LV11061B - System and method for reheat steam temperature control in circulating fluidizided bed boilers - Google Patents

Description

LV 11061

SYSTEM AND METHOD FOR REHEAT STEAM TEMPERATURE CONTROL IN CIRCULATING FLUIDIZED BED BOILERS

The present invention relates to a povver plant including a two-stage steam turbine and a steam generator plant having a fluidized bed combustion system that includes a fluidized bed combustor, at least one separator, and a gas flue comprising a reheater and superheater.

The present invention relates also to a method of controlling reheater temperatures in a steam generator having a fluidized bed combustion system that includes a fluidized bed combustor, at least one hot separator, and a reheater in a gas flue.

Several methods are presently known for controlling reheat steam temperatures.

One method of reheater temperature control is the use of a system for gas bypass over the reheater. Two separate flue gas passes are provided in the convection pass of the boiler (one for superheater and one for reheater), with means such as dampers dovvnstream of each to very the amount of flue gas flow over each section. The outlet steam temperature of the reheater can be controlled by varying the amount of flue gas flow betvveen the convection pass sections. The main disadvantage of this system is that the dampers are - 2 - located in a higher temperature (260 - 371 ’C) dust laden flue gas path making them susceptible to erosion and mechanical failure. Also, the steam temperature control range is limited with this type of sy$tem.

Another method of reheater outlet steam temperature control is by the use of external heat exchangers. With this approach, a portion of the recirculated solīds within the circulating fluidized bed system is diverted to an externally mounted fluidized bed heat exchanger, i.e. external heater exchanger (EHE), in which a section of or comlete reheater is located. By varying the amount of solids flow to the EHE, the quantity of heat transfer to the reheater and the reheater outlet steam temperature is controlled. The main disadvantages of this system are that the solids flow control valve is a high maintenance item and the reheat tube surface vvithin the EHE is subject to erosion. This effects the availability of the unit.

It has also been suggested in US 4.748.940 to arrange first reheater heating surfaces in a flue gas passage of a circulating fluidized bed combustor and to connect to this first reheater a second reheater disposed in an external heat exchanger (EHE). An adjustable by-pass line is connected in parallell to the reheater heating surfaces. The outlet temperature of the reheater is controlled by controlling the solids flow in the external heat exchanger and by controlling the steam flow in the two reheaters by means of the by-pass line. A further approach to the control of the reheater outlet steam temperature is by the use of spray desuperheater. This approach utilizēs spraying vvater for desuperheating and thereby controlling reheater outlet steam temperature. This is a simple approach, but not generally accepted because it degradēs the cycle efficiency.

Stili another approach is by the use of excess air. Excess air supplied to the boiler can be used for reheat steam temperature control. This approach, hovvever, is not favored because of its negative affect on boiler efficiency. A stili further approach is by the use of gas recirculation. By this approach, large quantities of flue gases are recirculated to achieve the rated reheater outlet steam temperature. This approach, hovvever, requires the use of a gas recirculation fan for handling a hot dust laden gas and requires additional povver consumption, vvhich makes this approach disadventageous. - 3 - - 3 - LV 11061

Accordingly, the present invention is directed to an improved method and system tor reheat steam temperature control.

SUMMARY AND OBJECTS OF THE INVENTION

It is the primary object of the present invention to provide an improved system and method for controlling the reheater (outlet) steam temperature in circulating fluidized bed boilers.

In accordance with a primary aspect of the present invention, a steam generator having a fluidized bed combustion system that includes a fluidized bed combustor, at least one separator, and a reheater in a flue gas pass and is characterized by - a first stage of reheater and a second or final stage of reheater sequentially disposed in a common gas flue, - means for dividing cold steam from a turbine into selective first and second portions and directing said first portion through the first stage of reheater, and - means for recombining the first and second portions and directing same through the second stage of reheater.

