Reclaiming apparatus, CO.SUB.2 .recovery apparatus including the same, and reclaiming method

Abstract

A reclaiming apparatus includes: a container; an absorption-liquid supply line for supplying the container with an absorption liquid containing an absorption agent; a water supply line for supplying the container with a water; a steam discharge line for discharging steam from the container; a heating device for heating a liquid containing at least one of the water or the absorption liquid; and a control device configured to determine, on the basis of a temperature of the liquid stored in the container, an ending timing of an absorption-agent recovery process of recovering steam containing the absorption agent via the steam discharge line by heating of the liquid with the heating device.

Claims

1. A reclaiming apparatus, comprising: a container; an absorption-liquid supply line for supplying the container with an absorption liquid containing an absorption agent; a water supply line for supplying the container with a water; a steam discharge line for discharging steam generated from the container; a heating device for heating a liquid containing at least one of the water or the absorption liquid; and a control device configured to determine an ending timing of an absorption-agent recovery process which recovers the steam containing the absorption agent via the steam discharge line by heating the liquid with the heating device based on the temperature of the liquid stored in the container.

2. The reclaiming apparatus according to claim 1, wherein the absorption-agent recovery process includes recovering steam containing the absorption agent via the steam discharge line, by heating the liquid with the heating device while supply of the absorption liquid to the container via the absorption-liquid supply line is shut off and while the container is supplied with the water via the water supply line.

3. The reclaiming apparatus according to claim 1, wherein the control device is configured to determine that the absorption-agent recovery process ends when the temperature of the liquid in the container decreases to a first predetermined temperature.

4. The reclaiming apparatus according to claim 3, wherein the control device is configured to set the first predetermined temperature depending on a pressure inside the container.

5. The reclaiming apparatus according to claim 3, wherein the control device is configured to set the first predetermined temperature depending on the temperature of the liquid in the container at the start of the absorption-agent recovery process.

6. The reclaiming apparatus according to claim 3, wherein the control device is configured to determine an ending timing of an absorption-liquid regeneration process performed before the absorption-agent recovery process by comparing between the temperature of the liquid in the container and a second predetermined temperature which is higher than the first predetermined temperature, and wherein the absorption-liquid regeneration process includes a process of separating non-volatile components which remains in the liquid inside the container and the absorption agent contained in the steam discharged to the steam discharge line, by heating the liquid with the heating device while the absorption liquid is supplied to the container via the absorption-liquid supply line.

7. The reclaiming apparatus according to claim 1, further comprising a valve, installed in the water supply line, for adjusting a supply amount of water to the container, wherein the control device is configured to stop supply of water to the container by closing the valve, if it is determined that the absorption-agent recovery process ends.

8. A CO.sub.2 recovery apparatus, comprising: an absorption tower configured to remove CO.sub.2 in exhaust gas by contacting with an absorption liquid containing an absorption agent; a regeneration tower for regenerating the absorption liquid from the absorption tower; and the reclaiming apparatus according to claim 1, wherein the CO.sub.2 recovery apparatus is configured such that at least a part of the absorption liquid stored in the regeneration tower is supplied to the container via the absorption-liquid supply line.

9. The CO.sub.2 recovery apparatus according to claim 8, further comprising a reflux water drum for separating CO.sub.2 containing gas released from the regeneration tower into CO.sub.2 gas and condensed water, wherein the CO.sub.2 recovery apparatus is configured at least a part of condensed water stored in the reflux water drum is supplied as the water to the container via the water supply line.

Description

BRIEF DESCRIPTION OF DRAWINGS

(1) FIG. 1 is a schematic diagram of a CO.sub.2 recovery apparatus to which a reclaiming apparatus according to an embodiment is applied.

(2) FIG. 2 is a schematic diagram of a reclaiming apparatus in a CO.sub.2 recovery apparatus depicted in FIG. 1.

(3) FIG. 3 is a flowchart of an example of the procedure of a reclaiming method according to an embodiment.

(4) FIG. 4 is a graph showing an example of a correlation relationship between the temperature of a liquid in a container and the non-volatile component in the liquid.

(5) FIG. 5 is a graph showing an example of correlation relationship between the temperature of a liquid inside a container and the concentration of the absorption agent in the liquid.

DETAILED DESCRIPTION

(6) Embodiments of the present invention will now be described in detail with reference to the accompanying drawings. It is intended, however, that unless particularly identified, dimensions, materials, shapes, relative positions and the like of components described in the embodiments shall be interpreted as illustrative only and not intended to limit the scope of the present invention.

