CN106381262B - 料液循环流化发酵装置 - Google Patents

料液循环流化发酵装置 Download PDF

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CN106381262B
CN106381262B CN201610706642.2A CN201610706642A CN106381262B CN 106381262 B CN106381262 B CN 106381262B CN 201610706642 A CN201610706642 A CN 201610706642A CN 106381262 B CN106381262 B CN 106381262B
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fermentation
fermentation tank
feed liquid
water pump
fermenting
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CN106381262A (zh
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黄如
黄如一
罗涛
梅自力
郭亭
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Biogas Institute of Ministry of Agriculture
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    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
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    • C12M29/18External loop; Means for reintroduction of fermented biomass or liquid percolate
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Abstract

本发明涉及沼气能源领域内的一种料液循环流化发酵装置,由发酵罐1和水泵7组成,发酵罐1上部为储气间2,储气间2下面为发酵间3;发酵罐1顶部设置有导气管11和带密封塞9的进料口8;发酵罐1底部设置有水泵出水口6,水泵出水口6与水泵7连接,水泵7进水口与循环管4连接;循环管进口5设置在发酵间3上部的四周;发酵罐1下侧部设置有检修口10。本发明克服了现有沼气动态发酵装置流场形态的设计缺乏优化,发酵原料形成底部堆积或顶部结壳,导致发酵效率低下的缺陷,提供的料液循环流化发酵装置发酵效率高,消耗动力少,不易堵塞。

Description

料液循环流化发酵装置
技术领域
本发明属于沼气能源领域,具体涉及一种料液循环流化发酵装置。
背景技术
发酵生产沼气是一项实用工程技术,利用厌氧发酵,处理农牧业废弃物、生活污水、生产废水等,同时产生优质清洁的生物质能源——沼气(主要成分为甲烷),兼具环保、能源、节能减排等多方面效益。但传统的沼气工程采用静态发酵工艺,发酵效率低下,产气率和污染物去除率都不高,严重制约产业发展。近年来,动态发酵技术得到一定程度的推广,并逐渐成为沼气工程的主流工艺形式。但现有动态发酵装置对流场形态的设计缺乏优化,发酵料液没有形成完整的循环流化通路,导致料液流化效率低下,物料混合不够均匀,有效发酵容积小。搅拌流场不均衡,容易使发酵原料形成底部堆积或顶部结壳,导致酸化等不良现象,发酵效率低下。一些较差的流场设计还容易造成物料的堵塞,损坏设备。
发明内容
本发明的目的是为了克服现有沼气动态发酵装置流场形态的设计缺乏优化,发酵原料形成底部堆积或顶部结壳,导致发酵效率低下的缺陷,为人们提供一种发酵效率高,消耗动力少,不易堵塞的料液循环流化发酵装置。
本发明的目的是通过下述技术方案来实现的。
本发明的料液循环流化发酵装置,其特征在于所述料液循环流化发酵装置由发酵罐1和水泵7组成,发酵罐1上部为储气间2,储气间2下面为发酵间3;发酵罐1顶部设置有导气管11和带密封塞9的进料口8;发酵罐1底部设置有水泵出水口6,水泵出水口6与水泵7连接,水泵7进水口与循环管4连接;循环管进口5设置在发酵间3上部的四周;发酵罐1下侧部设置有检修口10。
本发明在发酵罐四周设置循环管,通过水泵实现料液循环流化。其工作过程如下:
初始发酵料液从顶部进料口进入发酵罐,料液漫过循环管高度,留下小部分空间作为储气间。然后启动水泵,使发酵料液从循环管进口沿循环管进入水泵,从水泵出水口以设定速度进入发酵间,形成竖直向上的水流。发酵料液再从循环管流出,回到水泵的入口,通过水泵重新进入发酵间,形成一个闭式循环系统。该循环系统在内部形成流化,打破静态发酵,极大地提高了发酵料液的混合均匀性,大幅度提高了产气率并避免了料液结壳、堵塞等问题。
综上所述,本发明克服了现有沼气动态发酵装置流场形态的设计缺乏优化,发酵原料形成底部堆积或顶部结壳,导致发酵效率低下的缺陷,提供的料液循环流化发酵装置发酵效率高,消耗动力少,不易堵塞。
附图说明
图1为本发明的示意图。
图2为本发明的俯视示意图。
图中:1:发酵罐;2:储气间;3:发酵间;4:循环管;5:循环管进口;6:水泵出水口;7:水泵;8:进料口;9:密封塞;10:检修口;11:导气管。
具体实施方式
下面通过实施例进一步详述本发明,但本发明不仅限于所述实施例。
实施例一
本例的料液循环流化发酵装置如图1和图2所示,由发酵罐1和水泵7组成,发酵罐1上部为储气间2,储气间2下面为发酵间3;发酵罐1顶部设置有导气管11和带密封塞9的进料口8;发酵罐1底部设置有水泵出水口6,水泵出水口6与水泵7连接,水泵7进水口与循环管4连接;循环管进口5设置在发酵间3上部的四周;发酵罐1下侧部设置有检修口10。

Claims (1)

1.一种料液循环流化发酵装置,其特征在于所述料液循环流化发酵装置由发酵罐(1)和水泵(7)组成,发酵罐(1)上部为储气间(2),储气间(2)下面为发酵间(3);发酵罐(1)顶部设置有导气管(11)和带密封塞(9)的进料口(8);发酵罐(1)底部设置有水泵出水口(6),水泵出水口(6)与水泵(7)连接,水泵(7)进水口与循环管(4)连接;循环管进口(5)设置在发酵间(3)上部的四周;发酵罐(1)下侧部设置有检修口(10)。
CN201610706642.2A 2016-08-23 2016-08-23 料液循环流化发酵装置 Expired - Fee Related CN106381262B (zh)

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CN113308346A (zh) * 2021-06-29 2021-08-27 四川大学 一种沼气发酵罐及沼气系统

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1516921A1 (de) * 2003-09-19 2005-03-23 GE Jenbacher GmbH & Co. OHG Fermentationsanlage
CN1597917A (zh) * 2004-06-28 2005-03-23 华中科技大学 沼气发酵罐
CN201376917Y (zh) * 2009-03-24 2010-01-06 安阳艾尔旺环境工程有限公司 厌氧反应器立体液流搅拌装置
CN101724551A (zh) * 2009-12-17 2010-06-09 中国南方航空工业(集团)有限公司 全混合厌氧反应循环装置及沼气反应原料的循环方法
CN103374521A (zh) * 2013-02-04 2013-10-30 中国科学院青岛生物能源与过程研究所 一种机械与水力组合搅拌的秸秆厌氧发酵制沼气工程装置
CN203807467U (zh) * 2014-03-26 2014-09-03 北京兴星伟业生态环境工程技术有限公司 一种射流水力搅拌装置
CN206089670U (zh) * 2016-08-23 2017-04-12 农业部沼气科学研究所 料液循环流化发酵装置

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1516921A1 (de) * 2003-09-19 2005-03-23 GE Jenbacher GmbH & Co. OHG Fermentationsanlage
CN1597917A (zh) * 2004-06-28 2005-03-23 华中科技大学 沼气发酵罐
CN201376917Y (zh) * 2009-03-24 2010-01-06 安阳艾尔旺环境工程有限公司 厌氧反应器立体液流搅拌装置
CN101724551A (zh) * 2009-12-17 2010-06-09 中国南方航空工业(集团)有限公司 全混合厌氧反应循环装置及沼气反应原料的循环方法
CN103374521A (zh) * 2013-02-04 2013-10-30 中国科学院青岛生物能源与过程研究所 一种机械与水力组合搅拌的秸秆厌氧发酵制沼气工程装置
CN203807467U (zh) * 2014-03-26 2014-09-03 北京兴星伟业生态环境工程技术有限公司 一种射流水力搅拌装置
CN206089670U (zh) * 2016-08-23 2017-04-12 农业部沼气科学研究所 料液循环流化发酵装置

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