Method to reduce energy consumption during biomass pretreatment
A pretreatment, biomass technology, applied in water/steam pretreatment, fiber raw material treatment, fuel, etc., can solve the problems of industrial-scale application of pretreatment methods with high energy cost
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Embodiment 1-0
[0068] Embodiment 1-0 (comparative example) wheat straw (moisture content 15wt.-%)
[0069] Wheat straw bales were fluffed in a bale crusher (Tietjen) equipped with a rotating scraper operating at 3000 rpm, yielding granules with a particle size of 10-40 cm. This particle size ensures smooth delivery of the material and operation of the subsequent grinding step. The biomass material was pneumatically conveyed to a hammer mill (Tietjen VDK4.1 ) operating at 3000 rpm with a 30 mm sieve, where the wheat straw was chopped into pieces with an average particle size of 1-5 cm.
[0070] The chopped wheat straw was conveyed to the thermal pretreatment reactor with a syringe feeder (Metso; PDF 2545) followed by a conveying screw (Metso; FFS 211 ) and a plug screw (Metso; ADI 180). Syringe feeders convert mass flow Adjust to 400kg(DM) / h. The dry matter content of wheat straw was 85 wt.-%, the xylose content was 22.7 wt.-% and the lignin content was 16.6 wt.-%, resulting in PRP of ...
Embodiment 1-A
[0073] Embodiment 1-A wheat straw (moisture content 15wt.-%)
[0074] Biomass preparation was performed as defined in Example 1-0. Composition is identical with embodiment 1-0
[0075] By adjusting the exit area to 65mm 2 , modify the FPP (raw material processing parameter) to The measured steam consumption amounted to 403 kg / h and corresponds to a specific steam consumption of 1.0 kg per 1 kg of DM, which represents an effective 77% reduction in steam consumption compared to Example 1-0. The results are shown in Table 5.
Embodiment 1-B
[0076] Embodiment 1-B wheat straw (moisture content 15wt.-%)
[0077] Biomass preparation was performed as defined in Example 1-0. The dry matter content of wheat straw was 85 wt.-%, the xylose content was 21.3 wt.-% and the lignin content was 15.6 wt.-%, resulting in PRP of By adjusting the exit area to 90mm 2 , modify the FPP (raw material processing parameter) to The measured steam consumption amounted to 558 kg / h and corresponded to a specific steam consumption of 1.4 kg per 1 kg of DM, which represented an effective 68.2% reduction in steam consumption compared to Example 1-0. The results are shown in Table 5.
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