Report 1 – Heat Exchangers, Compressed Air Systems, Heat Sinks and Inline Fans

Report 1 – Heat Exchangers, Compressed Air Systems, Heat Sinks and Inline Fans

By: Armando Moncada, Certified Energy Manager


(Please Note: The United States Patent Office prohibits patenting work that is already part of published material. If it is not your work you cannot patent it. These reports are brief white papers not patent ideas. They are part of the public domain.

Secondly, these ideas are being shared in an open-source manner with everyone including designers, manufacturers and researchers to discover effective means of reducing energy costs. We encourage individuals, facility owners, businesses and research centers to explore the ideas and develop them even further. This idea pool is available to the public to directly address energy efficiency within product design, in an effort to globally update our technology, reduce CO2 emissions and reduce energy consumption. Good luck, be safe and have fun!)


The following is a presentation of findings associated with research related to building energy use. Research accomplished so far this year includes many topics, but this report seeks to compartmentalize the findings and focus on methods for reutilizing waste heat, optimizing heat sinks, refrigeration cycle optimization via compressed air, inline fans and energy recovery devices, a hot side + cold side dual thermal energy storage system (twin box system) and energy storage with compressed air tanks with a twin box system.

Each topic will be described below in list form, ten topics were selected.

 

1.      Thermal Energy Storage with Twin Boxes:

The twin box system is a thermal energy storage system that has a hot side and a cold side. It is applicable to large scale facilities that seek to optimize waste heat or waste cooling. If the refrigeration cycle were to be summarized as the process of moving heat from one volume to another, leaving the first volume colder and the second volume warmer, then the twin box system accomplishes that very idea by using thermal energy storage tanks.

The thermal energy storage tanks in mind are large scale boxes made of steel and filled with fine grain sand. The sand can be premixed with a specific percentage of graphite to increase heat transfer rates through the sand medium. Graphite percents may vary depending on how fine the sand is but should not exceed 15%. The thermal energy storage tanks interface with the working fluid for the building such as chilled water or heating hot water via typical piping connections and heat exchanger coils. It is easier to design the system to be of the crossflow type as opposed to the counter flow type to maximize the use of the space. Additionally, there should be three coils not two. The third is to regulate temperature extremes in case one side gets too hot or too cold, a third coil returns the temperature to a limited range and interfaces with outside air as the heat sink or heat source. This is applicable for days that are extremely hot or cold and the building is mostly calling for either heating or cooling. Lastly, the boxes are about the size of shipping containers and are filled with sand and graphite powder on site. Graphite is currently not priced within an acceptable range but could be manufactured specifically for this application at a lower price in large quantities at some point in the future by the manufacturer of the heat exchanger boxes.

Once the system is in operation heat transfer flows steadily from one box to the other as per building load requirements via compressed air. Air is compressed to a high pressure to ensure adequate heat transfer. After the expansion valve, an energy recovery device is installed to capture the pressure and convert it back to energy. A typical system piping layout between the boxes would look like a loop that goes directly to and from each box, allowing air to flow continuously from one heat exchanger coil to the other. At the entry to the hot box is the compressor and at the entry to the cold box is an expansion valve. There should also be a way to collect trapped moisture via a trap or drain down line of some kind.

This description is a standard description and describes what would be most likely adopted by the average engineer designing the system. There are methods for optimizing these components which will be described later. In short, the compressor is traded for an inline fan and the expansion valve is traded for a valve that can vary an aperture to adjust the pressure but simultaneously is shaped in a manner where the aperture is circular when fully open. The energy recovery device is simply a generator built into the compressed air line, placed after the expansion valve. It will most likely mimic compressed air storage generators in its design.

In Figure 1 below, one can observe that the standard dimensions do not exceed that of a shipping container. Systems should be designed to match acceptable shipping dimensions but not exceed them. One can also observe three pairs of pipe connections.

Figure 1. Heat Exchanger Boxes in Twin Box System, 1 of 2.

