CN109179753A - A kind of the demineralized water production technology and its special equipment of coal chemical industry - Google Patents

A kind of the demineralized water production technology and its special equipment of coal chemical industry Download PDF

Info

Publication number
CN109179753A
CN109179753A CN201811086813.1A CN201811086813A CN109179753A CN 109179753 A CN109179753 A CN 109179753A CN 201811086813 A CN201811086813 A CN 201811086813A CN 109179753 A CN109179753 A CN 109179753A
Authority
CN
China
Prior art keywords
water
reverse osmosis
concentrated
connect
coal chemical
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.)
Pending
Application number
CN201811086813.1A
Other languages
Chinese (zh)
Inventor
夏俊方
方小琴
尹竞
周耀水
张萌
肖龙博
陆魁
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.)
SHANGHAI JINGYU ENVIRONMENTAL ENGINEERING Co Ltd
Original Assignee
SHANGHAI JINGYU ENVIRONMENTAL ENGINEERING 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 SHANGHAI JINGYU ENVIRONMENTAL ENGINEERING Co Ltd filed Critical SHANGHAI JINGYU ENVIRONMENTAL ENGINEERING Co Ltd
Priority to CN201811086813.1A priority Critical patent/CN109179753A/en
Publication of CN109179753A publication Critical patent/CN109179753A/en
Pending legal-status Critical Current

Links

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
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • 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
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • 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
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions

Abstract

The invention discloses demineralized water production technologies and its special equipment of a kind of coal chemical industry, including reuse pool, first-stage reverse osmosis device, adsorbent equipment, second level reverse osmosis apparatus, oxidation reactor, mixed-bed resin tank and product pond etc..The technical process by by coal chemical industrial waste water handle it is up to standard after waste water recycling, then recycle-water using the series of process such as first-stage reverse osmosis, absorption, two-pass reverse osmosis, oxidation reaction, resin adsorption handle after obtain product water (resistivity >=5M Ω cm).This technique can be effectively removed remaining micro-content organism in recycle-water, so as to extend the regeneration period of mixed-bed resin, improve the production efficiency of demineralized water.

Description

A kind of the demineralized water production technology and its special equipment of coal chemical industry
Technical field
The invention belongs to coal chemical industry technical field of waste water processing, and in particular to a kind of desalination of coal chemical industry is aquatic Production. art and its special equipment.
Background technique
Coal chemical industry water consumption is big, and water pollution is serious, generates high risks to environment.Currently, coal chemical industry allows The project put into operation is mostly zero-emission project, and the waste water of generation carries out reuse and recycling is recycled with realistic meaning, such as It is extremely urgent what improves the problems such as recycle-water cyclic utilization rate.
Currently, coal chemical industry intermediate water reuse system mostly uses two steps ro, mixed-bed resin desalination process is used.Mixed bed Resin carries out ion exchange in water, carries out the purifying of water, uses and recycles in water power dodar to the 0.2 following return system of μ S/cm It uses.Resin has certain suction-operated to small organic molecule, and after absorption reaches saturation, organic molecule passes through mixed bed, causes Resin water outlet conductivity rises, mixed bed operation is abnormal, water-making ability decline, needs frequent progress resin regeneration, influences entire Coal chemical industry water system balance causes recycle-water can not internal consumption.Effectively to solve the problems, such as that mixed bed water-making ability declines, key exists In the removal of mixed bed entering organic matter of water.Contain micro-content organism currently, testing and analyzing in discovery water to recycle-water, minimizing technology has It is undesirable that effect is used alone in advanced oxidation processes, physisorphtion, biochemical method etc..
Summary of the invention
The present invention, which carries out easy in inactivation in desalting process for mixed-bed resin, leads to frequent regeneration and the low skill of water-making ability Art problem provides the demineralized water production technology and its special equipment of a kind of coal chemical industry, effectively removes remaining in recycle-water Micro-content organism solves the problems, such as that mixed bed water-making ability declines, extends the regeneration period of mixed-bed resin, improves reuse water circulation use Rate reduces Enterprises water operation cost.
Technical solution
In order to achieve the above technical purposes, the present invention provides a kind of demineralized water production technologies of coal chemical industry, special Sign is, it including the following steps:
(1) first-stage reverse osmosis: the recycle-water of coal chemical industrial waste water after processing is concentrated and separated, and obtains first-stage reverse osmosis production Water and concentrated water;
(2) it adsorbs: the first-stage reverse osmosis of step (1) being produced into water and carries out adsorption treatment, removal organic matter obtains absorption water outlet;
(3) oxidation reaction: the absorption water outlet in step (2) is subjected to oxidation reaction, remaining organic matter in water removal is gone to obtain Oxidation reaction water outlet;
(4) two-pass reverse osmosis: oxidation reaction water outlet in step (3) is concentrated and separated again, obtains two-pass reverse osmosis Produce water and concentrated water;
(5) resin adsorption: two-pass reverse osmosis obtained in step (4) is produced into water and carries out mixed-bed resin absorption, obtains desalination Water, that is, product water.
Further, in the step (1) during the concentration and separation of first-stage reverse osmosis, time of coal chemical industrial waste water after processing With water pH value between 5.5~7.5, operating pressure the salinity in recycle-water is concentrated, shape between 0.6~1.2MPa Water and concentrated water are produced at first-stage reverse osmosis, concentrated water carries out zero discharge treatment, produces water and carries out adsorption reaction.
Further, adsorbent absorption is utilized to guarantee organic matter removal in the step (2) during adsorption treatment.
Further, the absorption water outlet pH value of oxidation reaction is 7.0, the residence time 30~60 minutes in the step (3), oxygen Change reaction water outlet and carries out two-pass reverse osmosis processing.
Further, in the step (4) during the concentration and separation of two-pass reverse osmosis, the pH value of oxidation reaction water outlet exists Between 5.5~7.5, the production water of first-stage reverse osmosis is concentrated between 0.6~1.0MPa for operating pressure, and it is anti-to form second level Infiltration produces water and concentrated water, and concentrated water carries out reuse, produces water and carries out mixed-bed resin adsorption treatment.
A kind of special equipment of the demineralized water production technology of coal chemical industry, it is characterised in that: it includes first-stage reverse osmosis Device, adsorbent equipment, oxidation reactor, second level reverse osmosis apparatus, mixed-bed resin tank, raw water box, the first water producing tank, the first water inlet Case, the second inlet tank, the second water producing tank, product water tank, third water producing tank, the first intake pump, the second intake pump, third water inlet Pump, the 4th intake pump and the 5th intake pump;
The raw water box is connect with first-stage reverse osmosis device, and the first intake pump is housed on connecting line;The level-one reverse osmosis The concentrated water end of saturating device is connect with third water producing tank, is produced water end (W.E.) and is connect with the first water producing tank;First water producing tank and absorption fill Connection is set, the second intake pump is housed on connecting line;The water outlet of the adsorbent equipment is connect with the first inlet tank;Described first Inlet tank is connect with oxidation reactor device, and third intake pump is housed on connecting line;Oxidation reactor device water outlet It is connect with the second inlet tank;Second inlet tank is connect with second level reverse osmosis apparatus, and the 4th intake pump is housed on connecting line; The concentrated water end of the second level reverse osmosis apparatus is connect with raw water box, is produced water end (W.E.) and is connect with the second water producing tank;Second water producing tank It is connect with mixed-bed resin tank, the 5th intake pump is housed on connecting line.
Beneficial effect
A kind of demineralized water production technology and its special equipment for coal chemical industry provided by the invention, effectively removes back With micro-content organism remaining in water, solves the problems, such as that mixed bed water-making ability declines, extend the regeneration period of mixed-bed resin, improve back With water circulation use rate, Enterprises water operation cost is reduced.
Detailed description of the invention
Attached drawing 1 is the process flow chart of the embodiment of the present invention.
Attached drawing 2 is the equipment of the embodiment of the present invention connection relationship diagram.
Specific embodiment
With reference to the accompanying drawings and examples, the present invention will be further described.
Embodiment
As shown in Fig. 2, the special equipment of the demineralized water production technology of a kind of coal chemical industry, it includes first-stage reverse osmosis Device 1, adsorbent equipment 2, oxidation reactor 3, second level reverse osmosis apparatus 4, mixed-bed resin tank 5, raw water box 6, the first water producing tank 7, First inlet tank 8, the second inlet tank 9, the second water producing tank 10, product water tank 11, third water producing tank 12, the first intake pump 13, Two intake pumps 14, third intake pump 15, the 4th intake pump 16 and the 5th intake pump 17;
The raw water box 6 is connect with first-stage reverse osmosis device 1, and the first intake pump 13 is housed on connecting line;The level-one The concentrated water end of reverse osmosis unit 1 is connect with third water producing tank 13, is produced water end (W.E.) and is connect with the first water producing tank 7;First water producing tank 7 It is connect with adsorbent equipment 2, the second intake pump 14 is housed on connecting line;The water outlet of the adsorbent equipment 2 and the first inlet tank 8 Connection;First inlet tank 8 is connect with oxidation reactor device 3, and third intake pump 15 is housed on connecting line;The oxidation 3 water outlet of reactor assembly is connect with the second inlet tank 9;Second inlet tank 9 is connect with second level reverse osmosis apparatus 4, connection 4th intake pump 16 is housed on pipeline;The concentrated water end of the second level reverse osmosis apparatus 4 is connect with raw water box 6, produces water end (W.E.) and second Water producing tank 10 connects;Second water producing tank 10 is connect with mixed-bed resin tank 5, and the 5th intake pump 17 is housed on connecting line.
The demineralized water production technology of coal chemical industry is carried out using above-mentioned special equipment, it including the following steps:
The first step, the recycle-water of coal chemical industrial waste water after processing is concentrated and separated in first-stage reverse osmosis device 1, dense Division between pH value 5.5~7.5 of intaking, controls operating pressure between 0.6~1.2MPa from the process, will be in recycle-water Salinity is concentrated, and is formed first-stage reverse osmosis and is produced water and concentrated water, and concentrated water enters strong brine pond and carries out zero discharge treatment, produces water and enters Adsorption reaction process.
The first-stage reverse osmosis of the first step is produced water and is adsorbed to obtain adsorption reaction water outlet in adsorbent equipment 2 by second step, Such as organic matter is removed using activated carbon adsorption;
Absorption water outlet in second step is carried out oxidation reaction, obtains oxidation reaction water outlet, gone remaining in water removal by third step Organic matter, for water inlet pH value 7.0 or so, the residence time 30~60 minutes, oxidation reaction water outlet enters two-pass reverse osmosis process.
Oxidation reaction water outlet in third step is passed through second level reverse osmosis apparatus 4, is concentrated and separated, is being concentrated by the 4th step In separation process, between pH value 5.5~7.5 of intaking, operating pressure is controlled between 0.6~1.0MPa, by first-stage reverse osmosis It produces water to be concentrated, forms two-pass reverse osmosis and produce water and concentrated water, concentrated water enters reuse pool, produces water and enters in mixed-bed resin tank 5 Carry out adsorption reaction processing.
Structure depicted in this specification institute accompanying drawings of the embodiment of the present invention, ratio, size, quantity etc., only to cooperate specification Revealed content is not intended to limit the invention enforceable restriction item so that those skilled in the art understands and reads Part, therefore do not have technical essential meaning, the modification of any structure, the change of proportionate relationship or the adjustment of size are not influencing Under the effect of present invention can be generated and the purpose that can reach, it should all still fall in disclosed technology contents and obtain and can contain In the range of lid.Meanwhile it is cited such as "upper", "lower", "left", "right", " centre ", " clockwise ", " inverse time in this specification The term of needle " etc. is merely convenient to being illustrated for narration, rather than to limit the scope of the invention, relativeness It is altered or modified, under the content of no substantial changes in technology, when being also considered as the enforceable scope of the present invention.

Claims (6)

1. a kind of demineralized water production technology of coal chemical industry, which is characterized in that it including the following steps:
(1) first-stage reverse osmosis: the recycle-water of coal chemical industrial waste water after processing is concentrated and separated, obtain first-stage reverse osmosis produce water with Concentrated water;
(2) it adsorbs: the first-stage reverse osmosis of step (1) being produced into water and carries out adsorption treatment, removal organic matter obtains absorption water outlet;
(3) oxidation reaction: the absorption water outlet in step (2) is subjected to oxidation reaction, remaining organic matter in water removal is gone to be aoxidized Reaction water outlet;
(4) two-pass reverse osmosis: oxidation reaction water outlet in step (3) is concentrated and separated again, two-pass reverse osmosis is obtained and produces water With concentrated water;
(5) resin adsorption: two-pass reverse osmosis obtained in step (4) is produced into water and carries out mixed-bed resin absorption, obtains demineralized water i.e. Product water.
2. a kind of demineralized water production technology of coal chemical industry as described in claim 1, it is characterised in that: the step (1) During the concentration and separation of middle first-stage reverse osmosis, the recycle-water pH value of coal chemical industrial waste water after processing is between 5.5~7.5, behaviour Make pressure between 0.6~1.2MPa, the salinity in recycle-water is concentrated, forms first-stage reverse osmosis and produce water and concentrated water, it is dense Water carries out zero discharge treatment, produces water and carries out adsorption reaction.
3. a kind of demineralized water production technology of coal chemical industry as described in claim 1, it is characterised in that: the step (2) Adsorbent absorption is utilized to guarantee organic matter removal during middle adsorption treatment.
4. a kind of demineralized water production technology of coal chemical industry as described in claim 1, it is characterised in that: the step (3) 7.0, the residence time 30~60 minutes, oxidation reaction water outlet carries out at two-pass reverse osmosis the absorption water outlet pH value of middle oxidation reaction Reason.
5. a kind of demineralized water production technology of coal chemical industry as described in claim 1, it is characterised in that: the step (4) During the concentration and separation of middle two-pass reverse osmosis, the pH value of oxidation reaction water outlet between 5.5~7.5, operating pressure 0.6~ Between 1.0MPa, the production water of first-stage reverse osmosis is concentrated, two-pass reverse osmosis is formed and produces water and concentrated water, concentrated water carries out reuse, It produces water and carries out resin adsorption processing.
6. a kind of demineralized water production technology of coal chemical industry described in any one of the claims 1~5 claim Special equipment, it is characterised in that: it includes that first-stage reverse osmosis device (1), adsorbent equipment (2), oxidation reactor (3), second level are anti- Permeability apparatus (4), mixed-bed resin tank (5), raw water box (6), the first water producing tank (7), the first inlet tank (8), the second inlet tank (9), the second water producing tank (10), product water tank (11), third water producing tank (12), the first intake pump (13), the second intake pump (14), Third intake pump (15), the 4th intake pump (16) and the 5th intake pump (17);
The raw water box (6) connect with first-stage reverse osmosis device (1), and the first intake pump (13) are housed on connecting line;Described one The concentrated water end of grade reverse osmosis unit (1) is connect with third water producing tank (13), is produced water end (W.E.) and is connect with the first water producing tank (7);Described One water producing tank (7) is connect with adsorbent equipment (2), and the second intake pump (14) are housed on connecting line;The adsorbent equipment (2) goes out Water end (W.E.) is connect with the first inlet tank (8);First inlet tank (8) connect with oxidation reactor device (3), fills on connecting line There are third intake pump (15);Oxidation reactor device (3) water outlet is connect with the second inlet tank (9);Second water inlet Case (9) is connect with second level reverse osmosis apparatus (4), and the 4th intake pump (16) is housed on connecting line;The second level reverse osmosis apparatus (4) concentrated water end is connect with raw water box (6), is produced water end (W.E.) and is connect with the second water producing tank (10);Second water producing tank (10) and mixed Bed resin container (5) connects, and the 5th intake pump (17) is housed on connecting line.
CN201811086813.1A 2018-09-18 2018-09-18 A kind of the demineralized water production technology and its special equipment of coal chemical industry Pending CN109179753A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811086813.1A CN109179753A (en) 2018-09-18 2018-09-18 A kind of the demineralized water production technology and its special equipment of coal chemical industry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811086813.1A CN109179753A (en) 2018-09-18 2018-09-18 A kind of the demineralized water production technology and its special equipment of coal chemical industry

Publications (1)

Publication Number Publication Date
CN109179753A true CN109179753A (en) 2019-01-11

Family

ID=64911806

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811086813.1A Pending CN109179753A (en) 2018-09-18 2018-09-18 A kind of the demineralized water production technology and its special equipment of coal chemical industry

Country Status (1)

Country Link
CN (1) CN109179753A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104276709A (en) * 2014-09-30 2015-01-14 深圳能源资源综合开发有限公司 Coal chemical industry concentrated brine zero discharge technique and special equipment thereof
CN105417775A (en) * 2015-11-27 2016-03-23 宁波清水源水务科技有限公司 Reverse osmosis membrane treating and recycling method for printing and dyeing wastewater
CN106673290A (en) * 2016-12-26 2017-05-17 赛鼎工程有限公司 Zero-discharge treatment process for crushed coal pressurized gasification wastewater
CN209322593U (en) * 2018-09-18 2019-08-30 上海晶宇环境工程股份有限公司 A kind of special equipment of the demineralized water production technology of coal chemical industry

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104276709A (en) * 2014-09-30 2015-01-14 深圳能源资源综合开发有限公司 Coal chemical industry concentrated brine zero discharge technique and special equipment thereof
CN105417775A (en) * 2015-11-27 2016-03-23 宁波清水源水务科技有限公司 Reverse osmosis membrane treating and recycling method for printing and dyeing wastewater
CN106673290A (en) * 2016-12-26 2017-05-17 赛鼎工程有限公司 Zero-discharge treatment process for crushed coal pressurized gasification wastewater
CN209322593U (en) * 2018-09-18 2019-08-30 上海晶宇环境工程股份有限公司 A kind of special equipment of the demineralized water production technology of coal chemical industry

Similar Documents

Publication Publication Date Title
CN101781045B (en) Recycling and treating method for mine water containing suspended substances
CN101863530B (en) Continuous advanced treatment system of heavy metal ion-containing tail water and treatment method
CN102139976B (en) Treatment method for saliferous waste water from production process of MDI
CN103508637B (en) Traditional Chinese medicine wastewater treatment system and method for treating traditional Chinese medicine wastewater
CN104108813B (en) Refinery sewage desalination integrated processing technique and device
CN103641230B (en) Method for carrying out organic wastewater pretreatment by using an iron-carbon-Fenton-integrated reactor
CN105540971A (en) Process for crushed coal pressurized gasification industrial wastewater deep processing and high recovery rate
CN109133501A (en) Comprehensive treatment method for nonferrous metal ore wastewater
CN206266392U (en) A kind of papermaking wastewater zero-discharge treatment system
CN205258242U (en) Energy -concerving and environment -protective type heavy metal sewage treatment plant
CN107935300B (en) Process device and method for treating landfill leachate by non-membrane method
CN209322593U (en) A kind of special equipment of the demineralized water production technology of coal chemical industry
CN102963960B (en) Method for simultaneously recycling sulfuric acid and organic substances in m-cresol production wastewater
CN202072558U (en) Photovoltaic wastewater zero discharge system
CN101870505B (en) Method for using powdered resin for advanced treatment and reuse of printing and dyeing wastewater
CN102372337B (en) Method for advanced treatment and recycle of papermaking wastewater
CN202988881U (en) Waste acid and waste saline water treatment system combining inorganic synthesis with carbon absorption
CN202046959U (en) Reclaimed water reusing equipment
CN109179753A (en) A kind of the demineralized water production technology and its special equipment of coal chemical industry
CN105060575B (en) A kind of anti-electrodialysis of coupling and electrodialytic method for desalting seawater
CN103496807A (en) Industrial wastewater advanced treatment and recycling system
CN210796035U (en) High salt water recycling system that polycrystalline silicon production process produced
CN1644537A (en) Polyether polyatomic alcohol producing sewage recovering and utilizing treatment
CN204237642U (en) A kind of special purpose device of Coal Chemical Industry haline water purification process technique
CN103708652B (en) Industrial wastewater treatment method

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