CN106167289A - A kind of for black and odorous water processing means and catalyst particle preparation method thereof - Google Patents
A kind of for black and odorous water processing means and catalyst particle preparation method thereof Download PDFInfo
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- CN106167289A CN106167289A CN201610699564.8A CN201610699564A CN106167289A CN 106167289 A CN106167289 A CN 106167289A CN 201610699564 A CN201610699564 A CN 201610699564A CN 106167289 A CN106167289 A CN 106167289A
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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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/843—Arsenic, antimony or bismuth
- B01J23/8435—Antimony
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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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46133—Electrodes characterised by the material
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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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
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
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- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
A kind of for black and odorous water processing means and catalyst particle preparation method thereof, including cylinder (1), it is positioned at the water inlet (14) of cylinder (1) bottom, air inlet (17) and is positioned at outlet (15) and the air vent (12) at cylinder top, being parallel to stack shell direction in described cylinder (1) and arrange a carbon-point (7), the length of described carbon-point (7) extends to the top of outlet (15) from water inlet (14)；Described carbon-point is filled with catalyst filling between (7).This device can effectively remove the Organic substance in black and odorous water, ammonia nitrogen, colourity, by the black sordes matter deep oxidation in water body, makes water body recover self-purification function.Whole system stable operation, efficient, convenient, floor space is little, economical and green.
Description
Technical field
The present invention relates to a kind of technical field of sewage, especially relate to a kind of processing means for black and odorous water.
Background technology
In mid-term in 20th century, the Times river of Britain is one of river that black smelly problem occurs the most the earliest.Last century 70
In the age, the Rhine of Germany is owing to flowing through heavy industrial district, and trade effluent enters the Rhine, and its pollution has also reached peak.Simultaneously
Phase the U.S. river, Chicago, river, Delaware etc., also because suffering that severe contamination causes water body long-term black smelly.In Chinese Urbanization and
During process of industrialization is accelerated, owing to water pollution control is delayed with control measures, or limited in one's ability and low SI, one
A little urban water-body especially small and medium-sized cities water bodys, are directly becoming primary discharge passage and the place of industry, agricultural and sanitary wastewater,
Cause urban water-body large area contaminated, cause body eutrophication, form black and odorous water.So-called " black smelly ", principally falls into ring
Border view, physical index category.Refer to that visually river water presents the obvious abnormal color produced because of pollution (typically
Black or blacking up color), produce simultaneously and cause people to do not feel like oneself the abnormal smells from the patient even detested in olfactory sensation, be the aesthetic pollution of water body
Modal a kind of phenomenon.The black smelly phenomenon in China river occurs in Suzhou River the earliest, subsequently the Qinhuaihe River in Nanjing, Suzhou
, all there is black smelly phenomenon in various degree in outer fosse, the Huang Xiaohe in Wuhan and the inland river etc. in Ningbo.In recent decades, black smelly water
Scope and the degree of body are constantly aggravated, and in major part section, city, the whole nation, the water body overwhelming majority flowing through busy areas is subject to
Pollution in various degree.Two grades of the most each large watershed are more prominent with the black smelly problem in three grades of tributaries, and degradation by
Year improves.Such as Huaihe River, within 2014, National Environmental quality condition publication data show, master stream water quality whole year all more than IV class water,
But the bad V class water body of fork is more than 23%;In each big water system, the bad V class water quality level in Haihe River is the highest, state's control section prison
Survey data show, bad V class in master stream reaches 37%, bad V class in tributary reaches 44%.
Black and odorous water mainly water hypoxia causes, also the most relevant with body eutrophication and bed mud deposition.Country
Great water special project correlational study result shows, when dissolved oxygen is reduced to 2.0 mg/L, water body will be in anaerobic condition.Work as dissolving
When oxygen is 3mg/L ~ 5mg/L, Organic Pollutants In Water and ammonia-nitrogen content the most also can exceed surface water V class standard, present
Color has taste state, but with the presence of aquatile;When dissolved oxygen is more than 6 mg/L, water body is in aerobic state, organic matter degradation
Dramatically increasing with ammonia oxidation speed rate, water body starts have self-purification capacity.
The black-odor control of city river follows " external source reduction of discharging, endogenous desilting, purification of water quality, clear water supply, ecological recovery "
Technology path.Wherein external source reduces discharging and endogenous desilting is basis and premise, and purification of water quality is interim means, and hydrodynamic force is improved
Technology and ecological recovery are long-acting safeguards.
One is external source interrupter technique: external source block include city cut dirt receive pipe dough-making powder source control two kinds of situations.For shortage
Improve the water body of sewage collection system, by the sewage conduct built and transformation water body is littoral, sewage is dammed and includes sewage receipts in
Collection and processing system, cut down the directly discharge of pollutant from source.Carry out cutting dirt for the condition that there is no at present and receive the sewage of pipe,
Efficient primary reinforcement sewage disposal technology or technique can be used in position, rapidly and efficiently remove the pollutant in water, it is to avoid sewage
The in line pollution to water body.City surface source pollution is mainly derived from the pollutant contained in rainfall runoff, and it is main that it controls technology
Technology and ecological revetment technology etc. is controlled including the low impact in various cities exploitation (such as sponge city) technology, early-stage rainwater.City
The rubbish etc. of water body periphery is the important sources of area source pollutants, and therefore the cleaning of water body periphery rubbish is that pollution of area source controls
Important measures.
Two is endogenous control technology: technology of desilting and dredging generally has two kinds: one is to drain desilting after lake/river;Another
Plant is directly to remove mud from water with dredger.The range of application of the latter is relatively wide, and river,lake and reservior all can use it.Desilt and dredge energy
Relatively quickly improve water quality, but desilting process enters water body in a large number because disturbance is easily caused pollutant, has influence on water ecology system
Stablizing of system, thus there is certain ecological risks, it is impossible to as the Long term control measure of a kind of polluted-water.
Three is water purification technology: the water purification technology of city black and odorous water specifically includes that artificial aeration's oxygenation (is passed through
Air, pure oxygen or ozone etc.), Dissolved Oxygen in Water concentration and oxidation-reduction potential can be improved, alleviate black and odorous water situation.Germany
Thayer river, Britain Times river, Australia's Swan River, the Suzhou River etc. of China all have employed the side of aeration oxygen replenishing in administering
Method.Flocculation sediment technology is directed in the water body of urban polluted river add the medicaments such as iron salt, calcium salt, aluminium salt, is allowed to and water body
Middle dissolved phosphorus hydrochlorate forms insoluble solid and is precipitated in riverbed bed mud.But it should be noted that the expense of chemical flocculation
Higher, and produce more deposit, some chemical agent has certain toxicity, can form secondary when environmental condition changes dirty
Dye.Artificial Wetland Techniques is the technology utilizing soil microorganism plant ecosystem to be removed nutritive salt, uses more
Free water surface wetland or current wetland, wetland plant may select submerged plant or emergent aquactic plant.Ecological floating island is a kind of through artificial
Design-build, float on for animals and plants and growth of microorganism, the biological and ecological facility multiplied, perch on the water surface, by building water
Pollutant in water body are ingested, are digested by territory ecosystem, degraded etc., it is achieved purification of water quality.Stabilization pond is a kind of artificial-strengthening
The water purification technology that measure combines with self-purification function, such as many pools technology and Aquatic-plant Pond technology etc..Available
Polluted-water is purified by the littoral multiple natural pools of water body or artificial pool.
Four is hydrodynamic force improving environment: water transfer not only can be by pollutant dense in a large amount of clean water source diluting black and odorous waters
Degree, and the diffusion of pollutant can be strengthened, purify and export, for receiving the city that dirty load is high, hydrodynamic force is not enough, environmental carrying capacity is low
City's black and odorous water regulation effect is obvious.But calling clean water to improve quality of river water is the waste to water resource, should use as far as possible
Unconventional water source, such as recycled water and making use of rain and flood.To prevent from introducing new polluter during water transfer simultaneously.
Five is Ecological recovery technology: black and odorous water phenomenon causes algae to break out often caused by concentration of nitrogen and phosphorus in water is higher
Secondary problem, causes water quality deterioration, Algae toxins problem and other hydrobiological mortalities, then causes black smelly recurrence.City
River course, city eutrophication control it is crucial that the control of phosphorus, in current sewage disposal plant effluent standard, the index limits of phosphorus is far above
Surface water standard limited value.Therefore, limit phosphorus in local implementation region with good conditionsi or raising sewage total phosphorus discharge standard is extremely to have
The measure of effect.The phosphorus entering water body is deposited in bed mud with phos-phate forms mostly, therefore keeps cement interface alkalescence, has
Oxygen condition is the main behave that river course eutrophication controls.Algal grown Artificial Control technology includes various physics, chemistry and life
Thing technology.Physical control technology includes that algae is directly collected and kills algae etc. with ultraviolet, chemical control technology include adding inorganic or
Organic pressing down (killing) algae agent, BIOLOGICAL CONTROL technology includes planting algal control water plant or throwing in food algae Fish etc..These measures are general
Use when emergent.Water Ecological Recovery includes water plant and the reparation of aquatic animal (such as Fish, zoobenthos etc.) food chain
Build with Hydrology Ecosystem System.Utilize the food chain that ecological principle builds, can persistently remove in urban water-body pollutant and
Nutrient, improves water body habitat.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, it is provided that the Organic substance in a kind of effective removal black and odorous water, ammonia nitrogen, color
Degree, by the black sordes matter deep oxidation in water body, the dissolved oxygen during aeration improves water simultaneously, makes water body recover self-purification function.Whole
Individual system stable operation, efficient, convenient, floor space little, economical and green for black and odorous water processing means and catalysis thereof
Agent particle preparation method.
For realizing the object of the invention, it is provided that techniques below scheme: a kind of for black and odorous water processing means, including cylinder
Body (1), be positioned at cylinder (1) bottom water inlet (14), air inlet (17) and be positioned at cylinder top outlet (15) and row
QI KOU (12), it is characterised in that be parallel to stack shell direction in described cylinder (1) and a piece carbon-point (7) is set, described carbon-point (7)
Length extends to the top of outlet (15) from water inlet (14)；Described carbon-point is filled with catalyst particle between (7).
As preferably, described carbon-point (7) is held within outlet (15) and the porous plate up and down of water inlet (14) top
Between (6a, 6b).
As preferably, described upper and lower porous plate (6a, 6b) is fixed seat (10) by triangle and is fixed on the inwall of cylinder (1)
On.
As preferably, the bottom that carbon-point (7) passes the lower porous plate (6b) near water inlet (14) place is solid by carbon-point
Determine plate (9) to be fixed on this block porous plate (6)；Pass the upper end of the upper porous plate (6a) near outlet (15) by U-shaped
Pipe clamp (11) is fixed on porous plate (6a).
As preferably, described cylinder (1) is placed on base plate (4)；Described cylinder (1) top is openable end socket (3),
Described end socket (3) is sealed on cylinder (1) by fast therapy of waking up the patient from unconsciousness blue (2).
As preferably, described air inlet (17) connects the air intake installation (5) stretching into cylinder (1) inside, described air intake installation
(5) it is connected by the fixing pipe (8) of air inlet is fixing with the inwall of cylinder (1) in cylinder (1) inside.
As preferably, described cylinder (1) top also sets up cable interface (13).
As preferably, described cylinder (1) bottom arranges hand hole (16).
For realizing another object of the present invention, it is provided that a kind of catalyst particle preparation side for black and odorous water processing means
Method, it is characterised in that comprise the following steps:
(1) prepared by raw material: electricity the raw-material component of catalyst catalyst and the percetage by weight of each component be:
Coal dust 60 ~ 80%；
Butter of antimony. 1 ~ 5%；
Butter of tin 1 ~ 5%；
Iron powder 8 ~ 15%；
Aluminium powder 10 ~ 15%；
(2) by raw mill, final granularity≤5um is controlled.It is that 2:1 carries out mixing material powder and methane-nitrogen ratio
Gas-insulated air is heated to 1200 DEG C, weighs ethanol and 1% hard pitch of raw-material weight 50%, hard pitch is added wine
In essence, and add the sagging inhibitor of 0.1% and the carbonization accelerator of 0.1%, stir.It is subsequently adding the tar 1% of milled, limit
Grinding limit stirs, and makes mixed slurry；
(3) mixed slurry is spray-dried, it is ensured that particle size range controls, at 0.1 ~ 80um, to be then charged into Φ 600*1500's
In gum cover mould, at 80 ~ 120MPa condition of high voltage compacted under, make moulded products, after crushing and screening, it is ensured that moulded products
Cylinder or the length of side for a diameter of 0.1 ~ 800mm are the cube of 0.1 ~ 800mm；
(4) moulded products loading roasting kiln roasting, sintering temperature is 800 DEG C, and roasting time is 300 hours, and roasting completes
After use softening point to be less than 70 DEG C again soft pitch impregnate.The most again carry out roasting and dipping, enter the most altogether
Row 1 time, it is ensured that bulk density ＞ 1.5 of material；
(5) again to roasting with impregnated after material carry out carbonization at 2900 DEG C, carbonization time is 10 days.Roasting and carbonization
Cheng Jun is carried out under anaerobic.After carbonization completes, cool down with furnace temperature, then carry out crushing and screening i.e. prepared electricity catalyst catalyst one-tenth
Product.
Operation principle:
Electrode reaction by there being catalysis activity directly or indirectly produces hydroxyl radical free radical at normal temperatures and pressures, so that difficult biological
The Organic substance of degraded is converted into biodegradable Organic substance, or the Organic substance of difficult degradation changes into carbon dioxide and water.
Dominant response:
(3) comprehensive function of above procedure, Organic substance, ammonia nitrogen and the total nitrogen in degradation water.
The method have the benefit that this device is basically an electrolyzer, mainly by shell of reactor, carbon electrode with
And catalyst composition, cylindrical reactor can make water-flow equation more uniform, make treatment effect more preferable.
Accompanying drawing explanation
Fig. 1 is the external structure schematic diagram of the present invention.
Fig. 2 is the cross section structure schematic diagram of the present invention.
Fig. 3 be the present invention preferred version in perforated plate construction schematic diagram.
Fig. 4 is the air intake installation venthole schematic diagram of the present invention.
Fig. 5 is the structural representation of one specific embodiment of the present invention.
Detailed description of the invention
Below in conjunction with the accompanying drawings, the present invention is specifically described.
By attached Fig. 1 and 2 it will be seen that the present invention provide a kind of novel process device for processing black smelly waste water,
Including cylinder 1, it is positioned at the water inlet 14 bottom cylinder 1, air inlet 17 and is positioned at outlet 15 and the air vent at cylinder top
12, in cylinder 1, it is parallel to stack shell direction a piece carbon-point 7 is set, the length of carbon-point 7 extends to outlet 15 from water inlet 14
Top；It is filled with catalyst particle between carbon-point 7.
Carbon-point 7 is held within the porous plate up and down (6a, 6b) of the top of water inlet 14 and outlet 15.Porous up and down
Plate (6a, 6b) is fixed seat 10 by triangle and is fixed on the inwall of cylinder 1.Carbon-point 7 passes the lower porous plate near water inlet 14
The bottom of 6b is fixed on lower porous plate 6b by carbon-point fixed plate 9；Pass the portion of the upper porous plate 6a near outlet 15
Divide and be fixed on upper porous plate 6a by U-tube folder 11.Upper and lower porous plate (6a, 6b) is one and is drilled with the most lacunary above
Plate, water and gas all can pass through, and beneath air intake installation 5 gas out passes through upper and lower porous plate together with the water of aeration zone
(6a, 6b) enters into reaction zone.
Cylinder 1 is placed on base plate 4；Cylinder 1 top is openable end socket 3, and end socket 3 is sealed in by fast therapy of waking up the patient from unconsciousness orchid 2
On cylinder 1.Air vent 12 and cable interface 13 are arranged on end socket 3.
The air intake installation 5 within cylinder 1 is stretched in air inlet 17 connection, and air intake installation 5 is fixed by air inlet inside cylinder 1
Pipe 8 is fixing with the inwall of cylinder 1 to be connected.
Cylinder 1 top also sets up cable interface 13, and power circuit is connected in cylinder 1 by cable interface 13.Cylinder 1 end
Portion arranges hand hole 16, is used for loading and unloading catalyst particle.
The external dosing pump of water inlet 14, the external Aeration fan of air inlet 17.
Preferably cylinder 1 uses hydrostatic column to be made by rustless steel as reactor, wall body, is provided with in cylinder
A piece i.e. carbon-point 7 of electrode bar, stainless steel casing also can use as electrode in addition.It is only limitted to compared to electrode in traditional reactor
Being installed on inside and the single design of material, in the application, electric power polarity and electrode material can change the most flexibly, and one
Simply power cathode is connected, by outside cylinder with the electrode bar of axle center (central point of porous plate (6a, 6b) i.e. up and down) in the case of as
Wall connects positive source；Under special circumstances, electrode bar can be connect positive pole, cylinder body outer wall is connect negative pole, to reach preferably to process
Effect.
This device uses bottom water inlet, and the mode of top water outlet operates, and is locking device, and device bottom is provided with aerator
(i.e. air intake installation 5), the venthole of preferred air intake installation 5 designs, as shown in Figure 4 down.
The work process of this device is as follows:
During actual motion, arrange storage tank 18, storage tank 18 includes the outlet 19 of the water inlet 21 on top, bottom, storage tank
Bottom outlet is intake by the water inlet 14 bottom pipeline connector drum 1, and now sewage will be filled with whole reaction zone.At aeration
Under the effect of device (i.e. air intake installation 5), the water in device enters into the region (i.e. reaction zone) at carbon-point (7) place to carry out electricity and urges
When changing reaction, water has already been through abundant aeration, and catalyst particle is distributed evenly in whole under the effect of the fluid risen
Reaction zone.
After entering reaction zone, due to the air intake installation 5 bottom cylinder 1, sewage enters reaction zone and can be mixed uniformly, and opens
Begin to react.Traditional graphite electrode rod selected by electrode bar carbon-point (7) in the reaction region, and cost is the highest, and intensity is big, and catalysis is lived
Property is good, good conductivity, corrosion resistance are strong.Catalyst particle is special electric catalyst catalyst, treatment effeciency two dimension electricity relatively in the past
Pole reactor and common 3 D electrode reactor have greatly improved, and sewage here can fully mix due to aeration simultaneously
Even, improve mass-transfer efficiency.Therefore the processing means after improving is in reaction zone, and sewage treating efficiency has very than traditional reactor
Big raising, and ammonia nitrogen and the Organic substance in water body can effectively be removed.
Cylinder 1 bottom is provided that a fairly simple tubular type aerator 5, have simple in construction, coefficient of oxygen utilization high,
Dependable performance, pore are not easily blocked, sewage does not pours in down a chimney, hoop uniform force, life-span length, convenient to install and maintain, system price is low
The feature such as honest and clean, has broken away from that conventional ceramic aerator cost is high, the deficiency of easy fouling.
Being exhalant region on cylinder 1 top, sewage enters exhalant region via reaction zone, and after entering exhalant region, sewage is via going out
The mouth of a river 15 is discharged.Outlet 15 arranges pipeline and connects the circulation port 20 of storage tank 18, and for influent quality, this complete equipment requires
Good pH is 5 ~ 10.The technical process of this device is: from the pending waste water of black and odorous water outflow by entering bottom cylinder 1
It is internal that the mouth of a river 14 enters cylinder 1, proceeds by aeration by air inlet 17 and air intake installation 5 simultaneously, keep electric current density be 10 ~
30A/m2, voltage range is 2.5 ~ 5 V.Electric current density refers to by the electric current of water body divided by the numerical value of the sectional area of cylinder, electricity
Pressure refers to the magnitude of voltage being added between equipment outer wall and carbon electrode, and no matter how electrode becomes, and electric current density and voltage are all at this
In the range of change.
Embodiment 2: a kind of catalyst particle preparation method for black and odorous water processing means, comprises the following steps:
(1) prepared by raw material: electricity the raw-material component of catalyst catalyst and the percetage by weight of each component be:
Coal dust 60%；
Butter of antimony. 5%；
Butter of tin 5%；
Iron powder 15%；
Aluminium powder 15%；
(2) by raw mill, final granularity≤5um is controlled.It is that 2:1 carries out mixing material powder and methane-nitrogen ratio
Gas-insulated air is heated to 1200 DEG C, weighs ethanol and 1% hard pitch of raw-material weight 50%, hard pitch is added wine
In essence, and add the sagging inhibitor of 0.1% and the carbonization accelerator of 0.1%, stir.It is subsequently adding the tar 1% of milled, limit
Grinding limit stirs, and makes mixed slurry；
(3) mixed slurry is spray-dried, it is ensured that particle size range controls, at 0.1 ~ 80um, to be then charged into Φ 600*1500's
In gum cover mould, at 80 ~ 120MPa condition of high voltage compacted under, make moulded products, after crushing and screening, it is ensured that moulded products
Cylinder or the length of side for a diameter of 0.1 ~ 800mm are the cube of 0.1 ~ 800mm；
(4) moulded products loading roasting kiln roasting, sintering temperature is 800 DEG C, and roasting time is 300 hours, and roasting completes
After use softening point to be less than 70 DEG C again soft pitch impregnate.The most again carry out roasting and dipping, enter the most altogether
Row 1 time, it is ensured that bulk density ＞ 1.5 of material；
(5) again to roasting with impregnated after material carry out carbonization at 2900 DEG C, carbonization time is 10 days.Roasting and carbonization
Cheng Jun is carried out under anaerobic.After carbonization completes, cool down with furnace temperature, then carry out crushing and screening i.e. prepared electricity catalyst catalyst one-tenth
Product.
The specific embodiment of the application:
Certain river total length 8.8km, drainage area 46.4km2.This river was two sides agricultural irrigation diversion and water drainage originally, owing to economy is sent out
Exhibition, evolves as water drainage and river course for sewage discharge.This river imports without rainwash, and source water is industrial wastewater and sanitary sewage water
The power gradient is steady, current reciprocal, and hydrodynamic condition is poor, and self-purification capacity is poor, and water body environment is affected relatively big by seasonal variations, city
Change feature obvious.In the collecting-tank of this river course pumping plant along the river there is black smelly phenomenon in water body.
Sequence number refers to table 1: experimental result table
| Sequence number | Index | Water inlet | Water outlet |
| 1 | pH | 6-9 | 6-9 |
| 2 | COD (COD) | ≤150mg/L | ≤50mg/L |
| 3 | Ammonia nitrogen (NH3-N) | ≤25mg/L | ≤5mg/L |
| 4 | Total nitrogen (TN) | ≤40mg/L | ≤15mg/L |
| 5 | Float (SS) | ≤80mg/L | ≤10mg/L |
| 6 | Colourity | ≤200 | ≤1 |
Glass electrode method during wherein pH uses GB/T 920, COD uses the spectrophotography in GB/T 1901-89, ammonia nitrogen
Using the spectrophotography in GB/T 479, total nitrogen uses the spectrophotography in GB/T 11894, and float uses GB/
Gravimetric method in T11901, colourity uses the extension rate method in GB/T11903.
Claims (9)
1., for a black and odorous water processing means, including cylinder (1), it is positioned at the water inlet (14) of cylinder (1) bottom, air inlet
(17) and be positioned at outlet (15) and the air vent (12) at cylinder top, it is characterised in that be parallel in described cylinder (1)
Stack shell direction arranges a carbon-point (7), and the length of described carbon-point (7) extends to the top of outlet (15) from water inlet (14)；
Described carbon-point is filled with catalyst particle between (7).
One the most according to claim 1 is used for black and odorous water processing means, it is characterised in that described carbon-point (7) is fixed on
It is positioned between the porous plate up and down (6a, 6b) of outlet (15) and water inlet (14) top.
One the most according to claim 1 is used for black and odorous water processing means, it is characterised in that described upper and lower porous plate
(6a, 6b) fixes seat (10) by triangle and is fixed on the inwall of cylinder (1).
A kind of new device processed for black and odorous water, it is characterised in that carbon-point (7) passes and leans on
The bottom of the lower porous plate (6b) at nearly water inlet (14) place is fixed on this block porous plate (6) by carbon-point fixed plate (9)；Wear
The upper end going out the upper porous plate (6a) near outlet (15) is fixed on porous plate (6a) by U-tube folder (11).
5. according to claim 1 one kind for black and odorous water processing means, it is characterised in that described cylinder (1) is placed on base plate
(4) on；Described cylinder (1) top is openable end socket (3), and described end socket (3) is sealed in cylinder by fast therapy of waking up the patient from unconsciousness blue (2)
(1) on.
6. according to claim 1 one kind for black and odorous water processing means, it is characterised in that described air inlet (17) connection is stretched into
The air intake installation (5) that cylinder (1) is internal, described air intake installation (5) is internal by air inlet fixing pipe (8) and cylinder at cylinder (1)
(1) inwall is fixing to be connected.
One the most according to claim 1 is used for black and odorous water processing means, it is characterised in that described cylinder (1) top is also
Cable interface (13) is set.
One the most according to claim 1 is used for black and odorous water processing means, it is characterised in that described cylinder (1) bottom sets
Put hand hole (16).
9. the catalyst particle preparation method for black and odorous water processing means as described in one of claim 1 ~ 8, its
It is characterised by comprising the following steps:
(1) prepared by raw material: electricity the raw-material component of catalyst catalyst and the percetage by weight of each component be:
Coal dust 60 ~ 80%；
Butter of antimony. 1 ~ 5%；
Butter of tin 1 ~ 5%；
Iron powder 8 ~ 15%；
Aluminium powder 10 ~ 15%；
(2) by raw mill, final granularity≤5um is controlled；
It is that the gas-insulated air that 2:1 carries out mixing is heated to 1200 DEG C material powder and methane-nitrogen ratio, weighs raw material
The ethanol of weight 50% and 1% hard pitch, add hard pitch in ethanol, and adds the sagging inhibitor of 0.1% and the carbon of 0.1%
Change accelerator, stir；
Being subsequently adding the tar 1% of milled, grinding limit, limit stirs, and makes mixed slurry；
(3) mixed slurry is spray-dried, it is ensured that particle size range controls, at 0.1 ~ 80um, to be then charged into Φ 600*1500's
In gum cover mould, at 80 ~ 120MPa condition of high voltage compacted under, make moulded products, after crushing and screening, it is ensured that moulded products
Cylinder or the length of side for a diameter of 0.1 ~ 800mm are the cube of 0.1 ~ 800mm；
(4) moulded products loading roasting kiln roasting, sintering temperature is 800 DEG C, and roasting time is 300 hours, and roasting completes
After use softening point to be less than 70 DEG C again soft pitch impregnate；
The most again carry out roasting and dipping, carry out the most altogether 1 time, it is ensured that bulk density ＞ 1.5 of material；
(5) again to roasting with impregnated after material carry out carbonization at 2900 DEG C, carbonization time is 10 days, roasting and carbonization
Cheng Jun is carried out under anaerobic, after carbonization completes, cools down with furnace temperature, then carries out crushing and screening i.e. prepared electricity catalyst catalyst one-tenth
Product.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106693878A (en) * | 2017-01-23 | 2017-05-24 | 江苏省农业科学院 | Filler particles for improving quality of aquaculture water and purifying tail water, preparation method of filler particles, and reactor comprising filler particles |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| MX2014002238A (en) * | 2014-02-26 | 2015-08-26 | Univ Nac Autónoma De México | Method for the manufacture of dimensionally stable electrodes (anodes) of tin-antimony-ruthenium useful in the treatment of residual waters and products obtained by the same. |
| CN105110426A (en) * | 2015-09-24 | 2015-12-02 | 南通科技职业学院 | Preparation method of novel filling particle electrode material for treating organic wastewater |
| CN105236525A (en) * | 2015-11-15 | 2016-01-13 | 江苏丹诚环境工程有限公司 | Electro-catalysis treatment device for seawater circulation culture system |
| CN105289646A (en) * | 2015-11-15 | 2016-02-03 | 江苏丹诚环境工程有限公司 | Method for producing electrical accelerant catalyst of special type carbon material |
| CN205170460U (en) * | 2015-11-15 | 2016-04-20 | 江苏丹诚环境工程有限公司 | A electro -catalysis processing apparatus for sea water circulation farming systems |
-
2016
- 2016-08-22 CN CN201610699564.8A patent/CN106167289A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| MX2014002238A (en) * | 2014-02-26 | 2015-08-26 | Univ Nac Autónoma De México | Method for the manufacture of dimensionally stable electrodes (anodes) of tin-antimony-ruthenium useful in the treatment of residual waters and products obtained by the same. |
| CN105110426A (en) * | 2015-09-24 | 2015-12-02 | 南通科技职业学院 | Preparation method of novel filling particle electrode material for treating organic wastewater |
| CN105236525A (en) * | 2015-11-15 | 2016-01-13 | 江苏丹诚环境工程有限公司 | Electro-catalysis treatment device for seawater circulation culture system |
| CN105289646A (en) * | 2015-11-15 | 2016-02-03 | 江苏丹诚环境工程有限公司 | Method for producing electrical accelerant catalyst of special type carbon material |
| CN205170460U (en) * | 2015-11-15 | 2016-04-20 | 江苏丹诚环境工程有限公司 | A electro -catalysis processing apparatus for sea water circulation farming systems |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106693878A (en) * | 2017-01-23 | 2017-05-24 | 江苏省农业科学院 | Filler particles for improving quality of aquaculture water and purifying tail water, preparation method of filler particles, and reactor comprising filler particles |
| CN106693878B (en) * | 2017-01-23 | 2018-07-10 | 江苏省农业科学院 | Aquaculture water quality improves and tail water purification filler particles, preparation method and includes its reactor |
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