A drying apparatus for a rotary printing press

Abstract: In the drying apparatus for rotary printing press for drying the ink on the printed paper which has a direct fired deodorizing apparatus and a heat recovery apparatus for heating the hot air circulating in a drying apparatus by using the exhaust gas from the deodorizing apparatus, the drying apparatus and its control device are so adapted that a bypass line is installed on the hot air circulation line to bypass the heat recovery apparatus to control the temperature of printed paper and/or the temperature of hot air blowing from nozzles by adjusting the degree of opening of bypass damper disposed in the bypass line, and the burning amount of the burner for deodorization is controlled so that the deodorizing apparatus furnace temperature corresponding to the blowing hot air temperature or paper temperature is obtained. Further, the control device carries out the control in response to the change in printing speed. Thus, the control responsiveness can be enhanced.

Description: The invention relates to a drying control device for printed paper drying apparatus which evaporates the solvent in ink by blowing hot air onto the printed paper. More particularly it relates to a hot air heating type drying apparatus for a rotary printing press which evaporates the solvent in ink by feeding printed paper into a drying apparatus body having a negative pressure and by blowing hot air onto the paper. The apparatus, according to this invention can be applied to exhaust gas disposal apparatus for solvent-containing substances in the production process of plastic film and the like. Still more particularly, this invention relates to a paper temperature control device of drying apparatus for a rotary printing press. A conventional drying apparatus for a printing press will be described with reference to FIG. 5. Reference numeral 1 denotes a drying apparatus body, 2 denotes printed paper, 3 denotes a hot air blowing nozzle provided in the drying apparatus 1, 4 denotes a burner for heating the hot air, 5 denotes a blower for the first zone, 6 denotes a blower for the second zone, and 7 denotes an exhaust gas blower, and 8 denotes a deodorizing apparatus. The paper 2 printed by the printing press is fed into the drying apparatus body 1, and the hot air from the burner 4 is blown onto the paper through the hot air blowing nozzles 3 so that the solvent in ink is evaporated. The hot air, which has been blown onto the paper 2 in the drying apparatus body 1 from the hot air blowing nozzles 3, is returned to the suction side of the blower for the first zone 5 and the blower for the second zone 6, and is then reheated by the burner 4 and sent to the hot air blowing nozzles 3. Part of the hot air is sucked by the exhaust gas blower 7 and sent to the deodorizing apparatus 8, where the gas is deodorized. Part of the deodorized gas is returned to the drying apparatus body 1, and the remnant is discharged into the atmosphere. For pollution prevention, a negative pressure is produced in the drying apparatus body 1 to prevent the hot gas (exhaust gas) in the drying apparatus body 1 from discharging to the outside. The conventional drying apparatus for a rotary printing press shown in FIG. 5 has the following disadvantages: (1) The apparatus has a high consumption of fuel because the fuel supplied to the burner 4 is burned to reheat the hot air circulating in the drying apparatus body. (2) The operation cannot be performed while the amount of exhaust gas is restricted because if the concentration of solvent in the exhaust gas is raised by the restriction of exhaust gas discharged from the deodorizing apparatus 8, the temperature in a catalytic reactor provided in the deodorizing apparatus 8 becomes too high (rises to about 500 °C, the upper limit of temperature). (3) A large-size exhaust gas blower 7 is required. This is because large amounts of outside air (air for combustion) is introduced into the drying apparatus body 1 since the temperature of circulating hot air or the temperature of paper is kept at about 190-250 °C by controlling the burning conditions of burner 4 disposed in the circulation line, so that large amounts of exhaust gas must be discharged by the exhaust gas blower 7 to maintain the negative pressure in the drying apparatus body 1. (4) The capacity of burner 4 disposed in the circulation line must be 3-5 times higher than the capacity needed for normal operation in order to speed up the startup operation since the rotary printing press is frequently stopped for change of plates. To solve these problems, the inventors made an invention shown in FIG. 6 (refer to Japanese Patent Application No. 083912/1989 (1-083912)). In FIG. 6, reference numeral 1 denotes a drying apparatus body, 2 denotes printed paper, 3 denotes a hot air blowing nozzle, 4 denotes a preheating burner, 5 denotes a blower for the first zone, 6 denotes a blower for the second zone, 7 denotes an exhaust gas blower, 8 denotes a direct fired deodorizing apparatus, 9 denotes a heat recovery apparatus, 10 denotes a burner for deodorization, 11 denotes a preheater, 12 denotes a direct fired reactor, 13 denotes a hot air temperature control device for regulating burning at the burner 10 for deodorization for the direct fired deodorizing apparatus 8 based on a value detected by a temperature sensor 16 for the hot air blown from the nozzles, 14 denotes a paper temperature control device for regulating burning at the burner for deodorization 10 in