(7) First, a CO.sub.2 recovery apparatus will be described, to which a reclaiming apparatus according to some embodiments is applied.

(8) FIG. 1 is a schematic diagram of a CO.sub.2 recovery apparatus to which a reclaiming apparatus according to an embodiment is applied. The CO.sub.2 recovery apparatus shown in FIG. 1 is a device for recovering CO.sub.2 from exhaust gas discharged from a power generation facility or a factory, for instance. As depicted in the drawing, the CO.sub.2 recovery apparatus 1 includes an absorption tower 2 for causing an absorption liquid to absorb CO.sub.2 in exhaust gas from a power generation facility or the like, a regeneration tower 4 for regenerating the absorption liquid having absorbed CO.sub.2, a reflux water drum 6 configured to separate the released gas from the regeneration tower 4 into CO.sub.2 gas and condensed water, and return the condensed water to the regeneration tower 4, and a reclaiming apparatus 10 for reclaiming the absorption liquid.

(9) Exhaust gas containing CO.sub.2 is supplied to the absorption tower 2 via an exhaust gas introduction line 12. Further, a pretreatment device for pre-processing exhaust gas (desulfurization, cooling, etc.) may be installed at the upstream of the absorption tower 2, and the absorption tower 2 may be supplied with exhaust gas after treated with such pretreatment.

(10) The absorption tower 2 includes an absorption part 14 formed by a packed layer, for instance, and the absorption part 14 is supplied with a CO.sub.2 absorption liquid containing a CO.sub.2 absorption agent from above.

(11) The exhaust gas having flown into the absorption tower 2 via the exhaust gas introduction line 12 flows upward through the absorption tower 2 from the side of the tower bottom part of the absorption tower 2, and flows into the absorption part 14. Further, in the absorption part 14, exhaust gas makes counter-current contact with the CO.sub.2 absorption liquid supplied from the upper part of the absorption part 14, and thereby CO.sub.2 in exhaust gas is absorbed by the CO.sub.2 absorption liquid.

(12) The CO.sub.2 absorption liquid may be an aqueous solution of the CO.sub.2 absorption liquid.

(13) The type of the CO.sub.2 absorption agent is not particularly limited. For instance, alkanolamines such as monoethanolamine and diethanolamine, or a basic material other than amines such as sodium hydroxide, potassium hydroxide and calcium hydroxide can be used as the CO.sub.2 absorption agent.

(14) Exhaust gas deprived of CO.sub.2 gas through contact with the CO.sub.2 absorption liquid in the absorption part 14 is discharged outside from the tower top part 16 of the absorption tower 2.

(15) On the other hand, the CO.sub.2 absorption liquid having absorbed the CO.sub.2 gas in the exhaust gas in the absorption part 14 falls onto the tower bottom part of the absorption tower 2, and is stored in the tower bottom part. The CO.sub.2 absorption liquid stored in the tower bottom part of the absorption tower 2 is a rich absorption liquid 18 having a higher CO.sub.2 concentration than the CO.sub.2 absorption liquid described below stored in the tower bottom part of the regeneration tower 4. The rich absorption liquid 18 is supplied to the regeneration tower 4 from the absorption tower 2 via a rich liquid line 20 by a pump (not depicted) installed in the rich liquid line 20.

(16) Further, as depicted in FIG. 1, a heat exchanger 22 for exchanging heat between the rich absorption liquid flowing through the rich liquid line 20 and the lean absorption liquid flowing through the lean liquid line 36 may be installed in the rich liquid line 20. By heating the rich absorption liquid through heat exchange with the lean absorption liquid having a relatively high temperature, it is possible to promote regeneration of the absorption liquid in the regeneration tower 4 described below.

(17) The regeneration tower 4 includes a release part 24 that releases CO.sub.2 gas from the rich absorption liquid and a cleaning part 26 which cleans the CO.sub.2 gas released at the release part 24 with reflux water.

(18) The release part 24 includes a packing material, and is supplied from the rich absorption liquid from above through the rich liquid line 20. The rich absorption liquid is heated by the steam described below, in the release part 24, releases CO.sub.2 gas, and becomes a lean absorption liquid which contains a relatively low rate of CO.sub.2.

(19) The lean absorption liquid having released CO.sub.2 gas at the release part 24 descends from the regeneration tower 4, and is stored in the tower bottom part of the regeneration tower 4. The lean absorption liquid 28 is supplied, via a re-boiler line 30, to a regeneration heater (re-boiler) 32 installed in the re-boiler line 30. In the regeneration heater 32, the lean absorption liquid 28 exchanges heat with a heating medium (e.g. water steam), whereby at least a part of the lean absorption liquid 28 changes in phase to saturated steam, and is supplied to the tower bottom part of the regeneration tower 4. The saturated steam produced by the regeneration heater 32 as described above flows upward through the regeneration tower 4 toward the release part 24, and is used as a heating source for heating the rich absorption liquid at the release part 24.

