CN102515333A - Special flocculant for oily wastewater and manufacturing method for same - Google Patents
Special flocculant for oily wastewater and manufacturing method for same Download PDFInfo
- Publication number
- CN102515333A CN102515333A CN2011104261454A CN201110426145A CN102515333A CN 102515333 A CN102515333 A CN 102515333A CN 2011104261454 A CN2011104261454 A CN 2011104261454A CN 201110426145 A CN201110426145 A CN 201110426145A CN 102515333 A CN102515333 A CN 102515333A
- Authority
- CN
- China
- Prior art keywords
- parts
- water
- ppm
- special
- zero
- 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
Links
Abstract
The invention relates to the technical field of oil-field water treatment chemical, particularly to a special flocculant for oily wastewater and a manufacturing method for the same. The special flocculant comprises the following ingredients in parts by weight: 5-8 parts of polydimethyldiallylammonium chloride, 1-5 parts of polyacrylamide (APAM), 10-30 parts of aluminium polychlorid and 70-80 parts of distilled water. The special flocculant is strong in flocculation capacity, capable of rapidly demulsifying, fast in sedimentation speed and small in the volume of flocculating body, as well as is a novel flocculant effective in both alkaline condition and neutral condition.
Description
Technical field
The present invention relates to oil field water treatment agent technical field, special-purpose flocculation agent of especially a kind of oily(waste)water and method of manufacture thereof.
Background technology
In the oilfield exploitation, primary oil recovery is a power by natural energy; Secondary oil recovery keeps reservoir pressure with the man-made injection mode; TOR is to improve tar productivity through changing the characteristic of injecting water.Secondary, TOR are mainly carried out in the oil field at present.Every production 1t crude oil needs water filling 2 3t approximately, and the extraction water content in crude oil constantly rises, and water ratio is generally up to 70%~95%.Therefore produce a large amount of oily(waste)waters; The waste water complicated component; Except natural impurity such as the oil in water emulsion that contains solubility salt and heavy metal, suspension, solid particulate, hydrogen sulfide; Also contain the chemicaladditives that some are used for changing recovered water character, and the acids that injects the stratum, oxygen scavenger, lubricant, sterilant, scale inhibitor etc.It directly is used for re-injection causes reservoir choke easily, quicken pipeline corrosion, efflux and pollute, therefore must could re-injection or discharging through strict the processing.The most of refinery of China uses and gathers sulphur aluminum chloride (PACS) as the agent of oily(waste)water flocculation treatment, and its main drawback is that the settling of floccus speed that forms is slow, in low temperature, low-cloudy water flocculation treatment, is prone to cause " race sail " phenomenon; Treatment effect is undesirable; And can bring secondary pollution to environment, foulings such as turnover pipeline, molten cylinder are serious, are difficult to remove.Bodied ferric sulfate (PFS) has characteristics such as flocculation ability is strong, alumen ustum is big, sedimentation is fast, and is applied widely, but also has avoided secondary pollution.But, use popularization difficult in the oil field because of complex manufacturing, cost height and the residual colourity in water.
Summary of the invention
The object of the present invention is to provide special-purpose flocculation agent of a kind of oily(waste)water and method of manufacture thereof; It mainly solves above-mentioned existing in prior technology defective; This special use flocculation agent have flocculation ability strong, can fast emulsion breaking, settling velocity is fast, the flocs unit volume is little, it is effective a kind of novel flocculant equally under alkalescence and neutrallty condition.
For realizing above-mentioned purpose, the present invention realizes like this.
The special-purpose flocculation agent of a kind of oily(waste)water, it is characterized in that: it is 5~8 parts of Poly Dimethyl Diallyl Ammonium Chlorides according to the composition of parts by weight, 1~5 part of SEPIGEL 305 (APAM), 10~30 parts of Poly aluminum Chloride (PAC)s, 70~80 parts of zero(ppm) water.
The method of manufacture of the special-purpose flocculation agent of a kind of aforesaid oily(waste)water is characterized in that: A, Poly Dimethyl Diallyl Ammonium Chloride is dissolved in 10 parts the zero(ppm) water and do not stop to stir, and subsequent use; B, SEPIGEL 305 is dissolved in 10 parts the zero(ppm) water and do not stop to stir, subsequent use; C, will remain zero(ppm) water and add in the reaction vessel; And stir; And then Poly aluminum Chloride (PAC) is added in the reaction vessel; Continuation is stirred, and will dissolve good Poly Dimethyl Diallyl Ammonium Chloride, polyacrylamide solution after 30 minutes and add in the reaction vessel, stirs after 1 hour to get product again.
The advantage that prescription of the present invention and method can embody is:
1, the Poly Dimethyl Diallyl Ammonium Chloride that uses in the special-purpose flocculation agent of the disclosed a kind of oily(waste)water of the present invention is a kind of strong cation polyelectrolyte; Have very strong breakdown of emulsion flocculation ability to containing oil-in-water emulsion in the sewage in a large number, also have very strong water separation capability simultaneously;
2, the SEPIGEL 305 (APAM) that uses in the special-purpose flocculation agent of the disclosed a kind of oily(waste)water of the present invention is for suspended particle; Thick, high, the particle band positive charge of concentration, water Ph value are neutral or alkaline sewage, owing to contain the solids that suspend in a certain amount of polar group ability planar water in the SEPIGEL 305 molecular chain; Making builds bridge between particle forms big throw out; Therefore it quickens the sedimentation of the particle in the suspension-s, and the clarification of very significantly accelerating solution is arranged, and promotes effects such as filtration.
2, it is big that the Poly aluminum Chloride (PAC) that uses in the special-purpose flocculation agent of the disclosed a kind of oily(waste)water of the present invention has a molecular structure, the characteristics of high adsorption capacity, and solvability is good in water, and active high, the alumen ustum that cohesion forms in water body is big, and sedimentation is fast, more must be in flocculating effect.
3,, especially in the oil field waste treating processes, use the special-purpose flocculation agent of oily(waste)water provided by the invention to have the breakdown of emulsion ability at oily(waste)water; And can precipitate by rapid flocculation, the flocculation particle is big and tight, and the flocculation quantity of slag is few; Be convenient to filtering separation; Water quality treatment is limpid, and each item index reaches secondary water filling and direct emission request, and cost is lower.
Embodiment
Embodiment 1:A, 5 parts of Poly Dimethyl Diallyl Ammonium Chlorides are dissolved in 10 parts the zero(ppm) water and do not stop to stir, subsequent use; B, 1 part of SEPIGEL 305 is dissolved in 10 parts the zero(ppm) water and do not stop to stir, subsequent use; C, 50 parts of zero(ppm) water are added in the reaction vessels; And stir; And then 10 parts of Poly aluminum Chloride (PAC)s are added in the reaction vessel; Continuation is stirred, and will dissolve good Poly Dimethyl Diallyl Ammonium Chloride, polyacrylamide solution after 30 minutes and add in the reaction vessel, stirs after 1 hour to get product again.
Embodiment 2:A, 6 parts of Poly Dimethyl Diallyl Ammonium Chlorides are dissolved in 10 parts the zero(ppm) water and do not stop to stir, subsequent use; B, 3 parts of SEPIGEL 305s are dissolved in 10 parts the zero(ppm) water and do not stop to stir, subsequent use; C, 60 parts of zero(ppm) water are added in the reaction vessels; And stir; And then 20 parts of Poly aluminum Chloride (PAC)s are added in the reaction vessel; Continuation is stirred, and will dissolve good Poly Dimethyl Diallyl Ammonium Chloride, polyacrylamide solution after 30 minutes and add in the reaction vessel, stirs after 1 hour to get product again.
Embodiment 3:A, 8 parts of Poly Dimethyl Diallyl Ammonium Chlorides are dissolved in 20 parts the zero(ppm) water and do not stop to stir, subsequent use; B, 5 parts of SEPIGEL 305s are dissolved in 20 parts the zero(ppm) water and do not stop to stir, subsequent use; C, 40 parts of zero(ppm) water are added in the reaction vessels; And stir; And then 30 parts of Poly aluminum Chloride (PAC)s are added in the reaction vessel; Continuation is stirred, and will dissolve good Poly Dimethyl Diallyl Ammonium Chloride, polyacrylamide solution after 30 minutes and add in the reaction vessel, stirs after 1 hour to get product again.
Being merely preferred embodiment of the present invention in sum, is not to be used for limiting practical range of the present invention.Be that all equivalences of doing according to the content of claim of the present invention change and modification, all should be technological category of the present invention.
Claims (2)
1. the special-purpose flocculation agent of an oily(waste)water, it is characterized in that: it is 5~8 parts of Poly Dimethyl Diallyl Ammonium Chlorides according to the composition of parts by weight, 1~5 part of SEPIGEL 305,10~30 parts of Poly aluminum Chloride (PAC)s, 70~80 parts of zero(ppm) water.
2. the method for manufacture of the special-purpose flocculation agent of oily(waste)water as claimed in claim 1 is characterized in that: A, Poly Dimethyl Diallyl Ammonium Chloride is dissolved in 10 parts the zero(ppm) water and do not stop to stir, and subsequent use; B, SEPIGEL 305 is dissolved in 10 parts the zero(ppm) water and do not stop to stir, subsequent use; C, will remain zero(ppm) water and add in the reaction vessel; And stir; And then Poly aluminum Chloride (PAC) is added in the reaction vessel; Continuation is stirred, and will dissolve good Poly Dimethyl Diallyl Ammonium Chloride, polyacrylamide solution after 30 minutes and add in the reaction vessel, stirs after 1 hour to get product again.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011104261454A CN102515333A (en) | 2011-12-19 | 2011-12-19 | Special flocculant for oily wastewater and manufacturing method for same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011104261454A CN102515333A (en) | 2011-12-19 | 2011-12-19 | Special flocculant for oily wastewater and manufacturing method for same |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102515333A true CN102515333A (en) | 2012-06-27 |
Family
ID=46286484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011104261454A Pending CN102515333A (en) | 2011-12-19 | 2011-12-19 | Special flocculant for oily wastewater and manufacturing method for same |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102515333A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104787845A (en) * | 2015-03-30 | 2015-07-22 | 金浦新材料股份有限公司 | Composite reverse-phase demulsifying agent for treating oil refinery sewage and preparation method of composite reverse-phase demulsifying agent |
CN105060446A (en) * | 2015-09-16 | 2015-11-18 | 天津亿利科能源科技发展股份有限公司 | Organic macromolecular flocculating agent for polymer-bearing sewage and preparation method for organic macromolecular flocculating agent |
CN105621565A (en) * | 2014-11-07 | 2016-06-01 | 中国石油天然气股份有限公司 | Composite water treatment agent for oil field wastewater, and preparation method thereof, and oil field wastewater treatment method |
CN104817150B (en) * | 2015-05-22 | 2016-07-20 | 华东理工大学 | A kind of compound demulsifying flocculant |
CN105967350A (en) * | 2016-07-07 | 2016-09-28 | 安徽国能亿盛环保科技有限公司 | Enzyme-containing sewage treating agent and preparation method thereof |
CN108217812A (en) * | 2018-01-10 | 2018-06-29 | 东莞市盛源石油化工有限公司 | A kind of oily waste water treatment agent |
CN110104836A (en) * | 2019-06-02 | 2019-08-09 | 上海纳米技术及应用国家工程研究中心有限公司 | A kind of enhanced processing method suitable for water-base cutting fluid waste water |
CN113683171A (en) * | 2020-05-19 | 2021-11-23 | 中海油能源发展股份有限公司 | Flocculant for treating polymer flooding output liquid and preparation method thereof |
CN114314958A (en) * | 2022-01-11 | 2022-04-12 | 大庆市中良科技开发有限公司 | Pretreatment method for crude oil electric desalting high-concentration sewage of refinery |
CN115536119A (en) * | 2022-11-01 | 2022-12-30 | 新疆聚力环保科技有限公司 | Waste water treatment agent for waste oil regeneration and preparation method thereof |
-
2011
- 2011-12-19 CN CN2011104261454A patent/CN102515333A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105621565A (en) * | 2014-11-07 | 2016-06-01 | 中国石油天然气股份有限公司 | Composite water treatment agent for oil field wastewater, and preparation method thereof, and oil field wastewater treatment method |
CN104787845A (en) * | 2015-03-30 | 2015-07-22 | 金浦新材料股份有限公司 | Composite reverse-phase demulsifying agent for treating oil refinery sewage and preparation method of composite reverse-phase demulsifying agent |
CN104817150B (en) * | 2015-05-22 | 2016-07-20 | 华东理工大学 | A kind of compound demulsifying flocculant |
CN105060446A (en) * | 2015-09-16 | 2015-11-18 | 天津亿利科能源科技发展股份有限公司 | Organic macromolecular flocculating agent for polymer-bearing sewage and preparation method for organic macromolecular flocculating agent |
CN105060446B (en) * | 2015-09-16 | 2017-06-13 | 天津亿利科能源科技发展股份有限公司 | Polymer-bearing waste-water treatment organic polymer coargulator and preparation method thereof |
CN105967350A (en) * | 2016-07-07 | 2016-09-28 | 安徽国能亿盛环保科技有限公司 | Enzyme-containing sewage treating agent and preparation method thereof |
CN108217812A (en) * | 2018-01-10 | 2018-06-29 | 东莞市盛源石油化工有限公司 | A kind of oily waste water treatment agent |
CN110104836A (en) * | 2019-06-02 | 2019-08-09 | 上海纳米技术及应用国家工程研究中心有限公司 | A kind of enhanced processing method suitable for water-base cutting fluid waste water |
CN113683171A (en) * | 2020-05-19 | 2021-11-23 | 中海油能源发展股份有限公司 | Flocculant for treating polymer flooding output liquid and preparation method thereof |
CN114314958A (en) * | 2022-01-11 | 2022-04-12 | 大庆市中良科技开发有限公司 | Pretreatment method for crude oil electric desalting high-concentration sewage of refinery |
CN114314958B (en) * | 2022-01-11 | 2023-12-26 | 大庆市中良科技开发有限公司 | Pretreatment method for electric desalting high-concentration sewage of crude oil in refinery |
CN115536119A (en) * | 2022-11-01 | 2022-12-30 | 新疆聚力环保科技有限公司 | Waste water treatment agent for waste oil regeneration and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102515333A (en) | Special flocculant for oily wastewater and manufacturing method for same | |
CN101066818B (en) | Process of treating oil-bearing sewage for ternary combination flooding in oil field | |
CN102863097B (en) | Standardized treatment reinjection method of sulfur-containing waste liquid of high sulfur-containing oil and gas field | |
US20100155337A1 (en) | Process of treating sewage in ternary combination flooding | |
CN102476877B (en) | Silicon-removing and oil-removing composite method of oil-containing sewage for boiler reuse | |
CN109574394B (en) | Fracturing flowback fluid treatment method | |
CN104826578A (en) | Fly ash modified adsorbent and preparing method thereof and method of treating oily sewage | |
CN103332666B (en) | Sinking agent in a kind of wet-process phosphoric acid concentration treating processes | |
CN102442748B (en) | Deep treatment method of naphthenic acid wastewater | |
CN106315795A (en) | Inorganic flocculating agent for coking waste water | |
CN103215064A (en) | Method for removing metal in high-acid heavy crude oil | |
Zhao et al. | Influence of using Enteromorpha extract as a coagulant aid on coagulation behavior and floc characteristics of traditional coagulant in Yellow River water treatment | |
CN102442747B (en) | Treatment method for discharging naphthenic acid wastewater within controlling index of national standard | |
CN106277430A (en) | A kind of fracturing outlet liquid being applicable to gas well processes and circulation utilization method | |
CN101746868B (en) | Composite flocculant for treating oily wastewater | |
Zeng et al. | Experimental study on chitosan composite flocculant for treating papermaking wastewater | |
CN103819060A (en) | Integrated disposal technology for waste emulsion liquid, electroplating wastewater and landfill leachate | |
CN113582316A (en) | Dithiocarbamate water purifier and preparation method and application thereof | |
CN105271466A (en) | Oily scum dehydrator and preparation method thereof | |
CN104478048B (en) | A kind of preparation method of Industrial Wastewater Treatment medicament | |
CN106630293A (en) | Emergency treatment method for antimony-exceeded waste water at low temperature | |
CN112939166A (en) | Flocculating agent for treating oil-containing sewage of delayed coking in petroleum refining | |
CN101323474A (en) | Novel oilfield sewage disposal coagulant | |
CN112250155A (en) | Heavy medium rapid-settling water treatment system and method | |
CN105668954B (en) | A method of it breaking steady medicament and breaks steady chemicals treatment oil field polymer-containing oil sludge using this |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C05 | Deemed withdrawal (patent law before 1993) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120627 |