首页> 外国专利> Controlling operation of steam reformer, comprises producing synthesis gas having e.g. hydrogen from hydrocarbon-containing input and water vapor, and guiding water vapor steam through steam reformer in first and second temperature regions

Controlling operation of steam reformer, comprises producing synthesis gas having e.g. hydrogen from hydrocarbon-containing input and water vapor, and guiding water vapor steam through steam reformer in first and second temperature regions

机译:控制蒸汽重整器的操作,包括产生具有例如10%的合成气。来自含烃输入物和水蒸气的氢,并在第一和第二温度区域引导水蒸气通过蒸汽重整器

摘要

The method for controlling the operation of steam reformer (14), comprises producing a synthesis gas comprising carbon monoxide and hydrogen from a hydrocarbon-containing input and water vapor, and guiding water vapor steam through the steam reformer in a first temperature region below the predetermined temperature, where the specific heat capacity of the steam reformer is kept above the predetermined temperature limit value, which increases with the temperature at a specific value during the warm start of the steam reformer. The method for controlling the operation of steam reformer (14), comprises producing a synthesis gas comprising carbon monoxide and hydrogen from a hydrocarbon-containing input and water vapor, guiding water vapor steam through the steam reformer in a first temperature region below the predetermined temperature, where the specific heat capacity of the steam reformer is kept above a predetermined temperature limit value, which increases with the temperature at a specific value during the warm start of the steam reformer, and guiding the water vapor steam through the steam reformer in a second temperature region above the predetermined temperature, where the specific heat capacity of the steam reformer is kept above the predetermined temperature limit value, which is constant at a specific value during the warm start of the steam reformer. The temperature limit of the specific heat capacity of the water vapor stream increases linearly with the temperature at specific value in the first temperature region. The predetermined temperature is 750[deg] C. The specific value of the specific heat capacity of the water vapor stream is 200 kJ/hour[deg] C. The flow-rate of the water vapor steam in each reformer tube of the steam reformer is kept at 95 kg/hour in the second temperature region.
机译:用于控制蒸汽重整器(14)的操作的方法,包括从含烃输入物和水蒸气产生包含一氧化碳和氢的合成气,以及在低于预定温度的第一温度区域中引导水蒸气通过蒸汽重整器。蒸汽重整器的比热容保持在预定温度极限值以上的温度,该温度在蒸汽重整器的热启动期间随温度达到特定值而增加。用于控制蒸汽重整器(14)的操作的方法,包括从含烃输入物和水蒸气产生包含一氧化碳和氢的合成气,在低于预定温度的第一温度区域中引导水蒸气通过蒸汽重整器。 ,其中蒸汽重整器的比热容保持在预定温度极限值以上,该温度极限值在蒸汽重整器热启动期间随温度升高到特定值而增加,并在第二秒内引导水蒸气通过蒸汽重整器在预定温度以上的温度区域,蒸汽重整器的比热容保持在预定温度极限值以上,该预定温度极限值在蒸汽重整器的热启动期间恒定在特定值。水蒸气流的比热容的温度极限随着温度在第一温度区域中的特定值线性增加。预定温度为750℃。水蒸气流的比热容的比值为200kJ /小时℃。蒸汽重整器的每个重整管中水蒸气的流量。在第二温度区域保持在95公斤/小时。

著录项

  • 公开/公告号DE102008046800A1

    专利类型

  • 公开/公告日2010-03-18

    原文格式PDF

  • 申请/专利权人 LINDE AG;

    申请/专利号DE20081046800

  • 发明设计人 RIETH WILHELM;

    申请日2008-09-11

  • 分类号C01B3/32;

  • 国家 DE

  • 入库时间 2022-08-21 18:28:47

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