CN209602282U - A kind of sanitary sewage deodorization direct purification separation equipment - Google Patents
A kind of sanitary sewage deodorization direct purification separation equipment Download PDFInfo
- Publication number
- CN209602282U CN209602282U CN201920294448.7U CN201920294448U CN209602282U CN 209602282 U CN209602282 U CN 209602282U CN 201920294448 U CN201920294448 U CN 201920294448U CN 209602282 U CN209602282 U CN 209602282U
- Authority
- CN
- China
- Prior art keywords
- deodorization
- water
- separator
- disinfection
- sewage
- 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.)
- Active
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 81
- 238000000926 separation method Methods 0.000 title claims abstract description 56
- 238000004332 deodorization Methods 0.000 title claims abstract description 55
- 238000000746 purification Methods 0.000 title claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 116
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 49
- 238000005345 coagulation Methods 0.000 claims abstract description 38
- 230000015271 coagulation Effects 0.000 claims abstract description 38
- 239000005416 organic matter Substances 0.000 claims abstract description 37
- 239000002002 slurry Substances 0.000 claims abstract description 29
- 230000001351 cycling effect Effects 0.000 claims abstract description 3
- 230000007246 mechanism Effects 0.000 claims description 43
- 238000002156 mixing Methods 0.000 claims description 31
- 229910001385 heavy metal Inorganic materials 0.000 claims description 22
- 239000003814 drug Substances 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 12
- 230000008719 thickening Effects 0.000 claims description 12
- 238000000227 grinding Methods 0.000 claims description 10
- 238000001556 precipitation Methods 0.000 claims description 10
- 230000001590 oxidative effect Effects 0.000 claims description 9
- 238000005086 pumping Methods 0.000 claims description 9
- 239000004744 fabric Substances 0.000 claims description 8
- 238000009434 installation Methods 0.000 claims description 8
- 238000004880 explosion Methods 0.000 claims description 7
- 239000002893 slag Substances 0.000 claims description 7
- 239000002781 deodorant agent Substances 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 230000001737 promoting effect Effects 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 12
- 238000000034 method Methods 0.000 description 20
- 230000008569 process Effects 0.000 description 9
- 239000007789 gas Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 239000010801 sewage sludge Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 239000003570 air Substances 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 150000002736 metal compounds Chemical class 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000006424 Flood reaction Methods 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 244000000010 microbial pathogen Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- -1 phosphorus compound Chemical class 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Treatment Of Sludge (AREA)
Abstract
A kind of sanitary sewage deodorization direct purification separation equipment, including bracket and the quick-fried crushing device of the sundries being fixed on bracket, sterilize deodorization coagulation device, turbid separator, organic matter body refuse separator, the sewage discharge port of the quick-fried crushing device of sundries is connected with the sewage feed inlet of disinfection deodorization coagulation device, the discharge port of disinfection deodorization coagulation device is connected with the feed inlet of turbid separator, the external cycling use of water pond of the water outlet of turbid separator or tank, the slurry outlet of turbid separator bottom is connected with the feed inlet of organic matter body refuse separator, the outlet of sewer of organic matter body refuse separator is connected by pipeline with the sewage feed inlet of disinfection deodorization coagulation device.The utility model can retain the energy of organic matter and organic matter in sewage;The sewage of impure complex working condition can be handled;Filter efficiency is high, and filtration yield is big;Cost of equipment, operating cost are low.
Description
Technical field
The utility model relates to environmental protection equipment technical fields, and in particular to a kind of sanitary sewage deodorization direct purification separation dress
It is standby.
Background technique
It is well known that sanitary sewage is the sewage that people's daily life generates, ingredient mainly includes various washes
With sewage, rubbish, excrement etc..These substances may be summarized to be organic matter, inanimate matter, a small amount of inorganic salts and heavy metal substance.
If these sanitary sewages are directly discharged into water body without processing, following problem will lead to: first, aerobic Assessment of Organic Pollution,
Aerobic decomposition, causes oxygen content of water to decline under the biological chemistry action of microorganism, and water quality is deteriorated;Second, water body is rich
Nutrient laden, nitrogen in organic matter, phosphorus compound enters water body leads to water eutrophication;Third, organic matter is in anoxic in water body
Corruption is decomposed under environment, is generated foul gas, is seriously affected surrounding enviroment;4th, stench leads to pathogenic microorganism mass propagation,
Aggravate surrounding enviroment to deteriorate;5th, if micro heavy pollutant will be led without disposition direct emission water body in sanitary sewage
Heavy metal pollution diffusion is caused, under the heavy metal accumulation effect of plant, exists into the hidden danger in human foods chain, eventually leads to
The mankind are endangered by heavy metal pollution.
