CN208843888U - A kind of processing system of printed wiring board organic sewage - Google Patents

A kind of processing system of printed wiring board organic sewage Download PDF

Info

Publication number
CN208843888U
CN208843888U CN201820613517.1U CN201820613517U CN208843888U CN 208843888 U CN208843888 U CN 208843888U CN 201820613517 U CN201820613517 U CN 201820613517U CN 208843888 U CN208843888 U CN 208843888U
Authority
CN
China
Prior art keywords
tank
sludge
slot
reaction
sewage
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
Application number
CN201820613517.1U
Other languages
Chinese (zh)
Inventor
胡爽
喻科
吴骏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nanjing Bomao Environmental Protection & Technology Co Ltd
Chengdu Bomao Technology Co Ltd
Original Assignee
Nanjing Bomao Environmental Protection & Technology Co Ltd
Chengdu Bomao Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nanjing Bomao Environmental Protection & Technology Co Ltd, Chengdu Bomao Technology Co Ltd filed Critical Nanjing Bomao Environmental Protection & Technology Co Ltd
Priority to CN201820613517.1U priority Critical patent/CN208843888U/en
Application granted granted Critical
Publication of CN208843888U publication Critical patent/CN208843888U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The utility model discloses a kind of processing systems of printed wiring board organic sewage, including catch basin, conditioning tank, composite wastewater conditioning tank, copper-stripping reaction slot, first stage precipitation tank, contact break reactive tank, sulphur removal reactive tank, flocculation reaction slot, second-level settling pond, biochemical reaction tank, sludge concentration tank, the conditioning tank, boring aeration device is equipped in comprehensive and sewage conditioning tank, the copper-stripping reaction slot, contact break reactive tank, sulphur removal reactive tank, machine mixer is respectively arranged in flocculation reaction slot, it is respectively arranged with gear mud inclined tube in sedimentation basin level-one and sedimentation basin second level and adds to the materialization sludge pipe of sludge concentration tank, diving mixer is housed in the biochemical reaction tank, microporous aeration disc and sludge pump are simultaneously added to the biochemical sludge pipe of sludge concentration tank.The utility model has the technical effect that the preposition pretreating process for eliminating organic sewage acid out and coagulation, and the adjustment by way of water distribution and to last part technology is stable with insurance system.

Description

A kind of processing system of printed wiring board organic sewage
Technical field
The utility model relates to a kind of Industrial sewage treatment system, especially a kind of processing of printed wiring board organic sewage System.
Background technique
Printed wiring board factory, sewage species are various, and water-quality constituents is complicated, wherein organic sewage (containing waste liquid) clay content it is high, High organic content, pH value are high, have certain viscosity, in common technology, need individually to carry out acid out and flocculated materialization is located in advance Reason.
Organic sewage main indicator:
Common organic sewage treatment process:
1, organic sewage flow to catch basin from workshop certainly, then is promoted to the tune that conditioning tank carries out water quality and water by pump Section;
2, sewage in conditioning tank is pumped into acid precipitation reaction slot, sulfuric acid is added in slot, adjust pH value to 2.5-3, sewage can analyse It a large amount of hydroxy resin and floats, is separated from sewage by slag-scraper out;
3, acid precipitation reaction slot water outlet enter coagulation tank 1, added in coagulation tank 1 sodium hydroxide, PAC carry out acid-base neutralization and Flocculation, water outlet enter coagulation tank 2, added in coagulation tank 2 PAM help it is solidifying.Water outlet enters back segment precipitating/air-flotation system and carries out muddy water Separation, water outlet flow to composite wastewater conditioning tank;
4, mixed composite wastewater sequentially enters copper-stripping reaction slot, first stage precipitation tank, contact break reactive tank, removes reaction of Salmon-Saxl To go copper ion and complex copper in water removal, final outflow water enters biochemical reaction tank for slot, flocculation reaction slot, second-level settling pond, removes The pollutants such as COD, ammonia nitrogen, total nitrogen in sewage;
5, in the process caused by sludge drain into sludge concentration tank and be concentrated, it is to be drained off.
It facts have proved that there are following disadvantages with system processing organic sewage:
1, organic sewage PH is alkaline, usual PH > 12, and acid precipitation reaction need to adjust sewage PH value and usually adjust PH to acid It is subsequent to add alkali tune pH value to be conducive to flocculate to 8-9 again to 2.5-3.Its front and back adjusts pH value repeatedly and consumes a large amount of medicaments;
2, organic sewage pretreatment is independent treatment process unit, need to increase the investment cost of a whole set of processing equipment.Fortune Between the departure date, since the acid and alkali corrosion in its reaction process is stronger, the later period can also generate certain maintenance cost;
3, acid precipitation reaction slot and coagulation tank 1 are required to preferable PH control.Fluctuation and medicament due to water water quality Dosage accurately controls problem, and artificial adjust then is difficult to balance, and adjusts frequency height, so needing higher automatic control requirement;
4, the organic sludge that organic sewage generates after processing has certain viscosity, and dehydrating effect is not good enough, and easily blocking filter Cloth.
Summary of the invention
A kind of effective and treatment effect is provided purpose of the utility model is to solve above-mentioned the deficiencies in the prior art The processing system of good printed wiring board organic sewage.
To achieve the goals above, a kind of processing system of printed wiring board organic matter water designed by the utility model, Including catch basin, conditioning tank, composite wastewater conditioning tank, copper-stripping reaction slot, first stage precipitation tank, contact break reactive tank, sulphur removal reactive tank, Flocculation reaction slot, second-level settling pond, biochemical reaction tank, sludge concentration tank are equipped in the conditioning tank, comprehensive and sewage conditioning tank Boring aeration device, the copper-stripping reaction slot, sulphur removal reactive tank, are respectively arranged with mechanical stirring in flocculation reaction slot at contact break reactive tank Machine is respectively arranged with gear mud inclined tube in sedimentation basin level-one and sedimentation basin second level and adds to the materialization sludge pipe of sludge concentration tank, institute It states and diving mixer, microporous aeration disc and sludge pump is housed in biochemical reaction tank and added to the biochemical spoil disposal of sludge concentration tank Pipe.
A kind of processing system for printed wiring board organic sewage that the utility model obtains, technical effect have following five Point:
1, the independent pretreatment unit of leading portion complexity in conventional treatment method can be saved, organic sewage need not be using acid Analysis, the pretreatment of coagulation, precipitation and separation, simplify technique, and save one-time investment expense;
2, organic sewage is alkalinity, and PH higher can be used to adjust the pH value of composite wastewater (PH is acidity), save a large amount of medicines Agent expense;
3, the content of organics in organic sewage is higher, can be provided more carbon in biochemical reaction tank denitrification Source, so that its denitrification better effect, the additional amount of carbon source when reducing script denitrification;
4, flocculation sedimentation, sludge mix organic sewage with copper-contained sludge together with other sewage in copper-stripping reaction slot, Better effect when sludge dewatering;
5, it is verified through longtime running, the microorganism in the system mesophytization reaction tank can be degraded well in organic sewage Organic matter, because the proportion of organic sewage is different, the composite wastewater COD after pretreatment is generally 400-800mg/l, raw 60-100mg/l can be down to by changing reaction tank water outlet COD, and removal rate adds proper amount of carbon source, the removal rate of total nitrogen can up to 85% or more Reach 90% or more.
Detailed description of the invention
Fig. 1 is the processing system of wiring board organic sewage under original technology
Fig. 2 is the processing system of the wiring board organic sewage of embodiment 1
In figure: catch basin 1, conditioning tank 2, composite wastewater conditioning tank 3, copper-stripping reaction slot 4, first stage precipitation tank 5, contact break reaction Slot 6, sulphur removal reactive tank 7, flocculation reaction slot 8, second-level settling pond 9, biochemical reaction tank 10, sludge concentration tank 11.
Specific embodiment
The present invention will be further described with reference to the accompanying drawings and examples;
Embodiment 1:
As shown in Fig. 2, a kind of processing system of printed wiring board organic sewage provided by the utility model, on realizing State purpose, a kind of processing system of printed wiring board organic matter water designed by the utility model, including catch basin 1, conditioning tank 2, composite wastewater conditioning tank 3, copper-stripping reaction slot 4, first stage precipitation tank 5, contact break reactive tank 6, sulphur removal reactive tank 7, flocculation reaction slot 8, second-level settling pond 9, biochemical reaction tank 10, sludge concentration tank 11 are equipped in the conditioning tank 1, comprehensive and sewage conditioning tank 2 and wear Hole aerator 12, the copper-stripping reaction slot 4, sulphur removal reactive tank 7, are respectively arranged with machinery in flocculation reaction slot 8 at contact break reactive tank 6 Blender 13 is respectively arranged with gear mud inclined tube 14 in sedimentation basin level-one 5 and sedimentation basin second level 9 and adds to the object of sludge concentration tank 11 Change sludge pipe 18, in the biochemical reaction tank 10 equipped with diving mixer 15, microporous aeration disc 16 and sludge pump 17 and add to The biochemical sludge pipe 19 of sludge concentration tank 11.The method for carrying out the processing of printed wiring board organic sewage using above system is as follows It is described:
Organic sewage initially enters catch basin 1, and partial suspended sludge deposits in catch basin 1, regular manual cleaning to dirt Mud thickener 11;1 internal upper part sewage of catch basin to conditioning tank 2 is pumped to cache, in conditioning tank 2 organic sewage by a certain percentage with it is comprehensive Other sewage mixing, mixed composite wastewater in sewage conditioning tank 3 is closed to remove absolutely by copper-stripping reaction slot 4, first stage precipitation tank 5 Most copper ion and suspended matter simultaneously adjust pH value, and sludge drains into sludge condensation by materialization sludge pipe 18 in first stage precipitation tank 5 Pond 11;The water outlet of first stage precipitation tank 5 enters contact break reaction tank 6, sulphur removal reaction tank 7, flocculation tank 8, second-level settling pond 9 and removes remnants Copper ion, suspended matter and complex copper, sludge drains into sludge concentration tank 11 by materialization sludge pipe 18 in second-level settling pond 9;Two The grade water outlet of sedimentation basin 9 enters biochemical reaction tank 10, and the pollutants such as COD, ammonia nitrogen, total nitrogen are removed in biochemical reaction tank 10, biochemical Sludge periodically drains into sludge concentration tank 11 by biochemical sludge pipe 19 in reaction tank 10;The discharge of 10 standard water discharge of biochemical reaction tank.
Embodiment 2:
A kind of processing system of printed wiring board organic sewage provided by the utility model, general structure and embodiment 1 Unanimously, unlike in the present embodiment, machine mixer can be changed to boring aeration device.
Embodiment 3:
A kind of processing system of printed wiring board organic sewage provided by the utility model, general structure and embodiment 1 Unanimously, unlike in the present embodiment, biochemical reaction tank can be changed to A/O or CASS pool process by SBR technique.

Claims (2)

1. a kind of processing system of printed wiring board organic sewage, including catch basin (1), conditioning tank (2), composite wastewater conditioning tank (3), copper-stripping reaction slot (4), first stage precipitation tank (5), contact break reactive tank (6), sulphur removal reactive tank (7), flocculation reaction slot (8), two Grade sedimentation basin (9), biochemical reaction tank (10), sludge concentration tank (11), it is characterised in that the conditioning tank (2), comprehensive and sewage tune Boring aeration device (12) are equipped in section pond (3);The copper-stripping reaction slot (4), contact break reactive tank (6), sulphur removal reactive tank (7), machine mixer (13) are respectively arranged in flocculation reaction slot (8), are filled in first stage precipitation tank (5) and second-level settling pond (9) There is gear mud inclined tube (14) and adds to the materialization sludge pipe (18) of sludge concentration tank (11);It is equipped in the biochemical reaction tank (10) Diving mixer (15), microporous aeration disc (16) and sludge pump (17) add biochemical reaction tank (10) to sludge concentration tank (11) Biochemical sludge pipe (19).
2. a kind of processing system of printed wiring board organic sewage according to claim 1, it is characterised in that: the copper removal Reactive tank (4), contact break reactive tank (6), blender is paddle blade in sulphur removal reactive tank (7), mixing speed be it is fast mixed, flocculation is anti- Answering blender in slot (8) is frame blade, and mixing speed is slow mixed;The first stage precipitation tank (5), second-level settling pond (9) are oblique Pipe sedimentation basin;The biochemical reaction tank (10) is SBR structure.
CN201820613517.1U 2018-04-27 2018-04-27 A kind of processing system of printed wiring board organic sewage Expired - Fee Related CN208843888U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820613517.1U CN208843888U (en) 2018-04-27 2018-04-27 A kind of processing system of printed wiring board organic sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820613517.1U CN208843888U (en) 2018-04-27 2018-04-27 A kind of processing system of printed wiring board organic sewage

Publications (1)

Publication Number Publication Date
CN208843888U true CN208843888U (en) 2019-05-10

Family

ID=66351346

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820613517.1U Expired - Fee Related CN208843888U (en) 2018-04-27 2018-04-27 A kind of processing system of printed wiring board organic sewage

Country Status (1)

Country Link
CN (1) CN208843888U (en)

Similar Documents

Publication Publication Date Title
CN105948414B (en) A kind of emulsifying liquid waste water processing system and its treatment process
CN103848542B (en) Advanced wastewater treatment technology for sewage treatment and upgrading and reconstruction
CN106430781B (en) Desulfurization wastewater zero-emission treatment system and treatment method for recycling sludge
CN103864260A (en) Method for processing viscose fiber production wastewater
CN104086041B (en) A kind of surface active agent wastewater treatment system and technique
CN107285489A (en) A kind of device and method of desulfurization wastewater pretreatment
CN104860447A (en) Novel wet-process flue gas desulfurization wastewater treatment system
CN207193054U (en) A kind of distributing trade effluent integrated treatment unit based on Internet of Things
CN110272147A (en) Copper ore dressing wastewater treatment and renovation device and method
CN106517578A (en) Heavy metal wastewater treatment method by breaking complexes by granular sludge and ceramic membrane
CN108409053B (en) Treatment method of organic sewage of printed circuit board
CN208843888U (en) A kind of processing system of printed wiring board organic sewage
CN204981415U (en) Dissolved -air air -floating device
CN203382613U (en) Treatment equipment for removing fluorine and calcium ions in wastewater of coal chemical industries
CN206901925U (en) The device of novel desulphurization wastewater treatment
CN206437998U (en) The monitoring system of PAM concentration in mixed liquor containing PAM
CN213446615U (en) Ethylene-vinyl acetate copolymer adhesive wastewater treatment device
CN100509644C (en) Treatment method of calcium carbide waste water
CN113501596A (en) Pretreatment process for high-oil high-suspended matter wastewater
CN113429083A (en) Zero-liquid discharge treatment process and system for tar processing and needle coke mixed wastewater
CN206156977U (en) Device of high chemical oxygen demand of concurrent processing , high ammonia -nitrogen concentration , high phosphorus waste water
KR100846693B1 (en) Livestock waste water treatment plant by aerobic denitrification
CN106673307A (en) Method and system for monitoring PAM concentration in PAM-containing mixed solution
CN204874103U (en) Novel wet flue gas desulfurization effluent disposal system
CN110498560A (en) A kind of textile printing and dyeing wastewater processing method

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190510

Termination date: 20210427

CF01 Termination of patent right due to non-payment of annual fee