EP1266182A1 - A device and a method for transferring heat and use thereof - Google Patents
A device and a method for transferring heat and use thereofInfo
- Publication number
- EP1266182A1 EP1266182A1 EP01918055A EP01918055A EP1266182A1 EP 1266182 A1 EP1266182 A1 EP 1266182A1 EP 01918055 A EP01918055 A EP 01918055A EP 01918055 A EP01918055 A EP 01918055A EP 1266182 A1 EP1266182 A1 EP 1266182A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- medium
- heat
- flow
- transferring member
- heat transferring
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/003—Feed-water heater systems
Definitions
- the present invention relates to a device for transferring heat, comprising a first member for transferring heat from a first medium flowing in a first circuit, to a second medium flowing in a second circuit, and a method for transferring heat, in which heat is transferred from a first flowing medium to a second flowing medium by means of a first heat transferring member, and use thereof.
- the invention is applicable in heating of different mediums in several technical applications, but for illuminating, but not in any way restricting the invention, from now the application when so called boiler feed water for steam production is to be heated before it is supplied to the steam generating step of the process will be described , which step is desired within the pulp and paper industry for instance.
- the recovery condensate When producing steam for use in different process steps within the pulp and paper industry and the following use of the steam, about two thirds of the water quantity which is consumed for generation of the steam required may be reused in the state of a so called recovery condensate.
- the recovery condensate must be deluted by approximately 50% further water for maintaining the water quantity required for the steam production.
- the recovery condensate as well as the added water, which together constitute the boiler feed water have to be puri- fied by filtration so as to provide for the high degree of purity which is demanded for as regards the water which is supplied to one or more steam boilers.
- the boiler feed water has such a high temperature as possible when being supplied to the steam boiler.
- a first object of the present invention is to provide a device of the type defined in the introduction, which reduces the above discussed problems of such already known devices to a great extent.
- the device comprises a second member for transferring heat from a third medium to said second medium and a means arranged to divide the flow of the second medium into a first flow part flowing through the first heat transferring member in a first circuit part and into a second flow part flowing through the second heat transferring member in a second circuit part and adapt the size of said first flow part to the size of the flow of the first medium flowing through the first heat transferring member so as to reduce the loss of exergy at the first heat transferring member and increase the temperature of the second medium.
- the first heat transferring member may be used with a minimum of exergy losses through adaption of the size of the flow of the second medium which passes through the first heat transferring member, to the flow of the first medium which passes through the first heat transferring member while a part of the second medium being heated by another source of heat, i.e.
- a third medium deriving from for example a waste heat source, so that the second medium, in a possible mixture of the first and the second flow part, gets a higher temperature than what would be the case if only the first heat transferring member was used and the whole flow of the second medium would be brought to flow through the first heat transferring member.
- the third medium has usually a lower temperature than the first medium.
- the basic principle is that equal mass flows at the primary and secondary side of the first heat trans- ferring member minimizes the loss of exergy when the heat is transferred, on condition that the first and the second medium have substantially the same specific heat capacity.
- the device includes a means connecting the first and the second circuit, arranged downstream the first heat transferring member in relation to the flow direction of the first medium, and upstream said dividing means in relation to the flow direction of the second medium, to bring the first medium and a fourth medium flowing to the intermixing means together, the first and the fourth medium being arranged to jointly constitute at least a portion of the second medium.
- a fourth medium for example fresh water
- the first medium for example a recovery condensate
- the device comprises a third member for transferring heat from said third medium to the fourth medium, which member is arranged upstream the intermixing means in relation to the flow direction of the fourth medium .
- the third heat transferring member makes it possible to use the third medium, for example a hot flow of waste heat from a bleachery, such as an EOP filtrate, for heat- ing the fourth medium, for example a fresh water, so that the highest temperature allowed of the second medium immediately after the intermixing medium may be obtained also during conditions when the fourth medium before heating has a proportionately low temperature and/or when the first medium before in- termixing with the fourth medium has a proportionately low temperature or a low flow.
- a bleachery such as an EOP filtrate
- the dividing means is arranged to adapt the size of said first flow part so that this flow is substantially as big as the flow of the first medium.
- This embodiment is especially suitable in the case when the first and the second medium have substantially the same specific heat capacity since equal flows in combination with the same specific capacity of the two mediums will result in an optimum heat transferring, as regards the lowest possible loss of exergy, from the first medium to the second medium at the first heat transferring member.
- a second object of the present invention is to provide a method of the type defined in the introduction, which method reduces the above discussed problems of already known such methods to a large extent.
- This second object is obtained according to the invention through that heat is transferred from a third medium to said second medium by means of a second heat transferring member by the fact that the flow of said second medium is divided into a first flow part which is heated by the first medium at the first heat transferring member and into a second flow part which is heated by the third medium at the second heat transferring member and that the size of said first flow part is adapted to the size of the flow of the first medium flowing through the first heat transferring member so that the loss of exergy at the first heat transferring member is reduced and the temperature of the second medium is increased.
- the invention also relates to the use of a device according to the invention and/or a method according to the invention for heating water for steam production.
- Fig 1 is a schematical illustration of a system for preheating of boiler feed water in accordance with the state of art
- Fig 2 is a schematical illustration of an alternative system for preheating of boiler feed water
- Fig 3 is a schematical illustration of a device according to the invention.
- Fig 4 is a schematical illustration of a variant of the device according to the invention
- Fig 5 is a schematical illustration of a further variant of the device according to the invention shown in a part view.
- Fig 1 a system for preheating of boiler feed water intended for steam production is illustrated.
- the system is designed in ac- cordance with already known art used in the paper and pulp industry.
- a heat exchanger 1 is arranged for transferring heat from a recovery condensate 2 flowing in a first circuit 3, to a boiler feed water 4 flowing in a second circuit 5.
- the recovery condensate 2 is constituted by reused condensated steam from differ- ent steps in the process which require the use of steam.
- the recovery condensate 2 by emitting of heat, is brought to a lower temperature, preferably in the order of 25-50°C at a position 8 downstream the heat exchanger 1 and the boiler feed water 4 is brought to a higher temperature, preferably in the or- der of 60-80°C, at a position 9 downstream the heat exchanger 1 .
- the boiler feed water is pumped by means of a pump 15 to one or more boiler feed water tanks 10 and further to one or more boilers for steam production, for example soda, oil and/or bark boilers, which steam is used in different steps of the process in producing pulp and/or paper. From these process steps a part of the cooled steam is reused and brought back, as mentioned above, in the shape of the recovery condensate 2 to be used as a part of the boiler feed water 4.
- the recovered amount of recovery condensate is not enough for maintaining the required boiler feed water quantity and thus further water must be added .
- fresh water 1 1 is usually used, which is mixed with the recovery condensate 2 in a mixing tank 12. To avoid salt precipitation in the following steam production the fresh water 1 1 undergoes one or more deionisation steps as regards cations and anions in an ion exchanger arrangement 13 before the fresh water 1 1 reaches the mixing tank 12.
- the water flowing from the mixing tank 12 thus constitutes the boiler feed water 4, but before this may be used for steam production it has to be purified further by filtration, the remaining impurities being removed in a filtering equipment 14 and there- after heated by the recovery condensate 2 through the heat exchanger 1 as previously described.
- the pump 15 is suitably used for bringing the boiler feed water to flow to the boiler feed water tanks 10.
- the pump 15 often with advantage may be arranged upstream the filtering equipment 14 in relation to the flow direction of the boiler feed water 4, i.e. between the mixing position 12 and the filtering equipment 14, so as to press in- stead of sucking, the boiler feed water 4 through the filtering equipment 14 and therethrough avoid the risk of cavitation in the filtering equipment 14.
- a device according to the invention for transferring heat comprises a first member 1 for transferring heat from a first medium 2 flowing in a first circuit 3, to a second medium 4 flowing in a second circuit 5. Furthermore, the device comprises a second member 16 for transferring heat from a third medium 17 to said second medium 4 and a means 18 arranged to divide the flow of the second medium 4 into a first flow part 19 flowing through the first heat transferring member 1 in a first circuit part 20 and into a second flow part 21 flowing through the second heat transferring member 16 in a second circuit part 22.
- the dividing means 18 is in this connection arranged to adapt the size of said first flow part 19 to the size of the flow of the first medium 2 flowing through the first heat transferring member 1 .
- the illustrated embodiment of the device according to the invention includes a means 12 which connects the first 3 and the second 5 circuit and which is arranged downstream the first heat transferring member 1 in relation to the flow direction of the first medium 2, and upstream said dividing means 1 8 in relation to the flow direction of the second medium 4, to bring the first medium 2 and the fourth medium 1 1 flowing to the intermixing means 12 together, the first 2 and fourth 1 1 medium being arranged to jointly constitute the second medium 4.
- Such a device may for example be used for solving the problems discussed in the introduction when heating boiler feed water in the pulp and paper industry.
- the first and the second heat transferring members are preferably heat exchangers of the counter flow type, the first medium a re- covery condensate, and the second medium boiler feed water and the fourth medium is preferably fresh water.
- an arrangement 14 for purifying and/or filtrating the second medium 4 is arranged between the intermixing means 12 and the dividing means 18.
- the fil- tering arrangement 14 is a mixed bed filter.
- a third medium originates preferably from some other waste heat source present in the manufacturing process.
- a so-called EOP-filtrate from a bleachery arrangement may for example be used, since this filtrate is a residual product from the bleachery, which in some cases is available and is not used as a heat source, but is simply removed from the process through an outlet.
- a required feature of the third medium 17 is that it has a temperature which exceeds the temperature of the second medium 4 so that heat may be transferred from the third medium 1 7 to the second medium 4.
- the third medium 17 could be any energy source which is able to heat the second medium 4 in a sufficient way and the second heat transferring member 16 could be of any kind, in the embodiment example the third me- dium 17 is a fluidum arranged to flow in a third circuit 23 and the second heat transferring member 16 is a heat exchanger.
- the recovery condensate 2 i.e. condensated water steam
- the recovery condensate 2 flows in the first circuit 3 to the first heat exchanger 1 where the recovery condensate 2 emits heat to the boiler feed water 4.
- the recovery condensate is brought to flow to the mixing tank 12.
- fresh water 1 1 is added to the mixing tank 12.
- the added fresh water quantity varies depending upon the present flow of the recovery condensate 2 which in its turn depends on to which extent steam may be reused in the process 35 for the rest.
- fresh water 1 1 corresponding to approximately half the flow of the recovery condensate is required.
- the temperature of the fresh water 1 1 may vary in high degree depending upon the present season etc.
- the flow and the temperature of the recovery condensate 2 may vary, and therefore it has to be seen to that the boiler feed water 4, when leaving the mixing tank 12 for flowing in the second circuit 5, does not have a too high temperature when it reaches the mixed bed filter 14.
- the purpose of the mixed bed filter 14 is to purify the boiler feed water 4 before this is used for steam production and this purifying and/or filtrating step requires that the boiler feed water 4 has a temperature not exceeding approximately 50°C. This means that the boiler feed water 4 immediately after the mixing tank 12 often has a temperature in the order of 1 5-45°C.
- the intermixing means 12 does not necessarily have to include a vessel, such as a feed water mixing tank, in all applications, but in some cases it may for example be a three-way pipe coupling , with or without valves, for connecting the conduits of the first and the fourth medium to the conduit of the second medium, so as to bring the first and the fourth medium together to constitute at least a portion of the second medium.
- a vessel such as a feed water mixing tank
- the intermixing means 12 does not necessarily have to include a vessel, such as a feed water mixing tank, in all applications, but in some cases it may for example be a three-way pipe coupling , with or without valves, for connecting the conduits of the first and the fourth medium to the conduit of the second medium, so as to bring the first and the fourth medium together to constitute at least a portion of the second medium.
- other available and suitable mediums may be brought to the intermixing means to constitute a portion of the second medium.
- the boiler feed water is pumped further to the dividing means 18 which for example is constituted by an adjustable three-ways valve, for division in the first flow part 1 9 and in the second flow part 21 .
- the first flow part 19 flows in the first circuit part 20 to the first heat exchanger 1 and further to the boiler feed water tank/tanks 10.
- heat exchangers may be of so called counter flow type.
- the second flow part 21 flows in the second circuit part 22 to the second heat exchanger 16 and further to the boiler feed water tank/tanks 10.
- the first flow part 1 9 of the boiler feed water 4 is thus heated by the recovery condensate 2 at the first heat exchanger 1 and in this connection the size of the first flow part 19 is adapted to the size of the flow of the recovery condensate 2 by means of the valve 18 for obtaining an optimum heat transferring , i.e. heat transferring during conservation of the exergy, to the boiler feed water 4.
- the second flow part 21 is heated by the waste heat source, here EOP-filtrate 23, at the second heat exchanger 16. Cer- tainly, the optimum sizes of the flow parts 19, 21 are also depending upon the supply of for example EOP-filtrate and its energy contents and thus the flows 1 9, 21 are also adapted thereto. In many operation cases there are, however, plenty of EOP-filtrate with a temperature in the order of 70-75°C, which means that through adapting of the two flow parts 1 9, 21 so that the two heat exchangers 1 , 16 are well balanced, i.e.
- the medium which has the highest specific heat capacity should if possible have a lower flow than the other medium with lower specific heat ca- pacity for obtaining optimum heat transferring as regards the conservation of exergy.
- the mediums have different specific heat capacity the medium which has the highest specific heat capacity should if possible have a lower flow than the other medium with lower specific heat ca- pacity for obtaining optimum heat transferring as regards the conservation of exergy.
- no disadvantage if there is an excess of the third medium 17 so that this has a larger mass flow than the second flow part 21 .
- the device illustrated in Fig 3 has a means 24 arranged downstream the first heat transferring member 1 in relation to the flow direction of the first flow part 19, and downstream the second heat transferring member 16 in relation to the flow direction of the second flow part 21 , to connect the first 20 and the second 22 circuit part.
- the connection means 24 may be a pipe which connects the circuit parts 20, 22 so that communication therebetween is obtained, such as illustrated in Fig 3, or it may be a common pipe of the two circuit parts 20, 22 for bringing the two flow parts 19, 21 to flow in this pipe on the way to the boiler feed water tanks 10, as illustrated in Fig 5 for instance.
- the management of the flow parts 1 9, 21 downstream the heat exchangers 1 , 16 and possibly mixing of these for equalisation of temperature for instance and the number of boiler feed water tanks 1 0, may be varied to provide the current needs which are present for feeding the steam generating process step.
- the temperature of the boiler feed water is increased by means of steam received from the following steam generating step, which steam has a temperature of approximately 120-140°C, until the boiler feed water boils with the purpose of forcing oxygen present in the boiler feed water away.
- the part of this heating of the boiler feed water which may be performed by means of the device according to the invention, before the boiler feed water reaches the boiler feed water tanks, thus saves steam and therefore fuel. In this way the process may accordingly be performed in a way which involves lower costs.
- a variant of the device according to the invention is il- lustrated.
- the device comprises a third member 25 for transferring heat from the third medium 17 to the fourth medium 1 1 , which member is arranged upstream the intermixing means 12 in relation to the flow direction of the fourth medium 1 1 .
- the third heat transferring member 25 is arranged at the third circuit 23 downstream the second heat transferring member 16 in relation to the flow direction of the third medium 17.
- a means 26 is arranged by which means a desired part of the flow of the third medium 17 may be brought to flow to a position 27 at the third circuit 23 downstream the third heat transferring member 25 in relation to the flow direction of the third medium 17 without flowing through the third heat transferring member 25.
- the embodiment in Fig 4 means that the EOP-filtrate 17, if required, may be used to heat the fresh water 1 1 .
- the matter stand in a way that the highest temperature allowed, as regards the performance of the mixed bed filter, is desired to achieve in the mixing tank 12.
- the fresh water may be proportionately cold and looked at over the year the temperature may vary in the interval from some few °C to approximately 25°C.
- the EOP-filtrate After passing through the second heat exchanger 16 the EOP-filtrate has a temperature in the order of 25-50°C. The temperature variation depending on the size and the temperature of the present second flow part 21 , and the flow and the temperature of the EOP-filtrate upstream the heat exchanger 16. In this connection the EOP-filtrate 17 thus has a temperature sufficient to be used for heating the fresh water 1 1 too.
- the abovementioned by-pass means 26, including an adjustable three-ways valve and a pipe 29, is arranged so that, if required, a portion of or the whole EOP-filtrate may flow in the third circuit 23 without passing through the third heat exchanger 25.
- Fig 5 a part view of an alternative embodiment of the device according to the invention comprising an additional member 30 for transferring heat from an additional medium 31 to the second medium 4.
- the additional heat transferring member 30 is arranged downstream the second heat transferring member 16 in relation to the flow direction of the second flow part 21 .
- the other flow part 21 of the boiler feed water 4 may be heated further through heat transferring from the additional medium 31 , preferably a sometimes present heat source in the shape of a fluidum originating from so-called blowing of one or more steam generating boilers, at the additional heat transferring member 30.
- the additional heat transferring member 30 should instead be arranged downstream the first heat transferring member 1 in relation to the flow direction of the first flow part 19 with the purpose to further heat the first flow part 19 of the boiler feed water 4.
- the embodiment according to Fig 4 could be designed with a closed third circuit 23.
- an interstep fluidum could flow in the third circuit 23, preferably a very clean such fluidum, through which interstep fluidum heat would be transferred from the third medium, for example EOP-filtrate, to the second medium, for example boiler feed water, and possibly to a fourth medium, for example fresh water.
- one additional heat transferring member in the shape of for example a heat exchanger arranged at the third circuit 23 for transferring heat from the third medium, the EOP-filtrate, for instance, to the interstep fluidum, is suitably used.
- the advantage with such an embodiment is that the risk that contaminated fluidum will reach the clean boiler feed water is reduced.
- the fact is that it has to be secured to the utmost possible extent that the third medium, the EOP-filtrate for instance, which is usually very unclean, does not come into the boiler feed water pipe in the event of a possi- ble damage in for example a heat exchanger.
- controlling and regulating equipments 32, 33 are suitably used for controlling the dividing means 18 and regulating the two flow parts 19, 21 of the second medium 4, and for controlling the by-pass means 26 and regulating the amount of the third medium 17 which is by-passed the possible third heat transferring member 25 instead of through the same.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Steam Or Hot-Water Central Heating Systems (AREA)
- Central Heating Systems (AREA)
- Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
- Paper (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
Claims
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE0001062 | 2000-03-24 | ||
SE0001062A SE0001062D0 (en) | 2000-03-24 | 2000-03-24 | Preheating of feed water |
SE0004378A SE518085C2 (en) | 2000-03-24 | 2000-11-29 | Device and method for transferring heat and use thereof |
SE0004378 | 2000-11-29 | ||
PCT/SE2001/000624 WO2001073365A1 (en) | 2000-03-24 | 2001-03-23 | A device and a method for transferring heat and use thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1266182A1 true EP1266182A1 (en) | 2002-12-18 |
EP1266182B1 EP1266182B1 (en) | 2005-09-14 |
Family
ID=26655038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP01918055A Expired - Lifetime EP1266182B1 (en) | 2000-03-24 | 2001-03-23 | A device and a method for transferring heat and use thereof |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1266182B1 (en) |
AT (1) | ATE304690T1 (en) |
AU (1) | AU2001244926A1 (en) |
DE (1) | DE60113391T2 (en) |
ES (1) | ES2248301T3 (en) |
SE (1) | SE518085C2 (en) |
WO (1) | WO2001073365A1 (en) |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE347074C (en) * | 1970-06-08 | 1972-06-24 | J Lilljeqvist | |
US4137965A (en) * | 1975-07-21 | 1979-02-06 | John J. Fallon, Jr. | Waste heat recovery system |
US4318366A (en) * | 1980-04-01 | 1982-03-09 | Aqua-Chem, Inc. | Economizer |
US4489679A (en) * | 1983-12-12 | 1984-12-25 | Combustion Engineering, Inc. | Control system for economic operation of a steam generator |
US4745757A (en) * | 1987-02-24 | 1988-05-24 | Energy Services Inc. | Combined heat recovery and make-up water heating system |
US5045272A (en) * | 1990-02-16 | 1991-09-03 | Westinghouse Electric Corp. | Fluid temperature balancing system |
SE470194B (en) * | 1991-06-24 | 1993-11-29 | Sune Enar Holmstroem | Method of balancing two fluid flows which flow through a heat exchanger and arrangement for this |
BE1010594A3 (en) * | 1996-09-02 | 1998-11-03 | Cockerill Mech Ind Sa | Process for conducting the boiler boiler and forced circulation for its implementation. |
US5918570A (en) * | 1997-11-05 | 1999-07-06 | Greenwich Hospital | Deaerated feedwater supply system for a boiler system and a method for deaerating boiler feedwater |
DE19810357A1 (en) * | 1998-03-10 | 1999-09-16 | Olsberg Hermann Everken Gmbh | Ventilation heater |
-
2000
- 2000-11-29 SE SE0004378A patent/SE518085C2/en unknown
-
2001
- 2001-03-23 AU AU2001244926A patent/AU2001244926A1/en not_active Abandoned
- 2001-03-23 AT AT01918055T patent/ATE304690T1/en not_active IP Right Cessation
- 2001-03-23 EP EP01918055A patent/EP1266182B1/en not_active Expired - Lifetime
- 2001-03-23 DE DE60113391T patent/DE60113391T2/en not_active Expired - Lifetime
- 2001-03-23 ES ES01918055T patent/ES2248301T3/en not_active Expired - Lifetime
- 2001-03-23 WO PCT/SE2001/000624 patent/WO2001073365A1/en active IP Right Grant
Non-Patent Citations (1)
Title |
---|
See references of WO0173365A1 * |
Also Published As
Publication number | Publication date |
---|---|
SE0004378L (en) | 2001-09-25 |
SE518085C2 (en) | 2002-08-20 |
EP1266182B1 (en) | 2005-09-14 |
ES2248301T3 (en) | 2006-03-16 |
WO2001073365A1 (en) | 2001-10-04 |
DE60113391D1 (en) | 2005-10-20 |
ATE304690T1 (en) | 2005-09-15 |
SE0004378D0 (en) | 2000-11-29 |
AU2001244926A1 (en) | 2001-10-08 |
DE60113391T2 (en) | 2006-06-14 |
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