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    • 2. 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。