Method for removing soot by scattering steel balls in a heat-exchanger

Abstract: The known method for removing soot or the like adhered to heat transfer tubes of a heat-exchanger by providing a steel ball scatterer above the heat transfer tubes and intermittently scattering steel balls towards the heat transfer tubes, is improved. The improvements reside in that a steel ball scattering rate is chosen small at the time of commencing the scattering and thereafter it is increased either in a stepwise manner or continuously. Preferably, within a main body casing of the heat-exchanger (1), a plurality of steel ball collision preventing plates having their central portions warped upwards are provided between the steel ball scatterer (3) and the heat transfer tube group (2), in order to prevent fins (8b) of finned heat transfer tubes (8) from being damaged by steel balls falling from the steel ball scatterer and directly colliding against the fins.

Description: BACKGROUND OF THE INVENTION: Field of the Invention: The present invention relates to a method for removing soot or the like adhered to surfaces of heat transfer tubes in a heat-exchanger of an exhaust gas economizer or the like by intermittently scattering steel balls towards said heat transfer tubes. Description of the Prior Art: A method of such kind is known for example from US-A-2 949 282. In order to remove soot or the like adhering to surfaces of heat transfer tubes in a heat-exchanger of an exhaust gas economizer or the like, a heat-exchanger having a steel ball scattering device assembled therein has heretofore come into practical use. Fig. 1 is a general vertical cross-section view showing one example of such heat-exchanger in the prior art, and Fig. 2 is a perspective view partly cut away of the same heat-exchanger. In these figures, reference numeral 1 designates a main body casing of a heat-exchanger, in which heat transfer tube groups 2 are disposed and steel ball scatterers 3 are provided above (on the upstream of) the heat transfer tube groups. To these steel ball scatterers 3 are fed steel balls from a steel ball feeder 4. The steel balls scattered by the steel ball scatterers 3 would fall while removing soot or the like adhered to the heat transfer groups 2. Then they would be returned to the above-mentioned steel ball feeder 4 by a steel ball conveyor 5. Reference numeral 6 designates a gas inlet, numeral 7 designates a gas outlet, the gas inlet 6 is provided at one end of the heat-exchanger main body 1 above the steel ball scatterers 3, and the gas outlet 7 is provided at one side portion of the heat-exchanger main body 1 lower than the heat transfer tube groups 2. Fig. 3 is a perspective view showing one example of the steel ball scatterer 3, and in this figure, reference numeral 3a designates a steel ball feed pipe having a square cross-section and numeral 3b designates a scattering plate, whose upper surface configuration forms a part of a spherical surface. The number of steel ball scatterers 3 disposed within the heat-exchanger is determined depending upon a projection cross-section area of the heat transfer tube groups and a steel ball scattering area of one steel ball scatterer, and if the steel ball scattering area of one steel ball scatterer is broad, the number of the disposed steel ball scatterers can be made small. In the case of removing soot or the like adhered to surfaces of heat transfer tubes in a heat-exchanger of an exhaust gas economizer or the like by scattering steel balls by means of the above-described steel ball scattering device, a scattering rate and a scattering method of steel balls are regulated depending upon the amount of soot or the like adhered to the heat transfer tubes. More particularly, in the case where the adhered amount is much (an adhering rate is large), unless steel balls are continuously scattered at a large rate, the adhered amount of soot or the like would increase and a predetermined heat transfer performance could not be maintained. On the other hand, in the case where the adhered amount is little, a heat transfer performance could be maintained even if the scattering rate is made small or even if intermittent scattering at a long time interval is effected. In addition, a scattering range and a scattering height of steel balls of a steel ball scatterer are, in the case of the spherical surface type scatterer shown in Fig. 3, represented by the following equations: scattering range x = η·v o ·cos ϑ·t scattering height y = η·v o ·ϑ·t - 1 2 g·t² where η: restitution coefficient between a steel ball and a scattering plate, v o : velocity of a steel ball when it collides with a scattering plate, ϑ: angle (with respect to the horizontal direction) of a velocity of a steel ball flying out of a scatterer, t: time elapsted after collision, and g: acceleration by gravity. As will be seen from these equations, a scattering range as well as a scattering height are related to the velocity (v o ) of a steel ball when it collides with a scattering plate. (This collision velocity (v o ) is proportional to a square root of a height of fall in the case of natural falling.) Accordingly, as steel balls are made to fall onto a scattering plate from a higher position, the steel balls can be scattered over a broader range. In the case of removing soot by intermittently