Illumination-carbon dioxide united-regulation and control photo-bioreactor
A technology of photobioreactor and carbon dioxide, applied in the direction of photobioreactor, bioreactor/fermenter combination, specific-purpose bioreactor/fermenter, etc., which can solve the problems of hysteresis and passivity
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Embodiment 1
[0033] Combustion calorific values of several typical microalgae, including Zhanjiang Isochrysis (golden algae), Tetraphyllum (marine green algae), Chlorella (freshwater green algae) and Spirulina (cyanobacteria), using a combustion heat measurement device Measured, respectively: 2.2±0.08, 1.7±0.02, 2.0±0.03 and 2.1±0.01, unit x10 4 J / g.
[0034]Taking Isochrysis zhanjiang as the culture, measure the different culture systems, including under the fluorescent light source (the input light intensity of the culture system is 50-250 μ mol / (m 2 ·s)) 0.5L tubular airlift reactor, 1L plate reactor, 1.5L plate reactor, 3L shake flask, 30L plate reactor, 100L plate reactor and under natural light (the input light intensity of the culture system is 50-2000μmol / (m 2 ·s)) 100L plate reactor, the light energy utilization rate calculated based on the biomass increment to the total input light energy during harvesting is: 9.3%, 6.0%, 6.4%, 3.9%, 3.2%, 3.5% and 1.2% respectively .
Embodiment 2
[0036] Under the condition of standard 3x F / 2 medium, in the 500mL tubular photobioreactor, aerate according to the aeration rate of 100mL / min (the volume ratio of 2% CO 2 ), 14:10 light-to-dark ratio cultivates Isochrysis zhanjiang, and the aeration volume of the section without light is adjusted to 50% and 20% of the normal level respectively, and F is measured at the beginning and end points of the section without light v / F m Compared with the normal level, the 50% and 20% groups decreased by 1.0% and 7.5% respectively, and the ventilation volume of 20% was determined as the minimum ventilation volume. Among them, the low-ventilation biomass content was 0.423g / L, about 8.7% higher than that of the normal-ventilation group (0.389g / L).
Embodiment 3
[0038] On the basis of the culture conditions described in Example 2, on the basis of maintaining the constant air intake rate, using the control process of the present invention, a dynamic CO 2 Supplementary dinoflagellates from Zhanjiang were cultivated. The conditional culture described in Example 2 was used as a control. The culture results show that the CO in the system can 2 The total amount of feed decreased to less than 70% of the control group, and at the same time, the biomass increased by 5-40% compared with the control group, with an average increase ratio of 20%.
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