CN2558645Y - Equalizing/unequalizing water treating composite reactor - Google Patents
Equalizing/unequalizing water treating composite reactor Download PDFInfo
- Publication number
- CN2558645Y CN2558645Y CN 02244848 CN02244848U CN2558645Y CN 2558645 Y CN2558645 Y CN 2558645Y CN 02244848 CN02244848 CN 02244848 CN 02244848 U CN02244848 U CN 02244848U CN 2558645 Y CN2558645 Y CN 2558645Y
- Authority
- CN
- China
- Prior art keywords
- chamber
- water
- communicated
- dry powder
- balanced
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The utility model relates to a balanced or imbalanced water treatment composite reactor. The reactor has the structure that: a liquid negative pressure generator (1) is communicated with a raw water inlet pipe; a rotational mixing reactor (19) is communicated with the liquid negative pressure generator (1) through a raw water conveying pipe (3); a dry-power balling gun (4) is arranged to input medicament into the raw water conveying pipe (3); an imbalance high effective reactor (20) is provided with a drum (21); a rotational coagulation chamber (23) is positioned in the drum; a settling chamber (38) used for slurry-residue separation is installed at the bottom of the drum and communicated with the rotational coagulation chamber; a clarifying chamber (25) is arranged between the drum and the rotational coagulation chamber; a water collecting tank (26)is installed on the top of the drum and communicated with the clarifying chamber (25); a clarified raw water outlet (27) is arranged on the drum and communicated with the water collecting chamber; an active flocculation generator (33) is arranged on the top of the drum and communicated with the rotational coagulation chamber. The utility model has the advantages of high utilization rate of the active flocculation, quick reaction, high clarifying and purifying rate, low medicament consumption and being capable of being applied to various raw waters.
Description
Technical field:
The utility model relates to a kind of waterpower active flocculus mass circular form primary water and handle equipment complex.
Background technology:
With regard to clarification equipment, tool typical case, authority's active flocculus mass (body refuse) circulating reaction equipment (equipment) mainly contains two classes both at home and abroad at present: a class is prototype and the modified version of the mechanical accelerating purifying pool Accelator Clarifier of U.S. Lnfilco company production in 1936; Another kind of is prototype and the modified version of the circulatior clarifier Circulator Clarifier that the forties occurs in last century.Advantages such as the former has, and reaction effect is good, and subject range is wide, and the medicine consumption is low.But front-end investment is big, the running cost height, and structure is complicated, not easy care.The latter has avoided the former deficiency, have simple in structure, less investment, running cost low etc. advantage; Deficiencies such as but it is higher to bring medicine to consume, and (parameters such as flow velocity, turbidity, temperature, start-stop time are changed) subject range is narrower.(" plumbing design manual " the 3rd table 7-21).Over more than 60 year, the latter many useful improvement or improvement have been carried out both at home and abroad.As adjust length of throat; Increase " two is anti-" degree of depth; Add backflow umbrella cover; Increase quantity of reflux; The body refuse circulation; Increase filtration process; Reaction chamber and body refuse circular integration; Change interior outside dimension etc.But all do not change the basic parameter and the performance of this kind equipment, as the layout of reaction energy GT and GT, the distribution of process section linear flow speed, backflow concentration, reaction efficiency etc.
The utility model content:
The purpose of this utility model is in order to overcome above deficiency, a kind of active flocculus mass utilization ratio height to be provided, being swift in response, reaction energy distributes rationally, and coagulation effect is good, defecate and purify efficient height, the medicine consumption is low, former water subject range is wide, simple in structure, and investment, working cost is low, floor space is few, start soon easy-maintaining, the balanced/nonbalanced water treatment compound reactor that use range is wide.
The purpose of this utility model is achieved like this:
The utility model water treatment compound reactor comprises the liquid negative pressure generator (1) that is communicated with former water inlet pipe, the eddy flow mixing reactor (19) that is communicated with the liquid negative pressure generator by former water transfer lime (3), the equivalent dry powder balling iron (4) of input medicament in former water transfer lime (3), lack of balance high efficiency reactor (20), cylindrical shell (21) is arranged in the lack of balance high efficiency reactor, be positioned at tube intravital cyclone coagulation chamber (23), be positioned at the slag slurry separate and subside chamber (38) that contains slag notch that communicates with the cyclone coagulation chamber of cylindrical shell bottom, be positioned at the clarifying chamber (25) between cylindrical shell and cyclone coagulation chamber, be positioned at the water leg that communicates with the clarifying chamber (26) on cylindrical shell top, the former water out of the clarification that is communicated with water leg (27) is arranged on the cylindrical shell, the active flocculus mass producer (33) that communicates with the cyclone coagulation chamber is arranged at cylindrical shell top, the liquid negative pressure generator can be converted to kinetic energy with former water pressure, utilize liquid flow velocity to entrainment effect and produce negative pressure, in order to adsorption activity floc sedimentation producer, equivalent dry powder balling iron, damp vapour in dust that produces during delivering medicament and the absorption balling iron makes the medicament drying; The eddy flow mixing reactor utilizes the rotational flow mode to quicken mixing and reaction of medicament and former water; The reacted former water of cyclone coagulation chamber and equivalent medicament, carry out the hybrid reaction second time at the medicament of this chamber and the input of active flocculus mass producer and the active flocculus mass that the active flocculus mass return line refluxes, in rotational flow, produce coagulation, be deposited on slag slurry separate and subside chamber; Current active flocculus mass filtering layer through the ingress, clarifying chamber bottom the cyclone coagulation chamber in clarifying chamber's enters the clarifying chamber, net is caught mechanism makes reacted former water obtain clarification, the former grain slag slurry separate and subside chamber that water leg is used to collect after the clarification is used to collect the slag slurry that transforms owing to deactivated floc sedimentation, and the while, it was again the pressure space of slurry handler; The active flocculus mass producer is in order to produce active flocculus mass; Equivalent dry powder balling iron is driven by dc speed-regulating motor, has different dry powder pharmaceutical mixing functionss in order to injecting former water transfer lime with removal thing equivalent mealy medicine in the former water.
Equivalent dry powder balling iron comprises the water medicine mixing section (7) that contains no pressure water import and medicament inlet that communicates with former water transfer lime in the above-mentioned water treatment compound reactor, what be positioned at water medicine mixing section is subjected to motor-operated spiral conveyer (9), the dry powder balling iron housing (11) that communicates with medicament inlet, be positioned at the tapered screw handling machinery (13) that is subjected to motor-operated band blade in dry powder balling iron housing exit, the tapered screw handling machinery of band blade can make different dry powder pharmaceuticals mix.
Have in the above-mentioned water treatment compound reactor and the gas negative pressure generator (16) that contains the dry powder pharmaceutical import that communicates with dry powder balling iron housing by the dry powder pharmaceutical transfer lime, active flocculus mass producer (33) communicates with the gas negative pressure generator by dry powder pharmaceutical transfer lime (34), and the gas negative pressure generator is in order to suck dry powder pharmaceutical.
Above-mentioned active flocculus mass producer, equivalent dry powder balling iron are communicated with the liquid negative pressure generator by pipeline respectively, form the circulation closed system.
There is an end to be communicated with the eddy flow mixing reactor in the above-mentioned water treatment compound reactor by pipeline, and the other end stretches into the floc sedimentation return line (24) in the cyclone coagulation chamber, the active flocculus mass return line is delivered to top, cyclone coagulation chamber with active flocculus mass, finishes active flocculus mass round-robin function.
On the above-mentioned slag slurry separate and subside locular wall compressed air inlet (37) is arranged, slag slurry separate and subside is indoor the slurry treater that communicates with compressed air inlet, utilizes pressurized air that slurry is pushed mummification, pack.
The rubber bag tank (40) that communicates with compressed air inlet is arranged in the above-mentioned slurry treater, be positioned at that slag slurry separate and subside is indoor that locate with respect to cyclone coagulation chamber and settling pocket slag slurry inlet (41) starches the hinged blanking cover (42) that the slag slurry inlet can be blocked in separate and subside chamber with slag, the foamed rubber pad (44) that contains drainage tray (43) is arranged on the blanking cover, drainage tray (45) is arranged on the rubber bag tank outer wall.
Above-mentioned slag slurry separate and subside chamber is a cone, gas enters the rubber bag tank from compressed air inlet, the slag slurry inlet is blocked in the blanking cover pop-up, continuous production along with the slag slurry, the gas that will be filled in the rubber bag tank under the pressure for the treatment of water is discharged gradually, blanking cover rotates thereupon the slag slurry inlet is opened, when slag is starched when the heavy collection of slag slurry settling pocket is full, gas is filled into rubber bag tank again, risen along with rubber bag tank constantly fills, the slag slurry of heavy collection in slag slurry settling pocket extruded, and the water that squeezes out the then drainage tray on the rubber bag tank outer wall is pressed against slag slurry settling pocket top, micropore and drainage tray by the foamed rubber on the blanking cover enter the bottom, clarifying chamber, after treating that rubber bag tank is by complete inflation, open slag slurry bleed valve, the slag after the discharging extruding is starched, finish slag slurry extruding discharging work, enter next working cycle again.
The gas-floating chamber (28) that has top to communicate in the above-mentioned water treatment compound reactor with the former water out of clarification on the lack of balance high efficiency reactor cylindrical shell, water inlet pipe and primary water that gas-floating chamber has the bottom to have and is communicated with air dissolved pump (29) export, air dissolved pump is in order to produce the micro-bubble of high dispersing, former water after the reaction clarification enters gas-floating chamber via top, clarifying chamber water leg, utilize the micro-bubble of the high dispersing of air dissolved pump generation to remove to adhere to micro-floccule residual in the water, make reacted former water obtain into clarification as carrier.
Have in the above-mentioned water treatment compound reactor and contain the monitor controller (16) that is contained in the active filtering layer monitoring sensor (47) on the lack of balance reactor shell inwall; monitor controller can have been bought on market; active filtering layer altitude information be can gather and water ph value, conductivity data gone out; starting or the dosage of closing the slurry handler and adjusting active flocculus mass producer and equivalent dry powder balling iron; the alarm of balling iron medicament magnitude of recruitment is provided; the magnetic valve fault alarm; system fault alarm provides protections such as power failure, the system fault.
Referring to Fig. 1, former water is along in the pipeline course of conveying, at first pass through negative pressure generator, before entering the eddy flow mixing reactor, directly will remove thing equivalent dry powder pharmaceutical with former water by equivalent dry powder balling iron and add in the pipe, the medicament of input enters the eddy flow mixing reactor with former water and reacts.Reacted former water sucks the active flocculus mass in the lack of balance high efficiency reactor in the process that enters the lack of balance high efficiency reactor, carry out coagulating at the indoor new active flocculus mass of throwing in the active flocculus mass producer of cyclone coagulation, the floc sedimentation that coagulating generates sinks to bottom, cyclone coagulation chamber, and water enters the clarifying chamber through bottom, cyclone coagulation chamber and clarifies.Uply then plough under water leg and go into gas-floating chamber, the water after further obtaining clarifying is discharged by the gas-floating chamber rising pipe.
The utility model is simple in structure, investment, working cost is low, floor space is few, (compare floor space with existing treatment facility and dwindle 1/3), active flocculus mass utilization ratio height is swift in response, reaction times, existing clarification equipment shortened 2～3 times, the administration system tube is clean small and exquisite, the stepless adjustment of dosage, and coagulation effect is good, defecate and purify efficient height, the medicine consumption is low, removes hardness scale and can reach more than 90%, and the desalination rate can reach more than 50%, delivery turbidity＜1 °, the level of automation height, applied widely, can be widely used in all water purification processes that add chemical agent.Both can be used as drinking water treatment equipment or service water pre-processing device---effectively remove impurity such as calcium in the water, magnesium, iron, manganese plasma and salt, silicon, organism, bacterium, also can be used as advanced treatment of wastewater middle-end equipment---turbid equipment falls in middle water reuse.
Description of drawings:
Fig. 1 is the utility model structural representation.
Fig. 2 is an equivalent dry powder balling iron structural representation.
Fig. 3 is eddy flow mixing and reaction chamber and cyclone coagulation chamber connection diagram.
Fig. 4 is slag slurry separate and subside cell structure synoptic diagram.
Fig. 5 is a rubber bag tank topping up procedure chart among Fig. 4.
Fig. 6 blocks the state graph of slag slurry inlet for blanking cover among Fig. 4.
Fig. 7 is an I portion enlarged view among Fig. 6.
Fig. 8 is an II portion enlarged view among Fig. 6.
Embodiment:
Referring to Fig. 1, Fig. 2, the liquid negative pressure generator 1 of outsourcing is connected with former water inlet pipe 2 and former water transfer lime 3 respectively.Equivalent dry powder balling iron 4 comprises the water medicine mixing section 7 that contains no pressure water import 5 and medicament outlet 6 that is communicated with former water transfer lime 3 as shown in Figure 2, is arranged in the spiral conveyer 9 that water medicine mixing section is driven by dc speed-changing motor 8.At water medicine mixing section front end control valve 10 is arranged.In the dry powder balling iron housing 11 that is communicated with medicament inlet dc speed-changing motor 12 is arranged, the tapered screw handling machinery 13 of the band blade that is positioned at the medicament exit that is connected with dc speed-changing motor.Dry powder balling iron housing is communicated with liquid negative pressure generator and outsourcing gas negative pressure generator 16 by dry powder pharmaceutical transfer lime 14,15 respectively.Dry powder pharmaceutical import 17 is arranged on the gas negative pressure generator 16, and the gas negative pressure generator is communicated with air compressor 18.Outsourcing eddy flow mixing reactor 19 is communicated with former water transfer lime 3.The cyclone coagulation chamber 23 that is communicated with eddy flow mixing reactor 19 by transfer lime 22 is arranged in the cylindrical shell 21 of lack of balance high efficiency reactor 20, and transfer lime 22 tangentially is connected as shown in Figure 3 with cyclone coagulation chamber 23 walls.One end of floc sedimentation return line 24 is communicated with transfer lime 22 and the other end stretches into cyclone coagulation chamber bottom.Being positioned between cylindrical shell and cyclone coagulation chamber has clarifying chamber 25, and the water leg 26 that communicates with the clarifying chamber is arranged at its top.The former water out 27 of the clarification that is communicated with water leg 26 is arranged on the cylindrical shell.Gas-floating chamber 28 is communicated with and the liquid delivery tube 30 that is communicated with air dissolved pump 29 is arranged at the bottom with the former water out 27 of clarification, and primary water exports 31 once more.The primary water exit is connected with primary water transfer lime 32 once more.Active flocculus mass producer 33 places the cylindrical shell top and is communicated with it.The active flocculus mass producer is communicated with gas negative pressure generator 16 and liquid negative pressure generator 1 by dry powder pharmaceutical transfer lime 34 and dust adsorption tube 35.The cone slag slurry separate and subside chamber 38 that contains slag notch 36 and compressed air inlet 37 that is communicated with the cyclone coagulation chamber is arranged at the cylindrical shell bottom.Referring to Fig. 4～Fig. 8, slurry handler 39 comprises the regulation and control elastic caoutchouc capsule 40 that is arranged in slag slurry separate and subside chamber, is positioned at slag slurry slag slurry inlet 41 places, separate and subside chamber one end and is hinged on blanking cover 42 on the slag slurry separate and subside chamber.The foamed rubber 44 that contains drainage tray 43 is arranged on the blanking cover, drainage tray 45 is arranged on the rubber bag tank outer wall.Active filtering layer monitoring sensor 47 in the monitor controller 46 of outsourcing is contained on the cylinder inboard wall.Control valve is housed respectively on each pipeline.
Claims (10)
1, compound reactor is handled in balanced/non-even Hengshui, it is characterized in that comprising the liquid negative pressure generator (1) that is communicated with former water inlet pipe, the eddy flow mixing reactor (19) that is communicated with the liquid negative pressure generator by former water transfer lime (3), the equivalent dry powder balling iron (4) of input medicament in former water transfer lime (3), lack of balance high efficiency reactor (20), cylindrical shell (21) is arranged in the lack of balance high efficiency reactor, be positioned at tube intravital cyclone coagulation chamber (23), be positioned at the slag slurry separate and subside chamber (38) that contains slag notch that communicates with the cyclone coagulation chamber of cylindrical shell bottom, be positioned at the clarifying chamber (25) between cylindrical shell and cyclone coagulation chamber, be positioned at the water leg that communicates with the clarifying chamber (26) on cylindrical shell top, the former water out of the clarification that is communicated with water leg (27) is arranged on the cylindrical shell, and the active flocculus mass producer (33) that communicates with the cyclone coagulation chamber is arranged at cylindrical shell top.
2, balanced/nonbalanced water treatment compound reactor according to claim 1, it is characterized in that equivalent dry powder balling iron comprises the water medicine mixing section (7) that contains no pressure water import and medicament inlet that communicates with former water transfer lime, what be positioned at water medicine mixing section is subjected to motor-operated spiral conveyer (9), the dry powder balling iron housing (11) that communicates with medicament inlet is positioned at the tapered screw handling machinery (13) that is subjected to motor-operated band blade in dry powder balling iron housing exit.
3, balanced/nonbalanced water treatment compound reactor according to claim 1 and 2, it is characterized in that the gas negative pressure generator (16) that contains the dry powder pharmaceutical import that communicates with dry powder balling iron housing by the dry powder pharmaceutical transfer lime is arranged, active flocculus mass producer (33) communicates with the gas negative pressure generator by dry powder pharmaceutical transfer lime (34).
4, balanced/nonbalanced water treatment compound reactor according to claim 1 and 2 is characterized in that active flocculus mass producer, equivalent dry powder balling iron are communicated with the liquid negative pressure generator by pipeline respectively.
5, balanced/nonbalanced water treatment compound reactor according to claim 1 and 2 is characterized in that having an end to be communicated with the eddy flow mixing reactor by pipeline and the other end stretches into the floc sedimentation return line (24) in the cyclone coagulation chamber.
6, balanced/nonbalanced water treatment compound reactor according to claim 1 and 2 is characterized in that on the slag slurry separate and subside locular wall compressed air inlet (37) being arranged, and slag slurry separate and subside is indoor the slurry treater that communicates with compressed air inlet.
7, balanced/nonbalanced water treatment compound reactor according to claim 6, it is characterized in that having in the slurry treater rubber bag tank (40) that communicates with compressed air inlet, be positioned at that slag slurry separate and subside is indoor that locate with respect to cyclone coagulation chamber and settling pocket slag slurry inlet (41) starches the hinged blanking cover (42) that the slag slurry inlet can be blocked in separate and subside chamber with slag, the foamed rubber pad (44) that contains drainage tray (43) is arranged on the blanking cover, drainage tray (45) is arranged on the rubber bag tank outer wall.
8, balanced/nonbalanced water treatment compound reactor according to claim 6 is characterized in that slag slurry separate and subside chamber is a cone.
9, balanced/nonbalanced water treatment compound reactor according to claim 1 and 2, the gas-floating chamber (28) that it is characterized in that having top to communicate with the former water out of clarification on the lack of balance high efficiency reactor cylindrical shell, water inlet pipe and primary water that gas-floating chamber has the bottom to have and is communicated with air dissolved pump (29) export.
10, balanced/nonbalanced water treatment compound reactor according to claim 1 and 2 is characterized in that having containing the monitor controller (46) that is contained in the active filtering layer monitoring sensor (47) on the lack of balance reactor shell inwall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02244848 CN2558645Y (en) | 2002-11-22 | 2002-11-22 | Equalizing/unequalizing water treating composite reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02244848 CN2558645Y (en) | 2002-11-22 | 2002-11-22 | Equalizing/unequalizing water treating composite reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2558645Y true CN2558645Y (en) | 2003-07-02 |
Family
ID=33716628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02244848 Expired - Fee Related CN2558645Y (en) | 2002-11-22 | 2002-11-22 | Equalizing/unequalizing water treating composite reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2558645Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110156227B (en) * | 2019-05-31 | 2021-12-03 | 濮阳可利威化工有限公司 | Sewage treatment system and method |
-
2002
- 2002-11-22 CN CN 02244848 patent/CN2558645Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110156227B (en) * | 2019-05-31 | 2021-12-03 | 濮阳可利威化工有限公司 | Sewage treatment system and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102225803A (en) | Biomembrane reactor, waste water treating system and method for treating waste water | |
| CN102249491A (en) | Deep treatment device and process for secondary treatment effluent of urban sewage plant | |
| CN109110992A (en) | A kind of plasma coagulation integrated effluent disposal system and processing method | |
| CN101704617A (en) | Equipment for reclaiming and processing petrified enterprise sewage and process technology thereof | |
| CN108706822A (en) | Biological rotary cage integration pilot-plant | |
| CN106977054A (en) | Municipal wastewater cleaning system construction technology | |
| CN201400630Y (en) | Chemical fiber wastewater treatment system | |
| CN110550844A (en) | Domestic sewage's processing system | |
| CN209602282U (en) | A kind of sanitary sewage deodorization direct purification separation equipment | |
| CN2558645Y (en) | Equalizing/unequalizing water treating composite reactor | |
| CN202099169U (en) | Device for advanced treatment of secondary effluent in municipal sewage plant | |
| CN108467165A (en) | A kind of efficient dephosphorization rural domestic sewage treatment system | |
| CN2651237Y (en) | Unitary sewage purifying desliming rapid treating apparatus | |
| CN106554133A (en) | A kind of sewage disposal automation control system | |
| CN202156985U (en) | Wastewater reuse treatment equipment | |
| CN109721185A (en) | A kind of reinforced ammonia nitrogen waste water processing system and ammonia nitrogen waste water treatment method | |
| CN104843943B (en) | A kind of industrial sewage process method and device | |
| CN210393887U (en) | Small-size sewage treatment integration equipment | |
| CN208762357U (en) | A kind of energy saving sewage treating machine of classification | |
| CN208429964U (en) | A kind of dispersion type domestic wastewater high-efficient purification equipment | |
| CN2217013Y (en) | High efficiency apparatus for treating high turbidity waste water | |
| CN208667399U (en) | A kind of efficient dephosphorization rural domestic sewage treatment system | |
| CN206692514U (en) | A kind of portable Sewage Disposal | |
| CN201062223Y (en) | Apparatus for purifying sewage | |
| CN202968347U (en) | Screw type sludge dehydrating machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |