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Multiple feedstocks

Scenario-1 Single Feedstock, Multiple Refineries with No Integration... [Pg.70]

Scenario-4 Multiple Feedstocks, Multiple Refineries with Integration and Increased Market Demand... [Pg.74]

Phase II biorefinery (single feedstock, multiple processes and multiple major products)... [Pg.6]

Plasma fractionation is unusual in pharmaceutical manufacturing because it involves the processing of proteins and the preparation of multiple products from a single feedstock. A wide range of unit operations are utilized to accompHsh these tasks. They are Hsted in Table 3 some are common to a number of products and all must be closely integrated. The overall manufacturing operation can be represented as a set of individual product streams, each based on the processing of an intermediate product derived from a mainstream fractionation process (Fig. 1). [Pg.527]

Internal sultones, formed from internal alkenes, may also occur. These react less readily than corresponding terminal sultones. In addition, feedstock materials contain alkenes with multiple points of unsaturation, which may form unsaturated sultones such as the unsaturated y-sultone upon sulfonation. [Pg.444]

Engineered biocatalysts with altered specificity have been developed. A Rhodococcus strain capable of DBT as well as BT desulfurization has been developed by cloning dsz genes into a strain-containing BT desulfurization pathway. The variety of sulfur compounds in petroleum feedstocks and complexity of the problem may require use of a consortium rather than a single bacterial strain. Alternately, use of multiple bioreactors each with a single dominant strain may be employed to achieve maximum desulfurization [299],... [Pg.146]

Fig. 19.3. Example of high-resolution experiments on complex mixtures, showing the multiple elemental compositions possible at a single nominal mass. Top panel four elemental compositions at m/z 225 in the positive ion electrospray mass spectrum of a diesel oil feedstock (from Wu et al. [17]). Bottom panel multiple compositions at m/z 455 in the negative ion electrospray spectrum of olive oil (from Marshall et al. [18]). Fig. 19.3. Example of high-resolution experiments on complex mixtures, showing the multiple elemental compositions possible at a single nominal mass. Top panel four elemental compositions at m/z 225 in the positive ion electrospray mass spectrum of a diesel oil feedstock (from Wu et al. [17]). Bottom panel multiple compositions at m/z 455 in the negative ion electrospray spectrum of olive oil (from Marshall et al. [18]).
Ensuring a constant feed supply is very important, because most of the biomass is only available on a seasonal basis. In such cases continuous operation of the conversion facility will require either extensive long-term storage of the feedstock or a feed reactor that is flexible enough to accommodate multiple feedstocks. Most thermal conversion processes demand a finely divided, substantially dry feed and therefore some pre-treatment is required to match the feedstock to the process. The main pre-treatment operations are [19] ... [Pg.148]

The biomass is fed overbed through multiple feed chutes using air jets to help distribute the fuel over the surface of the bed. Variable-speed screw conveyors are usually used to meter the fuel feed rate and control steam output. Feedstocks such as bark and waste wood are chipped to a top size of 25 mm (1 in) to ensure complete combustion. The bed usually consists of sand around 1 m (3 ft) deep. This serves to retain the fuel in the furnace, extending its in-furnace residence time and increasing combustion efficiency. It also provides a heat sink to help maintain bed temperature during periods of fluctuating fuel moisture content. [Pg.39]

Hydrogen production from carbonaceous feedstocks requires multiple catalytic reaction steps For the production of high-purity hydrogen, the reforming of fuels is followed by two water-gas shift reaction steps, a final carbon monoxide purification and carbon dioxide removal. Steam reforming, partial oxidation and autothermal reforming of methane are well-developed processes for the production of hydro-... [Pg.113]


See other pages where Multiple feedstocks is mentioned: [Pg.534]    [Pg.185]    [Pg.180]    [Pg.81]    [Pg.378]    [Pg.426]    [Pg.235]    [Pg.483]    [Pg.440]    [Pg.218]    [Pg.1005]    [Pg.58]    [Pg.212]    [Pg.223]    [Pg.92]    [Pg.224]    [Pg.42]    [Pg.90]    [Pg.140]    [Pg.56]    [Pg.72]    [Pg.439]    [Pg.379]    [Pg.558]    [Pg.213]    [Pg.4]   
See also in sourсe #XX -- [ Pg.72 , Pg.73 , Pg.74 ]

See also in sourсe #XX -- [ Pg.72 , Pg.73 , Pg.74 ]




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Scenario-1 Single Feedstock, Multiple Refineries with No Integration

Scenario-2 Single Feedstock, Multiple Refineries with Integration

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