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Process development data

Analysis of process development data - The following illustrates how PDU data can be used to develop a commercial SCFCO2 plant s process design. This data is provided by Marc Sims on pyrethrins, a natural insecticide extracted with subcritical and supercritical carbon dioxide from pyrethrum flowers (a species of chrysanthemum). [Pg.137]

Utilization of process development data for process design and economic evaluation of alternative commercial plant designs ... [Pg.143]

Laborelec s future realisations are vibration analysis, control of inspection robots, and all types of system monitoring. LabVIEW will be used as common tool for developers for the coming years. The synergy effect of a common language for everything concerning acquisition, analysis and processing of data will be beneficial for the whole company. [Pg.1009]

Based on the bench-scale data, two coal-to-acetylene processes were taken to the pilot-plant level. These were the AVCO and Hbls arc-coal processes. The Avco process development centered on identifying fundamental process relationships (29). Preliminary data analysis was simplified by first combining two of three independent variables, power and gas flow, into a single enthalpy term. The variation of the important criteria, specific energy requirements (SER), concentration, and yield with enthalpy are indicated in Figure 12. As the plots show, minimum SER is achieved at an enthalpy of about 5300 kW/(m /s) (2.5 kW/cfm), whereas maximum acetylene concentrations and yield are obtained at about 7400 kW/(m /s) (3.5 kW/cfm). An operating enthalpy between these two values should, therefore, be optimum. Based on the results of this work and the need to demonstrate the process at... [Pg.391]

The data most frequentiy collected and reported in catalyst performance evaluations are activity or turnover number, selectivity to the desired product(s), overall yield, catalyst life, and the identities and yields of by-products produced. These data are used to further catalyst or process development research efforts, to monitor catalyst manufacture, and to provide quaUty assurance information to catalyst users. [Pg.197]

During process development, a model can be developed as soon as a conceptual flow sheet has been formulated. This model can be updated as more information about the process is obtained. Even at an early stage in the project, the model can be used to assess the preliminary economics of the process and the effect of technological changes on these economics. The model can aid in interpreting pilot-plant data and allows the study of many process alternatives. [Pg.72]

Direct-Liquefaction Kinetics All direct-liquefac tion processes consist of three basic steps (1) coal slurrying in a vehicle solvent, (2) coal dissolution under high pressure and temperature, and (3) transfer of hydrogen to the dissolved coal. However, the specific reac tion pathways and associated kinetics are not known in detail. Overall reaction schemes and semiempirical relationships have been generated by the individual process developers, but apphcations are process specific and limited to the range of the specific data bases. More extensive research into liquefaction kinetics has been conducted on the laboratory scale, and these results are discussed below. [Pg.2372]

It is not unusual to have several inherent safety reviews during the product/process development effort. Early reviews will often not have all of the information required for Steps 1 to 9. The follow-up items will describe what is necessary to obtain the missing information such as toxicity data on new intermediates or products of undesired reactions. [Pg.122]

The overall process of data interpretation and the development of suitable remedial strategies once a set of causes has been identified, is set out in Figure 6.4. The two-stage process of confirming the initial causal hypothesis is recommended to overcome the tendency to jump to a premature conclusion and to interpret all subsequent information on the basis of this conclusion. [Pg.268]

Gasification Process-Development Unit from fault trees Unavailability data systems and components ... [Pg.41]

DATA BOUNDARY Coal-gasification Process Development unit systems and... [Pg.50]

In this study detailed fault trees with probability and failure rate calculations were generated for the events (1) Fatality due to Explosion, Fire, Toxic Release or Asphyxiation at the Process Development Unit (PDU) Coal Gasification Process and (2) Loss of Availability of the PDU. The fault trees for the PDU were synthesized by Design Sciences, Inc., and then subjected to multiple reviews by Combustion Engineering. The steps involved in hazard identification and evaluation, fault tree generation, probability assessment, and design alteration are presented in the main body of this report. The fault trees, cut sets, failure rate data and unavailability calculations are included as attachments to this report. Although both safety and reliability trees have been constructed for the PDU, the verification and analysis of these trees were not completed as a result of the curtailment of the demonstration plant project. Certain items not completed for the PDU risk and reliability assessment are listed. [Pg.50]

The earher the information on resource efficiency is used in synthesis design, the more efficient process development wiU be. Therefore, appropriate metrics are initially applied to a choice of literature protocols and prehminary experimental data. As knowledge about the process increases, for example, during scale up, it is successively fed into the mass balance. In addition, environmental impacts associated with the mass balance can be evaluated. [Pg.200]


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