System and method for auxiliary fluid circuit heating or cooling of a superheater during startup and shutdown operations

Patent metadata

Field	Value
Publication number	US-9228452-B2
Application number	US-201313774103-A
Country	US
Kind code	B2
Filing date	Feb 22, 2013
Priority date	Feb 22, 2013
Publication date	Jan 5, 2016
Grant date	Jan 5, 2016

Abstract

System and method for pre-startup or post-shutdown preparation for such power plants are disclosed which are subject to frequent startups and shutdowns, such as a solar operated power plant. The system and method introduces an auxiliary fluid flow to be circulated in an opposite direction to a direction of normal working fluid flow responsible for producing electricity. That is, if the working fluid flow in a first direction for operating the power plant, than the auxiliary fluid flows in a second direction, opposite to the first direction. The auxiliary fluid flows in the second direction for a predetermined time and at a predetermined conditions through a plurality of superheater panel arrangements of solar receiver former to activation of the working fluid circuit, as pre-startup preparation of the power plant, and after cessation of the working fluid circuit, as post-shutdown preparation of the power plant, to attain predetermined conditions in the superheater.

First claim

What is claimed is:

1. A method for at least one of pre-startup preparations and post-shutdown preparations of a solar operated power plant, the solar operated power plant comprising a solar receiver having a superheater section comprising a plurality of superheater panel arrangements, wherein each of the superheater panel arrangements comprises bottom and top headers disposed in a horizontal or sloped manner and connected by a number of vertically disposed heat absorbing tubes, the method comprising:
circulating a working fluid flow in a first direction from an inlet of the superheater section to an outlet of the superheater section; and
circulating in a second direction opposite to that of the first direction an auxiliary fluid flow of varying parameters, one parameter being temperature of the auxiliary fluid flow based on process variables of the superheater section, from the outlet of the superheater section to the inlet of the superheater section, the auxiliary fluid flow circulating:
before circulating the working fluid flow, as the pre-startup preparation of the solar operated power plant during which the auxiliary fluid flow is of a temperature higher than a highest temperature of the headers to gradually heat the headers, and
after cessation of the working fluid flow, as the post-shutdown preparation of the solar operated power plant during which the auxiliary fluid flow is of a temperature lower than a temperature of the headers to gradually cool the headers.

2. The method of claim 1 , wherein the temperature of the auxiliary fluid flow varies for gradual heating or gradual cooling of the headers to minimize thermal stress thereon.

3. The method of claim 1 , wherein the varying parameters of the auxiliary fluid flow, further includes parameters of pressure and flow rate of the auxiliary fluid flow entering the superheater section.

4. The method of claim 3 , wherein the varying parameters of the auxiliary fluid flow vary for gradual heating or gradual cooling of the headers to minimize thermal stress thereon.

5. The method of claim 1 , wherein circulating the auxiliary fluid flow is for a predetermined time period for the pre-startup preparations and post-shutdown preparations to attain a temperature distribution to avoid superheater panel arrangement component thermal stress.

6. The method of claim 1 , wherein the auxiliary fluid flow is circulated until the headers in the superheater panel arrangements are cooled to a desired temperature after power plant shut down.

7. The method of claim 6 , wherein the desired temperature of the superheater section after power plant shut down is predetermined as are temperatures for the superheater panel arrangements, pre-startup preparations, and temperature gradient of the headers.

8. The method of claim 1 , wherein the auxiliary fluid flow is circulated until the headers are heated to a desired temperature for normal operation of the superheater section.

9. The method of claim 8 , wherein the desired temperature for normal operation of the superheater section is predetermined as are the temperatures for the superheater panel arrangements, pre-startup preparations, normal operation parameters of the working fluid flow, and temperature gradient of the headers.

10. The method of claim 1 , wherein process variables of the superheater section are predetermined as are the temperature of the headers, temperature of pipes fluidly connecting the plurality of superheater panel arrangements and pressure within the superheater section.

Assignees

• Alstom Technology Ltd

Inventors

• Terdalkar Rahul J
• Bauver Wesley P
• Sambor Thomas W

Classifications

• F03G6/121

  Controlling or monitoring · CPC title

• F03G6/067

  Binary cycle plants where the fluid from the solar collector heats the working fluid via a heat exchanger · CPC title

• F01K5/02 Primary

  used in regenerative installation · CPC title

• F03G6/065

  having a Rankine cycle · CPC title

• F22B1/006

  using solar heat · CPC title