CN201241154Y - White-rot fungi solid fermentation system - Google Patents

White-rot fungi solid fermentation system Download PDF

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CN201241154Y
CN201241154Y CNU2008200986078U CN200820098607U CN201241154Y CN 201241154 Y CN201241154 Y CN 201241154Y CN U2008200986078 U CNU2008200986078 U CN U2008200986078U CN 200820098607 U CN200820098607 U CN 200820098607U CN 201241154 Y CN201241154 Y CN 201241154Y
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fermentation
fermentation reactor
reactor
white rot
temperature
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段传人
朱丽平
姚月良
向凌海
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Chongqing University
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Abstract

本实用新型提出一种白腐菌固体发酵系统,包括控制系统、发酵反应器、供热系统、加湿器及氧气泵等;发酵反应器中央均匀环绕布置有循环水保温管,循环水保温管与发酵反应器外部单独设置的供热系统连接,形成供热回路;加湿器和氧气泵分别通过通蒸汽管道和通氧气管道连接发酵反应器,通蒸汽管道亦在发酵反应器中央均匀环绕布置;发酵反应器内底部设置有滤水装置,内设置有温度探头;控制系统具有显示和设定温度、湿度的控制面板。本系统结构简单,便于操作,可自动控制白腐菌发酵的温度,湿度,通气量,可以实现发酵过程的自动控制,利于白腐真菌高产木质素降解酶,提高发酵均匀性,缩短发酵周期,提高生产率。

Figure 200820098607

The utility model proposes a white rot fungus solid fermentation system, which includes a control system, a fermentation reactor, a heating system, a humidifier and an oxygen pump, etc.; the center of the fermentation reactor is uniformly surrounded by circulating water insulation pipes, and the circulation water insulation pipes and The heating system separately set outside the fermentation reactor is connected to form a heating circuit; the humidifier and the oxygen pump are respectively connected to the fermentation reactor through the steam pipe and the oxygen pipe, and the steam pipe is also uniformly arranged around the center of the fermentation reactor; A water filtering device is installed at the bottom of the reactor, and a temperature probe is installed inside; the control system has a control panel for displaying and setting temperature and humidity. The system is simple in structure and easy to operate. It can automatically control the temperature, humidity, and ventilation of white rot fungi fermentation, and can realize automatic control of the fermentation process, which is beneficial to the high production of lignin degrading enzymes by white rot fungi, improves the uniformity of fermentation, and shortens the fermentation cycle. Improve productivity.

Figure 200820098607

Description

白腐菌固体发酵系统 White rot solid fermentation system

技术领域 technical field

本实用新型涉及一种发酵装置,具体涉及一种用于白腐菌固体发酵的自动化反应装置,本装置可用于环境保护、生物制浆、食品酿造等领域。The utility model relates to a fermentation device, in particular to an automatic reaction device for white rot fungus solid fermentation. The device can be used in the fields of environmental protection, biological pulping, food brewing and the like.

背景技术 Background technique

白腐菌的独特和有效的降解能力,使其成为环境保护领域的一支强劲的生力军,将这类对异生物质具有光谱进攻性丝状真菌的活性潜能,转化为对环境中不同状态介质内的污染物的现实控制,是各国科学家和相关工业界共同的追求目标和不懈的努力方向。尽管相比于成熟的细菌体系而言,白腐真菌在环境保护中的应用,还处于探索和建立阶段;尽管由于这类菌生理代谢的特殊性和对环境因子近乎苛刻的要求,成为实现工业化的严重障碍;但是这一切,并没有阻挡人们在环境保护实践中利用白腐真菌固体发酵的种种研究、开发和尝试。The unique and effective degradation ability of white rot fungi makes it a powerful new force in the field of environmental protection. It transforms the active potential of this kind of filamentous fungi with spectrum attack on xenobiotics into media of different states in the environment. Realistic control of pollutants in the environment is the common pursuit goal and unremitting direction of efforts of scientists and related industries in various countries. Although compared with the mature bacterial system, the application of white rot fungi in environmental protection is still in the stage of exploration and establishment; although due to the particularity of the physiological metabolism of this type of bacteria and the almost harsh requirements for environmental factors, it has become a However, all of this has not stopped people from using various researches, developments and attempts of solid fermentation of white rot fungi in environmental protection practices.

将白腐菌固体发酵应用于污染处理的最初和最多的实践,是在生物制浆和水污染控制领域,生物制浆是利用微生物所具有的分解木素的能力来除去制浆原料中的木素,使植物组织与纤维彼此分离制成纸浆的过程。一般是在对植物纤维原料进行化学处理或机械磨浆前对其进行生物预处理,目前生物制浆已经进入了工厂化阶段,并取得了良好的效果。The initial and largest practice of applying white rot fungus solid fermentation to pollution treatment is in the field of biopulping and water pollution control. Biopulping uses the ability of microorganisms to decompose lignin to remove wood from pulping raw materials. Pulping is the process of separating plant tissue and fibers from each other to make pulp. Generally, biological pretreatment is carried out on plant fiber raw materials before chemical treatment or mechanical refining. At present, biological pulping has entered the stage of industrialization and achieved good results.

生物制浆技术是一种高效清洁的制浆工艺。利用白腐菌固体发酵对木素的降解作用脱除木素,可以减轻造纸工业的环境污染问题。白腐菌是自然界降解木素最有效的一类微生物,它能产生降解木素或变性木素的活性酶系,木素过氧化物酶(LiP)、锰过氧化物酶(MnP)和酚氧化酶(漆酶,Laccase)系统构成了白腐菌降解木素的主要活性酶系。白腐菌的这一特性已经利用在生物制浆、生物漂白等研究领域,有些已经进入中试阶段,显示了其良好的应用前景。Biopulping technology is an efficient and clean pulping process. Using white rot fungus solid fermentation to degrade lignin to remove lignin can alleviate the environmental pollution problem of paper industry. White rot fungi are the most effective type of microorganisms that degrade lignin in nature. They can produce active enzymes that degrade lignin or denatured lignin, lignin peroxidase (LiP), manganese peroxidase (MnP) and phenol The oxidase (laccase, Laccase) system constitutes the main active enzyme system for the degradation of lignin by white rot fungi. This characteristic of white rot fungi has been used in research fields such as biopulping and biobleaching, and some have entered the pilot test stage, showing its good application prospects.

在文献<<丝状真菌发酵生产中形态的影响与发酵罐设计>>(生物技术-2003年1期)一文中提到专门针对丝状真菌的发酵罐的设计,由于促使菌球形成并不能克服真菌发酵液粘稠带来的所有问题,而且对有些真菌其菌球形成不利于发酵产物的生产,一个简单的方法就是把发酵液稀释,但稀释发酵液只能暂时缓解发酵液粘稠问题,设计特殊的发酵系统才能从根本上解决发酵过程中发酵液粘稠所带来的困难及其它一系列问题。In the literature <<The influence of morphology in the fermentation production of filamentous fungi and the design of fermenter>> (Biotechnology-2003 Issue 1), it is mentioned that the design of the fermenter specially for filamentous fungi cannot be achieved by promoting the formation of bacterial balls. To overcome all the problems caused by the viscous fermentation liquid of fungi, and for some fungi, the formation of bacteria balls is not conducive to the production of fermentation products. A simple method is to dilute the fermented liquid, but diluting the fermented liquid can only temporarily relieve the viscous problem of the fermented liquid Only by designing a special fermentation system can we fundamentally solve the difficulties caused by the viscosity of the fermentation broth during the fermentation process and a series of other problems.

