scholarly journals Corrosion of Materials in a Simulated CAES Exhaust Gas Environment

Author(s):  
Holger Lukas

Cold end corrosion due to sulfuric acid is a phenomenum not uncommon in boilers and exhaust gas waste heat boilers. Normally, the operating conditions can be changed to reduce or eliminate the corrosion. In a Compressed Air Energy Storage (CAES) plant, this is not a practical solution. This paper presents the preliminary results of corrosion testing of various materials in a simulated CAES recuperator environment.

Author(s):  
Holger Lukas ◽  
Bhupen Mehta

Cold end corrosion and deposit formation due to sulfuric acid is a phenomenon not uncommon in boilers and waste heat boilers. Normally, the operating conditions can be changed to reduce or eliminate the corrosion and deposition problem. In a Compressed Air Energy Storage (CAES) recuperator, changing the operating conditions is not a practical solution. This paper presents the results of three different test periods using various materials at different operating temperatures.


Author(s):  
M. Nakhamkin ◽  
E. Swensen ◽  
R. B. Schainker ◽  
R. Pollak

A number of analyses concluded that in order to be cost effective a compressed air energy storage (CAES) plant should have a recuperator, which recovers the low pressure (LP) expander’s exhaust gas heat for preheating the cold cavern air before it enters the high pressure (HP) combustor(s). The use of a recuperator reduces heat rate, and accordingly fuel consumption, by as much as 20–25%. Therefore all feasibility studies on CAES performed for various utilities included a recuperator, and the first CAES plant to be built in the U.S., the 110 MW CAES plant for the Alabama Electric Cooperative (AEC) will utilize a recuperator with a 75% effectiveness.


Author(s):  
Michael Nakhamkin ◽  
John R. Stange ◽  
Richard Marshall ◽  
Robert Pelini ◽  
Robert B. Schainker

This paper presents solutions to the extensive corrosion problems affecting recuperators in Compressed Air Energy Storage (CAES) applications. Two advanced designs for a 50 MW CAES plant were engineered: (a) a two-section counterflow arrangement with a replaceable cold end section which operates with tube wall temperatures below the exhaust gas dew point temperature, (b) a three-section design with a flow arrangement which eliminates tube wall temperatures below the exhaust gas dew point temperature. Presented in this paper are a general description, design specifics, performance and cost data for these two conceptual designs. Technical and economic analyses were performed to determine the most practical and economic design.


Author(s):  
Kent Udell ◽  
Michael Beeman

The performance of CAES is evaluated for various configurations, with and without thermal energy storage. First, a conventional compressed air energy storage process is modeled using a time series iterative forward differencing method to simulate the round trip efficiency, exergy storage, cavern temperatures and pressures, and the gas expander exit temperature of a CAES plant. The computational model was validated experimentally by comparing trended data of the compression cycle of a 280 HP Gardener-Denver tandem horizontal two-stage compressor to computational results. It was found that the process of cooling the compressors resulted in a large exergy loss and the inefficiencies of the expanders lead to higher temperature gas being exhausted back to ambient pressures. Second, Advanced Adiabatic Compressed Air Energy Storage (AACAES) was simulated to study the effectiveness of storing the thermal energy removed from the compressors to be added to the compressed air as it enters the expanders at a later time. Third, the concept of increasing the capacity of the thermal energy storage systems to allow recharge with concentrated solar heat was explored. It was found that the thermal efficiency of converting the solar thermal energy to power would be high (> 60%). Further, the expander exhaust temperature and exergy are high (> 500 K), implying that additional waste heat energy recovery will be possible. Taken together, the results of this study show that an integrated, high efficiency, on-demand, water-free, solar energy delivery system is possible if combined with an AACAES system.


2020 ◽  
Vol 180 ◽  
pp. 02002
Author(s):  
Iulian Vlăducă ◽  
Claudia Borzea ◽  
Dan Ionescu ◽  
Alexandra Ţăranu ◽  
Răzvan Ciobanu ◽  
...  

The paper presents the prototype of the first Romanian Compressed Air Energy Storage (CAES) installation. The relatively small scale facility consists of a twin-screw compressor, driven by a 110 kW threephase asynchronous motor, which supplies pressurized air into a 50m3 reservoir, of 20 bar maximum pressure. The air from the vessel is released into a twin-screw expander, whose shaft spins a 132 kW electric generator. The demonstrative model makes use of a 5m3 water tank acting as heat transfer unit, for minimising losses and increasing efficiency and the electric power generated. Air compression and decompression induce energy losses, resulting in a low efficiency, mainly caused by air heating during compression, waste heat being released into the atmosphere. A similar problem is air cooling during decompression, lowering the electric power generated. Thus, using a thermal storage unit plays an essential role in the proper functioning of the facility and in generating maximum electric power. Supervisory control and data acquisition is performed from the automation cabinets. During commissioning tests, a constant stable power of around 50 kW with an 80 kW peak was recorded.


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