CN109019972A - A kind of bath sewage processing unit and method - Google Patents
A kind of bath sewage processing unit and method Download PDFInfo
- Publication number
- CN109019972A CN109019972A CN201810975048.2A CN201810975048A CN109019972A CN 109019972 A CN109019972 A CN 109019972A CN 201810975048 A CN201810975048 A CN 201810975048A CN 109019972 A CN109019972 A CN 109019972A
- Authority
- CN
- China
- Prior art keywords
- tank
- sewage
- filter device
- pool
- coagulative precipitation
- 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.)
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Links
- 239000010865 sewage Substances 0.000 title claims abstract description 53
- 238000012545 processing Methods 0.000 title claims abstract description 16
- 238000000034 method Methods 0.000 title claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 230000001112 coagulating effect Effects 0.000 claims abstract description 25
- 238000001556 precipitation Methods 0.000 claims abstract description 21
- 230000003750 conditioning effect Effects 0.000 claims abstract description 20
- 230000015271 coagulation Effects 0.000 claims abstract description 17
- 238000005345 coagulation Methods 0.000 claims abstract description 17
- 239000010802 sludge Substances 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 14
- 230000001954 sterilising effect Effects 0.000 claims abstract description 12
- 230000029087 digestion Effects 0.000 claims abstract description 11
- 239000002351 wastewater Substances 0.000 claims abstract description 10
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000006004 Quartz sand Substances 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- 238000004062 sedimentation Methods 0.000 claims description 8
- 239000000701 coagulant Substances 0.000 claims description 6
- 238000011001 backwashing Methods 0.000 claims description 3
- 238000003672 processing method Methods 0.000 claims description 3
- 239000013049 sediment Substances 0.000 claims description 3
- 239000006228 supernatant Substances 0.000 claims description 3
- 230000032258 transport Effects 0.000 claims description 3
- 230000009885 systemic effect Effects 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 3
- 238000003287 bathing Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 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
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of bath sewage processing unit and methods, belong to technical field of waste water processing.In order to handle, water is larger, the lower bath sewage of pollution level achievees the purpose that reuse, the inventive system comprises sequentially connected first filter device, conditioning tank, coagulation reaction tank, coagulative precipitation tank, intermediate pool, the second filter device, sterilization pool and discharge pond, the mud discharging mouths of coagulative precipitation tank to connect with sludge digestion tank.The present invention treated sewage meets the requirement of the non-systemic contact of " reclaimed water reuse is in the water standard of landscape water body " CJ/T95-2000 human body, and device operation is safe reliable, energy-efficient, economical rationality.
Description
Technical field
The invention belongs to technical field of waste water processing, more specifically to a kind of bath sewage processing unit and method.
Background technique
With the continuous development of tourist industry, the Quantity of holiday village is also increasing, and consequent is different type
The operational process such as villa, hotel, dining room in a certain amount of sanitary sewage that discharges, wherein including bath sewage.Bath sewage is
A kind of water is larger, and pollution level is low, convenient for the high-quality water resource of reclaimed water of recycling.In order to preferably utilize water resource, bathing
Sewage needs to be handled by simple and economic method, to realize recycling.
Summary of the invention
Goal of the invention: in view of the above-mentioned problems existing in the prior art, the purpose of the present invention is to provide a kind for the treatment of effects
Stabilization, economical rationality, bath sewage easy to operate processing unit, another object of the present invention is to provide use the device
Bath sewage processing method.
Technical solution: to solve the above-mentioned problems, the technical solution adopted in the present invention is as follows:
The present invention relates to a kind of bath sewage processing unit, including it is the first filter device, conditioning tank, coagulation reaction tank, mixed
Solidifying sedimentation basin, intermediate pool, the second filter device, sterilization pool, discharge pond and sludge digestion tank, first filter device,
Conditioning tank, coagulation reaction tank, coagulative precipitation tank, intermediate pool, the second filter device, sterilization pool and discharge pond are sequentially connected, institute
The mud discharging mouth for the coagulative precipitation tank stated is connect with the sludge digestion tank.
It further include accident pool, the discharge pond is connect with the accident pool, the accident pool and the adjusting
Pond connection.
It further include surmounting pipe, the conditioning tank is connect by the pipe that surmounts with the discharge pond.
First filter device includes twice grid, and first of grid spacing is 6mm, and second grid spacing is
1mm。
The coagulative precipitation tank is perpendicular stream sediment structure.
Second filter device is quartz sand filter tank.
Preferably, the diameter of the quartz sand filter tank is 800mm, and quantity is 2, in the quartz sand filter tank
Equipped with backwashing pump.
The invention further relates to a kind of bath sewage processing methods using above-mentioned apparatus, comprising the following steps:
(1) bath sewage is filtered by the first filter device, then drains into conditioning tank；
(2) homogenizing that sewage water quantity and quality is carried out in conditioning tank is adjusted, and sewage is then discharged into coagulation reaction tank；
(3) dosing coagulant into coagulation reaction tank, sewage is sufficiently mixed with coagulant react after enter coagulative precipitation tank；
(4) sewage carries out coagulating sedimentation, gained supernatant overflow to intermediate pool in coagulative precipitation tank, and intermediate pool goes out
Water enters the second filter device, and the sludge of coagulative precipitation tank is periodically discharged into sludge digestion tank, transports outward after sludge digestion, concentration；
(5) enter sterilization pool after sewage being filtered, adsorbed through the second filter device；
(6) it is discharged into discharge pond after the sterilized pond disinfection of sewage, below standard waste water, which enters conditioning tank by accident pool, to carry out
Reprocessing, waste water up to standard carry out reuse or discharge.
Residence time of the sewage in conditioning tank is 8h, and the residence time in coagulation reaction tank is 15min,
Residence time in coagulative precipitation tank is 1.5h, and the residence time in intermediate pool is 1h, the residence time in sterilization pool
For 1.5h.
The utility model has the advantages that compared with the prior art, the present invention is handled bath sewage using physical chemistry method, and treated
Sewage meets the requirement of the non-systemic contact of " reclaimed water reuse is in the water standard of landscape water body " CJ/T 95-2000 human body, can
As greening water, high treating effect, device operation is safe reliable, energy-efficient, economical rationality.At bath sewage of the invention
Reason device and method have not only widened the Processing tecchnics of this kind of sewage, but also also have certain borrow to the improvement of other sewage
Mirror meaning.
Detailed description of the invention
Fig. 1 is bath sewage processing unit schematic diagram of the invention.
Specific embodiment
The present invention is further described below combined with specific embodiments below.
Embodiment 1
A kind of bath sewage processing unit of the present embodiment, as shown in Figure 1, include sequentially connected first filter device,
Conditioning tank, coagulation reaction tank, coagulative precipitation tank, intermediate pool, the second filter device, sterilization pool, discharge pond and accident pool, coagulation
The mud discharging mouth of sedimentation basin is connect with sludge digestion tank, and discharge pond is connect with accident pool, and accident pool is connect with conditioning tank.It adjusts
Be additionally provided in pond directly with discharge pond connect surmount pipe, if the bath sewage processing unit be not normally functioning or sewage without
When need to handle, sewage can also be by surmounting pipe overflow to the discharge of discharge pond.
Wherein: the first filter device is provided with twice grid, and first of grid spacing is 6mm, and second grid spacing is
1mm。
Coagulative precipitation tank is using perpendicular stream sediment structure, and the sedimentation time is short, good separating effect, and occupied area is few.
Second filter device is quartz sand filter tank, and the diameter of quartz sand filter tank is 800mm, and quantity is 2, quartz sand
Backwashing pump is equipped in filtering ponds.
The present embodiment is handled sewage using above-mentioned apparatus, and handled object is the bathing dirt for being mixed with sanitary sewage
The index of correlation of water, water quality and quantity is shown in Table 1.
Water quality, the water of waste water handled by 1 embodiment 1 of table
The step of processing are as follows:
(1) bath sewage is filtered by the first filter device, removes bulky grain sundries and finely ground particle substance therein, so
After be discharged into conditioning tank；
(2) homogenizing for carrying out sewage water quantity and quality is adjusted, and sewage is then promoted to coagulation reaction tank by elevator pump；
(3) dosing coagulant into coagulation reaction tank, make sewage be sufficiently mixed with coagulant react after enter coagulating sedimentation
Pond；
(4) sewage carries out coagulating sedimentation in coagulative precipitation tank, gained supernatant by overflow weir overflow to intermediate pool,
Intermediate pool water outlet is lifted by high-pressure hydraulic pump to the second filter device, and the sludge of coagulative precipitation tank is periodically discharged into sludge and disappears
Change pond, is acted on by prolonged sludge digestion, the sludge being finally concentrated is handled by sanitation cart outward transport；
(5) sewage is in the second filter device, by the retention, filtering, suction-operated of quartz sand, by objects such as most of SS
Matter removes, and then water outlet enters sterilization pool；
(6) sewage is discharged into discharge pond after ozonization, and below standard waste water, which enters conditioning tank by accident pool, to carry out again
Processing, waste water up to standard carry out reuse or discharge.
Wherein, residence time of the sewage in conditioning tank is 8h, and the residence time in coagulation reaction tank is 15min,
Residence time in coagulative precipitation tank is 1.5h, and the residence time in intermediate pool is 1h, the residence time in sterilization pool
For 1.5h.
The correlation water index of sewage is shown in Table 2 after processing, it can be seen that final outflow water water quality fully meets " recycled water time
Water standard for landscape water body " the non-systemic contact of CJ/T 95-2000 human body requirement.
The water quality indicator of 2 embodiment of table, 1 processed waste water
Claims (9)
1. a kind of bath sewage processing unit, which is characterized in that including the first filter device, conditioning tank, coagulation reaction tank, coagulation
Sedimentation basin, intermediate pool, the second filter device, sterilization pool, discharge pond and sludge digestion tank, first filter device are adjusted
Section pond, coagulation reaction tank, coagulative precipitation tank, intermediate pool, the second filter device, sterilization pool and discharge pond are sequentially connected, described
The mud discharging mouth of coagulative precipitation tank connect with the sludge digestion tank.
2. the apparatus according to claim 1, which is characterized in that it further include accident pool, the discharge pond and the thing
Gu Chi connection, the accident pool are connect with the conditioning tank.
3. the apparatus according to claim 1, which is characterized in that further include surmounting pipe, the conditioning tank passes through described
Surmount pipe to connect with the discharge pond.
4. the apparatus according to claim 1, which is characterized in that first filter device includes twice grid, and first
Road grid spacing is 6mm, and second grid spacing is 1mm.
5. the apparatus according to claim 1, which is characterized in that the coagulative precipitation tank is perpendicular stream sediment structure.
6. the apparatus according to claim 1, which is characterized in that second filter device is quartz sand filter tank.
7. device according to claim 6, which is characterized in that the diameter of the quartz sand filter tank is 800mm, quantity
It is 2, backwashing pump is equipped in the quartz sand filter tank.
8. a kind of bath sewage processing method using such as any one of claim 1~7 described device, which is characterized in that packet
Include following steps:
(1) bath sewage is filtered by the first filter device, then drains into conditioning tank；
(2) homogenizing that sewage water quantity and quality is carried out in conditioning tank is adjusted, and sewage is then discharged into coagulation reaction tank；
(3) dosing coagulant into coagulation reaction tank, sewage is sufficiently mixed with coagulant react after enter coagulative precipitation tank；
(4) sewage carries out coagulating sedimentation, gained supernatant overflow to intermediate pool in coagulative precipitation tank, intermediate pool be discharged into
Enter the second filter device, the sludge of coagulative precipitation tank is periodically discharged into sludge digestion tank, transports outward after sludge digestion, concentration；
(5) enter sterilization pool after sewage being filtered, adsorbed through the second filter device；
(6) it is discharged into discharge pond after the sterilized pond disinfection of sewage, below standard waste water enters conditioning tank by accident pool and located again
Reason, waste water up to standard carry out reuse or discharge.
9. according to the method described in claim 8, it is characterized in that, residence time of the sewage in conditioning tank be 8h,
Residence time in coagulation reaction tank is 15min, and the residence time in coagulative precipitation tank is 1.5h, in intermediate pool
Residence time is 1h, and the residence time in sterilization pool is 1.5h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810975048.2A CN109019972A (en) | 2018-08-24 | 2018-08-24 | A kind of bath sewage processing unit and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810975048.2A CN109019972A (en) | 2018-08-24 | 2018-08-24 | A kind of bath sewage processing unit and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109019972A true CN109019972A (en) | 2018-12-18 |
Family
ID=64627535
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810975048.2A Pending CN109019972A (en) | 2018-08-24 | 2018-08-24 | A kind of bath sewage processing unit and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109019972A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109574322A (en) * | 2019-01-17 | 2019-04-05 | 四川鸿鹏新材料有限公司 | A kind of waste water treatment process |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203392984U (en) * | 2013-08-13 | 2014-01-15 | 河北龙淼环保工程有限公司 | Bio-contact oxidation integrated sewage treatment system |
| CN203845896U (en) * | 2014-05-15 | 2014-09-24 | 张龙助 | Integrated sewage treating and reusing system for dormitory buildings |
| CN107285545A (en) * | 2017-07-25 | 2017-10-24 | 杭州绿色环保技术开发有限公司 | A kind of cadmium ammonia waste water technique of zero discharge of thin-film solar cells production line |
| CN208762312U (en) * | 2018-08-24 | 2019-04-19 | 江苏开放大学（江苏城市职业学院） | A kind of device being exclusively used in bath sewage processing |
-
2018
- 2018-08-24 CN CN201810975048.2A patent/CN109019972A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203392984U (en) * | 2013-08-13 | 2014-01-15 | 河北龙淼环保工程有限公司 | Bio-contact oxidation integrated sewage treatment system |
| CN203845896U (en) * | 2014-05-15 | 2014-09-24 | 张龙助 | Integrated sewage treating and reusing system for dormitory buildings |
| CN107285545A (en) * | 2017-07-25 | 2017-10-24 | 杭州绿色环保技术开发有限公司 | A kind of cadmium ammonia waste water technique of zero discharge of thin-film solar cells production line |
| CN208762312U (en) * | 2018-08-24 | 2019-04-19 | 江苏开放大学（江苏城市职业学院） | A kind of device being exclusively used in bath sewage processing |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109574322A (en) * | 2019-01-17 | 2019-04-05 | 四川鸿鹏新材料有限公司 | A kind of waste water treatment process |
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| PB01 | Publication | ||
| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181218 |