CN116675392B - Biochemical pharmaceutical engineering waste water circulation purifying system - Google Patents
Biochemical pharmaceutical engineering waste water circulation purifying system Download PDFInfo
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- CN116675392B CN116675392B CN202310865342.9A CN202310865342A CN116675392B CN 116675392 B CN116675392 B CN 116675392B CN 202310865342 A CN202310865342 A CN 202310865342A CN 116675392 B CN116675392 B CN 116675392B
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- wastewater
- filter
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- 239000002351 wastewater Substances 0.000 title claims abstract description 97
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 78
- 238000001914 filtration Methods 0.000 claims abstract description 62
- 238000011282 treatment Methods 0.000 claims abstract description 50
- 230000007246 mechanism Effects 0.000 claims abstract description 46
- 238000001179 sorption measurement Methods 0.000 claims abstract description 37
- 230000003647 oxidation Effects 0.000 claims abstract description 26
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 26
- 238000000746 purification Methods 0.000 claims abstract description 19
- 239000007787 solid Substances 0.000 claims abstract description 19
- 238000001704 evaporation Methods 0.000 claims abstract description 16
- 230000008020 evaporation Effects 0.000 claims abstract description 16
- 239000002245 particle Substances 0.000 claims abstract description 16
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000003640 drug residue Substances 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims description 158
- 239000007788 liquid Substances 0.000 claims description 39
- 239000000706 filtrate Substances 0.000 claims description 20
- 238000002791 soaking Methods 0.000 claims description 16
- 239000002689 soil Substances 0.000 claims description 15
- 238000004140 cleaning Methods 0.000 claims description 12
- 239000000945 filler Substances 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 230000009471 action Effects 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 7
- 239000011159 matrix material Substances 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 4
- 238000012856 packing Methods 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 238000004064 recycling Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 20
- 238000010586 diagram Methods 0.000 description 9
- 230000009286 beneficial effect Effects 0.000 description 8
- 239000003344 environmental pollutant Substances 0.000 description 7
- 231100000719 pollutant Toxicity 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 238000005406 washing Methods 0.000 description 7
- 238000011010 flushing procedure Methods 0.000 description 6
- 241000196324 Embryophyta Species 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 230000000712 assembly Effects 0.000 description 3
- 238000000429 assembly Methods 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000001360 synchronised effect Effects 0.000 description 2
- 241000736262 Microbiota Species 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 229940088710 antibiotic agent Drugs 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000010826 pharmaceutical waste Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/46—Regenerating the filtering material in the filter
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/46—Regenerating the filtering material in the filter
- B01D24/4668—Regenerating the filtering material in the filter by moving the filtering element
- B01D24/4673—Regenerating the filtering material in the filter by moving the filtering element using rotary devices or vibration mechanisms, e.g. stirrers
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/343—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the pharmaceutical industry, e.g. containing antibiotics
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/32—Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The application relates to the technical field of water treatment, in particular to a biochemical pharmaceutical engineering wastewater circulation purification system, which comprises: the primary filtering mechanism is used for carrying out primary filtering treatment on suspended matters and solid particles in the wastewater; the adsorption and filtration mechanism is connected with the primary filtration mechanism to carry out adsorption treatment on organic matters and drug residues in the wastewater subjected to primary filtration treatment; the oxidation box is connected with the adsorption filtering mechanism, and an ozone generator is arranged in the oxidation box so as to carry out ozone oxidation treatment on the wastewater after the adsorption treatment; the evaporation condenser is connected with the oxidation box to perform evaporation treatment on the oxidized wastewater, and collect condensate for recycling. The application is provided with the primary filtering mechanism, and suspended matters and solid particles in the wastewater can be subjected to primary filtering treatment through the primary filtering mechanism; the adsorption filtration mechanism is arranged in the application, so that the adsorption treatment can be carried out on organic matters and drug residues in the wastewater after the preliminary filtering treatment.
Description
Technical Field
The application relates to the technical field of water treatment, in particular to a biochemical pharmaceutical engineering wastewater circulating and purifying system.
Background
The pharmaceutical industry mainly comprises chemical pharmacy, biological pharmacy, chinese patent medicines, pesticides and the like, and the pharmaceutical industry wastewater mainly comprises antibiotics production wastewater, synthetic drug production wastewater, chinese patent medicine production wastewater, washing water, flushing wastewater and the like in the production process of various preparations. The pharmaceutical wastewater is characterized by complex composition and high organic pollutant content, and the pharmaceutical wastewater has large water quality, water quantity and pollutant variety due to large variety of products in intermittent production in pharmaceutical factories. Generally, the organic pollution concentration in the pharmaceutical wastewater is high, so that the chromaticity is deep, the toxicity is high, and the concentration of solid suspended matters is also high.
