CONTINUOUS CENTRIFUGE AND AIR DISCHARGE METHOD FOR CONTINUOUS CENTRIFUGE
20220001398 · 2022-01-06
Assignee
Inventors
Cpc classification
B04B1/00
PERFORMING OPERATIONS; TRANSPORTING
B04B2005/0464
PERFORMING OPERATIONS; TRANSPORTING
B04B11/02
PERFORMING OPERATIONS; TRANSPORTING
B04B2007/025
PERFORMING OPERATIONS; TRANSPORTING
B04B11/04
PERFORMING OPERATIONS; TRANSPORTING
B04B15/08
PERFORMING OPERATIONS; TRANSPORTING
International classification
B04B11/02
PERFORMING OPERATIONS; TRANSPORTING
B04B15/08
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A valve bridge portion, in which four valves A to D are connected in a bridge shape, is interposed between sample lines to a rotor of a continuous centrifuge. A microcomputer is able to open and close the valves A to D independently and is capable of switching between top feed and bottom feed to the sample line. When sample supply is started, switching between the top feed and the bottom feed is performed multiple times, and in the middle of switching and sending a sample liquid, the microcomputer executes an operation of temporarily increasing a liquid pressure multiple times by temporarily closing an outlet valve (C or D) and then immediately opening the valve. As a result of repeating the operation of switching between the said sample feed directions and temporarily increasing the liquid pressure, air that accumulates inside the rotor can be effectively discharged.
Claims
1. A continuous centrifuge, comprising: a cylindrical rotor for separating a sample, a centrifuge chamber in which the rotor is accommodated, a drive mechanism for rotating the rotor, and sample lines for continuously supplying and discharging the sample to the rotor during rotation of the rotor, wherein an air discharge mode is arranged which performs an operation in which the sample is alternately flowed to the rotor by top feed and bottom feed while the rotor is rotated, and an operation in which the sample line is temporarily throttled in a manner as increasing a flow speed of the sample line after switching a feed direction, and then the sample line is opened.
2. The continuous centrifuge according to claim 1, wherein the sample lines comprise: a sample supply line connected to a sample tank, a sample discharge line connected to a collection tank, an upper line joined to an upper passage of the rotor, and a lower line joined to a lower passage of the rotor; and the sample supply line, the sample discharge line, the upper line and the lower line are bridge-connected and each of four valves is arranged in each of four bridges, respectively.
3. The continuous centrifuge according to claim 2, wherein the valves are operated to be opened and closed independently by a control portion which controls centrifugal separation working; and the control portion a) sets a sample supply direction to the rotor to top feed or bottom feed by opening only two of the four valves which face each other, b) closes the valve located on a discharge side among the opened valves after the sample is discharged from the rotor to make a flow path pressure reach a predetermined peak pressure, and then opens the valve located on the discharge side again to return the flow path pressure to a normal state, c) closes the two valves opened in the Step a) and opens the rest valves to reverse the sample supply direction to the rotor, and d) discharges bubbles in the rotor by repeating the Step b) and the Step c).
4. The continuous centrifuge according to claim 3, wherein in the Step b), by repeating, multiple times, two operations comprising an operation of closing the valve located on the discharge side for a short time and an operation of opening the valve for a certain time, a state in which the flow path pressure reaches the predetermined peak pressure is generated multiple times.
5. The continuous centrifuge according to claim 3, wherein the repeating step of d) is executed multiple times.
6. The continuous centrifuge according to claim 3, wherein the four valves are arranged outside the centrifuge chamber, and are opened and closed using compressed air or electric power as a power source.
7. The continuous centrifuge according to claim 6, wherein the rotor comprises a cylindrical rotor body, an upper rotor cover and a lower rotor cover which are attached so as to close an upper opening and a lower opening of the rotor body, and a core which partitions an interior into a plurality of spaces for separating the sample, and the upper line is connected to the upper rotor cover on an upper side of a rotation axis of the rotor body, and the lower line is connected to the lower rotor cover on a lower side of the rotation axis of the rotor body.
8. The continuous centrifuge according to claim 7, wherein the core comprises a hollow cylindrical body portion in which blade-shaped partition walls evenly dividing the interior of the rotor into the plurality of spaces are protruded on an outer circumferential portion, and end surface portions which are arranged in a manner as closing an upper end and a lower end of the body portion.
