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Wright, Christopher T.

Publications and source records attributed to Wright, Christopher T..

Procter and Gamble Technology Process Assessment for Bioenergy Production

P&G intends to replace as much as their current heat and power by renewable energy sources. For 2014, P&G’s total energy including electricity, natural gas and steam is approximately 1,540,000 MMBTU annually (Table 2). The biomass and wastes around P&G facility can be grouped into six categories (Figure 6): (1) Agriculture residue and grass, (2) Refuse (inorganic) solid material, (3) Food waste, (4) Organic waste stream, (5) livestock manure, (6) wastewater and sludge. The six feedstock sources can provide a total energy of 3,520,000 MMBTU per year (Table 10), among which the agriculture residue is the biggest fraction, about 67%, followed by livestock manures 27%. Therefore, the available energy sources around P&G facility are enough to meet their energy needs. These energy feedstocks would be treated by two processes: anaerobic digestion for biogas subsequently for heat and power and thermochemical process (combustion, pyrolysis and gasification) for heat and power (Figure 8 and 9). For AD, a one-stage complete mixing digester is preferable; and fluidized bed reactors are favorable for thermochemical process.

09 BIOMASS FUELS↗

Performance and Efficiency of Biomass Densification Equipment (CRADA Final Report)

In 2008, a CRADA between the INL and Vermeer was signed and work began between the two parties to look at improvements in grinding processes for agricultural crop residues. Preprocessing is a critical operation in the biomass feedstock assembly system of a lignocellulosic biorefinery. Preprocessing is typically accomplished using industrial grinders to grind, chop, or otherwise size-reduce biomass materials into a suitable feedstock for conversion to biofuels and bioproducts. Various components of commercial preprocessing equipment capable of handling large-format material (such as large square bales) can be modified or altered to change the overall productivity and efficiency of the process. Many factors affect machine capacity and efficiency and the physical characteristics of preprocessed biomass. Ultimately, grinder capacity and efficiency can be enhanced by selecting hammer and screen configurations that optimize grinder performance-based mass flow and energy consumption. Variations in grinder capacity and efficiency were evaluated by altering the type, number, and orientation of the hammer; the screen type and size; and the rotational drum speed of the grinder. Fuel use and grinder capacity were compared with each modification made to the grinder system and the original design of the horizontal grinder test platform. Modifications evaluated in this study resulted in a significant increase in grinder capacity and efficiency.

09 BIOMASS FUELS↗

Optimizing Hammermill Performance Through Screen Selection and Hammer Design

Background: Mechanical preprocessing, which includes particle size reduction and mechanical separation, is one of the primary operations in the feedstock supply system for a lignocellulosic biorefinery. It is the means by which raw biomass from the field or forest is mechanically transformed into an on-spec feedstock with characteristics better suited for the fuel conversion process. Results: This work provides a general overview of the objectives and methodologies of mechanical preprocessing and then presents experimental results illustrating (1) improved size reduction via optimization of hammer mill configuration, (2) improved size reduction via pneumatic-assisted hammer milling, and (3) improved control of particle size and particle size distribution through proper selection of grinder process parameters. Conclusion: Optimal grinder configuration for maximal process throughput and efficiency is strongly dependent on feedstock type and properties, such moisture content. Tests conducted using a HG200 hammer grinder indicate that increasing the tip speed, optimizing hammer geometry, and adding pneumatic assist can increase grinder throughput as much as 400%.

09 BIOMASS FUELS↗

Experimental Study of the Structure of a Wingtip Vortex

A complete look at the near-field development and subsequent role-up of a wingtip vortex from a NACA 0015 wing section is investigated. Two separate but equally important surveys of the vortex structure in the region adjacent to the wingtip and approximately one chord length downstream of the trailing edge are performed. The two surveys provide qualitative flow-visualization an quantitative velocity measurement data. The near-field development and subsequent role-up of the vortex structures is strongly influenced by the angle-of-attack and the end-cap treatment of the wing section. The velocity field near the wingtip of the NACA 0015 wing section was measured with a triple-sensor hot wire probe and compared to flow visualization images produced with titanium tetrachloride smoke injection and laser illumination. The flat end-cap results indicate the formation of multiple, relatively strong vortex structures as opposed to the formation of a single vortex produced with the round end-cap. The multiple vortices generated by the flat end-cap are seen to rotate around a common ce te in a helical pattern until they eventually merge into a single vortex. Compared to a non-dimensional loading parameter, the results of the velocity and flow visualization data shows a "jetlike" axial velocity profile for loading parameter values on the order of 0.1 and a "wakelike" profile for much lower loading parameter values.

Anderson, Elgin A.↗