There are many processing mode of sanitary sewage at present, mainly pass through tamisage, the precipitation method, filtration method, gas floatation process, floating method
The solid pollution substance in water removal in suspended state is removed with hyperfiltration;Then using microorganism in aerobic environment/anaerobic environment
Under metabolism, be metabolized the organic pollutant of colloidal state in sewage and be converted into stable innocuous substance;Decline uses
Method of chemical treatment such as is neutralized, is adsorbed at the various forms polluter in analysis sewage.
CN 201720177421.0 discloses a kind of combined type sanitary sewage integration apparatus, and tank body is separated into aeration
Area and oxygen fluidization regions, settling zone and filtering area handle country life sewage using A/O method;201601839798.8 disclosure of CN
A kind of integrated apparatus of residents country life sewage treatment, by cylinder-shaped body be separated into two aerobic zones, two detest
Oxygen area and a settling zone handle country life sewage using double A/O methods;CN 201611266498.1 discloses a kind of rural area
Domestic sewage processing system, including setting pot, conditioning tank, hydrolysis acidification pool, SBR biochemical reaction tank etc. handle township using SBR method
Village's sanitary sewage;CN 201620051932.3 discloses a kind of rural compact community stain disease low energy consumption ecological wet land treating system,
Including sedimentation basin, aeration oxidation pool, secondary settling tank, artificial wet land system etc., the treatment effect of sewage is improved using artificial swamp,
Reduce energy consumption.
The substantial treatment of these traditional disposing techniques mainly utilizes microbial fermentation (aerobic fermentation/anaerobic fermentation) to drop
The organic matter of sewage is solved, realizes sanitary sewage separation at filter residue and clear water.There are the following problems for these traditional disposing techniques, the
One, during handling organic matter using microbial technology, generate toxic and harmful gas, compound and a large amount of microbial bacterias
Group causes substantive harm to ambient air, water, soil;Second, wasting can fire directly as ecologic biological fertilizer or low-carbon
The organic matter of material;Third, generation are largely difficult to be utilized, sludge based on cenobium pollutant, these are difficult to dry dirt
It is burned after mud landfill or solidification landfill or drying and produces serious secondary pollution problem;4th existing sanitary sewage disposal is set
It applies and occupies a large amount of fields with equipment and the pollution sources new to formation, substantive damage is produced to the water, soil, gas of environment.
Summary of the invention
Technical problem to be solved in the utility model is to overcome the shortcomings of above-mentioned background technique, provides a kind of can be reserved for
Organic matter material in sanitary sewage, remove heavy metal pollution in sanitary sewage, directly by complicated sanitary sewage separation at
Organic matter filter residue, heavy metal, clear water, and investment operation is at low cost, be not take up field, treatment effeciency is high, water quality can qualified discharge,
Treatment process be not bullied temperature influence sanitary sewage deodorization direct purification separation equipment.
The utility model solve its technical problem the technical solution adopted is that, a kind of separation of sanitary sewage deodorization direct purification
Equipment, including bracket and the quick-fried crushing device of the sundries being fixed on bracket, disinfection deodorization coagulation device, turbid separator, organic
Matter body refuse separator, the sewage feed inlet of the sewage discharge port of the quick-fried crushing device of sundries and the disinfection deodorization coagulation device
It is connected, the discharge port of the disinfection deodorization coagulation device is connected with the feed inlet of the turbid separator, the turbid
The external cycling use of water pond of the water outlet of separator or tank, slurry outlet and the organic matter of turbid separator bottom
The feed inlet of body refuse separator is connected, and the outlet of sewer of the organic matter body refuse separator passes through pipeline and the disinfection
The sewage feed inlet of deodorization coagulation device is connected, and the external slag charge fortune storage of the slag notch of the organic matter body refuse separator is set
It applies.
Further, the quick-fried crushing device of the sundries includes the quick-fried broken suction pump of sundries, flowmeter, pipeline and/or dirty tank of receiving, described
The quick-fried broken suction pump of sundries is set in sanitary sewage pond and by the sewage feed inlet phase of pipeline and the disinfection deodorization coagulation device
Connection, the flowmeter is set on the pipeline or the feed inlet of the disinfection deodorization coagulation device, the quick-fried broken suction of sundries
Pump be set to it is described receive in dirty tank, broken send the sundries received in the sanitary sewage received in dirty tank is quick-fried for the suction of suspended mixture to disappearing
The feed inlet of malicious deodorization coagulation device, it is described receive dirty tank be independently arranged or with the disinfection deodorization coagulation device integral type be arranged.
