CN103496804B - Stone machining wastewater treatment method - Google Patents
Stone machining wastewater treatment method Download PDFInfo
- Publication number
- CN103496804B CN103496804B CN201310436387.0A CN201310436387A CN103496804B CN 103496804 B CN103496804 B CN 103496804B CN 201310436387 A CN201310436387 A CN 201310436387A CN 103496804 B CN103496804 B CN 103496804B
- Authority
- CN
- China
- Prior art keywords
- sewage
- wastewater treatment
- sedimentation
- clear water
- stone
- 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.)
- Active
Links
Abstract
The invention provides a stone machining wastewater treatment method. The method comprises the following steps: providing a stone machining wastewater treating device, wherein a microcomputer water quality monitoring device in the stone machining wastewater treating device can measure the PH (potential of hydrogen) value and the flow of the wastewater; then carrying out treatment of coagulation sedimentation, regulation of potential of hydrogen and the like on the wastewater by using a microcomputer water quality pH regulating device; stirring the wastewater which is subjected to the pH regulation, by a self-stirring wastewater lift pump, and transmitting to a main sedimentation container, carrying out primary sedimentation, then injecting into a water storage sedimentation container, carrying out secondary sedimentation. After the secondary sedimentation, the clear water can be led out through a clear water outlet of the middle part of the water storage sedimentation container, and the recovered wastewater can be directly used for stone production.
Description
Technical field
The present invention relates to a kind of method of wastewater treatment, particularly relate to a kind of stone wastewater treatment process.
Background technology
Along with developing of processing of stone industry, the waste water that processing of stone produces also increases thereupon, brings very large impact to people's living environment, even can cause the serious waste of serious pollution and destruction and resource.
Mostly the method for wastewater treatment that current Ornamental Stone Industry uses, be to adopt and dig multiple pond and carry out one by one filtering, precipitating, or by the mode that multiple iron flask precipitates one by one.Its shortcoming is, floor space is large, sedimentation effect is not good, cannot meet existing stone material throughput.The sewage of institute's output, inevitably permeates the ground.The a large amount of acidity contained in the clear water be precipitated out or alkaline matter, can cause serious destruction to machine and stone surface, causes the stone material produced not reach desirable luster effect.For reaching ideal effect, processing of stone enterprise can only use civil running water on polissoir, causes the significant wastage of water resources.And also there is very large potential safety hazard (personnel may fall in pond because of carelessness) in this method.
Another treatment process is disposed of sewage with steel tower formula treatment tank, and the weak point of this equipment is: because treatment tank is placed in more than ground very eminence, be not easy to produce jumbo treatment system.As jumbo treatment system need be produced, very high manpower and financial resources need be dropped into.Also there is very large potential safety hazard.In use, because of the difference of geological condition, jumbo treatment tank such as may to collapse at the situation, and bring hidden trouble can to the productive life of people, the clear water of this kind of method institute output equally also can produce serious destruction to machine and stone surface.
Summary of the invention
For above-mentioned problems of the prior art; the object of the present invention is to provide a kind of stone wastewater treatment unit; the waste water produced in processing of stone can be met the needs of processing of stone by after treatment, reaches conservation, protection of the environment, guarantee are produced smoothly, the effect of Improving The Quality of Products.
To achieve these goals, the technical solution used in the present invention is as follows:
A kind of stone wastewater treatment process, its step comprises:
Step 1: a kind of stone wastewater treatment unit is provided, this device comprises water quality regulation unit, settlement of sewage processing unit, and described water quality regulation unit comprises micro computer water monitoring device, micro computer water quality acid-alkali accommodation device; Described micro computer water monitoring device comprises microcomputer data provides plate, online pH detector and under meter; Described micro computer water quality acid-alkali accommodation device comprises microcomputer data dash receiver and PLC automatic control system; Described settlement of sewage processing unit comprises sewage collecting basin, certainly mixes formula sewage pump, primary precipitate container, clear water thrust-augmenting nozzle, retaining precipitation vessel;
Step 2: micro computer water monitoring device uses online pH detector and under meter to carry out pH value and flow measurement to sewage;
Step 3: provide plate to provide take off data by microcomputer data and manually input required flocculation agent scale parameter as required to the microcomputer data dash receiver of micro computer water quality pH value regulator, operating executive system by PLC automatic control system and the coagulating sedimentation of sewage and potential of hydrogen are regulated;
Step 4: the sewage regulated through potential of hydrogen flows into ditch and carries out primary sedimentation by certainly mixing after formula sewage pump stirs through being delivered to primary precipitate container by guide pipe;
Step 5: the clear water after primary sedimentation injects retaining precipitation vessel by clear water thrust-augmenting nozzle and guide pipe and carries out secondary sedimentation;
Step 6: after secondary sedimentation, clear water is derived by being arranged on container clear water output with it in the middle part of retaining precipitation vessel;
Further, the described executive system in described step 3 is the first electrically operated valve of individually annotate in sewage flocculation agent, alkali lye and the acid solution controlled by PLC automatic control system, the second electrically operated valve and the 3rd electrically operated valve.
Further, described acid solution is the hydrochloric acid of 1mol/L; Described alkali lye is the sodium hydroxide of 5mol/L; Described flocculation agent is polymer alumina or polyaluminium sulfate.
Further, buffer substrate tablet is all equipped with in the described guide pipe lower end in described step 4 and step 5.
Further, the described primary precipitate container upper end oral area in described step 4 is provided with profile of tooth spoiler and annular clear water ditch.
Further, primary precipitate container described in described step 1 and described retaining precipitation vessel is Upper cylindrical shape lower taper and bottom is installed in underground.
Advantage of the present invention and beneficial effect:
(1) water quality regulation unit can automatically adjust to the potential of hydrogen of sewage, reaches required potential of hydrogen standard, and the clear water after regulating and filtering can be directly used in stone material production through reclaiming, and can not produce harm to machine and stone material.
(2) precipitation vessel being partly placed in underground does not limit by geologic condition, and simultaneously without the need to building the pedestal of large tough, cost just can produce relatively large sewage disposal device under dropping into lower prerequisite.
(3) whole stone wastewater treatment unit level of automation is higher, and the whole process completed from water quality monitoring (WQM) to wastewater treatment only needs 2-3 name operator, saves human cost.
Accompanying drawing explanation
Fig. 1 is the process flow sheet of stone wastewater treatment process of the present invention;
Fig. 2 is the structural representation of stone wastewater treatment process institute of the present invention using appts;
Fig. 3 is the process flow sheet of the water quality monitoring (WQM) regulation system of stone wastewater treatment process of the present invention.
Embodiment
In order to make object of the present invention, technical scheme and advantage clearly understand, below in conjunction with accompanying drawing, the present invention is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the present invention, be not intended to limit the present invention.
As shown in Figure 1, Figure 2 and Figure 3, the present invention comprises the following steps the process that processing of stone settlement of sewage is carried out:
First, the sewage that machinery equipment 1 processing stone material produces carries out coagulating sedimentation via micro computer water monitoring device 2 and micro computer water quality acid-alkali accommodation device 3 pairs of sewage in ditch 4 and potential of hydrogen regulates process, and its treating processes is:
The numerical value that online pH detector in micro computer water monitoring device 2 and under meter are monitored provides plate to be sent to the microcomputer data dash receiver of micro computer water quality acid-alkali accommodation device 3 by microcomputer data.The scale parameter that adds of flocculation agent inputs microcomputer data dash receiver by the artificial character according to stone material and waste strength.The first electrically operated valve controlled separately by PLC control system, the second electrically operated valve, the parameter of the 3rd electrically operated valve received by microcomputer data dash receiver throw in a certain proportion of flocculation agent, alkali lye or acid solution in trend sewage.Flocculation agent can selective polymerization aluminum chloride or polyaluminium sulfate, and alkali lye can select concentration to be in the pH compound alkali of about 5mol/L, pH and powder or sodium hydroxide, and acid solution can select concentration to be the hydrochloric acid of 1mol/L.Sewage after flocculation agent precipitation process and potential of hydrogen regulate enters sewage collecting basin 5.
Then, certainly mixing formula sewage pump 6 will stir through the sewage of potential of hydrogen process in sewage collecting basin 5 and be promoted to guide pipe 8, injects primary precipitate container 7 carry out first time precipitation in guide pipe 8 via the buffering of buffer substrate tablet 9.Buffer substrate tablet 9 can cushion flow velocity when sewage injects and make sewage directed flow, reduces when waste liquid injects impact sedimentary in container.
Then, when sewage precipitates and expires to vessel port in primary precipitate container 7, flowed into the annular clear water ditch 11 of vessel port by profile of tooth spoiler 10, sewage through profile of tooth spoiler 10 can precipitate more even.When the liquid level in annular clear water ditch 11 overflows across clear water thrust-augmenting nozzle 12, liquid just can inject the guide pipe of retaining precipitation vessel 16 along clear water thrust-augmenting nozzle 12, and carries out secondary sedimentation by buffer substrate tablet injection retaining precipitation vessel 16.
