Cascaded power plant using low and medium temperature source fluid

• US 4,700,543 A
• Filed: 12/27/1985
• Issued: 10/20/1987
• Est. Priority Date: 07/16/1984
• Status: Expired due to Term

• Current Assignee: Ormat Industries Limited
• Original Assignee: Ormat Turbines Ltd.
• Inventors: Moritz, Alex, Krieger, Zvi
• Primary Examiner(s): Ostrager, Allen M.
• Application Number:
  US06/813,724
• Time in Patent Office: 662 Days
• Field of Search: 60/655, 60/698
• US Class Current: 60/655
• CPC Class Codes: F01K 23/02 the engine cycles being thermally coupled
• CPC Class Codes: F01K 3/185 using waste heat from outside the plant F02G5/00 takes precedence
• CPC Class Codes: F03G 7/04 using pressure differences or thermal differences occurring in nature F03G7/06 takes precedence

Abstract

A plurality of independent, closed Rankine cycle power plants, each of which has a vaporizer, is operated by serially applying a medium or low temperature source fluid to the vaporizers of the power plants for producing heat depleted source fluid. A preheater is provided for each vaporizer; and said heat depleted source fluid is applied to all of the preheaters in parallel. The heat depleted source fluid thus serves to heat the operating fluid to the evaporization temperature, while the source fluid applied to the vaporizers supplies the latent heat of vaporization to the operating fluid of the power plant. The present invention is advantageous, as compared to a conventional cascaded power plant of the type described, because the temperature drop of the source fluid can be increased without reducing the efficiency. Alternatively, the temperature drop can be maintained but the efficiency can be increased. In either case, the power produced by the power plant according to the present invention is increased.

Claims

1. A power plant operating on a source of low or medium temperature fluid comprising:

(a) a plurality of closed Rankine cycle power plant modules each having a vaporizer associated therewith responsive to source fluid for converting operating fluid of the power plant modules to vapor, said modules being arranged in a plurality of levels, each level comprising a plurality of modules;

(b) means for applying source fluid in parallel to each vaporizer in a level to produce heat depleted source fluid, means for applying heat depleted source fluid from a level to each vaporizer in parallel in the succeeding level;

(c) a preheater associated with each vaporizer for preheating operating fluid that is vaporized in the associated vaporizer; and

(d) means for applying heat depleted source fluid from the lowest level to all of the preheaters in parallel.

2. Apparatus according to claim 1 constructed and arranged so that the modules are arranged into a plurality of levels, including means for applying the heat depleted source fluid to all of the preheaters in parallel independently of the levels of the preheaters.

3. Apparatus according to claim 1 including means for applying the heat depleted source fluid to all of the preheaters in parallel independently of the levels of the preheaters.

4. A power plant according to claim 1 wherein said source is an industrial fluid.

5. A power plant according to claim 1 wherein said source is industrial waste heat fluid.

6. A method for operating a plurality of independent, closed cycle power plant modules, each having a vaporizer and a preheater, said method comprising the steps of:

(a) arranging the modules into a plurality of levels, each level comprising a plurality of modules;

(b) applying a medium or low temperature source fluid in parallel to each vaporizer in a level to produce heat depleted source fluid;

(c) applying heat depleted source fluid from an upper level to each vaporizer in parallel in the succeeding lower level; and

(d) applying heat depleted fluid from the lowest level to all of the preheaters in parallel.

7. A method according to claim 6 including the step of arranging the modules into a plurality of levels, and applying the heat depleted source fluid to all of the preheaters in parallel independently of the levels of the preheaters.

8. A method according to claim 6 including the step of applying the heat depleted source fluid to all of the preheaters in parallel independently of the levels of the preheaters.

9. A method according to claim 6 wherein the source fluid is an industrial fluid.

10. A method according to claim 6 wherein the source fluid is industrial waste heat.