WO2021246318A1

WO2021246318A1 - Method for producing methane from co2 in cement production exhaust gas, and methanation apparatus

Info

Publication number: WO2021246318A1
Application number: PCT/JP2021/020406
Authority: WO
Inventors: 佳典 ▲高▼山; 始川崎; 琢磨高馬; 卓哉小松
Original assignee: 三菱マテリアル株式会社
Priority date: 2020-06-04
Filing date: 2021-05-28
Publication date: 2021-12-09

Abstract

In the production of methane from an exhaust gas from a cement production facility, an acidic component such as SOx, NOx and a halogen and a harmful component such as H₂O and dust are removed from the exhaust gas, and the exhaust gas from which the acidic component and the harmful component have been removed is brought into contact with a CO₂ absorbent material to separate and collect CO₂. In this manner, the deterioration in the absorption capability of the CO₂ absorbent material can be prevented and the cement production exhaust gas can be treated properly to produce methane properly. As a result, energy-induced CO₂ can be reduced and the greenhouse gas emission reduction effect can be improved.

Description

Cement manufacturing method and methane conversion equipment from CO2 in exhaust gas

The present invention relates to a method for producing methane from _{CO 2} in cement production exhaust gas and a methaneization apparatus.

The present application is Japanese Patent Application No. 2020-97644 and Japanese Patent Application No. 2020-97645 filed in Japan on June 4, 2020, and Japanese Patent Application No. 2020-101458 filed in Japan on June 11, 2020. Claim priority based on, and use its contents here.

In various combustion facilities such as thermal power generation, efforts are being made to reduce _{CO 2} generated and emitted by combustion in order to reduce greenhouse gases. In particular, since most of the energy required for social activities is obtained from fossil fuels such as coal, oil, and natural gas, _{the amount of CO 2} generated from this fossil fuel is enormous, and CO _{2 originating from this energy} Is effective in controlling global warming.

_{As a technique for reducing CO 2 in} combustion exhaust gas, for example, the methanation method described in Patent Document 1 is conventionally known. That is, it is a method of obtaining methane by separating carbon dioxide contained in combustion exhaust gas and reacting it with hydrogen. In this methanation method, a step of bringing the combustion exhaust gas into contact with a carbon dioxide absorber to absorb carbon dioxide in the combustion exhaust gas, and a gas containing carbon dioxide as a main component by heating the carbon dioxide absorber that has absorbed carbon dioxide. The step of taking out the sulfur compound, the step of adding the first amount of hydrogen to the gas containing carbon dioxide as the main component, and then passing it through a desulfurizing device filled with a desulfurizing agent to remove the sulfur compound in the gas, and the step of removing the sulfur compound. It includes a step of adding a second amount of hydrogen to the gas that has undergone the removal step and converting it into methane by a methanation reaction that has passed through a methanation catalyst.
In this methanation method, carbon dioxide to which hydrogen is added is passed through a desulfurizer filled with a desulfurizing agent to remove sulfur compounds in the gas.

JP-A-2019-172595

However, since the exhaust gas of cement equipment (cement manufacturing exhaust gas) contains a large amount of oxides other than sulfur compounds, for example, even if a desulfurizer as described in Patent Document 1 is used, the cement manufacturing exhaust gas can be appropriately used. It cannot be processed and methane cannot be produced properly.

The present invention has been made in view of such circumstances, and provides a methane production method and a methane conversion apparatus from _{CO 2 in} cement production exhaust gas, which can appropriately treat cement production exhaust gas and appropriately produce methane. The purpose is.

In the methane production method in the cement production exhaust gas of the present invention, acidic components and harmful components are removed from the exhaust gas of the cement manufacturing facility, and the acidic components and the exhaust gas from which the harmful components have been removed are brought into contact _{with the CO 2 absorber.} CO ₂ is separated and recovered, and hydrogen is added to the _{separated and recovered CO 2 to generate methane.}

Here, harmful components SOx, NOx, such as acid component and H _{2 O,} the dust such as halogen contained in the cement manufacturing exhaust gas may degrade the CO ₂ absorption capacity affect the CO ₂ absorbing material. Furthermore, the dust contained in the cement manufacturing exhaust gas (mainly the powder of the cement raw material) adheres to the inside of the equipment piping to form a scale, which increases the pressure loss of the piping and the amount of gas that can be processed _{by the CO 2 separation and recovery device.} There is a risk of reducing the amount.