9. The continuous centrifuge according to claim 8, wherein a liquid sending pump and a pressure gauge are arranged in the sample supply line, and the opening and closing of the valve located on the discharge side in the Step b) is controlled by the control portion based on output of the pressure gauge.
10. The continuous centrifuge according to claim 1, wherein a flow path limiting mechanism is arranged for increasing the flow path pressure on a downstream side of the rotor when the top feed or the bottom feed is set.
11. An air discharge method for a continuous centrifuge, wherein the continuous centrifuge comprises: a cylindrical rotor for separating a sample, a centrifuge chamber in which the rotor is accommodated, a drive mechanism for rotating the rotor, sample lines for continuously supplying and discharging the sample to the rotor during rotation of the rotor, and a control portion which controls centrifugal separation working, and in the continuous centrifuge, bubbles in the rotor are discharged in a manner that a) an operation is performed in which the sample is alternately flowed to the rotor by top feed and bottom feed while the rotor is rotated, and b) an operation is performed in which the sample line is temporarily throttled in a manner as increasing a flow speed of the sample line after switching a feed direction, and then the sample line is opened.
12. The air discharge method for a continuous centrifuge according to claim 11, wherein the sample lines comprise: a sample supply line connected to a sample tank, a sample discharge line connected to a collection tank, an upper line joined to an upper passage of the rotor, and a lower line joined to a lower passage of the rotor; the sample supply line, the sample discharge line, the upper line and the lower line are bridge-connected and each of four valves is arranged in each of four bridges, respectively; and the control portion c) sets a sample supply direction to the rotor to top feed or bottom feed by opening only two of the four valves which face each other, d) closes the valve located on a discharge side among the opened valves after the sample is discharged from the rotor to make a flow path pressure reach a predetermined peak pressure, and then opens the valve located on the discharge side again to return the flow path pressure to a normal state, e) closes the two valves opened in the Step c) and opens the rest valves to reverse the sample supply direction to the rotor, and f) discharge bubbles in the rotor by repeating the Step d) and the Step e).
13. The air discharge method for a continuous centrifuge according to claim 12, wherein in the Step d), by repeating, multiple times, two operations comprising an operation of closing the valve located on the discharge side for a short time and an operation of opening the valve for a certain time, a state in which the flow path pressure reaches the predetermined peak pressure is generated multiple times.
14. The air discharge method for a continuous centrifuge according to claim 13, wherein the repeating step of f) is executed multiple times.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0019]
[0020]
[0021]
[0022]
[0023]
[0024]
[0025]
[0026]
[0027]
[0028]
[0029]
DESCRIPTION OF THE EMBODIMENTS
EXAMPLE 1
[0030] An example of the present invention is described below based on drawings. Moreover, in the following drawings, the same parts are designated by the same symbols and repeated description is omitted.
[0031]
[0032] Because the rotor 100 is rotationally driven at a high speed, during centrifugal separation, the interior of the chamber 11 is kept in a depressurized state for a purpose of suppressing heat generated by windage loss or frictional heat with atmosphere during operation. In order to keep the chamber 11 in the depressurized state, a not-shown discharge port which discharges air inside the chamber 11 is formed in the body portion of the chamber 11, and a vacuum pump which is not shown is connected to the discharge port. The chamber 11 is fixed to the base 12 by a plurality of bolts 13, and the base 12 is fixed to a floor surface by a plurality of bolts 14.
[0033] The control device portion 50 accommodates a cooling device (not shown) for cooling the interior of the chamber 11, the vacuum pump (not shown), a lift drive device (not shown) for moving the rotor 100 to a predetermined location, a centrifuge controller (a control device) (not shown) for driving and controlling the rotor 100, and the like. An operation panel 60 which is a place for operating/inputting is arranged on an upper part of the control device portion 50. The control device is configured by an electronic circuit (not shown) including a microcomputer and a storage device, and controls the entire continuous centrifuge including drive control of the rotor 100, drive of the liquid sending pump, and control of a plurality of valves A to D described later.
[0034]
[0035] Inside the rotor 100, a rotor core 130 is installed for introducing an injected sample into a high gravity field. The rotor core 130 divides the interior of the rotor 100 into a plurality of centrifugal separation spaces by a core body 131 and blade-shaped partition walls 132 (132a to 132f described later with reference to
[0036] A sample passing hole forming a part of the lower sample passage penetrates through an axial center of the lower shaft 105, and the sample passing hole connects a sample passage 121 formed in the lower rotor cover 120 and a lower connection portion 71.
[0037] The sample is supplied to the interior of the rotor 100 before the centrifugal separation. The sample is supplied as shown by arrows 75b and 75c via the lower pipe 72 connected to the lower connection portion 71, passes through the lower bearing portion 20, passes through the sample passing hole of the lower shaft 105, and is introduced to the interior of the rotor 100 upward from below. Introducing the sample into the rotor 100 from the sample passage 121 on the lower side in this way is called “bottom feed”. When the sample sent out by the liquid sending pump 77 (described later in
[0038] The sample introduced into the rotor 100 is moved to a high centrifugal force field by the rotor core 130 to be separated into a precipitate and a supernatant, and the supernatant (the waste liquid) passes through the sample passing hole of the upper shaft 32 from the sample passage 111 formed in the upper rotor cover 110, passes through the interior of drive portion 30, and is discharged upward from an upper connection portion 81 as shown by an arrow 85a. The sample which has been discharged as shown by the arrow 85a is sent out through the upper pipe 82 as shown by an arrow 85b.
[0039]
[0040] A fitting shaft 123 is formed along a central rotation shaft center on an inner side of the lower rotor cover 120, and the sample passage 121 is formed at the shaft center. An O ring 125 is interposed between the lower rotor cover 120 and the rotor body 101, and an O ring 126 is interposed between the fitting shaft 123 and a fitting hole (not visible in the diagram) formed in the lower surface of the core body 131. Similarly, an O ring 115 and an O ring 133 are also interposed between the upper rotor cover 110 and the rotor body 101. Pins 128a and 128b which are fitted into positioning holes arranged on the lower surface of the core body 131 are attached to two places on the upper circumference of the lower rotor cover 120.
[0041]
[0042] When the motor (not shown) of the drive portion 30 rotates, the upper shaft 32 rotates, and the entire rotor 100 also rotates in synchronization with the upper shaft 32. Because the lower shaft 105 is rotatably supported by the lower bearing portion 20 (see
[0043]
[0044] The valve bridge portion 90 is a flow path switching mechanism configured by four bridge-connected valves A to D. By the valve bridge portion 90, a first flow path direction (the bottom feed) in which the sample is flowed from the lower pipe 72 toward the upper pipe 82 and a second flow path direction (the top feed) in which the sample is flowed from the upper pipe 82 toward the lower pipe 72 are switched. Among four connection points of the valve bridge portion 90, two connection points on the tank side are the inflow point 73a of the sample supplied from the sample tank 70 by the sample supply line and a sample discharge point 83a for discharging the sample to the collection tank 86 via the sample supply line. The rest two connection points on the rotor 100 side are a lower line connection point 72a connected to the lower pipe 72 and an upper line connection point 82a connected to the upper pipe 82. The valves A to D are respectively the same components, and can be opened and closed using high-pressure air as a drive source to control whether to open or close the flow path. The opening/closing operation of the valves A to D is performed according to an instruction of the microcomputer 52 included in the control device 51. Moreover, the types of the valves A to D are arbitrary, and an electromagnetic valve using electric power may be used as long as the opening/closing control can be directly or indirectly executed according to the instruction of the microcomputer 52. In addition, with regard to the valves A to D, a valve which can select only two positions, namely “a fully open position” or “a fully closed position”, is sufficient, and an opening adjustable valve may also be used which is capable of selecting any intermediate position such as half opening or the like.
[0045] The lower pipe 72, the upper pipe 82, the supply pipe 73, and a discharge pipe 83 can be appropriately set to a pipe with elasticity such as a silicon tube, a pipe with no elasticity such as a stainless pipe, or the like. However, in order to perform an air releasing process of the application, the stainless pipe or the like with no elasticity is preferable. The control device 51 includes the microcomputer 52, and performs, by executing a computer program, the management of the entire centrifugal separation working including the control of the delivery and discharge of the sample by the drive of the liquid sending pump 77, the control of the opening and closing of the valves A to D of the valve bridge portion 90, and the pressure measurement of the sample by using the pressure sensor 76. The liquid sending pump 77 is driven by the control of the microcomputer 52 as shown by the dotted line. The output of the pressure sensor 76 is transmitted to the microcomputer 52 by a signal line. Although not shown here, air pipes for sending out the high-pressure air are connected to the valves A to D of the valve bridge portion 90, and the opening/closing operation of the valves A to D is performed in a manner that the microcomputer 52 controls the supply or cutoff of the high-pressure air to each air pipe. With respect to the direction of the continuous sample injection into the interior of the rotor 100 during the centrifugal separation working, the so-called bottom feed is general in which the injection is performed from the lower side as shown by the arrow 75c of
[0046]
[0047]
[0048] In a table in
[0049]
[0050] At the timing t.sub.1, while the bottom feed state is maintained, a waiting state is maintained until a certain time T1 (seconds) elapses, and then the valve C is closed. That is, the valves A, B, C, D=(closed, open, closed, closed). Then, the pressure 95 of the liquid rapidly increases as shown by an arrow 95a. Here, when the pressure 95 reaches a predetermined pressure threshold (a peak pressure) P2 as shown by an arrow 95b , the microcomputer 52 opens the valve C, and returns the state to the state of the valves A, B, C, D=(closed, open, open, closed). Then, the pressure of the liquid sharply decreases from P2 and returns to a normal feed pressure P1 as shown by an arrow 95c. When the normal feed pressure P1 elapses for a certain time T2 (seconds), the valve C is closed again to increase the pressure, and when the pressure reaches the pressure threshold P2 as shown by an arrow 95d, the valve C is opened. In this way, the state, in which the valve C is closed to act as a flow path limiting mechanism for making the pressure reach the pressure threshold P2, and the pressure threshold P2 is used as the peak pressure, is repeated three times as shown by the arrows 95, 95d, and 95e. Thereafter, the waiting state is maintained for a time T3 (seconds), and the air releasing process at the time of the first feed is completed.
[0051] Next, at the timing t.sub.2, the bottom feed is switched to the top feed in a manner that the valves A, B, C, D=(open, closed, closed, open). At this time, the state may be maintained in which the liquid sending pump 77 is operated. A waiting state is maintained until a certain time T1 (seconds) elapses from the timing t.sub.2, and then the valve D is closed. That is, the valves A, B, C, D=((open, closed, closed, closed). Then, the pressure 95 of the liquid rapidly increases as shown by an arrow 95f. Here, when the pressure 95 reaches the predetermined pressure threshold P2 as shown by an arrow 95g, the microcomputer 52 opens the valve D, and returns the state to the state of the valves A, B, C, D=(open, closed, closed, open). Then, the pressure of the liquid sharply decreases from P2 and returns to the normal feed pressure P1 as shown by an arrow 95h. When the normal feed pressure P1 elapses for the certain time T2 (seconds), the valve D is closed again to increase the pressure, and when the pressure reaches the pressure threshold P2 as shown by an arrow 95i, the valve D is opened. In this way, the state in which the valve D acting as a flow path limiting mechanism is closed to make the pressure reach the pressure threshold P2 is repeated three times as shown by the arrows 95g, 95i, and 95j. Thereafter, the waiting state is maintained for the time T3 (seconds), and the air releasing process at the time of the second feed is completed.
[0052] Similarly, the top feed is switched to the bottom feed at the timing t.sub.3 to produce three pressure peaks as shown by arrows 95k to 95m by the air releasing process at time of the third feed. Finally, the bottom feed is switched to the top feed at the timing t.sub.4 to produce three pressure peaks as shown by arrows 95n to 95p by the air releasing process performed by the second top feed. Finally, the top feed is switched to the bottom feed at the timing is in a manner that the valves A, B, C, D=(closed, open, open, closed), and the entire air releasing process is completed. Here, the time T1, the time T2, and the time T3 may be appropriately set, for example, T1, T2, and T3 can be set to about several seconds.
[0053] In this way, in the example, in a sample feed which includes the valve bridge portion 90 performing the flow path switching, the pressure sensor 76 capable of measuring the line pressure, and the liquid sending pump 77 supplying the sample, after the rotor 100 is stabilized at the low-speed rotation, the first air releasing procedure by the switching operation between the bottom feed and the top feed is performed. Furthermore, in the example, after the feed direction is set, the second air releasing procedure is performed so as to generate a pressure increase which occurs in a short time once or more. During the switching, the sample is flowed by the top feed or the bottom feed, and the line pressure temporarily increases to the peak pressure which is the pressure threshold P2 determined previously and does not exceed an allowable pressure Pmax of the centrifuge. That is, an air discharge mode for performing an operation is realized, and in the operation, the pressure of the liquid is increased to the threshold P2 by closing one of the valves in the open operation, and after the pressure reaches the threshold P2, the valve which is temporarily closed is opened again. As a result, the bubbles contained in the sample in the rotor 100 can be automatically removed by the automatic control performed by the control portion. After the timing t.sub.5, the rotor 100 is accelerated to high-speed rotation, the sample is sent to the rotor 100 from the lower line 72, and the continuous centrifugal separation working is executed by the high-speed rotation of the rotor 100.
[0054] Next, a procedure of the air releasing process by the continuous centrifuge 1 is described with reference to a flowchart of
[0055] When the air releasing process (Step 205) at the time of the bottom feed is completed, the microcomputer 52 opens the valves A and D and closes the valves B and C, thereby switching the bottom feed to the top feed (Step 206), and the counter X of the setting number of times of the feed direction is increased by one (Step 207). Next, the microcomputer 52 supplies the sample by the top feed and conducts the air releasing process conducted in
[0056] Next, the detailed procedure of the air releasing process (Step 205) is described with reference to
[0057] Next, the microcomputer 52 waits until the predetermined time T2 elapses (Step 257), judges whether or not the counter Y indicating the number of times that the valve C is closed reaches the specified value (here is 3), and if the counter Y does not reach the specified value, the process returns to Step 253, and Steps 253 to 257 are repeated Y times in total. If the counter Y reaches the specified value of 3 in Step 258, the microcomputer 52 waits until the predetermined time T3 elapses (Step 259), and the process returns to the original Step 205. In this way, the bottom feed and the top feed are switched X times in total, and the pressure increase and the flow path opening operation are respectively performed Y times when each feed is executed. As described above, by repeatedly applying the pressure fluctuation in the line and arranging the “air discharge mode” for switching the flow direction, the bubbles mixed in the flow path are almost discharged from the line.
[0058] Moreover, in Step 255, when the pressure threshold P2 is reached, the valves which can be automatically controlled by the microcomputer 52 are opened and closed, and the rotation speed of the liquid sending pump 77 may also be controlled at the same time. By setting the rotation speed of the liquid sending pump 77 higher than a rotation speed used during a normal sample injection, the flow speed in the pipe can be sharply increased, and thus the air is easily released, and at the same time the time required to reach the pressure threshold P2 can be shortened, and thus the tact time for completing the air releasing process performed X=4 times can be shortened.
[0059] Meanwhile, the function of the “ air discharge mode” can be utilized not only in the air releasing process, but also in a stopped CIP process (a line cleaning process). In many cases, stains which are derived from the sample inside the rotor and the core after the centrifugal separation are generally line-cleaned using an alkaline aqueous solution, and are further cleaned using WFI in order that no alkaline components remain, and it is necessary to prevent stains and alkaline components from remaining in the dead space. If the above control method is adopted, the pressure, the flow direction, the flow speed, and the like of the line can be automatically changed, and the cleanability of the wetted portion after the centrifugal separation is expected to be improved. Furthermore, by combining with a method of cleaning a line while rotating a rotor at a low speed, which is shown in Japanese Patent Laid-Open 2011-177703, the cleaning effect is expected to be further improved.
[0060] Moreover, in many cases, for a sample feed system which is a separate device from the continuous centrifuge 1, a four-way valve which plays a role of the valves A to D even in conventional products is adopted. The above is described in the form of controlling this 4-way valve, but instead of the sample feed system, the present invention can also be realized by arranging new valves near an upper seal portion and a lower seal portion of the continuous centrifuge 1. The effects of the pressure fluctuation and the flow speed fluctuation can be expected in the case where a valve is arranged as close as possible to the centrifugal separation portion to perform the opening/closing operation. The control portion responsible for the valve control may be arranged on the sample feed system side, or may be arranged on the continuous centrifuge 1 side.
[0061] In addition, the pipe used for connecting to the sample feed system and the continuous centrifuge 1 may be a tube such as a silicon tube, but in the case where an SIP is incorporated or the like, the pipe may also be a stainless pipe. An automatic pinch valve may be used if the pipe is a tube pipe, an automatic diaphragm valve may be used if the pipe is a stainless pipe, and the type of the valve does not matter as long as the pipe has a function of opening and closing the flow path. Furthermore, without being limited to a component called a valve, the same effect can be expected as long as the component has a function of blocking the flow path.
[0062] According to the example, the total number of times of the switching between the top feed and the bottom feed is set to X, the number of times of the operation of the automatic valve which is opened after the pressure is increased to the pressure threshold P is set to Y times at each switching, the opening/closing interval time of the automatic valve is set to T1, T2, and T3, and the above X, Y, and T1, T2, and T3 are stored in the microcomputer 52 as parameters, and thereby the air releasing process can be performed fully automatically using the microcomputer 52. If the bubbles remaining in the rotor are automatically removed before the high-speed rotation of the rotor 100, the liquid sending pressure of the sample during the centrifugal separation working can be kept low, the continuous supply of the sample to the rotor 100 can be stable, and a good centrifugal separation performance can be obtained.
[0063] Although the present invention is described above on the basis of the example, the present invention is not limited to the above-described example, and various changes may be made without departing from the gist of the present invention. For example, in the continuous centrifuge 1 of the example described above, the example of the bottom feed in which the sample to be separated is put into the rotor 100 from the lower pipe 72 has been described, but the present invention is not limited thereto. The case of the centrifugal separation working by the top feed may also be applied similarly in which the sample is put into the rotor 100 from the upper pipe 82 and the waste liquid or the separated sample is collected into the collection tank 86 from the lower pipe 72.
REFERENCE SIGNS LIST
[0064] 1 continuous centrifuge
[0065] 10 centrifugal separation portion
[0066] 11 chamber
[0067] 12 base
[0068] 13, 14 bolt
[0069] 16 lift
[0070] 17 arm
[0071] 18 evaporator
[0072] 19 protector
[0073] 20 lower bearing portion
[0074] 30 drive portion
[0075] 32 upper shaft
[0076] 40 wiring/pipe group
[0077] 50 control device portion
[0078] 51 control device
[0079] 52 microcomputer
[0080] 60 operation panel
[0081] 70 sample tank
[0082] 71 lower connection portion
[0083] 72 lower pipe
[0084] 72a lower line connection point
[0085] 73 supply pipe
[0086] 73a sample inflow point
[0087] 75a-75e flow of sample
[0088] 76 pressure sensor
[0089] 77 liquid sending pump
[0090] 81 upper connection portion
[0091] 82 upper pipe
[0092] 82a upper line connection point
[0093] 83 discharge pipe
[0094] 83a sample discharge point
[0095] 85a-85f flow of waste liquid
[0096] 86 collection tank
[0097] 90 valve bridge portion
[0098] 95 liquid pressure
[0099] 100 rotor
[0100] 101 rotor body
[0101] 101a upper opening
[0102] 101b lower opening
[0103] 102 female screw
[0104] 105 lower shaft
[0105] 110 upper rotor cover
[0106] 111 sample passage
[0107] 114 male screw
[0108] 115 O ring
[0109] 117 second male screw
[0110] 118 O ring
[0111] 119 nut
[0112] 120 lower rotor cover
[0113] 120a opening portion
[0114] 121 sample passage
[0115] 122 sample branch passage
[0116] 123 fitting shaft
[0117] 124 male screw
[0118] 125-127 O ring
[0119] 128a, 128b positioning pin
[0120] 129 nut
[0121] 130 rotor core
[0122] 131 core body
[0123] 131a core upper surface
[0124] 131b core lower surface
[0125] 132, 132a-132f partition wall
[0126] 133 O ring
[0127] 134 sample passing hole
[0128] 135, 135a-135f core end surface groove
[0129] 137 separation space
[0130] 145 radial passage
[0131] 176-178 flow of sample
[0132] 180-182 flow of sample
[0133] A1 rotation axis (of rotor)