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  • 权利要求
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    • 专利摘要:
    1513837 Biochemical purification of oil well effluents SOC NATIONALE ELF AQUITAINE (PRODUCTION) 25 Nov 1975 [26 Nov 1975] 48407/75 Heading C1C A method of purifying effluents from oil well drilling, includes the following steps: (a) acidifying the effluent to precipitate the clay contained in it; (b) separating the precipitate formed; (c) neutralizing the liquid separated from the precipitate; (d) adding to said liquid a bacterial culture which has been obtained by aerobic growth of sewage or soil bacteria in an aqueous medium which contains oil well drilling additive and nutrient substance containing nitrogen and phosphorus but not carbon; (e) adding to said liquid nitrogen and phosphorus bearing nutrient substances and allowing it to stand in aerobic condition until the bacteria have substantially grown and until the biochemical oxygen demand of the liquid has decreased to below a predetermined limit; (f) separating the liquid with the view to discarding it, and recovering a fraction of the remaining bacteria mycelium. The final liquid (f) may be treated further with a chemical flocculating agent to give a further precipitate and a non-polluting liquid effluent. The growth of bacteria in (e) may be allowed to continue until the BOD of the liquid does not exceed 40 mg/1; the time taken may be 5 to 10 hours at ambient temperature. The acidification (a) is carried out to give a pH of 5 while in the neutralization (c) the pH is 6 to 8.
    公开号:SU793375A3
    申请号:SU752193206
    申请日:1975-11-26
    公开日:1980-12-30
    发明作者:Гийерм Мишель；Гратакос Жейм；Сирвинс Андре；Трамье Бернар
    申请人:Сосьете Насьональ Де Петроль Д"Акитэн (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR CLEANING WASTE WATER
    The invention relates to methods for treating wastewater containing leagues, nosulphonates and / or biopolymers, and can be used in the purification of sewage formed during the drilling of oil wells. A known method of treating wastewater generated during the drilling of oil wells and containing lignosulphonates, which consists in that the effluent is treated with mineral acid, such as sulfuric, hydrochloric, nitric, to a pH of 2.5-6, the sediment is removed and the purification of the water carried out with the help of natural silicates silt oxides or metal hydroxides ij. The degree of purification from lignosulfonates is 60%. In order to increase the degree of purification before the purification, water is neutralized to a pH of 6-8 and subjected to biological purification with adapted microorganisms with nitrogen and phosphorus as a nutrient feed. Preferably, 40-60% of nitrogen is introduced in the form of nitrates, and 60-40% in the form of ammonium salts, and the purification of water is carried out. With a salt of iron or gshyumin and lime. The wastewater generated by the drilling of wells contains organic compounds that contain carbon, namely lignosulfonates or polysaccharides, known as biopolymers. Having been subjected to biological treatment of wastewater, only nitrogen and phosphorus are introduced as nutrient feed into them. Thus, carbon-containing substances are not introduced into the sewage, which force microorganisms to biologically affect the presence of carbon-containing substances in the sewage water, in particular lignosulfonates, and thus destroy IR. The method is carried out as follows (Cym. The waste water formed during oil drilling is acidified with a supernatural acid to precipitate the clay contained in them. The sediment is removed and the water is neutralized to pH 6-8 and subjected to biological purification, in the presence of adapted microorganisms and nutrients in the form of nitrogen and phosphorus compounds.
    For example, it is possible to prepare in advance pieces of microorganisms grown in drilling muds containing lignosulfonates or biopolymers; the strains are then consumed to treat wastewater containing such substances.
    Ammonium nitrate, ammonium sulfate and ammonium phosphate are introduced as nitrogen and phosphorus compounds.
    Water after biological treatment is subjected to purification with an iron or aluminum salt and lime.
    Example. 100 m of clean water is injected into a tank, 20 m of drilling mud are injected and treated with sulfuric acid to pH 5. Flrul clay is present in the waste water. The waste is separated, and the water is neutralized to pH 6, nutrient supplements are introduced in the form of nitrogen and phosphorus compounds, and microorganisms adapted to lignosulfonates. If it is necessary to bring the final value of the MIC (biological oxygen consumption) to a minimum of 10-20, water is subjected to additional purification with salts of iron or aluminum and lime.
    In tab. Figure 1 shows the comparative results of the experiment on three different waste waters containing lignosulfonates, without additional purification of water with salts of iron or aluminum and lime.
    MIC waste
    water mg
    MIC after processing, processing, MGO2 / L
    Degree of cleaning,% MIC before processing, MGOp / L MIC after processing, 113 27 56 17.5 Degree of cleaning,% 72 93 80 94
    Thus, the degree of purification by this method without the reagent purification of water is 75-80%, and only 39-60% is known.
    PRI mme R 2. The experiment was carried out as in Example 1, but with liquid wastes containing lignosulfonates with VPK 500 mg. The experiment was continued for 7 days, after which MIC 38 mg-Ol / l. The obtained (adapted culture) of microorganisms can be introduced into wastewater containing lignosulfonates.
    Example 3. To the precipitate obtained as a result of water treatment in Example 1, 100 m of liquid drilling flows containing biopolymers were added, the pH was adjusted to 7. Ammonium nitrate was added to the mixture in an amount of 5 mg of nitrogen per liter (per 100 mg O2 / l for MIC). Air is dispersed into water for 6 hours. Upon reaching the MIC
    0 40 mgOl / l stop the flow of air and stand for 1 hour. Take the supernatant in a volume of 75 m. 100 m of liquid waste is added to the remaining drilling fluid and the treatment is repeated 5.
    The operation can be repeated up to three times. The purity of the MIC is 93.0%.
    In tab. Figure 2 shows the characteristics of the wastewater before and after treatment, including after-treatment of water. After biological treatment.
    Table 1
    145 145
    230 230
    141
    29 83
    58
    80 43
    39
    75
    Table 2 230 - 145 58 8 29 75 97 80 84 COD before treatment, 2080 - 980 mgOl / l COD nocyie obra1500 404 1000 28 cleanings, mgOp / l Degree of purification. 28 81 - 65 Suspended substances before treatment mg / l 685 Suspended substances after treatment 1140 O 1110 5 ki, mg / l Purification degree,% Hydrocarbons up to 12 - - treatment, mg / l
    Hydrocarbons after treatment, mg / l 6
    50
    权利要求:
    Claims (3)
    [1]
    Degree of cleaning,% 1 - without additional treatment; 2nd water purification. Claim 1. The method of purification of wastewater generated during the drilling of oil wells and containing lignosulfonates, which includes treatment with mineral acid, separation of sediment and additional treatment of water, characterized in that, in order to increase the degree of purification, before purification water is neutralized to pH 6 8 and subjected to biological purification by adapted microorganisms with the introduction of nitrogen and phosphorus compounds as biogenic nutrition.
    Table 2 100 - 99
    2 o 12 4
    13 75 80 100 54 85 1250 -980 1250 480800300 O 621969 600 -400 730 O450O 100-100
    [2]
    2. Method pop. 1, differing from the fact that 40-60% of nitrogen compounds are introduced in the form of nitrates, and 60-40% in the form of ammonium salts.
    [3]
    3. The method according to paragraph.n. 1 and 2, about the fact that after-treatment of water is carried out with an iron or aluminum salt and lime. Sources of information taken into account during the examination 1. Acceptance of France, 2205485, CL.C 02 C 1/00, C 02 C 5/00, 1974.
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    Semenova et al.2015|Improved flowsheet of wastewater treatment from nitrogen a containing compounds
    同族专利:
    公开号 | 公开日
    IT1049723B|1981-02-10|
    US4035289A|1977-07-12|
    EG12077A|1979-03-31|
    ES442786A1|1977-04-01|
    AT345226B|1978-09-11|
    CH609018A5|1979-02-15|
    NO146462C|1982-10-06|
    FR2292677A1|1976-06-25|
    DE2553146C2|1983-05-05|
    NO146462B|1982-06-28|
    CA1054268A|1979-05-08|
    FR2292677B1|1979-02-23|
    ATA888175A|1978-01-15|
    DE2553146A1|1976-08-12|
    NO753930L|1976-05-28|
    MX3086E|1980-03-27|
    BE835739A|1976-05-19|
    NL7513436A|1976-05-31|
    GB1513837A|1978-06-14|
    AU8680975A|1977-06-09|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    LT5057B|2001-12-05|2003-09-25|Viešoji Įstaiga "Grunto Valymo Technologijos"|Biological preparation for removing crude oil and petroleum product contaminants from soil and water, method for production and use thereof|US2259419A|1937-10-23|1941-10-14|Dow Chemical Co|Well drilling|
    US3152983A|1961-12-12|1964-10-13|Socony Mobil Oil Co Inc|Microbial disposal of oily wastes|
    JPS5113348B1|1968-04-27|1976-04-27|
    US3763038A|1970-04-10|1973-10-02|Kurita Water Ind Ltd|Process for purifying water that contains organic matter|
    US3871956A|1970-06-03|1975-03-18|Bioteknika International|Microbial degradation of petroleum|
    US3728253A|1971-05-05|1973-04-17|Univ California|Accelerated biological-chemical wastewater treatment|
    US3933627A|1971-06-28|1976-01-20|Banque Pour L'expansion Industrielle "Banexi"|Process for biologically eliminating organic waste matter|US4234421A|1979-03-05|1980-11-18|Dover Jr Virgil L|Land restoration following oil-well drilling|
    US4353803A|1979-03-05|1982-10-12|Dover Jr Virgil L|Land restoration following oil-well drilling and products useful therefor|
    EP0030803A1|1979-12-05|1981-06-24|Serck Industries Limited|Apparatus and method for treating an aqueous effluent which contains suspended oil particles|
    US4536293A|1981-06-30|1985-08-20|Babineaux Iii David|Method of treating waste water|
    US4447330A|1981-06-30|1984-05-08|Babineaux Iii David|Method of treating waste water|
    JPS58194799A|1982-05-07|1983-11-12|Hitachi Ltd|Preparation of silicon single crystal|
    DE3245593A1|1982-07-03|1983-06-09|Wolfgang 7982 Baienfurt Kappler|METHOD FOR DISPOSAL OF USED DEEP DRILLING|
    US4818410B1|1988-01-14|1998-06-30|Petrolite Corp|Method of removing water soluble organics from oil process water|
    CA2084881C|1990-06-08|1998-01-06|John Cunningham|Controlled-release microbe nutrients and method for bioremediation|
    FR2669916B1|1990-11-30|1993-09-10|Lyonnaise Eaux Dumez|METHOD FOR THE BIOLOGICAL DEGRADATION OF FAT AND GREASE WASTE.|
    US5354477A|1992-04-07|1994-10-11|Champion Technologies|Low molecular weight amines and amine quaternaries for the removal of soluble organics in oil field produced water|
    US5364532A|1992-09-03|1994-11-15|Petrolite Corporation|Method of removing water soluble organics from oil process water|
    US5637223A|1992-09-03|1997-06-10|Petrolite Corporation|Method of removing water soluble organics from oil process water|
    US5853592A|1992-09-03|1998-12-29|Baker Hughes Incorporated|Method of removing water soluble organics from oil process water with an organic acid and a mineral acid having a plurality of pKa's|
    US5314620A|1993-04-02|1994-05-24|Harvey Universal, Inc.|Cutting oil treatment|
    US5632886A|1993-04-02|1997-05-27|Harvey Universal, Inc.|Cutting oil treatment apparatus|
    US6159379A|1999-05-04|2000-12-12|Baker Hughes Incorporated|Organic ammonium salts for the removal of water soluble organics in produced water|
    GB2358015A|2000-01-07|2001-07-11|Cuthbertson Maunsell Ltd|Treatment of oil-based drilling mud cuttings|
    WO2002033031A1|2000-10-17|2002-04-25|Earth Alive Resources Inc.|Cleaning solution to remove hydrocarbons from a substrate|
    US7052901B2|2000-10-31|2006-05-30|Baker Hughes Incorporated|Bacteria-based and enzyme-based mechanisms and products for viscosity reduction breaking of viscoelastic fluids|
    US20070029752A1|2004-09-17|2007-02-08|Mccann Edward D|Apparatus for transporting drilling fluid additives and methods of making and using same|
    CA2683435A1|2007-04-04|2008-10-16|Tvt Us Corp.|Fixed film bioprocess for removing carbon compounds in oil and gas drilling sludge|
    EP2445601B1|2009-06-25|2014-09-03|FracPure Holdings LLC|Method of making pure salt from frac-water/wastewater|
    US9896355B2|2014-01-22|2018-02-20|Michael Green|Method and apparatus for an expandable industrial waste water treatment system|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7438681A|FR2292677B1|1974-11-26|1974-11-26|
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