首页> 外国专利> Fermentation of pourable, cuttable, stackable/fluid biomass e.g. grass cuttings for biogas production, comprises pretreating and then fermenting the biomass in reusable, gas-tight fermenter up to complete or to large extent mineralization

Fermentation of pourable, cuttable, stackable/fluid biomass e.g. grass cuttings for biogas production, comprises pretreating and then fermenting the biomass in reusable, gas-tight fermenter up to complete or to large extent mineralization

机译:可倾倒,可切割,可堆叠/流体生物质的发酵,例如用于产生沼气的草屑,包括预处理然后在可重复使用的气密性发酵罐中发酵生物质,以完全或很大程度上矿化

摘要

The method for the fermentation of pourable, cuttable, stackable or fluid biomass e.g. grass cuttings for biogas production, comprises pretreating and then fermenting the biomass in a reusable, gas-tight fermenter (1) up to a complete or to a large extent mineralization, and removing the biomass from the fermenter to refill new biomass. The pretreatment and inoculation of the biomass are optionally carried out. The pretreatment includes addition of water, sanitization, homogenization, grinding or dehydration. The biomass is inoculated before, during or after filling with inoculation material. The method for the fermentation of pourable, cuttable, stackable or fluid biomass e.g. grass cuttings for biogas production, comprises pretreating and then fermenting the biomass in a reusable, gas-tight fermenter (1) up to a complete or to a large extent mineralization, and removing the fermented biomass from the fermenter to refill new biomass. The pretreatment and inoculation of the biomass are optionally carried out. The pretreatment includes addition of water, sanitization, homogenization, grinding or dehydration. The biomass is inoculated before, during or after filling with fluid or non-fluid inoculation material. The inoculation materials are: thermophile and mesophile; thermophile and psychrophile; psychrophile and mesophile; or thermophile, mesophile and psychrophile. The inoculation of the biomass takes place with two different inoculation materials in such a manner that the inoculation materials are introduced after filling the fermenter, at which the conditions suitable for the microorganisms are controlled. The biomass is displaced with additives before, during or after bringing into the fermenter. The additives affect the fermentation of the biomass with nutrients and/or ferments for the microorganisms involved in the fermentation, buffer substrate for the pH value adjustment or water for adjustment a desired solid content. The inoculation of the individual loads partially takes place after filling of fermenting substrate or percolate by container-internal circulation. The fermenter is filled in charge-wise manner and further loads are added before the loads are fermented completely, or is continuously filled, where the continuous filling takes place as the biomass present in the fermenter is reduced, so that the filling takes place without discharge of biomass from the fermenter. The resulting biomasses are sorted in such a way that only biomasses suitable for a common fermentation arrive into a common fermenter or are mixed so that easily fermentable material arrives together with hard fermentable materials into the fermenter. The biomasses of same kind or same origin are fermented in the common fermenter. The pre-formed product e.g. biogas is sucked off before charge-wise filling of the fermenter. Infiltrated air is removed