CN108439696A - A kind of processing method of microbiological pharmacy fermentation waste liquid - Google Patents
A kind of processing method of microbiological pharmacy fermentation waste liquid Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G1/00—Mixtures of fertilisers belonging individually to different subclasses of C05
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/343—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the pharmaceutical industry, e.g. containing antibiotics
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
- C02F3/342—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the enzymes used
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Abstract
The invention discloses a kind of processing methods of microbiological pharmacy fermentation waste liquid, include the following steps：The fermented waste fluid of generation is placed in preliminary treatment pond, then hydrolase is added thereto, and it is stirred in real time, to form runny fermented waste fluid, again activated carbon is added into preliminary treatment pond, and fermented waste fluid is mixed under conditions of 40 55 degrees Celsius, by treated, fermented waste fluid is again placed in heating bath, and it is heated in 120 150 degrees Celsius of environment, temperature in heating bath is restored to room temperature, and fermented waste fluid is carried out to stand 3 6h, after the completion of being stood to fermented waste fluid, separation is filtered to fermented waste fluid, to form waste water and sediment.The present invention can realize the processing to fermented waste fluid, additionally it is possible to be converted and be prepared into fertilizer, harmless, pollution-free, low energy consumption, at low cost to realizing, and turns waste into wealth.
Description
Technical field
The present invention relates to liquid waste disposal technique field more particularly to a kind of processing methods of microbiological pharmacy fermentation waste liquid.
Background technology
It is reported that whole world pharmaceutical products, which have nearly half, at present is especially synthesized by Microbe synthesis
When the drug of molecular structure complexity, microbial method has better economic benefit, micro- life not only than chemical synthesis simplicity
Object drug pharmacy has become research hotspot at present.But microbial medicine pharmacy also produces a large amount of zymotic fluid waste residue simultaneously,
Main ingredient is：Soy meal, methionine, lysine, vegetable oil, starchy material etc., it is necessary to carry out cost-effective thorough place
Reason, otherwise to water body, air it is very harmful, urgent need take effective ways to handle or recycle it.At present to micro- life
The processing of object pharmacy fermentation liquid waste residue has the methods of plate compression, the drying of scraper-type drum, natural drying, but cannot meet section
Energy, environmentally friendly basic demand are for this purpose, we have proposed a kind of processing methods of microbiological pharmacy fermentation waste liquid.
Invention content
The present invention proposes a kind of processing method of microbiological pharmacy fermentation waste liquid, to solve to propose in above-mentioned background technology
The problem of.
The present invention proposes a kind of processing method of microbiological pharmacy fermentation waste liquid, includes the following steps：
S1：The fermented waste fluid of generation is placed in preliminary treatment pond, then adds hydrolase thereto, and stirred in real time to it,
To form runny fermented waste fluid, activated carbon is added into preliminary treatment pond again, and under conditions of 40-55 degrees Celsius
Fermented waste fluid is mixed so that activated carbon can adsorb fermented waste fluid pernicious gas and color and luster, and adsorption time
The activated carbon in fermented waste fluid is taken out for 60-80min after the completion；
S2：By treated in S1, fermented waste fluid is again placed in heating bath, and is added in 120-150 degrees Celsius of environment
Heat during heating needs that fermented waste fluid is mixed in real time, and heating time will add after the completion for 20-30min
Temperature in hot pond is restored to room temperature, and carries out standing 3-6h to fermented waste fluid, spare；
S3：After the completion of being stood to fermented waste fluid, separation is filtered to fermented waste fluid, to form waste water and precipitation
Object；
S4：The waste water formed in S3 is placed in reaction tank, and adds catabolic enzyme into reaction tank, and catabolic enzyme and waste water rub
Your mass ratio is 1：100, then reaction tank is sealed, also needs to ensure that the temperature in reaction tank is maintained at 25-40 degrees Celsius,
80-100min is reacted in the state of real-time stirring, after the completion, waste water is filtered again, removes generated precipitation；
S5：The detection that pH value is carried out to generated waste water in S4 need to so that pH value is 6.5-7.5, if waste water be more than 7.5 or
Person is less than 6.5, then needs that its pH value is adjusted, and to ensure that pH value is in 6.5-7.5, after the completion, then completes to waste water
Processing；
S6：The sediment formed in S3 is placed in rabbling mechanism, and adds activated carbon into rabbling mechanism, again to sediment
Interior pernicious gas and color and luster is adsorbed, and in absorption, is stirred in real time by rabbling mechanism, after the completion, will be active
Charcoal takes out, that is, completes the processing to sediment.
Preferably, in S2, before being heated to fermented waste fluid, heating bath need to be sealed, then in heating bath
Side is connected to escape pipe, and waste gas treatment mechanism is communicated with outside escape pipe, so as to be carried out to exhaust gas caused by heating
It collects and handles, pollution is generated to environment to avoid it.
Preferably, the adsorption temp in S6 is 30-45 degrees Celsius, adsorption time 15-30min.
Preferably, by treated in S6, sediment is again placed in concentration mechanism, is then concentrated to sediment, dense
Contracting temperature is less than 70 degrees Celsius, and concentration time is that after the completion it is dried again processing in 10-16min, and needs to ensure
Water content in sediment is less than 20%, is then mixed with bio-feritlizer charging, you can obtain Crop fertilizer.
Then and bio-fertilizer preferably, crude protein, amino acid, vitamins and minerals are contained in the sediment,
Material charging mixing, is effectively increased the nutritional ingredient of sediment.
Preferably, 10cm need to be more than in the diameter of above-mentioned used activated carbon, and activated carbon surface offers multiple run through
The through-hole of activated carbon.
A kind of processing method of microbiological pharmacy fermentation waste liquid proposed by the present invention, advantageous effect are：The microorganism system
The processing method of medicine fermented waste fluid can not only realize the processing to fermented waste fluid, additionally it is possible to it is converted and is prepared into fertilizer, from
And realize that harmless, pollution-free, low energy consumption, at low cost, turn waste into wealth, meets and national efficiently utilize resource, energy saving and pollution alleviation synergy
Scientific and technological industry policy, economic benefit, environmental benefit, social benefit are very notable, avoid the pollution to environment.
Specific implementation mode
With reference to specific embodiment, the present invention will be further described.
Embodiment 1
The present invention proposes a kind of processing method of microbiological pharmacy fermentation waste liquid, includes the following steps：
S1：The fermented waste fluid of generation is placed in preliminary treatment pond, then adds hydrolase thereto, and stirred in real time to it,
To form runny fermented waste fluid, activated carbon is added into preliminary treatment pond again, and right under conditions of 40 degrees Celsius
Fermented waste fluid is mixed so that activated carbon can adsorb fermented waste fluid pernicious gas and color and luster, and adsorption time is
60min takes out the activated carbon in fermented waste fluid after the completion；
S2：By treated in S1, fermented waste fluid is again placed in heating bath, and is heated in 120 degrees Celsius of environment,
During heating, it needs that fermented waste fluid is mixed in real time, and heating time is that 20min after the completion will be in heating bath
Temperature restore to room temperature, and standing 3h is carried out to fermented waste fluid, it is spare；
S3：After the completion of being stood to fermented waste fluid, separation is filtered to fermented waste fluid, to form waste water and precipitation
Object；
S4：The waste water formed in S3 is placed in reaction tank, and adds catabolic enzyme into reaction tank, and catabolic enzyme and waste water rub
Your mass ratio is 1：100, then reaction tank is sealed, also needs to ensure that the temperature in reaction tank is maintained at 25 degrees Celsius,
80min is reacted in the state of stirring in real time, after the completion, waste water is filtered again, removes generated precipitation；
S5：The detection that pH value is carried out to generated waste water in S4 need to so that pH value is 6.5-7.5, if waste water be more than 7.5 or
Person is less than 6.5, then needs that its pH value is adjusted, and to ensure that pH value is in 6.5-7.5, after the completion, then completes to waste water
Processing；
S6：The sediment formed in S3 is placed in rabbling mechanism, and adds activated carbon into rabbling mechanism, again to sediment
Interior pernicious gas and color and luster is adsorbed, and in absorption, is stirred in real time by rabbling mechanism, after the completion, will be active
Charcoal takes out, that is, completes the processing to sediment.
In S2, before being heated to fermented waste fluid, heating bath need to be sealed, be then connected in heating bath side
Escape pipe, and waste gas treatment mechanism is communicated with outside escape pipe, so as to being collected to exhaust gas caused by heating and
Processing generates pollution to avoid it to environment.
Adsorption temp in S6 is 30 degrees Celsius, adsorption time 15min.
By treated in S6, sediment is again placed in concentration mechanism, is then concentrated to sediment, thickening temperature
Less than 70 degrees Celsius, and concentration time is that after the completion it is dried again processing, and need to ensure in sediment in 10min
Water content is less than 20%, is then mixed with bio-feritlizer charging, you can obtain Crop fertilizer.
Contain crude protein, amino acid, vitamins and minerals in the sediment, it is then mixed with bio-feritlizer charging
It closes, is effectively increased the nutritional ingredient of sediment.
In the diameter of above-mentioned used activated carbon need to be more than 10cm, and activated carbon surface offer it is multiple through activated carbon
Through-hole.
Embodiment 2
The present invention proposes a kind of processing method of microbiological pharmacy fermentation waste liquid, includes the following steps：
S1：The fermented waste fluid of generation is placed in preliminary treatment pond, then adds hydrolase thereto, and stirred in real time to it,
To form runny fermented waste fluid, activated carbon is added into preliminary treatment pond again, and right under conditions of 45 degrees Celsius
Fermented waste fluid is mixed so that activated carbon can adsorb fermented waste fluid pernicious gas and color and luster, and adsorption time is
65min takes out the activated carbon in fermented waste fluid after the completion；
S2：By treated in S1, fermented waste fluid is again placed in heating bath, and is heated in 130 degrees Celsius of environment,
During heating, it needs that fermented waste fluid is mixed in real time, and heating time is that 24min after the completion will be in heating bath
Temperature restore to room temperature, and standing 4h is carried out to fermented waste fluid, it is spare；
S3：After the completion of being stood to fermented waste fluid, separation is filtered to fermented waste fluid, to form waste water and precipitation
Object；
S4：The waste water formed in S3 is placed in reaction tank, and adds catabolic enzyme into reaction tank, and catabolic enzyme and waste water rub
Your mass ratio is 1：100, then reaction tank is sealed, also needs to ensure that the temperature in reaction tank is maintained at 30 degrees Celsius,
85min is reacted in the state of stirring in real time, after the completion, waste water is filtered again, removes generated precipitation；
S5：The detection that pH value is carried out to generated waste water in S4 need to so that pH value is 6.5-7.5, if waste water be more than 7.5 or
Person is less than 6.5, then needs that its pH value is adjusted, and to ensure that pH value is in 6.5-7.5, after the completion, then completes to waste water
Processing；
S6：The sediment formed in S3 is placed in rabbling mechanism, and adds activated carbon into rabbling mechanism, again to sediment
Interior pernicious gas and color and luster is adsorbed, and in absorption, is stirred in real time by rabbling mechanism, after the completion, will be active
Charcoal takes out, that is, completes the processing to sediment.
In S2, before being heated to fermented waste fluid, heating bath need to be sealed, be then connected in heating bath side
Escape pipe, and waste gas treatment mechanism is communicated with outside escape pipe, so as to being collected to exhaust gas caused by heating and
Processing generates pollution to avoid it to environment.
Adsorption temp in S6 is 35 degrees Celsius, adsorption time 20min.
By treated in S6, sediment is again placed in concentration mechanism, is then concentrated to sediment, thickening temperature
Less than 70 degrees Celsius, and concentration time is that after the completion it is dried again processing, and need to ensure in sediment in 12min
Water content is less than 20%, is then mixed with bio-feritlizer charging, you can obtain Crop fertilizer.
Contain crude protein, amino acid, vitamins and minerals in the sediment, it is then mixed with bio-feritlizer charging
It closes, is effectively increased the nutritional ingredient of sediment.
In the diameter of above-mentioned used activated carbon need to be more than 10cm, and activated carbon surface offer it is multiple through activated carbon
Through-hole.
Embodiment 3
The present invention proposes a kind of processing method of microbiological pharmacy fermentation waste liquid, includes the following steps：
S1：The fermented waste fluid of generation is placed in preliminary treatment pond, then adds hydrolase thereto, and stirred in real time to it,
To form runny fermented waste fluid, activated carbon is added into preliminary treatment pond again, and right under conditions of 50 degrees Celsius
Fermented waste fluid is mixed so that activated carbon can adsorb fermented waste fluid pernicious gas and color and luster, and adsorption time is
75min takes out the activated carbon in fermented waste fluid after the completion；
S2：By treated in S1, fermented waste fluid is again placed in heating bath, and is heated in 140 degrees Celsius of environment,
During heating, it needs that fermented waste fluid is mixed in real time, and heating time is that 27min after the completion will be in heating bath
Temperature restore to room temperature, and standing 5h is carried out to fermented waste fluid, it is spare；
S3：After the completion of being stood to fermented waste fluid, separation is filtered to fermented waste fluid, to form waste water and precipitation
Object；
S4：The waste water formed in S3 is placed in reaction tank, and adds catabolic enzyme into reaction tank, and catabolic enzyme and waste water rub
Your mass ratio is 1：100, then reaction tank is sealed, also needs to ensure that the temperature in reaction tank is maintained at 35 degrees Celsius,
95min is reacted in the state of stirring in real time, after the completion, waste water is filtered again, removes generated precipitation；
S5：The detection that pH value is carried out to generated waste water in S4 need to so that pH value is 6.5-7.5, if waste water be more than 7.5 or
Person is less than 6.5, then needs that its pH value is adjusted, and to ensure that pH value is in 6.5-7.5, after the completion, then completes to waste water
Processing；
S6：The sediment formed in S3 is placed in rabbling mechanism, and adds activated carbon into rabbling mechanism, again to sediment
Interior pernicious gas and color and luster is adsorbed, and in absorption, is stirred in real time by rabbling mechanism, after the completion, will be active
Charcoal takes out, that is, completes the processing to sediment.
In S2, before being heated to fermented waste fluid, heating bath need to be sealed, be then connected in heating bath side
Escape pipe, and waste gas treatment mechanism is communicated with outside escape pipe, so as to being collected to exhaust gas caused by heating and
Processing generates pollution to avoid it to environment.
Adsorption temp in S6 is 40 degrees Celsius, adsorption time 25min.
By treated in S6, sediment is again placed in concentration mechanism, is then concentrated to sediment, thickening temperature
Less than 70 degrees Celsius, and concentration time is that after the completion it is dried again processing, and need to ensure in sediment in 14min
Water content is less than 20%, is then mixed with bio-feritlizer charging, you can obtain Crop fertilizer.
Contain crude protein, amino acid, vitamins and minerals in the sediment, it is then mixed with bio-feritlizer charging
It closes, is effectively increased the nutritional ingredient of sediment.
In the diameter of above-mentioned used activated carbon need to be more than 10cm, and activated carbon surface offer it is multiple through activated carbon
Through-hole.
Embodiment 4
The present invention proposes a kind of processing method of microbiological pharmacy fermentation waste liquid, includes the following steps：
S1：The fermented waste fluid of generation is placed in preliminary treatment pond, then adds hydrolase thereto, and stirred in real time to it,
To form runny fermented waste fluid, activated carbon is added into preliminary treatment pond again, and right under conditions of 55 degrees Celsius
Fermented waste fluid is mixed so that activated carbon can adsorb fermented waste fluid pernicious gas and color and luster, and adsorption time is
80min takes out the activated carbon in fermented waste fluid after the completion；
S2：By treated in S1, fermented waste fluid is again placed in heating bath, and is heated in 150 degrees Celsius of environment,
During heating, it needs that fermented waste fluid is mixed in real time, and heating time is that 30min after the completion will be in heating bath
Temperature restore to room temperature, and standing 6h is carried out to fermented waste fluid, it is spare；
S3：After the completion of being stood to fermented waste fluid, separation is filtered to fermented waste fluid, to form waste water and precipitation
Object；
S4：The waste water formed in S3 is placed in reaction tank, and adds catabolic enzyme into reaction tank, and catabolic enzyme and waste water rub
Your mass ratio is 1：100, then reaction tank is sealed, also needs to ensure that the temperature in reaction tank is maintained at 40 degrees Celsius,
100min is reacted in the state of stirring in real time, after the completion, waste water is filtered again, removes generated precipitation；
S5：The detection that pH value is carried out to generated waste water in S4 need to so that pH value is 6.5-7.5, if waste water be more than 7.5 or
Person is less than 6.5, then needs that its pH value is adjusted, and to ensure that pH value is in 6.5-7.5, after the completion, then completes to waste water
Processing；
S6：The sediment formed in S3 is placed in rabbling mechanism, and adds activated carbon into rabbling mechanism, again to sediment
Interior pernicious gas and color and luster is adsorbed, and in absorption, is stirred in real time by rabbling mechanism, after the completion, will be active
Charcoal takes out, that is, completes the processing to sediment.
In S2, before being heated to fermented waste fluid, heating bath need to be sealed, be then connected in heating bath side
Escape pipe, and waste gas treatment mechanism is communicated with outside escape pipe, so as to being collected to exhaust gas caused by heating and
Processing generates pollution to avoid it to environment.
Adsorption temp in S6 is 45 degrees Celsius, adsorption time 30min.
By treated in S6, sediment is again placed in concentration mechanism, is then concentrated to sediment, thickening temperature
Less than 70 degrees Celsius, and concentration time is that after the completion it is dried again processing, and need to ensure in sediment in 16min
Water content is less than 20%, is then mixed with bio-feritlizer charging, you can obtain Crop fertilizer.
Contain crude protein, amino acid, vitamins and minerals in the sediment, it is then mixed with bio-feritlizer charging
It closes, is effectively increased the nutritional ingredient of sediment.
In the diameter of above-mentioned used activated carbon need to be more than 10cm, and activated carbon surface offer it is multiple through activated carbon
Through-hole.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto,
Any one skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (6)
1. a kind of processing method of microbiological pharmacy fermentation waste liquid, which is characterized in that include the following steps：
S1：The fermented waste fluid of generation is placed in preliminary treatment pond, then adds hydrolase thereto, and stirred in real time to it,
To form runny fermented waste fluid, activated carbon is added into preliminary treatment pond again, and under conditions of 40-55 degrees Celsius
Fermented waste fluid is mixed so that activated carbon can adsorb fermented waste fluid pernicious gas and color and luster, and adsorption time
The activated carbon in fermented waste fluid is taken out for 60-80min after the completion；
S2：By treated in S1, fermented waste fluid is again placed in heating bath, and is added in 120-150 degrees Celsius of environment
Heat during heating needs that fermented waste fluid is mixed in real time, and heating time will add after the completion for 20-30min
Temperature in hot pond is restored to room temperature, and carries out standing 3-6h to fermented waste fluid, spare；
S3：After the completion of being stood to fermented waste fluid, separation is filtered to fermented waste fluid, to form waste water and precipitation
Object；
S4：The waste water formed in S3 is placed in reaction tank, and adds catabolic enzyme into reaction tank, and catabolic enzyme and waste water rub
Your mass ratio is 1：100, then reaction tank is sealed, also needs to ensure that the temperature in reaction tank is maintained at 25-40 degrees Celsius,
80-100min is reacted in the state of real-time stirring, after the completion, waste water is filtered again, removes generated precipitation；
S5：The detection that pH value is carried out to generated waste water in S4 need to so that pH value is 6.5-7.5, if waste water be more than 7.5 or
Person is less than 6.5, then needs that its pH value is adjusted, and to ensure that pH value is in 6.5-7.5, after the completion, then completes to waste water
Processing；
S6：The sediment formed in S3 is placed in rabbling mechanism, and adds activated carbon into rabbling mechanism, again to sediment
Interior pernicious gas and color and luster is adsorbed, and in absorption, is stirred in real time by rabbling mechanism, after the completion, will be active
Charcoal takes out, that is, completes the processing to sediment.
2. a kind of processing method of microbiological pharmacy fermentation waste liquid according to claim 1, it is characterised in that：In S2,
Before being heated to fermented waste fluid, heating bath need to be sealed, then be connected to escape pipe, and escape pipe in heating bath side
Outside is communicated with waste gas treatment mechanism, right to avoid its so as to which exhaust gas caused by heating is collected and is handled
Environment generates pollution.
3. a kind of processing method of microbiological pharmacy fermentation waste liquid according to claim 1, it is characterised in that：In S6
Adsorption temp is 30-45 degrees Celsius, adsorption time 15-30min.
4. a kind of processing method of microbiological pharmacy fermentation waste liquid according to claim 1, it is characterised in that：It will be in S6
Sediment after reason is again placed in concentration mechanism, is then concentrated to sediment, and thickening temperature is less than 70 degrees Celsius, and dense
The contracting time is that after the completion it is dried again processing in 10-16min, and need to ensure that the water content in sediment is less than 20%,
Then it is mixed with bio-feritlizer charging, you can obtain Crop fertilizer.
5. a kind of processing method of microbiological pharmacy fermentation waste liquid according to claim 4, it is characterised in that：The precipitation
Contain crude protein, amino acid, vitamins and minerals in object, then feeds and mix with bio-feritlizer, be effectively increased precipitation
The nutritional ingredient of object.
6. a kind of processing method of microbiological pharmacy fermentation waste liquid according to claim 1, it is characterised in that：In above-mentioned institute
10cm need to be more than using the diameter of activated carbon, and activated carbon surface offers multiple through-holes through activated carbon.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109179840A (en) * | 2018-10-16 | 2019-01-11 | 青岛蓝杉知本科技有限公司 | Device and method for treating biopharmaceutical residual liquid |
| CN110395841A (en) * | 2019-05-17 | 2019-11-01 | 高邮市宇航化工机械厂 | Wastewater treating technique in a kind of biopharmaceutical production processes |
| CN113233642A (en) * | 2021-05-07 | 2021-08-10 | 江苏绿科生物技术有限公司 | Efficient method for treating fermentation waste liquid |
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| CN109179840B (en) * | 2018-10-16 | 2021-07-02 | 青岛蓝杉知本科技有限公司 | Processing apparatus of bio-pharmaceuticals raffinate |
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| CN113233642A (en) * | 2021-05-07 | 2021-08-10 | 江苏绿科生物技术有限公司 | Efficient method for treating fermentation waste liquid |
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