A catalyst preparation method for methane carbon dioxide reforming to synthesis gas
A carbon dioxide and catalyst technology, which is applied in the field of preparation of supported nickel-based catalysts, can solve the problems of low metal utilization in carrier channels, accelerate product deep oxidation, increase catalyst cost, etc., improve conversion rate and product selectivity, and avoid further Oxidation, the effect of accelerating the adsorption and desorption speed
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0027] The spent hydrotreating catalyst (MoCo / Al 2 o 3), the oil on the surface of the catalyst was removed by extraction, and dried at 110°C for 8 h. The obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 9.1wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.8wt% of catalyst precursor A weight in terms of elements, Ni accounting for 3.1wt% of catalyst precursor A weight in terms of elements, V accounting for 1.9wt% of catalyst precursor A weight in terms of elements; Activation in a mixed atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction conditions are 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the reduced and activated catalyst precursor A is mixed with 300mL of 10% mass concentration of Sorbet Add the alcohol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3M...
Embodiment 2
[0029] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, and dried at 110°C for 8 h. The obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 9.1wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.8wt% of catalyst precursor A weight in terms of elements, Ni accounting for 3.1wt% of catalyst precursor A weight in terms of elements, V accounting for 1.9wt% of catalyst precursor A weight in terms of elements; Activation in a mixed atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction conditions are 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the reduced and activated catalyst precursor A is mixed with 300mL of 10% mass concentration of Sorbet Add the alcohol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3...
Embodiment 3
[0031] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, and dried at 110°C for 8 h. The obtained catalyst was calcined at 450°C for 4 h to obtain catalyst precursor A, in which Mo accounted for 9.1wt% of the weight of catalyst precursor A in terms of elements, and Co was Accounting for 1.8wt% of catalyst precursor A weight in terms of elements, Ni accounting for 3.1wt% of catalyst precursor A weight in terms of elements, V accounting for 1.9wt% of catalyst precursor A weight in terms of elements; Activation in a mixed atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction conditions are 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the reduced and activated catalyst precursor A is mixed with 300mL of 10% mass concentration of Sorbet Add the alcohol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com