Cellulose Chemistry and Technology

ADVANCES IN THE CHEMISTRY, PHYSICS AND TECHNOLOGY
OF PULP, PAPER AND CELLULOSE-BASED MATERIALS

ISSN 2457-9459 (Online)
ISSN-L 0576-9787 (Print)


2023

Journal Citation Reports
Impact factor 2023: 1.3
5-Year Impact Factor: 1.2
Article Influence® Score: 0.140
Ranked 9 out of 23
MATERIALS SCIENCE, PAPER & WOOD (Q2)

Scopus
CiteScore 2023: 2.3
SNIP: 0.405

SCImago
SJR: 0.264
H-Index: 42
Ranked Q3

 

Title
Second-generation ethanol through alkaline fractionation of pine and aspen wood
Authors
Mikael Jansson Niklas Berglin and Leelo Olm

Received November 19, 2009
Published Volume 44 Issue 1-3 January-March
Keywords bioethanol, alkaline pretreatment, converted pulp mill, pine, aspen, mass balance, energy balance,

Abstract
Pre-treatment studies on pine and aspen wood with alkaline fractionation were performed, the experimental results obtained being used as input for assessing the conversion of an existing pulp mill to ethanol and lignin production. By the LignoBoost process, the extracted lignin could be used in the lime kiln to replace fuel oil, while the lignin not needed in the lime kiln could be sold as a by-product. In addition to fuel applications, lignin could be used in a wide range of bio-based product applications, which would increase the value of the extracted lignin and increase the total revenues. A WinGEMS model was used to calculate mass and energy balances, and the results were used for an economic evaluation of the concept. The assessment indicated that the proposed alkaline concept would have reasonable production costs from both pine and aspen wood, comparable with the bioethanol produced from grain in Northern Europe today, i.e. about 0.45 €/L ethanol (~5 SEK/L). The production rate of a typical mill producing 1000 tonnes of pulp per day before conversion would be in the order of 140 000 m3 of ethanol per year, as depending on the raw wood material. The corresponding lignin production would range from 25 000 to 63 000 tonnes per year. The use of alkaline delignification to produce a substrate with low lignin content for the enzymatic hydrolysis builds entirely on known and well-proven technology, yet it needs to be further developed. The process chain from enzymatic hydrolysis to ethanol is very similar to that used today for grain ethanol. Altogether, the technical risk should therefore be low.


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