CN101955298A - 畜禽养殖污物厌氧消化液处理方法 - Google Patents
畜禽养殖污物厌氧消化液处理方法 Download PDFInfo
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- CN101955298A CN101955298A CN2010102615981A CN201010261598A CN101955298A CN 101955298 A CN101955298 A CN 101955298A CN 2010102615981 A CN2010102615981 A CN 2010102615981A CN 201010261598 A CN201010261598 A CN 201010261598A CN 101955298 A CN101955298 A CN 101955298A
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- livestock
- anaerobic
- anaerobic digestion
- aerobic
- poultry cultivation
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- 244000144972 livestock Species 0.000 title claims abstract description 27
- 244000144977 poultry Species 0.000 title claims abstract description 27
- 239000007788 liquid Substances 0.000 title claims abstract description 20
- 230000001488 breeding Effects 0.000 title abstract description 7
- 239000003344 environmental pollutant Substances 0.000 title abstract 6
- 231100000719 pollutant Toxicity 0.000 title abstract 6
- 230000029087 digestion Effects 0.000 claims abstract description 35
- 239000012528 membrane Substances 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000004062 sedimentation Methods 0.000 claims abstract description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 5
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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[P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 5
- 239000011574 phosphorus Substances 0.000 claims abstract description 5
- 238000010992 reflux Methods 0.000 claims abstract description 4
- 239000006228 supernatant Substances 0.000 claims abstract description 4
- 238000003672 processing method Methods 0.000 claims description 9
- VSCWAEJMTAWNJL-UHFFFAOYSA-K Aluminium chloride Chemical compound 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- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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Classifications
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
畜禽养殖污物厌氧消化液处理方法属于废水处理技术;畜禽养殖污物厌氧消化制取沼气后残余的厌氧消化液经预沉池静沉后,进入低速离心机分离,离心后上清液进入化学强化一级处理池,投加絮凝剂强化厌氧消化液中磷的去除,厌氧消化液由一级处理池进入缺氧一好氧膜生物反应器,在缺氧一好氧区完成有机物和氮磷的高效同步生物脱除,经好氧区的膜组件分离后,清水回流至畜禽养殖污物厌氧消化系统,从而实现畜禽养殖污物处理过程零排放;好氧区的污泥混合液经回流泵回流至缺氧反应器中进行反硝化;本发明为畜禽养殖污物厌氧消化全过程提供一种污水零排放和节水降耗的思路。
Description
畜禽养殖污物厌氧消化液处理方法
技术领域
[0001] 本发明涉及的是一种废水处理方法,具体地说是畜禽养殖污物厌氧消化液的处理 方法。
背景技术
[0002] 随着国民经济的发展和人民生活水平的提高,我国养殖业得到了迅猛发展,并且 由家庭小型养殖向集约化大中型、规模化养殖场发展,这些规模化的养殖场,为人民生活提 供了丰富的肉、禽、蛋、奶,但其养殖过程所产生的污物也带来了严重的环境污染问题。在这 种严峻的形势下,厌氧消化工艺以其利用畜禽粪便产生能源的特性引起全世界的关注。所 谓厌氧消化是在厌氧环境和适宜的温度、营养等条件下,使厌氧微生物大量繁殖并利用他 们的生命活动,将有机废物中的有机物转化为简单的有机物(如:ch4,co2等)的过程。厌 氧消化生产沼气是将环境保护、能源回收与生态良性循环结合起来的综合系统技术。湿式 厌氧消化以其较高的处理和产气效率得以广泛应用。然而,湿式厌氧消化技术在应用过程 中存在重要的技术瓶颈一厌氧消化液的安全处置,这与现在的节能减排、节水降耗等发 展策略相背离,尤其是厌氧消化液当中所含有的高浓度污染物质,直接排放会造成严重的 环境污染。厌氧消化液的安全处置问题,已经关系到湿式厌氧消化的应用是否符合环保需 求,目前厌氧消化液的消纳和利用问题已经成为制约沼气工程建设的重要因素。
发明内容
[0003] 本发明抓住这一问题,提出了对其处理与回用的新途径,实现对厌氧消化液的安 全处置,并借助于深度处理技术使其满足回用水质要求,从而实现湿式厌氧消化过程的“污 水零排放”这一目标。
[0004] 本发明的目的在于提供畜禽养殖污物厌氧消化液的处理方法及相关应用设计参 数,本发明的目的是这样实现的:
[0005] 1、一种畜禽养殖污物厌氧消化液处理方法,其特征在于:畜禽养殖污物厌氧消化 制取沼气后残余的厌氧消化液经预沉池静沉后,进入低速离心机分离,离心后上清液进入 化学强化一级处理池,投加絮凝剂强化厌氧消化液中磷的去除,厌氧消化液由一级处理池 进入缺氧_好氧膜生物反应器,在缺氧_好氧区完成有机物和氮磷的高效同步生物脱除,经 缺氧_好氧膜生物反应器的好氧区的膜组件分离后,清水回流至畜禽养殖污物厌氧消化系 统,从而实现畜禽养殖污物处理过程零排放,好氧区的污泥混合液经回流泵回流至缺氧反 应器中进行反硝化,清水经循环水泵间歇式回流至畜禽养殖污物厌氧消化系统。
[0006] 2、所述的预沉池调节停留时间为12h〜48h。
[0007] 3、所述的低速离心机转速为800r/min〜1200r/min。
[0008] 4、所述的化学强化一级处理采用的絮凝剂为聚合氯化铝铁、聚合氯化铝。
[0009] 5、所述的缺氧-好氧膜生物反应器为分体式膜生物反应器。
[0010] 6、所述的好氧区膜组件为中空纤维膜或平板膜。[0011] 7、所述在缺氧_好氧膜生物反应器的好氧池底部配置曝气系统。
[0012] 本发明的有益效果是:可承担和完成畜禽养殖污物厌氧消化液的深度处理,使之 能够回用于系统中,实现污物处理过程中的零排放,环保效果好,且节能减排,节水降耗。另 外,本方法还可推广应用于高浓度废水的深度处理与回用中,实现达标排放,适用范围广。
具体实施方式:
[0013] 下面举实例对本发明进行详细描述。
[0014] 将新鲜牛粪在湿式状态下经两相厌氧消化后,残留的厌氧消化液水质条件测定如 下:C0D平均为3900mg/L ;氨氮平均为490mg/L ;磷酸盐平均为50mg/L。为高有机污染、高 氨氮和高磷负荷的高浓度有机废水。
[0015] 将厌氧消化液导流至预沉池,经24h预沉后,采用虹吸方法提取上清液至化学强 化一级处理池,向化学强化一级处理池中投加絮凝剂聚合氯化铝铁15. Omg/L,然后在40r/ min条件下进行搅拌lOmin,静置30后,上消液虹吸入缺氧池,缺氧池放置搅拌器用于搅拌 混合污泥,缺氧池停留15h后,进入好氧池,好氧池放置聚偏氟乙烯材质的膜组件,膜丝孔 径为0. 2 μ m,膜面积为0. 3m2,采用的膜通量为7Lm2/h ;好氧池停留时间为28h。为了控制 膜污染,膜出水端抽吸泵采用运行8min,停2min的运行方式。好氧池内溶解氧浓度维持在 3. O〜4. Omg/L范围内,缺氧池内溶解氧浓度维持在小于0. 2mg/L范围内。好氧区的污泥混 合液经回流泵回流至缺氧反应器中进行反硝化。跨膜压差达到400kPa时,采用0. 5% NaOH 溶液浸泡30h后,使得受污染的膜组件恢复其通量。
[0016] 经3周的稳定运行,处理效果如下:
[0017] 氨氮平均去除率达到98. 1%,COD平均去除率达到96. 3%,磷酸盐平均去除率达 到76. 6%。处理后的水回流至两相厌氧消化装置的产气无不利影响,实现牛粪两相厌氧消 化过程的污水零排放。
4
Claims (7)
- 一种畜禽养殖污物厌氧消化液处理方法,其特征在于:畜禽养殖污物厌氧消化制取沼气后残余的厌氧消化液经预沉池静沉后,进入低速离心机分离,离心后上清液进入化学强化一级处理池,投加絮凝剂强化厌氧消化液中磷的去除,厌氧消化液由一级处理池进入缺氧‑好氧膜生物反应器,在缺氧‑好氧区完成有机物和氮磷的高效同步生物脱除,经缺氧‑好氧膜生物反应器的好氧区的膜组件分离后,清水回流至畜禽养殖污物厌氧消化系统,从而实现畜禽养殖污物处理过程零排放,好氧区的污泥混合液经回流泵回流至缺氧反应器中进行反硝化,清水经循环水泵间歇式回流至畜禽养殖污物厌氧消化系统。
- 2.根据权利要求1所述畜禽养殖污物厌氧消化液处理方法,其特征在于所述的预沉池 调节停留时间为12h〜48h。
- 3.根据权利要求1所述畜禽养殖污物厌氧消化液处理方法,其特征在于所述的低速离 心机转速为800r/min〜1200r/min。
- 4.根据权利要求1所述畜禽养殖污物厌氧消化液处理方法,其特征在于所述的化学强 化一级处理采用的絮凝剂为聚合氯化铝铁、聚合氯化铝。
- 5.根据权利要求1所述畜禽养殖污物厌氧消化液处理方法,其特征在于所述的缺 氧_好氧膜生物反应器为分体式膜生物反应器。
- 6.根据权利要求1所述畜禽养殖污物厌氧消化液处理方法,其特征在于所述的好氧区 膜组件为中空纤维膜或平板膜。
- 7.根据权利要求1所述畜禽养殖污物厌氧消化液处理方法,其特征在于所述在缺 氧_好氧膜生物反应器的好氧池底部配置曝气系统。
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