On the other hand, in the present invention, deterioration of the absorption capacity of the _{CO 2} absorber can be suppressed by removing the acidic component and the harmful component before separating and recovering the exhaust gas from the cement manufacturing facility. _{Therefore, CO 2} can be efficiently recovered from the cement manufacturing exhaust gas. Therefore, the efficiency of methanation is also improved.

In the method for producing methane in the exhaust gas produced by cement, the acidic component contains any one of SOx, NOx and halogen.
The harmful components _{comprises H} 2 O, a dust.

In the methane production method in the cement production exhaust gas, it is preferable to generate methane after removing water from the _{separated and recovered CO 2.}

Since the reaction of methane is CO ₂ + 4H ₂ → CH ₄ + 2H ₂ O, if the separated and recovered CO ₂ contains a large amount of water, the amount of H ₂ O on the right side of the reaction formula increases, so methane is generated. It becomes difficult to do. In the above aspect, _{since water is removed from the separated and recovered CO 2} and hydrogen is added thereto to generate methane, the methane production reaction is facilitated and the efficiency of methanogenesis is improved.

In the methaneization apparatus from the cement manufacturing exhaust gas CO ₂ of the present invention, the cement manufacturing facility is provided with a harmful component removing unit for removing acidic components and harmful components from the exhaust gas from the cement manufacturing facility, and the acidic components and the harmful components. comprises a CO ₂ separation collector to the removed said exhaust gas into contact with CO ₂ absorbent to separate and recover the CO _2, and methane production unit for generating methane by adding hydrogen to the separated and collected CO _2, the.

The cement manufacturing exhaust gas CO ₂ methane conversion apparatus further includes a dehumidifying section for removing water from the separated and recovered CO ₂ , and the methane manufacturing section adds hydrogen to the _{water-removed CO 2.} It is good to produce methane.

According to the present invention, by appropriately removing harmful components from _{CO 2 in} the exhaust gas of a cement manufacturing facility _{, deterioration of the absorption capacity of the CO 2} absorber is suppressed, and the cement manufacturing exhaust gas is appropriately treated to produce methane. It can be produced properly, which can reduce _{CO 2 from energy sources.}

It is a flowchart which shows the procedure _{of the CO 2} utilization method in the cement manufacturing exhaust gas which concerns on one Embodiment of this invention. It is a simplified view showing a CO ₂ utilization system of cement production in the exhaust gas of the above embodiments. It is a block diagram which shows the schematic structure of the methanation apparatus of the said embodiment.

Hereinafter, embodiments of the methane production method and the methaneization apparatus from _{CO 2} in the cement production exhaust gas of the present invention will be described with reference to the drawings.

_{In this embodiment, after appropriately removing acidic components and harmful components from CO 2} in cement manufacturing exhaust gas, methane is generated, and the methane is used as a partial or total alternative fuel for fossil fuels for cement manufacturing facilities. This is an example of using it.

[ _{Configuration of CO 2} utilization system]
As _{shown in FIG. 2, the CO 2} utilization system 100 includes a cement manufacturing facility 50 and an exhaust gas treatment facility 30 connected to and used in the cement manufacturing facility 50. In the present embodiment, the exhaust gas treatment facility 30 _{adds hydrogen to the exhaust gas from the exhaust gas or CO 2} separated and recovered from the exhaust gas to generate methane, and the generated methane is used as fossil fuel for the cement production facility 50. Supplied as an alternative fuel in part or in whole.

[Structure of cement manufacturing equipment]
As shown in FIG. 2, the cement manufacturing facility 50 includes a raw material storage 1 for individually storing limestone, clay, silica stone, iron raw materials, etc. as cement raw materials, and a raw material mill and dryer for crushing and drying these cement raw materials. 2 and a preheater 3 that preheats the powdered cement raw material supplied through the raw material supply pipe 22 and obtained by this raw material mill, and a calcining furnace 4 that calcins the cement raw material preheated by the preheater 3. It is provided with a cement calcined kiln 5 for calcining a calcined cement raw material, a cooler 6 for cooling a cement clinker after being calcined by the cement calcined kiln 5, and the like.

The cement firing kiln 5 is a cylindrical rotary kiln that is slightly inclined sideways, and by rotating around the axis, the cement raw material supplied from the preheater 3 is sent to the kiln front portion 5b to the kiln tail portion 5a while being sent to the kiln front portion 5b. In the process of sending, the burner 8 of the front part 5b of the kiln heats and fires at about 1450 ° C. to form a cement clinker. The generated cement clinker is sent from the kiln front portion 5b to the cooler 6. A fuel supply line 15 for supplying fuel including fossil fuels such as coal and petroleum is connected to the burner 8. In addition to the fuel supply line 15, a supply system (not shown) for an alternative heat source such as waste plastic or waste tire is also provided to supplement the heat energy. The cement clinker is cooled to a predetermined temperature by the cooler 6 and then sent to the finishing process.

As shown in FIG. 2, the preheater 3 is constructed in which a plurality of cyclones 13 (four in the example shown in FIG. 2) that circulate the exhaust gas generated in the cement firing kiln 5 are connected in the vertical direction. A calciner 4 is connected between the cyclone 13 at the bottom and the cyclone 13 above it. The cement raw material calcined by the combustion gas of the calcining furnace 4 is supplied from the lowermost cyclone 13 to the kiln tail portion 5a of the cement calcined kiln 5.

The calcining furnace 4 has a burner 41 inside, and by burning fuel such as coal supplied from the fuel supply line 42, the cement raw material sent from the upper cyclone 13 is calcined. The calcined cement raw material is supplied to the lowermost cyclone 13 via the rising duct 25 together with the exhaust gas generated by the calcined. The cement raw material is supplied from the lowermost cyclone 13 to the kiln tail portion 5a of the cement firing kiln 5. On the other hand, the rising duct 25 sends the exhaust gas from the kiln tail portion 5a of the cement firing kiln 5 to the lowermost cyclone 13, and the exhaust gas generated in the calcining furnace 4 is also supplied to the cyclone 13 through the rising duct 25. To. Therefore, the exhaust gas from the cement firing kiln 5 and the exhaust gas from the calcining furnace 4 are integrated and passed through the preheater 3 from the lower side to the upper side, and then introduced into the raw material mill and the dryer 2 through the exhaust pipe 9.

The raw material mill and the dryer 2 are adapted to crush and dry the cement raw material at the same time by introducing the exhaust gas from the calcining furnace 4 and the cement firing kiln 5. An exhaust gas treatment line 12 including a dust collector 10, a chimney 11, and the like is connected to the raw material mill and the dryer 2.

[Composition of exhaust gas treatment equipment]
The exhaust gas treatment facility 30 includes an exhaust gas collection line 311 that collects exhaust gas generated in the cement firing kiln 5 and the calcination furnace 4 and before being discharged from the chimney 11, and CO from the exhaust gas sent from the exhaust gas collection line 311. _It _{is provided with a methaneization device 31 that separates and recovers 2} and adds hydrogen to the separated and recovered CO 2 to generate methane, and a methane supply device 32 that supplies the generated methane to the cement production facility 50.

The exhaust gas collection line 311 is connected between the dust collector 10 and the chimney 11 in the exhaust gas treatment line 12 of the cement manufacturing facility 50, and collects a part of the exhaust gas generated during cement firing. Since it is exhaust gas generated by cement firing, it includes some exhaust gas from combustion of fuel such as coal, but it also contains a large amount of exhaust gas derived from limestone.

(Composition of methanizer)
Methanation apparatus 31 includes a CO ₂ separation and recovery device 310 for separating and recovering CO ₂ from flue gas, hydrogen mixed for mixing by supplying hydrogen (e.g. hydrogen gas) in the CO ₂ separated recovered by CO ₂ separation and recovery device 310 It includes a unit 316 and a methane production unit 317 that produces methane from _{CO 2 mixed with hydrogen.}

CO ₂ separation and recovery device 310, as shown in FIG. 3, and acid components such as SOx and NOx from the exhaust gas collected by the exhaust gas collecting line _{311, H} 2 O, harmful component removing unit for removing harmful components such as dust and 312, and the CO ₂ separation collector 313 for separating and recovering CO ₂ from the harmful components have been removed exhaust gas, a compression unit 314 for compressing the recovered CO _2, to remove water from the compressed CO ₂ It is provided with a dehumidifying unit 315.

The exhaust gas sent from the exhaust gas collection line 311 may include not only the combustion exhaust gas of fossil fuels such as coal, petroleum coke, and heavy oil, but also the combustion exhaust gas such as waste plastics and waste tires. In this case, CO _2, for example, as would fall about 20 several percent, it is included gases and acidic components and harmful components other than CO _2. Therefore, the harmful component removing unit 312 removes acidic components (for example, acid gases such as nitrogen oxides (NOx) and sulfur oxides (SOx)) and harmful components from the exhaust gas, and is filled with an aqueous NaOH solution or the like. It is equipped with a scraper, a dehumidifier, an electrostatic dust collector, etc. By removing these acidic components and harmful components, halogens (fluorine (F), chlorine (Cl), bromine (Br), iodine (I), etc.) are also removed along with NOx, which will be _{used in the next CO 2} separation and recovery. It prevents deterioration of the absorbent material (CO ₂ absorbent material) of the amine compound and suppresses the decrease in absorption capacity.

As a desulfurization method (SOx removal method), a wet limestone gypsum method, a magnesium hydroxide method, and a soda absorption method are known. These are methods of absorbing SOx with an alkaline solution, and there is a method of using coal ash as a dry method. Further, as a method for simultaneously treating desulfurization (SOx removal) and denitration (NOx removal), there are a dry method, an activated carbon method, and an electron beam method. As the denitration method, there are a catalytic reduction method (SCR method and the like) and a non-catalytic reduction method as a dry method, and an oxidation absorption method, an oxidation reduction method and an equimolar absorption method as a wet method.

On the other hand, the SOx of the exhaust gas from the cement manufacturing equipment is generally several tens of ppm or less because the suspension preheater functions as a desulfurization device.

Here, it is considered that there is no significant difference in the affinity between the amine compound and the impurity component in either the chemical absorption method or the physical adsorption method regarding the influence of impurities on the absorbent material for _{CO 2 separation and recovery.} In the recovery of CO ₂ by the CO ₂ separation collector 313, SOx in the exhaust gas is coupled with an amine compound in the absorbent, CO ₂ absorption rate with the passage of inhibiting time the absorption capacity of the amine compound is greatly reduced. As described above, the amine compound is strongly basic, and halogens such as NOx, Cl and F other than SOx tend to be adsorbed on the _{CO 2 absorbent.}

In addition, the Ni catalyst, which is widely used as a catalyst for methanation, removes harmful components because the sulfur compound reacts on the surface of the Ni catalyst under the sulfur compound mixed with _{H 2 and covers the surface to deteriorate the yield of methanation.} It is necessary to remove the sulfur compound in the part 312. Similarly, NOx and halogens (Cl, F, etc.) may adhere to the surface of the Ni catalyst and deteriorate the yield of methanation, so it is necessary to remove them by the harmful component removing unit 312.

In the present embodiment, any of the above removal methods may be used as the desulfurization (SOx removal) and denitration (NOx removal) methods by the harmful component removing unit 312. For example, in the present embodiment, any of the above desulfurization methods and any of the above denitration methods are used to remove oxidizing gases such as nitrogen oxides (NOx) and sulfur oxides (SOx).

CO ₂ separation collector 313 is made common CO ₂ recovery apparatus, the inside absorbs CO ₂ CO ₂ absorbent (amine compound liquid absorbing material dissolved in water, the amine compound to the porous material A supported solid absorbent or the like) is provided, and the exhaust gas after the harmful components or the like are removed comes into contact with the solid absorbent, so that CO _{2 in} the exhaust gas is absorbed by the CO _{2 absorbent.} Then, such as by heating the CO ₂ absorbing material that has absorbed CO _2, is recovered by extraction of CO ₂ from the CO ₂ absorber. The CO ₂ separation / recovery unit 313 _{discharges the exhaust gas after CO 2} has been removed to the outside. The compression unit 314 compresses the recovered CO ₂ by applying a pressure of 0.1 MPa or more, preferably 0.5 to 1.0 MPa. Dehumidifying unit 315, by cooling the compressed CO _2, removing the moisture contained in the CO _2. This dehumidification is performed to remove the moisture before the methanation because it affects the oxidation of the Ni-based catalyst in the methanation apparatus.

The hydrogen mixing unit 316 _{supplies hydrogen to the dehumidified CO 2} to mix and pressurize it. As hydrogen, hydrogen gas generated by artificial photosynthesis using renewable energy, decomposition of water, etc. can be used. The amount of hydrogen added by the hydrogen mixing unit 316 _{is appropriately set so that the concentration of hydrogen in CO 2} (mixed gas) after the hydrogen is mixed becomes a concentration at which methane can be easily produced.

The methane production unit 317 produces methane from _{CO 2 mixed with hydrogen.} The methane production unit 317 is composed of a general methane production apparatus, and includes a plurality of reactors (not shown) filled with catalysts that are active in methaneization, and CO _{2 in which hydrogen is mixed in these reactors.} Methane is produced by supplying and reacting. For example, Ni, Pt, Pd, and Cu are used as the hydrogenation catalyst, but in the methanation catalyst, in particular, Al ₂ O ₃ , Cr ₂ O ₃ , SiO ₂ , Mg _{Al 2} O ₄ , TiO ₂ , and so on. Supported Ni and Ni alloys such as ZrO _{2 are used.}

The conditions for a general methanation reaction (CO ₂ + 4H ₂ → CH ₄ + 2H ₂ O) are a temperature of 200 ° C. to 700 ° C., preferably 200 ° C. to 350 ° C., and a pressure of 0.1 to 3 MPa. The reaction is carried out in multiple stages in order to improve the reaction yield of methane.

(Composition of methane supply device)
As shown in FIG. 2, the methane supply device 32 is connected to a tank 322 that compresses and stores methane produced by the methaneization device 31 by a pump 321 and a tank 322, and stores methane in a burner 8 of the kiln front portion 5b. And a methane supply line 323 for sending to each of the burners 41 of the calcination furnace 4. The methane supply line 323 is a fuel supply line 15 that supplies fuel such as coal and petroleum to the burner 8 of the cement firing kiln 5, and a fuel supply line 42 that supplies fuel such as coal to the burner 41 of the calcination furnace 4. Connected to each. As a result, methane is supplied to each of the

burners

8 and 41 together with the fuel.

[How to utilize _{CO 2]}
_{A method of reducing and effectively utilizing CO 2 in} the exhaust gas of the cement manufacturing equipment 50 by using _{the CO 2} utilization system 100 described above will be described with reference to the flowchart shown in FIG.

In the cement manufacturing facility 50, a powdery cement raw material obtained by crushing and drying limestone, clay, silica stone, iron raw material, etc. as a cement raw material is preheated, and the preheated cement raw material is calcined and then fired. Then, by cooling this, a cement clinker is manufactured. Exhaust gas generated in the cement firing kiln 5 and the calcining furnace 4 due to the production of this cement clinker is introduced into the raw material mill and the dryer 2 through the exhaust pipe 9 after passing through the preheater 3 from the lower side to the upper side, and is used as a cement raw material. After being used for drying, it is discharged from the chimney 11 via the dust collector 10.

In this cement manufacturing process, a part of the exhaust gas generated during cement firing is collected from between the dust collector 10 of the exhaust gas treatment line 12 and the chimney 11 by the exhaust gas collection line 311 of the methanization apparatus 31. Next, the harmful component removing unit 312 removes the acidic component and the harmful component from the exhaust gas. In this noxious component removal unit 312, the nitrogen oxides (NOx) and sulfur oxides (SOx), halogen, and _H 2 O, such as dust are removed. Then, the CO ₂ separation and recovery unit 313 extracts CO ₂ from the exhaust gas and separates and recovers it. At this time, _{the exhaust gas from which CO 2} has been removed is discharged to the outside.

Next, the recovered CO ₂ is compressed by applying a pressure of 0.1 MPa or more, preferably 0.5 to 1.0 MPa by the compression unit 314, and the water contained in the _{CO 2 is removed by the dehumidifying unit 315.} _{Then, hydrogen is supplied to the dehumidified CO 2} by the hydrogen mixing unit 316, mixed, and pressurized. Then, the methane production unit 317 produces methane from _{CO 2 mixed with hydrogen.}

The methane produced in this way is stored in the tank 322 of the methane supply device 32. Then, the methane stored in the tank 322 is supplied to the cement firing kiln 5 and the calcining furnace 4 via the methane supply line 323. Fossil fuels such as oil and coal are supplied to the cement fired kiln 5 from the fuel supply line 15. By supplying methane, a part of the fossil fuel can be replaced with methane. Fossil fuels can be reduced. Similarly, in the calcination furnace 4, fossil fuels can be reduced because part or all of the fuel such as coal is replaced with methane.

In the present embodiment, before separating and recovering the exhaust gas from the cement manufacturing facility 50, acidic components such as SOx, NOx and halogen contained _{in CO 2 of the} _{cement manufacturing exhaust gas and harmful components such as H 2} O and dust are removed. As a result, deterioration of the absorption capacity of _{the CO 2 absorber can be suppressed.} _{Therefore, CO 2} can be efficiently recovered from the cement manufacturing exhaust gas. In addition, the CO ₂ absorber can also maintain stable performance for a long period of time. Then, by converting the appropriately treated CO ₂ to methane, it is possible to reduce the CO ₂ emissions from cement production facility 50 uses this methane as an alternative fuel for cement kiln 5 and the calciner 4 This makes it possible to effectively utilize methane. In particular, since fossil fuels such as coal and petroleum, which are a major cause of global warming, are replaced with methane derived from limestone, the use of fossil fuels _{can be reduced, CO 2} originating from energy can be reduced, and greenhouse gases can be reduced. The effect can be enhanced.

Further, since water is removed from the separated and recovered CO ₂ and hydrogen is added thereto to produce methane, oxidation of the Ni-based catalyst in the methane conversion apparatus 31 can be suppressed.

The present invention is not limited to the configuration of the above embodiment, and various changes can be made to the detailed configuration without departing from the spirit of the present invention.

For example, in the above embodiment, the dehumidifying unit 315, by cooling the compressed CO _2, it is assumed that the removal of moisture contained in the CO _2, is not limited thereto, from the CO ₂ separated recovered Any method can be used as long as the water can be removed.

Further, although the generated methane is supplied to both the cement firing kiln 5 and the calcining furnace 4, it may be supplied to either one.
Furthermore, although methane was generated using the exhaust gas from both the cement firing kiln 5 and the calcining furnace 4, it can also be applied to cement manufacturing equipment that does not have a calcining furnace. In that case, the cement firing kiln can be used. Produces methane from the exhaust gas of the kiln.

By appropriately removing harmful components from _{CO 2 in} the exhaust gas of cement manufacturing equipment, _{deterioration of the absorption capacity of the CO 2} absorber can be suppressed, and the cement manufacturing exhaust gas can be treated appropriately to produce methane appropriately. Therefore, CO ₂ originating from energy can be reduced.

1 Raw material storage 2 Raw material mill and dryer 3 Preheater 4 Temporary firing furnace 5 Cement firing kiln

5a Kiln bottom

5b Kiln front 6 Cooler 8 Burner 9 Exhaust pipe 10 Dust collector 11 Chimney 12 Exhaust gas treatment line 13 Cyclone 15 Fuel supply line 22 Raw material supply Pipe 25 Rising duct 30 Exhaust gas treatment equipment 31 Methaneization device 310 CO ₂ Separation and recovery device 311 Exhaust gas collection line 312 Harmful component removal section 313 CO ₂ Separation and recovery section 314 Compression section 315 Dehumidifying section 316 Hydrogen mixing section 317 Methane production section 32 Methane supply Equipment 321 Pump 322 Tank 323 Methane supply line 41 Burner 42 Fuel supply line 50 Cement production equipment 100 CO ₂ utilization system

Claims

The acidic component and the harmful component are removed from the exhaust gas of the cement manufacturing facility, and the exhaust gas from which the acidic component and the harmful component have been removed are brought into contact with the CO 2 absorber to separate and recover CO 2, and the separated and recovered CO. A method for producing methane from CO 2 in cement production exhaust gas, which comprises adding hydrogen to 2 to produce methane.
The method for producing methane from CO 2 in the exhaust gas produced by cement according to claim 1, wherein halogen is removed together with the acidic component and the harmful component.
After water was removed from the CO 2 separated recovered methane production method from CO 2 in cement production in the exhaust gas according to claim 1 or 2, characterized in that to produce methane.
The cement manufacturing facility, by contacting the hazardous component removing unit for removing the acidic components and harmful components from the exhaust gas from the cement manufacturing facility, the exhaust gas the acidic component and the harmful components have been removed in the CO 2 absorbing material CO and CO 2 separation collector for a 2 to separate and recover, methanation from CO 2 in cement production in the exhaust gas and by adding hydrogen to the separated and collected CO 2 methane production unit which generates methane, characterized in that it comprises a Device.
The methaneization apparatus from CO 2 in the cement manufacturing exhaust gas according to claim 4, wherein the harmful component removing unit removes halogen as well as the acidic component and the harmful component.
Methanation apparatus from CO 2 in cement production in the exhaust gas according to claim 4 or 5, further comprising a dehumidifying unit for removing moisture from the CO 2 separated recovered.