ACTIVE HEAT EXCHANGE SYSTEM DEVELOPMENT FOR LATENT HEAT THERMAL ENERGY STORAGE, TOPICAL REPORT

by GRUMMAN AEROSPACE CORPORATION CORPORATION,

Technical Report, 1980

Barcode

CSP Unique ID 190682872

Status

Electronic Resource

Call number

**Click on MARC view for more information on this report.**

Publication

DOE NASA 0039 79 1; Report; January 1980.

Language

Library's review

ABSTRACT:
This topical report describes the selection and evaluation phase of a program to develop active heat exchange concepts for latent heat thermal energy storage systems applicable to the utility industry. An evaluation of suitable storage media with melting points in the temperature range of
Show More
interest (250 to 400°C) limited the candidates to molten salts from the chloride, hydroxide and nitrate families, based on high storage capacity, good corrosion characteristics and availability in large quantities at reasonable cost. The specific salt recommended for laboratory tests was a chloride eutectic (20. 5KCL • 24. 5NaCL • 55. 0MgCL2% by wt.), with a nominal melting point of 385°C.

Various active heat exchange concepts were identified from among three generic categories: scrapers, agitators/vibrators and slurries. The more practical ones were given a more detailed technical evaluation and an economic comparison with a passive tube-shell design for a reference application (300 MWt storage for 6 hours). Two concepts were selected for hardware development: 1) a direct contact heat exchanger in which molten salt droplets are injected into a cooler counter flowing stream of liquid metal carrier fluid, and 2) a rotating drum scraper in which molten salt is sprayed onto the circumference of a rotating drum, which contains the fluid heat sink in an internal annulus near the surface. A fixed scraper blade removes the solidified salt from the surface which has been nickel plated to decrease adhesion forces.

In addition to improving performance by providing a nearly constant heat transfer rate during discharge, these active heat exchanger concepts were estimated to cost at least 25% less than the passive tube-shell design.
Show Less
Page: 0.1329 seconds