The present disclosure relates to systems and methods for increasing the output of a volumetric fluid expander that utilizes exhaust gases as a working fluid.
Waste heat energy is necessarily produced in many processes that generate energy or convert energy into useful work, such as a power plant. Typically, such waste heat energy is released into the ambient environment. In one application, waste heat energy is generated from an internal combustion engine. Exhaust gases from the engine have a high temperature and pressure and are typically discharged into the ambient environment without any energy recovery process. Alternatively, some approaches have been introduced to recover waste energy and re-use the recovered energy in the same process or in separate processes. However, there is still demand for enhancing the efficiency of energy recovery.
Various aspects are described in this disclosure, which include, but are not limited to, the following aspects. In general, an exhaust gas energy recovery system for an internal combustion engine having an air intake and an exhaust outlet is disclosed. The energy recovery system can include a water injection system that expands the volume of a working fluid (e.g. exhaust) received by a volumetric fluid expander. The water injection mechanism can include a water injector and a pump for providing pressurized water to the water injector. In one aspect, the water injector is positioned to inject water at a location between the air intake and the volumetric fluid expander to cause a volumetric expansion. Example locations are: at the air intake, upstream of a supercharger or turbocharger, in the intake manifold, in the cylinders of the engine, in the exhaust manifold of the engine, and at a location between the engine and the fluid expander.
In one aspect of the disclosure, the volumetric fluid expander is provided to generate useful work by expanding a working fluid. In one application, the volumetric fluid expander can be utilized to recover waste energy from a power plant, such as waste heat energy from a fuel cell or an internal combustion engine. The power plant may be provided in a vehicle or may be provided in a stationary application such as could be the case when the power plant is used as a generator. In one possible configuration and by non-limiting example, the volumetric fluid expander is used for an internal combustion engine with a water injection mechanism.
In one example, the working fluid is all or part of the exhaust gas stream from an internal combustion engine or a fuel cell. In another example, the working fluid is separate from and heated by a waste heat stream from an internal combustion engine or a fuel cell, such as is disclosed in Patent Cooperation Treaty International Publication Number WO 2013/130774. WO 2013/130774 discloses that the working fluid can be used in a Rankine cycle where the working fluid may be a solvent such as ethanol, n-pentane, or toluene. The entirety of WO 2013/120774 is hereby incorporated by reference herein.
As shown, the volumetric fluid expander includes a housing having an inlet port configured to admit the working fluid at a first pressure and an outlet port configured to discharge the working fluid at a second pressure lower than the first pressure. The expander also includes first and second twisted meshed rotors rotatably disposed in the housing that are configured to be rotated by the working fluid and to transfer the working fluid from the inlet to the outlet. Each rotor is provided with a plurality of lobes oriented such that when one lobe of the first rotor is leading with respect to the inlet port, one lobe of the second rotor is trailing with respect to the inlet port. The expander additionally includes an output shaft that is rotated by movement of the rotors such that energy recovered by the volumetric fluid expander can be transferred back to the power plant.
In another aspect of the disclosure, an exhaust gas energy recovery system is provided. The system includes an internal combustion engine, a volumetric fluid expander, and a water injection mechanism. The combustion engine includes at least one cylinder and an exhaust gas outlet for conveying an exhaust gas stream at a first pressure. The volumetric fluid expander includes a housing and an output shaft. The housing has an inlet and an outlet, and the inlet is in fluid communication with the exhaust gas outlet. The volumetric fluid expander is configured to generate useful work at the output shaft by expanding the exhaust gas stream to a second pressure lower than the first pressure generally without reducing the volume of the exhaust gas stream as the exhaust gas stream moves from the housing inlet to the outlet. In some embodiments, the volumetric fluid expander includes first and second twisted meshed rotors rotatably disposed in the housing. The rotors have an equal number of lobes, and the lobes of the first rotor do not contact the lobes of the second rotor.
The water injection mechanism is configured to inject water into the cylinder at an exhaust cycle of the cylinder. In some embodiments, the water injection mechanism is configured to inject water into the cylinder before the exhaust cycle of the cylinder begins. The water injection mechanism may include a plurality of water injectors, a water pump device, a water reservoir tank, and a controller. The water injector is configured to inject water into the cylinder. The water pump device is connected to the water injector, and the water tank is connected to the water pump device. The controller may be configured to control the water injector to selectively inject water into the cylinder at or before the exhaust cycle of the cylinder.
The output shaft of the volumetric fluid expander may be coupled to an output shaft of the combustion engine, a hydraulic motor and/or a generator.
In yet another aspect of the disclosure, a method for recovering exhaust gas energy is provided. The method includes injecting, by a water injection mechanism, water into a cylinder of an engine at an exhaust cycle of the cylinder, wherein the injected water vaporizes within the cylinder; collecting, via an exhaust manifold of the engine, exhaust gas stream mixed with the vaporized water;
supplying the exhaust gas stream into a volumetric fluid expander, the exhaust gas stream having a first pressure; and generating, by the volumetric fluid expander, useful work at an output shaft of the expander by expanding the exhaust gas stream to a second pressure lower than the first pressure.
Various embodiments will be described in detail with reference to the drawings, wherein like reference numerals represent like parts and assemblies throughout the several views. Reference to various embodiments does not limit the scope of the claims attached hereto. Additionally, any examples set forth in this specification are not intended to be limiting and merely set forth some of the many possible embodiments for the appended claims.
Referring now to
As shown, expansion device 20 has a housing 22 with a fluid inlet 24 and a fluid outlet 26 through which the fluid 12-1 undergoes a pressure drop to transfer energy to the output shaft 38. The inlet port 24 is configured to admit the working fluid 12-1 at a first pressure whereas the outlet port 26 is configured to discharge the working fluid 12-2 at a second pressure lower than the first pressure. The output shaft 38 is driven by synchronously connected first and second interleaved counter-rotating rotors 30, 32 which are disposed in a cavity 28 of the housing 22. Each of the rotors 30, 32 has lobes that are twisted or helically disposed along the length of the rotors 30, 32. Upon rotation of the rotors 30, 32, the lobes at least partially seal the fluid 12-1 against an interior side of the housing at which point expansion of the fluid 12-1 only occurs to the extent allowed by leakage which represents and inefficiency in the system. In contrast to some expansion devices that change the volume of the fluid when the fluid is sealed, the volume defined between the lobes and the interior side of the housing 22 of device 20 is constant as the fluid 12-1 traverses the length of the rotors 30, 32. Accordingly, the expansion device 20 is referred to as a “volumetric device” as the sealed or partially sealed fluid volume does not change.
As additionally shown in
As shown, the first and second rotors 30 and 32 are fixed to respective rotor shafts, the first rotor being fixed to an output shaft 38 and the second rotor being fixed to a shaft 40. Each of the rotor shafts 38, 40 is mounted for rotation on a set of bearings (not shown) about an axis X1, X2, respectively. It is noted that axes X1 and X2 are generally parallel to each other.
The first and second rotors 30 and 32 are interleaved and continuously meshed for unitary rotation with each other. With renewed reference to
The output shaft 38 is rotated by the working fluid 12 as the fluid undergoes expansion from the higher first pressure working fluid 12-1 to the lower second pressure working fluid 12-2. As may additionally be seen in both
In one aspect of the geometry of the expander 20, each of the rotor lobes 30-1 to 30-4 and 32-1 to 32-4 has a lobe geometry in which the twist of each of the first and second rotors 30 and 32 is constant along their substantially matching length 34. As shown schematically at
In another aspect of the expander geometry, the inlet port 24 includes an inlet angle 24-1, as can be seen schematically at
Furthermore, and as shown in
In another aspect of the expander geometry, the outlet port 26 includes an outlet angle 26-1, as can be seen schematically at
The efficiency of the expander 20 can be optimized by coordinating the geometry of the inlet angle 24-1 and the geometry of the rotors 30, 32. For example, the helix angle HA of the rotors 30, 32 and the inlet angle 24-1 can be configured together in a complementary fashion. Because the inlet port 24 introduces the fluid 12-1 to both the leading and trailing faces of each rotor 30, 32, the fluid 12-1 performs both positive and negative work on the expander 20.
To illustrate,
In generalized terms, the fluid 12-1 impinges on the trailing surfaces of the lobes as they pass through the inlet port opening 24b and positive work is performed on each rotor 30, 32. By use of the term positive work, it is meant that the fluid 12-1 causes the rotors to rotate in the desired direction: direction R1 for rotor 30 and direction R2 for rotor 32. As shown, fluid 12-1 will operate to impart positive work on the trailing surface 32-2b of rotor 32-2, for example on surface portion 47. The fluid 12-1 is also imparting positive work on the trailing surface 30-4b of rotor 30-1, for example of surface portion 46. However, the fluid 12-1 also impinges on the leading surfaces of the lobes, for example surfaces 30-1 and 32-1, as they pass through the inlet port opening 24b thereby causing negative work to be performed on each rotor 30, 32. By use of the term negative work, it is meant that the fluid 12-1 causes the rotors to rotate opposite to the desired direction, R1, R2.
Accordingly, it is desirable to shape and orient the rotors 30, 32 and to shape and orient the inlet port 24 such that as much of the fluid 12-1 as possible impinges on the trailing surfaces of the lobes with as little of the fluid 12-1 impinging on the on the leading lobes such that the highest net positive work can be performed by the expander 20.
One advantageous configuration for optimizing the efficiency and net positive work of the expander 20 is a rotor lobe helix angle HA of about 35 degrees and an inlet angle 24-1 of about 30 degrees. Such a configuration operates to maximize the impingement area of the trailing surfaces on the lobes while minimizing the impingement area of the leading surfaces of the lobes. In one example, the helix angle is between about 25 degrees and about 40 degrees. In one example, the inlet angle 24-1 is set to be within (plus or minus) 15 degrees of the helix angle. In one example, the helix angle is between about 25 degrees and about 40 degrees. In one example, the inlet angle 24-1 is set to be within (plus or minus) 15 degrees of the helix angle HA. In one example, the inlet angle is within (plus or minus) 10 degrees of the helix angle. In one example, the inlet angle 24-1 is set to be within (plus or minus) 5 degrees of the helix angle HA. In one example, the inlet angle 24-1 is set to be within (plus or minus) fifteen percent of the helix angle HA while in one example, the inlet angle 24-1 is within ten percent of the helix angle. Other inlet angle and helix angle values are possible without departing from the concepts presented herein. However, it has been found that where the values for the inlet angle and the helix angle are not sufficiently close, a significant drop in efficiency (e.g. 10-15% drop) can occur.
Referring to
As can be seen at
The volumetric fluid expander 20 operates to recover energy from exhaust gases of the engine 202. The exhaust gases discharged from the cylinders 204 through the exhaust manifold 208 have a higher pressure than ambient pressure, and, thus, contain energy that can be recovered by the volumetric fluid expander 20. To recuperate energy from the exhaust gases, the volumetric fluid expander 20 is configured to receive the exhaust gases from the engine 202, and expand the exhaust gases so that the exhaust gases have a lower pressure when they are discharged from the expander 20 than the exhaust gases entering the expander 20. The volumetric fluid expander 20 recuperates energy from the exhaust gases as the exhaust gases expand within the expander 20, and generates a mechanical work out of the recovered energy.
In some embodiments, the volumetric fluid expander as described herein is used for the volumetric fluid expander 20. For example, the volumetric fluid expander 20 includes a housing, a plurality of rotors, and an output shaft. The housing has inlet and outlet ports. The inlet port is in fluid communication with the exhaust manifold to receive the exhaust gases from the cylinders 204. The outlet port discharges the exhaust gases that have been expanded within the expander 20. The plurality of rotors is arranged within the housing and operates to expand the exhaust gases. As shown above with reference to
The volumetric fluid expander 20 of this type is advantageous in combination with the disclosed water injection system because multiphase flow that may be caused by the water injection system does not adversely affect the expander or its constituent components. In comparison, some other types of systems, such as a centrifugal turbine system, are not able to accommodate multiphase flow without damage and/or significant reductions in efficiency.
Referring to
In this example, the water injection mechanism 230 includes a plurality of water injectors 232, a water pump device 234, a water tank 236, and a controller 238. A water injector 232 is installed for each cylinder 204 and is configured to inject water into the cylinder 204. The water pump device 234 is connected to the water injectors 232 and configured to selectively supply water to the water injectors 232. The water pump device 234 is in fluid communication with the water tank 236 and operates to provide water from the water tank 236 to the water injectors 232. In some embodiments, the controller 238 may be connected to the water pump device 234 and configured to activate the water pump device 234 to provide water to the water injectors 232 in such a manner that the water injectors 232 inject water into the cylinders 204 at or before the exhaust cycle of the cylinders 204. Additionally or alternatively, the controller 238 may be configured to activate the water pump device 234 and each water injector 232 to selectively inject water into the cylinder 204 at or before the exhaust cycle of the cylinder 204.
The water injection mechanism 230 also functions to reduce a cooling load of the engine 202 because the water injected to the cylinder 204 functions as part of an engine cooling system. The water introduced into the cylinder 204 cools down engine components such as engine heads and pistons. As a result, the water injection mechanism 230 may share a cooling load with the engine cooling system such as a radiator or a heat exchanger.
In some embodiments, the water injection mechanism 230 may selectively operate only when the exhaust gases alone from the engine 202 is not sufficient for operating the volumetric fluid expander 20. Typically, an engine operating at a low RPM does not generate a sufficient volume of exhaust gases for operation of the volumetric fluid expander 20 that is directly connected to the exhaust manifold 208 of the engine 202. In this case, the water injection mechanism 230 operates to inject water into the cylinders 204 to increase a volume of the entire exhaust gases, which have been mixed with vaporized water. When the engine operates at a high RPM in which a sufficient volume of exhaust gases is generated from the engine, the water injection mechanism 230 need not operate.
In one possible, but non-limiting, embodiment, an engine running below a threshold output value (e.g. about 1,500 RPM which may be around 15% load of the engine with an exhaust gas temperature in the range of about 200° C. to about 250° C.) may generate exhaust gases that would not be sufficient to operate the volumetric fluid expander 20 at a desired efficiency or output. Accordingly, when the engine is running below the threshold output value, the water injection mechanism 230 may be operated to add a volume of vaporized water into the exhaust gases, as discussed above. In contrast, where an engine operates at or above the threshold output value (e.g. about 2,000 RPM which may be around 50% load of the engine with an exhaust gas temperature exceeding 350oC), the engine may generate exhaust gases that would be sufficient to operate the volumetric fluid expander 20 at a desired efficiency or output.
The water injection mechanism 230 in all of the configurations shown at
The various embodiments described above are provided by way of illustration only and should not be construed to limit the claims attached hereto. Those skilled in the art will readily recognize various modifications and changes that may be made without following the example embodiments and applications illustrated and described herein, and without departing from the true spirit and scope of the following claims.
This application is a continuation-in-part of and claims priority to PCT International Patent application PCT/US2013/078089 filed on 27 Dec. 2013 which claims priority to U.S. Patent Application Ser. No. 61/748,744 filed on 3 Jan. 2013. Each of the aforementioned disclosures is incorporated herein by reference in its entirety.
Number | Date | Country | |
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61748744 | Jan 2013 | US |
Number | Date | Country | |
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Parent | PCT/US2013/078089 | Dec 2013 | US |
Child | 14790745 | US |