US3194216A - Method and apparatus for preboiler cleanup of a once-through steam generator - Google Patents

Method and apparatus for preboiler cleanup of a once-through steam generator Download PDF

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US3194216A
US3194216A US267515A US26751563A US3194216A US 3194216 A US3194216 A US 3194216A US 267515 A US267515 A US 267515A US 26751563 A US26751563 A US 26751563A US 3194216 A US3194216 A US 3194216A
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feedwater
line
outlet
shutoff valve
inlet
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Hilary A Grabowski
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Combustion Engineering Inc
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Priority to US267515A priority Critical patent/US3194216A/en
Priority to GB940864A priority patent/GB1044053A/en
Priority to ES0297748A priority patent/ES297748A1/en
Priority to CH352864A priority patent/CH459263A/en
Priority to BE645379D priority patent/BE645379A/xx
Priority to NL6402944A priority patent/NL6402944A/xx
Priority to FR968174A priority patent/FR1390595A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G9/00Cleaning by flushing or washing, e.g. with chemical solvents

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  • broken line represents a furnace and its associated gas pass, through which hot combustion gases flow.
  • Fuel and air are supplied to the furnace by Way of burner 11, which fuel is burned in the furnace 10 to thereby generate the hot combustion gases.
  • a fluid circuit Contained within the furnace and its associated rear gas pass is a fluid circuit comprised of economizer 12, furnace wall steam generating tubes 14, superheater 18, and reheater 28.
  • Numeral 16 designates a boiler throttle valve arrangement which is used during startup and other critical times.
  • the feedwater. system is made up of feedwater line 60 the inlet of which is supplied with water from the condenser 32 and the outlet of which is connected to the economizer 12. Positioned within this feedwater line 6i) is a condensate pump 34, filter and demineralizer 36,
  • the low pressure feedwater heater is made up of two heaters 38 and 40 which are in parallel flow relationship with one another.
  • the branched lines leading to the heaters 33 and 40 contain shutoff valves 42 and 44 respectively.
  • the high pressure feedwater heater is made up of two feedwater heaters and 52 which are also in parallel.
  • the branched lines leading to these two heaters contain shutoff valves54 and 56 respectively. The purpose of these parallel heaters and the shutoff valves in such parallel lines will be described more fully at a later time.
  • a bypass line 64 extends from the outlet of feedwater line 60 to the hotwell 33 and contains a shutoff valve 66. Bypass line 64 is connected to the feedwater line outlet upstream of the feedwater shutoif valve 62.
  • feedwater shutoff valve 62 When it is desired to clean or flush out the fluid circuit associated with the once-through steam generator, feedwater shutoff valve 62 is closed, and the valve 66 in the bypass line 64 is opened.
  • Feedwater pump 48 is started up, thus forcing water through the feedwater system and the bypass line 64.
  • the fluid is allowed to continue to circulate through this circuit until a predetermined degree of purity of the water is sensed by any wellknown chemical analyzer, 58, which is shown positioned within the feedwater line 60 downstream of the high pressure feedwater heaters.
  • any deposits of foreign material which may have formed, or had become trapped within the feedwater heater sections will be flushed out, and removed from the water as it passes through the filter and demineralizer 36.
  • Device 36 removesboth the soluble and insoluble impurities from the water.
  • the amount of power required to drive the feedwater pump 48 during full load operation is quite large, and it is not economical to drive the pump at this high rating during the cleanup operation.
  • the turbine 70 is thus operated during the startup cycle such that it will drive the feedwater pump 48 at only a minor percentage of creased flow therethrough during the cleanup cycle.
  • the rate at which it is driven during full load operation for example 15% of full load operation.
  • the temperature of the Water being circulated is heated in the de-aerator to a temperature of approximately 230 F. during the preboiler cleanup cycle.
  • the high and low pressure feedwater heaters have been constructed of parallel heaters in order to enable an in- Thus if shutoif valve 42 is closed during a portion of the cleanup cycle, and all of the fluid is allowed to flow through heater 4%, the flow rate therethrough will be twice as large as it would have been if the flow had been allowed to pass through both of the parallel heaters. The same is true of the high pressure heaters 5t and 52..
  • valves 42 and 54 would be closed, forcing the entire flow to pass through the low pressure heater 4t) and the high pressure heater 52.
  • analyzer 533 senses a predetermined degree of cleanliness of the water
  • valves 42 and 54 can be opened, and valves 44 and 56 closed.
  • the cycle is then repeated until the other two heaters 38 and 50 are cleaned out and analyzer 58 again senses a predetermined degree of purity.
  • the water should be cleaned to a high degree of purity, for example 20 parts per billion of foreign material.
  • shutoff valve 66 in the bypass line 6 5 is closed, and the feedwater valve 62 is opened.
  • the heat exchange members positioned Within the furnace and its associated gas pass can thereafter be cleaned.
  • the feedwater heaters can contain more than two sections in parallel. For example, if three were in parallel, and two of them were shut-01f, the flow rate through the remaining one would be three times greater than would be the case if all of them were open to flow.
  • bypass line 64 By providing the steam generator with bypass line 64, it is possible to first clean the feedwater system removing the impurities from the elements within this system, and thereafter cleaning the portion of the fluid circuit contained within the furnace. Without this bypass line all of the impurities flushed out of the feedwater system would be carried on into the boiler circuit contained Within the furance. Some of these impurities thus flushed into the furnace circuit could settle out or become entrapped within various parts of this circuit. This is especially true due to the fact that the flow rate established by feedwater pump 48 during the boiler cleanup cycle is relatively small.
  • a forced flow once-through steam generator having a fluid circuit
  • the fluid circuit including a feedwater system through which water flows, said feedwater systern including a feedwater line having an inlet and an outlet, feedwater heating means positioned within said feedwater line a feedwater pump in said feedwater line, means positioned in the feedwater line for removing impurities from the Water, a furnace including fuel burning means for creating hot combustion gases, heat exchange means positioned within the furnace for generating steam therein, said heat exchange means having an inlet and an outlet, the outlet of said feedwater line being connected to the heat exchange means inlet, a first shutoff valve positioned in said feedwater line prior to its outlet, a bypass line having an inlet and an outlet, a second shutoff valve positioned in the bypass line, the bypass line inlet being connected to the feedwater line upstream of the first shutoff valve and the bypass line outlet being connected to the feedwater line inlet, whereby when it is desired to clean the fluid circuit the first shutoff valve can be closed and the second shutoff valve opened to
  • a force flow once-through steam generator having a fluid circuit
  • the fluid circuit including a feedwater sys tern through which water flows, said feedwater system including a feedwater line having an inlet and an outlet, first and second feedwater heating means positioned within said feedwater line, said first and second feedwater heating means being in parallel flow relationship with one another, said feedwater line containing branched lines leading to and from both said first and second feedwater heating means, a first shutoff valve positioned in one of the branched lines, a second shutoff valve positioned in the other branched line, a pump in said feedwater line, means positioned in the feedwater line for removing impurities from the water, a furnace including fuel burning means for creating hot combustion gases, heat exchange means positioned within the furnace for generating steam therein, said heat exchange means having an inlet and outlet, the outlet of said feedwater line being connected to the heat exchange means inlet, a third shutoff valve positioned in said feedwater line prior to its outlet, a bypass line having an inlet and an outlet
  • a method of cleaning the fluid circuit of a forced flow once-through steam generator comprising a furnace, a fluid circuit including a feed- Water system having an inlet and an outlet, a steam generating circuit positioned in the.furnace,.which steam generating circuit is connected to the outlet of the feedwater system, a bypass extending from the feedwater system outlet to the feedwater system inlet, the feedwater system including a pump, feedwater heating means, and means for removing impurities from the fluid, which method comprises the steps of starting the pump to force fluid through the feedwater system, passing all of the pumped fluid through the bypass until the fluid reaches a predetermined degree of purity to thus clean 'out the feedwater system, and thereafter passing all of the pumped fluid into the steam generating circuit to thus clean the steam generating circuit.
  • a method of cleaning the fluid circuit of a forced flow once-through steam generator comprising a furnace, a fluid circuit including a feedwater system having an inlet and an outlet, a steam generating circuit positioned in the furnace, which steam generating circuit is connected to the outlet of the feedwater system, a bypass extending from the feedwater system outlet to the feedwater system inlet, the feedwater system including a pump means, at least two feedwater heaters in parallel, and means for removing impurities from the Water,
  • Which method comprises the steps of operating the pump means to force fluid through the feedwater system at a rate which is a predetermined minor percentage of the rate at which the fluid flows when the steam generator is operating at full load capacity, passing all of the fluid through one of the feedwater heaters and then through the bypass until the fluid reaches a predetermined degree of purity, thereafter successively passing all of the fluid through each of the remaining feedwater heaters and the bypass until the fluid reaches a predetermined degree of purity, and thereafter passing 5 6 all of the pumped fluid into the steam generating circuit

