Method of utilizing thermal energy

• US 4,756,162 A
• Filed: 04/09/1987
• Issued: 07/12/1988
• Est. Priority Date: 04/09/1987
• Status: Expired due to Fees

• Current Assignee: Abraham Dayan
• Original Assignee: Abraham Dayan
• Inventors: Dayan, Abraham
• Primary Examiner(s): Ostrager, Allen M.
• Application Number:
  US07/040,835
• Time in Patent Office: 460 Days
• Field of Search: 62/476, 60/649, 60/673
• US Class Current: 60/673
• 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 is provided for utilizing sensible heat energy supplied by a high-temperature heating fluid, employing a multi-component working fluid thermodynamic cycle, wherein a solution rich in a lower boiling component is heated in a vapor generator in counter-current heat exchange with the heating fluid to produce a vapor-fluid mixture which is separated in a rectifier into a lean solution and a vapor mixture; the enthalpy of the vapor mixture is optionally increased in a superheater by counter-current heat exchange with said heating fluid at its highest temperature; the vapor mixture is then expanded thereby to perform the function of the cycle; and the spent vapor mixture is dissolved in said lean solution in an absorber so as to regenerate the rich solution; characterized in that the rich solution leaving the absorber is compressed and divided into a first and second parts; the first part is heated by counter-current heat exchange with said lean solution drawn from the rectifier, whereafter said first part of the rich solution is recycled to the vapor generator; whereas the second part of the rich solution extracts additional heat from the heating fluid leaving the vapor generator, by counter-current heat exchange, and is then fed into the rectifier for counter-current mass and heat exchange with the vapor-liquid mixture formed in the vapor generator.

Claims

1. A method for utilizing sensible heat energy supplied by a high-temperature heating fluid for power generation, employing a multi-component working fluid thermodynamic cycle, wherein

a solution having a higher concentration of lower boiling component or components (hereinafter "rich solution") is heated in a vapor generator in counter-current heat exchange with the heating fluid to produce a vapor-liquid mixture which is introduced into a lower zone of a rectifier and separated therein into a solution having a lower concentration of said lower boiling component or components (hereinafter "lean solution") and a vapor mixture;

the enthalpy of the vapor mixture in counter-current heat exchange with said heating fluid at its highest temperature;

the vapor mixture is then expanded to a low pressure level thereby to perform the function of the cycle; and

the spent vapor mixture is introduced into an absorber wherein it is dissolved in said lean solution, under heat rejection to an external coolant, so as to regenerate a rich solution;

said method being characterized in that;

(a) the pressure of the rich solution regenerated in the absorber is increased and the solution is divided into a first and second parts;

(b) said first part of the rich solution is heated in a regenerative heat exchanger by counter-current heat exchange with said lean solution which is drawn from the lower zone of the rectifier, whereafter said first part of the rich solution is recycled to the vapor generator, whereas said lean solution is decompressed by means of an expansion device and fed to the absorber;

(c) said second part of said rich solution is passed through a preheater to extract, by counter-current heat exchange, additional heat from the heating fluid leaving the vapor generator, whereby said second part of said rich solution is heated to the liquid saturation state and is then fed into the upper zone of the rectifier for counter-current mass and heat exchange with said vapor-liquid mixture, thereby to increase the concentration of the lower boiling component in said vapor mixture;

(d) the mass flow-rate of said first part of the rich solution is determined so as to render its apparent heat capacity mass flow rate substantially equal to that of said lean solution passing counter-current thereto through the regenerative preheater;

(e) the composition of the vapor mixture leaving the rectifier is adjusted, by controlling the pressure of the rich solution leaving the absorber and the mass flow rate of the higher boiling component, or components, circulating between the absorber and the rectifier, within technological limits, so that, for a selected vapor mixture flow rate, the temperature of the vapor mixture leaving the superheater is maximized.

2. A method according to claim 1, characterized in that the absorber is of the heat recuperative type wherein the regenerated rich solution is recirculated through the absorber through continuous flow channels in an indirect heat exchange relationship with the fluid mixture in the absorber so as to extract a substantial proportion of the heat of absorption generated therein.

3. A method according to claim 2 wherein the absorber is a multi-stage recuperative absorber.

4. A method according to claim 1 wherein at least one internal stream of working fluid is passed through the vapor generator for counter-current heat transfer to a portion of the rich solution therein, thereby recovering some of the heat energy of said internal stream (or streams).

5. A method according to claim 1 wherein the working fluid system comprises ammonia as a lower boiling component and water as the carrier fluid.

6. A method according to claim 5 wherein the working fluid system consists of a mixture of ammonia and water.

7. A method according to claim 4, wherein the vapor mixture from the superheater is expanded in a first turbine to produce mechanical work, the partially spent vapor mixture from said first turbine is recirculated through the superheater to increase its enthalpy and is then expanded in a second turbine to produce additional mechanical work, the spent vapor mixture from said second turbine is passed through the vapor generator therein to transfer some of its thermal energy to the rich solution, whereafter the vapor mixture is expanded in a third turbine to generate more mechanical work and the spent vapor mixture from said third turbine is recycled to the absorber.

8. A method according to claim 7 wherein the working fluid system comprises ammonia as a lower boiling component and water as the carrier fluid.