CN106542671A - Intelligent zero-emission sewage disposal system - Google Patents
Intelligent zero-emission sewage disposal system Download PDFInfo
- Publication number
- CN106542671A CN106542671A CN201610935765.3A CN201610935765A CN106542671A CN 106542671 A CN106542671 A CN 106542671A CN 201610935765 A CN201610935765 A CN 201610935765A CN 106542671 A CN106542671 A CN 106542671A
- Authority
- CN
- China
- Prior art keywords
- clear water
- sludge
- disposal system
- sewage disposal
- sedimentation tank
- 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.)
- Granted
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 85
- 239000010802 sludge Substances 0.000 claims abstract description 62
- 229920003023 plastic Polymers 0.000 claims abstract description 31
- 239000004033 plastic Substances 0.000 claims abstract description 31
- 238000004062 sedimentation Methods 0.000 claims abstract description 27
- 238000004140 cleaning Methods 0.000 claims abstract description 19
- 239000000725 suspension Substances 0.000 claims abstract description 12
- 238000011084 recovery Methods 0.000 claims abstract description 11
- 238000010790 dilution Methods 0.000 claims abstract description 10
- 239000012895 dilution Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 7
- 238000003825 pressing Methods 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 6
- 238000009825 accumulation Methods 0.000 claims description 4
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 6
- 239000010797 grey water Substances 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 5
- 239000002245 particle Substances 0.000 abstract description 5
- 239000003513 alkali Substances 0.000 abstract description 4
- 229920000426 Microplastic Polymers 0.000 abstract description 3
- 230000007935 neutral effect Effects 0.000 abstract description 3
- 230000008021 deposition Effects 0.000 abstract description 2
- 230000008569 process Effects 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 description 5
- 238000009413 insulation Methods 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 3
- 108010010803 Gelatin Proteins 0.000 description 3
- 229920000168 Microcrystalline cellulose Polymers 0.000 description 3
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 3
- 239000010425 asbestos Substances 0.000 description 3
- 239000004203 carnauba wax Substances 0.000 description 3
- 229920000159 gelatin Polymers 0.000 description 3
- 239000008273 gelatin Substances 0.000 description 3
- 235000019322 gelatine Nutrition 0.000 description 3
- 235000011852 gelatine desserts Nutrition 0.000 description 3
- 125000005456 glyceride group Chemical group 0.000 description 3
- 235000019813 microcrystalline cellulose Nutrition 0.000 description 3
- 239000008108 microcrystalline cellulose Substances 0.000 description 3
- 229940016286 microcrystalline cellulose Drugs 0.000 description 3
- 239000002006 petroleum coke Substances 0.000 description 3
- 229910052895 riebeckite Inorganic materials 0.000 description 3
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 3
- 210000002268 wool Anatomy 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- ZXMGHDIOOHOAAE-UHFFFAOYSA-N 1,1,1-trifluoro-n-(trifluoromethylsulfonyl)methanesulfonamide Chemical class FC(F)(F)S(=O)(=O)NS(=O)(=O)C(F)(F)F ZXMGHDIOOHOAAE-UHFFFAOYSA-N 0.000 description 1
- 239000004709 Chlorinated polyethylene Substances 0.000 description 1
- -1 DEG C Acid imide Chemical class 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- AXNBHOOQHIIQFA-UHFFFAOYSA-N [S].C(F)(F)F Chemical compound [S].C(F)(F)F AXNBHOOQHIIQFA-UHFFFAOYSA-N 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a kind of intelligent zero-emission sewage disposal system, is related to regenerated plastics processing technique field, it is made up of Sedimentation tank, sludge carrier pipe road, sludge delivery pump, pressure filter, clear water recovery channel, sludge dilution water pipeline and clear water delivery pump.Sewage disposal system of the present invention is applied to the process of recycled plastic granules cleaning sullage, it is easy to operate, the clear water for obtaining is re-used for into down batch particle cleaning after separating suspension plastic grain and sludge, to save the water consumption of cleaning plastic grain and avoid sewage neutral and alkali material from environment being polluted because of direct discharge；And by clear water backwash and the setting of stirring blade, sludge is diluted, to prevent sludge to be difficult to pump out because deposition is serious.
Description
Technical field：
The present invention relates to regenerated plastics processing technique field, and in particular to a kind of intelligent zero-emission sewage disposal system.
