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CHARACTERIZATION OF A BIOMASS MILLING PILOT ... - circe

CHARACTERIZATION OF A BIOMASS MILLING PILOT ... - circe

CHARACTERIZATION OF A BIOMASS MILLING PILOT ... - circe

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milled biomass characteristics analysis: particle size<br />

distribution, moisture content, bulk density, particle<br />

shape factor and chemical composition as function<br />

particle size. The properties variations permit to assess<br />

the influence of the parameters mentioned in final milled<br />

material.<br />

2 <strong>BIOMASS</strong> <strong>MILLING</strong> <strong>PILOT</strong> PLANT<br />

Experimental facility characterization should analyse<br />

the design and operational parameters needed to satisfy<br />

the particle size requeriment with the lowest milling<br />

energy consumption.<br />

The size requirements are fixed by the final energetic<br />

conversion technology and can be expressed by range of<br />

particle sizes, or by more specific granulometric<br />

regulations.<br />

Biomass shows a high heterogeneity in connection<br />

with inherent mechanical and physical properties, and in<br />

reception conditions (moisture content, raw particle<br />

size…). Flexibility in experimental comminution facility<br />

permit to carry out several tests varying:<br />

Type of mill<br />

Equipment combinations<br />

Operational parameters<br />

Biomass mechanical properties represent a relevant<br />

parameter to select the adequate type of mill. Biomass is<br />

mainly composed of non-brittle materials [11] in contrast<br />

with other energetic resources as coal. Several studies<br />

show three types of mills as the most appropriate for<br />

biomass milling: hammer mills, knife mills and also disc<br />

mills in specific conditions [11].<br />

Studied facility is composed of two mills: a hammer<br />

mill and duplex mill [8]. Hammer mill with horizontal<br />

axis and a drive of 11kW comprises 6 hammers arranged<br />

on 3 radial lines. Duplex mill with a drive of 4kW consist<br />

of three hammers in revolution that carry out two<br />

different milling actions: impact breakage of hammers<br />

against particles and breakage by shearing stress between<br />

the hammer, particles and a fixed element inside the<br />

milling chamber.<br />

Grinders are the main equipment in any milling<br />

facility. However, classifying equipments are<br />

incorporated to separate the particles as function their<br />

size. The classifier has operational flexibility which<br />

increases the number of possible mills configuration<br />

allowing the most suitable solid treatment.<br />

Classifying systems select those particles whose size<br />

satisfies the final requirement. Classifier can be used as a<br />

previous stage to separate the particles which satisfy the<br />

size requirement, as a final stage to guarantee the particle<br />

size of final product or as an intermediate stage to convey<br />

the coarse particle again to mill (recirculation flow).<br />

When the upper limit size is fixed, coarse particle can be<br />

eliminated or can be passed by the mill a number of times<br />

necessary to obtain the desired size. In case of lower size<br />

limit, the fine particles are eliminated of the final milled<br />

product.<br />

Milling facility also incorporates auxiliary solid<br />

handling equipment to convey the particles between the<br />

main equipments. At CIRCE milling biomass facility<br />

(e.g. Fig. 1), three different systems are installed to<br />

convey solids. First of all, a belt conveyor is used to feed<br />

the biomass to the mills. Subsequently, pneumatic<br />

conveying, composed of two fans to generate the air<br />

flow, and two equipments (cyclone and bag filter) to<br />

separate the air-particles flow, carries the pulverized<br />

biomass from mills to the final bin. Finally, coarse<br />

particle recirculation is conveyed to mills using an screw<br />

conveyor.<br />

The different combinations between hammer mill,<br />

duplex mills and screen classifier provide five milling<br />

configurations:<br />

1. Configuration A.1: hammer mill<br />

2. Configuration A.2: hammermill and screen<br />

classifier<br />

3. Configuración B.1: duplex mill<br />

4. Configuración B.2: duplex mill and screen<br />

classifier<br />

5. Configuración C: hammer mill, screen<br />

classifier and duplex mill.<br />

Experimental tests in A.1 and A.2 configurations are<br />

focused on the hammer mill analysis:<br />

A.1. Hammer mill.<br />

Particle size is fixed by the internal screen opening<br />

size. Particles pass trough the hammer mill and are<br />

directly carried by pneumatic conveying to the bin. .<br />

A.2. Hammer mill with recirculation to the same mill.<br />

Milled biomass particles in hammer mill are<br />

conveyed to the screen classifier where fines are<br />

separated from the coarse ones. Fine particles are<br />

directly transported to the bin, whereas coarse<br />

particles are conveyed again to the hammer mill<br />

until a suitable particle size is achieved. In this<br />

configuration, the goal particle size is fixed by the<br />

screen opening size in the classifier.<br />

Third and fourth configurations allow the study to be<br />

focused on duplex mill:<br />

B.1. Duplex mill.<br />

As in the A.1 configuration, particles pass trough the<br />

duplex mill before they are being transported by<br />

pneumatic conveying to the bin. Internal screen<br />

determines the final particle size.<br />

B.2. Duplex mill with recirculation to the same mill.<br />

This configuration is similar to A.2. In case finer<br />

particle sizes are needed, this configuration allows<br />

the particle flow to pass several times trough the<br />

mill until the suitable size is reached.<br />

The last configuration is focused on the combination<br />

between both mills with a screening intermediate stage:<br />

C. Hammer mill with recirculation to the duplex mill.<br />

In this configuration (e.g. Fig. 1) the milling and<br />

classifying process are the same as in A.2 configuration,<br />

except for the coarse recirculation. In this case, the coarse<br />

particles are redirected to the duplex mill. The facility<br />

allows both recirculation types.<br />

Configuration changes can be made by means of<br />

removable pneumatic conveying ducts. The combinations<br />

between configurations and internal screens allow to<br />

obtain the suitable particle size in the process.<br />

To control the equipment of the facility, an control<br />

automatic system and data acquisition have been<br />

implemented. The main elements are:<br />

Programable logic Control (PLC): it is the main<br />

control unit. It collets all plant information, and<br />

it take the action on the plant.<br />

Distributed input/output units: they are remote<br />

device, where signals from sensor an signals to<br />

actuators are connect to the PLC<br />

Variable speed drivers: It is the main actuator<br />

in the mill plant. With this we can regulate the<br />

angular speed and the power supply to mill, fan<br />

and others devices.

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