RANKINE CYCLE MID-TEMPERATURE RECUPERATION
A system and method for recuperation is provided including a boiler wherein air and exhaust gas recirculation pass through the boiler and are cooled by thermal transfer with a coolant. The system includes an expander receiving coolant from the boiler, a recuperator receiving coolant from the expander, a condenser receiving coolant from the recuperator; a pump pumping coolant from the condenser to a low temperature portion of the boiler, and a valve, which allows coolant to pass directly from the boiler to the recuperator.
Latest International Engine Intellectual Property Company LLC Patents:
When a Rankine Cycle Waste Heat Recovery (RC-WHR) is applied to air systems (both clean air and EGR), it preferably delivers target air temperatures to be reached for engine emissions compliance. It also tries to achieve as high a cycle efficiency as possible for example to improve engine Brake Specific Fuel Consumption (BSFC). Additionally, recuperation is often desired to help increase the cycle efficiency, regardless, when very dry fluids with narrow P-h dome are used as coolant. However, with a recuperator for energy exchange between pump-out coolant and exhaust from expander in the conventional RC-WHR system, the amount of recuperation, which is limited by the coolant temperature flowing out of recuperator, is constrained by the target air temperature. This constraint limits the cycle efficiency and bsfc improvement from RC-WHR system.
SUMMARYOne or more embodiments provide a system and method for recuperation including a boiler wherein air and exhaust gas recirculation pass through the boiler and are cooled by thermal transfer with a coolant. The system includes an expander receiving coolant from the boiler, a recuperator receiving coolant from the expander, a condenser receiving coolant from the recuperator, a pump pumping coolant from the condenser to a low temperature portion of the boiler, and a valve, which allows coolant to pass directly from the boiler to the recuperator.
In operation, air plus EGR 110 is fed into the boiler 120. An expander 130 is in fluid connection with the boiler and a recuperator 140. Coolant flows from the boiler 120 to the expander 130 and then to the recuperator 140. Some coolant passes from the recuperator 140 into the condenser loop 145 where the coolant then passes through the condenser 150 and is pumped by pump 160 back to the recuperator 140. Finally, coolant passes from the recuperator 140 back to the boiler 120. The coolant in the boiler 120 acts to reduce the temperature of the air plus EGR 110 until the desired temperature at the intake manifold is achieved.
More specifically, instead of plumbing or piping the coolant (or refrigerant) from the pump 260 directly to the recuperater 240, the coolant is first directed to the low temperature section of heat exchanger (boiler) 220. After heated up to a certain degree, the refrigerant is routed to recuperator 240 for recuperation, and then introduced back to boiler 220 for further heating. By piping the coolant in this way, the target temperature is not a constraint to recuperation any more. By adding a multi-position 3-way valve 265, the target temperature may be easily assured. For example, the temperature in the intake manifold 270 may be measured using a temperature sensor 268. Data from the temperature sensor 260 may be passed to a valve control 267 to determine the settings for the valve 265, that is whether the valve should be opened more, closed more, or remain in the same setting so as to deliver the desired temperature at the intake manifold 270.
Consequently, by carefully designing the two sections of the boiler 120, a larger amount of energy may be recuperated, thus increasing the cycle efficiency and providing a BSFC improvement. Additionally, the target intake manifold temperature and the better BSFC improvement may both be achieved in such a system. Stated another way, the target air temperature (fresh air+EGR) at the intake manifold may now be maintained more accurately and consistently under all operating conditions.
With regard to coolants, coolants having a dry, narrow and much skewed P-h dome lead to large portion of energy contained in dry exhaust from the expander. This constitutes a great potential for recuperation, even with little superheat.
In the prior plumbing setup shown in
In the new setup shown in
Additionally, at supercritical conditions, where the coolant's temperature and pressure exceed a boundary point and take on properties between those of a liquid and a gas, additional changes occur. More specifically, supercritical conditions provide higher expansion ratio, and as anticipated, cycle efficiency is improved, but at much more moderate margin. The selection of maximum system pressure also requires evaluation of system weight.
Claims
1. A recuperation system including:
- a boiler, wherein air and exhaust gas recirculation pass through the boiler and are cooled by thermal transfer with a coolant;
- an expander receiving coolant from the boiler;
- a recuperator receiving coolant from the expander;
- a condenser receiving coolant from the recuperator;
- a pump pumping coolant from the condenser to a low temperature portion of the boiler; and
- a valve, wherein the valve allows coolant to pass directly from the boiler to the recuperator.
2. The system of claim 1 wherein the valve is a three-way valve.
3. The system of claim 1 further including a temperature sensor detecting the temperature at the intake manifold.
4. The system of claim 3 further including a valve control controlling the valve.
5. The system of claim 4 wherein the valve control receives an indication of the temperature at the intake manifold from the temperature sensor.
6. The system of claim 5 wherein the valve control adjusts the position of the valve in response to the temperature at the intake manifold.
7. A recuperation method including:
- cooling air and exhaust gas recirculation passing through a boiler by thermal transfer with a coolant;
- receiving the coolant from the boiler at an expander;
- receiving the coolant from the expander at a recuperator;
- receiving the coolant from the recuperator at a condenser;
- pumping coolant from the condenser to a low temperature portion of the boiler; and
- actuating a valve to allow coolant to pass directly from the boiler to the recuperator.
8. The method of claim 7 wherein the valve is a three-way valve.
9. The method of claim 7 further including detecting the temperature at the intake manifold using a temperature sensor.
10. The method of claim 9 further including controlling the valve using a valve control.
11. The method of claim 10 wherein the valve control receives an indication of the temperature at the intake manifold from the temperature sensor.
12. The method of claim 11 wherein the valve control adjusts the position of the valve in response to the temperature at the intake manifold.
Type: Application
Filed: May 3, 2012
Publication Date: May 7, 2015
Applicant: International Engine Intellectual Property Company LLC (Lisle, IL)
Inventor: Chunyi Xia (Naperville, IL)
Application Number: 14/397,523
International Classification: F01K 23/10 (20060101); F01N 5/02 (20060101);