2019
DOI: 10.1016/j.powtec.2019.06.008
|View full text |Cite
|
Sign up to set email alerts
|

Numerical prediction of the mean residence time of solid materials in a pilot-scale rotary kiln

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
2
1

Citation Types

0
9
0

Year Published

2020
2020
2024
2024

Publication Types

Select...
6
1

Relationship

1
6

Authors

Journals

citations
Cited by 18 publications
(9 citation statements)
references
References 20 publications
0
9
0
Order By: Relevance
“…The TPS was obtained as the commercial product FlourPlast GP2 from Rodenburg Biopolymers (Oosterhout, The Netherlands). Biochar was made from a pine tree bark (Pinus sylvestris) residue stream at 450 °C and a residence time of around 12 min, using a lab-scale pyrolysis unit as described in [31]. Biochar was ground in a Retsch S1 planetary ball mill (Retsch, Haan, Germany) and sieved using a Retsch AS200 Basic sieving apparatus (Retsch, Haan, Germany) to achieve a mean particle size of 18.9 µm (P10 = 4.8 µm, P90 = 59.98 µm).…”
Section: Methodsmentioning
confidence: 99%
“…The TPS was obtained as the commercial product FlourPlast GP2 from Rodenburg Biopolymers (Oosterhout, The Netherlands). Biochar was made from a pine tree bark (Pinus sylvestris) residue stream at 450 °C and a residence time of around 12 min, using a lab-scale pyrolysis unit as described in [31]. Biochar was ground in a Retsch S1 planetary ball mill (Retsch, Haan, Germany) and sieved using a Retsch AS200 Basic sieving apparatus (Retsch, Haan, Germany) to achieve a mean particle size of 18.9 µm (P10 = 4.8 µm, P90 = 59.98 µm).…”
Section: Methodsmentioning
confidence: 99%
“…A detailed description of the pilot-scale reactor can be found in [20]. Biochar was produced in the pilot-scale reactor in a pyrolysis gas atmosphere in a single 8 h run for every biomass stream.…”
Section: Pyrolysismentioning
confidence: 99%
“…Biochar was produced in the pilot-scale reactor in a pyrolysis gas atmosphere in a single 8 h run for every biomass stream. Mean residence time (MRT) was determined theoretically using an adapted version of the Sullivan's equation as explained in [20]. The schematic representation of both reactors can be found in Figure S1.…”
Section: Pyrolysismentioning
confidence: 99%
“…Residence time distribution (RTD) and mean residence time were critical and quantitative properties describing the complex motion behaviors of particles in the rotary heat exchanger. Researchers paid more attention to measuring the residence time of biomass materials in reactors in pretreatment processes. Moreover, transport processing control and equipment design could be guided by these key properties. Several numerical methods could be adopted to obtain detailed information about the mixing process in a bed of spherical and spherical-like biofuel particles on grate firing systems. However, the number of gasifiable fuels and the efficiency of gasification processes were directly affected by the heat requirement for drying pretreatment. The heat and mass transfer processes of biomass fuels were significantly influenced by the motion behaviors of biomass particles in drying equipment. A considerable number of studies were carried out on the development of residence time of nonspherical biomass particles within a variety of rotary cylinders.…”
Section: Introductionmentioning
confidence: 99%