Heat recovery steam generator and multidrum evaporator
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
F28D-015/00
F22B-021/18
출원번호
US-0113875
(2012-04-10)
등록번호
US-9921001
(2018-03-20)
국제출원번호
PCT/US2012/032828
(2012-04-10)
§371/§102 date
20131025
(20131025)
국제공개번호
WO2012/148656
(2012-11-01)
발명자
/ 주소
Jackson, Bradley N.
출원인 / 주소
Nooter/Eriksen, Inc.
대리인 / 주소
Polster Lieder Woodruff & Lucchesi, L.C.
인용정보
피인용 횟수 :
0인용 특허 :
15
초록▼
An evaporator for a heat recovery steam generator has two horizontal steam drums of moderate size, one located slightly higher than the other. It also includes a coil having tubes located in the flow of a hot gas. The lower drum communicates with the inlets of the tubes for the coil. The outlets of
An evaporator for a heat recovery steam generator has two horizontal steam drums of moderate size, one located slightly higher than the other. It also includes a coil having tubes located in the flow of a hot gas. The lower drum communicates with the inlets of the tubes for the coil. The outlets of the tubes communicate with the upper drum. A drain line connects the bottom of the upper drum with the lower region of the lower drum, so that water will flow from the upper drum to the lower drum. Water, which is primarily in the liquid phase, enters the lower drum through an inlet line and mixes with water from the upper drum. The mixture flows through into the coil. Here some of it transforms into saturated steam while the rest remains as saturated water. The saturated steam and saturated water flow into the upper drum where the steam escapes and the water flows back into the lower drum to recirculate through the coil. Owing to their moderate sizes, the drums can withstand high pressures without having excessive wall thickness, and this enables the evaporator to be set into operation with minimal or no hold points. Yet the two drums provide a retention time—and the protection that it provides—of a single large capacity drum having substantial wall thickness.
대표청구항▼
1. A heat recovery steam generator comprising: a housing having an inlet into which a hot gas is directed and an outlet through which the gas can be discharged, configured to form an internal exhaust gas flow path within the housing so that the gas can flow through the housing from its inlet to its
1. A heat recovery steam generator comprising: a housing having an inlet into which a hot gas is directed and an outlet through which the gas can be discharged, configured to form an internal exhaust gas flow path within the housing so that the gas can flow through the housing from its inlet to its outlet;an economizer located in the housing configured such that the gas can flow through it, the economizer having a configuration for receiving liquid feedwater and for elevating the temperature of the feedwater;an evaporator configured for converting liquid water, into saturated steam, said evaporator comprising: an upper drum positioned to be external to the housing's internal exhaust gas flow path and oriented horizontally, the upper drum having at least one steam-water separation device; at least one lower drum positioned to be external to the housing's internal exhaust gas flow path and oriented horizontally and located at an elevation less than the upper drum; a drain line connecting the lower region of the upper drum to the lower drum; an inlet line opening into one of the drums; an outlet line leading out of the upper region of the upper drum; a coil having tubes located in a flow of a hot gas and provided with inlets and outlets, with the inlets of the tubes being in communication with the lower drum and the outlets of the tubes being in communication with the upper drum; the evaporator having its coil located in the housing upstream, in the flow of gas, from the economizer, with the inlet line of the evaporator being connected to the economizer to be capable of receiving from the economizer water that has undergone heating in the economizer; anda superheater located in the housing upstream from the evaporator, with the outlet line of the evaporator being connected to the superheater. 2. A heat recovery steam generator according to claim 1 wherein the tubes of the evaporator coil are in fluid flow communication with the lower drum at the bottom of the lower drum. 3. A heat recovery steam generator according to claim 2 wherein the tubes of the evaporator coil are in fluid flow communication with the upper drum at the bottom of the upper drum. 4. A heat recovery steam generator according to claim 3 wherein the evaporator tubes extend vertically and have their inlets at their lower ends connected to a distribution header, which distribution header is positioned within the internal exhaust gas flow path, and further comprising a downcomer in fluid flow connection with the lower drum and with the said distribution header. 5. A heat recovery steam generator according to claim 4 wherein the outlets of the evaporator tubes are at the upper ends of the tubes and further comprising at least one riser connecting the outlets of the tubes with the upper drum. 6. A heat recovery steam generator according to claim 3 wherein the evaporator inlet line opens into the lower drum. 7. A heat recovery steam generator according to claim 3 wherein the evaporator drain line opens into the lower region of the lower drum. 8. A heat recovery steam generator according to claim 1 wherein at least one of the evaporator drums is cylindrical. 9. A heat recovery steam generator according to claim 1 wherein the upper and lower evaporator drums are cylindrical. 10. The heat recovery steam generator of claim 1, further comprising the lower drum having a steam outlet, and the upper drum having a steam inlet, and a steam vent conduit in fluid flow connection with the lower drum steam outlet and the upper drum steam inlet. 11. The heat recovery steam generator of claim 1, further comprising the lower drum steam outlet being located at the top of the lower drum, and the upper drum steam inlet being located the upper region side of the upper drum. 12. The heat recovery steam generator of claim 1, further comprising the upper drum and lower drum each having walls, the said walls being four inches to about five inches thick. 13. The heat recovery steam generator of claim 1 wherein: the tubes of the evaporator coil are in fluid flow communication with the lower drum at the bottom of the lower drum;the tubes of the evaporator coil are in fluid flow communication with the upper drum at the bottom of the upper drum;the evaporator tubes extend vertically and have their inlets at their lower ends in fluid flow connection with a distribution header, and further comprising a downcomer in fluid flow connection with the lower drum and with the distribution header;the outlets of the evaporator tubes are at the upper ends of the tubes and further comprising at least one riser in fluid flow connection with the outlets of the evaporator tubes and with the upper drum;the evaporator inlet line opens into the lower drum, and the evaporator drain line opens into the lower region of the lower drum; andthe lower drum having a steam outlet, the upper drum having a steam inlet, and a steam vent conduit in fluid flow connection with the lower drum steam outlet and the upper drum steam inlet. 14. The heat recovery steam generator of claim 13, further comprising the upper drum and lower drum each having walls, the said walls being about four inches to five inches thick. 15. The heat recovery steam generator of claim 1 wherein the superheater is a high pressure superheater, the evaporator is a high pressure evaporator, and the economizer is a high pressure economizer. 16. A process for converting water into saturated steam in a heat recovery steam generator: said heat recovery steam generator comprising:a housing having an inlet into which a hot gas is directed and an outlet through which the gas is discharged, configured to form an internal exhaust gas flow path within the housing so that the exhaust gas can flow through the housing from its inlet to its outlet;an economizer located within the housing such that the exhaust gas flows through it, the economizer being connected to a source of feedwater for elevating the temperature of the feedwater;an evaporator for converting water, which is primarily in the liquid phase, into saturated steam, said evaporator comprising: an upper drum oriented horizontally positioned to be external to the housing's internal exhaust gas flow path and; at least one lower drum positioned to be external to the housing's internal exhaust gas flow path and oriented horizontally and located at an elevation less than the upper drum; a drain line connecting the lower region of the upper drum to the lower drum; an inlet line opening into one of the drums; an outlet line leading out of the upper region of the upper drum; a coil having tubes located in a flow of a hot gas and provided with inlets and outlets, with the inlets of the tubes being in communication with the lower drum and the outlets of the tubes being in communication with the upper drum; the evaporator having its coil located in the housing upstream, in the flow of exhaust gas, from the economizer, with the inlet line of the evaporator being connected to the economizer to receive from the economizer water that has undergone heating in the economizer; anda superheater located within the housing upstream, in the flow of the exhaust gas, from the evaporator, with the outlet line of the evaporator being connected to the superheater; andthe method comprising the steps of:introducing a flow of water from the economizer into one of two horizontal steam drums, so that the lower drum contains water that is in the liquid phase; directing water from the lower steam drum into the said evaporator coil, and heating water in the evaporator coil sufficiently to transform the water into saturated water and saturated steam;directing saturated water and steam from the evaporator coil into the upper steam drum;directing saturated water in the upper steam drum into the lower steam drum; andwithdrawing the saturated steam from the upper steam drum. 17. The process according to claim 16 wherein in the step of withdrawing the saturated steam from the upper steam drum the saturated steam flows from the upper steam drum into the superheater. 18. The process according to claim 16 wherein the steam drums are cylindrical and have longitudinal axes that are horizontal. 19. The process according to claim 18 wherein the steam drums are cylindrical. 20. The process of claim 16 wherein the lower drum has a steam outlet, and the upper drum has a steam inlet, further comprising the step of steam flowing from the lower drum steam outlet into the upper drum steam inlet. 21. The process of claim 20 wherein in the step of steam flowing from the lower drum steam outlet into the upper drum steam inlet, the steam flows out of the top of the lower steam drum and flows into the upper region side of the upper drum.
Csathy Denis G. (Minneapolis MN) Hung Wendell L. Y. (Minneapolis MN), Waste heat boiler for abstraction of heat energy from gaseous effluent containing corrosive chemical contaminants.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.