Process for the Conversion of a Solid Material Containing Hemicellulose, Cellulose and Lignin
a technology of lignin and hemicellulose, which is applied in the direction of glucose production, sugar derivates, biofuels, etc., can solve the problems of reducing the purity of the resulting product of the main hydrolysis step, the displacement is no longer uniform along the entire tube cross section, and the back mixing is reduced, and the flow rate is sufficient. , to achieve the effect of reducing the back mixing, reducing the contamination of the second hydrolysate product solution with c5
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example 1
[0155]Non-limiting FIGS. 1A, 1B, 1C, 2A and 2B illustrate an example of the process according to the invention.
[0156]The illustrated process is carried out in a reactor sequence of 6 hydrolysis reactors (R1 to R6). The hydrolysis reactors are operated at a temperature of 20° C. and a pressure of 0.1 MegaPascal. The process is operated in a sequence of cycles, each cycle being carried out within a 8 hour cycle period.
[0157]FIG. 1A illustrates the start of a new cycle. At the start of a new cycle, dried wood chips (101) have just been loaded into reactor (R1) via solid inlet line (102). Reactor (R2) contains an intermediate prehydrolysate solution and a solid material containing cellulose and lignin. The hemicellulose is already at least partly hydrolysed. Reactor (R3) contains a displacement fluid (such as for example iso-octane) and a solid material containing cellulose and lignin. Reactors (R4) and (R5) each contain an intermediate hydrolysate solution. The intermediate hydrolysate...
example 2
s of Woodchips in a Continuous Operation
Experimental Set-Up
[0176]In this lab-scale example on a vertical board 7 tubular reactors made of transparent PVC were mounted in a row, the reactors having a height of 0.53 m and a diameter of 0.053 m. Each reactor was equipped with a glass filter plate pore size 0 at the bottom and top (removable at both ends, to allow filling with woodchips and emptying lignin particles). Both bottom and top of each reactor had a liquid tight closure screwed at both ends, said closure having one (central) opening for allowing liquids to be fed to the reactor or liquids to be drained or pumped out of the reactor, with a diameter of 1 / 16 inch. All reactors were identical.
[0177]Storage tanks were present for: fresh 37% hydrochloric acid solution, tridecane displacement fluid, fresh 41-42% HCl solution (cooled to 0° C.). Also present was a tank for receiving a mixture of both used displacement fluid as well as pre-hydrolysate as well as a tank for receiving a m...
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