CN202519239U - Roller cellulose solid state fermentation ethanol reactor - Google Patents
Roller cellulose solid state fermentation ethanol reactor Download PDFInfo
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- CN202519239U CN202519239U CN201220027108.6U CN201220027108U CN202519239U CN 202519239 U CN202519239 U CN 202519239U CN 201220027108 U CN201220027108 U CN 201220027108U CN 202519239 U CN202519239 U CN 202519239U
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- C12M—APPARATUS 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
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/12—Bioreactors or fermenters specially adapted for specific uses for producing fuels or solvents
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/16—Solid state fermenters, e.g. for koji production
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- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
- C12M27/06—Stirrer or mobile mixing elements with horizontal or inclined stirrer shaft or axis
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- 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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Abstract
本实用新型公开一种滚筒式纤维素固态发酵乙醇反应器,包括外罐体和空套在外罐体内腔中的内罐体,旋转主轴从内罐体和外罐体的底部伸入内罐体内腔中,在内罐体内腔中的旋转主轴上固接多个三角形桨叶,旋转主轴固接内罐体且通过位于外罐体底部的密封的轴承装置与外罐体相接;旋转主轴是中空管状,在内罐体内腔中的旋转主轴上开有多个通气孔;内罐体内腔通过管道连接位于外罐体外部的渗透膜分离装置的输入口,渗透膜分离装置的输出口通过管道连接旋转主轴且与旋转主轴相通;物料利用自重和固定的搅拌桨叶实现发酵物料的充分搅拌,从而提高发酵效率,便于将酵母和营养液喷淋到内罐体,可以在补充纤维素酶、酵母和营养液时做到无菌操作。
The utility model discloses a drum-type cellulose solid-state fermentation ethanol reactor, which comprises an outer tank body and an inner tank body hollowly sleeved in the inner cavity of the outer tank body, and a rotating spindle extends into the inner tank body from the bottom of the inner tank body and the outer tank body In the cavity, a plurality of triangular paddles are fixed on the rotating shaft in the inner cavity of the inner tank, and the rotating shaft is fixed to the inner tank and connected to the outer tank through a sealed bearing device located at the bottom of the outer tank; the rotating shaft is Hollow tubular, with multiple ventilation holes on the rotating shaft in the inner tank cavity; the inner tank cavity is connected to the input port of the permeable membrane separation device located outside the outer tank body through a pipeline, and the output port of the permeable membrane separation device is passed through a pipeline It is connected to the rotating main shaft and communicated with the rotating main shaft; the material is fully stirred by its own weight and fixed stirring blades, thereby improving the fermentation efficiency, and it is convenient to spray the yeast and nutrient solution into the inner tank, which can be added in cellulase, Aseptic operation should be done when yeast and nutrient solution are used.
Description
技术领域 technical field
本实用新型属于发酵设备技术领域,具体涉及纤维素固态发酵乙醇反应器。 The utility model belongs to the technical field of fermentation equipment, in particular to a cellulose solid-state fermentation ethanol reactor.
背景技术 Background technique
纤维素固态发酵乙醇是指在很少自由水存在下,在有一定湿度的水不溶性固体基质中,通过酶解和糖化发酵的过程。传统的发酵反应器是由主轴带动搅拌桨来混合物料,但是在纤维素固态发酵过程中,纤维素在酶解和发酵时较为粘稠,发酵物是固态的,所以不易搅拌均匀,这样会导致发酵过程中热量传导不均匀,不利于发酵过程中物料温度的测量和控制,也不利于物料的充分发酵,导致发酵不彻底,所以发酵效率很低,发酵周期长,且在发酵后期,纤维素酶、 酵母及营养液没有全部用完就和废渣一起倒掉了,这样浪费了资源也增加了生产成本。 Cellulose solid-state fermentation ethanol refers to the process of enzymatic hydrolysis and saccharification fermentation in a water-insoluble solid matrix with a certain humidity in the presence of little free water. In the traditional fermentation reactor, the main shaft drives the stirring paddle to mix the materials. However, in the solid-state fermentation process of cellulose, the cellulose is relatively viscous during enzymatic hydrolysis and fermentation, and the fermented product is solid, so it is difficult to stir evenly, which will cause Uneven heat conduction during the fermentation process is not conducive to the measurement and control of the material temperature during the fermentation process, and is also not conducive to the full fermentation of the material, resulting in incomplete fermentation, so the fermentation efficiency is very low, the fermentation cycle is long, and in the later stage of fermentation, the cellulose Enzymes, yeast and nutrient solution are not all used up and are dumped together with the waste residue, which wastes resources and increases production costs.
发明内容 Contents of the invention
本实用新型的目的是为克服上述现有技术缺陷而提供一种滚筒式纤维素固态发酵乙醇反应器,能充分搅拌物料,使发酵充分,提高发酵效率。 The purpose of this utility model is to provide a drum-type cellulose solid-state fermentation ethanol reactor to overcome the above-mentioned defects of the prior art, which can fully stir the materials, make the fermentation sufficient, and improve the fermentation efficiency.
本实用新型通过以下技术方案实现上述目的:包括外罐体和空套在外罐体内腔中的内罐体,内罐体和外罐体顶部开口处设有密封门,旋转主轴从内罐体和外罐体的底部伸入内罐体内腔中,在内罐体内腔中的旋转主轴上固接多个三角形桨叶,旋转主轴固接内罐体且通过位于外罐体底部的密封的轴承装置与外罐体相接;旋转主轴是中空管状,在内罐体内腔中的旋转主轴上开有多个通气孔;在外罐体外部的旋转主轴上固定套接齿轮盘,齿轮盘连接电机的输出轴;内罐体内腔通过管道连接位于外罐体外部的渗透膜分离装置的输入口,渗透膜分离装置的输出口通过管道连接旋转主轴且与旋转主轴相通。 The utility model achieves the above-mentioned purpose through the following technical solutions: comprising an outer tank body and an inner tank body which is empty in the inner cavity of the outer tank body, a sealed door is arranged at the top opening of the inner tank body and the outer tank body, The bottom of the outer tank extends into the inner cavity of the inner tank, and a plurality of triangular paddles are fixed on the rotating shaft in the inner tank, and the rotating shaft is fixed to the inner tank and passes through a sealed bearing device located at the bottom of the outer tank It is connected with the outer tank; the rotating shaft is hollow and tubular, and there are multiple ventilation holes on the rotating shaft in the inner cavity of the inner tank; a gear plate is fixedly sleeved on the rotating shaft outside the outer tank, and the gear plate is connected to the output of the motor shaft; the inner cavity of the inner tank is connected to the input port of the permeable membrane separation device located outside the outer tank body through a pipeline, and the output port of the permeable membrane separation device is connected to the rotating main shaft through a pipeline and communicated with the rotating main shaft.
本实用新型通过内罐体的转动,发酵罐中的物料利用自重和固定的搅拌桨叶实现发酵物料的充分搅拌,从而提高发酵效率。主轴上有孔便于将酵母和营养液喷淋到内罐体,可以在补充纤维素酶、酵母和营养液时做到无菌操作,杜绝污染。 In the utility model, through the rotation of the inner tank body, the materials in the fermenter can fully stir the fermented materials by their own weight and fixed stirring paddles, thereby improving the fermentation efficiency. There are holes on the main shaft to facilitate the spraying of yeast and nutrient solution to the inner tank, which can achieve aseptic operation when replenishing cellulase, yeast and nutrient solution to prevent pollution.
附图说明 Description of drawings
图1是本实用新型的结构示意图; Fig. 1 is the structural representation of the utility model;
图中:1内罐体;2外罐体;3进料口和废渣出口;4旋转主轴;5三角形桨叶;6通气孔;7轴承装置,8电机;9齿轮盘;10渗透膜分离装置;11管道;12密封门;13检测仪表。 In the figure: 1 inner tank body; 2 outer tank body; 3 feed inlet and waste residue outlet; 4 rotating main shaft; 5 triangular paddle; 6 vent hole; 7 bearing device, 8 motor; ; 11 pipes; 12 sealed doors; 13 detection instruments. the
具体实施方式 Detailed ways
参见图1,本实用新型包括发酵内罐体1和外罐体2,内罐体1空套在外罐体2内腔中,将内罐体1和外罐体2水平放置,为卧式滚筒结构。内罐体1和外罐体2之间为空心夹层,可以通入蒸汽和水,间接进行物料的加热和冷却。内罐体1和外罐体2顶部开口用密封门12密封,在密封门12上设置检测仪表13,检测仪表13为压力传感器、温度传感器等。在内罐体1与外罐体2的顶部开有进料口和废渣出口3。旋转主轴4从内罐体1和外罐体2的底部伸入内罐体1内腔中。在内罐体1内腔中,在旋转主轴4上固定焊接多个三角形桨叶5。旋转主轴4是中空管体形状。在内罐体1内腔中,在旋转主轴4上开有多个通气孔6,通气孔6用于纤维素酶、酵母和营养液的喷淋补充。将旋转主轴4焊接在内罐体1上,并且旋转主轴4通过位于外罐体2底部的密封的轴承装置7与外罐体2相接,这样,就使旋转主轴4和内罐体1同时旋转而外罐体2不旋转。
Referring to Fig. 1, the utility model includes a fermenting inner tank body 1 and an outer tank body 2, the inner tank body 1 is set empty in the inner cavity of the outer tank body 2, and the inner tank body 1 and the outer tank body 2 are placed horizontally to form a horizontal drum structure. There is a hollow interlayer between the inner tank body 1 and the outer tank body 2, through which steam and water can be introduced to indirectly heat and cool materials. The top openings of the inner tank body 1 and the outer tank body 2 are sealed with a
在外罐体2外部的旋转主轴4上固定套接齿轮盘9,齿轮盘9连接电机8的输出轴。内罐体1内腔通过管道11连接位于外罐体2外部的渗透膜分离装置10的输入口,使内罐体1内腔与渗透膜分离装置10相通,渗透膜分离装置10用于分离乙醇和回收纤维素酶、酵母及营养液。渗透膜分离装置10的输出口通过管道11连接旋转主轴4,并且与旋转主轴4中空管体相通。在内罐体1连接磁力塞,用于控制渗透膜分离装置10的开通与闭合。渗透膜分离装置10另外的一个输出口用以连接外部的乙醇收集器。
A gear plate 9 is fixedly sleeved on the rotating
本实用新型使用时,先打开密封门12,投入纤维素固态发酵基质,电机8开始转动,通过齿轮盘9带动旋转主轴4和内罐体1同时转动,物料在内罐体1的转动下利用自身的自重和固定的三角形桨叶5进行搅拌,均匀混合。在搅拌过程中,通过中空管体的旋转主轴4通入纤维素酶、酵母和营养液,对物料进行喷淋,纤维素物料进行同步糖化发酵。通过密封门12上的检测仪表13对发酵过程中的参数进行测量,利用管道11通入蒸汽或冷却水对内罐体1中的物料进行温度调节。纤维素酶解发酵时,可以通过向内、外罐体1、2之间的夹层通入蒸汽对物料进行温度补偿,也可以通入冷却水对物料进行降温。发酵后期通过渗透膜分离装置10分离出乙醇和纤维素酶、酵母及营养液,将纤维素酶、酵母及营养液通过管道11和中空管体的旋转主轴4再次重新输送到内罐体1中,循环使用,这样不仅充分的利用了资源而且还减少对环境的污染,节约成本,提高生产效率。
When the utility model is used, first open the
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| CN201220027108.6U CN202519239U (en) | 2012-01-20 | 2012-01-20 | Roller cellulose solid state fermentation ethanol reactor |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103045461A (en) * | 2013-01-07 | 2013-04-17 | 海南椰国食品有限公司 | Method for continuously producing biological cellulose gel |
| CN103695502A (en) * | 2013-12-13 | 2014-04-02 | 广西丰浩糖业集团有限公司 | Method for preparing sugar from yam starch |
| CN105830805A (en) * | 2016-05-30 | 2016-08-10 | 江苏沃绿宝有机农业开发有限公司 | Vegetable seedling raising substrate screening machine |
-
2012
- 2012-01-20 CN CN201220027108.6U patent/CN202519239U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103045461A (en) * | 2013-01-07 | 2013-04-17 | 海南椰国食品有限公司 | Method for continuously producing biological cellulose gel |
| CN103045461B (en) * | 2013-01-07 | 2014-07-16 | 海南椰国食品有限公司 | Method for continuously producing biological cellulose gel |
| CN103695502A (en) * | 2013-12-13 | 2014-04-02 | 广西丰浩糖业集团有限公司 | Method for preparing sugar from yam starch |
| CN103695502B (en) * | 2013-12-13 | 2016-06-29 | 广西丰浩糖业集团有限公司 | A kind of Rhizoma Dioscoreae starch method for manufacturing sugar |
| CN105830805A (en) * | 2016-05-30 | 2016-08-10 | 江苏沃绿宝有机农业开发有限公司 | Vegetable seedling raising substrate screening machine |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121107 Termination date: 20150120 |
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| EXPY | Termination of patent right or utility model |