the direct fired deodorizing apparatus 8 based on the value detected by a paper temperature sensor 17, and 15 denotes a selector switch. At the startup before the normal operation, the exhaust gas blower 7 is activated to draw the outside air (air for combustion) into the drying apparatus body 1. The outside air drawn into the drying apparatus body 1 is directed from the exhaust gas blower 7 to the inside of heat transfer tube of the preheater 11, the direct fired reactor 12, the outside of heat transfer tube of the preheater 11, and the inside of heat transfer tube of the heat recovery apparatus 9 in that sequence. Also, the outside air drawn into the drying apparatus body 1 is circulated in the drying apparatus body 1 by activating the blower for the first zone 5 and the blower for the second zone 6. Then, the air circulating in the drying apparatus body 1 is heated by igniting and burning the preheating burner 4. The air in the drying apparatus body 1 is directed as the air for combustion from the exhaust gas blower 7 to the inside of heat transfer tube in the preheater 11 and to the direct fired reactor 12. Then, the fuel for the burner for deodorization 10 is ignited and burned. The produced exhaust gas is directed from the outside of heat transfer tube of the preheater 11 to the inside of heat transfer tube of the heat recovery apparatus 9. This exhaust gas, after preheating the air, is discharged out of the drying apparatus body 1. Thus, the circulating air in the drying apparatus body 1 can be heated rapidly to a specified temperature at the startup before the normal operation. When this condition is established, the preheating burner 4 is turned off to start the normal operation. In the normal operation, the paper 2 printed by the rotary printing press is fed into the drying apparatus body 1, while hot air is blown into the paper passage through the hot air blowing nozzles 3 so that the printed paper 2 is exposed to the hot air and the solvent contained in the ink on the paper is evaporated. The hot air containing the evaporated solvent (exhaust gas of about 140-170 °C) is returned to the outside of heat transfer tube of heat recovery apparatus 9 at the suction side of the blower for the first zone 5 and the blower for the second zone 6, where the hot air is reheated to about 190-250 °C by the exhaust gas passing through the inside of heat transfer tube of the heat recovery apparatus 9, namely the exhaust gas fed from the direct fired reactor 12 of the direct fired deodorizing apparatus 8 (exhaust gas of about 400-500 °C), and directed to the hot air blowing nozzles 3. Part of the hot air in the drying apparatus body 1 is sucked by the exhaust gas blower 7 and fed into the preheater 11 of the direct fired deodorizing apparatus 8, where part of the hot air is preheated by the exhaust gas from the direct fired reactor 12. Next, the hot air is directed to the direct fired reactor 12 which is heated to about 700-1000 °C by the burner for deodorization 10, where the evaporated solvent in the hot air is burned for the deodorization of hot air. The exhaust gas produced at this time is directed to the inside of heat transfer tube of the heat recovery apparatus 9 for the above-described heat exchanging and is then discharged out of the drying apparatus body 1. The heat recovery apparatus 9 can use a shell and tube heat exchanger or a plate type heat exchanger. When drying is controlled based on the hot air tempera-ture, the set value of deodorizing apparatus furnace temperature on the hot air temperature control device 13 is calculated for correction from the value detected by the blowing hot air temperature sensor 16. Based on the result, the burning amount of the burner for deodorization 10 is controlled, and the temperature of hot air blowing from the nozzles is kept at the set value. When drying is performed by paper temperature control, the set value of deodorizing apparatus furnace temperature on the paper temperature control device 14 is calculated for correction from the value detected by the paper temperature sensor 17. Based on the result, the burning at the burner for deodorization 10 is controlled, and the temperature of hot air blowing from the nozzles is kept at the set value. The conventional drying control device for the rotary printing press shown in FIG. 6 has the following disadvantage: since the deodorizing capability of the direct fired deodorizing apparatus 8 relates directly to the furnace temperature of direct fired reactor 12 as shown in FIG. 7, the furnace temperature must be not less than the lower limit T DL in order to comply with the regulations regarding the odor concentration. For the conventional drying control device for the rotary printing press shown in FIG. 6, nevertheless, the furnace temperature of the direct fired deodorizing apparatus 8 is not controlled. For example, in the paper temperature control, when the thermal load is decreased (for example, when the printing speed decreases), the burning amount of the burner for deodorization 10 is decreased, sometimes resulting in a decrease in deodorizing apparatus furnace temperature down to a value less than the lower limit. In the apparatus disclosed in Japanese Patent Application No. 083912/1989 (1-083912), the controllability is not high because the blowing hot air temperature does not respond to the temperature change in the reaction furnace 12 since the heat capacity of the heat exchanger 9 is high, when a speed change (i.e., thermal load fluctuation) occurs