CN206438128U - A kind of device for carrying out heated at constant temperature to fermentation tank using steam waste heat - Google Patents
A kind of device for carrying out heated at constant temperature to fermentation tank using steam waste heat Download PDFInfo
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- CN206438128U CN206438128U CN201720052185.XU CN201720052185U CN206438128U CN 206438128 U CN206438128 U CN 206438128U CN 201720052185 U CN201720052185 U CN 201720052185U CN 206438128 U CN206438128 U CN 206438128U
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- fermentation tank
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Abstract
The utility model is related to a kind of device for carrying out heated at constant temperature to fermentation tank using steam waste heat, belong to fermenting and producing equipment technical field, device includes waste heat steam recovery device, waste heat recovery pipeline, temperature control panel and fermentation tank heater, waste heat steam recovery device is connected by waste heat recovery pipeline with fermentation tank heater, waste heat recovery pipeline is provided with temperature control panel and automatic regulating valve, and automatic regulating valve is connected with temperature control panel；The heater that ferments includes the steam-heating pipe of fermentation tank and fermentation tank interlayer, and steam-heating pipe includes at least two steam inlets.The present apparatus utilizes the waste gas discharged in Starch Production to be heated to fermentation tank, instead of Boiler Steam, and reduction energy consumption saves cost, and temperature control is flexibly constant, it is ensured that fermentation temperature is constant, can also meet the fermentation demand of different microbial inoculums, heats faster evenly.
Description
Technical field
The utility model is related to one kind and fermentation tank progress constant temperature in saccharomyces boulardii fermentation process is added using steam waste heat
The device of heat, belongs to fermenting and producing equipment technical field.
Background technology
Saccharomyces boulardii (Saccharomyces boulardii) is a kind of probiotics yeast bacterium, belongs to the Asia of saccharomyces cerevisiae
Kind, have in terms of suppressing enteric pathogenic bacteria, degraded enterotoxin, improving host immunity and balance intestine microenvironment
Significant advantage.Saccharomyces boulardii is widely used in the medicine for the treatment of diarrhoea, can effectively treat various intestinal inflammatories.Its micro- life
State formulation application effectively reduces the quantity of pathogen and reduces the concentration of its toxin, be conducive to animal health fast in animal husbandry
The growth of speed, has a extensive future in animal husbandry.
Containing abundant nutriment in corn steep liquor, mainly including protein, auxin and some precursor substances etc.,
The nutriments such as nitrogen source, carbon source and inorganic salts can be provided for microbial fermentation.It is industrial at present to be sent out by raw material of corn steep liquor
Ferment produces saccharomyces boulardii.Saccharomyces boulardii has heat resistance, can be grown at a temperature of 37 DEG C.But there are some researches show fermenting
The most suitable fermentation temperature of saccharomyces boulardii is 30 DEG C in journey.
Therefore in practical operation, on the one hand producers should regulate and control Bradley yeast according to production needs by adjusting temperature
The most suitable fermentation temperature of bacterium, on the other hand should try one's best and ensure the constant of saccharomyces boulardii fermentation temperature with stably, improving fermentation water
It is flat, it is ensured that the stability of product quality.
Existing fermentation mode of heating is that fermentation tank is directly heated using Boiler Steam, and temperature is too high then to use recirculated water
Cooling, causes the significant wastage of the energy, and accurately can not quickly control the temperature of fermentation tank.Therefore, a kind of pin of design is needed badly
To the constant temperature heating device of fermentation tank in saccharomyces boulardii fermentation process.
Utility model content
In view of the shortcomings of the prior art, the utility model provides one kind using steam waste heat to saccharomyces boulardii fermentation process
In fermentation tank carry out heated at constant temperature device, temperature can adjust, while can guarantee that the fermentation of saccharomyces boulardii in fermentation process
Temperature is constant, homogeneous.
