Method and system in a paper machine and software product
View Patent ↗The invention comprises a method and a system in a paper machine, and also a software product, allowing one or more tools to be generated for indicating the state of the paper production process in terms of energy consumption to the operating staff of the paper machine. This allows continual monitoring of the state of the paper production process and/or its energy efficiency combined with efforts to develop the manners of running the paper machine and its dryer section in a more favourable direction. In one embodiment of the invention, the dry solids content DSC of the press section can be calculated by means of the evaporation amount of the dryer section, the production of finished paper and the final paper moisture as follows: DSC=m pap,d /(m pap,d +m H2O ), in which m pap,d is the dry mass flow of the paper web to the dryer section and m H2O is the water mass flow to the dryer section. m H2O is obtained by summing up the mass flow of the water discharged from the dryer section and the evaporated water mass flow.
1. A method for determining a dry solids content of a web passing from a press section to a dryer section of a paper machine, the method comprising:
measuring a dry mass flow m pap,d of the paper web;
measuring a water mass flow contained in the web leaving a dryer section;
measuring a temperature of the exhaust air from a hood;
measuring a moisture of the exhaust air from the hood;
measuring an amount of exhaust air from the hood;
calculating a water mass flow m ev evaporated from the web in the dryer section based upon the temperature, moisture and amount of exhaust air from the hood;
calculating a mass flow m H2O of water contained in the web passing from the press section to the dryer section by summing up the water mass flow contained in the web leaving the dryer section and the water mass flow of the water m ev evaporated from the web in the dryer section; and
calculating the dry solids content DSC of the web passing from the press section to the dryer section by the formula: DSC=m pap,d /(m pap,d +m H2O ).
2. The method according to claim 1 , wherein the dry solids content DSC of the web passing from the press section to the dryer section is compared with predetermined limit values, the comparison allowing indication of the value of the dry solids content DSC relative to said limit values on a user interface provided in connection with the paper machine.
3. The method according to claim 2 , wherein a gauge is displayed on the user interface of the paper machine with areas of different colours and an indicator indicating these areas, each area of different colour being disposed to illustrate the value of the dry solids content DSC within a range between given predetermined limit values.
4. A computer readable medium encoded with a computer program executable by a computer to perform the steps of the method according to claim 3 .
5. A computer readable medium encoded with a computer program executable by a computer to perform the steps of the method according to claim 2 .
6. The method according to claim 2 , wherein determination of the limit values is made by at least one of empirical, mathematical and statistical means.
7. The method according to claim 1 , wherein operation of the paper machine is controlled based upon the calculated dry solids content DSC of the web passing from the press section to the dryer section.
8. The method according to claim 6 , wherein felt or wire replacement shutdowns are timed based upon the calculated dry solids content DSC of the web passing from the press section to the dryer section.
9. A computer readable medium encoded with a computer program executable by a computer to perform the steps of the method according to claim 8 .
10. A computer readable medium encoded with a computer program executable by a computer to perform the steps of the method according to claim 7 .
11. A computer readable medium encoded with a computer program executable by a computer to perform the steps of the method according to claim 1 .
12. The method according to claim 1 , wherein the calculated dry solids content DSC is used as an indicator of at least one of an error, a malfunction, and a required service.
13. The method according to claim 1 , wherein the calculated dry solids content DSC after the press section is used for adjustment of settings at the wet end of the paper machine.
14. The method according to claim 1 , wherein at least one of the settings adjusted is pressure in a dewatering device, chemical feed rate, linear pressure in the press, and press steam box parameters.
15. A system for determining a dry solids content of a web passing from a press section to a dryer section of a paper machine, the system comprising:
means for receiving a value of a dry mass flow m pap,d of the paper web;
means for receiving a value of a water mass flow contained in the web leaving the dryer section;
means for measuring a temperature of an exhaust air from a hood;
means for measuring a moisture of the exhaust air from the hood;
means for measuring an amount of the exhaust air from the hood;
means in the dryer section for calculating a water mass flow of the water evaporated from the web based upon the temperature, moisture and amount of exhaust air from the hood;
means for calculating a water mass flow of the water m H2O contained in the web passing from a press section to the dryer section by summing up the water mass flow of the water contained in the paper leaving the dryer section and the water mass flow of the water evaporated from the web in the dryer section; and
means for calculating the dry solids content DSC of the web passing from the press section to the dryer section by the formula: DSC=m pap,d /(m pap,d +m H2O ).
16. The system according to claim 15 , further comprising:
a paper machine user interface;
a gauge disposed in the user interface for indicating the value of the dry solids content DSC;
means for comparing the dry solids content DSC of the web passing from the press section to the dryer section with predetermined limit values; and
means for indicating the value of the dry solids content DSC in the gauge of the paper machine user interface compared to said limit values.
17. The system according to claim 16 , wherein the gauge comprises areas of different colours, each area of different colour being disposed to illustrate the value of the dry solids content DSC in a range between given predetermined limit values, and an indicator disposed to indicate said areas.
18. The system according to claim 15 , further comprising means for controlling operation of the paper machine based upon the calculated dry solids content DSC of the web passing from the press section to the dryer section.
19. A method for determining efficiency of heat recovery in a paper machine, comprising:
calculating a heat recovery heat flow Q rec ;
calculating a heat flow Q pw required for heating a flow of process water consumed during heating of fresh water to the temperature required for a process;
calculating a heat flow Q MR required for heating ventilation air of machine room ventilation;
calculating a heat flow Q sup required for heating supply air of a dryer section;
calculating an evaporation amount m ev of the dryer section;
determining a dimensioned evaporation amount in the dyer section m ev, dim ; and
calculating the heat recovery efficiency EFF rec by the formula:
EFF rec =( Q rec /( Q pw +Q MR +Q sup ))*( m ev, dim /m ev ).
20. The method according to claim 19 , further comprising:
measuring a temperature of the exhaust air from a hood;
measuring a moisture of exhaust air from the hood;
measuring an amount of exhaust air from the hood; and
calculating an evaporation amount m ev of the dryer section based upon the temperature, moisture and amount of exhaust air from the hood.
21. A computer readable medium encoded with a computer program executable by a computer to perform the steps of the method according to claim 20 .
22. A computer readable medium encoded with a computer program executable by a computer to perform the steps of the method according to claim 19 .
23. The system according to claim 19 , further comprising a user interface, which is provided with a main level including one or more main variables relevant for the energy use of the paper machine dryer section and the runnability systems, said main variables comprising one or more of:
an overall specific heat energy consumption of the paper machine;
a specific heat energy consumption of the dryer section;
a specific heat energy consumption of the evaporation;
a heat recovery efficiency;
a dry solids content after the press;
a heat flow of the secondary condenser; and
an indicator of the operation of the runnability components.
24. The system according to claim 23 , further comprising a gauge for each main variable, the gauge comprising red, yellow and green areas as symbols of a good, passable and poor values of the variable measured.
25. The system according to claim 24 , wherein the user interface is provided with one or more supplementary pages in the monitoring system for displaying information about the state of at least one of the paper machine and its dryer section by using supplementary variables comprising one or more of:
fouling degree of the heat recovery;
underpressure or overpressure of a hood false ceiling space of the dryer section;
secondary/primary heat flow ratio; and
pressure difference of a process water heat exchanger or heat exchangers in heat recovery.
26. The system according to claim 23 , wherein the user interface is provided with one or more supplementary pages in the monitoring system for displaying information about the state of at least one of the paper machine and its dryer section by using supplementary variables comprising one or more of:
fouling degree of the heat recovery;
underpressure or overpressure of a hood false ceiling space of the dryer section;
secondary/primary heat flow ratio; and
pressure difference of a process water heat exchanger or heat exchangers in heat recovery.