CN108975533B - Intelligent sewage treatment method for sapphire substrate factory - Google Patents

Intelligent sewage treatment method for sapphire substrate factory Download PDF

Info

Publication number
CN108975533B
CN108975533B CN201810805264.2A CN201810805264A CN108975533B CN 108975533 B CN108975533 B CN 108975533B CN 201810805264 A CN201810805264 A CN 201810805264A CN 108975533 B CN108975533 B CN 108975533B
Authority
CN
China
Prior art keywords
sewage
wastewater
sewage treatment
brushing
slicing
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
Application number
CN201810805264.2A
Other languages
Chinese (zh)
Other versions
CN108975533A (en
Inventor
秦光临
李志强
蔡金荣
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.)
Tunghsu Group Co Ltd
Original Assignee
Jiangsu Jeshine New Material 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 Jiangsu Jeshine New Material Co ltd filed Critical Jiangsu Jeshine New Material Co ltd
Priority to CN201810805264.2A priority Critical patent/CN108975533B/en
Publication of CN108975533A publication Critical patent/CN108975533A/en
Application granted granted Critical
Publication of CN108975533B publication Critical patent/CN108975533B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/38Treatment of water, waste water, or sewage by centrifugal separation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/06Controlling or monitoring parameters in water treatment pH
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/42Liquid level

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)
  • Physical Water Treatments (AREA)

Abstract

The invention relates to an intelligent sewage treatment method for a sapphire substrate factory, which comprises the following steps: (1) and (4) classification: classifying sewage generated in the sapphire substrate production process according to characteristics, wherein the sewage comprises a slicing and grinding process sewage; b. acid washing and alkali washing process sewage; c. the finished product pieces scrub the waste water; d. sewage from other processes; (2) pretreatment: slicing and grinding process sewage in the step (1); b. acid washing and alkali washing process sewage; c. pre-treating the finished piece brushing wastewater; (3) conventional sewage treatment: and (3) inputting the sewage pretreated in the step (2) and sewage of other procedures into a sewage treatment station for unified treatment. The invention can realize automatic unattended operation of sewage treatment, reduces the probability of blockage and corrosion of pipelines of a sewage system through the pretreatment of the sewage treatment units in each process, realizes the recycling of the brushing waste water, and provides a set of intelligent and automatic technical scheme for saving water resources and manpower resources.

Description

Intelligent sewage treatment method for sapphire substrate factory
Technical Field
The invention relates to an intelligent sewage treatment method for a sapphire substrate factory, and belongs to the technical field of industrial sewage treatment generated by processing of sapphire substrates.
Background
Sapphire substrate processing involves many processes, and the produced sewage nature difference of every process is big, and the sewage that is rich in large granule solid impurity granule blocks up the pipeline easily, and the sewage that contains the acidizing fluid corrodes the pipeline easily, and finished product piece scrubs waste water and its quality of water is superior to industrial tap water, can collect the back and supply section, the grinding process to use, and traditional sewage treatment is with above-mentioned sewage direct collection to the sewage treatment station, carries out unified processing in the sewage treatment pond. However, the centralized sewage treatment brings a series of problems to sapphire substrate processing factories, such as: the sewage conveying pipeline is blocked, and a large amount of manpower is consumed for dredging after the blockage; the acid-containing sewage corrodes a sewage conveying pipeline, so that the sewage leaks and the natural environment of soil is damaged; the finished piece brushing wastewater is directly discharged to a sewage station, so that the sewage treatment cost is increased, and the waste of water resources is caused.
A classification treatment scheme for wastewater generated in a sapphire substrate processing step has not been retrieved.
Disclosure of Invention
In order to overcome the defects of the prior art, the invention aims to provide an intelligent sewage treatment method for a sapphire substrate factory, which realizes automatic unattended operation of sewage treatment, reduces the pipeline blockage and corrosion probability of a sewage system through pretreatment of sewage treatment units in each process, realizes recycling of scrubbing waste water, and provides an intelligent and automatic technical scheme for saving water resources and manpower resources.
The technical scheme adopted by the invention for solving the technical problems is as follows:
an intelligent sewage treatment method for a sapphire substrate factory comprises the following steps:
(1) and (4) classification: classifying sewage generated in the sapphire substrate production process according to characteristics, wherein the sewage comprises a slicing and grinding process sewage; b. acid washing and alkali washing process sewage; c. the finished product pieces scrub the waste water; d. sewage from other processes;
(2) pretreatment: slicing and grinding process sewage in the step (1); b. acid washing and alkali washing process sewage; c. respectively pretreating the finished piece brushing wastewater;
(3) conventional sewage treatment: and (3) inputting the sewage pretreated in the step (2) and sewage of other procedures into a sewage treatment station for unified treatment.
In the pretreatment step of step (2), a pretreatment method of the sewage in the slicing and grinding process is as follows:
(1) the sewage of the slicing and grinding process enters a centrifugal separator after being pressurized by a centrifugal pump, large-particle solid impurities are discharged after being separated by the centrifugal separator, and the rest sewage enters a liquid collecting tank;
(2) and the sewage in the liquid collecting tank overflows to a sewage treatment station after natural sedimentation.
Preferably, the slicing and grinding engineering sewage can be subjected to coarse filtration to filter out large particles, and then enters a centrifugal separator for separation.
After coarse filtration and/or centrifugal separation, natural overflow enters the sewage treatment station again, prevents that sewage pipeline from blockking up, also reduces the required manpower and materials cost that consumes of mediation after the follow-up jam.
In the pretreatment step of step (2), the pretreatment method of the acid washing process wastewater is as follows:
(1) neutralizing the sewage collected by the sewage collecting pipeline in the acid washing process and the sewage collected by the sewage collecting pipeline in the alkali washing process in a pH neutralization tank;
(2) when the pH value measured by the pH value measuring sensor is lower than a set value, transmitting a starting signal to the pneumatic diaphragm pump, and starting the pneumatic diaphragm pump to operate;
(3) after the pneumatic diaphragm pump is started, lime water is pumped into a pH neutralization pond to neutralize excessive acid-containing sewage;
(4) when the pH value measured by the pH value measuring sensor reaches a set value, transmitting a stop signal to the pneumatic diaphragm pump, and stopping the operation of the pneumatic diaphragm pump;
(5) and naturally overflowing the sewage neutralized by the pH neutralization tank to a sewage treatment station.
Preferably, the pH set point is between 6 and 8.
The acid-containing sewage is neutralized and then enters the sewage treatment station, so that the corrosion of the acid-containing sewage to a conveying pipeline can be prevented.
As a preferred technical solution of the present application, in the pretreatment step of step (2), the pretreatment method of c. finished piece brushing wastewater is as follows:
(1) collecting the scrubbed wastewater to a scrubbing wastewater collecting tank by a finished piece scrubbing wastewater collecting pipeline;
(2) when the liquid level sensor cannot sense the liquid level, transmitting an opening signal to the second electromagnetic valve, and opening an industrial tap water pipeline for supplementing the shortage of finished product piece brushing wastewater;
(3) when the liquid level sensor senses the liquid level, a closing signal is transmitted to the first electromagnetic valve, the first electromagnetic valve is closed, and industrial tap water is prevented from flowing back to the brushing wastewater collecting tank;
(4) when the liquid level in the brushing wastewater collecting tank is higher than the overflow port, the brushing wastewater automatically overflows to a sewage treatment station.
The finished piece brushing wastewater is conveyed to other procedures with low requirements on water quality to be used firstly, and then enters a sewage treatment step, so that water resources can be recycled, and the sewage treatment cost is also reduced.
Advantageous effects
The method classifies sewage of each process of a sapphire substrate factory, carries out pretreatment after classification, and converges the sewage to a sewage treatment station for unified treatment after pretreatment, thereby reducing the workload of subsequent sewage treatment, reducing the sewage treatment cost and preventing the waste caused by direct discharge of part of reusable water.
Drawings
FIG. 1 is a flow chart of an intelligent sewage treatment method of a sapphire substrate factory according to the invention;
FIG. 2 is a schematic structural diagram of a sewage pretreatment method in a slicing and grinding process;
FIG. 3 is a schematic structural diagram of a sewage pretreatment method in an acid washing and alkali washing process;
FIG. 4 is a schematic structural diagram of a pretreatment method of finished piece brushing wastewater;
wherein: 1-slicing and grinding process sewage collecting pipeline; 2-a centrifugal pump; 3-a centrifugal separator; 4-a liquid collecting tank; 5-first-stage natural settling separation wall; 6-secondary natural settling separation wall; 7-a sewage collecting pipeline in the acid washing process; 8-collecting sewage in an alkaline washing process; 9-pH neutralization tank; 10-pH measuring sensor; 11-a first pneumatic diaphragm pump; 12-lime water storage tank; 13-finished product piece brushing wastewater collection pipeline; 14-brushing a wastewater collecting tank; 15-a second pneumatic diaphragm pump; 16-a first solenoid valve; 17-a second solenoid valve; 18-a liquid level sensor; 19-control signal transmission loop; 20-a sewage treatment station; 21-water pipeline for the procedures of brushing waste water reinjection slicing and grinding; 22-industrial tap water line.
Detailed Description
In order that the present invention may be more clearly understood, the following detailed description is given in conjunction with the examples. The present invention will now be described in further detail with reference to the accompanying drawings. These drawings are simplified schematic views illustrating only the basic structure of the present invention in a schematic manner, and thus show only the constitution related to the present invention.
Example 1
FIG. 1 shows a flow chart of an intelligent sewage treatment method of a sapphire substrate factory, and as shown in FIG. 1, firstly, sewage generated in a sapphire substrate production process is classified according to characteristics, including a. slicing and grinding process sewage; b. acid washing and alkali washing process sewage; c. the finished product pieces scrub the waste water; d. sewage from other processes; slicing and grinding the sewage in the step a; b. acid washing and alkali washing process sewage; c. respectively pretreating the finished piece brushing wastewater; finally, inputting the pretreated sewage and sewage of other procedures into a sewage treatment station for unified treatment;
referring to fig. 1 and fig. 2, (1) sewage collected by a sewage collecting pipeline 1 in the slicing and grinding process is pressurized by a centrifugal pump 2 and then enters a centrifugal separator 3, large-particle solid impurities are discharged after separation by the centrifugal separator 3, and the rest sewage enters a liquid collecting tank 4; (2) the sewage in the liquid collecting tank 4 overflows to a sewage treatment station 20 after two-stage natural sedimentation through a primary natural sedimentation partition wall 5 and a secondary natural sedimentation partition wall 6;
referring to fig. 1 and 3, (1) the sewage collected by the sewage collecting pipeline 7 of the acid washing process and the sewage collected by the sewage collecting pipeline 8 of the alkali washing process are neutralized in a pH neutralization tank 9; (2) when the pH value measured by the pH value measuring sensor 10 is lower than a set value (pH 7), transmitting a start signal to the first pneumatic diaphragm pump 11, and starting the first pneumatic diaphragm pump 11; (3) after the first pneumatic diaphragm pump 11 is started, lime water is pumped into the pH neutralization pond 9 from the lime water storage tank 12 to neutralize excessive acid-containing sewage; (4) when the pH value measured by the pH value measuring sensor 10 reaches a set value, a stop signal is transmitted to the first pneumatic diaphragm pump 11, and the first pneumatic diaphragm pump 11 stops running (the sapphire substrate processing technology determines that the amount of acid-containing sewage is certainly larger than that of alkali-containing sewage, so that only lime water is needed to neutralize the acid sewage in the pH neutralizing tank 9); (5) the sewage neutralized by the pH neutralization tank 9 naturally overflows to a sewage treatment station 20;
referring to fig. 1 and 4, (1) the finished piece brushing wastewater collecting pipeline 13 collects the brushed wastewater into the brushing wastewater collecting tank 14 (note: the finished piece brushing wastewater has better water quality than industrial tap water, and can be used for slicing and grinding processes); (2) when the liquid level sensor 18 senses the liquid level, transmitting an opening signal to the first electromagnetic valve 16, and reinjecting the slice by using the second pneumatic diaphragm pump 15 and the scrubbing wastewater, and reinjecting the finished product slice by using the water pipeline 21 in the grinding process to scrub the wastewater to the slicing and grinding process for use; (3) when the liquid level sensor 18 does not sense the liquid level, an opening signal is transmitted to the second electromagnetic valve 17, the industrial tap water pipeline 22 is opened, the shortage of finished product piece brushing wastewater is supplemented by the industrial tap water reinjection slicing and grinding process water pipeline 21, and meanwhile, the first electromagnetic valve 16 is closed to prevent the industrial tap water from flowing back to the brushing wastewater collecting tank 14; (4) when the liquid level in the brushing wastewater collecting tank 14 is higher than the overflow port, the brushing wastewater automatically overflows to the sewage treatment station 20; the whole sewage treatment system is controlled by a control signal transmission loop 19.
It will be understood by those skilled in the art that, unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the prior art and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.
The meaning of "and/or" as used herein is intended to include both the individual components or both.
The term "connected" as used herein may mean either a direct connection between components or an indirect connection between components via other components.
The protection of the present invention is not limited to the above embodiments. Variations and advantages that may occur to those skilled in the art may be incorporated into the invention without departing from the spirit and scope of the inventive concept and the scope of the appended claims is intended to be protected.

Claims (2)

1. An intelligent sewage treatment method for a sapphire substrate factory is characterized by comprising the following steps:
(1) and (4) classification: classifying sewage generated in the sapphire substrate production process according to characteristics, wherein the sewage comprises a slicing and grinding process sewage; b. acid washing and alkali washing process sewage; c. the finished product pieces scrub the waste water; d. sewage from other processes;
(2) pretreatment: slicing and grinding process sewage in the step (1); b. acid washing and alkali washing process sewage; c. respectively pretreating the finished piece brushing wastewater;
(3) conventional sewage treatment: inputting the sewage pretreated in the step (2) and sewage of other procedures into a sewage treatment station for unified treatment;
in the pretreatment step of the step (2), a pretreatment method of sewage in slicing and grinding procedures is as follows:
(1) the sewage of the slicing and grinding process enters a centrifugal separator after being pressurized by a centrifugal pump, large-particle solid impurities are discharged after being separated by the centrifugal separator, and the rest sewage enters a liquid collecting tank;
(2) the sewage in the liquid collecting tank overflows to a sewage treatment station after natural sedimentation;
in the pretreatment step of the step (2), a pretreatment method of sewage in acid washing and alkali washing processes is as follows:
(1) neutralizing the sewage collected by the sewage collecting pipeline in the acid washing process and the sewage collected by the sewage collecting pipeline in the alkali washing process in a pH neutralization tank;
(2) when the pH value measured by the pH value measuring sensor is lower than a set value, transmitting a starting signal to the pneumatic diaphragm pump, and starting the pneumatic diaphragm pump to operate;
(3) after the pneumatic diaphragm pump is started, lime water is pumped into a pH neutralization pond to neutralize excessive acid-containing sewage;
(4) when the pH value measured by the pH value measuring sensor reaches a set value, transmitting a stop signal to the pneumatic diaphragm pump, and stopping the operation of the pneumatic diaphragm pump;
(5) naturally overflowing the sewage neutralized by the pH neutralization tank to a sewage treatment station;
in the pretreatment step of the step (2), the pretreatment method of the finished product piece brushing wastewater is as follows:
(1) collecting the scrubbed wastewater to a scrubbing wastewater collecting tank by a finished piece scrubbing wastewater collecting pipeline;
(2) when the liquid level sensor senses the liquid level, transmitting an opening signal to the first electromagnetic valve, and utilizing the second pneumatic diaphragm pump, a washing wastewater reinjection section and a grinding process to reinject a finished product sheet with a water pipeline to wash the wastewater to the section and grinding process for use;
(3) when the liquid level sensor cannot sense the liquid level, transmitting an opening signal to the second electromagnetic valve, opening an industrial tap water pipeline, supplementing the deficiency of finished product piece brushing wastewater by using the industrial tap water pipeline in the processes of reinjection slicing and grinding, and closing the first electromagnetic valve to prevent the industrial tap water from flowing back to the brushing wastewater collecting tank;
(4) when the liquid level in the brushing wastewater collecting tank is higher than the overflow port, the brushing wastewater automatically overflows to a sewage treatment station.
2. The intelligent wastewater treatment method of sapphire substrate factory as recited in claim 1, wherein said pH setting value is between 6-8.
CN201810805264.2A 2018-07-20 2018-07-20 Intelligent sewage treatment method for sapphire substrate factory Active CN108975533B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810805264.2A CN108975533B (en) 2018-07-20 2018-07-20 Intelligent sewage treatment method for sapphire substrate factory

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810805264.2A CN108975533B (en) 2018-07-20 2018-07-20 Intelligent sewage treatment method for sapphire substrate factory

Publications (2)

Publication Number Publication Date
CN108975533A CN108975533A (en) 2018-12-11
CN108975533B true CN108975533B (en) 2021-09-03

Family

ID=64549034

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810805264.2A Active CN108975533B (en) 2018-07-20 2018-07-20 Intelligent sewage treatment method for sapphire substrate factory

Country Status (1)

Country Link
CN (1) CN108975533B (en)

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08226923A (en) * 1995-02-22 1996-09-03 Hitachi Ltd Automatic analyzer
CN103319023A (en) * 2013-05-10 2013-09-25 浙江卓锦工程技术有限公司 Process and system for treatment of ceramic processing wastewater
JP5413587B2 (en) * 2009-10-22 2014-02-12 栗田工業株式会社 Ultrapure water production method and production apparatus for ion exchange resin purification equipment
CN104355440A (en) * 2014-10-24 2015-02-18 苏州富奇诺水治理设备有限公司 Sewage classified treatment method
CN205133285U (en) * 2015-10-22 2016-04-06 广东深泰环保科技有限公司 Circuit board processing procedure waste water classification system
CN106378876A (en) * 2016-09-23 2017-02-08 镇江环太硅科技有限公司 Diamond wire slicing cooling liquid integrated treatment method for sapphire and silicon wafers
CN106542673A (en) * 2016-11-08 2017-03-29 中国核电工程有限公司 A kind of nuclear power plant's on-radiation produces waste water reclamation Application way
CN106673080A (en) * 2015-11-10 2017-05-17 哈尔滨市宏天锐达科技有限公司 Environmental protection treatment method for recovery treatment and reutilization of wastewater in oil refining process
CN106865831A (en) * 2017-04-19 2017-06-20 杭州意来客电器设备有限公司 Sewage water treatment method and application
CN108117238A (en) * 2018-02-12 2018-06-05 安徽江淮汽车集团股份有限公司 A kind of auto industry wastewater treatment fully automatic system and control method
CN108191177A (en) * 2018-03-25 2018-06-22 绍兴柯桥涵雷服饰科技有限公司 A kind of sheet plant effuent classification processing unit

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006061779A (en) * 2004-08-25 2006-03-09 Japan Organo Co Ltd Method and apparatus for treating and separating waste water
CN101386457A (en) * 2008-10-28 2009-03-18 北京首钢国际工程技术有限公司 Comprehensive recovery and utilization method of various waste waters in iron and steel plant
US8398006B2 (en) * 2010-11-24 2013-03-19 Organic Energy Corporation Mechanized separation of mixed solid waste and recovery of recyclable products
JP2012229481A (en) * 2011-04-27 2012-11-22 Japan Metals & Chem Co Ltd Method for separating and recovering valuable material from used lithium ion battery
CN102531280A (en) * 2011-12-16 2012-07-04 深圳市祐林环保有限公司 Method for treating wastewater of printed circuit board
CN107555673A (en) * 2017-09-20 2018-01-09 苏州东吴黄金文化发展有限公司 A kind of method of high efficiente callback electroforming waste liquid and useless underwater gold

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08226923A (en) * 1995-02-22 1996-09-03 Hitachi Ltd Automatic analyzer
JP5413587B2 (en) * 2009-10-22 2014-02-12 栗田工業株式会社 Ultrapure water production method and production apparatus for ion exchange resin purification equipment
CN103319023A (en) * 2013-05-10 2013-09-25 浙江卓锦工程技术有限公司 Process and system for treatment of ceramic processing wastewater
CN104355440A (en) * 2014-10-24 2015-02-18 苏州富奇诺水治理设备有限公司 Sewage classified treatment method
CN205133285U (en) * 2015-10-22 2016-04-06 广东深泰环保科技有限公司 Circuit board processing procedure waste water classification system
CN106673080A (en) * 2015-11-10 2017-05-17 哈尔滨市宏天锐达科技有限公司 Environmental protection treatment method for recovery treatment and reutilization of wastewater in oil refining process
CN106378876A (en) * 2016-09-23 2017-02-08 镇江环太硅科技有限公司 Diamond wire slicing cooling liquid integrated treatment method for sapphire and silicon wafers
CN106542673A (en) * 2016-11-08 2017-03-29 中国核电工程有限公司 A kind of nuclear power plant's on-radiation produces waste water reclamation Application way
CN106865831A (en) * 2017-04-19 2017-06-20 杭州意来客电器设备有限公司 Sewage water treatment method and application
CN108117238A (en) * 2018-02-12 2018-06-05 安徽江淮汽车集团股份有限公司 A kind of auto industry wastewater treatment fully automatic system and control method
CN108191177A (en) * 2018-03-25 2018-06-22 绍兴柯桥涵雷服饰科技有限公司 A kind of sheet plant effuent classification processing unit

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
"Multivariate Analysis and Chemometric Characterisation of Textile Wastewater Streams";Kavsek et al;《ACTA CHIMICA SLOVENICA》;20130618;第60卷(第2期);第375-382页 *
"含氰含铬电镀废水的分类处理工程实例";林华等;《工业水处理》;20091031;第29卷(第10期);第63-65页 *
"建筑陶瓷污水的性质和处理工艺优化研究";齐人斌等;《中国陶瓷》;20170228;第53卷(第2期);第77-81页 *

Also Published As

Publication number Publication date
CN108975533A (en) 2018-12-11

Similar Documents

Publication Publication Date Title
CN108532720A (en) Multifunctional rain storage pond intelligence control system and control method
CN208267000U (en) Recyclable reutilization system based on sanitary sewage
CN215861001U (en) Sediment stuff pump shaft seal water system
CN108975533B (en) Intelligent sewage treatment method for sapphire substrate factory
CN103086542B (en) Recycling process and system for wooden activated carbon industrial wastewater
CN104018210A (en) Electroplating washing device and washing system
CN106032298A (en) Household water purifying system with waste water recycling function
CN207063058U (en) A kind of effluent cycle reutilization system of energy-conserving and environment-protective
CN201835315U (en) Novel water environment treatment system in residential district
CN204981398U (en) Integrated equipment that technology drainage of running water water factory was retrieved
CN212425631U (en) Viscose fiber acid waste water sulfuric acid recycle system
CN114534497A (en) Automatic ultrafiltration control system
CN209446356U (en) Water quality online analyzer pretreatment unit
CN210280124U (en) Water system for inserting machine
LU505308B1 (en) Method for utilizing reuse water of industrial wastewater of power plant to desulfurization process water
CN208762315U (en) A kind of rainwater recycles the device of manufacture recirculated water
CN209161721U (en) A kind of strong brine minimizing device
CN106049622A (en) Wastewater recycling system for building
CN112591876A (en) Offline recovery cleaning method of distributed sewage treatment MBR system
CN205839889U (en) A kind of wastewater recycling system being applicable to building
CN215667188U (en) Waste water recycling system
CN204427966U (en) A kind of fully automatic water-saving Environment protection cleaning system
CN215480456U (en) Novel sludge recovery system that self-loopa was washed
CN216998011U (en) A sewage pretreatment systems for toothpaste manufacture factory
CN215823843U (en) Receive milk cleaning system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Application publication date: 20181211

Assignee: Zhejiang Zhaojing New Material Technology Co.,Ltd.

Assignor: JIANGSU JESHINE NEW MATERIAL Co.,Ltd.

Contract record no.: X2022980008188

Denomination of invention: An intelligent sewage treatment method for sapphire substrate factory

Granted publication date: 20210903

License type: Common License

Record date: 20220627

EE01 Entry into force of recordation of patent licensing contract
TR01 Transfer of patent right

Effective date of registration: 20230104

Address after: 100102 20628, Floor 2, Building A1, No. 1, Huangchang West Road, Dougezhuang, Chaoyang District, Beijing

Patentee after: Youran Walker (Beijing) Technology Co.,Ltd.

Address before: 212200 new materials Industrial Park, Youfang Town, Yangzhong City, Zhenjiang City, Jiangsu Province

Patentee before: JIANGSU JESHINE NEW MATERIAL Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20230626

Address after: 050035 No. 369, Zhujiang Avenue, high tech Zone, Shijiazhuang, Hebei

Patentee after: TUNGHSU GROUP Co.,Ltd.

Address before: 100102 20628, Floor 2, Building A1, No. 1, Huangchang West Road, Dougezhuang, Chaoyang District, Beijing

Patentee before: Youran Walker (Beijing) Technology Co.,Ltd.

TR01 Transfer of patent right