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Journal ArticleDOI

Influence of pyrolysis temperature and heating rate on the production of bio-oil and char from safflower seed by pyrolysis, using a well-swept fixed-bed reactor

Özlem Onay
- 01 May 2007 - 
- Vol. 88, Iss: 5, pp 523-531
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TLDR
In this paper, fast pyrolysis of safflower seed ( Carthamus tinctorius L.) was investigated with the aim to study the product distribution and their chemical compositions and to identify optimum process conditions for maximizing the bio-oil yield.
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This article is published in Fuel Processing Technology.The article was published on 2007-05-01. It has received 330 citations till now. The article focuses on the topics: Char & Pyrolysis.

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Citations
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Journal ArticleDOI

A comparative review of biochar and hydrochar in terms of production, physico-chemical properties and applications

TL;DR: In this paper, an updated review on the fundamentals and reaction mechanisms of the slow-pyrolysis and hydrothermal carbonization (HTC) processes, identifies research gaps, and summarizes the physicochemical characteristics of chars for different applications in the industry.
Journal ArticleDOI

Biochar production by sewage sludge pyrolysis

TL;DR: In this article, pyrolyzed sludge was used to assess the effect of pyrolysis temperature, residence time and biomass chemical impregnation on the yield of biochar production.
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Biomass pyrolysis: A review of the process development and challenges from initial researches up to the commercialisation stage

TL;DR: In this article, a review of various pyrolysis process, especially focusing on the effects of essential parameters, the process design, the reactors and the catalysts on the process, is presented.
Journal ArticleDOI

Operating parameters for bio-oil production in biomass pyrolysis: A review

TL;DR: In this paper, a review on parameters that influence the pyrolysis process, such as temperature, reaction time, heating rate, gas flow rate, feed rate, particle size and biomass composition, is presented.
Journal ArticleDOI

A review on the upgradation techniques of pyrolysis oil

TL;DR: In this paper, the authors provided insights on the properties of bio-oil obtained from various feedstock and several available mechanisms for biooil upgrading, including catalytic cracking, hydrodeoxygenation, esterification, supercritical extraction and steam reforming processes.
References
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Journal ArticleDOI

Fast pyrolysis processes for biomass

TL;DR: Fast pyrolysis for production of liquids has developed considerably since the first experiments in the late 1970s as mentioned in this paper, leading to significant advances in process development and a wide range of reactor configurations that have been developed to meet the stringent requirements for high yields of useful liquids, for use as a fuel in boilers, engines and turbines and as a source of chemical commodities.
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Fast pyrolysis of microalgae to produce renewable fuels

TL;DR: In this paper, fast pyrolysis tests of microalgae were performed in the fluid bed reactor, where the experiments were completed at temperature of 500 degreesC with a heating rate of 600 degreesC s(-1) and a sweep gas (N-2) flow rate of 0.4 m(3) h(-1), and a vapour residence time of 2-3 s.
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Fast pyrolysis of biomass in free-fall reactor for hydrogen-rich gas

TL;DR: In this paper, the pyrolysis behavior of two typical biomasses (legume straw and apricot stone) in a free-fall reactor was studied, and the total ratio of CO and H 2 in the gas product reached 65.4 and 55.7 mol% respectively.
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Steam reforming of model compounds and fast pyrolysis bio-oil on supported noble metal catalysts

TL;DR: In this article, the authors investigated the use of noble metal-based catalysts for the steam reforming of a few model compounds and that of an actual bio-oil and found that the Pt/ceria-zirconia sample showed essentially constant activity, while extensive carbonaceous deposits were observed on the quartz reactor walls.
Journal ArticleDOI

Influence of temperature on the products from the flash pyrolysis of biomass

TL;DR: In this article, a mixture of mixed wood waste was pyrolysed in a fluidized bed reactor at 400, 450, 500 and 550°C, and the results showed that only low quantities of hydrocarbons were present and the oxygenated and polar fractions were dominant.
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