Cogenerating system

Patent metadata

Field	Value
Publication number	US-9874114-B2
Application number	US-201514791066-A
Country	US
Kind code	B2
Filing date	Jul 2, 2015
Priority date	Jul 17, 2014
Publication date	Jan 23, 2018
Grant date	Jan 23, 2018

Abstract

A cogenerating system includes a Rankine cycle, a high-temperature heat transfer medium circuit, a low-temperature heat transfer medium circuit, a bypass channel, a heat exchanger, and a flow rate adjustment mechanism. The high-temperature heat transfer medium circuit is configured such that an evaporator is supplied with a high-temperature heat transfer medium by a high-temperature heat transfer medium heat exchanger. The low-temperature heat transfer medium circuit is configured such that a condenser is supplied with a low-temperature heat transfer medium by a low-temperature heat transfer medium heat exchanger. The flow rate adjustment mechanism includes at least a flow rate limiter that limits the flow rate of the high-temperature heat transfer medium to be supplied to the evaporator, and adjusts a ratio of the flow rate of the high-temperature heat transfer medium flowing through the bypass channel to the flow rate of the high-temperature heat transfer medium flowing through the evaporator.

First claim

What is claimed is:

1. A cogenerating system comprising:
a first circuit that circulates a first heat transfer medium flowing therein;
a Rankine cycle that circulates a working fluid flowing therein;
a second circuit that circulates a second heat transfer medium flowing therein, a temperature of the second heat transfer medium being lower than a temperature of the first medium;
a first heat source;
a first heat exchanger that is disposed on the first circuit, transfers heat of the first heat source to the first heat transfer medium, and evaporates the working fluid;
a second heat exchanger that is disposed sharedly on the first circuit and the Rankine cycle, and transfers heat of the first heat transfer medium to the working fluid;
a pump that is disposed on the Rankine cycle, and circulates the working fluid;
an expander that is disposed on the Rankine cycle, and expands the working fluid;
a third heat exchanger that is disposed sharedly on the Rankine cycle and the second circuit, transfers heat of the working fluid to the second heat transfer medium, and condenses the expanded working fluid;
a second heat source having a temperature lower than a temperature of the first heat source; and
a fourth heat exchanger that is disposed on the second circuit, and transfers heat of the second heat transfer medium to the second heat source, wherein the first circuit includes a first portion and a second portion, the first portion being located between a portion where the first heat transfer medium flows out from the first heat exchanger and a portion where the first heat transfer medium flows into the second heat exchanger, the second portion being located between a portion where the first heat transfer medium flows out from the second heat exchanger and a portion where the first heat transfer medium flows into the first heat exchanger,
wherein the cogenerating system further comprises:
a first bypass channel that that connects the first portion to the second portion of the first circuit to flow the first heat transfer medium from the first portion to the second portion;
a fifth heat exchanger that is disposed sharedly on the second circuit and the first bypass channel, and transfers heat of the first heat transfer medium to the second heat transfer medium; and
an adjustment mechanism that adjusts a ratio of an amount of the first heat transfer medium flowing in the first bypass channel to an amount of the first heat transfer medium flowing into the second heat exchanger in the first circuit, and
wherein the adjustment mechanism allows or stops a flow of the first heat transfer medium into the second heat exchanger in the first circuit.

2. The cogenerating system according to claim 1 , wherein the adjustment mechanism comprises a first valve and a second valve, the first valve being located between the first portion and the portion where the first heat transfer medium flows into the second heat exchanger in the first circuit, the second valve being located on the first bypass channel.

3. The cogenerating system according to claim 2 , wherein the first valve comprises a fixed throttle valve.

4. The cogenerating system according to claim 1 , wherein the adjustment mechanism comprises a three way valve, and is located at the first portion of the first circuit.

5. The cogenerating system according to claim 1 , wherein in the second circuit, the fifth heat exchanger is located between a portion where the second heat transfer medium flows out from the third heat exchanger and a portion where the second heat transfer medium flows into the fourth heat exchanger.

6. The cogenerating system according to claim 1 , further comprising a first tank that is disposed on the first circuit, and stores a part of the first heat transfer medium, or a second tank that is disposed on the second circuit, and stores a part of the second heat transfer medium.

7. The cogenerating system according to claim 1 , wherein the boiling point of the first heat transfer medium at atmospheric pressure is higher than an operating temperature of the first heat transfer medium.

8. The cogenerating system according to claim 1 , further comprising:
a burner that generates combustion gas, the combustion gas constituting the first heat source;
a gas passage where the combustion gas flows; and
a sixth heat exchanger that is disposed sharedly on the gas passage and the second circuit, recovers latent heat of the combustion gas, and transfers the latent heat of the combustion gas to the second heat transfer medium,
wherein the first heat exchanger is disposed on the gas passage,
wherein in the gas passage, the sixth heat exchanger is located downstream of the first heat exchanger in a flowing direction of the combustion gas, and
wherein in the second circuit, the sixth heat exchanger is located between a portion where the second heat transfer medium flows out from the fourth heat exchanger and a portion where the second heat transfer medium flows into the third heat exchanger.

9. The cogenerating system according to claim 1 , wherein the first circuit includes a third portion and a fourth portion, the third portion being located between the second portion and the portion where the first heat transfer medium flows into the first heat exchanger, the fourth portion being located between the third portion and the portion where the first heat transfer medium flows into the first heat exchanger,
wherein the cogenerating system further comprises:
a burner that generates combustion gas, the combustion gas constituting the first heat source;
a gas passage where the combustion gas flows;
a second bypass channel that connects the third portion to the fourth portion of the first circuit, causing the first heat transfer medium to flow from the third portion to the fourth portion; and
a sixth heat exchanger that is disposed sharedly on the gas passage and the second bypass channel, and transfers heat of the first heat source to the first heat transfer medium,

wherein the first heat exchanger is disposed on the gas passage,
wherein in the gas passage, the sixth heat exchanger is located downstream of the first heat exchanger in a flowing direction of the combustion gas, and
wherein the cogenerating system further comprises a third valve, located on the second bypass channel.

10. The cogenerating system according to claim 9 , further comprising a seventh heat exchanger that is disposed sharedly on the second circuit and the second bypass channel, and transfers heat of the first heat transfer medium to the second heat transfer medium,
wherein in the second bypass channel, the third portion, the seventh heat exchanger, the sixth heat exchanger and the forth portion are arranged in this order.

11. The cogenerating system according to claim 10 , wherein in the second circuit, the seventh heat exchanger is located between a portion where the second heat transfer medium flows out from the fourth heat exchanger and a portion where the second heat transfer medium flows into the third heat exchanger.

12. The cogenerating system according to claim 11 , wherein in the second circuit, the fifth heat exchanger is located between a portion where the second heat transfer medium flows out from the third heat exchanger and a portion where the second heat transfer medium flows into the fourth heat exchanger.

13. The cogenerating system according to claim 1 , further comprising:
a burner that generates combustion gas, the combustion gas constituting the first heat source;
a gas passage where the combustion gas flows;
a third circuit that circulates a third heat transfer medium flowing therein, a temperatur

Assignees

• Panasonic Ip Man Co Ltd

Inventors

• Okaichi Atsuo
• Hikichi Takumi
• Kido Osao

Classifications

• F24D2101/10

  Gas turbines; Steam engines or steam turbines; Water turbines, e.g. located in water pipes · CPC title

• F24D2103/13

  characterised by their heat exchangers · CPC title

• F24D18/00

  Small-scale combined heat and power [CHP] generation systems specially adapted for domestic heating, space heating or domestic hot-water supply · CPC title

• F24D3/08

  in combination with systems for domestic hot-water supply · CPC title

• F01K17/02

  for heating purposes, e.g. industrial, domestic (F01K17/06 takes precedence; domestic- or space-heating systems, e.g. central-heating systems, in general F24D1/00, F24D3/00, F24D9/00) · CPC title