from the fermenter after the charge-wise filling with biomass in order to provide anaerobic conditions, where the removal of air takes place via draining or displacement through other gases and/or gas mixtures. After charge-wise filling with biomass, an aerobic pre-fermentation phase (acid formation phase) is produced, in that air infiltrated during filling in the fermenter is discharged, or additional air or oxygen is added. The aerobic pre-fermentation phase is extended by repeating three to five times sucking off and renewed ventilating. After the aerobic pre-fermentation phase, gas mixture consisting of oxygen-less and/or oxygen-free and variable product e.g. biogas is removed, before the product formation is strengthened and/or before the collection of product is begun. The biomass is mechanically compressed before beginning the fermentation. The water is added to the biomass in order to prevent spontaneous heating and -ignition or to reach a desired dry substance portion. The fermenter is provided with a drainage device to collect the resulting percolate. The biomass is separated into liquid phases and solid phase during the fermentation. The collected liquid is removed from the fermenter, while the solid portions remain in the fermenter. The separation of the substrates into the fluid- and the solid phase is reached and the substrate present in the plant acts as filter mass, by which the liquid portions are passed through and removed, while the solid portions remain in the fermenter. A small negative pressure or same absolute pressure as outside of the fermenter is constantly maintained by suitable devices. The process is carried out manually or automatically with computer or microprocessor under analysis of suitable sensor signals. An independent claim is included for a device for the fermentation of pourable, cuttable, stackable or fluid biomass.
机译:发酵可倾倒,可切割,可堆叠或液体生物质的方法,例如用于沼气生产的草屑包括:在可重复使用的气密性发酵罐(1)中对生物质进行预处理,然后进行发酵,直至完全或很大程度上矿化;然后从发酵罐中去除生物质以补充新的生物质。任选地进行生物质的预处理和接种。预处理包括加水,消毒,均质,研磨或脱水。在填充接种材料之前,之中或之后接种生物质。发酵可倾倒,可切割,可堆叠或液体生物质的方法,例如用于生产沼气的草屑包括:在可重复使用的气密性发酵罐(1)中对生物质进行预处理,然后进行发酵,直至完全或很大程度上矿化;然后从发酵罐中去除发酵后的生物质,以补充新的生物质。任选地进行生物质的预处理和接种。预处理包括加水,消毒,均质,研磨或脱水。在填充流体或非流体接种材料之前,之中或之后接种生物质。接种材料为:嗜热菌和嗜温菌;嗜热者和嗜冷者;嗜温和嗜温;或嗜热,嗜温和嗜温的人。用两种不同的接种材料进行生物质的接种,使得在填充发酵罐后将接种材料引入,在该处控制适合于微生物的条件。在进入发酵罐之前,之中或之后,用添加剂置换生物质。添加剂影响营养物质和/或发酵中涉及的微生物的发酵,用于调节pH值的缓冲底物或用于调节所需固体含量的水,从而影响生物质的发酵。在通过容器内部循环填充发酵底物或渗透物之后,部分地进行各个负载的接种。发酵罐以装料方式进行填充,并在完全发酵或连续填充之前添加​​其他负载,其中由于发酵罐中存在的生物量减少而进行连续填充,因此填充无需排放即可进行来自发酵罐的生物质。以这样的方式对所得生物质进行分选:仅适合于普通发酵的生物质进入普通发酵罐或进行混合,以使易于发酵的材料与硬质发酵材料一起进入发酵罐。在普通发酵罐中发酵相同种类或相同来源的生物质。预制产品例如在发酵罐按装料方式进行灌装之前,应先清除沼气。在用生物质按电荷填充之后,从发酵罐中除去渗入的空气,以提供厌氧条件,其中空气的去除是通过排放或通过其他气体和/或气体混合物置换来进行的。在用生物质按电荷填充之后,产生有氧的预发酵阶段(形成酸的阶段),其中排出在填充到发酵罐中的过程中渗透的空气,或者添加额外的空气或氧气。通过重复吸吮并重新通风三到五次,可以延长有氧发酵的阶段。在好氧的预发酵阶段之后,混合气体由无氧和/或无氧的可变产物组成,例如:在加强产品形成之前和/或开始收集产品之前,应去除沼气。在开始发酵之前,将生物质机械压缩。将水添加到生物质中以防止自发加热和点火或达到所需的干燥物质部分。发酵罐设有排水装置以收集所得的渗滤液。在发酵过程中,生物质被分为液相和固相。从发酵罐中除去收集的液体,而固体部分保留在发酵罐中。达到了将底物分离成液相和固相的作用,并且植物中存在的底物起着过滤器的作用,液体部分通过并被除去,而固体部分则保留在发酵罐中。通过合适的装置可以始终保持一个很小的负压或与发酵罐外部相同的绝对压力。该过程通过计算机或微处理器在适当的传感器信号分析下手动或自动执行。包括用于可倾倒,可切割,可堆叠或流体生物质发酵的设备的独立权利要求。

著录项

  • 公开/公告号DE102007036049A1

    专利类型

  • 公开/公告日2009-02-05

    原文格式PDF

  • 申请/专利权人 FUS ANDREAS;

    申请/专利号DE20071036049

  • 发明设计人 FUS ANDREAS;

    申请日2007-08-01

  • 分类号C12M1/107;C12M1/24;C12P5/02;

  • 国家 DE

  • 入库时间 2022-08-21 19:09:40

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