Background technology：
Recycled plastic granules are belonging in plastic grain this category, and regenerated plastics are exactly then to reclaim used new
The plastics that material or discarded plastics are produced by Luo bars machine, then a kind of granular plastics are cut into by pelleter
Grain.Due to containing dust and greasy dirt etc. in salvage material, it is therefore desirable to which plastic grain is cleaned.Conventional aqueous alkali is carried out clearly
Wash, but the sewage after cleaning, due to containing alkaline matter, environmental pollution is serious, therefore directly can not discharge.And due to modeling
Material particle cleaning hourly water consumption is larger, if the sewage discharge of a plastic grain will be cleaned directly, it will increase cleaning
Use water cost.At present simplest sewage water treatment method is exactly to utilize natural sedimentation, but be deposited in the sludge of bottom it is easy because
Seriously overstock and be difficult to pump out, increase difficulty to Treatment of Sludge.
The content of the invention：
The technical problem to be solved is to provide one kind to incite somebody to action after separating suspension plastic grain and sludge
To clear water be re-used for down batch particle cleaning, to play saving water for cleaning amount and avoid sewage neutral and alkali Substances Pollution simultaneously
The intelligent zero-emission sewage disposal system of environment.
The technical problem to be solved is realized using following technical scheme：
A kind of intelligent zero-emission sewage disposal system, by Sedimentation tank, sludge carrier pipe road, sludge delivery pump, pressure filter, clear
Water Sproading pipeline, sludge dilution water pipeline and clear water delivery pump composition, the Sedimentation tank bottom is provided with mud mouth and clear water enters
Mouthful, the upper strata suspension plastic grain in Sedimentation tank is purged by filter screen, and the related middle level clear water of lower floor's sludge passes through mud mouth
Enter in sludge carrier pipe road, and Jing sludge delivery pumps are sent in pressure filter, the filter pressing motor spindle is provided with clear water reserviors, Jing filter pressings
Rear clear water flows into clear water reserviors, and, to drawing off after a certain amount of, the clear water delivery pump on the one hand will be clearly for the sludge accumulation in pressure filter
Clear water in pond pumps into clear water recovery channel to carry out down the cleaning of batch plastic grain, clear water is pumped into sludge on the other hand dilute
Water pipeline is released, pumps in Sedimentation tank to dilute the sludge for being difficult to pump out by clear water import.
Inside the Sedimentation tank, bottom side is transversely provided with spiral helicine stirring blade.Stirring blade fits through sludge dilution and send
The clear water rapid dilution sludge that waterpipe is sent into, to save the water consumption of dilution sludge.
The Sedimentation tank internal vertical is provided with multiple mud rooms, each mud room one mud mouth of correspondence.By multiple dirts
Mud room and the setting of mud mouth, accelerate the velocity of discharge of sludge water, prevent sludge to be difficult to pump out because long-time overstocks.
The mud room is structure of the longitudinal section in inverted trapezoidal.By the design of inverted trapezoidal, it is easy to make by action of gravity
Sludge is quickly discharged.
The curved structure of the filter screen, is fixedly mounted in the rotating shaft rotated by Motor drive by connecting rod.Using electricity
Machine band electric filter rotates to remove automatically upper strata suspension plastic grain, reduces human input.
Valve is equipped with the sludge carrier pipe road, clear water recovery channel and sludge dilution water pipeline.
It is a further object to provide a kind of technique that sewage disposal is carried out using above-mentioned sewage disposal system, step
It is rapid as follows：
(1) alkaline sewage after clean plastic grain is pumped in Sedimentation tank, and adds agglomerator, is stood after being sufficiently stirred for
Layering, so as to form the three-decker of upper strata suspension plastic grain, middle level clear water and lower floor's sludge, suspension plastic grain in upper strata leads to
Drainage screen is removed, and the related middle level clear water of lower floor's sludge enters sludge carrier pipe road by the mud mouth of Sedimentation tank bottom；
(2) the sludge water Jing sludge delivery pumps in sludge carrier pipe road are sent in pressure filter, and the clear water Jing after filter pressing is flowed into
Clear water reserviors, the sludge accumulation in pressure filter is to drawing off after a certain amount of；
(3) on the one hand the clear water in clear water reserviors pumps into clear water recovery channel by clear water delivery pump to carry out down batch plastics
The cleaning of grain, on the other hand pumps into sludge by clear water delivery pump and dilutes water pipeline, by the clear water import of Sedimentation tank bottom
Pump in Sedimentation tank the sludge for pumping out is difficult to dilute；
Upper strata suspension plastic grain in the Sedimentation tank assembles agglomerating by adding agglomerator, and agglomerator is by weighing as follows
The raw material of amount number is made：10 parts of Microcrystalline Cellulose, 3 parts of chlorinated polyethylene, 2 parts of hydrogenated rosin glyceride, Brazil wax 1
Part, 0.5 part of gelatin, 0.5 part of C5 Petropols, 0.5 part of lanonol, 0.5 part of asbestos wool, 0.3 part of petroleum coke micropowder, double fluoroforms
0.3 part of alkane sulfimide, its preparation method is：Brazil wax and gelatin are added in hydrogenated rosin glyceride, is sufficiently mixed
Microwave treatment 5min under microwave frequency 2450MHz, power 700W, adds C5 Petropols and petroleum coke micropowder, mixing
Continue microwave treatment 5min after uniform, gained mixture proceeds to sealing and standing 3h in 0-5 DEG C of environment immediately, be subsequently adding chlorination and gather
Ethylene and lanonol, and 120-130 DEG C of insulation mixing 10min is heated to, subsequent natural cooling cooling treats that temperature is down to 70-80
Microcrystalline Cellulose, asbestos wool and double trifluoromethanesulfonimides, insulation mixing 10min, gained mixture is added to be placed in -5- after DEG C
Sealing and standing 3h in 0 DEG C of environment, finally makes powder using super micron mill.
The consumption of the agglomerator is that every liter of cleaning sullage uses 0.05-0.1g.
By adding water-fast agglomerator, under flocculation and adsorption, the plastic grain of suspension is made to assemble agglomerating,
In order to remove the less plastic grain of granularity by filter screen；And agglomerator is eliminated together with plastic grain, so as to keep away
Exempt from secondary pollution.
The invention has the beneficial effects as follows：Sewage disposal system of the present invention is applied to recycled plastic granules cleaning sullage
Process, easy to operate, high degree of automation, the clear water for obtaining is re-used for down after separating suspension plastic grain and sludge
Particle cleaning is criticized, to save the water consumption of cleaning plastic grain and avoid sewage neutral and alkali material from ring being polluted because directly discharging
Border；And by clear water backwash and the setting of stirring blade, sludge is diluted, to prevent sludge pump to be difficult to because deposition is serious
Go out.
Description of the drawings：
Fig. 1 is the structure top view of the present invention；
Fig. 2 is the structure rearview of the present invention；
Wherein：1- Sedimentation tanks；2- sludge carrier pipes road；3- sludge delivery pumps；4- pressure filter；5- clear water recovery channels；6-
Sludge dilutes water pipeline；7- clear water delivery pumps；8- mud mouths；9- clear water imports；10- filter screens；11- clear water reserviors；12- stirring slurries
Leaf；13- mud rooms；14- connecting rods；15- motors；16- rotating shafts；17- valves.
Specific embodiment：
In order that technological means, creation characteristic, reached purpose and effect that the present invention is realized are easy to understand, tie below
Conjunction is specifically illustrating and embodiment, and the present invention is expanded on further.
As shown in Figure 1, 2, a kind of intelligent zero-emission sewage disposal system, defeated by Sedimentation tank 1, sludge carrier pipe road 2, sludge
Pump 3, pressure filter 4, clear water recovery channel 5, sludge dilution water pipeline 6 and clear water delivery pump 7 is sent to constitute, Sedimentation tank bottom is provided with
Mud mouth 8 and clear water import 9, the upper strata suspension plastic grain in Sedimentation tank are purged by filter screen 10, and lower floor's sludge is related
Middle level clear water is entered in sludge carrier pipe road by mud mouth, and Jing sludge delivery pumps are sent in pressure filter, and filter pressing motor spindle sets
There are clear water reserviors 11, clear water Jing after filter pressing flows into clear water reserviors, to drawing off after a certain amount of, clear water is conveyed the sludge accumulation in pressure filter
On the one hand clear water in clear water reserviors is pumped into clear water recovery channel to carry out down the cleaning of batch plastic grain by pump, on the other hand will be clear
Water pumps into sludge dilution water pipeline, is pumped into dilute the sludge for being difficult to pump out in Sedimentation tank, in Sedimentation tank by clear water import
Portion bottom side is transversely provided with spiral helicine stirring blade 12, and Sedimentation tank internal vertical is provided with multiple mud rooms 13, each mud room pair
A mud mouth is answered, mud room is structure of the longitudinal section in inverted trapezoidal.The curved structure of the filter screen, is fixed by connecting rod 14
Installed in being driven by motor 15 in the rotating shaft 16 of rotation, sludge carrier pipe road, clear water recovery channel and sludge dilute water pipeline
On be equipped with valve 17.
Agglomerator to Sedimentation tank into is added using the amount of 0.05g agglomerators according to every liter of cleaning sullage, promote upper strata to suspend
Particle aggregation is agglomerating, removes in order to filter screen.
The preparation method of agglomerator is：1 part of Brazil wax and 0.5 part of gelatin are added in 2 parts of hydrogenated rosin glycerides,
Microwave treatment 5min under microwave frequency 2450MHz, power 700W is sufficiently mixed, 0.5 part of C5 Petropols and 0.3 is added
Part petroleum coke micropowder, continues microwave treatment 5min after mix homogeneously, gained mixture proceeds to sealing and standing in 0-5 DEG C of environment immediately
3h, is subsequently adding 3 parts of chlorinated polyethylenees and 0.5 part of lanonol, and is heated to 120-130 DEG C of insulation mixing 10min, subsequently natural
Cool, 10 parts of Microcrystalline Cellulose, 0.5 part of asbestos wool and 0.3 part of double fluoroform sulphur are added after temperature is down to 70-80 DEG C
Acid imide, insulation mixing 10min, gained mixture is placed in sealing and standing 3h in -5-0 DEG C of environment, finally using super micron mill
Make powder.
Result shows, is processed after cleaning sullage using above-mentioned processing system, suspension plastic grain in sewage and outstanding
The clearance rate of floating mud granule reaches more than 99%, and the clear water of acquisition can be re-used for down the cleaning of batch plastic grain.
The ultimate principle and principal character and advantages of the present invention of the present invention has been shown and described above.The technology of the industry
Personnel it should be appreciated that the present invention is not restricted to the described embodiments, the simply explanation described in above-described embodiment and description this
The principle of invention, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, these changes
Change and improvement is both fallen within scope of the claimed invention.The claimed scope of the invention by appending claims and its
Equivalent thereof.
Claims (6)
1. intelligent zero-emission sewage disposal system, it is characterised in that：By Sedimentation tank, sludge carrier pipe road, sludge delivery pump, filter pressing
Machine, clear water recovery channel, sludge dilution water pipeline and clear water delivery pump composition, the Sedimentation tank bottom are provided with mud mouth and clear
Water inlet, the upper strata suspension plastic grain in Sedimentation tank are purged by filter screen, and the related middle level clear water of lower floor's sludge passes through
Mud mouth is entered in sludge carrier pipe road, and Jing sludge delivery pumps are sent in pressure filter, and the filter pressing motor spindle is provided with clear water reserviors, Jing
Clear water after filter pressing flows into clear water reserviors, the sludge accumulation in pressure filter to drawing off after a certain amount of, the clear water delivery pump one side
Clear water in clear water reserviors is pumped into into clear water recovery channel to carry out down the cleaning of batch plastic grain, clear water is pumped into into dirt on the other hand
Mud dilutes water pipeline, pumps in Sedimentation tank to dilute the sludge for being difficult to pump out by clear water import.
2. intelligent zero-emission sewage disposal system according to claim 1, it is characterised in that：Bottom side inside the Sedimentation tank
It is transversely provided with spiral helicine stirring blade.
3. intelligent zero-emission sewage disposal system according to claim 1, it is characterised in that：The Sedimentation tank internal vertical
Multiple mud rooms are provided with, each mud room one mud mouth of correspondence.
4. intelligent zero-emission sewage disposal system according to claim 1, it is characterised in that：The mud room is longitudinal section
Structure in inverted trapezoidal.
5. intelligent zero-emission sewage disposal system according to claim 1, it is characterised in that：The curved knot of the filter screen
Structure, is fixedly mounted in the rotating shaft rotated by Motor drive by connecting rod.
6. intelligent zero-emission sewage disposal system according to claim 1, it is characterised in that：The sludge carrier pipe road,
Valve is equipped with clear water recovery channel and sludge dilution water pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610935765.3A CN106542671B (en) | 2016-11-01 | 2016-11-01 | Intelligent zero-emission sewage disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610935765.3A CN106542671B (en) | 2016-11-01 | 2016-11-01 | Intelligent zero-emission sewage disposal system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106542671A true CN106542671A (en) | 2017-03-29 |
| CN106542671B CN106542671B (en) | 2019-11-05 |
Family
ID=58392208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610935765.3A Active CN106542671B (en) | 2016-11-01 | 2016-11-01 | Intelligent zero-emission sewage disposal system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106542671B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107952503A (en) * | 2017-10-25 | 2018-04-24 | 百奥森（江苏）食品安全科技有限公司 | A kind of Cirulation type grain washing device |
Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2809221Y (en) * | 2005-04-15 | 2006-08-23 | 中国矿业大学 | Automatic dredging treatment equipment for fine coal slime in mine sump |
| CN2825752Y (en) * | 2005-07-04 | 2006-10-11 | 徐州天科机械制造有限公司 | Automatic dredging and dehydrating equipment for mine sump |
| CN101234811A (en) * | 2008-01-17 | 2008-08-06 | 杭州富兴环保机械有限公司 | Device for treating polyester beverage bottle recycling sewage |
| CN201400631Y (en) * | 2009-04-24 | 2010-02-10 | 杭州恒达环保实业有限公司 | Plastic cleaning wastewater treatment system |
| CN201769295U (en) * | 2010-07-07 | 2011-03-23 | 甘肃大禹节水股份有限公司 | Waste plastic water floating device |
| CN103203348A (en) * | 2013-03-29 | 2013-07-17 | 卓建立 | Built-in static pressure sludge discharging machine |
| CN203346119U (en) * | 2013-03-04 | 2013-12-18 | 云南玉加宝人造板有限公司 | Sewage treatment system for wood chip washing |
| CN103922503A (en) * | 2014-04-10 | 2014-07-16 | 界首市双特新材料科技有限公司 | Water purification cycle process in modified reprocessed plastic production |
| CN203916171U (en) * | 2014-06-30 | 2014-11-05 | 河南永华能源有限公司 | Multidirectional walking automatic Synthesis waste removal equipment |
| CN204134279U (en) * | 2014-10-22 | 2015-02-04 | 冯宇 | The sludge drainage system of efficient concentration sedimentation basin |
| CN104801075A (en) * | 2015-03-30 | 2015-07-29 | 南通华新环保设备工程有限公司 | Center suspended type sludge scraper |
| CN105036382A (en) * | 2015-06-08 | 2015-11-11 | 德清华宇链传动有限公司 | Industrial water recycling device |
| CN105366845A (en) * | 2015-12-09 | 2016-03-02 | 吕清胜 | Mine wastewater automatic processing recycling system |
-
2016
- 2016-11-01 CN CN201610935765.3A patent/CN106542671B/en active Active
Patent Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2809221Y (en) * | 2005-04-15 | 2006-08-23 | 中国矿业大学 | Automatic dredging treatment equipment for fine coal slime in mine sump |
| CN2825752Y (en) * | 2005-07-04 | 2006-10-11 | 徐州天科机械制造有限公司 | Automatic dredging and dehydrating equipment for mine sump |
| CN101234811A (en) * | 2008-01-17 | 2008-08-06 | 杭州富兴环保机械有限公司 | Device for treating polyester beverage bottle recycling sewage |
| CN201400631Y (en) * | 2009-04-24 | 2010-02-10 | 杭州恒达环保实业有限公司 | Plastic cleaning wastewater treatment system |
| CN201769295U (en) * | 2010-07-07 | 2011-03-23 | 甘肃大禹节水股份有限公司 | Waste plastic water floating device |
| CN203346119U (en) * | 2013-03-04 | 2013-12-18 | 云南玉加宝人造板有限公司 | Sewage treatment system for wood chip washing |
| CN103203348A (en) * | 2013-03-29 | 2013-07-17 | 卓建立 | Built-in static pressure sludge discharging machine |
| CN103922503A (en) * | 2014-04-10 | 2014-07-16 | 界首市双特新材料科技有限公司 | Water purification cycle process in modified reprocessed plastic production |
| CN203916171U (en) * | 2014-06-30 | 2014-11-05 | 河南永华能源有限公司 | Multidirectional walking automatic Synthesis waste removal equipment |
| CN204134279U (en) * | 2014-10-22 | 2015-02-04 | 冯宇 | The sludge drainage system of efficient concentration sedimentation basin |
| CN104801075A (en) * | 2015-03-30 | 2015-07-29 | 南通华新环保设备工程有限公司 | Center suspended type sludge scraper |
| CN105036382A (en) * | 2015-06-08 | 2015-11-11 | 德清华宇链传动有限公司 | Industrial water recycling device |
| CN105366845A (en) * | 2015-12-09 | 2016-03-02 | 吕清胜 | Mine wastewater automatic processing recycling system |
Non-Patent Citations (8)
| Title |
|---|
| 冶金工业部《冶金工业综合利用一百例》编委会: "《冶金工业综合利用一百例》", 30 September 1986, 冶金工业部安全环保司 * |
| 刘志和等: "《混凝土骨料生产》", 31 May 2016, 中国水利水电出版社 * |
| 太湖水环境修复示范项目技术专家组: "《高度处理净化槽结构设计与维护管理指南》", 30 April 2007, 中国环境科学出版社 * |
| 张林生: "《机械工业废水处理技术及典型工程》", 30 April 2008, 机械工业出版社 * |
| 徐利华: "《陶瓷坯釉料制备技术》", 31 October 2012 * |
| 朱靖等: "A/O工艺处理废塑料碱洗废水", 《再生资源研究》 * |
| 谢锋等: "《中国废塑料污染现状和绿色技术》", 31 March 2011, 中国环境科学出版社 * |
| 顾文卿: "《2005版新编选煤实用技术手册（第6卷）"》", 30 November 2005 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107952503A (en) * | 2017-10-25 | 2018-04-24 | 百奥森（江苏）食品安全科技有限公司 | A kind of Cirulation type grain washing device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106542671B (en) | 2019-11-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN210528947U (en) | Compound cereal enzymolysis fermenting installation | |
| CN106738434A (en) | A kind of waste and old composite paper-plastic material paper separates-moulds the operating method that skin granulates production system | |
| CN110065179A (en) | A kind of regeneration PC plastic alloy modification regenerative system and method | |
| CN212309404U (en) | Mixing and dissolving device for production and processing of dust suppressant | |
| CN115431440A (en) | Washing, sorting and recycling production line and process for plastic-packaged household garbage | |
| CN105421563B (en) | The technique of concret waste water comprehensive reutilization system | |
| CN106542671A (en) | Intelligent zero-emission sewage disposal system | |
| CN202823981U (en) | Cleaning system of reprocessed plastic | |
| CN110743476B (en) | Multifunctional calcium hydroxide preparation tank and preparation method | |
| CN111170585A (en) | A kind of livestock and poultry manure recycling engineering fermentation system and fermentation method | |
| CN202865196U (en) | System for recovering cutting fluid and silicon carbide in waste mortar in silicon wafer cutting | |
| CN106564998A (en) | Zero-discharge treatment process of recycled plastic high-concentration alkaline water | |
| CN102030916B (en) | An integrated device suitable for thermal regeneration of waste rubber | |
| CN208115716U (en) | A kind of efficient bionass fuel pelletizer | |
| KR101769762B1 (en) | A waste vinyl recycling apparatus having a waste heat recovery unit | |
| CN213077511U (en) | A device for preparing powdery washing powder particles | |
| CN215750221U (en) | Dust type rubber is retrieved and granulation equipment | |
| CN107053528A (en) | The processing method of waste or used plastics processing system and waste or used plastics | |
| CN214426264U (en) | Granule material cooling reposition of redundant personnel filtration system based on circulating water | |
| CN205662359U (en) | Abandonment aluminum foil composite paper's recycle device | |
| CN103963184A (en) | Polystyrene recycling and pelletization device | |
| CN206653558U (en) | Waste or used plastics processing system | |
| CN211133171U (en) | Spiral filtering washing machine | |
| CN223534946U (en) | Waste alkali liquor recovery system for pot mold | |
| CN207954381U (en) | A kind of worn-out agricultural film recycling process equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Intelligent zero discharge sewage treatment system Effective date of registration: 20201022 Granted publication date: 20191105 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: ANHUI HUANJIA TIANYI RENEWABLE RESOURCES Co.,Ltd. Registration number: Y2020980007072 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20211119 Granted publication date: 20191105 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: ANHUI HUANJIA TIANYI RENEWABLE RESOURCES Co.,Ltd. Registration number: Y2020980007072 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Intelligent zero discharge sewage treatment system Effective date of registration: 20211124 Granted publication date: 20191105 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: ANHUI HUANJIA TIANYI RENEWABLE RESOURCES Co.,Ltd. Registration number: Y2021980013047 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20221026 Granted publication date: 20191105 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: ANHUI HUANJIA TIANYI RENEWABLE RESOURCES Co.,Ltd. Registration number: Y2021980013047 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |