Feed conversion ratio

PROJECT STUDY MODULE (SCIENCE FOUNDATION) What Are the Benefits of using Phase and NSP Enzymes in Poultry Feed? TONIBI I. SENIBO 149054259. 2/07/2015.  Table of Contents Page 1. Abstract …………………………………… 3 2. Glossary ……………………………………… 3 3. Introduction ……………………………………. 4 4. Aims and objectives ………………………… 6 5. Findings and Analysis ……………………… 7 6. Results ………………………………………. 11 7. Discussion & Conclusion ……………………

birds but also the feed conversion ratio of our birds. My hypothesis is that the birds reared in bright light will not only grow better but also have a better feed conversion ratio. The reasons that lead me to believe this will be the case is because I feel like the birds reared in bright light will be more active and more prone to eat. I believe this increase in activity due to the bright light will increase the birds size therefor contributing to a better feed conversion ratio. The next variable

reactants. The conversion of reactant is found to increase with increase in catalyst loading from 1.91% to 11.5% (Figure 7). It is observed that up to the catalyst loading of 7.66% conversion of toluene increases sharply due to the presence of a large number of active sites available for the reactants. However, above catalyst loading of 7.66% although the surface area is provided for reaction, the increase in toluene conversion is negligible due to the shortage of limiting reactant in constant feed flow.

three different feed types fed to Epinephelus coioides. These feed types include a soy-based plant protein pellet (AQUA-LIFE), fish meal pellets (Ridley Aqua Feeds) and whole Pilchards. The fish had their dry weight and length measured prior to the commencement of the trial. 12 tanks, with 5 fish per tank were fed the three different feed types. All fish were fed every day of the 5 week trial period. The results showed the fish meal pellets had the most efficient food conversion ratio (FCR) value (0

lunch room waste, office papers, boxes and wood pallets etc. Table 2.1 Sources of MSW and their Examples (Gary, 2010) MSW is a heterogeneous feedstock containing materials with widely varying sizes, shapes and composition. This can be difficult to feed into thermal treatment plants especially gasifiers (Valkenburg et al., 2008) and can lead to variable behavior of the treatment process. The

liquid fuel consisting of gasoline range aromatic hydrocarbons. The product composition of the upgraded bio-oils varied with Si/Al ratio and the pore structure of the zeolites. Low organic product yields and rapid deactivation of the catalysts are the drawbacks associated with zeolite catalysis. Recently, Carlson et al. demonstrated that high catalyst to feed ratios and high heating rates attenuate the catalyst deactivation despite improving organic product yields. Poor organic product yields (due

1. [INTRUDUCTION] Photovoltaic cell is electric generating cells that convert sunlight energy into electrical energy; it is the most important and sustainable electrical energy generating system, solar electric cell energy has grown rapidly and a popular resource of energy. On like most electricity generating system has footpath of (CO2) produce, either during construction of the system or when in operation. Photovoltaic cell also known as the solar panel is one of the Morden means of generating

ACETIC ACID BY THE CHIYODA/UOP ACETICA™ PROCESS Aspen Model Documentation Index • Process Summary • About This Process • Process Definition • Process Conditions • Physical Property Models and Data • Chemistry/Kinetics • Key Parameters • Selected Simulation Results: Blocks Streams • References PEP Process Module 1 19 Aug 1999 SRI Consulting Process Summary This Aspen Plus model simulates the production of acetic acid by low pressure methanol

RCR is stored in a 500 L feed tank with a coil heater connected to the tank that rise RCR temperature to 100 °C to maintain a liquid phase and avoid freezing. The feed-tank is connected to a high-pressure dosing pump that can dispense flow rates from 0.0 to 70 ml/min. Hydrogen flows from a high pressure cylinder (150 bar) equipped with a pressure

The best esterification conditions were show at 50oC, 20% methanol to oil molar ratio and 0.4% by volume sulfuric acid after 5 h a reaction could reduce FFA content in feed stock to less than 1.88% Hence, the esterification of the alkali refining process decreased the FFA of esterified oil to the requisite level. The value of acid was reduced beneath 0.86 mg KOH/g esterification