CN101830593B - Zeolite pretreatment technology of high-concentration emulsified oil wastewater - Google Patents

Zeolite pretreatment technology of high-concentration emulsified oil wastewater Download PDF

Info

Publication number
CN101830593B
CN101830593B CN2010101778981A CN201010177898A CN101830593B CN 101830593 B CN101830593 B CN 101830593B CN 2010101778981 A CN2010101778981 A CN 2010101778981A CN 201010177898 A CN201010177898 A CN 201010177898A CN 101830593 B CN101830593 B CN 101830593B
Authority
CN
China
Prior art keywords
zeolite
emulsified oil
concentration
wastewater
concentration emulsified
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
CN2010101778981A
Other languages
Chinese (zh)
Other versions
CN101830593A (en
Inventor
袁松虎
吴高明
吴高宏
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.)
WUHAN WUTUO TECHNOLOGY Co Ltd
Original Assignee
WUHAN WUTUO 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 WUHAN WUTUO TECHNOLOGY Co Ltd filed Critical WUHAN WUTUO TECHNOLOGY Co Ltd
Priority to CN2010101778981A priority Critical patent/CN101830593B/en
Publication of CN101830593A publication Critical patent/CN101830593A/en
Application granted granted Critical
Publication of CN101830593B publication Critical patent/CN101830593B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Water Treatment By Sorption (AREA)

Abstract

The invention relates to a zeolite pretreatment technology of high-concentration emulsified oil wastewater, solving the problems that the existing treatment technology of emulsified oil wastewater has complex process, high operating cost and poor emulsified oil treatment effect, and is easy to cause secondary pollution. The technical scheme of the invention is as follows: firstly the temperature of high-concentration emulsified oil wastewater in an adjusting pool is adjusted to 0-70 DEG C, the pH value is adjusted to 0.5-2, secondly the high-concentration emulsified oil wastewater is sent to a device filled with zeolite particles, wherein the particle size of artificial zeolite is 10-50 meshes, the filling content is 2-10kg per cubic meter water and the residence time of wastewater is 0.5-2h; and finally effluent enters a post-treatment unit. The technology of the invention is simple and has low investment and operation costs, easy operations, no any chemical additive and no secondary pollution; and the oil content of the pretreated emulsified oil wastewater can be reduced to below 100mg/L and the CODCr can be lowered to below 2000mg/L, which completely meets the inflow requirements of the post-treatment biological treatment unit.

Description

The Zeolite pretreatment technology of high-concentration emulsified oil wastewater
Technical field
The present invention relates to a kind of waste water treatment process, the pretreated technology of employing zeolite of a kind of specifically metallurgy industry Steel Mill high-concentration emulsified oil wastewater.
Background technology
At steel industry, in order to eliminate the distortion heat that cold rolling of strip steel produces, cold rolling production uses emulsion to make lubricated or refrigerant mostly; Oil in water emulsion concentration is high; Mainly be made up of the MO more than the 2000mg/L or vegetables oil, emulsifying agent and water, oil in water emulsion is the milkiness shape in sewage, and oil droplet size is generally 0.1~25 μ m; The electronegative hydration shell of oil droplet appearance parcel one deck; Emulsification is steady state under the Action of Surfactant in water, and the elaioleucite stable for extended periods of time is difficult to separate with the method for machinery.The principal feature of Steel Mill's emulsifiable oil waste water is: 1. organic content is high, is generally COD Cr10000~25000mg/L; 2. complex chemical composition; Staple has oiliness improver, rust-inhibiting additive, hydrotropy additive and emulsifying agent etc., and 3. oily sub content is high, more than 2000mg/L; If do not deal carefully with; Certainly will cause severe contamination to environment, cause water body COD to raise, hydrobionts such as fish are difficult to existence and even dead.So the cold rolling of strip steel system of China Steel industry, the processing of emulsifiable oil waste water is a professional difficult problem always.
Processing to emulsifiable oil waste water at present mainly comprises physico-chemical processes, ultrafiltration membrance filter method and biological process.These three class methods respectively have shortcoming: (1) physico-chemical processes is through changing conditioned disjunction interpolation medicament emulsion to be taken off surely, thereby reaches the effect of breaking milk and removing oil, generally includes to add sour heating method and chemical agent breakdown of emulsion method.This method advantage is that reduced investment, treatment effect are good; But the assurance of process parameters is difficulty relatively; In addition, often need add various chemicaladditivess (like various flocculation agents) in the treating processes, can produce a large amount of chemical sludges; Like this, bring new problem of environmental pollution when having caused breakdown of emulsion to deoil.(2) ultrafiltration process belongs to membrane separation process, is to rely on film and pressure to reach separating effect, and it is effective to deoil, but its shortcoming is a facility investment expense height, and operational process is safeguarded complicated, is difficult to promote the wider application.(3) utilize the biological process oil removing, because the special state of oil in water emulsion, directly use biological process to handle to exist big problem, thereby the biological process use that normally combines with additive method is as carry out a biological disposal upon behind the chemical demulsification or after the ultrafiltration again.Cold-rolling emulsified oil reduces oil-contg and COD significantly through the physico-chemical process of front CrAfter the concentration, have biological degradability preferably, in follow-up anaerobism or aerobic treatment, organism wherein can effectively be utilized by the biological activity bacterial classification, realizes the further reduction and the standard wastewater discharge of pollutent.Physical chemistry-biota bonded method is maximum a kind of emulsion treatment process of domestic usefulness at present, but as previously mentioned, has serious secondary pollution problem equally as the physico-chemical processes of pretreatment technology.
Therefore the processing of emulsifiable oil waste water is the problem that experts and scholars study always, and and for example " environment protection " 1996 02 phases disclose and introduced the adsorption treatment of use natural zeolite replacement activated carbon to lower concentration oily(waste)water (oil content is less than 2%) in the paper that is called " pre-test of zeolite oil removing performance ".It is to adopt vesicular structure and the bigger serface characteristic of utilizing natural zeolite; Utilize absorption principle that the lower concentration oily substance in the waste water is adsorbed removal, there is following problem in this oil removing mode: 1, because be when utilizing absorption principle to remove the emulsifiable oil waste water of lower concentration; Because the loading capacity of zeolite is limited; Then must change zeolite immediately after saturated, regular lot is changed the increase that zeolite can cause running cost, and the discarded zeolite that changes can form stores; Its post-processed or regeneration are again technical barriers, cause processing cost high.2; For aforesaid high-concentration emulsified oil wastewater; If it is saturated to adopt the absorption principle processing then will soon reach absorption, deoiling effect is poor, when actual treatment great deal of high concentration emulsifiable oil waste water, is difficult to carry out; Therefore the zeolite treatment emulsifiable oil waste water only is in theoretical analysis and laboratory stage at present, is difficult to practical application.
Summary of the invention
To the objective of the invention is in order solving the problems of the technologies described above, to provide that a kind of technology is simple, investment and running cost is low, simple to operate, oil removal efficiency is high, the Zeolite pretreatment technology of the high-concentration emulsified oil wastewater of safety and non-secondary pollution.
Technical scheme of the present invention comprises that elder generation arrives 0-70 ℃ with the high-concentration emulsified oil wastewater temperature regulation in the equalizing tank, and pH sends into emulsifiable oil waste water then and is filled with artificial zeolite's particulate device to 0.5-2, and artificial zeolite's particle diameter is the 10-50 order, and loading level is 2-10kg/m 3Water, retention time of sewage are 0.5-2 hour, and last water outlet gets into the subsequent disposal unit.
Said adjusting high-concentration emulsified oil wastewater temperature is to regulate through in equalizing tank, feeding steam-heated method, and the pH value is to regulate through the method that adds the vitriol oil, and the vitriol oil can alleviate the corrosive nature to follow-up equipment.
Said artificial zeolite's particle diameter is the 30-50 order, and the amount of filling a vacancy is 5-10kg/m 3Water, the emulsifiable oil waste water residence time is 0.5-2 hour.
Acid waste water behind the breaking milk and removing oil adds alkali adjusting pH and further removes organic pollutant to coagulating sedimentation takes place between the 6-9 automatically, and water outlet gets into the subsequent disposal unit more then.Said pH value is regulated and can be selected as required, preferably adopts sodium hydroxide to regulate the pH value.
Said subsequent disposal unit is a biological processing unit.
Saidly be filled with artificial zeolite in artificial zeolite's particle device because of after the treatment of high concentration emulsifiable oil waste water consumed by part, can through additional artificial zeolite's particle in device with assurance device in artificial zeolite's loading level requirement.
Zeolite according to the invention is preferably the artificial zeolite owing to need under acidic conditions, to have certain dissolubility, and the artificial zeolite is that flyash and aqueous sodium hydroxide solution obtain material at 95 ℃ of following priming reactions, can on market, buy.
High-concentration emulsified oil wastewater according to the invention is meant the emulsion liquid of oil and tensio-active agent coexistence formation, and oil-contg even reaches more than the 5000mg/L COD more than 2000mg/L CrConcentration even can be up to 1,000,000 mg/L more than 10000mg/L.
Said artificial zeolite's particulate device that is filled with can be the device of tank or canned structure, can be used for filling the artificial zeolite and feeds emulsifiable oil waste water.
The contriver is through discover that the inorganic mineral in artificial zeolite's material can be dissolved out for many years under low pH condition; In the presence of the porous material artificial zeolite with high-concentration emulsified oil wastewater in tensio-active agent and oily substance react; Thereby make it take off the effect that surely reaches breakdown of emulsion, utilize this principle treatment of high concentration emulsifiable oil waste water effective.
Further, when the acid waste water of handling through the artificial zeolite requires to regulate PH to 6-9 for satisfying water outlet,, further remove organism and oil content, particularly COD because coagulating sedimentation can take place automatically in the variation of its acidic conditions CrContent.
Beneficial effect:
1, pretreatment technology effect of demulsification and oil removal of the present invention is good, is specially adapted to the treatment of high concentration oil in water emulsion, and the oil-contg of the emulsifiable oil waste water after the processing can drop to below the 100mg/L, COD CrBe reduced to below the 2000mg/L, can satisfy the unitary water inlet requirement of subsequent biological treatment fully, effectively guarantee the qualified discharge of final high-concentration emulsified oil wastewater, significant aspect energy-saving and emission-reduction that promote enterprise and Sustainable development.
2, processing unit of the present invention is very simple, the zeolite raw material is easy to get; Easy and simple to handle, to compare with the ultrafiltration oil removing process that present cold rolling mill generally adopts, cost of investment and running cost can reduce about 2/3rds; Need not to add any chemicaladditives, environment is not caused any secondary pollution.
3, the present invention has changed the usual understanding of present zeolite oil removing, is not the suction principle of utilizing zeolite; But discovered the consumption principle of zeolite, promptly under low PH condition, make the artificial zeolite be partly dissolved the back and react, with consumption artificial zeolite's principle oil removing with tensio-active agent and oily substance in the high-concentration emulsified oil wastewater; Therefore only need the zeolite of supplement consumed; And need not often to change zeolite, time saving and energy saving, easy and simple to handle; Can there be the post-processed problem of the saturated back of absorption zeolite yet, have further significantly reduced operation and maintenance cost.
4, the inventive method is specially adapted to handle the high-concentration emulsified oil wastewater from Steel Mill, for oil-containing and COD CrHigh other industry such as machinery industry cutting fluid oil in water emulsion and medical emulsifying liquid waste water are suitable for too.
Specific embodiment
Be example with emulsion below from Steel Mill and liquid medicine injection, further concrete elaboration implementation method of the present invention.
Embodiment 1:
Cold-rolling emulsion waste water is sent into equalizing tank, feed steam and adjust the temperature to 60 ℃, adding vitriol oil adjusting pH is 1, and (artificial zeolite's particle diameter is 30 orders, and loading level is 5kg/m then cold-rolling emulsion to be sent into artificial zeolite's jar 3Water), intermittently stir and continue reaction after 1 hour, tangible demulsifying phenomenon occurs, a large amount of scum silica frost appear in the waste water top layer, and the water body state is converted into limpid clear state by initial oyster white emulsification attitude.Continuation adds sodium hydroxide and regulates pH to 7-8 in the acidity of skim oil slick is useless, the immediate and obvious flocculation sediment, and water quality condition is clearly better, and reaction finishes the after-filtration water outlet.Monitoring result shows, initial oil content and COD in the emulsifiable oil waste water CrConcentration is respectively 5010mg/L and 56000mg/L, is reduced to 48mg/L and 1340mg/L after the pre-treatment respectively, satisfies the unitary water inlet requirement of subsequent biological treatment fully.After system moves for some time,, satisfy the filling requirement of zeolite through in artificial zeolite's jar, adding artificial zeolite's material to replenish the artificial zeolite who is disappeared and by consumption.
Embodiment 2, and just initial pH is that 7 medical injection emulsifying liquid waste waters are sent into equalizing tank, 0-70 ℃ of control emulsifying liquid waste water temperature, and adding vitriol oil adjusting pH is 0.5-2, (artificial zeolite's particle diameter is the 10-50 order, and loading level is 2-10kg/m to send into artificial zeolite's jar 3Water), intermittently stir and continue reaction after 0.5-2 hour, tangible demulsifying phenomenon occurs; A large amount of scum silica frost appear in the waste water top layer; The water body state is converted into limpid clear state by initial oyster white emulsification attitude, adds sodium hydroxide then and regulates pH to 6-9, the immediate and obvious flocculation sediment; Water quality condition is clearly better, and reaction finishes the after-filtration water outlet.Monitoring result shows, waste water COD Cr1000mg/L and 30mg/L have been reduced to oil concentration by 50000mg/L and 5000mg/L.
The comparative example 1: will be that 7 medical injection emulsifying liquid waste water is sent into equalizing tank with embodiment 2 identical initial pH, 0-70 ℃ of control emulsifying liquid waste water temperature do not regulated pH, and (artificial zeolite's particle diameter is the 10-50 order, and loading level is 2-10kg/m to send into artificial zeolite's jar 3Water), intermittently stir and continue reaction after 0.5-2 hour, do not observe any demulsifying phenomenon, monitoring result shows, waste water COD CrConcentration still about 50000mg/L, explains that simple zeolite adsorption can not produce treatment effect to high-concentration emulsified liquid.
The comparative example 2: just send into equalizing tank with embodiment 2 identical medical injection emulsifying liquid waste waters; 0-70 ℃ of control emulsifying liquid waste water temperature, adding vitriol oil adjusting pH is 0.5-2, but does not mix with zeolite; Intermittently stir and continue reaction after 0.5-2 hour; Do not observe any demulsifying phenomenon, monitoring result shows, waste water COD CrConcentration still about 50000mg/L, explains that simply adding the acid heating does not have treatment effect basically to high-concentration emulsified liquid.

Claims (7)

1. the Zeolite pretreatment technology of a high-concentration emulsified oil wastewater; It is characterized in that; Comprise earlier the high-concentration emulsified oil wastewater temperature regulation in the equalizing tank is arrived 0-70 ℃, pH sends high-concentration emulsified oil wastewater into the device that is filled with zeolite granular then to 0.5-2; Artificial zeolite's particle diameter is the 10-50 order, and loading level is 2-10kg/m 3Water, retention time of sewage are 0.5-2 hour, and last water outlet gets into the subsequent disposal unit.
2. the Zeolite pretreatment technology of high-concentration emulsified oil wastewater as claimed in claim 1 is characterized in that, said zeolite is the artificial zeolite.
3. the Zeolite pretreatment technology of high-concentration emulsified oil wastewater as claimed in claim 1; It is characterized in that; Said adjusting high-concentration emulsified oil wastewater temperature is to regulate through in equalizing tank, feeding steam-heated method, and the pH value is to regulate through the method that adds the vitriol oil.
4. like the Zeolite pretreatment technology of claim 1 or 2 or 3 described high-concentration emulsified oil wastewaters, it is characterized in that said zeolite particle diameter is the 30-50 order, loading level is 5-10kg/m 3Water, retention time of sewage are 0.5-2 hour.
5. like the Zeolite pretreatment technology of claim 1 or 2 or 3 described high-concentration emulsified oil wastewaters; It is characterized in that; Regulate pH to coagulating sedimentation takes place between the 6-9 automatically through the acid waste water after the zeolite oil removing, further remove organism, and then get into the subsequent disposal unit.
6. the Zeolite pretreatment technology of high-concentration emulsified oil wastewater as claimed in claim 1 is characterized in that, said subsequent disposal unit is a biological processing unit.
7. like the Zeolite pretreatment technology of claim 1 or 2 or 3 described high-concentration emulsified oil wastewaters; It is characterized in that; Saidly be filled with zeolite in the zeolite granular device because of after the treatment of high concentration emulsifiable oil waste water is partly dissolved consumption, through additional zeolite granular in device with assurance device in the loading level requirement of zeolite.
CN2010101778981A 2010-05-14 2010-05-14 Zeolite pretreatment technology of high-concentration emulsified oil wastewater Expired - Fee Related CN101830593B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010101778981A CN101830593B (en) 2010-05-14 2010-05-14 Zeolite pretreatment technology of high-concentration emulsified oil wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010101778981A CN101830593B (en) 2010-05-14 2010-05-14 Zeolite pretreatment technology of high-concentration emulsified oil wastewater

Publications (2)

Publication Number Publication Date
CN101830593A CN101830593A (en) 2010-09-15
CN101830593B true CN101830593B (en) 2012-07-04

Family

ID=42714836

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010101778981A Expired - Fee Related CN101830593B (en) 2010-05-14 2010-05-14 Zeolite pretreatment technology of high-concentration emulsified oil wastewater

Country Status (1)

Country Link
CN (1) CN101830593B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107055936A (en) * 2017-01-03 2017-08-18 浙江新化化工股份有限公司 A kind of preprocess method of high consistency perfume wastewater
CN111434621A (en) * 2019-01-11 2020-07-21 油服环境科技(广州)有限公司 Composite medicament for rapidly treating concentrated solution of emulsified oil wastewater
CN115259536B (en) * 2022-09-09 2024-06-11 云南曲靖呈钢钢铁(集团)有限公司 High-efficiency wastewater treatment system and technology for steel rolling production line

Also Published As

Publication number Publication date
CN101830593A (en) 2010-09-15

Similar Documents

Publication Publication Date Title
Yu et al. A review of treating oily wastewater
An et al. Emerging usage of electrocoagulation technology for oil removal from wastewater: a review
CN104163539B (en) A kind of processing method of coal chemical industrial waste water
CN103771650B (en) A kind for the treatment of process of coal gasification waste water
CN204824453U (en) Desulfurization pretreatment of water device that gives up
CN101475272A (en) Pretreatment process for oily watewater of cold rolling mill
CN105731707A (en) MVR processing unit and method for wastewater containing oil and salt
CN101519250B (en) Emulsifiable solution waste water processing method
CN101708912A (en) Emulsifying liquid wastewater membrane treatment process
CN207130086U (en) A kind of salt-containing waste water treating device
CN102145952A (en) Method for treating fracturing reverse drainage liquid of petroleum exploitation by microwave rapid catalysis
CN102344214B (en) Physicochemical comprehensive treatment system for dangerous waste liquid
CN104556535A (en) Sewage treatment method
CN106315973A (en) Treatment method of high-salt and high-calcium industrial wastewater
CN106277449A (en) The processing method of acidic industrial effluent
CN106277597A (en) The processing method of the higher fatty acid waste water of food industry
CN101830593B (en) Zeolite pretreatment technology of high-concentration emulsified oil wastewater
CN102583809A (en) Silicon and oil removing system for oily sewage
CN203922951U (en) A kind of fluorine-contained wastewater treatment system
CN103819060B (en) A kind of waste emulsified mixture, electroplating wastewater, Landfill joint disposal technology
CN201971688U (en) Silicon and oil removing system for oily sewage
CN106186559A (en) The processing method of high-sulfate height Organic substance industrial wastewater
CN101643251A (en) Method for treating oily wastewater in catering industry
CN207468425U (en) A kind of high-concentration emulsified liquid processing system
CN205616731U (en) Integrated advanced treatment unit who contains formaldehyde, methyl alcohol waste water

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

Granted publication date: 20120704

Termination date: 20180514

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