(20) The lean absorption liquid (containing a lean absorption liquid that has not changed its phase in the regeneration heater 32) stored in the tower bottom part of the regeneration tower 4 is taken out from the tower bottom part of the regeneration tower 4, and is supplied to the absorption part 14 of the absorption tower 2 via the lean liquid line 36 by a feeding pump (not depicted) installed in the lean liquid line 36, thereby being re-utilized as the above described CO.sub.2 absorption liquid. Further, a cooler 38 for cooling the lean absorption liquid may be installed in the lean liquid line 36.

(21) The CO.sub.2 gas released from the rich absorption liquid at the release part 24 flows upward toward the cleaning part 26 installed above the release part 24 in the regeneration tower 4. The cleaning part 26 removes the absorption agent remaining in the CO.sub.2 gas as the CO.sub.2 gas from the release part 24 makes gas-liquid contact with the cleaning liquid supplied from above the cleaning part 26.

(22) The cleaning part 26 is not particularly limited as long as it is capable of promoting gas-liquid contact between CO.sub.2 gas and the first cleaning liquid. For instance, the cleaning part 26 may include one or more stages of trays or a packed layer.

(23) The CO.sub.2 gas after passing through the cleaning part 26 is released from the tower top part of the regeneration tower 4, and is supplied to the CO.sub.2 gas line 40. A condenser 42 is installed in the CO.sub.2 gas line 40, and in the condenser 42, CO.sub.2 gas is cooled and steam in the CO.sub.2 gas is condensed. The CO.sub.2 gas after passing through the condenser 42 is supplied to the reflux water drum 6 installed on the outlet side of the CO.sub.2 gas line 40.

(24) The reflux water drum 6 is configured to separate released gas from the regeneration tower 4 (CO.sub.2-containing gas) into CO.sub.2 gas and condensed water.

(25) The condensed water 44 separated by the reflux water drum 6 is stored in the tower bottom part of the reflux water drum 6. The condensed water 44 is supplied to the cleaning part 26 of the regeneration tower 4 as a cleaning liquid, via the reflux water line 46. Further, the condensed water 44 is supplied to the reclaiming apparatus 10 described below, via the water supply line 58.

(26) On the other hand, CO.sub.2 gas separated by the reflux water drum 6 is released from the reflux water drum 6 via a recovery line 48 connected to the tower top part of the reflux water drum 6, compressed by a compressor (not depicted) installed in the recovery line 48, and is taken out of the system as product CO.sub.2, for instance.

(27) Next, a reclaiming apparatus 10 according to some embodiments will be described. The reclaiming apparatus 10 is configured to remove non-volatile components such as impure substances from exhaust gas and depleted substances of the absorption liquid accumulating due to repetitive re-utilization of the absorption liquid in the CO.sub.2 recovery apparatus 1, from a CO.sub.2 absorption liquid including such non-volatile components, and recover the CO.sub.2 absorption agent and return the CO.sub.2 absorption agent to the CO.sub.2 recovery apparatus 1.

(28) Further, reclaiming of the absorption liquid by the reclaiming apparatus 10 may be performed when the concentration of the absorption agent of the lean absorption liquid 28 or the rich absorption liquid 18 reaches a predetermined value or higher, during an operation period of the CO.sub.2 recovery apparatus 1.

(29) In the following description, a CO.sub.2 absorption liquid containing a CO.sub.2 absorption agent is reclaimed. Nevertheless, the absorption agent and the absorption liquid according to the present invention is not limited to this. For instance, the absorption agent may be a H.sub.2S absorption agent that absorbs H.sub.2S, and the absorption liquid may be a H.sub.2S absorption liquid that contains a H.sub.2S absorption agent.

(30) Further, in the following description, the CO.sub.2 absorption agent and the CO.sub.2 absorption liquid may be referred to as merely an absorption agent and an absorption liquid, respectively.

(31) FIG. 2 is a schematic diagram of a reclaiming apparatus 10 in a CO.sub.2 recovery apparatus 1 depicted in FIG. 1. As depicted in FIG. 2, the reclaiming apparatus 10 includes a container 50 for storing an absorption liquid and water, an absorption-liquid supply line 54 for supplying the container 50 with an absorption liquid, a water supply line 58 for supplying water to the container 50, a steam discharge line 62 for discharging steam from the container 50, and a heating device 52 for heating a liquid containing water and an absorption liquid.

