Method and apparatus for thermal power generation

• US 4,164,849 A
• Filed: 09/30/1976
• Issued: 08/21/1979
• Est. Priority Date: 09/30/1976
• Status: Expired due to Term

• Current Assignee: United States Department of Energy (Government of the United States of America)
• Original Assignee: United States Department of Energy (Government of the United States of America)
• Inventors: Mangus, James D.
• Primary Examiner(s): Ostrager, Allen M.
• Application Number:
  US04/728,478
• Time in Patent Office: 1,055 Days
• Field of Search: 60/644, 60/653, 60/679, 60/680, 122/483
• US Class Current: 60/679
• CPC Class Codes: F01K 3/181 using nuclear heat F01K3/26 takes precedence
• CPC Class Codes: F01K 3/262 by means of heat exchangers
• CPC Class Codes: G21D 5/14 and also superheated by reactor coolant
• CPC Class Codes: Y02E 30/00 Energy generation of nuclear origin

Abstract

A method and apparatus for power generation from a recirculating superheat-reheat circuit with multiple expansion stages which alleviates complex control systems and minimizes thermal cycling of system components, particularly the reheater. The invention includes preheating cold reheat fluid from the first expansion stage prior to its entering the reheater with fluid from the evaporator or drum component.

Claims

1. Apparatus for thermal power generation comprising:

a. a circulating vaporizable utilization fluid,

b. an evaporator wherein said fluid is vaporized,

c. a drum wherein liquid is separated from said vaporized fluid so as to form a liquified portion and a saturated vapor portion,

d. a superheater wherein said vapor portion is superheated,

e. a first expansion means wherein said superheated fluid is expanded,

f. heat exchange means wherein said expanded fluid is in heat exchange relation with fluid from one of said evaporator, said drum, and said superheater, and is preheated, subsequent to said expansion,

g. a reheater wherein said preheated fluid is resuperheated,

h. at least one second expansion means wherein said resuperheated fluid is expanded,

i. a condenser wherein said last-named fluid is condensed, and

j. means to combine liquid from said liquified portion and said condensed fluid prior to entry into said evaporator.

2. The apparatus of claim 1 wherein said heat exchange means comprises tubing through said drum whereby said expanded fluid is passed through the interior of said tubes in heat exchange relation with fluid contained within said drum.

3. The apparatus of claim 1 wherein said heat exchange means comprises a tube and shell heat exchanger whereby said expanded fluid is passed through the interior of said tubes and said first portion is passed along the exterior of said tubes prior to entry into said superheater.

4. The apparatus of claim 1 wherein said heat exchange means comprises a steam ejector whereby a portion of the superheated fluid discharged from said superheater is mixed with said expanded fluid prior to entry into said reheater.

5. An improved apparatus for thermal power generation of the type wherein a vaporizable fluid is circulated through a superheat-reheat thermal cycle such that said fluid serially flows through an evaporator, drum, superheater, a first turbine, a reheater, and a second turbine, liquid in said vaporizable fluid upon discharge of said fluid from said evaporator being separated in said drum so as to form a liquified portion and a saturated vapor portion, wherein the improvement comprises:

heat exchange means placing in heat transfer relation fluid discharged from said first turbine and said liquified and vapor portions within said drum, prior to said fluid discharged from said first turbine entering said reheater,

means to direct fluid from said first turbine to said heat exchange means, and

means to direct fluid from said heat exchange means to said reheater.

6. A thermal power plant comprising a first circuit circulating a coolant between a heat source and a steam generation system and a utilization circuit circulating a vaporizable fluid between said steam generation system and expansion means, said steam generation system comprising an evaporator, superheater, and reheater, said utilization circuit comprising a drum and heat exchange means, said vaporizable fluid having liquid separated therefrom in said drum, said expansion means comprising a first turbine and a second turbine, said heat exchange means placing in heat transfer relation fluid from said first turbine and fluid from one of said evaporator and drum, and conduits flow connecting said steam generation system and said utilization circuit in a manner such that said coolant passes in parallel through said superheater and said reheater and then collectively through said evaporator, and the main stream of said vaporizable fluid passes serially through said evaporator, said drum, said superheater, said first turbine, said heat exchange means, said reheater, and said second turbine.

7. The plant of claim 6 wherein said heat exchange means places in heat transfer relation fluid discharged from said evaporator, such that said main steam passes serially through said evaporator, said heat exchange means, said drum, said superheater, said first turbine, said heat exchange means, said reheater, and said second turbine.

8. The plant of claim 6 wherein said first circuit comprises a primary circuit circulating a first coolant in heat exchange relation with an intermediate circuit circulating an intermediate coolant, said intermediate coolant being in heat exchange relation with said steam generation system.

9. The plant of claim 8 wherein said first coolant comprises a liquid metal, said intermediate coolant comprises a liquid metal, and said vaporizable fluid comprises water.

10. Apparatus for thermal power generation comprising:

a. a circulating vaporizable utilization fluid,

b. an evaporator wherein said fluid is vaporized,

c. a drum wherein liquid is separated from said vaporized fluid so as to form a liquified portion and a saturated vapor,

d. a superheater wherein said saturated vapor is superheated,

e. a first expansion means wherein said superheated fluid is expanded,

f. heat exchange means wherein said expanded fluid is in heat exchange relation with fluid from one of said evaporator, said drum, and said superheater, and is preheated, subsequent to said expansion,

g. a reheater wherein said preheated fluid is resuperheated, and

h. at least one second expansion means wherein said resuperheated fluid is expanded.

11. A method of thermal power generation utilizing a vaporizable fluid comprising the steps of:

a. passing said fluid through an evaporator wherein said fluid is vaporized,

b. passing said vaporized fluid through a drum such that liquid is separated from said vaporized fluid so as to form a liquified portion and a saturated vapor subsequent to vaporization in said evaporator,

c. pasing said saturated vapor through a superheater wherein said saturated vapor is superheated,

d. passing said superheated fluid through a first expansion means wherein said superheated fluid is expanded,

e. passing said expanded fluid through a heat exchange means such that said expanded fluid is in heat exchange relation with fluid from one of said evaporator, said drum, and said superheater, and is preheated,

f. passing said preheated fluid through a reheater such that said preheated fluid is resuperheated, and

g. passing said resuperheated fluid through at least one second expansion means such that said resuperheated fluid is expanded.