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Product yields with temperature wood chips

ABSTRACT The radiative pyrolysis of wood (thick cylinders and chip beds) has been investigated experimentally for external radiative heat fluxes in the range 28-80kW/m, resulting in maximum sample temperatures of 600-950K. Radial temperature profiles, product yields and composition, and devolatilization rates have been measured. The influences of wood variety (hardwoods and softwoods) on the pyrolysis characteristics are discussed and comparisons are made with biomass (agricultural residues). [Pg.1143]

Although hardwoods have a lower lignin content and so give a higher yield of sugars, softwoods are preferred where ethanol is the desired end product. This is because hardwoods have more pentose sugars, which are not readily fermented by common yeasts. In a typical batch process sawdust and wood chips are loaded into the reactor vessel and treated with dilute sulphuric acid (0.5% concentration) at temperatures between 130 and 200°C for about three hours. Ideally, the sugars should be removed from the reaction zone before they, in turn, have time to break down. [Pg.551]

Commercially, most cellulose is extracted from wood by one of two methods, the kraft (sulfate) process or the steam explosion process. The product of these reactions is wood pulp, which consists primarily of cellulose. In the kraft process, wood chips are treated with a solution of sodium hydroxide (NaOH) and sodium sulfide (Na2S) at temperatures of about 175°C (35o°F) for two to six hours. This process usually results in a yield of about 40 to 45 percent wood pulp. The pulp is then treated with a bleaching agent, such as calcium or sodium hypochlorite (Ca(0Cl)2 or NaCIO) or chlorine dioxide (C102) to remove the color of lignin and other impurities. [Pg.197]

If an especially good product is desired, the recrystallized material is sublimed at 130-140°/1 mm. A still better product with no trace of color may be obtained by subliming the recrystallized tetracyanoethylene through activated carbon. For example, 35 g. of tetracyanoethylene is placed in a glass thimble and covered with 20-25 g. of activated wood charcoal chips (4-8 mesh). The mouth of the thimble is covered with a coarse grade of filter paper which is held in place by wiring. The thimble is placed in a sublimer, and the sublimation is carried out at 1-2 mm. (bath temperature 175-190°). The tetracyanoethylene is recovered in 80-90% yield as a colorless, hard crystalline mass that melts at 201-202° (sealed tube). [Pg.67]

Several extraction processes for production of larch arabinogalactan have been patented. All involve chipping or grinding larch heartwood - generally waste wood and the butt cut - and extracting the finely divided wood with water. The rate of extraction is dependent upon the size of the chips and the extraction temperature the yield is dependent upon the amount of gum present in the raw material (6). [Pg.980]


See other pages where Product yields with temperature wood chips is mentioned: [Pg.26]    [Pg.156]    [Pg.238]    [Pg.156]    [Pg.26]    [Pg.245]    [Pg.257]    [Pg.311]    [Pg.318]    [Pg.480]    [Pg.11]    [Pg.1360]    [Pg.304]    [Pg.447]    [Pg.882]    [Pg.321]    [Pg.332]    [Pg.121]   
See also in sourсe #XX -- [ Pg.234 ]




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