(32) Further, an absorption liquid valve 56 for adjusting the supply amount of absorption liquid to the container 50 is installed in the absorption-liquid supply line 54, and a water valve 60 (valve) for adjusting the supply amount of water to the container 50 is installed in the water supply line 58.

(33) In some embodiments, the heating device 52 may be configured to heat a liquid inside the container through heat exchange between the liquid inside the container and a heating medium.

(34) In an illustrative embodiment depicted in FIG. 2, the heating device 52 includes a U-shaped steam pipe installed inside the container 50. The heating device 52 is supplied with a heating medium via a heating medium via a heating medium supply line 64. Further, the heating device 52 heats a liquid inside the container through heat exchange between the liquid and the heating medium.

(35) The heating medium supplied to the heating device 52 may be water vapor or oil, for instance.

(36) Further, a heating medium valve 66 for adjusting the supply amount of the heating medium to the heating device 52 may be installed in the heating medium supply line 64.

(37) In some embodiments, the heating device 52 may be configured to heat a liquid inside the container 50 by electricity.

(38) Further, in some embodiments, the heating device 52 may be installed outside the container 50. For instance, although not depicted, the heating device 52 may be configured to heat mixture of water and an absorption liquid before being supplied to the container 50, at downstream of a merge point of the absorption-liquid supply line 54 and the water supply line 58.

(39) As depicted in FIG. 1, a lean absorption liquid from the lean liquid line 36 is supplied to the absorption-liquid supply line 54. In the embodiment depicted in FIG. 1, the lean absorption liquid is supplied to the absorption-liquid supply line 54 from the lean liquid line 36 upstream of the heat exchanger 22. Nevertheless, in another embodiment, the lean absorption liquid may be supplied to the absorption-liquid supply line 54 from the lean liquid line 36 downstream of the heat exchanger 22.

(40) Further, as depicted in FIG. 1, a part of the condensed water 44 stored in the reflux water drum 6 is supplied to the water supply line 58.

(41) Further, water supplied to the container 50 is not limited to the condensed water from the reflux water drum 6. The container 50 may be supplied with water from another supply source, instead of, or in addition to, the condensed water from the reflux water drum 6.

(42) Further, as depicted in FIG. 1, the outlet of the steam discharge line 62 is connected to the regeneration tower 4. That is, steam discharged from the container 50 is supplied to the regeneration tower 4.

(43) The reclaiming apparatus 10 further includes a waste liquid line 68 for discharging a waste liquid from the container 50, and a waste liquid tank 78 for storing a waste liquid from the waste liquid line 68. A waste liquid valve 70, a cooler 72, and a pump 74 are installed in the waste liquid line 68.

(44) Further, the reclaiming apparatus 10 includes a temperature sensor 82 for measuring the temperature inside the container 50, a pressure sensor 84 for measuring the pressure inside the container 50, and a control device (control device) 80 for controlling operation of the reclaiming apparatus 10.

(45) The temperature sensor 82 may be installed in the liquid-phase part inside the container 50, and configured to measure the temperature of the liquid-phase part. The pressure sensor 84 may be installed in the gas-phase part inside the container 50.

(46) The control device 80 includes, for instance, a central processing unit (CPU), a random access memory (RAM), a read only memory (ROM), and a storage medium or the like that is readable with a computer. Further, the series of processes for realizing the various functions is stored in the storage medium or the like in the form of program, for instance. As the CPU reads the program out to the RAM or the like and executes processing and calculation of information, various functions are realized.

(47) The control device 80 is configured to receive measurement results of the temperature sensor 82 and the pressure sensor 84. Further, the control device 80 may be configured to perform an open-close control or an opening-degree control on various valves including the absorption liquid valve 56 and the water valve 60, for instance.

(48) Hereinafter, described is a procedure of reclaiming the absorption liquid by using the reclaiming apparatus 10 having the above configuration. Herein, FIG. 3 is a flowchart of an example of the procedure of a reclaiming method according to an embodiment.

(49) In the reclaiming method described below, the open-close control of the valves and determination of the ending timing of each step (absorption liquid regeneration step and absorption agent recovery step), for instance, may be executed by the above described control device 80.

(50) As depicted in FIG. 3, in the reclaiming method according to an embodiment, firstly, an absorption liquid regeneration (reclaiming) step (process) is performed (step S100), then, an absorption liquid recovery step (process) is performed (step S110), and then a discharge step is performed (step S120).