Preferably the steam generator includes means for controlling the temperature of the second or final stage of the reheater and comprises means for by-passing a selected portion of cold steam around said first stage reheater directly to said second or final stage reheater. A method according to the present invention is characterized by - dividing the reheater into a first and second or final stage reheater and sequentially disposing the first and second stages of the reheater in a common gas flue, - dividing cold steam returning to the reheater into selective first and second portions and directing the first portion through the first stage of reheater and - recombining the first portion and the second portion and directing the same through the second or final stage of reheater. 4

BRIEF DESCRIPTION OF THE DRAVVING

The above and other objects and advantages of the present invention will become apparent from the follovving description when read in conjuntion with the accompanying drawings wherein:

Fig. 1 is a schematic diagram illustrating a typical circulating fluidized bed boiler system embodying the present invention;

Fig. 2 is a schematic diagram illustrating another embodiment of the present invention; and

Fig. 3 is a schematic diagram illustrating an arrangement of two typical boilers connected to a single turbine.

DETAILED DESCRIPTION OF A PREFERRED EMBODIMENT

Referring to Fig. 1, a povver plant embodying a typical circulating fluidized bed boiler with superheater and reheater is illustrated with the system incorporating a preferred embodiment of the present invention. The boiler system, designated generally by the numeral 10, comprises a fluid bed combustor 12 having a combustion chamber 14 into which combustible material, non-combustible material, possibly additives or recirculated material, primary air and secondary air are fed. In the combustion chamber, the bed is maintained in fluidized State by having the correct inventory of bed material and flow of air. The combustion chamber is provided with a bottom 16 having a grid-like construction through vvhich fluidizing air is introduced. The combustion chamber vvalls are preferably constructed with membrane type tube vvalls, vvith or vvithout a refractory covering.

First and second stages of superheaters 18 and 20 are located vvithin the combustion chamber. The combustion chamber materiāls are caried from the combustion chamber by way of flues 22 to a hot separator 24 vvherein the solids are separated from the flue gases for return by way of particle recycling - 5 - - 5 - LV 11061 system 26, 28 and 30 to the bottom of the combustion chamber for recirculation. These may be passed through fluidized bed coolers or the like prior to return to the combustion chamber.

The details of circulation Circuit for the feed vvater and the primary superheaters are not illustrated as they do not form an essential part of the present invention.

Flue gases from the hot separator pass along by way of flue 32 to a convection pass 34. A single stage superheater 38 is placed or located in the convection pass with reheaters 40 and 42 located dovvnstream of the superheater 38 and upstream of an economizer surface 44. The reheater is illustrated as two stages with 42 being a first stage and 40 being a second or final stage. The reheater may have more than two stages, with the final stage just down stream from superheater 38 such as 40 is located. These are arranged as counter flow heat exchangers with the gas flow direction down and the reheat steam flow direction up. The placement of the superheater 38 vvithin this pass helps keep the temperature of the gas flow to reheater 40 below the critical temperature. This arrangement together with the bypass feature as will be explained enables a unique and effective control of the temperatures vvithin the reheater sections.

When the steam temperature leaving the particular section (in a counter flow heat exchanger arrangement) is close to the gas temperature entering that section, reducing the steam flow to that section will result in a considerable reduction in heat absorption. As the steam temperature approaches the gas temperature, the effective thermal heat available for heat transfer is reduced. This provides the basis for the principle used for the reheat temperature control system in accordance with the present invention.

The generating system as illustrated in Fig. 1 is supplying steam to a two-stage turbine. In the illustrated arrangement, steam from superheater 38 flovvs via an outlet header 46 and supply line 48 by way of valve 50 to the inlet side of the high pressure turbine (HPT) 52. Cold steam leaving the turbine 52 retums by way of return line 53 to the reheaters 42 and 40. At the reheater, a bypass line 54 joins the return line 53 at 55 and bypasses a portion of the cold steam with the remaining portion of the steam going by - 6 - way of differential control valve 56 to the inlet header 58 of the first stage reheater 42.

The steam passing through the reheater 42 exists by way of a header 60 and rejoins or combines with the bypass portion of the cold steam at 62. A flow control valve 64 is provided in the bypass line 54 for control of the flow betvveen the inlet manifold of the first stage reheater 42 and the bypass line. The recombined steam at 62 flows into inlet header 66 of the second or final stage reheater 40 vvhere it is further heated and flows by way of outlet header 68, supply line 70 and valve 72 to the second stage or lower stage of the turbine (IPT) 74. The selective proportioning of the cold steam betvveen the bypass line 54 and the second stage of the reheater 42 provides an effective and efficient means of controlling the temperature in the reheater stages.

The location of the first stage reheater 42 along the flue gas path is so shosen that bypassing the required portion of the cold reheat steam directly to the second stage reheater 40 cannot increase the steam temperature leaving the first stage reheater to more than the allovved mētai temperature for the reheater tube material. A limit will be set to protect the first stage reheater materiāls from exceeding their allovvable mētai temperature. The value of 566 °C is a typica! limit and may vary depending upon the actual design conditions. The purpose of the system is such that the maximum tube outside surface temperature will not exceed the allovvable mētai temperature limit for the material selected.

The arrangement of the control valves 56 and 64 is so chosen that controlability is achieved throughout the steam temperature control range and permits ali reheater surfaces to be placed in the convection pass of the boiler, eliminating the need for in furnace reheater surfaces. This also makes feasible a simplified start-up scheme when more than one boiler for example is connected to a common turbine system. In this arrangement, the set of valves provide a means for reheat steam flow balancing under various operating conditions.

In the circulating fluidized bed boiler, the combustion takes place in a fluidized bed of inert material. The fluidized bed material leaving the combustor is retumed by means of a hot collector (such as a hot cyclone) through suitable sealing device. In operation, air and fuel are delivered to the combustion - 7 - - 7 - LV 11061 chamber 14 vvherein the bed material is maintained in a fluidized State by having the correct flow of air and bed material. The fluidizing air is introduced through a grid-like grating or construction at 16 in the bottom of the chamber. The flue gas and combustion products, along with the carry over solids, first convey heat to the superheaters 18 and 20 and are conveyed by way of flue 22 into the hot separator 24 vvherein the solids are separated and returned to the combustion chamber through the recycling arrangement 26, 28 and 30. The hot flue gases are then conveyed from the hot separator(s) by way of flue 32 to the convection pass section 34 vvherein the final stage superheater 38 and the reheater stages 40 and 42 are located.

Three superheater stages are disposed in the described system, these being 18 and 20 and 38, with 38 being in the flue gas convection pass. Desuperheaters may be positioned betvveen the superheater stages for steam temperature control if necessary. The two stages 40 and 42 of the reheater are positioned in the convection pass 34 and in conjuction with the control valves and interconnecting piping so that precise control of the reheater outlet steam temperature is possible. The piping system is such that cold steam reentering this system at pipe 53 is selectively divided into tvvo streams at the juncture 55 thereof vvith the bypass line 54. One stream passes to the first stage reheater and is distributed through inlet header 58. The other steam goes to the second stage reheater by way of valve 64 and inlet header 66. The selective division of the stream will be in proportion to the temperature control necessary, vvhich is accomplished by the valves 56 and 64.

The hot steam leaving the first stage reheater from the outlet header 60 is mixed vvith the cold steam via the bypass line 54 after or down stream of the flow control valve 64 and the blended stream enters the second stage reheater by way of the inlet header 66. The flow through the first stage reheater is controlled by proper manipulation of the tvvo control valves 56 and 64, vvhich in turn control the steam temperature leaving the second stage reheater 40. Hot steam from the second or final stage reheater is directed back to the turbine by way of the hot reheat steam line 70. A differential pressure responsive control unit 80 Controls the setting of valve 56 for controlling the pressure differential available for the control valve 64. The control unit 80 is responsive to the pressure differential betvveen the cold - 8 - steam return line 53 and the outlet pressure at juncture 62 of the outlet of reheater 42 and the bypass line 54. This is indicated by phantom line 84 in Fig. 1. The control unit 80 is set to control the valve 56 as a function of load on the boiler.

The valve 64 in the bypass line 54 is controlled by temperature responsive control unit 82 vvhich responds to the temperature of the outlet steam from the second or final stage reheater 40. This is indicated by phantom line 86 in Fig. 1. In the illustrated embodiment, as an example the temperature of reheater 40 is maintained vvithin the limit of about 538 °C, plus or minus 10 ”C. As the temperature of the steam leaving reheater 40 begins to increase above 543 °C, the valve 64 is opened to bypass additional cold steam directly to reheater 40. As the temperature begins to fall belovv 532 °C, the valve 64 is closed to reduce the flow of bypass cold steam to the second stage 40.

In Fig. 2, a system identical to Fig. 1, but with superheater 38 located betvveen the reheaters 40 and 42, is disclosed. A single staged superheater 38 is placed in the convection pass, with second stage reheater 40 located upstreams and first stage reheater 42 dovvnstream of the superheater. An economizer 44 is located dovvnstream of the superheater 38. This is in contrast to what was shovvn in Fig. 1. The placement of the second stage reheater 40 upstream of the superheater 38 allovvs it to pick up more heat at lower loads. This gives it the potential to extend its steam temperature control range, while having little if any effect on the superheater control range. This potential extension of the reheat steam temperature control range vvill enhance the coupling of two units to one turbine easier as to temperature matching capabilities.

The present arrangement, with second stage reheater 40 upstream of superheater 38, gives even greater control over the temperature in the reheater stages. As the gas now passes reheater 40 before it passes superheater 38, it may not be belovv the critical temperature for reheater 40 up to some load of the boiler. Thus, with superheater 38 in the pass behind the reheater 40, the gas temperature vvill be belovv the critical temperature for reheater 40 only until after about 25% to 30% load is reached. At this time cold steam is available for control of the temperature in accordance vvith this invention. If a higher load point is reguired, the tube mētai materiāls could be - 9 - - 9 - LV 11061 upgraded to allovv a maximum load of about 35% to 40%. This point of not requiring flow through the reheater until the unit is at 25% to about 40% load is another advantage of this invention.

Referring to Fig. 3, a system identical to Fig. 1, but with a duplicate boiler, is disclosed. In this system, the components of the first boiler arrangement are identified by the same reference numerals as in Fig. 1, with the second boiler arrangement being identified with the same numbers primed. Therefore, in this arrangement, a boiler turbine system is disclosed vvherein two boilers are supplying steam to a single turbine. One essential feature required for this type of system is that means be provided for controlling the amount of reheat steam flow to each boiler, so that the steam temperature at reheat outlet is vvithin limits at ali possible operating conditions. In the illustrated system, duplicate Controls and piping are provided for the two boilers.

The control valves 56 and 64 for the reheat steam temperature control can be used for flow balancing and maintaining the reheater outlet temperature vvithin limits under both normai and abnormal operating conditions. In this arrangement, pressure reducing valves 80 and 82, along with desuperheaters 76 and 78, provide for flexibility during cold start-up, hot start-up and also when starting the second unit vvhile the first one is on line. This simple system eliminates the need for a sophisticated steam blending system. It provides a simple and effective system and method for reheat outlet steam temperature control under varying load conditions.