 

2.      Refrigeration Cycle Optimization:

The refrigeration cycle typically uses refrigerants at its core process. Even chillers that work off chilled water have a heat exchanger adjacent to the compressor where chilled water drops off its heat and the refrigerant picks up the heat. Compressed air is strongly recommended as a substitute for refrigerant for multiple reasons. Air is abundant, it is free, the greenhouse gas warming potential is zero, as a working fluid the heat transfer conductivity is competitive with refrigerants in their gaseous state. If enhanced conductivity is desired, one can add helium to the compressed air in a ratio that is acceptable to the design engineer. See Table 1 on page 9 for thermal conductivity values associated with potential refrigerants. The central reason for switching to air is because common refrigerants become liquid at higher pressures, air can achieve higher pressures without liquefying which in turn means the delta T (difference in temperature) that is achievable is much greater. This implies that by operating at higher delta T’s the equipment can move heat much faster.

Working at higher pressures often implies consuming more energy. There is a strong need for an energy recovery device to be placed within the piping system directly after the expansion valve. By placing an energy recovery device in the system, the system can work at a much higher pressure and larger delta T, allowing heat transfer to occur more efficiently without paying the cost. The COP, (Coefficient of Performance), increases when one includes the energy recovery device. The energy returned to the system is subtracted from the energy input into the system and the net energy is much lower than expected. For example non-adiabatic compressed air storage has recorded efficiencies near 60%. The energy recovery device could be very sophisticated, compact and mounted inline. A bulge in the piping and the whirring of the machine would be the only way to know that it is there. It could be as simple as a spiral that spins with the air flow.

The scenario of compressed air with a higher working pressure for the refrigeration cycle implies that one would only need three pieces of equipment – a compressor, an expansion valve, and an energy recovery device. In a typical system a compressor would build up the pressure, the heat would be transferred to a medium, the enthalpy of the working fluid drops, then the expansion valve returns the working fluid to a lower pressure and the piping in that part of the system is ready to absorb heat and the cycle begins again. In an optimized system with an inline fan there is a constant flow that is defined by the fan RPM. As the fan spins the mass flow rate increases then the aperture on the opposite side, which in a typical system would be the expansion valve, modulates its cross-sectional area to provide the required pressure difference between both sides. The two systems are similar, but it is predictable that a compressor is less efficient than an inline fan if we count the number of reciprocating moving parts, these represent continuous losses of kinetic energy as they represent inertial losses every time the part accelerates and decelerates.

                                                         

 3.      Multiple Inline Fans:

The argument for multiple inline fans is also considered. Inline fans may have different designs, but they always have a blade angle. The blade angle in an ideal scenario is mathematically predictable as a composite of two vectors – mass flow rate velocity and circumferential velocity associated with the spin of the blade about its axis. In a condenser fan for example the mass flow rate of the air moving through the condenser would be considered constant and if the RPM is constant then the blade angle would only vary with radius. The further out on the blade we look the flatter the angle of the blade would need to be to move through the air in a streamlined manner. Installing multiple inline fans is an attempt to direct flow along different paths in the piping of the compressed air system in a manner where the fan blade angle more closely matches the flow rate + angular velocity composite vector. Briefly stated, as the fan speed increases, the fan blade angle should be steeper relative to the plane of spin. In summary, this strategy is represented with a layout where approximately three inline fans exist in parallel to each other and the system can choose which fan to operate via valves and automated controls. Each fan matches a different flow rate with its blade angle.

 

4.      Condenser Fan Blade Angle Optimization:

Condenser fans are often made of very thin sheet metal that is stamped flat with little variance in the blade angle and then added onto the condenser equipment with a few points of connection, the angle of the blade does not change with a change in the distance from the central axis. Examples where the blade angle is calculated very precisely include wind turbine blades or propellors for planes. If we were to calculate the measured air velocity moving vertically through the condenser and measure the velocity along the plane of rotation, we would realize that the angle should change with distance from the central axis and be a composite vector of the two velocities as described in the previous strategy.

 

5.      Heat Sink Optimization and Thermal Energy Storage Systems:

The best heat sinks are the coldest ones. Compared to a water-cooling tower, or an outside air condenser, where the difference in temperature might be 20 - 30 degrees F, a very cold heat sink changes the electrical consumption of upstream equipment such as pumps and fans. This scenario predicts that pumps and fans can operate at a slower speed consuming less electricity, because the heat transfer rate is dependent upon the mass flow rate times the difference in temperature.

Energy storage in the form of a cooled volume of water is a common method of storing cooling for assistance in reducing kW demand charges during peak hours. Furthermore, the electricity that is used at night helps the local electric utility reduce distribution line losses when delivering power. The demand charges can be such a significant part of a facility owner’s bill that thermal energy storage systems have been developed to offset electricity used during peak hours. Two methods for optimizing heat sinks will be discussed - Radiant Panels or Night Sky Cooling Coupled with Heat Pumps and Nighttime Outside Air Cooling of a Sand Bank using Heat Pumps.

 

6.      Radiant Sky Night Cooling Coupled with Heat Pumps:

Radiant Panels or Night Sky Cooling is a method for cooling a medium using radiation from space. The panels radiate heat out into space, but also the night sky radiates the coldness of space back to the panels, and therefore temperatures can be obtained that are colder than the surrounding air. Radiation panels function because of the temperature difference between space and the medium to be cooled. Water or another working fluid is circulated via heat exchanger tubing or some other conductive medium to the panels and then back to the cold reservoir. In an optimized scenario, a heat pump would be added to the system to increase the temperature difference, allowing for the radiation to space to happen at an increased rate. This enables the thermal energy storage medium, for example a cold-water tank or a pool that is insulated with a cover to avoid water loss and heat gain, to reach colder temperatures. Without the heat pump, the system is almost entirely passive, the user pays energy costs only to recirculate the heat transfer fluid, in this system the user pays to operate a heat pump system with compressed air as the working medium. Secondly an expansion valve is required and lastly an energy recovery device is installed after the expansion valve in order to operate at higher pressures and also to achieve higher temperatures. Although more energy is invested to move the heat, more heat is being removed from the reservoir. It is important to note because radiant panels can achieve very cold temperatures but only for an intermittent period of time. It should also be noted that radiant panels have been developed that operate during the day by blocking the wavelengths associated with daylight, enabling cooling to occur even with the sun directly overhead.

 

 7.      Sand Bank Thermal Energy Storage Coupled with Heat Pumps and Nighttime Cooling, Radiant Panels are an Optional Add-On:

Volumes filled with fine grain sand stand as a good argument for thermal energy storage type systems. The heat transfer rate of moist fine grain sand can be as high as 1.7 W/m-K, while the value for water rests at 0.6 W/m-K. Graphite is much higher and can easily achieve 200 W/m-K. In an energy storage system that utilizes sand, water corrosion is no longer an issue. Also, graphite when added to the fine grain sand can increase the conduction rate significantly even if added in only small percentages.

Other benefits include access to cooler nighttime temperatures, the use of night sky cooling radiant panels, reduced electrical demand charges, ability to size cooling equipment to a smaller scale if the amount of cooling is no longer 100% on demand, rather some of the cooling is stored from the nighttime cooling process at the sand bank heat sink.

The benefit of compressed air is that one can choose the operating delta T and achieve colder temperatures in a shorter amount of time. If an energy recovery device is used, the majority of the energy used for compression is recovered. Most refrigerants phase change to liquid at higher pressures which places a ceiling on the maximum delta T achievable.

The sand bank system is almost self-explanatory. It is a heat sink connected to the working fluid of the HVAC system, for example chilled water, with two heat exchanger coils. One for the working fluid and one for the compressed air. The compressed air piping moves heat to the outside environment via a condenser typically, but a night sky cooling radiant panel could also be utilized. Cooling takes place at night in an effort to make use of cooler outside air temperatures. Lastly, high working pressure is utilized on the hot side of the compressed air loop to further increase the delta T. An energy recovery device is also utilized to conserve energy.

A side note worth mentioning: In a system that is only attempting to store cooling via sand at a cold temperature and expels waste heat to the environment, waste heat cannot be utilized later, although obvious it allows for a comparison to be drawn between a singular system and twin box system.