The wastewater purification equipment in the prior art has the following problems: the utility model provides a waste water purification equipment among the prior art only can carry out filtration treatment to the impurity in the waste water, and is relatively poor to the treatment effect of pollutant in the waste water to waste water purification equipment among the prior art can't carry out synchronous clearance to the filter screen after filtering waste water, a biochemical pharmaceutical engineering waste water purification system of patent number CN202110868617.5 for example, including effluent water sump, purification unit and water storage tank, purification unit locates the side of effluent water sump, the top left end of effluent water sump is connected with the sewage inlet tube, the bottom of effluent water sump is connected with first drinking-water pipe, the right-hand member of first drinking-water pipe is connected with the suction pump, the top of suction pump is connected with first inlet tube, the upper end of first inlet tube is connected with the left side upper end of purification unit, be connected with communicating pipe between purification unit and the water storage tank, the right side lower extreme of water storage tank is fixed with the discharge pipe. This waste water purifying equipment only can carry out filtration treatment to the impurity in the waste water, and is relatively poor to the treatment effect of pollutant in the waste water to waste water purifying equipment among the prior art can't carry out synchronous clearance to the filter screen after filtering waste water, leads to the filter screen to be stopped up very easily, influences purifying effect.
Disclosure of Invention
In the summary, a series of concepts in a simplified form are introduced, which will be further described in detail in the detailed description. The summary of the application is not intended to define the key features and essential features of the claimed subject matter, nor is it intended to be used as an aid in determining the scope of the claimed subject matter.
To at least partially solve the above problems, the present application provides a biochemical pharmaceutical engineering wastewater circulation purification system, comprising:
the primary filtering mechanism is used for carrying out primary filtering treatment on suspended matters and solid particles in the wastewater;
the adsorption and filtration mechanism is connected with the primary filtration mechanism to carry out adsorption treatment on organic matters and drug residues in the wastewater subjected to primary filtration treatment;
the oxidation box is connected with the adsorption filtering mechanism, and an ozone generator is arranged in the oxidation box so as to carry out ozone oxidation treatment on the wastewater after the adsorption treatment;
the evaporation condenser is connected with the oxidation box to perform evaporation treatment on the oxidized wastewater, and collect condensate for recycling.
The biochemical pharmaceutical engineering wastewater circulating and purifying system further comprises an artificial wetland, wherein the artificial wetland comprises a wetland pool, a soil filler layer is arranged at the upper end inside the wetland pool, water flows are converged at the top of the soil filler layer, and a plurality of aquatic plants are planted on the soil filler layer; the soil packing layer bottom is provided with the water permeability matrix layer, and water permeability matrix layer bottom is provided with out the water layer, and the inner wall of play water layer runs through and installs the drain pipe, and the drain pipe is connected with the primary filter mechanism.
The drain pipe is provided with a water suction pump, and the drain pipe is internally provided with a stainless steel metal filter screen.
The adsorption and filtration mechanism is an activated carbon adsorption and filtration device.
The primary filter mechanism comprises a primary filter box, the primary filter box comprises a water inlet, a semicircular box body, a rectangular box body and a base which are fixedly connected in sequence from top to bottom, a circular drain pipe is fixed in a transverse round hole at the joint of the semicircular box body and the rectangular box body in a sealing way, two ends of the circular drain pipe are respectively provided with an end cover, and a water outlet pipe is arranged on one end cover; a water collecting port is arranged above the middle part of the circular drain pipe, the water collecting port is positioned right below the water inlet, the circular drain pipe is sealed and rotated with an annular mounting frame, and the upper end of the annular mounting frame is sealed and rotated on the inner annular surface of the semicircular box body; a plurality of mounting grooves are uniformly and circumferentially arranged on the annular mounting frame, and filter material components are arranged in the plurality of mounting grooves; the inside of the rectangular box body is provided with soaking liquid, so that the filter material component rotating to the lower part of the inside of the rectangular box body is soaked and cleaned by the soaking liquid; the rotary gear is fixed on the annular mounting frame and meshed with a gear at the output end of the rotary motor, and the rotary motor is fixed on the primary filter box.
The filter material washing machine is characterized in that a washing water inlet is formed in one end of the rectangular box body, a washing water outlet is formed in the other end of the rectangular box body, and a washing assembly used for washing the filter material assembly moving to the lower portion of the rectangular box body is arranged in the washing water inlet.
When the installation groove of the annular installation frame moves to the lower part of the water inlet and the upper part of the water collecting port, an adsorption and filtration channel is formed.
The filter material component comprises a filter material box, wherein filter materials are filled in the filter material box, and the volume of the filter materials is two thirds of that of the filter material box; the filter material box is fixed in the mounting groove of the annular mounting frame, the outer end of the filter material box is of an arc surface structure, the arc surface structure is coplanar with the outer annular surface of the annular mounting frame, a plurality of liquid inlets are uniformly formed in the arc surface structure, the front side surface and the rear side surface of the filter material box are respectively coplanar with the front side surface and the rear side surface of the annular mounting frame, and a plurality of liquid through holes are uniformly formed in the rear side surface of the filter material box; the inner end of the filter box is of a planar structure, a plurality of filtrate outlets are uniformly arranged on the planar structure, and the filtrate outlets are opposite to the water collecting port; the semicircular ring fixed at the front end inside the semicircular box body hermetically slides on the front side surface of the filter material box; the semicircular plugging ring fixed at the rear end inside the semicircular box body hermetically slides on the rear side surface of the filter material box, and the semicircular plugging ring can be plugged on a liquid through hole of the filter material box moving into the semicircular box body.