目前,大多数机械搅拌的发酵罐都是安装径向流的涡轮式搅拌桨,但近来的研究表明轴向流的搅拌桨在真菌发酵的许多方面具有优势。在以水和CMC为介质的冷模实验表明,轴向流搅拌桨较之径向流桨,在介质的混合性能、传质效果和功率消耗等方面均有明显改善,在对微生物发酵实验中发现轴向流搅拌桨能更好地适用于高密度和高粘度的微生物发酵搅拌,高密度培养最终可使菌体浓度提高12%,产物含量提高10%,高粘度发酵可使生产强度提高20%。而有的研究表明在装配涡轮桨、轴向流桨的发酵罐中,只要给定的容量传质系数一致,真菌的代谢产物生产没有明显差别。轴向流的翼型桨具有剪切性能温和、输送效率高、混合迅速、低能耗及传质系数高等优点,已成功地应用于生产赤霉素、井冈霉素等工业发酵罐。另一种设计是在发酵罐中安装两种不同的搅拌桨,在两根分离的驱动杆上安装了两个不同的搅拌桨,并可以不同的速度旋转,每个桨起不同的作用,在发酵罐底部可安装一个高速的涡轮桨,主要用于打碎气泡和氧的大量传输,在上面则安装一个慢速的轴向流搅拌桨,它使发酵液流向底部的涡轮桨。两种桨的配合使用可以改善发酵液的混合。对产黄青霉素发酵的研究表明,采用轴向流桨和涡轮桨组合替代传统沿用的多层涡轮桨,可以强化混合和供氧,并可通过调整桨径和搅拌转速来保证适宜的剪切环境(青霉素发酵需要较强的剪切环境)。研究丝状真菌发酵的替代混合体系一方面是为了改进大体积液体的混合,另一方面是涡轮桨的高剪切力(特别是高速旋转时)会使微生物菌丝断裂,影响菌体形态、生长和代谢活力,不利于有些发酵产物的生产。如搅拌速率提高后,由于剪切力导致菌丝体的变形和损害,导致土曲霉(ATerreus)衣康酸产量的急剧下降。必须指出,搅拌率的提高将导致氧传输率的上升及溶解氧的增加,而溶解氧有时也会使真菌的代谢产物生产降低,如以出芽短梗霉(Apullulans)生产细胞外多糖,就是溶解氧而不是剪切力使其产量下降;另外,在发酵的不同时期,菌体对剪切力的敏感程度不同,液泡化将使菌丝容易破碎。对于高搅拌速度所产生的剪切力除对菌丝的物理损伤外,对其亦会产生生理抑制,但这方面的研究并不多。Roukas研究了黑曲霉Aniger在不同搅拌速率下发酵生产柠檬酸的情况,检测了TCA循环中的几种关键酶,结果是顺乌头酸酶和异柠檬酸脱氢酶活性随搅拌速率的增加而上升,而柠檬酸合成酶的活性下降,而这正是柠檬酸积累所不希望的。径向流涡轮桨的高剪切力会导致一些丝状真菌发酵产物的形成受抑制,但轴向流翼型桨的剪切力也未必比涡轮桨低,有研究报导在同样的叶轮直径罐直径比情况下,轴向流搅拌桨(被认为是低剪切力系统)比涡轮桨所引起的菌丝破坏更大,但轴向流桨能使大体积发酵液得到更好地混合,从而改善营养物质的分配和溶解氧的供给。Li等在生产规模上对Aoryzae的流加发酵研究表明,叶轮功率的增加对生物量、菌体形态及裂殖的影响不大。At present, most mechanically stirred fermenters are equipped with radial flow turbine impellers, but recent studies have shown that axial flow impellers have advantages in many aspects of fungal fermentation. The cold model experiment with water and CMC as the medium shows that the mixing performance of the medium, the mass transfer effect and the power consumption of the axial flow impeller are significantly improved compared with the radial flow impeller. In the microbial fermentation experiment It is found that the axial flow stirring paddle is more suitable for high-density and high-viscosity microbial fermentation and stirring. High-density cultivation can finally increase the bacterial concentration by 12%, and the product content by 10%. High-viscosity fermentation can increase the production intensity by 20%. %. However, some studies have shown that in fermenters equipped with turbo paddles and axial flow paddles, as long as the given volume and mass transfer coefficients are consistent, there is no significant difference in the production of fungal metabolites. The airfoil paddle with axial flow has the advantages of mild shear performance, high conveying efficiency, rapid mixing, low energy consumption and high mass transfer coefficient, and has been successfully used in the production of industrial fermentation tanks such as gibberellin and Jinggangmycin. Another design is to install two different stirring paddles in the fermenter. Two different stirring paddles are installed on two separate drive rods and can rotate at different speeds. Each paddle plays a different role. A high-speed impeller can be installed at the bottom of the fermenter, which is mainly used to break up air bubbles and transmit a large amount of oxygen, and a slow axial flow stirring impeller can be installed on it to make the fermentation liquid flow to the impeller at the bottom. The combined use of the two paddles can improve the mixing of the fermentation broth. The research on the fermentation of chryseopenicillin production shows that the combination of axial flow impeller and turbine impeller instead of the traditional multi-layer impeller can strengthen the mixing and oxygen supply, and can ensure a suitable shear environment by adjusting the diameter of the impeller and the stirring speed (Penicillin fermentation requires a strong shearing environment). The study of alternative mixing systems for filamentous fungal fermentation is on the one hand to improve the mixing of large volumes of liquids, and on the other hand, the high shear force of the turbine blade (especially when rotating at high speed) will break the microbial hyphae, affecting the shape of the bacteria, Growth and metabolic activity are detrimental to the production of some fermentation products. If the stirring rate is increased, the deformation and damage of the mycelia due to the shear force will lead to a sharp decline in the itaconic acid production of Aspergillus terreus (ATerreus). It must be pointed out that the increase of stirring rate will lead to the increase of oxygen transmission rate and the increase of dissolved oxygen, and dissolved oxygen will sometimes reduce the production of metabolites of fungi, such as the production of extracellular polysaccharides by Apullulans, which is to dissolve Oxygen rather than shear force makes the yield decrease; in addition, in different periods of fermentation, the sensitivity of the bacteria to shear force is different, and the vacuolization will make the mycelia easy to break. In addition to the physical damage to the hyphae, the shear force generated by high stirring speed will also cause physiological inhibition to it, but there are not many studies in this area. Roukas studied the fermentative production of citric acid by Aspergillus niger Aniger at different stirring speeds, and detected several key enzymes in the TCA cycle. The results showed that the activities of aconitase and isocitrate dehydrogenase increased with the increase of stirring speed. increased, while the activity of citrate synthase decreased, which is undesirable for citrate accumulation. The high shear force of the radial flow turbine impeller can lead to the inhibition of the formation of some filamentous fungal fermentation products, but the shear force of the axial flow airfoil impeller may not be lower than that of the turbine impeller. Studies have reported that the same impeller diameter tank diameter Under normal circumstances, the axial flow impeller (considered as a low shear force system) caused more mycelium damage than the turbine impeller, but the axial flow impeller can make the large volume of fermentation liquid be better mixed, thereby improving Distribution of nutrients and supply of dissolved oxygen. The fed-batch fermentation research of Aoryzae on a production scale by Li et al. showed that the increase of impeller power had little effect on biomass, cell morphology and fission.