In operation, from a cold start, combustion is initiated in the combustion chamber 14 with the introduction of fuel and combustion air. As heat is generated as a result of the combustion, the hot gases of combustion move upvvard in the combustion chamber transferring heat to the vvater in the combustion chamber vvalls and to superheaters 18 and 20. The hot gas, combustion products, and solids pass from the combustion chamber along flue 22 into the hot separator 24 vvhere the solids are separated for return to the combustion chamber. The hot flue gas passes along flue 32 into the convection pass 34 vvhere the heat is transferred in sequence to the superheater 38, the second or final stage reheater 40, and the first stage reheater 42. The flow of hot gas through the system begins before the flow of cold steam. The boiler is fired and fuel burns for a period of time providing hot 10 - gas before steam is generated and starts the turbine. Cold reheat steam does not start flovving until after the turbine starts.

As the hot gas give up their heat to the water and steam in the water walls, in superheaters and reheaters, the temperature drops so that it is less at each successive stage. It should be noted that the gas temperature leaving the combustion chamber outlet at full load will be in the range of 843 to 927 °C. The greater the temperature differential betvveen the gas and the vvater, the greater the heat transfer will be, and the cooler the gas will be as it passes from the respective heater.

Therefore, as the gas passes superheater 38, it will be belovv the critical temperature for reheater 40 up to some load of the boiler. Thus, with superheater 38 in the gas pass ahead of the reheater 40, the gas temperature will be belovv the critical temperature for reheater 40 until after about 40% to 50% load is reached. At this time cold steam is available for control of the temperature in accordance with this invention. This point of not requiring flow through the reheater until the unit is at 50% load is another advantage of this invention. Most Standard systems require flow through the reheater during the earlier stages of start-up (hot or cold), to protect some from burn out. Thus, an expensive by-pass system must be utilized. Hovvever, with this system's physical layout, a bypass is not required and system start-up periods can be shortened.

Other modifications and changes are possible in the foregoing disclosure and in some instances, some features may be employed vvithout the corresponding use of other features. Accordingly, while the present invention has been illustrated and described with respect to a specific embodiment, it is to be understood that numerous changes and modifications may be made therein vvithout departing from the spirit and scope of the invention as defined in the appended claims. LV 11061 CLAIMS: 1. A power plant including a two-stage steam turbine and a boiler combustion system that includes a combustor (12) and a convection pass section, vvherein a superheater (38) and a first and a second or final stage of reheater sequentially disposed in the gas flue (34), characterized by - the boiler system of fluidized bed combustor vvherein at least one separator (24) is disposed betvveen the boiler radiation and convective sections and further including means for dividing steam from the high pressure section of the two-staged turbine into selective first and second portions, and means (62) for recombining said steam portions, said former means providing directing said selective first steam portion to the first stage of the reheater and directing said selective second steam portion to the recombination means (62) placed at the inlet of the second stage of reheater and connected to the outlet of the first stage of the reheater. 2. A povver plant according to claim 1, characterized by - the superheater (38) being arranged dovvnstream of said second stage of reheater (40). 3. A povver plant according to claim 1, characterized by the means (54,64) for dividing the cold steam comprising a by-pass line (54) with at least one flow control valve (64), for by-passing a selected portion of cold steam from a turbine around the first stage of reheater (42) directly to the second or final stage of reheater (40). 4. A povver plant according to claim 1, characterized by at least one pressure control valve (56) at the inlet to the first stage of reheater (42), the valve being responsive to the difference betvveen the return steam pressure and the outlet steam pressure of the first stage of reheater. 5. A power plant according to claim 1, characterized by the means (64) for dividing the cold steam being responsive to outlet temperature of the second stage of reheater (40). 6. A method of controlling reheater temperatures in a steam generator having a two-staged steam turbine and a first and second stage of reheater in a common convection pass section, whereby the cold steam at the inlet to the first stage of reheater at a juncture is divided into two steam portions, the first steam portion being directed to the first stage of reheater and the second steam portions being directed through a bypass line around the first stage of reheater to the inlet of the second stage of reheater, characterized by the flow rāte of the first steam portion being controlled by a first flow control valve (56) arranged betvveen the juncture and the first stage reheater and the flow rāte of the second steam portion being controlled by a second flow control valve (64) arranged in the bypass. 7. A method according to claim 6, characterized by the second flow rāte control valve, being controlled by temperature control unit (82), responsive to the temperature of the outlet steam of the second or final stage of reheater. 8. A method according to claim 6, characterized by the first flow rāte control valve, being controlled by a pressure control unit (82), responsive to the pressure difference betvveen the return steam pressure and the outlet steam pressure of the first stage reheater.

