CN204897638U - Effluent disposal system of pharmaceutical factory of traditional chinese medicine - Google Patents
Effluent disposal system of pharmaceutical factory of traditional chinese medicine Download PDFInfo
- Publication number
- CN204897638U CN204897638U CN201520426749.2U CN201520426749U CN204897638U CN 204897638 U CN204897638 U CN 204897638U CN 201520426749 U CN201520426749 U CN 201520426749U CN 204897638 U CN204897638 U CN 204897638U
- Authority
- CN
- China
- Prior art keywords
- pond
- chinese medicine
- traditional chinese
- pharmaceutical factory
- tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Abstract
The utility model discloses an effluent disposal system of pharmaceutical factory of traditional chinese medicine, its characterized in that: the pharmaceutical factory of traditional chinese medicine is connecting grille (1) in proper order, equalizing basin (2), PH regulating pondage (3), thoughtlessly congeal reaction tank (4), coagulating sedimentation tank (5), middle pond (6), UASB reactor (7), oxygen deficiency pond (8), contact oxidation tank (9), two heavy pond (10), middle pond (11), quartzy sand filter (12) and carbon filter (13), clean water basin (14), wherein coagulating sedimentation tank (5) are connected with charge device A (17), contact oxidation tank (9) are connected with fan (16), two heavy pond (10) are connected with charge device B (15), coagulating sedimentation tank (5) are connected with two heavy pond (10), quartzy sand filter (12), UASB reactor (7) are connected with concentrated pond (18), hydroextractor (19). The efficient handling pharmaceutical factory of traditional chinese medicine of this system waste water is reduced the incidence of disease, improves health, improves ecological environment.
Description
Technical field
The utility model belongs to field of Environment Protection waste disposal plant, relates to a kind of pharmaceutical factory of traditional Chinese medicine Waste Water Treatment particularly.
Background technology
Root, stem, the leaf of pharmaceutical factory of traditional Chinese medicine's waste water mainly plant, the bone, skin, angle etc. of animal, discharge waste water in the course of processing.The general water yield is little, also often cutout, but organic concentration is very high, most Gao Shikeda 6000mg/L.Its waste water main source has following five parts: (1) pre-treatment workshop wash, bubble medicine waste water; (2) extract workshop to rinse, decoct, boil waste water; (3) sewage between douching wheels; (4) a small amount of molasses water of formulating plant; (5) mill portion water coolant.
Waste water characteristic: (1) waste water COD
crchange in concentration is large, generally between 300-6000mg/L; (2) in sewage silt particle and the dregs of a decoction more, also containing floating matter; (3) in medicinal material, toxic substance is made into pulvis in the course of processing, does not enter in water, therefore nontoxic in waste water.
Summary of the invention
The purpose of this utility model is to provide a kind of pharmaceutical factory of traditional Chinese medicine Waste Water Treatment, and this system effectively processes pharmaceutical factory of traditional Chinese medicine's waste water, reduces disease, improves health, improve the ecological environment.
The purpose of this utility model and solve its technical problem underlying and realize by the following technical solutions: a kind of pharmaceutical factory of traditional Chinese medicine Waste Water Treatment, it is characterized in that, the pharmaceutical factory of traditional Chinese medicine connects grid 1, equalizing tank 2, pH adjustment pond 3, coagulation reaction tank 4, coagulative precipitation tank 5, intermediate pool 6, UASB reactor 7, anoxic pond 8, contact-oxidation pool 9, second pond 10, intermediate pool 11, quartz filter 12 and charcoal filter 13, clean water basin 14 successively, and wherein coagulative precipitation tank 5 is connected with chemicals dosing plant A17; Contact-oxidation pool 9 is connected with blower fan 16; Second pond 10 is connected with chemicals dosing plant B15; Coagulative precipitation tank 5 is connected with second pond 10, quartz filter 12; UASB reactor 7 is connected with concentration basin 18, water extracter 19.
Described UASB reactor 7 is connected with desulphurization system by gas holder.
The built-in high-performance bio elastic filler of described anoxic pond 8.
Described contact-oxidation pool 9 is made up of pond body, filler, water-distributing device and oxygenic aeration system.
Described second pond 10 is designed to inclined tube-type settling tank.
The utility model compared with prior art has obvious advantage and beneficial effect.From above technical scheme, the utility model has following characteristics: while utilizing refuse, can also bring economic benefit, tally with the national condition.Although waste water treatment project does not directly produce economic benefit; but project implementation has wide influence by the protection of locality; make the development of industry and inhabitation industry not by the restriction of environment; socio-economic development and Environmental Protection Target are coordinated; to huge benefit be brought to local economy, be mainly manifested in the following aspects:
1) increment of land price;
2) reduce disease, improve health;
3) improve the ecological environment.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is native system pharmaceutical factory of traditional Chinese medicine sewage treatment technology process figure.
Mark in figure: 1, grid, 2, equalizing tank, 3, pH adjusts pond, 4, coagulation reaction tank, 5, coagulative precipitation tank, 6, intermediate pool, 7, UASB reactor, 8, anoxic pond, 9, contact-oxidation pool, 10, second pond, 11, intermediate pool, 12, quartz filter, 13, charcoal filter, 14, clean water basin, 15, chemicals dosing plant B, 16, blower fan, 17, chemicals dosing plant A, 18, concentration basin, 19, water extracter.
Embodiment
Below in conjunction with accompanying drawing and preferred embodiment, to according to a kind of pharmaceutical factory of traditional Chinese medicine Waste Water Treatment system embodiment, feature and the effect thereof that the utility model proposes, be described in detail as follows.
See Fig. 1-2, a kind of pharmaceutical factory of traditional Chinese medicine Waste Water Treatment, it is characterized in that, the pharmaceutical factory of traditional Chinese medicine connects grid 1, equalizing tank 2, pH adjustment pond 3, coagulation reaction tank 4, coagulative precipitation tank 5, intermediate pool 6, UASB reactor 7, anoxic pond 8, contact-oxidation pool 9, second pond 10, intermediate pool 11, quartz filter 12 and charcoal filter 13, clean water basin 14 successively, and wherein coagulative precipitation tank 5 is connected with chemicals dosing plant A17; Contact-oxidation pool 9 is connected with blower fan 16; Second pond 10 is connected with chemicals dosing plant B15; Coagulative precipitation tank 5 is connected with second pond 10, quartz filter 12; UASB reactor 7 is connected with concentration basin 18, water extracter 19.
Described UASB reactor 7 is connected with desulphurization system by gas holder.
The built-in high-performance bio elastic filler of described anoxic pond 8.
Described contact-oxidation pool 9 is made up of pond body, filler, water-distributing device and oxygenic aeration system.
Described second pond 10 is designed to inclined tube-type settling tank.
Native system sewage treatment technology process:
A, grid
Factory effluent is collected through pipeline and is entered in sewage works, and sewage works leading portion arranges grid to remove larger suspended particulate matter in sewage, reduces subsequent treatment process load.
B, equalizing tank
Because wastewater flow fluctuation is comparatively large, excessive change will be unfavorable for the normal running of waste water disposal facility equipment and ensure treatment effect.Operation system setting equalizing tank, its object is to equal to sewage enforcement water quality and quantity and regulates, ensureing Sewage treatment systems stable smooth operation, ensure total system qualified discharge.
C, UASB reactor
In waste water, first the macromolecule organic of difficult degradation carries out acidification hydrolization at this, formation is easy to biodegradable low molecule organic matter, polyprotonic acid is converted into unit acid, and be oxidized to ammonia nitrogen, sulfide and carbon monoxide etc., then the aerogenesis stage is entered, some unit acid is converted into biogas, and biogas is recycled after entering desulphurization system after being collected by gas holder.
D, A level biological treatment tank (anoxic pond)
1) object is set:
Sewage is mixed further, to make full use of in pond high-performance bio elastic filler as bacteria carrier, by facultative microbe, dissolved organic matter difficult in sewage is converted into resolvability organism, larger molecular organics is hydrolyzed into small organic molecule, be beneficial to the further oxygenolysis of rear road O level biological treatment tank, pass through the nitre charcoal nitrogen of backflow simultaneously under the effect of nitrifier, can part nitrification and denitrification be carried out, remove ammonia nitrogen.
Mixed liquid recycle ratio is that 150%(is arranged on contact-oxidation pool end), arrange two, the using and the reserved,
2) design feature:
Built-in high-performance bio elastic filler, has again acidication function, may be adjusted to as O level bio-oxidation pond simultaneously, to increase the biochemical residence time, improves processing efficiency.
E, O level biological treatment tank (biological contact oxidation pond)
1) object is set:
This pond is the core of this sewage disposal, divide two sections, the last period is under higher organic loading, biochemical degradation under jointly being participated in by the microflora being attached to a large amount of different generas on filler and adsorption, remove the various organic substances in sewage, the organic content in sewage is significantly reduced.Back segment is when organic loading is lower, and by the effect of nitrifier, the ammonia nitrogen under the condition of oxygen amount abundance in degradation of sewage, also makes the COD value in sewage be reduced to lower level simultaneously, sewage is purified.
2) design feature:
This pond is made up of parts such as pond body, filler, water-distributing device and oxygenic aeration systems.
This pond, based on biomembrance process, has the feature of activated sludge process concurrently.
In pond, filler adopts elastic stereo combined stuffing, and it is large that this filler has specific surface area, long service life, the corrosion-resistant not conglomeration blocking of easy to be filmed.Filler is freely unfolded in water, and to the multi-level cutting of underwater bubble do, more relatively add aeration effect, filler becomes cage to install, and dismounting, maintenance are conveniently.
Secondary is divided in this pond, makes water quality be degraded into gradient, reaches good treatment effect, and design simultaneously adopts the measure of corresponding water conservancy diversion turbulent flow, makes global design more rationalization.
In pond, aerating pipelines selects high-quality ABS to manage, corrosion-resistant.Aeration head selects micro porous aeration head, does not block, and coefficient of oxygen utilization is high.
F, second pond
1) object is set:
Carry out solid-liquid separation and remove in biochemistry pool the microbial film and suspended sludge that peel off, sewage is really purified.
2) design feature:
Be designed to inclined tube-type settling tank, its sludge degradation is effective.
Adopt V-notch weir water outlet, make water outlet effect stability.
G, quartz filter and charcoal filter
Object is set:
Chlorine residue in COD, BOD, SS, microorganism, colloid, particle, suspended impurity, water, colourity and stink in further removal water, reach emission standard and enter qualified discharge pond.
Native system water outlet operative norm: the related request of " Chinese medicine class pharmaceutical industry pollution discharge standard " (GB21906-2008) table 2.Use native system Inlet and outlet water water-quality guideline, see the following form,
Table 1-1 Inlet and outlet water water-quality guideline table look-up
| Project | Influent quality index | Effluent quality index |
| PH(zero dimension) | 6~9 | 6~9 |
| COD cr（mg/L） | ≤2800 | ≤100 |
| BOD 5（mg/L） | ≤1200 | ≤20 |
| SS（mg/L） | ≤450 | ≤50 |
| Colourity | 400 times | 50 times |
The above, it is only preferred embodiment of the present utility model, not any pro forma restriction is done to the utility model, anyly do not depart from technical solutions of the utility model content, the any simple modification done above embodiment according to technical spirit of the present utility model, equivalent variations and modification, all still belong in the scope of technical solutions of the utility model.
Claims (5)
1. pharmaceutical factory of traditional Chinese medicine's Waste Water Treatment, it is characterized in that: the pharmaceutical factory of traditional Chinese medicine connects grid (1), equalizing tank (2), pH adjustment pond (3), coagulation reaction tank (4), coagulative precipitation tank (5), intermediate pool (6), UASB reactor (7), anoxic pond (8), contact-oxidation pool (9), second pond (10), intermediate pool (11), quartz filter (12) and charcoal filter (13), clean water basin (14), wherein coagulative precipitation tank (5) and chemicals dosing plant A(17 successively) be connected; Contact-oxidation pool (9) is connected with blower fan (16); Second pond (10) and chemicals dosing plant B(15) be connected; Coagulative precipitation tank (5) is connected with second pond (10), quartz filter (12); UASB reactor (7) is connected with concentration basin (18), water extracter (19).
2. a kind of pharmaceutical factory of traditional Chinese medicine as claimed in claim 1 Waste Water Treatment, is characterized in that: described UASB reactor (7) is connected with desulphurization system by gas holder.
3. a kind of pharmaceutical factory of traditional Chinese medicine as claimed in claim 1 Waste Water Treatment, is characterized in that: the built-in high-performance bio elastic filler of described anoxic pond (8).
4. a kind of pharmaceutical factory of traditional Chinese medicine as claimed in claim 1 Waste Water Treatment, is characterized in that: described contact-oxidation pool (9) is made up of pond body, filler, water-distributing device and oxygenic aeration system.
5. a kind of pharmaceutical factory of traditional Chinese medicine as claimed in claim 1 Waste Water Treatment, is characterized in that: described second pond (10) is designed to inclined tube-type settling tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520426749.2U CN204897638U (en) | 2015-06-19 | 2015-06-19 | Effluent disposal system of pharmaceutical factory of traditional chinese medicine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520426749.2U CN204897638U (en) | 2015-06-19 | 2015-06-19 | Effluent disposal system of pharmaceutical factory of traditional chinese medicine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204897638U true CN204897638U (en) | 2015-12-23 |
Family
ID=54919830
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520426749.2U Expired - Fee Related CN204897638U (en) | 2015-06-19 | 2015-06-19 | Effluent disposal system of pharmaceutical factory of traditional chinese medicine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204897638U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106630275A (en) * | 2016-12-09 | 2017-05-10 | 宜兴市苏嘉环保设备有限公司 | Zero-discharge treatment process for pickling passivation wastewater |
-
2015
- 2015-06-19 CN CN201520426749.2U patent/CN204897638U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106630275A (en) * | 2016-12-09 | 2017-05-10 | 宜兴市苏嘉环保设备有限公司 | Zero-discharge treatment process for pickling passivation wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106167340B (en) | AAO continuous flow aerobic granular sludge nitrogen and phosphorus removal process and system | |
| CN105585122B (en) | A kind of high-ammonia nitrogen low C/N is than waste water treatment system and treatment process | |
| CN103880248B (en) | A kind of coking wastewater processing system and treatment process | |
| CN103241908B (en) | Large-scale pig farm wastewater treatment method | |
| CN108046518B (en) | Enhanced nitrogen and phosphorus removal device and method for low-carbon source sewage | |
| CN103496787A (en) | Biochemical simultaneous phosphorus and nitrogen removal method of domestic sewage | |
| CN103896442A (en) | Pig farm wastewater treatment method | |
| CN105366811A (en) | Sewage treatment plant sludge treatment system, and treatment method thereof | |
| CN110395851A (en) | High aititude urban wastewater treatment method based on nitrogen phosphorus capture and whole process autotrophic denitrification | |
| CN104609651B (en) | A kind of Large-scale pig farm advanced waste treatment system | |
| CN105366889B (en) | A kind of town sewage high standard denitrification dephosphorization system without additional carbon | |
| WO2022170787A1 (en) | Device and method for synchronously treating sewage and sludge by using step feed shortcut nitrification-anaerobic ammonia oxidation combination | |
| CN209081680U (en) | Continuous flow municipal sewage nitrification and nitrogen rejection facility | |
| CN109095727B (en) | Denitrification and carbon removal device and method for high-ammonia-nitrogen low-carbon-nitrogen-ratio sewage | |
| CN204981512U (en) | Pig farm effluent treatment plant | |
| CN114291942A (en) | Catalytic electrolysis municipal sewage purification system and purification method | |
| CN110104873A (en) | Municipal wastewater advanced treatment apparatus and its method | |
| CN203582658U (en) | Multi-stage aeration reclaimed water treatment system for medium and small towns | |
| CN113501620A (en) | Municipal sewage purification and regeneration system and method based on anaerobic and electrolytic denitrification | |
| CN109231673B (en) | A/O combined micro-electric field-Fe/C reinforced dephosphorization device and application thereof | |
| CN202099169U (en) | Device for advanced treatment of secondary effluent in municipal sewage plant | |
| CN204897638U (en) | Effluent disposal system of pharmaceutical factory of traditional chinese medicine | |
| CN201268653Y (en) | Advanced treatment apparatus for wastewater containing ammonia nitrogen and phosphor | |
| CN106986506B (en) | Integrated industrial water purifier | |
| CN105502660A (en) | Reverse-flow type biological contact device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151223 Termination date: 20190619 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |