CN113024014A - Hospital sewage treatment method - Google Patents
Hospital sewage treatment method Download PDFInfo
- Publication number
- CN113024014A CN113024014A CN202110120632.1A CN202110120632A CN113024014A CN 113024014 A CN113024014 A CN 113024014A CN 202110120632 A CN202110120632 A CN 202110120632A CN 113024014 A CN113024014 A CN 113024014A
- Authority
- CN
- China
- Prior art keywords
- parts
- wastewater
- hospital
- microorganisms
- treatment method
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- 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
-
- 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
-
- 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
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F2103/003—Wastewater from hospitals, laboratories and the like, heavily contaminated by pathogenic microorganisms
-
- 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
- C02F3/348—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the way or the form in which the microorganisms are added or dosed
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention belongs to the field of sewage treatment, and particularly relates to a hospital sewage treatment method, which comprises the following steps: s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; s2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 1-6% of the weight of the wastewater; treating for 2-5 days; s3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner; s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 30-50 minutes, and standing for 60-120 minutes; directly discharging the supernatant; the addition amount of the flocculating agent is 1-10% of the weight of the clear liquid. The invention effectively removes COD in the hospital sewagecrBOD and NH3‑N。
Description
Technical Field
The invention belongs to the technical field of sewage treatment, and particularly relates to a hospital sewage treatment method.
Background
The hospital sewage refers to sewage discharged from hospitals (comprehensive hospitals, professional hospitals and other types of hospitals) to natural environments or urban pipelines. The water quality varies with the nature and scale of the hospital and the area in which it is located. The amount of sewage discharged by each sickbed per day is about 200-1000L. The main pollutants contained in hospital sewage are: pathogens (parasitic eggs, pathogenic bacteria, viruses, etc.), organic matter, floating and suspended matter, radioactive contaminants, etc., untreatedThe total bacteria content in the raw sewage reaches 108More than one/mL. The principle of hospital sewage treatment is as follows: the quality and the flow are divided, and the local separation treatment is carried out, so that the pollution is eliminated nearby at a pollution source. The main treatment method is precipitation and disinfection. The disinfectant commonly used in China is liquid chlorine, and in order to improve the disinfection efficiency and prevent secondary pollution, the ozonization method is mostly adopted for disinfection, and the discharge standard can be reached after disinfection treatment. The sludge produced in the treatment process is usually treated by a lime disinfection method and a high-temperature composting method. The prior hospital sewage treatment method is used for treating COD in sewagecrBOD and NH3The removal rate of-N is low.
Disclosure of Invention
The technical problem to be solved by the invention is to provide a hospital sewage treatment method for improving COD in sewagecrBOD and NH3-removal rate of N.
In order to solve the technical problems, the technical scheme of the invention is as follows:
a hospital sewage treatment method comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater;
s2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 1-6% of the weight of the wastewater; treating for 2-5 days;
s3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 30-50 minutes, and standing for 60-120 minutes; directly discharging the supernatant;
the addition amount of the flocculating agent is 1-10% of the weight of the clear liquid.
In the hospital sewage treatment method provided by the invention, the sterilization temperature in the step S1 is preferably 110-135 ℃.
In the hospital sewage treatment method provided by the present invention, preferably, the microorganism in step S2 is one or more of citrobacter buchneri, flavobacterium aquaticum, flavobacterium marinum, nitrobacter alkalophilus, bacillus subtilis, bacillus licheniformis, micrococcus luteus, rhizopus nigricans, rhizopus chinensis, ester producing yeast, bifidobacterium, mucor racemosus and mucor rouxii.
In the hospital sewage treatment method provided by the present invention, preferably, the microorganism is flavobacterium marinum, bacillus subtilis, rhizopus nigricans, ester producing yeast, bifidobacterium, mucor racemosus and mucor rouxii.
In the hospital sewage treatment method provided by the invention, the weight ratio of the flavobacterium marinum, the bacillus subtilis, the rhizopus nigricans, the ester-producing yeast, the bifidobacterium, the mucor racemosus and the mucor rouxii is preferably 1-5: 0.5-2: 1-3: 0.5-1: 1-5: 1-2.
In the hospital sewage treatment method provided by the invention, the weight ratio of the flavobacterium marinum, the bacillus subtilis, the rhizopus nigricans, the ester-producing yeast, the bifidobacterium, the mucor racemosus and the mucor rouxii is preferably 3:1:2:1:0.5:5: 1.
In the hospital sewage treatment method provided by the present invention, preferably, the added amount of the microorganism is 5% by weight of the wastewater.
In the hospital sewage treatment method provided by the invention, preferably, the flocculant mainly comprises the following raw materials in parts by weight: 10-35 parts of aluminum sulfate, 2-18 parts of tannin, 3-41 parts of acrylonitrile resin, 12-32 parts of azobisisobutyronitrile, 5-19 parts of sodium thiosulfate, 2-27 parts of sodium dodecyl benzene sulfonate, 7-33 parts of hexadecyl trimethyl ammonium bromide and 17-40 parts of acetic acid.
In the hospital sewage treatment method provided by the invention, preferably, the flocculant mainly comprises the following raw materials in parts by weight: 22 parts of aluminum sulfate, 13 parts of tannin, 6 parts of acrylonitrile resin, 13 parts of azodiisobutyronitrile, 9 parts of sodium thiosulfate, 7 parts of sodium dodecyl benzene sulfonate, 14 parts of hexadecyl trimethyl ammonium bromide and 23 parts of acetic acid.
By adopting the technical scheme, the tubular sterilization machine is adopted to treat the hospital sewageVarious pathogenic bacteria, viruses and other microorganisms in the feed are killed, so that the problem of environmental pollution caused by pathogenic bacteria is solved; decomposing organic matters in hospital sewage by using microorganisms, centrifuging by using a continuous flow centrifuge to remove thalli, and finally flocculating and precipitating the inorganic matters in the sewage by using a flocculating agent to effectively remove CODcrBOD and NH3-N. The bacillus subtilis and the mucor racemosus in the invention can reduce COD in hospital sewagecrBOD and NH3the-N content has a significant effect.
Detailed Description
The following further describes the embodiments of the present invention. It should be noted that the description of the embodiments is provided to help understanding of the present invention, but the present invention is not limited thereto. In addition, the technical features involved in the embodiments of the present invention described below may be combined with each other as long as they do not conflict with each other.
Example 1
The embodiment provides a hospital sewage treatment method, which comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; the sterilization temperature is 135 ℃.
S2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 6% of the weight of the wastewater; treating for 2 days; the microorganism is Flavobacterium marinum, Bacillus subtilis, Rhizopus nigricans, ester-producing yeast, Bifidobacterium, Mucor racemosus and Mucor rouxii, and the weight ratio of the microorganisms is 5:0.5:1:3:1:1: 2.
S3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 30 minutes, and standing for 120 minutes; directly discharging the supernatant;
the addition amount of the flocculant is 1 percent of the weight of the clear solution.
The flocculant mainly comprises the following raw materials in parts by weight: 10 parts of aluminum sulfate, 18 parts of tannin, 3 parts of acrylonitrile resin, 32 parts of azodiisobutyronitrile, 5 parts of sodium thiosulfate, 27 parts of sodium dodecyl benzene sulfonate, 7 parts of hexadecyl trimethyl ammonium bromide and 17 parts of acetic acid.
Example 2
The embodiment provides a hospital sewage treatment method, which comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; the sterilization temperature is 110 ℃.
S2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 1% of the weight of the wastewater; treating for 5 days; the microorganism is Flavobacterium marinum, Bacillus subtilis, Rhizopus nigricans, ester-producing yeast, Bifidobacterium, Mucor racemosus and Mucor rouxii with a weight ratio of 1:2:2:1:0.5:5: 1.
S3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 50 minutes, and standing for 60 minutes; directly discharging the supernatant;
the addition amount of the flocculant is 10 percent of the weight of the clear solution.
The flocculant mainly comprises the following raw materials in parts by weight: 35 parts of aluminum sulfate, 2 parts of tannin, 41 parts of acrylonitrile resin, 12 parts of azodiisobutyronitrile, 19 parts of sodium thiosulfate, 2 parts of sodium dodecyl benzene sulfonate, 33 parts of hexadecyl trimethyl ammonium bromide and 40 parts of acetic acid.
Example 3
The embodiment provides a hospital sewage treatment method, which comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; the sterilization temperature was 121 ℃.
S2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 5% of the weight of the wastewater; treating for 3 days; the microorganism is Flavobacterium marinum, Bacillus subtilis, Rhizopus nigricans, ester-producing yeast, Bifidobacterium, Mucor racemosus and Mucor rouxii with a weight ratio of 3:1:2:1:0.5:5: 1.
S3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 40 minutes, and standing for 80 minutes; directly discharging the supernatant;
the addition amount of the flocculant is 5 percent of the weight of the clear solution.
The flocculant mainly comprises the following raw materials in parts by weight: 22 parts of aluminum sulfate, 13 parts of tannin, 6 parts of acrylonitrile resin, 13 parts of azodiisobutyronitrile, 9 parts of sodium thiosulfate, 7 parts of sodium dodecyl benzene sulfonate, 14 parts of hexadecyl trimethyl ammonium bromide and 23 parts of acetic acid.
Example 4
The embodiment provides a hospital sewage treatment method, which comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; the sterilization temperature was 115 ℃.
S2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 3% of the weight of the wastewater; treating for 4 days; the microorganism is Bacillus subtilis, Rhizopus nigricans, ester-producing yeast, Bacillus bifidus, Mucor racemosus and Mucor rouxii at a weight ratio of 1:2:1:0.5:5: 1.
S3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 35 minutes, and standing for 80 minutes; directly discharging the supernatant;
the addition amount of the flocculant is 7 percent of the weight of the clear solution.
The flocculant mainly comprises the following raw materials in parts by weight: 18 parts of aluminum sulfate, 9 parts of tannin, 33 parts of acrylonitrile resin, 19 parts of azobisisobutyronitrile, 11 parts of sodium thiosulfate, 8 parts of sodium dodecyl benzene sulfonate, 27 parts of hexadecyl trimethyl ammonium bromide and 34 parts of acetic acid.
Example 5
The embodiment provides a hospital sewage treatment method, which comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; the sterilization temperature is 120 ℃.
S2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 3% of the weight of the wastewater; treating for 4 days; the microorganism is bacillus subtilis, rhizopus nigricans, bifidobacterium, mucor racemosus and mucor rouxii in a weight ratio of 1:2:0.5:5: 1.
S3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 46 minutes, and standing for 90 minutes; directly discharging the supernatant;
the addition amount of the flocculant is 8 percent of the weight of the clear solution.
The flocculant mainly comprises the following raw materials in parts by weight: 31 parts of aluminum sulfate, 12 parts of tannin, 13 parts of acrylonitrile resin, 24 parts of azodiisobutyronitrile, 9 parts of sodium thiosulfate, 21 parts of sodium dodecyl benzene sulfonate, 16 parts of hexadecyl trimethyl ammonium bromide and 18 parts of acetic acid.
Example 6
The embodiment provides a hospital sewage treatment method, which comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; the sterilization temperature is 135 ℃.
S2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 4% of the weight of the wastewater; treating for 4 days; the microorganism is Flavobacterium nigerum, Rhizopus nigricans, ester-producing yeast, Bifidobacterium, Mucor racemosus and Mucor rouxii, and the weight ratio is 3:1:2:1:1: 2.
S3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 39 minutes, and standing for 110 minutes; directly discharging the supernatant;
the addition amount of the flocculant is 4 percent of the weight of the clear solution.
The flocculant mainly comprises the following raw materials in parts by weight: 28 parts of aluminum sulfate, 15 parts of tannin, 27 parts of acrylonitrile resin, 30 parts of azobisisobutyronitrile, 11 parts of sodium thiosulfate, 13 parts of sodium dodecyl benzene sulfonate, 9 parts of hexadecyl trimethyl ammonium bromide and 21 parts of acetic acid.
Example 7
The embodiment provides a hospital sewage treatment method, which comprises the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater; the sterilization temperature is 125 ℃.
S2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 3% of the weight of the wastewater; treating for 3 days; the microorganism is Flavobacterium marinum, Bacillus subtilis, Rhizopus nigricans, ester-producing yeast, Bifidobacterium and Mucor rouxii in a weight ratio of 5:1:1:2:1: 2.
S3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 44 minutes, and standing for 86 minutes; directly discharging the supernatant;
the addition amount of the flocculant is 7 percent of the weight of the clear solution.
The flocculant mainly comprises the following raw materials in parts by weight: 18 parts of aluminum sulfate, 11 parts of tannin, 3 parts of acrylonitrile resin, 32 parts of azodiisobutyronitrile, 16 parts of sodium thiosulfate, 18 parts of sodium dodecyl benzene sulfonate, 7 parts of hexadecyl trimethyl ammonium bromide and 17 parts of acetic acid.
Test examples
In order to verify the beneficial technical effects of the invention, the medical wastewater is treated according to the above examples, and then the quality of the treated water is detected, and the results are shown in table 1.
TABLE 1 Water quality results (mg/L) of Hospital waste Water treated in examples
As can be seen from the above table, COD in the hospital wastewater treated by the methods of examples 1 to 5crBOD and NH3The content of-N was significantly lower than that of the hospital wastewater treated by the methods of examples 6 and 7, in which COD was contained in the hospital wastewater treated by the method of example 3crBOD and NH3The lowest content of-N. Bacillus subtilis was reduced in the microorganism used in the microbial treatment in example 6 and Mucor racemosus was reduced in the microorganism used in the microbial treatment in example 7, and it was found that Bacillus subtilis and Mucor racemosus contribute to the reduction of COD in hospital wastewatercrBOD and NH3the-N content has a significant effect.
The embodiments of the present invention have been described in detail, but the present invention is not limited to the described embodiments. It will be apparent to those skilled in the art that various changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, and the scope of protection is still within the scope of the invention.
Claims (9)
1. A hospital sewage treatment method is characterized by comprising the following steps:
s1, sewage sterilization: after collecting sewage generated by a hospital, continuously passing through a tubular sterilization machine for sterilization to obtain sterilized wastewater;
s2, microbial treatment: cooling the sterilized wastewater, and adding microorganisms into the cooled wastewater, wherein the addition amount of the microorganisms is 1-6% of the weight of the wastewater; treating for 2-5 days;
s3, centrifugal separation: carrying out centrifugal separation on the wastewater treated by the microorganisms in the step S2 by using a continuous flow centrifugal machine, discharging the centrifuged clear liquid to a flocculation tank, and killing thalli in a centralized manner;
s4, flocculation treatment: adding a flocculating agent into the clear liquid discharged into the flocculating tank, stirring for 30-50 minutes, and standing for 60-120 minutes; directly discharging the supernatant;
the addition amount of the flocculating agent is 1-10% of the weight of the clear liquid.
2. The hospital sewage treatment method according to claim 1, wherein the sterilization temperature in step S1 is 110-135 ℃.
3. The hospital sewage treatment method according to claim 1, wherein the microorganisms in step S2 are one or more of citrobacter buchneri, flavobacterium aquaticum, flavobacterium marinum, nitrobacter alkalophilus, bacillus subtilis, bacillus licheniformis, micrococcus luteus, rhizopus nigricans, rhizopus chinensis, ester-producing yeast, bifidobacterium, mucor racemosus, and mucor rouxii.
4. The hospital wastewater treatment method according to claim 3, wherein the microorganisms are Flavobacterium marinum, Bacillus subtilis, Rhizopus nigricans, Saccharomyces esterificans, Bifidobacterium longum, Mucor racemosus and Mucor rouxii.
5. The hospital sewage treatment method according to claim 4, wherein the weight ratio of the Flavobacterium marinum, the Bacillus subtilis, the Rhizopus nigricans, the ester-producing yeast, the Bifidobacterium longum, the Mucor racemosus and the Mucor rouxii is 1-5: 0.5-2: 1-3: 0.5-1: 1-5: 1-2.
6. The hospital sewage treatment method according to claim 5, wherein the weight ratio of Flavobacterium marinum, Bacillus subtilis, Rhizopus nigricans, Saccharomyces esterificans, Bifidobacterium longum, Mucor racemosus and Mucor rouxii is 3:1:2:1:0.5:5: 1.
7. The hospital sewage treatment method according to claim 1, wherein said microorganisms are added in an amount of 5% by weight of the wastewater.
8. The hospital sewage treatment method according to claim 1, wherein the flocculant is mainly composed of the following raw materials in parts by weight: 10-35 parts of aluminum sulfate, 2-18 parts of tannin, 3-41 parts of acrylonitrile resin, 12-32 parts of azobisisobutyronitrile, 5-19 parts of sodium thiosulfate, 2-27 parts of sodium dodecyl benzene sulfonate, 7-33 parts of hexadecyl trimethyl ammonium bromide and 17-40 parts of acetic acid.
9. The hospital sewage treatment method according to claim 8, wherein the flocculant is mainly composed of the following raw materials in parts by weight: 22 parts of aluminum sulfate, 13 parts of tannin, 6 parts of acrylonitrile resin, 13 parts of azodiisobutyronitrile, 9 parts of sodium thiosulfate, 7 parts of sodium dodecyl benzene sulfonate, 14 parts of hexadecyl trimethyl ammonium bromide and 23 parts of acetic acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110120632.1A CN113024014A (en) | 2021-01-29 | 2021-01-29 | Hospital sewage treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110120632.1A CN113024014A (en) | 2021-01-29 | 2021-01-29 | Hospital sewage treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN113024014A true CN113024014A (en) | 2021-06-25 |
Family
ID=76459398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110120632.1A Pending CN113024014A (en) | 2021-01-29 | 2021-01-29 | Hospital sewage treatment method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113024014A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114906979A (en) * | 2022-04-14 | 2022-08-16 | 郯城瑞源无害化处理有限公司 | Photocatalytic anaerobic treatment process for sewage treatment |
Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101037655A (en) * | 2006-11-29 | 2007-09-19 | 金明记 | High-effective microorganism complex agent and method of using the same for treating city sewage |
| CN101585622A (en) * | 2008-05-20 | 2009-11-25 | 北京锦奥华荣科技有限公司 | Method and system for safely treating medical wastewater and capable of preventing microbial contamination |
| CN101591107A (en) * | 2008-05-26 | 2009-12-02 | 北京锦奥华荣科技有限公司 | The safe waste water treatment method of small hospital |
| CN103130335A (en) * | 2011-11-27 | 2013-06-05 | 西安瑞捷生物科技有限公司 | Germ composite polluted water treatment agent |
| CN103525870A (en) * | 2013-10-23 | 2014-01-22 | 嘉兴学院 | Microbial flocculant as well as preparation method and application thereof |
| CN205653303U (en) * | 2016-03-18 | 2016-10-19 | 浙江汉诺软件有限公司 | Hospital passes catch disease district sewage treatment plant |
| CN106927634A (en) * | 2017-04-10 | 2017-07-07 | 浙江省现代建筑设计研究院有限公司 | Waste water treatment system for hospitals |
| CN106947722A (en) * | 2017-04-28 | 2017-07-14 | 连云港中新污水处理有限公司 | Microbial bacterial agent and preparation method thereof and the application in sewage disposal |
| CN206599507U (en) * | 2017-03-10 | 2017-10-31 | 珠海盛博环保科技有限公司 | A kind of Medical wastewater treatment device |
| CN107935316A (en) * | 2017-12-13 | 2018-04-20 | 四川知创空间孵化器管理有限公司 | A kind of method for handling medical waste water |
| CN108503128A (en) * | 2018-03-02 | 2018-09-07 | 云南龙帜环境工程有限公司 | A kind for the treatment of process of pharmacy waste water |
| CN109020020A (en) * | 2018-07-16 | 2018-12-18 | 成都赋阳技术开发有限公司 | A kind of medical waste water processing unit |
| CN109896712A (en) * | 2019-04-09 | 2019-06-18 | 黑龙江省福林环保科技有限公司 | A kind of sewerage integrated treatment process of Green Hospital |
| CN109896713A (en) * | 2019-04-09 | 2019-06-18 | 黑龙江省福林环保科技有限公司 | A method of sewage is handled using ABS microbial bacterial agent |
| WO2019133923A1 (en) * | 2017-12-28 | 2019-07-04 | Sustainable Community Development, Llc. | Microbial-based composition and method of use |
| CN110627300A (en) * | 2018-06-25 | 2019-12-31 | 扬州市扬子江运动器材有限公司 | Hospital sewage environmental protection processing system |
| CN111793565A (en) * | 2019-04-09 | 2020-10-20 | 黑龙江省福林环保科技有限公司 | ABS microbial agent for sewage treatment and preparation method thereof |
| CN111808756A (en) * | 2020-06-10 | 2020-10-23 | 郑州和合生物工程技术有限公司 | Microbial agent for treating catering grease wastewater and treatment method |
| CN211921141U (en) * | 2020-03-26 | 2020-11-13 | 山东清德环保设备有限公司 | Hospital virus waste water integration filters treatment device that disappears |
| CN211946662U (en) * | 2019-12-03 | 2020-11-17 | 河南普洛斯环境工程有限公司 | Bury formula medical sewage treatment plant integratively |
-
2021
- 2021-01-29 CN CN202110120632.1A patent/CN113024014A/en active Pending
Patent Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101037655A (en) * | 2006-11-29 | 2007-09-19 | 金明记 | High-effective microorganism complex agent and method of using the same for treating city sewage |
| CN101585622A (en) * | 2008-05-20 | 2009-11-25 | 北京锦奥华荣科技有限公司 | Method and system for safely treating medical wastewater and capable of preventing microbial contamination |
| CN101591107A (en) * | 2008-05-26 | 2009-12-02 | 北京锦奥华荣科技有限公司 | The safe waste water treatment method of small hospital |
| CN103130335A (en) * | 2011-11-27 | 2013-06-05 | 西安瑞捷生物科技有限公司 | Germ composite polluted water treatment agent |
| CN103525870A (en) * | 2013-10-23 | 2014-01-22 | 嘉兴学院 | Microbial flocculant as well as preparation method and application thereof |
| CN205653303U (en) * | 2016-03-18 | 2016-10-19 | 浙江汉诺软件有限公司 | Hospital passes catch disease district sewage treatment plant |
| CN206599507U (en) * | 2017-03-10 | 2017-10-31 | 珠海盛博环保科技有限公司 | A kind of Medical wastewater treatment device |
| CN106927634A (en) * | 2017-04-10 | 2017-07-07 | 浙江省现代建筑设计研究院有限公司 | Waste water treatment system for hospitals |
| CN106947722A (en) * | 2017-04-28 | 2017-07-14 | 连云港中新污水处理有限公司 | Microbial bacterial agent and preparation method thereof and the application in sewage disposal |
| CN107935316A (en) * | 2017-12-13 | 2018-04-20 | 四川知创空间孵化器管理有限公司 | A kind of method for handling medical waste water |
| WO2019133923A1 (en) * | 2017-12-28 | 2019-07-04 | Sustainable Community Development, Llc. | Microbial-based composition and method of use |
| CN108503128A (en) * | 2018-03-02 | 2018-09-07 | 云南龙帜环境工程有限公司 | A kind for the treatment of process of pharmacy waste water |
| CN110627300A (en) * | 2018-06-25 | 2019-12-31 | 扬州市扬子江运动器材有限公司 | Hospital sewage environmental protection processing system |
| CN109020020A (en) * | 2018-07-16 | 2018-12-18 | 成都赋阳技术开发有限公司 | A kind of medical waste water processing unit |
| CN109896712A (en) * | 2019-04-09 | 2019-06-18 | 黑龙江省福林环保科技有限公司 | A kind of sewerage integrated treatment process of Green Hospital |
| CN109896713A (en) * | 2019-04-09 | 2019-06-18 | 黑龙江省福林环保科技有限公司 | A method of sewage is handled using ABS microbial bacterial agent |
| CN111793565A (en) * | 2019-04-09 | 2020-10-20 | 黑龙江省福林环保科技有限公司 | ABS microbial agent for sewage treatment and preparation method thereof |
| CN211946662U (en) * | 2019-12-03 | 2020-11-17 | 河南普洛斯环境工程有限公司 | Bury formula medical sewage treatment plant integratively |
| CN211921141U (en) * | 2020-03-26 | 2020-11-13 | 山东清德环保设备有限公司 | Hospital virus waste water integration filters treatment device that disappears |
| CN111808756A (en) * | 2020-06-10 | 2020-10-23 | 郑州和合生物工程技术有限公司 | Microbial agent for treating catering grease wastewater and treatment method |
Non-Patent Citations (1)
| Title |
|---|
| 许张昱: "湖州市医院污水处理模式及其监测的研究", 《湖州师范学院学报》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114906979A (en) * | 2022-04-14 | 2022-08-16 | 郯城瑞源无害化处理有限公司 | Photocatalytic anaerobic treatment process for sewage treatment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5654005B2 (en) | Waste water treatment method and waste water treatment system | |
| US20090166280A1 (en) | Wastewater purifying system in hospitals | |
| Jiménez-Cisneros et al. | The elimination of helminth ova, faecal coliforms, Salmonella and protozoan cysts by various physicochemical processes in wastewater and sludge | |
| CN112243428B (en) | System and method for treating wastewater and providing class A sludge | |
| US20020189998A1 (en) | Processes and apparatus for potable water purification that include bio-filtration, and treated water from such processes and apparatus | |
| CN106977040A (en) | The technique that slaughtering wastewater is handled using UCT | |
| CN106746160B (en) | Treatment method of vancomycin production wastewater | |
| CN108164002A (en) | A kind of microorganism and the method for nanoscale PAC built-up flocculants processing cultivation water | |
| CN106746161A (en) | A kind of rifamycin produces the processing method of waste water | |
| CN113024014A (en) | Hospital sewage treatment method | |
| US20050112740A1 (en) | Waste metals recycling-methods, processed and systems for the recycle of metals into coagulants | |
| CN103739144A (en) | Detergent synthesis wastewater treatment technology | |
| Abdeen et al. | Fecal coliform removal in a sulfate reduction, autotrophic denitrification and nitrification integrated (SANI) process for saline sewage treatment | |
| CN111362505A (en) | Treatment process of pig farm wastewater | |
| WO2019200775A1 (en) | Wastewater circulating cleaning treatment method capable of reducing sludge amount | |
| JP3900796B2 (en) | Method and apparatus for treating organic wastewater | |
| JP6852214B2 (en) | Sewage treatment system | |
| CN113735392A (en) | Method for treating preserved fruit processing wastewater | |
| Fujioka et al. | The microbial quality of a wetland reclamation facility used to produce an effluent for unrestricted non-potable reuse | |
| CN105271617A (en) | Internal consumption type antibiotic wastewater treatment process system | |
| JP2020179390A (en) | Sewage treatment system | |
| CN110627300A (en) | Hospital sewage environmental protection processing system | |
| CN107352741A (en) | A kind of processing method of dyeing wastewater | |
| JP6741907B1 (en) | Sewage treatment system | |
| CN216445209U (en) | Pig slaughtering wastewater treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210625 |