Finally, after secondary sedimentation, water quality is very limpid, and water-based is moderate, can meet the needs that processing of stone is produced completely, can not produce any destruction and impact to stone material and machine.When clear water water level is higher than clear water output 14, namely accessible machine uses.The precipitation vessel of retaining is simultaneously provided with retaining deposit water level 15, can carry out retaining with the different demands in satisfied production to the clear water after precipitation.
The powder precipitated in primary precipitate container 7 and retaining precipitation vessel 16 is starched the pressure that can produce by waterhead and is starched thrust-augmenting nozzle 13 process that follow-up precipitation treatment device carries out precipitating of leading by powder and reclaim.
The above embodiment only have expressed embodiments of the present invention, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the scope of the claims of the present invention.It should be pointed out that for the person of ordinary skill of the art, without departing from the inventive concept of the premise, can also make some distortion and improvement, these all belong to protection scope of the present invention.Therefore, the protection domain of patent of the present invention should be as the criterion with claims.
Claims (5)
1. a stone wastewater treatment process, is characterized in that,
Step 1: a kind of stone wastewater treatment unit is provided, this device comprises water quality regulation unit, settlement of sewage processing unit, and described water quality regulation unit comprises micro computer water monitoring device, micro computer water quality acid-alkali accommodation device; Described micro computer water monitoring device comprises microcomputer data provides plate, online pH detector and under meter; Described micro computer water quality acid-alkali accommodation device comprises microcomputer data dash receiver and PLC automatic control system; Described settlement of sewage processing unit comprises sewage collecting basin, certainly mixes formula sewage pump, primary precipitate container, clear water thrust-augmenting nozzle, retaining precipitation vessel;
Step 2: micro computer water monitoring device uses online pH detector and under meter to carry out pH value and flow measurement to sewage;
Step 3: provide plate to provide take off data by microcomputer data and manually input required flocculation agent scale parameter as required to the microcomputer data dash receiver of micro computer water quality pH value regulator, operating executive system by PLC automatic control system and the coagulating sedimentation of sewage and potential of hydrogen are regulated;
Step 4: the sewage regulated through potential of hydrogen flows into ditch and carries out primary sedimentation by certainly mixing after formula sewage pump stirs through being delivered to primary precipitate container by guide pipe;
Step 5: the clear water after primary sedimentation injects retaining precipitation vessel by clear water thrust-augmenting nozzle and guide pipe and carries out secondary sedimentation;
Step 6: after secondary sedimentation, clear water is derived by being arranged on container clear water output with it in the middle part of retaining precipitation vessel; Wherein,
Described primary precipitate container upper end oral area in described step 4 is provided with profile of tooth spoiler and annular clear water ditch.
2. stone wastewater treatment process according to claim 1, it is characterized in that, the described executive system in described step 3 is the first electrically operated valve of individually annotate in sewage flocculation agent, alkali lye and the acid solution controlled by PLC automatic control system, the second electrically operated valve and the 3rd electrically operated valve.
3. stone wastewater treatment process according to claim 2, is characterized in that, described acid solution is the hydrochloric acid of 1mol/L; Described alkali lye is the sodium hydroxide of 5mol/L; Described flocculation agent is polymer alumina or polyaluminium sulfate.
4. stone wastewater treatment process according to claim 1, is characterized in that, buffer substrate tablet is all equipped with in the described guide pipe lower end in described step 4 and step 5.
5. stone wastewater treatment process according to claim 1, is characterized in that, primary precipitate container described in described step 1 and described retaining precipitation vessel is Upper cylindrical shape lower taper and bottom is installed in underground.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310436387.0A CN103496804B (en) | 2013-09-23 | 2013-09-23 | Stone machining wastewater treatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310436387.0A CN103496804B (en) | 2013-09-23 | 2013-09-23 | Stone machining wastewater treatment method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103496804A CN103496804A (en) | 2014-01-08 |
CN103496804B true CN103496804B (en) | 2015-05-13 |
Family
ID=49862097
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310436387.0A Active CN103496804B (en) | 2013-09-23 | 2013-09-23 | Stone machining wastewater treatment method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103496804B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104193117B (en) * | 2014-09-24 | 2017-04-26 | 厦门福润源环保科技有限公司 | Treatment device of processing wastewater of jade |
CN105331435A (en) * | 2015-10-15 | 2016-02-17 | 当涂县维思共创工业产品设计有限公司 | Aluminum profile anti-rust lubricant |
CN107364987A (en) * | 2017-07-24 | 2017-11-21 | 仁怀市攀峰石材加工厂 | A kind of stone wastewater processing system and processing method |
CN115304196A (en) * | 2022-09-15 | 2022-11-08 | 福建省华辉石业股份有限公司 | Stone processing wastewater treatment equipment and operation method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2685326Y (en) * | 2004-02-11 | 2005-03-16 | 上海市政工程设计研究院 | Coagulant feeding quantity controlling device |
KR100770024B1 (en) * | 2006-01-11 | 2007-10-30 | 주식회사 삼영건설기술공사 | Apparatus for controlling the quality of water real-time for reducing pipe corrosion in a water supply pipe |
CN201002008Y (en) * | 2006-10-11 | 2008-01-09 | 上海立源水处理科技发展有限公司 | Multi-unit automatic medicine-adding controlling equipment |
CN202099144U (en) * | 2011-05-22 | 2012-01-04 | 陕西华诚首创环保科技有限公司 | Chemical oxygen demand (COD) monitoring waste liquid treatment device |
CN202440391U (en) * | 2012-03-01 | 2012-09-19 | 环球石材(福建)有限公司 | Full-automatic and circular stone sewage treating device |
CN103011356A (en) * | 2012-08-15 | 2013-04-03 | 重庆水务集团股份有限公司 | Method for controlling automatic chemical dosing of high-turbidity water system |
-
2013
- 2013-09-23 CN CN201310436387.0A patent/CN103496804B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2685326Y (en) * | 2004-02-11 | 2005-03-16 | 上海市政工程设计研究院 | Coagulant feeding quantity controlling device |
KR100770024B1 (en) * | 2006-01-11 | 2007-10-30 | 주식회사 삼영건설기술공사 | Apparatus for controlling the quality of water real-time for reducing pipe corrosion in a water supply pipe |
CN201002008Y (en) * | 2006-10-11 | 2008-01-09 | 上海立源水处理科技发展有限公司 | Multi-unit automatic medicine-adding controlling equipment |
CN202099144U (en) * | 2011-05-22 | 2012-01-04 | 陕西华诚首创环保科技有限公司 | Chemical oxygen demand (COD) monitoring waste liquid treatment device |
CN202440391U (en) * | 2012-03-01 | 2012-09-19 | 环球石材(福建)有限公司 | Full-automatic and circular stone sewage treating device |
CN103011356A (en) * | 2012-08-15 | 2013-04-03 | 重庆水务集团股份有限公司 | Method for controlling automatic chemical dosing of high-turbidity water system |
Also Published As
Publication number | Publication date |
---|---|
CN103496804A (en) | 2014-01-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103496804B (en) | Stone machining wastewater treatment method | |
CN104150652B (en) | A kind of chemical industrial park centralized wastewater treatment factory water inletting monitoring regulation system and method | |
CN103823418A (en) | PLC control system for urban sewage treatment plants | |
CN107364987A (en) | A kind of stone wastewater processing system and processing method | |
CN103482790B (en) | A kind of stone wastewater treatment unit | |
EP3180117B1 (en) | A system for analysis and reuse of waste liquids | |
CN203461909U (en) | Treatment device for stone processing wastewater | |
CN103482791B (en) | Method for waste water sedimentation treatment in stone machining | |
CN106430704A (en) | Movable integrated coating wastewater treating device and treating method thereof | |
CN206188528U (en) | Portable integration application effluent treatment plant | |
CN103482795B (en) | A kind of stone wastewater precipitation treatment device | |
CN103482789A (en) | Waste water quality adjusting system for stone machining | |
CN203451318U (en) | Device for sedimentation treatment of stone processing wastewater | |
CN107792957A (en) | A kind of stone wastewater processing unit | |
CN203324722U (en) | Automatic control device of steel wire pickling and phosphating wastewater processing system | |
CN207660595U (en) | Oil field shaft mouth chemicals dosing plant | |
CN205398194U (en) | Beneficiation wastewater adds medicine automatic control device | |
CN111635069A (en) | Bone gelatin wastewater treatment and recycling device and process thereof | |
CN209507828U (en) | A kind of moveable system for being applied to the wastewater treatment of soil remediation containing heavy metal | |
CN204643929U (en) | Decorporation formula sewage treatment equipment | |
CN204848510U (en) | Remove arsenic purifier | |
CN204687085U (en) | Intelligent concrete mixing plant waste water useless slurry process control system | |
CN202717621U (en) | Environment-friendly dredging residual water metering and coagulation treatment device | |
CN107585908A (en) | Automatic business processing control system for titanium processing pickling sewage | |
CN209210596U (en) | High-sulfate, high-COD waste water processing unit |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |