CN204293986U - A kind of threonine fermentation liquid pretreatment system - Google Patents
A kind of threonine fermentation liquid pretreatment system Download PDFInfo
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- CN204293986U CN204293986U CN201420703432.4U CN201420703432U CN204293986U CN 204293986 U CN204293986 U CN 204293986U CN 201420703432 U CN201420703432 U CN 201420703432U CN 204293986 U CN204293986 U CN 204293986U
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- 239000007788 liquid Substances 0.000 title claims abstract description 67
- 238000000855 fermentation Methods 0.000 title claims abstract description 41
- 230000004151 fermentation Effects 0.000 title claims abstract description 41
- AYFVYJQAPQTCCC-UHFFFAOYSA-N Threonine Natural products CC(O)C(N)C(O)=O AYFVYJQAPQTCCC-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 239000004473 Threonine Substances 0.000 title claims abstract description 19
- 241000894006 Bacteria Species 0.000 claims abstract description 19
- 239000002893 slag Substances 0.000 claims abstract description 17
- 238000003860 storage Methods 0.000 claims abstract description 16
- 239000012530 fluid Substances 0.000 claims abstract 5
- 238000007599 discharging Methods 0.000 claims description 2
- 238000004064 recycling Methods 0.000 abstract description 3
- 230000002538 fungal effect Effects 0.000 description 10
- 238000001914 filtration Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 241000233866 Fungi Species 0.000 description 6
- 239000000919 ceramic Substances 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 108090000862 Ion Channels Proteins 0.000 description 1
- 102000004310 Ion Channels Human genes 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Treatment Of Sludge (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及发酵液预处理装置,具体说的是一种苏氨酸发酵液预处理系统。 The utility model relates to a fermentation liquid pretreatment device, in particular to a threonine fermentation liquid pretreatment system.
背景技术 Background technique
苏氨酸发酵液在进行陶瓷膜过滤时,苏氨酸发酵液内含有一种玉米浆水解液产生的丝絮状物,极易堵塞陶瓷膜过滤器、及膜通道的,造成陶瓷膜运行压力过高,过滤效率降低,生产能力达不到设计要求,需要停止过滤设备,对过滤设备进行清洗再生,甚者还需要拆出陶瓷膜元件进行人工清理。浪费了大量的清洗药品及人力,影响物料正常运行。 When the threonine fermentation broth is filtered by ceramic membrane, the threonine fermentation broth contains silk flocs produced by corn steep liquor hydrolyzate, which can easily block the ceramic membrane filter and membrane channels, resulting in the operating pressure of the ceramic membrane. If it is too high, the filtration efficiency will be reduced, and the production capacity will not meet the design requirements. It is necessary to stop the filtration equipment, clean and regenerate the filtration equipment, or even remove the ceramic membrane element for manual cleaning. A lot of cleaning chemicals and manpower are wasted, which affects the normal operation of materials.
苏氨酸菌渣原有处理工艺在处理过程中使用8吨四效降膜蒸发器浓缩,原处理设备占地面积较大,投资高,需浪费大量的生蒸汽、电力,造成生产成本高。且需要排放大量污水及废气,污染环境。 The original treatment process of threonine bacterial residue uses an 8-ton four-effect falling film evaporator to concentrate during the treatment process. The original treatment equipment occupies a large area and requires high investment. It needs to waste a lot of raw steam and electricity, resulting in high production costs. And it needs to discharge a large amount of sewage and waste gas, polluting the environment.
实用新型内容 Utility model content
本实用新型为解决上述技术问题,提供一种苏氨酸发酵液预处理系统,对苏氨酸发酵液进行筛分,保证苏氨酸发酵液的丝絮状物被分离出去,同时利用菌渣处理装置进行二次过滤,对滤渣回收再利用。 In order to solve the above-mentioned technical problems, the utility model provides a threonine fermentation liquid pretreatment system, which screens the threonine fermentation liquid to ensure that the silk flocs of the threonine fermentation liquid are separated, and at the same time utilizes the bacteria residue The processing device performs secondary filtration and recycles the filter residue for reuse.
为实现上述技术目的,所采取的技术方案是:一种苏氨酸发酵液预处理系统,由预处理装置和菌渣处理装置组成,所述的菌渣处理装置由竖直设置的菌渣罐、菌渣泵、多台板框压滤机、清液中转罐、清液泵和袋式过滤器组成, 所述的预处理装置由发酵罐、下料泵、压力曲筛、筛上物中转箱、袋式滤网和发酵液储罐组成,发酵罐的出料口连接下料泵,下料泵通过下料管道与压力曲筛连接,压力曲筛的筛下部分通过管道与发酵储液罐连通,压力曲筛的筛上部分通过管道与筛上物中转箱连接,在筛上物中转箱内设有袋式滤网,筛上物中转箱通过管道与发酵储液罐连通,发酵储液罐通过管道与菌渣罐连接,菌渣罐与每台板框压滤机连接的管道上均设有菌渣泵,每台板框压滤机的出液管与清液中转罐连通,清液中转罐通过清液泵与袋式过滤器连接。 In order to achieve the above technical purpose, the technical solution adopted is: a threonine fermentation liquid pretreatment system, which is composed of a pretreatment device and a fungal residue treatment device, and the fungal residue treatment device is composed of a vertically arranged fungal residue tank , bacteria residue pump, multiple plate and frame filter presses, clear liquid transfer tank, clear liquid pump and bag filter. Box, bag filter and fermentation liquid storage tank, the discharge port of the fermentation tank is connected to the feeding pump, the feeding pump is connected to the pressure curved screen through the feeding pipeline, and the under-screen part of the pressure curved screen is connected to the fermentation storage liquid through the pipeline The tank is connected, the oversize part of the pressure curved sieve is connected with the oversize transfer box through a pipeline, and a bag filter is arranged in the oversize transfer box, and the oversize transfer box is connected with the fermentation liquid storage tank through a pipeline, and the fermentation storage The liquid tank is connected to the fungal residue tank through pipelines, and the fungal residue pump is installed on the pipeline connecting the fungal residue tank and each plate and frame filter press, and the liquid outlet pipe of each plate and frame filter press is connected to the clear liquid transfer tank. The clear liquid transfer tank is connected with the bag filter through the clear liquid pump.
本实用新型有益效果: Beneficial effects of the utility model:
1、本预处理装置利用压力曲筛进行一级分离,再通过中转箱进行二次分离,保证苏氨酸发酵内的丝絮状物被完全分离。 1. This pretreatment device uses a pressure curved sieve for primary separation, and then performs secondary separation through a transfer box to ensure that the silk flocs in the threonine fermentation are completely separated.
2、菌渣罐出料泵与板框通过管道相连,经管道进入板框,板框滤液流至清液中转罐经清液中转泵通过管道进入清液储罐,清液通过袋式过滤器过滤进入下一工序进行回收,其产生的滤饼成型,可直接出售。苏氨酸菌渣处理装置工艺在处理过程不使用蒸汽,电力消耗低,占地面积小。不产生污水和废气,处理效率高,节约成本,提高了处理效率。并且可以回收菌渣中包含的一部分苏氨酸,增加了经济效益。 2. The discharge pump of the bacteria residue tank is connected to the plate frame through the pipeline, and enters the plate frame through the pipeline, and the plate and frame filtrate flows to the clear liquid transfer tank through the clear liquid transfer pump and enters the clear liquid storage tank through the pipeline, and the clear liquid passes through the bag filter Filtration enters the next process for recycling, and the resulting filter cake is shaped and can be sold directly. The threonine bacterial residue treatment device process does not use steam during the treatment process, with low power consumption and small footprint. No sewage and waste gas are produced, the treatment efficiency is high, the cost is saved, and the treatment efficiency is improved. Moreover, a part of threonine contained in the fungus residue can be recovered, thereby increasing economic benefits.
附图说明 Description of drawings
图1为本实用新型的结构示意图; Fig. 1 is the structural representation of the utility model;
图中:1、发酵罐,2、下料泵,3、压力曲筛,4、筛上物中转箱,5、袋式滤网,6、发酵液储罐,7、下料管道,8、出液管,801、搅拌棒,802、搅拌棒,803、搅拌叶片,804、擦板,9、菌渣罐,10、菌渣泵,11、板框压滤机,12、清液中转罐,13、清液泵,14、袋式过滤器。 In the figure: 1. Fermentation tank, 2. Feeding pump, 3. Pressure curved screen, 4. Transfer box for sieve, 5. Bag filter, 6. Fermentation liquid storage tank, 7. Discharging pipeline, 8. Outlet pipe, 801, stirring rod, 802, stirring rod, 803, stirring blade, 804, wiping plate, 9, bacteria residue tank, 10, bacteria residue pump, 11, plate and frame filter press, 12, clear liquid transfer tank , 13, clear liquid pump, 14, bag filter.
具体实施方式 Detailed ways
如图所示,一种苏氨酸发酵液预处理系统,由预处理装置和菌渣处理装置组成,所述的菌渣处理装置由竖直设置的菌渣罐9、菌渣泵10、多台板框压滤机11、清液中转罐12、清液泵13和袋式过滤器14组成, 所述的预处理装置由发酵罐1、下料泵2、压力曲筛3、筛上物中转箱4、袋式滤网5和发酵液储罐6组成,发酵罐1的出料口连接下料泵2,下料泵2通过下料管道7与压力曲筛3连接,压力曲筛3的筛下部分通过管道与发酵储液罐6连通,压力曲筛3的筛上部分通过管道与筛上物中转箱4连接,在筛上物中转箱4内设有袋式滤网5,筛上物中转箱4通过管道与发酵储液罐6连通,发酵储液罐6通过管道与菌渣罐9连接,菌渣罐9与每台板框压滤机11连接的管道上均设有菌渣泵10,每台板框压滤机11的出液管与清液中转罐12连通,清液中转罐12通过清液泵13与袋式过滤器14连接。 As shown in the figure, a threonine fermentation liquid pretreatment system is composed of a pretreatment device and a fungus residue treatment device. The fungus residue treatment device is composed of a vertically arranged fungal residue tank 9, a fungal residue pump 10, multiple A platen frame filter press 11, a clear liquid transfer tank 12, a clear liquid pump 13 and a bag filter 14 are composed, and the pretreatment device is composed of a fermenter 1, a feed pump 2, a pressure curved sieve 3, and an oversize The transfer box 4, the bag filter 5 and the fermentation liquid storage tank 6 are composed. The discharge port of the fermentation tank 1 is connected to the feeding pump 2, and the feeding pump 2 is connected to the pressure curved screen 3 through the feeding pipeline 7, and the pressure curved screen 3 The under-sieve part of the sieve is communicated with the fermentation liquid storage tank 6 through a pipeline, and the over-sieve part of the pressure curved sieve 3 is connected with the oversize transfer box 4 through a pipeline, and a bag filter 5 is arranged in the oversize transfer box 4, and the sieve The upper material transfer box 4 is communicated with the fermentation liquid storage tank 6 through a pipeline, and the fermentation liquid storage tank 6 is connected with the fungus residue tank 9 through a pipeline, and the pipeline connecting the bacteria residue tank 9 and each plate and frame filter press 11 is provided with bacteria The slag pump 10 and the outlet pipe of each plate and frame filter press 11 are connected to the clear liquid transfer tank 12 , and the clear liquid transfer tank 12 is connected to the bag filter 14 through the clear liquid pump 13 .
