CN203319996U - Fermentation tank - Google Patents
Fermentation tank Download PDFInfo
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- CN203319996U CN203319996U CN2013202537727U CN201320253772U CN203319996U CN 203319996 U CN203319996 U CN 203319996U CN 2013202537727 U CN2013202537727 U CN 2013202537727U CN 201320253772 U CN201320253772 U CN 201320253772U CN 203319996 U CN203319996 U CN 203319996U
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Abstract
The utility model provides a fermentation tank. The fermentation tank comprises a fermentation tank main body, an air pipeline, a material line, a jacket and a steam pipeline, wherein the fermentation tank main body is placed in the jacket, the air pipeline and the material line are communicated with the fermentation tank main body, and the steam pipeline is respectively communicated with the air pipeline and the material line; an air intake valve and the like are connected on the air pipeline in series; an inoculation port, a feeding port, a ventilation opening, a discharging port and an exhaust port are formed in the fermentation tank main body, and a stirring part is arranged inside the fermentation tank main body; the material line is connected with the discharging port and is connected with a material line valve in series; the exhaust port is connected with an exhaust pipe with an exhaust valve; a cooling water entering pipeline and a cooling water drainage pipeline are communicated on the jacket, and valves are arranged on the cooling water entering pipeline and the cooling water drainage pipeline; the jacket is communicated with a circulation water tank, a pipeline communicated with the circulation water tank is communicated with the steam pipeline, and a steam valve is arranged on the steam pipeline; the fermentation tank main body and the jacket are respectively communicated with blow-off pipes. The fermentation tank is reasonable in structure, can be used for ensuring the smooth proceeding of microorganism fermentation and has a good fermentation effect.
Description
Technical field
The utility model relates to zymotechnique, particularly a kind of fermentor tank.
Background technology
Fermentor tank, refer to the industrial device that is used for carrying out the microorganism fermentation.In design and processing, should note vertebration, reasonable.Can tolerate steam sterilizing, have try one's best minimizing, material and transmission ofenergy performance of certain turndown ratio, contents strong, and can necessarily regulate so that clean, reduce pollution, be suitable for production and the energy saving of multiple product.
The utility model content
The utility model purpose is in order to overcome the deficiencies in the prior art, and a kind of fermentor tank is provided, and it can guarantee carrying out smoothly of microorganism fermentation, and ferment effect is good.
In order to achieve the above object, the utility model is by the following technical solutions:
A kind of fermentor tank, comprise fermentor tank main body, airline ,Liao road, chuck and vapour line;
Described fermentor tank main body is put and is installed in chuck, and described airline Ji Liao road is communicated with the fermentor tank main body; Described airline Ji Liao is communicated with respectively vapour line on road;
Be serially connected with material road valve on described material road;
Be serially connected with air intake valve, filtration under diminished pressure valve, prefilter and sterilizing filter on described airline;
Be provided with inoculation mouth, charging opening, ventilation opening, discharge port, venting port on described fermentor tank main body, described fermentor tank body interior is provided with mixing component;
Described discharge port is connected with described material road;
Corresponding mixing component disposes the adjustment switchboard;
Described venting port is arranged on fermentor tank main body top, and described venting port is connected with a vapor pipe, on described vapor pipe, is serially connected with vent valve;
Be communicated with water coolant on described chuck and enter pipeline and water coolant discharge pipeline, described water coolant enters on pipeline and water coolant discharge pipeline and all is provided with valve; Described chuck is communicated with a cyclic water tank, is communicated with the first vapour line on the pipeline of communication loop water tank, and described the first vapour line is communicated with chuck; Be provided with steam valve on described the first vapour line;
Described fermentor tank main body and chuck are communicated with respectively blow-off pipe.
As preferably, also be provided with thief hole on described fermentor tank main body, described thief hole is connected with sampling line, is serially connected with the sampling line valve on described sampling line; Be communicated with the second vapour line on described sampling line.
As preferably, fermentor tank main body capacity is 20L or 200L or 2000L.
Compared with prior art, the utlity model has following beneficial effect:
Fermentor tank described in the utility model is vertebration, rationally; Can tolerate steam sterilizing, certain turndown ratio is arranged, contents is less, material and the transmission ofenergy performance stronger, and be convenient to clean, reduce and pollute, be suitable for production and the energy saving of multiple product.Can guarantee carrying out smoothly of microorganism fermentation, and ferment effect is good.
The accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the butterfly valve that the utility model is applied to;
Fig. 3 is the stopping valve that the utility model is applied to;
Fig. 4 is the diaphragm valve that the utility model is applied to;
Fig. 5 is the check valve that the utility model is applied to;
Fig. 6 is the magnetic valve that the utility model is applied to;
Fig. 7 is the ball valve that the utility model is applied to.