(51) In the absorption liquid regeneration step (S100), firstly, the absorption liquid valve 56 and the water valve 60 are opened, and the absorption liquid and water are supplied to the container 50. Next, the heating medium valve 66 is opened, and supply of a heating medium (e.g. steam) to the heating device 52 is started. Further, while supplying at least one of the absorption liquid or water to the container 50 (typically, supplying both of the absorption liquid and water), the liquid inside the container 50 (mixture of the absorption liquid and water) is heated, and the non-volatile component (depleted materials of the absorption liquid or the like) remaining tin the liquid inside the container 50 and the absorption agent contained in the steam discharged to the steam discharge line 62 are separated (step S102).

(52) In step S102, a liquid inside the contained is heated by the heating device 52, and the non-volatile component (absorption agent and water) in the liquid are evaporated. The steam containing the absorption agent produced in the container 50 is discharged from the container 50 via the steam discharge line 62. On the other hand, the non-volatile component contained in the liquid accumulates inside the container 50 even when the liquid is heated, and concentrated in the liquid inside the container 50 with time. Accordingly, the absorption agent contained in the liquid and the non-volatile component are separated.

(53) Further, steam containing the absorption agent discharged from the container 50 via the steam discharge line 62 is returned to the regeneration tower 4 of the CO.sub.2 recovery apparatus 1. The absorption agent returned to the regeneration tower 4 is used again as an absorption liquid that absorbs CO.sub.2 in the CO.sub.2 recovery apparatus 1.

(54) In step S102, the container 50 may be supplied with the absorption liquid and/or water, so that the liquid-surface level inside the container 50 falls within a predetermined range. Further, the opening degrees of the absorption liquid valve 56 and the water valve 60 may be adjusted so that the ratio of the absorption liquid to the container 50 to the supply amount of water is at a predetermined value.

(55) Further, the temperature and the supply amount of the heating medium supplied to the heating device 52 may be set so that a liquid that contains the absorption liquid and water inside the container 50 is boiling.

(56) Next, the temperature TL of a liquid stored inside the container 50 is obtained by the temperature sensor 82, and the ending timing of the absorption liquid regeneration step S100 is determined on the basis of the temperature TL.

(57) Specifically, the temperature T1 of the above described liquid is compared to the second predetermined temperature Tth2 (step S104). Further, the second predetermined temperature Tth2 is higher than the first predetermined temperature Tth1 described below.

(58) Further, in a case where the above described temperature TL of the liquid is lower than the second predetermined temperature Tth2 (No in step S104), the absorption liquid regeneration step S100 is not ended, and the step S102 is continued. That is, while supplying the container 50 with the absorption liquid and water, a step of heating the liquid inside the container 50 is continued, and the non-volatile component contained in the liquid inside the container 50 is condensed even further.

(59) On the other hand, when the above described temperature TL of the liquid increases and reaches the second predetermined temperature Tth2 (Yes in step S104), it is determined that it is the ending timing of the absorption liquid regeneration step S100. Accordingly, the absorption liquid valve 56 is closed, and supply of the absorption liquid to the container 50 is stopped (step S106).

(60) The boiling point of the liquid inside the container 50 changes depending on the concentration of the non-volatile component in the liquid. Specifically, the higher the concentration of the non-volatile component in the liquid, the higher the boiling point of the liquid. Thus, the temperature of the liquid heated by the heating device 52 can be used as an index of the non-volatile component of the liquid.

(61) Further, as the temperature difference between the liquid in the container 50 and the heating medium becomes small, the amount of heat exchange decreases. Thus, the non-volatile component is less likely to be condensed further in the liquid.

(62) Thus, by setting the second predetermined temperature Tth2 appropriately and comparing the temperature TL of the liquid inside the container 50 to the second predetermined temperature Tth2, it is possible to determine whether the non-volatile component is condensed sufficiently in the liquid inside the container 50. Thus, on the basis of the temperature of the liquid inside the container 50, it is possible to determine the ending timing of the above described absorption liquid regeneration step S100 easily and quickly.

(63) Once the above described absorption liquid regeneration step (step S100) ends, the absorption liquid recovery step is performed (step S110).

(64) In the absorption liquid recovery step (S110), by supplying the container 50 with water (condensed water from the reflux water drum 6, or the like) via the water supply line 58 and heating the liquid with the heating device 52 in a state where supply of the absorption liquid from the absorption-liquid supply line 54 is shut off, the absorption agent remaining in the liquid is evaporated together with water. The steam containing the absorption agent produced in the container 50 is discharged (recovered) from the container 50 via the steam discharge line 62 (step S112).

(65) In step S112, the container 50 may be supplied with water, so that the liquid-surface level inside the container 50 falls within a predetermined range.

(66) Further, the temperature and the supply amount of the heating medium supplied to the heating device 52 may be set so that a liquid that contains the absorption liquid and water inside the container 50 is boiling.

(67) In step S112, the absorption liquid is not supplied to the container 50, and thus the concentration of the non-volatile component contained in the liquid does not basically change. Furthermore, in step S112, the volatile component containing the absorption agent in the liquid is volatilized while supplying water to the container 50, and thus the concentration of the absorption agent in the liquid decreases.

(68) Next, the temperature TL of a liquid stored inside the container 50 is obtained by the temperature sensor 82, and the ending timing of the absorption liquid recovery step (S110) is determined on the basis of the temperature TL.

(69) Specifically, the temperature TL of the above described liquid is compared to the first predetermined temperature Tth1 (step S114).

(70) Further, in a case where the above described temperature TL of the liquid is higher than the first predetermined temperature Tth1 (No in step S114), the absorption liquid recovery step S110 is not ended, and the step S112 is continued. That is, while supplying the container 50 with water, a step of heating the liquid inside the container 50 is continued, and the concentration of the absorption agent contained in the liquid inside the container 50 is further reduced.

(71) On the other hand, when the above described temperature TL of the liquid decreases and reaches the first predetermined temperature Tth1 (Yes in step S104), it is determined that it is the ending timing of the absorption liquid recovery step S110, and the water valve 60 is closed, and supply of water to the container 50 is stopped (step S116). Further, the heating medium valve 66 is closed, and supply of the heating medium to the heating device 52 is stopped, thereby stopping heating the liquid inside the container 50.

(72) The boiling point of the liquid inside the container 50 containing water and the absorption liquid changes depending on the concentration of the absorption agent of the liquid. Further, the boiling point of the absorption agent (amines or the like) has a higher boiling point than water. Thus, the higher the concentration of the absorption agent in the liquid, the higher the boiling point of the liquid. Thus, the temperature of the liquid heated by the heating device 52 can be used as an index of the absorption agent of the liquid.

(73) Thus, by setting the first predetermined temperature Tth1 appropriately and comparing the temperature TL of the liquid inside the container 50 to the first predetermined temperature Tth1, it is possible to determine readily and quickly whether the concentration of the absorption agent is condensed sufficiently in the liquid inside the container 50.

(74) Further, it is possible to end the absorption agent recovery step (S110) after the concentration of the absorption agent in the liquid inside the container 50 is sufficiently reduced, and thus it is possible to reduce the loss due to discharge to the outside of the system of the absorption agent entrained by the waste liquid discharged from the container 50 in the subsequent discharge step S120.

(75) Further, in step S102 or step S112, when the liquid inside the container 50 is heated, a strong alkaline material such as caustic soda may be added to the liquid to recover the absorption liquid.

(76) Inside the container 50, strong acidic materials in the depleted materials in the absorption liquid may react with the absorption agent (amines or the like) and produce thermally stable salts. Thus, a strong alkaline material is added as described above to bond the strong alkaline material with the strong acidic materials constituting the thermally stable salts with the absorption agent. In this way, it is possible to liberate and recover the weak alkaline absorption agent.

(77) In the discharge step (S120), the waste liquid valve 70 is opened, and the pump 74 installed in the waste liquid line 68 is started. Accordingly, the waste liquid containing reclaiming sludge remaining in the container 50 after completion of the absorption liquid recovery step S110 is discharged from the container 50, and is sent to the waste liquid tank 78 via the waste liquid line 68.

(78) The waste liquid discharged from the container 50 may be cooled by the cooler 72 installed in the waste liquid line 68, and then sent to the waste liquid tank 78.

(79) When discharge of the waste liquid from the container 50 and transportation of the waste liquid to the waste liquid tank 78 are completed, the pump 74 is stopped and the waste liquid valve 70 is closed, thereby ending the discharge step.

(80) According to the above described reclaiming method, on the basis of the temperature of the liquid heated by the heating device 52, it is possible to easily and quickly determine the ending timing of the absorption liquid regeneration step (step S100) of separating the absorption agent and the non-volatile component from the liquid inside the container 50, and the absorption agent recovery step (S110) of recovering steam containing the absorption agent. Thus, it is possible to perform reclaiming of the absorption liquid more efficiently.

(81) Further, by using the control device 80 configured to perform the above described reclaiming method, it is possible to automatically determine the ending timing of the absorption liquid regeneration step (S100) and the absorption agent recovery step (S110) on the basis of the temperature obtained by the temperature sensor 82. Further, when it is determined that the absorption liquid regeneration step (S100) and the absorption agent recovery step (S110) are ended, it is possible to automatically proceed to the subsequent step by performing an appropriate open-close control on the absorption liquid valve 56, the water valve 60, and/or the waste liquid valve 70. Thus, it is possible to perform reclaiming of the absorption liquid more efficiently.

(82) Further, normally, during operation of the CO.sub.2 recovery apparatus 1, the pressure of the absorption tower 2 is constant, and thus the pressure inside the container 50 being in communication with the absorption tower 2 via the steam discharge line 62 is also constant. Thus, at a specific pressure inside the container 50, the temperature of the liquid inside the container 50 and the concentration of the non-volatile material or the absorption agent in the liquid have a specific correlation relationship. Thus, as described above, the liquid temperature inside the container 50 can be used as an index of the concentration of the non-volatile material or the absorption agent in the liquid, and thus it is possible to appropriately determine the ending timings of the absorption agent recovery step (S110) and the absorption liquid regeneration step (S100) by using the temperature thresholds (the first predetermined temperature and the second predetermined temperature).

(83) The first predetermined temperature Tth1 for determining the end of the absorption liquid recovery step (S110) may be set depending on the pressure inside the container 50.

(84) Setting the first predetermined temperature Tth1 depending on the pressure inside the container 50 will be described with reference to FIGS. 4 and 5.

(85) FIG. 4 is a graph showing an example of a correlation relationship between the boiling point of the liquid inside the container 50, and the concentration of the non-volatile component in the liquid, at the time when the pressure inside the container 50 is Pa and Pb, respectively. Herein, the pressure Pa is smaller than the pressure Pb (Pa<Pb).

(86) FIG. 5 is a graph showing an example of a correlation relationship between the boiling point of the liquid inside the container 50 (i.e. the temperature of the liquid), and the concentration of the absorption agent in the liquid, at the time when the pressure inside the container 50 is Pa and Pb, respectively. The pressures Pa, Pb are the same as the pressures Pa, Pb in FIG. 4.

(87) In the following description, the liquid inside the container 50 is sufficiently heated, and the temperature of the liquid is the same as the boiling point of the liquid.

(88) In the absorption liquid regeneration step (S100) performed before the absorption liquid recovery step (S110), the non-volatile component is gradually condensed in the liquid inside the container 50, and thus the concentration of the non-volatile component in the liquid increases gradually.

(89) With reference to the graph in FIG. 4, at the start time of the absorption liquid regeneration step (S100), the concentration of the non-volatile component is low (the concentration at this time is C0), and the solution temperature in the liquid is T a0 when the pressure inside the container is Pa, and T b0 when the pressure inside the container is Pb.

(90) Further, as the concentration of the non-volatile component in the liquid increases with heating of the liquid, the boiling point of the liquid increases accordingly, and the temperature of the liquid in the container 50 increases.

(91) Herein, the ending timing of the absorption liquid regeneration step (S110) may be determined on the basis of the second predetermined temperature Tth2, which is a threshold that does not depend on the pressure.

(92) That is, in both of the cases where the pressure inside the container is Pa and Pb, when the liquid temperature inside the container 50 reaches the second predetermined temperature Tth2, it may be determined that the concentration of the non-volatile component in the liquid has increased sufficiently and the absorption liquid regeneration step (S100) ended. At this time, the temperature T_a2 (the pressure inside the container is Pa), and the temperature T_b2 (the pressure inside the container is Pb) at the end of the absorption liquid regeneration step (S100) are equal to Tth2, regardless of the pressure inside the container.

(93) Next, with reference to FIG. 5, the temperature at the start of the absorption liquid regeneration step (S110) is the same as the temperature at the end of the absorption liquid regeneration step (S100), and is T_a2 when the pressure inside the container is Pa, and T_b2 when the pressure inside the container is Pb. As described above, T_a2 and T_b2 are the same as Tth2.

(94) Herein, as depicted in FIG. 5, the boiling point of the liquid (temperature of the liquid) decreases with a decrease in the concentration of the absorption agent. The correlation relationship between the concentration of the absorption agent in the liquid inside the container 50 and the boiling point (temperature of the liquid) differs depending on the pressure inside the container. Thus, for instance, in a case where the absorption liquid recovery step (S110) should be ended at the time when the concentration of the absorption agent in the liquid decreases sufficiently to C1, the boiling point of the liquid (temperature of the liquid) corresponding to the concentration C1 also differs depending on the pressure. In the graph of FIG. 5, the boiling point of the liquid corresponding to the above described concentration C1 is T_a1 when the pressure inside the cylinder is Pa, and is T_b1 when the pressure inside the cylinder Pb. Further, in the graph of FIG. 5, T_a1<T_b1.

