Indoor climate and ventilation JENS PEDER PEDERSEN Jens Peder Pedersen Indoor climate and ventilation INDOOR CLIMATE Thermal indoor climate Air temperature‚ air velocity and air humidity Atmospheric indoor climate: = Air quality: pollutions as dust‚ air humidity‚ gasses and smell The psychical environment Page 2 Jens Peder Pedersen Indoor climate and ventilation INDOOR CLIMATE Physical and chemical demands for the indoor climate 1. Suitable temperature 2. Suitable
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HLM HLM CONSULTANTS LTD HLM File No.: ARBE3100_A1_2014 April 2014 Basement Construction Prepared for: DreamHome Furniture Group ARBE3100 – Construction Technology 3 The University of Newcastle Callaghan NSW 2308 Prepared by: HLM Consultants Ltd HLM Basement Construction ARBE3100 – Construction Technology 3 Assignment 1 CONTENTS EXECUTIVE SUMMARY ................................................................................................................ 3 1
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Electrochemical production of hydrogen from water Presented by: Heba A. Alsabagh Hiba M. Maghayreh Hiba N. Abu Zaghleh Sahar M. Alissa University of Jordan Faculty of Engineering & Technology Department of Chemical Engineering Supervised by: 0078381 0076527 0076528 0072918 Dr. Hatem Alsyouri December‚ 2011 Chapters: Introduction Literature Survey Process Selection and Design Process Description Material and Energy Balances Design 2 Chapters: Feasibility Study
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enriched by attending and passing several specialized and accredited courses in different fields of management‚ training‚ and self development. This allowed me to become a Certified Trainer in Management from the Institute of Leadership and Management ILM-UK and to start a new stage of my career as a freelance trainer and consultant dealing with variety of business and professional people from different levels of experience and in multidisciplinary fields. With this unique blend of strong education
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Surge Tank Design CHE4042F Process Dynamics and Control Project 1 20 April 2013 Group 26 Table of Contents List of Figures ii List of Tables ii Glossary iii A. Analysis of Plant Data 1 B. Simulation of Surge Tank 2 i. Modelling the Surge Tank in Xcos 2 ii. Frequency Fluctuations in Density Data 5 iii. Testing of Model for the Product Density 6 iv. Comparison of Unconstrained and Constrained Output Volume of the Surge Tank 7 C. Control of Surge Tank 8 i. Implementation
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the vertical stress at a point 12 m below the mid-point of one of the longer sides (a) using influence factors‚ (b) by means of Newmark’s chart. 5. The backfill behind a retaining wall above the water table consists of a sand of unit weight 17 KN/m3‚ having shear strength parameters c / = 0‚φ / = 370 . The height of the wall is 6 m and the surface of the wall backfill is horizontal. Determine the total active thrust on the wall according to the Rankine theory. If the wall is prevented from yielding
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Module 2 Flexi EDGE BTS Installation Planning Confidential – IPR applies 1 © Nokia Siemens Networks Module 2 - Installation Planning / MNa / 2007-05-08 Module 2 - Flexi EDGE BTS installation planning After completing this module‚ the participant will be able to: Theory: • Describe the site requirements for Flexi EDGE BTS • Describe installation options for Flexi EDGE BTS • Describe the DC Power options for Flexi EDGE BTS • Describe transmission options for Flexi EDGE BTS • Describe external
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QUESTION: 1. Determine physicochemical parameters for Palm Oil Mill Effluent (POME)‚ fresh empty fruit bunch(EFB)‚ and palm oil boiler ash. State the reference(s). 2. Determine the mass of each components at initial raw compost mixture that consist of POME+EFB(300metric ton)+ash+additive. Stat your answer in metric ton and consider any nutrient losses. The final compost should have: C/N<30‚ N=1.8%‚ P=0.5%‚ K=3.4%‚ Mg=0.8% Given: a) Composting time: 45 days b) Composting system:
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65 W/m2⋅K 6.3 W/m2⋅K 102.5°C 51.8°C‚ 3203°C 6.3 m/s 0.35 W‚ 5.25 W 15 mW (a) 18‚405 W; (b) $12‚900 254.7 K 4.3 W 0.42‚ 264 W (a) 0.32 W/m2⋅K‚ 0.32 W/m2⋅K‚ 2.1 W/m2⋅K (a) 8.1 W; (b) 0.23 kg/h (a) 0‚ 144 W‚ 144 W‚ 0; 0‚ 144 W‚ 144 W‚ 0; (b) 2.04×105 W/m3; (c) 39.0 W/m2⋅K (a) 4.86 MW; (b) 9.22 kW; (c) 4.87 MW; (d) 4.87 MW (a) 300°C; (b) 3.89 MW; (c) 3.19 kW; (d) 3.89 MW 2.41‚ 312 W‚ 1.25‚ 600 W (a) 0.223 W; (b) 3.44 W 100°C 1.42 1.43 1.45 1.46 1.47 1.48 1.49 1.51 1.52 1.53 1.54 1.55 1.57 1.58 1.59
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Understanding Gas-Condensate Reservoirs How does a company optimize development of a gas-condensate field‚ when depletion leaves valuable condensate fluids in a reservoir and condensate blockage can cause a loss of well productivity? Gas-condensate fields present this puzzle. The first step must be to understand the fluids and how they flow in the reservoir. Li Fan College Station‚ Texas‚ USA Billy W. Harris Wagner & Brown‚ Ltd. Midland‚ Texas A. (Jamal) Jamaluddin Rosharon‚ Texas Jairam
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