   

8.      Compressed Air Energy Storage using a Twin Box System, and a Waste Heat Recovery Coil:

Compressed Air is a very attractive form of energy storage because it is so simple, tanks are easy to manufacture, and the specialty parts that require more precise manufacturing are few or off the shelf. Compressed Air Energy Storage can be brought to very high pressures and store considerable amounts of energy. The drawbacks are that there is a space requirement for the large tanks and the round-trip efficiency may be close to 60% for the best systems. Engineers have investigated recycling the waste heat to achieve higher efficiency. This is very possible but has yet to be commercialized. The only thing that eternally remains true for compressed air storage is when the energy is generated and the compressed air is discharged, the decompressed air is very cold and the cooling is free.

A compressed air system that interfaces well with the ideas described so far would require utilizing the free cooling effectively, but also making use of the waste heat is a straightforward method for getting a discount on the energy used to compress the air.

A compressed air energy storage system is by default a heat generation device, as well as a cooling device during decompression. During peak hours clients can make use of energy that is generated via the decompression of the air, which can then be applied to HVAC cooling loads. At nighttime when the compression of the air begins, heat is generated, and that heat can be brought into either the HVAC system for heating or a thermal energy system that stores heat. In addition, if the air being generated doesn’t meet heating specifications, it can be compressed and brought to a higher temperature.

  

9.      Compressed Air with Hydraulics in Exchange of a Typical Compressor for Higher Pressures:

Compressors, when analyzed mechanically, are slightly inefficient because the main piston reciprocates back and forth linearly losing inertia constantly. Energy is required to accelerate the part, then accelerate the part in the opposite direction. One of the ways in which compressed air systems could be optimized is with an inline fan. An inline fan cannot achieve higher pressures as easily because it doesn’t form a complete pressure seal. In this optimization strategy, the concept of having a threaded cylinder spinning slowly and pumping hydraulic fluid without any reciprocating parts can function as a device for increasing the efficiency of the air compression. A compression cycle could occur where hydraulics are added to the system using a hydraulic fluid pump that is essentially a large threaded cylinder with the capacity to create a good seal. Potential materials for the cylinder might be stainless steel, while potential materials for the seal since it will be under high pressure might be nylon or another rigid plastic with a low coefficient of friction.

 

10. Shutter Valves as a substitute for other types of Valves.

Although minor energy saving could be calculated, this measure is intended to optimize valves that regulate air flow in compressed air systems with precision and quick reaction time.

A shutter valve is a valve that operates like a hexagonal camera shutter, enabling calibration to occur with precision in a short amount of time.

See Figure 2 below. A shutter valve will be in demand if compressed air systems that modulate in speed become popular, for the reason that as the inline fan increases its RPM, the shutter valve would work in tandem with the inline fan and create the required pressure differential in a brief period of time using a PID (Proportion Integral Derivative Controller) loop and a pressure sensor.

It may be in demand from a controls engineer’s perspective for hydronic flow as well but would be redesigned more robustly for a denser fluid. Control engineers often spend a large amount of time coordinating valve position with GPM flow rate. To reduce calibration time, points are marked out ahead of time in 10% increments on the outer wheel, which controls the aperture area. For incompressible fluids, aperture area is expected to be proportional to GPM, for a similar pumping head pressure.

 

Fig. 2. Shutter Valve

 


 Table 1 – Thermal Conductivity of Materials

 

Thermal Conductivity of Common Materials

 

Material

Thermal Conductivity

Watts/ meter - Kelvin

 

 

Graphite

200-500

Sand Course

0.25

Sand Fine Dry

0.34

Sand Fine Moist

1.7-2.3

Water

0.6

 

 

Helium

0.1513

Nitrogen

0.02598

Oxygen

0.02674

Air

0.025969

R-32 (gas)

0.0124

R-32 (liquid)

0.135

R-454B (gas)

0.013

R-454B (liquid)

0.1054

 

 

Aluminum

237

Copper

401

Steel

45

Stainless Steel

15-25

Titanium

21.6-21.9

 

 

 

 

 

 

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