摘要:
A modified ⊖-Al2O3-supported nickel reforming catalyst and its use for producing synthesis gas from natural gas, more specifically to a nickel reforming catalyst expressed by the following formula 1, having improved coke resistance, high-temperature catalysis stability and catalytic activity, which is prepared by coating nickel or mixture of nickel and cocatalyst (M1-M2-Ni) on a Al2O3 support modified with metal (M3-M4-ZrO2/⊖-Al2O3), and its use for producing synthesis gas from natural gas through steam reforming, oxygen reforming or steam-oxygen reforming, M1-M2-Ni/M3-M4-ZrO2/⊖-Al2O3 (1) wherein M1 is an alkali metal; each of M2 and M3 is an alkaline earth metal; and M4 is a IIIB element or a lanthanide.
摘要翻译:改性的⊖-Al 2 O 3负载的镍重整催化剂及其用于从天然气制备合成气的用途,更具体地说,涉及由下式1表示的镍重整催化剂,具有改善的耐焦性,高温催化稳定性和催化活性, 通过在用金属(M3-M4-ZrO2 /⊖-Al2O3)改性的Al 2 O 3载体上涂覆镍或镍和助催化剂(M1-M2-Ni)的混合物制备,以及其用于通过蒸汽重整从天然气生产合成气的用途 ,氧气重整或蒸汽 - 氧气重整,其中M1是碱金属; M2和M3各自为碱土金属; M4是IIIB元素或镧系元素。
摘要:
A modified &thgr;-Al2O3-supported nickel reforming catalyst and its use for producing synthesis gas from natural gas, more specifically to a nickel reforming catalyst expressed by the following formula 1, having improved coke resistance, high-temperature catalysis stability and catalytic activity, which is prepared by coating nickel or mixture of nickel and cocatalyst (M1—M2—Ni) on a &thgr;-Al2O3 support modified with metal (M3—M4—ZrO2/&thgr;-Al2O3), and its use for producing synthesis gas from natural gas through steam reforming, oxygen reforming or steam-oxygen reforming, M1—M2—Ni/M3—M4—ZrO2/&thgr;-Al2O3 (1) wherein M1 is an alkali metal, each of M2 and M3 is an alkaline earth metal; and M4 is a IIIB element or a lanthanide.
摘要翻译:改性的θ-Al 2 O 3负载的镍重整催化剂及其用于从天然气生产合成气的用途,更具体地说,涉及由下式1表示的镍重整催化剂,具有改善的耐焦性,高温催化稳定性和催化活性, 通过在用金属(M3-M4-ZrO 2 /θ-Al 2 O 3)改性的θ-Al 2 O 3载体上涂覆镍或镍和助催化剂(M1-M2-Ni)的混合物制备,以及其用于从天然气生产合成气的用途 蒸汽重整,氧气重整或蒸汽 - 氧气重整,其中M1是碱金属,M2和M3各自是碱土金属; M4是IIIB元素或镧系元素。
摘要:
Disclosed is a plate type steam reformer comprising a plate type burner capable of heating a broad area of a reactor as a heat source, positioned on a bottom of the reformer; a reforming reactor requiring a relatively high temperature, positioned over the burner; a high temperature water gas shift reactor requiring a relatively moderate temperature, positioned over the reforming reactor; a low temperature water gas shift reactor requiring a relatively low temperature, positioned over the high temperature water gas shift reactor; and dividing plates positioned between the above three reactors and between the reforming reactor and the burner such that combustion exhaust gas produced in the burner supplies heat to the above reactors.
摘要:
The compact steam reformer of the present invention integrally comprises a housing; a reforming reactor having an upper mixing compartment for mixing natural gas and steam and a lower compartment for accommodating a catalyst bed; a natural gas feeding coiled pipe through which natural gas is introduced while being heated; a steam generating coiled pipe in which pure water is converted to steam by the exhaust; a metal fiber burner for heating the reforming reactor; a high-temperature converter for primarily removing carbon monoxide from a synthetic gas; a low-temperature converter for secondarily reducing the carbon monoxide level of the synthetic gas; and a heat exchanger, provided between the high-temperature converter and the low-temperature converter, for cooling the gas effluent from the high-temperature converter.