Abstract:
The invention relates to a method and a device for treating contaminated water in a steam power installation, and to a corresponding steam power installation. According to the invention, steam and water are separated between a first steam-collecting drum of a pressure level and a second steam-collecting drum of a lower pressure level.

Description:
CROSS REFERENCE TO RELATED APPLICATIONS 
     This application is the U.S. National Stage of International Application No. PCT/EP2004/010899, filed Sep. 29, 2004 and claims the benefit thereof. The International Application claims the benefits of European Patent application No. 04001043.1 filed Jan. 20, 2004. All of the applications are incorporated by reference herein in their entirety. 
     FIELD OF THE INVENTION 
     The present invention relates to a method and device for treating contaminated water in a steam power plant. The present invention also relates to a steam power plant. 
     BACKGROUND OF THE INVENTION 
     Such a steam power plant generally contains a number of steam drums, with which steam is generated at different power levels, it being possible to feed said steam to a steam turbine in particular. Impurities in the water/steam circuit of the steam power plant must be removed. The impurities become more concentrated in the respective steam drum. The extraction of saturated steam from the steam drums causes non-volatile substances to remain in the steam drums. These non-volatile substances are removed from the circuit by elutriation. The circuit thereby loses energy and water, which has to be fed back in again in the form of additional water, known as deionized water. This incurs additional costs. It is also an environmental burden. 
     To keep energy losses low, it has already been proposed that the elutriation water should be transferred from the high-pressure level steam drums to the lower-pressure steam drums, in which it can expand (so-called boiler cascading blowdown). Some of the energy of the additionally introduced elutriation water can then be converted to power by evaporating it and routing the steam thus obtained to the steam turbine. One disadvantage of this is however that all the impurities are transferred from one pressure level to the next. 
     It is also known that the elutriated water in the steam drum of one pressure level can be expanded in a separator and the water and steam separated. The steam is then transferred at low pressure into a collection tank for degassing and to heat up the water contained therein. 
     SUMMARY OF THE INVENTION 
     The object of the invention is to allow contaminated water in a steam power plant with a number of pressure levels to be purified in a technically simple and effective manner. 
     This object is achieved according to the invention with a method and device for treating contaminated water in a steam power plant, wherein a water-steam separation operation takes place between a first steam drum of a first pressure level and a second steam drum of a lower second pressure level. The object is also achieved with a steam power plant, having an inventive device. The present invention allows the frequency of elutriation to be reduced compared with the prior art. It also allows the quantity of elutriation water to be disposed of and the consumption of deionized water supplied to be kept at a low level. 
     In one advantageous development of the invention, separated, contaminated water is fed to a collection tank for further processing during the water/steam separation operation. The elutriation water removed from a number of steam drums is thus collected centrally and then processed. The volume of the collection tank can be kept low. 
     Steam separated during the water/steam separation operation is advantageously fed to the second steam drum. This allows particularly good energy utilization, which ultimately results in an increase in the power that can be generated by the steam power plant. 
     In one advantageous embodiment of the invention the water/steam separation operation takes place between a third steam drum of a third pressure level, which is higher than the first pressure level, and the second steam drum. This allows elutriation to take place more effectively. 
     In a particularly advantageous embodiment of the invention a further water/steam separation operation takes place between the third steam drum and the first steam drum. Further inspissation (concentration) allows the elutriation flow to be reduced. Also the quantity of elutriation water to be disposed of and the consumption of deionized water supplied can be kept at a low level. 
     Steam separated in the further water/steam separation operation is advantageously fed to the first steam drum. This allows a further better utilization of energy. 
     Contaminated water separated during the further water/steam separation operation is fed into the first water/steam separation operation. The separated contaminated water can therefore be subjected to a double water/steam separation operation, allowing more energy to be recycled. 
     It is particularly advantageous for the water/steam separation operation to take place in a separator. This allows water and steam to be separated in a particularly simple and economic manner. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWING 
       An exemplary embodiment of the invention is described in more detail below with reference to the accompanying schematic drawing, in which: 
       The FIGURE shows an exemplary embodiment of an inventive device for treating contaminated water in a steam power plant. 
     
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     The FIGURE shows an inventive device in the form of a purification device  1 , which is part of a steam power plant for power generation. To simplify the representation, elutriation paths in particular are shown from the steam power plant, which serve to remove elutriation water that occurs during the elutriation of steam drums of the steam power plant. 
     Within the steam power plant a high-pressure (HP) steam drum  3  is provided with an HP pressure level, a medium-pressure (MP) steam drum  4  is provided with an MP pressure level, which is lower than the HP pressure level, and a low-pressure (LP) pressure drum  5  is provided with an LP pressure level, which is lower than the MP pressure level. The steam drums  3 ,  4 ,  5  are used during operation of the steam power plant to generate steam from water contained in the steam drums  3 ,  4 ,  5 , in each instance in an evaporator (not shown). This steam is fed via superheaters assigned to the steam drums  3 ,  4 ,  5  to one or more turbines in the steam power plant  2 . The steam drums  3 ,  4 ,  5  therefore each have an upper outlet  6 ,  7  or  8 , at which the steam can exit from the different pressure levels. 
     For the purposes of purification the steam drums  3 ,  4 ,  5  are elutriated. To this end they each have a lower outlet  9 ,  10  or  11 , at which the concentrated, contaminated water from the steam drums  3 ,  4  or  5  is partially elutriated. The steam drums  3 ,  4 ,  5  are connected to each other via the elutriation lines mentioned above. 
     In order on the one hand to prevent elutriated impurities also being carried along in the elutriation path from one steam drum to the next and on the other hand to ensure that energy still contained in the elutriated water is largely utilized, the elutriation water is subjected to a water/steam separation operation. To this end a separating means in the form of a medium-pressure separator flask  12  is disposed in the elutriation path from the HP steam drum  3  to the MP steam drum  4 , allowing a water/steam separation operation in the MP pressure level. The medium-pressure separator flask  15  has an inlet  13 , which is connected to the lower outlet  9  of the HP steam drum  3  via an elutriation line. Elutriation water can be routed from the HP steam drum into the medium-pressure separator flask  12  via this elutriation line. The elutriation water can evaporate in the medium-pressure separator flask  12  according to the MP pressure level. The medium-pressure separator flask  12  has an upper outlet  14 , which is connected to an inlet  15  of the MP steam drum  4 . The steam separated in the medium-pressure separator flask  12  can be routed via this connection for recycling in the MP steam drum  4 . 
     The medium-pressure separator flask  12  also has a lower outlet  16 , which is connected via an elutriation line and a valve to an inlet  17  of a separating means in the form of a low-pressure separator flask  18 , which makes a water/steam separation operation possible in the LP pressure level. Separated contaminated water can be routed into the low-pressure separator flask  18  via this lower outlet  16 , so that said water can be subjected to the LP water/steam separation operation there. The lower outlet of the MP steam drum  4  is also connected via an elutriation line and a valve to the inlet  17  of the low-pressure separator flask  18 , to introduce elutriated water. The elutriation water fed in can evaporate in the low-pressure separator flask  18  according to the LP pressure level. 
     The low-pressure separator flask  18  has an upper outlet  19 , which is connected to an inlet  20  of the LP steam drum  5  for the introduction of separated steam. The low-pressure separator flask  18  also has a lower outlet  21 , which is connected via an elutriation line and a valve to an inlet  22  of a collection tank  23  for the introduction of the separated contaminated water. The inlet  22  of the collection tank  23  is also connected via an elutriation line to the lower outlet  11  of the LP steam drum, to feed elutriated water from the LP steam drum to the collection tank  23 . The collection tank  23  collects the contaminated separated elutriation water that is not further used and expands it there. The collection tank  23  has an upper outlet  24 , at which steam is released either to the atmosphere or to a condenser (not shown), and a lower outlet  25 , at which the remaining waste water condensate with the further concentrated impurities is disposed of from the circuit or reprocessed. 
     In the above exemplary embodiment two separator flasks  12  and  18  were advantageously used. It is also possible to provide just one or a number of these separator flasks. If only the low-pressure separator flask  18  is provided, the outlet  9  of the HP steam drum  3  is connected directly to the inlet  17  of the low-pressure separator flask  18 , to introduce elutriated water.