Abstract: The present disclosure generally relates to a method and a system for controlling the pretreatment and/or enzymatic hydrolysis of a lignocellulosic material. The method and system allow for savings with respect to energy consumption and costs.

Abstract: The present disclosure generally relates to a controlled method for pretreatment and/or enzymatic hydrolysis of a lignocellulosic material. The method comprises first pretreating the lignocellulosic material suboptimally, and then subjecting the material to mechanical refining.

Abstract: The present disclosure generally relates to a method for treatment of a lignocellulosic biomass. The method comprises the steps of pretreating the lignocellulosic biomass material in a pretreatment arrangement to form a pretreated biomass slurry; optionally hydrolysing the pretreated biomass slurry in a hydrolysis unit; retrieving gaseous SO2 from the pretreatment arrangement to provide an SO2 gas stream; treating the SO2 gas stream with an alkaline solution to provide a sulfite/bisulfite solution; supplying at least a part of the sulfite/bisulfite solution to at least one of: a) the lignocellulosic biomass material prior to pretreating the lignocellulosic biomass material in the pretreatment arrangement; b) the lignocellulosic biomass material n the pretreatment arrangement; c) the pretreated biomass slurry discharged from the reactor vessel; d) the hydrolysate or fermentable sugars of the hydrolysate.

Abstract: The present disclosure generally relates to a method for controlled pretreatment of lignocellulosic biomass. The method comprises the steps of: Pretreating (S10) a lignocellulosic biomass material in a pretreatment arrangement, the pretreating comprising impregnating (S10A) the lignocellulosic biomass with an SO2 feed in an impregnation vessel of the pretreatment arrangement; collecting (S20) a number of process parameters of the pretreatment, which process parameters include at least a feed parameter related to the total amount of lignocellulosic biomass input to the pretreatment arrangement, and a dry matter parameter related to the dry matter content of lignocellulosic biomass input to the pretreatment arrangement; and adjusting (S30) the SO2 feed in response to the process parameters.

Abstract: The present disclosure generally relates to a pretreatment arrangement (100) for pretreatment of lignocellulosic biomass. The pretreatment arrangement (100) comprises a reactor vessel (101) having an upstream inlet (102) for receiving biomass and a downstream outlet for discharging biomass (103). The pretreatment arrangement (104) further comprises a sluice vessel (104). The present disclosure also relates to a method (200) for pretreating lig- nocellulosic biomass.

Abstract: The present disclosure generally relates to a pretreatment arrangement (100) for pretreatment of lignocellulosic biomass comprising a reactor vessel (101) having an upstream inlet (102) for receiving biomass and a downstream outlet (103) for discharging biomass. The pretreatment arrangement (100) further comprises a gas valve (104) and gas flow control means (106).

Abstract: The present disclosure generally relates to a method and a system for forming a storage stable hydrolysate from a lignocellulosic material and to a hydrolysate formed by such a method. It also relates to the use of the hydrolysate to reduce and/or control microbial contamination during storage and/or fermentation. Additionally, the present disclosure relates to a method and a system for reducing and/or controlling microbial contamination in a separate hydrolysis and fermentation (SHF) process.

Abstract: A method and system for control of a microbial fermentation process involving co-fermentation of sugars from lignocellulosic biomass to fermentation products by means of fermentation microorganisms is provided. A residual sugar indicator parameter RSI is measured, which parameter directly or indirectly indicates the concentration of residual sugars, during fermentation in the fermentation vessel (31). The amount of fermentation media added to the fermentation vessel is automatically adapted in a predetermined manner in response to the residual sugar indicator parameter, so as to achieve efficient co-fermentation of sugars to fermentation products.

Abstract: The present invention provides a method for decreasing the fermentation inhibition in a process for producing a target chemical from a pretreated cellulosic material, the process comprising enzymatic hydrolysis of the pretreated cellulosic material and fermentation of hydrolysed material, wherein the fermentation inhibitory properties of the material subjected to fermentation is decreased by an addition of at least one reducing agent to the pretreated material or hydrolysed material. Moreover, the present invention provides the use of dithionite for decreasing the fermentation inhibitory properties of a material being subjected to simultaneous enzymatic hydrolysis and fermentation.

Abstract: The present invention provides a method for decreasing the fermentation inhibition in a process for producing a target chemical from a pretreated cellulosic material, the process comprising enzymatic hydrolysis of the pretreated cellulosic material and fermentation of hydrolysed material, wherein the fermentation inhibitory properties of the material subjected to fermentation is decreased by an addition of at least one reducing agent to the pretreated material or hydrolysed material. Moreover, the present invention provides the use of dithionite for decreasing the fermentation inhibitory properties of a material being subjected to simultaneous enzymatic hydrolysis and fermentation.