CN103112971B - Coagulation-floatation and co-coagulation solid-liquid separation device and solid-liquid separation method - Google Patents
Coagulation-floatation and co-coagulation solid-liquid separation device and solid-liquid separation method Download PDFInfo
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- CN103112971B CN103112971B CN201310071802.7A CN201310071802A CN103112971B CN 103112971 B CN103112971 B CN 103112971B CN 201310071802 A CN201310071802 A CN 201310071802A CN 103112971 B CN103112971 B CN 103112971B
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- 239000007788 liquid Substances 0.000 title claims abstract description 88
- 238000000926 separation method Methods 0.000 title claims abstract description 32
- 238000005345 coagulation Methods 0.000 title claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 256
- 238000006243 chemical reaction Methods 0.000 claims abstract description 112
- 239000010865 sewage Substances 0.000 claims abstract description 107
- 239000007787 solid Substances 0.000 claims abstract description 41
- 230000015271 coagulation Effects 0.000 claims abstract description 28
- 238000000034 method Methods 0.000 claims abstract description 19
- 230000008569 process Effects 0.000 claims abstract description 13
- 239000000701 coagulant Substances 0.000 claims description 52
- 239000000126 substance Substances 0.000 claims description 47
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 42
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 36
- 239000003814 drug Substances 0.000 claims description 32
- 239000002699 waste material Substances 0.000 claims description 27
- 239000000377 silicon dioxide Substances 0.000 claims description 21
- 238000005054 agglomeration Methods 0.000 claims description 19
- 238000009826 distribution Methods 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 16
- 230000001105 regulatory effect Effects 0.000 claims description 16
- 230000000630 rising effect Effects 0.000 claims description 15
- 239000003002 pH adjusting agent Substances 0.000 claims description 14
- 238000005070 sampling Methods 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 9
- 230000000694 effects Effects 0.000 claims description 8
- 238000000746 purification Methods 0.000 claims description 5
- 230000008719 thickening Effects 0.000 claims description 4
- 238000005520 cutting process Methods 0.000 claims description 3
- 239000006185 dispersion Substances 0.000 claims description 3
- 238000005188 flotation Methods 0.000 abstract description 5
- 239000002893 slag Substances 0.000 abstract description 3
- 239000000084 colloidal system Substances 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 6
- 230000001112 coagulating effect Effects 0.000 description 3
- 238000009300 dissolved air flotation Methods 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 238000005354 coacervation Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
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- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
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- 238000010348 incorporation Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
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Abstract
本发明属于污水处理设备，特别涉及一种混凝气浮共凝聚固液分离装置及其分离方法；其特征在于：所述的分离装置是在污水池处依序装设污水加药混合系统、多相介质泵溶气系统、混合反应共凝聚系统和共凝聚固液分离装置；本发明不仅设计合理，结构紧凑，具有独立的混合共凝聚反应和共凝聚固液分离系统，而且实现优化混凝气浮共凝聚气浮分离过程，还在排浮渣方式上采用变水位排渣方式，具有简易便捷、整套设备占地小、投资少、效率高等特点。特别适用于处理生产和生活过程中产生污水与废水中的胶体和悬浮物，实现固液分离。
The invention belongs to sewage treatment equipment, in particular to a coagulation air flotation co-coagulation solid-liquid separation device and its separation method; it is characterized in that: the separation device is a sewage dosing and mixing system sequentially installed at the sewage pool, Multiphase medium pump dissolved air system, mixed reaction coagulation system and coagulation solid-liquid separation device; the invention not only has reasonable design, compact structure, has independent mixed coagulation reaction and coagulation solid-liquid separation system, but also realizes optimized coagulation The air flotation, coagulation and air flotation separation process also adopts the variable water level slag discharge method in the scum discharge method, which is simple and convenient, the whole set of equipment occupies a small area, less investment, and high efficiency. It is especially suitable for the treatment of colloids and suspended solids in sewage and wastewater produced in production and living processes, and to achieve solid-liquid separation.
Description
Technical field
The invention belongs to and sewage disposal device, relate in particular to a kind of coagulation air-float co-agglomeration equipment for separating liquid from solid and separation method thereof.
Background technology
Air floating water purification technology be one efficiently, solid-liquid separation technique fast, start from ore dressing, this technology is quite subject to the concern of Chinese scholars and is developed rapidly in water treatment field, be widely used at present feedwater, especially the purifying treatment of low temperature, low turbid, rich algae water, and municipal effluent and Industrial Wastewater Treatment.Air supporting process, according to the producing method difference of bubble, can be divided into electrolysis-coagulation air supporting, gas distribution air supporting and air-dissolving air-float, and partial reflux formula pressure air-dissolving air-float is wherein technique the most frequently used in water treatment.Air supporting is the release of reducing pressure suddenly of the air by being dissolved in the water, and forms a large amount of microbubbles, and the wadding grain floating after coagulation is removed, and reaches water purification object.The quality of effect depends on the adhesion situation of bubble and wadding grain.The basic form adhering to mainly contains three kinds: bubble adheres to the direct collision of wadding grain; Bubble is separated out from wadding grain surface; Bubble is growth or parcel from wadding intergranular gap.Existing air-flotation separation equipment is mainly realized solid-liquid separation by absorption and the jacking of bubble and particle, and effect is unstable, and efficiency ratio is poor.Flotation waste water treatment technological process makes full use of the contact medium effect of microbubble, make microbubble, micro-floccule in suitable reactor, carry out contact flocculation, it is one that the homophase of particulate matter and out-phase contact flocculation process are melted to two, final form be applicable to separating, it is stable that bubble--flco is aggregate altogether, thereby has improved daf efficiency.
At present, traditional air-float technology is all first coagulating agent and coagulant aids fully to be mixed with pending water, then adopts the mode of following current to make pending water and dissolved air water carry out coagulating, reaches the object of water treatment.This traditional water technology time is long, needs to arrange coagulation dosing unit and coagulating unit simultaneously, causes forming common cohesion bubble--and flco is aggregate altogether, and separating effect is poor, and floor space is large, and cost of equipment is also high.
Summary of the invention
The present invention is intended to avoid the shortcoming and defect part existing in above-mentioned technology, a kind of coagulation air-float co-agglomeration equipment for separating liquid from solid and separation method thereof are provided, and this coagulation air-float co-agglomeration equipment for separating liquid from solid is by hybrid reaction system is set independently, independently solid-liquid separation system is realized the optimization of coagulation air-float co-agglomeration dissolved air flotation process; In row's scum silica frost mode, adopt the water level deslagging mode that becomes simultaneously, therefore, this coagulation air-float co-agglomeration equipment for separating liquid from solid is not only reasonable in design, compact construction, there is independently hybrid reaction and solid-liquid separation system, and realize and optimize coagulation air-float co-agglomeration dissolved air flotation process, there is simple and easy convenient, whole plant and take up an area little, less investment, efficiency high.
The present invention adopts following technical scheme to realize: described coagulation air-float co-agglomeration equipment for separating liquid from solid, is characterized in that: described tripping device is at sewage lagoon place, sequentially install sewage dosing mixing system, multiphase medium pump air dissolving system, the common condensed system of hybrid reaction and condense altogether equipment for separating liquid from solid, described sewage dosing mixing system is comprised of waste pipe, sewage variable valve, sewage vacuum tensimeter, tensimeter, jet variable valve first, sump pump, pH adjusting agent medicine-chest, PAC coagulating agent medicine-chest, PAM coagulant aids medicine-chest, dosing house steward, suction medicine variable valve, medicine absorbing tube, dosing pump and sewage dissolved air water house steward, insert in sewage lagoon one end of described waste pipe, the other end of waste pipe is connected with the import of sump pump, sequentially installs sewage variable valve, sewage vacuum tensimeter and jet variable valve first with sump pump on the waste pipe being connected, on the waste pipe between its sewage vacuum tensimeter and jet variable valve first, by pipeline, be sequentially connected pH adjusting agent medicine-chest, PAC coagulating agent medicine-chest, on the pipe between described pH adjusting agent medicine-chest and waste pipe, sequentially install pH regulator valve first, pH under meter and pH regulator valve second, on pipeline between described PAC coagulating agent medicine-chest and waste pipe, sequentially install PAC coagulating agent variable valve first, PAC coagulating agent flow meter and PAC coagulating agent variable valve second, PAM coagulant aids medicine-chest is set after PAC coagulating agent medicine-chest, and the outside of described PAM coagulant aids medicine-chest is connected with the import of dosing pump by medicine absorbing tube, on its medicine absorbing tube, medicine variable valve is inhaled in installing, and described sewage pump outlet is connected with multiphase medium pump air dissolving system by sewage dissolved air water house steward, on described sewage dissolved air water house steward, sequentially install dissolved air water tensimeter, sewage dissolved air water variable valve first, sewage dissolved air water under meter, sewage dissolved air water variable valve second and sewage dissolved air water sampling valve, with the one end that is connected jet pipeline on dissolved air water house steward between dissolved air water tensimeter and dissolved air water variable valve first, the other end of described jet pipeline is connected on waste pipe, on its jet pipeline, sequentially install ejector, fluidic flowmeter and jet variable valve second, described multiphase medium pump air dissolving system is comprised of dissolved air water house steward, sampling valve, dissolved air water variable valve first, dissolved air water under meter, dissolved air water variable valve second, dissolved air water house steward variable valve, gas-liquid pressure table, dissolved air water arm A, dissolved air water arm B and gas-liquid mixing pump, on described dissolved air water house steward, sequentially install gas-liquid pressure table and dissolved air water house steward variable valve, one end of described dissolved air water arm B enters after A place is connected with sewage dissolved air water house steward in path hybrid reaction pipe, the other end of described dissolved air water arm B is connected with the exit end of gas-liquid mixing pump by dissolved air water house steward, sequentially installs dissolved air water arm B variable valve first, dissolved air water arm B under meter, dissolved air water arm B variable valve second and dissolved air water arm B sampling valve on described dissolved air water arm B, one end of described dissolved air water arm A enters in the hybrid reaction pipe of large footpath after being connected by pipeline with chemical feeding points D after being connected with the B point place of central diameter hybrid reaction pipe water side again, the other end of its dissolved air water arm A is connected with the dissolved air water house steward of gas-liquid mixing pump, sequentially installs dissolved air water arm A variable valve first, dissolved air water arm A under meter, dissolved air water arm A variable valve second on described dissolved air water arm A, the entrance end of described gas-liquid mixing pump condenses together in the separate housings in equipment for separating liquid from solid and connects by pipeline, and on this pipeline, sequentially install gas meter first and gas regulating valve first, on the import of its gas-liquid mixing pump and the pipeline of outlet, install gas-jet device, gas meter second and gas regulating valve second, described hybrid reaction altogether condensed system is comprised of path hybrid reaction pipe assembly, central diameter hybrid reaction pipe, pipe connecting, pipeline and large footpath hybrid reaction pipe assembly, and described path hybrid reaction pipe assembly is comprised of path hybrid reaction pipe, path vent valve, path dosing arm, path chemicals addition control valve first, path dosing under meter and path chemicals addition control valve second, described path hybrid reaction pipe is installed path vent valve by pipeline, the C point place of its path hybrid reaction pipe one end connects one end of path dosing arm, it is upper that the other end of described path dosing arm is connected to dosing house steward, and on its path dosing arm, sequentially installs path chemicals addition control valve first, path dosing under meter and path chemicals addition control valve second, the chemical feeding points C place of described path hybrid reaction pipe one end is connected with one end of central diameter hybrid reaction pipe by pipe connecting, the other end of described central diameter hybrid reaction pipe is connected to by pipeline on the chemical feeding points D of the large footpath dosing arm in the hybrid reaction pipe assembly of large footpath, described large footpath hybrid reaction pipe assembly is by large footpath hybrid reaction pipe, large footpath dosing arm, large footpath chemicals addition control valve first, large footpath dosing under meter and large footpath chemicals addition control valve second, rising pipe and go out water regulating valve and form, described large footpath hybrid reaction pipe is installed large footpath vent valve by pipeline, its large footpath hybrid reaction pipe connects one end of large footpath dosing arm, and the other end of described large footpath dosing arm connects on dosing house steward, on its large footpath dosing arm, sequentially install large footpath chemicals addition control valve first, large footpath dosing under meter and large footpath chemicals addition control valve second, the rising pipe of described large footpath hybrid reaction pipe is connected on separator tube bottom through the separate housings, the back-up ring that condense in equipment for separating liquid from solid altogether, on its rising pipe, installs out water regulating valve, described common cohesion equipment for separating liquid from solid is by separate housings, back-up ring, perforation header, separator tube, distribution pipe, cone separator, scum layer district, scum pipe, isolate water pipe, high-order water shoot, header tank pipe connecting, header tank, low level water shoot, water valve, drain pipe port, vent valve, evacuated tube and supporting leg composition, described separate housings supports by supporting leg, in its shell, lower central is provided with separator tube, described separator tube bottom is connected with rising pipe, along its separator tube bottom periphery, be provided with back-up ring, described perforation header is the circle around back-up ring, one end of its perforation header is connected with header tank bottom by isolating water pipe through separate housings, header tank pipe connecting bottom surface in described header tank connects the top of high-order water shoot, and the bottom of described high-order water shoot is connected on the hypomere of low level water shoot, and installs water valve on more than high-order water shoot low level water shoot, the top of described low level water shoot is connected with header tank bottom, and the bottom of its low level water shoot is drain pipe port, at the bottom of described separate housings, outer middle part connects evacuated tube, described evacuated tube installing vent valve, along multiple cone separators that distribute on the separator tube periphery of back-up ring top, installing distribution pipe in described each cone separator, described separate housings top middle part forms scum silica frost collecting region, and described outside, scum layer district is provided with scum pipe.
