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US3576178A Expired / Lapsed US ⏱️ 0.0 years remaining

Shell-and-tube steam generator with economizer

Assignee: Combustion Engineering Inc
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Filing: 1969-12-24
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Granted: 1971-04-27
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Expires: 1989-12-24
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Abstract

Abstract A shell and tube vapor-generator is provided in which vaporizable liquid is transformed into vapor by passing it in heat transfer relation with heating fluid conducted through the tubes and a method for operating the same. The vaporizable liquid is preheated to about saturation temperature before being passed to the vapor-generating section of the unit. At full load operation the liquid is preheated by passing it in indirect heat transfer relation with the heating fluid conducted through the tubes. At low load operation it is preheated by condensing a portion of the vapor produced in the vapor-generating section and at intermediate loads preheating is accomplished by a combination of the two.

Inventors

  • 👤 Paul C Zmola

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 16:22
CPC Classifications
F; F22; F22B; F22B1/00; F22B1/02; F22B1/023; F22B1/026; F22B35/00; F22B35/004

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 165 words
The method of operating a vapor generator including a vessel containing a bundle of heat exchange tubes having an evaporator portion comprising the steps of: a. passing a heating fluid through said tubes; b. supplying a vaporizable liquid to said vessel for circulation through said evaporator portion; c. preheating said vaporizable liquid prior to admitting it to said evaporator portion; i. when the inlet temperature of said liquid is high, by passing it in indirect heat exchange relation with said heating fluid, ii. when the inlet temperature of said liquid is relatively low, by passing it in direct contact with vapor from said evaporator portion, and iii. when the inlet temperature of said liquid is intermediate said high and low temperatures, by passing part of said liquid in indirect heat transfer relation with said heating fluid and part in direct contact with vapor from said evaporator portion; and d. vaporizing the preheated liquid by directing it in relation to the tubes in said evaporator portion.
Claim 2
Independent Claim 165 words
The method of operating a vapor generator including a vessel containing a bundle of heat exchange tubes having an evaporator portion comprising the steps of: a. passing a heating fluid through said tubes; b. supplying a vaporizable liquid to said vessel for circulation through said evaporator portion; c. preheating said vaporizable liquid prior to admitting it to said evaporator portion; i. when the inlet temperature of said liquid is high, by passing it in indirect heat exchange relation with said heating fluid, ii. when the inlet temperature of said liquid is relatively low, by passing it in direct contact with vapor from said evaporator portion, and iii. when the inlet temperature of said liquid is intermediate said high and low temperatures, by passing part of said liquid in indirect heat transfer relation with said heating fluid and part in direct contact with vapor from said evaporator portion; and d. vaporizing the preheated liquid by directing it in relation to the tubes in said evaporator portion.
Claim 3
Dependent Claim 37 words
The method of operating a vapor generator as recited in claim 1 wherein proportionately greater amounts of vaporizable liquid are preheated by heat transfer from said heating fluid as the inlet temperature of the liquid is increased.
Claim 4
Dependent Claim 46 words
The method of operating a vapor generator as recited in claim 2 in which the amount of vaporizable liquid passed in heat exchange relation with said vapor is decreased as the amount of vaporizable liquid passed in heat exchange relation with said heating fluid is increased.
Claim 5
Dependent Claim 60 words
The method of operating a vapor generator as recited in claim 1 wherein all of the vaporizable liquid is preheated by heat transfer from said vapor at liquid inlet temperatures of up to about 300* F., and all of said vaporizable liquid is preheated by heat transfer from said heating fluid at liquid temperatures of about 400* F. or higher.
Claim 6
Independent Claim 165 words
The method of operating a vapor generator including a vessel containing a bundle of heat exchange tubes having an evaporator portion comprising the steps of: a. passing a heating fluid through said tubes; b. supplying a vaporizable liquid to said vessel for circulation through said evaporator portion; c. preheating said vaporizable liquid prior to admitting it to said evaporator portion: i. when the load on the vapor generator is high, by passing it in indirect heat exchange relation with said heating fluid; ii. when the load on the vapor generator is relatively low, by passing it in direct contact with vapor from said evaporator portion; and iii. when the load on the vapor generator is intermediate said high and low loads, by passing part of said liquid in indirect heat transfer relation with said heAting fluid and part in direct contact with vapor from said evaporator portion; and d. vaporizing the preheated liquid by directing it in relation to the tubes in said evaporator portion.
Claim 7
Independent Claim 165 words
The method of operating a vapor generator including a vessel containing a bundle of heat exchange tubes having an evaporator portion comprising the steps of: a. passing a heating fluid through said tubes; b. supplying a vaporizable liquid to said vessel for circulation through said evaporator portion; c. preheating said vaporizable liquid prior to admitting it to said evaporator portion: i. when the load on the vapor generator is high, by passing it in indirect heat exchange relation with said heating fluid; ii. when the load on the vapor generator is relatively low, by passing it in direct contact with vapor from said evaporator portion; and iii. when the load on the vapor generator is intermediate said high and low loads, by passing part of said liquid in indirect heat transfer relation with said heAting fluid and part in direct contact with vapor from said evaporator portion; and d. vaporizing the preheated liquid by directing it in relation to the tubes in said evaporator portion.
Claim 8
Dependent Claim 36 words
The method of operating a vapor generator as recited in claim 5 wherein proportionately greater amounts of vaporizable liquid are preheated by transfer from said heating fluid as the inlet temperature of the liquid is increased.
Claim 9
Dependent Claim 46 words
The method of operating a vapor generator as recited in claim 6 in which the amount of vaporizable liquid passed in heat exchange relation with said vapor is decreased as the amount of vaporizable liquid passed in heat exchange relation with said heating fluid is increased.
Claim 10
Dependent Claim 61 words
The method of operating a vapor generator as recited in claim 5 wherein all of the vaporizable liquid is preheated by heat transfer from said vapor at liquid inlet temperatures of up to about 300* F., and all of said vaporizable liquid is preheated by heat transfer from said heating fluid at liquid inlet temperatures of about 440* F., or higher.
Claim 11
Dependent Claim 34 words
The method of operating a vapor generator as recited in claim 5 further including the step of superheating that part of the vapor from the evaporator portion that does not preheat the vaporizable liquid.
Claim 12
Dependent Claim 179 words
A vapor generator comprising: a. a vertically elongated pressure vessel; b. axially spaced tube sheets dividing the vessel into heating fluid inlet and outlet chamber and a vapor-generating chamber therebetween; c. a bundle of tubes extending through said vapor-generating chamber and having their ends communicating with said heating fluid inlet and outlet chambers for circulation of heating fluid through said tubes; d. means within said vapor-generating chamber defining an evaporator section and a preheat section; e. baffle means surrounding said tube bundle in concentrically spaced relation from the wall of said vessel to form an annular passage therebetween; said flow passage being in fluid communication with said evaporator section at the lower end thereof; f. means for admitting a portion of the vapor generated in said evaporator section to said annular flow passage; g. means for supplying vaporizable liquid to said vapor generator including: i. first supply for passing said liquid to said annular flow passage into heat exchange relation with the vapor present therein; and ii. second supply means for passing said liquid directly to said preheat section.
Claim 13
Dependent Claim 179 words
A vapor generator comprising: a. a vertically elongated pressure vessel; b. axially spaced tube sheets dividing the vessel into heating fluid inlet and outlet chamber and a vapor-generating chamber therebetween; c. a bundle of tubes extending through said vapor-generating chamber and having their ends communicating with said heating fluid inlet and outlet chambers for circulation of heating fluid through said tubes; d. means within said vapor-generating chamber defining an evaporator section and a preheat section; e. baffle means surrounding said tube bundle in concentrically spaced relation from the wall of said vessel to form an annular passage therebetween; said flow passage being in fluid communication with said evaporator section at the lower end thereof; f. means for admitting a portion of the vapor generated in said evaporator section to said annular flow passage; g. means for supplying vaporizable liquid to said vapor generator including: i. first supply for passing said liquid to said annular flow passage into heat exchange relation with the vapor present therein; and ii. second supply means for passing said liquid directly to said preheat section.
Claim 14
Dependent Claim 64 words
A vapor generator as recited in claim 10 wherein said baffle means is in open fluid communication with said evaporator section at the top and bottom ends thereof and the opening at the top of the said baffle means is effective to admit vapor from said evaporator section to said flow passage while that at the bottom admits heated liquid to said evaporator section.
Claim 15
Dependent Claim 22 words
A vapor generator as recited in claim 11 wherein said liquid is heated to substantially its saturation temperature in said flow passage.
Claim 16
Dependent Claim 37 words
A vapor generator as recited in claim 10 including control means for regulating the supply of vaporizable liquid through said first and second supply means in response to changes in the temperature of the liquid being passed.
Claim 17
Dependent Claim 36 words
A vapor generator as recited in claim 10 including control means for regulating the supply of vaporizable liquid through said first and second supply means in response to changes in load on said vapor generator. amounts
Claim 18
Dependent Claim 85 words
A vapor generator as recited in claim 14 wherein said control means includes means for passing all of the liquid supplied to said vapor generator through said first supply means during low load operation of said vapor generator, means for passing all of the liquid supplied to said vapor generator through said first supply means during high load operation of said vapor generator, and means for passing liquid through both of said supply means in controlled amounts during intermediate load operation of said vapor generator.
Claim 19
Dependent Claim 27 words
A vaPor generator as recited in claim 11 wherein said preheat section includes means for directing the flowing liquid in crossflow relation to the tubes extending therethrough.
Claim 20
Dependent Claim 41 words
A vapor generator as recited in claim 16 including means defining a superheat section in said vapor-generating chamber disposed above said evaporator section and said means including means for directing the flowing fluid in crossflow relation to the tubes extending therethrough.

References Cited (Backward Citations)

US3147743A Cited
US3385268A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-04-26 1974-10-26 1975-04-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-04-26 1978-10-26 1979-04-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-04-26 1982-10-26 1983-04-27 $7700.00 Window Closed / Lapsed

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