The inner end of the filter material box is a strip-shaped box body, the outer end of the filter material box is a fan-shaped box body, a plurality of filtrate outlets are arranged on the strip-shaped box body, and a plurality of liquid inlets are arranged on the fan-shaped box body; the left end and the right end of the inner wall of the strip-shaped box body are respectively connected with a material guiding inclined plate which is obliquely arranged towards the direction of the filtrate outlet in a rotating mode, the lower ends of the two material guiding inclined plates can be blocked on the left and the right supporting blocks of the inner wall of the strip-shaped box body, and when the filter material component rotates to the lower side of the rectangular box body, the two material guiding inclined plates can rotate towards the direction of the liquid inlet under the action of the filter material in the strip-shaped box body and the gravity of the filter material component.
The filter material assembly further comprises a linkage worm, two ends of the linkage worm are rotated on the side faces of the front side and the rear side of the filter material box, and a gear fixed at the front end of the linkage worm is meshed with an outer gear fixed on the outer pipe face of the circular drain pipe; the driving sprocket fixed at the front end of the linkage worm is connected with two driven sprockets through a chain, the two driven sprockets are fixed on two rotating shafts, two ends of the two rotating shafts are respectively rotated on the front side surface and the rear side surface of the filter material box, a plurality of stirring rods are respectively fixed on the shaft bodies of the two rotating shafts in the filter material box, and the axis of the linkage worm and the axis of the two rotating shafts are coplanar.
The filter material assembly further comprises worm wheels, two ends of the linkage worm are engaged with the two worm wheels relatively, one end of each worm wheel rotates on a support at the inner end of the filter material box through a short shaft, eccentric positions at the other ends of the two worm wheels are respectively provided with an eccentric shaft, the two eccentric shafts slide in push-pull sliding grooves of the two push-pull sliding racks, the two push-pull sliding racks slide on the front side and the rear side surfaces of the inner side of the filter material box, and a transverse shaft fixed at the inner end of the filter material box slides in through shaft holes of the two push-pull sliding racks; and cleaning brushes are fixed on the two push-pull sliding racks and slide on the filtrate outlets.
The inner end of the filter material box is of an arc-shaped opening structure, and the arc-shaped opening structure is hermetically and slidably arranged on the outer tube surface of the circular drain pipe; the opening size of the arc-shaped opening structure is smaller than the opening size of the water collecting opening on the circular drain pipe.
Compared with the prior art, the application at least comprises the following beneficial effects:
the biochemical pharmaceutical engineering wastewater circulating and purifying system is provided with the primary filtering mechanism, and suspended matters and solid particles in wastewater can be subjected to primary filtering treatment through the primary filtering mechanism; the adsorption filtration mechanism is arranged in the wastewater treatment device and is an activated carbon adsorption filter, so that organic matters and drug residues in the wastewater subjected to preliminary filtration treatment can be adsorbed, the organic matters and drug residues in the wastewater are reduced, and the removal effect of pollutants in the wastewater is improved; the inside of the application is also provided with an oxidation box, and an ozone generator is arranged in the oxidation box so as to carry out ozone oxidation treatment on the wastewater after the adsorption treatment, thereby improving the removal effect of the undegradable pollutants in the wastewater; the application is internally provided with the evaporation condenser, so that the waste water after the oxidation treatment can be subjected to the evaporation treatment, in the evaporation process, the non-volatile substances in the pharmaceutical waste water are gradually concentrated, after the concentration to a certain degree, the concentrate can be subjected to centrifugal separation, crystallization and the like, the corresponding treatment is carried out according to the difference of solid substances obtained by crystallization, and condensate can be recycled; the inside of the primary filter mechanism is provided with a plurality of filter material components which are recycled, each filter material component can be soaked and cleaned by the soaking liquid filled in the rectangular box body after the suspended matters and solid particles in the wastewater are subjected to primary filtering treatment, so that the suspended matters and solid particles filtered out of the filter material components are removed, the filter material components are filtered again conveniently, the blocking probability of the filter material components is reduced, and the filtering effect of the filter material components is improved.
In order to make the above objects, features and advantages of the present application more comprehensible, preferred embodiments accompanied with figures are described in detail below.
Drawings
The accompanying drawings are included to provide a further understanding of the application and are incorporated in and constitute a part of this specification, illustrate the application and together with the embodiments of the application, serve to explain the application. In the drawings:
FIG. 1 is a schematic diagram of an overall structure according to an embodiment of the present application;
fig. 2 is a schematic structural diagram of an artificial wetland provided by an embodiment of the application;
FIG. 3 is a schematic structural diagram of a primary filtering mechanism according to an embodiment of the present application;
FIG. 4 is a first directional cross-sectional block diagram of a primary filter mechanism provided in an embodiment of the present application;
FIG. 5 is a cross-sectional view of a second direction of a primary filter mechanism according to an embodiment of the present application;
FIG. 6 is a schematic diagram of a partial structure of a primary filter mechanism according to an embodiment of the present application;
fig. 7 is a schematic structural diagram of a primary filter box according to an embodiment of the present application;
FIG. 8 is a schematic diagram II of a primary filter tank according to an embodiment of the present application;
fig. 9 is a schematic structural view of a circular drain pipe according to an embodiment of the present application;
FIG. 10 is a schematic view of an annular mounting frame according to an embodiment of the present application;
FIG. 11 is a schematic diagram of a filter assembly according to an embodiment of the present application;
fig. 12 is a schematic structural diagram of a filter assembly according to an embodiment of the present application;
FIG. 13 is a schematic view of a partial structure of a filter assembly according to an embodiment of the present application;
fig. 14 is a cross-sectional view of a filter media assembly according to an embodiment of the present application.
Icon: an artificial wetland 1; a wetland tank 101; a soil filler layer 102; a water stream 103; aquatic plants 104; a water permeable substrate layer 105; a water outlet layer 106; a drain pipe 107; a primary filter mechanism 2; an adsorption filtration mechanism 3; an oxidation tank 4; an evaporation condenser 5; a primary filter box 6; a semicircle 601; a semicircular occlusion ring 602; a circular drain pipe 7; water collection port 701; an annular mounting frame 8; a filter assembly 9; a filter box 901; a liquid inlet 902; a liquid passing hole 903; a filtrate outlet 904; a guide bevel board 905; a linked worm 906; a gear 907; a drive sprocket 908; driven sprocket 909; a rotation shaft 910; a worm wheel 911; an eccentric shaft 912; the carriage 913 is pushed and pulled.
Detailed Description
In order to enable those skilled in the art to better understand the technical solutions of the present application, the technical solutions of the embodiments of the present application will be clearly and completely described below, and it is obvious that the described embodiments are only some embodiments of the present application, not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the application without making any inventive effort, are intended to be within the scope of the application.
The present application is described in further detail below with reference to the drawings and examples to enable those skilled in the art to practice the application by referring to the description.
It will be understood that terms, such as "having," "including," and "comprising," as used herein, do not preclude the presence or addition of one or more other elements or groups thereof.
The application is described in further detail below with reference to fig. 1-14.
Example 1
As shown in fig. 1 to 14, a biochemical pharmaceutical engineering wastewater circulation purification system includes: a primary filter mechanism 2 for primarily filtering suspended matters and solid particles in the wastewater; the adsorption and filtration mechanism 3 is connected with the primary filtration mechanism 2 to carry out adsorption treatment on organic matters and drug residues in the wastewater subjected to primary filtration treatment; the oxidation box 4 is connected with the adsorption filtering mechanism 3, and an ozone generator is arranged in the oxidation box 4 so as to carry out ozone oxidation treatment on the wastewater after the adsorption treatment; and the evaporation condenser 5 is connected with the oxidation tank 4, so as to perform evaporation treatment on the oxidized wastewater, and collect condensate for recycling.
The working principle and the beneficial effects of the application are as follows:
when the wastewater is treated, the wastewater is firstly conveyed into the primary filter mechanism 2, suspended matters and solid particles in the wastewater can be subjected to primary filtration treatment through the primary filter mechanism 2, then the wastewater is conveyed into the adsorption filter mechanism 3, the adsorption filter mechanism 3 can be an activated carbon adsorption filter, the adsorption filter mechanism 3 can perform adsorption treatment on organic matters and drug residues in the wastewater subjected to primary filtration treatment, the organic matters and drug residues in the wastewater are reduced, and the removal effect on pollutants in the wastewater is improved; the wastewater after adsorption and filtration enters an oxidation tank 4, an ozone generator is arranged in the oxidation tank 4, so that the wastewater after adsorption treatment can be subjected to ozone oxidation treatment, the effect of removing nondegradable pollutants in the wastewater is improved, and the oxidation tank 4 can be replaced by an anaerobic tank to perform oxidation treatment on the wastewater; after the wastewater is oxidized, the wastewater enters an evaporation condenser 5, the evaporation condenser 5 can perform evaporation treatment on the oxidized wastewater, in the evaporation process, non-volatile substances in the wastewater are gradually concentrated, after the non-volatile substances are concentrated to a certain degree, the concentrate can be subjected to centrifugal separation, crystallization and the like, corresponding treatments are performed according to the difference of solid substances obtained through crystallization, and condensate can be recycled.
Example two
1-14, on the basis of the above embodiment, the biochemical pharmaceutical engineering wastewater circulation purification system further comprises an artificial wetland 1, wherein the artificial wetland 1 comprises a wetland tank 101, a soil filler layer 102 is arranged at the upper end inside the wetland tank 101, water flow 103 is converged at the top of the soil filler layer 102, and aquatic plants 104 are planted on the soil filler layer 102; the bottom of the soil packing layer 102 is provided with a water permeable matrix layer 105, the bottom of the water permeable matrix layer 105 is provided with a water outlet layer 106, and a drain pipe 107 penetrating through the water outlet layer 106 is connected with the primary filter mechanism 2.
The working principle and the beneficial effects of the application are as follows:
in the biochemical pharmaceutical engineering wastewater circulation purification system, by the arrangement of the soil filler layer 102, the aquatic plants 104, the water-permeable matrix layer 105 and the aerobic and anaerobic microbiota in the wetland tank 101, harmful substances in wastewater are further removed by utilizing the triple synergistic effect of the physical chemistry and the biology of soil, media, plants and microorganisms, and the purification effect of wastewater is improved.
The drain pipe 107 is provided with a water suction pump, so that the efficiency of wastewater entering the primary filter mechanism 2 through the drain pipe 107 is improved.
The adsorption and filtration mechanism 3 is an activated carbon adsorption filter.
Example III
1-14, on the basis of the above embodiment, the primary filter mechanism 2 comprises a primary filter box 6, wherein the primary filter box 6 comprises a water inlet, a semicircular box body, a rectangular box body and a base which are fixedly connected in sequence from top to bottom, a circular drain pipe 7 is sealed and fixed in a transverse round hole at the joint of the semicircular box body and the rectangular box body, end covers are arranged at two ends of the circular drain pipe 7, and a water outlet pipe is arranged on one end cover; a water collecting port 701 is arranged above the middle part of the circular drain pipe 7, the water collecting port 701 is positioned right below the water inlet, the circular drain pipe 7 is provided with a sealing rotary annular mounting frame 8, and the upper end of the annular mounting frame 8 is sealed and rotated on the inner annular surface of the semicircular box body; a plurality of mounting grooves are uniformly and circumferentially arranged on the annular mounting frame 8, and filter material components 9 are arranged in the plurality of mounting grooves; the inside of the rectangular box body is provided with soaking liquid, so that the filtering material component 9 rotating to the lower part of the inside of the rectangular box body is soaked and cleaned by the soaking liquid; the annular mounting frame 8 is provided with a rotary gear which is meshed with a gear at the output end of the rotary motor, and the rotary motor is fixed on the primary filter box 6.
The working principle and the beneficial effects of the application are as follows:
in the biochemical pharmaceutical engineering wastewater circulating and purifying system, when the primary filtering mechanism 2 is used, a rotary motor can drive a rotary gear to rotate through a gear after being started, an annular mounting frame 8 can be driven to rotate and circulate by taking the axis of a circular drain pipe 7 as the center when the rotary gear rotates, and different filter material components 9 can be driven to move below a water inlet or move into soak solution in a rectangular box body when the annular mounting frame 8 rotates; after the wastewater enters the primary filter box 6 through the water inlet, the wastewater can fall into the filter material assembly 9 moving to the lower part of the water inlet, so that the wastewater is filtered through the filter material assembly 9, suspended matters and solid particles in the wastewater are filtered and purified effectively, the wastewater after filtering and purifying enters the circular drain pipe 7 through the water collecting port 701 above the middle part of the circular drain pipe 7, the wastewater can be discharged through the circular drain pipe 7 for subsequent treatment, the filter material assemblies 9 are alternately used, and after the suspended matters and the solid particles are filtered out by the filter material assembly 9, the wastewater can be rotationally moved into the soaking liquid at the lower end in the rectangular box body for soaking and cleaning, so that the suspended matters and the solid particles filtered out by the filter material assembly are removed conveniently, the blockage probability of the filter material assembly is reduced, and the filtering effect of the filter material assembly is improved.
One end of the rectangular box body is provided with a flushing water inlet, the other end of the rectangular box body is provided with a flushing water outlet, a flushing assembly used for flushing the filter material assembly 9 moving to the lower part of the rectangular box body is arranged in the flushing water inlet, when the installation groove of the annular installation frame 8 moves to the lower part of the water inlet and the upper part of the water collecting port 701, a filtering channel is formed, so that the soaking liquid at the lower end in the rectangular box body flows, and the cleaning effect on the filter material assembly 9 can be improved.
Example IV
1-14, the filter material assembly 9 comprises a filter material box 901, wherein filter material is filled in the filter material box 901, and the volume of the filter material is two thirds of the volume of the filter material box 901; the filter material box 901 is fixed in the mounting groove of the annular mounting frame 8, the outer end of the filter material box 901 is of an arc surface structure, the arc surface structure is coplanar with the outer annular surface of the annular mounting frame 8, a plurality of liquid inlets 902 are uniformly formed in the arc surface structure, the front side surface and the rear side surface of the filter material box 901 are coplanar with the front side surface and the rear side surface of the annular mounting frame 8 respectively, and a plurality of liquid inlets 903 are uniformly formed in the rear side surface of the filter material box 901; the inner end of the filter tank 901 is of a planar structure, a plurality of filtrate outlets 904 are uniformly arranged on the planar structure, and the plurality of filtrate outlets 904 are arranged opposite to the water collecting port 701; the semicircular ring 601 fixed at the front end inside the semicircular box body hermetically slides on the front side surface of the filter material box 901; the semicircular plugging ring 602 fixed at the rear end inside the semicircular box body hermetically slides on the rear side surface of the filter material box 901, and the semicircular plugging ring 602 can be plugged on the liquid through hole 903 of the filter material box 901 moving into the semicircular box body.