scattering steel balls, soot or the like having adhered to heat transfer tubes by that time would leave the heat transfer tubes and would scatter simultaneously with scattering of the steel balls, and so, a concentration of soot and the like in an exhaust gas would be temporarily increased. Generally, on the downstream side of a heat-exchanger is disposed an electric dust collector, and if its dust collecting power is insufficient, soot or the like would be released into the atmospheric air, and contamination of the atmospheric air would be resulted. Therefore, in the case of abrupt increase of a soot concentration in an exhaust gas as described above, it is necessary to design a capacity of an electric dust collector so as to meet such abrupt increase, and so, a scale of the apparatus would become large. Fig. 4 is a longitudinal cross-section view showing a part of a finned heat transfer tube 8, and Fig. 5 is a transverse cross-section view of the same. With reference to these figures, a top portion of a fin 8b is mounted to a pipe 8a. From US-A-2949282 is known an apparatus for cleaning heat exchange means by scattering cleaning particles onto surfaces of the heat exchanger to be cleaned. In this apparatus by the provision of valves in each of separate supply ducts for supply of entraining fluid and cleaning particles provided at different levels between multiple groups of heat exchanger tubes, a discharge velocity of the respective tubes can be regulated independently from the other tubes. However, the duration of discharge or the intensity of discharge is only varied depending on the area to be reached by the cleaning particles and amplitudes of angular oscillations of the discharge tubes moved by means of rotated crank levers are controlled in order to adjust the rate at which a beaten zone moves over the area to be cleaned. SUMMARY OF THE INVENTION: It is the object of the present invention to provide a novel method for removing soot by scattering steel balls in a heat-exchanger, in which abrupt increase of soot or the like in an exhaust gas can be mitigated, hence a capacity of a peripheral instrument such as an electric dust collector can be designed low, and installation space and expense can be saved. According to the present invention, there is provided a method for removing soot or the like in a heat-exchanger, wherein soot or the like adhered to heat transfer tubes of the heat-exchanger is removed by intermittently scattering steel balls towards the heat transfer tubes, improved in that a steel ball scattering rate is chosen small at the time of commencing the scattering and thereafter it is increased. According to a preferred embodiment of the present invention, there is provided the above method for removing soot or the like in a heat-exchanger, wherein the scattering rate is increased in a stepwise manner. According to still another embodiment, the scattering rate is increased continuously. According to the present invention, as featured above, a scattering rate of steel balls intermittently scattered for the purpose of removing soot is chosen small at the time of commencing the scattering in each scattering period, thereafter it is increased either in a stepwise manner or continuously, and finally a predetermined amount of steel balls are scattered. Thereby, soot or the like adhered to heat transfer tubes is gradually removed, hence a concentration of soot discharged in an exhaust gas would not rise abruptly, and so, a capacity of an associated electric dust collector can be made small (accordingly, the dust collector can be made less expensive). The above-mentioned object and advantages of the present invention will become more apparent by reference to the following description of preferred embodiments of the invention taken in conjunction with the accompanying drawings. BRIEF DESCRIPTION OF THE DRAWINGS: In the accompanying drawings: Fig. 1 is a general vertical cross-section view showing one example of a heat-exchanger in the prior art to which the present invention is pertinent; Fig. 2 is a perspective view partly cut away of the same heat-exchanger in the prior art; Fig. 3 is a perspective view showing one example of a steel ball scatterer in the prior art; Fig. 4 is a longitudinal cross-section view showing a part of a finned heat transfer tube; Fig. 5 is a transverse cross-section view of the same; Figs. 6 and 7 are diagrams showing effects and advantages of the present invention; DESCRIPTION OF THE PREFERRED EMBODIMENTS: Now a preferred embodiment of the method according to the present invention will be described in greater detail. The preferred embodiment is practiced by making use of the apparatus shown in Fig. 1. In this figure, at first, gas containing soot or the like is introduced through a gas inlet 6, and after the gas has been made to perform heat-exchange at the heat transfer tube group 2, it is made to flow out through a gas outlet 7. Then soot or the like would adhere to the heat transfer tubes in the heat transfer group 2, and would degrade a heat transfer performance of the tubes. When the heat transfer performance has been degraded up to a certain heat transfer performance value, steel balls are scattered for the purpose of recovering a heat transfer performance. On this occasion, a scattering rate is chosen small at the time of commencing the scattering, thereafter the scattering rate is increased either in a stepwise manner or continuously as by regulating a rotational speed of a rotary ejector associated with a steel ball feeder 4, and eventually a predetermined amount of steel balls are scattered to recover the heat transfer performance. One preferred embodiment has been practiced on the assumption of one example of the case where heat is collected from an exhaust gas of a coal-fired boiler, and the conditions of practical enforcement are as follows: 1) Inflow exhaust gas conditions (a) gas flow rate 9400 Nm³/h (b) concentration of soot or the like 150 mg/Nm³ (c) temperature inlet 130°C and outlet 90°C 2) Apparatus specification (a) heat transfer tube specification tube diameter 34 mm, thickness 3.2 mm fin diameter 64 mm, thickness 1.6 mm fin pitch 2.5 fins/in (b) heat transfer area : 82 m² (c) horizontal cross-section area of apparatus : 1 m² As a result of operation under such conditions, a heat transfer performance of the heat transfer tubes changed as shown in Fig. 6. More particularly, in the case of not scattering steel balls, a specific heat transfer performance is lowered up to 0.82 in 24 hours as shown by a dash line in Fig. 6. Then, at first, in the case where steel balls (5 mm in diameter) were scattered at a rate of 450 kg/cm²h once every 6 hours each time for one hour through the heretofore known method, a specific heat transfer performance was maintained at 0.95 - 1.0 as shown by solid lines in Fig. 6. However, a concentration of soot in an exhaust gas immediately after commencement of the scattering amounted to 1700 mg/Nm³ which is about 17 times as large as a concentration upon stoppage of scattering (about 100 mg/Nm³) as shown in Fig. 7. Next, as one preferred embodiment of the present invention, for 20 minutes after commencement of scattering of steel balls, steel balls were scattered at a scattering rate 1/3 times as small as the predetermined scattering rate (450 kg/m²h), that is, at a rate of 150 kg/m²h, thereafter steel balls were scattered at a rate of 600 kg/m²h for 40 minutes, and the total scattered amount of steel balls was equalized to that in the heretofore known method. In this case, recovery of a specific heat transfer performance was equal to that in the heretofore known method indicated by solid lines in Fig. 6. Nevertheless a concentration of soot in an exhaust gas was about 1/3.3 times as small as that in the heretofore known method and about 5.1 times as large as that upon stoppage of scattering as indicated by dash lines in Fig. 7. In other words, according to the above-described embodiment of the present invention, since a peak of a concentration of soot in an exhaust gas is remarkably lowered as compared to that in the case of the heretofore known method, an electric dust collector having a capacity about 1/3 times as small as that in the prior art could suffice. Accordingly, the object can be achieved with an extremely small-sized and less expensive electric dust collector. It is to be noted that while the change of a scattering rate of steel balls was performed in two steps in the method of the above-described embodiment, the number of steps could be further increased or a scattering rate could be changed continuously. As will be apparent from the detailed description of the preferred embodiment of the present invention above, the present invention can bring about the following effects and advantages. That is, when steel balls for removing soot are intermittently scattered towards heat transfer tubes in a heat-exchanger, by regulating a scattering rate of steel balls either in a stepwise manner or continuously, abrupt increase of soot or the like in an exhaust gas can be mitigated. Accordingly, an installation capacity of peripheral instruments such as, for example, an electric dust collector or the like can be designed low, and in accordance thereto, an installation space and an installation expense can be saved. In addition, as a soot concentration of an exhaust gas becomes low, the problem of contamination of the atmospheric air can also be resolved.

Claims: A method for removing soot or the like in a heat exchanger, wherein soot or the like adhered to heat transfer tubes of a heat exchanger is removed by intermittently scattering steel balls towards said heat transfer tubes; characterized in that a steel ball scattering rate is chosen small at the time of commencing the scattering and thereafter it is increased. The method of claim 1, wherein the scattering rate is increased in a stepwise manner. The method of claim 1, wherein the scattering rate is increased continuously.

Inventors: FUJIIKE HIROSHI, HIGASHI TSUNEO, KATO MASAMI, MAKINO KATSUAKI, MIYAMOTO HIROSHI, NAKAMURA SATOSHI, TANAKA TADASHI, FUJIIKE, HIROSHI C/O MIHARA MACHINERY WORKS OF, HIGASHI, TSUNEO, C/O MIHARA MACHINERY WORKS OF, KATO, MASAMI, C/O CHUBU ELECTRIC POWER CO. INC., MAKINO, KATSUAKI, C/O HIROSHIMA TECHNICAL INST., MIYAMOTO, HIROSHI, C/O HIROSHIMA TECHNICAL INST., NAKAMURA, SATOSHI, C/O CHUBU ELECTRIC POWER CO., TANAKA, TADASHI, C/O CHUBU ELECTRIC POWER CO. INC.
Applicants: CHUBU ELECTRIC POWER, MITSUBISHI HEAVY IND LTD, CHUBU ELECTRIC POWER COMPANY, INCORPORATED, MITSUBISHI JUKOGYO KABUSHIKI KAISHA
Application year: 1991
Main classification: F28G1
IPC codes: F28G1