CN205088225U - Liquid fermentation , distillation and experimental fermentation system of measurement integration - Google Patents
Liquid fermentation , distillation and experimental fermentation system of measurement integration Download PDFInfo
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- CN205088225U CN205088225U CN201520807722.8U CN201520807722U CN205088225U CN 205088225 U CN205088225 U CN 205088225U CN 201520807722 U CN201520807722 U CN 201520807722U CN 205088225 U CN205088225 U CN 205088225U
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Abstract
The utility model provides a liquid fermentation, distillation and experimental fermentation system of measurement integration, including fermentation cylinder, automatic temperature control device and online metering device, online metering device includes level gauge and metering tank, the level gauge sets up on the fermentation cylinder, the metering tank passes through distillage discharging pipe and fermentation cylinder intercommunication. The utility model discloses a temperature of experimental fermentation system in can accurate controlled reaction jar, product quality has been guaranteed to the volume of measuring raw material consumption, product yield fast, has reduced the intermediate material loss, has reduced workman intensity of labour.
Description
Technical field
The utility model relates to a kind of fermentation engineering equipment, is specifically related to a kind of liquid fermenting, distillation and metering integrated test fermentation system.
Background technology
Fermentation technique occupies very consequence in China's drinks is produced, and fermentor tank is widely used in the industries such as milk-product, beverage, biotechnology, pharmacy, fine chemistry industry.In biomass to alcohol conversion process, the control of temperature is the important step of fermentation, and temperature controlled quality directly has influence on the efficiency of fermentation and the quality of fermentation, but the most temperature-control performance of current fermentor tank is poor.Need by the alcohol distillation in fermented liquid out after fermentation ends, in order to the data such as grain consumption, starch utilization ratio in accurate calculation alcohol production process, need to ensure that the yield of alcohol in still-process is to reduce error, but there is loss of material by fermentor tank to middle conveying processes such as distillation towers at product, corresponding error can be produced when calculating the data such as grain consumption, starch utilization ratio.
Utility model patent ZL201320855613.4 discloses a kind of solid-state vertical type fermentation, self-circulation cooling, distillation integrated apparatus.This device comprises solid-state vertical digester, washing tower, washing pump, gas holder, recycle gas water cooler, recirculation blower, strainer, distillage water cooler, solid-state vertical digester by tank body, be arranged on whipping appts, drawing mechanism, opening for feed, distillage discharge nozzle, biochemical reaction pneumatic outlet, manhole at the bottom of tank, go out claw, distillation steam-in, recycle gas cooling air inlet form.This device adopts the solid-state vertical digester of high fill-ratio, achieve self-emptying, production efficiency is high, be applicable to anaerobic and aerobic solid state fermentation simultaneously, when fermentation ends, for need distillation material, this equipment can be utilized to distill, decrease while decreasing material handling distillage volatilize in transit produce loss.Its application direction is solid state fermentation, is not suitable for liquid submerged fermentation, and has the following disadvantages: do not configure metering system accurately in fermentor tank, and products obtained therefrom cannot measure; Be not equipped with temperature control system accurately, temperature controls inaccurate.
Utility model content
The technical problems to be solved in the utility model is, for the deficiencies in the prior art, provide one can quick metering raw material consumption amount, product yield, temperature precise control, reduce intermediate material loss, reduce the liquid fermenting of labor strength, distillation and metering integrated test fermentation system.
For achieving the above object, the technical scheme that the utility model is taked is:
A kind of liquid fermenting, distillation and metering integrated test fermentation system, comprise fermentor tank, also comprise thermostat and on-line metering device, described on-line metering device comprises liquidometer and test tank, described liquidometer is arranged on fermentor tank, and described test tank is communicated with fermentor tank by distillage discharge nozzle.
Preferably, described fermentor tank comprises tank body, stirring mechanism and baffle, described stirring mechanism is arranged in tank body, described baffle is arranged on tank body medial surface, described tank body top is provided with dog-house, visor and culture transferring pipeline, described tank base is provided with discharge port and steam inlet, described tank body outside is provided with chuck, described chuck side is provided with chuck circulating line, described chuck circulating line sets gradually jacket steam inlet pipe, 3rd valve, 4th valve and jacket steam go out pipe, described jacket steam inlet pipe arranges the first valve, described jacket steam goes out on pipe to arrange the second valve, described thermostat is arranged between the 3rd valve and the 4th valve.
Preferably, the height of described tank body and diameter are than being 1:1 ~ 1.5:1.
Preferably, described stirring mechanism comprises agitator motor, stir shaft and support, and stir shaft arranges stirring rake, described agitator motor is arranged on tank body top, described stir shaft one end is connected with agitator motor, and the other end is connected with support, and described support is fixed on tank base.
Preferably, described stirring rake length and tank body radius ratio are 0.6:1 ~ 0.8:1, and described stirring rake is 2 groups, and the angle of described stirring rake and stir shaft is 60 degree or 120 degree.
Preferably, described thermostat comprises temperature sensor, PLC and well heater, described temperature sensor is arranged on tank body, described heater inlet end is provided with thermostat(t)ed water from top to bottom successively and goes out pipe, the 5th valve and thermostat(t)ed water inlet pipe, described thermostat(t)ed water goes out pipe and is provided with the 6th valve, described thermostat(t)ed water inlet pipe is provided with the 7th valve, described heater outlet end is provided with recycle pump, and described temperature sensor, well heater, recycle pump, the 5th valve, the 6th valve are connected with PLC respectively with the 7th valve.
Preferably, described liquid fermenting, distillation and metering integrated test fermentation system also comprise CIP washing unit, CIP washing unit is connected with fermentor tank, described CIP washing unit comprises scavenging pump and CIP cleans shower nozzle, described scavenging pump and CIP clean shower nozzle and are connected, and described CIP cleans shower nozzle and is arranged in fermentor tank.
Preferably, described distillage discharge nozzle is provided with distillage water cooler.
The beneficial effects of the utility model:
The utility model adopts thermostat to control the temperature in chuck, guarantee that temperature-stable in fermentor tank is in set(ting)value, avoids the impact of human factor, more accurate to the control of temperature, ensure that efficiency and the quality of fermentation, reduce the labour intensity of workman; Adopt on-line metering device, can the changing conditions of material liquid volume in monitor fermentation process constantly, after fermentation ends, product-collecting, in test tank, can calculate the evaluation index such as grain consumption, starch utilization ratio of process of the test by product-collecting amount, charging capacity and raw starch content.
A kind of liquid fermenting of the present utility model, distillation and metering integrated test fermentation system accurately can control the temperature in retort, quick metering raw material consumption amount, product yield, ensure that quality product, decrease intermediate material loss, reduce labor strength.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment 1.
Fig. 2 is the structural representation of the utility model embodiment 2.
In figure: 1-tank body, 2-agitator motor, 3-stir shaft, 4-stirring rake, 5-support, 6-dog-house, 7-liquidometer, 8-chuck, 9-baffle, 10-discharge port, 11-steam inlet, 12-scavenging pump, 13-CIP cleans shower nozzle, 14-visor, 15-culture transferring pipeline, 16-distillage discharge nozzle, 17-distillage water cooler, 18-test tank, 19-jacket steam inlet pipe, 20-jacket steam goes out pipe, 21-fermentor tank, 22-temperature sensor, 23-first valve, 24-second valve, 25-the 3rd valve, 26-the 4th valve, 27-thermostat(t)ed water goes out pipe, 28-thermostat(t)ed water inlet pipe, 29-well heater, 30-PLC controller, 31-recycle pump, 32-the 5th valve, 33-the 6th valve, 34-the 7th valve, 35-chuck circulating line.
Embodiment
Below by specific embodiment, the utility model is described further.
Embodiment 1
As shown in Figure 1, a kind of liquid fermenting, distillation and metering integrated test fermentation system, comprise fermentor tank 21, thermostat and on-line metering device.
Fermentor tank 21 comprises tank body 1, stirring mechanism and baffle 9, stirring mechanism is arranged in tank body 1, baffle 9 is arranged on tank body 1 medial surface, tank body 1 top is provided with dog-house 6, visor 14 and culture transferring pipeline 15, discharge port 10 and steam inlet 11 is provided with bottom tank body 1, tank body 1 outside is provided with chuck 8, and the height of tank body 1 and diameter are than being 1:1 ~ 1.5:1.The dispersion effect that baffle 9 can strengthen feed liquid and enter tank steam is set, makes stirring more even.Chuck 8 side is provided with chuck circulating line 35, chuck circulating line 35 is disposed with jacket steam inlet pipe 19, the 3rd valve 25, thermostat, the 4th valve 26 and jacket steam and goes out pipe 20, jacket steam inlet pipe 19 is provided with the first valve 23, and jacket steam goes out on pipe 20 to arrange the second valve 24.Liquefaction, distillation or sterilizing time, open the first valve 23 and the second valve 24, close the 3rd valve 25 and the 4th valve 26, steam enters chuck circulating line 35 by jacket steam inlet pipe 19, enters chuck 8 subsequently, goes out pipe 20 discharge after circulation from jacket steam.
Stirring mechanism comprises agitator motor 2, stir shaft 3 and support 5, and stir shaft 3 arranges stirring rake 4, and agitator motor 2 is arranged on tank body 1 top, and stir shaft 3 one end is connected with agitator motor 2, and the other end is connected with support 5, and support 5 is fixed on bottom tank body 1.Stirring rake 4 length and tank body 1 radius ratio are 0.6:1 ~ 0.8:1, and stirring rake is 2 groups, and stirring rake 4 is 60 degree or 120 degree with the angle of stir shaft 3.
Thermostat comprises temperature sensor 22, PLC 30 and well heater 29, temperature sensor 22 is arranged on tank body 1, well heater 29 entrance end is provided with thermostat(t)ed water from top to bottom successively and goes out pipe 27, the 5th valve 32 and thermostat(t)ed water inlet pipe 28, thermostat(t)ed water goes out pipe 27 and is provided with the 6th valve 33, thermostat(t)ed water inlet pipe 28 is provided with the 7th valve 34, well heater 29 exit end is provided with recycle pump 31, and temperature sensor 22, well heater 29, recycle pump 31, the 5th valve 32, the 6th valve 33 are connected with PLC 30 respectively with the 7th valve 34.During fermentation temperature control, close the first valve 23 and the second valve 24, open the 3rd valve 25, the 4th valve 26, open thermostat.When fermentation jar temperature is higher than design temperature, signal is passed to PLC 30 by temperature sensor 22, PLC 30 controls the 6th valve 33 and the 7th valve 34 is opened, 5th valve 32 is closed, thermostat(t)ed water enters chuck circulating line 35 by thermostat(t)ed water inlet pipe 28, enter chuck 8 subsequently, go out pipe 27 from thermostat(t)ed water after circulation and discharge, reduce fermentation jar temperature; When fermentation jar temperature is lower than design temperature, signal is passed to PLC 30 by temperature sensor 22, PLC 30 controls the 6th valve 33 and the 7th valve 34 is closed, 5th valve 32 is opened, well heater 29 and recycle pump 31 start, water circulates between chuck 8 and well heater 29, raises fermentation jar temperature.Thermostat according to the switch of the automatic temperature control valve door of water in chuck 8, can regulate inlet and the output of water, guarantees that temperature-stable is in set(ting)value.
On-line metering device comprises liquidometer 7 and test tank 18, and liquidometer 7 is arranged on fermentor tank 21, and test tank 18 is communicated with fermentor tank 21 by distillage discharge nozzle 16, distillage discharge nozzle 16 is provided with distillage water cooler 17.Liquidometer 7 can record the changing conditions of material liquid volume in fermenting process constantly, to fermentation ends, steam is passed in chuck 8, distillage water cooler 17 passes into refrigerant, can the crude alcohol steamed be collected in test tank 18, decrease while decreasing material handling distillage volatilize in transit produce loss.The evaluation index such as grain consumption, starch utilization ratio of process of the test can be calculated by the amount of crude alcohol, charging capacity and raw starch content.
Working process: raw material drops in fermentor tank 21 through dog-house 6, add water, after startup tank deck stirring mechanism stirs, steam inlet 11 passes into steam, be warming up to design temperature 86 DEG C of liquefaction reactions, after timing 2h, open thermostat, chuck 8 passes into thermostat(t)ed water cooling, be cooled to design temperature 32 DEG C, cultured distiller's yeast is pressed in fermentor tank 21 through culture transferring pipeline 15, sealing and fermenting after cultivation 3h, liquidometer 7 can record the changing conditions of material liquid volume in fermenting process constantly, to fermentation ends, vapor distillation is passed in chuck 8, distillage water cooler 17 passes into refrigerant, can the crude alcohol steamed be collected in test tank 18, by the amount of crude alcohol, charging capacity and raw starch content can calculate the grain consumption of process of the test, the evaluation indexes such as starch utilization ratio.
Embodiment 2
As shown in Figure 2, a kind of liquid fermenting, distillation and metering integrated test fermentation system, substantially the same manner as Example 1, difference is: also comprise CIP washing unit in the present embodiment, CIP washing unit is connected with fermentor tank 21, CIP washing unit comprises scavenging pump 12 and CIP cleans shower nozzle 13, and scavenging pump 12 and CIP clean shower nozzle 13 and be connected, and CIP cleans shower nozzle 13 and is arranged in fermentor tank 21.When needing cleaning, sterilizing, utilize scavenging pump 12 pairs of scavenging solutions (alkali lye, disinfectant etc.) to pressurize, high-pressure cleaning liquid cleans shower nozzle 13 from CIP and is sprayed onto that fermentor tank 21 internal surface carries out cleaning, sterilizing, and this purging method need not be taken apart or mobile equipment, decrease labour intensity, improve efficiency.
Test fermentation system temperature of the present utility model controls more accurate, and quick metering raw material consumption amount, product yield, ensure that the efficiency of fermentation and the quality of product, decrease intermediate material loss, reduce labor strength.
Claims (8)
1. a liquid fermenting, distillation and metering integrated test fermentation system, comprise fermentor tank, it is characterized in that: also comprise thermostat and on-line metering device, described on-line metering device comprises liquidometer and test tank, described liquidometer is arranged on fermentor tank, and described test tank is communicated with fermentor tank by distillage discharge nozzle.
2. a kind of liquid fermenting according to claim 1, distillation and metering integrated test fermentation system, it is characterized in that: described fermentor tank comprises tank body, stirring mechanism and baffle, described stirring mechanism is arranged in tank body, described baffle is arranged on tank body medial surface, described tank body top is provided with dog-house, visor and culture transferring pipeline, described tank base is provided with discharge port and steam inlet, described tank body outside is provided with chuck, described chuck side is provided with chuck circulating line, described chuck circulating line sets gradually jacket steam inlet pipe, 3rd valve, 4th valve and jacket steam go out pipe, described jacket steam inlet pipe arranges the first valve, described jacket steam goes out on pipe to arrange the second valve, described thermostat is arranged between the 3rd valve and the 4th valve.
3. a kind of liquid fermenting according to claim 2, distillation and metering integrated test fermentation system, is characterized in that: the height of described tank body and diameter are than being 1:1 ~ 1.5:1.
4. a kind of liquid fermenting according to claim 2, distillation and metering integrated test fermentation system, it is characterized in that: described stirring mechanism comprises agitator motor, stir shaft and support, stir shaft arranges stirring rake, described agitator motor is arranged on tank body top, described stir shaft one end is connected with agitator motor, the other end is connected with support, and described support is fixed on tank base.
5. a kind of liquid fermenting according to claim 4, distillation and metering integrated test fermentation system, it is characterized in that: described stirring rake length and tank body radius ratio are 0.6:1 ~ 0.8:1, described stirring rake is 2 groups, and the angle of described stirring rake and stir shaft is 60 degree or 120 degree.
6. a kind of liquid fermenting according to claim 1 and 2, distillation and metering integrated test fermentation system, it is characterized in that: described thermostat comprises temperature sensor, PLC and well heater, described temperature sensor is arranged on tank body, described heater inlet end is provided with thermostat(t)ed water from top to bottom successively and goes out pipe, 5th valve and thermostat(t)ed water inlet pipe, described thermostat(t)ed water goes out pipe and is provided with the 6th valve, described thermostat(t)ed water inlet pipe is provided with the 7th valve, described heater outlet end is provided with recycle pump, described temperature sensor, well heater, recycle pump, 5th valve, 6th valve is connected with PLC respectively with the 7th valve.
7. a kind of liquid fermenting according to claim 1, distillation and metering integrated test fermentation system, it is characterized in that: also comprise CIP washing unit, CIP washing unit is connected with fermentor tank, described CIP washing unit comprises scavenging pump and CIP cleans shower nozzle, described scavenging pump and CIP clean shower nozzle and are connected, and described CIP cleans shower nozzle and is arranged in fermentor tank.
8. a kind of liquid fermenting according to claim 1, distillation and metering integrated test fermentation system, is characterized in that: described distillage discharge nozzle is provided with distillage water cooler.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520807722.8U CN205088225U (en) | 2015-10-19 | 2015-10-19 | Liquid fermentation , distillation and experimental fermentation system of measurement integration |
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| CN201520807722.8U CN205088225U (en) | 2015-10-19 | 2015-10-19 | Liquid fermentation , distillation and experimental fermentation system of measurement integration |
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| CN205088225U true CN205088225U (en) | 2016-03-16 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107674797A (en) * | 2017-11-18 | 2018-02-09 | 干鑫驰 | A kind of Craft Beer high-efficiency fermenting equipment |
| CN107988000A (en) * | 2017-12-28 | 2018-05-04 | 中粮长城葡萄酒（烟台）有限公司 | A kind of pressure-bearing type sparkling wine fermentation tank |
| CN110684664A (en) * | 2019-12-02 | 2020-01-14 | 邯郸市正德节能环保有限公司 | Biological bacterium culture method |
-
2015
- 2015-10-19 CN CN201520807722.8U patent/CN205088225U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107674797A (en) * | 2017-11-18 | 2018-02-09 | 干鑫驰 | A kind of Craft Beer high-efficiency fermenting equipment |
| CN107988000A (en) * | 2017-12-28 | 2018-05-04 | 中粮长城葡萄酒（烟台）有限公司 | A kind of pressure-bearing type sparkling wine fermentation tank |
| CN107988000B (en) * | 2017-12-28 | 2021-06-22 | 中粮长城葡萄酒（烟台）有限公司 | Pressure-bearing type foaming wine fermentation tank |
| CN110684664A (en) * | 2019-12-02 | 2020-01-14 | 邯郸市正德节能环保有限公司 | Biological bacterium culture method |
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| 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160316 Termination date: 20181019 |