The working principle and the beneficial effects of the application are as follows:
in the biochemical pharmaceutical engineering wastewater circulating and purifying system, when a filter material assembly 9 moves to the position right below a water inlet, wastewater enters a filter material box 901 through a plurality of liquid inlet holes 902, suspended matters and solid particles in the wastewater are filtered out through a filter material in the filter material box 901, and the filtered wastewater flows into a water collecting port 701 through a plurality of filtrate outlets 904, so that the wastewater enters a circular drain pipe 7; the semicircular ring 601 fixed at the front end inside the semicircular box body hermetically slides on the front side surface of the filter material box 901, and the semicircular ring 601 plays a role in blocking and limiting; the semicircular plugging ring 602 fixed at the rear end inside the semicircular box body hermetically slides on the rear side surface of the filter material box 901, and the semicircular plugging ring 602 cooperates with the semicircular ring 601 to play a role of blocking and limiting on one hand, and on the other hand, the semicircular plugging ring is used for plugging a plurality of liquid through holes 903 on the rear side surface of the filter material box 901 when the filter material assembly 9 moves to a water inlet, so that waste water is prevented from flowing out through the plurality of liquid through holes 903 during filtration; when the filter material component 9 moves to the water inlet gradually, the filtering treatment is stopped gradually, as the filter material is filled in the filter material box 901, the volume of the filter material is two thirds of the volume of the filter material box 901, when the filter material component 9 moves to the soaking liquid at the lower end in the rectangular box body, the filter material box 901 is gradually inverted, so that the filter material rolls in the filter material box 901, the filter material can be cleaned better through the soaking liquid, at the moment, the semicircular plugging ring 602 releases the plugging of the plurality of liquid holes 903 on the rear side surface of the filter material box 901, and the filtered suspended matters and solid particles in the filter material can be discharged through the plurality of liquid inlet holes 902 on the cambered surface structure and the plurality of liquid holes 903 on the rear side surface of the filter material box 901, thereby achieving the effect of cleaning the suspended matters and solid particles in the filter material, facilitating the filtering use again, reducing the plugging probability during the filtering, and improving the filtering effect.
Example five
1-14, on the basis of the above embodiment, the inner end of the filter material box 901 is a strip-shaped box body, the outer end of the filter material box 901 is a fan-shaped box body, a plurality of filtrate outlets 904 are arranged on the strip-shaped box body, and a plurality of liquid inlets 902 are arranged on the fan-shaped box body; the left and right ends of the inner wall of the strip-shaped box body are respectively connected with a material guiding inclined plate 905 which is obliquely arranged towards the direction of the filtrate outlet 904 in a rotating way, the lower ends of the two material guiding inclined plates 905 can be blocked on the left and right stop blocks of the inner wall of the strip-shaped box body, and when the filter material assembly 9 rotates to the lower part of the rectangular box body, the two material guiding inclined plates 905 can rotate towards the direction of the liquid inlet 902 under the action of filter materials in the strip-shaped box body and self gravity.
The working principle and the beneficial effects of the application are as follows:
in the biochemical pharmaceutical engineering wastewater circulating and purifying system, the inner end of the filter material box 901 is a strip-shaped box body, the outer end of the filter material box 901 is a fan-shaped box body, so that when the filter material assembly 9 moves below a water inlet, filter materials are gathered in the strip-shaped box body under the action of gravity, the filter material structure is compact, suspended matters and solid particles in wastewater are effectively removed, and when the filter material assembly 9 moves into a soaking liquid, the filter materials move into the fan-shaped box body under the action of gravity, and therefore the filter materials are dispersed, and better cleaning through the soaking liquid is facilitated; and the material guiding inclined plates 905 are obliquely arranged on the inner wall of the strip-shaped box body towards the direction of the filtrate outlet 904, when the filter material component 9 rotates to the lower part of the rectangular box body, the two material guiding inclined plates 905 can rotate towards the direction of the liquid inlet 902 under the action of the filter material in the strip-shaped box body and self gravity, at the moment, the filter material in the strip-shaped box body can be guided towards the middle part of the fan-shaped box body through the two material guiding inclined plates 905, and when the filter material is continuously piled up, the filter material gradually disperses towards the two sides of the inner side of the fan-shaped box body under the action of self gravity and the buoyancy of the soaking liquid, so that the dispersion effect of the filter material is further improved, and the cleaning effect is ensured; when the filter material component 9 moves to the lower part of the water inlet, the filter material in the fan-shaped box body can be guided and conveyed to the middle part of the strip-shaped box body through the two guide inclined plates 905, and the middle part of the strip-shaped box body is scattered to two sides, so that the uniformity of the filter material paved in the strip-shaped box body is improved, and the filtering effect is ensured.
Example six
As shown in fig. 1-14, on the basis of the above embodiment, the filter material assembly 9 further includes a linkage worm 906, two ends of the linkage worm 906 rotate on the front and rear side surfaces of the filter material box 901, and a gear 907 fixed at the front end of the linkage worm 906 is meshed with an external gear fixed on the outer pipe surface of the circular drain pipe 7; the driving sprocket 908 fixed at the front end of the linkage worm 906 is connected with two driven sprockets 909 through a chain, the two driven sprockets 909 are fixed on two rotating shafts 910, two ends of the two rotating shafts 910 are rotated on the front side and the rear side of the filter material box 901, a plurality of material stirring rods are fixed on the shaft bodies of the two rotating shafts 910 in the filter material box 901, and the axis of the linkage worm 906 and the axis of the two rotating shafts 910 are coplanar.
The working principle and the beneficial effects of the application are as follows:
in the biochemical pharmaceutical engineering wastewater circulating and purifying system, when the annular mounting frame 8 rotates around the axis of the circular drain pipe 7, different filter material assemblies 9 can be driven to move when the annular mounting frame 8 rotates, so that gears 907 in the filter material assemblies 9 are driven to contact with different positions of an outer gear ring on the outer tube surface of the circular drain pipe 7, the gears 907 are driven to rotate around the axis of the gears 907, the gears 907 can drive the linkage worm 906 to rotate when the gears 907 rotate, the driving sprocket 908 can be driven to rotate when the linkage worm 906 rotates, the driving sprocket 908 is connected with two driven sprockets 909 through a chain, so that the two driven sprockets 909 rotate, the two rotating shafts 910 are driven to rotate through the rotation of the two rotating shafts 910, the stirring of the filter material in the filter material box 901 is carried out through the rotation of the two rotating shafts 910, the improvement of the dispersing effect of the filter material is facilitated, and the cleaning effect of the filter material in the soaking liquid is also facilitated.
Example seven
As shown in fig. 1-14, on the basis of the above embodiment, the filter assembly 9 further includes a worm wheel 911, two ends of a linkage worm 906 are engaged with the two worm wheels 911 relatively, one end of the two worm wheels 911 is rotated on a support at the inner end of the filter box 901 through a short shaft, eccentric shafts 912 are fixed at the eccentric positions at the other ends of the two worm wheels 911, the two eccentric shafts 912 slide in push-pull sliding grooves of the two push-pull sliding frames 913, the two push-pull sliding frames 913 slide on front and rear side surfaces of the inner side of the filter box 901, and a transverse shaft fixed at the inner end of the filter box 901 slides in through-shaft holes of the two push-pull sliding frames 913; a cleaning brush is fixed to both push-pull carriages 913, and slides on the plurality of filtrate outlets 904.
The inner end of the filter material box 901 is of an arc-shaped opening structure, and the arc-shaped opening structure is hermetically slid on the outer tube surface of the circular drain pipe 7; the opening size of the arc-shaped opening structure is smaller than the opening size of the water collecting opening 701 on the circular drain pipe 7.
The working principle and the beneficial effects of the application are as follows:
in the biochemical pharmaceutical engineering wastewater circulating and purifying system, when the linkage worm 906 rotates, two worm gears 911 can be meshed and driven to rotate, when the worm gears 911 rotate, the eccentric shafts 912 can be driven to rotate and move in a surrounding mode, and when the eccentric shafts 912 move in a surrounding mode, the positions of the eccentric shafts 912 in the sliding grooves of the sliding carriages 913 are changed, so that the sliding carriages 913 are driven to slide on the front side and the rear side of the inner side of the filter material box 901 and slide on the transverse shafts, the transverse shafts play a limiting role, the sliding stability of the sliding carriages 913 is improved, and when the sliding carriages 913 slide, the cleaning brushes can be driven to brush a plurality of filtrate outlets 904, a certain degree of self-cleaning effect is achieved, and the blockage of the plurality of filtrate outlets 904 is prevented from affecting the water outlet effect.
In the description of the present application, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings are merely for convenience in describing the present application and simplifying the description, and do not indicate or imply that the device or element being referred to must have a specific orientation, be configured and operated in a specific orientation, and therefore should not be construed as limiting the present application.
In the present application, unless explicitly specified and limited otherwise, the terms "mounted," "connected," "secured," and the like are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally formed; may be mechanically connected, may be electrically connected or may be in communication with each other; either directly or indirectly, through intermediaries, or both, may be in communication with each other or in interaction with each other, unless expressly defined otherwise. The specific meaning of the above terms in the present application can be understood by those of ordinary skill in the art according to the specific circumstances.
Although embodiments of the present application have been disclosed above, it is not limited to the details and embodiments shown and described, it is well suited to various fields of use for which the application would be readily apparent to those skilled in the art, and accordingly, the application is not limited to the specific details and illustrations shown and described herein, without departing from the general concepts defined in the claims and their equivalents.
Claims (5)
1. A biochemical pharmaceutical engineering wastewater circulation purification system, comprising: a primary filtering mechanism (2) for carrying out primary filtering treatment on suspended matters and solid particles in the wastewater; the adsorption and filtration mechanism (3), the adsorption and filtration mechanism (3) is connected with the primary filtration mechanism (2) to carry out adsorption treatment on organic matters and drug residues in the wastewater after primary filtration treatment; the oxidation box (4) is connected with the adsorption filtering mechanism (3), and an ozone generator is arranged in the oxidation box (4) so as to perform ozone oxidation treatment on the wastewater after adsorption treatment; the evaporation condenser (5) is connected with the oxidation tank (4) to perform evaporation treatment on the oxidized wastewater, and condensate is collected and recycled;
the primary filter mechanism (2) comprises a primary filter box (6), the primary filter box (6) comprises a water inlet, a semicircular box body, a rectangular box body and a base which are fixedly connected in sequence from top to bottom, a circular drain pipe (7) is sealed and fixed in a transverse round hole at the joint of the semicircular box body and the rectangular box body, two ends of the circular drain pipe (7) are respectively provided with an end cover, and a water outlet pipe is arranged on one end cover; a water collecting port (701) is arranged above the middle part of the circular drain pipe (7), the water collecting port (701) is positioned right below the water inlet, the circular drain pipe (7) is sealed and rotated with an annular mounting frame (8), and the upper end of the annular mounting frame (8) is sealed and rotated on the inner annular surface of the semicircular box body; a plurality of mounting grooves are uniformly and circumferentially arranged on the annular mounting frame (8), and filter material components (9) are arranged in the plurality of mounting grooves; the inside of the rectangular box body is provided with soaking liquid, so that the filtering material component (9) rotating to the lower part of the inside of the rectangular box body is soaked and cleaned by the soaking liquid; a rotary gear is fixed on the annular mounting frame (8) and meshed with a gear at the output end of a rotary motor, and the rotary motor is fixed on the primary filter box (6);
the filter material assembly (9) comprises a filter material box (901), wherein the filter material box (901) is filled with filter materials, and the volume of the filter materials is two thirds of that of the filter material box (901); the filter material box (901) is fixed in a mounting groove of the annular mounting frame (8), an arc surface structure at the outer end of the filter material box (901) is coplanar with the outer annular surface of the annular mounting frame (8), a plurality of liquid inlets (902) are uniformly formed in the arc surface structure, the front side surface and the rear side surface of the filter material box (901) are coplanar with the front side surface and the rear side surface of the annular mounting frame (8) respectively, and a plurality of liquid through holes (903) are uniformly formed in the rear side surface of the filter material box (901); the inner end of the filter box (901) is of a planar structure, a plurality of filtrate outlets (904) are uniformly arranged on the planar structure, and the plurality of filtrate outlets (904) are arranged opposite to the water collecting port (701); the semicircular ring (601) fixed at the front end inside the semicircular box body hermetically slides on the front side surface of the filter material box (901); a semicircular plugging ring (602) fixed at the rear end inside the semicircular box body is hermetically slid on the rear side surface of the filter material box (901), and the semicircular plugging ring (602) can be plugged on a liquid through hole (903) of the filter material box (901) moving into the semicircular box body;
the inner end of the filter material box (901) is a strip-shaped box body, the outer end of the filter material box (901) is a fan-shaped box body, a plurality of filtrate outlets (904) are arranged on the strip-shaped box body, and a plurality of liquid inlets (902) are arranged on the fan-shaped box body; the left end and the right end of the inner wall of the strip-shaped box body are respectively and rotatably connected with a material guiding inclined plate (905) which is obliquely arranged towards the direction of a filtrate outlet (904), the lower ends of the two material guiding inclined plates (905) can be blocked on the left and the right stop blocks of the inner wall of the strip-shaped box body, and when the filter material component (9) rotates below the rectangular box body, the two material guiding inclined plates (905) can rotate towards the direction of a liquid inlet (902) under the action of filter materials in the strip-shaped box body and self gravity;
the filter material assembly (9) further comprises a linkage worm (906), two ends of the linkage worm (906) are rotated on the front side surface and the rear side surface of the filter material box (901), and a gear (907) fixed at the front end of the linkage worm (906) is meshed with an outer gear ring fixed on the outer tube surface of the circular drain pipe (7); a driving sprocket (908) fixed at the front end of the linkage worm (906) is connected with two driven sprockets (909) through a chain, the two driven sprockets (909) are fixed on two rotating shafts (910), two ends of the two rotating shafts (910) are rotated on the front side surface and the rear side surface of the filter material box (901), a plurality of stirring rods are fixed on shaft bodies of the two rotating shafts (910) in the filter material box (901), and the axis of the linkage worm (906) and the axis of the two rotating shafts (910) are coplanar;
the filter material assembly (9) further comprises worm wheels (911), two ends of the linkage worm (906) are oppositely meshed with the two worm wheels (911), one end of each worm wheel (911) rotates on a support seat at the inner end of the filter material box (901) through a short shaft, eccentric positions at the other ends of the two worm wheels (911) are respectively provided with an eccentric shaft (912), the two eccentric shafts (912) slide in push-pull sliding grooves of the two push-pull sliding carriages (913), the two push-pull sliding carriages (913) slide on the front side and the rear side surfaces of the inner side of the filter material box (901), and a transverse shaft fixed at the inner end of the filter material box (901) slides in through shaft holes of the two push-pull sliding carriages (913); a cleaning brush is fixed on each of the two push-pull carriages (913), and the cleaning brush slides on the plurality of filtrate outlets (904).
2. The biochemical pharmaceutical engineering wastewater circulation purification system according to claim 1, further comprising an artificial wetland (1), wherein the artificial wetland (1) comprises a wetland tank (101), a soil filler layer (102) is arranged at the upper end inside the wetland tank (101), water flow (103) is converged at the top of the soil filler layer (102), and aquatic plants (104) are planted on the soil filler layer (102); the bottom of the soil packing layer (102) is provided with a water permeable matrix layer (105), the bottom of the water permeable matrix layer (105) is provided with a water outlet layer (106), and a drain pipe (107) penetrating through the water outlet layer (106) is connected with the primary filter mechanism (2).
3. A biochemical pharmaceutical engineering wastewater circulation purification system according to claim 2, wherein a water suction pump is provided on the water discharge pipe (107).
4. The biochemical pharmaceutical engineering wastewater circulation purification system according to claim 1, wherein the adsorption filtration mechanism (3) is an activated carbon adsorption filter.
5. The biochemical pharmaceutical engineering wastewater circulation purification system according to claim 1, wherein the inner end of the filter material box (901) is of an arc-shaped opening structure, and the arc-shaped opening structure is hermetically sliding on the outer tube surface of the circular drain tube (7); the opening size of the arc-shaped opening structure is smaller than the opening size of the water collecting opening (701) on the circular drain pipe (7).
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