Summary of the invention
First object of the present invention is to provide a kind of fungal bacterial strain LP-16 (Fusarium oxysporum).
Second object of the present invention has been to provide the isolation medium of above-mentioned fungal bacterial strain.
The 3rd object of the present invention is to provide a kind of microbial inoculum that comprises above-mentioned fungal bacterial strain.
The 4th object of the present invention is to provide the preparation method of above-mentioned microbial inoculum.
The 5th object of the present invention is to provide a kind of zine ion treatment agent.
The 6th object of the present invention is to provide a kind of method of Treatment of Zinc-containing Wastewater.
For reaching this object, the present invention by the following technical solutions:
First aspect, the invention provides a kind of fungal bacterial strain LP-16 (Fusarium oxysporum), be preserved in China Committee for Culture Collection of Microorganisms's common micro-organisms center (CGMCC), address: No. 3, Yard 1, BeiChen xi Road, Chaoyang District, Beijing City, 100101, preservation date is on August 16th, 2013, and deposit number is CGMCC No.8037.
Second aspect, the invention provides a kind of as described in first aspect the isolation medium of fungal bacterial strain LP-16, for separating of described fungal bacterial strain LP-16; Described isolation medium comprises 0.1~0.4g/L sodium acetate, 0.05~0.2g/L yeast extract, 5~25g/L agar, 40~60mg/L Zn
2+, 0.01~0.12g/L MgSO
47H
2o, 0.001~0.010g/L K
2hPO
4with 0.05~0.2g/L paraxin, and pH=7.0;
Preferably, described isolation medium comprises 0.2~0.3g/L sodium acetate, 0.1~0.2g/L yeast extract, 10~20g/L agar, 45~55mg/L Zn
2+, 0.03~0.1g/L MgSO
47H
2o, 0.003~0.008g/L K
2hPO
4with 0.08~0.15g/L paraxin, and pH=7.0;
Further preferably, described isolation medium comprises 0.2461g/L sodium acetate, 0.15g/L yeast extract, 15g/L agar, 50mg/L Zn
2+, 0.05g/L MgSO
47H
2o, 0.005g/L K
2hPO
4with 0.1g/L paraxin, and pH=7.0.
Preferably, also add 2ml trace element solution in isolation medium every liter described, described trace element solution comprises 1~5g/L CaCl
22H
2o, 1~5g/L2.5g H
3bO
3, 0.5~1.2g/L ZnCl
24H
2o, 0.5~1.5g/L FeCl
36H
2o, 0.3~0.6g/L ZnSO
47H
2o, 0.1~0.4g/L Na
2moO
42H
2o and 0.003~0.008g/LCuSO
45H
2o.
Further preferably, described trace element solution comprises 2~4g/L CaCl
22H
2o, 1~3g/L H
3bO
3, 0.7~1g/LZnCl
24H
2o, 0.8~1.2g/L FeCl
36H
2o, 0.4~0.5g/L ZnSO
47H
2o, 0.2~0.3g/LNa
2moO
42H
2o and 0.005~0.006g/L CuSO
45H
2o.
Still more preferably, described trace element solution comprises 3.7g CaCl
22H
2o, 2.5g H
3bO
3, 0.87gZnCl
24H
2o, 1.0g FeCl
36H
2o, 0.44g ZnSO
47H
2o, 0.29g Na
2moO
42H
2o and 0.005g CuSO
45H
2o.
The third aspect, the invention provides a kind of fungal inoculant, and this fungal inoculant comprises the fungal bacterial strain LP-16 described in first aspect.
Fourth aspect, the invention provides the preparation method of the fungal inoculant as described in the third aspect, and described method comprises:
(1) culture dish is cultivated: fungal bacterial strain LP-16 as claimed in claim 1 is inoculated on solid medium under aseptic condition to 20-30 ℃, preferably 22-28 ℃, further preferably cultivate at 25 ℃ 4-6 days, preferably 4.4-5.5 days, further preferably 5 days; Described solid medium comprises following component: potato is soaked powder 4-6g/L, preferred 4.5-5.5g/L, further preferred 5g/L, glucose or sucrose 15-25g/L, preferred 17-23g/L, further preferred 20g/L, agar 13-18g/L, preferred 14-17g/L, further preferred 16g/L, paraxin 0.1g/L;
(2) first order seed is cultivated: the bacterial classification that step (1) is cultivated is inoculated in liquid nutrient medium under aseptic condition, 20-30 ℃, and preferred 22-28 ℃, further preferably cultivates 5-7 days at 25 ℃, and preferably 5.5-6.5 days, more preferably 6 days, makes first order seed; Described liquid nutrient medium comprises following component: potato is soaked powder 4-6g/L, preferred 4.5-5.5g/L, further preferred 5g/L, glucose or sucrose 15-25g/L, preferred 17-23g/L, further preferred 20g/L, paraxin 0.1g/L;
(3) secondary seed is cultivated: by the volume ratio of liquid nutrient medium, be 5-15%, preferably 8-12%, more preferably 10% inoculum size, step (2) gained first order seed is inoculated in fermentor tank, aeration, cultivates 5-7 days, preferably 5.5-6.5 days, further preferably 6 days, makes secondary seed;
(4) mixing fermentation culture: be 10-20%, preferably 12-18%, more preferably 15% inoculum size by the volume ratio of liquid nutrient medium, secondary seed is inoculated in fermentor tank, carry out high density fermentation cultivation, obtain microbial inoculum.
During culture dish is cultivated, culture temperature can be 20 ℃, 21 ℃, 22 ℃, 23 ℃, 24 ℃, 25 ℃, 26 ℃, 27 ℃, 28 ℃, 29 ℃ or 30 ℃; Incubation time can be 4 days, 4.5 days, 110 hours, 5 days, 130 hours, 5.5 days or 6 days; In solid medium used potato to soak powder can be 4g/L, 4.2g/L, 4.5g/L, 4.7g/L, 4.9g/L, 5g/L, 5.lg/L, 5.3g/L, 5.5g/L, 5.8g/L or 6g/L, glucose or sucrose can be 15g/L, 16g/L, 17g/L, 18g/L, 19g/L, 20g/L, 21g/L, 22g/L, 23g/L, 24g/L or 25g/L, and agar can be 13g/L, 14g/L, 15g/L, 16g/L, 17g/L or 18g/L.
During first order seed is cultivated, culture temperature can be 20 ℃, 21 ℃, 22 ℃, 23 ℃, 24 ℃, 25 ℃, 26 ℃, 27 ℃, 28 ℃, 29 ℃ or 30 ℃; Incubation time can be 5 days, 5.5 days, 140 hours, 6 days, 150 hours, 6.5 days or 7 days; In liquid nutrient medium used potato to soak powder can be 4g/L, 4.2g/L, 4.5g/L, 4.7g/L, 4.9g/L, 5g/L, 5.lg/L, 5.3g/L, 5.5g/L, 5.8g/L or 6g/L, glucose or sucrose can be 15g/L, 16g/L, 17g/L, 18g/L, 19g/L, 20g/L, 21g/L, 22g/L, 23g/L, 24g/L or 25g/L.
During secondary seed is cultivated, the volume ratio that inoculum size is pressed liquid nutrient medium can be 5%, 6%, 7%, 8%, 9%, 10%, 11%, 12%, 13%, 14% or 15%; Incubation time can be 5.5 days, 140 hours, 6 days, 150 hours or 6.5 days.
In mixing fermentation culture, the volume ratio that inoculum size is pressed liquid nutrient medium can be 10%, 11%, 12%, 13%, 14%, 15%, 16%, 17%, 18%, 19% or 20%.
The 5th aspect, the invention provides a kind of zine ion treatment agent, and described zine ion treatment agent comprises the fungal bacterial strain LP-16 as described in first aspect; Preferably, described in, be treated to and remove or reclaim.
The 6th aspect, the invention provides a kind of method of Treatment of Zinc-containing Wastewater, described method comprises: by the fungal bacterial strain LP-16 as described in first aspect, fungal inoculant as described in the third aspect or the zine ion treatment agent as described in the 5th aspect with as described in zinc-containing water contact.
Preferably, the method for Treatment of Zinc-containing Wastewater of the present invention comprises:
(1) the pH value of zinc-containing water is adjusted to 5.0-8.0, preferred 5.5-7, further preferably 6.0;
(2) in water body, add the fungal bacterial strain LP-16 as described in first aspect, fungal inoculant or the zine ion treatment agent as described in the 5th aspect as described in the third aspect, in 10-35 ℃, preferred 15-30 ℃, further preferably 25 ℃, concussion 4-8 hour, preferably 5-7 hour, further preferably 6 hours, concussion speed 90-180rpm, preferred 100-160rpm, further preferred 120rpm;
(3) standing 8-16 hour, preferred 10-14 hour, further preferably 12 hours.
In the method for Treatment of Zinc-containing Wastewater of the present invention, the pH value of zinc-containing water can be 5.0,5.5,5.8,5.9,6.0,6.1,6.2,6.5,7.0,7.5 or 8.0; Treatment temp can be 10 ℃, 11 ℃, 12 ℃, 13 ℃, 14 ℃, 15 ℃, 16 ℃, 17 ℃, 18 ℃, 19 ℃, 20 ℃, 21 ℃, 22 ℃, 23 ℃, 24 ℃, 25 ℃, 26 ℃, 27 ℃, 28 ℃, 29 ℃, 30 ℃, 31 ℃, 32 ℃, 33 ℃, 34 ℃ or 35 ℃; The concussion time can be 4 hours, 4.5 hours, 5 hours, 5.5 hours, 6 hours, 6.5 hours, 7 hours, 7.5 hours or 8 hours; Concussion speed can be 90rpm, 100rpm, 110rpm, 120rpm, 130rpm, 140rpm, 150rpm, 160rpm, 170rpm or 180rpm; Time of repose can be 8 hours, 8.5 hours, 9 hours, 9.5 hours, 10 hours, 10.5 hours, 11 hours, 11.5 hours, 12 hours, 12.5 hours, 13 hours, 13.5 hours, 14 hours, 14.5 hours, 15 hours, 15.5 hours or 16 hours.
In the method for Treatment of Zinc-containing Wastewater of the present invention, described in be treated to and remove or reclaim the zine ion in described zinc-containing water.
Beneficial effect of the present invention:
(1) fungal bacterial strain LP-16 of the present invention has growth soon, and mycelia surface-area is large, and adsorptive capacity is large, and the zine ion in zinc-containing water can effectively be removed or reclaim to the advantage of high adsorption capacity.
(2) method of Treatment of Zinc-containing Wastewater of the present invention has the advantage of " low input, high production ".
(3), in the method for Treatment of Zinc-containing Wastewater of the present invention, without adding a large amount of chemical agents, thereby avoided the generation of follow-up refuses such as a large amount of precipitation body refuses.
Preservation information
Classification And Nomenclature: Fusarium oxysporum (Fusarium oxysporum);
Preservation date: on August 16th, 2013;
Depositary institution: China Committee for Culture Collection of Microorganisms's common micro-organisms center (be called for short: CGMCC), address: No. 3, Yard 1, BeiChen xi Road, Chaoyang District, Beijing City, 100101;
Deposit number: CGMCC No.8037.
Embodiment
Below by embodiment, further illustrate technical scheme of the present invention.
The separation of embodiment 1 fungal bacterial strain LP-16
The separation of fungal bacterial strain LP-16 of the present invention comprises following steps:
(1) by 10 grams, packed in the triangular flask that contains 90 ml sterile waters by the fresh soil sample of heavy metal contamination;
(2) with granulated glass sphere, break up, stir evenly, make soil supension;
(3) utilize coating method that soil supension is coated on isolation medium flat board, the consisting of of described isolation medium: sodium acetate, anhydrous 0.2406g/L, yeast extract 0.15g/L, agar 15g/L, paraxin 0.1g/L, Zn
2+50mg/L, the MgSO of 0.05g/L
47H
2the K of O and 0.005g/L
2hPO
4, all the other are deionized water, and pH=7.0,120 ℃ of autoclave sterilizations 30 minutes;
(4) be coated with isolation medium is cultivated 2~4 days under the condition of 30 ℃, obtained single bacterial strain;
(5) described single bacterial strain is accessed in fresh described isolation medium and proceeds separation and Culture, obtain the bacterial strain of purifying;
(6) to the operation of the purifying bacterial strain repeating step (5) obtaining in step (5) 3~5 times, take and guarantee the single bacterial strain that resulting bacterial strain is Economical Purification, obtain fungal bacterial strain of the present invention and in 4 ℃ of preservations.
The preparation of embodiment 2 microbial inoculums
The preparation of the microbial inoculum in the present invention comprises following steps:
1) Petri Dishes cultivates: purified original strain (Fusarium oxysporum) is inoculated in respectively on solid medium under aseptic condition, under room temperature (25 ℃) condition, cultivates 5 days; Solid medium has following composition: potato is soaked powder 5g/L, glucose 20g/L, agar 15g/L, paraxin 0.1g/L;
2) first order seed is cultivated: the bacterial classification that step 1) is cultivated is inoculated in respectively liquid nutrient medium under aseptic condition, under room temperature (25 ℃) condition, cultivates 6 days, makes first order seed suspension; Liquid nutrient medium has following composition: potato is soaked powder 5g/L, glucose 20g/L, paraxin 0.1g/L;
3) secondary seed is cultivated: the inoculum size that is 10% by the volume ratio of liquid nutrient medium, first order seed is inoculated into respectively in the fermentor tank of 2.5L, and in fermentor tank, the cumulative volume of nutrient solution is 1.5L, suitably aeration, cultivates 6 days, makes secondary seed;
4) mixing fermentation culture: the inoculum size that is 15% by the volume ratio of liquid nutrient medium, secondary seed is inoculated in the fermentor tank of 10L, the substratum cumulative volume in fermentor tank is 7L, carries out high density fermentation cultivation, obtains microbial inoculum.
The impact of zinc ion concentration on fungi LP-16 absorption zine ion ability in embodiment 3 waste water
Secure ph is 6.0 liquid enlarged culturing base 6 equal portions, and every part of culture volume is 150mL, packs in 250mL triangular flask.In these 6 bottles of solution, contain respectively Zn
2+concentration is 12,24,36,48,60,120mg/L.In these 6 bottles of liquid nutrient mediums, inoculate fungi LP-16 thalline of the present invention, temperature of reaction is 25 ℃, shaking culture 6 hours, and rotating speed is 120RPM, the solution of mycetome is carried out centrifugal, measures Zn in centrifugal rear liquid
2+concentration, observes the degree that thalli growth state and thalline adsorb, fungi LP-16 bacterial strain absorption Zn in the waste water of Different Zinc ionic concn
2+effect as shown in table 1.
The impact of zinc ion concentration on bacterial strain absorption zine ion ability in table 1, waste water
Zinc ion concentration (mg/L) |
Concentration (mg/L) after absorption |
Adsorption efficiency |
12 |
3.33 |
72.25% |
24 |
9.1 |
62.08% |
36 |
14.7 |
59% |
48 |
27.9 |
41.88% |
60 |
29.9 |
50.17% |
120 |
68.3 |
43.08% |
Table 1 result shows, along with the increase of zinc ion concentration, this thalline reduces gradually to the absorption of zine ion, and the continuation increase of zinc ion concentration can affect the growth of this bacterial classification on the contrary, then affects the adsorption efficiency to zine ion.
The impact of embodiment 4 thalline dosages on zine ion ability in fungi LP-16 absorption waste water
Secure ph is 6.0 liquid enlarged culturing base, and volume is 150mL, packs in 250mL triangular flask.In solution, contain Zn
2+concentration is 60mg/L.In nutrient solution, add respectively 0.5,1,2,5, the fungi LP-16 thalline of 10g, temperature of reaction is 25 ℃, shaking culture 6 hours, rotating speed 120RPM, cultured bacteria suspension is centrifugal, measure Zn in centrifugal rear liquid
2+concentration, observes the degree that thalli growth state and thalline adsorb, and the effect that under different thalline dosages, fungi LP-16 adsorbs zine ion in waste water is in Table 2.
Table 2, the impact of thalline dosage on bacterial strain absorption zine ion ability
As seen from the results in Table 2, the most economical when dosage is 5g thalline, cost performance is the highest.
Embodiment 5 pH value in reaction reclaim the impact of zine ion ability from waste water on fungi LP-16
Secure ph is respectively 3.0,4.0,5.0,6.0,7.0 liquid enlarged culturing base, and volume is 150mL, packs in 250mL triangular flask.In solution, contain Zn
2+concentration is 60mg/L.The fungi LP-16 thalline of inoculating 2g in nutrient solution, temperature of reaction is 25 ℃, and shaking culture 6 hours, turns 120RPM, and speed is centrifugal by cultured bacteria suspension, measures Zn in centrifugal rear liquid
2+concentration, observes the degree that thalli growth state and thalline adsorb, and the effect of the lower fungi LP-16 absorption of differential responses pH value zine ion is in Table 3.
Table 3, the impact of pH value on bacterial strain absorption zine ion ability
Table 3 result is visible, and bacterial strain is 5.0 o'clock at pH, and adsorption efficiency is the highest, and PH is 6.0 and takes second place for 7.0 o'clock, illustrates: fungi LP-16 is that adsorption efficiency between 5.0-7.0 is best at pH.
The impact of embodiment 6 temperature of reaction on zine ion ability in fungi LP-16 absorption waste water
Secure ph is 6.0 liquid enlarged culturing base, and volume is 150mL, packs in 250mL triangular flask.In solution, contain Zn
2+concentration is 60mg/L, inoculates 2g fungi LP-16 thalline in nutrient solution, and temperature of reaction is respectively 15,20,25,30 ℃, shaking culture 6 hours, and rotating speed 120RPM, cultured bacteria suspension is centrifugal, measure Zn in centrifugal rear liquid
2+concentration, observes the degree that thalli growth state and thalline adsorb, and at differential responses temperature, the effect of fungi LP-16 absorption zine ion is in Table 4.
Table 4, the impact of temperature of reaction on bacterial strain absorption zine ion ability
Table 4 result shows, when temperature of reaction is between 15-30 ℃, fungi LP-16 thalline all has good effect for the absorption of zine ion in waste water, especially between 20-30 ℃, show adsorption efficiency and promote gradually, show in this temperature range, concrete adsorption effect is become better and better.
The impact of embodiment 7 duration of oscillations on zine ion ability in fungi LP-16 absorption waste water
Secure ph is 6.0 liquid enlarged culturing base, and volume is 150mL, packs in 250mL triangular flask.In solution, contain Zn
2+concentration is 60mg/L.The fungi LP-16 thalline of inoculating 2g in nutrient solution, temperature of reaction is 25 ℃, and shaking culture 10min, 30min, 2h, 4h, 6h, turn 120RPM respectively, and speed is centrifugal by cultured bacteria suspension, measures Zn in centrifugal rear liquid
2+concentration, observes the degree that thalli growth state and thalline adsorb, and under the condition of different duration of oscillations, the effect of fungi LP-16 absorption zine ion is in Table 5.
Table 5, the impact of different duration of oscillation on bacterial strain absorption zine ion ability
Table 5 result shows, in the scope that is 10min-6h at duration of oscillation, the adsorption effect of thalline is better; Particularly, when the earthquake time is 2h, adsorption efficiency is the highest, shows that thalline adsorption effect is now best.
Applicant statement, the present invention illustrates of the present invention by above-described embodiment, but that the present invention is not limited to is above-mentioned, does not mean that the present invention must rely on above-mentioned could enforcement.Person of ordinary skill in the field should understand, any improvement in the present invention, to the selection of the interpolation of the equivalence replacement of the selected raw material of the present invention and ancillary component, concrete mode etc., within all dropping on protection scope of the present invention and open scope.