所述的擦板可设置多个,对出料口位置进行擦拭,防止发酵液在发酵罐出料口处造成堵塞。 A plurality of wipers can be provided to wipe the position of the discharge port to prevent the fermentation liquid from clogging the discharge port of the fermenter.
将发酵罐内注入未处理的苏氨酸发酵液,发酵液由下料泵持续输入压力曲筛,压力曲筛将发酵液分为筛上液和筛下液,筛下液达到过滤标准送入发酵液储罐,上层的筛上液通管道再次输送入中转箱,由中转箱中的袋式滤网进行过滤,中转箱设有可打开的箱盖,可将袋式滤网取出清洗,防止阻塞,同时,可将滤网设置多层,进行多级过滤,滤网的网洞从中转箱进料口至出料口逐渐变小,该种设置可对絮状物完全过滤,同时又不影响发酵液的传输流动,筛上液和筛下液一起混入发酵液储罐进行储存,发酵液储罐内的初级苏氨酸溶液通入菌渣罐中。 Inject the untreated threonine fermentation liquid into the fermenter, and the fermentation liquid is continuously input into the pressure curved sieve by the feeding pump, and the pressure curved sieve divides the fermentation liquid into the upper liquid and the lower liquid, and the lower liquid reaches the filtration standard and is sent into the Fermentation liquid storage tank, the upper sieve liquid pipeline is transported into the transfer box again, and is filtered by the bag filter in the transfer box. The transfer box is equipped with an openable box cover, which can be taken out for cleaning to prevent Blocking, at the same time, the filter can be set in multiple layers to perform multi-stage filtration. The mesh hole of the filter gradually becomes smaller from the inlet to the outlet of the transfer box. This setting can completely filter the flocs without Affect the transmission flow of the fermentation broth, the sieve liquid and the sieve liquid are mixed into the fermentation liquid storage tank for storage, and the primary threonine solution in the fermentation liquid storage tank is passed into the fungus residue tank.
菌渣罐竖直设置将菌渣靠重力作用从排渣口送入菌渣泵,菌渣罐1内的菌渣由菌渣泵送入每台板框压滤机,板框压滤机3将菌渣分为清液和菌渣泥饼,清液由清液中转罐收集,可将清液中转罐分为多级,按从高到低从小到大排列,将菌渣罐及板框压滤机均设置在高处,靠重力作用将清液全部收集,收集完成的清液通过清液泵送入袋式过滤器进行二次过滤,过滤后的清液由出液管送出,送下一工序进行回收。 The slag tank is vertically set, and the slag is sent to the slag pump from the slag outlet by gravity. The slag in the slag tank 1 is sent to each plate and frame filter press by the slag pump, and the plate and frame filter press 3 The fungus residue is divided into clear liquid and fungal mud cake, and the clear liquid is collected by the clear liquid transfer tank. The clear liquid transfer tank can be divided into multiple levels, arranged from high to low, small to large, and the fungal residue tank and plate frame The filter presses are all installed at high places, and all the clear liquid is collected by gravity, and the collected clear liquid is pumped into the bag filter for secondary filtration through the clear liquid pump, and the filtered clear liquid is sent out through the liquid outlet pipe, sent to Recycling is carried out in the next process.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420703432.4U CN204293986U (en) | 2014-11-21 | 2014-11-21 | A kind of threonine fermentation liquid pretreatment system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420703432.4U CN204293986U (en) | 2014-11-21 | 2014-11-21 | A kind of threonine fermentation liquid pretreatment system |
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| Publication Number | Publication Date |
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| CN204293986U true CN204293986U (en) | 2015-04-29 |
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| CN201420703432.4U Expired - Lifetime CN204293986U (en) | 2014-11-21 | 2014-11-21 | A kind of threonine fermentation liquid pretreatment system |
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2014
- 2014-11-21 CN CN201420703432.4U patent/CN204293986U/en not_active Expired - Lifetime
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