JP5991677B2 - Exhaust gas treatment equipment - Google Patents

Description

  The present invention relates to an exhaust gas treatment apparatus. More specifically, the present invention relates to an exhaust gas treatment apparatus used for purifying exhaust gas containing harmful substances such as HCl and SOx discharged from a combustion apparatus such as a waste incinerator, a gasification furnace, and a melting furnace.

  Exhaust gas discharged from combustion facilities such as waste incinerators contains toxic substances such as acid gases such as HCl (hydrogen chloride, hydrochloric acid) and SOx (sulfur oxide), NOx, dioxins, and dust. Yes. In order to remove these harmful substances, an exhaust gas treatment device is provided on the outlet side of the combustion facility.

  The general process in the exhaust gas treatment apparatus will be described. First, the high temperature exhaust gas discharged from the combustion apparatus is cooled to a predetermined temperature by water spraying in a temperature reducing tower, and then HCl, SOx by spraying with slaked lime, sodium bicarbonate, or the like. The acid gas such as is removed. Next, soot dust is collected through a dust collector such as a bag filter. After the temperature of the exhaust gas is raised by a reheater, the exhaust gas is passed through a catalyst tower and denitration and dioxin are decomposed and removed by an ammonia coexisting catalyst. The treated process gas is sucked by the induction fan and discharged from the chimney.

  Patent Document 1 describes an exhaust gas treatment apparatus that treats HCl with slaked lime and treats SOx that cannot be treated with slaked lime with a Na-based alkali agent (alkali metal compound) such as sodium bicarbonate.

JP 2010-221150 A

  However, since Na-based alkaline agents such as sodium bicarbonate are expensive, an exhaust gas treatment apparatus capable of treating exhaust gas at a low cost by reducing the amount of Na-based alkaline agents such as sodium bicarbonate is desired.

  The present invention has been made in consideration of such circumstances, and an object of the present invention is to provide an exhaust gas treatment apparatus that enables removal of harmful substances from exhaust gas at a lower cost of treatment chemicals.

In order to solve the above problems, the present invention provides the following means.
That is, the exhaust gas treatment apparatus of the present invention includes a dust collector that introduces exhaust gas and discharges a processing gas, a gas passage that introduces the exhaust gas into the dust collector, and a first HCl that detects the HCl concentration of the exhaust gas. A detection unit, a first SOx detection unit that detects the SOx concentration of the exhaust gas, and a Ca-based alkaline agent or a Ca-based alkaline agent and a Na-based alkaline agent having a weight determined by the control command based on the control command. An alkali supply unit that supplies the alkali agent to the gas flow path; and a control device that determines the weight of the alkali agent and sends the control command. The control device is detected by the first HCl detection unit. and HCl concentration that is, to increase the weight of the Ca-based alkali agent HCl / SOx ratio calculated from the SOx concentration detected by the first SOx detection unit in the case of more than a predetermined value HCl / SOx ratio is characterized by increasing the weight of the Na-based alkaline agent in the case of less than a predetermined value.

  According to the above configuration, by optimizing the weight of the alkaline agent supplied to the exhaust gas based on the HCl / SOx ratio, high exhaust gas treatment performance can be obtained with a minimum amount of treatment agent, and a cheaper treatment agent. The operation of the exhaust gas treatment device is possible at a cost.

  According to the said structure, since the weight of Na type alkali agent is increased only when HCl / SOx ratio is below a predetermined value, the usage-amount of Na type alkali agent can be reduced more.

The exhaust gas treatment apparatus further includes an H ₂ O detection unit that detects an H ₂ O concentration of the exhaust gas, and a humidifying unit that humidifies the exhaust gas, and the control device has an H ₂ O concentration of a predetermined value or less. In this case, it is preferable that the exhaust gas is humidified using the humidifying means and the weight of the alkaline agent is not changed.

According to the above configuration, when the H ₂ O concentration is equal to or lower than the predetermined value, only the humidification process is performed, so that the process can be performed at a lower cost. Further, by increasing the moisture concentration of the exhaust gas by humidification, the reactivity of HCl and the like in the exhaust gas can be increased and the desalination rate can be improved.

The exhaust gas treatment apparatus further includes a temperature detection unit that detects a temperature of the exhaust gas flowing into the dust collector, wherein the control device has an H ₂ O concentration equal to or lower than a predetermined value and the exhaust gas temperature is a predetermined temperature. In the above case, the weight of the Na-based alkaline agent may be increased.

According to the above configuration, since the processing is performed without supplying moisture to the exhaust gas even when the H ₂ O concentration is low, the exhaust gas can be processed without lowering the temperature of the dust collector below a predetermined temperature.

  In the exhaust gas treatment apparatus, it is preferable that the control device does not change the weight of the alkaline agent when the SOx concentration of the exhaust gas is a predetermined value or less.

  According to the above configuration, since the control based on the HCl / SOx ratio is performed only when the SOx concentration of the exhaust gas is a predetermined value or more, the detection means for the processing gas discharged from the dust collector can be omitted. Thus, the exhaust gas treatment apparatus can be operated at a lower cost of the treatment agent.

  The exhaust gas treatment apparatus further includes a second SOx detection unit that detects the SOx concentration of the processing gas, and the control device changes the weight of the alkaline agent when the SOx concentration of the processing gas is a predetermined value or less. Preferably not.

  According to the above configuration, the exhaust gas treatment apparatus can be operated at a lower cost of the treatment agent by performing the control based on the HCl / SOx ratio only when the SOx concentration of the treatment gas is a predetermined value or more.

  In the exhaust gas treatment apparatus, it is preferable that the control device increases the weight of the Ca-based alkaline agent and does not change the weight of the Na-based alkaline agent when the HCl concentration of the exhaust gas is a predetermined value or more. .

  According to the above configuration, when the HCl concentration of the exhaust gas is high, only the Ca-based alkaline agent is increased, so that the amount of Na-based alkaline agent used can be further reduced.

  The exhaust gas treatment apparatus further includes a second HCl detection unit that detects an HCl concentration of the processing gas, and the control device is configured to reduce a weight of the Ca-based alkaline agent when the HCl concentration of the processing gas is equal to or higher than a predetermined value. It is preferable not to change the weight of the Na-based alkaline agent.

  According to the above configuration, when the HCl concentration of the processing gas is high, only the Ca-based alkaline agent is increased, so that the amount of Na-based alkaline agent used can be further reduced.

  Further, in the exhaust gas treatment apparatus, the dust collector is a bag filter, and includes a weight measurement computing unit that measures a deposited weight per unit area of the surface body layer deposited on the surface of the bag filter, and the control It is preferable that the apparatus does not change the weight of the alkaline agent when the deposition weight is equal to or greater than a predetermined value.

  According to the above configuration, the exhaust gas treatment device can be operated at a lower cost of the treatment agent by performing the control based on the HCl / SOx ratio only when the surface accumulation layer of the bag filter is thin.

  Further, in the exhaust gas treatment apparatus, the dust collector is a bag filter, and includes a weight measurement computing unit that measures a deposition weight per unit area of a surface deposition layer deposited on a surface of the bag filter, and the control The apparatus increases the weight of the Ca-based alkaline agent when the deposition weight is equal to or less than a predetermined value and the HCl / SOx ratio is equal to or greater than the predetermined value, and the deposition weight is equal to or greater than the predetermined value or the HCl / SOx ratio. When is less than a predetermined value, it is preferable to increase the weight of the Na-based alkaline agent.

  According to the above configuration, when the deposition weight of the surface deposition layer of the bag filter is equal to or less than the predetermined value, the Ca chloride alkaline agent amount can be stably generated by increasing the Ca alkali agent, and the dust collection It is possible to suppress a reduction in exhaust gas treatment performance in the apparatus.

  The exhaust gas treatment apparatus further includes a second SOx detection unit that detects the SOx concentration of the process gas, and a second HCl detection unit that detects the HCl concentration of the process gas. It is preferable to increase the Na-based alkaline agent when the HCl concentration of the gas is not more than a predetermined value and the SOx concentration of the processing gas is not less than the predetermined value.

  According to the above configuration, when the SOx concentration of the processing gas is high, the processing gas can be neutralized by the Na-based alkaline agent.

The exhaust gas treatment apparatus further includes an H2O detection unit that detects an H2O concentration of the exhaust gas, and a humidifying unit that humidifies the exhaust gas, and the control device has an SOx concentration of the treatment gas of a predetermined value or more. The weight of the Ca-based alkaline agent is increased when the H2O concentration is equal to or higher than a predetermined value, and the humidifying means is used when the SOx concentration of the processing gas is equal to or higher than the predetermined value and the H2O concentration is equal to or lower than the predetermined value. Rukoto to humidify the exhaust gas Te is preferred.

According to the above configuration, when the H ₂ O concentration is equal to or lower than the predetermined value, only the humidification process is performed, so that the process can be performed at a lower cost. Moreover, the desalination rate can be improved by humidifying the HCl or the like in the exhaust gas into an aqueous solution to cause a solid-liquid reaction.

In the exhaust gas treatment apparatus, the dust collector is a bag filter, and includes a H ₂ O detection unit that detects the H ₂ O concentration of the exhaust gas. The alkali supply unit is a Ca-based alkaline agent, and has a specific surface area of 12 -15 m ² / g, pore volume of 0.03 to 0.07 cm ³ / g, special slaked lime equivalent to JIS special name, specific surface area of 30 m ² / g or more, pore volume of 0.1 to 0.3 cm ³ / G of high-reaction slaked lime can be supplied, and the control device may selectively use the special slaked lime and the high-reaction slaked lime based on the H ₂ O concentration and the HCl / SOx ratio.

According to the said structure, the usage-amount of the highly reactive slaked lime which is high cost can be reduced by clarifying the use conditions from which the direction which uses special slaked lime becomes high efficiency.
Moreover, the differential pressure | voltage rise in a dust collector by excess lime supply can be prevented.

  Further, in the exhaust gas treatment apparatus, the desulfurization rate when using the special slaked lime and the desulfurization rate when using the high-reaction slaked lime, the boundary line for selectively using the special slaked lime and the high-reaction slaked lime created from It is preferable that the control device includes a figure, and the special slaked lime and the highly reactive slaked lime are selectively used based on the selectively used boundary diagram.

In the exhaust gas treatment apparatus, it is preferable that the separate boundary diagram is created from a performance diagram composed of the HCl / SOx ratio and the desulfurization rate created for each of the plurality of H ₂ O concentrations.

  In the exhaust gas treatment apparatus, it is preferable to use Fourier transform infrared measurement for the first HCl detection unit and the first SOx detection unit.

  According to the present invention, by optimizing the weight of the alkaline agent supplied to the exhaust gas based on the HCl / SOx ratio, high exhaust gas treatment performance can be obtained with a minimum amount of treatment agent, and a cheaper treatment agent. The operation of the exhaust gas treatment device is possible at a cost.

1 is a system diagram of an exhaust gas treatment apparatus according to a first embodiment of the present invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 2nd embodiment of this invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 3rd embodiment of this invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 4th embodiment of this invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 5th embodiment of this invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 6th embodiment of this invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 7th embodiment of this invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 8th embodiment of this invention. It is a systematic diagram of the exhaust gas processing apparatus which concerns on 9th embodiment of this invention. It is a performance diagram which shows the desulfurization rate in case water concentration is 20 vol%. It is a performance diagram which shows the desulfurization rate in case water concentration is 18 vol%. It is a performance diagram which shows the desulfurization rate in case water concentration is 16 vol%. It is a boundary-line figure which uses Ca type alkali agent properly. FIG. 3 is a boundary diagram of proper use of Ca-based alkaline agent at a gas temperature of 170 ° C. FIG. 3 is a boundary diagram for properly using a Ca-based alkaline agent at a gas temperature of 150 ° C.

(First embodiment)
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
As shown in FIG. 1, the exhaust gas treatment device 1 of the present embodiment includes a dust collector 3, a gas flow path 5 for introducing exhaust gas 4 discharged from the combustion facility 2 into the dust collector 3, and a dust collector 3. The first HCl detection unit 6 that detects the HCl concentration of the exhaust gas 4 introduced into the exhaust gas, the first SOx detection unit 7 that detects the SOx concentration of the exhaust gas 4, the control device 8, and the alkaline agent are supplied to the gas flow path 5. And a chimney 13 that discharges the processing gas 9 discharged from the dust collector 3 to the atmosphere.

  The first HCl detection unit 6 and the second SOx detection unit 22 are measuring instruments using FT-IR (Fourier transform infrared measurement), but are a mass spectrometer, gas chromatography, vacuum ultraviolet light / mass spectrometer. An optical detector such as an absorptiometer or a laser measuring device can also be employed.

The combustion facility 2 is, for example, a combustion furnace, an incinerator, a pyrolysis furnace, or a melting furnace.
Inside the dust collector 3, a bag filter (catalyst bag filter) that is isolated in a plurality of chambers and carries a bag filter or a catalyst is provided in each chamber. As the catalyst, a titanium-vanadium catalyst containing titanium oxide, vanadium pentoxide, molybdenum oxide, tungsten oxide, or the like can be used.

  The alkali supply part 10 is provided in the downstream of the slaked lime supply part 11 which supplies Ca (calcium) type | system | group alkaline agents, such as slaked lime, and the sodium bicarbonate which supplies Na (sodium) type | system | group alkaline agents, such as sodium bicarbonate. And a supply unit 12. That is, the exhaust gas 4 flowing through the gas flow path 5 is configured such that a Ca-based alkaline agent is first supplied and then a Na-based alkaline agent is supplied.

  The slaked lime supply unit 11 is configured to supply a Ca-based alkaline agent having a weight determined by a control command sent from the control device 8. Similarly, the baking soda supply unit 12 is configured to supply a Na-based alkaline agent having a weight determined by a control command sent from the control device 8.

The alkaline agent is a neutralizing agent for neutralizing acidic gas components such as hydrogen chloride (HCl, hydrochloric acid) and sulfur oxide (SOx).
The Ca-based alkaline agent is generally Ca (OH) ₂ (slaked lime). Hereinafter, the Ca-based alkaline agent will be described as slaked lime.
The Na-based alkaline agent is generally NaHCO ₃ (sodium bicarbonate, sodium bicarbonate). Hereinafter, the Na-based alkaline agent will be described as baking soda.

  The control device 8 receives the HCl concentration of the exhaust gas 4 detected by the first HCl detection unit 6 and the SOx concentration of the exhaust gas 4 detected by the first SOx detection unit 7 and supplies alkali based on the detection value. The weight of the alkali agent supplied from the unit 10 is determined and a control command is sent to the alkali supply unit 10.

Next, the control method of the exhaust gas treatment apparatus 1 of the present embodiment will be described.
The control device 8 of this embodiment is configured such that the ratio of the HCl concentration (ppm) detected by the first HCl detection unit 6 to the SOx concentration (ppm) detected by the first SOx detection unit 7, that is, the HCl / SOx ratio = β is calculated, and the amount of alkaline agent used is controlled based on the value of β.

  Specifically, the control device 8 performs control to increase the weight of slaked lime when β is larger than a predetermined value (for example, 3 to 5). Then, when β is smaller than a predetermined value, the control device 8 supplies a predetermined weight of slaked lime to the gas flow path 5 and performs control to increase the weight of the baking soda.

  As described above, the value of β is 3 to 5, for example. This value is a value that assumes a case where the HCl concentration in the exhaust gas 4 is slightly high (800 ppm to 1200 ppm) and the SOx concentration is high (200 ppm to 300 ppm). That is, when the SOx concentration of the exhaust gas 4 is high, control is performed to supply baking soda to the gas flow path 5 in addition to slaked lime in order to reduce the SOx concentration.

According to the above embodiment, the weight of the alkaline agent supplied to the exhaust gas 4 is optimized by determining the weight of the alkaline agent composed of the Ca-based alkaline agent and the Na-based alkaline agent based on β which is the HCl / SOx ratio. Therefore, the exhaust gas treatment device 1 can be operated at a lower cost of the treatment agent.
Furthermore, since the weight of the Na-based alkaline agent such as baking soda is increased only when the HCl / SOx ratio = β is equal to or less than the predetermined value, the amount of Na-based alkaline agent used can be further reduced.

(Second embodiment)
Hereinafter, an exhaust gas treatment apparatus 1B according to a second embodiment of the present invention will be described with reference to the drawings.
FIG. 2 is a system diagram showing an example of the exhaust gas treatment apparatus 1B according to the present embodiment. In the present embodiment, differences from the first embodiment described above will be mainly described, and description of similar parts will be omitted.

As shown in FIG. 2, in the exhaust gas treatment apparatus 1 </ b> B of the present embodiment, a temperature reducing tower 15 is provided on the upstream side of the gas flow path 5 as a humidifying means for reducing the exhaust gas temperature and humidifying the exhaust gas 4. Yes. The temperature reducing tower 15 is supplied with temperature-reduced water from a water supply device 17 through a temperature-reducing water pipe 16. Further, on the downstream side of the first HCl detector 6, _{H 2} O detection unit 18 for detecting the concentration of _{H 2} O is provided. Further, on the upstream side of the alkali supply unit 10, a water vapor supply unit 19 is provided as a humidifying means for humidifying the exhaust gas 4.

Next, a control method of the exhaust gas treatment apparatus 1B of the present embodiment will be described.
The control device 8 of the present embodiment is characterized in that the exhaust gas 4 is treated in consideration of the H ₂ O concentration in the exhaust gas 4 in addition to the HCl / SOx ratio. That is, the control device 8 performs control to humidify the exhaust gas 4 when the H ₂ O concentration of the exhaust gas 4 detected by the H ₂ O detection unit 18 is a predetermined value or less (for example, 20% or less). Specifically, the control device 8 sends a control command for supplying water vapor to the gas flow path 5 to the water vapor supply unit 19 when the H ₂ O concentration is a certain value or less, or A control command for increasing the amount of water in the temperature reducing tower 15 is sent to the water supply device 17.

On the other hand, when the H ₂ O concentration is a certain value or more, the same control as in the first embodiment is performed. That is, the exhaust gas 4 is treated by controlling the amount of alkaline agent (slaked lime, baking soda) based on the value of HCl / SOx ratio = β.

According to the above embodiment, by referring to the H ₂ O concentration in addition to the HCl / SOx ratio, the Ca-based alkaline agent, the moisture / steam, and the Na-based alkaline agent that is less affected by the moisture concentration are selectively used and adjusted. More optimal treatment of the exhaust gas 4 can be performed.
Further, when the H ₂ O concentration is equal to or lower than the predetermined value, only the humidification process is performed, so that the process can be performed at a lower cost. Further, by increasing the water concentration in the exhaust gas 4 by humidification, the reactivity of HCl or the like in the exhaust gas 4 can be increased, and the desalination rate can be improved.

  In the above embodiment, the control device 8 monitors the SOx concentration of the exhaust gas 4, and when the SOx concentration of the exhaust gas 4 is a predetermined value (for example, 100 ppm) or less, the weight of the alkali agent is not changed, that is, the HCl / SOx ratio. It is good also as a structure which does not perform control based on. By performing such control, exhaust gas treatment can be performed at a lower cost.

(Third embodiment)
Hereinafter, an exhaust gas treatment apparatus 1C according to a third embodiment of the present invention will be described with reference to the drawings.
FIG. 3 is a system diagram showing an example of the exhaust gas treatment apparatus 1C according to the present embodiment. In the present embodiment, differences from the first embodiment described above will be mainly described, and description of similar parts will be omitted.

The apparatus configuration of the exhaust gas treatment apparatus 1 </ _b > C of the present embodiment is provided with an H ₂ O detection unit 18 and a water vapor supply unit 19 similar to those of the second embodiment in addition to the apparatus configuration of the first embodiment. . Furthermore, a temperature detector 21 is provided on the inlet side of the dust collector 3, and the detected temperature is configured to be input to the control device 8.

Next, a control method of the exhaust gas treatment apparatus 1C according to the third embodiment will be described.
The control device 8 of the present embodiment is characterized by determining whether to humidify the exhaust gas 4 or supply baking soda to the exhaust gas 4 according to the temperature of the exhaust gas 4 flowing into the dust collector 3.
That is, the control device 8 monitors the temperature detected by the temperature detection unit 21. For example, the H ₂ O concentration is a predetermined value or less (for example, 18 vol% or less) and the exhaust gas detected by the temperature detection unit 21 is used. When the temperature is equal to or higher than a predetermined value (for example, 180 ° C. or higher), control is performed to increase the baking soda supplied from the baking soda supply unit 12.
On the other hand, when the H ₂ O concentration is a certain value or more, the same control as in the first embodiment is performed. That is, the exhaust gas 4 is treated by controlling the amount of alkaline agent (slaked lime, baking soda) based on the value of HCl / SOx ratio = β.

According to the above embodiment, when the H ₂ O concentration is low, the treatment is performed without supplying moisture to the exhaust gas 4, so the exhaust gas 4 is treated without lowering the temperature of the dust collector 3 below a predetermined temperature. be able to.

In addition, if it is not necessary to consider the temperature of the exhaust gas 4 introduced into the dust collector 3, the control for humidifying the exhaust gas 4 by the water vapor supply unit 19 when the H ₂ O concentration is a predetermined value or less (for example, 18 vol% or less). It is good also as composition which performs.
Moreover, it is also possible to combine the configuration of this embodiment with the temperature reducing tower 15 of the second embodiment to further humidify the exhaust gas 4 on the upstream side.

(Fourth embodiment)
Hereinafter, an exhaust gas treatment apparatus 1D according to a fourth embodiment of the present invention will be described with reference to the drawings.
FIG. 4 is a system diagram showing an example of the exhaust gas treatment apparatus 1D according to the present embodiment.
In addition to the apparatus configuration of the second embodiment, the apparatus configuration of the exhaust gas processing apparatus 1D of the present embodiment is provided with a second SOx detection unit 22 that detects the SOx concentration of the processing gas 9 discharged from the dust collector 3. Is. As the second SOx detector 22, a measuring instrument using Fourier transform infrared measurement can be employed.

Next, a control method of the exhaust gas treatment apparatus 1D according to the fourth embodiment will be described.
The control device 8 of this embodiment is characterized by determining whether or not to perform control based on the HCl / SOx ratio according to the SOx concentration of the processing gas 9 discharged from the dust collector 3.
That is, the control device 8 does not change the supply amount (weight) of the alkaline agent when the SOx concentration of the processing gas 9 detected by the second SOx detection unit 22 is a predetermined value (for example, 15 ppm to 20 ppm) or less. Take control. On the other hand, when the SOx concentration of the processing gas 9 detected by the second SOx detector 22 is equal to or higher than a predetermined value, the same control as in the first to third embodiments is performed. That is, the exhaust gas 4 is treated by controlling the amount of alkali agent (slaked lime, baking soda) used based on the value of the HCl / SOx ratio = β or by humidifying the exhaust gas 4 according to the H ₂ O concentration.

  According to the above embodiment, the control of increasing the weight of slaked lime or baking soda is performed only when the SOx concentration of the processing gas 9 is equal to or higher than a predetermined value, so that the exhaust gas 4 can be processed at a lower cost.

  In addition, it is also possible to add a temperature detection unit 21 installed upstream of the dust collector 3 of the third embodiment to the configuration of the present embodiment to manage the temperature of the dust collector 3. Is possible.

(Fifth embodiment)
Hereinafter, an exhaust gas treatment apparatus 1E according to a fifth embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 5, the apparatus configuration of the exhaust gas treatment apparatus 1E of the present embodiment is a second apparatus that detects the HCl concentration of the process gas 9 discharged from the dust collector 3 in addition to the apparatus configuration of the fourth embodiment. An HCl detector 23 is provided. As the second HCl detector 23, a measuring instrument using Fourier transform infrared measurement can be employed.

The control device 8 of the present embodiment is characterized in that the HCl concentration of the processing gas 9 discharged from the dust collector 3 is used as a material for determining whether or not to perform control based on the HCl / SOx ratio.
That is, the control device 8 does not change the supply amount (weight) of the alkaline agent when the HCl concentration of the processing gas 9 detected by the second HCl detection unit 23 is a predetermined value (for example, 5 ppm to 10 ppm) or less. Take control.
On the other hand, when the HCl concentration of the processing gas 9 detected by the second HCl detector 23 is equal to or higher than a predetermined value, the same control as in the fourth embodiment is performed. That is, the exhaust gas 4 is processed based on the SOx concentration of the processing gas 9, the value of the HCl / SOx ratio = β, the H ₂ O concentration of the exhaust gas 4, and the like.

  According to the above embodiment, the control of increasing the weight of slaked lime or baking soda is performed only when the HCl concentration of the processing gas 9 is equal to or higher than a predetermined value, so that the exhaust gas 4 can be processed at a lower cost.

(Sixth embodiment)
Hereinafter, an exhaust gas treatment apparatus 1F according to a sixth embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 6, the apparatus configuration of the exhaust gas treatment apparatus 1 </ b> F of the present embodiment is a unit of surface body stacking deposited on the surface of the bag filter that is the dust collector 3 in addition to the apparatus configuration of the fifth embodiment. A weight measurement computing unit 24 for measuring the deposited weight per area is provided. The weight measurement calculator 24 indirectly measures the accumulated weight from the bag pressure loss of the dust collector 3, the filtration speed, and the like.

The control device 8 of the present embodiment is characterized by determining whether or not to perform control based on the HCl / SOx ratio according to the state of the surface deposition layer of the bag filter that is the dust collector 3.
That is, the control device 8 changes the supply amount (weight) of the alkaline agent, for example, immediately after backwashing or within a certain period from the start of backwashing when the deposited weight is a predetermined value (for example, 100 g / m ² ) or more. Control that does not occur.
On the other hand, when the accumulated weight is equal to or smaller than the predetermined value, the same control as in the first to fifth embodiments is performed. That is, the exhaust gas 4 is processed based on the SOx concentration of the processing gas 9, the HCl concentration of the processing gas 9, the value of the HCl / SOx ratio = β, the H ₂ O concentration of the exhaust gas 4, and the like.

According to the above embodiment, only when the surface deposition layer deposited on the surface of the bag filter becomes thin, the treatment of the exhaust gas 4 based on the value of HCl / SOx ratio = β, the H ₂ O concentration of the exhaust gas 4 and the like. Therefore, the exhaust gas 4 can be processed at a lower cost.

(Seventh embodiment)
Hereinafter, an exhaust gas treatment apparatus 1G according to a seventh embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 7, in addition to the apparatus configuration of the exhaust gas treatment apparatus 1 of the first embodiment, the apparatus configuration of the exhaust gas treatment apparatus 1G of the present embodiment is the same as the second SOx detection unit 22, as in the sixth embodiment. A second HCl detector 23 and a weight measuring calculator 24 are provided, and a disk-shaped rotary atomizer 25 is further provided upstream of the gas flow path 5. The rotary atomizer 25 is provided with a slurry supply unit 26 that supplies slaked lime slurry to the rotary atomizer 25.

For example, when the weight per unit area of the surface deposition layer is a predetermined value (for example, 100 g / m ² ) or more immediately after backwashing or within a certain period from the start of backwashing, the control device 8 supplies sodium bicarbonate. Control to increase the baking soda supplied from the section 12 is performed.
When the accumulated weight is equal to or less than a predetermined value and the value of HCl / SOx ratio = β is equal to or greater than a predetermined value (for example, 3 to 5), control is performed to increase the slaked lime slurry supplied to the rotary atomizer 25. .

Further, after the slaked lime slurry is charged, even if the HCl concentration of the processing gas 9 is a predetermined value (for example, 500 ppm) or less, if the SOx concentration of the processing gas 9 is the predetermined value (for example, 100 ppm) or more, the control for increasing the baking soda is performed. Do.
On the other hand, when the deposited weight is equal to or greater than a predetermined value, or when the value of β is equal to or smaller than the predetermined value, the weight of the alkaline agent is not controlled.

According to the above embodiment, even when the surface deposited layer immediately after backwashing is thin, by increasing the weight of the slaked lime slurry in the rotary atomizer 25 on the upstream side of the dust collector 3, the Ca chloride-based reactant amount can be stabilized. It is possible to reduce the exhaust gas treatment performance in the dust collector 3.
Further, when the SOx concentration of the processing gas 9 is high, the processing gas 9 can be neutralized with sodium bicarbonate.

  In this embodiment, the rotary atomizer 25 is installed as a supply destination of the slaked lime slurry, but when spraying the slaked lime slurry, it may be introduced into the temperature reducing tower 15 and sprayed. The temperature reduction effect of the exhaust gas 4 can be obtained at the same time.

(Eighth embodiment)
Hereinafter, an exhaust gas treatment apparatus 1H according to an eighth embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 8, in addition to the apparatus configuration of the exhaust gas treatment apparatus 1G of the seventh embodiment, the apparatus configuration of the exhaust gas treatment apparatus 1H of the present embodiment is similar to the H ₂ O detection unit 18 in the second embodiment, A water vapor supply unit 19 is provided, and a water supply unit 27 is provided in addition to the slurry supply unit 26 in the rotary atomizer 25.

As in the seventh embodiment, the control device 8 controls the supply amount (weight) of the alkaline agent when the deposition weight of the surface deposition layer of the bag filter is a predetermined value (for example, 100 g / m ² ) or more. Absent.
When the accumulated weight is equal to or less than a predetermined value and the value of HCl / SOx ratio = β is equal to or greater than a predetermined value (for example, 3 to 5), control is performed to increase the slaked lime slurry supplied to the rotary atomizer 25. .

Further, after the slaked lime slurry is charged, if the HCl concentration of the processing gas 9 is not more than a predetermined value (for example, 500 ppm) and the SOx concentration of the processing gas 9 is not less than the predetermined value (for example, 100 ppm), the alkali is based on the H ₂ O concentration. Control the agent and humidification. Specifically, when the H ₂ O concentration is equal to or higher than a predetermined value (for example, 18 vol%), control is performed to increase slaked lime, and when the H ₂ O concentration is equal to or lower than the predetermined value, water is poured into the rotary atomizer 25. Alternatively, steam is supplied to the exhaust gas 4 to humidify the exhaust gas 4.
On the other hand, when the deposited weight is equal to or greater than a predetermined value, or when the value of β is equal to or smaller than the predetermined value, the weight of the alkaline agent is not controlled.

According to the above embodiment, when the H ₂ O concentration is equal to or lower than the predetermined value, only the humidification process is performed, so that the process can be performed at a lower cost. In addition, the desalination rate can be improved by performing a solid-liquid reaction by bringing HCl or the like in the exhaust gas 4 into an aqueous solution state by humidification.

(Ninth embodiment)
Hereinafter, an exhaust gas treatment apparatus 1J according to a ninth embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 9, the apparatus configuration of the exhaust gas treatment apparatus 1J of the present embodiment includes an H ₂ O detection unit 18 similar to that of the second embodiment in addition to the apparatus configuration of the exhaust gas treatment apparatus 1A of the first embodiment. Furthermore, it is the apparatus structure by which the slaked lime supply part 11 is comprised from the special slaked lime supply part 11a and the highly reactive slaked lime supply part 11b.

The special slaked lime supply unit 11 a is configured to supply industrial gas slaked lime (hereinafter referred to as special slaked lime) equivalent to the JIS special number to the gas flow path 5 in accordance with a command from the control device 8. The highly reactive slaked lime supply unit 11 b is configured to supply highly reactive slaked lime, which is a dedicated chemical for acid gas components, to the gas flow path 5.
High-reaction slaked lime is an acid gas remover whose specific surface area and pore volume are about three times that of special slaked lime. However, highly reactive slaked lime is more disadvantageous in terms of cost than special slaked lime.

Specifically, the special slaked lime has a specific surface area of 12 to 15 m ² / g, a pore volume of 0.07 cm ³ / g, and an average particle size of 5.0 to 7.0 μm.
The specific surface area of the highly reactive slaked lime is 30 m ² / g or more, the pore volume is 0.2 cm ³ / g, and the average particle size is 8.0 to 12.0 μm.

The control device 8 of the present embodiment controls the usage amount of the alkaline agent based on the HCl / SOx ratio = β and the H ₂ O concentration. Specifically, in addition to the control of the first embodiment, the control device 8 uses slaked lime using a Ca-based alkaline agent selective boundary diagram (hereinafter referred to as a selective boundary diagram) created based on the desulfurization performance. The control which uses properly is performed.

Here, a method for creating a boundary diagram will be described.
First, when each of special slaked lime and highly reactive slaked lime is used, k _SOx (reaction rate constant), L (surface deposited layer thickness), and LV (filtration rate) are used, according to the following formula (1). Desulfurization rate η _SOx is calculated.

k _SOx is a reaction rate constant and is determined by slaked lime physical properties, α and β described below, temperature, and the like. The slaked lime physical properties are pore volume, specific surface area, etc., and _kSOx increases as these values increase. L / LV represents the reaction time.

k _SOx can be calculated using the following formula (2).
k _SOx = F (α) · G (β) · H (C _H2O ) (2)
α is a ratio of the HCl concentration of the exhaust gas treatment device to the slaked lime supply amount and the SOx concentration, and is a value that serves as an index indicating how much slaked lime is a reactant with respect to the HCl concentration and the SOx concentration, Using C _{Ca (OH) 2} (slaked lime supply amount), C _HCl (inlet HCl concentration), and C _SOx (inlet SOx concentration), it can be calculated by the following formula (3).
α = C _{Ca (OH) 2} /(0.5·C _HCl + C _SOx ) (3)

For example, HCl and SOx react with slaked lime by the following reaction.
Ca (OH) ₂ + 2HCl → CaCl ₂ + 2H ₂ O
Ca (OH) ₂ + SO ₂ → CaSO ₃ + 2H ₂ O

As described above, β is the ratio between the HCl concentration and the SOx concentration, and can be calculated by the following formula (4).
β = _CHCl / _CSOx (4)
C _H2O is the moisture concentration.

L is the thickness of the surface deposition layer (dust layer) deposited on the surface of the bag filter, C _d (dust concentration), u _N (flow velocity), t (reaction time / dust volume time), ρ (surface deposition) It can be calculated by the following formula (5) using the layer bulk density. n is a constant.

That is, the desulfurization rate η _SOx can be calculated by substituting the formula (2), the LV value, and the formula (5) into the formula (1). Here, k _SOx can be obtained by substituting Equation (3), Equation (4), and C _H2O into Equation (2).

Next, the desulfurization rate η _SOx under each exhaust gas treatment condition (temperature, α, β, moisture concentration) is calculated using the above mathematical formula. For example, a performance diagram is created for each moisture concentration for special slaked lime and highly reactive slaked lime.
FIG. 10 is a performance diagram showing the desulfurization rate _ηSOx with respect to the HCl / SOx ratio β when the water concentration is 20 vol%. FIG. 11 is a performance diagram showing the desulfurization rate η _SOx with respect to the HCl / SOx ratio β when the water concentration is 18 vol%. 12, when the water content 16 vol%, a performance diagram showing the desulfurization rate eta _SOx against HCl / SOx ratio beta.

In these figures, the intersection of the performance curves of special slaked lime and highly reactive slaked lime is obtained. Actually, a plurality of performance diagrams are created in steps of about 1% of the moisture concentration, and the intersection point is obtained from each performance diagram. That is, if the value of from the intersection point β is small, can not maintain a high reaction slaked an unless desulfurization efficiency eta _SOx. If the value of β is larger than this intersection, it is more efficient to use special slaked lime, and it is not necessary to use highly reactive slaked lime that requires high costs.

Then, the relationship between the β value of the X coordinate axis of the intersection and the moisture concentration is made into a graph as shown in FIG. 13, and this is used as a boundary diagram. According to this separately used boundary diagram, if the point where the measured β and moisture concentration are plotted is higher than the separately used boundary line obtained by a plurality of intersections, the desulfurization rate η _SOx is better when the special slaked lime is used. Becomes higher. That is, it is possible to use a low-cost and high-efficiency Ca-based alkaline agent.
As can be seen from FIGS. 12 and 13, the lower the moisture concentration, the lower the desulfurization rate η _SOx of the special slaked lime, and the β range that requires highly reactive slaked lime is expanded.

Next, a control method of the exhaust gas treatment apparatus 1J of the present embodiment will be described.
The control apparatus 8 of this embodiment determines the usage-amount of an alkaline agent based on the value of HCl / SOx ratio = (beta) similarly to the exhaust gas processing apparatus 1 of 1st embodiment.

Here, with regard to slaked lime, the optimum type (low cost and high efficiency) of the Ca-based alkaline agent is selected and used based on the proper boundary diagram as shown in FIG. That is, the H ₂ O concentration (water concentration) and the value of the HCl / SOx ratio = β are plotted on the boundary diagram, and the special slaked lime and the highly reactive slaked lime are used separately.

According to the said embodiment, the usage-amount of the high-reaction slaked lime which is high cost can be reduced by clarifying the use conditions from which the direction which uses special slaked lime becomes high efficiency.
In other words, since the desulfurization rate _ηSOx is strongly influenced by the correlation between the moisture concentration and the HCl / SOx ratio, the type of Ca alkaline agent is changed or the amount is adjusted depending on the moisture concentration value and the HCl / SOx ratio. By performing optimal control, it is possible to obtain high exhaust gas treatment performance with a minimum amount and at a low cost.
Moreover, the differential pressure | voltage rise in the dust collector 3 by excess lime supply can be prevented.

The first HCl detection unit 6, the first SOx detection unit 7, and the H ₂ O detection unit 18 are provided upstream of the dust collector 3, and the installation location thereof is from the dust collector 3 to the combustion facility 2. It can be anywhere between the exits. Further, when the HCl concentration, the SOx concentration, and the H ₂ O concentration at the outlet of the combustion facility 2 can be predicted, measurement is not necessary, and a separate boundary diagram may be created based on the predicted value.

(Modification of the ninth embodiment)
Next, a modification of the ninth embodiment will be described. In this modification, a Ca-based alkaline agent use boundary diagram is created for each use temperature, and slaked lime is selected and used based on this use boundary diagram.

For example, the boundary diagram for proper use at a filtration rate LV = 0.8 m / min, a gas temperature T = 170 ° C., and α = 3 is as shown in FIG. The boundary diagram for proper use at the filtration rate LV = 0.8 m / min, the gas temperature T = 150 ° C., and α = 3 (that is, when the temperature is changed with respect to FIG. 14) is as shown in FIG. Become.
According to FIG.14 and FIG.15, the use condition range of the special name slaked lime which is low cost and highly efficient becomes wide as gas temperature is low temperature and moisture concentration is high.

  The technical scope of the present invention is not limited to the above embodiment, and various modifications can be made without departing from the spirit of the present invention. For example, in each embodiment described above, the alkaline agent is configured to be supplied to the downstream side of the first SOx detection unit 7 and the first HCl detection unit 6, but is configured to be supplied to the upstream side of these detection units. Also good.