目前,也有多种发酵装置的相关专利文献报道,如公开号为CN1958779的中国专利文献公开了“一种固态发酵装置”,它是一种适用于多种微生物规模化发酵的固态发酵装置。它包括主体框架,主体框架内设的1至多个发酵单元;其中的发酵单元由通气板及通气板间设置物料发酵袋构成,该装置结构简单、容易制作,在该装置的发酵单元内发酵能够有效地克服大容量固态发酵反应器中物料温度分布不均一、易感染杂菌、传质传热性差等缺陷。但是,该装置只能解决对水分要求不高的微生物固体发酵,而且没有灭菌设备,所以从装置的应用来看还缺乏一些必要的附件设备。At present, there are also relevant patent literature reports on various fermentation devices. For example, the Chinese patent literature with publication number CN1958779 discloses "a solid-state fermentation device", which is a solid-state fermentation device suitable for large-scale fermentation of various microorganisms. It includes a main frame, and one or more fermentation units are set in the main frame; the fermentation unit is composed of a ventilation plate and a material fermentation bag arranged between the ventilation plates. The device has a simple structure and is easy to manufacture. It effectively overcomes the defects of uneven material temperature distribution, easy infection of bacteria, and poor mass and heat transfer in large-capacity solid-state fermentation reactors. However, this device can only solve microbial solid fermentation that does not require high water content, and there is no sterilization equipment, so it still lacks some necessary accessory equipment from the perspective of the application of the device.

公开号为CN1786159的中国专利文献还公开了“一种真菌发酵产漆酶的深层固体发酵方法及其装置“,它是将真菌在合成液体培养基中发酵预培养获得菌种种液,与已用蒸汽灭菌的草类生物质原料混合均匀,并放入发酵罐内发酵,发酵过程中,进行间歇式的排气-通氧循环换气操作,发酵后,取出物料,挤出酶液。其装置包括发酵罐、真空泵、氧气瓶、蒸汽发生器、控制系统,发酵罐是恒温罐,其上部与真空泵连接,下部与氧气瓶、蒸汽发生器分别连接,控制系统与发酵罐、真空泵、氧气瓶分别连接。该技术采用间歇式的排气-通氧循环换气操作,提高了气体交换效率和微生物产酶的能力,解决了菌种污染的问题,设备简单,可自动控制操作,提高了发酵器单位容积的发酵原料装载量,实现真菌发酵产漆酶的高产高效。但是该技术是针对于应用到真菌发酵产漆酶的深层固体发酵,对于白腐菌固体发酵高效降解木质素的工艺条件研究方面考虑的不够全面,在白腐菌接种方式上存在一些缺陷,接种应选择在发酵罐内接,减少污染,并且发酵罐本身的灭菌问题也没有解决.The Chinese patent document with the publication number CN1786159 also discloses "a deep-layer solid fermentation method and device for producing laccase by fungal fermentation". The grass biomass raw materials sterilized by steam are mixed evenly, and put into the fermentation tank for fermentation. During the fermentation process, intermittent exhaust-oxygen cycle ventilation operation is performed. After fermentation, the materials are taken out and the enzyme liquid is squeezed out. Its device includes fermenter, vacuum pump, oxygen bottle, steam generator, control system, fermenter is a constant temperature tank, its upper part is connected with vacuum pump, its lower part is respectively connected with oxygen bottle and steam generator, and the control system is connected with fermenter, vacuum pump, oxygen Bottles are connected separately. This technology adopts intermittent exhaust-oxygen cycle ventilation operation, which improves the gas exchange efficiency and the ability of microorganisms to produce enzymes, and solves the problem of bacterial contamination. The equipment is simple and can be automatically controlled to increase the unit volume of the fermenter. The loading capacity of fermentation raw materials can achieve high yield and high efficiency of fungal fermentation to produce laccase. However, this technology is aimed at the submerged solid fermentation applied to the production of laccase by fungal fermentation. The research on the process conditions for the efficient degradation of lignin by solid fermentation of white rot fungi is not considered comprehensive enough. There are some defects in the inoculation method of white rot fungi. It should be selected to connect in the fermenter to reduce pollution, and the sterilization problem of the fermenter itself has not been solved.

另外,公开号为CN2784419的中国专利文献公开了一种“固体发酵罐”,其包括罐体,所述罐体设置有接种口、进料口、排气口、取样口、测温口、进气口、出料口,所述罐体的外周分布有外夹套,所述外夹套设置有进口和出口,所述罐体套装于转动轴,在罐腔内所述转动轴套装有螺旋片,所述转动轴通过连轴器连接减速器,所述减速器通过轮带连接电机,其特征在于:所述叶片、转动轴分别设置为中空,所述转动轴通过设置在转动轴轴腔一端的密封件连接万向管道,所述密封件将轴腔隔为左腔和右腔,万向管道的输入端穿过密封件后伸入左腔,万向管道的输出端开口与右腔连通,左腔分别与螺旋叶片的螺旋入口连接相通,螺旋叶片的螺旋出口分别与右腔连接相通。该发酵罐对其内部的物料灭菌时,罐体内的物料不会粘在一块,而且罐体内的温度、湿度容易控制,物料的发酵周期较短。固体发酵罐。但是该装置的应用范围没有描述清楚,比如在低温的微生物固体发酵时,如何来自动控制温度,通氧气时没有考虑对氧气的除菌所带来的污染,另外还缺乏观察窗口,这样不利于观察微生物生长的及时情况。In addition, the Chinese patent literature with the publication number CN2784419 discloses a "solid fermentation tank", which includes a tank body, and the tank body is provided with an inoculation port, a feed port, an exhaust port, a sampling port, a temperature measurement port, an inlet Gas port, discharge port, the outer circumference of the tank body is distributed with an outer jacket, the outer jacket is provided with an inlet and an outlet, the tank body is sleeved on the rotating shaft, and the rotating shaft is sleeved with a screw in the tank cavity. The rotating shaft is connected to the reducer through a coupling, and the reducer is connected to the motor through a belt. The seal at one end is connected to the universal pipe, and the seal divides the shaft chamber into a left chamber and a right chamber. The input end of the universal pipe passes through the seal and then extends into the left chamber, and the output end of the universal pipe is connected to the right chamber. The left cavity is respectively connected with the spiral inlet of the spiral blade, and the spiral outlet of the spiral blade is respectively connected with the right cavity. When the fermenter sterilizes the materials in the tank, the materials in the tank will not stick together, and the temperature and humidity in the tank are easy to control, and the fermentation period of the materials is short. Solid fermenter. However, the scope of application of the device is not clearly described, such as how to automatically control the temperature during low-temperature microbial solid fermentation, the pollution caused by the sterilization of oxygen is not considered when passing oxygen, and there is also a lack of observation window, which is not conducive to Observe the timely situation of microbial growth.

白腐菌在制浆造纸方面虽然有很多的应用研究,也显示了非常好的效果,但在实际应用方面,仍然存在很多问题。首先,由于白腐菌在木片或纸浆表面生长繁殖以及酶分泌受到基质pH值、氧化还原电位、菌体的营养需求以及温度和湿度等影响,使得白腐菌产生的木素降解酶酶活力较低;其次,白腐菌产生木素降解酶的培养过程是一个氧耗速率极高的培养过程,而目前的发酵工业是采用深层通风培养来实现,需要较高的搅拌转速,对白腐菌产酶非常不利,导致白腐菌扩大培养困难,不能满足实际生物制浆过程的需要;最后,白腐菌在降解木素的同时也伴随有纤维素的降解,这将影响纸张的强度性能。总之,白腐菌生物制浆过程的最大困难是难以迅速、大量地发酵产生木素降解酶,现有的发酵装置均不能有效地解决此问题,这是白腐菌生物制浆技术工业化应用所面临的主要问题。Although there are many applied researches on white rot fungi in pulping and papermaking, and they have shown very good results, there are still many problems in practical application. First of all, because the growth and reproduction of white rot fungi on the surface of wood chips or pulp and the enzyme secretion are affected by the pH value of the substrate, redox potential, nutritional requirements of the bacteria, temperature and humidity, etc., the activity of the lignin-degrading enzymes produced by white rot fungi is relatively low. Secondly, the cultivation process of white rot fungi to produce lignin-degrading enzymes is a culture process with a very high oxygen consumption rate, while the current fermentation industry is realized by deep ventilation culture, which requires a high stirring speed, which is harmful to the production of white rot fungi. The enzyme is very unfavorable, which makes it difficult to expand the cultivation of white rot fungi, which cannot meet the needs of the actual biopulping process; finally, the degradation of lignin by white rot fungi is accompanied by the degradation of cellulose, which will affect the strength properties of paper. In short, the biggest difficulty in the biopulping process of white rot fungi is that it is difficult to quickly and massively ferment lignin-degrading enzymes. None of the existing fermentation devices can effectively solve this problem. The main problem faced.

实用新型内容Utility model content

本实用新型的目的在于针对上述技术的不足,提出一种白腐真菌固体发酵系统,其可以高效降解木质素,并且结构更加简单、实用、容量大。The purpose of this utility model is to address the shortcomings of the above technologies, and propose a solid fermentation system for white rot fungi, which can efficiently degrade lignin, and has a simpler structure, more practicality, and a larger capacity.

本实用新型的技术方案如下:The technical scheme of the utility model is as follows:

一种白腐菌固体发酵系统,包括控制系统和发酵反应器,还包括有连接发酵反应器的供热系统、加湿器和氧气泵等。所述发酵反应器中央均匀环绕布置有循环水保温管,保温管与发酵反应器外部单独设置的供热系统连接,形成供热回路,以使在反应器内能均匀地保持需要的温度。所述加湿器和氧气泵分别通过通蒸汽管和通氧气管连接发酵反应器,以使反应器内保持需要的湿度和氧气,通蒸汽管亦在发酵反应器中央均匀环绕布置,以使湿度均匀。所述发酵反应器内底部设置有滤水装置,以使发酵完后清洗方便,污水可以直接流出。所述发酵反应器上有取样口和出气口,在试验中需要及时取样,取样口直径10cm,可以自动打开和关闭,从这里取样可以保证发酵材料不染菌,而出气口是专门为白腐菌这种需氧型真菌设计的,这样更利于氧气的畅通,保证白腐菌更好的生长,并在发酵反应器内设置有温度探头,以随时反映出反应器内的温度,以便控制。所述供热系统、加湿器、氧气泵、温度探头均通过控制线或信号线与控制系统连接,控制系统具有显示和设定温度、湿度的控制面板,可以对发酵的温度、湿度、供氧等各种工艺条件进行设定和控制。A white-rot fungus solid fermentation system includes a control system, a fermentation reactor, and a heating system connected to the fermentation reactor, a humidifier, an oxygen pump, and the like. The center of the fermentation reactor is evenly arranged with circulating water insulation pipes, and the insulation pipes are connected to the heat supply system separately provided outside the fermentation reactor to form a heat supply circuit so that the required temperature can be maintained uniformly in the reactor. The humidifier and the oxygen pump are respectively connected to the fermentation reactor through a steam pipe and an oxygen pipe to maintain the required humidity and oxygen in the reactor, and the steam pipe is also uniformly arranged around the center of the fermentation reactor to make the humidity uniform. . The inner bottom of the fermentation reactor is provided with a water filtering device, so that cleaning is convenient after fermentation, and the sewage can flow out directly. There is a sampling port and an air outlet on the fermentation reactor. During the test, samples need to be taken in time. The diameter of the sampling port is 10 cm, which can be opened and closed automatically. Sampling from here can ensure that the fermentation material is not contaminated with bacteria, and the air outlet is specially designed for white rot. Bacteria, an aerobic fungus, is designed to facilitate the smooth flow of oxygen and ensure better growth of white rot fungi. A temperature probe is installed in the fermentation reactor to reflect the temperature in the reactor at any time for control. The heating system, humidifier, oxygen pump, and temperature probe are all connected to the control system through control lines or signal lines. The control system has a control panel for displaying and setting temperature and humidity, which can control the temperature, humidity, and oxygen supply of fermentation. and other process conditions to set and control.

所述供热系统为电热水容器,通过循环管路连接发酵反应器内的循环水保温管;电热水容器的进水由潜水泵控制,电热水容器和潜水泵均通过控制线连接控制系统。The heating system is an electric hot water container, which is connected to the circulating water insulation pipe in the fermentation reactor through a circulation pipeline; the water intake of the electric hot water container is controlled by a submersible pump, and both the electric hot water container and the submersible pump are connected to the control system through a control line.

所述发酵反应器为发酵罐或发酵池结构,在所述发酵反应器的周围包有一层海绵保温套,在发酵罐或池体底部设置有放料孔,可以自动打开和关闭。The fermentation reactor is a structure of a fermenter or a fermentation tank, and a layer of sponge insulation cover is wrapped around the fermentation reactor, and a discharge hole is arranged at the bottom of the fermenter or tank body, which can be opened and closed automatically.

所述温度探头和湿度探头通过取样口或出气口插入在发酵反应器内,或设置在观察窗内,在氧气泵里设置除菌滤膜。自动控制面板上设置有内循环水加热指示灯、温度设定旋钮、实时温度显示窗、总电源的开关、供热系统与潜水泵工作状态指示灯和供热系统、潜水泵电源开关。The temperature probe and the humidity probe are inserted into the fermentation reactor through the sampling port or the gas outlet, or are set in the observation window, and a sterilizing filter membrane is set in the oxygen pump. The automatic control panel is equipped with internal circulating water heating indicator light, temperature setting knob, real-time temperature display window, main power switch, heating system and submersible pump working status indicator light and heating system, submersible pump power switch.

本装置的优点Advantages of this device

(1)本系统结构简单,便于操作,可以自动控制白腐菌发酵的温度,湿度,通气量,可以实现发酵过程的自动控制,利于白腐真菌高产木质素降解酶,提高发酵均匀性,缩短了发酵周期,提高了生产率,通过放大发酵装置,扩大发酵容量,可以直接应用到造纸工业前处理中。(1) The system is simple in structure and easy to operate. It can automatically control the temperature, humidity, and ventilation of white rot fungi fermentation, and can realize automatic control of the fermentation process, which is beneficial to the high production of lignin degrading enzymes by white rot fungi, improves the uniformity of fermentation, and shortens the time of fermentation. The fermentation cycle is shortened, and the productivity is improved. By enlarging the fermentation device and expanding the fermentation capacity, it can be directly applied to the pretreatment of the papermaking industry.

(2)发酵反应器上的观察窗口可以清晰的观察到白腐真菌的生长情况,便于及时调节温度,湿度,通气量等参数。(2) The observation window on the fermentation reactor can clearly observe the growth of white rot fungi, which is convenient for timely adjustment of parameters such as temperature, humidity, and ventilation.

(3)将加热系统与发酵反应器分离设置,可以更好的控制试验所需的温度,且发酵反应器外部有一层保温套,保证温度更加稳定,在反应器内均匀布置循环水保温管,可以保证整个发酵过程受热均匀,并且还能使倒进的物料疏松均匀。(3) Separate the heating system from the fermentation reactor, which can better control the temperature required for the test, and there is a layer of insulation cover outside the fermentation reactor to ensure a more stable temperature, and evenly arrange circulating water insulation pipes in the reactor, It can ensure that the entire fermentation process is evenly heated, and it can also make the poured materials loose and even.

(4)发酵反应器底部设置的滤水器,一方面可以滤去由于通蒸气时盖子上向下滴的水,一方面起到通气的作用,使氧气供应更加均匀充分。(4) The water filter installed at the bottom of the fermentation reactor can filter out the water dripping from the lid when the steam is ventilated, and also play the role of ventilation to make the oxygen supply more uniform and sufficient.

(5)本系统底部有放料口,可以自动打开和关闭,处理发酵材料时既可以从这里放料,也可以放出冲洗用的水,这样便于彻底清洗。氧气泵里用的除菌滤膜,通入无菌空气,降低杂菌污染率,可提高产品的品质。(5) There is a discharge port at the bottom of the system, which can be opened and closed automatically. When processing fermentation materials, it can be discharged from here, and water for washing can also be discharged, which is convenient for thorough cleaning. The sterilizing filter membrane used in the oxygen pump can pass in sterile air, reduce the contamination rate of bacteria, and improve the quality of the product.

附图说明 Description of drawings

图1是本系统的结构示意图;Fig. 1 is the structural representation of this system;

图2是控制面板结构示意图;Fig. 2 is a schematic diagram of the structure of the control panel;

图3是发酵罐的结构示意图;Fig. 3 is the structural representation of fermentation tank;

图4是发酵罐盖的示意图;Fig. 4 is the schematic diagram of fermenter lid;

图5是本系统的控制原理图;Fig. 5 is the control schematic diagram of this system;

图1中,1发酵自动控制系统(包括发酵罐内温度的设定,发酵罐内实际温度显示,加热水桶的工作指示等),2电热水容器,3潜水泵,4循环水出水管道,5循环水进水管道,6温度探头线,7电源线,8电源插座,9发酵罐,10通蒸气管道,11超声波加湿器,12通氧气管道,13氧气泵,14发酵罐支架。In Fig. 1, 1 fermentation automatic control system (including the setting of the temperature in the fermentation tank, the actual temperature display in the fermentation tank, the working instruction of the heating bucket, etc.), 2 electric hot water container, 3 submersible pump, 4 circulating water outlet pipe, 5 Circulating water inlet pipe, 6 temperature probe line, 7 power cord, 8 power socket, 9 fermenter tank, 10 steam pipe, 11 ultrasonic humidifier, 12 oxygen pipe, 13 oxygen pump, 14 fermenter support.

图2中,1-1发酵罐内预设温度表,1-2发酵罐内温度实时显示表,1-3总电源打开按钮,1-4锁,1-5总电源关闭按钮,1-6总电源开关指示灯,1-7电热水容器和潜水泵电源开关,1-8电热水容器和潜水泵电源开关指示灯。In Fig. 2, 1-1 preset temperature gauge in the fermenter, 1-2 real-time temperature display table in the fermenter, 1-3 total power on button, 1-4 lock, 1-5 total power off button, 1-6 Main power switch indicator light, 1-7 electric water tank and submersible pump power switch, 1-8 electric water tank and submersible pump power switch light.

图3中,9-1发酵罐盖,9-2湿度计,9-3自动控制阀门,9-4通氧换气有孔管,9-5循环水保温管,9-6放料孔,9-7有孔滤水器,9-8放水阀。In Fig. 3, 9-1 fermenter cover, 9-2 hygrometer, 9-3 automatic control valve, 9-4 perforated pipe for oxygen ventilation, 9-5 circulating water insulation pipe, 9-6 discharge hole, 9-7 has a porous water filter, and 9-8 drain valve.

图4中,9-9观察窗,9-10出气孔,9-11温度探头插孔,9-12取样孔。Among Fig. 4, 9-9 observation window, 9-10 air outlet, 9-11 temperature probe jack, 9-12 sampling hole.

具体实施方式 Detailed ways

参见图1,本白腐真菌固体发酵系统主要由发酵自动控制系统1、发酵罐9、与发酵罐连接的电热水容器2、超声波加湿器11、氧气泵13、循环潜水泵3等组成,它们通过管路或线路连接成一个完整的发酵系统,管道连接方式:超声波加湿器11的蒸气出口用通蒸气管道10(1寸塑料水管)与发酵罐进气口连接。氧气泵13通过通氧气管道12连接发酵罐9。循环潜水泵3的出水通过循环水进水管道5与发酵罐9的入水口连接,再将发酵罐出水通过循环水出水管道4连接,直接将加热/冷却水排回电热水容器2内;温度探头插入发酵罐温度探头插孔9-11(见图4)内并应放到底为止,通过温度探头线6连接发酵自动控制系统1;停止加水蒸气时,应先将发酵罐通气孔用棉塞堵上,防止空气回流带入污染。发酵自动控制系统1通过电源线7与电源插座8连接。发酵罐9安装在发酵罐支架14上,罐体外可加上海绵保温套。Referring to Fig. 1, the white rot fungus solid fermentation system is mainly composed of a fermentation automatic control system 1, a fermentation tank 9, an electric hot water container 2 connected to the fermentation tank, an ultrasonic humidifier 11, an oxygen pump 13, and a circulating submersible pump 3. A complete fermentation system is connected by pipelines or lines. The pipeline connection mode: the steam outlet of the ultrasonic humidifier 11 is connected with the air inlet of the fermenter with a steam pipeline 10 (1-inch plastic water pipe). The oxygen pump 13 is connected to the fermenter 9 through the oxygen pipeline 12 . The outlet water of the circulating submersible pump 3 is connected to the water inlet of the fermenter 9 through the circulating water inlet pipe 5, and then the outlet water of the fermenter is connected through the circulating water outlet pipe 4, and the heating/cooling water is directly discharged back into the electric hot water container 2; Insert the probe into the temperature probe socket 9-11 (see Figure 4) of the fermentation tank and put it to the bottom, and connect the fermentation automatic control system 1 through the temperature probe line 6; Plug it to prevent the backflow of air from bringing pollution. The fermentation automatic control system 1 is connected with a power socket 8 through a power cord 7 . Fermentation tank 9 is installed on the fermentation tank support 14, and the sponge insulation cover can be added outside the tank.

结合参见图2,其中发酵罐9全部用不锈钢制成,可以容纳250kg的固体发酵材料,底部设置有一有孔滤水器9-7,在有孔滤水器上、发酵罐的中央均匀环绕布置有循环水保温管9-5,循环水保温管9-5的两端通过进出水管路与外部的电热水容器2连接,其上有自动控制阀门9-3,形成循环。发酵罐内还均匀绕布有通氧换气有孔管9-4,通氧换气有孔管9-4与外部的超声波加湿器11和氧气泵13相连,为其供氧换气。参见图3,发酵罐盖9-1上有两个圆形取样孔9-12,一出气孔9-10,一温度探头插孔9-11和两个观察窗9-9。发酵罐的底部有放料孔9-6和放水阀9-8。See Fig. 2 in combination, wherein the fermenter 9 is all made of stainless steel, can hold 250kg of solid fermentation material, and a perforated water filter 9-7 is arranged at the bottom, and is evenly arranged around the center of the perforated water filter and the fermenter Circulating water insulation pipe 9-5 is arranged, and the two ends of circulating water insulation pipe 9-5 are connected with external electric hot water container 2 by water inlet and outlet pipelines, and automatic control valve 9-3 is arranged on it, forms circulation. The perforated tube 9-4 for oxygen ventilation is evenly distributed in the fermentation tank, and the perforated tube 9-4 for oxygen ventilation is connected to the external ultrasonic humidifier 11 and oxygen pump 13 for oxygen supply and ventilation. Referring to Fig. 3, there are two circular sampling holes 9-12, an air outlet 9-10, a temperature probe jack 9-11 and two observation windows 9-9 on the fermenter cover 9-1. The bottom of the fermentation tank has a discharge hole 9-6 and a drain valve 9-8.

再结合参见图4,自动控制面板设置有发酵罐内预设温度表1-1,发酵罐内温度实时显示表1-2,总电源打开按钮1-3,锁1-4,总电源关闭按钮1-5,总电源开关指示灯1-6,电热水容器和潜水泵电源开关1-7,电热水容器和潜水泵电源开关指示灯1-8。Referring again to Fig. 4, the automatic control panel is provided with a preset temperature gauge 1-1 in the fermenter, a real-time temperature display gauge 1-2 in the fermenter, a total power on button 1-3, a lock 1-4, and a total power off button 1-5, total power switch indicator light 1-6, electric hot water container and submersible pump power switch 1-7, electric hot water container and submersible pump power switch indicator light 1-8.

本系统的控制原理如图5所示,通过温度预设器设置所需温度,由温控仪控制电热水桶内水的加热,并控制循环泵为发酵罐提供循环水,由温度探头感知罐内的温度,并通过温控仪控制进行显示。继电保护器和空气开关用于对电热水桶和循环泵进行保护。The control principle of this system is shown in Figure 5. The required temperature is set through the temperature presetter, the temperature controller controls the heating of the water in the electric hot water tank, and the circulating pump is controlled to provide circulating water for the fermentation tank, and the temperature probe senses the temperature in the tank. The temperature is displayed through the temperature controller control. The relay protector and air switch are used to protect the electric hot water bucket and circulation pump.

整套装置操作流程:The operation process of the whole device:

本系统在使用前预先对发酵罐内部进行全面灭菌,采用高压灭菌锅连接管道通蒸气的方式或者直接用10%的次氯酸钠喷雾灭菌,经过实验证明,用10%的次氯酸钠喷雾灭菌后盖严固体发酵罐盖40min完全可以达到无菌的目的,这种方法既安全又简单。在电热水桶中注入不少于2/3总容量的自来水(不许干烧);把温度探头插入发酵罐插口内,连接好各通气管道和通氧管道以及温度探头;将电热水容器预设温度为45℃(循环水最高温度值);接着是打开电源,控制箱上自行设置好发酵所需温度,然后是把灭菌好的固体发酵基质一部分放入发酵罐中冷却,另外放入超净工作台中冷却,冷却后,开始接种,菌种为之前在造纸原料(木屑或者竹材)中驯化培养后的白腐菌复合菌种,用分层接种的方式来进行,这样可以省去搅拌的步骤,进而保证白腐菌在大型发酵装置中正常生长并高效产酶降解木质素,接种完毕后,插上配电箱三孔插头电源,联通超声波加湿器电源,加湿;联通氧气泵,进行充气;向上合上(通电)空气开关;按下控制面板绿色电源开关,联通总电源,此时面板绿灯亮;旋动温度旋钮到预定发酵罐内需要的温度(35℃-40℃之间),通蒸气,通氧气,发酵罐开始工作。测定温度和湿度,以后每20d从取样口处取10g发酵原料进行相关测定。至发酵完成发酵完成后;按红色按钮关总电源;向下按空气开关断电,拔下所有电源插头;所有旋钮(四个)全部回零;拆除通气通循环水连接管,取出温度探头;取出产物;倒掉电热水桶和加湿器中的水;清洗发酵罐;取出循环水泵拭干保存;完成。Before use, the system fully sterilizes the interior of the fermenter in advance, and uses the method of connecting the pipeline to steam through the autoclave or directly sprays sterilizing with 10% sodium hypochlorite. It has been proved by experiments that after spraying with 10% sodium hypochlorite Closing the lid of the solid fermenter for 40 minutes can completely achieve the purpose of sterility. This method is safe and simple. Inject no less than 2/3 of the total capacity of tap water into the electric hot water tank (dry boiling is not allowed); insert the temperature probe into the socket of the fermenter, connect the ventilation pipes, oxygen pipes and temperature probes; set the electric water tank to the preset temperature 45°C (the highest temperature value of circulating water); then turn on the power, set the temperature required for fermentation on the control box, and then put a part of the sterilized solid fermentation substrate into the fermenter to cool, and put it into the ultra-clean Cool in the workbench. After cooling, start inoculation. The bacteria are the white rot fungus composite bacteria that have been domesticated and cultivated in the papermaking raw materials (sawdust or bamboo). The method of inoculation is carried out in layers, which can save the step of stirring , and then ensure the normal growth of white rot fungus in the large-scale fermentation device and efficiently produce enzymes to degrade lignin. After inoculation, plug in the power supply of the three-hole plug in the distribution box, and connect to the power supply of the ultrasonic humidifier to humidify; connect to the oxygen pump to inflate; Turn on (power on) the air switch upward; press the green power switch on the control panel to connect to the main power supply, and the green light on the panel is on at this time; turn the temperature knob to the desired temperature in the fermenter (between 35°C and 40°C), and turn on Steam, oxygen, and the fermenter starts to work. Measure the temperature and humidity, and then take 10g of fermentation raw materials from the sampling port every 20d for related determination. After the fermentation is completed, press the red button to turn off the main power; press the air switch down to power off, and unplug all the power plugs; all the knobs (four) are all returned to zero; remove the ventilation and circulating water connection pipe, and take out the temperature probe; Take out the product; pour out the water in the electric hot water bucket and humidifier; clean the fermentation tank; take out the circulating water pump and dry it for storage; complete.

以下是本系统用于纤维素和木质素降解酶固体发酵大规模生产应用实例:The following are the application examples of this system for solid fermentation of cellulose and lignin degrading enzymes in large-scale production:

根据白腐真菌生物学特性,白腐真菌的最佳生长条件为28℃~39℃,湿度在60%左右,每天通气时间为2h,pH值为4.5左右。首先选择白腐真菌菌株,经菌种斜面试管培养、锥形瓶中液体扩大培养,7L发酵罐液体扩大培养,用液体菌种接种到玻璃瓶中进行固体发酵,经过12天发酵进行驯化,待接种到发酵罐中的草本或者木本纤维原料中发酵。其中液体培养基配方为L-1:葡萄糖10g,磷酸二氢钾3g,硫酸镁1.5g,硫酸铜0.015g,硫酸亚铁0.2g,硫酸锰0.2g,酒石酸钠2mmol,吐温2g,VB10.001g。固体发酵溶液配方为L-1:葡萄糖10g,磷酸二氢钾3g,硫酸镁1.5g,硫酸铜0.015g,硫酸亚铁0.2g,硫酸锰0.2g,酒石酸钠2mmol,吐温2g,VB10.001g,苯甲醇6mmol,H2O25g,以竹材与麸皮(质量比为8∶2)的混合物为白腐真菌发酵原料,用固体发酵溶液来混匀,含水率约60%,分装在纱布袋子里,在立式高压灭菌锅中,0.5MPa,121℃下,灭菌30min,冷却后放入发酵罐中,分层接种,接种物为经在玻璃瓶中固体发酵驯化12d后的白腐菌种。自然发酵10天后开始取物料,挤出酶液,测定木素过氧化物酶(LiP)、锰过氧化物酶(MnP)、漆酶(Laccase)的酶活,以后每10天测定一次酶活,每10天测定一次纤维素和木质素降解率。According to the biological characteristics of white rot fungi, the best growth conditions for white rot fungi are 28°C to 39°C, humidity around 60%, aeration time of 2 hours per day, and pH value of around 4.5. First select the white rot fungus strain, culture it in inclined test tubes, expand the liquid in the conical flask, expand the culture in the 7L fermenter, inoculate the liquid strain into the glass bottle for solid fermentation, and domesticate it after 12 days of fermentation. Ferment in the herbaceous or woody fiber raw material inoculated in the fermenter. The liquid medium formula is L-1: glucose 10g, potassium dihydrogen phosphate 3g, magnesium sulfate 1.5g, copper sulfate 0.015g, ferrous sulfate 0.2g, manganese sulfate 0.2g, sodium tartrate 2mmol, Tween 2g, VB 1 0.001g. The formula of solid fermentation solution is L-1: glucose 10g, potassium dihydrogen phosphate 3g, magnesium sulfate 1.5g, copper sulfate 0.015g, ferrous sulfate 0.2g, manganese sulfate 0.2g, sodium tartrate 2mmol, Tween 2g, VB10.001g , benzyl alcohol 6mmol, H 2 O 2 5g, take the mixture of bamboo and bran (mass ratio is 8:2) as white rot fungus fermentation raw material, mix with solid fermentation solution, moisture content is about 60%, pack in In a gauze bag, in a vertical autoclave, 0.5MPa, 121°C, sterilize for 30 minutes, put it into a fermenter after cooling, and inoculate in layers. The inoculum is domesticated by solid fermentation in a glass bottle for 12 days. White rot bacteria. After 10 days of natural fermentation, start to take materials, squeeze out the enzyme solution, and measure the enzyme activities of lignin peroxidase (LiP), manganese peroxidase (MnP) and laccase (Laccase), and then measure the enzyme activity every 10 days , the cellulose and lignin degradation rates were measured every 10 days.

根据发酵罐内所需温度,设定电热水桶内温度,此温度适当比发酵罐内预设温度高3-5℃,通过潜水泵使发酵罐中的进水管和出水管进行水循环达到对发酵罐保温的作用,加湿器与发酵罐之间连有一根通蒸汽管来达到对白腐菌固体发酵过程保湿的作用,通过温湿度计来测定发酵罐内的温度、湿度。氧气泵一端与发酵桶之间连有一通氧气管来达到通氧气的作用,控制箱来控制温度参数。这些管道连接好之后,发酵罐可以正常工作了。According to the required temperature in the fermenter, set the temperature in the electric hot water barrel, which is 3-5°C higher than the preset temperature in the fermenter, and use the submersible pump to circulate the water in the water inlet and outlet pipes in the fermenter to achieve the desired effect on the fermenter. For the function of heat preservation, there is a steam pipe connected between the humidifier and the fermenter to achieve the effect of moisturizing the white rot fungus solid fermentation process, and the temperature and humidity in the fermenter are measured by a thermo-hygrometer. An oxygen pipe is connected between one end of the oxygen pump and the fermenter to achieve the effect of passing oxygen, and the control box is used to control the temperature parameters. After these pipes are connected, the fermenter can work normally.

以下是对比实验:The following is a comparative experiment:

实验室已经研究证实,以黄孢原毛平革菌、朱红栓菌(购买于中科院微生物所)、平菇(购于重庆市农科所)三种白腐真菌的复合菌种接种到以竹材为原料中进行固体发酵的结果表明,利用不同培养条件下白腐真菌复合菌种处理的竹材中,木质素、半纤维素的降解程度,处理前后竹材干物质的损失以及体内干物质消化率等均有很大的差异,温度高低影响白腐真菌固体发酵的时间和竹材木质素的降解率。同时,不同的菌种适宜生长的温度也不尽相同。实验中中所选用菌种适宜温度都在28~32℃之间。就水分含量和通风状况而言,往往相互影响。若处理竹材的水分含量过低,就会使菌丝生长受到抑制。而含水量过高则导致通风不良,影响O2的通入,而且发酵过程中产生的CO2和热量得不到及时散失,对菌丝的生长不利。实验结果表明,由于白腐真菌对木质素的降解很大程度上是一种氧化过程,在培养所需三种菌种时,充氧是其产生木质素过氧化酶的必要条件,否则不产酶或产酶很少。所以,在保持竹材含水量适宜的条件下,充足的氧气供应对白腐真菌的生长及处理效果至关重要。固体发酵竹材的总水分应控制在3∶1为最佳。除了上述影响因素外,白腐真菌在开始生长时还需要基质处于无菌和高度需氧的环境。在有杂菌存在时,杂菌可能占优势,致使处理失败。因此,为了达到提高竹材消化率的目的必须抑制不利菌的生长。The laboratory has confirmed that the composite strains of Phanerochaete chrysosporium, Trametes vermilion (purchased from the Institute of Microbiology, Chinese Academy of Sciences), and Pleurotus ostreatus (purchased from the Chongqing Institute of Agricultural Sciences) were used to inoculate bamboo as a The results of solid fermentation in the raw materials showed that the degradation degree of lignin and hemicellulose, the loss of dry matter of bamboo before and after treatment, and the digestibility of dry matter in the body of bamboo treated with white rot fungi under different culture conditions were all the same. There is a big difference, the temperature affects the solid fermentation time of white rot fungi and the degradation rate of bamboo lignin. At the same time, the suitable growth temperature of different strains is not the same. The optimum temperature for the strains selected in the experiment is between 28 and 32°C. In terms of moisture content and ventilation, there is often an interaction. If the moisture content of the treated bamboo is too low, the growth of mycelia will be inhibited. Excessive water content will lead to poor ventilation and affect the introduction of O2 , and the CO2 and heat generated during the fermentation process will not be dissipated in time, which is unfavorable to the growth of mycelia. The experimental results show that since the degradation of lignin by white-rot fungi is largely an oxidation process, oxygenation is a necessary condition for the production of lignin peroxidase when cultivating the three required strains, otherwise no lignin peroxidase will be produced. Enzymes or enzymes are rarely produced. Therefore, under the condition of maintaining a suitable moisture content in bamboo, sufficient oxygen supply is very important for the growth and treatment effect of white rot fungi. The total moisture of solid fermented bamboo should be controlled at 3:1, which is the best. In addition to the aforementioned influencing factors, white rot fungi require a sterile and highly aerobic environment in the substrate to initiate growth. In the presence of miscellaneous bacteria, miscellaneous bacteria may dominate, resulting in failure of treatment. Therefore, in order to achieve the purpose of improving the digestibility of bamboo, it is necessary to inhibit the growth of unfavorable bacteria.

白腐真菌被发现具有自身合成并分泌多种胞外过氧化物酶的能力,它们在竹材上能产生木质素过氧化物酶、锰过氧化物酶和漆酶。其中,LiP和MnP是木质素降解中两类关键酶,在分子氧的参与下,依靠自身形成的H2O2触发启动一系列自由基链反应,彻底氧化竹材中的木质素。但三种不同菌株产生的酶种类和活性不同,从而直接影响着竹材的降解效果。从图中可知,当以黄孢原毛平革菌、朱红栓菌、平菇为菌株处理竹材的过程中,木质素过氧化物酶的活力在第9d达到最大值,为28.3U/g。锰过氧化合物酶的活力在第8d达到最大值,为12.6U/g。说明该这三种菌株能产生较高活力的木质素过氧化物酶、锰过氧化合物酶和漆酶,是降解竹材的优良菌株。White-rot fungi have been found to have the ability to synthesize and secrete a variety of extracellular peroxidases, and they can produce lignin peroxidase, manganese peroxidase and laccase on bamboo. Among them, LiP and MnP are two key enzymes in the degradation of lignin. With the participation of molecular oxygen, a series of free radical chain reactions are triggered by the H 2 O 2 formed by themselves, and the lignin in bamboo wood is completely oxidized. However, the types and activities of enzymes produced by the three different strains were different, which directly affected the degradation effect of bamboo. It can be seen from the figure that when the bamboo was treated with Phanerochaete chrysosporium, Trametes vermilion and Pleurotus ostreatus as strains, the activity of lignin peroxidase reached the maximum on the 9th day, which was 28.3 U/g. The activity of manganese peroxidase reached the maximum value of 12.6 U/g on the 8th day. It shows that these three strains can produce lignin peroxidase, manganese peroxidase and laccase with high activity, and they are excellent strains for degrading bamboo.

表1 白腐菌处理时间对竹材主要组分降解率的影响Table 1 Effect of white rot fungus treatment time on the degradation rate of main components of bamboo

Figure Y200820098607D00111
Figure Y200820098607D00111

而在用其他装置用白腐菌对竹材发酵进行降解时得出的一组数据是:A set of data obtained when using other devices to degrade bamboo fermentation with white rot fungi is:

表2 白腐菌处理时间对竹材主要组分降解率的影响Table 2 Effect of white rot fungus treatment time on the degradation rate of main components of bamboo

Figure Y200820098607D00112
Figure Y200820098607D00112

Figure Y200820098607D00121
Figure Y200820098607D00121

从表1和表2的对比可以看出,应用此装置对造纸原料进行发酵,高效降解木质素方面有很大的改进,木质素降解率明显高于利用以前的固体发酵装置效果,同样的纤维素降解率更低,这正是造纸生产中最需要的理想效果,即高效降解木质素,更低的降解纤维素,以确保造纸原料的节省和充分利用。对木质素的高效降解可以减轻造纸工业中利用强碱对木质素降解的化学污染进而造成的废水污染。这对环保方面的作用非常明显。From the comparison of Table 1 and Table 2, it can be seen that the application of this device to ferment papermaking raw materials has greatly improved the efficient degradation of lignin, and the lignin degradation rate is significantly higher than that of the previous solid fermentation device. The same fiber The degradation rate of lignin is lower, which is the ideal effect most needed in papermaking production, that is, efficient degradation of lignin and lower degradation of cellulose, so as to ensure the saving and full utilization of papermaking raw materials. The efficient degradation of lignin can reduce the chemical pollution caused by the degradation of lignin by strong alkali in the paper industry and the waste water pollution. This has a very obvious effect on environmental protection.

Claims (7)

1、白腐菌固体发酵系统,包括控制系统、发酵反应器,其特征在于:还包括有连接发酵反应器的供热系统、加湿器、氧气泵;所述发酵反应器中央均匀环绕布置有循环水保温管,循环水保温管与发酵反应器外部单独设置的供热系统连接,形成供热回路;所述加湿器和氧气泵分别通过通蒸汽管道和通氧气管道连接发酵反应器,通蒸汽管道亦在发酵反应器中央均匀环绕布置;所述发酵反应器内底部设置有滤水装置;所述发酵反应器上有取样口、出气口和观察窗,并在发酵反应器内设置有温度探头;所述供热系统、加湿器、氧气泵、温度探头均通过控制线或信号线与控制系统连接,控制系统具有显示和设定温度、湿度的控制面板。1. The white rot fungus solid fermentation system, including a control system and a fermentation reactor, is characterized in that: it also includes a heating system connected to the fermentation reactor, a humidifier, and an oxygen pump; the center of the fermentation reactor is evenly arranged with circulation The water insulated pipe and the circulating water insulated pipe are connected to the heating system provided separately outside the fermentation reactor to form a heating circuit; the humidifier and the oxygen pump are respectively connected to the fermentation reactor through the steam pipe and the oxygen pipe, and the steam pipe It is also uniformly arranged around the center of the fermentation reactor; the bottom of the fermentation reactor is provided with a water filter; the fermentation reactor has a sampling port, an air outlet and an observation window, and a temperature probe is provided in the fermentation reactor; The heating system, humidifier, oxygen pump, and temperature probe are all connected to the control system through control lines or signal lines, and the control system has a control panel for displaying and setting temperature and humidity. 2、根据权利要求1所述的白腐菌固体发酵系统,其特征在于:所述供热系统为电热水容器,通过循环管路连接发酵反应器内的循环水保温管;电热水容器的进水由潜水泵控制,电热水容器和潜水泵均通过控制线连接控制系统。2. The white rot fungus solid fermentation system according to claim 1, characterized in that: the heating system is an electric hot water container, which is connected to the circulating water insulation pipe in the fermentation reactor through a circulation pipeline; The water is controlled by the submersible pump, and both the electric hot water container and the submersible pump are connected to the control system through the control line. 3、根据权利要求1或2所述的白腐菌固体发酵系统,其特征在于:所述发酵反应器为发酵罐或发酵池结构。3. The white-rot fungus solid fermentation system according to claim 1 or 2, characterized in that: the fermentation reactor is a fermenter or a fermenter structure. 4、根据权利要求3所述的白腐菌固体发酵系统,其特征在于:自动控制面板上设置有有发酵反应器内预设温度表、发酵反应器内温度实时显示表、总电源打开按钮、锁、总电源关闭按钮、总电源开关指示灯、供热系统和潜水泵电源开关以及供热系统和潜水泵电源开关指示灯。4. The white-rot fungus solid fermentation system according to claim 3, characterized in that: the automatic control panel is provided with a preset temperature gauge in the fermentation reactor, a real-time display of the temperature in the fermentation reactor, a general power on button, Lock, main power off button, main power switch indicator light, heating system and submersible pump power switch and heating system and submersible pump power switch indicator light. 5、根据权利要求4所述的白腐菌固体发酵系统,其特征在于:所述在氧气泵里设置除菌滤膜。5. The white rot fungus solid fermentation system according to claim 4, characterized in that: the oxygen pump is provided with a sterilizing filter membrane. 6、根据权利要求5所述的白腐菌固体发酵系统,其特征在于:在所述发酵反应器的周围包有一层海绵保温套。6. The white rot fungus solid fermentation system according to claim 5, characterized in that: a layer of sponge insulation is wrapped around the fermentation reactor. 7、根据权利要求6所述的白腐菌固体发酵系统,其特征在于:在发酵反应器或池体底部设置有可自动关闭或打开的放料孔。7. The white rot fungus solid fermentation system according to claim 6, characterized in that: there is a discharge hole that can be automatically closed or opened at the bottom of the fermentation reactor or the tank body.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104711236A (en) * 2015-03-11 2015-06-17 湖南大学 Lignin-degrading enzyme regulator and application thereof
CN109439515A (en) * 2018-12-19 2019-03-08 广州甲宝机械有限公司 A kind of spiral biological second level that declines spreads cultivation device and method
CN109810882A (en) * 2019-03-19 2019-05-28 绥化学院 System and method for large-scale production of fungal solid fermentation products
WO2019114275A1 (en) * 2017-12-12 2019-06-20 陈军瑞 Enzymatic hydrolysis apparatus with fixing mechanism
CN110499248A (en) * 2019-07-31 2019-11-26 江苏大学 A solid-state fermentation humidity control system
CN114106988A (en) * 2012-10-26 2022-03-01 麻省理工学院 Humidity Control in Chemical Reactors

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114106988A (en) * 2012-10-26 2022-03-01 麻省理工学院 Humidity Control in Chemical Reactors
CN104711236A (en) * 2015-03-11 2015-06-17 湖南大学 Lignin-degrading enzyme regulator and application thereof
CN104711236B (en) * 2015-03-11 2017-10-31 湖南大学 Lignin-degrading enzymes adjusting control agent and its application
WO2019114275A1 (en) * 2017-12-12 2019-06-20 陈军瑞 Enzymatic hydrolysis apparatus with fixing mechanism
CN109439515A (en) * 2018-12-19 2019-03-08 广州甲宝机械有限公司 A kind of spiral biological second level that declines spreads cultivation device and method
CN109810882A (en) * 2019-03-19 2019-05-28 绥化学院 System and method for large-scale production of fungal solid fermentation products
CN109810882B (en) * 2019-03-19 2022-07-05 绥化学院 System and method for large-scale production of fungal solid fermentation products
CN110499248A (en) * 2019-07-31 2019-11-26 江苏大学 A solid-state fermentation humidity control system
CN110499248B (en) * 2019-07-31 2022-12-16 江苏大学 Solid state fermentation humidity control system

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