CN109481988A - A kind of high temperature waste precipitate processing unit and treatment process - Google Patents
A kind of high temperature waste precipitate processing unit and treatment process Download PDFInfo
- Publication number
- CN109481988A CN109481988A CN201811597771.8A CN201811597771A CN109481988A CN 109481988 A CN109481988 A CN 109481988A CN 201811597771 A CN201811597771 A CN 201811597771A CN 109481988 A CN109481988 A CN 109481988A
- Authority
- CN
- China
- Prior art keywords
- inner cylinder
- high temperature
- outer cylinder
- snorkel
- settling 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- 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
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The present invention discloses a kind of high temperature waste precipitate processing unit, first settling tank has the outer cylinder and inner cylinder being nested with, inner cylinder upper end is tightly connected snorkel one end and high-temperature material feed pipe, there are spilling water gaps between the fixed ring-like reverse flow baffle of inner cylinder and outer cylinder, and outer cylinder lower section forms slag-drip opening, upper end forms overflow sink；Second settling tank has the outer cylinder and inner cylinder being nested with, spray equipment is arranged in inner cylinder upper end, the snorkel other end is connected to inner cylinder upper end and is located at below spray equipment, outlet between snorkel and inner cylinder upper end inner wall is equipped with filter screen, the overflow sink of first settling tank is connected to the inner cylinder upper end of the second settling tank by sewage pipe and sewage pipe is located at below filter screen, inner cylinder is fixed between ring-like reverse flow baffle and outer cylinder there are spilling water gap, and outer cylinder lower section forms slag-drip opening, upper end formation overflow sink；Snorkel is equipped with water inlet pipe above the first settling tank.Invention additionally discloses corresponding treatment process.The present invention can directly, quickly handle high temperature waste material.
Description
Technical field
The present invention relates to tailings glass technology, in particular to a kind of high temperature waste precipitate processing unit and treatment process.
Background technique
Traditional tailings disposal plant is by sedimentation basin, rake frame, transmission mechanism, hoisting mechanism, feeder and unloader
Structure composition.When for handling tailing, tailing sewage is discharged into concentration basin by feeder, and three oxygen are put into concentration basin
Change aluminium and form mud, then rake frame is down in concentration basin by hoisting mechanism, transmission mechanism is recycled to drive rake frame to concentration
Mud in pond is stirred, and so that the slag in mud is deposited in the lower part of concentration basin by gravity and is arranged by shedding mechanism
Out, the water separated then is in the top of concentration basin and is discharged by overflow.There are concentration basin land occupations for this processing unit
The defects such as area is big, and investment is big, inconvenient for operation, high failure rate, and treatment effeciency is low.
After there is dealer to have developed tailing sewage rapid precipitation enrichment facility, occupied area is small, and automatization level is high, circulation
Water water quality is high, and treatment effeciency is high.
But in currently available technology, there are no the processing units dedicated for high temperature waste material, so, it is useless for high temperature
Expect the reprocessing that can only first cool down by a series of complex equipment, can not accomplish direct, quick, efficient process high temperature waste material.
Summary of the invention
It is simple with structure, can directly locate the purpose of the present invention is to provide a kind of high temperature waste precipitate processing unit
The advantages that reason, quick processing.
It is an object of the invention to also provide a kind of high temperature waste precipitate treatment process.
To achieve the goals above, solution of the invention is:
A kind of high temperature waste precipitate processing unit, including the first, second two settling tanks and snorkels；First settling tank tool
There are the first outer cylinder and the first inner cylinder, the first inner cylinder is nested in the first outer cylinder, and the upper end of the first inner cylinder is tightly connected snorkel
One end, the feed pipe of the upper end of the first inner cylinder also airtight connection high-temperature material, the outer wall of the first inner cylinder are fixed with first ring-like time
Baffle is flowed, there are the first spilling water gap between the outer rim of the first ring-like reverse flow baffle and the inner wall of the first outer cylinder, the first outer cylinder
Following diameter is gradually reduced to form the first slag-drip opening, and the upper end of the first outer cylinder forms the first overflow sink；Second settling tank has
Second outer cylinder and the second inner cylinder, the second inner cylinder are nested in the second outer cylinder, and spray equipment, snorkel is arranged in the upper end of the second inner cylinder
The other end be then connected to the upper end of the second inner cylinder and be located at the lower section of spray equipment, in the other end outer wall of snorkel and second
Outlet between the upper end inner wall of cylinder is equipped with the filter screen of ventilation dustproof, and the first overflow sink is connected in second by sewage pipe
The upper end of cylinder and the nozzle of sewage pipe are located at the lower section of filter screen, and the outer wall of the second inner cylinder is fixed with the second ring-like reverse flow baffle,
There are the second spilling water gap, the following diameter of the second outer cylinder between the outer rim of second ring-like reverse flow baffle and the inner wall of the second outer cylinder
It is gradually reduced to form the second slag-drip opening, the upper end of the second outer cylinder forms the second overflow sink；The gap of second overflow sink with
Sewage pipe independently separates；Snorkel is equipped with water inlet pipe close to the top of the first settling tank.
The feed pipe of the high-temperature material shape that is tilted down is connected to the upper end of the first inner cylinder.
Venetian blind is equipped with by the side of the second settling tank in water inlet pipe in the snorkel.
Inspection manhole is equipped with by the side of the second settling tank in venetian blind in the snorkel.
The gap of the second overflow sink and the water inlet pipe of snorkel connect, clear after can re-using precipitating
Water, resource reutilization avoid wasting.
The filter screen is three-layer composite structure, and upper layer and lower layer are respectively Stainless steel mesh, and intermediate one layer is brown piece.
The first, second ring-like reverse flow baffle is oblique, between the first, second ring-like reverse flow baffle and horizontal plane
Tilt angle is 60 °.
The first, second ring-like reverse flow baffle is separately fixed at the lower end of the first, second inner cylinder.
High temperature waste material is sent into the first settling tank from feed pipe, is opened simultaneously by a kind of high temperature waste precipitate treatment process
The spray equipment above water inlet pipe and the second settling tank above snorkel, the water flow that snorkel top water inlet pipe is sent into are rinsed high
Warm waste material, on the one hand, material in high temperature waste material enters the first inner cylinder together with the water that water inlet pipe comes out, and another rise sinks down into the
One outer cylinder bottom makes sludge by once standing, being concentrated, natural than reprecipitation, declines slag naturally by the first deslagging of bottom
Mouth discharge, meanwhile, water level is increased naturally by the first outer cylinder and flows into the first overflow sink, is sent into the second settling tank by sewage pipe
The second inner cylinder in, on the other hand, the high-temperature gas in high temperature waste material is directed to the second settling tank by snorkel, then fills through spray
The shower water for setting feeding rinses high-temperature gas, and gas gives off gas up to standard by filter screen filtration and obstructs dust, makes height
Dust in wet body enters the second inner cylinder, the sewage of sewage pipe, dust and shower water in high-temperature gas with shower water
The second outer cylinder bottom is sunk down into together, it is natural than reprecipitation by secondary standing, concentration, decline slag naturally by bottom the
The discharge of two slag-drip openings, meanwhile, water level is increased naturally by the second outer cylinder and flows into the second overflow sink, clear water is discharged by gap,
Clear water can reuse or qualified discharge.
After adopting the above scheme, when the present invention is suitable for processing high temperature waste material, after high temperature waste material is rinsed by water, high temperature waste material
In solid material formed muddy water stand, be concentrated in the first inner cylinder decanting zone of the first settling tank, reach waste residue concentration
65% or more, water passes through the static pool up overflow of the first outer cylinder, then send through sewage pipe to the second settling tank, and high temperature waste material
In gas the second settling tank is guided by snorkel, gas one in high temperature waste material enters the second settling tank and is filled by spray
The water spray set, the clean gas after spray are discharged into atmosphere through filter screen, meet environmental requirement, and spray makes dust therein
Equal solid materials also form muddy water, this muddy water stands in the second inner cylinder decanting zone of the second settling tank together with sewage, is concentrated,
Water passes through the static pool up overflow of the second outer cylinder, keeps water limpider, then clear water is discharged by gap, and clear water can reuse
Or qualified discharge.
Structure of the invention is simple, flexible in size, can be made according to the requirement of different clients, and occupied area is small, automation
It is horizontal high, high temperature waste material especially can directly, be quickly handled, treatment effeciency is high, and circulating water quality is high.
Detailed description of the invention
Fig. 1 is structure front view of the invention；
Fig. 2 is structure top view of the invention；
Fig. 3 is A-A cross-sectional view of the invention；
Fig. 4 is the enlarged drawing of filter screen of the present invention.
Label declaration
First settling tank 1, the first outer cylinder 11, the first inner cylinder 12, the first ring-like reverse flow baffle 13, the first spilling water gap 14,
First slag-drip opening 15, the first overflow sink 16, sewage pipe 17；
Second settling tank 2, the second outer cylinder 21, the second inner cylinder 22, the second ring-like reverse flow baffle 23, the second spilling water gap 24,
Second slag-drip opening 25, the second overflow sink 26；
Snorkel 3, water inlet pipe 31, venetian blind 32, inspection manhole 33；
Feed pipe 4；
Spray equipment 5；
Filter screen 6, Stainless steel mesh 61, brown piece 62.
Specific embodiment
Referring to shown in Fig. 1 to Fig. 3, a kind of high temperature waste precipitate processing unit that the present invention discloses, including the first settling tank
1, the second settling tank 2 and snorkel 3.
First settling tank 1 has the first outer cylinder 11 and the first inner cylinder 12.First inner cylinder 12 is nested in the first outer cylinder 11.The
The upper end of one inner cylinder 12 is tightly connected one end of snorkel 3.The charging of the upper end of first inner cylinder 12 also airtight connection high-temperature material
Pipe 4, this feed pipe 4 shape that is preferably tilted down are connected to the upper end of the first inner cylinder 12, it is heavy into first to be conducive to high-temperature material
Shallow lake tank 1.The outer wall of first inner cylinder 12 is fixed with a first ring-like reverse flow baffle 13, and the first ring-like reverse flow baffle 13 is preferably fixed
In the lower end of the first inner cylinder 12, the first ring-like reverse flow baffle 13 is preferably oblique, the first ring-like reverse flow baffle 13 and horizontal plane
Between tilt angle be 60 °, between the outer rim of the first ring-like reverse flow baffle 13 and the inner wall of the first outer cylinder 11 there are first overflow
Water space 14.The following diameter of first outer cylinder 11 is gradually reduced to form the first slag-drip opening 15.The upper end of first outer cylinder 11 forms the
One overflow sink 16.
Second settling tank 2 has the second outer cylinder 21 and the second inner cylinder 22.Second inner cylinder 22 is nested in the second outer cylinder 21.The
Spray equipment 5 is arranged in the upper end of two inner cylinders 22.The other end of snorkel 3 is then connected to the upper end of the second inner cylinder 22, and snorkel 3
The other end be located at the lower section of spray equipment 5, going out between the other end outer wall of snorkel 3 and the upper end inner wall of the second inner cylinder 22
Mouth is equipped with the filter screen 6 of ventilation dustproof, and filter screen 6 can use three-layer composite structure, and upper layer and lower layer are respectively that play a supportive role
Stainless steel mesh 61, intermediate one layer be ventilation dustproof brown piece 62.First overflow sink 16 is connected to the by sewage pipe 17
The upper end of two inner cylinders 22, and the nozzle of sewage pipe 17 is located at the lower section of filter screen 6.The outer wall of second inner cylinder 22 is fixed with one
Two ring-like reverse flow baffles 23, the second ring-like reverse flow baffle 23 are preferably secured to the lower end of the second inner cylinder 22, the second ring-like reflux gear
Plate 23 is preferably oblique, and the tilt angle between the second ring-like reverse flow baffle 23 and horizontal plane is 60 °, the second ring-like reflux gear
There are the second spilling water gaps 24 between the outer rim of plate 23 and the inner wall of the second outer cylinder 21.The following diameter of second outer cylinder 21 gradually contracts
The second slag-drip opening 25 of small formation.The upper end of second outer cylinder 21 forms the second overflow sink 26, the gap of the second overflow sink 26
It is independently separated with sewage pipe 17.In this way, the first overflow sink 16 is connected to 22 (i.e. second precipitating of the second inner cylinder by sewage pipe 17
System) secondary precipitation is carried out, mainly prevent dust by vapor with outer in the filter screen 6 that gas outlet is equipped with large area
Row directs out discharge by vapor after filter screen 6, and dust then drops to precipitating inside water and passes through 25 row of the second slag-drip opening
Out.
Snorkel 3 is equipped with water inlet pipe 31 close to the top of the first settling tank 1.In order to make resource reutilization, avoid wasting,
The gap of two overflow sinks 26 is connect with the water inlet pipe 31 of snorkel 3, the clear water after can re-using precipitating.Snorkel 3
In water inlet pipe 31 by the second settling tank 2 side be equipped with venetian blind 32, for adjusts control ventilatory capacity size.Snorkel 31
In venetian blind 32 by the second settling tank 2 side can be equipped with inspection manhole 33, operation convenient to overhaul.
Present invention further teaches a kind of high temperature waste precipitate treatment process, by high temperature waste material (such as high temperature slag) from feed pipe
4 are sent into the first settling tank 1, while opening the spray equipment 5 of 2 top of water inlet pipe 31 and the second settling tank of 3 top of snorkel,
The water flow that 3 top water inlet pipe 31 of snorkel is sent into rinses high temperature waste material, on the one hand, the material in high temperature waste material goes out with water inlet pipe 31
The water come mixes together to form muddy water into the first inner cylinder 12, and another rise sinks down into 11 bottom of the first outer cylinder, make sludge by one
Secondary standing, concentration, it is natural than reprecipitation, decline slag naturally and is discharged by the first slag-drip opening of bottom 15, meanwhile, water level passes through the
One outer cylinder 11 increases naturally flows into the first overflow sink 16, is sent into the second inner cylinder 22 of the second settling tank 2 by sewage pipe 17,
On the other hand, the high-temperature gas in high temperature waste material is directed to the second settling tank 2, then the spray being sent into through spray equipment 5 by snorkel 3
High-temperature gas is rinsed in water drenching, and gas goes out gas up to standard by 6 filtering emission of filter screen, and filter screen 6 obstructs dust, makes high temperature
Dust in gas is formed together muddy water into the second inner cylinder 22 with shower water, the dirt in the sewage of sewage pipe 17, high-temperature gas
Angstrom and the muddy water that is formed of shower water sink down into 21 bottom of the second outer cylinder together, by secondary standing, concentration, naturally than reprecipitation,
Decline slag naturally to be discharged by the second slag-drip opening of bottom 25, meanwhile, water level increases inflow second by the second outer cylinder 21 naturally
Clear water is discharged by gap in overflow sink 26, secondary precipitation treated clear water can qualified discharge or reuse be sent to snorkel 3.
Above-described embodiment and schema and non-limiting product form and style of the invention, any technical field it is common
The appropriate changes or modifications that technical staff does it all should be regarded as not departing from patent category of the invention.
Claims (9)
1. a kind of high temperature waste precipitate processing unit, it is characterised in that: including the first, second two settling tanks and snorkels；The
One settling tank has the first outer cylinder and the first inner cylinder, and the first inner cylinder is nested in the first outer cylinder, and the upper end of the first inner cylinder, which seals, to be connected
One end of tracheae, the feed pipe of the upper end of the first inner cylinder also airtight connection high-temperature material are connected, the outer wall of the first inner cylinder is fixed with
First ring-like reverse flow baffle, there are the first spilling water gap between the outer rim of the first ring-like reverse flow baffle and the inner wall of the first outer cylinder,
The following diameter of first outer cylinder is gradually reduced to form the first slag-drip opening, and the upper end of the first outer cylinder forms the first overflow sink；Second
Settling tank has the second outer cylinder and the second inner cylinder, and the second inner cylinder is nested in the second outer cylinder, and spray is arranged in the upper end of the second inner cylinder
Device, the other end of snorkel are then connected to the upper end of the second inner cylinder and are located at the lower section of spray equipment, the other end of snorkel
Outlet between outer wall and the upper end inner wall of the second inner cylinder is equipped with the filter screen of ventilation dustproof, and the first overflow sink passes through sewage pipe
The nozzle for being connected to the upper end of the second inner cylinder and sewage pipe is located at the lower section of filter screen, and the outer wall of the second inner cylinder is fixed with the second ring
Type reverse flow baffle, there are the second spilling water gap between the outer rim of the second ring-like reverse flow baffle and the inner wall of the second outer cylinder, outside second
The following diameter of cylinder is gradually reduced to form the second slag-drip opening, and the upper end of the second outer cylinder forms the second overflow sink；Second overflow water
The gap of slot is independently separated with sewage pipe；Snorkel is equipped with water inlet pipe close to the top of the first settling tank.
2. a kind of useless form sediment of high temperature as described in claim 1 expects heavy processing unit, it is characterised in that: the charging of the high-temperature material
The pipe shape that is tilted down is connected to the upper end of the first inner cylinder.
3. a kind of high temperature waste precipitate processing unit as described in claim 1, it is characterised in that: intaking in the snorkel
Pipe is equipped with venetian blind by the side of the second settling tank.
4. a kind of high temperature waste precipitate processing unit as claimed in claim 3, it is characterised in that: in blinds in the snorkel
Curtain is equipped with inspection manhole by the side of the second settling tank.
5. a kind of high temperature waste precipitate processing unit as described in claim 1, it is characterised in that: the second overflow sink
The connection of the water inlet pipe of gap and snorkel.
6. a kind of high temperature waste precipitate processing unit as described in claim 1, it is characterised in that: the filter screen is three layers multiple
Structure is closed, upper layer and lower layer are respectively Stainless steel mesh, and intermediate one layer is brown piece.
7. a kind of high temperature waste precipitate processing unit as described in claim 1, it is characterised in that: described first, second is ring-like
Reverse flow baffle is oblique, and the tilt angle between the first, second ring-like reverse flow baffle and horizontal plane is 60 °.
8. a kind of high temperature waste precipitate processing unit as described in claim 1, it is characterised in that: described first, second is ring-like
Reverse flow baffle is separately fixed at the lower end of the first, second inner cylinder.
9. a kind of high temperature waste precipitate treatment process, it is characterised in that: using as claimed in any of claims 1 to 8 in one of claims
High temperature waste material is sent into the first settling tank from feed pipe, while being opened on snorkel by a kind of high temperature waste precipitate processing unit
Spray equipment above the water inlet pipe and the second settling tank of side, the water flow that snorkel top water inlet pipe is sent into rinse high temperature waste material,
On the one hand, the material in high temperature waste material enters the first inner cylinder together with the water that water inlet pipe comes out, and another rise sinks down into the first outer cylinder
Bottom makes sludge by once standing, being concentrated, natural to decline slag naturally than reprecipitation and be discharged by the first slag-drip opening of bottom,
Meanwhile water level is increased naturally by the first outer cylinder and flows into the first overflow sink, is sent into the second of the second settling tank by sewage pipe
In inner cylinder, on the other hand, the high-temperature gas in high temperature waste material is directed to the second settling tank by snorkel, then is sent into through spray equipment
Shower water rinse high-temperature gas, gas gives off gas up to standard by filter screen filtration and obstructs dust, makes high-temperature gas
In dust enter the second inner cylinder with shower water, sewage, the dust in high-temperature gas and the shower water one of sewage pipe remove
It is sink to the second outer cylinder bottom, it is natural than reprecipitation by secondary standing, concentration, decline slag naturally by the second deslagging of bottom
Mouth discharge, meanwhile, water level is increased naturally by the second outer cylinder and flows into the second overflow sink, clear water is discharged by gap, clear water can
Reuse or qualified discharge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811597771.8A CN109481988B (en) | 2018-12-26 | 2018-12-26 | High Wen Feiliao precipitation treatment device and treatment process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811597771.8A CN109481988B (en) | 2018-12-26 | 2018-12-26 | High Wen Feiliao precipitation treatment device and treatment process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109481988A true CN109481988A (en) | 2019-03-19 |
| CN109481988B CN109481988B (en) | 2023-09-05 |
Family
ID=65712064
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811597771.8A Active CN109481988B (en) | 2018-12-26 | 2018-12-26 | High Wen Feiliao precipitation treatment device and treatment process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109481988B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114655940A (en) * | 2022-04-20 | 2022-06-24 | 北京万机汇机电工程技术有限公司 | Preparation method and system device of nitrous oxide |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020000162A1 (en) * | 2000-06-30 | 2002-01-03 | Alberto Falzone | Water apparatus for treating industrial waste products |
| CN102267751A (en) * | 2010-10-26 | 2011-12-07 | 苏木清 | Rapid precipitation and concentration tank for tailing sewage |
| CN105521674A (en) * | 2014-10-21 | 2016-04-27 | 富鼎电子科技(嘉善)有限公司 | Purification device |
| CN205235573U (en) * | 2015-11-09 | 2016-05-18 | 黄山中发耐磨材料有限公司 | Waste water cyclic utilization system is handled to intermediate frequency furnace flue gas |
| CN105800787A (en) * | 2016-05-30 | 2016-07-27 | 农业部沼气科学研究所 | Integrated autotrophic synchronous biological denitrification granulation device |
| CN106833694A (en) * | 2017-03-29 | 2017-06-13 | 攀枝花市银江金勇工贸有限责任公司 | A kind of town and country lightweight discarded object destructive distillation carbonization treatment system |
| CN208260428U (en) * | 2018-04-27 | 2018-12-21 | 李伟 | A kind of industrial waste gas desulfation dust-extraction device |
| CN209530308U (en) * | 2018-12-26 | 2019-10-25 | 厦门清胜环保科技有限公司 | A kind of high temperature waste precipitate processing unit |
-
2018
- 2018-12-26 CN CN201811597771.8A patent/CN109481988B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020000162A1 (en) * | 2000-06-30 | 2002-01-03 | Alberto Falzone | Water apparatus for treating industrial waste products |
| CN102267751A (en) * | 2010-10-26 | 2011-12-07 | 苏木清 | Rapid precipitation and concentration tank for tailing sewage |
| CN105521674A (en) * | 2014-10-21 | 2016-04-27 | 富鼎电子科技(嘉善)有限公司 | Purification device |
| CN205235573U (en) * | 2015-11-09 | 2016-05-18 | 黄山中发耐磨材料有限公司 | Waste water cyclic utilization system is handled to intermediate frequency furnace flue gas |
| CN105800787A (en) * | 2016-05-30 | 2016-07-27 | 农业部沼气科学研究所 | Integrated autotrophic synchronous biological denitrification granulation device |
| CN106833694A (en) * | 2017-03-29 | 2017-06-13 | 攀枝花市银江金勇工贸有限责任公司 | A kind of town and country lightweight discarded object destructive distillation carbonization treatment system |
| CN208260428U (en) * | 2018-04-27 | 2018-12-21 | 李伟 | A kind of industrial waste gas desulfation dust-extraction device |
| CN209530308U (en) * | 2018-12-26 | 2019-10-25 | 厦门清胜环保科技有限公司 | A kind of high temperature waste precipitate processing unit |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114655940A (en) * | 2022-04-20 | 2022-06-24 | 北京万机汇机电工程技术有限公司 | Preparation method and system device of nitrous oxide |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109481988B (en) | 2023-09-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102267751B (en) | Rapid precipitation and concentration tank for tailing sewage | |
| CN102267767B (en) | Rapid tailing sewage processing system | |
| CN209530308U (en) | A kind of high temperature waste precipitate processing unit | |
| CN109481988A (en) | A kind of high temperature waste precipitate processing unit and treatment process | |
| CN107285495A (en) | A kind of lithium ion battery production wastewater treatment device | |
| CN104129892A (en) | Integrated fish wastewater filtering barrel and using method thereof | |
| CN206081805U (en) | Filter pot | |
| CN105417862A (en) | Wastewater treatment system | |
| CN106115971B (en) | A kind of sewage-treatment plant | |
| CN206881242U (en) | High efficiency oil-water separate tank | |
| CN209464716U (en) | One heavy metal species tailings disposal plant | |
| CN206607110U (en) | Sewage-treatment plant | |
| CN205850312U (en) | Oil-water separation processing system | |
| CN210145588U (en) | Be applicable to grid for mine domestic sewage treatment | |
| CN203904101U (en) | Integrated equipment for comprehensive treatment of rainwater | |
| CN109481987A (en) | One heavy metal species tailings disposal plant and treatment process | |
| CN212632244U (en) | Multi-effect cyclone spray tower | |
| CN203990087U (en) | Glass fiber reinforced plastic settling tank | |
| CN205228211U (en) | Take coolant tank of overflow launder | |
| CN209010191U (en) | A kind of dross cleaning plant | |
| CN208933110U (en) | Primary sedimentation tank | |
| CN209683297U (en) | A kind of CNC finishing impression equipment central fluid supply cold supply system | |
| CN207158820U (en) | Chemical Manufacture reactant mixture decontaminates purifying box | |
| CN104003547B (en) | A kind of rainwater comprehensive treating process integration apparatus | |
| CN105352341A (en) | Cooling water tank with overflow groove |
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 |