Cryogenik waste heat utilization for DESY and European XFEL 2nd Workshop on Energy for Sustainable Science at Research Infrastructurs Jens-Peter Jensen,

Slides:



Advertisements
Similar presentations
Louise Trygg Energy Efficiency and models for that Louise Trygg, PhD Energy system Linköping University.
Advertisements

Use of renewable energy in the Provinces of Treviso headquarters Maurizio Tufaro Treviso Paving the way for self – sufficient regional Energy supply based.
DIRECTION DE LA RECHERCHE Marc FLORETTE Jeudi 29 mai 2008 The advantage of mCHP as a high efficiency gas solution for the residential market Gas industry.
Heat Recovery for Commercial Buildings
Thomas Parker, Head of Energy Division Responsible Renewable Recyclable Thomas Parker October 2013.
Engineering Department EN Cooling and Ventilation issues 1 FUTURE EXPLOITATION OF THE EAST AREA EN-CV Michel OBRECHT.
ESS Cooling and Heat Recovery system Thomas Hjern
UTSW Thermal Energy Plants, Power Generation and Electrical System What do we do to meet the Emission Reduction, Energy usage Reduction and Electrical.
Integrating a Saving Energy controller in Existing Air Condition units Case Study.
Geothermal Energy David McArdle. What is it? Geothermal energy - The process of extracting power from underground heat that is produced by the earth’s.
Cogeneration.
Richard Simmons Drilling Company, Inc. 60 Drill Rig Drive, Buchanan, Virginia Telephone (540) Geothermal Heating & Cooling How it Works.
GEOTHERMAL DIRECT HEAT UTILIZATION. DISTRICT HEATING.
High Temperature Cooling of Cryoplants and RF Systems at the European Spallation Source 2 nd Workshop Energy for Sustainable Science at Research Infrastructures.
Euroheat & Power Why is there not more combined heat and power?
ESS Cryogenic System Process Design Philipp Arnold Section Leader Cryogenics CEC – ICMC 2015 June 29, 2015.
Energy Efficiency Office, EMSD
Chilled water Meyrin consolidation Study 1 st Part Many thanks for their contribution to: Pasquale Alemanno, Fortunato Candito, Alexander Putzu.
THE DISTRICT COOLING NETWORK THAT OUTPERFORMS NATURALLY PAGE ENERGY IS OUR FUTURE, WE MUST SAVE IT! EEMOD’S Nantes – 15 / 09 / 2009 > Overall chiller system.
Conceptual Design Study - Cryogenic Requirements How to decide the layout of ILC cryogenic system Conceptual design of cryogenic system Layout of cryogenic.
Lecture Objectives: Specify Exam Time Finish with HVAC systems –HW3 Introduce Projects 1 & 2 –eQUEST –other options.
Technology details, potential and experiences of Trigeneration
W. Schufft: Challenges for electrical power engineering IP 2007, Pernink Challenges for Electrical Power Engineering.
Accelerators for ADS March 2014 CERN Approach for a reliable cryogenic system T. Junquera (ACS) *Work supported by the EU, FP7 MAX contract number.
Smartcool Systems Inc. Providing effective and reliable energy efficiency solutions for HVAC-R customers around the globe.
Erica Lindström Report on Sessions B1 and B2. Boosting accelerator electrical efficiency at the ESFR Presented by Mr. Jean François Bouteille The new.
Thomas Parker Head of Energy Division Sustainable Accelerators.
Proposals of high efficiency accelerator components from AAA Green-ILC WG H. Hayano, KEK
IMPROVING COOLING SYSTEM EFFICIENCY WITH PRE-COOLING AJ Schutte 15 August 2012.
Global Design Effort1 September 20-22, 2006 MAC Review Power and Water breakout (mixed results) Marc Ross GDE.
Cooling plant upgrade Jose Botelho Direito, Michele Battistin, Stephane Berry, Sebastien Roussee 2 nd SPD Cooling Workshop 30/11/201112nd SPD.
2005/06/22 ALBA Building Project David Carles Engineering Services Division - CELLS.
DESY. Deutsches Elektronensynchrotron Introduction of DESY and MKK group Jens-Peter Jensen Asset and Maintenance Management Workshop 2013 Genf,
DISTRICT HEATING District heating is an infrastructure which allows heat generated in a centralized location to be distributed to residential homes and.
Cryogenic refrigeration for the XFEL facility. Current status of the commissioning. Wilhelm Hanspeter Grenoble, June 4th, 2015.
J. G. Weisend II for the ESS Team Energy Efficiency & Recovery at ESS.
Project X Workshop - Cryogenics1 Project X CRYOGENICS Arkadiy Klebaner.
ESS Cooling System - Interface with DTL 1 John Jurns Cooling System Engineer.
ESS Cooling System - Interface with RFQ 1 John Jurns Cooling System Engineer.
Ullrich, DESY Dubna GDE XFEL The European X-Ray Laser Project X-Ray Free-Electron Laser 1 Water cooling XFEL Desingn of the XFEL water cooling.
1 Energy Solutions for Production Supported by: The sole responsibility for the content of this presentation lies with the authors. It does not necessarily.
Multi-pipe Systems “An Opportunity To Combine Heating and Cooling”
ILC Utility Design Study for Kitakami-site
Update on the PSB Cooling and Ventilation Systems
ENV-5022B/ENVK5023B Low Carbon Energy
Book E3 Section 1.4 Air-conditioning
N. Hasan1, P. Knudsen2 and V. Ganni2
Dana M. Arenius Jefferson Laboratory Cryogenics Dept Head
(Potential) Site and Utilities
Variable Frequency Drive Savings Calculator Tools
COOLING & VENTILATION INFRASTRUCTURE
Energy Management at DESY and a new Energy Monitoring System
Overview of Talks. Report from Parallel Session IIb Energy Management & Procurement at RIs Frank Lehner, DESY.
Commissioning and First Cooldown of XFEL Linac
BriXS – MariX WG 8,9 LASA December 13, 2017.
Different scales of installation
WP Coordinaten XFEL RF Operation
Thank you for the opportunity to present our energy efficient product
Application of High Efficiency Chillers in Hong Kong Baptist Hospital
The Benefit of Including Energy Recovery System Analysis
Cryogenic cavern in Asian site
Mathew C. Wright January 26, 2009
ENV-5022B/ENVK5023B Low Carbon Energy
District heating in Finland 2017
SOLAR PANELS SAVING IN YOUR HOME!
Maintenance at ALBA facility: Strategy for the conventional services
ESR2 Process Cycle Design
ESR2 Process Cycle Design
Energy Management Introduction Rantharu Attanayake BSc. (Eng), MSc, MBA EE – Energy Management Mobile :
Sustainable Heating and Cooling in Sweden
Presentation transcript:

Cryogenik waste heat utilization for DESY and European XFEL 2nd Workshop on Energy for Sustainable Science at Research Infrastructurs Jens-Peter Jensen, Eva Leister Energy for Sustainable Science Genf,

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 2 DESY campus

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 3 DESY premises heat distribution XFEL cryogenics plant district heating transfer station XFEL injector Heat distribution pipes 110 °C (red) Heat pipes 80 °C (blue)

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 4 Energy foot print of DESY and XFEL DESY premises in 2015 ff > Electrical energy: 160 GWh, 25 MW > Heating energy: 20 GWh, 10 MW > Dominated by the accelerators and experimental halls XFEL operation at 10 Hz in 2016 ff > Electrical energy:120 GWh, 20 MW > Heating energy: 10 GWh, 5 MWSchenefeld premises > Cryogenics electrical energy at 10 Hz: 24 GWh/a  Heating demand is predominant on the Schenefeld and Osdorf premises  XFEL cryogenic plant is on the DESY premises, ex HERA cryogenics plant > XFEL cryogenics waste heat utilization possible for DESY premises

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 5 Cryogenics

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 6 Coldbox Dewar Subcooler oil seperator compressors air cooler He preheater The helium-heater is only used when the subcooler is cooling down or heating up. Helium Oil Breox B35 Oil-Helium mixture 6 K 300 K 40°C 75°C XFEL modules tunnel injector Cryogenic Plant Functionality 50°C heat exchanger to the heat distribution return pipe

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 7 Oilsystem of the XFEL Cryogenic Plant heat exchanger for cryogenics waste heat utilization air/oil cooler low pressure compressors

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 8 Temperature Plot of the Breox Oil in 2012 average: 70,2 °C oil temperature of the high pressure compressor in 2012

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 9 Heat emission of 1 street of the cryogenic plant in 2012 average value: 823 kW

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 10 District heating transfer station UST 48 UST 8 UST 47 UST 28c UST 49 UST 72 UST 24UST 30 UST 25b3 UST 25 UST 25c UST 1d UST 54 UST 2 UST 1a UST 7 UST 5 UST 10 UST 16 UST 17 UST 3b UST 3 UST 80b UST 62 UST 64 UST 69 UST 67 UST 67-2 UST UST CFEL 46 UST ZOQ 45 4a UST CSSB 3a UST 11a UST Nanolab 20a UST FLASHII UST PXN 22 Vattenfall district heat supply Heat Distribution Sceme of DESY Premises XFEL cryogenic UST = heat substation cuts for calculations exist access to heat distribution

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 11 Simulation Models for MATLAB/Simulink district heat transfer station heat substation heat pipesheat exchanger of the cryogenic plant

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 12 Classified Heat Load Curve of street of the cryogenic plant 2 streets of the cryogenic plant DESY heat consumption ,9 GWh/a

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 13 Results of Cryogenic Heat Utilization 1 street2 streets heat extraction4,6 GWh/a7,0 GWh/a cost savings 1) €/a €/a payback period 2) 2,6 a1,7 a cash value after 10 years 3) € € CO 2 -Emission 4) t-CO 2 /a1.669 t-CO 2 /a 1)price for district heat: 0,05 €/kWh 2)investment costs: 592 k€ 3)refunding rate: 10 % 4)district heat: 238 g CO 2 /kWh

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 14 Waste Heat Utilization from the XFEL Water Cooling Pump House DESY campus Pump House Schenefeld

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 15 cooling towers klystrons: 7500 kW magnets: 500 kW compression chiller air conditioning: 800 kW electronic racks: 200 kW (water cooled) heat exchanger 30°C 8°C 20°C summer T air >16°C winter T air <16°C heat exchanger Water Cooling of XFEL Injector and Main Linac XTL 45°C 14°C 30°C 18°C 28°C 25°C 40°C Electronic rack cooling in winter

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 16 District heating transfer station UST 48 UST 8 UST 47 UST 28c UST 49 UST 72 UST 24UST 30 UST 25b3 UST 25 UST 25c UST 1d UST 54 UST 2 UST 1a UST 7 UST 5 UST 10 UST 16 UST 17 UST 3b UST 3 UST 80b UST 62 UST 64 UST 69 UST 67 UST 67-2 UST UST CFEL 46 UST ZOQ 45 4a UST CSSB 3a UST 11a UST Nanolab 20a UST FLASHII UST PXN 22 Vattenfall district heat supply Heat Distribution Sceme of DESY Premises XHMP waste heat pump UST = heat substation cuts for calculations

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 17 Waste Heat Pump Calculation > Heat pump: 630 kW, T cond = 85 °C, T vap = 40 °C > Heat is transferred into the heat distribution return pipe > Investment costs are 725 k€ > Without heat utilization from the cryogenics 1 heat pump heat economy4,6 GWh/a cost savings 1) €/a payback period 2) 9,8 a Cash value after 10 years 3) € CO 2 -Emission 4) 745 t-CO 2 /a 1) price for district heating: 0,05 €/kWh electricity: 0,15 €/kWh 2) investment costs: € 3) adequate target rate: 10 % 4) district heating: 238 g-CO 2 /kWh elecricity: 336 g-CO 2 /kWh

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 18 Conclusion Cooling water waste heat utilization with heat pump > The most waste heat goes into the cooling water > The cooling water temperatures are to low for direct transfer into the heat distribution pipes > One needs a heat pump to boost the temperature > The savings does not pay back the invest and service costs and > The XFEL pump house XHMP is near the cryogenics hall > The heat pump is in competition with the cryogenics > This makes it even more uneconomic

Jens-Peter Jensen, Eva Leister | Energy for Sustainable Science | | page 19 Conclusion XFEL Cryogenic oil waste heat utilization The utilization of the oil waste heat pays back after 2 – 3 years Heat pump utilization to boost low temperatures does not pay