste shell,

반응조 내에서 패각을 염산에 용해시키는 반응단계 ; 상기 반응단계에서 얻어진 염화칼슘 혼합용액(A)에 CaO 또는 CaCO3 를 첨가하는 중화단계 ; 상기 중화단계를 통과한 염화칼슘 혼합용액(B)에 과망간산칼륨(KMnO4)을 첨가하는 정제 1 단계 ; 상기 정제 1 단계를 통과한 염화칼슘 혼합용액(C)에 과산화수소(H2O2) 및 활성탄(active carbon)을 첨가하는 정제 2 단계 ; 및 상기 정제 2 단계를 통과한 염화칼슘 혼합 용액(D)을 여과시키는 단계를 포함하는 것을 특징으로 하는 패각을 이용한 액상 염화칼슘의 제조방법을 제공한다.A reaction step of dissolving the shell in hydrochloric acid in the reactor; A neutralization step of adding CaO or CaCO 3 to the calcium chloride mixture solution (A) obtained in the reaction step; A first step of purifying potassium permanganate (KMnO 4 ) to the calcium chloride mixed solution (B) passed through the neutralization step; Refining two steps of adding hydrogen peroxide (H 2 O 2 ) and activated carbon to the calcium chloride mixed solution (C) that has passed through the first refining step; And it provides a method for producing a liquid calcium chloride using a shell characterized in that it comprises the step of filtering the calcium chloride mixed solution (D) passed through the purification step.

이하에서는 본 발명의 제조방법을 단계별로 상세히 설명한다.Hereinafter will be described in detail step by step the manufacturing method of the present invention.

[제 1 단계 : 반응단계 (반응조 단계)] [Step 1: Reaction stage (reactor stage)]

본 단계는 패각(꼬막, 조개, 제첩, 바지락 등)을 염산에 용해시키는 단계로써, 반응조 내부에 패각과 염산을 투입하여, 패각을 염산에 용해시켜 염화칼슘혼합용액(A)을 제조하는 단계이다. 상기 반응단계 이전에, 상기 패각을 물로 세척한 후, 용도에 따라 입도를 조절하여 분쇄한 후 반응조에 투입하는 것이 바람직하다.This step is a step of dissolving the shells (knapsack, shellfish, confectionery, clam, etc.) in hydrochloric acid, by putting the shells and hydrochloric acid in the reactor, dissolving the shells in hydrochloric acid to prepare a calcium chloride mixture (A) . Before the reaction step, it is preferable to wash the shell with water, and then pulverized by adjusting the particle size according to the use, and then put into the reactor.

본 단계에서는 패각의 불순물은 용해되지 않고 침전되며, 패각의 칼슘성분과 염산은 반응하여 염화칼슘혼합용액이 된다. 본 단계에서는 염화칼슘의 농도가 25중량%로 될 때까지 용해시키는 것이 바람직하다.In this step, the shell impurities are precipitated without dissolution, and the calcium component and hydrochloric acid of the shell react to form a calcium chloride mixture solution. In this step, it is preferable to dissolve until the concentration of calcium chloride reaches 25% by weight.

반응식 1 : 패각(CaCO3+불순물) + 염산(HCl) →염화칼슘혼합용액(CaCl2) + H2CO3 (H2CO3 ↔H2O + CO2 ) + 수용성 불순물 + CO2Scheme 1: shell (CaCO 3 + impurity) + hydrochloric acid (HCl) → calcium chloride mixture (CaCl 2 ) + H 2 CO 3 (H 2 CO 3 ↔ H 2 O + CO 2 ) + water-soluble impurities + CO 2

본 단계에서 염산은 패각의 주성분인 탄산칼슘 화합물 성분과 반응하여 염화칼슘을 제조하기 위해서 투입된다. 이때 염산은 패각에 존재하는 불순물과도 반응하여 유기물질이 발생되고, 상기 유기물질은 미량의 염소화합물로 조성되어 있으며, 나머지 염소화합물은 하기 제2단계에서의 중화시에 pH가 조절됨과 동시에 불순물이 정제되는 것이다.In this step, hydrochloric acid is added to produce calcium chloride by reacting with the calcium carbonate compound component, which is the main component of the shell. At this time, hydrochloric acid also reacts with impurities present in the shell to generate an organic material, and the organic material is composed of a trace amount of chlorine compound, and the remaining chlorine compound is impurity at the same time the pH is adjusted during neutralization in the second step. This is to be purified.

하지만, 패각이 염산에 녹으면서 이산화탄소에 의하여 다량의 기포(거품)이 발생하기 때문에, 반응(용해)시간이 많이 소요되어 공정이 길어지게 되어, 농도를 높이는데 어려움이 따르게되고, 대량으로 생산하는 것이 거의 불가능하다는 문제가 있었다.However, as the shell is dissolved in hydrochloric acid, a large amount of bubbles (bubbles) are generated by carbon dioxide, which requires a lot of reaction (dissolution) time, resulting in a long process, and difficulty in increasing the concentration. There was a problem that it was almost impossible.

상기와 같은 문제점을 해결하기 위하여, 본 반응단계에서는 반응조 내부에 패각을 넣은 후, 패각위에 염산을 스프레이에 의하여 분사하여 염화칼슘혼용액을 제조하는 것이 바람직하다는 것을 발견하게 되었다. 특히, 용해할 때의 분사설비는 반응조의 측면 보다는 반응조 상부의 뚜껑 부위에 설치하는 것이 특히 바람직하다. 염산을 스프레이에 의하여 분사하는 것은, 염산의 공급과 동시에 발생한 이산화탄소에 의한 기포(거품)를, 염산의 분사에 의하여 제거 시키는 것으로서, 연속작업을 할 수 있다는 점에서 특징이 있는 것이다.In order to solve the above problems, it was found that in this reaction step, after putting the shell inside the reactor, it is preferable to prepare a calcium chloride mixed solution by spraying hydrochloric acid on the shell by spraying. In particular, it is particularly preferable that the dispensing equipment at the time of dissolution is installed in the lid portion of the upper portion of the reaction vessel rather than the side of the reaction vessel. Spraying hydrochloric acid by spraying removes bubbles (bubbles) by carbon dioxide generated at the same time as the supply of hydrochloric acid, which is characterized in that continuous operation can be performed.

본 단계에서 투입되는 염산은 18~20W/V% 용액의 것이 작업능률성의 면에서 바람직하며, 본 단계에서 염산은 염화칼슘의 농도가 25W/V% 될 때까지 투입하여 용해시키는 것이 바람직하다.The hydrochloric acid added in this step is preferably 18 to 20 W / V% in terms of work efficiency. In this step, hydrochloric acid is preferably dissolved until the concentration of calcium chloride is 25 W / V%.

[제 2 단계 : CaO 또는 CaCO3를 첨가하는 중화단계][Second Step: Neutralization Step of Adding CaO or CaCO 3 ]

본 단계는 상기 염화칼슘혼합용액(A)에 생석회(CaO) 또는 CaCO3를 첨가하여 pH를 조정하는 단계이다. 상기 염화칼슘혼합액은 강산성(pH가 1 내지 2)의 용액이다. 이러한 강산성의 용액에서는 염산에 의해 용해되어 불순물로 남아있는 각종 금속성 의 물질을 제거할 수 없으므로, 이러한 각종 금속성의 물질을 금속수산물 M(OH)2·(OH)3(여기에서 M은 금속이온임)의 형태로 침전시켜 제거하기 위하여 염화칼슘혼합용액의 pH를 조정하는 단계이다.This step is to adjust the pH by adding quicklime (CaO) or CaCO 3 to the calcium chloride mixture (A). The calcium chloride mixture is a solution of strong acidity (pH of 1-2). In this strongly acidic solution, it is not possible to remove various metallic substances dissolved by hydrochloric acid and remain as impurities. Therefore, these various metallic substances can be removed from the metal aquatic product M (OH) 2 · (OH) 3 ( where M is a metal ion). Step of adjusting the pH of the calcium chloride mixture solution to precipitate out in the form of).

본 단계의 CaO 또는 CaCO3 에의한 중화 단계에서, 이산화탄소의 발생으로 인한 기포(거품)은 통풍장치를 통하여 제거될 수 있다.In the neutralization step by CaO or CaCO 3 in this step, bubbles (bubbles) due to the generation of carbon dioxide can be removed through the ventilator.

상기 패각으로부터 얻어진 생석회가 아닌, 공업적으로 생산하거나 광물질로부터 얻어진 산화칼슘을 첨가하는 경우에는 상기 염화칼슘혼합용액이 혼탁해지는 문제가 있다. In the case of adding calcium oxide obtained industrially or from minerals other than quicklime obtained from the shell, there is a problem that the calcium chloride mixture solution becomes cloudy.

[제 3 단계 : 과망간산칼륨(KMnO4)을 첨가하는 정제 1 단계][3rd step: 1st step of purification by adding potassium permanganate (KMnO4)]

본 단계는 상기 중화단계를 통과한 염화칼슘혼합용액(B)에 과망간산칼륨(potassium permanganate)을 첨가하는 정제단계이다. 상기 과망간산칼륨은 강력한 산화제로써 패각의 불순물인 Fe, Mn, Mg, Al, K 등을 산화시켜 제거하는 작용을 하는 것이다. This step is a purification step of adding potassium permanganate (potassium permanganate) to the calcium chloride mixture (B) passed through the neutralization step. The potassium permanganate is a powerful oxidant to oxidize and remove Fe, Mn, Mg, Al, K and the like impurities of the shell.

과망간산칼륨은 산화제로서, 이의 당량은 Mn이 환원되어지는 정도에 따라 차이가 있다. 예로써, Mn2+가 환원될 때, 그의 당량은 1/5Mol(31.6g)이다. 즉, MnO4-+8H++5e(전위계수) → Mn2++4H2O 또는 2KMnO4 →K2O+2MnO+5O이다.Potassium permanganate is an oxidizing agent and its equivalent varies depending on the degree to which Mn is reduced. By way of example, when Mn 2+ is reduced, its equivalent is 1/5 Mol (31.6 g). That is, MnO4- + 8H ++ 5e (potential coefficient) → Mn2 ++ 4H2O or 2KMnO4 → K2O + 2MnO + 5O.

특히, 본 발명에서 염화칼슘을 제조할 때에 사용되는 염산용액은 다음과 같은 반응특성을 가지고 있어서, 이러한 점을 회피하기 위하여서는 정제단계에서 반드시 필요한 것이다. 2KMnO4 + 16HCL →2KCl + 2MnCl2 + 5Cl2 + 8H2OIn particular, the hydrochloric acid solution used when preparing the calcium chloride in the present invention has the following reaction characteristics, it is necessary in the purification step to avoid this point. 2KMnO 4 + 16HCL → 2KCl + 2MnCl 2 + 5Cl 2 + 8H 2 O

[제 4 단계 : 과산화수소 및 활성탄을 첨가하는 정제 2 단계][4th step: 2nd step of purification by adding hydrogen peroxide and activated carbon]

본 단계는 상기 정제 1 단계를 통과한 염화칼슘혼합용액(C)에 과산화수소(H2O2) 및 활성탄(activated carbon)을 첨가하는 단계이다. 본 단계에서 과산화수소는 강한 산화제로 작용하여 담백질 등 수용성 불순물과 유기물질 등을 분해시켜 제거하는 작용을 하며, 활성탄은 유기물 등을 흡착·탈취·탈색 시킴으로써 백색도(APHA)를 향상시키는 작용을 한다. 본 단계에서 염화칼슘혼합용액의 pH가 5.5 - 7.0이 되도록 염산을 가하여 조정할 수 있다. 이는 액상 염화칼슘의 순도, 백색도 등을 높이려는 정제 2 단계의 효율성을 향상시킬 뿐만 아니라, 액상 염화칼슘의 수요가 대부분 pH가 중성의 것이 요구되는 것에 사용되기 때문이다.This step is a step of adding hydrogen peroxide (H 2 O 2 ) and activated carbon (activated carbon) to the calcium chloride mixture (C) passed through the first step of purification. In this step, hydrogen peroxide acts as a strong oxidant to decompose and remove water-soluble impurities such as protein and organic substances, and activated carbon improves APHA by adsorbing, deodorizing and decolorizing organic substances. In this step it can be adjusted by adding hydrochloric acid so that the pH of the calcium chloride mixture solution is 5.5-7.0. This not only improves the efficiency of the two stages of purification to increase the purity, whiteness, etc. of the liquid calcium chloride, but also because the demand for the liquid calcium chloride is mostly used for which the pH is required to be neutral.

[제 5 단계 : 여과 단계][Step 5: Filtration Step]

본 단계는 상기 정제 2 단계를 통과한 염화칼슘혼합용액(D)를 여과시키는 단계이다. 여과의 방법에는 특별한 제한이 없으나, 압력여과기(press filter) 등을 사용하여 여과하는 것이 바람직하다.This step is a step of filtering the calcium chloride mixture solution (D) passed through the purification step 2. There is no particular limitation on the method of filtration, but filtration using a pressure filter or the like is preferable.

도 3을 참조하여 본 발명의 액상 염화칼슘의 제조방법을 설명한다. 우선, 반응기(3)에 투입된 패각을 염산 저장조(1)에 의하여 공급되는 염산에 녹여 염화칼슘 혼합용액을 제조한다. 특히, 염산은 반응기내의 상부에 장착된 염산 스프레이 장치를 통하여 분사함이 바람직하다. 반응에 의하여 발생한 이산화탄소 등의 가스는 가스 세정탑(8)으로 이송되고, 염화칼슘 혼합용액은 이송 배관을 통하여 패각용해탱크(2)로 이송된다. 패각 용해탱크(2)로 이송된 염화칼슘 혼합용액 중 일부는 다시 반응조(3)로 이송되고, 일부는 패각 반응탱크(4)로 이송된다. 산화칼슘 저장탱크(7)에서 산화칼의 공급을 통하여, 염화칼슘 혼합용액의 pH가 조절된다. 또한, 산화칼슘 저장탱크와 선택적으로 탄산칼슘 저장탱크가 구비될 수도 있다. 상기 반응탱크를 통과한 염화칼슘 혼합용액은 별도로 구비된 탱크를 통하여 공급되는 과망간산 칼륨, 과산화수소 및 활성탄과 반응하여 정제된 후, 필터 프레스에 의한 여과를 거쳐 염화칼슘 저장탱크(5)로 이송됨으로써, 본 공정에 의한 액상 염화칼슘을 얻을 수 있다. Referring to Figure 3 will be described a method for producing a liquid calcium chloride of the present invention. First, the shell injected into the reactor 3 is dissolved in hydrochloric acid supplied by the hydrochloric acid storage tank 1 to prepare a calcium chloride mixed solution. In particular, the hydrochloric acid is preferably sprayed through a hydrochloric acid spray apparatus mounted on top of the reactor. Gas such as carbon dioxide generated by the reaction is transferred to the gas scrubber tower 8, and the calcium chloride mixed solution is transferred to the shell dissolution tank 2 through a transfer pipe. Some of the calcium chloride mixed solution transferred to the shell dissolution tank 2 is transferred to the reaction tank 3 again, and a portion of the calcium chloride mixed solution is transferred to the shell reaction tank 4. Through the supply of calcium oxide in the calcium oxide storage tank 7, the pH of the calcium chloride mixed solution is adjusted. In addition, a calcium oxide storage tank and optionally a calcium carbonate storage tank may be provided. The calcium chloride mixed solution passed through the reaction tank is purified by reaction with potassium permanganate, hydrogen peroxide and activated carbon supplied through a tank provided separately, and then transferred to the calcium chloride storage tank 5 through filtration by a filter press. The liquid calcium chloride by this can be obtained.

이하, 실시예를 통하여 본 발명을 더욱 상세하게 설명한다. 단, 실시예는 본 발명을 예시하기 위한 것이지, 하기 실시예 만으로 본 발명을 한정하는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to Examples. However, an Example is for illustration of this invention and does not limit this invention only to the following Example.

[실시예 1] Example 1

수세한 꼬막 1000kg 에 염산용액을 반응조에 투입하되, 염화칼슘의 농도가 25W/V%가 될 때까지 18W/V%의 염산용액 1.88m3을 투입한다. 상기 염화칼슘 혼합용액을 중화조로 이동시켜 CaO 40 kg를 투입하여 pH를 5.5로 조절한 다음, 상기 중화조를 통과한 염화칼슘 혼합용액에 과망간산칼륨(KM) 50g을 첨가하여 불순물을 산화시킨다. 상기 정제된 염화칼슘 혼합용액 H2O2용액 80 g 및 활성탄 5kg을 첨가하고 마지막으로 압력여과기로 여과시킴으로써 액상 염화칼슘 5m3을 제조하였다.Hydrochloric acid solution is added to the reaction vessel with 1000 kg of washed water, and 1.88 m 3 of 18 W / V% hydrochloric acid solution is added until the calcium chloride concentration reaches 25 W / V%. The calcium chloride mixture solution was transferred to a neutralization tank, 40 kg of CaO was added to adjust the pH to 5.5, and then 50 g of potassium permanganate (KM) was added to the calcium chloride mixture solution passed through the neutralization tank to oxidize impurities. Liquid calcium chloride 5m 3 was prepared by adding 80 g of the purified calcium chloride mixed solution H 2 O 2 solution and 5 kg of activated carbon and finally filtering with a pressure filter.

[실시예 2]Example 2

수세한 꼬막 1000kg을 반응조에 넣고, 염화칼슘의 농도가 25W/V%가 될 때까지 염산용액을 스프레이 하여 분사하는 것을 제외하고는, 실시예 1과 동일한 방법으로 액상염화칼슘을 제조하였다.A liquid calcium chloride was prepared in the same manner as in Example 1, except that 1000 kg of washed pinch was placed in a reactor and sprayed by spraying hydrochloric acid solution until the concentration of calcium chloride was 25 W / V%.

[실시예 3]Example 3

CaO 대신 CaCO3 70 g을 첨가하는 것을 제외하고는 실시예 1과 동일한 방법으로 액상염화칼슘을 제조하였다.Liquid calcium chloride was prepared in the same manner as in Example 1, except that 70 g of CaCO 3 was added instead of CaO.

하기 표 1은 패각류의 구성성분을 조사한 결과이다. Table 1 below shows the results of investigating the components of shellfish.

상기 실시예 1에 의하여 제조된 액상 염화칼슘을 유도결합플라즈마분광기(inductively coupled plasma atomatic emission spectrometer, IPC)를 이용하여 분석을 하였으며 그 결과는 하기 표 2와 같다. The liquid calcium chloride prepared in Example 1 was analyzed using an inductively coupled plasma atomatic emission spectrometer (IPC), and the results are shown in Table 2 below.

[표 1] 패각류의 구성성분Table 1 Components of Shellfish

탄산칼슘Calcium carbonate 기타 성분Other ingredients 꼬막Cock 95~97중량%95-97 wt% 단백질 3~4%, 미량의 Al, Fe, Mg 등3 ~ 4% protein, trace amount of Al, Fe, Mg 바지락Clam 95~96중량%95-96 wt% 단백질 4~5%, 미량의 AL 등4 ~ 5% protein, trace amount of AL

[표 2] 액상 염화칼슘의 IPC 분석표Table 2 Table of IPC Analysis of Liquid Calcium Chloride

농도 (단위 ppm)Concentration in ppm 성분 ingredient Al Al As As Mn Mn Pb Pb PO4 3- PO 4 3- SO4 2- SO 4 2- 실시예 1Example 1 1.391.39 불검출Not detected 4.864.86 불검출Not detected 불검출Not detected 359.90359.90 실시예 2Example 2 0.750.75 불검출Not detected 2.72.7 불검출Not detected 불검출Not detected 불검출Not detected 실시예 3Example 3 0.900.90 불검출Not detected 2.02.0 불검출Not detected 불검출Not detected 불검출Not detected

[표 3] 액상 염화칼슘의 물성[Table 3] Physical Properties of Liquid Calcium Chloride

실시예 1Example 1 실시예 2Example 2 실시예 3Example 3 성분 및함량(W/V%)Ingredients and Content (W / V%) CaCl2 :18.5, Fe:0.005Mg:불검출CaCl 2: 18.5, Fe: 0.005Mg: Not detected CaCl2 : 18.0,Fe : 0.005,Mg, Al:불검출CaCl 2 : 18.0, Fe: 0.005, Mg, Al: Not detected CaCl2 : 20.0,Fe: 0.005,Mg, Al:불검출CaCl 2 : 20.0, Fe: 0.005, Mg, Al: Not detected 외관Exterior 무색투명transparent 무색투명transparent 무색투명transparent 순도 %Purity% 18.5%18.5% 18.018.0 18.918.9 비중importance 1.1601.160 1.1581.158 1.1641.164 흡광도Absorbance 44 33 22 pHpH 5.5~7.05.5-7.0 6.56.5 7.07.0

상기에서, 외관은 투명 Nessler Tube를 사용하여 측정하였다. 순도는 EDTA 정량 및 액체비중계(Hydrometer Method)에 의하여 측정하였으며, 비중은 20℃에서 액체 비중측정계(Densimeter Hydrometer Method Density Meter)에 의하여 측정하였고, 흡광도는 비색계(Colorimeter)를 이용하여 측정하였다. In the above, the appearance was measured using a transparent Nessler Tube. Purity was measured by EDTA quantitation and Hydometer Method, specific gravity was measured by a Densimeter Hydrometer Method Density Meter at 20 ° C., and absorbance was measured using a colorimeter.

상기 살펴본 바와 같이, 본 발명의 제조방법은 천연해양자원인 패각을 활용하여 저렴하고, 고순도의 액상염화칼슘을 간략화된 공정을 통하여 제조할 수 있는 우수한 효과가 있다.As described above, the manufacturing method of the present invention is inexpensive by utilizing the shell, which is a natural marine resource, and has an excellent effect of producing a high purity liquid calcium chloride through a simplified process.

또한, 본 발명의 제조방법은 염산과 패각이 반응함에 따라 발생하는 이산화탄소에 의한 거품을, 염산의 스프레이 분사를 통하여 제거함으로써 액상염화칼슘이 공정시간을 단축시키고, 대량생산을 가능하게 하는 우수한 효과가 있다. In addition, the manufacturing method of the present invention has an excellent effect that the liquid calcium chloride shortens the process time and enables mass production by removing the carbon dioxide bubbles generated by the reaction of the hydrochloric acid and the shell through the spray injection of hydrochloric acid. .

도 1은 본 발명의 제조공정을 도시한 것이다.1 illustrates a manufacturing process of the present invention.

도 2a 는 시판 중인 액상염화칼슘의 X선 회절 분석 결과를 나타낸 것이다.Figure 2a shows the results of X-ray diffraction analysis of commercially available liquid calcium chloride.

또 2b는 본 발명의 실시예 1에 따라 제조된 탄산칼슘의 X선 회절 분석 결과를 나타낸 것이다.In addition, 2b shows the results of X-ray diffraction analysis of the calcium carbonate prepared according to Example 1 of the present invention.

도 3은 액상 염화칼슘의 제조공정도를 나타낸 것이다.Figure 3 shows a manufacturing process of the liquid calcium chloride.

[도면의 부호에 대한 설명][Description of Symbols in Drawing]

1. 염산 저장조 2. 패각 용해 탱크1. hydrochloric acid storage tank 2. shell melting tank

3. 패각 반응탱크 4. 패각 반응 탱크3. Shell reaction tank 4. Shell reaction tank

5. 액상염화칼슘 저장 탱크 6. 희석조5. Liquid Calcium Chloride Storage Tank 6. Dilution Tank

7. 산화칼슘 저장탱크 7'. 염산 계량 탱크7. Calcium oxide storage tank 7 '. Hydrochloric acid metering tank

8. 가스세정탑(scruber) 8. Gas scrubber

Claims (4)

반응조 내에서 패각을 염산에 용해시키는 반응단계 ; 상기 반응단계에서 얻어진 염화칼슘 혼합용액(A)에 CaO 또는 CaCO3 를 첨가하는 중화단계 ; 상기 중화단계를 통과한 염화칼슘 혼합용액(B)에 과망간산칼륨(KMnO4)을 첨가하는 정제 1 단계 ; 상기 정제 1 단계를 통과한 염화칼슘 혼합용액(C)에 과산화수소(H2O2) 및 활성탄(active carbon)을 첨가하는 정제 2 단계 ; 및 상기 정제 2 단계를 통과한 염화칼슘 혼합 용액(D)을 여과시키는 단계A reaction step of dissolving the shell in hydrochloric acid in the reactor; A neutralization step of adding CaO or CaCO 3 to the calcium chloride mixture solution (A) obtained in the reaction step; A first step of purifying potassium permanganate (KMnO 4 ) to the calcium chloride mixed solution (B) passed through the neutralization step; Refining two steps of adding hydrogen peroxide (H 2 O 2 ) and activated carbon to the calcium chloride mixed solution (C) that has passed through the first refining step; And filtering the mixed calcium chloride solution (D) after passing through the purification step 2. 를 포함하는 것을 특징으로 하는 액상 염화칼슘의 제조방법.Method for producing a liquid calcium chloride comprising a. 제 1항에 있어서, The method of claim 1, 상기 반응단계는 반응조 내부의 패각에 염산을 스프레이하여 공급함으로써 염화칼슘 혼합용액을 제조하는 것임을 특징으로 하는 액상 영화칼슘의 제조방법.The reaction step is a method for producing a liquid calcium film, characterized in that to prepare a calcium chloride mixed solution by spraying and supplying hydrochloric acid to the shell inside the reactor. 제 1항에 있어서, The method of claim 1, 상기 반응단계에서 투입되는 염산은 18~20W/V% 임을 특징으로 하는 액상 염화칼슘의 제조방법.Hydrochloric acid added in the reaction step is a method for producing a liquid calcium chloride, characterized in that 18 ~ 20W / V%. 제 1항에 있어서, The method of claim 1, 상기 중화단계에서 CaO 또는 CaCO3는 상기 염화칼슘 혼합용액의 pH가 10.0 이상이 되도록 첨가하고, 상기 정제 2단계에서 pH가 5.5 ~ 7.0되도록 추가로 염산을 가하는 것을 특징으로 하는 액상 염화칼슘의 제조방법.CaO or CaCO 3 in the neutralization step is added so that the pH of the calcium chloride mixture solution is 10.0 or more, and hydrochloric acid is added to the pH so that the pH is 5.5 ~ 7.0 in the second purification step.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101110783B1 (en) 2009-11-17 2012-02-16 한국지질자원연구원 Purification of calcium carbonate by acid treatment
KR20210082657A (en) * 2019-12-26 2021-07-06 ㈜시대에코텍 Flake type calcium chloride drying device of liquid calcium chloride using a shell and Flake type calcium chloride manufacturing method

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KR100680326B1 (en) * 2005-04-26 2007-02-08 삼일화학공업 주식회사 Method of preparing liquid calcium chloride using shell
KR100713803B1 (en) * 2006-11-29 2007-05-02 주식회사 와이씨씨 Melting apparatus of calcite and method of preparing liquid calcium chloride using calcite
CN103159247B (en) * 2013-03-07 2015-11-18 中国科学院青海盐湖研究所 A kind of method of zellon saponification liquor associating carbide slag manufacture calcium chloride
KR102590858B1 (en) * 2022-12-07 2023-10-20 주식회사 와이씨씨 Manufacturing method of snow remover using oyster shells

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101110783B1 (en) 2009-11-17 2012-02-16 한국지질자원연구원 Purification of calcium carbonate by acid treatment
KR20210082657A (en) * 2019-12-26 2021-07-06 ㈜시대에코텍 Flake type calcium chloride drying device of liquid calcium chloride using a shell and Flake type calcium chloride manufacturing method
KR102330802B1 (en) * 2019-12-26 2021-11-24 주식회사 무한 Flake type calcium chloride drying device of liquid calcium chloride using a shell and Flake type calcium chloride manufacturing method

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