CN109607760A - A kind of dyeing waste water biological carbon filter disused stuffing material dystopy is from generation method - Google Patents
A kind of dyeing waste water biological carbon filter disused stuffing material dystopy is from generation method Download PDFInfo
- Publication number
- CN109607760A CN109607760A CN201910072213.8A CN201910072213A CN109607760A CN 109607760 A CN109607760 A CN 109607760A CN 201910072213 A CN201910072213 A CN 201910072213A CN 109607760 A CN109607760 A CN 109607760A
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- China
- Prior art keywords
- waste water
- hydro
- dyeing waste
- dystopy
- filter
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Classifications
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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
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
-
- 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
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
- C02F2003/003—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms using activated carbon or the like
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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
- C02F2103/30—Nature of the water, waste water, sewage or sludge to be treated from the textile industry
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The invention discloses a kind of dyeing waste water biological carbon filter disused stuffing material dystopys from generation method; it is characterized in that; it takes the rejected particles active carbon of enriched microorganism and organic matter in biological aerated filter to add into the closed reaction kettle of hydro-thermal, adds iron powder and manganese substance, heating carries out hydro-thermal reaction;After hydro-thermal reaction, it is down to room temperature to reaction kettle, discharging simultaneously separates acquisition iron carbon composite and hydro-thermal liquid;Iron carbon composite is added again into biological aerated filter as additional fillers, for adsorbing nitrogen phosphorus, organic matter and heavy metal in dyeing waste water;Hydro-thermal liquid is back to wastewater treatment front end to handle.Operation of the present invention is simple, is easy to be engineered, and provides a kind of feasible method for dyeing waste water biological carbon filter disused stuffing material dystopy is spontaneous.
Description
Technical field
The present invention relates to a kind of dyeing waste water biological carbon filter disused stuffing material dystopys from generation method, belongs to environmental protection technology neck
Domain.
Background technique
General textile technology process include: singe, desizing, kiering, bleaching, dyeing, stamp, the processes such as final finishing, printing and dyeing
Waste water is the general name for the waste water that above-mentioned process procedure generates.And in actual production, dyeing waste water complicated components, variation water quality be big,
Organic matter is difficult to degrade, biodegradability is poor, and conventional processing method is difficult that secondary treatment yielding water is made to reach high standard emission request,
Thus developing advanced treatment process on the basis of two stage treatment is that common method is transformed in sewage plant.
For dyeing waste water, commonly a kind of advanced treatment process is Gas biological filter at present.Biological aerated filter
Usually with the granulated filler of filling such as granular activated carbon (GAC) be carrier, be aerated in pond, by biodegrade with
It absorbs and filter two kinds of reaction process and merges the treatment process in same processing unitary reactor.Biological aerated filter is initially
With the organic matter in the absorption of granular activated carbon and interception capacity removal sewage, with the growth of aeration time, granular activated carbon
Surface grown a large amount of biomembrane, micro- using the high concentration activity of biomembrane appended by filter material surface when sewage flows through filter bed
Biological oxidation decomposition and the utilization lesser feature of granular activated carbon partial size, the bioflocculation for giving full play to microorganism are made
With, physical absorption and the crown_interception of biomembrane and filler, realize the efficient removal of pollutant.In treatment of dyeing wastewater process
In, with the growth of aeration time, gradually the biomembrane on adsorption saturation and the surface GAC constantly thickens filler GAC, to guarantee
The operation of BAF efficient stable, filter tank are backwashed, it is therefore an objective to be discharged the suspended matter retained on filtrate, be increased biomembrane
Activity, accelerate mass transport process etc., with the increase of backwash number, partial filler loss is serious, needs to carry out the portion of filler
Divide replacement, the rejected particles active carbon of a large amount of enriched microorganisms and organic matter can be generated, cause the serious wasting of resources.
Summary of the invention
The technical problems to be solved by the present invention are: how to realize that dyeing waste water biofilter rejected particles active carbon is filled out
Expect resource utilization, realizes that the dystopy of biological carbon filter disused stuffing material is spontaneous.
In order to solve the above-mentioned technical problem, the invention adopts the following technical scheme:
A kind of dyeing waste water biological carbon filter disused stuffing material dystopy is from generation method, which comprises the following steps:
Step 1): the rejected particles active carbon of enriched microorganism and organic matter in biological aerated filter is taken to add to hydro-thermal
In closed reaction kettle, iron powder and manganese substance are added, heating carries out hydro-thermal reaction;
Step 2): after hydro-thermal reaction, being down to room temperature to reaction kettle, discharging and separating obtain iron carbon composite and
Hydro-thermal liquid;
Step 3): iron carbon composite is added again into biological aerated filter as additional fillers, for adsorbing print
Contaminate nitrogen phosphorus, organic matter and the heavy metal in waste water;
Step 4): hydro-thermal liquid is back to wastewater treatment front end and is handled.
Preferably, in the step 1) rejected particles active carbon the volume added be reactor volume 40%-
85%, in a kettle plus water makes liquid level rise to the 50%-70% of effective height.
Preferably, the mass ratio of iron powder and rejected particles active carbon is 1:5-1:8 in the step 1), and manganese substance is adopted
The MnSO for being 0.05-0.1mol/L with total Mn concentration4Solution.
Preferably, the heating method in the step 1) is using steam heating, heat-conducting oil heating or electric heating, heating temperature
Degree is 160-240 DEG C, heating time 0.5-5h.
Preferably, temperature of reaction kettle is down to 60 DEG C or less in the step 2).
Preferably, it adds after mixing ferrimanganic composite material with other conventional fillers in the step 3) to aeration and biological
Additional fillers are used as in filter tank, iron carbon composite accounts for the 30%-50% of total filler quality.
The present invention is to the discarded of the enriched microorganism and organic matter generated in biological aerated filter advanced treatment process
Granular activated carbon carries out hydrothermal carbonization processing, and suitable molysite and manganese substance, rejected particles are added during hydrothermal carbonization
The compound base high-performance adsorbent material of ferrimanganic is made by hydrothermal carbonization in active carbon.In addition, a small amount of hydro-thermal liquid that water-heat process generates
It is back to wastewater treatment front end.The microcellular structure and quantity of active carbon can be changed in hydro-thermal process, makes discarded granular activated carbon water
Hot recycling, a large amount of microorganisms and organic matter for being enriched in rejected particles activated carbon surface are carbonized in water-heat process forms biology
The removal ability of pollutant can be improved in charcoal, the iron and manganese substance of composite material, and the hydrothermal product of acquisition is added again to exposure
Gas biofilter carries out advanced treating as filler, to dyeing waste water, realizes that the dystopy of filter tank disused stuffing material is spontaneous.
Compared with prior art, the invention has the following advantages:
(1) this method can realize that the dystopy of biological carbon filter disused stuffing material is spontaneous, change the microcellular structure and number of active carbon
It measures, the compound adsorbing material of ferrimanganic can be made by adding iron powder and manganese substance in water-heat process, and granular activated carbon that will be discarded provides
Sourceization utilizes;
(2) this method has fully considered the organic matter and enriched microorganism of granular activated carbon adsorption, by its same particle
Active carbon carries out hydro-thermal process jointly, in addition to the regeneration for realizing granular activated carbon, organic matter and enrichment to adsorption
Microorganism can realize that charcoal is made in carbonization, be back to biological aerated filter jointly.
Detailed description of the invention
Fig. 1 is process schematic representation of the dyeing waste water biological carbon filter disused stuffing material dystopy provided by the invention from generation method.
Specific embodiment
In order to make the present invention more obvious and understandable, hereby with preferred embodiment, and attached drawing is cooperated to be described in detail below.
Embodiment 1
A kind of dyeing waste water biological carbon filter disused stuffing material dystopy is from generation method, comprising the following steps:
Step 1): the rejected particles active carbon of enriched microorganism and organic matter in biological aerated filter is taken, iron is added
To hydro-thermal closed reactor, wherein the mass ratio of iron powder and rejected particles active carbon is 1:6, is then thrown for powder and substance containing manganese
Add up the MnSO that Mn concentration is 0.07mol/L4Solution;The volume that adds of rejected particles active carbon is the 50% of reactor volume,
In a kettle plus water makes liquid level rise to the 65% of effective height, heats 180min under the conditions of 180 DEG C;
Step 2): after hydro-thermal reaction, being down to 50 DEG C to reaction kettle, discharging to filter device, by filtration treatment,
Separation obtains ferrimanganic mixed base regeneration biological charcoal;
Step 3): a small amount of hydro-thermal liquid generated in water-heat process is back to front end sewage treatment process, the regeneration of acquisition
Charcoal is added again into biological aerated filter makes the height biological aerated filter of mixed fillers high as additional fillers
The removal rate of 70%, COD of degree improves 40% compared with blank group, and the removal rate of total nitrogen improves 30% compared with blank group, heavy metals removal
Rate improves 35% compared with blank group.
Embodiment 2
A kind of dyeing waste water biological carbon filter disused stuffing material dystopy is from generation method, comprising the following steps:
Step 1): the rejected particles active carbon of enriched microorganism and organic matter in biological aerated filter is taken, iron is added
To hydro-thermal closed reactor, wherein the mass ratio of iron powder and rejected particles active carbon is 1:8, is then thrown for powder and substance containing manganese
Add up the MnSO that Mn concentration is 0.1mol/L4The volume that adds of solution, rejected particles active carbon is the 60% of reactor volume,
In a kettle plus water makes liquid level rise to the 70% of effective height, heats 4h under the conditions of 200 DEG C;
Step 2): after hydro-thermal reaction, being down to 60 DEG C to reaction kettle, discharging to filter device, by filtration treatment,
Ferrimanganic mixed base regeneration biological charcoal;
Step 3): a small amount of hydro-thermal liquid generated in water-heat process is back to front end sewage treatment process, the regeneration of acquisition
Charcoal is added again into biological aerated filter makes the height biological aerated filter of mixed fillers high as additional fillers
The removal rate of 75%, COD of degree improves 50% compared with blank group, and the removal rate of total nitrogen mentions 40% compared with blank group, heavy metal removing rate
40% is improved compared with blank group.
Claims (6)
1. a kind of dyeing waste water biological carbon filter disused stuffing material dystopy is from generation method, which comprises the following steps:
Step 1): the rejected particles active carbon of enriched microorganism and organic matter is taken in biological aerated filter to add closed to hydro-thermal
In reaction kettle, iron powder and manganese substance are added, heating carries out hydro-thermal reaction;
Step 2): after hydro-thermal reaction, it is down to room temperature to reaction kettle, discharging simultaneously separates acquisition iron carbon composite and hydro-thermal
Liquid;
Step 3): iron carbon composite is added again into biological aerated filter as additional fillers, useless for adsorbing printing and dyeing
Nitrogen phosphorus, organic matter and heavy metal in water;
Step 4): hydro-thermal liquid is back to wastewater treatment front end and is handled.
2. dyeing waste water biological carbon filter disused stuffing material dystopy as described in claim 1 is from generation method, which is characterized in that described
The volume of rejected particles active carbon added is the 40%-85% of reactor volume in step 1), and in a kettle plus water makes
Liquid level rises to the 50%-70% of effective height.
3. dyeing waste water biological carbon filter disused stuffing material dystopy as described in claim 1 is from generation method, which is characterized in that described
The mass ratio of iron powder and rejected particles active carbon is 1:5-1:8 in step 1), and manganese substance uses total Mn concentration for 0.05-
The MnSO of 0.1mol/L4Solution.
4. dyeing waste water biological carbon filter disused stuffing material dystopy as described in claim 1 is from generation method, which is characterized in that described
Using steam heating, heat-conducting oil heating or electric heating, heating temperature is 160-240 DEG C for heating method in step 1), when heating
Between be 0.5-5h.
5. dyeing waste water biological carbon filter disused stuffing material dystopy as described in claim 1 is from generation method, which is characterized in that described
Temperature of reaction kettle is down to 60 DEG C or less in step 2).
6. dyeing waste water biological carbon filter disused stuffing material dystopy as described in claim 1 is from generation method, which is characterized in that described
It is added into biological aerated filter after mixing ferrimanganic composite material with other conventional fillers in step 3) as additional fillers, iron
Carbon composite accounts for the 30%-50% of total filler quality.
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102616922A (en) * | 2012-04-23 | 2012-08-01 | 重庆康达环保产业(集团)有限公司 | PACT (Production Analysis Control Technique) novel process for treating non-biodegradable waste water by using circularly-reproducible powdered activated carbon |
CN104383880A (en) * | 2014-12-03 | 2015-03-04 | 东华大学 | Preparation method of alloy active coke catalytic packing for deep processing industrial wastewater |
CN106512973A (en) * | 2016-11-10 | 2017-03-22 | 中南大学 | Regeneration method of low-carbon-loss activated carbon |
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- 2019-01-25 CN CN201910072213.8A patent/CN109607760A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102616922A (en) * | 2012-04-23 | 2012-08-01 | 重庆康达环保产业(集团)有限公司 | PACT (Production Analysis Control Technique) novel process for treating non-biodegradable waste water by using circularly-reproducible powdered activated carbon |
CN104383880A (en) * | 2014-12-03 | 2015-03-04 | 东华大学 | Preparation method of alloy active coke catalytic packing for deep processing industrial wastewater |
CN106512973A (en) * | 2016-11-10 | 2017-03-22 | 中南大学 | Regeneration method of low-carbon-loss activated carbon |
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Application publication date: 20190412 |