Further, the disinfection deodorization coagulation device includes disinfection flocculant basin, meter charging gear, one or more phases
The vortex mixing tank of connection;The disinfection flocculant basin is equipped with disinfection deodorant basin and flocculant basin, and the disinfection is anti-
Smelly dose of storage Cans and meter charging gear, flocculant basin and meter charging gear or the disinfection flocculant basin and meter charging gear
It is set to the top of vortex mixing tank, the discharge port of the disinfection flocculant basin is connected with the feed inlet of the meter charging gear
It is logical, it is connected in the discharge port and the feed end of the vortex mixing tank of the meter charging gear;Or disinfection deodorant storage Cans, wadding
Solidifying agent basin or disinfection flocculant basin are independently arranged, and the discharge port of basin is connected with the feed inlet of meter charging gear, and meter is given
Expect to be connected in the discharge port and the feed end of vortex mixing tank of device.
Further, the turbid separator includes muddy water separation chamber, muddy water separator, slurry thickening cone, the muddy water
The import of separation chamber is connect with the disinfection deodorization coagulation device discharge port, and the slurry thickening cone is arranged at muddy water separation chamber bottom
Portion, the muddy water separator setting separate chamber outlet end in muddy water, and flocculated slurry is settled before muddy water separator, and in slag
Starch concentration deposition in thickening cone.
Further, muddy water separator >=2 realize multistage muddy water separation to sewage, improve separative efficiency and effect
Fruit.
Further, the organic matter body refuse separator includes promoting drainage mechanism, slag-liquid separation mechanism, negative pressure pumping water machine
Structure, power mechanism;The promotion drainage mechanism is connected with slag-liquid separation mechanism, the water outlet and negative pressure of the slag-liquid separation mechanism
The inlet pipeline of water pumping mechanism is connected;The promotion drainage mechanism includes shell, main shaft and discontinuous helical blade, the non-company
Continuous helical blade is fixed on the main shaft and is located in the shell;The slag-liquid separation mechanism includes sandwich shell, filtering
Cloth, the filter are fixed in the semicircle grate plate slot of sandwich shell, the sandwich shell and the promotion drainage mechanism
Shell is fitted close, and compresses the filter cloth, realizes mud-water separation;The negative pressure pumping water mechanism includes that centrifugal high pressure draws water
Pump, pipeline form underbalance effect by the suction of centrifugal high pressure suction pump at sandwich shell, accelerate sewage sludge or slurries
Middle pulp water separation.
Further, middle water purifier, the water inlet of the middle water purification installation and the turbid separator are additionally provided with
Water outlet be connected;The middle water purification installation include medicament basin, meter charging gear, vortex mixing tank, cleaned filter chamber,
Non-sticky filter, slurry precipitation bucket, the medicament basin, meter charging gear are set to the top of the vortex mixing tank, the medicine
The discharge port of agent basin is connected with the feed inlet of the meter charging gear, the discharge port of the meter charging gear and vortex mixing
It is connected in the feed end of tank;The discharge port of the vortex mixing tank is connected to the cleaned filter chamber, the non-sticky filter
Chamber outlet end is separated set on the muddy water;The slurry precipitation bucket is set to the cleaned filter chamber bottom, the slag of reactive crystallization
Slurry is deposited in slurry precipitation bucket before non-sticky filter.
Further, middle water purification installation is heavy metal ion remove device, by the way that heavy metals removal medicament, realization pair is added
The heavy metal ion of middle water is reacted and crystalline deposit, Water warfare in realization.
Further, be additionally provided with oily-water seperating equipment, the oily-water seperating equipment be set to the quick-fried crushing device import of the sundries or
Exit can be set to oil separator or floating-oil collector, realize water-oil separating.
Further, it is additionally provided with peculiar smell catalyzing, oxidizing and purifying device, the peculiar smell catalyzing, oxidizing and purifying device includes catalysis oxygen
Change clarifier, sucktion fan and air hose;Described air hose one end respectively with disinfection deodorization coagulation device, turbid separator, middle water
Purifier, organic matter body refuse separator are connected, and the other end is connected with sucktion fan, the other end of sucktion fan and urge
Change oxidation, purification device to be connected, be drawn into after catalyzing, oxidizing and purifying device is disposed by the gas that the equipment to disposal process discharges
It is discharged into atmosphere, the pollution to reduce in treatment process, to atmosphere.
