Waste heat recovery system and waste heat recovery method

Patent metadata

Field	Value
Publication number	US-9732637-B2
Application number	US-201514662735-A
Country	US
Kind code	B2
Filing date	Mar 19, 2015
Priority date	Apr 4, 2014
Publication date	Aug 15, 2017
Grant date	Aug 15, 2017

Abstract

A waste heat recovery system includes: a heater which evaporates a working medium by exchanging heat between supercharged air supplied to an engine and the working medium; an expander which expands the working medium which has flowed out from the heater; a power recovery device connected to the expander; a condenser which condenses the working medium which has flowed out from the expander; a cooling medium supply pipe for supplying a cooling medium to an air cooler which cools the supercharged air which has flowed out from the heater; a cooling medium pump which is provided in the cooling medium supply pipe and which sends the cooling medium to the air cooler; and a branch pipe which bifurcates a part of the cooling medium flowing in the cooling medium supply pipe, to the condenser, in such a manner that the working medium is cooled by the cooling medium.

First claim

The invention claimed is:

1. A waste heat recovery system, comprising:
a heater which evaporates a working medium by exchanging heat between supercharged air supplied to an engine and the working medium;
an expander which expands the working medium which has flowed out from the heater;
a power recovery device connected to the expander;
a condenser which condenses the working medium which has flowed out from the expander;
a cooling medium supply pipe for supplying a cooling medium to an air cooler which cools the supercharged air which has flowed out from the heater;
a cooling medium pump which is provided in the cooling medium supply pipe and which sends the cooling medium to the air cooler; and
a branch pipe which directs a part of the cooling medium flowing in the cooling medium supply pipe, to the condenser, in such a manner that the working medium is cooled by the cooling medium.

2. The waste heat recovery system according to claim 1 , further comprising:
an adjustment valve which is provided in the branch pipe, the degree of opening thereof being adjustable; and
a controller which controls the degree of opening of the adjustment valve in such a manner that a temperature of the supercharged air which has flowed out from the air cooler is equal to or lower than a set temperature.

3. The waste heat recovery system according to claim 2 , further comprising:
a circulating pump which sends the working medium which has flowed out from the condenser to the heater,
wherein the controller halts the circulating pump, when a temperature differential obtained by subtracting the temperature of the cooling medium before flowing into the condenser from the temperature of the cooling medium after having flowed out from the condenser has become equal to or greater than a reference temperature, or when a pressure differential obtained by subtracting a pressure of the cooling medium after having flowed out from the condenser from the pressure of the cooling medium before flowing into the condenser has become equal to or lower than a reference pressure.

4. The waste heat recovery system according to claim 3 , further comprising:
a first bypass flow channel which bypasses the heater;
a first bypass valve provided in the first bypass flow channel;
a second bypass flow channel which bypasses the expander;
a second bypass valve provided in the second bypass flow channel; and
a shut-off valve which can shut off the inflow of the working medium which has flowed out from the heater, to the expander,
wherein the controller halts the circulating pump, and also opens the first bypass valve and the second bypass valve and closes the shut-off valve while maintaining the degree of opening of the adjustment valve at a designated degree of opening, when the temperature differential has become equal to or greater than the reference temperature, or when the pressure differential has become equal to or lower than the reference pressure.

5. The waste heat recovery system according to claim 4 , wherein the controller closes the adjustment valve when the temperature of the working medium located between the first bypass flow channel and the expander on the downstream side of the heater has become equal to or lower than a threshold value.

6. The waste heat recovery system according to claim 2 , wherein, when the temperature of the supercharged air after having flowed out from the air cooler is equal to or lower than a designated temperature which is lower than the set temperature, the controller adjusts the degree of opening of the adjustment valve, in such a manner that a temperature differential obtained by subtracting a temperature of the cooling medium before flowing into the condenser from the temperature of the cooling medium after having flowed out from the condenser becomes a specified temperature: or in such a manner that a pressure differential obtained by subtracting a pressure of the cooling medium after having flowed out from the condenser from the pressure of the cooling medium before flowing into the condenser becomes a specified pressure.

7. The waste heat recovery system according to claim 6 , wherein the controller adjusts the number of revolutions of the circulating pump in such a manner that the temperature of the cooling medium after having flowed out from the condenser is equal to or lower than a defined value.

8. The waste heat recovery system according to claim 1 ,
wherein the engine is a ship engine,
the cooling medium supply pipe is configured to be able to supply seawater, as the cooling medium, into the air cooler, and
the branch pipe is configured to be able to supply seawater, as the cooling medium, into the condenser.

9. A waste heat recovery method for recovering waste heat from supercharged air supplied to an engine; comprising:
evaporating a working medium by a heater, by supplying the supercharged air to the heater;
cooling the supercharged air by exchanging heat between the supercharged air which has flowed out from the heater and the cooling medium, by an air cooler;
recovering motive power from the working medium, by expanding the working medium which has flowed out from the heater, by an expander; and
condensing the working medium which has flowed out from the expander, by a condenser,
wherein, the working medium is condensed in the condenser by directing a part of the cooling medium supplied to the air cooler in the cooling step, to the condenser, and an amount of the cooling medium supplied to the condenser is adjusted in such a manner that a temperature of the supercharged air which has flowed out from the air cooler becomes equal to or less than a set temperature.

10. The waste heat recovery method according to claim 9 , further comprising:
a working medium circulating step of sending the working medium which has flowed out from the condenser, to the heater,
wherein, in the working medium circulating step, a sending operation for sending, to the heater, the working medium which has flowed out from the condenser is halted, when a temperature differential obtained by subtracting a temperature of the cooling medium before flowing into the condenser from the temperature of the cooling medium after having flowed out from the condenser has become equal to or greater than the reference temperature, or when a pressure differential obtained by subtracting a pressure of the cooling medium after having flowed out from the condenser from the pressure of the cooling medium before flowing into the condenser has become equal to or lower than a reference pressure.

11. The waste heat recovery method according to claim 10 ,
wherein, in the condensing step, the amount of the cooling medium supplied to the condenser is maintained so as to fall within a prescribed range, when the temperature differential has become equal to or greater than the reference temperature, or when the pressure differential has become equal to or lower than the reference pressure, and
in the working medium circulating step, when the temperature differential has become equal to or greater than the reference temperature, or when the pressure differential has become equal to or lower than the reference pressure, the sending operation is halted, the working medium after having flowed out from the condenser before flowing into the heater is merged with the working medium which has flowed out from the heater, and the merged working medium is made to flow to the condenser without flowing into the expander.

12. The waste heat recovery method according to claim 11 , wherein, in the condensing step, the supply of the cooling medium to the condenser is halted when the temperature of the working

Assignees

• Kobe Steel Ltd
• Miura Kogyo Kk
• Asahi Shipping Co Ltd
• Tsuneishi Shipbuilding Co Ltd

Inventors

• Tanaka Yuji
• Takahashi Kazuo
• Fujisawa Ryo
• Adachi Shigeto
• Narukawa Yutaka

Classifications

• F02B61/00

  Adaptations of engines for driving vehicles or for driving propellers; Combinations of engines with gearing (the engine torque being divided by a differential gear for driving a scavenging or charging pump and the engine output shaft F02B39/06; adaptations or combinations of rotary-piston or oscillating-piston engines F02B53/14) · CPC title

• F01K23/02 Primary

  the engine cycles being thermally coupled · CPC title

• Y02T10/146

  Cross-Sectional Technologies · mapped topic

• F02B61/04

  for driving propellers · CPC title

• Y02T10/126

  Cross-Sectional Technologies · mapped topic