CN103755000B - A kind of High-efficiency sewage treatment separator - Google Patents
A kind of High-efficiency sewage treatment separator Download PDFInfo
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- CN103755000B CN103755000B CN201410039607.0A CN201410039607A CN103755000B CN 103755000 B CN103755000 B CN 103755000B CN 201410039607 A CN201410039607 A CN 201410039607A CN 103755000 B CN103755000 B CN 103755000B
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Abstract
The present invention relates to waste disposal plant, particularly a kind of High-efficiency sewage treatment separator.It comprises water inlet pipe, water inlet pipe described in it is communicated with at least more than one Pressure chamber, described Pressure chamber is connected with the pressure control device for control pressure size, described Pressure chamber is connected with materialization medicament and adds pipe, and described water inlet pipe and described materialization medicament add pipe and be arranged in parallel and be jointly connected and gather to described Pressure chamber import.By vibrational power flow of the present invention, adding medicine while water feeding of water pump, as alkali, acid, flocculation agent and some specific material; Arrive Pressure chamber after carrying out vigorous reaction, then require discharge according to former water or water outlet or carry out advanced treatment, pre-treatment in early stage and last advanced treatment can be carried out to all kinds of sewage; Suspended substance and COD clearance high.
Description
Technical field
The present invention relates to waste disposal plant, particularly a kind of High-efficiency sewage treatment separator.
Background technology
In traditional sewage treatment process (especially when pre-treatment in early stage and ultimate depth process), add medication amount large, long reaction time, drug diffusion, infiltration, mixing are uneven, and a lot of facility function singleness.In whole sewage treatment process, facilities and equipment is huge, and floor space is many, and enterprise investment is large, and thus some aspect limits the development of enterprise.CN102807260A (2012-12-5) discloses a kind of dross dehydration integration air-float machine, but this device still can not solve these problems highlighted.
Summary of the invention
The object of this invention is to provide a kind of can to multiple types sewage carry out pre-treatment in early stage and/or last advanced treatment, suspended substance and the high High-efficiency sewage treatment separator of COD clearance.
Above-mentioned technical purpose of the present invention is achieved by the following technical programs:
A kind of High-efficiency sewage treatment separator, comprise water inlet pipe, water inlet pipe described in it is communicated with at least more than one Pressure chamber, described Pressure chamber is connected with the pressure control device for control pressure size, described Pressure chamber is connected with materialization medicament and adds pipe, and described water inlet pipe and described materialization medicament add pipe and be arranged in parallel and be jointly connected and gather to described Pressure chamber import.
By vibrational power flow of the present invention, adding medicine while water feeding of water pump, as alkali, acid, flocculation agent and some specific material; Arrive Pressure chamber after carrying out vigorous reaction, then require discharge according to former water or water outlet or carry out advanced treatment.This device at municipal wastewater, wastewater from chemical industry, butcher, food, papermaking, weaving, printing and dyeing, leather, plating, refining of petroleum, man-made fiber, paint, rubber, medicine and other fields have sewage disposal purposes widely, comprise fish pond and remove suspended substance, oxygenation and sterilization, can carry out pre-treatment in early stage and last advanced treatment to all kinds of sewage; Suspended substance and COD clearance high.
As preferably, described pressure control device comprises and to be arranged in parallel with described water inlet pipe and the blast main communicated and be arrangeding in parallel and the penstock communicated with described blast main.
According to actual water quality and manipulation require control pressure size, reach suspended substance and the high requirement of COD clearance.
As preferably, described Pressure chamber comprises the first step Pressure chamber, second stage Pressure chamber and the third stage Pressure chamber that connect setting successively up and down, described first step Pressure chamber is externally connected with first step outlet pipe, described second stage Pressure chamber is externally connected with second stage outlet pipe, and described third stage Pressure chamber is externally connected with third stage outlet pipe; Described first step outlet pipe, second stage outlet pipe and third stage outlet pipe be arranged in parallel and are jointly communicated to rising pipe; Described first step outlet pipe, second stage outlet pipe, third stage outlet pipe and described rising pipe are respectively arranged with first step valve, second stage valve, third stage valve and flowing water Valve.
Water feeding of water pump is to first step Pressure chamber, and adding medicine while water inlet, as alkali, acid, flocculation agent and some specific material; First step Pressure chamber is arrived after carrying out vigorous reaction, add coagulant aids or advanced treatment agent simultaneously, as arrived first step Pressure chamber (or release) after the vigorous reactions such as ferrous iron, hydrogen peroxide, Powdered Activated Carbon, carry out neutralizing or entering air-floating apparatus after other reactions, by air-floating apparatus, remove dirt (as SS, gelatinoid, oils etc.).
As preferably, described Pressure chamber is 316L stainless steel rectangular box structure.
Body structure of the present invention can the high temperature of acidproof and 100 degrees centigrade, can according to the free design volume for the treatment of capacity and flow.
As preferably, bottom described Pressure chamber, be connected with water outlet high-density microvesicle jet apparatus.
More preferably, described water outlet high-density microvesicle jet apparatus is jet-flow air-floatation apparatus.
Further preferably, the described jet-flow air-floatation apparatus dissolving that comprises at least plural liquid-gas jet device and communicate with described liquid-gas jet device.
As preferably, described water outlet high-density microvesicle jet apparatus is externally connected with microfiltration membrane treatment unit or ultrafiltration membrane treatment device or film bioreactor device.
According to actual raw water quality and effluent quality requirement, microfiltration membrane treatment unit or ultrafiltration membrane treatment device or film bioreactor device are set further, meet the demand of Water condition occasion.
In sum, the present invention has following beneficial effect: by vibrational power flow of the present invention, adding medicine while water feeding of water pump, as alkali, acid, flocculation agent and some specific material; Arrive Pressure chamber after carrying out vigorous reaction, then require discharge according to former water or water outlet or carry out advanced treatment.This device at municipal wastewater, wastewater from chemical industry, butcher, food, papermaking, weaving, printing and dyeing, leather, plating, refining of petroleum, man-made fiber, paint, rubber, medicine and other fields have sewage disposal purposes widely, comprise fish pond and remove suspended substance, oxygenation and sterilization, can carry out pre-treatment in early stage and last advanced treatment to all kinds of sewage; Suspended substance and COD clearance high.
Accompanying drawing explanation
Fig. 1 is one of High-efficiency sewage treatment separator schematic diagram of the present invention;
Fig. 2 is High-efficiency sewage treatment separator schematic diagram two of the present invention.
Embodiment
Below in conjunction with accompanying drawing, the present invention is described in further detail.
As shown in Figure 1, High-efficiency sewage treatment separator comprises water inlet pipe 1, water inlet pipe 1 is communicated with at least more than one Pressure chamber 2, Pressure chamber 2 is connected with the pressure control device 3 for control pressure size, Pressure chamber 2 is connected with materialization medicament and adds pipe 4, and water inlet pipe 1 and materialization medicament add pipe 4 and be arranged in parallel and be jointly connected and gather to Pressure chamber import 20.Pressure chamber is 316L stainless steel rectangular box structure.
Adopt apparatus of the present invention to process dyeing waste water, the results are shown in Table 1.
As shown in Figure 2, pressure control device 3 can be such as comprise be arrangeding in parallel with water inlet pipe 1 and the blast main 31 communicated and be arrangeding in parallel with blast main and the penstock 32 communicated.
Pressure chamber can be one, more than two or three, can take the circumstances into consideration to select according to the different situations of raw water quality.Common sewage selects the device with two Pressure chamber, adopts three stage pressure bin device process to needing the sewage of special advanced treatment.
Such as Xinchang is new and becomes sewage plant to contain the detection of high density orange pectin wastewater separating resulting, and COD drops to 1985mgL from 7800mgL.The former water COD of ether of cellulose 35000 drops to less than 6000.Wash bottle wastewater drops to 200 from 1700.Starch wastewater drops to about 300 from 1600.Pharmacy waste water drops to 1200 from 26000.Electronic printing, washing lotion drops to 320 from 5580.Coal tar drops to 4000 from 12000, and above result is only flash liberation, also can separating for several times again, and degraded is removed more.
General needs 2 ~ 5 kilograms of pressure in Pressure chamber.Materialization medicament adds the dosage in pipe 4, according to water quality as potential of hydrogen is determined.Sometimes must according to processing requirements, the acid-base condition of Ti Gong Xia mono-Walk, instead of neutral, then adjustment gathers aluminium or ferrous sulfate, aluminium iron sulfate, potassium aluminium sulfate, pX(flocculation agent) etc., consumption as required, can from 10pPML to 900PPmL not etc., the general proportioning of acid amides is within 3 percent ~ 10, then adds as required in waste water.
Such as Pressure chamber 2 comprises the first step Pressure chamber 21, second stage Pressure chamber 22 and the third stage Pressure chamber 23 that connect setting successively up and down, first step Pressure chamber 21 is externally connected with first step outlet pipe 211, second stage Pressure chamber 22 is externally connected with second stage outlet pipe 221, and third stage Pressure chamber 23 is externally connected with third stage outlet pipe 231; First step outlet pipe 211, second stage outlet pipe 221 and third stage outlet pipe 231 be arranged in parallel and are jointly communicated to rising pipe 5; First step outlet pipe 211, second stage outlet pipe 221, third stage outlet pipe 231 and rising pipe 5 are respectively arranged with first step valve 212, second stage valve 222, third stage valve 232 and flowing water Valve 51.
Being connected with water outlet high-density microvesicle jet apparatus 6 bottom Pressure chamber 2, for being involved in air, the suspended substances such as SS being taken out of.Water outlet high-density microvesicle jet apparatus 6 can be jet-flow air-floatation apparatus, and jet-flow air-floatation apparatus can be the dissolving device (not illustrating in the drawings) comprising at least plural liquid-gas jet device and communicate with liquid-gas jet device.
In order to reduce related substances content in discharge water further, improving discharge water standard, microfiltration membrane treatment unit or ultrafiltration membrane treatment device or film bioreactor device 7 outside water outlet high-density microvesicle jet apparatus 6, can be connected with further.
This specific embodiment is only explanation of the invention; it is not limitation of the present invention; those skilled in the art can make to the present embodiment the amendment not having creative contribution as required after reading this specification sheets, as long as but be all subject to the protection of patent law in right of the present invention.
Claims (5)
1. a High-efficiency sewage treatment separator, comprise water inlet pipe (1), it is characterized in that: described water inlet pipe (1) is communicated with at least more than one Pressure chamber (2), described Pressure chamber (2) is connected with the pressure control device (3) for control pressure size, described Pressure chamber (2) is connected with materialization medicament and adds pipe (4), and described water inlet pipe (1) and described materialization medicament add manages (4) and be arranged in parallel and be jointly connected and gather to described Pressure chamber import (20);
Described Pressure chamber (2) comprises the first step Pressure chamber (21), second stage Pressure chamber (22) and the third stage Pressure chamber (23) that connect setting successively up and down, described first step Pressure chamber (21) is externally connected with first step outlet pipe (211), described second stage Pressure chamber (22) is externally connected with second stage outlet pipe (221), and described third stage Pressure chamber (23) is externally connected with third stage outlet pipe (231); Described first step outlet pipe (211), second stage outlet pipe (221) and third stage outlet pipe (231) be arranged in parallel and are jointly communicated to rising pipe (5); Described first step outlet pipe (211), second stage outlet pipe (221), third stage outlet pipe (231) and described rising pipe (5) are respectively arranged with first step valve (212), second stage valve (222), third stage valve (232) and flowing water Valve (51);
Described Pressure chamber (2) bottom is connected with water outlet high-density microvesicle jet apparatus (6);
Described pressure control device (3) comprises and to be arranged in parallel with described water inlet pipe (1) and the blast main communicated (31) and be arrangeding in parallel with described blast main and the penstock communicated (32).
2. a kind of High-efficiency sewage treatment separator according to claim 1, is characterized in that: described Pressure chamber is 316L stainless steel rectangular box structure.
3. a kind of High-efficiency sewage treatment separator according to claim 2, is characterized in that: described water outlet high-density microvesicle jet apparatus (6) is jet-flow air-floatation apparatus.
4. a kind of High-efficiency sewage treatment separator according to claim 3, is characterized in that: the dissolving that described jet-flow air-floatation apparatus comprises at least plural liquid-gas jet device and communicates with described liquid-gas jet device.
5. a kind of High-efficiency sewage treatment separator according to claim 3, is characterized in that: described water outlet high-density microvesicle jet apparatus (6) is externally connected with microfiltration membrane treatment unit or ultrafiltration membrane treatment device or film bioreactor device (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410039607.0A CN103755000B (en) | 2014-01-28 | 2014-01-28 | A kind of High-efficiency sewage treatment separator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410039607.0A CN103755000B (en) | 2014-01-28 | 2014-01-28 | A kind of High-efficiency sewage treatment separator |
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| Publication Number | Publication Date |
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| CN103755000A CN103755000A (en) | 2014-04-30 |
| CN103755000B true CN103755000B (en) | 2016-01-06 |
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| CN201410039607.0A Active CN103755000B (en) | 2014-01-28 | 2014-01-28 | A kind of High-efficiency sewage treatment separator |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104787822B (en) * | 2015-05-06 | 2016-12-07 | 浙江天濮环保科技有限公司 | A kind of sewage separating device |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2487729Y (en) * | 2001-06-11 | 2002-04-24 | 萧启芳 | Water purifying treater |
| CN203715354U (en) * | 2014-01-28 | 2014-07-16 | 汤征 | Separator for efficient sewage treatment |
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- 2014-01-28 CN CN201410039607.0A patent/CN103755000B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2487729Y (en) * | 2001-06-11 | 2002-04-24 | 萧启芳 | Water purifying treater |
| CN203715354U (en) * | 2014-01-28 | 2014-07-16 | 汤征 | Separator for efficient sewage treatment |
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| CN103755000A (en) | 2014-04-30 |
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Effective date of registration: 20160912 Address after: 313000, Zhejiang, Huzhou Province, eight Li Zhen, Wuxing science and Technology Innovation Park, No. 29 standard workshop, two floor A District Patentee after: ZHANG LIMING Address before: 313000 Zhejiang City, Wuxing Province, Chaoyang District, the streets of the old town of gold lane, Lane 202, room 8, Patentee before: Tang Zheng |
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Effective date of registration: 20201113 Address after: Room 1510, 15 / F, Meixin business building, Fenghuang street, Wuxing District, Huzhou City, Zhejiang Province Patentee after: Tangshi (Huzhou) Business Management Co., Ltd Address before: Area a, 2 / F, No.29 standard factory building, Wulidian Town, Huzhou City, Huzhou City, Zhejiang Province 313000 Patentee before: Zhejiang Tianpu Environmental Protection Technology Co.,Ltd. |