In figure:
1-fermentor tank main body; 11-thief hole; 12-venting port; 2-chuck; 21-cyclic water tank.
Now with specific embodiment, the utility model is described in further detail by reference to the accompanying drawings.
Embodiment
As shown in Figures 1 to 7, be fermentor tank described in the utility model, comprise fermentor tank main body 1, airline ,Liao road, chuck 2 and vapour line.
Fermentor tank main body 1 is put and is installed in chuck 2, and airline Ji Liao road is communicated with fermentor tank main body 1.
Be serially connected with material road valve (material is provided with diaphragm valve and butterfly valve on road) on the material road; Be serially connected with air intake valve, filtration under diminished pressure valve, prefilter and sterilizing filter (being provided with stopping valve and diaphragm valve on airline) on airline.
Airline Ji Liao is communicated with respectively vapour line on road.
Be provided with inoculation mouth, charging opening, ventilation opening, discharge port, venting port 12, thief hole 11 on fermentor tank main body 1, fermentor tank main body 1 inside is provided with mixing component.
Discharge port Yu Liao road connects; Corresponding mixing component disposes the adjustment switchboard.
Be communicated with water coolant on chuck 2 and enter pipeline and water coolant discharge pipeline; Water coolant enters on pipeline and water coolant discharge pipeline all to be provided with valve (cooling water inlet pipe is provided with butterfly valve on road, is provided with butterfly valve and magnetic valve on the cooling water drainage water lines).Chuck 2 is communicated with a cyclic water tank 21, on the pipeline of communication loop water tank 21 (being provided with butterfly valve and check valve on the pipeline of communication loop water tank), is communicated with the first vapour line, and the first vapour line is communicated with chuck 2; Be provided with steam valve (being provided with stopping valve on vapour line) on vapour line.
Fermentor tank main body 1 and chuck 2 are communicated with respectively blow-off pipe (being provided with butterfly valve on blow-off line).
Fermentor tank main body 1 capacity is 20L or 200L or 2000L.Actual application is as follows:
One, sky disappears
Before feeding intake, gas circuit ,Liao road, fermentor tank must carry out sterilizing with steam, eliminate the miscellaneous bacteria at all dead angles, and the assurance system is in sterile state.
1, the sky of airline disappears
(1) before the logical steam of airline, the valve that must will lead to reducing valve shuts, and makes steam first by vapor filter, then enters sterilizing filter.
(2) filter core of sterilizing filter can not bear too high temperature and pressure, and therefore, during sterilizing, vapor pressure remains on 0.13Mpa, must not surpass 0.15Mpa.
(3) during sky disappears process, the vent valve of sterilizing filter lower end should be opened slightly, discharges water of condensation.
(4) the sky time of disappearing should continue about 30 to 40 minutes, when equipment is first when using or for a long time need not rear startuping, preferably adopted intermittent sky to disappear, and after sky disappears for the first time, sky disappears once to suspend 3 to 5 hours again, with the elimination gemma.
(5) strainer of sky after disappearing, should ventilate and approximately within 20 to 30 minutes, dry up, then by the valve closes of gas circuit.
2, fermentor tank main body sky disappears
(1) directly steam is passed in tank and carry out sky and disappear.
(2) when sky disappears, the vent valve Ji Liao Lu Deliao road valve of the inoculation mouth on tank, exhaust line should be opened slightly, be made steam pass through these valves and discharge, keep tank pressure is 0.1Mpa simultaneously, 121 ℃ of temperature.
(3) the sky time of disappearing is 30 to 40 minutes, in particular cases, can adopt intermittently sky to disappear.
(4), when the fermentation ullage disappears, the water in chuck should be bled off.
(5) after sky disappears and finishes, the water of condensation in tank should be drained, and the vent valve of vapor pipe is opened, prevent from causing the tank body negative pressure and damage.
Two, real disappearing
Disappearing in fact is just add substratum in tank after, with steam, substratum is carried out the process of sterilizing.
1, after sky disappears and finishes, should as early as possible the substratum prepared be added in tank from charging opening, now chuck planted agent evaporated condensation water.
2, substratum should first gelatinization before advancing tank, and the formula ratio of general substratum be take 70% left and right of tank body total volume and calculated (substratum that foam is many is 65% left and right, and the substratum that foam is few can reach 75 to 80%), and should be taken into account the factors such as water of condensation and inoculum size.
3, open the steam valve of the first vapour line be communicated with chuck, enter the chuck pre-heating stage; And the unlatching mixing component, be controlled at than the slow speed of revolution; When temperature is raised to 90 ℃ in tank, close the steam valve of the first vapour line, slowly open the internal layer steam valve, then by ventilation opening and discharge port two-way, advance steam, and open the vent valve of tank deck vapor pipe, slowly exhaust.
4, rise to 0.1Mpa when tank pressure, when temperature is raised to 121 ℃, keep tank pressure and temperature sterilizing after 20 to 30 minutes, the vent valve of Xian Guan top exhaust line, then stop steam and enter.
A) open entering and the valve of escape route of water coolant, in chuck water flowing cooling, open air intake valve and vent valve simultaneously, the maintenance tank pressure is 0.08Mpa, until the tank temperature drop is to inoculation temp.
B) the real elimination in bacterium and process of cooling in tank, mixing component should start and turns round and be controlled at lower rotating speed.
Three, inoculation
1, adopt the flame sealing inoculation, inoculation should first be ready to alcohol cotton, pliers, tweezers and transfering loop in advance.
2, in bacterial classification is packed Erlenmeyer flask into, inoculum size is determined according to processing requirement.
3, drain the interior air of tank, the alcohol cotton is trapped among to inoculation mouthful and lights on every side, turn on the lid of inoculation mouth, and ventilate in tank, make mouth that Bas Discharged be arranged, guarantee the interior malleation of tank.
4, the bacterial classification of triangular flask is poured in tank in the middle of fire ring, will be inoculated a mouthful cover cap and be tightened in after sterilizing on flame on the inoculation mouth.
Four, cultivate
1, after seed access fermentor tank, can carry out the temperature control cultivation, the tank pressure general control is at 0.02Mpa to 0.1Mpa.
2, leavening temperature is determined according to processing requirement, by cyclic water tank, carrys out the controlled fermentation temperature.When leavening temperature during below or above technique initialization, but cyclic water tank Automatic-heating or cooling.
3, in substratum, the rotating speed of mixing component is adjusted the speed regulating control plate according to processing requirement, the rotating speed that can not bear over the design of tank body.
4, in culturing process, feed supplement can be carried out with reference to inoculation method.
5, when fermentation will be taken a sample to check midway, can sample by thief hole.Before sampling, the pipe valve of sampling line need be used steam sterilizing, prevents living contaminants and causes misleading, and sampling will be used steam flush sampling line valve after finishing equally.
Five, discharging
1, discharging Cong Liao road discharging.
2, after discharging finishes, should discharge water immediately and clean fermentor tank Ji Liao road (comprising material road valve), and start mixing component, make to clean thoroughly.
The utility model is not limited to above-mentioned embodiment, if various changes of the present utility model or modification are not broken away to spirit and scope of the present utility model, if, within these changes and modification belong to claim of the present utility model and equivalent technologies scope, the utility model also is intended to comprise these changes and change.
Claims (3)
1. a fermentor tank, is characterized in that, comprises fermentor tank main body, airline ,Liao road, chuck and vapour line;
Described fermentor tank main body is put and is installed in chuck, and described airline Ji Liao road is communicated with the fermentor tank main body; Described airline Ji Liao is communicated with respectively vapour line on road;
Be serially connected with material road valve on described material road;
Be serially connected with air intake valve, filtration under diminished pressure valve, prefilter and sterilizing filter on described airline;
Be provided with inoculation mouth, charging opening, ventilation opening, discharge port, venting port on described fermentor tank main body, described fermentor tank body interior is provided with mixing component;
Described discharge port is connected with described material road;
Corresponding mixing component disposes the adjustment switchboard;
Described venting port is arranged on fermentor tank main body top, and described venting port is connected with a vapor pipe, on described vapor pipe, is serially connected with vent valve;
Be communicated with water coolant on described chuck and enter pipeline and water coolant discharge pipeline, described water coolant enters on pipeline and water coolant discharge pipeline and all is provided with valve; Described chuck is communicated with a cyclic water tank, is communicated with the first vapour line on the pipeline of communication loop water tank, and described the first vapour line is communicated with chuck; Be provided with steam valve on described the first vapour line;
Described fermentor tank main body and chuck are communicated with respectively blow-off pipe.
2. fermentor tank according to claim 1, is characterized in that, on described fermentor tank main body, also is provided with thief hole, and described thief hole is connected with sampling line, is serially connected with the sampling line valve on described sampling line; Be communicated with the second vapour line on described sampling line.
3. fermentor tank according to claim 1 and 2, is characterized in that, fermentor tank main body capacity is 20L or 200L or 2000L.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202537727U CN203319996U (en) | 2013-05-10 | 2013-05-10 | Fermentation tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202537727U CN203319996U (en) | 2013-05-10 | 2013-05-10 | Fermentation tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203319996U true CN203319996U (en) | 2013-12-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013202537727U Expired - Fee Related CN203319996U (en) | 2013-05-10 | 2013-05-10 | Fermentation tank |
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103911286A (en) * | 2014-03-27 | 2014-07-09 | 江苏绿扬生物电子工程有限公司 | Sterile charging device of animal cell suspension culture bioreactor |
| CN103937672A (en) * | 2014-03-27 | 2014-07-23 | 江苏绿扬生物电子工程有限公司 | Bioreactor thermostat |
| CN104004622A (en) * | 2014-05-29 | 2014-08-27 | 劳卓昌 | Fruit wine fermentation tank |
| CN104003767A (en) * | 2014-06-11 | 2014-08-27 | 中国科学院城市环境研究所 | Kitchen waste aerobic fermentation equipment with capability of rapid drying |
| CN104531505A (en) * | 2014-12-19 | 2015-04-22 | 宜昌三峡制药有限公司 | Batching and water filling system and method in neomycin sulfate fermentation production |
| CN105505744A (en) * | 2016-01-07 | 2016-04-20 | 盐城市雨露农业科技有限公司 | Liquid strain seed tank and using method thereof |
| CN106434281A (en) * | 2016-10-08 | 2017-02-22 | 江西天祥通用航空股份有限公司 | Pretreatment system used for solid fermentation |
| CN107744693A (en) * | 2017-10-24 | 2018-03-02 | 翔天农业开发集团股份有限公司 | A kind of aseptic filtration method of air in liquid fungus seed |
| CN108939103A (en) * | 2018-08-06 | 2018-12-07 | 江苏丰泽生物工程设备制造有限公司 | A kind of defoaming pipeline totality bactericidal unit and its application method |
| CN109464683A (en) * | 2018-11-21 | 2019-03-15 | 苏建南 | A kind of sterilizing methods for biofermentation |
| CN110747121A (en) * | 2019-10-29 | 2020-02-04 | 刘本德 | Chinese herbal medicine extraction element |
| CN117228819A (en) * | 2023-11-15 | 2023-12-15 | 江苏今石环境有限责任公司 | Heterotrophic nitrification and aerobic denitrification strain in-situ expansion culture system and method |
-
2013
- 2013-05-10 CN CN2013202537727U patent/CN203319996U/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103911286A (en) * | 2014-03-27 | 2014-07-09 | 江苏绿扬生物电子工程有限公司 | Sterile charging device of animal cell suspension culture bioreactor |
| CN103937672A (en) * | 2014-03-27 | 2014-07-23 | 江苏绿扬生物电子工程有限公司 | Bioreactor thermostat |
| CN104004622A (en) * | 2014-05-29 | 2014-08-27 | 劳卓昌 | Fruit wine fermentation tank |
| CN104003767A (en) * | 2014-06-11 | 2014-08-27 | 中国科学院城市环境研究所 | Kitchen waste aerobic fermentation equipment with capability of rapid drying |
| CN104531505A (en) * | 2014-12-19 | 2015-04-22 | 宜昌三峡制药有限公司 | Batching and water filling system and method in neomycin sulfate fermentation production |
| CN104531505B (en) * | 2014-12-19 | 2016-02-24 | 宜昌三峡制药有限公司 | To prepare burden in neomycinsulphate fermentative production water-adding system and method |
| CN105505744A (en) * | 2016-01-07 | 2016-04-20 | 盐城市雨露农业科技有限公司 | Liquid strain seed tank and using method thereof |
| CN106434281A (en) * | 2016-10-08 | 2017-02-22 | 江西天祥通用航空股份有限公司 | Pretreatment system used for solid fermentation |
| CN107744693A (en) * | 2017-10-24 | 2018-03-02 | 翔天农业开发集团股份有限公司 | A kind of aseptic filtration method of air in liquid fungus seed |
| CN107744693B (en) * | 2017-10-24 | 2018-11-20 | 翔天农业开发集团股份有限公司 | A kind of aseptic filtration method of air in liquid fungus seed |
| CN108939103A (en) * | 2018-08-06 | 2018-12-07 | 江苏丰泽生物工程设备制造有限公司 | A kind of defoaming pipeline totality bactericidal unit and its application method |
| CN109464683A (en) * | 2018-11-21 | 2019-03-15 | 苏建南 | A kind of sterilizing methods for biofermentation |
| CN110747121A (en) * | 2019-10-29 | 2020-02-04 | 刘本德 | Chinese herbal medicine extraction element |
| CN117228819A (en) * | 2023-11-15 | 2023-12-15 | 江苏今石环境有限责任公司 | Heterotrophic nitrification and aerobic denitrification strain in-situ expansion culture system and method |
| CN117228819B (en) * | 2023-11-15 | 2024-05-10 | 江苏今石环境有限责任公司 | Heterotrophic nitrification and aerobic denitrification strain in-situ expansion culture system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20131204 Termination date: 20160510 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |