CN204607979U - Semi-continuous type produces the device of Sunmorl N 60S - Google Patents
Semi-continuous type produces the device of Sunmorl N 60S Download PDFInfo
- Publication number
- CN204607979U CN204607979U CN201520202942.8U CN201520202942U CN204607979U CN 204607979 U CN204607979 U CN 204607979U CN 201520202942 U CN201520202942 U CN 201520202942U CN 204607979 U CN204607979 U CN 204607979U
- Authority
- CN
- China
- Prior art keywords
- fermentor tank
- tank
- import
- glucose
- mycelium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Abstract
The utility model belongs to the technical field of fermentative Production Sunmorl N 60S, is specially the device that semi-continuous type produces Sunmorl N 60S.Employing comprises female tank, at least two fermentor tanks and impeller pump, is provided with liquid caustic soda import, glucose import, the import of inoculation bacterium, is provided with fermented liquid outlet in female tank lower end at the top of female tank; Described fermentor tank top is provided with liquid caustic soda import, glucose import, is provided with fermented liquid outlet in fermentor tank lower end; The top of described fermentor tank is also provided with the import of mycelium glucose, and this mycelium glucose import exports with the mycelium glucose of female tank lower end and is connected; The fermented liquid outlet of described female tank lower end and the fermented liquid outlet of fermentor tank lower end all connect the technical scheme of impeller pump to postorder device by pipeline, for the Aspergillus niger glucose sodium saccharate solution of each fermentor tank supply containing high density, shorten the unproductive time of single batch fermentation technique, improve equipment use efficiency, reduce in storage tank the production environment stabilized in fermentor tank.
Description
Technical field
The utility model belongs to the technical field of fermentative Production Sunmorl N 60S, is specially the device that semi-continuous type produces Sunmorl N 60S.
Background technology
Sunmorl N 60S large-scale commercial production generally adopts biological fermentation process, basic production technique is for first to carry out seed culture, cultured seed moves into fermentor tank, control operating parameter well, adopt single batch fermentation method, each fermentor tank isolated operation, single tank puts acid, Problems existing: fermentation period is long, the non-fermented time is long, and plant factor is low.
Utility model content
The purpose of this utility model is to provide a kind of semi-continuous type to produce the device of Sunmorl N 60S for above-mentioned Problems existing.Employing comprises female tank, at least two fermentor tanks and impeller pump, is provided with liquid caustic soda import, glucose import, the import of inoculation bacterium, is provided with fermented liquid outlet in female tank lower end at the top of female tank; Described fermentor tank top is provided with liquid caustic soda import, glucose import, is provided with fermented liquid outlet in fermentor tank lower end; The top of described fermentor tank is also provided with the import of mycelium glucose, and this mycelium glucose import exports with the mycelium glucose of female tank lower end and is connected; The fermented liquid outlet of described female tank lower end and the fermented liquid outlet of fermentor tank lower end all connect the technical scheme of impeller pump to postorder device by pipeline, can be the Aspergillus niger glucose sodium saccharate solution of each fermentor tank supply containing high density, shorten the unproductive time of single batch fermentation technique, improve equipment use efficiency, reduce in storage tank the production environment stabilized in fermentor tank, reduce labor strength.
The technical solution of the utility model is:
Semi-continuous type produces the device of Sunmorl N 60S, comprises female tank, at least two fermentor tanks and impeller pump, is provided with liquid caustic soda import, glucose import, the import of inoculation bacterium, is provided with fermented liquid outlet in female tank lower end at the top of female tank; Described fermentor tank top is provided with liquid caustic soda import, glucose import, is provided with fermented liquid outlet in fermentor tank lower end; It is characterized in that, the top of described fermentor tank is also provided with the import of mycelium glucose, and this mycelium glucose import exports with the mycelium glucose of female tank lower end and is connected; The fermented liquid outlet of described female tank lower end and the fermented liquid outlet of fermentor tank lower end all connect impeller pump to postorder device by pipeline.
Feature of the present utility model also has:
Described female tank is two, is female tank A and female tank B.
Described fermentor tank is three, for fermentor tank A, fermentor tank B, fermentor tank C, be arranged in parallel, described fermentor tank A lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank A connects the mycelium glucose import of fermentor tank B and fermentor tank C respectively; Described fermentor tank B lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank B connects the mycelium glucose import of fermentor tank C.
Described fermentor tank is four, for fermentor tank A, fermentor tank B, fermentor tank C, fermentor tank D, be arranged in parallel, described fermentor tank A lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank A connects the mycelium glucose import of fermentor tank B respectively, the mycelium glucose import of fermentor tank C and the mycelium glucose import of fermentor tank D; Described fermentor tank B lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank B connects the mycelium glucose import of fermentor tank C and the mycelium glucose import of fermentor tank D; Described fermentor tank C lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank C connects the mycelium glucose import of fermentor tank D.
Pipeline between female tank mycelium glucose outlet and the import of fermentor tank mycelium glucose is provided with impeller pump.
Pipeline between the outlet of fermentor tank mycelium glucose and the import of next fermentor tank mycelium glucose is provided with impeller pump.
The beneficial effects of the utility model are:
For fermentor tank provides continuously, fermentation is required contains mycelium glucose solution to female tank, and fermentor tank utilizes fermentation of Aspergillus niger consumption of glucose, realizes semi-successive cultivation Sunmorl N 60S.First fermentor tank self realizes fermentative production Sunmorl N 60S, also can provide material containing aspergillus niger strain for postorder fermentor tank, after fermentation ends by fermented liquid outlet by centrifugal pumping to finishing operations.
Each female tank, fermentor tank recycle pump are coupled together, wherein one to two female tank, puts into this female tank by cultured seed, first cultivates this female tank, observe the mycelia condition of production, when mycelia sends out fork, detect the residual sugar of this fermentation, detect residual sugar and reach a half, pour this female tank Partial fermentation liquid (containing mycelium glucose liquid glucose) into fermentor tank, in fermentor tank, stream adds glucose, and reach certain tank and hold, fermentor tank operates by processing requirement.Pour the fermented liquid of female tank into other fermentor tank by same way, a female tank can ensure that multiple fermentor tank normally runs simultaneously.
This semi-continuous type is produced after the device of Sunmorl N 60S runs continuously, can be the Aspergillus niger glucose sodium saccharate solution of each fermentor tank supply containing high density, shorten the unproductive time of single batch fermentation technique, improve equipment use efficiency, reduce in storage tank the production environment stabilized in fermentor tank, reduce labor strength.
Save fermentation period: mycelia in other fermentor tank poured into by female tank fermented liquid just can produce acid, when saving single tank, bacterial classification accesses adaptive phase and the production phase of fermentor tank, and the minimizing time is 8-10 hour.
Easy to operate: as long as the strict processing requirement controlling female tank, ensure that the fermentation of female tank is normal, other fermentor tank all normally can produce acid, because mycelia has grown produce acid, the ability of condition of compatibility strengthens, and there is part microbiological contamination problem, also can not affect mycelia normal growth in other tank.
Production serialization: can adapt to increase or reduce the quantity of fermentor tank according to respective condition, ensure there is a tank all the time at blowing is favourable to the operation of each operation below.
Use rear effect comparison as follows:
Fermentor tank 280 cubes 7 covers, full fermentation period is 40 hours, and single tank puts tank volume 230 cubes, and fermented liquid concentration 30% calculates, and every day produces acid 327.47 tons.
Use the same fermentor tank of semi-continuous type: fermentor tank 280 cubes 7 covers, fermentation period is 36 hours (fermented liquid tank switching time 2 h), and single tank puts tank volume 230 cubes, and fermented liquid concentration 30% calculates, every day produces acid 363.86 tons, improves and produces calculation amount 11.11%.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment 1,
Wherein, the female tank of 1-, the import of 2-glucose, the import of 3-liquid caustic soda, 4-inoculates bacterium import, the import of 5-mycelium glucose, 6-fermentor tank A, 7-fermentor tank B, 8-fermentor tank C, 9-fermentor tank D, 10-impeller pump (E6), 11-impeller pump (E14), 12-impeller pump (E16), 13-impeller pump (E19), 14-impeller pump (E23), 15-fermented liquid exports, and 16-mycelium glucose exports.
Embodiment
Below by specific embodiment, the technical solution of the utility model is described in detail.
embodiment 1
Semi-continuous type produces the device of Sunmorl N 60S, amounting to 2 female tanks 1 is female tank A and female tank B, 4 fermentor tanks are fermentor tank A6, fermentor tank B7, fermentor tank C8, fermentor tank D9,5 impeller pumps are respectively impeller pump (E6) 10, impeller pump (E14) 11, impeller pump (E16) 12, impeller pump (E19) 13, impeller pump (E23) 14.
Be provided with liquid caustic soda import 3, glucose import 2, inoculation bacterium import 4 at the top of female tank 1, be provided with fermented liquid outlet 15 in female tank 1 lower end; Described fermentor tank top is provided with liquid caustic soda import 3, glucose import 2, is provided with fermented liquid outlet 15 in fermentor tank lower end; The top of described fermentor tank is also provided with mycelium glucose import 5, this mycelium glucose import 5 exports 16 with the mycelium glucose of female tank lower end and is connected, and the mycelium glucose outlet 16 of female tank lower end will be added in four fermentor tanks containing mycelial glucose solution respectively by impeller pump (E6) 10 produces Sunmorl N 60S; The fermented liquid outlet 15 of described female tank lower end and the fermented liquid outlet 15 of fermentor tank lower end all connect impeller pump (E23) 14 to postorder device by pipeline.
Described fermentor tank is four, and be fermentor tank A6, fermentor tank B7, fermentor tank C8, fermentor tank D9, be arranged in parallel, the effect of four fermentor tanks utilizes fermentation of Aspergillus niger consumption of glucose, realizes semi-successive cultivation Sunmorl N 60S.
Described fermentor tank A lower end is also provided with mycelium glucose outlet 16, the mycelium glucose outlet 16 of this fermentor tank A connects the mycelium glucose import 5 of respectively fermentor tank B, the mycelium glucose import 5 of fermentor tank C and the mycelium glucose import 5 of fermentor tank D, first fermentor tank A self realizes fermentative production Sunmorl N 60S, also can simultaneously for fermentor tank B, fermentor tank C, fermentor tank D provide the material containing aspergillus niger strain.
The mycelium glucose outlet 16 that described fermentor tank B lower end is also provided with mycelium glucose outlet 16, this fermentor tank B connects the mycelium glucose import 5 of fermentor tank C and the mycelium glucose import 5 of fermentor tank D; Described fermentor tank C lower end is also provided with the mycelium glucose import 5 of the mycelium glucose outlet 16 connection fermentor tank D of mycelium glucose outlet 16, this fermentor tank C.
Pipeline between female tank mycelium glucose outlet and the import of fermentor tank mycelium glucose is provided with impeller pump (E6) 10.
Pipeline between the mycelium glucose outlet 16 and fermentor tank B7 mycelium glucose import 5 of fermentor tank A6 is provided with impeller pump (E14) 11, fermentor tank B, fermentor tank C, fermentor tank D provide material containing aspergillus niger strain.
Pipeline between the mycelium glucose outlet 16 and fermentor tank C8 mycelium glucose import 5 of fermentor tank B7 is provided with impeller pump (E16) 12, fermentor tank C, fermentor tank D provides material containing aspergillus niger strain.
Pipeline between the mycelium glucose outlet 16 and fermentor tank D9 mycelium glucose import 5 of fermentor tank C8 is provided with impeller pump (E19) 13, and fermentor tank D provides the material containing aspergillus niger strain.
Claims (6)
1. semi-continuous type produces the device of Sunmorl N 60S, comprises female tank, at least two fermentor tanks and impeller pump, is provided with liquid caustic soda import, glucose import, the import of inoculation bacterium, is provided with fermented liquid outlet in female tank lower end at the top of female tank; Described fermentor tank top is provided with liquid caustic soda import, glucose import, is provided with fermented liquid outlet in fermentor tank lower end; It is characterized in that, the top of described fermentor tank is also provided with the import of mycelium glucose, and this mycelium glucose import exports with the mycelium glucose of female tank lower end and is connected; The fermented liquid outlet of described female tank lower end and the fermented liquid outlet of fermentor tank lower end all connect impeller pump to postorder device by pipeline.
2. semi-continuous type according to claim 1 produces the device of Sunmorl N 60S, and it is characterized in that, described female tank is two, is female tank A and female tank B.
3. semi-continuous type according to claim 1 produces the device of Sunmorl N 60S, it is characterized in that, described fermentor tank is three, for fermentor tank A, fermentor tank B, fermentor tank C, be arranged in parallel, described fermentor tank A lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank A connects the mycelium glucose import of fermentor tank B and fermentor tank C respectively; Described fermentor tank B lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank B connects the mycelium glucose import of fermentor tank C.
4. semi-continuous type according to claim 1 produces the device of Sunmorl N 60S, it is characterized in that, described fermentor tank is four, for fermentor tank A, fermentor tank B, fermentor tank C, fermentor tank D, be arranged in parallel, described fermentor tank A lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank A connects the mycelium glucose import of fermentor tank B respectively, the mycelium glucose import of fermentor tank C and the mycelium glucose import of fermentor tank D; Described fermentor tank B lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank B connects the mycelium glucose import of fermentor tank C and the mycelium glucose import of fermentor tank D; Described fermentor tank C lower end is also provided with the outlet of mycelium glucose, and the mycelium glucose outlet of this fermentor tank C connects the mycelium glucose import of fermentor tank D.
5. semi-continuous type according to claim 1 produces the device of Sunmorl N 60S, it is characterized in that, the pipeline between female tank mycelium glucose outlet and the import of fermentor tank mycelium glucose is provided with impeller pump.
6. semi-continuous type according to claim 1 produces the device of Sunmorl N 60S, it is characterized in that, the pipeline between the outlet of fermentor tank mycelium glucose and the import of next fermentor tank mycelium glucose is provided with impeller pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520202942.8U CN204607979U (en) | 2015-04-07 | 2015-04-07 | Semi-continuous type produces the device of Sunmorl N 60S |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520202942.8U CN204607979U (en) | 2015-04-07 | 2015-04-07 | Semi-continuous type produces the device of Sunmorl N 60S |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204607979U true CN204607979U (en) | 2015-09-02 |
Family
ID=53960546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520202942.8U Active CN204607979U (en) | 2015-04-07 | 2015-04-07 | Semi-continuous type produces the device of Sunmorl N 60S |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204607979U (en) |
-
2015
- 2015-04-07 CN CN201520202942.8U patent/CN204607979U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104312834B (en) | A kind of preparation method of Sugarcane fruit wine | |
| WO2020042481A1 (en) | Method for continuously culturing aspergillus niger seeds and producing citric acid using same | |
| CN105385713A (en) | Sodium gluconate fermentation method based on cyclic thallus utilization | |
| CN103614428B (en) | A kind of method of fermenting and producing L tryptophans | |
| CN103074401B (en) | Method for producing neomycin sulfate | |
| CN103695315B (en) | A kind of fermentable produces the method for chitin oligosaccharide | |
| CN103146525B (en) | Production method of soft type composite multi-micro-function yeast | |
| CN101880699B (en) | Method for producing chitooligosaccharides by using microbial fermentation | |
| CN108085280A (en) | A kind of method of high density fermentation acetobacter | |
| CN104087624A (en) | Method for producing citric acid by continuous fermentation of Aspergillus niger | |
| CN108203710B (en) | Method for inducing trichoderma reesei to produce cellulase by using pure straw solid material supplementing and material supplementing device used in method | |
| CN103627740A (en) | Microbial cell conversion method for producing 2-keto-D-gluconic acid | |
| CN101104863A (en) | Method for fermenting lysine | |
| CN204607979U (en) | Semi-continuous type produces the device of Sunmorl N 60S | |
| CN105671115A (en) | Method for constructing microorganism co-culture system for producing bacterial cellulose | |
| CN101638674B (en) | Method for manufacturing citric acid by utilizing cane sugar hydrolysate fermentation method | |
| CN101638675B (en) | Method for manufacturing citric acid by cane sugar fermentation method | |
| CN101886108B (en) | Fermentation method of co-production of astaxanthin and Fructooligosaccharide | |
| CN108239602A (en) | A kind of production technology of complex microbial inoculum | |
| CN100537775C (en) | A kind of method of coercing strategy raising hyaluronic acid volume of production of fermentation production with intermittent high pH | |
| CN103966273A (en) | Method for producing DHA through Crypthecodinium cohnii fermentation | |
| CN101974500A (en) | Production method of high-purity and intermediate-temperate alpha-amylase | |
| CN104877918B (en) | A kind of soy molasses spot jade gill fungus fluid nutrient medium and application | |
| CN110129293A (en) | A kind of industrial fermentation extracting method of glucose oxidase | |
| Khongsay et al. | Improvement of continuous ethanol fermentation from sweet sorghum juice by Saccharomyces cerevisiae using stirred tank bioreactor coupling with plug flow bioreactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |