KR20010018327A - Appratus and method of titanium production by contineous process - Google Patents
Appratus and method of titanium production by contineous process Download PDFInfo
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- C—CHEMISTRY; METALLURGY
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- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1263—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction
- C22B34/1268—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams
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Abstract
Description
본 발명은 연속공정에 의한 티타늄 제조장치 및 방법에 관한 것으로, 더욱 상세하게는 티타늄 제조시 반응동안 생성된 전자들을 환원반응에 참여케하므로서 석출 티타늄의 위치, 형태 및 형상제어가 가능하고, 원료물질과 환원제 및 반응염들을 계속적으로 공급 및 회수할 수 있는 장치를 설치하므로서 티타늄의 연속 제조가 가능한 연속공정에 의한 티타늄 제조장치 및 방법에 관한 것이다.The present invention relates to a titanium manufacturing apparatus and method by a continuous process, and more particularly, it is possible to control the position, form and shape of the precipitated titanium by participating in the reduction reaction of the electrons generated during the reaction in the production of titanium, raw material The present invention relates to a titanium production apparatus and method by a continuous process that enables continuous production of titanium by providing a device capable of continuously supplying and recovering a reducing agent and a reaction salt.
일반적으로 티타늄은 비강도가 크고 화학적 내식성이 우수하여 항공기소재, 내식을 요하는 화학공업 및 의용·생체재료에 등에 널리 사용되는 금속소재이다.In general, titanium is a metal material that is widely used in aircraft materials, chemical industry requiring medical corrosion, and medical and biological materials because of its high specific strength and excellent chemical corrosion resistance.
현재 티타늄 제조는 도 1에 예시된 바와 같이 금속 열환원법의 일종인 크롤(Kroll)법에 의해 제조가 되는데, 이의 대략적인 제조공정은 반응용기(6)내에 원료물질로서 사염화티타늄(Ti2Cl4)와 환원제로서 마그네슘(Mg) 그리고 반응염들로서 염화마그네슘(MgCl2), 염화칼륨(KCl), 염화리튬(LiCl) 등을 혼합 장입한 후, 700 ∼ 1000℃의 온도에서 수시간 동안 환원공정을 실시한 후, 온도를 상온으로 냉각하여 반응용기 속에 고착되있는 티타늄을 반응염이나 환원제로부터 용해 분리하여 회수하는 방법으로 제조하고 있다.At present, titanium is manufactured by the Kroll method, which is a kind of metal thermal reduction method as illustrated in FIG. 1, and an approximate manufacturing process thereof includes titanium tetrachloride (Ti 2 Cl 4 ) as a raw material in the reaction vessel (6). ) And magnesium (Mg) as a reducing agent and magnesium chloride (MgCl 2 ), potassium chloride (KCl) and lithium chloride (LiCl) as reaction salts were mixed and charged, followed by a reduction process for several hours at a temperature of 700 to 1000 ° C. Thereafter, the temperature is cooled to room temperature to prepare titanium, which is fixed in the reaction vessel, by dissolving and recovering the titanium from the reaction salt or the reducing agent.
그러나 이와 같은 티타늄 제조공정은 반응용기(6) 내에 원료물질과 환원제 및 반응염 등을 동시에 혼합 장입하여, 장입물들의 직접적인 물리적 접촉에 의한 환원반응에 의해 티타늄이 석출되는 1회식의 단속적 공정인 관계로 매회 장입시마다 반응용기와 반응물들을 교환시켜야만하며, 반응에 필요한 온도 상승 및 냉각시 장시간이 소요될 뿐 아니라 석출 티타늄의 분리 회수시 미반응 염이나 환원제의 손실이 많으며, 특히 석출 티타늄이 반응용기(6) 벽에 고착이 되므로 석출물의 회수가 용이하지 않는 등 생산성 및 효율이 낮고 생산비용이 높다는 많은 문제점이 발생하고 있다.However, such a titanium manufacturing process is a one-time intermittent process in which titanium is precipitated by a reduction reaction by direct physical contact of charge materials by simultaneously charging and mixing raw materials, a reducing agent, and a reaction salt in the reaction vessel (6). The reactor and the reactants must be exchanged every time the furnace is charged.In addition to the temperature rise and cooling required for the reaction, it takes a long time to cool down. 6) There are many problems in that productivity and efficiency are low and production cost is high, because it is not easy to recover precipitates because it sticks to the wall.
본 발명은 상기와 같은 문제점을 해소하기 위해, 종래의 티타늄 제조법에서와 같이 반응용기(6)내에서 장입물들의 직접적인 물리적 접촉에 의한 티타늄의 환원 제조공정이 아닌 전자의 이동에 의해 반응이 진행될 수 있도록 반응용기(6)와 원료 장입용기(14) 사이를 양호한 도체(8)로 연결하므로서, 석출 티타늄의 위치, 형태 및 형상제어를 가능하게 하고, 또한 조업을 중단시키지 않고도 반응기간 동안 필요한 원료물질, 환원제 및 염들을 계속적으로 공급 및 회수할 수 있는 장치를 설치하므로서 티타늄을 연속적으로 제조할 수 있는데 본 발명의 목적이 있다.The present invention, in order to solve the above problems, the reaction can be carried out by the movement of electrons rather than the reduction production process of titanium by direct physical contact of the charges in the reaction vessel (6) as in the conventional titanium production method. By connecting a good conductor 8 between the reaction vessel 6 and the raw material charging vessel 14 so as to enable control of the position, form and shape of the precipitated titanium, and also the necessary raw materials for the reaction period without stopping the operation. It is an object of the present invention to continuously produce titanium by installing a device capable of continuously supplying and recovering reducing agents and salts.
이와 같은 목적을 달성하기 위해 본 발명은 금속 티타늄을 제조함에 있어서, 반응용기(6)와 원료물질 장입용기(14) 사이에 전자의 이동이 양호한 도체(8)를 연결하여 반응중에 형성된 전자의 이동경로를 제공하므로서 석출 탄탈륨의 위치, 형태 및 형상제어가 가능한 것을 특징으로 하며, 또한 반응기간 동안 필요한 원료물질, 환원제 및 염들을 계속적으로 공급 및 회수할 수 있는 장치를 설치하므로서 조업을 중단시키지 않고도 티타늄의 연속공정 및 제조가 가능한 것을 특징으로 하는 연속공정에 의한 티타늄의 제조장치 및 방법에 관한 것이다.In order to achieve the above object, the present invention, in the production of metal titanium, by connecting the conductor (8) having good movement of electrons between the reaction vessel (6) and the raw material charging container (14) the movement of the electrons formed during the reaction It is possible to control the position, form and shape of precipitated tantalum by providing a path, and also by installing a device that can continuously supply and recover necessary raw materials, reducing agents and salts during the reaction period, without interrupting operation It relates to an apparatus and method for producing titanium by a continuous process, characterized in that the continuous process and production of.
도 1은 종래의 티타늄 제조 장치1 is a conventional titanium manufacturing apparatus
도 2는 본 발명에 사용된 티타늄 연속 제조 장치Figure 2 is a titanium continuous manufacturing apparatus used in the present invention
〈도면의 주요부분에 대한 부호의 설명〉<Explanation of symbols for main parts of drawing>
1 : 발열체 2 : 가스취입구1: heating element 2: gas inlet
3 : 교반기 4 : 진공펌프3: stirrer 4: vacuum pump
5 : 가스배출구 6 : 반응용기5: gas outlet 6: reaction vessel
7 : 진공용기 8 : 외부도체7: vacuum container 8: outer conductor
9 : 환원제 및 반응염 장입봉 10 : 원료물질 주입구9: reducing agent and reaction salt loading rod 10: raw material inlet
11 : 2차 냉각장치 12 : 1차 냉각장치11: 2nd cooling device 12: 1st cooling device
13 : 환원제 및 반응염 장입용기 14 : 원료물질 장입용기13: reductant and reactive salt charging container 14: raw material charging container
15 : 환원제 및 반응염 장입 및 회수구 16 : 원료물질 장입 및 회수구15 charging and recovery port of reducing agent and reaction salt 16 charging and recovery of raw material
17 : 진공벨브17: vacuum valve
이하 첨부된 도면에 의해 상세히 설명하면 다음과 같다.Hereinafter, described in detail by the accompanying drawings as follows.
도 2는 본 발명에 사용된 티타늄 연속 제조장치의 개략도로서 크게 반응용기와 원료물질과 환원제 및 반응염들을 반응기간 동안 연속적인 공급 및 회수가 가능하도록 설계된 장치 그리고 주변장치들로 구성 되어 있다.Figure 2 is a schematic diagram of the titanium continuous manufacturing apparatus used in the present invention is largely composed of the reactor and the raw material, the reducing agent and the reaction salt and the device designed to enable continuous supply and recovery during the reaction period and peripheral devices.
한편 본 발명에 의한 티타늄 제조공정을 상세하게 기술하면, 먼저 상온에서 반응용기(6)내에 환원제로서 마그네슘과 반응염들로서 염화마그네슘, 염화칼륨, 염화리튬 등을 혼합하여 장입한 후, 진공펌프(4)를 이용하여 1O-3토르(torr) 정도의 진공을 유지한 후, 온도를 200 ∼ 300℃로 상승시킨 후, 아르곤 가스를 취입(2)하여 반응용기(6)내를 아르곤 분위기로 형성시킨 후, 반응온도를 700 ∼ 1000℃로 상승시켜 반응용기(6) 내에 있는 환원제와 반응염들을 완전히 용해시키면, 반응용기(6)내에 존재하는 마그네슘 환원제는 ①식에서 보여 주는 것처럼 이온화 되면서 전자를 발생하게 된다.Meanwhile, the titanium production process according to the present invention will be described in detail. First, the mixture is charged with magnesium chloride, potassium chloride, lithium chloride, and the like as a reducing agent in a reaction vessel 6 at room temperature, and then vacuum pump 4 After maintaining a vacuum of about 10 -3 torr (torr), and after raising the temperature to 200 ~ 300 ℃, by blowing the argon gas (2) to form the inside of the reaction vessel (6) in an argon atmosphere When the reaction temperature is increased to 700 to 1000 ° C. to completely dissolve the reducing agent and the reaction salt in the reaction vessel 6, the magnesium reducing agent present in the reaction vessel 6 is ionized as shown in the equation 1 to generate electrons. .
2Mg → 2Mg2++ 4e---------- ① 2Mg → 2Mg 2+ + 4e - --------- ①
이때 반응용기내(6)로 원료장입용기(14)를 전자의 이동이 용이한 도체로 제조된 원료장입구(10)에 매달아 침적시키고 원료물질인 사염화티타늄을 원료장입구(10)를 통해 주입시키면, ①식에 의해 생성된 전자들이 반응용기(6)로 부터 반응용기(6)와 원료물질 장입용기(14) 사이에 연결된 외부회로인 도체(8)를 경유하여 원료물질 장입용기(14)에 이르게 되며, 원료물질 장입용기(14)내에 ②식에 의해 생성된 티타늄 이온들과 반응하여 식 ③에서 보여 주 듯 티타늄으로 환원하게 되며, 따라서 반응용기(6)내의 전체 반응식은 다음 ④식으로 표현될 수 있다.At this time, the raw material loading container 14 is suspended in the reaction container 6 in the raw material charging inlet 10 made of a conductor which can easily move electrons, and titanium tetrachloride, which is a raw material, is injected through the raw material charging inlet 10. Then, the electrons generated by the equation 1 through the conductor 8 which is an external circuit connected between the reaction vessel 6 and the raw material charging container 14 from the reaction container 6 through the raw material charging container 14 And react with the titanium ions produced by ② in the raw material charging container 14 to reduce it to titanium as shown in Equation ③. Therefore, the overall reaction in the reaction container 6 is expressed as Can be expressed.
TiCl4→Ti4++ 4Cl---------- ② TiCl 4 → Ti 4+ + 4Cl - --------- ②
Ti4++ 4e-→Ti --------- ③ Ti 4+ + 4e - → Ti --------- ③
TiCl4+ 2Mg → Ti + 2MgCl2--------- ④TiCl 4 + 2Mg → Ti + 2MgCl 2 --------- ④
한편 소정의 공정이 종료된 후, 원료장입 용기(14)내에 석출된 티타늄의 회수는 원료장입 용기(14)를 1차 냉각구역(12)에서 충분히 냉각 시킨 후,On the other hand, after the predetermined process is completed, the recovery of titanium deposited in the raw material loading container 14 is performed after the raw material charging container 14 is sufficiently cooled in the primary cooling zone 12,
원료장입구(16)를 통해 끄집어 내어 2차 냉각구역(11)에서 상온까지 충분히 냉각시킨 후 회수한다.It is taken out through the raw material charging inlet 16 and is sufficiently cooled in the secondary cooling zone 11 to room temperature and then recovered.
이처럼 본 발명에서 사용한 제조장치 및 공정을 적용시, 티타늄의 연속제조가 가능하며, 조업기간 동안 필요한 원료물질이나 환원제 및 반응염들을 상기에 기술한 원료물질의 공급 및 회수와 동일한 방법으로 조업의 중단없이 계속적으로 공급 및 회수가 가능할 뿐 아니라 더 높은 생산성을 위해서는 상기 각 물질들의 공급 및 회수장치의 수와 크기 및 모양을 조업자가 원하는 규모로 설치하므로서 다양한 조업이 가능하다.As described above, when applying the manufacturing apparatus and process used in the present invention, it is possible to continuously manufacture titanium, and to stop the operation in the same manner as supplying and recovering the raw materials, reducing agents and reaction salts necessary during the operation period as described above. In addition to being able to continuously supply and recover, and for higher productivity, various operations are possible by installing the number, size, and shape of the supply and recovery devices of the above materials on a scale desired by an operator.
이상에서 상술한 바와 같이 본 발명은, 종래 반응물질들의 직접적인 물리적 접촉에 의한 티타늄 제조법과 달리 전자의 이동에 의한 환원반응이므로 원료물질의 선택의 폭이 넓고, 저품위 원료물질의 사용 및 고순도의 석출물을 얻을 수 있을 뿐 아니라 석출물의 위치, 형태 및 형상을 제어할 수 있는 장점이 있으며, 특히 연속적 조업이 가능함으로서 단속적인 종래 제조법에 비해 생산성이 높고 저비용, 고효율 등의 여러 장점이 있다.As described above, the present invention, unlike the conventional titanium production method by direct physical contact of the reactants, because of the reduction reaction by the movement of electrons, the choice of raw materials is wide, the use of low-grade raw materials and high-purity precipitates In addition to being able to obtain, there is an advantage that can control the position, form and shape of the precipitate, in particular the continuous operation is possible, there are a number of advantages, such as high productivity, low cost, high efficiency compared to the intermittent manufacturing method.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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KR20020023868A (en) * | 2001-12-26 | 2002-03-29 | 박형호 | Titanium manufacturing apparatus and method by outer cooling method |
KR20020023867A (en) * | 2001-12-26 | 2002-03-29 | 박형호 | Continuous manufacturing apparatus and method of titanium by exchange type |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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KR20020023868A (en) * | 2001-12-26 | 2002-03-29 | 박형호 | Titanium manufacturing apparatus and method by outer cooling method |
KR20020023867A (en) * | 2001-12-26 | 2002-03-29 | 박형호 | Continuous manufacturing apparatus and method of titanium by exchange type |
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