in the printing press or when an attempt is made to change a control target value (instrumental set value) of blowing hot air temperature. Furthermore, according to this conventional art, the hot air can be heated in about one minute by using the preheating burner 4 at the startup, but the apparatus has no effective mechanism for cooling the hot air when the printing speed is decreased due to troubles or adjustments in the printing press during the normal operation. That is, the responsiveness of paper temperature is very low because the deodorizing apparatus furnace temperature has a lower limit for providing proper deodorizing capability and because the heat capacity of the heat exchanger is high. Therefore, the paper temperature exceeds the specified value for a long period of time, resulting in a heavy paper loss. The object of this invention as defined by the appended claims is to provide a drying apparatus in which the deodorizing apparatus furnace temperature is kept at a specified value, and the deodorizing apparatus furnace temperature does not decrease to a value less than the lower limit when the thermal load, such as the printing speed, changes. The drying apparatus according to claim 1, when drying is performed by paper temperature control, the set value of deodorizing apparatus furnace temperature on the paper temperature control device is corrected on the basis of the value detected by the paper temperature sensor, and the result is sent to the deodorizing apparatus furnace temperature control device. Based on the corrected set value and the value detected by the deodorizing apparatus furnace temperature sensor, the set value of deodorizing apparatus furnace temperature on the deodorizing apparatus furnace temperature control device is calculated. The calculation result is used to control the burning amount of the burner for deodorization to keep the paper temperature at the set value. In the drying apparatus according to claim 2, which improves on the invention disclosed in the Japanese Patent Application No. 083912/1989 (1-083912), a bypass line is installed on the first zone hot air circulation line to bypass the heat recovery apparatus, and the bypass amount is controlled by the paper temperature on the drying apparatus side or by the blowing hot air temperature in order to give a drying apparatus having high control responsiveness. Furthermore, a means can be provided to simultaneously control the furnace temperature of the direct fired reactor on the basis of the blowing hot air temperature. On changing the printing speed, the heat capacity is lowered because the hot air in the first zone hot air circulation line is bypassed without passing through the heat recovery apparatus. Therefore, the temperature of blowing hot air is rapidly changed by controlling the deodorizing apparatus furnace temperature, which enables the control to be carried out so that the paper temperature remains constant. The drying apparatus according to claim 5 has high control responsiveness as compared with the drying apparatus disclosed in the Japanese Patent Application No. 083912/1989 (1-083912). In this embodiment, a bypass line is installed on the first zone heat recovery line to bypass the heat recovery apparatus, and the bypass amount is controlled by the paper temperature at the exit side of drying apparatus or by the blowing hot air temperature. Furthermore, a means can be provided to simultaneously control the furnace temperature of the direct fired reactor based on the blowing hot air temperature or the paper temperature on the exit side of drying apparatus. When the printing speed is changed, the heating amount of hot air in the first zone circulation line can be quickly controlled by directing part of the hot air in the heat recovery line to the bypass line. Thus, together with the control of deodorizing apparatus furnace temperature, the temperature of blowing hot air is rapidly changed, enabling the control to be carried out so that the paper temperature is constant. FIG. 1 is a schematic view of a first embodiment of the drying control device for the printed paper drying apparatus according to this invention, FIG. 2 is a schematic view of a second embodiment of the drying control device for the printed paper drying apparatus according to this invention, FIG. 3 is a graph comparing the controllability of the drying apparatus of this invention with that of the drying apparatus of conventional art shown in FIG.14, FIG. 4 is a schematic view of a fifth embodiment of the drying control device for the printed paper drying apparatus according to this invention, FIG. 5 is a schematic view of a typical conventional drying apparatus, FIG. 6 is a schematic view of another typical conventional drying apparatus, and FIG. 7 is a graph showing the relationship between the deodorizing apparatus furnace temperature and the odor concentration in exhaust gas. The first embodiment of the drying apparatus for rotary printing press according to the first aspect of this invention is shown in FIG. 1. Reference numeral 1 denotes a drying apparatus body, 2 denotes printed paper, 3 denotes a hot air blowing nozzle, 4 denotes a preheating burner, 5 denotes a blower for the first zone, 6 denotes a blower for the second zone, 7 denotes an exhaust gas blower, 8 denotes a direct fired deodorizing apparatus, 9 denotes a heat recovery apparatus, 10 denotes a burner for deodorization, 11 denotes a preheater, 12 denotes a direct fired reactor, 13 denotes a hot air temperature control device, 14 denotes a paper temperature control device, 15 denotes a selector switch, 16 denotes a blowing hot air temperature sensor, 17 denotes a paper temperature sensor, 18 denotes a control device for deodorizing apparatus furnace temperature, and 19 denotes a deodorizing apparatus furnace temperature sensor. Next, the operation of the drying apparatus for rotary printing press shown in FIG. 1 will be described specifically. When drying is controlled based on the hot air temperature, the set value of deodorizing apparatus furnace temperature on the hot air temperature control device 13 is corrected on the basis of the value detected by the blowing hot air temperature sensor 16. The result is sent to the deodorizing apparatus furnace temperature control device 18. The set value in the control device 18 of deodorizing apparatus furnace temperature is calculated from this corrected set value and the detected value obtained from the deodorizing apparatus furnace temperature sensor 19. Based on the result, the burning amount of the burner for deodorization 10 is controlled, and the temperature of hot air blowing from the nozzles is kept at the set value. When drying is controlled based on the paper temperature, the set value of deodorizing apparatus furnace temperature on the paper temperature control device 14 is corrected on the basis of the value detected by the paper temperature sensor 17. The result is sent to the deodorizing apparatus furnace temperature control device 18. The set value of deodorizing apparatus furnace temperature is calculated from this corrected set value and the detected value obtained from the deodorizing apparatus furnace temperature sensor 19. Based on the result, the burning amount of the burner for deodorization 10 is controlled, and the temperature of hot air blowing from the nozzles is kept at the set value. For example, when the printing speed is decreased and the paper temperature is increased, the set value for deodorizing apparatus furnace temperature on the paper temperature control device 14 is reduced on the basis of the value detected by the paper temperature sensor 17. The set value of deodorizing apparatus furnace temperature on the deodorizing apparatus furnace temperature control device 18 is calculated from the reduced set value and the detected value obtained from the deodorizing apparatus furnace temperature sensor 19. Based on the result, the burning amount of the burner for deodorization 10 is decreased to keep the paper temperature at the set value. In the drying apparatus for rotary printing press according to the first aspect of this invention, for example, when the paper temperature control is used as described above, the set value of deodorizing apparatus furnace temperature on the paper temperature control device is corrected on the basis of the value detected by the paper temperature sensor, and the result is sent to the deodorizing apparatus furnace temperature control device. The set value of deodorizing apparatus furnace temperature on the deodorizing apparatus furnace temperature control device is calculated from the corrected set value and the detected value obtained from the deodorizing apparatus furnace temperature sensor. Based on the result, the burning amount of the burner for deodorization is controlled to keep the paper temperature at the set value. Thus, since the furnace temperature of the direct fired deodorizing apparatus is controlled, the deodorizing apparatus furnace temperature can be kept at the set value when the printing speed or other thermal load is changed, so that the deodorizing apparatus furnace temperature is not decreased to a value less than the lower limit. The second embodiment of the drying apparatus for rotary printing press according to the second aspect of this invention will be described with reference to FIGS. 2 and 3. In FIG. 2, reference numeral 1 denotes a drying apparatus body, 2 denotes printed paper, 3 denotes a hot air blowing nozzle, 4 denotes a preheating burner, 5 denotes a blower for the first zone, 6 denotes a blower for the second zone, 7 denotes an exhaust gas blower, 8 denotes a direct fired deodorizing apparatus, 9 denotes a heat recovery apparatus, 10 denotes a burner for deodorization, 11 denotes a preheater, 12 denotes a direct fired reactor, 16 denotes a hot air temperature sensor for the first zone, 17 denotes a paper temperature sensor, 20 denotes a bypass line, 21 denotes an automatic bypass damper 22 denotes a motor or cylinder, 23 denotes a function generator, 24 denotes a deodorizing apparatus furnace temperature sensor, 26 denotes a control output setting device, 27 denotes a printing speed sensor, TIC-1 denotes a paper temperature regulator, and TIC-2 denotes a deodorizing apparatus furnace temperature regulator. The principal configuration of this embodiment is the same as that of the drying apparatus shown in FIG. 6, except that a bypass line 20 is installed on the first zone hot air circulation line, and an automatic bypass damper 21 is disposed midway in the line 20. The paper temperature regulator TIC-1 is linked to the motor 22 (or cylinder) disposed to the automatic bypass damper 21 and the preheating burner 4 for startup in order to send control signals. The deodorizing apparatus furnace temperature regulator TIC-2 controls the burning amount of the burner for deodorization so that the furnace temperature obtained from the deodorizing apparatus furnace temperature sensor 24 takes a specified value, via the function generator 23 which calculates the output in accordance with the temperature signal of the first zone hot air temperature sensor 16. The control output setting device 26 provides a reset value of output of the paper temperature control device TIC-1. While the printing speed sensor 27 detects printing speeds at regular intervals, the control output setting device 26 outputs the reset value in accordance with the change rate of printing speed with time. Next, the operation of the drying apparatus for rotary printing press shown in FIG. 2 will be described specifically. At the startup before the normal operation, the exhaust gas blower 7 is activated to draw the outside air (air for combustion) into the drying apparatus body 1. The outside air drawn into the drying apparatus body 1 is directed from the exhaust gas blower 7 to the inside of heat transfer tube of the preheater 11, the direct fired reactor 12, the outside of heat transfer tube of the preheater 11, and the inside of heat transfer tube of the heat recovery apparatus 9 in that sequence. Also, the outside air drawn into the drying apparatus body 1 is circulated in the drying apparatus body 1 by activating the blower for the first zone 5 and the blower for the second zone 6. Then, the air circulating in the drying apparatus body 1 is heated by igniting and burning the preheating burner 4. The air in the drying apparatus body 1 is directed as the air for combustion from the exhaust gas blower 7 to the inside of heat transfer tube in the preheater 11 and to the direct fired reactor 12. Then, the fuel for the burner for deodorization 10 is ignited and burned. The produced exhaust gas is directed from the outside of heat transfer tube of the preheater 11 to the inside of heat transfer tube of the heat recovery apparatus 9. This exhaust gas, after preheating the air circulating in the drying apparatus body 1, is discharged out of the drying apparatus body 1. Thus, the circulating air in the drying apparatus body 1 can be heated rapidly to a specified temperature at the startup before the normal operation. When this condition is established, the preheating burner 4 is turned off to start the normal operation. In the normal operation, the paper 2 printed by the rotary printing press is fed into the drying apparatus body 1, while hot air is blown into the paper passage through the hot air blowing nozzles 3 so that the printed paper 2 is exposed to the hot air and the solvent contained in the ink on the paper is evaporated. The hot air containing the. evaporated solvent (exhaust gas of about 140-170 °C) is returned to the outside of heat transfer tube of heat recovery apparatus 9 at the suction side of the blower for the first zone 5 and the blower for the second zone 6, where the hot air is reheated to about 190-250 °C by the exhaust gas passing through the inside of heat transfer tube of the heat recovery apparatus 9, namely the exhaust gas fed from the direct fired reactor 12 of the direct fired deodorizing apparatus 8 (exhaust gas of about 400-500 °C), and directed to the hot air blowing nozzles 3. Part of the hot air in the drying apparatus body 1 is sucked by the exhaust gas blower 7 and fed into the preheater 11 of the direct fired deodorizing apparatus 8, where part of the hot air is preheated by the exhaust gas from the direct fired reactor 12. Next, the hot air is directed to the direct fired reactor 12 which is heated to about 700-1000 °C by the burner for deodorization 10, where the evaporated solvent in the hot air is burned for the deodorization of hot air. The exhaust gas produced at this time is directed to the inside of heat transfer tube of the heat recovery apparatus 9 for the above-described heat exchanging and is then discharged out of the drying apparatus body 1. FIG. 3 shows the relationship between the degree of opening of the control damper 21 disposed in the first zone hot air circulation line 20 and the paper temperature (temperature sensor 17) or the hot air blowing temperature (temperature sensor 16) and also the relationship between the degree of opening of the control damper 21 and the furnace temperature of the direct fired reactor 12. When the printing speed is changed during the operation of printing press, for example, when the printing speed is decreased from a to b, the paper temperature begins increasing. Thus, the deviation σ of actual paper temperature from the target value Z of paper temperature increases gradually. Therefore, to decrease the deviation σ, control is carried out to open the bypass damper 21 in the first zone hot air circulation line 20 so that the temperature of hot air in the first zone is decreased. Thus, the hot air temperature in the first zone T 1 is suddenly decreased, and the paper temperature is soon returned to the target value Z. By determining the furnace temperature T 3 in the deodorizing apparatus 8 corresponding to the hot air temperature in the first zone T 1 by an equation of T 3 = f(T 1 ) , the furnace temperature of the deodorizing apparatus 8 decreases in accordance with the hot air temperature in the first zone, so that a certain heat recovery rate can be secured. For example, in the conventional drying apparatus disclosed in the Japanese Patent Application No. 083912/1989 (1-083912), since the hot air temperature in the first zone is controlled only by the control of furnace temperature, the response of the paper temperature is considerably delayed as compared with the present invention, as indicated by the dotted line in FIG.3. As described above, according to the second aspect of this invention, the drying of printed paper can be controlled with high responsiveness to the change in printing speed by controlling the furnace temperature of the deodorizing apparatus 8 corresponding to the hot air temperature in the first zone while controlling the degree of opening of the bypass damper 21 in the first zone circulation line 20 so that the paper temperature is constant. For example, when the printing speed is changed from 375 m/min to 200 m/min, the temperature of printed paper begins increasing gradually from 125 °C. The paper temperature returns to the set value within one minute according to this invention, whereas it returns to the set value in 5-10 minutes in the apparatus disclosed in the Japanese Patent Application No. 083912/1989 (1-083912). According to the second aspect of this invention, in the drying apparatus for rotary printing press for drying the ink on the printed paper having a direct fired deodorizing apparatus and a heat recovery apparatus for heating the hot air circulating in the drying apparatus by using the exhaust gas from the deodorizing apparatus, a bypass line is installed on the hot air circulation line to bypass the heat recovery apparatus to control the paper temperature and/or blowing hot air temperature by regulating the degree of opening of bypass damper installed in the bypass line, and to control the burning amount of the burner for deodorization so that the deodorizing apparatus furnace temperature corresponding to the blowing hot air temperature is obtained. Therefore, this drying apparatus of this invention achieves the following effects: (a) The apparatus is compact and has a low consumption of fuel. (b) The apparatus has significantly high controllability against external disturbances such as changes in printing speed. Next, the third embodiment of the drying apparatus for rotary printing press, according to the third aspect of this invention, will be described with reference to FIG. 4. In FIG. 4, reference numeral 1 denotes a drying apparatus body, 2 denotes printed paper, 3 denotes a hot air blowing nozzle, 4 denotes a preheating burner, 5 denotes a blower for the first zone, 6 denotes a blower for the second zone, 7 denotes an exhaust gas blower, 8 denotes a direct fired deodorizing apparatus, 9 denotes a heat recovery apparatus, 10 denotes a burner for deodorization, 11 denotes a preheater, 12 denotes a direct fired reactor, 16 denotes a hot air temperature sensor for the first zone, 17 denotes a paper temperature sensor, 20' denotes a bypass line of the heat recovery line, 21 denotes an automatic bypass damper, 22 denotes a motor or cylinder, 23 denotes a function generator, 24 denotes a deodorizing apparatus furnace temperature sensor, TIC-1 denotes a paper temperature regulator, and TIC-2 denotes a deodorizing apparatus furnace temperature regulator. The principal configuration of this embodiment is the same as that of the drying apparatus shown in FIG. 5, except that a bypass line 20' is installed on the first zone hot air circulation line, and an automatic bypass damper 21 is disposed midway in the line 20'. The paper temperature regulator TIC-1 is linked to the motor 22 (or cylinder) mounted to the automatic bypass damper 21 and the preheating burner for startup 4 to send control signals. The deodorizing apparatus furnace temperature regulator TIC-2 controls the burning amount of the burner for deodorization so that the furnace temperature obtained from the deodorizing apparatus furnace temperature sensor 24 takes a specified value, via the function generator 23 which calculates the output in accordance with the temperature signal of the first zone hot air temperature sensor 16. The equivalent effect can be achieved when TIC-2 performs the control via a function generator 23' which calculates the output in accordance with the temperature signal of the paper temperature sensor 17. Next, the operation of the drying apparatus for rotary printing press shown in FIG. 4 will be described specifically. At the startup before the normal operation, the exhaust gas blower 7 is activated to draw the outside air (air for combustion) into the drying apparatus body 1. The outside air drawn into the drying apparatus body 1 is directed from the exhaust gas blower 7 to the inside of heat transfer tube of the preheater 11, the direct fired reactor 12, the outside of heat transfer tube of the preheater 11, and the inside of heat transfer tube of the heat recovery apparatus 9 in that sequence. Also, the outside air drawn into the drying apparatus body 1 is circulated in the drying apparatus body 1 by activating the blower for the first zone 5 and the blower for the second zone 6. Then, the air circulating in the drying apparatus body 1 is heated by igniting and burning the preheating burner 4. The air in the drying apparatus body 1 is directed as the air for combustion from the exhaust gas blower 7 to the inside of heat transfer tube in the preheater 11 and to the direct fired reactor 12. Then, the fuel for the burner for deodorization 10 is ignited and burned. The produced exhaust gas is directed from the outside of heat transfer tube of the preheater 11 to the inside of heat transfer tube of the heat recovery apparatus 9. This exhaust gas, after preheating the air circulating in the drying apparatus body 1, is discharged out of the drying apparatus body 1. Thus, the circulating air in the drying apparatus body 1 can