(95) Thus, depending on the pressure inside the cylinder, the first predetermined temperature Tth1 is set appropriately, according to the corresponding pressure.

(96) For instance, for the pressure Pa inside the container, the first predetermined temperature Tth1 is set to be T_a1, and for the pressure Pb inside the container, the first predetermined temperature Tth1 is set to be T_b1. In this case, the temperature inside the container at the end of the absorption liquid recovery step (S110) is T_a1, and T_b1, respectively.

(97) In this case, the temperature threshold for determining the ending timing of the absorption liquid recovery step (S110) is the first predetermined threshold Tth1, which is a temperature value. As the above threshold, the temperature difference from the start of the absorption liquid recovery step (S110) may be used.

(98) For instance, when the pressure inside the container is Pa, the difference ΔTa between the liquid temperature T_a2 at the start of the absorption liquid recovery step (S110) and the liquid temperature T_a1 corresponding to the absorption agent concentration C1 may be set as a threshold (ΔTa=T_a2−T_a1), and it may be determined that the absorption liquid recovery step (S110) ends when the liquid temperature decreases by ΔTa from the start of the absorption liquid recovery step (S110).

(99) Also when the pressure is Pb, the difference ΔTb between the liquid temperature T_b2 at the start of the absorption liquid recovery step (S110) and the liquid temperature T_b1 corresponding to the absorption agent concentration C1 may be set as a threshold (ΔTb=T_b2−T_b1), and it may be determined that the absorption liquid recovery step (S110) ends when the liquid temperature decreases by ΔTb from the start of the absorption liquid recovery step (S110).

(100) As described above, also in a case where the temperature difference from the start of the absorption liquid recovery step (S110) is used as a threshold, it is possible to set an appropriate threshold ΔT depending on the pressure (ΔTa or ΔTb described above).

(101) As described above, by setting the first predetermined temperature Tth1 or ΔT corresponding to the pressure inside the container 50, even in a case there is a change in the pressure inside the container 50, it is possible to set the first predetermined temperature Tth1 or ΔT appropriately according to the pressure, decrease the concentration of the absorption agent of the solvent in the container 50 sufficiently, and then end the absorption agent recovery process. Accordingly, it is possible to suppress loss of the absorption liquid by reclaiming effectively.

(102) Embodiments of the present invention were described in detail above, but the present invention is not limited thereto, and various amendments and modifications may be implemented.

(103) Further, in the present specification, an expression of relative or absolute arrangement such as “in a direction”, “along a direction”, “parallel”, “orthogonal”, “centered”, “concentric” and “coaxial” shall not be construed as indicating only the arrangement in a strict literal sense, but also includes a state where the arrangement is relatively displaced by a tolerance, or by an angle or a distance whereby it is possible to achieve the same function.

(104) For instance, an expression of an equal state such as “same” “equal” and “uniform” shall not be construed as indicating only the state in which the feature is strictly equal, but also includes a state in which there is a tolerance or a difference that can still achieve the same function.

(105) Further, for instance, an expression of a shape such as a rectangular shape or a cylindrical shape shall not be construed as only the geometrically strict shape, but also includes a shape with unevenness or chamfered corners within the range in which the same effect can be achieved.

(106) On the other hand, an expression such as “comprise”, “include”, “have”, “contain” and “constitute” are not intended to be exclusive of other components.

DESCRIPTION OF REFERENCE NUMERALS

(107) 1 CO.sub.2 recovery apparatus 2 Absorption tower 4 Regeneration tower 6 Reflux water drum 10 Reclaiming apparatus 12 Exhaust gas introduction line 14 Absorption part 16 Tower top part 18 Rich absorption liquid 20 Rich liquid line 22 Heat exchanger 24 Release part 26 Cleaning part 28 Lean absorption liquid 30 Re-boiler line 32 Regeneration heater 36 Lean liquid line 38 Cooler 40 CO.sub.2 gas line 42 Condenser 44 Condensed water 46 Reflux water line 48 Recovery line 50 Container 52 Heating device 54 Absorption-liquid supply line 56 Absorption liquid valve 58 Water supply line 60 Water valve (valve) 62 Steam discharge line 64 Heating medium supply line 66 Heating medium valve 68 Waste liquid line 70 Waste liquid valve 72 Cooler 74 Pump 78 Waste liquid tank 80 Control device 82 Temperature sensor 84 Pressure sensor