Moisture separator reheater with thermodynamically enhanced means for substantially eliminating condensate subcooling

Claim 3

The method of claim 1 wherein the ratio of pressure of exhausted scavenging steam from said second reheater to the pressure of exhausted scavenging steam from said first reheater is at least 1.5:1.

Claim 4

In a moisture separator reheater having a vapor-tight shell, means for passing cool wet shellside steam therethrough, means within said shell for removing entrained moisture from said shellside steam, and first and second reheaters therein for raising the temperature of said dried shellside steam, said reheaters each being comprised of an inlet header, an outlet header, and a plurality of substantially parallel heat exchange tubes comprising a tube bundle connected therebetween and extending along said shell longitudinally and in heat-transfer relationship with said shellside steam and wherein said first reheater is supplied with saturated tubeside steam at a temperature and pressure less than the temperature and pressure at which saturated tubeside steam is supplied to said second reheater, the improvement comprising: means for providing an additional flow of steam to the inlet header of said first reheater sufficient to substantially eliminate condensate subcooling within said tubes, said means comprising a high differential pressure thermocompressor; means for supplying exhausted steam from said first reheater to a low-pressure input of said thermocompressor; means for supplying exhausted steam from said second reheater to a high-pressure input of said thermocompressor; and means for supplying the output of said thermocompressor to the inlet header of said first reheater.

Claim 5

In a moisture separator reheater having a vapor-tight shell, means for passing cool wet shellside steam therethrough, means within said shell for removing entrained moisture from said shellside steam, and first and second reheaters therein for raising the temperature of said dried shellside steam, said reheaters each being comprised of an inlet header, an outlet header, and a plurality of substantially parallel heat exchange tubes comprising a tube bundle connected therebetween and extending along said shell longitudinally and in heat-transfer relationship with said shellside steam and wherein said first reheater is supplied with saturated tubeside steam at a temperature and pressure less than the temperature and pressure at which saturated tubeside steam is supplied to said second reheater, the improvement comprising: means for providing an additional flow of steam to the inlet header of said first reheater sufficient to substantially eliminate condensate subcooling within said tubes, said means comprising a high differential pressure thermocompressor; means for supplying exhausted steam from said first reheater to a low-pressure input of said thermocompressor; means for supplying exhausted steam from said second reheater to a high-pressure input of said thermocompressor; and means for supplying the output of said thermocompressor to the inlet header of said first reheater.

Claim 6

The apparatus of claim 3 wherein said thermocompressor operates with a pressure ratio of high-pressure steam to low-pressure steam which is at least 1.5:1.

Claim 7

The apparatus of claim 3 wherein the steam taken from the exhaust header of said second reheater constitutes approximately 2 to 10 percent of the total inlet steam to the inlet header of said second stage reheater.

Claim 8

The apparatus of claim 3 wherein steam flow into the inlet ends of respective tubes in at least said second stage tube bundle is partially restricted to provide a greater flow of saturated steam into the tubes thereof which are subject to greater heat-transfer loading than other tubes of said bundle.

Claim 9

The apparatus of claim 3 wherein said individual heat-transfer tubes in said tube bundles 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 10

The apparatus of claim 3 wherein said individual heat-transfer tubes in said tube bundles are disposed in a substantially horizontal plane and said inlet and outlet headers comprise separate chambers of a unitary header structure.

Claim 11

A moisture separator reheater adapted to receive relatively wet, low-temperature inlet steam at an inlet thereof and for drying and reheating said inlet steam to produce dry hot outlet steam and comprising: (a) pressure-tight shell; (b) at least one steam inlet means located along one surface of said shell; (c) at least one steam outlet means located along another surface of said shell; (d) means adjacent said inlet for removing entrained moisture from inlet steam; (e) a first tube bundle heat exchanger located longitudinally within said shell and disposed between said inlet and outlet and in heat-exchange relationship with steam passing between said inlet and outlet; (f) a second tube bundle located longitudinally within said shell interposed between said first tube bundle and said steam outlet means and in heat-exchange relationship with steam passing between said inlet and outlet; (g) a first header extending along a first end of said first stage tube bundle and receiving in pressure-sealed relationship the ends of said tubes comprising said first stage tube bundle and having therein a baffle separating said header into a plurality of chambers including an inlet one of which is open to one end of said tubes and an exhaust one of which is open to the remaining end of said tubes; (h) a second header extending along a first end of said second tube bundle and receiving in pressure-sealing relationship the ends of said tubes comprising said second tube bundle and having therein a baffle separating said header into a plurality of chambers including an inlet chamber which is open to one end of each of said tubes and an exhaust chamber which is open to the other end of each of said tubes; (i) means for directing relatively cool moist steam into said shell through said steam inlet in said shell to allow the same to pass in heat-exchange relationship with said first and said second tube bundles and emerge from said steam outlet on said other surface of said shell as hot dry steam; (j) means for supplying a first flow of saturated high-pressure tubeside steam at a first high pressure and substantially above the temperature of shellside steam entering said shell inlet to the inlet chamber of said first header; (k) means for supplying a second flow of saturated high-pressure tubeside steam at a second high pressure substantially above the pressure of said first flow of tubeside steam to the inlet chamber of said second header; (l) pumping means operative to recirculate steam from the exhaust chamber of said first header to the inlet chamber thereof, adapted to receive motive steam from the exhaust chamber of said second header, to isentropically expand the same and to entrain steam from said first header exhaust chamber therein to provide a second steam input to the inlet chamber of said first header, both of said inputs to said first header input chamber being saturated or slightly superheated steam; (m) said second steam input from said pumping means to said inlet chamber of said first header being of sufficient mass flow rate to substantially eliminate condensate subcooling within the tubes of said first tube bundle.

Claim 12

A moisture separator reheater adapted to receive relatively wet, low-temperature inlet steam at an inlet thereof and for drying and reheating said inlet steam to produce dry hot outlet steam and comprising: (a) pressure-tight shell; (b) at least one steam inlet means located along one surface of said shell; (c) at least one steam outlet means located along another surface of said shell; (d) means adjacent said inlet for removing entrained moisture from inlet steam; (e) a first tube bundle heat exchanger located longitudinally within said shell and disposed between said inlet and outlet and in heat-exchange relationship with steam passing between said inlet and outlet; (f) a second tube bundle located longitudinally within said shell interposed between said first tube bundle and said steam outlet means and in heat-exchange relationship with steam passing between said inlet and outlet; (g) a first header extending along a first end of said first stage tube bundle and receiving in pressure-sealed relationship the ends of said tubes comprising said first stage tube bundle and having therein a baffle separating said header into a plurality of chambers including an inlet one of which is open to one end of said tubes and an exhaust one of which is open to the remaining end of said tubes; (h) a second header extending along a first end of said second tube bundle and receiving in pressure-sealing relationship the ends of said tubes comprising said second tube bundle and having therein a baffle separating said header into a plurality of chambers including an inlet chamber which is open to one end of each of said tubes and an exhaust chamber which is open to the other end of each of said tubes; (i) means for directing relatively cool moist steam into said shell through said steam inlet in said shell to allow the same to pass in heat-exchange relationship with said first and said second tube bundles and emerge from said steam outlet on said other surface of said shell as hot dry steam; (j) means for supplying a first flow of saturated high-pressure tubeside steam at a first high pressure and substantially above the temperature of shellside steam entering said shell inlet to the inlet chamber of said first header; (k) means for supplying a second flow of saturated high-pressure tubeside steam at a second high pressure substantially above the pressure of said first flow of tubeside steam to the inlet chamber of said second header; (l) pumping means operative to recirculate steam from the exhaust chamber of said first header to the inlet chamber thereof, adapted to receive motive steam from the exhaust chamber of said second header, to isentropically expand the same and to entrain steam from said first header exhaust chamber therein to provide a second steam input to the inlet chamber of said first header, both of said inputs to said first header input chamber being saturated or slightly superheated steam; (m) said second steam input from said pumping means to said inlet chamber of said first header being of sufficient mass flow rate to substantially eliminate condensate subcooling within the tubes of said first tube bundle.

Claim 13

The apparatus of claim 1 wherein the steam taken from the exhaust chamber of the second header constitutes approximately 2 to 10 percent of the total inlet steam to the inlet chamber of said second stage tube bundle.

Claim 14

The apparatus of claim 9 wherein tubeside steam flow into certain of the tubes of at least said second stage tube bundle is restricted to allow greater saturated steam flow to enter the inlet ends of U tubes of at least said second stage tube bundle which are subjected to greater heat transfer loading than other tubes of said tube bundle.

Claim 15

The apparatus of claim 9 wherein said individual U tubes in said tube bundles are oriented in a substantially vertical plane and said baffles in said headers divide said headers into upper and lower chambers.

Claim 16

The apparatus of claim 9 wherein said individual U tubes in said tube bundles are disposed in a substantially horizontal plane and said baffles in said headers are disposed in a substantially vertical plane to separate said header into side-by-side sections.

Claim 17

The apparatus of claim 9 wherein said pumping means is a thermocompressor requiring a high differential in pressure between motive fluid and suction fluid for its operation having no moving parts and which operates to combine a high-pressure flow of motive steam with a relatively low-pressure flow of suction steam to produce an increased volume of intermediate pressure steam.

Claim 18

The apparatus of claim 14 wherein said thermocompressor operates with a pressure ratio of high-pressure fluid to low-pressure fluid of at least 1.5:1.