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Cleaning By Liquid Or Steam (AREA)

Description

July 13, 1965 H. A. GRABOWSKI METHOD AND APPARATU S FOR PREBOILER CLEANUP 0 A ONCE-THROUGH STEAM GENERATOR Filed March 25, 1963 FURNACE INVENTOR HILARY A. GRABOW SKI WI. UAW
United States Patent M METHDD AND APPARATUS FOR PREBOILER CLEANUP OF A ONCE-THROUGH STEAM GENERATOR Hilary A. Grabowski, West Simsbury, Conn., assignor to Combustion Engineering, Inc, Windsor, Conn., a corporation of Delaware Filed Mar. 25, 1963, Ser. No. 267,515 4 Claims. (Cl. 122-379) This invention relates to a forced flow once-through steam generator, and in particular to a method of operation for cleaning the fluid circuit associated with such a forced flow once-through steam generator.
In a once-through steam generator it is important to maintain the fluid flowing through the fluid circuit at a relatively high degree of purity in order to prevent the formation of deposits on the tubes within the heat exchange members, and also on the turbine blades. Deposits in boiler tubes could lead to overheating and failtire of the tube metal; deposits on the turbine blades results in high pressure drops across the steam turbine stages, thus reducing the output capacity of the turbine. For this reason, the fluid supplied to the steam generator is continuously filtered, demineralized, and de-aerated during operation; and on occasion, generally just before eachstartup of the unit, the fluid circuit is flushed to remove any deposits of salts or other corrosive materials which may have been formed or become trapped in any of the heat exchanger tubes, and interconnecting piping. It is an object of this invention to provide novel means and a method of operation thereof for quickly and efficiently cleaning the fluid circuit associated with a forced flow once-through steam generator. ()ther objects and advantages of the invention will become apparent from the following specification and accompanying drawing wherein the figure shows a diagrammatic representation of a forced fiow once-through steam generator system embodying my invention.
Looking now to the drawing, broken line represents a furnace and its associated gas pass, through which hot combustion gases flow. Fuel and air are supplied to the furnace by Way of burner 11, which fuel is burned in the furnace 10 to thereby generate the hot combustion gases.
Contained within the furnace and its associated rear gas pass is a fluid circuit comprised of economizer 12, furnace wall steam generating tubes 14, superheater 18, and reheater 28. Numeral 16 designates a boiler throttle valve arrangement which is used during startup and other critical times.
Fluid enters the circuit contained within the furnace 'and its associated gas pass flowing first through the This heated water then enters the tubes 14 lining 3,194,216 Patented July 13, 1965 ICC During startup of the unit steam must be slowly admitted to the turbine in order to prevent thermal shock thereto. Thus it is necessary to bypass some of the steam produced in the steam generator during the startup cycle. For this reason the line leading to the high pressure turbine 20 contains a shutoff valve 22, and a bypass line 24 is provided containing shutoff valve 26 which extends from a point upstream of valve 22 to the condenser 32.
The feedwater. system is made up of feedwater line 60 the inlet of which is supplied with water from the condenser 32 and the outlet of which is connected to the economizer 12. Positioned within this feedwater line 6i) is a condensate pump 34, filter and demineralizer 36,
driven by steam generated in the auxiliary boiler '68; The
steam discharged from turbine 70 is used for heating the feedwater flowing through de-aerator 46. Line 71 completes the circuit for the auxiliary boiler 65.
As shown, the low pressure feedwater heater is made up of two heaters 38 and 40 which are in parallel flow relationship with one another. The branched lines leading to the heaters 33 and 40 contain shutoff valves 42 and 44 respectively. Similarly, the high pressure feedwater heater is made up of two feedwater heaters and 52 which are also in parallel. The branched lines leading to these two heaters contain shutoff valves54 and 56 respectively. The purpose of these parallel heaters and the shutoff valves in such parallel lines will be described more fully at a later time. i A bypass line 64 extends from the outlet of feedwater line 60 to the hotwell 33 and contains a shutoff valve 66. Bypass line 64 is connected to the feedwater line outlet upstream of the feedwater shutoif valve 62.
The operation of the system will now be described. When it is desired to clean or flush out the fluid circuit associated with the once-through steam generator, feedwater shutoff valve 62 is closed, and the valve 66 in the bypass line 64 is opened. Feedwater pump 48 is started up, thus forcing water through the feedwater system and the bypass line 64. The fluid is allowed to continue to circulate through this circuit until a predetermined degree of purity of the water is sensed by any wellknown chemical analyzer, 58, which is shown positioned within the feedwater line 60 downstream of the high pressure feedwater heaters. During this preboiler cleanup operation, any deposits of foreign material which may have formed, or had become trapped within the feedwater heater sections will be flushed out, and removed from the water as it passes through the filter and demineralizer 36. Device 36 removesboth the soluble and insoluble impurities from the water.
The amount of power required to drive the feedwater pump 48 during full load operation is quite large, and it is not economical to drive the pump at this high rating during the cleanup operation. The turbine 70 is thus operated during the startup cycle such that it will drive the feedwater pump 48 at only a minor percentage of creased flow therethrough during the cleanup cycle.
the rate at which it is driven during full load operation, for example 15% of full load operation.
It is well recognized that an increase in temperature and in flow rate results in a more efiicient and quick cleanup cycle. Thus the temperature of the Water being circulated is heated in the de-aerator to a temperature of approximately 230 F. during the preboiler cleanup cycle. The high and low pressure feedwater heaters have been constructed of parallel heaters in order to enable an in- Thus if shutoif valve 42 is closed during a portion of the cleanup cycle, and all of the fluid is allowed to flow through heater 4%, the flow rate therethrough will be twice as large as it would have been if the flow had been allowed to pass through both of the parallel heaters. The same is true of the high pressure heaters 5t and 52.. Thus during the first part of a cleanup cycle valves 42 and 54 would be closed, forcing the entire flow to pass through the low pressure heater 4t) and the high pressure heater 52. When analyzer 533 senses a predetermined degree of cleanliness of the water, valves 42 and 54 can be opened, and valves 44 and 56 closed. The cycle is then repeated until the other two heaters 38 and 50 are cleaned out and analyzer 58 again senses a predetermined degree of purity. The water should be cleaned to a high degree of purity, for example 20 parts per billion of foreign material. At this time shutoff valve 66 in the bypass line 6 5 is closed, and the feedwater valve 62 is opened. The heat exchange members positioned Within the furnace and its associated gas pass can thereafter be cleaned.
Obviously, the feedwater heaters can contain more than two sections in parallel. For example, if three were in parallel, and two of them were shut-01f, the flow rate through the remaining one would be three times greater than would be the case if all of them were open to flow.
By providing the steam generator with bypass line 64, it is possible to first clean the feedwater system removing the impurities from the elements within this system, and thereafter cleaning the portion of the fluid circuit contained within the furnace. Without this bypass line all of the impurities flushed out of the feedwater system would be carried on into the boiler circuit contained Within the furance. Some of these impurities thus flushed into the furnace circuit could settle out or become entrapped within various parts of this circuit. This is especially true due to the fact that the flow rate established by feedwater pump 48 during the boiler cleanup cycle is relatively small.
Although only one embodiment of the invention has been shown and described, it is to beunderstood that the invention is not to be limited thereto. The invention could be utilized in other alternative arrangements. For example although a monotube once-through type unit has been illustrated, the invention would apply equally as well to a once-through steam generator including a recirculation system such as described in my co-pending application filed on even date herewith and entitled Boiler Cleanup Method for Combined Circulation Steam Generator, Serial No. 267,588.
What I claim is:
it. In a forced flow once-through steam generator having a fluid circuit, the fluid circuit including a feedwater system through which water flows, said feedwater systern including a feedwater line having an inlet and an outlet, feedwater heating means positioned within said feedwater line a feedwater pump in said feedwater line, means positioned in the feedwater line for removing impurities from the Water, a furnace including fuel burning means for creating hot combustion gases, heat exchange means positioned within the furnace for generating steam therein, said heat exchange means having an inlet and an outlet, the outlet of said feedwater line being connected to the heat exchange means inlet, a first shutoff valve positioned in said feedwater line prior to its outlet, a bypass line having an inlet and an outlet, a second shutoff valve positioned in the bypass line, the bypass line inlet being connected to the feedwater line upstream of the first shutoff valve and the bypass line outlet being connected to the feedwater line inlet, whereby when it is desired to clean the fluid circuit the first shutoff valve can be closed and the second shutoff valve opened to permit fluid to be circulated through the feedwater system and said bypassline, and when the water therein reaches a predetermined purity, the first shutoff valve can be opened and the second shutoff valve closed to permit cleaning of the heat exchange means.
2. In a force flow once-through steam generator having a fluid circuit, the fluid circuit including a feedwater sys tern through which water flows, said feedwater system including a feedwater line having an inlet and an outlet, first and second feedwater heating means positioned within said feedwater line, said first and second feedwater heating means being in parallel flow relationship with one another, said feedwater line containing branched lines leading to and from both said first and second feedwater heating means, a first shutoff valve positioned in one of the branched lines, a second shutoff valve positioned in the other branched line, a pump in said feedwater line, means positioned in the feedwater line for removing impurities from the water, a furnace including fuel burning means for creating hot combustion gases, heat exchange means positioned within the furnace for generating steam therein, said heat exchange means having an inlet and outlet, the outlet of said feedwater line being connected to the heat exchange means inlet, a third shutoff valve positioned in said feedwater line prior to its outlet, a bypass line having an inlet and an outlet, a fourth shutoff valve positioned in the bypass line, the bypass line inlet being connected to the feedwater line upstream of the third shutoff valve, and the bypass line outlet being connected to the feedwater line inlet.
3; A method of cleaning the fluid circuit of a forced flow once-through steam generator, the steam generator comprising a furnace, a fluid circuit including a feed- Water system having an inlet and an outlet, a steam generating circuit positioned in the.furnace,.which steam generating circuit is connected to the outlet of the feedwater system, a bypass extending from the feedwater system outlet to the feedwater system inlet, the feedwater system including a pump, feedwater heating means, and means for removing impurities from the fluid, which method comprises the steps of starting the pump to force fluid through the feedwater system, passing all of the pumped fluid through the bypass until the fluid reaches a predetermined degree of purity to thus clean 'out the feedwater system, and thereafter passing all of the pumped fluid into the steam generating circuit to thus clean the steam generating circuit. a
4. A method of cleaning the fluid circuit of a forced flow once-through steam generator, the steam generator comprising a furnace, a fluid circuit including a feedwater system having an inlet and an outlet, a steam generating circuit positioned in the furnace, which steam generating circuit is connected to the outlet of the feedwater system, a bypass extending from the feedwater system outlet to the feedwater system inlet, the feedwater system including a pump means, at least two feedwater heaters in parallel, and means for removing impurities from the Water, Which method comprises the steps of operating the pump means to force fluid through the feedwater system at a rate which is a predetermined minor percentage of the rate at which the fluid flows when the steam generator is operating at full load capacity, passing all of the fluid through one of the feedwater heaters and then through the bypass until the fluid reaches a predetermined degree of purity, thereafter successively passing all of the fluid through each of the remaining feedwater heaters and the bypass until the fluid reaches a predetermined degree of purity, and thereafter passing 5 6 all of the pumped fluid into the steam generating circuit 2,907,305 10/59 Profos 122379 to thus clean the steam generating circuit. 3,009,325 11/61 Pirsh 122-1 3,010,853 11/61 Elliott 13413 References Cited by the Examiner 3,085,915 4/63 Heitmann et a1.
UNITED STATES PATENTS 5 FOREIGN PATENTS 1,064,855 6/13 Parry. 617,110 3/61 Canada. 1,791,923 2/31 Eule 122-379 X 386,042 12/23 Germany. 1,892,093 12/32 Battistella. 2 55 12 51 Webb 134 22 10 PERCY L. PATRICK, Przmary Examiner. 2,858,808 11/ 58 ROWand 122379 FREDERICK KETTERER, Examiner.

