Controllable inlet header partitioning

Claim 2

In a tube and shell reheater having a vapor-tight shell, inlet means for passing cool wet shellside steam thereinto, means within said shell for removing entrained moisture from said shellside steam, and outlet means for removing reheated shellside steam therefrom, at least one reheater therein for raising the temperature of said dried shellside steam, said reheater comprised of an inlet header, including a tubesheet, an outlet header, and a plurality of substantially parallel heat-exchange tubes comprising a tube bundle connected therebetween and extending within said shell between said inlet and said outlet means and in heat-transfer relationship with said shellside steam, the improvement comprising: first means supplying said inlet header with a supply of saturated steam at a temperature and at a pressure both of which are higher than the corresponding characteristic of shellside steam passed into said shell for reheating; partition means within said inlet header for creating therein an auxiliary inlet header which is coupled with and covers inlet ends of a preselected group of said tubes at said tubesheet; separate means for supplying a controllable supply of saturated steam at essentially the same temperature and pressure as said first steam supply means to said auxiliary inlet header; variable flow control means associated with said second steam supply means for controlling the flow rate of saturated steam into said auxiliary header and for independently controlling steam flow rates in said preselected group of tubes; said flow control means being responsive to the loading of said reheater and effective to maintain flow rates in all of said tubes sufficient to substantially eliminate condensate subcooling therein at all values of reheater loading without requiring excessive scavenging steam flow rates in any of said tubes.

Claim 3

The apparatus of claim 1 wherein said auxiliary header comprises a flanged cylindrical segment, and is suitably attached to said tubesheet inlet face to avoid loss of active tubes.

Claim 4

The apparatus of claim 1 wherein said auxiliary header consists of a baffle plate attached to the header inner wall at one end and to the face of said tubesheet at the other end and extends the length of said inlet header.

Claim 5

The apparatus of claim 1 wherein said auxiliary header partition is perforated.

Claim 6

The apparatus of claim 1 wherein said inlet header partitioning represents multiple partitions, with multiple steam supply means and control means therefor.

Claim 7

The apparatus of claim 1 wherein said inlet ends of said tubes are differentially orificed to distribute steam flow from tube to tube based on heat transfer demand.

Claim 8

The apparatus of claim 1 wherein said individual heat transfer tubes in said tube bundle are U-tubes and are oriented in a substantially vertical plane and said inlet and outlet headers comprise separate chambers of a unitary header structure.

Claim 9

The apparatus of claim 1 wherein said individual heat transfer tubes in said tube bundle are U-tubes and are oriented in a substantially horizontal plane and said inlet and outlet headers comprise separate chambers of a unitary header structure.

Claim 10

A moisture separator reheater for demoisturizing and superheating exhaust steam from an early stage of a nuclear steam turbine-generator and comprising: (a) a vapor-tight shell; (b) inlet means for passing wet cool shellside steam exhausted from said early turbine stage into said shell; (c) outlet means for removing dry superheated steam from said shell; (d) moisture separator means adjacent said steam inlet means for removing essentially all entrained moisture from said inlet shellside steam; (e) at least one reheater within said shell between said moisture separator means and said steam outlet means for superheating said dried inlet steam and comprising an inlet header with a tubesheet an outlet header with a tubesheet and a plurality of heat-exchange tubes for passing hot saturated tubeside steam in heat-exchange relationship with said shellside steam; (f) partition means within said inlet header for forming an auxiliary inlet header within said inlet header adjacent said inlet header tubesheet and coupled with a preselected number of inlet apertures for said heat-exchange tubes at said tubesheet; (g) first means for supplying from a source associated with said early turbine stage a first flow of saturated steam at a temperature and pressure higher than those characteristics of said inlet shellside steam to the main body of said inlet header; (h) second means branching from said first supply means for supplying from said source, a second flow of saturated steam at essentially the same temperature and pressure as said first flow to said auxiliary inlet header; (i) means responsive to turbine loading to control the flow rate of said second flow of saturated steam to said auxiliary inlet header to control steam flow rates in said preselected tubes as a function of turbine loading and to maintain flow rates in all of said tubes sufficient to substantially eliminated condensate subcooling therein at all values of turbine loading without requiring excessive scavenging steam flow rates in any of said tubes.

Claim 11

A moisture separator reheater for demoisturizing and superheating exhaust steam from an early stage of a nuclear steam turbine-generator and comprising: (a) a vapor-tight shell; (b) inlet means for passing wet cool shellside steam exhausted from said early turbine stage into said shell; (c) outlet means for removing dry superheated steam from said shell; (d) moisture separator means adjacent said steam inlet means for removing essentially all entrained moisture from said inlet shellside steam; (e) at least one reheater within said shell between said moisture separator means and said steam outlet means for superheating said dried inlet steam and comprising an inlet header with a tubesheet an outlet header with a tubesheet and a plurality of heat-exchange tubes for passing hot saturated tubeside steam in heat-exchange relationship with said shellside steam; (f) partition means within said inlet header for forming an auxiliary inlet header within said inlet header adjacent said inlet header tubesheet and coupled with a preselected number of inlet apertures for said heat-exchange tubes at said tubesheet; (g) first means for supplying from a source associated with said early turbine stage a first flow of saturated steam at a temperature and pressure higher than those characteristics of said inlet shellside steam to the main body of said inlet header; (h) second means branching from said first supply means for supplying from said source, a second flow of saturated steam at essentially the same temperature and pressure as said first flow to said auxiliary inlet header; (i) means responsive to turbine loading to control the flow rate of said second flow of saturated steam to said auxiliary inlet header to control steam flow rates in said preselected tubes as a function of turbine loading and to maintain flow rates in all of said tubes sufficient to substantially eliminated condensate subcooling therein at all values of turbine loading without requiring excessive scavenging steam flow rates in any of said tubes.

Claim 12

The apparatus of claim 9 wherein said auxiliary header comprises a flanged cylindrical member, suitably attached to said tubesheet inlet face to avoid loss of active tubes.

Claim 13

The apparatus of claim 9 wherein said auxiliary header consists of a baffle plate attached to the header inner wall at one end and to the face of said tubesheet at the other end along the length thereof.

Claim 14

The apparatus of claim 9 wherein said auxiliary header partition is perforated.

Claim 15

The apparatus of claim 9 wherein said inlet header partitioning represents multiple partitions, with multiple steam supply means and control means therefor.

Claim 16

The apparatus of claim 9 wherein said inlet ends of said tubes are differentially orificed to distribute steam flow from tube to tube based on heat-transfer demand.

Claim 17

The apparatus of claim 9 wherein said individual heat-transfer tubes in said tube bundle are U-tubes and are oriented in a substantially vertical plane and said inlet and outlet headers comprise separate chambers of a unitary header structure.

Claim 18

The apparatus of claim 9 wherein said individual heat-transfer tubes in said tube bundle are U-tubes and are oriented in a substantially horizontal plane and said inlet and outlet headers comprise separate chambers of a unitary header structure.