Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Process improvement limiting

The i j -configuration of the 6,7-double bond in pre-vitamin D is critical to its subsequent thermal rearrangement to the active vitamin. A photochemical isomerization of pre-vitamin D to yield the inactive trans-isoTnen occurs under conditions of synthesis, and is especially detrimental if there is a significant short wavelength component, eg, 254 nm, to the radiation continuum used to effect the synthesis. This side reaction reduces overall yield of the process and limits conversion yields to ca 60% (71). Photochemical reconversion of the inactive side product, tachysterol, to pre-vitamin D allows recovery of the product which would otherwise be lost, and improves economics of the overall process (70). [Pg.392]

The critical characteristic on each component was analysed, calculated from the analysis and the value obtained was plotted against the process capability indices, Cpk and Cp, for the characteristic in question. See Appendix V for descriptions of the 21 components analysed, including the values of Cp and Cp from the SPC data supplied. Note that some components studied have a zero process capability index. This is a default value given if the process capability index calculated from the SPC data had a mean outside either one of the tolerance limits, which was the case for some of the components submitted. Although it is recognized that negative process capability indices are used for the aim of process improvement, they have little use in the analyses here. A correlation between positive values (or values which are at least within the tolerance limits) will yield a more deterministic relationship between design capability and estimated process capability. [Pg.57]

MW fraction increases the melt flow, thus improving the processability but at the cost of toughness, stiffness, and stress crack resistance. In addition, the improvement in performance through narrowing the MWD is restricted by the catalyst, the process hardware, and the process control limitations. Dow has developed a reactor grade HDPE of optimized breadth, peak, and shape of MWD... [Pg.289]

Much has been published about simulations of research and development (R D), but in the area of research process improvement there are still many challenges. This chapter consists of two main parts, covering current approaches, which have met limited acceptance, and newer approaches aimed more directly at overcoming the most likely areas of cognitive difficulty that research managers face when making decisions on performance improvement. [Pg.248]

Ahluwalia and Goyal94 have pointed out some disadvantages of biosorption such as the early saturation of biomass, which can be a problem since metal desorption is necessary prior to further use, irrespective of the metal value. Furthermore, the potential for biological process improvement is limited because cells are not performing an active metabolism. [Pg.398]

In a later publication [ 129], using the same equipment, Liu et al. describe process improvements in the electrochemical fluorination of octanoyl chloride in which formation of polymeric tar at the anode surface was limited by addition of a mercaptan (1-methyl-1-propanethiol), and by constant current density operation (7 mA cm-2). Continuous operation was achieved by frequent additions of a solution of reactant in hydrogen fluoride. Conversion of reactant to perfluori-nated products was increased to 80%, with good selectivity. [Pg.225]

Despite the limited data in the area of viscosity, the results reported so far are encouraging they indicate possible applications of polyrotaxanes in rheology control and melt processability improvement. [Pg.315]

Tn commercial petroleum refining, isomerization of light paraffins has been A applied for many years. Until recently the scope of the process was limited, however, and its main application was isomerization of butane as feed preparation for alkylation processes. Generally, except for a few specific cases, no commercial justification could be found for isomerization of pentane and hexane fractions since in most cases the quality requirements for motor gasoline could be met by alternative processing routes and by addition of various additives, such as lead tetraalkyls, to improve fuel burning characteristics. [Pg.526]

This chapter describes the discovery of a new asymmetric isomerization process, improvements in the catalyst, some practical aspects, and the scope and limitation of the process, with emphasis on developments during commercial manufacturing [4],... [Pg.146]


See other pages where Process improvement limiting is mentioned: [Pg.309]    [Pg.518]    [Pg.208]    [Pg.47]    [Pg.153]    [Pg.93]    [Pg.100]    [Pg.9]    [Pg.323]    [Pg.215]    [Pg.215]    [Pg.229]    [Pg.37]    [Pg.538]    [Pg.83]    [Pg.213]    [Pg.9]    [Pg.15]    [Pg.59]    [Pg.292]    [Pg.317]    [Pg.322]    [Pg.158]    [Pg.706]    [Pg.167]    [Pg.309]    [Pg.518]    [Pg.938]    [Pg.954]    [Pg.731]    [Pg.777]    [Pg.200]    [Pg.789]    [Pg.554]    [Pg.197]    [Pg.79]    [Pg.9]    [Pg.421]    [Pg.84]    [Pg.83]    [Pg.209]    [Pg.436]   


SEARCH



Limiting processes

Process limitations

Processes process improvement

Processing improvement

Processing limitations

Processing process limitations

© 2024 chempedia.info