Patent Application
20180044702
The present invention relates to a method and an apparatus for producing organic substances, and particularly relates to a production method and a production apparatus suitable for producing ethanol from a raw material gas such as a synthetic gas.
Plants that produce ethanol from a raw material gas such as a synthetic gas are well known (refer to Patent Documents 1 to 3). Patent Documents 1 to 3 disclose producing ethanol from a synthetic gas by a fermentation action of a certain type of anaerobic microorganisms.
Patent Document 4 discloses producing CO and H2O from CO2 and H2 by a reverse shift reaction using a reverse shift reaction catalyst (formula (1)):
CO2+H2→CO+H2O (1)
The reverse shift reaction catalyst contains an alkali earth metal carbonates of Ca, Sr or Ba and a complex oxide of Ca, Sr or Ba and Ti, Al, Zr, Fe, W or Mo. A temperature condition for the reverse shift reaction is 700 degrees C. or higher.
Patent Document 1: Japanese Patent Application Publication No. 2004-504058
Patent Document 2: International Patent Application Publication No. WO2011/087380
Patent Document 3: United States Patent Application Publication No. US2013/0065282A1
Patent Document 4: Japanese Patent Application Publication No. 2010-194534
According to the knowledge of the inverters, the anaerobic microorganisms mentioned above intake more CO than H2 and CO2 for fermentation. Therefore, a generation efficiency of ethanol can be enhanced by subjecting the H2 and CO2 in the raw material gas to a reverse shift reaction, and thereby converting CO2 into CO. On the other hand, in a case of Patent Document 2, an operating cost may be high for the reverse shift reaction because it is required to make a temperature 700 degrees C. or higher.
In view of the above, it is an objective of the present invention to make it possible for a raw material gas to perform the reverse shift reaction under low temperature conditions, and thereby reducing the operating cost and enhancing efficiency of generating organic substances such as ethanol.
To solve the problems mentioned above, a method of the present invention provides a method for producing organic substances from a raw material gas containing CO2 and H2, the method including steps of: subjecting the raw material gas to a reverse shift reaction; and generating organic substances from the raw material gas after the reverse shift reaction, wherein: the raw material gas is contacted with a reverse shift reaction catalyst in the subjecting step; the reverse shift reaction catalyst includes a support and a catalyst metal supported by the support; and the catalyst metal includes a transition metal.
An apparatus of the present invention provides an organic substance producing apparatus that produces organic substances from a raw material gas containing CO2 and H2, the apparatus including: a reverse shift reactor subjecting the raw material gas to a reverse shift reaction; and an organic substance generator generating the organic substances from the raw material gas after the reverse shift reaction, wherein: the reverse shift reactor includes a reverse shift reaction catalyst contactable with the raw material gas; the reverse shift reaction catalyst includes a support and a catalyst metal supported by the support; and the catalyst metal includes a transition metal.
By the reverse shift reaction, the CO2 in the raw material gas can be converted into CO. By using the reverse shift reaction catalyst, conversion efficiency can be sufficiently enhanced. Moreover, a temperature condition can be set at 150 to 500 degrees C., which is lower than the temperature condition (700 degrees C. or higher) of Patent Document 4 mentioned above. Accordingly, smaller energy is required for the reverse shift reaction, and an operation cost can be reduced. An efficiency of generating organic substances such as ethanol can be enhanced by making the raw material gas CO rich by the reverse shift reaction.
The transition metal may be Fe, Sc, Ti, V, Cr, Mn, Co, Ni, Cu, Zn, Y, Zr, Nb, Mo, Tc, Ru, Rh, Pd, Ag, Cd, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu, Hf, Ta, W, Re, Os, Ir, Pt, Au or Hg, for example.
Preferably, the catalyst metal includes Fe with at least one kind of metal selected from a group of Al, Ga, In, Cu, Ag, Au, Pd, and Mn added thereto.
Preferably, the catalyst metal includes Fe with Pd added thereto.
By this arrangement, the conversion efficiency of the reverse shift reaction can be further enhanced.
Preferably, the support may be composed of at least one selected from a group of SiO2, CeO2, TiO2, Al2O3, MgO, ZrO2, ZSM-5 (zeolite).
Preferably, an offgas generated in the generating step is mixed with the raw material gas before the reverse shift reaction.
Preferably, the apparatus further includes an offgas passage adapted to send out an offgas from the organic substance generator therethrough, the offgas passage extending to the reverse shift reactor.
By this arrangement, CO2 generated at the time of producing the organic substances can be subjected to the reverse shift reaction, thereby being converted into CO and used for the production of the organic substances. Thus, CO2 and CO can be used in a cyclic manner.
Preferably, the generating step includes a step of culturing microorganisms in a liquid culture medium; and the microorganisms fermentatively generate the organic substances from the raw material gas after the reverse shift reaction.
Preferably, the organic substance generator includes a culture tank adapted to culture microorganisms in a liquid culture medium therein; and the microorganisms fermentatively generate the organic substances from the raw material gas after the reverse shift reaction.
The efficiency of fermentative generation of the organic substances by the microorganisms can be enhanced by increasing a concentration of CO by the reverse shift reaction.
According to the present invention, the raw material gas can be subjected to the reverse shift reaction under a relatively low temperature condition, and thereby the operation cost can be reduced. By converting CO2 of the raw material gas into CO by the reverse shift reaction, the efficiency of generating the organic substances such as ethanol can be enhanced.
Embodiments of the present invention will be described hereinafter with reference to the drawings.
The raw material gas generator 2 is a waste disposal facility in this embodiment. Wastes may include municipal wastes, tires, biomass, wooden chips and plastic wastes. The waste disposal facility 2 is provided with a melting furnace. In the melting furnace, the wastes are burnt by a highly-concentrated oxygen gas and decomposed at a low-molecular level. Eventually, the raw material gas g1 (synthetic gas) is generated.
The raw material gas g1 (synthetic gas) may contain CO, H2 and CO2 as major constituents. A constituent ratio may be around 30 vol % of CO, around 30 vol % of H2 and around 30 vol % of CO2, but it is not required that the constituent ratio should be as given above. Most of the remaining constituents of the raw material gas g1 may be N2. The raw material gas g1 may further include minute amount of impure constituents such as H2S, O2 and benzene.
As shown in
The reverse shift reactor 12 is disposed at a point of the gas supply passage 10 on a downstream side with respect to the gas purifier 11. A reverse shirt reaction catalyst 20 is received in the reverse shift reactor 12. The reverse shift reaction catalyst 20 includes a support 21 and a catalyst metal 22. The support 21 may be composed of SiO2, CeO2, TiO2, Al2O3, MgO, ZrO2 or ZSM-5. In this embodiment, the support 21 is composed of silicon oxide (SiO2). The catalyst metal 22 is supported by the support 21. The supported catalyst may be prepared by wet impregnation, co-precipitation, Schlenk Line, or the like.
The catalyst metal 22 may include a transition metal such as Fe.
Preferably, the catalyst metal 22 may include Fe with at least one kind of metal from among Al, Ga, In, Cu, Ag, Au, Pd, and Mn added thereto. One kind of metal may be added or two or more kinds of metal may be added.
More preferably, the catalyst metal 22 is composed of Fe with Pd added thereto.
A content rate of the catalyst metal 22 in the reverse shift reaction catalyst 20 may be preferably 5 wt % to 50 wt % of the entire reverse shift reaction catalyst 20 and more preferably around 20 wt of the entire reverse shift reaction catalyst 20.
A content rate of added constituents (Al, Ga, In, Cu, Ag, Au, Pd or Mn) in the catalyst metal 22 may be preferably 0.1 wt % to 1.0 wt % of the entire catalyst metal 22 and more preferably around 0.2 wt % of the entire catalyst metal 22.
A heater 12h (temperature controller) is disposed in the reverse shift reactor 12. A temperature of an inside of the reverse shift reactor 12, and thereby a temperature of the reverse shift reaction catalyst 20 can be controlled to be a desired temperature by the heater 12h.
The organic substance generator 13 is disposed subsequent to the reverse shift reactor 12. The organic substance generator 13 is provided with a culture tank. A liquid culture medium is stored in the culture tank. Gas-utilizing microorganisms are cultured in the liquid culture medium. Anaerobic bacteria disclosed in the Patent Documents 1 to 3 mentioned above may be used as the gas-utilizing microorganisms, for example. The gas-utilizing microorganisms synthesize ethanol (C2H5OH), etc. from CO and H2, etc. by a fermentative action thereof.
A refiner 14 is disposed subsequent to the organic substance generator 13. The refiner 14 is composed of a distillation tower.
An offgas passage 15 extends from the organic substance generator 13. An offgas purifier 16 is disposed at a point along the offgas passage 15. The offgas purifier 16 includes a desulfurizing portion and a water eliminating portion. A downstream end of the offgas passage 15 is joined to the gas supply passage 10 at a point between the gas purifier 11 and the reverse shift reactor 12.
Ethanol (organic substance) is generated by the organic substance producing system 1 in the following manner:
The raw material gas g1 is generated by burning wastes at the waste disposal facility 2.
The raw material gas g1 is introduced to the gas supply passage 10.
Impure components such as H2S, O2 and benzene in the raw material gas g1 are removed in the gas purifier 11. The impure components may be removed by using a catalyst. The impure components may be removed by condensation. Thereby, the raw material gas g1 is purified.
Subsequently, the raw material gas g1 is introduced to the reverse shift reactor 12.
A temperature of the reverse shift reactor 12 is controlled to be 150 degrees C. to 500 degrees C. by the heater 12h.
A pressure of the reverse shift reactor 12 may be set at 0.8 to 2 atmospheric pressure (gauge pressure), for example.
The raw material gas g1 is contacted with the reverse shift reaction catalyst 20 in the reverse shift reactor 12. Thereby, at least a portion of CO2 and H2 in the raw material gas g1 is subjected to a reverse shift reaction as expressed in the following formula (1):
CO2+H2→CO+H2O (1)
Accordingly, CO2 in the raw material gas g1 can be converted into CO. The raw material gas after the reverse shift reaction is referred to as “raw material gas g2” hereinafter. CO concentration is higher in the raw material gas g2 than in the raw material gas g1 before the reverse shift reaction. CO2 concentration and H2 concentration are lower in the raw material gas g2 than in the raw material gas g1.
By using the reverse shift reaction catalyst 20 having a structure and composition mentioned above as a catalyst, a conversion efficiency of CO2→CO can be sufficiently enhanced. The conversion efficiency of 20% or higher can be achieved, for example.
By using Fe with a minute amount of Pb added thereto as the catalyst metal 22, the conversion efficiency can be enhanced to around 50%.
Thereby, the CO concentration in the raw material gas g2 can be made sufficiently high.
Moreover, temperature condition of about 150 degrees C. to 500 degrees C. may be sufficient for the reverse shift reaction, which is much lower than the temperature condition (700 degrees C. or higher) in the Patent Document 1 mentioned above. Accordingly, energy required for the heater 12h can be reduced, and therefore, an operation cost can be reduced.
The raw material gas g2 from the reverse shift reactor 12 is introduced into the liquid culture medium in the organic substance generator 13. Then the gas-utilizing microorganisms in the liquid culture medium take in CO and H2 in the raw material gas g2 and perform fermentation, thereby generating the target substance, ethanol.
The gas-utilizing microorganisms of this kind perform fermentation taking in more H2 than CO. Therefore, the efficiency of generating ethanol can be enhanced by making the CO concentration of the raw material gas g2 high in the reverse shift reaction step.
A portion b1 of the liquid culture medium in the organic substance generator 13 is taken out and sent out to the refiner 14 composed of a distillation tower. The liquid culture medium b1 is distilled in the refiner 14. Thereby, the ethanol (EtOH) can be refined.
An amount of the culture medium in the organic substance generator 13 is arranged to be maintained constant by newly replenishing the culture medium to the organic substance generator 13 in an amount corresponding to the sent out amount.
CO2 is generated as a by-product during the fermentation of ethanol mentioned above. Therefore, a large amount of CO2 is contained in an offgas g3 from the organic substance generator 13. Besides CO2, the offgas g3 contains CO, H2, etc. of the raw material gas g2 that were not used for the fermentation. The offgas g3 is sent to the offgas purifier 16. Impure components of the offgas g3 such as H2O and a minute amount of H2S are removed in the offgas purifier 16.
After that, the offgas g3 is joined to the gas supply passage 10 via the offgas passage 15 and mixed with the raw material gas g1 in the gas supply passage 10. Thereby, CO2 in the offgas g3 can be provided to the reverse shift reactor 12 together with the raw material gas g1 for the reverse shift reaction. In short, CO2 generated in the fermentation step as the by-product can be converted into CO, and the CO can be sent to the organic substance generator 13 as a part of the raw material gas g2 and can be used for fermentation. Thereby, CO2 and CO can be used in a cyclic manner in which the CO2 and CO are repeatedly converted into each other.
Other embodiments of the present invention will be described hereinafter. Same reference numerals are used in the drawings to designate parts that correspond to those in foregoing embodiments and description thereof will be omitted.
The hydrogen generator 5 is disposed at a point along a gas supply passage 10 from the carbon dioxide generator 4.
The hydrogen generator 5 may be a steam reforming plant for natural gas such as methane (CH4). The methane is steam-reformed as expressed in the following formula (2):
CH4+H2O→CO+3H2 (2)
The reformed gas (CO, H2) is mixed with the CO2 from the carbon dioxide generator 4. Thereby, a raw material gas g1 (synthetic gas) containing CO, H2 and CO2 can be obtained. The raw material gas g1 is supplied to a reverse shift reactor 12 via a gas purifier 11, and thereby subjected to a reverse shift reaction. Thus, a CO rich raw material gas g2 can be obtained. Thereby, an efficiency of generation of ethanol in an organic substrate generator 13 can be enhanced.
The present invention is not limited to the embodiments described above. Various modifications can be made without departing from the scope and spirit of the invention.
For example, the catalyst metal 22 of the reverse shift reaction catalyst 20 may be composed only of Fe, without containing the added constituents.
The organic substrate generator 13 may generate ethanol by bringing the raw material gas g2 into contact with the metal catalyst instead of by microbial fermentation.
b1 culture medium
g1 raw material gas
g2 raw material gas after the reverse shift reaction
g3 offgas
1 organic substance producing system
2 waste disposal facility (raw material gas generator)
2B raw material gas generator
3 organic substance producing apparatus
4 carbon dioxide generator
5 hydrogen generator
10 gas supply passage
11 gas purifier
12 reverse shift reactor
12
h heater (temperature controller)
13 organic substance generator
14 refiner
15 offgas passage
16 offgas purifier
20 reverse shift reaction catalyst
21 support (silicon oxide substrate)
22 catalyst metal
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015-057556 | Mar 2015 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2016/058431 | 3/17/2016 | WO | 00 |
