US2016138837A1PendingUtilityA1

Heat pump arrangement and method for operating heat pump arrangement

Assignee: SIEMENS AGPriority: Jun 14, 2013Filed: Jun 4, 2014Published: May 19, 2016
Est. expiryJun 14, 2033(~6.9 yrs left)· nominal 20-yr term from priority
F25B 9/002F25B 7/00F25B 30/00F25B 30/02Y02B30/52
49
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Claims

Abstract

A heat pump arrangement including a first heat pump through which a first fluid flows, a second heat pump through which a second fluid flows, and a heat exchanger to transfer heat from the first fluid to the second fluid. The heat is transferred from the first fluid to the second fluid at a fluid temperature of at least 120° C. for the second fluid. The first fluid and the second fluid each have a volumetric heating capacity of at least 500 kJ/m3 when the heat is transferred from the first fluid to the second fluid. Useful heat is extracted from the second fluid at a fluid temperature of at least 120° C. for the second fluid, and the first fluid and the second fluid each have a volumetric heating capacity of at least 500 kJ/m 3 when the useful heat is extracted.

Claims

exact text as granted — not AI-modified
1 - 10 . (canceled) 
     
     
         11 . A method for operating a heat pump system in which a first fluid flows through a first heat pump, a second fluid flows through a second heat pump, and heat is transferred from the first fluid to the second fluid using a heat exchanger, the method comprising:
 extracting useful heat from the second fluid at a fluid temperature of at least 120° C. for the second fluid, the first fluid and the second fluid each having a volumetric heating capacity of at least 500 kJ/m 3  when the useful heat is extracted.   
     
     
         12 . The method as claimed in  claim 11 , wherein the useful heat is extracted from the second fluid at a fluid temperature of at least 150° C. 
     
     
         13 . The method as claimed in  claim 12 , wherein the useful heat is extracted from the second fluid at a fluid temperature of at least 160° C. 
     
     
         14 . The method as claimed in  claim 11 , wherein the first fluid is a fluoroketone. 
     
     
         15 . The method as claimed in  claim 11 , wherein the second fluid is one of water and a fluoroketone. 
     
     
         16 . The method as claimed in  claim 11 , wherein the first fluid and the second fluid are different fluids. 
     
     
         17 . The method as claimed in  claim 11 , wherein the heat is transferred from the first fluid to the second fluid isothermally. 
     
     
         18 . The method as claimed in  claim 11 , wherein the first fluid and the second fluid each have a volumetric heating capacity of at least 1000 kJ/m 3  when the useful heat is extracted from the second fluid. 
     
     
         19 . The method as claimed in  claim 11 , wherein the first fluid and the second fluid each have a volumetric heating capacity of at least 1200 kJ/m 3  when the useful heat is extracted from the second fluid. 
     
     
         20 . The method as claimed in  claim 11 , wherein the first fluid and the second fluid each have a volumetric heating capacity of at least 1500 kJ/m 3  when the useful heat is extracted from the second fluid. 
     
     
         21 . A heat pump system, comprising:
 a first heat pump through which a first fluid flows;   a second heat pump through which a second fluid flows; and   a heat exchanger configured to transfer heat from the first fluid to the second fluid, the heat being transferred from the first fluid to the second fluid at a fluid temperature of at least 120° C. for the second fluid, the first fluid and the second fluid each having a volumetric heating capacity of at least 500 kJ/m 3  when the heat is transferred from the first fluid to the second fluid.   
     
     
         22 . The heat pump system as claimed in  claim 21 , wherein at least one temperature rise of the first fluid and the second fluid is increased by two-stage compression. 
     
     
         23 . A heat pump system as claimed in  claim 21 , wherein the second fluid is isothermally compressible using a liquid ring compressor.

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