CN1225562C - Method of producing titanium enriched material using titanium mineral - Google Patents
Method of producing titanium enriched material using titanium mineral Download PDFInfo
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Abstract
本发明公开了一种利用钛矿资源生产富钛料的方法,本发明能有效回收利用钒钛磁铁矿表内矿、表外矿和风化矿中各种有价元素。本发明的技术方案为:钒钛磁铁矿经预选抛尾或风化矿洗矿后再经磁化焙烧阶段磨选,使脉石矿物分离得钛铁精矿,或者此钛铁精矿和钒钛铁精矿按一定比例混合后配加粘结剂和碳质还原剂混匀后造球团进行预还原或直接入炉,在电高炉或矿热炉冶炼生产的高钛渣和半钢,合金铁水经双联法吹钒铬,所得含钒铬的钢渣用湿法提取分离钒铬,而高钛渣进入钛渣的火法冶金选矿过程,生产出人造金红石和微晶玻璃。人造金红石富钛料和煤细磨按一定比例混合后配加粘结剂制成含碳钛粒,在焙烧炉内焙烧冷却后,筛分分级成+0.3mm~-1.4mm粒级含碳金红石富钛料。
The invention discloses a method for producing titanium-rich material by using titanium ore resources. The invention can effectively recycle and utilize various valuable elements in vanadium-titanium magnetite surface ores, surface ores and weathered ores. The technical scheme of the present invention is: the vanadium-titanium magnetite is subjected to pre-selection, throwing tailings or weathered ore washing, and then undergoes magnetization roasting stage grinding, so that the gangue minerals are separated to obtain ilmenite concentrate, or the ilmenite concentrate and vanadium-titanium Iron concentrate is mixed in a certain proportion, then mixed with binder and carbonaceous reducing agent, and then pelletized for pre-reduction or directly into the furnace. High-titanium slag, semi-steel and alloy produced by smelting in electric blast furnace or submerged arc furnace The molten iron is blown with vanadium and chromium by the dual method, and the obtained steel slag containing vanadium and chromium is separated by wet extraction, and the high titanium slag enters the pyrometallurgical beneficiation process of titanium slag to produce artificial rutile and glass-ceramics. The artificial rutile titanium-rich material and coal finely ground are mixed in a certain proportion and then added with a binder to make carbon-containing titanium particles. After roasting and cooling in the roaster, they are sieved and classified into carbon-containing rutile with particle size of +0.3mm~-1.4mm Titanium-rich material.
Description
技术领域technical field
本发明属于钛矿(钒钛磁铁矿、钛砂矿)金属矿物选冶方法,特别是从岩矿型钒钛磁铁矿表内矿、表外矿和风化矿制造钢铁产品、提取硫酸法钛白粉厂使用的高品位酸溶性富钛料及氯化法钛白粉厂使用的含碳金红石富钛料和钒铬产品并综合利用其它有价元素的选冶方法。The present invention belongs to titanium ore (vanadium-titanium magnetite, titanium sand ore) metal mineral dressing and smelting method, especially from rock ore type vanadium-titanium magnetite surface ore, surface ore and weathered ore to manufacture iron and steel products, extract sulfuric acid method High-grade acid-soluble titanium-rich materials used in titanium dioxide factories, carbon-containing rutile titanium-rich materials and vanadium-chromium products used in chloride-process titanium dioxide factories, and comprehensive utilization of other valuable elements.
背景技术Background technique
在自然界钛资源通常以氧化物状态和其他金属氧化物,特别是和氧化铁形成固溶体(金红石),或者独立矿物(钒钛磁铁矿、钛砂矿等)。本发明所称钛矿是指具有工业价值的钛矿床(原生钒钛磁铁矿和钛砂矿),即边界品位原生矿(钒钛磁铁矿)TiO2≥5%~6%、钛砂矿(钛铁矿)矿物≥10kg/m3的钛矿床。原生钒钛磁铁矿中的钛赋存在钛磁铁矿和钛铁矿二种目的矿物中,钒钛磁铁矿的TiO2以钛铁矿(FeO·TiO2)和钛铁晶石(2FeO·TiO2)为客晶矿物与主晶矿物磁铁矿(FeO·Fe2O3)呈类质同象存在,用机械物理的选矿方法不能将铁、钛分离。这种钒钛磁铁矿储量巨大,在开采利用时将占地质储量70%的TFe<23%低品位矿、表外矿和风化矿当采矿废石排弃。实际这些采矿废石连同表内矿中富矿、中矿一样认定为铁和钒资源的同时主要确认它为钛资源。钒钛磁铁矿作为钛矿资源用于生产钛白、金属钛和其它钛系列产品。通常原生钒钛磁铁矿首先进入选铁厂,经磁选使强磁性的钛磁铁矿和弱磁性的钛铁矿、硫化物及硅酸盐矿物分离成为含钒钛铁精矿。这种铁精矿作为炼铁原料进入高炉一氧气转炉钢铁冶炼流程〔如我国的攀枝花钢铁(集团)公司,俄罗斯的秋索夫冶金工厂等〕,或铁的直接还原流程生产钢铁产品。由于含有~0.3%的V2O5而具有较高经济价值,在炼钢过程中可产出钒渣,是钒产品的重要原料。但铁选厂分选出的钒钛铁精矿中仍然还存在2%~6%的粒状钛铁矿,此外钛磁铁矿中钛、铁类质同象存在,选矿方法无法分离,这是一些钒钛铁精矿铁低钛高TiO2>12%的主要原因之一,造成后续钢铁冶炼过程的巨大困难。鉴于钒钛磁铁矿精矿含钛量占原矿含钛总量的比重很大,以攀枝花兰尖矿区为例,其占有率超过50%~60%,对于一个以钒钛磁铁矿为主要炼铁原料的攀枝花钢铁公司来说,这一部分伴随铁矿物开采下山进入高炉冶炼的二氧化钛,其绝对数量每年可高达60万吨~70万吨TiO2,但是这种钒钛铁精矿含钛品位低,加上钢铁冶炼工艺的要求,特别是高炉—转炉流程,在高炉配料中需要添加酸性溶剂和碱性溶剂,使产出的钛渣二氧化钛含量不超过25%,高炉冶炼才能顺行,以致迄今尚无工业化的方法从钛渣中提取钛产品和大量利用这种钛渣的方法,造成每年约350万吨这种钛渣的堆集,形成巨大的环境压力。In nature, titanium resources are usually in the form of oxides and other metal oxides, especially iron oxides, forming solid solutions (rutile), or independent minerals (vanadium-titanium magnetite, titanium placer, etc.). Titanium ore referred to in the present invention refers to titanium ore deposits (primary vanadium-titanium magnetite and titanium placer) with industrial value, that is, cut-off grade primary ore (vanadium-titanium magnetite) TiO 2 ≥ 5% to 6%, titanium sand Titanium deposits with ore (ilmenite) minerals ≥ 10kg/ m3 . The titanium in the primary vanadium-titanium magnetite exists in the two purpose minerals of titano-magnetite and ilmenite . ·TiO 2 ) is a guest crystal mineral and the main crystal mineral magnetite (FeO·Fe 2 O 3 ) exists in the same quality, and iron and titanium cannot be separated by mechanical and physical beneficiation methods. This kind of vanadium-titanium-magnetite has huge reserves, and low-grade ore with TFe<23%, external ore and weathered ore, which account for 70% of the geological reserve, will be discarded as mining waste during mining and utilization. In fact, these mining waste rocks are identified as iron and vanadium resources, together with the rich ore and medium ore in the table, and it is mainly confirmed as titanium resources. Vanadium-titanium magnetite is used as a titanium ore resource for the production of titanium dioxide, titanium metal and other titanium series products. Usually the primary vanadium-titanium magnetite first enters the iron concentrator, and the strong magnetic titano-magnetite and weak magnetic ilmenite, sulfide and silicate minerals are separated into vanadium-containing ilmenite concentrate through magnetic separation. This iron concentrate enters the blast furnace-converter oxygen furnace iron and steel smelting process (such as my country's Panzhihua Iron and Steel (Group) Company, Russia's Tyusov Metallurgical Plant, etc.) as ironmaking raw materials, or iron direct reduction process to produce iron and steel products. Because it contains ~0.3% V 2 O 5 , it has high economic value, and vanadium slag can be produced in the steelmaking process, which is an important raw material for vanadium products. However, there are still 2% to 6% granular ilmenite in the vanadium-titanium-iron concentrate separated by the iron beneficiation plant. In addition, titanium and iron are isomorphic in titano-magnetite, and the beneficiation method cannot be separated. One of the main reasons why some vanadium-titanium ferroconcentrate iron is low in titanium and high in TiO 2 >12%, which causes great difficulties in the subsequent iron and steel smelting process. In view of the fact that the titanium content of vanadium-titanium magnetite concentrate accounts for a large proportion of the total titanium content of the original ore, taking Panzhihua Lanjian mining area as an example, its share exceeds 50% to 60%. For Panzhihua Iron and Steel Co., Ltd., which is the raw material for ironmaking, the absolute amount of titanium dioxide that enters the blast furnace smelting along with the mining of iron ore can be as high as 600,000 to 700,000 tons of TiO 2 per year, but this vanadium-titanium ferroconcentrate contains titanium Low grade, coupled with the requirements of the iron and steel smelting process, especially the blast furnace-converter process, acidic solvents and alkaline solvents need to be added to the blast furnace ingredients, so that the titanium dioxide content of the produced titanium slag does not exceed 25%, and the blast furnace smelting can go smoothly. As a result, there is no industrialized method to extract titanium products from titanium slag and a large number of methods to utilize this titanium slag, resulting in the accumulation of about 3.5 million tons of this titanium slag every year, forming a huge environmental pressure.
由于进入直接还原流程的含钒钛铁精矿,所产钛渣含TiO2通常<60%,难于进入现有制造人造金红石的过程,所以至今没有用类似钒钛铁精矿这样低品位钛资源为原料成功的提取含碳人造金红石富钛料的方法,用于氯化法钛白粉厂生产氯化法金红石钛白、海绵钛、钛材等。Due to the vanadium-containing ilmenite concentrate that enters the direct reduction process, the titanium slag produced usually contains less than 60% TiO 2 , and it is difficult to enter the existing process of manufacturing artificial rutile, so low-grade titanium resources such as vanadium ilmenite concentrate have not been used so far The method of successfully extracting carbon-containing artificial rutile titanium-rich materials as raw materials is used in the production of chloride-process rutile titanium dioxide, sponge titanium, titanium materials, etc. in the chloride-process titanium dioxide factory.
选铁厂采用一段磨矿一次磁选回收钛矿中钛磁铁矿,选铁厂尾矿作为选钛厂原矿,采用重选——电选流程回收+0.074mm粒状钛铁矿,采用强磁一一浮选流程回收-0.075mm粒状钛铁矿,生产TiO247%钛精矿,选钛厂钛(TiO2)回收率20%,从采矿计算到钛精矿,现在钛回收率3.95%。低品位钛精矿(TiO243%~53%)用于硫酸法钛白粉厂生产硫酸法钛白,“三废”排放量特大,环境污染极为严重。生产一吨二氧化钛,要副产绿矾(7水硫酸亚钛)2.5~4t、20%废硫酸7~11t、酸性废水100~250t、酸性含尘废气15000~20000m3、废渣0.2~0.3t(干基计)。生产一吨二氧化钛,需4t左右硫酸,除了生成硫酸亚铁耗用部分硫酸,其余硫酸全部变成废水、废气、废渣,如此大量废物的排放量,其它化工产品几乎没有。硫酸法钛白粉厂迫于“三废”治理,急切需要用高品位酸溶性富钛料为原料。国内外用岩矿(原生矿)或钛砂矿电冶炼生产酸溶性富钛料,二氧化钛品位只有TiO241%~72%,至今没有生产高品位TiO275%~92%的酸溶性富钛料。The iron dressing plant adopts one-stage grinding and one-time magnetic separation to recover titanium magnetite in titanium ore, and the tailings of the iron dressing plant are used as the raw ore of the titanium dressing plant, and the gravity separation-electric separation process is used to recover +0.074mm granular ilmenite, and the strong magnetic One by one flotation process recovery - 0.075mm granular ilmenite, production of TiO 2 47% titanium concentrate, titanium (TiO 2 ) recovery rate of 20% in the titanium beneficiation plant, calculated from mining to titanium concentrate, the current titanium recovery rate is 3.95% . Low-grade titanium concentrate (TiO 2 43%~53%) is used in sulfuric acid titanium dioxide factory to produce sulfuric acid titanium dioxide. The discharge of "three wastes" is extremely large and the environmental pollution is extremely serious. To produce one ton of titanium dioxide, 2.5-4t of green vitriol (
矿山开采钒钛磁铁矿,将占地质储量约70%的低品位矿、表外矿和风化矿当采矿废石排弃,攀西地区每年约有1000多万吨钛矿资源当采矿废石排弃。When mining vanadium-titanium magnetite, the low-grade ore, off-surface ore and weathered ore, which account for about 70% of the geological reserves, are discarded as mining waste rocks. There are more than 10 million tons of titanium ore resources in Panxi area as mining waste rocks every year. reject.
发明内容Contents of the invention
本发明的目的:一是将目前钒钛矿入选铁品位由TFe34%~40%,降低到TFe22%~30%,降低原矿入选铁品位TFe10%,三种目的矿物(钛磁铁矿、粒状钛铁矿和硫化物)混合选冶;二是钛回收率由目前的3.95%提高到70%(从采矿计算到钛铁精矿)、铁回收率由目前的56.99%提高到70%(从采矿计算到铁水)、钒回收率由目前的26.83%提高到70%(从采矿计算到钒渣);三是节约资源、保护资源,合理开发综合利用钒钛资源,将目前当作采矿废石排弃的占钒钛矿地质储量70%的低品位矿、表外矿、风化矿全部回收利用;四是生产TiO275%~92%适合于硫酸法钛白粉厂使用的酸溶富钛料;五是生产TiO2>92%~96%适合于氯化法钛白粉厂使用的低钙镁含碳金红石富钛料;六是目前攀枝花钢铁公司开发利用攀西钒钛磁铁矿以铁为主,生产50吨铁才副产一吨二氧化钛,钛铁比1/50,而攀枝花金钛高科技有限责任公司利用本发明的方法以钛为主开发利用攀西钒钛磁铁矿,综合平衡回收铁、钒、铬等其它有价元素,钛铁比1/3,生产一吨二氧化钛,副产3吨铁。攀西钒钛磁铁矿(钒钛矿)实质是钛矿。Purpose of the present invention: the one, be reduced to TFe22%~30% by TFe34%~40% by TFe34%~40% at present by TFe34%~40%, reduce raw ore and select iron grade TFe10%, three purpose minerals (titanium magnetite, granular titanium Iron ore and sulfide) mixed dressing and smelting; second, the recovery rate of titanium is increased from the current 3.95% to 70% (calculated from mining to ilmenite concentrate), and the recovery rate of iron is increased from the current 56.99% to 70% (from mining Calculated to molten iron), vanadium recovery rate increased from the current 26.83% to 70% (calculated from mining to vanadium slag); the third is to save resources, protect resources, rationally develop and comprehensively utilize vanadium and titanium resources, and treat the current waste rock as mining The discarded low-grade ore, off-surface ore, and weathered ore, which account for 70% of the geological reserves of vanadium-titanium ore, are all recycled; the fourth is to produce 75% to 92% of TiO 2 acid-soluble titanium-rich materials suitable for use in sulfuric acid titanium dioxide factories; Fifth, the production of TiO 2 >92%-96% is suitable for the use of low-calcium magnesium carbon-containing rutile titanium-rich materials used in chloride-process titanium dioxide factories; sixth, the development and utilization of Panxi vanadium-titanium magnetite by Panzhihua Iron and Steel Company is mainly iron , produce 50 tons of iron to produce one ton of titanium dioxide by-product, the ratio of titanium to iron is 1/50, and Panzhihua Jinti High-tech Co., Ltd. utilizes the method of the present invention to mainly develop and utilize Panxi vanadium-titanium magnetite, comprehensively balanced recovery Iron, vanadium, chromium and other valuable elements, the ratio of titanium to iron is 1/3, one ton of titanium dioxide is produced, and 3 tons of iron are produced by-product. Panxi vanadium-titanium magnetite (vanadium-titanium ore) is essentially titanium ore.
本发明通过下述技术方案予以实现:钒钛磁铁矿(或钛砂矿)经预选抛尾或风化矿洗矿后再经磁化焙烧阶段磨选,使脉石矿物分离得钛铁精矿(或钛砂精矿),或者此钛铁精矿(或钛砂精矿)和钒钛铁精矿(或钛精矿)按一定比例混合后配加粘结剂(膨润土等)和碳质还原剂混匀后造球团进行预还原或直接入炉,在电高炉或矿热炉冶炼生产TiO2>68%的高钛渣(熔分钛渣)和半钢(合金铁水),合金铁水经双联法吹钒铬,所得含钒铬的钢渣用湿法提取分离钒铬,高钛渣(溶分钛渣)隔绝空气冷却经破碎磨矿重力选矿后,将二氧化钛品位提高到TiO275%~92%,用雷蒙磨粉碎至细度0.045mm~0.075mam的酸溶性富钛料,高钛渣(熔分钛渣)进入钛渣的火法冶金选矿过程,生产出人造金红石富钛料(TiO2>92%~96%)和微晶玻璃。为提高金红石富钛料在氯化沸腾炉(流态化床)的氯化率、钛的利用率和防止氯化熔盐堵塞氯化沸腾炉孔网,将煤渗入到金红石富钛料中,配加粘结剂(木浆等)混匀造粒,焙烧后隔离空气或通入隋性气体冷却后,筛分成+0.3mm~1.4mm粒级含碳金红石富钛料。The present invention is realized through the following technical scheme: the vanadium-titanium magnetite (or titanium placer ore) is pre-selected and discarded or weathered ore is washed and then subjected to magnetization and roasting stage grinding, so that the gangue minerals are separated to obtain ilmenite concentrate ( or titanium sand concentrate), or this ilmenite concentrate (or titanium sand concentrate) and vanadium-titanium iron concentrate (or titanium concentrate) are mixed in a certain proportion and then added with binder (bentonite, etc.) and carbonaceous reduction After the agent is mixed, the pellets are pre-reduced or directly put into the furnace, and the high-titanium slag (melted titanium slag) and semi-steel (alloy molten iron) with TiO 2 >68% are produced in the electric blast furnace or submerged arc furnace. Double blowing of vanadium and chromium, the obtained steel slag containing vanadium and chromium is extracted and separated from vanadium and chromium by wet method, high titanium slag (dissolved titanium slag) is isolated from air and cooled, and after crushing, grinding and gravity separation, the grade of titanium dioxide is increased to TiO 2 75% ~92%, acid-soluble titanium-rich material crushed to a fineness of 0.045mm-0.075mam by Raymond mill, high-titanium slag (melted titanium slag) enters the pyrometallurgical beneficiation process of titanium slag, and artificial rutile titanium-rich material is produced (TiO 2 >92%~96%) and glass-ceramics. In order to improve the chlorination rate of rutile titanium-rich material in the chlorination fluidized bed furnace (fluidized bed), the utilization rate of titanium and to prevent the chlorination molten salt from clogging the hole network of the chlorination fluidized bed, coal is infiltrated into the rutile titanium-rich material, and added The binder (wood pulp, etc.) is mixed and granulated, and after roasting, the air is isolated or cooled by inert gas, and then sieved into carbon-containing rutile and titanium-rich materials with a particle size of +0.3mm to 1.4mm.
本发明的方法包括如下的工艺步骤:Method of the present invention comprises following processing step:
①-70~0mm钛矿预选抛尾生产工艺流程:-70~0mm钛矿经预先筛分机(1)、电磁辊(2)粗选,电磁辊(3)扫选排弃尾矿1;预选矿石经预先及检查筛分机(4),+10mm矿石进细碎机(5),-10~0mm矿石经脱磁后进入一段磨矿机(6)磨矿;磨机排矿经螺旋分级筛(7)分级,+3mm矿石返回磨机再磨,-3~0mm矿石进入第一次重选或弱磁选打头工艺流程;①-70~0mm titanium ore pre-selection tailings production process: -70~0mm titanium ore is roughed by pre-screening machine (1), electromagnetic roller (2), and electromagnetic roller (3) sweeps and discards tailings 1 ; pre-selection The ore is pre-screened and inspected by the screening machine (4), +10mm ore enters the fine crusher (5), -10~0mm ore is demagnetized and then enters the first stage of grinding machine (6) for grinding; the ore discharged from the mill passes through the spiral classifying screen ( 7) Classification, +3mm ore returns to the mill for regrinding, -3~0mm ore enters the first gravity separation or weak magnetic separation process;
②+70mm风化矿洗矿生产工艺流程:风化矿经隔筛(8),+70mm矿块经碎石机(9)破碎到-70~0mm,经洗矿机(10)洗矿;+10mm矿石进入细碎机(5),-10mm矿石进入第一段磨矿机(6);磨机排矿经螺旋分级筛(7)分级,+3mm矿石返回磨机(6)再磨,-3~0mm矿石进入第一次重选或弱磁选打头工艺流程;②+70mm weathered ore washing production process: weathered ore is screened (8), +70mm ore block is crushed to -70~0mm by stone crusher (9), and ore is washed by ore washing machine (10); +10mm The ore enters the fine crusher (5), and the -10mm ore enters the first stage grinding machine (6); the ore discharged from the mill is classified by the spiral classifying screen (7), and the +3mm ore is returned to the mill (6) for regrinding, -3~ 0mm ore enters the first gravity separation or weak magnetic separation process;
③按磁化焙烧阶段磨选“磨矿一重选一弱磁选一磁化焙烧一磨矿一重选一强磁选”工艺流程生产钛铁精矿或钛砂精矿:-70mm钛矿经预选抛尾或风化矿洗矿后,-10mm的矿石经一段磨矿(6);磨机排矿经螺旋分级筛(7)分级,+3mm的矿石返回磨机(6)再磨,-3mm的矿石进入重力选矿机(11)粗选,排弃尾矿2得粗精矿1,中矿经弱磁选机(12)粗选得粗精矿2;弱磁选尾矿脱磁、过滤干燥(13)后进入沸腾炉或回转窑或斜坡式焙烧炉磁化焙烧(14);磁化焙烧粗精矿和粗精矿1、粗精矿2进入二段磨机(15)细磨,二段磨机排矿经脱磁螺旋分级筛或水力旋流器(16)分级;+0.15mm矿石返回磨机(15)再磨,-0.15mm已单体解离的矿物经重力选矿机(17)进行第二次重选粗选,得精矿3和尾矿3;重选中矿经一次中场强磁选机(18)粗选得精矿4,中场强磁选尾矿脱磁经二次中场强磁选机(19)扫选排弃尾矿4得精矿5;精矿3、精矿4和精矿5混合得钛铁精矿或钛砂精矿;③Produce ilmenite concentrate or titanium sand concentrate according to the process flow of "grinding-gravity separation-weak magnetic separation-magnetization roasting-grinding-gravity separation-strong magnetic separation" in the magnetization roasting stage: -70mm titanium ore is pre-selected and discarded Or after the weathered ore is washed, the -10mm ore goes through a stage of grinding (6); the ore discharged from the mill is graded by the spiral classifying screen (7), the +3mm ore is returned to the mill (6) for regrinding, and the -3mm ore enters Gravity concentrator (11) roughing, discarding tailings 2 to get rough concentrate 1 , medium ore roughed by weak magnetic separator (12) to get rough concentrate 2 ; weak magnetic tailings demagnetization, filtering and drying (13 ) into fluidized fluidized furnace or rotary kiln or slope type roaster for magnetization roasting (14); magnetization roasting coarse concentrate and coarse concentrate 1 and coarse concentrate 2 enter the second-stage mill (15) for fine grinding, and the second-stage mill discharges ore Classification by demagnetizing spiral classifying screen or hydrocyclone (16); +0.15mm ore is returned to mill (15) for regrinding, and -0.15mm minerals that have been dissociated from monomers are subjected to gravity concentrator (17) for the second time Gravity separation roughing, get concentrated ore 3 and tailings 3 ; Gravity separation ore gets concentrated ore 4 through a field-strength magnetic separator (18) roughing, and field-strength magnetic separation tailings demagnetization passes secondary field strength Magnetic separator (19) sweeps and discards tailings 4 to obtain concentrate 5 ; concentrate 3 , concentrate 4 and concentrate 5 are mixed to obtain ilmenite concentrate or titanium sand concentrate;
④按磁化焙烧阶段磨选“磨矿一弱磁选一强磁选一磁化焙烧一磨矿一弱磁选一强磁选”工艺流程生产钛铁精矿或钛砂精矿:-70mm钛矿经预选抛尾或风化矿洗矿后,-10mm的矿石经一段磨矿(6),磨机排矿经螺旋分级筛(7)分级,+3mm矿石返回磨矿机(6)再磨;-3~0mm矿石进入弱磁选机(12)粗选得粗精矿1和粗精矿2,粗精矿2脱磁进入第一次中场强磁选机(18)排弃尾矿2得粗精矿3;粗精矿3过滤干燥(13)进入沸腾炉或回转窑或斜坡式焙烧炉磁化焙烧(14);磁化焙烧粗精矿和粗精矿1进入第二段磨机(15)细磨,第二段磨机排矿经螺旋分级筛或水力旋流器(16)分级;+0.15mm矿返回二段磨矿机(15)再磨,-0.15mm矿石经弱磁选机(12)得精矿4,弱磁选尾矿经脱磁进入第二次中场强磁选机(19)得精矿5,二次中场强磁选机(19)尾矿经脱磁进入第三次中场强磁选机(20)排弃尾矿3得精矿6;精矿4、精矿5和精矿6混合得钛铁精矿或钛砂精矿;④Produce ilmenite concentrate or titanium sand concentrate according to the process of magnetization roasting stage "grinding-weak magnetic separation-strong magnetic separation-magnetization roasting-grinding-weak magnetic separation-strong magnetic separation": -70mm titanium ore After the pre-selected tailings or weathered ore washing, the -10mm ore is subjected to one-stage grinding (6), the ore discharged from the mill is graded by the spiral classifying screen (7), and the +3mm ore is returned to the grinding machine (6) for regrinding;- The 3-0mm ore enters the weak magnetic separator (12) for rough separation to obtain coarse concentrate 1 and coarse concentrate 2 , and the coarse concentrate 2 is demagnetized and enters the first high-field strong magnetic separator (18) to discard tailings 2 to obtain Coarse concentrate 3 ; Coarse concentrate 3 is filtered and dried (13) and enters fluidized fluidized furnace or rotary kiln or slope type roaster magnetized roasting (14); Magnetized roasted coarse concentrate and coarse concentrate 1 enter the second stage mill (15) to fine Grinding, the second-stage mill discharges ore and is classified by a spiral classifying screen or a hydrocyclone (16); +0.15mm ore is returned to the second-stage ore mill (15) for regrinding, and -0.15mm ore is passed through a weak magnetic separator (12 ) to obtain concentrate 4 , the tailings of the weak magnetic separation enter the second high-field magnetic separator (19) through demagnetization to obtain concentrate 5 , and the tailings of the secondary high-field magnetic separator (19) enter the second high-field magnetic separator (19) through demagnetization. The three-time field strong magnetic separator (20) discards tailings 3 to obtain concentrate 6 ; concentrate 4 , concentrate 5 and concentrate 6 are mixed to obtain ilmenite concentrate or titanium sand concentrate;
⑤磁化焙烧阶段磨选生产的钛铁精矿或钛砂精矿电炉冶炼生产高钛渣或熔分钛渣:钛铁精矿或钛砂精矿,或者此钛铁精矿、钛砂精矿和钒钛铁精矿或钛精矿按一定比例混合后配加粘结剂及碳质还原剂混匀后(22),造球团(23),进回转窑(24)预还原或直接入炉,在电高炉或矿热炉(25)冶炼生产合金铁水和TiO2>68%的高钛渣或熔分钛渣;合金铁水经双联法吹钒铬,所得含钒铬的钢渣用湿法冶金提取分离钒铬;而高钛渣或熔分钛渣隔绝空气冷却后进入重力选矿过程生产高品位酸溶性富钛料;高钛渣、熔分钛渣或进入火法冶金选矿过程生产金红石富钛料;⑤High titanium slag or melted titanium slag produced by electric furnace smelting of ilmenite concentrate or titanium sand concentrate produced in the magnetization roasting stage: ilmenite concentrate or titanium sand concentrate, or the ilmenite concentrate, titanium sand concentrate Mix with vanadium-titanium iron ore concentrate or titanium concentrate in a certain proportion, add binder and carbonaceous reducing agent after mixing (22), make pellets (23), enter the rotary kiln (24) for pre-reduction or directly enter Furnace, smelting in electric blast furnace or submerged arc furnace (25) to produce alloy molten iron and TiO 2 >68% high titanium slag or molten titanium slag; Vanadium and chromium are extracted and separated by conventional metallurgy; high-titanium slag or molten titanium slag enters the gravity beneficiation process to produce high-grade acid-soluble titanium-rich materials after being isolated from the air; high-titanium slag, molten titanium slag enters the pyrometallurgical beneficiation process to produce rutile Titanium-rich material;
⑥高钛渣或熔分钛渣重力选矿生产高品位酸溶性富钛料:高钛渣或熔分钛渣送入用真空泵(27)抽掉空气或输入隋性气体的冷却炉(26)中冷却后,进行破碎(28),磨矿(29),重力选矿(30),尾矿加工成微晶玻璃;中矿返回电炉冶炼(25),重力选矿精矿为TiO275%~92%酸溶性富钛料经雷蒙磨(31)磨成细度为0.045mm~0.075mm的酸溶性富钛料;⑥ High-grade titanium slag or melted titanium slag gravity beneficiation to produce high-grade acid-soluble titanium-rich material: high-titanium slag or melted titanium slag is sent to the cooling furnace (26) where air is removed by vacuum pump (27) or inert gas is input After cooling, carry out crushing (28), ore grinding (29), gravity beneficiation (30), tailings are processed into glass-ceramics; medium ore is returned to electric furnace smelting (25), and gravity beneficiation concentrate is TiO 2 75%~92% The acid-soluble titanium-rich material is ground into an acid-soluble titanium-rich material with a fineness of 0.045 mm to 0.075 mm by Raymond mill (31);
⑦高钛渣或熔分钛渣或酸溶性富钛料火法冶金选矿生产金红石富钛料:高钛渣或熔分钛渣或未经雷蒙磨(31)细磨的酸溶性富钛料进入保温结晶氧化炉(32),用电弧加热吹氧或用氧气一燃料喷枪或氧气、空气直流等离子发生器向保温氧化炉(32)加热吹氧,同时加入硅石、氟化物添加剂,对高钛渣或酸溶性富钛料进行深度氧化,使高钛渣或富钛料中的主要以Ti3O5为基的固熔体含钛矿物黑钛石中的低价钛氧化物氧化成八面体结构的金红石TiO2,钙镁等杂质被排除在外,进入硅酸盐玻璃体内,形成金红石化富钛料,此金红石化富钛料在缓冷器(33)中使金红石晶粒长大冷却后经破碎(34),磨矿(35)和重选(36)排弃尾矿,得TiO2>92%~96%低钙镁人造金红石富钛料,中矿返回保温氧化炉(32)再次熔炼氧化,以提高钛的回收率,尾矿加工成微晶玻璃;⑦High-titanium slag or molten titanium slag or acid-soluble titanium-rich material pyrometallurgical beneficiation to produce rutile titanium-rich material: high-titanium slag or molten titanium slag or acid-soluble titanium-rich material that has not been finely ground by Raymond mill (31) Enter heat preservation crystallization oxidation furnace (32), blow oxygen with electric arc heating or oxygen-fuel spray gun or oxygen, air DC plasma generator to heat preservation oxidation furnace (32) heating and blow oxygen, add silica, fluoride additive simultaneously, to high titanium Deep oxidation of slag or acid-soluble titanium-rich material, so that the low-valent titanium oxide in the solid solution titanium-containing mineral black titanite mainly based on Ti 3 O 5 in high-titanium slag or titanium-rich material is oxidized into octahedron The structure of rutile TiO 2 , calcium and magnesium and other impurities are excluded and enter the silicate glass to form rutile titanium-rich material. The rutile titanium-rich material makes the rutile grains grow in the slow cooler (33) After cooling, through crushing (34), ore grinding (35) and gravity separation (36), the tailings are discarded to obtain TiO 2 >92% to 96% low-calcium magnesium artificial rutile titanium-rich material, and the middle ore is returned to the heat preservation oxidation furnace (32 ) to smelt and oxidize again to increase the recovery rate of titanium, and process the tailings into glass-ceramics;
⑧、火法冶金选矿生产的TiO2>92%~96%低钙镁人造金红石富钛料生产含碳金红石富钛料:金红石富钛料和固定碳C>60%的煤经磨机(37)、(38)细磨到-0.045mm和粘结剂配料(39)混匀,C/TiO2>20%~30%,粘结剂0.3%~0.6%,造粒(40);含碳钛粒在900℃~950℃焙烧炉内焙烧20分钟(41);然后将含碳钛粒送入用真空泵(42)抽掉空气或有隋性气体的冷却器(43)中防止含碳钛粒氧化冷却后,经双层螺旋分级筛或二台单层螺旋分级机(44)分级,-0.3mm粒级和+1.4mm粒级含碳钛粒返回磨机(37)再磨循环利用,得+0.3mm~-1.4mm粒级的含碳金红石富钛料。⑧. TiO 2 produced by pyrometallurgical beneficiation > 92% ~ 96% low-calcium magnesium artificial rutile titanium-rich material to produce carbon-containing rutile titanium-rich material: rutile titanium-rich material and coal with fixed carbon C > 60% are passed through the mill (37 ), (38) finely grind to -0.045mm and mix with binder ingredients (39), C/TiO 2 >20%~30%, binder 0.3%~0.6%, granulate (40); carbon Titanium grains are roasted in 900 DEG C~950 DEG C roasting furnaces for 20 minutes (41); Then, carbon-containing titanium grains are sent into a cooler (43) with a vacuum pump (42) to evacuate air or inert gas to prevent carbon-containing titanium After the particles are oxidized and cooled, they are classified by double-layer spiral classifying sieves or two single-layer spiral classifiers (44), and the carbon-containing titanium particles of -0.3 mm and +1.4 mm are returned to the mill (37) for regrinding and recycling. A carbon-containing rutile titanium-rich material with a particle size of +0.3mm~-1.4mm is obtained.
本发明产生了如下的有益效果:一是资源利用效率高,将目前钒钛矿入选铁品位由TFe34%~40%,降低到TFe22%~30%,降低原矿入选铁品位TFe10%;二是钛回收率由目前的3.95%提高到70%(从采矿计算到钛铁精矿)、铁回收率由目胶的56.99%提高到70%(从采矿计算到铁水)、钒回收率由目前的26.83%提高到70%(从采矿计算到钒渣);三是节约资源、保护资源,合理开发综合利用资源,能有效回收利用钒钛磁铁矿表内矿、表外矿和风化矿(或钛砂矿)中各种有价元素,钛矿资源开采利用率由目前的30%提高到100%;四是生产TiO2 75%~92%适合于硫酸法钛白粉厂使用的酸溶富钛料;五是生产TiO2>92%~96%适合于氯化法钛白粉厂使用的低钙镁含碳金红石富钛料;六是目前攀枝花钢铁公司开发利用攀西钒钛磁铁矿以铁为主,生产50吨铁才副产一吨二氧化钛,钛铁比1/50,而攀枝花金钛高科技有限责任公司实施该专利开发利用攀西钒钛磁铁矿以钛为主,综合平衡回收铁、钒、铬等其它有价元素,钛铁比1/3,生产一吨二氧化钛,副产3吨铁。攀西钒钛磁铁矿(钒钛矿)实质是钛矿。The present invention has produced the following beneficial effects: one, the resource utilization efficiency is high, the currently selected iron grade of vanadium-titanium ore is reduced from TFe34% to 40% to TFe22% to 30%, and the raw ore selected iron grade TFe10% is reduced; the other is titanium The recovery rate is increased from the current 3.95% to 70% (calculated from mining to ilmenite concentrate), the recovery rate of iron is increased from 56.99% to 70% (calculated from mining to molten iron), and the recovery rate of vanadium is increased from the current 26.83 % is increased to 70% (calculated from mining to vanadium slag); the third is to save resources, protect resources, rationally develop and comprehensively utilize resources, and can effectively recycle vanadium-titanium magnetite surface ore, surface ore and weathered ore (or titanium all kinds of valuable elements in placer), and the utilization rate of titanium ore resources has been increased from the current 30% to 100%; the fourth is to produce TiO 2 75%-92% acid-soluble titanium-rich materials suitable for use in sulfuric acid titanium dioxide factories Fifth, the production of TiO 2 >92% to 96% is suitable for the use of low-calcium magnesium carbon-containing rutile titanium-rich materials used by chloride-process titanium dioxide factories; sixth, Panzhihua Iron and Steel Company is currently developing and utilizing Panxi vanadium-titanium magnetite with iron as its Mainly, only one ton of titanium dioxide is produced by producing 50 tons of iron, and the ratio of titanium to iron is 1/50. Panzhihua Jinti High-tech Co., Ltd. implements this patent to develop and utilize Panxi vanadium-titanium magnetite, which is mainly titanium, and comprehensively balances the recovery of iron , vanadium, chromium and other valuable elements, the ratio of titanium to iron is 1/3, one ton of titanium dioxide is produced, and 3 tons of iron are produced by-product. Panxi vanadium-titanium magnetite (vanadium-titanium ore) is essentially titanium ore.
附图说明Description of drawings
图1为本发明的工艺流程图;Fig. 1 is a process flow diagram of the present invention;
图2为本发明的预选抛尾工艺流程图;Fig. 2 is the process flow chart of the pre-selected tail throwing process of the present invention;
图3为本发明的风化矿洗矿工艺流程图;Fig. 3 is the weathered ore washing process flow chart of the present invention;
图4为本发明的另一工艺流程图。Fig. 4 is another process flow chart of the present invention.
具体实施方式Detailed ways
以下将结合附图和具体实施例对本发明作进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments.
如图1、4所示,-70mm钛矿(钒钛磁铁矿、钛砂矿)经预选抛尾或风化矿洗矿后-10mm矿石,再经磁化焙烧阶段磨选矿,使脉石矿物分离得钛铁精矿(或钛砂精矿),或者此钛铁精矿(或钛砂精矿)和钒钛铁精矿(或钛精矿)按一定比例混合后配加粘结剂(膨润土等)和碳质还原剂混匀后造球团进行预还原或直接入炉,在电高炉或矿热炉冶炼生产TiO2>68%的高钛渣(熔分钛渣)和半钢(合金铁水),合金铁水经双联法吹钒铬,所得含钒铬的钢渣用湿法提取分离钒铬,高钛渣(溶分钛渣)隔绝空气冷却经破碎磨矿重力选矿后,将二氧化钛品位提高到TiO275%~92%,用雷蒙磨粉碎至细度0.045mm~0.075mm的酸溶性富钛料,高钛渣(熔分钛渣)进入钛渣的火法冶金选矿过程,生产出人造金红石富钛料(TiO2>92%~96%)和微晶玻璃。为提高金红石富钛料在氯化沸腾炉(流态化床)的氯化率、钛的利用率和防止氯化熔盐堵塞氯化沸腾炉孔网,将煤渗入到金红石富钛料中,配加粘结剂(木浆等)混匀造粒,焙烧后隔离空气或通入隋性气体冷却后,筛分成+0.3mm~-1.4mm粒级含碳金红石富钛料。As shown in Figures 1 and 4, -70mm titanium ore (vanadium-titanium magnetite, titanium placer) is pre-selected and washed by tailings or weathered ore, and -10mm ore is washed by magnetization and roasting to separate gangue minerals. Obtain ilmenite concentrate (or titanium sand concentrate), or this ilmenite concentrate (or titanium sand concentrate) and vanadium-titanium iron concentrate (or titanium concentrate) are mixed in a certain proportion and then added with binder (bentonite etc.) mixed with carbonaceous reducing agent, pelletized for pre-reduction or directly into the furnace, smelted in electric blast furnace or submerged arc furnace to produce TiO 2 >68% high-titanium slag (melted titanium slag) and semi-steel (alloy molten iron), the alloy molten iron is blown with vanadium and chromium by double-link method, and the obtained steel slag containing vanadium and chromium is extracted and separated from vanadium and chromium by wet method. Increase TiO 2 75% to 92%, use Raymond mill to pulverize acid-soluble titanium-rich materials with a fineness of 0.045mm to 0.075mm, high titanium slag (melted titanium slag) enters the pyrometallurgical beneficiation process of titanium slag, production Artificial rutile titanium-rich materials (TiO 2 >92%-96%) and glass-ceramics were produced. In order to improve the chlorination rate of rutile titanium-rich material in the chlorination fluidized bed furnace (fluidized bed), the utilization rate of titanium and to prevent the chlorination molten salt from clogging the hole network of the chlorination fluidized bed, coal is infiltrated into the rutile titanium-rich material, and added The binder (wood pulp, etc.) is mixed and granulated. After roasting, isolate the air or pass in an inert gas to cool it, and sieve it into carbon-containing rutile and titanium-rich materials with a particle size of +0.3mm~-1.4mm.
如图2所示,矿石预选抛尾生产工艺流程,其过程是:-70mm钛矿(钒钛磁铁矿、钛砂矿)经预先筛分机(1),经电磁辊(2)粗选,电磁辊(3)扫选排弃尾矿1,预选矿石经预先及检查筛分机(4),+10mm矿石进入细碎机(5)细碎,-10~0mm矿石经脱磁后进入一段磨矿机(6)磨矿,磨机排矿经脱磁螺旋分级筛(7)分级,+3mm矿石返回磨机再磨,-3~0mm矿石进入第一次重选或弱磁选打头工艺流程。As shown in Figure 2, the ore pre-selection tailings production process, the process is: -70mm titanium ore (vanadium-titanium magnetite, titanium placer) is pre-screened (1), roughed by electromagnetic rollers (2), The electromagnetic roller (3) sweeps and discards the tailings 1 , the pre-selected ore is pre-screened and inspected by the screening machine (4), the +10mm ore enters the fine crusher (5) for fine crushing, and the -10~0mm ore enters the first-stage grinding machine after demagnetization (6) Grinding, the ore discharged from the mill is classified by the demagnetizing spiral grading screen (7), the +3mm ore returns to the mill for regrinding, and the -3~0mm ore enters the first re-election or weak magnetic separation process.
如图3所示,风化矿洗矿生产工艺流程,其过程是:风化矿经隔筛(8),+70mm矿块经碎石机(9)破碎到-70~0mm,经洗矿机(10),+10mm矿石进入细碎机(5)细碎,-10~0mm矿石进入第一段磨矿机(6)磨矿,磨机排矿经脱磁螺旋分级筛(7)分级,+3mm矿石返回一段磨机(6)再磨,-3~0mm矿石进入第一次重选或弱磁选打头工艺流程。As shown in Figure 3, the weathered ore washing production process is as follows: the weathered ore passes through the screen (8), the +70mm ore block is crushed to -70 ~ 0mm by the stone crusher (9), and the ore washing machine ( 10), +10mm ore enters the fine crusher (5) for fine crushing, -10~0mm ore enters the first stage grinding machine (6) for grinding, and the ore discharged from the mill is classified by the demagnetizing spiral classifying screen (7), +3mm ore Return to the first section of the mill (6) for regrinding, and the -3-0mm ore enters the first gravity separation or weak magnetic separation process.
如图1所示,磁化焙烧阶段磨选“磨矿一重选一弱磁选一磁化焙烧一磨矿一重选一强磁选”工艺流程生产钛铁精矿(或钛砂矿),其过程是:-70mm钛矿(钒钛磁铁矿、钛砂矿)经预选抛尾或风化矿洗矿后-10mm的矿石经一段磨矿(6),磨机排矿经脱磁螺旋分级筛(7)分级,大于3mm的矿石返回磨机(6)再磨,小于3mm的矿石进入重力选矿机(11)粗选,排弃尾矿2得粗精矿1,中矿经弱磁选机(12)粗选得粗精矿2,弱磁选尾矿脱磁、过滤干燥(13)后进入沸腾炉(或回转窑或斜坡式焙烧炉)磁化焙烧(14),磁化焙烧粗精矿和粗精矿1、粗精矿2进入二段磨机(15)细磨,二段磨机排矿经脱磁螺旋分机筛(或水力旋流器)(16)分级,+0.15mm矿石返回磨机(15)再磨,-0.15mm已单体解离的矿物(目的矿物和脉石矿物)经重力选矿机(17)进行第二次重选粗选,得精矿3和尾矿3,重选中矿经一次中场强磁选机(18)粗选得精矿4,中场强磁选尾矿脱磁经二次中场强磁选机(19)扫选排弃尾矿4得精矿5,精矿3、精矿4和精矿5混合得钛铁精矿(或钛砂精矿)。As shown in Figure 1, in the magnetization roasting stage, the grinding process of "grinding-gravity separation-weak magnetic separation-magnetization roasting-grinding-gravity separation-strong magnetic separation" produces ilmenite concentrate (or titanium placer). The process is : -70mm titanium ore (vanadium-titanium magnetite, titanium sand ore) is pre-selected and washed, and the -10mm ore is subjected to one-stage grinding (6), and the ore is discharged through the demagnetizing spiral classifying screen (7 ) classification, the ore greater than 3mm returns to the mill (6) for regrinding, the ore less than 3mm enters the gravity separator (11) for rough separation, and the tailings 2 are discarded to obtain the coarse concentrate 1 , and the middle ore is passed through the weak magnetic separator (12 ) roughing to obtain coarse concentrate 2 , tailings demagnetized by weak magnetic separation, filtered and dried (13), then enter the fluidized fluidized furnace (or rotary kiln or slope type roaster) for magnetization roasting (14), and magnetize roast the coarse concentrate and coarse concentrate 1. Coarse ore 2 enters the secondary mill (15) for fine grinding, and the ore discharged from the secondary mill is classified by the demagnetizing spiral sub-machine screen (or hydrocyclone) (16), and the +0.15mm ore returns to the mill (15 ) re-grinding, -0.15mm monomer dissociated minerals (purpose minerals and gangue minerals) are subjected to gravity concentrator (17) for the second re-election roughing to obtain concentrate 3 and tailings 3 , and re-centre Through the rough separation of the high-field magnetic separator (18) to obtain the concentrate 4 , the demagnetization of the tailings by the high-field magnetic separator (19) sweeps and discards the tailings 4 to obtain the concentrate 5 , Concentrate 3 , Concentrate 4 and Concentrate 5 are mixed to obtain ilmenite concentrate (or titanium sand concentrate).
如图4所示,磁化焙烧阶段磨选“磨矿一弱磁选一强磁选一磁化焙烧一磨矿一弱磁选一强磁选”工艺流程生产钛铁精矿(或钛砂矿),其过程是:-70mm钛矿(钒钛磁铁矿、钛砂矿)经预选抛尾或风化矿洗矿后-10mm的矿石经一段磨矿(6),磨机排矿经脱磁螺旋分级筛(7)分级,+3mm矿石返回磨矿机(6)再磨,-3~0mm矿石进入弱磁选机(12)粗选得粗精矿1和粗精矿2,粗精矿2脱磁进入第一次中场强磁选机(18)排弃尾矿2得粗精矿3,粗精矿3过滤干燥(13)进入沸腾炉(或回转窑或斜坡式焙烧炉)磁化焙烧(14),磁化焙烧粗精矿和粗精矿1进入第二段磨机(15)细磨,第二段磨机排矿经脱磁螺旋分级筛(或水力旋流器)(16)分级,+0.15mm矿返回二段磨矿机(15)再磨,-0.15mm矿石经弱磁选机(12)得精矿4,弱磁选尾矿经脱磁进入第二次中场强磁选机(19)得精矿5,二次中场强磁选机(19)尾矿经脱磁进入第三次中场强磁选机(20)排弃尾矿3得精矿6,精矿4、精矿5和精矿6混合得钛铁精矿(或钛砂精矿)。As shown in Figure 4, in the magnetization roasting stage, the grinding process of "grinding-weak magnetic separation-strong magnetic separation-magnetization roasting-grinding-weak magnetic separation-strong magnetic separation" produces ilmenite concentrate (or titanium placer) , the process is: -70mm titanium ore (vanadium-titanium magnetite, titanium placer) is pre-selected, thrown tailings or weathered ore washing, and -10mm ore is subjected to a stage of grinding (6), and the ore discharge of the mill is passed through the demagnetization spiral Grading sieve (7) for classification, +3mm ore returns to ore mill (6) for regrinding, -3~0mm ore enters weak magnetic separator (12) for rough separation to obtain coarse concentrate 1 and coarse concentrate 2 , coarse concentrate 2 Demagnetization enters the first high-strength magnetic separator (18) and discards the tailings 2 to obtain the coarse concentrate 3 , and the coarse concentrate 3 is filtered and dried (13) and enters the fluidized bed furnace (or rotary kiln or slope type roaster) for magnetization roasting ( 14), the magnetized roasted coarse concentrate and the coarse concentrate 1 enter the second stage mill (15) for fine grinding, and the second stage mill discharges ore and is classified by the demagnetizing spiral classifying screen (or hydrocyclone) (16), The +0.15mm ore is returned to the second-stage grinding machine (15) for regrinding, the -0.15mm ore is passed through the weak magnetic separator (12) to obtain concentrate 4 , and the tailings of the weak magnetic separation are demagnetized and enter the second high-strength magnetic separation Machine (19) gets concentrated ore 5 , and the tailings of secondary field strong magnetic separator (19) enters the third time of field strong magnetic separator (20) through demagnetization and gets rid of tailings 3 to get concentrated ore 6 , and concentrated ore 4. Concentrate 5 and concentrate 6 are mixed to obtain ilmenite concentrate (or titanium sand concentrate).
如图1、4所示,磁化焙烧阶段磨选生产的钛铁精矿(或钛砂矿)电炉冶炼生产高钛渣(熔分钛渣),其过程是:钛铁精矿(或钛砂矿),或者此钛铁精矿(或钛砂矿)和钒钛铁精矿(或钛精矿)按一定比例混合后配加粘结剂(膨润土等)及碳质还原剂混匀后(22),造球团(23),进回转窑(24)预还原或直接入炉,在电高炉或矿热炉(25)冶炼生产半钢(合金铁水)和高钛渣(熔分钛渣)(TiO2>68%),合金铁水经双联法吹钒铬,所得含钒铬的钢渣用湿法冶金提取分离钒铬,而高钛渣(熔分钛渣)隔绝空气冷却后进入重力选矿过程生产高品位酸溶性富钛料,或高钛渣(熔分钛渣)进入火法冶金选矿过程生产金红石富钛料。As shown in Figures 1 and 4, the ilmenite concentrate (or titanium sand ore) produced in the magnetization roasting stage is smelted in an electric furnace to produce high-titanium slag (melted titanium slag). The process is: ilmenite concentrate (or titanium sand) ore), or this ilmenite concentrate (or titanium placer) and vanadium-titanium iron concentrate (or titanium concentrate) are mixed in a certain proportion and added with binder (bentonite, etc.) and carbonaceous reducing agent after mixing ( 22), make pellets (23), enter the rotary kiln (24) for pre-reduction or directly enter the furnace, and produce semi-steel (alloy molten iron) and high-titanium slag (melted titanium slag) in the electric blast furnace or submerged arc furnace (25). ) (TiO 2 >68%), the alloyed molten iron is blown with vanadium and chromium by the dual method, and the obtained steel slag containing vanadium and chromium is extracted and separated by hydrometallurgy, and the high titanium slag (melted titanium slag) enters the gravity after being isolated from the air and cooled. The beneficiation process produces high-grade acid-soluble titanium-rich materials, or high-titanium slag (melted titanium slag) enters the pyrometallurgical beneficiation process to produce rutile titanium-rich materials.
如图1、4所示,利用高钛渣(熔分钛渣)生产高品位酸溶性富钛料,其过程是:高钛渣(熔分钛渣)送入用真空泵(27)抽掉空气或输入隋性气体的冷却炉(26)中冷却后,进行破碎(28),磨矿(29),重力选矿(30),尾矿加工成微晶玻璃,中矿返回电炉冶炼(25),TiO275%~92%酸酸溶性富钛料经雷蒙磨(31)磨成细度为0.045mm~0.075mm的酸溶性富钛料作为生产硫酸法钛白最理想的原料。As shown in Figures 1 and 4, the high-grade acid-soluble titanium-rich material is produced by utilizing high-titanium slag (melted titanium slag), and the process is: the high-titanium slag (melted titanium slag) is sent into the vacuum pump (27) to take out the air Or after cooling in the cooling furnace (26) of input inert gas, carry out crushing (28), ore grinding (29), gravity separation (30), tailings are processed into glass-ceramics, medium ore is returned to electric furnace smelting (25), TiO 2 75%-92% acid-acid-soluble titanium-rich material is ground by a Raymond mill (31) into an acid-soluble titanium-rich material with a fineness of 0.045mm-0.075mm, which is the most ideal raw material for the production of sulfuric acid process titanium white.
如图1、4所示,利用高钛渣(熔分钛渣)或酸溶性富钛料火法冶金选矿生产金红石富钛料,其过程是:高钛渣(熔分钛渣)或未经雷蒙磨(31)细磨的酸溶性富钛料进入保温结晶氧化炉(32),用电弧加热吹氧或用氧气一燃料喷枪或氧气(空气)直流等离子发生器向保温氧化炉(32)加热吹氧,同时加入硅石、氟化物添加剂,对高钛渣或酸溶性富钛料进行深度氧化,使高钛渣或富钛料中的主要含钛矿物黑钛石(Ti305为基的固熔体)中的低价钛氧化物氧化成八面体结构的金红石(TiO2),钙镁等杂质被排除在外,进入硅酸盐玻璃体内,形成金红石化富钛料,此金红石化富钛料在缓冷器(33)中使金红石晶粒长大冷却后经破碎(34),磨矿(35)和重选(36)排弃尾矿,得TiO2>92%~96%低钙镁人造金红石富钛料,中矿返回保温氧化炉(32)再次熔炼氧化,以提高钛的回收率,尾矿加工成微晶玻璃。如图1、4所示,利用低钙镁人造金红石富钛料(TiO2>92%~96%)生产含碳金红石富钛料,其过程是:金红石富钛料(TiO2>92%~98%)和煤(固定碳C>60%)经磨机(37)、(38)细磨到-0.045mm(-325目)和粘结剂(木浆等)配料(39)混匀(C/TiO2>20%~30%,粘结剂0.3%~0.6%),造粒(40),含碳钛粒在900℃~950℃焙烧炉内焙烧20分钟(41),然后将含碳钛粒送入用真空泵(42)抽掉空气或有隋性气体的冷却器(43)中防止含碳钛粒氧化冷却后,经双层螺旋分级筛或二台单层螺旋分级机(44)分级,-0.3mm粒级和+1.4mm粒级含碳钛粒返回磨机(37)再磨(37)循环利用,+0.3mm~-1.4mm粒级的含碳金红石富钛料作为生产氯化法金红石钛白最理想的原料。As shown in Figures 1 and 4, using high-titanium slag (melted titanium slag) or acid-soluble titanium-rich material pyrometallurgical beneficiation to produce rutile titanium-rich material, the process is: high titanium slag (melted titanium slag) or untreated The acid-soluble titanium-rich material finely ground by Raymond mill (31) enters the thermal insulation crystallization oxidation furnace (32), blows oxygen with electric arc heating or uses oxygen-fuel spray gun or oxygen (air) DC plasma generator to thermal insulation oxidation furnace (32) Heating and blowing oxygen, adding silica and fluoride additives at the same time, deeply oxidizes high-titanium slag or acid-soluble titanium-rich material, so that the main titanium-containing mineral black titanite (
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1320141C (en) * | 2005-06-16 | 2007-06-06 | 昆明理工大学 | Method for preparing rutile type titanium-rich material from primary titanium-rich material |
| CN100383051C (en) * | 2005-09-01 | 2008-04-23 | 中南大学 | Method for producing artificial rutile from rock ore type ilmenite concentrate |
| CN100357470C (en) * | 2005-09-27 | 2007-12-26 | 梅卫东 | Method for preparing ferro-titantium, steel and ferrovanadium from vanadium-titantium iron headings |
| CN101476031A (en) * | 2009-01-20 | 2009-07-08 | 杨伟 | Method for preparing magnetic attraction iron ore from non-magnetic attraction iron ore |
| CN102206044A (en) * | 2010-03-31 | 2011-10-05 | 徐州康腾微晶玻璃制品科技有限公司 | Red microcrystalline glass and manufacturing method thereof |
| CN102154531B (en) * | 2011-03-25 | 2012-12-05 | 喀左县钒钛资源综合开发利用工程技术研究中心 | Method for producing artificial rutile from titanium-containing blast furnace slags |
| CN102605184A (en) * | 2011-10-14 | 2012-07-25 | 谢廷声 | Method for producing vanadium complex iron alloy and titanium slag by sefstromite |
| CN102430472A (en) * | 2011-12-26 | 2012-05-02 | 东北大学 | A kind of direct reduction-magnetic separation separation method of vanadium-titanium magnetite |
| CN103146916B (en) * | 2013-02-25 | 2017-09-26 | 崔西川 | A kind of method of granulating of high titanium slag, golden red stone flour |
| CN103736588B (en) * | 2014-01-16 | 2014-12-17 | 玉溪大红山矿业有限公司 | Efficient beneficiation method of comprehensively recovering low-grade vanadium titano-magnetite |
| CN103736585A (en) * | 2014-01-24 | 2014-04-23 | 云南新立有色金属有限公司 | Method and system for separating high-chrome ilmenite |
| CN103949404B (en) * | 2014-03-24 | 2016-04-13 | 甘肃酒钢集团宏兴钢铁股份有限公司 | A kind of refractory iron ore fine ore graded combination processing method |
| FI20155066A (en) * | 2015-01-30 | 2016-07-31 | Outotec Finland Oy | Process for the preparation of titanium oxide containing slag and pig iron from ilmenite, and a plant |
| CN106145187A (en) * | 2015-04-24 | 2016-11-23 | 四川航都钛业科技有限公司 | A kind of use vanadium titano-magnetite or technique that titanium chats is raw material production titanium dioxide |
| CN106854705A (en) * | 2015-12-09 | 2017-06-16 | 云南冶金新立钛业有限公司 | It is suitable to ore-proportioning method and its application of titanium slag electric furnace smelting process |
| CN106498109B (en) * | 2016-11-23 | 2017-08-29 | 昆明理工大学 | A kind of method of grade titanium slag in use vanadium titano-magnetite concentrate production |
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| CN114282715A (en) * | 2021-12-17 | 2022-04-05 | 矿冶科技集团有限公司 | METHOD AND APPLICATION OF PREDICTION OF MINERALIZATION PROCESS OF VANADIUM-TINOMAGNETITE |
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