1 2/9/2014 Energy Savings, Power Reliability, Environmental Stewardship The benefits of on-site cooling, heating and power.

Slides:



Advertisements
Similar presentations
You have been given a mission and a code. Use the code to complete the mission and you will save the world from obliteration…
Advertisements

1.Why is the moist adiabatic lapse rate lower than the dry- adiabatic lapse rate? Heat is released during condensation. 2.When temperatures are below freezing,
Renewables (CHP), Global Warming, and Energy Efficiency Richard Brent Solar Government Affairs Lake Tahoe, California July 28, 2005 California Manufacturers.
ABENGOA SOLAR Solar Power for a Sustainable World Past, Present, and Future of Solar Thermal Generation Bruce Kelly Abengoa Solar, Incorporated Berkeley,
Qualified Energy Recovery A Green Power Technology No additional fuel consumption Near zero emissions with air cooled OEC Inside the fence installation.
Recovered Energy Generation
Use of Regeneration in Vapor Power Cycles
Air Conditioners.
ACTIVE LEARNING PROCESS
ME 416/516 Basic Energy Units, Terms and Calculations War Eagle! Roll Tide!
Chapter 11 Refrigeration Cycles Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 5th edition by Yunus A. Çengel.
Chapter 9 REFRIGERATION AND LIQUEFACTION
1 ISAT Module III: Building Energy Efficiency Topic 1: Gas Mixtures, P-v-T Behavior Introduction to Building Energy Efficiency Gas Mixtures P-v-T.
Refrigeration Cycles د/ محمود عبدالوهاب.
Refrigeration Cycles CHAPTER 11: PTT 201/4 THERMODYNAMICS
Presentation Heading Air Source Heat Pumps Jordan Jeewood
June Energy consumption in Korea 4 primary & final energy consumption CO 2 emissions LNG Nuclear Renewables, etc Oil Coal Energy Industrial.
MA Metal Finishing Forum Tools and Techniques for Optimizing Metal Finishing Process/Environmental MA Metal Finishing Forum Kevin L. Klink, P.E.
ACADs (08-006) Covered Keywords Chilled Water System Description Supporting Material
Water Distribution Systems – Part 1
Energy-Efficient Process Cooling
* A chiller capable of producing water temperatures of low 40s on the evaporator side and above 135° on the condenser side.
1 1 BASICS OF ENERGY MANAGEMENT Section A - Energy Basics.
DOE - Chiller System Optimization Opportunities With Gas Engine-Driven Cooling Systems.
CUSTOMIZED ENVIRONMENTAL
Exhaust Heat Recovery Systems
Power Plant Construction and QA/QC Section 2.3– Steam Generators
Improve Facility Operation through Commissioning-A Case Study Mingsheng Liu, Ph.D., P. E. University of Nebraska.
Antero Punttila Analyzing most typical energy saving measures Energy Efficiency of Steam and Condensate Systems Antero Punttila, Motiva Oy.
Chapter 10 VAPOR AND COMBINED POWER CYCLES
UCSD Medical Center - Hillcrest Campus Case Study Gerry White Facilities Design & Construction University of California, San Diego.
Thermal Mass Flow Meters Market and applications.
COMBUSTION CONTROL IN BOILERS 1 Dept. of Electronics & Instrumentation, Narayana Engineering College, Nellore.
Solutions for Flaring Reduction Dual-Fuel & Gas Engines
1 POLYGENERATION OF ELECTRICITY, HEAT and ULTRA PURE WATER for SEMICONDUCTOR INDUSTRY Chuanfeng Liu Supervisors: Andrew Martin EGI KTH Aapo Sääsk Xzero.
Technologies for CCS on Natural Gas Power Systems Satish Reddy April 2104.
Bolland Hybrid power production systems – integrated solutions Olav Bolland Professor Norwegian University of Science and Technology (NTNU) KIFEE-Symposium,
First Solar FuelSmart™: Powering Energy Security
Chemistry 17.1.
Waste Heat to Power Recovery from Diesel Generator.
Waste Heat Generator (WHG)
Air Conditioners.
Heat & Thermodynamics Test Prep Game.
Addition 1’s to 20.
25 seconds left…...
Energy Saving in Hospitals: Hong Kong Initiatives
Equal or Not. Equal or Not
Slippery Slope
Automotive Technology
EnvironmentEnvironnementCanada Nusa Dua, Bali, Indonesia September 5 – 7, Part 4: LFG Utilization.
10 CHAPTER Refrigeration Cycles.
Week 1.
Lecture 36 Combustion Reactions.
IIFREEE 2014 for MENA – AMMAN, JORDAN ORC-Based Heat Recovery System for Energy Efficient Industries By: Dr. Salih Manasra CEO
“Delivering cleantech energy solutions for a sustainable future, now.”
Cogeneration.
Pacific School Of Engineering. Guided By:- Asst.Prof.Vatsal patel Submitted by:-  Kotadiya Reshma :  Ladva Piyush : 
Solar cooling systems.
Air Emission Benefits of CHP Air Innovations Conference August 10, 2004 Joel Bluestein Energy and Environmental Analysis, Inc. Prepared under contract.
Operation and Maintenance
Energy Efficiency in Industrial and Commercial Facilities 2003 Energy and Environmental Conference September 16, 2003.
Plant Utility System (TKK-2210) 14/15 Semester 4 Instructor: Rama Oktavian Office Hr.: M-F
Refrigeration Basics 101.
Heat engines played a key role in the development of the modern industrial world. Steam locomotives were an important early use of the steam engine. Electric.
Asia Pacific Business Outlook Conference March 27, 2007
THERMAL POWER PLANT.
I Need A Space Heating System Let’s Look At A Central Steam Plant Option.
EGEE 102 – Energy Conservation And Environmental Protection Energy Efficiency.
Energy Conservation CERD /12/2017
Presentation transcript:

1 2/9/2014 Energy Savings, Power Reliability, Environmental Stewardship The benefits of on-site cooling, heating and power

2 UTC Research Center – Technology Advancement Hamilton Sundstrand Aerospace & Industrial Pratt & Whitney Aircraft Engines, Gas Turbines & Space Propulsion Sikorsky Helicopters On-site & Transportation UTC Fuel Cells Otis Elevators, Escalators & People Moving Systems Carrier Heating, Cooling & Refrigeration Chubb Security & Fire Protection UTC POWER OVERVIEW

3 Cooling, Heating & Power Fuel CellsHeat-to-Energy Power & Heat On-site power solutions UTC PRODUCT OVERVIEW

4 Waste Heat Solutions for On-Site Generation

5 Provides: Up to 200 kW electrical power Benefits: Zero fuel costs Zero emissions Waste heat above 500°F (gaseous) 2 – 4 Year payback 20% IRR or higher PURECYCLE TM 200

6 Conventional Industrial Facility 20 MCF/hr Natural Gas Industrial Facility with PureCycle TM Power System 20 MCF/hr Natural Gas REDUCED ELECTRIC NEED

7 PRODUCT CONCEPT PureCycle Power System reverses air conditioning cycle CoolingElectricity Air conditioner ElectricityHeat PureCycle Power System NO X Fuel Cost

8 Electrical Power Waste Heat Gas > 500°F Power Module Rejected Heat PURECYCLE TM 200 SCHEMATIC Waste heat enters the evaporator and vaporizes a pressurized working fluid. 1 The hot vapor is then expanded through a turbine to drive a generator producing electric power. 2 The condenser cools the expanded vapor, returning it to liquid form. 3 The cooled liquid re-enters the power module, where the pump re- pressurizes it and returns it to the evaporator. 4

9 SYSTEM COMPONENTS 8 x 40 x 8 (11,600 lbs) 11 x 6 x 6 (7,000 lbs) 6 x 10 x 10 (13,000 lbs)

10 TURBINE / GENERATOR

11 POWER MODULE

12 Pressurized Exhaust Evaporator DVR Valve Heat Source 2)Ambient Exhaust (ex: most industrial processes) To Power Module & Condenser 1)Pressurized Exhaust (ex: Recip, Turbine) STANDARD INSTALLATIONS Blower Heat Source Evaporator

13 Low O & M costs – estimated at about 0.7 ¢/kW-hr for full maintenance (both scheduled and unscheduled) Uses existing production components from Carrier –Minimizes cost, increases reliability PureCycle system requires no operator –No steam/water in power cycle –Remotely monitored, unattended operation Closed-cycle operation Minimal scheduled maintenance duties –Replace filters –Check oil levels –Replace lube oil –Refrigerant make-up OPERATION & MAINTENANCE

14 CARRIER SERVICE NETWORK 80 field offices in the US Continuous Remote Monitoring – 24 x 7 Internet access via web browser Carrier Monitoring Center Alarms, service predictions Dispatch field technicians Detect and correct problems early, to maintain savings and productivity

15 Gases: Input Temperature > 500F; Heat input > 8.5 mmbtu/hr APPLICATION GUIDE Q in = m dot x c p x (T in – T out ) Heat Input = mass flow x specific heat x exhaust temp. drop (btu/hr) (lbs/hr) (btu/lb/F) (F) Q in must equal 8,500,000 btu/hr to make 200 kW (lbs/hr) = SCFM x 60 x (use density of air at STP) (lbs/hr) = ACFM x 60 x density (use density of air at actual T, P) C p = 0.26 (conservative, for lean burning natural gas) T out = 300 F

kW 400 kW200 kW THERMAL REQUIREMENTS

17 Source: derived from U.S. EPA, National Emissions Inventory Database Estimated Annual U.S. Industrial Waste Heat Quantities (300 F reference temperature) 29 QUADS BTUs/YEAR (US) Nationwide: 420 trillion BTUs per year industrial waste heat Temperature range of interest

18 APPLICATIONS Landfill Gas Gas Compression Chemicals Metals Petroleum Brick & Ceramic Top Industries Recip Engines Gas Turbines Flares Thermal Oxidizers Furnace Incinerators Key Equipment Waste Heat Electricity

19 PRODUCT RELEASE 3 Field Tests Commercially Available since July Week Lead-time Landfill Flare Austin Energy (Austin, TX) Landfill Recip Exhaust US Energy (Danville, IL) Burner UTRC (Hartford, CT)

20 Initial focus in CA and New England States MARKET STRATEGY 8 ¢/kWh or more Number of facilities CA75,000 NE16,000 CA utility territories Annual average power output (kW) Avg electric price (¢/kWh) No incentives Customer payback (yrs) PG&E SCE SDG&E Million GWh Industrial power > 8 ¢/kWh PG&E SCE SDG&E

21 TEMP. DERATE EFFECT

22 (909)