Preparation f beta-poly malic acid and salt thereof
A technology of polymalic acid and malate, which is applied in the field of fermentation engineering, can solve the problems of no large-scale application of β-polymalic acid, high production cost, and long fermentation cycle, so as to shorten the fermentation cycle, increase yield, Reduces the effect of feedback inhibition
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Embodiment 1
[0048] Prepare β-polymalic acid, β-polymalate and pullulan as follows:
[0049] The first step, culture medium preparation
[0050] ①Activation medium: potato dextrose medium, sterilized at 121°C for 15 minutes;
[0051] ② Preparation of fermentation medium (w / v): 10% glucose, 0.2% NaNO 3 , 0.01% KH 2 PO 4 , 0.02% MgSO 4 ·7H 2 O, 0.05% KCl, pH 4.0-4.5, sterilized at 121°C for 15 minutes.
[0052] The second step, the activation of bacteria
[0053] The strain of Aureobasidium pullulans ipe-1 stored at 4°C was transferred to the slant of the activation medium, and the activation culture was carried out at 25°C for 48 hours.
[0054] The third step, seed cultivation
[0055] Inoculate the activated seed culture on the slant into a 500ml Erlenmeyer flask containing 100ml of fermentation medium, and culture it with shaking at 25°C and 200r / min for 48 hours.
[0056] The fourth step, inoculation and fermentation
[0057] The culture obtained in the third step was inoculat...
Embodiment 2
[0063] Prepare β-polymalic acid, β-polymalate and pullulan as follows:
[0064] The first step, culture medium preparation
[0065] Same as Example 1
[0066] The second step, the activation of bacteria
[0067] Same as Example 1
[0068] The third step, seed cultivation
[0069] Same as Example 1
[0070] The fourth step, inoculation and fermentation
[0071] Inoculate the culture obtained in the third step into a 7L fermenter with 4L of fermentation medium at an inoculum size of 10%, with an initial pH of 4.0-4.5, a temperature of 25°C, an aeration rate of 0.5-2.5vvm, and a rotation speed of 600-700r / min, cultivated for 7 days, at this time, the bacteria were partially autolyzed, and the sugar consumption rate decreased. Finally, the content of β-polymalic acid in the fermented liquid was 8.7g / L, and the molecular weight was in a wide range of 5KDa-1000kDa.
[0072] Step 5 Preparation of β-polymalic acid and by-product pullulan
[0073] ① Centrifuge the β-polymalic ...
Embodiment 3
[0077] Prepare β-polymalic acid, β-polymalate and pullulan as follows:
[0078] The first step, culture medium preparation
[0079] Same as Example 1
[0080] The second step, the activation of bacteria
[0081] Same as Example 1
[0082] The third step, seed cultivation
[0083] Same as Example 1
[0084] The fourth step, inoculation and fermentation
[0085]Inoculate the culture obtained in the third step into the fermentation medium, pH 4.0-4.5, temperature 25°C, air flow 0.5-2.5vvm, rotation speed 600-700r / min, cultivate for 72h, start pump 1 to make the cells pass through Membrane module A (see attached picture, membrane pore size 0.8μm) is backflowed into the fermenter, the pressure difference is 0.05-0.1mpa, the permeate 1 is concentrated by membrane module B (see attached picture, molecular weight cut-off 100KDa), and the concentrated solution is returned to the storage tank 1. The permeate 2 is returned to the fermenter. Control the content of β-polymalic acid ...
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