CN102268303B - Method for preparing biological diesel oil by using sludge from municipal wastewater treatment plant - Google Patents
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- 239000010802 sludge Substances 0.000 title claims abstract description 59
- 238000000034 method Methods 0.000 title claims abstract description 8
- 238000004065 wastewater treatment Methods 0.000 title abstract description 4
- 239000002283 diesel fuel Substances 0.000 title abstract 4
- 239000010841 municipal wastewater Substances 0.000 title abstract 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 27
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000007062 hydrolysis Effects 0.000 claims abstract description 16
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 16
- 238000005886 esterification reaction Methods 0.000 claims abstract description 14
- 239000002994 raw material Substances 0.000 claims abstract description 10
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims abstract description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000003756 stirring Methods 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 239000003225 biodiesel Substances 0.000 claims description 30
- 239000000203 mixture Substances 0.000 claims description 21
- 239000010865 sewage Substances 0.000 claims description 19
- 230000032050 esterification Effects 0.000 claims description 13
- 238000000605 extraction Methods 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 11
- 239000012141 concentrate Substances 0.000 claims description 7
- 239000002244 precipitate Substances 0.000 claims description 7
- 150000007524 organic acids Chemical class 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract 1
- 239000011259 mixed solution Substances 0.000 abstract 1
- 230000001376 precipitating effect Effects 0.000 abstract 1
- 230000000717 retained effect Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 12
- 241000196324 Embryophyta Species 0.000 description 9
- 238000001035 drying Methods 0.000 description 6
- 239000003921 oil Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 3
- 210000002421 cell wall Anatomy 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 240000002791 Brassica napus Species 0.000 description 1
- 235000011293 Brassica napus Nutrition 0.000 description 1
- 240000003133 Elaeis guineensis Species 0.000 description 1
- 235000001950 Elaeis guineensis Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 240000006711 Pistacia vera Species 0.000 description 1
- 235000003447 Pistacia vera Nutrition 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002551 biofuel Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 150000002895 organic esters Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 150000003904 phospholipids Chemical class 0.000 description 1
- 235000020233 pistachio Nutrition 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Treatment Of Sludge (AREA)
Abstract
Description
技术领域 technical field
本发明属于清洁能源开发领域,涉及生物柴油的制备,具体涉及利用城市污水厂污泥制取生物柴油的方法。The invention belongs to the field of clean energy development, and relates to the preparation of biodiesel, in particular to a method for preparing biodiesel from sludge of urban sewage plants.
背景技术 Background technique
城市污水处理厂的大量建设,使剩余污泥大量产生并已经成为影响大气和水环境的一大重要污染源,但是剩余污泥中含有约20%的可酯化成分。另一方面,生物柴油作为清洁的可再生能源,是优质的石油柴油代用品。生物柴油以大豆和油菜籽等油料作物、油棕和黄连木等油料林木果实、工程微藻等油料水生植物以及动物油脂、餐饮废油等为原料制成,其制备成本的75%来自于原材料。The massive construction of urban sewage treatment plants has produced a large amount of excess sludge and has become an important source of pollution affecting the atmosphere and water environment. However, excess sludge contains about 20% of esterifiable components. On the other hand, as a clean renewable energy source, biodiesel is a high-quality substitute for petroleum diesel. Biodiesel is made from oil-bearing crops such as soybeans and rapeseeds, oil-bearing forest fruits such as oil palm and pistachio, engineering microalgae and other oil-bearing aquatic plants, animal fats, and waste catering oils, etc., and 75% of its preparation cost comes from raw materials .
利用城市污水处理厂污泥制取生物柴油在国内尚未有报道,国外的专利目前有2项:(1)专利申请号:US20040956069,专利持有人:Zappi Mark E;FrenchWilliam Todd;Hernandez Rafael;Dufreche Stephen Thomas,专利名称:Productionof biodiesel and other valuable chemicals from wastewater treatment plant sludges;(2)专利申请号:US20090429858,专利持有人:Miguel ASCON;DoloresASCON,专利名称:Methods and systems for production of biofuels and bioenergyproducts from sewage sludge.。以上专利,均采用干污泥进行原位酯化,但是污泥干化过程中构成细胞壁的磷脂处于生物质体的最外层,使其转化为有机酯的条件非常苛刻,而包在细胞壁内的有机酸只能部分酯化。另一方面,在污泥干化过程中,为获得5%含水率的干污泥需要经过离心、烘干、粉碎等过程,必将消耗大量的能量,且在污泥烘干过程中,部分VFA以及醇类也将不可避免地挥发掉,减少了剩余污泥向生物柴油的转化率。总之,原位酯化干剩余污泥,将无法避免酯化条件高、能量耗费大、生物柴油转化率低的问题。There are no reports in China on the production of biodiesel from sludge from urban sewage treatment plants. There are currently two foreign patents: (1) Patent application number: US20040956069, patent holder: Zappi Mark E; FrenchWilliam Todd; Hernandez Rafael; Dufreche Stephen Thomas, patent name: Production of biodiesel and other valuable chemicals from wastewater treatment plant sludges; (2) patent application number: US20090429858, patent holder: Miguel ASCON; DoloresASCON, patent name: Methods and systems for production of biofuels y rombioener g sewage sludge.. The above patents all use dry sludge for in-situ esterification, but during the sludge drying process, the phospholipids that make up the cell wall are in the outermost layer of the biomass, making the conditions for converting them into organic esters very harsh, and they are enclosed in the cell wall. organic acids can only be partially esterified. On the other hand, in the sludge drying process, in order to obtain dry sludge with a moisture content of 5%, it needs to go through processes such as centrifugation, drying, and crushing, which will consume a lot of energy, and in the sludge drying process, some VFA and alcohols will also inevitably volatilize, reducing the conversion rate of excess sludge to biodiesel. In short, the in-situ esterification and drying of excess sludge cannot avoid the problems of high esterification conditions, high energy consumption, and low conversion rate of biodiesel.
发明内容 Contents of the invention
为了克服上述现有技术的不足,本发明的目的在于提供一种利用城市污水厂污泥制取生物柴油的方法,在节能的前提下,尽量保留剩余污泥中的可酯化成分以提高大分子有机酸的浓度,从而最大可能地提高生物柴油的转化率并降低污泥制取生物柴油成本。In order to overcome the above-mentioned deficiencies in the prior art, the purpose of the present invention is to provide a method for producing biodiesel from sludge from urban sewage plants. On the premise of energy saving, the esterifiable components in the remaining sludge should be kept as much as possible to increase the biodiesel production efficiency. The concentration of molecular organic acids can increase the conversion rate of biodiesel as much as possible and reduce the cost of producing biodiesel from sludge.
为了实现上述目的,本发明采用的技术方案是:In order to achieve the above object, the technical scheme adopted in the present invention is:
利用城市污水厂污泥制取生物柴油的方法,包括以下步骤:The method for producing biodiesel from sludge of urban sewage plant comprises the following steps:
第一步,生物强化水解:以污水处理厂产生的初沉污泥或剩余污泥为原料,首先沉淀浓缩使其浓度在20~25g/L范围,然后在浓缩后的每升污泥中添加OD600为0.5~0.6的纯酵母菌20~40ml,35℃下强化水解2~4天;The first step, biologically enhanced hydrolysis: use the primary sludge or excess sludge produced by the sewage treatment plant as raw material, first precipitate and concentrate to make the concentration within the range of 20-25g/L, and then add 20-40ml of pure yeast with OD 600 of 0.5-0.6, strengthen hydrolysis at 35°C for 2-4 days;
第二步,化学酯化:取1L水解后的生物强化水解污泥混合液,加入1~1.2L甲醇,再滴加0.07~0.1L质量分数为98%的浓硫酸溶液,在70~80℃温度下搅拌反应24小时;The second step, chemical esterification: take 1L of the hydrolyzed biologically enhanced hydrolyzed sludge mixture, add 1-1.2L of methanol, and then dropwise add 0.07-0.1L of concentrated sulfuric acid solution with a mass fraction of 98%, at 70-80°C Stirring reaction at high temperature for 24 hours;
第三步,萃取:将化学酯化后的混合液在空气中自然降温至室温,加入1L正己烷,混合3~5min,3000~3500rpm转速下离心3~5min。The third step, extraction: naturally cool down the chemically esterified mixture to room temperature in the air, add 1 L of n-hexane, mix for 3-5 minutes, and centrifuge at 3000-3500 rpm for 3-5 minutes.
为提高产率,可将所述的萃取过程反复进行三次。In order to increase the yield, the extraction process can be repeated three times.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
以城市污水处理厂污泥为原材料强化水解并对其上清液进行酯化制取生物柴油,无污泥离心干化以及油脂提取过程,在污泥制取生物柴油转化率提高了25%的条件下降低污泥制取生物柴油成本费用的20-30%,。Using sludge from urban sewage treatment plants as raw material to strengthen hydrolysis and esterify its supernatant to produce biodiesel, no sludge centrifugal drying and oil extraction process, the conversion rate of sludge to biodiesel has increased by 25% 20-30% of the cost of producing biodiesel from sludge can be reduced under certain conditions.
具体实施方式 Detailed ways
下面结合实施例对本发明做进一步详细说明。The present invention will be described in further detail below in conjunction with the examples.
实施例一Embodiment one
利用城市污水厂污泥制取生物柴油的方法,包括以下步骤:The method for producing biodiesel from sludge of urban sewage plant comprises the following steps:
第一步,生物强化水解:以污水处理厂产生的初沉污泥或剩余污泥为原料,首先沉淀浓缩使其浓度为20g/L,然后在浓缩后的每升污泥中添加OD600为0.5的纯酵母菌40ml,35℃下强化水解4天;The first step, bio-enhanced hydrolysis: use the primary sludge or excess sludge produced by the sewage treatment plant as raw material, first precipitate and concentrate to make the concentration 20g/L, and then add OD 600 to each liter of concentrated sludge as 0.5 pure yeast 40ml, strengthen hydrolysis at 35°C for 4 days;
第二步,化学酯化:取1L水解后的生物强化水解污泥混合液,加入1L甲醇,再滴加0.1L质量分数为98%的浓硫酸溶液,在80℃温度下搅拌反应24小时;The second step, chemical esterification: take 1L of the hydrolyzed biologically enhanced hydrolyzed sludge mixture, add 1L of methanol, then dropwise add 0.1L of concentrated sulfuric acid solution with a mass fraction of 98%, and stir and react at 80°C for 24 hours;
第三步,萃取:将化学酯化后的混合液在空气中自然降温至室温,加入1L正己烷,混合5min,3000rpm转速下离心5min,即得生物柴油。The third step, extraction: naturally cool down the chemically esterified mixture to room temperature in the air, add 1 L of n-hexane, mix for 5 minutes, and centrifuge at 3000 rpm for 5 minutes to obtain biodiesel.
实施例二Embodiment two
利用城市污水厂污泥制取生物柴油的方法,包括以下步骤:The method for producing biodiesel from sludge of urban sewage plant comprises the following steps:
第一步,生物强化水解:以污水处理厂产生的初沉污泥或剩余污泥为原料,首先沉淀浓缩使其浓度为25g/L,然后在浓缩后的每升污泥中添加OD600为0.5的纯酵母菌20ml,35℃下强化水解2天;The first step, biologically enhanced hydrolysis: using the primary sludge or excess sludge produced by the sewage treatment plant as raw material, first precipitate and concentrate to make the concentration 25g/L, and then add OD 600 to each liter of concentrated sludge as 0.5 pure yeast 20ml, strengthen hydrolysis at 35°C for 2 days;
第二步,化学酯化:取1L水解后的生物强化水解污泥混合液,加入1.2L甲醇,再滴加0.07L质量分数为98%的浓硫酸溶液,在70℃温度下搅拌反应24小时;The second step, chemical esterification: take 1L of the hydrolyzed biologically enhanced hydrolyzed sludge mixture, add 1.2L of methanol, then dropwise add 0.07L of concentrated sulfuric acid solution with a mass fraction of 98%, and stir and react at 70°C for 24 hours ;
第三步,萃取:将化学酯化后的混合液在空气中自然降温至室温,加入1L正己烷,混合3min,3000rpm转速下离心5min,即得生物柴油。The third step, extraction: naturally cool the mixture after chemical esterification to room temperature in the air, add 1 L of n-hexane, mix for 3 minutes, and centrifuge at 3000 rpm for 5 minutes to obtain biodiesel.
实施例三Embodiment Three
利用城市污水厂污泥制取生物柴油的方法,包括以下步骤:The method for producing biodiesel from sludge of urban sewage plant comprises the following steps:
第一步,生物强化水解:以污水处理厂产生的初沉污泥或剩余污泥为原料,首先沉淀浓缩使其浓度为21.5g/L,然后在浓缩后的每升污泥中添加OD600为0.56的纯酵母菌35ml,35℃下强化水解3天;The first step, bio-enhanced hydrolysis: use the primary sludge or excess sludge produced by the sewage treatment plant as raw material, first precipitate and concentrate to make the concentration 21.5g/L, and then add OD 600 to each liter of concentrated sludge 35ml of 0.56 pure yeast, enhanced hydrolysis at 35°C for 3 days;
第二步,化学酯化:取1L水解后的生物强化水解污泥混合液,加入1.2L甲醇,再滴加0.084L质量分数为98%的浓硫酸溶液,在80℃温度下搅拌反应24小时;The second step, chemical esterification: take 1L of the hydrolyzed biologically enhanced hydrolyzed sludge mixture, add 1.2L of methanol, then dropwise add 0.084L of concentrated sulfuric acid solution with a mass fraction of 98%, and stir and react at 80°C for 24 hours ;
第三步,萃取:将化学酯化后的混合液在空气中自然降温至室温,加入1L正己烷,混合5min,3500rpm转速下离心3min,即得生物柴油。The third step, extraction: naturally cool down the chemically esterified mixture to room temperature in the air, add 1 L of n-hexane, mix for 5 minutes, and centrifuge at 3500 rpm for 3 minutes to obtain biodiesel.
实施例四Embodiment Four
利用城市污水厂污泥制取生物柴油的方法,包括以下步骤:The method for producing biodiesel from sludge of urban sewage plant comprises the following steps:
第一步,生物强化水解:以污水处理厂产生的初沉污泥或剩余污泥为原料,首先沉淀浓缩使其浓度为24g/L,然后在浓缩后的每升污泥中添加OD600为0.6的纯酵母菌25ml,35℃下强化水解4天;The first step, biologically enhanced hydrolysis: use the primary sludge or excess sludge produced by the sewage treatment plant as raw material, first precipitate and concentrate to make the concentration 24g/L, and then add OD 600 to each liter of concentrated sludge as 25ml of 0.6 pure yeast, enhanced hydrolysis at 35°C for 4 days;
第二步,化学酯化:取1L水解后的生物强化水解污泥混合液,加入1L甲醇,再滴加0.1L质量分数为98%的浓硫酸溶液,在75℃温度下搅拌反应24小时;The second step, chemical esterification: take 1L of the hydrolyzed biologically enhanced hydrolyzed sludge mixture, add 1L of methanol, then dropwise add 0.1L of concentrated sulfuric acid solution with a mass fraction of 98%, and stir and react at 75°C for 24 hours;
第三步,萃取:将化学酯化后的混合液在空气中自然降温至室温,加入1L正己烷,混合5min,3300rpm转速下离心4min,即得生物柴油。The third step, extraction: naturally cool down the chemically esterified mixture to room temperature in the air, add 1 L of n-hexane, mix for 5 minutes, and centrifuge at 3300 rpm for 4 minutes to obtain biodiesel.
实施例五Embodiment five
利用城市污水厂污泥制取生物柴油的方法,包括以下步骤:The method for producing biodiesel from sludge of urban sewage plant comprises the following steps:
第一步,生物强化水解:以污水处理厂产生的初沉污泥或剩余污泥为原料,首先沉淀浓缩使其浓度为23g/L,然后在浓缩后的每升污泥中添加OD600为0.5的纯酵母菌40ml,35℃下强化水解4天;The first step, bio-enhanced hydrolysis: use the primary sludge or excess sludge produced by the sewage treatment plant as raw material, first precipitate and concentrate to make the concentration 23g/L, and then add OD 600 to each liter of concentrated sludge as 0.5 pure yeast 40ml, strengthen hydrolysis at 35°C for 4 days;
第二步,化学酯化:取1L水解后的生物强化水解污泥混合液,加入1.04L甲醇,再滴加0.07L质量分数为98%的浓硫酸溶液,在80℃温度下搅拌反应24小时;The second step, chemical esterification: take 1L of the hydrolyzed biologically enhanced hydrolyzed sludge mixture, add 1.04L of methanol, then dropwise add 0.07L of concentrated sulfuric acid solution with a mass fraction of 98%, and stir and react at 80°C for 24 hours ;
第三步,萃取:将化学酯化后的混合液在空气中自然降温至室温,加入1L正己烷,混合3min,3000rpm转速下离心3min,即得生物柴油。The third step, extraction: naturally cool the mixture after chemical esterification to room temperature in the air, add 1 L of n-hexane, mix for 3 minutes, and centrifuge at 3000 rpm for 3 minutes to obtain biodiesel.
在实施例五的条件下,生物柴油产率为9.24%(以干污泥计),本发明所用的纯酵母菌、浓硫酸、甲醇以及正己烷等试剂价格低廉,来源广泛,有效降低了制备成本。Under the conditions of Example 5, the yield of biodiesel was 9.24% (in terms of dry sludge). The reagents such as pure yeast, concentrated sulfuric acid, methyl alcohol and normal hexane used in the present invention are cheap and have a wide range of sources, effectively reducing the production cost. cost.
另外,为进一步提高生物柴油的产率,可以将制备过程中的萃取反复进行三次,每次取上次萃取结果的上清液进行进一步的萃取,加入试剂正己烷的量可略有减少。In addition, in order to further increase the yield of biodiesel, the extraction during the preparation process can be repeated three times, and the supernatant of the last extraction result is taken each time for further extraction, and the amount of n-hexane added can be slightly reduced.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1962820A (en) * | 2006-11-29 | 2007-05-16 | 任春山 | Process for making bio-diesel oil by using municipal sludge |
| CN101018867A (en) * | 2003-10-02 | 2007-08-15 | 密西西比州立大学 | Production of biodiesel and other valuable chemicals from wastewater treatment plant sludges |
| WO2009132249A3 (en) * | 2008-04-25 | 2009-12-30 | Evolution Energy Production, Inc. | Methods and systems for producing biofuels and bioenergy products from sewage sludge, including recalcitrant sludge |
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|---|---|---|---|---|
| CN101018867A (en) * | 2003-10-02 | 2007-08-15 | 密西西比州立大学 | Production of biodiesel and other valuable chemicals from wastewater treatment plant sludges |
| CN1962820A (en) * | 2006-11-29 | 2007-05-16 | 任春山 | Process for making bio-diesel oil by using municipal sludge |
| WO2009132249A3 (en) * | 2008-04-25 | 2009-12-30 | Evolution Energy Production, Inc. | Methods and systems for producing biofuels and bioenergy products from sewage sludge, including recalcitrant sludge |
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