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Table integrated chemical synthesizer

In addition to the coal properties, the reasonable and unified boundary conditions need to be defined in order to evaluate and compare processes. The first section of Table 5.11 presents process-related variables. The gasification pressure was set to 30 bar, a typical value for integrated gasification combined cycle (IGCC) power plants as well as some chemical syntheses (e.g., Fischer-Tropsch) [60,65]. In the case of slagging entrained-flow gasification, the gasification temperature was set at >100 K above the ash fluid temperature for the reasons discussed in Section 4.5.2. A typical value is between -1-100 and -1-150 K [61]. The thermal capacity of the modeled reactors was set to a thermal input of 500 MW on the basis of the LHV as a suitable size for a state-of-the-art reactor. [Pg.156]

These four diagram types provide information for the main gas components and performance parameters as a function of O2, H2O, and fuel consumption at a glance. Because the information needed has now been defined, more complex calculations can be carried out for the two coals shown in Table 5.10 at 30 bar. This pressure is selected because of the suitability for various chemical syntheses [10] and integrated gasification combined cycle (IGCC) power generation including CO2 capture as well [11]. [Pg.292]

Some sample results of calculations of stellar yields, i.e. the mass of a nuclear species freshly synthesized and ejected from a star of given initial mass and chemical composition, are given in Tables 7.2, 7.3 and 7.4. The last column of Table 7.2 gives an IMF-integrated yield which can be compared with the Solar-System abundances. [Pg.229]

We have described an approach to host plant resistance that involves the use of plant oxidative enzymes to irrevocably deprive the insect of nutrients. We have emphasized that the chemical reactions catalyzed by POD and PPO have the potential to destroy a variety of essential or limiting amino acids (Table X). In particular, these reactions are adept at destroying lysine and cysteine. Integral lysine is necessary for proper enzymatic hydrolysis of protein. Cysteine and methionine, amongst other uses, are required to synthesize trjrpsin. The action of PPO and POD in conjunction with Pi s are proposed to place a severe strain on the insect for high sulphur amino acid intake. This strain may be further exacerbated by the complementary action of quinones... [Pg.187]


See other pages where Table integrated chemical synthesizer is mentioned: [Pg.240]    [Pg.77]    [Pg.122]    [Pg.115]    [Pg.165]    [Pg.284]    [Pg.348]    [Pg.191]    [Pg.167]    [Pg.324]   
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