be heated rapidly to a specified temperature at the startup before the normal operation. When this condition is established, the preheating burner 4 is turned off to start the normal operation. In the normal operation, the paper 2 printed by the rotary printing press is fed into the drying apparatus body 1, while hot air is blown into the paper passage through the hot air blowing nozzles 3 so that the printed paper 2 is exposed to the hot air and the solvent contained in the ink on the paper is evaporated. The hot air containing the evaporated solvent (exhaust gas of about 140-170 °C) is returned to the outside of heat transfer tube of heat recovery apparatus 9 at the suction side of the blower for the first zone 5 and the blower for the second zone 6, where the hot air is reheated to about 190-250 °C by the exhaust gas passing through the inside of heat transfer tube of the heat recovery apparatus 9, namely the exhaust gas fed from the direct fired reactor 12 of the direct fired deodorizing apparatus 8 (exhaust gas of about 400-500 °C) , and directed to the hot air blowing nozzles 3. Part of the hot air in the drying apparatus body 1 is sucked by the exhaust gas blower 7 and fed into the preheater 11 of the direct fired deodorizing apparatus 8, where part of the hot air is preheated by the exhaust gas from the direct fired reactor 12. Next, the hot air is directed to the direct fired reactor 12 which is heated to about 700-1000 °C by the burner for deodorization 10, where the evaporated solvent in the hot air is burned for the deodorization of hot air. The exhaust gas produced at this time is directed to the inside of heat transfer tube of the heat recovery apparatus 9 for the above-described heat exchanging and is then discharged out of the drying apparatus body 1. FIG. 3 shows the relationship between the degree of opening of the control damper 21 disposed in the bypass line 20' connected to the hot air line from the deodorizing apparatus 8 and the paper temperature (temperature sensor 17) or the hot air blowing temperature (temperature sensor 16) and also the relationship between the degree of opening of the control damper 21 and the furnace temperature of the direct fired reactor 12. When the printing speed is changed during the operation of printing press, for example, when the printing speed is decreased from a to b, the paper temperature T S begins increasing. Thus, the deviation σ of actual paper temperature T S from the target value Z of paper temperature increases gradually. Therefore, to decrease the deviation σ control is carried out to open the bypass damper 21 in the bypass line 20' so that the temperature of hot air in the first zone is decreased. Thus, the hot air temperature in the first zone T 1 is suddenly decreased, and the paper temperature is soon returned to the target value Z. By determining the furnace temperature T 3 in the deodorizing apparatus 8 corresponding to the hot air temperature in the first zone T 1 or the paper temperature T S at the exit side of drying apparatus by an relational equation of T 3 = f(T 1 ) or T 3 = f(T S ) , the furnace temperature of the deodorizing apparatus 8 decreases with the decrease in the first zone hot air temperature T 1 or with the increase in the paper temperature T S , so that a certain heat recovery rate can be secured. In the conventional drying apparatus disclosed in the Japanese Patent Application No. 083912/1989 (1-083912), since the hot air temperature in the first zone is controlled only by the control of furnace temperature, the response of the paper temperature is considerably delayed as compared with the present invention, as indicated by the dotted line in FIG. 3. As described above, the drying of printed paper can be controlled with high responsiveness to the change in printing speed by regulating the furnace temperature in the deodorizing apparatus 8 corresponding to the first zone hot air temperature or the paper temperature while controlling the degree of opening of the bypass damper 21 in the bypass line 20' so that the paper temperature is constant. For example, when the printing speed is changed from 375m/min to 200 m/min, the temperature of printed paper begins increasing gradually from 125 °C. The paper temperature returns to the set value within one minute according to this invention, whereas it returns to the set value in 5-10 minutes in the apparatus disclosed in the Japanese Patent Application No. 083912/1989 (1-083912). According to the fifth aspect of this invention, in the drying apparatus for rotary printing press for drying the ink on the printed paper which has a direct fired deodorizing apparatus and a heat recovery apparatus for heating the hot air circulating in the drying apparatus by using the exhaust gas from the deodorizing apparatus, a bypass line is installed on the hot air circulation line to bypass the heat recovery apparatus to control the paper temperature and/or blowing hot air temperature by regulating the degree of opening of bypass damper disposed in the bypass line, and the burning amount of the burner for deodorization is controlled so that the deodorizing apparatus furnace temperature corresponding to the blowing hot air temperature or paper temperature is obtained. Therefore, this drying apparatus of this invention achieves the following effects: (a) The apparatus is compact and has a low consumption of fuel. (b) The apparatus has significantly high controllability against external disturbances such as changes in printing speed.

Claims: A drying apparatus for a rotary printing press wherein hot air is blown onto printed paper (2) to dry the printed paper by evaporating the solvent in ink, and the hot air is reheated by using the exhaust gas from a direct fired deodorizing apparatus (8), comprising a hot air temperature control device (13) for correcting a set value for a deodorizing apparatus furnace temperature on the basis of a value detected by a temperature sensor (16) of hot air blowing from nozzles upon the printed paper, a paper temperature control device (14) for correcting the set value for the deodorizing apparatus furnace temperature on the basis of a value detected by a temperature sensor (17) of the printed paper, and a deodorizing apparatus furnace temperature control device (18) for calculating a burning amount of a deodorization burner (10) in the direct fired deodorizing apparatus (8) on the basis of the set value from the hot air temperature control device (13) or from a paper temperature control device (14) and also on the basis of the value detected by a deodorizing apparatus furnace temperature sensor (19). A drying apparatus for a rotary printing press for drying ink on printed paper (2) which has a direct fired deodorizing apparatus (8) and a heat recovery apparatus (9) for heating hot air circulating in said drying apparatus by using the exhaust gas of the deodorizing apparatus (8), comprising a bypass line (20) installed so that hot air for drying the printed paper can bypass the heat recovery apparatus (9) disposed in a hot air circulation line, means (TIC-1) for controlling a temperature (17) of the printed paper (2) and/or a temperature (16) of hot air blowing from nozzles by adjusting the degree of opening of a bypass damper (21) disposed in said bypass line (20), and means (TIC-2) for controlling a burning amount of a deodorization burner (10) on the basis of the temperature (16) of the hot air blowing from nozzles upon the printed paper so that a deodorizing apparatus furnace temperature obtained from a deodorazing apparatus furnace temperature sensor (24) takes a specified value. The drying apparatus according to claim 2, characterized in that the means (TIC-1) for controlling a temperature (17) of the printed paper (2) and/or a temperature (16) of the hot air blowing from nozzles upon the printed paper adjust the degree of opening of the bypass damper (21) disposed in the bypass line (20) and the burning amount of a preheating burner (4). The drying apparatus according to claim 2 or 3, characterized in that a control output setting device (26) which modifies a controlling function of the controlling means (TIC-1) in accordance with the change rate of the printing speed with time when, as the printing speed is being detected by a printing speed detector (27), the change rate of the printing speed with time exceeds a specified range. A drying apparatus for a rotary printing press for drying ink on printed paper (2) which has a direct fired deodorizing apparatus (8) and a heat recovery apparatus (9) for reheating hot air circulating in the drying apparatus by using the exhaust gas of the deodorizing apparatus (8), comprising a bypass line (20') installed on an exhaust gas line from the deodorizing apparatus (8) to bypass the heat recovery apparatus (9) so as to possibly discharge part of the exhaust gas from the deodorizing apparatus (8) without passing through the heat recovery apparatus (9), means (TIC-1) for controlling a temperature (17) of printed paper and/or a temperature (16) of hot air blowing from nozzles by adjusting a degree of opening of a bypass damper disposed in the bypass line, and means (TIC-2) for controlling a burning amount of a deodorization burner (10) on the basis of the temperature (16) of the hot air blowing from nozzles upon the printed paper so that a deodorizing apparatus furnace temperature obtained from a deodorazing apparatus furnace temperature sensor (24) takes a specified value. The ink drying apparatus according to claim 5, characterized in that the means (TIC-1) for controlling a temperature (17) of the printed paper (2) and/or a temperature (16) of hot air blowing from nozzles upon the printed paper adjust the degree of opening of the bypass damper (21) disposed in the bypass line (20) and the burning amount of a preheating burner (4).

Inventors: KUNO HIROAKI, KUWADA CHIE, TANOUCHI KUNIAKI, YOKOO KAZUTOSHI, YOSHIDA MINORU, KUNO, HIROAKI, KUWADA, CHIE, TANOUCHI, KUNIAKI, YOKOO, KAZUTOSHI, YOSHIDA, MINORU, KUNO, HIROAKI, C/O HIROSHIMA TECHN. INSTITUTE, KUWADA, CHIE, C/O MITSUBISHI JUKOGYO K.K., TANOUCHI, KUNIAKI, C/O MITSUBISHI JUKOGYO K.K., YOKOO, KAZUTOSHI, C/O HIROSHIMA TECHN. INSTITUTE, YOSHIDA, MINORU, C/O MIHARA MACHINERY WORKS
Applicants: MITSUBISHI HEAVY IND LTD, MITSUBISHI JUKOGYO KABUSHIKI KAISHA
Application year: 1991
Main classification: B41F23
IPC codes: F26B23, B41F23