1, 1B, 1C, 1D, 1E, 1F, 1G, 1H, 1J Exhaust gas treatment device 2 Combustion equipment 3 Dust collector 4 Exhaust gas 5 Gas flow path 6 First HCl detection portion 7 First SOx detection portion 8 Control device 9 Treatment Gas 10 Alkali supply unit 11 Slaked lime supply unit 11a Special slaked lime supply unit 11b High reaction slaked lime supply unit 12 Sodium bicarbonate supply unit 15 Temperature reducing tower 16 Temperature-reducing water pipe 17 Water supply device 18 H2O detection unit 19 Water vapor supply unit 21 Temperature detection unit 22 2 SOx detector 23 Second HCl detector 24 Weighing calculator 25 Rotary atomizer 26 Slurry supply unit 27 Water supply unit

Claims (15)

A dust collector for exhaust gas being introduced and exhausting process gas;
A gas flow path for introducing the exhaust gas into the dust collector;
A first HCl detector for detecting the HCl concentration of the exhaust gas;
A first SOx detector that detects the SOx concentration of the exhaust gas;
An alkali supply unit that supplies a Ca-based alkaline agent having a weight determined by the control command based on the control command, or an alkaline agent containing a Ca-based alkaline agent and a Na-based alkaline agent to the gas flow path;
A controller for determining the weight of the alkaline agent and sending the control command,
When the HCl / SOx ratio calculated from the HCl concentration detected by the first HCl detector and the SOx concentration detected by the first SOx detector is a predetermined value or more, the control device An exhaust gas treatment apparatus characterized by increasing the weight of the agent and increasing the weight of the Na-based alkaline agent when the HCl / SOx ratio is not more than a predetermined value . An H ₂ O detector for detecting the H ₂ O concentration of the exhaust gas;
Humidifying means for humidifying the exhaust gas,
Wherein the control device, H 2 _O concentration is humidified the exhaust gas by using the humidifying means in the case of less than the predetermined value, the exhaust gas processing device according to claim 1, characterized in that the weight of the alkaline agent is not changed . A temperature detector for detecting the temperature of the exhaust gas flowing into the dust collector;
3. The exhaust gas treatment according to claim 2 , wherein the control device increases the weight of the Na-based alkaline agent when the H ₂ O concentration is equal to or lower than a predetermined value and the temperature of the exhaust gas is equal to or higher than a predetermined temperature. apparatus. The exhaust gas treatment apparatus according to any one of claims 1 to 3 , wherein the control device does not change the weight of the alkaline agent when the SOx concentration of the exhaust gas is a predetermined value or less. A second SOx detector that detects the SOx concentration of the processing gas;
The exhaust gas treatment device according to any one of claims 1 to 4 , wherein the control device does not change the weight of the alkaline agent when the SOx concentration of the treatment gas is a predetermined value or less. The control device increases the weight of the Ca-based alkaline agent and does not change the weight of the Na-based alkaline agent when the HCl concentration of the exhaust gas is a predetermined value or more. exhaust gas treatment apparatus according to any one of 5. A second HCl detector for detecting the HCl concentration of the process gas;
The control device increases the weight of the Ca-based alkaline agent and does not change the weight of the Na-based alkaline agent when the HCl concentration of the processing gas is a predetermined value or more. The exhaust gas treatment apparatus according to any one of claims 6 to 6 . The dust collector is a bag filter;
Comprising a weight measuring calculator for measuring a weight deposited per unit area of the surface body layer deposited on the surface of the bag filter;
The exhaust gas treatment apparatus according to any one of claims 1 to 7 , wherein the control device does not change a weight of the alkaline agent when the accumulated weight is equal to or greater than a predetermined value. The dust collector is a bag filter;
A weight measuring calculator for measuring the weight of the surface deposition layer deposited on the surface of the bag filter per unit area;
The controller increases the weight of the Ca-based alkaline agent when the deposition weight is equal to or less than a predetermined value and the HCl / SOx ratio is equal to or greater than a predetermined value.
When the deposited weight is not less than a predetermined value, or the HCl / SOx ratio is not more than a predetermined value,
The exhaust gas treatment apparatus according to claim 1, wherein the weight of the Na-based alkaline agent is increased. A second SOx detector for detecting the SOx concentration of the processing gas;
A second HCl detector for detecting the HCl concentration of the processing gas,
10. The controller according to claim 9, wherein the control device increases the Na-based alkaline agent when an HCl concentration of the processing gas is a predetermined value or less and an SOx concentration of the processing gas is a predetermined value or more. Exhaust gas treatment equipment. An H ₂ O detector for detecting the H ₂ O concentration of the exhaust gas;
Humidifying means for humidifying the exhaust gas,
The control device increases the weight of the Ca-based alkaline agent when the SOx concentration of the processing gas is a predetermined value or more and the H ₂ O concentration is a predetermined value or more,
The SOx concentration in the treated gas is higher than a predetermined value, and exhaust gas treatment of claim 10 wherein the H _{2 O} concentration is characterized that you humidify the flue gas with the humidified means when more than a predetermined value apparatus. The dust collector is a bag filter;
An H ₂ O detector for detecting the H ₂ O concentration of the exhaust gas;
As the alkali supply unit Ca-based alkali agent, a specific surface area 12~15m ² / g, and Japanese Patent slaked lime JIS Japanese Patent considerable a pore volume 0.03~0.07cm ³ / g, a specific surface area of ^{30 m} 2 / g or more, and a highly reactive slaked lime having a pore volume of 0.1 to 0.3 cm ³ / g can be supplied,
The exhaust gas treatment apparatus according to claim 2, wherein the control device selectively uses the special slaked lime and the highly reactive slaked lime based on the H ₂ O concentration and the HCl / SOx ratio. The desulfurization rate when using the special slaked lime, and the desulfurization rate when using the high-reaction slaked lime, comprising a boundary diagram for properly using the special slaked lime and the high-reaction slaked lime,
The exhaust gas treatment device according to claim 12, wherein the control device selectively uses the special slaked lime and the highly reactive slaked lime based on the selectively used boundary diagram. The exhaust gas treatment apparatus according to claim 13, wherein the proper boundary diagram is created from a performance diagram composed of the HCl / SOx ratio and the desulfurization rate created for each of the plurality of H ₂ O concentrations.   The exhaust gas treatment apparatus according to any one of claims 1 to 14, wherein Fourier transform infrared measurement is used for the first HCl detection unit and the first SOx detection unit.

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