Patent Application
20120055661
The present application generally relates to thermal storage systems and specifically to high temperature energy storage systems typically used in concentrated solar thermal plants.
High temperature energy storage systems are particularly important for solar thermal applications because they provide continuity and stability of operation during daily solar cycles. Portion of the solar energy collected during the sunlit hours is stored at high temperatures and used during night of cloudy hours. Typical operating temperatures of such systems are between 200 to 1000 degrees Fahrenheit. A large variety of materials are used for thermal storage. Based on whether the materials change their physical state during the charge and discharge cycle, there are single-phase or phase-change processes. Most current technologies use single phase liquid or solid materials. Various salt mixtures in their molten state are applied for liquid storage, while solid state materials—such as high purity graphite and concrete—are not fully developed yet.
The most often used energy storage material in solar power systems is molten salt. This is a mixture of 60 percent sodium nitrate and 40 percent potassium-nitrate, commonly called saltpeter. It is used in liquid (single) phase to store thermal energy by increasing its temperature. It is utilized because it is possible to circulate it as a fluid, it is an efficient medium to store thermal energy and its operating temperatures are compatible with requirements of the currently applied high-pressure and high-temperature steam turbines. It is non-flammable, non-toxic and is commonly used in the chemical and metals industries as a heat-transfer fluid. There are two typical configurations of single-phase molten salt storage systems: In a single-storage tank system, stratification is used to separate the colder bottom from the hot upper layers. In two-tank systems the hot and “cold” liquids are kept in separate tanks.
Beside their benefits, there are considerable disadvantages of single-phase liquid-salt systems: Their melting temperatures are high (400-550° F.); therefore, to avoid freeze-up of critical components (piping, heat exchangers, pumps, valves etc) the complete system requires backup heating and constant circulation through most of the life cycle of the system. The liquid salt requires decoupling of typically three closed loops: primary heat transfer fluid (solar collection media) loop, heat storage media loop and power cycle working fluid loop. The decoupling of these high-temperature loops results in increased complexity and cost of fluid-handling as well as loss of efficiency caused by multiple stages of heat exchange. Another source of thermodynamic inefficiency results from the sliding temperature (or sensible heat) nature of the energy storage: The lowest temperature of the storage medium drives the power generation cycle efficiency.
Phase-change materials (PCMs) provide an alternative for thermal energy storage. PCMs have the potential of providing a more efficient means of energy storage as the temperature change is minimal or zero due to the latent heat of the phase change process. PCM systems typically operate near the solid-liquid equilibrium utilizing the latent heat of fusion (or melting). For high temperature storage required in concentrated solar applications, mostly inorganic salt mixtures are used because their melting temperature is in the desired range and because their relatively high phase-change enthalpy.
Single phase solid thermal storage—mostly concrete and purified graphite—systems are largely in a research and development phase. Their disadvantage is the difficult heat transfer between the storage media and the fluid of the primary loop as well as the working fluid.
Based on configuration and working principle, there are four main system arrangements: Single tank, Dual tank, Encapsulated and Solid state systems. Both the single and dual tank systems apply molten liquid storage materials. The single storage tank relies on stratification to separate the hot from the “cold” liquid layers in the tank. The tank is always full—the liquid level is constant. The hot liquid is charged and discharged from the top portion of the tank while the relatively colder liquid is pumped in and out from the bottom of the tank. In a dual tank system the liquid is pumped from the “cold” to the “hot” tank during the charging cycle and the direction of the flow is reversed during the discharge cycle. The tank levels vary during the cycle. The encapsulated systems use small pockets of thermal storage materials encapsulated and sealed-up in shells for permanent containment. The capsules are typically submerged in a heat transfer fluid. The solid state systems—as described above—have internal hollow or porous structures to facilitate the heat transfer between the thermal fluid and the solid storage material.
The currently known high temperature thermal storage systems have the following main challenges and disadvantages: The liquid, sensitive-heat systems are inherently complex and expensive because of the specialty equipment and materials required for fluid handling, flow-control and heat exchange. The encapsulated systems have a challenge caused by poor heat transfer from the primary heat transfer fluid to the thermal storage material encapsulated typically in spherical shells. The encapsulation process is also expensive as the capsule design needs to withstand high thermal expansions, high pressure and temperature conditions and at the same time provide high thermal conductivity. The low-cost, solid-state storage materials are typically poor thermal conductors and therefore they require high percentage of porous, hollow-space per active storage volume to improve the heat transfer rate. The high porosity results in low average density of the thermal storage system, thus lowering its efficiency, increasing size and cost.
The present application thus describes one embodiment of the invention that may take the form of helically grooved, thin-wall, tubular encapsulation of phase change material (PCM). A permanently sealed, flexible, thin wall tube may be the containment shell of the encapsulated PCM. A helical grooving or “rifling” rolled into the thin wall of the tube may provide the radial and lateral-axial flexibility of the capsule to accommodate the thermal expansion and contraction during the charging and discharging process. The length of the tube may be significantly larger than its diameter. The tube may be completely filled with molten liquid PCM and sealed off at manufacturing. The thermal contraction induced torsion of the helically rifled tube will result in a fractured, graveled solidification of the PCM.
The present application further describes one embodiment of the invention that may take the form of pressure rated steam pipe or vessel that may be filled with PCM tube capsules. Three or more tubes may form a bundle to closely fit into the larger steam pipe. The tube-capsule bundle may fill the entire length of the steam pipe. The steam pipe may have one or multitude of liquid water ports and one or multitude of steam ports. The liquid port may be used for feedwater inlet or condensate drain outlet. The steam port may be used for steam inlet or outlet. Multitude of horizontally oriented steam pipes (filled with PCM capsule tubes) may be stacked on each other to fill the thermal storage container space. The liquid water ports may be connected to a common water header and the steam ports may be connected to a common steam header. The container housing the steam pipes and encapsulated PCM, is insulated to minimize heat losses. To increase the thermal storage capacity and the thermal conductivity, the space between the steam pipes may be filled with thermal oil during the commissioning of the installation.
The present application further describes the flow of steam in a charging and discharging operation mode. In charging mode the steam flows from the heat source—that may be a solar thermal steam generator—to the multitude of steam pipes (PCM container vessels) of the storage container. The steam flows through the space left between the tubular capsules, heating and melting the PCM in the tubes and thereby storing the thermal energy. As the latent heat of the steam transfers into the capsules, the condensed steam drains out of the steam vessels through the liquid port. In discharging operation mode, the feedwater is pumped through the liquid ports of the steam pipes and flows through the hollow space between the capsules. The hot molten PCM inside the tube-capsules, heats the feedwater and the evaporated steam leaves the steam pipes at the steam ports.
These and other features of the present application will become apparent to one of ordinary skill in the art upon review of the following detailed description when taken in conjunction with the several drawings and the appended claims.
Referring now to the drawings, in which like numerals indicate like elements throughout the several views,
a depicts the process flow of the thermal storage module in thermal charging mode. The superheated or saturated steam supplied by the steam generator flows through the steam header 303 and steam distributors (or risers) 313 to the battery of horizontal steam vessels 301. The steam flow 309 passes through the steam vessel 301 and heats up the relatively cold PCM capsule tubes inside the vessels. The phase change material is heated and in the process undergoes gradual melting in the tubes and thus the heat is stored in the PCM capsules. The condensed steam (liquid condensate) is drained through the liquid risers/distributors 312 and steam trap 314 into the condensate receiver 304. The liquid level in the receiver is controlled by a level control loop and valve 310 and the temperature of the condensate output is controlled by a temperature control loop and control valve 311. The main condensate supply pump 305 may or may not supply the condensate 302 which may or may not be blended with the condensate from the receiver and the condensate flow is forwarded by a feedwater pump 306 to the steam generator.
b depicts the process flow of the thermal storage module in thermal discharging mode. In general the flow pattern of the charging mode reverses in the discharging mode. The condensate 302 from the main steam load is supplied by the condensate pump 305 and is pumped through valve 310 and the completely filled receiver vessel 304. The liquid condensate enters into the battery of pressure vessels through the distribution system 312. The heat stored in the PCM tubes heats and evaporates the liquid and the generated steam leaves the battery and it is collected thru the collection risers 313 to the steam header 303. The pressure of the generated steam is controlled by control loop and valve 308. The temperature of the steam is controlled by a de-superheater loop and valve 315.
a depicts the typical use of the present application in a generic solar steam process. In the charging mode the steam is supplied by the solar steam generator 401 to the steam load (steam consuming process) 402 and to the thermal storage system 403. The condensate is collected by the condensate line 404 and pumped by condensate pump 407. The leaving condensate 409 from the thermal storage is mixed with process condensate and the feedwater 406 is pumped by the feedwater pump 408 to the solar steam generator 401. The loop connecting the solar steam generator 401 and the thermal storage system 403 is referred to as the primary loop 411. The loop connecting the steam process 402 and the thermal storage system 403 is referred to as the secondary loop 412. In the discharging mode the direction of the flow through the thermal storage 403 reverses: condensate 430 is pumped through the thermal storage and steam 431 is supplied to the main steam supply line 405.
b depicts a specialized configuration of the present application whereby the duties of the thermal storage system is split into a designated preheating and evaporation system 403 and a designated superheating 422 system. In the discharging cycle, saturated steam is generated in the designated evaporator block and the saturated steam flows to the superheater block for additional heating. The benefit of such configuration is that the composition of the PCM material can be optimized for the two different functions and thereby cost savings and/or efficiency improvement can be achieved.
c depicts the typical use of the present application in a generic power generation system. The function of the thermal storage system is identical to the one described and depicted in
d shows the typical use of present application in an integrated solar desalination and power generation system. The low-pressure exhaust steam of the steam turbine is used as heating source of the desalination system 420. Seawater 447 is supplied to the desalination system by the seawater pump 446 and cooling water 448 is discharged to the sea along with concentrated brine 424. Distilled water 421 is supplied for users by the distilled water pump 422.