Further, the quick-fried broken suction pump of the sundries, including explosion cone, anti-blocking coarse crushing knife group, grinding knife group fine crushing, impeller,
Main shaft and shell;The explosion cone, the moving knife of anti-blocking coarse crushing knife group, the moving knife of grinding knife group fine crushing and impeller are successively from feed inlet
End starts to be fixed on main shaft, and the stationary knife of the anti-blocking coarse crushing knife group, the stationary knife of grinding knife group fine crushing are sequentially fixed on shell;
It can be achieved to there are bulk suspended matters to carry out broken disposition in the sewage sludge of suction.
Further, the muddy water separator, non-sticky filter are one of non-sticky strainer, filter cloth, filter core form, pass through big face
Long-pending strainer filter cloth structure type realizes suspended particulates and sewage separation.
Further, it is additionally provided with electric control gear or/and power generator, the electric control gear controls the operating entirely equipped, institute
It states power generator and provides electric power for field sewage treatment.
Further, it is additionally provided with water quality detecting device, the water quality detecting device is arranged in sanitary sewage deodorization direct purification
The water outlet for separating equipment, for detecting effluent quality, the water qualified discharge that guarantees that treated.
Further, sanitary sewage deodorization direct purification separation equipment can integral installation set in move vehicle or movement
It is standby upper, can the source of sewage to different zones timely disposed.
The course of work:
Sanitary sewage is after the suction of the quick-fried broken suction pump of the sundries of the quick-fried crushing device of sundries, by explosion cone, anti-blocking thick
Broken knife group, grinding knife group fine crushing realization are crushed bulk suspended matter and particle, and sanitary sewage is drawn into as suspended mixture
It receives in dirty tank, dirty tank of receiving directly is connected with disinfection deodorization coagulation device;In disinfection deodorization coagulation device, disinfection flocculant exists
Under the action of counting charging gear, it is proportionally added into medicament and is mixed to vortex mixing tank with sewage progress strength;
Mixed sewage enters turbid separator, and sewage realizes sewage by muddy water separator in muddy water separation chamber
It is separated with suspended matter, the suspended matter flocculation after separation deposits in slurry thickening cone, and is discharged into organic matter body refuse separator.
Middle water after separation, which can be directly entered, to be recycled, or is drained into middle water purifier and is further disposed;
In middle water purification installation, purification medicament is added to middle water by meter charging gear, and force in vortex mixing tank
It is stirred, then realizes water, dirty separation by non-sticky filter in cleaned filter chamber, wherein water quality realizes qualified discharge,
Sludge or slurry deposit to slurry precipitation bucket, and flow into organic matter body refuse separator;
In organic matter body refuse separator, the high-moisture percentage body refuse of deposition is promoted by negative pressure pump suction and helical blade
And squeezing action, body refuse moisture content is reduced, subsequent body refuse is facilitated further to dispose;
During disposing sewage, peculiar smell, the foul smell of generation can pass through the sucktion fan of peculiar smell catalyzing, oxidizing and purifying device
Suction, outlet after disposing into catalyzing, oxidizing and purifying device can avoid the pollution in disposal process to atmosphere;
When disposing oily wastewater, oily-water seperating equipment is set before and after the quick-fried crushing device of sundries, is realized to oil slick in sewage
Processing;
In disposition when containing heavy metal containing sewage, heavy metal ion remove device is set after middle water purification installation, passes through chemistry
The mode of reaction, realizes heavy metal compound and sewage separation, and heavy metal compound goes forward side by side one by the discharge of the slurry head of bottom
Step disposition.
The utility model has the beneficial effects that
(1) the utility model disposes sewage using flocculation and large area physical filtering mode, can retain sewage to greatest extent
The energy of middle organic matter and organic matter, the moisture percentage in sewage sludge after organic matter body refuse separator is low, can be used as methane-generating pit original
Material, organic fertilizer or even fuel carry out using energy source;
(2) disposal process uses physics, chemical mode, non-aerobic/anaerobic zymotechnique, and exhaust gas without secondary pollution generates,
The adaptability of technique is good, and treatment process is to external environment and temperature environment without particular/special requirement;The quick-fried broken suction pump of the sundries of configuration, can
The sewage of impure complex working condition is handled, equipment dependability and adaptability are improved;
(3) the non-sticky filter cloth form of " bow " or " it " font large area, In is preferably presented in muddy water separator, non-sticky filter
While ensuring sewage to suspended particulates filtering accuracy, filter efficiency and filtration yield, while muddy water separator, non-sticky mistake can be improved
Filter also uses the structure of cleaning easy to disassemble, is convenient for changing and safeguards;
(4) process device structure is simple and reliable, water energy qualified discharge during cost of equipment, operating cost are low, and treated;Phase
To sewage disposal device at present on the market, processing cost is greatly reduced;
(5) after wastewater efficient purifies equipment configurations in move vehicle or equipment, it can be directed to and be distributed township wide, at random
Village's source of sewage carries out timely efficient process, can not only reduce sewage network construction investment, while also adapting to some special operation conditions,
If mountain torrents/floods cause multiple spot source of sewage to carry out timely sewage disposal, epidemic situation is avoided the occurrence of.
Detailed description of the invention
Fig. 1 is the three dimensional structure diagram I of the utility model embodiment 1;
Fig. 2 is the three dimensional structure diagram II of the utility model embodiment 1;
Fig. 3 is the side view of the utility model embodiment 1;
Fig. 4 is the top view of the utility model embodiment 1;
Fig. 5 is the structural schematic diagram of the quick-fried broken suction pump of sundries in the utility model embodiment 1;
Fig. 6 is the structural schematic diagram of the organic matter body refuse separator in the utility model embodiment 1;
Fig. 7 is the three dimensional structure diagram of the utility model embodiment 2;
Fig. 8 is the top view of the utility model embodiment 2.
Specific embodiment
With reference to the accompanying drawings and examples, the utility model is described in further detail.
Embodiment 1
As shown in figs. 1 to 6, the utility model embodiment include bracket 6 and the fixed quick-fried crushing device 1 of sundries on the frame 6,
Sterilize deodorization coagulation device 2, turbid separator 3, organic matter body refuse separator 4, electric-control system 5.
The discharge port of the quick-fried crushing device 1 of sundries is connected with the feed inlet of disinfection deodorization coagulation device 2, disinfection deodorization coagulation dress
It sets 2 discharge port to be connected with the feed inlet of turbid separator 3, the mud discharging mouth and organic matter body refuse point of turbid separator 3
Feed inlet from device 4 is connected, and electric control gear 5 is separated with the quick-fried crushing device 1 of sundries, disinfection deodorization coagulation device 2, turbid respectively
Device 3, organic matter body refuse separator 4.
The quick-fried crushing device 1 of sundries includes the quick-fried broken suction pump 11 of sundries and pipeline 12, and the quick-fried broken suction pump 11 of sundries is mounted on bracket 6
On, including explosion cone 111, anti-blocking coarse crushing knife group 112,113 groups of grinding knife fine crushing, impeller 114, main shaft 115 and shell
116;Explosion cone 112, the moving knife of 112 groups of anti-blocking coarse crushing knife, the moving knife of grinding knife group 113 fine crushing and impeller 114 are successively from charging
Mouth end starts to be fixed on main shaft 115, and the stationary knife of anti-blocking coarse crushing knife group 112, the stationary knife of grinding knife group 113 fine crushing are sequentially fixed at
On shell 116;It can be achieved to there are bulk suspended matters to carry out broken disposition in the sewage sludge of suction.
Sterilizing deodorization coagulation device 2 includes vortex mixing tank 21, meter charging gear 22, disinfection flocculant basin 23;Disinfection
The discharge port of deodorant storage Cans 23 is connected with the feed inlet of meter charging gear 22, and is set to the top of vortex mixing tank 21,
The discharge port of meter charging gear 22 is connected with vortex mixing tank 21.
Turbid separator 3 includes level-one turbid separating mechanism 31, second level turbid separating mechanism 32, three-level turbid seperator
Structure 33 improves the efficiency or effect of turbid separation by classified filtering;Wherein level-one turbid separating mechanism 31 is separated comprising muddy water
Room I 311, muddy water separator I 312, muddy water separator II 313, slurry thickening cone I 314;Second level turbid separating mechanism 32 includes turbid
Water separation chamber II 321, muddy water separator III 322, muddy water separator IV 323, slurry thickening cone 324 II;Three-level turbid seperator
Structure 33 includes muddy water separation chamber III 331, muddy water separator V 332, slurry thickening cone III 334;Wherein muddy water separation chamber I 311
Import is connected with the discharge port of disinfection deodorization coagulation device 2, and the middle part of muddy water separation chambers at different levels is arranged in each muddy water separator
Or outlet end, slurry thickening cone are arranged in muddy water separation chamber bottom, flocculated slurry is settled before muddy water separator, and in slag
Starch concentration deposition in thickening cone.
Organic matter body refuse separator 4 include promoted drainage mechanism 41, slag-liquid separation mechanism 42, negative pressure pumping water mechanism 43,
Power mechanism 44;Power mechanism 44 and promotion drainage mechanism 41 connect, and provide power;Promote drainage mechanism 41 and slag-liquid separation
Mechanism 42 is connected, and the water outlet of slag-liquid separation mechanism 42 is connected with the inlet pipeline of negative pressure pumping water mechanism 43.
Muddy water separator I 312, muddy water separator II 313, muddy water separator III 322, muddy water separator IV 323 are adopted respectively
It is made with the stainless (steel) wire of non-sticky sludge, mesh mesh number is 5 mesh, 20 mesh, 100 mesh, 200 mesh;Separator for mud and water V 332 is adopted
It is made of Teflon filter cloth, is 500 mesh by mesh number, it can be ensured that treated water quality reaching standard.
In the course of work, sewage is extracted by the quick-fried crushing device 1 of sundries, is transported to disinfection deodorization coagulation device 2 and is carried out disinfection
And coagulation, the sewage after coagulation enter turbid separator 3, are separated by three-stage filtration, realize clear water discharge;It is wherein dirty
After mud deposits to slurry thickening cone, it is pipelined to organic matter body refuse separator 4, by the spiral in drainage mechanism 41
It squeezes and the filtering of slag-liquid separation mechanism 42, sludge after extruding is discharged from the mud mouth of drainage mechanism 41, the sewage of filters pressing is logical
Cross negative pressure pumping water mechanism 43 be drawn into disinfection deodorization coagulation device 2 in carry out again circular flocculation disposition.
Embodiment 2
As shown in Fig. 7~8, the utility model embodiment includes the quick-fried crushing device 1 of sundries, disinfection deodorization coagulation device 2, turbid
Separator 3, organic matter body refuse separator 4, electric-control system 5, bracket 6, heavy metal ion remove device 7.With embodiment 1
Difference is:
Deodorization coagulation device 2 is sterilized using double stirring systems, mainly includes vortex mixing tank 21, meter charging gear 22, disappear
Malicious flocculant basin 23, vortex mixing tank II 25;Sterilize the discharge port of deodorant storage Cans 23 and the feed inlet of meter charging gear 22
It is connected, and is set to the top of vortex mixing tank 21, the discharge port of meter charging gear 22 is connected with vortex mixing tank 21, whirlpool
The feed inlet of stream blending tank 25 II is connected with the discharge port of vortex mixing tank 21, the discharge port and turbid of vortex mixing tank 25 II
The feed inlet of separator 3 is connected;Turbid separator 3 includes two-stage turbid separating mechanism;It is the separation of level-one turbid respectively
Mechanism 31, second level turbid separating mechanism 32.The water inlet of heavy metal ion remove device 7 and the discharge outlet of turbid separator 3
It is connected, the water outlet of heavy metal ion remove device 7 is expelled directly out qualified clear water.
Heavy metal ion remove device 7 includes medicament basin 73, meter charging gear 72, vortex mixing tank 71, purification filtering
Room 74, non-sticky filter 75, slurry precipitation bucket 76;Medicament basin 73, meter charging gear 72 are set to the top of vortex mixing tank 71
The discharge port in portion, medicament basin 73 is connected with the feed inlet of meter charging gear 72, counts the discharge port and vortex of charging gear 72
Blending tank 71 is connected;The discharge port of vortex mixing tank 71 is connected to cleaned filter chamber 74, and the non-sticky setting of filter 75 is purifying
74 outlet end of filter chamber;Slurry precipitation bucket 76 is arranged in cleaned 74 bottom of filter chamber, and the slurry of reactive crystallization is in non-sticky filtering
It is deposited to before device 75 in slurry precipitation bucket.
The heavy metal ion in sewage can be removed by the way that heavy metal ion remove device 7 is arranged.
Those skilled in the art can carry out various modifications to the utility model and modification, if these modifications and variations
Within the scope of the claims of the present invention and its equivalent technology, then these modifications and variations are also in the guarantor of the utility model
Within the scope of shield.The prior art that the content being not described in detail in specification is known to the skilled person.
Claims (10)
1. a kind of sanitary sewage deodorization direct purification separation equipment, which is characterized in that including bracket and be fixed on miscellaneous on bracket
The quick-fried crushing device of object, disinfection deodorization coagulation device, turbid separator, organic matter body refuse separator, the quick-fried crushing device of sundries
Sewage discharge port with it is described disinfection deodorization coagulation device sewage feed inlet be connected, it is described disinfection deodorization coagulation device go out
Material mouth is connected with the feed inlet of the turbid separator, the external cycling use of water pond of the water outlet of the turbid separator or
The slurry outlet of tank, turbid separator bottom is connected with the feed inlet of the organic matter body refuse separator, described
The outlet of sewer of organic matter body refuse separator is connected by pipeline with the sewage feed inlet of the disinfection deodorization coagulation device.
2. sanitary sewage deodorization direct purification separation equipment according to claim 1, which is characterized in that the sundries is quick-fried broken
Device includes the quick-fried broken suction pump of sundries, flowmeter, pipeline and/or dirty tank of receiving, and the quick-fried broken suction pump of sundries is set to sanitary sewage
It is connected in pond and by pipeline with the sewage feed inlet of the disinfection deodorization coagulation device, the flowmeter is set to the pipeline
The feed inlet of the upper or described disinfection deodorization coagulation device, the quick-fried broken suction pump of sundries be set to it is described receive in dirty tank, it is described to receive dirt
Tank is independently arranged or is arranged with the disinfection deodorization coagulation device integral type.
3. sanitary sewage deodorization direct purification separation equipment according to claim 1, which is characterized in that the disinfection deodorization
Coagulation device includes disinfection flocculant basin, meter charging gear, one or more vortex mixing tanks being connected;The disinfection wadding
Solidifying agent basin is equipped with disinfection deodorant basin and flocculant basin, and the disinfection flocculant basin and meter charging gear are set to whirlpool
The top of blending tank is flowed, the discharge port of the disinfection flocculant basin is connected with the feed inlet of the meter charging gear, described
It counts and is connected in the discharge port and the feed end of the vortex mixing tank of charging gear.
4. sanitary sewage deodorization direct purification separation equipment according to claim 1, which is characterized in that the turbid separation
Device includes muddy water separation chamber, muddy water separator, slurry thickening cone, and the import of the muddy water separation chamber and the disinfection deodorization are mixed
The bottom of muddy water separation chamber is arranged in the discharge port connection of solidifying device, the slurry thickening cone, and the muddy water separator setting exists
The outlet end of muddy water separation chamber.
5. sanitary sewage deodorization direct purification separation equipment according to claim 1, which is characterized in that the organic matter mud
Slag separator includes promoting drainage mechanism, slag-liquid separation mechanism, negative pressure pumping water mechanism, power mechanism, the promotion water-strainer
Structure is connected with slag-liquid separation mechanism, and the water outlet of the slag-liquid separation mechanism is connected with the inlet pipeline of negative pressure pumping water mechanism;Institute
Stating and promoting drainage mechanism includes shell, main shaft and discontinuous helical blade, and the discontinuous helical blade is fixed on the main shaft
Above and it is located in the shell;The slag-liquid separation mechanism includes sandwich shell, filter cloth, the sandwich shell and the promotion
The shell of drainage mechanism is fitted close, and compresses the filter cloth, realizes mud-water separation;The negative pressure pumping water mechanism includes high pressure
It is centrifuged suction pump, pipeline.
6. sanitary sewage deodorization direct purification separation equipment according to claim 4, which is characterized in that it is net to be additionally provided with middle water
Makeup is set, and the water inlet of the middle water purification installation is connected with the water outlet of the turbid separator;The middle Water warfare
Device includes medicament basin, counts charging gear, vortex mixing tank, cleaned filter chamber, non-sticky filter, slurry precipitation bucket, described
Medicament basin, meter charging gear are set to the top of the vortex mixing tank, and the discharge port of the medicament basin and the meter are fed
The feed inlet of device is connected, and is connected in the discharge port and the feed end of vortex mixing tank of the meter charging gear;The whirlpool
The discharge port of stream blending tank is connected to the cleaned filter chamber, and the non-sticky filter is set to the muddy water and separates chamber outlet end;
The slurry precipitation bucket is set to the cleaned filter chamber bottom.
7. sanitary sewage deodorization direct purification separation equipment according to claim 6, which is characterized in that middle water purification installation
Realize that the heavy metal ion of centering water is reacted and crystallized by the way that heavy metals removal medicament is added for heavy metal ion remove device
It precipitates, Water warfare in realization.
8. the separation equipment of sanitary sewage deodorization direct purification described according to claim 1~one of 7, which is characterized in that also set
There is oily-water seperating equipment, the oily-water seperating equipment is set at the quick-fried crushing device import or export of the sundries.
9. the separation equipment of sanitary sewage deodorization direct purification described according to claim 1~one of 7, which is characterized in that also set
Have a peculiar smell catalyzing, oxidizing and purifying device, the peculiar smell catalyzing, oxidizing and purifying device include catalyzing, oxidizing and purifying device, sucktion fan and
Air hose, one end of the air hose respectively with disinfection deodorization coagulation device, turbid separator, middle water purifier, organic matter mud
Slag separator is connected, and the other end is connected with sucktion fan, the other end and catalyzing, oxidizing and purifying device of the sucktion fan
It is connected.
10. sanitary sewage deodorization direct purification separation equipment according to claim 2, which is characterized in that the sundries is quick-fried
Broken suction pump includes explosion cone, anti-blocking coarse crushing knife group, grinding knife group, impeller, main shaft and shell fine crushing, and the explosion bores, is anti-blocking
The moving knife of coarse crushing knife group, the moving knife of grinding knife group fine crushing and impeller are successively fixed on main shaft since feed inlet end, described anti-
The stationary knife of stifled coarse crushing knife group, the stationary knife of grinding knife group fine crushing are sequentially fixed on shell.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201920294448.7U CN209602282U (en) | 2019-03-08 | 2019-03-08 | A kind of sanitary sewage deodorization direct purification separation equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201920294448.7U CN209602282U (en) | 2019-03-08 | 2019-03-08 | A kind of sanitary sewage deodorization direct purification separation equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN209602282U true CN209602282U (en) | 2019-11-08 |
Family
ID=68405582
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201920294448.7U Active CN209602282U (en) | 2019-03-08 | 2019-03-08 | A kind of sanitary sewage deodorization direct purification separation equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN209602282U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112591986A (en) * | 2020-11-24 | 2021-04-02 | 遵义师范学院 | Integrated sewage restoration and treatment device and restoration and treatment method |
CN115502178A (en) * | 2022-10-08 | 2022-12-23 | 山东中和生态环保有限公司 | Organic garbage microbiological treatment equipment |
-
2019
- 2019-03-08 CN CN201920294448.7U patent/CN209602282U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112591986A (en) * | 2020-11-24 | 2021-04-02 | 遵义师范学院 | Integrated sewage restoration and treatment device and restoration and treatment method |
CN112591986B (en) * | 2020-11-24 | 2022-08-09 | 遵义师范学院 | Integrated sewage restoration and treatment device and restoration and treatment method |
CN115502178A (en) * | 2022-10-08 | 2022-12-23 | 山东中和生态环保有限公司 | Organic garbage microbiological treatment equipment |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107473471B (en) | Sewage purification treatment device | |
CN206255954U (en) | Efficient domestic sewage treatment system | |
CN102225803B (en) | Biomembrane reactor, waste water treating system and method for treating waste water | |
WO2015081658A1 (en) | Sludge treatment system and method therefor | |
CN102329051B (en) | Rubbish percolate treatment device by taking advanced oxidation and comprehensive membrane treatment as cores | |
CN107445400A (en) | A kind of sewage disposal system | |
CN101591118A (en) | Multifunctional general sewage treatment system | |
CN106977054A (en) | Municipal wastewater cleaning system construction technology | |
CN107298498A (en) | Industrial and mineral waste water high-efficiency purifies and recycled equipment | |
CN209602282U (en) | A kind of sanitary sewage deodorization direct purification separation equipment | |
CN207091183U (en) | A kind of industrial and mineral waste water high-efficiency purifies and recycled equipment | |
CN101898847A (en) | System for treating sewage containing nonylphenol polyoxyethylene ether and metabolites | |
CN207608474U (en) | Reactor for treating excess sludge by cavitation jet | |
CN107311348A (en) | Hu Chi river courses muddy water and sludge high-efficient purification processing equipment | |
CN210736409U (en) | Equipment for treating industrial desulfurization wastewater by using flue waste gas | |
CN2651237Y (en) | Unitary sewage purifying desliming rapid treating apparatus | |
CN207713606U (en) | A kind of processing system with excrement medical waste water | |
CN207259275U (en) | A kind of domestic sewage of villages and small towns high effect cleaningization handles and recycles equipment | |
JP4036650B2 (en) | Waste water treatment method and waste water treatment apparatus | |
CN209685531U (en) | Waste water treatment system | |
CN209619124U (en) | A kind of sewage disposal system | |
CN207142979U (en) | A kind of Hu Chi river courses muddy water and sludge high-efficient purification processing equipment | |
CN210163286U (en) | Domestic sewage treatment system based on segmented aeration biological treatment technology | |
CN110550845B (en) | Domestic sewage treatment system | |
CN2499397Y (en) | Life waste water treating device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |