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Table 6 : Input and output base features for chemical plant control problem.
Table 2. Summary of Proposed Energy-Efficiency Measures at Avdeevka Coke Chemical Plant
"... In PAGE 6: ... The end-use energy efficiency measures are thus an integral part of the proposed strategy for improving energy efficiency at Avdeevka. Table2 lists the proposed energy-efficiency measures recommended for implementation at Avdeevka Coke Chemical Plant. These measures are all cost-effective, with returns on investment ranging from 15% to over 1000%.... ..."
Table 2: Results for CHEMIMP: Chemical engineering plant models
"... In PAGE 11: ... We test the column interchange algorithm described in Section 3. The results are given in Table2 . The value of d is specified before and after the column interchange has been done.... ..."
Table 2: Results for CHEMIMP: Chemical engineering plant models
"... In PAGE 11: ... We test the column interchange algorithm described in Section 3. The results are given in Table2 . The value of d is speci ed before and after the column interchange has been done.... ..."
Table 2. Ranking of the 5 input features of the chemical plant data set from [27]
"... In PAGE 12: ... According to the ICM analyzer the third variable is the most important, then the flrst, while the remaining three were considered irrelevant. These results are compared with the FRFCO method in Table2 . The optimal number of clusters is again 6.... ..."
Table 5. Example of Phased Energy Efficiency Project at a Coke Chemical Plant
"... In PAGE 34: ... Jotting down your ideas and your reasons for organizing the project in the way you propose will help you later when you write your business plan. Table5 provides an example of how a project can be broken into phases. Table 5.... ..."
Table 3. The importance of different sources of information. A comparison of estimates by Swedish inspectors (n=10) and small European chemical companies (n=132)
"... In PAGE 4: ...ion. A scale was used, ranging from 1 (not important at all) to 5 (extremely important). This part of the questionnaire was designed to be in agreement with an previous survey addressing small chemical plants in five European countries [2 amp; 6]. Table3 shows the results from these questions to the inspectors, and... ..."
Table 3. The importance of different sources of information. A comparison of estimates by Swedish inspectors (n=10) and small European chemical companies (n=132)
in Proceedings of the 1st International Conference on Occupational Risk Prevention. ISBN 84-699-1242-9
"... In PAGE 4: ...ion. A scale was used, ranging from 1 (not important at all) to 5 (extremely important). This part of the questionnaire was designed to be in agreement with an previous survey addressing small chemical plants in five European countries [2 amp; 6]. Table3 shows the results from these questions to the inspectors, and... ..."
Table 4 Assumed composition of corn stover delivered to the plant gate
2004
"... In PAGE 16: ... Delivered feedstock cost rises by only $3/dry mt for the first 25 plants, but then jumps by $20/dry mt for the last ten plants. Modeling of the Ethanol Conversion Facility Table4 summarizes the chemical composition of the corn stover assumed in our process design (Sheehan et al. 2002).... ..."
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Table 1 Concentrations of chemical compounds in the process liquids.
1997
"... In PAGE 2: ...ontainers (see Fig. 2), is utilized. The goal of the control is to neutralize the process flow coming to the mixing vessel. Pilot plant tests were carried out using four different types of process liquids (I, II, III and IV; see Table1 and Fig. 3) and with two different process flow rates, 0.... ..."
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