CN105731679A - High turbidity integrated purifier and purification method thereof - Google Patents
High turbidity integrated purifier and purification method thereof Download PDFInfo
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- CN105731679A CN105731679A CN201410731822.7A CN201410731822A CN105731679A CN 105731679 A CN105731679 A CN 105731679A CN 201410731822 A CN201410731822 A CN 201410731822A CN 105731679 A CN105731679 A CN 105731679A
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Abstract
A high turbidity integrated purifier and a purification method thereof. Major pollutants in gas making wastewater contain coal particle suspended solids, cyanide, sulfide, volatile phenol and ammonia, and the pollutants volatilizing into the atmosphere produce secondary pollution. The purifier includes a base; the base is connected to a cylinder; the cylinder is internally provided with a swirl reaction chamber, a clarification chamber, a settling chamber, a clear water zone and a water gathering zone from bottom to top; the bottom of the swirl reaction chamber is connected to a water intake pipe; the top of the swirl reaction chamber is provided with a central mud transport bucket; the periphery of the swirl reaction chamber is provided with a mud bucket communicating with the swirl reaction chamber through a central mud transport pipe; the top of the mud bucket is connected to a clarified water pipe; the bottom of the mud bucket is connected to a mud collecting tube; the water gathering zone is connected to a collector pipe and a slag discharge pipe; and the collector pipe is connected to a drainage pipe. The invention can be applied to treatment of synthesis ammonia gas-making wastewater.
Description
Technical field:
The present invention relates to a kind of high concentrtion one depurator and purification method thereof.
Background technology:
With anthracite or coke for raw material production synthesize ammonia time, often produce 1t and synthesize ammonia and can discharge gasification wastewater 50～80t, its wastewater source to the spray of the semiwater gas that gas making steam stove produces, washing and cools down water in gas washing case and scrubbing tower.In gasification wastewater, contained major pollutants have coal grain class float, cyanide, sulfide, Volatile Phenols and ammonia nitrogen etc..Less demanding to water quality of the spray of semiwater gas, washing and cooling, processing method adopts precipitation, cooling closed cycle and precipitation, cooling, the biochemistry big class of closed cycle two.
Summary of the invention:
It is an object of the invention to provide a kind of high concentrtion one depurator and purification method thereof.
Above-mentioned purpose is realized by following technical scheme:
A kind of high concentrtion one depurator, its composition includes: base, described base is connected with cylinder, cyclone reaction room it is sequentially provided with from the bottom up in described cylinder, clarifying chamber, mud chamber, clear water zone, gathering ground, described bottom, cyclone reaction room is connected with water inlet pipe, described cyclone reaction ceiling end is provided with central defeated bucket, the periphery of described cyclone reaction room is provided with bucket, communicated with described cyclone reaction room by described central dredging tube, described bucket top is connected with clarification water pipe, described bucket bottom is connected with sludge pipe, described gathering ground and collector pipe, scum pipe connects, described collector pipe is connected with drain pipe.
Described high concentrtion one depurator, the ascending change in cross section of described cyclone reaction room.
Described high concentrtion one depurator, is provided with one group of inclined tube in described mud chamber.
A kind of purification method of described high concentrtion one depurator, the step of the method is as follows:
nullThe mixing water having added coagulant or flocculation aid enters cyclone reaction room eddy flow rising reaction formation floccule body from water inlet pipe，Due to the change that the cross section of reative cell is ascending，Along with current rise，Floccule body is constantly grown up and is not destroyed，Obstruct due to central defeated bucket，Excess sludge is sent into bucket separate with the floccule body in reative cell，Owing in reative cell, current are up-flow state，Floccule body is made to form superposed layer，Float in water is adsorbed、Filter、Precipitation，Floccule body is made constantly to grow up to precipitable yardstick，And a number of oils and Organic substance can be adsorbed，When the appropriate draining of unlatching primary water tube valve，Residual active sludge in superposed layer just constantly enters bucket through central defeated bucket and precipitates，Discharge with automatic mud removing valve then through sludge pipe，Reaction water continues to ascend into the cyclone clarification room being located at above reative cell and carries out first time clarification，Primary water ascends into tube settling room from clarifying chamber，Owing to inclined tube wetted perimeter is big，Hydraulic radius is little，Every inclined tube is exactly a Ge little mud chamber，Deposition efficiency is higher than clarifying chamber，Heavy for the clarifying chamber thinner floccule body not got off is precipitated，Enter clarifying chamber，The big floccule body reacted further precipitates，Precipitation water is through inflow gathering ground, clear water zone，Collector pipe is submerged water outlet，Discharged by outlet pipe，In water, the heavy light granules not gone down floats on the surface，Discharged by scum pipe.
Beneficial effects of the present invention:
Present invention process flow process is reasonable, simple in construction, and floor space is little, and place capacity is big, and two-stage precipitation adapts to high concentrtion and more severe sewage quality, and effluent quality is good, and sludge discharging period is long.
Present device is high, and water outlet can be directly entered follow-up equipment, eliminates centre lifting means and regulates structures, decreases middle water pump and pond, reduction operation energy consumption, saving operating cost and investment.
Accompanying drawing illustrates:
Accompanying drawing 1 is the structural representation of the present invention.
Detailed description of the invention:
Embodiment 1:
A kind of high concentrtion one depurator, its composition includes: base 1, described base is connected with cylinder 2, cyclone reaction room 3 it is sequentially provided with from the bottom up in described cylinder, clarifying chamber 4, mud chamber 5, clear water zone 6, gathering ground 7, described bottom, cyclone reaction room is connected with water inlet pipe 8, described cyclone reaction ceiling end is provided with central defeated bucket 9, the periphery of described cyclone reaction room is provided with bucket 10, communicated with described cyclone reaction room by described central dredging tube, described bucket top is connected with clarification water pipe 11, described bucket bottom is connected with sludge pipe 12, described gathering ground and collector pipe 13, scum pipe connects 14, described collector pipe is connected with drain pipe 15.
Embodiment 2:
High concentrtion one depurator according to embodiment 1, the ascending change in cross section of described cyclone reaction room.
Embodiment 3:
High concentrtion one depurator according to embodiment 1, is provided with one group of inclined tube in described mud chamber.
Embodiment 4:
A kind of purification method of high concentrtion one depurator described for one of embodiment 1-3, the step of the method is as follows:
nullThe mixing water having added coagulant or flocculation aid enters cyclone reaction room eddy flow rising reaction formation floccule body from water inlet pipe，Due to the change that the cross section of reative cell is ascending，Along with current rise，Floccule body is constantly grown up and is not destroyed，Obstruct due to central defeated bucket，Excess sludge is sent into bucket separate with the floccule body in reative cell，Owing in reative cell, current are up-flow state，Floccule body is made to form superposed layer，Float in water is adsorbed、Filter、Precipitation，Floccule body is made constantly to grow up to precipitable yardstick，And a number of oils and Organic substance can be adsorbed，When the appropriate draining of unlatching primary water tube valve，Residual active sludge in superposed layer just constantly enters bucket through central defeated bucket and precipitates，Discharge with automatic mud removing valve then through sludge pipe，Reaction water continues to ascend into the cyclone clarification room being located at above reative cell and carries out first time clarification，Primary water ascends into tube settling room from clarifying chamber，Owing to inclined tube wetted perimeter is big，Hydraulic radius is little，Every inclined tube is exactly a Ge little mud chamber，Deposition efficiency is higher than clarifying chamber，Heavy for the clarifying chamber thinner floccule body not got off is precipitated，Enter clarifying chamber，The big floccule body reacted further precipitates，Precipitation water is through inflow gathering ground, clear water zone，Collector pipe is submerged water outlet，Discharged by outlet pipe，In water, the heavy light granules not gone down floats on the surface，Discharged by scum pipe.
Claims (4)
1. a high concentrtion one depurator, its composition includes: base, it is characterized in that: described base is connected with cylinder, cyclone reaction room it is sequentially provided with from the bottom up in described cylinder, clarifying chamber, mud chamber, clear water zone, gathering ground, described bottom, cyclone reaction room is connected with water inlet pipe, described cyclone reaction ceiling end is provided with central defeated bucket, the periphery of described cyclone reaction room is provided with bucket, communicated with described cyclone reaction room by described central dredging tube, described bucket top is connected with clarification water pipe, described bucket bottom is connected with sludge pipe, described gathering ground and collector pipe, scum pipe connects, described collector pipe is connected with drain pipe.
2. high concentrtion according to claim 1 one depurator, is characterized in that: the ascending change in cross section of described cyclone reaction room.
3. high concentrtion according to claim 1 one depurator, is characterized in that: be provided with one group of inclined tube in described mud chamber.
4. a purification method for high concentrtion one depurator described for one of claim 1-3, is characterized in that: the step of the method is as follows:
nullThe mixing water having added coagulant or flocculation aid enters cyclone reaction room eddy flow rising reaction formation floccule body from water inlet pipe，Due to the change that the cross section of reative cell is ascending，Along with current rise，Floccule body is constantly grown up and is not destroyed，Obstruct due to central defeated bucket，Excess sludge is sent into bucket separate with the floccule body in reative cell，Owing in reative cell, current are up-flow state，Floccule body is made to form superposed layer，Float in water is adsorbed、Filter、Precipitation，Floccule body is made constantly to grow up to precipitable yardstick，And a number of oils and Organic substance can be adsorbed，When the appropriate draining of unlatching primary water tube valve，Residual active sludge in superposed layer just constantly enters bucket through central defeated bucket and precipitates，Discharge with automatic mud removing valve then through sludge pipe，Reaction water continues to ascend into the cyclone clarification room being located at above reative cell and carries out first time clarification，Primary water ascends into tube settling room from clarifying chamber，Owing to inclined tube wetted perimeter is big，Hydraulic radius is little，Every inclined tube is exactly a Ge little mud chamber，Deposition efficiency is higher than clarifying chamber，Heavy for the clarifying chamber thinner floccule body not got off is precipitated，Enter clarifying chamber，The big floccule body reacted further precipitates，Precipitation water is through inflow gathering ground, clear water zone，Collector pipe is submerged water outlet，Discharged by outlet pipe，In water, the heavy light granules not gone down floats on the surface，Discharged by scum pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410731822.7A CN105731679A (en) | 2014-12-06 | 2014-12-06 | High turbidity integrated purifier and purification method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410731822.7A CN105731679A (en) | 2014-12-06 | 2014-12-06 | High turbidity integrated purifier and purification method thereof |
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| Publication Number | Publication Date |
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| CN105731679A true CN105731679A (en) | 2016-07-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410731822.7A Withdrawn CN105731679A (en) | 2014-12-06 | 2014-12-06 | High turbidity integrated purifier and purification method thereof |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106830439A (en) * | 2017-03-17 | 2017-06-13 | 常州大学 | A kind of high turbidity raw sewage clarifier peculiar to vessel |
| CN107244760A (en) * | 2017-08-10 | 2017-10-13 | 安庆市凯立金刚石科技有限公司 | A kind of stone wastewater processing unit |
| CN108569798A (en) * | 2017-10-09 | 2018-09-25 | 丹阳雅奕智能电子技术有限公司 | Full-automatic water treatment device |
-
2014
- 2014-12-06 CN CN201410731822.7A patent/CN105731679A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106830439A (en) * | 2017-03-17 | 2017-06-13 | 常州大学 | A kind of high turbidity raw sewage clarifier peculiar to vessel |
| CN107244760A (en) * | 2017-08-10 | 2017-10-13 | 安庆市凯立金刚石科技有限公司 | A kind of stone wastewater processing unit |
| CN108569798A (en) * | 2017-10-09 | 2018-09-25 | 丹阳雅奕智能电子技术有限公司 | Full-automatic water treatment device |
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| C06 | Publication | ||
| PB01 | Publication | ||
| WW01 | Invention patent application withdrawn after publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20160706 |