Claims (1)

1. IN A FORCED FLOW ONCE-THROUGH STEAM GENERATOR HAVING A FLUID CIRCUIT, THE FLUID CIRCUIT INCLUDING A FEEDWATER SYSTEM THROUGH WHICH WATER FLOWS, SAID FEEDWATER SYSTEM INCLUDING A FEEDWATER LINE HAVING AN INLET AND AN OUTLET, FEEDWATER HEATING MEANS POSITIONED WITHIN SAID FEEDWATER LINE, A FEEDWATER PUMP IN SAID FEEDWATER LINE, MEANS POSITIONED IN THE FEEDWATER LINE FOR REMOVING IMPURITIES FROM THE WATER, A FURNACE INCLUDING FUEL BURNING MEANS FOR CRATING HOT COMBUSTION GASES, HEAT EXCHANGE MEANS POSITIONED WITHIN THE FURNANCE FOR GENERATING STEAM THEREIN, SAID HEAT EXCHANGE MEANS HAVING AN INLET AND AN OUTLET, THE OUTLET OF SAID FEEDWATER LINE BEING CONNECTED TO THE HEAT EXCHANGE MEANS INLET, A FIRST SHUTOFF VALVE POSITIONED IN AID FEEDWATER LINE PRIOR TO ITS OUTLET, A BYPASS LINE HAVING AN INLET AND AN OUTLET, A SECOND SHUTOFF VALVE POSITIONED IN THE BYPASS LINE, THE BYPASS LINE INLET BEING CONNECTED TO THE FEEDWATER LINE UPSTREAM OF THE FIRST SHUTOFF VALVE AND THE BYPASS LINE OUTLET BEING CONNECTED TO THE FEEDWATER LINE INLET, WHEREBY WHEN IT IS DESIRED TO CLEAN THE FLUID CIRCUIT THE FIRST SHUTOFF VALVE CAN BE CLOSED AND THE SECOND SHUTOFF VALVE OPENED TO PERMIT FLUID TO BE CIRCULATED THROUGH THE FEEDWATER SYSTEM AND SAID BYPASS LINE, AND WHEN THE WATER THEREIN REACHES A PREDETERMINED PURITY, THE FIRST SHUTOFF VALVE CAN BE OPENED AND THE SECOND SHUTOFF VALVE CLOSED TO PERMIT CLEANING OF THE HEAT EXCHANGE MEANS.
US267515A 1963-03-25 1963-03-25 Method and apparatus for preboiler cleanup of a once-through steam generator Expired - Lifetime US3194216A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
US267515A US3194216A (en) 1963-03-25 1963-03-25 Method and apparatus for preboiler cleanup of a once-through steam generator
GB940864A GB1044053A (en) 1963-03-25 1964-03-05 Apparatus and method for starting a forced through flow vapour generator and associated power plant
ES0297748A ES297748A1 (en) 1963-03-25 1964-03-18 Apparatus and method for starting a forced through flow vapour generator and associated power plant
CH352864A CH459263A (en) 1963-03-25 1964-03-18 Method for cleaning the working fluid flow circuit of a steam generator with forced flow, and device for carrying out the method
BE645379D BE645379A (en) 1963-03-25 1964-03-18
NL6402944A NL6402944A (en) 1963-03-25 1964-03-19
FR968174A FR1390595A (en) 1963-03-25 1964-03-20 Improvements made to processes and apparatus for starting up single-path steam generators

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3393564A (en) * 1966-11-02 1968-07-23 William H Simmons Sight level gauge clearing apparatus
US20110072818A1 (en) * 2009-09-21 2011-03-31 Clean Rolling Power, LLC Waste heat recovery system
WO2011141670A1 (en) * 2010-05-12 2011-11-17 Solios Environnement Method and device for unclogging a heat exchanger
US20140238507A1 (en) * 2007-03-27 2014-08-28 Christopher J. Bloch Method and apparatus for commissioning power plants

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US1064855A (en) * 1911-01-12 1913-06-17 Richard William Parry Feed-water heating and purifying means.
DE386042C (en) * 1921-01-20 1923-12-17 Aeg Process for maintaining the most constant outlet temperature possible for steam-heated water preheaters
US1791923A (en) * 1928-06-16 1931-02-10 Siemens Ag Multiway sludge valve
US1892093A (en) * 1932-12-27 Method of removing rust
US2556128A (en) * 1945-08-17 1951-06-05 Thomas L B Webb Method for removing scale
US2858808A (en) * 1954-04-08 1958-11-04 Babcock & Wilcox Co Method of operating a supercritical pressure vapor generator
US2907305A (en) * 1953-10-27 1959-10-06 Sulzer Ag Method of generating steam in a forced flow steam generator
CA617110A (en) * 1961-03-28 Lieberherr Arthur Method for draining the tube system of a steam generator
US3009325A (en) * 1955-05-27 1961-11-21 Babcock & Wilcox Co Once-through vapor generating and superheating unit
US3010853A (en) * 1959-05-14 1961-11-28 Solvent Service Inc Method of cleaning pipes and the like
US3085915A (en) * 1958-03-13 1963-04-16 Siemens Ag Method of removing rust from ironcontaining materials, particularly for the cleaning of boiler plants

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Publication number Priority date Publication date Assignee Title
US1892093A (en) * 1932-12-27 Method of removing rust
CA617110A (en) * 1961-03-28 Lieberherr Arthur Method for draining the tube system of a steam generator
US1064855A (en) * 1911-01-12 1913-06-17 Richard William Parry Feed-water heating and purifying means.
DE386042C (en) * 1921-01-20 1923-12-17 Aeg Process for maintaining the most constant outlet temperature possible for steam-heated water preheaters
US1791923A (en) * 1928-06-16 1931-02-10 Siemens Ag Multiway sludge valve
US2556128A (en) * 1945-08-17 1951-06-05 Thomas L B Webb Method for removing scale
US2907305A (en) * 1953-10-27 1959-10-06 Sulzer Ag Method of generating steam in a forced flow steam generator
US2858808A (en) * 1954-04-08 1958-11-04 Babcock & Wilcox Co Method of operating a supercritical pressure vapor generator
US3009325A (en) * 1955-05-27 1961-11-21 Babcock & Wilcox Co Once-through vapor generating and superheating unit
US3085915A (en) * 1958-03-13 1963-04-16 Siemens Ag Method of removing rust from ironcontaining materials, particularly for the cleaning of boiler plants
US3010853A (en) * 1959-05-14 1961-11-28 Solvent Service Inc Method of cleaning pipes and the like

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3393564A (en) * 1966-11-02 1968-07-23 William H Simmons Sight level gauge clearing apparatus
US20140238507A1 (en) * 2007-03-27 2014-08-28 Christopher J. Bloch Method and apparatus for commissioning power plants
US10480780B2 (en) 2007-03-27 2019-11-19 Boyle Energy Services And Technology, Inc. Method and apparatus for commissioning power plants
US10612771B2 (en) 2007-03-27 2020-04-07 Boyle Energy Services & Technology Method and apparatus for commissioning power plants
US10627104B2 (en) * 2007-03-27 2020-04-21 Boyle Energy Services & Technology, Inc. Method and apparatus for commissioning power plants
US10782015B2 (en) 2007-03-27 2020-09-22 Boyle Energy Services & Technology, Inc. Method and apparatus for commissioning power plants
US20110072818A1 (en) * 2009-09-21 2011-03-31 Clean Rolling Power, LLC Waste heat recovery system
US9243518B2 (en) * 2009-09-21 2016-01-26 Sandra I. Sanchez Waste heat recovery system
WO2011141670A1 (en) * 2010-05-12 2011-11-17 Solios Environnement Method and device for unclogging a heat exchanger
FR2960053A1 (en) * 2010-05-12 2011-11-18 Solios Environnement METHOD AND DEVICE FOR DISENGAGING HEAT EXCHANGER

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