Claims (8)

LV 11061 IERĪCE UN PAŅĒMIENS ŪDENS TVAIKA UZKARSĒŠANAS TEMPERATŪRAS REGULĒŠANAI KATLOS AR CIRKULĒJOŠU VERDOŠO SL4NI Izgudrojuma formula 1. Spēka iekārta, kas satur divpakāpju tvaika turbīnu un kurināmā sadedzināšanas sistēmu - katlu ar sadedzināšanas kameru (12) un konvektīvu caurplūdes posmu, kur pārkarsētājs (38) un tvaika sildītāja pirmā un otrā jeb pēdējā pakāpe ir secīgi uzstādīti dūmgāzu kanālā (34), atšķiras ar to, ka kurināmā sadedzināšanas sistēma satur katlu ar verdošā slāņa sadedzināšanas kameru, vismaz vienu separātoru (24), kas ir novietots starp katla radiācijas daļu un konvekcijas daļu, un papildus - ierīci no divpakāpju turbīnas augstspiediena sekcijas plūstošā tvaika sadalei izvēlētā pirmajā un otrajā daļā un ierīci (62) minēto tvaika daļu apvienošanai, pie kam minētā pirmā ierīce nodrošina izvēlētās pirmās tvaika daļas aizvadīšanu uz tvaika sildītāja pirmo pakāpi un izvēlētās otrās tvaika daļas aizvadīšanu uz apvienošanas ierīci (62), kas ir novietota pie tvaika sildītāja otrās pakāpes ieplūdes un savienota ar tvaika sildītāja pirmās pakāpes izplūdi.EN 11061 APPARATUS AND METHOD FOR ADJUSTING WATER PIPE SURFACE TEMPERATURE BOILERS WITH CIRCULAR VENTILATION SL4NI The invention 1. A power plant comprising a two-stage steam turbine and a combustion system - a boiler with a combustion chamber (12) and a convection flow stage, wherein the overheating (38) and the first and second or last stages of the steam heater are successively mounted in the flue gas channel (34), characterized in that the fuel combustion system comprises a boiler with a boiling chamber combustion chamber, at least one separator (24) positioned between the radiation portion of the boiler and the convection part and, in addition, a device for distributing the vapor vapor of the two-stage turbine high pressure section in the first and second parts selected and combining the device (62) with said steam portions, said first device providing removal of the first steam portion selected to the first stage of steam heater and selection removing the second vapor portion to the combining device (62) positioned at the second stage of the steam heater and connected to the first stage of the steam heater. 2. Spēka iekārta saskaņā ar 1.punktu, kas atšķiras ar to, ka tvaika pārkarsētājs (38), ir uzstādīts zemāk nekā tvaika sildītāja otrā pakāpe (40) plūsmas virzienā. -2-2. A power unit according to claim 1, wherein the vapor heater (38) is mounted lower than the second stage (40) of the steam heater in the direction of the flow. -2- 3. Spēka iekārta saskaņā ar 1.punktu, kas atšķiras ar to, ka aukstā tvaika sadales ierīces (54,64) satur apvedcauruļvadu (54) ar vismaz vienu tvaika plūsmas regulēšanas vārstu (64), lai aizvadītu izvēlētu daļu no turbīnas plūstošā aukstā tvaika apkārt tvaika sildītāja pirmajai pakāpei (42) tieši uz tvaika sildītāja otro jeb pēdējo pakāpi (40).3. A power plant according to claim 1, characterized in that the cold steam distribution means (54,64) comprises a bypass pipe (54) with at least one steam flow control valve (64) to remove a selected portion of the turbine flowing cold steam. around the first stage (42) of the steam heater directly to the second or last stage (40) of the steam heater. 4. Spēka iekārta saskaņā ar 1.punktu, kas atšķiras ar to,ka vismaz viens tvaika spiediena regulēšanas vārsts (56) ir uzstādīts pie tvaika sildītāja pirmās pakāpes (42) ieplūdes un regulē atplūdes tvaika spiediena un tvaika sildītāja pirmās pakāpes izplūdes tvaika spiediena starpību.4. A power plant according to claim 1, characterized in that at least one steam pressure control valve (56) is mounted at the inlet of the first stage (42) of the steam heater and regulates the difference between the return steam pressure and the first stage steam vapor pressure of the steam heater . 5. Spēka iekārta saskaņā ar 1.punktu, kas atšķiras ar to, ka satur ierīci (64) aukstā tvaika sadalei, kura regulē tvaika sildītāja otrās pakāpes (40) izplūdes tvaika temperatūru.5. A power plant according to claim 1, characterized in that it comprises a device (64) for distributing cold vapor, which regulates the vapor temperature of the second stage (40) of the steam heater. 6. Paņēmiens tvaika sildītāja temperatūru regulēšanai tvaika ģenerātorā, kas satur divpakāpju tvaika turbīnu un tvaika sildītāja pirmo un otro pakāpi kopējā konvektīvā caurplūdes posmā, pie kam aukstais tvaiks pie tvaika sildītāja pirmās pakāpes ieplūdes, savienojuma vietā tiek sadalīts divās tvaika plūsmas daļās, no kurām pirmo daļu ievada tvaika sildītāja pirmajā pakāpē un otro- pa apvedcauruļvadu aizvada apkārt tvaika sildītāja pirmajai pakāpei līdz tvaika sildītāja otrās pakāpes ieplūdei, atšķiras ar to, ka pirmās tvaika daļas patēriņu regulē ar pirmo plūsmas regulēšanas vārstu (56), kurš ir uzstādīts starp savienojuma vietu un tvaika sildītāja pirmo pakāpi un otrās tvaika daļas patēriņu regulē ar otru plūsmas regulēšanas vārstu (64), kurš ir uzstādīts apvedcauruļvadā.6. A method for regulating the temperature of a steam heater in a steam generator comprising a two-stage steam turbine and a first and second stage of a steam heater at a common convection flow stage at which the cold steam at the first-stage inlet of the steam heater is divided into two portions of the vapor stream from which the first a portion of the vapor heater is introduced in the first stage and the second passage is led around the first stage of the steam heater to the second stage of the steam heater, characterized in that the consumption of the first steam portion is controlled by the first flow control valve (56) mounted between the connection point and the first stage of the steam heater and the consumption of the second steam section are controlled by a second flow control valve (64) mounted in the bypass pipe. 7. Paņēmiens saskaņā ar 6.punktu, kas atšķiras ar to,ka satur otro tvaika patēriņa regulēšanas vārstu, kuru kontrolē ar temperatūras regulēšanas bloku (82), kurš regulē temperatūru tvaika sildītāja otrās jeb pēdējās pakāpes izplūdes tvaikam.7. A method according to claim 6, comprising a second steam control valve controlled by a temperature control unit (82) regulating the temperature of the second or last stage of the steam heater. 8. Paņēmiens saskaņā ar 6.punktu, kas atšķiras ar to, ka satur pirmo tvaika patēriņa regulēšanas vārstu, kuru kontrolē ar spiediena starpības regulēšanas bloku (82), kurš regulē atplūdes tvaika spiediena un tvaika sildītāja pirmās pakāpes izplūdes tvaika spiediena starpību.Method according to claim 6, characterized in that it comprises a first steam consumption control valve controlled by a differential pressure control unit (82) which controls the difference between the return steam pressure and the vapor pressure of the first stage of the steam heater.