CN105803002A - Method for preparing hydrogen by virtue of xylose - Google Patents
Method for preparing hydrogen by virtue of xylose Download PDFInfo
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- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 title claims abstract description 66
- 239000001257 hydrogen Substances 0.000 title claims abstract description 57
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 57
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 54
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 title claims abstract description 33
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 12
- 230000009603 aerobic growth Effects 0.000 claims abstract description 11
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 8
- 230000012010 growth Effects 0.000 claims abstract description 5
- 239000001963 growth medium Substances 0.000 claims description 14
- 230000001580 bacterial effect Effects 0.000 claims description 4
- 241000894006 Bacteria Species 0.000 claims 2
- 239000012531 culture fluid Substances 0.000 claims 2
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 claims 1
- 229910000397 disodium phosphate Inorganic materials 0.000 claims 1
- 229910052564 epsomite Inorganic materials 0.000 claims 1
- 230000001954 sterilising effect Effects 0.000 claims 1
- 238000002255 vaccination Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 26
- 239000007788 liquid Substances 0.000 abstract description 9
- 239000000758 substrate Substances 0.000 abstract description 9
- 241000588749 Klebsiella oxytoca Species 0.000 abstract description 7
- 238000000855 fermentation Methods 0.000 abstract description 7
- 238000011081 inoculation Methods 0.000 abstract description 7
- 150000002772 monosaccharides Chemical class 0.000 abstract description 6
- 238000005273 aeration Methods 0.000 abstract description 5
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
- 235000000346 sugar Nutrition 0.000 abstract description 5
- 150000002431 hydrogen Chemical class 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000002029 lignocellulosic biomass Substances 0.000 abstract description 3
- 230000000813 microbial effect Effects 0.000 abstract description 2
- 239000013587 production medium Substances 0.000 abstract description 2
- 238000012258 culturing Methods 0.000 abstract 1
- 239000002609 medium Substances 0.000 description 8
- 230000004151 fermentation Effects 0.000 description 4
- 239000002054 inoculum Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229920002488 Hemicellulose Polymers 0.000 description 2
- 239000001888 Peptone Substances 0.000 description 2
- 108010080698 Peptones Proteins 0.000 description 2
- AAELHWDCDSZXGG-UHFFFAOYSA-L [Na+].[Cl+].[Cl-].[Cl-] Chemical compound [Na+].[Cl+].[Cl-].[Cl-] AAELHWDCDSZXGG-UHFFFAOYSA-L 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 230000009604 anaerobic growth Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229940041514 candida albicans extract Drugs 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 235000019319 peptone Nutrition 0.000 description 2
- 239000012138 yeast extract Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P3/00—Preparation of elements or inorganic compounds except carbon dioxide
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Abstract
本发明公开了一种利用木糖制备氢气的方法,包括:1)取Klebsiella oxytoca GS‑4‑08菌种,培养获得种子液;2)取种子液接种于灭菌后的产氢培养基中,然后在35℃下进行好氧生长;培养得到的大量的Klebsiella oxytoca GS‑4‑08菌种培养液;3)对培养液进行曝氮气处理,曝氮气完毕后,将好氧生长到指数生长末期时的培养液按照100%的接种率投加到木糖溶液中;4)厌氧反应,收集氢气。本发明利用微生物厌氧发酵木糖制氢,具备治污、环保和产能等多重优越性,开发前景广阔。自然界中大量可再生的木质纤维类生物质丰富且廉价,木质纤维素水解成分主要是单糖,单糖中的五碳糖约占30~40%,因此,有效利用木糖产氢特性,对于扩展底物范围,降低生物制氢成本,实现生物制氢的工业化具有重要的意义。
The invention discloses a method for preparing hydrogen by using xylose, comprising: 1) taking Klebsiella oxytoca GS-4-08 strain, culturing to obtain seed liquid; 2) taking the seed liquid and inoculating it in a sterilized hydrogen production medium , and then aerobic growth at 35°C; a large amount of Klebsiella oxytoca GS-4-08 strain culture solution obtained from the cultivation; 3) Nitrogen treatment was carried out on the culture solution, and after the nitrogen aeration was completed, the aerobic growth to exponential growth The culture solution at the end stage was added to the xylose solution according to the inoculation rate of 100%; 4) Anaerobic reaction, hydrogen gas was collected. The invention utilizes microbial anaerobic fermentation of xylose to produce hydrogen, has multiple advantages such as pollution control, environmental protection, and production capacity, and has broad development prospects. A large amount of renewable lignocellulosic biomass in nature is abundant and cheap. The hydrolyzed components of lignocellulose are mainly monosaccharides, and the five-carbon sugars in monosaccharides account for about 30-40%. It is of great significance to expand the scope of substrates, reduce the cost of biohydrogen production, and realize the industrialization of biohydrogen production.
Description
技术领域 technical field
本发明属于新能源领域,涉及一种利用木糖制备氢气的方法。 The invention belongs to the field of new energy, and relates to a method for preparing hydrogen from xylose.
背景技术 Background technique
氢气作为高效、清洁、可再生的能源,越来越受到人们的关注。在多种制氢方法中,利用微生物厌氧发酵生物质(如有机废水、有机垃圾等)制氢,具备治污、环保和产能等多重优越性,开发前景广阔。研究者们做了很多卓有成效的研究工作,其中之一就是扩大底物利用范围。自然界中大量可再生的木质纤维类生物质丰富且廉价,如果能够解决利用木质纤维素作为原材料最终获取氢气这个关键问题,它将使得获取廉价氢气和实现产业化成为可能。木质纤维素主要有木质素、纤维素和半纤维素组成,纤维素和半纤维素的水解成分主要是单糖和少量的简单聚糖,其中单糖主要是以葡萄糖为主的六碳糖约占 60%~70%,以木糖为主的五碳糖约占30%~40%,而先前关于葡萄糖制备氢气已有所报道,而木糖则因为难分解等问题而没有得到应用。因此研究利用木糖等五碳糖产氢特性,对于扩展底物范围,降低生物制氢成本,实现生物制氢的工业化具有重要的意义。 As an efficient, clean and renewable energy, hydrogen has attracted more and more attention. Among various hydrogen production methods, the use of microbial anaerobic fermentation of biomass (such as organic wastewater, organic waste, etc.) to produce hydrogen has multiple advantages such as pollution control, environmental protection and production capacity, and has broad development prospects. Researchers have done a lot of fruitful research work, one of which is to expand the scope of substrate utilization. A large amount of renewable lignocellulosic biomass in nature is abundant and cheap. If the key problem of using lignocellulose as a raw material to obtain hydrogen can be solved, it will make it possible to obtain cheap hydrogen and realize industrialization. Lignocellulose is mainly composed of lignin, cellulose and hemicellulose. The hydrolyzed components of cellulose and hemicellulose are mainly monosaccharides and a small amount of simple polysaccharides, of which the monosaccharides are mainly six-carbon sugars of about It accounts for 60%~70%, and the five-carbon sugar mainly composed of xylose accounts for about 30%~40%. However, there have been reports on the preparation of hydrogen from glucose, while xylose has not been applied due to problems such as difficult decomposition. Therefore, it is of great significance to study the hydrogen production characteristics of five-carbon sugars such as xylose to expand the scope of substrates, reduce the cost of biological hydrogen production, and realize the industrialization of biological hydrogen production.
发明内容 Contents of the invention
发明目的:针对现有技术中存在的不足,本发明的目的是提供了一种利用木糖制备氢气的方法,降低生物制氢成本,实现生物制氢的工业化。 Purpose of the invention: In view of the deficiencies in the prior art, the purpose of the invention is to provide a method for producing hydrogen from xylose, reduce the cost of biological hydrogen production, and realize the industrialization of biological hydrogen production.
技术方案:为了实现上述发明目的,本发明采用的技术方案为: Technical solution: In order to realize the above-mentioned purpose of the invention, the technical solution adopted in the present invention is:
一种利用木糖制备氢气的方法,包括以下步骤: A method for producing hydrogen from xylose, comprising the steps of:
1)取Klebsiella oxytoca GS-4-08菌种,培养获得种子液; 1) Take the Klebsiella oxytoca GS-4-08 strain and cultivate it to obtain the seed solution;
2)取种子液接种于灭菌后的细菌生长培养基中,然后在35℃下进行好氧生长; 培养得到的大量的Klebsiella oxytoca GS-4-08菌种培养液; 2) Take the seed liquid and inoculate it in the sterilized bacterial growth medium, and then perform aerobic growth at 35°C; cultivate a large amount of Klebsiella oxytoca GS-4-08 strain culture liquid;
3)对产氢培养基进行曝氮气处理,曝氮气完毕后,将好氧生长到指数生长末期时的培养液按照100%的接种率投加到产氢培养基中; 3) Nitrogen aeration is performed on the hydrogen-producing medium. After the nitrogen aeration is completed, the culture solution grown aerobically to the end of exponential growth is added to the hydrogen-producing medium at an inoculation rate of 100%;
4)厌氧反应,收集氢气。 4) Anaerobic reaction, collecting hydrogen.
步骤1)中,用生长培养基培养种子液。 In step 1), the seed liquid is incubated with the growth medium.
步骤2)中,产氢培养基的配方为:0.5g/L KH2PO4、1.57g/L Na2HPO4·12H2O、0.1g/L MgSO4·7H2O。 In step 2), the formula of the hydrogen production medium is: 0.5g/L KH 2 PO 4 , 1.57g/L Na 2 HPO 4 ·12H 2 O, 0.1g/L MgSO 4 ·7H 2 O.
步骤2)中,产氢培养基的pH值为7.0左右。 In step 2), the pH value of the hydrogen-producing medium is about 7.0.
步骤2)中,在35℃下进行好氧生长12h。 In step 2), aerobic growth was carried out at 35°C for 12h.
步骤3)中,木糖溶液浓度为2~8g/L。 In step 3), the concentration of xylose solution is 2-8g/L.
步骤4)中,厌氧反应48h以上。 In step 4), the anaerobic reaction lasts for more than 48 hours.
有益效果:自然界中大量可再生的木质纤维类生物质丰富且廉价,木质纤维素水解成分主要是单糖,单糖中的五碳糖约占 30~40%,因此,有效利用木糖产氢特性,对于扩展底物范围,降低生物制氢成本,实现生物制氢的工业化具有重要的意义。本发明利用Klebsiella oxytoca GS-4-08菌种厌氧发酵木糖制氢,转化率为38.5mL氢气/g木糖,具备治污、环保和产能等多重优越性,开发前景广阔,可实现工业化。 Beneficial effects: A large amount of renewable lignocellulosic biomass in nature is abundant and cheap. Lignocellulose hydrolysis components are mainly monosaccharides, and five-carbon sugars in monosaccharides account for about 30-40%. Therefore, effective use of xylose to produce hydrogen It is of great significance to expand the scope of substrates, reduce the cost of biohydrogen production, and realize the industrialization of biohydrogen production. The invention uses Klebsiella oxytoca GS-4-08 strain to anaerobically ferment xylose to produce hydrogen, and the conversion rate is 38.5mL hydrogen/g xylose. It has multiple advantages such as pollution control, environmental protection and production capacity. It has broad development prospects and can realize industrialization .
附图说明 Description of drawings
图1是不同木糖浓度下的产氢结果图; Fig. 1 is the result figure of hydrogen production under different xylose concentrations;
图2是1%的接种率下的总产氢量结果图。 Fig. 2 is a result graph of total hydrogen production under 1% inoculum rate.
具体实施方式 detailed description
下面结合具体实施例对本发明做进一步的说明。 The present invention will be further described below in conjunction with specific embodiments.
实施例1 Example 1
一种利用木糖制备氢气的方法,包括以下步骤: A method for producing hydrogen from xylose, comprising the steps of:
1)取Klebsiella oxytoca GS-4-08菌种(为CN105524944A公开的菌种),用生长培养基活化,获得种子液;生长培养基的配方为:酵母膏5g/L、蛋白胨10g/L、氯化钠10g/L。 1) Take the Klebsiella oxytoca GS-4-08 strain (the strain disclosed in CN105524944A), activate it with the growth medium, and obtain the seed liquid; the formula of the growth medium is: yeast extract 5g/L, peptone 10g/L, chlorine Sodium chloride 10g/L.
2)取种子液,接种于灭菌后的生长培养基中,细菌活化温度35℃,转速180r/min,好氧生长12小时;再进行曝氮气处理;产氢培养基(发酵培养基)的配方为:KH2PO4 0.5g/L、Na2HPO4·12H2O 1.57 g/L、 MgSO4·7H2O 0.1g/L。 2) Take the seed liquid and inoculate it in the sterilized growth medium. The bacterial activation temperature is 35°C, the rotation speed is 180r/min, and the aerobic growth is performed for 12 hours; The formula is: KH 2 PO 4 0.5g/L, Na 2 HPO 4 ·12H 2 O 1.57 g/L, MgSO 4 ·7H 2 O 0.1g/L.
3)曝氮气完毕后,将好氧生长到指数生长末期时的培养液按照100%的接种率投加到产氢培养基中;在产氢培养基中添加木糖作为底物,72h的厌氧反应(发酵)中,每间隔12小时进行取样采集氢气的体积和含量,厌氧反应(发酵)温度为35℃。 3) After the nitrogen aeration is completed, the culture solution from aerobic growth to the end of exponential growth is added to the hydrogen-producing medium at a 100% inoculum rate; xylose is added as a substrate in the hydrogen-producing medium, and the anaerobic growth period of 72 hours During the oxygen reaction (fermentation), samples were taken every 12 hours to collect the volume and content of hydrogen, and the anaerobic reaction (fermentation) temperature was 35°C.
2~8g/L木糖浓度下的总产氢量,结果如图1所示,可以看出,当底物木糖的浓度分别2、4、6、8g/L时,产氢的量分别为72.69mL、93.73、100.48、104.28mL,木糖转化率分别为93.45%、63.45%、58.3%、62.5%。因此在厌氧发酵过程中,当增加底物浓度时,产氢量会得到相应的增加,但在2g/L时木糖转化率最大。 The results of the total hydrogen production under the xylose concentration of 2~8g/L are shown in Figure 1. It can be seen that when the substrate xylose concentrations are 2, 4, 6, and 8g/L, the hydrogen production is respectively were 72.69mL, 93.73, 100.48, and 104.28mL, and the conversion rates of xylose were 93.45%, 63.45%, 58.3%, and 62.5%, respectively. Therefore, in the process of anaerobic fermentation, when the substrate concentration is increased, the hydrogen production will be increased accordingly, but the conversion rate of xylose is the largest at 2g/L.
实施例2 Example 2
1%接种率条件下,木糖制备氢气的方法,包括以下步骤: Under the condition of 1% inoculum rate, the method for preparing hydrogen from xylose comprises the following steps:
1)取Klebsiella oxytoca GS-4-08菌种(为CN105524944A公开的菌种),用生长培养基活化,获得种子液;生长培养基的配方为:酵母膏5g/L、蛋白胨10g/L、氯化钠10g/L。 1) Take the Klebsiella oxytoca GS-4-08 strain (the strain disclosed in CN105524944A), activate it with the growth medium, and obtain the seed liquid; the formula of the growth medium is: yeast extract 5g/L, peptone 10g/L, chlorine Sodium chloride 10g/L.
2)取种子液,接种于灭菌后的生长培养基中,细菌活化温度35℃,转速180r/min,好氧生长12小时;再进行曝氮气处理;产氢培养基(发酵培养基)的配方为:KH2PO4 0.5g/L、Na2HPO4·12H2O 1.57 g/L、 MgSO4·7H2O 0.1g/L。 2) Take the seed liquid and inoculate it in the sterilized growth medium. The bacterial activation temperature is 35°C, the rotation speed is 180r/min, and the aerobic growth is performed for 12 hours; The formula is: KH 2 PO 4 0.5g/L, Na 2 HPO 4 ·12H 2 O 1.57 g/L, MgSO 4 ·7H 2 O 0.1g/L.
3)曝氮气完毕后,将好氧生长到指数生长末期时的培养液按照1%的接种率投加到产氢培养基中;在产氢培养基中添加木糖作为底物,72h的厌氧反应(发酵)中,每间隔12小时进行取样采集氢气的体积和含量,厌氧反应(发酵)温度为35℃。 3) After the nitrogen aeration is completed, the culture solution from aerobic growth to the end of exponential growth is added to the hydrogen-producing medium at an inoculation rate of 1%; xylose is added to the hydrogen-producing medium as a substrate, and the anaerobic growth period of 72 hours During the oxygen reaction (fermentation), samples were taken every 12 hours to collect the volume and content of hydrogen, and the anaerobic reaction (fermentation) temperature was 35°C.
1%的接种率下的总产氢量,结果如图2所示,可以看出,当木糖浓度为2g/L时,产氢量为48.8mL,与相同条件下,接菌率为100%的产氢培养基的产氢量减少13.8mL。因此,接菌率也是影响以木糖为底物进行产氢的因素之一,适当提高接菌率可以增加氢气的产量。 The results of the total hydrogen production under the inoculation rate of 1% are shown in Figure 2. It can be seen that when the xylose concentration is 2g/L, the hydrogen production is 48.8mL, which is 100% of the inoculation rate under the same conditions. The hydrogen production of the hydrogen-producing medium was reduced by 13.8mL. Therefore, the inoculation rate is also one of the factors affecting the hydrogen production using xylose as a substrate, and a proper increase in the inoculation rate can increase the hydrogen production.
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