会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 6. 发明申请
    • METHOD AND APPARATUS FOR PRODUCING DIRECT REDUCED IRON UTILIZING A CATALYTICAL PRETREATMENT OF HYDROCARBONS AS A SOURCE OF REDUCING GAS
    • 利用催化预处理作为还原气源的烃生产直接还原铁的方法和设备
    • WO2018024767A1
    • 2018-02-08
    • PCT/EP2017/069517
    • 2017-08-02
    • DANIELI & C. OFFICINE MECCANICHE S.P.A.HYL TECHNOLOGIES S.A. DE C.V.
    • CONDOSTA, MicheleDALLE NOGARE, DanielaPRIMAVERA, AlessandraMARTINIS, AlessandroZENDEJAS MARTINEZ, Eugenio
    • C21B13/00
    • A method and apparatus for producing direct reduced iron, said method comprising producing direct reduced iron using a pre-treated make-up gas as a reducing agent in a direct reduced iron reactor (10), and wherein producing direct reduced iron is carried-out using a zero-reformer process in which catalytic reformation of the pre-treated make-up gas is carried-out "in situ" within the direct reduced iron reactor (10) such that the pre-treated make-up gas is subjected to no further catalytic reaction besides the catalytic reactions that occur inside said direct reduced iron reactor (10),characterized in thatsaid method comprises: - pre-treating a stream of said make-up gas containing heavy hydrocarbons by subjecting the stream of make-up gas to a low temperature adiabatic reforming at a temperature comprised between 300°C and 600°C, prior to using said stream of make-up gas as a reducing agent for producing direct reduced iron; - subjecting said pre-treated stream of make-up gas to adjusting humidity content of said stream of make-up gas after said low temperature adiabatic reforming by bypassing said stream of make-up gas to selectively split said stream into a first part (128) of said stream of make-up gas and a second part (130) of said stream of make-up gas and subjecting said first part (128) to a water separation and then mixing said first part (128) to said second part (130) to obtain a reducing stream (146) to be sent to direct reduced iron production.
    • 一种用于生产直接还原铁的方法和设备,所述方法包括在直接还原铁反应器(10)中使用预处理的补充气体作为还原剂生产直接还原铁,并且其中 使用零重整器工艺进行生产直接还原铁的工艺,其中预处理的补充气体的催化重整是“原位”进行的。 在所述直接还原铁反应器(10)内,使得经预处理的补充气体除了在所述直接还原铁反应器(10)内发生的催化反应外不再发生催化反应,其特征在于,所述方法包括: - 在使用所述补充气流之前,通过使补充气体流经受在300℃和600℃之间的温度下的低温绝热重整,处理含有重质烃的所述补充气体流 气体作为生产直接还原铁的还原剂; - 在所述低温绝热重整之后,通过绕过所述补充气体流选择性地将所述流分成第一部分(128),使所述预处理补充气体流经过所述补​​充气体流调整湿度含量 )所述补充气体流和所述补充气体流的第二部分(130),并使所述第一部分(128)经历水分离,然后将所述第一部分(128)混合到所述第二部分(128) 130)以获得还原流(146),以发送至还原铁生产指导。
    • 7. 发明申请
    • METHOD AND APPARATUS FOR PRODUCTION OF DIRECT REDUCED IRON (DRI) UTILIZING COKE OVEN GAS
    • 利用焦炉煤气生产直接还原铁(DRI)的方法和设备
    • WO2013093640A2
    • 2013-06-27
    • PCT/IB2012/003062
    • 2012-12-21
    • HYL TECHNOLOGIES, S.A. DE C.V.DANIELI & C. OFFICINE MECCANICHE, S.P.A.
    • MARTINIS, AlessandroBECERRA-NOVOA, Jorge-octavioCONDOSTA, MicheleZENDEJAS-MARTINEZ, Eugenio
    • C21B13/00
    • C21B13/0073C01B2203/0227C01B2203/025C10G9/16C10G75/00C21B13/02C21B13/029C21B2100/66F27D25/00F27D25/008Y02P10/122Y02P10/126Y02P10/128Y02P10/136Y02P10/265Y02P10/283
    • Direct reduction process and plant for producing DRI comprising a reduction reactor and at least one reducing gas heater typically comprising a convective heating section and a radiant heating section for raising the reducing gas temperature to a level adequate for iron oxides reduction to metallic iron, typically above 850°C, wherein the reducing gas fed to the reduction reactor comprises a stream of reducing gas recycled from the reduction reactor and a make-up stream of coke oven gas containing carbon compounds which may form carbon deposits in the heating path of said heater, namely BTX and other complex carbon compounds. The heater is provided with means for feeding oxidizing agents, for example steam, steam and air and/or oxygen at predetermined heating tubes successively for eliminating the carbon deposits which may form inside the heating tubes of said heater without interrupting the operation of the plant. The make-up stream of cold COG can be combined with the recycled gas at a point in the gas heating path of the heater where the tubes have a skin wall temperature of at least 700°C, or when the mixture of recycled gas and COG is at a temperature above 700°C for minimizing clogging or fouling of heating equipment.
    • 用于生产DRI的直接还原方法和设备包括还原反应器和至少一个还原气体加热器,所述还原气体加热器通常包括对流加热部分和辐射加热部分,用于将还原气体温度升高到足以使铁 氧化物还原成金属铁,典型地在850℃以上,其中供入还原反应器的还原气体包括从还原反应器循环的还原气流和含碳化合物的焦炉气的补充气流,所述碳化合物可形成碳沉积物 在所述加热器的加热路径中,即BTX和其他复合碳化合物。 加热器设有用于在预定的加热管处连续供给氧化剂例如蒸汽,蒸汽和空气和/或氧气的装置,以消除可能在所述加热器的加热管内部形成的积碳,而不中断设备的运行。 冷COG的补充流可以与加热器的气体加热路径中的点处的再循环气体结合,其中管的壁表面温度为至少700℃,或者当再循环气体和COG的混合物 处于700℃以上的温度以最小化加热设备的堵塞或结垢。