Distillation and condensation subsystem (DCSS) control in kalina cycle power generation system

• US 6,158,220 A
• Filed: 01/13/1999
• Issued: 12/12/2000
• Est. Priority Date: 01/13/1999
• Status: Expired due to Fees

• Current Assignee: ALSTOM Power Inc. (General Electric Company)
• Original Assignee: ABB Alstrom Power Incorporated
• Inventors: Simon, Jonathan S., Hansen, Paul L., Kuczma, Paul D., Palsson, Jens O.
• Primary Examiner(s): NGUYEN, HOANG M
• Application Number:
  US09/229,363
• Time in Patent Office: 699 Days
• Field of Search: 60/645, 60/649, 60/651, 60/671, 60/673, 165/301, 165/302
• US Class Current: 60/649
• CPC Class Codes: F01K 25/065 with an absorption fluid remaining at least partly in the liquid state, e.g. water for ammonia F01K5/00 takes precedence

Abstract

A method of operating a Kalina cycle power generation system, includes directing a stream of vaporized binary working fluid to a turbine where it is expanded to produce power. A first portion of the expanded binary working fluid is directed to a distiller/condenser having multiple heat exchangers where, using the multiple heat exchangers, it is transformed into a first concentration binary working fluid, having a first concentration of a component of the binary working fluid, and a second concentration binary working fluid, having a second concentration of the component. At least the first concentration binary working fluid directed to a regenerative heat exchanger. A second portion of the expanded binary working fluid is directed to the regenerative heat exchanger where the first concentration binary working fluid is transformed into a vaporized binary working fluid and the second portion of expanded binary working fluid is transformed into a feed binary working fluid. The feed binary working fluid is directed to a vapor generator where it is vaporized. The binary working fluid flow within the distiller/condenser is actively regulated to maintain a desired relationship between the multiple heat exchangers.

Claims

1. A method of operating a Kalina cycle power generation system, comprising the steps of:

directing a stream of vaporized binary working fluid to a turbine;

expanding the vaporized binary working fluid in the turbine to produce power;

directing a first portion of the expanded binary working fluid to a distiller/condenser having multiple heat exchangers;

transforming the first portion of expanded binary working fluid using the multiple heat exchangers, into a first concentration binary working fluid, having a first concentration of a component of the binary working fluid, and a second concentration binary working fluid, having a second concentration of the component, in the distiller/condenser;

directing at least the first concentration binary working fluid to a regenerative heat exchanger;

directing a second portion of the expanded binary working fluid to the regenerative heat exchanger;

transforming the first concentration binary working fluid into a vaporized binary working fluid and the second portion of expanded binary working fluid into a feed binary working fluid, in the regenerative heat exchanger;

directing the feed binary working fluid to a vapor generator;

vaporizing the feed binary working fluid in the vapor generator; and

actively regulating a binary working fluid flow within the distiller/condenser to maintain a relationship between the multiple heat exchangers.

2. A method according to claim 1, wherein the binary working fluid flow is actively regulated to maintain the relationship between all but one of the multiple heat exchangers.

3. A method according to claim 1, wherein the relationship is a level of condensation.

4. A method according to claim 1, wherein the relationship is an amount of the first portion of expanded working fluid directed to respective ones of the multiple heat exchangers.

5. A method according to claim 1, wherein the binary working fluid flow within the distiller/condenser is actively regulated in a first mode to maintain the relationship between the multiple heat exchangers during variations in operating conditions occurring at a first rate and in a second mode to maintain the relationship between the multiple heat exchangers during variations in operating conditions occurring at a second rate which is slower than the first rate.

6. A Kalina cycle power generation system, comprising:

a turbine configured to expand a vaporized binary working fluid to produce power;

a distiller/condenser, having multiple condensing heat exchangers, configured to transform a first portion of expanded binary working fluid into a first concentration binary working fluid, having a first concentration of a component of the binary working fluid, and a second concentration binary working fluid, having a second concentration of the component;

a regenerative heat exchanger configured to transform the first concentration binary working fluid into a vaporized binary working fluid and a second portion of expanded binary working fluid into a feed binary working fluid;

a vapor generator configured to vaporize the feed binary working fluid;

at least one valve operable to regulate binary working fluid flow in the distiller/condenser; and

a controller configured to direct the operation of the at least one valve to maintain a relationship between the multiple heat exchangers.

7. A system according to claim 6, wherein the controller is configured to direct the operation of the at least one valve, to maintain the relationship between all but one of the multiple heat exchangers.

8. A system according to claim 6, wherein the relationship is a level of condensation.

9. A system according to claim 6, wherein the relationship is an amount of the first portion of expanded working fluid directed to respective ones of the multiple heat exchangers.

10. A system according to claim 6, wherein the controller is configured to direct the operation of the at least one valve in a first mode to maintain the relationship between the multiple heat exchangers during variations in operating conditions occurring at a first rate and in a second mode to maintain the relationship between the multiple heat exchangers during variations in the operating conditions occurring at a second rate which is slower than the first rate.