The technical solution of the utility model is as follows：
A kind of device for carrying out heated at constant temperature to fermentation tank using steam waste heat, including the afterheat steam time in Starch Production
Receiving apparatus, waste heat recovery pipeline, temperature control panel and fermentation tank heater；Waste heat steam recovery device passes through waste heat recovery
Pipeline is connected with fermentation heater, and waste heat recovery pipeline is provided with temperature control panel；
Waste heat steam recovery device includes dry waste gas retracting device, waste gas filter；
Temperature control panel includes temperature adjustment buttons, temperature display；Waste heat recovery pipeline is provided with automatic regulating valve,
Automatic regulating valve is connected with temperature control panel；
Fermentation tank heater includes fermentation tank and the fermentation tank interlayer on the outside of fermentation tank, and fermentation tank is pressed from both sides with fermentation tank
Steam-heating pipe is provided between layer, fermentation tank upper and lower side is respectively equipped with material inlet and material outlet；Steam-heating pipe includes steaming
Vapour air inlet and Crude product input, steam inlet are connected with waste heat recovery pipeline；Fermentation tank is provided with temperature sensor, temperature
Degree sensor is electrically connected with temperature control panel；The quantity of steam inlet and Crude product input is at least two.
Afterheat steam in Starch Production is reclaimed by dry waste gas retracting device, and is filtered out by waste gas filter miscellaneous
Matter, reclaims the afterheat steam of coming, and enters steam-heating pipe by waste heat recovery pipeline, and the roundabout arrangement of steam-heating pipe is centered around hair
In fermentation tank interlayer, zymotic fluid is entered in fermentation tank by material inlet, and temperature control panel is fermented by temperature sensor senses
The fermentation temperature of tank, with the temperature by controlling automatic regulating valve control fermentation, multiple steam inlets make temperature control more fast
Speed is sensitive, shortens response error, each position of the serpentine heating pipe on fermentation tank heater is quickly reached beneficial to steam, together
When make temperature control more uniform.
Preferred according to the utility model, it is additionally provided with pressure gauge on waste heat recovery pipeline.For detecting the pressure in pipeline
Value, causes manifold pressure superfluous to avoid hindering for some reason.
Preferred according to the utility model, the temperature display includes setting temperature value display screen and measurement temperature value is shown
Screen.
It is preferred according to the utility model, the temperature adjustment buttons include temperature setting button, temperature up-regulation button and
Temperature down button.
Preferred according to the utility model, the temprature control unit can adjust temperature in the range of 20~40.00 DEG C.
Preferred according to the utility model, the steam inlet is respectively arranged on the upper and lower ends of fermentation tank, the heating
Media outlet is respectively arranged on the upper and lower ends of fermentation tank.When making afterheat steam into steam-heating pipe, respectively from the upper of fermentation tank
Lower end enters simultaneously is heated, and accordingly, Crude product input also corresponds to the upper and lower side for being distributed in fermentation tank, it is to avoid fermentation tank
The temperature polarization of interior upper and lower side is serious, makes heating faster more uniform.
Preferred according to the utility model, the probe of the temperature sensor is inside fermentation tank.Monitoring fermentation in real time
Broth temperature in tank.
The beneficial effects of the utility model are：
1st, the device described in the utility model for being used in saccharomyces boulardii fermentation process carry out fermentation tank heated at constant temperature, can
By afterheat steam recovery section and temprature control unit, the temperature in control fermentation tank keeps constant, it is ensured that saccharomyces boulardii
In fermentation process, fermentation temperature is constant, improves the accuracy that technological parameter is set in production process.
2nd, the device described in the utility model for being used in saccharomyces boulardii fermentation process carry out fermentation tank heated at constant temperature, can
Needed to adjust fermentation temperature according to production, to meet the fermentation demand of different product.
3rd, the device described in the utility model for being used in saccharomyces boulardii fermentation process carry out fermentation tank heated at constant temperature, is adopted
Heated with the afterheat steam for being used for drying plumule, fiber and albumen powder discharge in Starch Production to fermentation tank, instead of Boiler Steam,
Realize the cascaded utilization of energy in production process.With make full use of steam waste heat, reduction energy consumption, save production cost, avoid
Row causes the excellent effect of environmental pollution outside waste vapour in the prior art.
4th, the technical solution of the utility model is worked simultaneously using multiple steam inlets and Crude product input, makes waste heat
Steam is more quick and is uniformly applied on fermentation tank, it is ensured that different parts in fermentation tank are accomplished with uniform heating, shortens temperature
The time required to control, heating is evenly, it is ensured that fermenting and producing is normally carried out.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model fermentation tank constant temperature heating device；
Wherein：1st, dry waste gas retracting device, 2, waste gas filter, 3, temperature control panel, 4, automatic regulating valve, 5,
Waste heat recovery pipeline, 6, fermentation tank heater, 7, pressure gauge.
Fig. 2 is schematic enlarged-scale view at A in Fig. 1；
Wherein：3-1, temperature setting button, 3-2, temperature up-regulation button, 3-3, temperature down button, 3-4, measurement temperature value
Display screen, 3-5 setting temperature value display screens.
Fig. 3 is the schematic enlarged-scale view of the utility model fermentation tank heater；
Fig. 4 is the fermentation heater knot that the utility model steam inlet, Crude product input set up fermentation tank two ends separately
Structure enlarged drawing；
Wherein：6-1, steam inlet, 6-2, Crude product input, 6-3, material inlet, 6-4, material outlet, 6-5, temperature
Spend sensor, 6-6, steam-heating pipe, 6-7, fermentation tank, 6-8 fermentation tank interlayers.
Embodiment
The utility model is described further below by embodiment and with reference to accompanying drawing, but not limited to this.
As Figure 1-4.
Embodiment 1：
A kind of device for carrying out heated at constant temperature to the fermentation tank in saccharomyces boulardii fermentation process using steam waste heat, including
Waste heat steam recovery device, waste heat recovery pipeline, temperature control panel and fermentation tank heater in Starch Production；Waste heat steams
Recovery device for steam is connected by waste heat recovery pipeline with fermentation tank heater, and waste heat recovery pipeline is provided with temperature control face
Plate；
Waste heat steam recovery device includes dry waste gas retracting device, waste gas filter；
Temperature control panel includes housing, the temperature-control circuit positioned at enclosure interior and the temperature positioned at surface of shell and adjusted
Button, temperature display are saved, temperature-control circuit is used to control the temperature of whole device to set, and temperature adjustment buttons include temperature
Settings button, temperature up-regulation button and temperature down button, temperature display includes setting temperature value display screen and measurement temperature value shows
Display screen；Waste heat recovery pipeline is provided with automatic regulating valve, and automatic regulating valve is connected with temperature control panel；Temperature control panel can
Choose Honeywell (HONEYWELL) temperature controller T9275 and reach temperature controlled purpose.
Fermentation tank heater includes fermentation tank and the fermentation tank interlayer on the outside of fermentation tank, and fermentation tank is pressed from both sides with fermentation tank
Steam-heating pipe is provided between layer, fermentation tank upper and lower side is respectively equipped with material inlet and material outlet；Steam-heating pipe includes steaming
Vapour air inlet and Crude product input, steam inlet are connected with waste heat recovery pipeline；Fermentation tank is provided with temperature sensor, temperature
Degree sensor is electrically connected with temperature control panel；The quantity of steam inlet and Crude product input is two, such as Fig. 1, Fig. 3
It is shown.
Afterheat steam in Starch Production is reclaimed by dry waste gas retracting device, and is filtered out by waste gas filter miscellaneous
Matter, reclaims the afterheat steam of coming, and enters steam-heating pipe by waste heat recovery pipeline, and the roundabout arrangement of steam-heating pipe is centered around hair
In fermentation tank interlayer, zymotic fluid is entered in fermentation tank by material inlet, and heat friendship is carried out by steam-heating pipe and steam waste heat
Change, temperature control panel is by the fermentation temperature of temperature sensor senses fermentation tank, with by controlling automatic regulating valve control hair
The temperature of zymotic fluid, reaches that the zymotic fluid that fermentation is required flows out from material outlet, into next process.Multiple steam inlets make temperature
Control is more rapid sensitive, shortens response error, and serpentine heating pipe on fermentation tank heater is quickly reached beneficial to steam
Each position, while making temperature control more uniform.
The present embodiment when fermentation tank constant temperature heating device works, passes through temperature setting so that fermentation temperature selects 30 DEG C as an example
Temperature setting is 30 DEG C by button, temperature up-regulation button and temperature down button.In Starch Production be used for dry plumule, fiber and
The waste gas of albumen powder discharge, is reclaimed by dry waste gas retracting device 1, is filtered through waste gas filter 2, gone miscellaneous in removing exhaust gas
Matter, the steam after filtering enters fermentation tank heater 6 by waste heat recovery pipeline 5.Fermentation tank heater 6 is provided with two steamings
Vapour air inlet 6-1, each position of the steam-heating pipe 6-6 in fermentation tank interlayer 6-8 is quickly reached beneficial to steam.Fermentation tank adds
Temperature sensor 6-5 is provided with thermal 6, temperature sensor is electrically connected with temperature control panel.Zymotic fluid is from material inlet 6-3
Into in fermentation tank, heat exchange is carried out by steam-heating pipe 6-6 and steam waste heat.When temperature sensor 6-5 detects hair
When temperature in fermentation tank is less than 30 DEG C, control to open or tune up automatic regulating valve 4 by temperature control panel, afterheat steam is from steaming
Vapour air inlet 6-1 enters in steam-heating pipe 6-6, and fermentation tank is heated.When the temperature in fermentation tank reaches 30 DEG C just
Close or turn down and automatically adjust valve 4, by adjusting steam, make the fermentation temperature in fermentation tank constant at 30 DEG C.Reach fermentation
Temperature and the zymotic fluid of fermentation time requirement discharge from material outlet 6-4, into next process, and condensed water is from Crude product input
6-2 is discharged.
Embodiment 2：
A kind of device for carrying out heated at constant temperature to the fermentation tank in saccharomyces boulardii fermentation process using steam waste heat, it is tied
Structure as described in Example 1, except that, be additionally provided with pressure gauge on waste heat recovery pipeline.For detecting the pressure value in pipeline,
Cause manifold pressure superfluous to avoid hindering for some reason.
Embodiment 3：
A kind of device for carrying out heated at constant temperature to the fermentation tank in saccharomyces boulardii fermentation process using steam waste heat, it is tied
Structure as described in Example 1, except that, the steam inlet is respectively arranged on the two ends of fermentation tank, and the heating medium goes out
Mouth is respectively arranged on the two ends of fermentation tank, as shown in Figure 4.When making afterheat steam into steam-heating pipe, respectively from the two of fermentation tank
End enters simultaneously is heated, and accordingly, Crude product input also corresponds to the two ends for being distributed in fermentation tank, it is to avoid two in fermentation tank
The temperature at end is simultaneously hot or simultaneously cold, polarization is serious, makes heating faster more uniform.
Embodiment 4：
A kind of device for carrying out heated at constant temperature to the fermentation tank in saccharomyces boulardii fermentation process using steam waste heat, it is tied
Structure as described in Example 1, except that, the probe of the temperature sensor monitors fermentation tank in real time inside fermentation tank
Interior fermentation temperature.
Claims (6)
1. a kind of device for carrying out heated at constant temperature to fermentation tank using steam waste heat, it is characterised in that reclaimed including afterheat steam
Device, waste heat recovery pipeline, temperature control panel and fermentation tank heater；Waste heat steam recovery device passes through waste heat recovery pipe
Road is connected with fermentation tank heater, and waste heat recovery pipeline is provided with temperature control panel；
Waste heat steam recovery device includes dry waste gas retracting device, waste gas filter；
Temperature control panel includes temperature adjustment buttons, temperature display；Waste heat recovery pipeline is provided with automatic regulating valve, automatically
Regulating valve is connected with temperature control panel；
Fermentation tank heater includes fermentation tank and the fermentation tank interlayer on the outside of fermentation tank, fermentation tank and fermentation tank interlayer it
Between be provided with steam-heating pipe, fermentation tank upper and lower side is respectively equipped with material inlet and material outlet；Steam-heating pipe enters including steam
Gas port and Crude product input, steam inlet are connected with waste heat recovery pipeline；Fermentation tank is provided with temperature sensor, and temperature is passed
Sensor is electrically connected with temperature control panel；The quantity of steam inlet and Crude product input is at least two.
2. the device according to claim 1 for carrying out heated at constant temperature to fermentation tank using steam waste heat, it is characterised in that remaining
Pressure gauge is additionally provided with recuperation of heat pipeline.
3. the device according to claim 1 for carrying out heated at constant temperature to fermentation tank using steam waste heat, it is characterised in that institute
Stating temperature display includes setting temperature value display screen and measurement temperature value display screen.
4. the device according to claim 1 for carrying out heated at constant temperature to fermentation tank using steam waste heat, it is characterised in that institute
Stating temperature adjustment buttons includes temperature setting button, temperature up-regulation button and temperature down button.
5. the device according to claim 1 for carrying out heated at constant temperature to fermentation tank using steam waste heat, it is characterised in that institute
State the upper and lower ends that steam inlet is respectively arranged on fermentation tank, the Crude product input is respectively arranged on up and down the two of fermentation tank
End.
6. the device according to claim 1 for carrying out heated at constant temperature to fermentation tank using steam waste heat, it is characterised in that institute
The probe of temperature sensor is stated inside fermentation tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720052185.XU CN206438128U (en) | 2017-01-17 | 2017-01-17 | A kind of device for carrying out heated at constant temperature to fermentation tank using steam waste heat |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201720052185.XU CN206438128U (en) | 2017-01-17 | 2017-01-17 | A kind of device for carrying out heated at constant temperature to fermentation tank using steam waste heat |
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| CN206438128U true CN206438128U (en) | 2017-08-25 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108467459A (en) * | 2018-04-16 | 2018-08-31 | 德莱创节能科技（苏州）有限公司 | A kind of styrene-butadiene latex production system of energy-saving and emission-reduction |
| CN108949508A (en) * | 2018-08-29 | 2018-12-07 | 天津科技大学 | A kind of fermentor residual neat recovering system and waste heat reclaiming process |
| CN113816775A (en) * | 2020-06-19 | 2021-12-21 | 江苏省家禽科学研究所 | Waste treatment device |
-
2017
- 2017-01-17 CN CN201720052185.XU patent/CN206438128U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108467459A (en) * | 2018-04-16 | 2018-08-31 | 德莱创节能科技（苏州）有限公司 | A kind of styrene-butadiene latex production system of energy-saving and emission-reduction |
| CN108467459B (en) * | 2018-04-16 | 2021-04-20 | 德莱创节能科技（苏州）有限公司 | Energy-saving and emission-reducing styrene-butadiene latex production system |
| CN108949508A (en) * | 2018-08-29 | 2018-12-07 | 天津科技大学 | A kind of fermentor residual neat recovering system and waste heat reclaiming process |
| CN108949508B (en) * | 2018-08-29 | 2023-10-03 | 天津科技大学 | Fermentation tank waste heat recovery system and waste heat recovery process |
| CN113816775A (en) * | 2020-06-19 | 2021-12-21 | 江苏省家禽科学研究所 | Waste treatment device |
| CN113816775B (en) * | 2020-06-19 | 2024-05-07 | 江苏省家禽科学研究所 | Waste treatment device |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220114 Address after: 250103 room A302, biological building, No. 28789, Jingshi East Road, Caishi street, Licheng District, Jinan City, Shandong Province Patentee after: Shandong baiaomadi Biotechnology Co.,Ltd. Address before: 250014 No. 19, ASTRI Road, Ji'nan, Shandong Patentee before: BIOLOGY INSTITUTE OF SHANDONG ACADEMY OF SCIENCES |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220309 Address after: 251600 No. 6, xushang Private Economic Industrial Park, Shanghe County, Jinan City, Shandong Province (east of Xinglong Street and south of Xingmin Street) Patentee after: Shandong Keqiao Biotechnology Co.,Ltd. Address before: 250103 room A302, biological building, No. 28789, Jingshi East Road, Caishi street, Licheng District, Jinan City, Shandong Province Patentee before: Shandong baiaomadi Biotechnology Co.,Ltd. |
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| TR01 | Transfer of patent right |