The separation method of described coagulation air-float co-agglomeration equipment for separating liquid from solid, is characterized in that: described separation method comprises the steps:
Step 1: coagulating agent, pH adjusting agent in described dosing mixing system suck by the effect of sump pump self-priming, chemical feeding quantity is by PAC coagulating agent flow meter and the control of pH under meter, the high speed rotating cutting of the impeller of process water pump, liquid is mixed with sewage, and its PAM coagulant aids is to join hybrid reaction chemical feeding points C and the D of condensed system altogether by dosing pump and path dosing under meter, large footpath dosing under meter control; Sump pump position in parallel is provided with ejector, by jet, sucks quantitative air, and its add-on is sewage quantity 1%, and air dissolves in sewage gas dispersion after repeatedly being cut by sump pump, and pressure maintains within the scope of 0.2-0.3Mpa;
Step 2: the hybrid reaction described in the mixed mixed medicine sewage of dosing enters by sump pump is total in the path hybrid reaction pipe of the path hybrid reaction pipe assembly in condensed system, the dissolved air water that its gas-liquid mixing pump produces adds an A and sewage dissolved air water under meter control add-on by dissolved air water, the ratio of its add-on accounts for 35% of total add-on, its dissolved air water adds a B and dissolved air water arm A under meter control add-on, and the ratio of its add-on accounts for 65% of total add-on; The mixed mixed medicine sewage of its dosing and dissolved air water bump in conjunction with generating a large amount of band gas flcos in condensed system altogether in hybrid reaction, then and the coagulant aids hybrid reaction adding by chemical feeding points D form the bubble of greater particle size and the copolymerized body of wadding grain, enter in common cohesion equipment for separating liquid from solid and separate;
Step 3: enter in the separator tube in described common cohesion equipment for separating liquid from solid with the mixture of the copolymerized body of wadding grain when multiphase medium pump air dissolving system completes the bubble that mixes medicine sewage and dissolved air water hybrid reaction and form greater particle size, by the distribution pipe of the multiple cone separators on separator tube, the gas-solid-liquid mixture that needs are separated separates by multiple range of distribution independently, because bubble is larger with the density of copolymerized body and the density difference of water of wadding grain, particle in the mixed medicine sewage of particle diameter ratio is large, this copolymerized body automatic-ascending forms scum layer district to separator tube top, by scum pipe, discharge, water after purification is collected by the perforation header of the bottom of separator tube, then discharges by high-low position water shoot, open the water valve on low level water shoot, now only scum silica frost is not arranged in draining, close the water valve on low level water shoot, its high-order water shoot starts draining, regulate the pipe connecting of high-order water shoot to make the elevation of water surface in header tank be applicable to row's scum silica frost, be convenient to the row's of realization scum silica frost, complete after deslagging, open the water valve on low level water shoot, carry out the draining of low level water shoot, so analogize, cyclical operation, controls the time that water valve is opened, and realizes scum silica frost thickening.
Principle and feature of the present invention are described below:
The present invention sequentially installs at sewage lagoon place by sewage dosing mixing system, multiphase medium pump air dissolving system, hybrid reaction be total to condensed system and condense altogether the tripping device that equipment for separating liquid from solid forms, its sewage dosing mixing system is comprised of waste pipe, sewage variable valve, sewage vacuum tensimeter, jet variable valve first, sump pump, pH adjusting agent medicine-chest, PAC coagulating agent medicine-chest, PAM coagulant aids medicine-chest, medicine absorbing tube, suction medicine variable valve, dosing pump and sewage dissolved air water house steward, its multiphase medium pump air dissolving system by dissolved air water be in charge of, arm sampling valve, dissolved air water variable valve first, dissolved air water under meter, dissolved air water variable valve second, dissolved air water variable valve third, gas-liquid pressure table, dissolved air water arm A, dissolved air water arm B and gas-liquid mixing pump form, it mixes aggregation system altogether and is comprised of path hybrid reaction pipe assembly, central diameter hybrid reaction pipe, pipe connecting, pipeline and large footpath hybrid reaction pipe assembly, when multiphase medium pump sucks the clear water being total in coacervation and separation device the pump housing and with multiphase medium pump parallel position, ejector is set on suction line, by jet air amount, vacuum noz(zle) air amount before pump, air is after multiphase medium pump is cut repeatedly, pressure maintains within the scope of 0.3-0.5Mpa, according to the characteristic of common cohesion and microbubble dispose procedure feature, adopt special reliever, make to disperse the air dissolving in water to be emitted fast, the micro-bubble diameter that it discharges is at 1-10 micron, by dissolved air water, add an A under meter, dissolved air water adds a B under meter control add-on, respectively with hybrid reaction altogether the dissolved air water of condensed system add and be connected, its path hybrid reaction pipe one end adds an A to be connected with gas-liquid mixing pump by dissolved air water, with end, is also connected with sump pump, and the other end is connected with central diameter hybrid reaction pipe, also adds a C to be connected with dosing pump, its central diameter hybrid reaction pipe the other end is connected with large footpath hybrid reaction pipe, and both junctions have dissolved air water to add a B, also add a D to be connected with dosing pump, its large footpath hybrid reaction pipe the other end directly enters into common cohesion equipment for separating liquid from solid by the water regulating valve that goes out on rising pipe, condense altogether equipment for separating liquid from solid by separate housings, back-up ring, perforation header, separator tube, distribution pipe, cone separator, scum layer district, scum pipe, isolate water pipe, high-order water shoot, header tank pipe connecting, header tank, low level water shoot, water valve, drain pipe port, vent valve, evacuated tube and supporting leg and form, the separate housings of condensing altogether equipment for separating liquid from solid adopts cylinder, in described common cohesion equipment for separating liquid from solid inside, be provided with separator tube, separator tube is provided with multiple distribution pipes, multiple back taper spargers, on the top of separator tube, it is disengaging zone, be provided with taper triphase separator, the upper outside of separator is provided with row's oil slick mud pipe, lower inside is provided with perforation header and back-up ring, perforation header is connected with the lower end of rising pipe, enter in the effluent collection case of common coacervation and separation device upper outside, inwardly be provided with two high-low-position water shoots, high-order water shoot top is provided with adjustable pipe connecting, low level water shoot is provided with water valve, evacuated tube and vent valve are installed outward at the bottom of separate housings, bottom of device outside is provided with supporting leg.
Feature of the present invention is:
1, the present invention has fully used the ultimate principle of coagulation air-float co-agglomeration, by molten gas gas releasing system, discharge intensive ultramicro air bubble, build bridge with flco, winding, net is caught effect, the copolymerized body that these three kinds of combinations form is in floating-upward process, can not be subject to shearing force impact and bubble is come off, scum silica frost is very stable, and water ratio reduces greatly, because the copolymerized body diameter forming is more much larger than traditional air supporting, also increase many with the density difference of water, according to Stokes'theorem, square being directly proportional of ascent rate and particle diameter, be directly proportional to the density difference of water to particle, so, ascent rate is faster than traditional air supporting, shorten the Reaction Separation time, separation efficiency and the stability of airfloat equipment have so greatly been improved.
2, on sump pump suction line, on position in parallel, ejector is set, by jet, sucks quantitative air, according to the characteristic of common cohesion and microbubble dispose procedure feature, realize microbubble and participate in coagulating directly, be conducive to the common cohesion of bubble and particle.
3, coagulant aids joins in the common condensed system of hybrid reaction by 2, improves adsorption bridging function; The mode that adds of dissolved air water adopts add at 2, can guarantee that sewage can part and bubble incorporation in the situation that of dosing, can make again most of bubble can in condensed system, not break prematurely altogether in hybrid reaction; The hybrid reaction changing the altogether dosing of condensed system can make medicament, sewage, dissolved air water three more fully effectively mix with the mode that adds dissolved air water, for the generation of copolymerized body provides favourable materialization space, and the stability of scum silica frost and upper i in raising.
4, formed bubble and flco altogether the mixed solution of the aggregate parallel direction of separator tube in common cohesion equipment for separating liquid from solid enter, on separator tube, by separate multiple disengaging zone, complete the solid-liquid separation in region separately, increased pneumatically supported freedom from jamming, minimizing is disturbed floating wadding slag, greatly improves separation efficiency.
5,, by becoming level control valve control row scum silica frost intermittence, the thickening of scum silica frost in common cohesion equipment for separating liquid from solid in realizations, can further reduce the water ratio of the slag of wadding a quilt with cotton, simple and convenient.
6, the present invention can be used for producing colloid and the suspended substance in sewage and waste water in process for producing life process, completes solid-liquid separation.
The comprehensive above technical scheme of taking, realizes object of the present invention.
Therefore, compared with prior art, the present invention is not only reasonable in design, compact construction, there is independently hybrid reaction and solid-liquid separation system, and realize and optimize coagulation air-float co-agglomeration dissolved air flotation process, there is simple and easy convenient, whole plant and take up an area little, less investment, efficiency high.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the invention will be further described.
The present invention has a width accompanying drawing.Wherein:
Accompanying drawing 1 is the main TV structure schematic diagram of specific embodiments of the invention.
In figure, 1, sewage lagoon, 2, waste pipe, 3, sewage variable valve, 4, sewage vacuum tensimeter, 5, coagulating agent medicine-chest, 6, pH regulator valve second, 7, pH under meter, 8, pH regulator valve first, 9, pH adjusting agent medicine-chest, 10, PAC coagulating agent variable valve second, 11, PAC coagulating agent flow meter, 12, PAC coagulating agent variable valve first, 13, PAM coagulant aids medicine-chest, 14, jet variable valve first, 15, ejector, 16, fluidic flowmeter, 17, jet pipeline, 18, jet variable valve second, 19, sump pump, 20, sewage dissolved air water tensimeter, 21, sewage dissolved air water house steward, 22, sewage dissolved air water variable valve first, 23, sewage dissolved air water under meter, 24, sewage dissolved air water variable valve second, 25, sewage dissolved air water sampling valve, 26, inhale medicine variable valve 27, medicine absorbing tube, 28, dosing pump, 29, dosing house steward, 30, path chemicals addition control valve first, 31, large footpath dosing arm, 32, path dosing under meter, 33, large footpath chemicals addition control valve first, 34, path chemicals addition control valve second, 35, large footpath dosing under meter, 36, path dosing arm, 37, large footpath chemicals addition control valve second, 38, pipeline, 39, support, 40, large footpath hybrid reaction pipe, 41, central diameter hybrid reaction pipe, 42, pipe connecting, 43, path hybrid reaction pipe, 44, large footpath vent valve, 45, path vent valve, 46, go out water regulating valve, 47, rising pipe, 48, gas-liquid mixing pump, 49, gas-liquid pressure table, 50, dissolved air water variable valve the third, 51, dissolved air water arm A variable valve first, 52, dissolved air water arm A under meter, 53, dissolved air water arm A variable valve second, 54, dissolved air water arm A, 55, dissolved air water house steward, 56, dissolved air water arm B variable valve first, 57, dissolved air water arm B under meter, 58, dissolved air water arm B variable valve second, 59, dissolved air water arm B, 60, dissolved air water arm B sampling valve, 61, gas regulating valve first, 62, gas-jet device, 63, gas regulating valve second, 64, gas meter second, 65, gas meter first, 66, separate housings, 67, back-up ring, 68, perforation header, 69, separator tube, 70, distribution pipe, 71, cone separator, 72, scum silica frost collecting region, 73, scum pipe, 74, isolate water pipe, 75, high-order water shoot, 76, header tank pipe connecting, 77, header tank, 78, low level water shoot, 79, water valve, 80, drain pipe port, 81, vent valve, 82, evacuated tube, 83, supporting leg.
Embodiment
Shown in Fig. 1, be specific embodiments of the invention, it is coagulation air-float co-agglomeration equipment for separating liquid from solid and the separation method thereof of using at certain factory processes production waste, described coagulation air-float co-agglomeration equipment for separating liquid from solid, is characterized in that: described tripping device is at sewage lagoon place, sequentially to install by sewage dosing mixing system, multiphase medium pump air dissolving system, hybrid reaction be total to condensed system and condense altogether equipment for separating liquid from solid, described sewage dosing mixing system is by waste pipe 2, sewage variable valve 3, sewage vacuum tensimeter 4, jet variable valve first 14, sump pump 19, pH adjusting agent medicine-chest 9, PAC coagulating agent medicine-chest 5, PAM coagulant aids medicine-chest 13, dosing house steward 29, inhale medicine variable valve 26, medicine absorbing tube 27, dosing pump 28 and sewage dissolved air water house steward 21 form, insert in sewage lagoon 1 bottom of described waste pipe 2, the other end of its waste pipe 2 is connected with the import of sump pump 19, on the waste pipe 2 being connected with sump pump 19, sequentially install sewage variable valve 3, sewage vacuum tensimeter 4 and jet variable valve first 14, on the waste pipe 2 between its sewage vacuum tensimeter 4 and jet variable valve first 14, by pipeline, be sequentially connected pH adjusting agent medicine-chest 9, PAC coagulating agent medicine-chest 5, on the pipe between described pH adjusting agent medicine-chest 9 and waste pipe 2, sequentially install pH regulator valve first 8, pH under meter 7 and pH regulator valve second 6, on pipeline between described PAC coagulating agent medicine-chest and waste pipe 2, sequentially install PAC coagulating agent variable valve first 12, PAC coagulating agent flow meter 11 and PAC coagulating agent variable valve second 10, PAM coagulant aids medicine-chest 13 is set after PAC coagulating agent case 13, and the outside of described PAM coagulant aids medicine-chest 13 is connected with the import of dosing pump 28 by medicine absorbing tube 27, on its medicine absorbing tube 27, medicine variable valve 26 is inhaled in installing, and the outlet of described sump pump 19 is connected with multiphase medium pump air dissolving system dissolved air water arm B59 by sewage dissolved air water house steward 21, on described sewage dissolved air water house steward 21, sequentially install sewage dissolved air water tensimeter 20, sewage dissolved air water variable valve first 22, sewage dissolved air water under meter 23, sewage dissolved air water variable valve second 24 and sewage dissolved air water sampling valve 25, with the one end that is connected jet pipeline 17 on sewage dissolved air water house steward 21 between sewage dissolved air water pressure table 20 and sewage dissolved air water variable valve first 22, the other end of described jet pipeline 17 is connected on waste pipe 2, on its jet pipeline 17, sequentially install ejector 15, fluidic flowmeter 16 and jet variable valve second 17, described multiphase medium pump air dissolving system is comprised of gas-liquid mixing pump 48, dissolved air water house steward 55, dissolved air water arm A54, dissolved air water arm B59, dissolved air water arm B sampling valve 60, dissolved air water arm B variable valve first 56, dissolved air water arm B under meter 57, dissolved air water arm B variable valve second 58, dissolved air water house steward variable valve 50 and gas-liquid pressure table 49, sequentially installs gas-liquid pressure table 49 and dissolved air water house steward variable valve 50 on described dissolved air water house steward 55, one end of described dissolved air water arm B59 enters after A place is connected with sewage dissolved air water house steward 21 in path hybrid reaction pipe 43, the other end of described dissolved air water arm B59 is connected with the exit end of gas-liquid mixing pump 48 by dissolved air water house steward 55, sequentially installs dissolved air water arm B variable valve first 56, dissolved air water arm B under meter 57, dissolved air water arm B variable valve second 58 and dissolved air water arm B sampling valve 60 on described dissolved air water arm B59, one end of described dissolved air water arm A54 enters in large footpath hybrid reaction pipe 40 after being connected by pipeline 38 with chemical feeding points D after being connected with the B point place of central diameter hybrid reaction pipe water side again, the other end of its dissolved air water arm A54 is connected with the dissolved air water house steward 55 of gas-liquid mixing pump 48, sequentially installs dissolved air water arm A variable valve first 51, dissolved air water arm A under meter 52, dissolved air water arm A variable valve second 53 on described dissolved air water arm A54, the entrance end of described gas-liquid mixing pump 48 condenses together in the separate housings 66 in equipment for separating liquid from solid and connects by pipeline, and on this pipeline, sequentially install gas meter first 65 and gas regulating valve first 61, on the import of its gas-liquid mixing pump 48 and the pipeline of outlet, install gas-jet device 62, gas meter second 64 and gas regulating valve second 63, described hybrid reaction altogether condensed system is comprised of path hybrid reaction pipe assembly, central diameter hybrid reaction pipe 41, pipe connecting 42, pipeline 38 and large footpath hybrid reaction pipe assembly, and described path hybrid reaction pipe assembly is comprised of path hybrid reaction pipe 43, path vent valve 45, path dosing arm 36, path chemicals addition control valve first 30, path dosing under meter 32 and path chemicals addition control valve second 34, described path hybrid reaction pipe 43 is installed path vent valve 45 by pipeline, the C point place of its path hybrid reaction pipe 43 one end connects one end of path dosing arm 36, the other end of described path dosing arm 36 is connected on dosing house steward 29, sequentially installs path chemicals addition control valve first 30, path dosing under meter 32 and path chemicals addition control valve second 34 on path dosing arm 36, the chemical feeding points C place of described path hybrid reaction pipe 43 one end is connected with one end of central diameter hybrid reaction pipe 41 by pipe connecting 42, the other end of described central diameter hybrid reaction pipe 41 is connected to by pipeline 38 on the chemical feeding points D of the large footpath dosing arm 31 in the hybrid reaction pipe assembly of large footpath, described large footpath hybrid reaction pipe assembly by large footpath hybrid reaction pipe 40, large footpath dosing arm 31, large footpath chemicals addition control valve first 33, large footpath dosing under meter 35 and large footpath chemicals addition control valve second 37, rising pipe 47, go out water regulating valve 46 and dissolved air water arm A54 forms, described large footpath hybrid reaction pipe is installed large footpath vent valve 44 by pipeline, its large footpath hybrid reaction pipe 40 connects one end of large footpath dosing arm 31, and the other end of described large footpath dosing arm 31 connects on dosing house steward 29, on its large footpath dosing arm, 29 sequentially install large footpath chemicals addition control valve first 33, large footpath dosing under meter 35 and large footpath chemicals addition control valve second 37, the rising pipe 47 of described large footpath hybrid reaction pipe 40 is connected on separator tube 69 bottoms through the separate housings 66, the back-up ring 67 that condense in equipment for separating liquid from solid altogether, on its rising pipe 47, installs out water regulating valve 46, described common cohesion equipment for separating liquid from solid is by separate housings 66, back-up ring 67, perforation header 68, separator tube 69, distribution pipe 70, cone separator 71, scum layer district 72, scum pipe 73, isolate water pipe 74, high-order water shoot 75, header tank pipe connecting 76, header tank 77, low level water shoot 78, water valve 79, drain pipe port 80, vent valve 81, evacuated tube 82 and supporting leg 83 form, described separate housings 66 supports by supporting leg 83, in its shell, lower central is provided with separator tube 69, described separator tube 69 bottoms are condensed and are connected altogether with rising pipe 47, along its separator tube 69 bottom peripheries, be provided with back-up ring 67, described perforation header 68 is the circles outside back-up ring 67, one end is connected with header tank 77 bottoms by isolating water pipe 74 through separate housings 66, header tank pipe connecting 76 bottom surfaces in described header tank 77 connect the top of high-order water shoot 75, and the bottom of described high-order water shoot 75 is connected on the hypomere of low level water shoot 78, on the low level water shoot 78 with high-order water shoot more than 75, install water valve 79, the top of described low level water shoot 78 is connected with header tank 77 bottoms, and the bottom of its low level water shoot 78 is drain pipe port 80, , middle part connects evacuated tube 82 at described the 66 end of separate housings, and described evacuated tube 82 is installed vent valve 81, along multiple cone separators 71 that distribute on separator tube 69 peripherys of back-up ring 67 tops, the interior installing distribution pipe 70 of described each cone separator 71, described separate housings 66 top middle parts form scum silica frost collecting region 72, and described 72 outsides, scum layer district are provided with scum pipe 73.Described path hybrid reaction pipe 43, central diameter hybrid reaction pipe 41 and large footpath hybrid reaction pipe 40 are installed in support 39 toward lower leaf from high.
Described ejector 15 is installed in the position parallel with sump pump 19.
Described separate housings 66 adopts cylinder.
The separation method of described coagulation air-float co-agglomeration equipment for separating liquid from solid, is characterized in that: this separation method comprises the steps:
Step 1: coagulating agent, pH adjusting agent in described dosing mixing system suck by sump pump 19 self-priming effects, chemical feeding quantity is by being controlled by PAC coagulating agent flow meter 11 and pH under meter 7, the high speed rotating cutting of the impeller of process water pump, liquid is mixed with sewage, and its PAM coagulant aids is to be controlled and joined hybrid reaction chemical feeding points C and the D of condensed system altogether by dosing pump 28 and path dosing under meter 32, large footpath dosing under meter 35; Sump pump 19 position in parallel is provided with ejector 15, by jet, sucks quantitative air, and its add-on is sewage quantity 1%, and air dissolves in sewage gas dispersion after repeatedly being cut by sump pump 19, and pressure maintains within the scope of 0.2-0.3Mpa;
Step 2: the hybrid reaction described in the mixed mixed medicine sewage of dosing enters by sump pump is total in the path hybrid reaction pipe 43 of the path hybrid reaction pipe assembly in condensed system, the dissolved air water that its gas-liquid mixing pump 48 produces adds an A and sewage dissolved air water under meter 23 to control add-on by dissolved air water, the ratio of its add-on accounts for 35% of total add-on, its dissolved air water adds a B and dissolved air water arm A under meter 52 to control add-on, and the ratio of its add-on accounts for 65% of total add-on; The mixed mixed medicine sewage of its dosing and dissolved air water bump in conjunction with generating a large amount of band gas flcos in condensed system altogether in hybrid reaction, then and the coagulant aids hybrid reaction adding by chemical feeding points D form the bubble of greater particle size and the copolymerized body of wadding grain, enter in common cohesion equipment for separating liquid from solid and separate;
Step 3: enter in the separator tube 69 in described common cohesion equipment for separating liquid from solid with the mixture of the copolymerized body of wadding grain when multiphase medium pump air dissolving system completes the bubble that mixes medicine sewage and dissolved air water hybrid reaction and form greater particle size, by the distribution pipe 70 of the multiple cone separators 71 on separator tube 69, the gas-solid-liquid mixture that needs are separated separates by multiple range of distribution independently, because bubble is larger with the density of copolymerized body and the density difference of water of wadding grain, particle in the mixed medicine sewage of particle diameter ratio is large, this copolymerized body automatic-ascending forms scum layer district 72 to separator tube 69 tops, by scum pipe, discharge, water after purification is collected by the perforation header 68 of the bottom of separator tube 69, then discharges by high-low position water shoot 75,78, open the water valve 79 on low level water shoot 78, now only scum silica frost is not arranged in draining, water valve 79 its high-order water shoots of closing on low level water shoot 78 start draining, regulate the pipe connecting on high-order water shoot 75 to make the elevation of water surface in header tank 77 be applicable to row's scum silica frost, be convenient to the row's of realization scum silica frost, complete after deslagging, open the water valve 79 on low level water shoot 78, carry out the draining of low level water shoot 78, so analogize, cyclical operation, controls the time that water valve 79 is opened, and realizes scum silica frost thickening.
The above; it is only preferably embodiment of the present invention; but protection scope of the present invention is not limited to this; allly be familiar with those skilled in the art in technical scope disclosed by the invention, within being equal to and replacing or change protection scope of the present invention all should be encompassed according to technical scheme of the present invention and design of the present invention thereof.
Claims (5)
1. a coagulation air-float co-agglomeration equipment for separating liquid from solid, is characterized in that: described tripping device is at sewage lagoon place, sequentially install sewage dosing mixing system, multiphase medium pump air dissolving system, the common condensed system of hybrid reaction and condense altogether equipment for separating liquid from solid, described sewage dosing mixing system is by waste pipe (2), sewage variable valve (3), sewage vacuum tensimeter (4), jet variable valve first (14), sump pump (19), pH adjusting agent medicine-chest (9), PAC coagulating agent medicine-chest (5), PAM coagulant aids medicine-chest (13), dosing house steward (29), inhale medicine variable valve (26), medicine absorbing tube (27), dosing pump (28) and sewage dissolved air water house steward (21) composition, insert in sewage lagoon (1) one end of described waste pipe (2), the other end of its waste pipe (2) is connected with the import of sump pump (19), on the waste pipe (2) being connected with sump pump (19), sequentially install sewage variable valve (3), sewage vacuum tensimeter (4) and jet variable valve first (14), waste pipe (2) between its sewage vacuum tensimeter (4) and jet variable valve first (14) is above sequentially connected pH adjusting agent medicine-chest (9), PAC coagulating agent medicine-chest (5) by pipeline, on the pipeline between described pH adjusting agent medicine-chest (9) and waste pipe (2), sequentially installs pH regulator valve first (8), pH under meter (7) and pH regulator valve second (6), on pipeline between described PAC coagulating agent medicine-chest (5) and waste pipe (2), sequentially install PAC coagulating agent variable valve first (12), PAC coagulating agent flow meter (11) and PAC coagulating agent variable valve second (10), PAM coagulant aids medicine-chest (13) is set after PAC coagulating agent medicine-chest (5), and the outside of described PAM coagulant aids medicine-chest (13) is connected with the import of dosing pump (28) by medicine absorbing tube (27), medicine variable valve (26) is inhaled in the upper installing of its medicine absorbing tube (27), and the outlet of described sump pump (19) is connected with multiphase medium pump air dissolving system by sewage dissolved air water house steward (21), on described sewage dissolved air water house steward (21), sequentially install sewage dissolved air water pressure table (20), sewage dissolved air water variable valve first (22), sewage dissolved air water under meter (23), sewage dissolved air water variable valve second (24) and sewage dissolved air water sampling valve (25), its sewage dissolved air water is pressed the one end that is connected jet pipeline (17) on the sewage dissolved air water house steward (21) between table (20) and sewage dissolved air water variable valve first (22), and the other end of described jet pipeline (17) is connected on waste pipe (2), on its jet pipeline (17), sequentially install ejector (15), fluidic flowmeter (16) and jet variable valve second (18), described multiphase medium pump air dissolving system is by gas-liquid mixing pump (48), dissolved air water house steward (55), dissolved air water arm A(54), dissolved air water arm B(59), dissolved air water arm B sampling valve (60), dissolved air water arm B variable valve first (56), dissolved air water arm B under meter (57), dissolved air water arm B variable valve second (58), dissolved air water house steward variable valve (50) and gas-liquid pressure table (49) form, and sequentially installs gas-liquid pressure table (49) and dissolved air water house steward variable valve (50) on described dissolved air water house steward (55), described dissolved air water arm B(59) one end after A place is connected, enter path hybrid reaction pipe (43) with sewage dissolved air water house steward (21) in, described dissolved air water arm B(59) the other end be connected with the exit end of gas-liquid mixing pump (48) by dissolved air water house steward (55), described dissolved air water arm B(59) on sequentially install dissolved air water arm B variable valve first (56), dissolved air water arm B under meter (57), dissolved air water arm B variable valve second (58) and dissolved air water arm B sampling valve (60), described dissolved air water arm A(54) one end enter in large footpath hybrid reaction pipe (40) after being connected by pipeline (38) with chemical feeding points D again after being connected with the B point place of central diameter hybrid reaction pipe water side, its dissolved air water arm A(54) the other end be connected with the dissolved air water house steward (55) of gas-liquid mixing pump (48), described dissolved air water arm A(54) on sequentially install dissolved air water arm A variable valve first (51), dissolved air water arm A under meter (52), dissolved air water arm A variable valve second (53), the entrance end of described gas-liquid mixing pump (48) condenses together in the separate housings (66) in equipment for separating liquid from solid and connects by pipeline, and on this pipeline, sequentially install gas meter first (65) and gas regulating valve first (61), on the import of its gas-liquid mixing pump (48) and the pipeline of outlet, install gas-jet device (62), gas meter second (64) and gas regulating valve second (63), described hybrid reaction altogether condensed system is comprised of path hybrid reaction pipe assembly, central diameter hybrid reaction pipe (41), pipe connecting (42), pipeline (38) and large footpath hybrid reaction pipe assembly, and described path hybrid reaction pipe assembly is comprised of path hybrid reaction pipe (43), path vent valve (45), path dosing arm (36), path chemicals addition control valve first (30), path dosing under meter (32) and path chemicals addition control valve second (34), described path hybrid reaction pipe (43) is installed path vent valve (45) by pipeline, the C point place of path hybrid reaction pipe (43) one end connects one end of path dosing arm (36), it is upper that the other end of described path dosing arm (36) is connected to dosing house steward (29), sequentially installs path chemicals addition control valve first (30), path dosing under meter (32) and path chemicals addition control valve second (34) on path dosing arm (36), the chemical feeding points C place of described path hybrid reaction pipe (43) one end is connected with one end of central diameter hybrid reaction pipe (41) by pipe connecting (42), the other end of described central diameter hybrid reaction pipe (41) is connected to by pipeline (38) on the chemical feeding points D of the large footpath dosing arm (31) in the hybrid reaction pipe assembly of large footpath, described large footpath hybrid reaction pipe assembly is by large footpath hybrid reaction pipe (40), large footpath dosing arm (31), large footpath chemicals addition control valve first (33), large footpath dosing under meter (35) and footpath chemicals addition control valve second (37), rising pipe (47) and go out water regulating valve (46) and form greatly, described large footpath hybrid reaction pipe (40) is installed large footpath vent valve (44) by pipeline, it is upper that one end of its large footpath hybrid reaction pipe (40) is connected to large footpath dosing arm (31), and the other end of described large footpath dosing arm is connected on dosing house steward (29), on described large footpath dosing arm (31), sequentially install large footpath chemicals addition control valve first (33), large footpath dosing under meter (35) and large footpath chemicals addition control valve second (37), the rising pipe (47) of described large footpath hybrid reaction pipe (40) is connected on separator tube (69) bottom through the separate housings (66), the back-up ring (67) that condense in equipment for separating liquid from solid altogether, installs out water regulating valve (46) on its rising pipe (47), described common cohesion equipment for separating liquid from solid is by separate housings (66), back-up ring (67), perforation header (68), separator tube (69), distribution pipe (70), cone separator (71), scum silica frost collecting region (72), scum pipe (73), isolate water pipe (74), high-order water shoot (75), header tank pipe connecting (76), header tank (77), low level water shoot (78), water valve (79), drain pipe port (80), vent valve (81), evacuated tube (82), supporting leg (83) composition, described separate housings (66) supports by supporting leg (83), in its shell, lower central is provided with separator tube (69), described separator tube (69) bottom is connected with rising pipe (47), along its separator tube (69) bottom periphery, be provided with back-up ring (67), described perforation header (68) is the circle around back-up ring (67), one end of its perforation header (68) is connected with header tank (77) bottom by isolating water pipe (74) through separate housings (66), header tank pipe connecting (76) bottom surface in described header tank (77) connects the top of high-order water shoot (75), the bottom of described high-order water shoot (75) is connected on the hypomere of low level water shoot (78), low level water shoot (78) the upper installing water valve (79) more than high-order water shoot (75), the top of described low level water shoot (78) is connected with header tank (77) bottom, and the bottom of low level water shoot (78) is drain pipe port (80), , middle part connects evacuated tube (82) at described the separate housings (66) end, described evacuated tube (82) installing vent valve (82), along the multiple cone separators (71) that distribute on separator tube (69) periphery of back-up ring (67) top, installing distribution pipe (70) in described each cone separator (71), described separate housings (66) top middle part forms scum layer district (72), and described outside, scum layer district (72) is provided with scum pipe (73).
2. by coagulation air-float co-agglomeration equipment for separating liquid from solid claimed in claim 1, it is characterized in that: described path hybrid reaction pipe (43), central diameter hybrid reaction pipe (41) and large footpath hybrid reaction pipe (40) are installed in support (39) toward lower leaf from high.
3. by coagulation air-float co-agglomeration equipment for separating liquid from solid claimed in claim 1, it is characterized in that: described ejector (15) is installed in the position parallel with sump pump (19).
4. by coagulation air-float co-agglomeration equipment for separating liquid from solid claimed in claim 1, it is characterized in that: described separate housings (66) adopts cylinder.
5. by the separation method of a kind of coagulation air-float co-agglomeration equipment for separating liquid from solid claimed in claim 1, it is characterized in that: this separation method comprises the steps:
Step 1: coagulating agent, pH adjusting agent in described dosing mixing system suck by sump pump (19) self-priming effect, chemical feeding quantity is controlled by PAC coagulating agent flow meter (11) and pH under meter (7), the high speed rotating cutting of the impeller of process water pump, liquid is mixed with sewage, and its PAM coagulant aids is to be controlled and joined hybrid reaction chemical feeding points C and the D of condensed system altogether by dosing pump (28) and path dosing under meter (32), large footpath dosing under meter (35); Sump pump (19) position in parallel is provided with ejector (15), by jet, suck quantitative air, its add-on is sewage quantity 1%, after air is cut repeatedly by sump pump (19), gas dispersion is dissolved in sewage, and pressure maintains within the scope of 0.2-0.3Mpa;
Step 2: the hybrid reaction described in the mixed mixed medicine sewage of dosing enters by sump pump is total in the path hybrid reaction pipe (43) of the path hybrid reaction pipe assembly in condensed system, the dissolved air water that its gas-liquid mixing pump (48) produces adds an A and sewage dissolved air water under meter (23) to control add-on by dissolved air water, the ratio of its add-on accounts for 35% of total add-on, its dissolved air water adds a B and dissolved air water arm A under meter (52) to control add-on, and the ratio of its add-on accounts for 65% of total add-on; The mixed mixed medicine sewage of its dosing and dissolved air water bump in conjunction with generating a large amount of band gas flcos in condensed system altogether in hybrid reaction, then and the coagulant aids hybrid reaction adding by chemical feeding points D form the bubble of greater particle size and the copolymerized body of wadding grain, enter in common cohesion equipment for separating liquid from solid and separate;
Step 3: enter in the separator tube (69) in described common cohesion equipment for separating liquid from solid with the mixture of the copolymerized body of wadding grain when multiphase medium pump air dissolving system completes the bubble that mixes medicine sewage and dissolved air water hybrid reaction and form greater particle size, by the distribution pipe (70) of the multiple cone separators (71) on separator tube (69), the gas-solid-liquid mixture that needs are separated separates by multiple range of distribution independently, because bubble is larger with the density of copolymerized body and the density difference of water of wadding grain, particle in the mixed medicine sewage of particle diameter ratio is large, this copolymerized body automatic-ascending forms scum layer district (72) to separator tube (69) top, by scum pipe, discharge, water after purification is collected by the perforation header (68) of the bottom of separator tube (69), then discharges by high-low position water shoot (75,78), open the water valve (79) on low level water shoot (78), now only scum silica frost is not arranged in draining, close the water valve (79) on low level water shoot (78), its high-order water shoot starts draining, regulate the pipe connecting on high-order water shoot (75) to make the elevation of water surface in header tank (77) be applicable to row's scum silica frost, be convenient to the row's of realization scum silica frost, complete after deslagging, open the water valve (79) on low level water shoot (78), carry out the draining of low level water shoot (78), so analogize, cyclical operation, controls the time that water valve (79) is opened, and realizes scum silica frost thickening.
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| CN103395909B (en) * | 2013-07-25 | 2014-07-16 | 大连交通大学 | Two-stage coagulation air-flotation separation equipment and method |
| CN103373795B (en) * | 2013-08-03 | 2014-08-06 | 大连交通大学 | Processing equipment and method for cutting fluid waste water |
| CN108328877A (en) * | 2018-04-03 | 2018-07-27 | 大连交通大学 | Coagulation air-float biological activated carbon group technology treated sewage system and method |
| CN109502675B (en) * | 2018-12-15 | 2021-06-08 | 浙江大学自贡创新中心 | Efficient oil-water separation method for different oil drop particle sizes |
| CN109896669A (en) * | 2019-04-29 | 2019-06-18 | 大连交通大学 | Mixing flocculation and flotation integrated machine |
| CN109956587B (en) * | 2019-04-30 | 2023-09-22 | 大连交通大学 | Quick separation system for coagulation air-floatation copolymerization |
| CN113045024A (en) * | 2019-12-26 | 2021-06-29 | 大连交通大学 | Coagulation and air floatation integrated experimental device |
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