Optimised method for breaking chlorella walls by mechanical crushing

Abstract

Disclosed is a method of mechanically crushing microalgae cells of the genus Chlorella at an industrial scale, the mechanical crushing being carried out in a horizontal ball mill system. In the method, the balls have an apparent density of between 2 and 3.5 kg/l, the filling rate of the crushing chamber is greater than or equal to 80%, and preferably greater than or equal to 85%, and the mechanical crushing is carried out continuously by a series of successive passes.

Claims

1. A process for the mechanical milling of cells of microalgae of the Chlorella genus, the mechanical milling being carried out in one or more horizontal bead mills, the one or more horizontal bead mills comprising zirconium silicate beads, wherein: the zirconium silicate beads have an apparent density of between 2 and 3.5 kg/l, a filling rate of a milling chamber of the one or more horizontal bead mills is greater than or equal to 80%, and wherein the mechanical milling is carried out in continuous mode by successive passes of said cells through said one or more horizontal bead mills.

2. The process of claim 1, wherein the microalgae of the Chlorella genus are selected from the group consisting of Chlorella vulgaris, Chlorella sorokiniana, and Chlorella protothecoides.

3. The process of claim 2, wherein the zirconium silicate beads have a diameter of less than 0.8 mm.

4. The process of claim 2, wherein the microalgae is Chlorella protothecoides.

5. The process of claim 1, wherein the zirconium silicate beads have a diameter of less than 1 mm.

6. The process of claim 1, wherein the filling rate of the milling chamber is greater than or equal to 85%.

7. The process of claim 6, wherein the microalgae of the Chlorella genus are selected from the group consisting of Chlorella vulgaris, Chlorella sorokiniana, and Chlorella protothecoides.

8. The process of claim 7, wherein the zirconium silicate beads have a diameter of less than 1 mm.

9. The process of claim 7, wherein the zirconium silicate beads have a diameter of less than 0.8 mm.

10. The process of claim 6, wherein the zirconium silicate beads have a diameter of less than 0.8 mm.

11. The process of claim 1, wherein the zirconium silicate beads have a diameter of less than 1 mm.

12. The process of claim 1, wherein the zirconium silicate beads have a diameter of less than 0.8 mm.

Description

DETAILED DESCRIPTION OF THE INVENTION

(1) The applicant company has found that the managed exploitation of the mechanical milling technology to break the wall of microalgae of the Chlorella genus, using a horizontal bead mill, makes it possible to achieve a desired degree of milling while optimizing the energy costs (OPEX) and investment costs (CAPEX).

(2) The improvement in the overall performance level of the facility is thus based on the choice of precise parameters which make it possible to optimize the OPEX and CAPEX or to find the best compromise.

(3) The process, in accordance with the invention, for the mechanical milling, on an industrial scale, of cells of microalgae of the Chlorella genus, the mechanical milling being carried out in a system of horizontal bead mill type, is therefore characterized in that: the beads have an apparent density of between 2 and 3.5 kg/l, and the filling rate of the milling chamber is greater than or equal to 80%.

(4) Apparent Density of the Beads

(5) As will be exemplified hereinafter, the zirconium silicate beads exhibit the best performance levels for this application by limiting the specific energy required to achieve the targeted degree of milling. Thus, the apparent density is between 2 and 3.5 kg/l, preferably between 2 and 3.2 kg/l.

(6) Filling Rate

(7) The filling rate is defined as being the empty volume of the milling chamber minus the volume occupied by the stirring system (generally defined by the supplier).

(8) The specific energy at lower filling rate is slightly higher than at high filling rate. Furthermore, the productivity therein is improved.

(9) Consequently, the process in accordance with the invention preferentially comprises: the use of zirconium silicate beads, and/or a filling rate greater than or equal to 85%.

(10) Preferably, the process uses zirconium silicate beads and a filling rate greater than 85%.

(11) The filling rate may be between 80% and 95%, in particular between 85% and 90%.

(12) A first embodiment of the process in accordance with the invention comprises carrying out the milling in continuous mode by means of a series of successive passes.

(13) The bead-milling operation is conventionally carried out according to several operating schemes: recirculation, single pass, multiple passes, etc.

(14) In one industrial configuration, a continuous system is preferred and involves a single-pass or multiple-pass operating mode.

(15) As will be exemplified hereinafter, the performance level is improved by increasing the number of passes since a higher degree of milling is obtained at equivalent residence time and without a significant increase in the specific energy.

(16) In the process in accordance with the invention, a multiple-pass mode (several mills in series) will be preferred for the optimization of the process on an industrial scale. In particular, the process may comprise 2, 3, 4, 5 passes or more.

(17) A second embodiment of the process in accordance with the invention comprises the use of beads having a diameter of less than 1 mm, preferably less than 0.8 mm. In one particular embodiment, the beads have a diameter of between 0.3 and 0.8 mm.

(18) The impact of the diameter of the milling beads is studied on the same zirconium silicate range (beads of the same density) with a diameter ranging from 0.3 mm to 1.7 mm.

(19) As will be exemplified hereinafter, the beads of small diameter allow a better energy performance level and also a better productivity.

(20) In order to enable those skilled in the art to choose their configuration in comparison with their specifications (sees favoring the OPEX or the CAPEX), the applicant company offers variants of its process in accordance with the invention.

(21) The applicant company has found that these options can be provided by adjusting: the cell density of the microalgae of the Chlorella genus to be milled, the peripheral speed of the milling disks.

(22) Cell Density

(23) The impact of the cell concentration of the biomass on the milling performance levels is evaluated by choosing a biomass from the same production batch, prepared at several concentrations (20%, 25.2% and 32.9%).

(24) The milling is carried out under the same conditions and the results are compared relative to the solids content of the samples thus generated.

(25) The results are interpreted from two different angles: by analyzing the impact of the cell concentration on the specific milling energy required to obtain a defined degree of milling, by analyzing from the productivity angle, the flow rate of introduction of the biomass (relative to the dry biomass) in comparison with the targeted degree of milling.

(26) Peripheral Speed of the Milling Disks

(27) The optimization of the milling also requires the optimal peripheral speed of the milling disks to be defined.

(28) The results are also interpreted from two different angles: by analyzing the specific milling energy as a function of the peripheral speed, by analyzing from the productivity angle, according to the peripheral speed, the flow rate required to achieve the targeted degree of milling.

(29) Moreover, problems of abrasion of the milling disks and chamber and also bead-wear problems are to be considered since they may have a not insignificant economic impact on the process.

(30) The applicant company therefore recommends limiting the peripheral speed to a value of less than 15 m/s (or even 13 m/s) in order to avoid excessive abrasion.

(31) Thus, in the case of the milling of a Chlorella, in particular of Chlorella protothecoides type, to optimize the OPEX, the applicant company has found that a first variant may be: to moderate the density of the microalgae to be milled to a level of less than 250 g/l and/or to choose a peripheral speed of the milling disks of less than 10 m/s.

(32) Preferably, the density of the microalgae to be milled is greater than or equal to 150 g/l and less than 250 g/l. Preferably, the peripheral speed of the milling disks is greater than or equal to 6 m/s and less than 10 m/s.

(33) To optimize the CAPEX, in the case of the milling of a Chlorella, in particular of Chlorella protothecoides type, the applicant company has found that it is necessary, conversely: to increase the cell density of the microalgae to be milled to a level of greater than 250 g/l and/or to choose a peripheral speed of the milling disks of greater than 10 m/s.

(34) Preferably, the density of the microalgae to be milled is greater than 550 g/l and less than or equal to 350 g/l. In particular, the peripheral speed of the milling disks may be between 10 m/s and 15 m/s, preferably between 11 m/s and 13 m/s.

(35) Of course, the present invention relates to any combination of embodiments described in the present application.

(36) The term industrial scale is preferably intended to mean a process in which: the volume of the milling chamber is greater than or equal to 100 liters, preferably greater than or equal to 500 liters; and/or the flow rate is greater than 1 m.sup.3/h; and/or a batch is from 1 to 200 m.sup.3.

(37) The invention will be understood more clearly from the examples which follow, which are intended to be illustrative and nonlimiting.

EXAMPLES

Example 1

Preparation of a Biomass of Chlorella protothecoides Microalgae and Presentation of the Tools Used

(38) The fermentation protocol is adapted from the one described entirely generally in patent application WO 2010/120923.

(39) The production fermenter is inoculated with a pre-culture of Chlorella protothecoides. The volume after inoculation reaches 9000 l.

(40) The carbon source used is a 55% w/w glucose syrup sterilized by application of a time/temperature scheme.

(41) The fermentation is a fed-batch fermentation during which the glucose flow rate is adjusted so as to maintain a residual glucose concentration of from 3 to 10 g/l.

(42) The production fermenter time is from 4 to 5 days.

(43) At the end of fermentation, the cell concentration reaches 185 g/l.

(44) During the glucose feed phase, the nitrogen content in the culture medium is limited so as to allow the accumulation of lipids in an amount of 50% (by weight of biomass).

(45) The fermentation temperature is maintained at 28 C.

(46) The fermentation pH before inoculation is adjusted to 6.8 and is then regulated on this same value during the fermentation.

(47) The dissolved oxygen is maintained at a minimum of 30% by controlling the aeration, the counter pressure and the stirring of the fermenter.

(48) The fermentation must is heat-treated over an HTST zone with a scheme of 1 min at 75 C. and cooled to 6 C.

(49) The biomass is then washed with decarbonated drinking water with a dilution ratio of 6 to 1 (water/must) and concentrated to 250 g/l (25% DCW Dry Cell Weight) by centrifugation using an Alfa Laval Feux 510.

(50) Bead-Milling Technology

(51) The fermentation biomass thus prepared is used to carry out a screening of the milling parameters on a laboratory bead mill:

(52) TABLE-US-00001 Machine Type LabStar LS1 Equipment LME Chamber volume (liter) 0.7 Peripheral speed (m/s) 8 to 12 Feed flow rate (kg/h) 10 to 90 Bead material Glass Zirconium Silicate Zirconium Oxide Bead diameter (mm) 0.3 to 1.7 Filling rate (%) 80 to 90%

(53) The results of the parameters studied are characterized by several points obtained using several successive passes at constant flow rate.

(54) The curves thus obtained for each series of parameters tested are then compared relative to one another in terms of specific energy or of productivity.

(55) Moreover, for the study of a specific parameter, the biomass used for the test comes from the same batch in order to dispense with the composition variability from one batch to another.

(56) Measurement of the Degree of Cell Breaking:

(57) The degree of milling is measured by microscopic counting of the residual cells after milling, relative to the initial reference sample.

(58) The samples are diluted to 1/800. The analysis is carried out by counting on a Malassez cell according to the standard method of use under an optical microscope at a magnification of 1040.

(59) The degree of cell breaking is determined by calculating the percentage of residual cells relative to the initial reference sample.

Example 2

Optimization of the Milling Parameters Bead Density

(60) The impact of the density of the milling beads is studied using a selection of beads made of materials having different densities but the same diameter (0.6 mm):

(61) TABLE-US-00002 Beads ZS (Zirconium ZO (Zirconium Glass Silicate) Oxide) Density 2.5 4 6 (kg/l) Apparent 1.5 2.5 3.6 density (kg/l) Chemical SiO.sub.2 (%) 72.5 ZrO.sub.2 (%) 55-65 ZrO.sub.2 + HfO.sub.2 (%) 95 com- Na.sub.2O (%) 13 SiO.sub.2 (%) 35-40 Y.sub.2O.sub.3 (%) 5 position CaO (%) 9 MgO (%) 4

(62) The comparison of the results obtained, presented in FIG. 1, at equivalent degree of milling according to the material of the beads used under the same operating conditions, demonstrates a significant difference in the specific energy consumed.

(63) The beads of high density (ZOzirconium oxide) cause a much higher specific energy consumption than the zirconium silicate beads.

(64) Although the glass beads have a lower density, the performance levels obtained are not as good, thereby requiring a higher number of passes to achieve the targeted degree of milling, generating a higher specific energy consumption.

(65) The zirconium silicate beads exhibit the best performance levels for this application by limiting the specific energy required to achieve the targeted degree of milling.

(66) Bead Diameter

(67) The impact of the diameter of the milling beads is studied on the same zirconium silicate range (beads of the same density) with a diameter ranging from 0.3 mm to 1.7 mm.

(68) The results obtained, presented in FIG. 2, under the same operating conditions while varying only the bead diameter, demonstrate a strong impact of this parameter on the milling performance levels.

(69) With a large diameter (in this case 1.7 mm), the number of passes and also the specific energy required to achieve the targeted degree of milling is significantly higher than with a small diameter.

(70) The difference between the 0.3 mm and 0.6 mm beads is less significant. The beads of small diameter allow a better energy performance level and also a better productivity.

(71) Chamber Filling Rate

(72) As shown in FIG. 3, the specific energy at low filling rate is slightly higher than when the filling rate is high.

(73) Furthermore, the productivity therein is improved (under the same operating conditions, the degree of milling obtained at the 1st and 2nd pass is higher at a filling rate of 90% than at a filling rate of 80%).

(74) Operating SchemeImpact of the Pass Mode

(75) As shown in FIG. 4, in terms of residence time in the milling chamber, the three operating schemes tested (single pass, multiple passes) are equivalent (1 pass at 30 kg/h/2 passes at 60 kg/h/3 passes at 90 kg/h).

(76) Moreover, the specific milling energy is almost equivalent to these three schemes.

(77) However, the performance level is improved by increasing the number of passes since a higher degree of milling is obtained at equivalent residence time and without a significant increase in the specific energy.

(78) A multiple-pass mode (several mills in series) will therefore be preferred for the optimization of the process on an industrial scale.

(79) Peripheral Speed of the Milling Disks

(80) According to FIG. 5: By analyzing relatively the specific milling energy as a function of the peripheral speed, the relative position of the curves with respect to one another demonstrates that, at a defined degree of milling, operation at a high peripheral speed requires a significantly higher specific energy.

(81) Crushing at moderate peripheral speed therefore makes it possible to achieve better energy performance levels.

(82) According to FIG. 6: Analyzing from the productivity angle, at a higher peripheral speed, a higher flow rate is obtained to reach the targeted degree of milling.

(83) The productivity of a facility will be higher when the peripheral speed is increased.

(84) In order to optimize an industrial facility, a compromise is to be defined between the operating expenses (OPEX) optimized at moderate peripheral speed and the capital expenditures (CAPEX) minimized at high peripheral speed.

(85) Moreover, problems of abrasion of the milling disks and chamber and also bead-wear problems are to be considered since they may have a not insignificant economic impact on the process.

(86) It is preferred to limit the peripheral speed to a value of less than 15 m/s (or even 13 m/s) in order to avoid excessive abrasion.

(87) Cell Density

(88) In addition to the physical parameters of the bead-milling facility, certain criteria regarding the biomass to be milled may have a not insignificant impact on the milling performance levels.

(89) Thus, the impact of the cell concentration of the biomass on the milling performance levels is evaluated.

(90) A biomass from the same production batch is prepared at several concentrations (20%, 25.2% and 32.9%).

(91) The milling is carried out under the same conditions and the results are compared relative to the solids content of the samples thus generated.

(92) According to FIG. 7: By analyzing relatively the impact of the cell concentration on the specific milling energy required to obtain a defined degree of milling, significant differences are demonstrated.

(93) At high cell concentration, the specific energy consumed at a given degree of milling is much higher than at a lower cell concentration.

(94) The milling of a cell biomass at a moderate concentration therefore makes it possible to achieve better energy performance levels than at a high concentration.

(95) According to FIG. 8: Analyzing from the productivity angle, at high cell concentration, an equivalent facility will make it possible to pass a higher flow rate while at the same time achieving the targeted degree of milling.

(96) In other words, the productivity of a facility will be higher when the cell concentration is increased.

DESCRIPTION OF THE FIGURES

(97) FIG. 1: Impact of the bead density (diameter 0.6 mm) on the milling performance levels

(98) FIG. 2: Impact of the bead (ZS) diameter on the milling performance levels

(99) FIG. 3: Impact of the chamber filling rate on the milling performance levels

(100) FIG. 4: Impact of the pass mode on the milling performance levels

(101) FIG. 5: Impact of the peripheral speed on the specific milling energy

(102) FIG. 6: Impact of the peripheral speed on the productivity of the milling operation

(103) FIG. 7: Impact of the cell concentration on the specific milling energy

(104) FIG. 8: Impact of the cell concentration on the productivity of the milling operation