CN105505830A - Acinetobacter strain for producing biosurfactant and application of acinetobacter strain - Google Patents

Acinetobacter strain for producing biosurfactant and application of acinetobacter strain Download PDF

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CN105505830A
CN105505830A CN201610038100.2A CN201610038100A CN105505830A CN 105505830 A CN105505830 A CN 105505830A CN 201610038100 A CN201610038100 A CN 201610038100A CN 105505830 A CN105505830 A CN 105505830A
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surfactant
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acinetobacter
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李慧娟
孙云鹏
丁瑞
葛圣松
崔志芳
朱孔福
李誉琦
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Shandong University of Science and Technology
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Abstract

The invention provides an acinetobacter strain for producing a biosurfactant and an application of the acinetobacter strain. The acinetobacter strain is obtained from a petroleum foul land through enrichment culture, dilution coating, screening and purification and is authenticated as acinetobacter. The invention discloses an enrichment culture medium and a fermentation culture medium for screening the strain, and the properties of the biosurfactant produced from the strain are analyzed. A carbon source used in the culture media is whey powder which is leftover remained after the extraction of cheese and is low in price and cost; the strain is high in breeding speed and metabolism speed, the biosurfactant produced through the metabolism can act as a biological degreaser at the room temperature, and the strain is environmentally friendly, toxic-free, pollution-free and good in biodegradability; a high-temperature strong-alkali environment required by a traditional chemical method oil removing is avoided, the energy consumption and the operation danger coefficient are decreased, and the secondary environmental pollution is avoided; and the strain is stable in performance and has good industrial application value.

Description

The acinetobacter calcoaceticus strain of one strain biosurfactant production and application thereof
Technical field
The present invention relates to the application of the acinetobacter calcoaceticus of biological technical field, be specifically related to acinetobacter calcoaceticus strain and the application thereof of a strain biosurfactant production.
Background technology
Bio-surfactant is the amphipathic compound that microorganism oozy class in metabolic process contains hydrophilic radical (as amino acid or polypeptide, disaccharides, oligosaccharides or polysaccharide etc.) and lipophilic group (as saturated or unsaturated fatty alcohol or lipid acid etc.).Bio-surfactant, except the feature with chemical surfactant, also has following features: (1) has higher surfactivity at oil-water interface; (2) nontoxic, safety, readily biodegradable, environmental friendliness; (3) there is very strong grease emulsifying ability; (4) reaction product can introduce the chemical group of novel type, and wherein some group is that chemical process is difficult to synthesis, and molecular structure type is various; (5) just can using biosurfactant under normal temperature, condition of normal pressure; (6) raw material that fermentation strain produces bio-surfactant extensively to exist and inexpensive at nature, is typical " green " technique.
Bio-surfactant mainly comprises glycolipid, lipopeptid, phosphatide, lipid acid, polysaccharide-composite of lipid and neutral lipid derivative etc., and known bio-surfactant is based on glycolipid.Bio-surfactant is due to features such as its good solubilising, emulsification, reduction tensio-active agent and environment friendly, obtain in environment remediation on the improvement of oily(waste)water, petroleum pollution ground, oil recovery industry, the field such as clean and apply widely, and infiltrate to other field.Research shows, the oil displacement efficiency of bio-surfactant than chemical surfactant oil displacement efficiency height 3.5-8 doubly, and price is only 30% of chemical surfactant.Bio-surfactant substituted chemistry tensio-active agent gradually becomes a kind of new research tendency.
The oil removing of the normal nulling part of metal-plated pre-treatment and rust cleaning, be the important procedure of plating, the quality of electroplated component treatment before plating quality, directly affects electrolytic coating quality.According to statistics, the major cause of plating piece 90% quality accident causes because treatment before plating is improper.The traditional technology of oil removing before metal current plating, mainly contains thermokalite pyrochemistry washing out method, ultrasonic oil removal, chemical reagent except wet goods; Wherein high temperature alkaline process energy consumption is large, seriously polluted is eliminated; Ultrasonic oil removal is large because of facility investment, limits its application in practice; Chemical reagent oil removing is the deoiling method that application is maximum at present, but, there is following shortcoming in traditional chemical reagent oil removing: under normal temperature, deoiling effect is poor, must heat during use (mostly more than 70 DEG C), deoiling effect dies down gradually along with the aging of tank liquor, not only waste resource but also caused the secondary pollution of greasy dirt, body refuse, also there is the problems such as high spumescence, high alkalinity and seriously corroded.Therefore a kind of less energy-consumption, safety and environmental protection, easily degraded, high efficiency degreaser is badly in need of in industrial production.
Summary of the invention
The object of the invention is the bacterial strain by filtering out a strain biosurfactant production, the bio-surfactant utilizing this bacterial strain to produce, reaches normal temperature oil removing, and biodegradable, free of contamination effect, be applied to Metal plating pre-treatment.
Technical scheme of the present invention is: adopt enrichment culture, dilution spread, purifying to obtain strain X H-2 from petroleum pollution, through identifying that this bacterium is acinetobacter (Acinetobactersp.XH-2).And submitted to China General Microbiological culture presevation administrative center to carry out culture presevation.
Enrichment medium used is (w/v, %): magnesium chloride 2, dipotassium hydrogen phosphate 6, potassium primary phosphate 3.8, iron trichloride 0.5, ammonium chloride 10, and additional cosmoline carries out enrichment culture as sole carbon source.
Fermention medium used is (w/v, %): whey powder 0.1, SODIUMNITRATE 0.1, potassium primary phosphate 0.2, Sodium phosphate dibasic 0.6, magnesium chloride hexahydrate 0.02, sodium-chlor 2, micro-1mL/L, Tween801, pH are 6, and distilled water is prepared.
Described strain X H-2 is fermentation culture 48h in described fermention medium, 4 DEG C of centrifugal 20min of 10000rpm, get supernatant liquor 6mol/LHCl and adjust pH to 2.0, after extracting 2 times with isopyknic ethyl acetate solution, merge organic phase concentrated on Rotary Evaporators, concentrated solution is poured in beaker, after naturally volatilizing, namely obtain the crude product of tensio-active agent.
In order to study the characteristic of this bio-surfactant further, this crude product is used to carry out composition analysis, the mensuration of micelle-forming concentration and stability analysis.
The bio-surfactant main component that the present invention announces, is tentatively judged as glycolipid class through qualitative analysis and the results of FT-IR.
After measured, the micelle-forming concentration of this bio-surfactant is 200mg/L, significantly lower than conventional chemical surfactant as sodium laurylsulfonate (2120mg/L), cetyl trimethylammonium bromide (1300mg/L).
Be applied to the removal that length is respectively 4cm, 2cm and 0.3cm steel disc surface anticorrosion oil, deoiling effect is good, and the time is short, only needs 16min.
The advantage that the present invention has and positively effect are:
Applicant screens the bacterial strain of a strain biosurfactant production from petroleum pollution, called after acinetobacter calcoaceticus XH-2, adopt the method for biological fermentation, to extract the byproduct whey powder after cheese, SODIUMNITRATE, inorganic salt for raw material, acinetobacter calcoaceticus XH-2 is utilized to produce Glycolipids Biosurfactants via, this bio-surfactant, under normal temperature condition, can remove the cosmoline of metallic surface.
Carbon source used in the present invention is tankage whey powder remaining after extracting cheese, and cheap, cost is low; Microbial reproduction is fast, metabolism is fast, using the bio-surfactant of microbial metabolism generation as biological degreasing agent, namely it play a role at normal temperatures, product environmental protection, nontoxic pollution-free, biological degradability are good, avoid the high temperature strong alkali environment needed for conventional chemical methods oil removing, reduce energy consumption and operational hazards coefficient, avoid secondary environmental pollution; Bio-surfactant made by the present invention is after the high Inversion phenomenon of difference, pH process, and surface tension variations is little, and after this bio-surfactant boils 10min through 100 DEG C, its oil removal efficiency does not reduce, and has good industrial application value.
Accompanying drawing explanation
Fig. 1 is the Determination of Critical Micelle Concentration figure of strain X H-2 of the present invention institute biosurfactant production
Fig. 2 is the infrared absorpting light spectra of bio-surfactant of the present invention
Fig. 3 is the design sketch of bio-surfactant of the present invention for oil removing before metal plating
Embodiment
The screening of acinetobacter calcoaceticus (Acinetobactersp.XH-2) bacterial strain of embodiment 1 biosurfactant production.
Sample from by the soil of petroleum pollution, the sample that the present embodiment uses is on-the-spot by the soil sample of crude oil pollution for Shandong region Shengli Oil Field recovers the oil, take 5g soil sample at 50mL enrichment medium (w/v, %: magnesium chloride 2, dipotassium hydrogen phosphate 6, potassium primary phosphate 3.8, iron trichloride 0.5, ammonium chloride 10, additional cosmoline is as sole carbon source) in cultivate, take out 1mL nutrient solution to be forwarded to again in enrichment medium, transfer after 3 times; Dilution spread, on blood agar, carries out line purifying to there being the bacterial strain of transparent circle on LB solid medium.
By single colony inoculation good for purifying in the LB liquid nutrient medium of 5mL, fermention medium (the w/v do not optimized is transferred to after activation 12h, %: glucose 1, peptone 1, potassium primary phosphate 0.2, Sodium phosphate dibasic 0.6, magnesium chloride hexahydrate 0.02, micro-1mL/L) in, after fermentation culture 2d, thalline abandoned by centrifugal fermented liquid, do the experiment of oil extraction circle with supernatant liquor and utilize JK9913 type Full-automatic tension instrument to adopt suspension ring method chart surface tension, and carrying out oil removing experiment.
Its oil extraction loop diameter of the strain X H-2 screened is 4.5cm, and surface tension is 32.58mN/m, has certain deoiling effect.
Select strain X H-2 as the original strain of biological degreasing agent, through identifying that this Pseudomonas is in acinetobacter.
The fermentation technology optimization of embodiment 2 strain X H-2.
With surface tension and oil removing time for index, the fermention medium of strain X H-2 and fermentation condition are optimized.
From LB solid plate, the mono-colony inoculation of picking strain X H-2 is in the LB liquid nutrient medium of 5mL, and after activation 12h, be transferred in fermention medium, the rotating speed of shaking table is 160rpm, and temperature is set to 30 DEG C.
Using glucose, sucrose, lactose, whey powder, glycerine, sweet oil, deep-fried twisted dough sticks waste oil as carbon source, using peptone, SODIUMNITRATE, ammonium sulfate, yeast extract (ferment is carried), dregs of beans as nitrogenous source, after fermentation 2d, carry out the mensuration of surface tension and oil removing time, the results are shown in Table 1 and 2, mainly determine the suitableeest carbon nitrogen source according to the oil removing time; And then carrying out concentration optimization, carbon source concentration is set to (w/v, %) 0.1,0.5,1.5,3, is set to nitrogen concentration (w/v, %) and is set to 0.1,0.2,1,3; Determine that carbon source is 0.1% whey powder, nitrogenous source is 0.1% SODIUMNITRATE.
Initial pH is set to 5,6,7,8,9,10, additional 1%Tween80 and SDS tensio-active agent.
Fermention medium (w/v, %) after optimization is: whey powder 0.1, SODIUMNITRATE 0.1, potassium primary phosphate 0.2, Sodium phosphate dibasic 0.6, magnesium chloride hexahydrate 0.02, sodium-chlor 2, micro-1mL/L, Tween801, pH are 6, and distilled water is prepared.
Fermentation condition comprises inoculum size and plants the optimization in age, and inoculum size (v/v, %) is set to 1,2,3,4,8; By be in early growth period (6h), exponential phase (12h), stationary phase (20h), decline phase (30h) bacterial strain be transferred in the fermention medium optimized, determining optimum inoculation amount 4% and planting age is 12h.
Table 1 different carbon source kind to the metallic surface oil removing time and produce the surface tension table look-up of tensio-active agent
Table 2 different nitrogen sources kind to the metallic surface oil removing time and produce the surface tension table look-up of tensio-active agent
Embodiment 3 utilizes the strain X H-2 bio-surfactant produced that ferments to prepare biological degreasing agent.
The mono-bacterium colony of strain X H-2 on picking LB solid plate is after 5mLLB liquid nutrient medium activation 12h, be transferred in the fermention medium of embodiment 2 optimization by 4% inoculum size, at 30 DEG C, 160rpm shaking table top fermentation cultivation 2d, get in supernatant liquor culture dish holding after fermented liquid is centrifugal, by long 4cm, wide 2cm, high 0.3cm steel disc is placed in one, and observes and records the time needed for oil removing.The results are shown in A in accompanying drawing 3, figure and be depicted as steel disc surface coverage oil film, in figure, B is depicted as the oil film on steel disc surface by Ex-all, and oil removing shortest time is, after for some time placed by steel disc after C is depicted as oil removing in 16min, figure, occur iron rust, show that steel disc oil film is divided.
Embodiment 4 utilizes strain X H-2 fermentation culture to prepare bio-surfactant, and carries out the research of the mensuration of micelle-forming concentration, composition preliminary evaluation and stability.
The fermented liquid of strain X H-2 fermentation culture 2d is obtained according to the method for embodiment 3, in 4 DEG C, the centrifugal 20min of rotating speed of 10000rpm, get supernatant liquor 6mol/LHCl and adjust pH to 2.0, after extracting 2 times with isopyknic ethyl acetate solution, merge organic phase concentrated on Rotary Evaporators, poured into by concentrated solution in beaker, after naturally volatilizing, namely obtain the crude product of tensio-active agent, output is 3.1g/L.
Obtained crude product is made into 10,20,50,100,200,300,400,500, the aqueous solution of 1000mg/L, measure its surface tension respectively and be depicted as curve, seeing shown in accompanying drawing 1.When bio-surfactant solution is from 0-50mg/L, surface tension drops to 38.58mN/m very soon from 75mN/m; Later decline is slow; When surfactant concentration reaches 200mg/L, surface tension reduces to 33.12mN/m; Sample concentration is higher than after 200mg/L, and the surface tension of solution almost no longer declines; Therefore, the CMC value of this tensio-active agent is 200mg/L, is starkly lower than conventional chemical surfactant sodium laurylsulfonate (SDS, 2120mg/L), cetyl trimethylammonium bromide (CTAB, 1300mg/L), its good surfactivity is more conducive to practical application.
Methylene blue-chloroform test is adopted to identify the charging property of this bio-surfactant.In methylene blue-chloroform test, above-mentioned tensio-active agent crude product is made into the solution of 0.3g/L, gets 5mL surfactant soln, add 10mL methylene blue and 5mL chloroform successively, fully after mixing, observe after leaving standstill several minutes.Experimental result is that water layer darkens, and shows that this bio-surfactant is cationic surfactant.
Tensio-active agent crude product KBr pressed disc method is carried out infrared spectra (FT-IR) analysis.The results are shown in accompanying drawing 2, as can be seen from the figure, 3390cm -1near there is strong and wide absorption peak, show to there is a large amount of-OH in this molecule; 2924cm -1and 2854cm -1absorption vibration belong to the absorption peak of aliphatics C-H, and 1460cm -1neighbouring absorption peak can belong to continuous print C-H vibration on molecule carbon chain to be caused; 1671cm -1the absorption peak at place from the stretching vibration of carbonyl, 1728cm -1near have the comparatively strong and absorption peak of point, show the existence having ester group; 1074cm -1with 1025cm -1the absorption peak at place, from the stretching vibration of C-O-C key, shows to there is carboxylate group in this molecule.With the glycolipid class infrared spectrogram contrast delivered, tentatively determine that this bio-surfactant is glycolipid compound.
Above-mentioned tensio-active agent crude product is made into the solution of 0.3g/L, carries out the stability analysis of this bio-surfactant under differing temps, pH and salinity process.
(1) temperature stability: this bio-surfactant solution is after (4 DEG C, room temperature, 60 DEG C, 100 DEG C) place 30min at different temperature, chart surface tension;
(2) pH stability: this bio-surfactant crude product different pH (2,4,6,8,10,12) buffer solution, after room temperature places 12h, chart surface tension;
(3) salinity stability: the solution of this bio-surfactant crude product different salinity (0-9%) is made into the solution that concentration is 0.3g/L, after room temperature places 12h, chart surface tension.
The results are shown in following table 3, under differing temps, pH and salinity process, surface tension variations is little, and this bio-surfactant has good stability and tolerance.The supernatant liquor of fermented liquid is after boiling water bath process 10min, and the impact of its oil removal efficiency is little.
Table 3 temperature, pH and salinity are on the impact of bio-surfactant stability
Above one embodiment of the present of invention have been described in detail, but described content being only preferred embodiment of the present invention, can not being considered to for limiting practical range of the present invention.All equalizations done according to the present patent application scope change and improve, and all should still belong within patent covering scope of the present invention.

Claims (5)

1. the acinetobacter calcoaceticus strain (Acinetobactersp.XH-2) of a strain biosurfactant production, is characterized in that: can produce bio-surfactant, and submits to China General Microbiological culture presevation administrative center to carry out culture presevation.
2. the acinetobacter calcoaceticus strain of a strain biosurfactant production according to claim 1, it is characterized in that: the screening method of described bacterial strain is: sample from by the soil of petroleum pollution, take 5g soil sample in 50mL enrichment medium, described enrichment medium (w/v, %) be: magnesium chloride 2, dipotassium hydrogen phosphate 6, potassium primary phosphate 3.8, iron trichloride 0.5, ammonium chloride 10 that additional cosmoline is as sole carbon source; Take out 1mL nutrient solution to be forwarded in enrichment medium, transfer after 3 times, dilution spread, on blood agar, carries out line purifying to there being the bacterial strain of transparent circle on LB solid medium again.
3. utilize the acinetobacter calcoaceticus strain of the strain biosurfactant production described in claim 1 to produce the method for bio-surfactant, it is characterized in that: from LB solid plate, picking list colony inoculation is in the LB liquid nutrient medium of 5mL, after activation 12h, be transferred in fermention medium, inoculum size 4%, fermention medium (w/v, %) be: whey powder 0.1, SODIUMNITRATE 0.1, potassium primary phosphate 0.2, Sodium phosphate dibasic 0.6, magnesium chloride hexahydrate 0.02, sodium-chlor 2, trace element 1mL/L, Tween801, pH is 6, distilled water is prepared, shaking speed is 160rpm, temperature is set to 30 DEG C, cultivate 2d, in 4 DEG C, the centrifugal 20min of 10000rpm, get supernatant liquor 6mol/LHCl and adjust pH to 2.0, after extracting 2 times with isopyknic ethyl acetate solution, merge organic phase concentrated on Rotary Evaporators, concentrated solution is poured in beaker, namely the crude product of tensio-active agent is obtained after naturally volatilizing.
4. method obtains bio-surfactant according to claim 3.
5. the application of bio-surfactant according to claim 4 before metal plating in oil removing.
CN201610038100.2A 2016-01-20 2016-01-20 The acinetobacter calcoaceticus strain and its application of one plant of biosurfactant production Expired - Fee Related CN105505830B (en)

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CN109652051A (en) * 2018-12-29 2019-04-19 克拉玛依中科恒信科技有限责任公司 Anti- newborn demulsification cleanup agent of one kind and preparation method thereof
CN111394271A (en) * 2019-09-12 2020-07-10 浙江大学 Acinetobacter for producing surfactant and application thereof
CN114075511A (en) * 2021-11-22 2022-02-22 山东科环环境管理咨询有限公司 Petroleum-polluted soil remediation agent and preparation process thereof

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Publication number Priority date Publication date Assignee Title
CN109652051A (en) * 2018-12-29 2019-04-19 克拉玛依中科恒信科技有限责任公司 Anti- newborn demulsification cleanup agent of one kind and preparation method thereof
CN111394271A (en) * 2019-09-12 2020-07-10 浙江大学 Acinetobacter for producing surfactant and application thereof
CN114075511A (en) * 2021-11-22 2022-02-22 山东科环环境管理咨询有限公司 Petroleum-polluted soil remediation agent and preparation process thereof

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