“…It was confirmed a posteriori by experiments (points) and leads to an increase of 5% in the combined yield of methacrolein and methacrylic acid in comparison to an isothermal operation at 4208C. Using 2 catalysts and 3 temperature zones, an additional 4% could be added to obtain a maximum value of 76% (18). In this context, the structured bed may be considered as the reduction of a multiple step process to one.…”
Section: Structuringmentioning
confidence: 70%
“…Typical results, summarized from (9), are shown in Table 1. The analysis Figure 4: Reaction network of the partial oxidation of (A) isobutene to methacrylic acid (18) and (B) o-xylene to phthalic anhydride adapted from (9).…”
“…It was confirmed a posteriori by experiments (points) and leads to an increase of 5% in the combined yield of methacrolein and methacrylic acid in comparison to an isothermal operation at 4208C. Using 2 catalysts and 3 temperature zones, an additional 4% could be added to obtain a maximum value of 76% (18). In this context, the structured bed may be considered as the reduction of a multiple step process to one.…”
Section: Structuringmentioning
confidence: 70%
“…Typical results, summarized from (9), are shown in Table 1. The analysis Figure 4: Reaction network of the partial oxidation of (A) isobutene to methacrylic acid (18) and (B) o-xylene to phthalic anhydride adapted from (9).…”
“…Examples where the water partial pressures have been found vital include the oxidation reactions of n-butane [28], propane [29], isobutene [30], and acrolein [31] on mixed metal oxides. Consequently, certain ranges of the partial pressure (these ranges should generally be considered as ratios of the hydrocarbon to oxygen to water) can have a large benefit on the selectivity to the desired partial oxidation products.…”
Section: The Role Of Co-feeds In the Educt Streammentioning
The sections in this article are
Introduction
Analyzing the Challenge of Heterogeneously Catalyzed Alkane Oxidation
Analysis on a Microscopic Basis of the Critical Steps of Paraffin Oxidation Utilizing Solid Catalysts Utilizing Solid Catalysts
A
Activation of Oxygen and Paraffin
B
Models for the Active Site
C
The Role of
Co
‐Feeds in the Educt Stream
D
The Role of the Crystalline Nature and the Admixture of Different Crystalline Phases for the Catalyst
E
The Role of the Acid–Base Interaction of Reactant and Catalyst
Analysis of the Technical Challenges of Paraffin Oxidation Utilizing Solid Catalysts
Conversion of Butane to Maleic Anhydride: An Overview of a Mature Technology
Manufacturing Technologies for
MA
from
n
‐Butane
The
VPO
‐Catalyst: Structural Basis and Synthetic Pathways
The
VPO
‐Catalyst: Reaction Pathways and Potential Active Sites of the Catalyst
Propane Oxidation to Acrylic Acid and Acrylonitrile: Getting Closer to a Technical Solution
Rutile‐Based Structures for Selective Propane Oxidation
Complex Bronze Structures Based on Molybdenum for Selective Propane Oxidation
Ethane to Acetic Acid: The Search for a Viable Pathway
Outlook
Acknowledgments
“…41 On a fundamental level, such reaction networks were mainly predicted from simulations and kinetic studies in the past. 42–47 Since the assumptions for such kinetic models ( e.g. , low conversion, isothermal conditions) are often rather simplified, more realistic parameters need to be considered to optimise the catalytic processes under operating conditions.…”
Improving process efficiency in selective oxidation of lower olefins over mixed metal oxide catalysts requires profound knowledge on the dynamic behaviour of exothermic reactions along the reactor. For this purpose,...
scite is a Brooklyn-based organization that helps researchers better discover and understand research articles through Smart Citations–citations that display the context of the citation and describe whether the article provides supporting or contrasting evidence. scite is used by students and researchers from around the world and is funded in part by the National Science Foundation and the National Institute on Drug Abuse of the National Institutes of Health.