CN209242876U - Six segmentation intelligent control medical waste water processors and its oil removal structure - Google Patents

Six segmentation intelligent control medical waste water processors and its oil removal structure Download PDF

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Publication number
CN209242876U
CN209242876U CN201822128802.7U CN201822128802U CN209242876U CN 209242876 U CN209242876 U CN 209242876U CN 201822128802 U CN201822128802 U CN 201822128802U CN 209242876 U CN209242876 U CN 209242876U
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reaction tank
pond
pump
dirty
section
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张成巍
孙德亮
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DALIAN GELANQING WATER ENVIRONMENT ENGINEERING Co Ltd
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DALIAN GELANQING WATER ENVIRONMENT ENGINEERING Co Ltd
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Abstract

The utility model discloses six segmentation intelligent control medical waste water processors and its oil removal structures, are related to water treatment field;Including six Duan Chi and component;Six sections of ponds include: collecting-tank, adjust oil separator, MBBR reaction tank, MBR reaction tank, clear water reserviors, sterilization pool, and the component includes: blower, metering dosing pump, self priming pump, charging pump, backwashing pump, disinfection drug basin, mixer of liquid medicine;It adjusts and is equipped with oil removal structure between oil separator and MBBR reaction tank, self-control box is arranged in described processor one end, and all components are connected to self-control box;The utility model has many advantages, such as that good effect, small investment, occupied area is small, process is short, flexible operation is easy, saves human and material resources, reduces pollutant load, reaches emission request.

Description

Six segmentation intelligent control medical waste water processors and its oil removal structure
Technical field
The utility model relates to field of waste water treatment, and in particular to a kind of six segmentation intelligent control medical waste water processors and Its oil removal structure.
Background technique
China implemented new standard " Discharge standard of water pollutants for medical organization " on January 1st, 2006.It is reported that newly Requirement of the standard to biological indicator etc. it is also higher than original standard, more perfect.By executing new standard, infectious disease Hospital can emission reduction COD70%, BOD emission reduction 80%, SS emission reduction 80%.General hospital's emission reduction COD50%, BOD emission reduction 60%, SS emission reduction 60%.With the development of China's medical industry, large amount of sewage discharges daily in medical institutions, these sewage may contain spreading venereal diseases Opportunistic pathogen, virus, chemical pollutant and radioactive substance will cause to seriously affect Ru uncontrolled to environmental and human health impacts.Doctor Sewage is treated, other than containing pollutants such as COD, BOD, it is often more important that contain a large amount of pathogenic bacteria.Hospital sewage after precipitation, There are 70 ~ 80% germ, virus and 90% worm egg to be transferred in sludge.Therefore, traditional processing method be to septic tank and Sewage, the sludge of discharge are effectively disinfected.Lazaretto ward and infectious hospital must be provided with dedicated septic tank.Change excrement Pond sludge every half a year drew clearly once by 1 year, and reply septic tank sludge is monitored when clear naughty.Septic tank and Sewage Disposal are dirty The induced worm egg death rate and excrement colibacillus group number of mud should respectively reach the requirement of > 95% and≤100MPN/g, and sludge up to standard is by special Door vehicle is sent to special disposal site disposition or carries out burning disposal.Cause the waste of great human and material resources and financial resources. Some is even handled and is not thorough, and causes the hidden danger of second of transmission.Since most of medical institutions do not carry out sanitary sewage With the separation of medical sewage, mixed sewage contains more grease, influences to inhibit aerobic bacteria activity, influences treatment effect. This amount of grease, it is necessary to separate in advance.
Summary of the invention
The purpose of the present invention is the deficiencies for the processing of the above medical waste water, propose a kind of six sections for handling medical waste water Formula intelligent control medical waste water processor and its oil removal structure.
To achieve the goals above, the technical scheme adopted by the utility model is six segmentation intelligent control medical waste waters Processor, it is characterised in that: including six Duan Chi and component;Six sections of ponds include: collecting-tank, adjust oil separator, MBBR reaction Pond, MBR reaction tank, clear water reserviors, sterilization pool, the component include: blower, metering dosing pump, self priming pump, charging pump, backwash Pump, disinfection drug basin, mixer of liquid medicine;It adjusts and is equipped with oil removal structure, the processor between oil separator and MBBR reaction tank Self-control box is arranged in one end, and all components are connected to self-control box;
The six segmentation intelligent control medical waste water processors further include cutting dirty pond and reflux pump, cut dirty pond in Inlet and outlet water Place is respectively equipped with first section of dirty plate, and second section of dirty plate, it is anti-with MBR that described first, second section dirty plate is located at MBBR reaction tank The two sides of pond cell compartment plate are answered, cuts in the pond of dirty pond and is laid with quartz sand, backwash tube, MBBR reaction tank and MBR are set along bottom of pond portion Reaction tank division wall bottom is equipped with permeable hole;
Described cutting in dirty pond is laid with for two layers of quartz sand point, upper layer quartz sand 100~150mm of thickness, 4~6mm of diameter, under Layer quartz sand 50~80mm of thickness, 8~12mm of diameter, the standard of the backwash tube is ND40 × 4,22 spacing of permeable hole 100mm, aperture Ф 10mm;The dirty plate of described first section and second section of dirty plate high 250mm, distance between plates 500mm, and two plates are symmetrical Positioned at MBBR reaction tank and MBR reaction tank cell compartment plate two sides;
Curtain hollow-fibre membrane is equipped in the MBR reaction tank to combine, bottom of pond is evenly distributed aerator, connection blower into Row aeration oxygen supply, MBR reaction tank is intake under the action of self priming pump, after curtain hollow-fibre membrane combined treatment, flows into clear water Pond;Periodically, clear water reserviors water inlet backwashes film in MBR reaction tank under the action of backwashing pump;
The oil removal structure is H-type grease trap, and H-type grease trap is across the wall adjusted oil separator and MBBR reaction tank Wall is divided into two parts on the basis of H-type grease trap central part, is respectively uniformly distributed in adjusting oil separator and MBBR reaction tank Portion;
The straight tube that two parts of the H-type grease trap pass through a tee tube respectively, are connected to tee tube upper and lower ends Section is constituted, and remaining two tube heads of two tee tubes are docking together by the U-PVC pipe that internal diameter is 100mm;
The straight pipe for being set to tee tube upper and lower ends is U-PVC pipe, and pipe diameter internal diameter is 100mm;
The straight pipe for being set to tee tube upper and lower ends include 4 sections, be respectively according to water (flow) direction the first pipeline section, Second pipeline section, third pipeline section and the 4th pipeline section;The first, the lower end that the 4th pipeline section is respectively connected to two tee tubes, the first pipeline section and Gap is arranged with the upper surface for the bottom of pond plate for adjusting oil separator, MBBR reaction tank respectively in 4th pipeline section;Second, third pipeline section difference Be connected to the upper end of tee tube, the second pipeline section and third pipeline section respectively with adjust oil separator, MBBR reaction tank pond top plate under Gap is arranged in surface;
When oil removal structure is worked, into adjust oil separator oily wastewater first from the first pipeline section of H-type grease trap Entrance enters, and by tee tube, the oily substance in water is blocked on the second pipeline section for adjusting H-type grease trap in oil separator, warp Sewage after crossing oil removal flows through adjusting oil separator by tee tube and enters H-type grease trap in MBBR reaction tank, and water flow stream It finally exports and flows out from the 4th pipeline section through tee tube;H-type grease trap obstructs the oily substance in water in conditioning tank, individually locates Reason, improves the treatment effect of disposed of in its entirety machine;
The six segmentation intelligent control medical waste water processors, blower are aerated MBBR reaction tank, MBR reaction tank Oxygen supply;Self priming pump acts on the water inlet of MBR reaction tank, is discharged through film process;Waste water enters adjusting in charging pump pumping collecting-tank Oil separator flows automatically to MBBR reaction tank;Backwashing pump acts on clear water reserviors water inlet and backwashes to the film of MBR reaction tank;Disappear Poison product basin connection metering dosing pump measures dosing into mixer of liquid medicine, and clear water reserviors water outlet is mixed through drug in mixer of liquid medicine Collaborate into sterilization pool;
The technique that six segmentation intelligent control medical waste water processors handle medical waste water includes six sections of processes:
First segment: it is collected in waste water to be processed in ground lower sump 1, is pumped to through charging pump 10 and adjusts oil separator 2;
Second segment: it adjusts and is equipped with H-type automatic oil-separation device in oil separator.After sewage enters conditioning tank stabilization, grease is Through separating.By H-type automatic oil-separation device, oil is blocked in conditioning tank, water flows automatically to MBBR reaction tank 3;
Third section: loading moving-bed biofilm filler in MBBR reaction tank 3, bottom of pond is evenly distributed aerator, couples blower 7 Carry out aeration oxygen supply;
4th section: the water outlet of MBBR reaction tank 3 is flowed through to cut a dirty plate and enter and be cut in dirty pond 15, through quartz sand be filtered processing, Impurity is isolated, a section dirty pond other side is entered by permeable hole 24, after again flowing through quartz sand filtration processing, flows through and cuts the dirty entrance of plate 20 In MBR reaction tank 4;Dirty 15 bottom of pond portion of pond recoil water pipe is cut, under the action of reflux pump 12, clear water reserviors 5 is periodically pumped and intakes Quartz sand in pond is backwashed, flushing water is back in MBBR reaction tank 3 and MBR reaction tank 4, and waste water is cut dirty pond filtering When, it the more can be collected the more more and formed the obstacle of aquaporin and form blocking by filtered impurity, be laid with the recoil water pipe of bottom of pond portion 22 under source pressure and the impact of the joint of gas pressure, several permeable holes 23 on water pipe spray, and water and gas penetrate Quartz sand blows off the impurity assembled in filtering ponds.
5th section: being equipped with curtain hollow-fibre membrane in MBR reaction tank 4 and combine, bottom of pond is evenly distributed aerator, couples blower 7 carry out aeration oxygen supply, and MBR reaction tank 4 is intake under the action of self priming pump 9, after curtain hollow-fibre membrane combined treatment, flow into Clear water reserviors 5;Periodically, the water inlet of clear water reserviors 5 backwashes film in MBR reaction tank 4 under the action of backwashing pump 11;
6th section: clear water reserviors 5 and 6 partition wall top of sterilization pool are equipped with pore, and pore is located at one end connection liquid medicine of sterilization pool 6 Mixer 16, the water outlet of clear water reserviors 5 flow to mixer of liquid medicine 16 by pore, sterilization pool 6 are entered after being sufficiently mixed with drug, is disappeared It is discharged after poisoning bacterium, drug is supplied by disinfection drug storage tank 14, and regulates and controls dose by metering dosing pump 8, in mixer of liquid medicine Disinfection drug is sodium hypochlorite, and the water of sterilized sterilization treatment is discharged up to national healthcare wastewater discharge standard.
Come the water outlet of self priming pump 9 and rushing for backwashing pump 11 of implementation phase with the control of the micro computer time relay Wash, realize with the Reverse Turning Control of the micro computer time relay: when self priming pump 9 is run, recoil water pump 11 is closed, MBR reaction Pond 4 intakes under the action of self priming pump 9, after film process, flows into clear water reserviors 5;When self priming pump 9 is closed, recoil water pump 11 is transported Row, the water inlet of clear water reserviors 5 are backwashed through hollow curtain type membrane of the backwashing pump 11 to MBR reaction tank 4;According to experiment, setting is certainly Sucking pump is run 13 minutes, is closed 3 minutes, that is, is realized setting 13 minutes and be discharged, recoil within 3 minutes.Every 16 minutes are a cycle.Together When, self-priming evacuates in order to prevent, and liquid-level switch is arranged, and when the water level in the pond MBR is lower than warning line, self priming pump 9 closes automatically It closes.
For the depth of water for keeping collecting-tank certain, to retain anaerobic bacteria flora therein, collecting-tank is gone out using liquid-level switch Water is controlled.When waste water level is lower than warning line in collecting-tank 1, charging pump 10 is closed;Waste water level is higher than warning water When position, charging pump 10 is opened.
Meanwhile in order to avoid influencing equipment life and treatment effect due to waste water overflows in the pond MBBR 3, using liquid-level switch The water inlet of the pond MBBR 3 is controlled, when waste water level is higher than warning line in the pond MBBR 3, charging pump 10 is closed;Waste water level is low When warning line, charging pump 10 is opened.
The pond MBR 4 is into waste water, and clear water, is gravity flow into waste water out, and clear water goes out through self priming pump 9 out, and outlet sets motor-driven valve (electricity Magnet valve), with self priming pump close synchronously.Curtain hollow-fibre membrane combination in the pond MBR is intake under the action of self priming pump 9 through film Silk is outer to enter film wire hollow cavity;It is then that film wire wall is penetrated to outside film wire from film wire hollow cavity under the effect of backwashing pump 11 when recoil Wall impact guarantees self-priming effect to wash out the solid for being attached to film wire outer wall.Here, backwash is intake using clear water reserviors 5, Enter film wire through backwashing pump 11 and backwash motor-driven valve (solenoid valve), the motor-driven valve (solenoid valve) and self priming pump 9 of backwash are different Step is closed.When 4 liquid level of the pond MBR is lower than warning line, backwashing pump 11 and recoil valve are also switched off.Backwashing pump 11 is also by clear water 5 Liquid level of pond, when 5 liquid level of clear water reserviors is lower than warning line, backwashing pump is closed.
According to experiment, measuring and calculating, it is speed-raising operating that 7 turns of frequencies of blower, which are set as 2 grades: one grades,;Two grades are to run well.When upper water When pump 10 is started to work, blower 7 is synchronous to enter one grade (running well);When charging pump 10 stops working, blower 7 is transferred to two Shelves operation.It is adjusted by switching circuit and frequency converter, control.
Dosing intelligent control: metering dosing pump 8 and 9 synchronously control of self priming pump;When self priming pump 9 is run, metering dosing pump 8 is transported Row;When self priming pump 9 is closed, metering dosing pump 8 is closed;The storage for measuring dosing pump 8 and disinfection drug basin 14 links;Disinfectant When drug in product basin 14 is lower than warning liquid level, metering dosing pump 8 is closed, meanwhile, charging pump 10 also links closing.And it is same Step alarm, alarm device beep, blinking red lamp;All automatic controls lead to self-control box (13), are uniformly controlled.
Backwash is cut dirty device pipe and is controlled using the time relay (micro computer), and backwash in every 4 hours is primary, and 20 points every time Clock.
Pipe fitting connection type in system are as follows: use 304 stainless steel tubes across the position of pool wall, match ring flange;Pipe in water Net is coupled with U-pvc, and 304 steel flanges, screw joints are used between the pipe network of two kinds of materials.Pipe network diameter DN40, curtain It is DN20 that hollow-fibre membrane, which combines hose, and all components control leads to self-control box 13, is uniformly controlled.
The utility model has many advantages, such as that good effect, small investment, occupied area are small, and process is short, flexible operation is easy, can save A large amount of human and material resources and financial resources are saved, guarantees to reduce pollutant load, can achieve the requirement of direct emission.In particular, by A series of treated sewage, stable sterilization effects.
Detailed description of the invention
Fig. 1 is the schematic diagram of H-type grease trap.
Fig. 2 is H-type grease trap installation effect sectional view.
Fig. 3 is six segmentation intelligent control medical waste water processor schematic diagrames.
Fig. 4 is to cut dirty pond schematic diagram.
Fig. 5 is six segmentation intelligent control medical waste water processor treatment process schematic diagrames.
Fig. 6 is the curtain hollow-fibre membrane combination self-priming schematic diagram in the pond MBR.
Fig. 7 is the curtain hollow-fibre membrane combination backwash schematic diagram in the pond MBR.
Fig. 8 is mixer of liquid medicine structural schematic diagram.
In figure, 1, collecting-tank, 2, adjusting oil separator, 3, MBBR reaction tank, 4, MBR reaction tank, 5, clear water reserviors, 6, disinfection Pond, 7, blower, 8, metering dosing pump, 9, self priming pump, 10, charging pump, 11, backwashing pump, 12, reflux pump, 13, self-control box, 14, Disinfection drug basin, 15, section dirty pond, 16, mixer of liquid medicine, 17, MBBR reaction tank and MBR reaction tank cell compartment plate, 18, upper layer Quartz sand, 19, lower layer's quartz sand, 20, first sections of dirty ponds, 21, second sections of dirty ponds, 22, backwash tube, 23, permeable hole, 24, thoroughly Water hole, 25, DN40 steel pipe, 26, the outer silk connection of DN40 steel pipe, 27, DN40 U-PVC female threaded union, 28, DN40 U-PVC Pipe, 29,90 degree of U-PVC threeway 40/16/40,30, DN40 U-PVC elbows, 31, H-type grease trap, 31-1, the second pipeline section, 31-2,5 DN100 U-PVC tee pipe fittings, the first pipeline section of 31-3,31-4, third pipeline section, 31-6, the 4th pipeline section, 31-7, DN100 U-PVC pipe.
Specific embodiment
The utility model is described in detail with reference to the accompanying drawings and embodiments.
Oil removal structure, it is characterised in that: including adjusting oil separator 2, MBBR reaction tank 3, H-type grease trap 31;The H-type every Oily device 31 is divided on the basis of 31 central part of H-type grease trap across the wall adjusted oil separator 2 and MBBR reaction tank 3 Two parts are respectively uniformly distributed inside adjusting oil separator 2 and MBBR reaction tank 3.
Two parts of the H-type grease trap 31 pass through tee tube a 31-2 and 31-5 respectively, are connected to tee tube 31- The straight pipe of 2 and 31-5 upper and lower ends is constituted, and remaining two tube heads of two tee tubes 31-2 and 31-5 are 100mm by internal diameter U-PVC pipe 7 be docking together.
The straight pipe for being set to tee tube 31-2 and 31-5 upper and lower ends is U-PVC pipe, and pipe diameter internal diameter is 100mm。
The straight pipe for being set to tee tube upper and lower ends includes 4 sections, is the first pipeline section respectively according to water (flow) direction 31-3, the second pipeline section 31-1, third pipeline section 31-4 and the 4th pipeline section 31-6;The first, the 4th pipe (31-3,31-6) section is respectively connected to The lower end of two tee tube 31-2, the first pipeline section 31-3 and the 4th pipeline section 31-6 respectively with adjust oil separator 2, MBBR reaction tank 3 Bottom of pond plate upper surface be arranged gap;Second, third pipeline section (31-1,31-4) is respectively connected to the upper end of tee tube 31-5, Second pipeline section 31-1 and third pipeline section 31-4 is arranged with the lower surface for the pond top plate for adjusting oil separator 2, MBBR reaction tank 3 empty respectively Gap.
Contain collecting-tank 1 using six segmentation intelligent control medical waste water processors of above-mentioned oil removal structure, adjusts oil separator 2, MBBR reaction tanks, 3, MBR reaction tanks 4, clear water reserviors 5,6 six part of sterilization pool.Also containing with lower component: blower 7 measures dosing Pump 8, self priming pump 9, charging pump 10, backwashing pump 11, disinfection drug basin 14, mixer of liquid medicine 16;Blower 7 is to MBBR reaction tank 3, MBR reaction tank 4 carries out aeration oxygen supply;Self priming pump 9 acts on the water inlet of MBR reaction tank 4, is discharged through film process;Charging pump 10 Waste water, which enters, in pumping collecting-tank 1 adjusts oil separator (2), flows automatically to MBBR reaction tank 3;Backwashing pump 11 acts on clear water reserviors 5 Water inlet backwashes the film of MBR reaction tank 4;The connection metering dosing pump 8 of disinfection drug basin 14 is into mixer of liquid medicine 16 Dosing is measured, the water outlet of clear water reserviors 5 is mixed through drug in mixer of liquid medicine 16 flows into sterilization pool 6.
Cut dirty pond 15 and be respectively equipped at Inlet and outlet water and cut a dirty plate 20, cut dirty plate 21, and cut a dirty plate be located at MBBR reaction tank and The two sides of MBR reaction tank cell compartment plate 17, cut in 15 pond of dirty pond and are laid with quartz sand, and backwash tube 22 is arranged along bottom of pond portion, are returning Timing backwashes quartz sand under the action of stream pump 12, and reflux pump backwashing water comes from clear water reserviors 5;MBBR reaction tank 3 with 4 division wall bottom of MBR reaction tank is equipped with permeable hole 24.
Cut two layers of laying of quartz sand point in dirty pond, upper layer quartz sand 18 100~150mm of thickness, 4~6mm of diameter, lower layer's stone 19 50~80mm of thickness of sand, 8~12mm of diameter, the standard of the backwash tube 22 are ND40 × 4,23 spacing of permeable hole 100mm, aperture Ф 10mm;Section dirty plate 20 and section dirty plate 21 is 250mm high, distance between plates 500mm, and two plates are symmetrically positioned in MBBR reaction tank and 17 two sides of MBR reaction tank cell compartment plate.
The technique of the six segmentation intelligent control medical waste water processors processing medical waste water, it is characterised in that processing work Skill includes six sections of processes:
First segment: it is collected in waste water to be processed in ground lower sump 1, is pumped to through charging pump 10 and adjusts oil separator 2;
Second segment: it adjusts and is equipped with H-type automatic oil-separation device in oil separator.After sewage enters conditioning tank stabilization, grease is Through separating.By H-type automatic oil-separation device, oil is blocked in conditioning tank, water flows automatically to MBBR reaction tank 3;(oil concentrates discharge, place Reason)
Third section: being filled with moving-bed biofilm filler in MBBR reaction tank 3, bottom of pond is evenly distributed aerator, couples blower 7 Carry out aeration oxygen supply;
4th section: the water outlet of MBBR reaction tank 3, which flows through, cuts dirty plate 20 into cutting in dirty pond 15, is filtered place through quartz sand Reason, isolation impurity, are entered by permeable hole 24 and cut the dirty pond other side, after again flowing through quartz sand filtration processing, are flowed through and are cut dirty plate 20 Into in MBR reaction tank 4;It cuts 15 bottom of pond portion of dirty pond and sets recoil water pipe, under the action of reflux pump 12, periodically pump clear water reserviors 5 water inlets backwash quartz sand in pond, and flushing water is back in MBBR reaction tank 3 and MBR reaction tank 4, and waste water is through cutting dirt When pond is filtered, it the more can be collected the more more and formed the obstacle of aquaporin and form blocking by filtered impurity, be laid with the anti-of bottom of pond portion Jet water spout 22 is under source pressure and the impact of the joint of gas pressure, several permeable holes 23 on water pipe spray, and water is gentle Body blows off the impurity assembled in filtering ponds through quartz sand.
5th section: being equipped with curtain hollow-fibre membrane in MBR reaction tank 4 and combine, bottom of pond is evenly distributed aerator, couples blower 7 carry out aeration oxygen supply, and MBR reaction tank 4 is intake under the action of self priming pump 9, after curtain hollow-fibre membrane combined treatment, flow into Clear water reserviors 5;Periodically, the water inlet of clear water reserviors 5 backwashes film in MBR reaction tank 4 under the action of backwashing pump 11;
6th section: clear water reserviors 5 and 6 partition wall top of sterilization pool are equipped with pore, and pore is located at one end connection liquid medicine of sterilization pool 6 Mixer 16, the water outlet of clear water reserviors 5 flow to mixer of liquid medicine 16 by pore, sterilization pool 6 are entered after being sufficiently mixed with drug, is disappeared It is discharged after poisoning bacterium, drug is supplied by disinfection drug storage tank 14, and regulates and controls dose by metering dosing pump 8, in mixer of liquid medicine Disinfection drug is sodium hypochlorite, and the water of sterilized sterilization treatment is up to national healthcare wastewater discharge standard, stably reaching standard discharge.
Six segmentation intelligent control medical waste water processors measure 8 intelligent control of dosing pump: metering dosing pump 8 and self priming pump 9 Synchronously control;When self priming pump 9 is run, metering dosing pump 8 is run;When self priming pump 9 is closed, metering dosing pump 8 is closed;Measure dosing Pump 8 and the storage of disinfection drug basin 14 link: when the drug in disinfection drug basin 14 is lower than warning liquid level, measuring dosing pump 8 close, meanwhile, charging pump 10 also links closing.And synchronous alarm, alarm device beep, blinking red lamp;
Backwash tube intelligent control: being controlled using the time relay (micro computer), and backwash in every 4 hours is primary, and every time 20 Minute.
All automatic controls lead to self-control box 13, are uniformly controlled.
Six segmentation intelligent control medical waste water processor structure sizes are shown in Table 1, and hydraulic detention time is shown in Table 2:
The design table (m) of 1 geometric dimension of table
By taking the following treating capacity of 20 ton per days as an example
Standby: water outlet reaches national healthcare discharge of wastewater primary standard.
When handling 25 ton per day, expansion collecting-tank is other constant.
2 hydraulic detention time of table
The preferable specific embodiment of the above, only the utility model, but protection scope of the present invention is not limited to In this, anyone skilled in the art within the technical scope of the present disclosure, technical side according to the present invention Case and its inventive concept are subject to equivalent substitution or change, should be covered by the protection scope of the present invention.

Claims (9)

1. oil removal structure, it is characterised in that: including adjusting oil separator, MBBR reaction tank, H-type grease trap;The H-type grease trap is worn The wall between oil separator and MBBR reaction tank is overregulated, two parts are divided on the basis of H-type grease trap central part, it is equal respectively Even be distributed in is adjusted inside oil separator and MBBR reaction tank.
2. oil removal structure according to claim 1, it is characterised in that: two parts of the H-type grease trap pass through respectively One tee tube, the straight pipe for being connected to tee tube upper and lower ends are constituted, and remaining two tube heads of two tee tubes pass through internal diameter It is docking together for the U-PVC pipe of 100mm.
3. oil removal structure according to claim 2, it is characterised in that: the straight tube for being set to tee tube upper and lower ends Duan Junwei U-PVC pipe, pipe diameter internal diameter are 100mm.
4. oil removal structure according to claim 2, it is characterised in that: the straight tube for being set to tee tube upper and lower ends Section includes 4 sections, is the first pipeline section, the second pipeline section, third pipeline section and the 4th pipeline section respectively according to water (flow) direction;The first, the 4th pipe Section is respectively connected to the lower ends of two tee tubes, the first pipeline section and the 4th pipeline section respectively with the pond that adjusts oil separator, MBBR reaction tank Gap is arranged in the upper surface of bottom plate;Second, third pipeline section is respectively connected to the upper end of tee tube, the second pipeline section and third pipeline section point Gap is not set with the lower surface for the pond top plate for adjusting oil separator, MBBR reaction tank.
5. six segmentation intelligent control medical waste water processors of the oil removal structure with claim 1, it is characterised in that: including six sections Pond and component;Six sections of ponds include: collecting-tank, adjust oil separator, MBBR reaction tank, MBR reaction tank, clear water reserviors, disinfection Pond, the component include: blower, metering dosing pump, self priming pump, charging pump, backwashing pump, disinfection drug basin, liquid medicine mixing Device;It adjusts and is equipped with oil removal structure between oil separator and MBBR reaction tank, self-control box is arranged in described processor one end, and all components connect It is connected to self-control box.
6. six segmentations intelligent control medical waste water processor according to claim 5, it is characterised in that: processor further includes Dirty pond and reflux pump are cut, a dirty pond is cut and is respectively equipped with first section of dirty plate at Inlet and outlet water, second section of dirty plate, described first, second section Dirty plate is located at the two sides of MBBR reaction tank Yu MBR reaction tank cell compartment plate, cuts in the pond of dirty pond and is laid with quartz sand, along bottom of pond portion Backwash tube is set, and MBBR reaction tank and MBR reaction tank division wall bottom are equipped with permeable hole.
7. six segmentations intelligent control medical waste water processor according to claim 6, it is characterised in that: described cuts dirty pond Two layers of laying of middle quartz sand point, upper layer quartz sand 100~150mm of thickness, 4~6mm of diameter, lower layer's quartz sand thickness 50~ 80mm, 8~12mm of diameter, the standard of the backwash tube are ND40 × 4, permeable hole 22 spacing 100mm, aperture Ф 10mm; Described first section dirty plate and second section of dirty plate high 250mm, distance between plates 500mm, and two plates be symmetrically positioned in MBBR reaction tank and MBR reaction tank cell compartment plate two sides.
8. six segmentations intelligent control medical waste water processor according to claim 5, it is characterised in that: the MBR is anti- Ying Chizhong is combined equipped with curtain hollow-fibre membrane, and bottom of pond is evenly distributed aerator.
9. six segmentations intelligent control medical waste water processor according to claim 5, it is characterised in that: clear water reserviors and disinfection Pond partition wall top is equipped with pore, and pore is located at one end connection mixer of liquid medicine of sterilization pool.
CN201822128802.7U 2018-12-18 2018-12-18 Six segmentation intelligent control medical waste water processors and its oil removal structure Active CN209242876U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109354342A (en) * 2018-12-18 2019-02-19 大连格兰清水环境工程有限公司 Six segmentation intelligent control medical waste water processors

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109354342A (en) * 2018-12-18 2019-02-19 大连格兰清水环境工程有限公司 Six segmentation intelligent control medical waste water processors

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