Material mixing and supplying system
11617993 · 2023-04-04
Assignee
Inventors
Cpc classification
B01F23/59
PERFORMING OPERATIONS; TRANSPORTING
B01F35/187
PERFORMING OPERATIONS; TRANSPORTING
B01F23/232
PERFORMING OPERATIONS; TRANSPORTING
B01F2101/2204
PERFORMING OPERATIONS; TRANSPORTING
B01F35/22162
PERFORMING OPERATIONS; TRANSPORTING
B01F35/71805
PERFORMING OPERATIONS; TRANSPORTING
B01F35/213
PERFORMING OPERATIONS; TRANSPORTING
B01F35/22161
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01F23/232
PERFORMING OPERATIONS; TRANSPORTING
B01F35/00
PERFORMING OPERATIONS; TRANSPORTING
B01F35/213
PERFORMING OPERATIONS; TRANSPORTING
B01F35/221
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A material mixing and supplying system is provided. The material mixing and supplying system includes a feeding module, at least three mixing and supplying barrels, a supply module, and a control unit, wherein the three mixing and supplying barrels are capable of mixing and supplying the mixed material. The supplying time of the mixed material is greater than a sum of the feeding time and the mixing time. A total operation number of the at least three mixing and supplying barrels is determined by a set amount of mixed material to be supplied by the material mixing and supplying system, and a total time to finish supplying the set amount of mixed material is determined by the total operation number.
Claims
1. A material mixing and supplying system, comprising: a feeding module for controlling an input of raw material; a supply module for supplying a mixed material to an external device; at least three mixing and supplying barrels connected in parallel and between the feeding module and the supply module, wherein each of the mixing and supplying barrels comprises a mixing module for stirring and mixing the raw material to obtain the mixed material; and a control unit electrically connected to the feeding module, the mixing and supplying barrels, and the supply module, wherein the control unit determines a feeding time, a mixing time, a supplying time, and a maintenance time of each of the mixing and supplying barrels to control a work sequence of the feeding module, the mixing and supplying barrels, and the supply module; wherein the supplying time is greater than a sum of the feeding time and the mixing time; and wherein a starting time point of the feeding time for the mixing and supplying barrel that is spare among the three mixing and supplying barrels is obtained by subtracting the sum of the feeding time and the mixing time from an end time point of the supplying time of one of the three mixing and supplying barrels; wherein a set amount of mixed material to be supplied by the material mixing and supplying system determines a total operation number of the at least three mixing and supplying barrels and the total operation number of the at least three mixing and supplying barrels determines a total time to supply the set amount of mixed material.
2. The material mixing and supplying system of claim 1, wherein each of the mixing and supplying barrels comprises a cleaning module for cleaning the mixing and supplying barrel after the supplying time.
3. The material mixing and supplying system of claim 1, wherein each of the mixing and supplying barrels comprises a conical bottom with an angle of 60 to 120 degrees.
4. The material mixing and supplying system of claim 1, wherein the feeding module comprises a plurality of control valves, and the number of control valves corresponds to the number of the mixing and supplying barrels, wherein each of the control valves comprises a plurality of valve blocks for controlling the input of different raw material.
5. The material mixing and supplying system of claim 1, further comprising a wet nitrogen device connected to the mixing and supplying barrels for providing nitrogen with atomized water to raise a humidity in the mixing and supplying barrels and to prevent the mixed material from drying and hardening.
6. The material mixing and supplying system of claim 1, wherein each of the mixing and supplying barrels further comprises an exhaust module for isolating and expelling exhaust to maintain the airtightness and pH in the mixing and supplying barrels.
7. The material mixing and supplying system of claim 6, wherein the exhaust module comprises a filter module for controlling a property of the expelled exhaust.
8. The material mixing and supplying system of claim 1, wherein the mixed material is slurry or chemical.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The structure as well as preferred modes of use, further objects, and advantages of this present disclosure will be best understood by referring to the following detailed description of some illustrative embodiments in conjunction with the accompanying drawings, in which:
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DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
(11) A material mixing and supplying system of the present disclosure will be described below with reference to the related figures, and for ease of understanding, the same elements in the following embodiment are marked the same.
(12)
(13) Referring to
(14) The control unit 104 of the material mixing and supplying system 100 is electrically connected to the feeding module 101, the mixing and supplying barrels 102a1, 102a2, 102a3, and the supply module 103. The control unit 104 controls, with signals, an input of the feeding module 101, a stirring or mixing time of the mixing and supplying barrels 102a1, 102a2, 102a3, and a supply of a mixed material by the supply module 103 to an output 105. In specific, by determining a feeding time, a mixing time, a supplying time, and a maintenance time of each mixing and supplying barrel 102a1, 102a2, 102a3, the control unit 104 is able to control a work sequence of the feeding module 101, the mixing and supplying barrels 102a1, 102a2, 102a3, and the supply module 103 to keep the supplying of mixed material continuous and non-stop throughout the process.
(15) The feeding module 101 includes one or a plurality of control valves 111, wherein the number of control valves 111 corresponds to the number of mixing and supplying barrels. Each control valve includes a plurality of valve blocks 112, wherein the number of valve blocks 112 may differ in corresponding to different raw materials. The valve blocks 112 may be of different sizes, wherein a large-size valve block reduces a feeding time, and a small-size valve block precisely adjusts the input.
(16) According to the embodiment of the present disclosure, the three mixing and supplying barrels 102a1, 102a2, 102a3 are setup in a predetermined space S with the best space utility rate. These three mixing and supplying barrels 102a1, 102a2, 102a3 have the same structure and functions; the functions include capabilities to mix, supply and store. Therefore, the mixing and supplying barrels 102a1, 102a2, 102a3 can supplement each other functional-wise, in other words, they can provide functional redundancy in the material mixing and supplying system 100. Also, since the mixing and supplying barrels of the present disclosure have both the mixing function and the supplying function, the time for transferring the mixed material from a mixing barrel to a supplying barrel is saved. The mixing and supplying barrels 102a1, 102a2, 102a3 are designed to have a conical bottom with an angle between 60 to 120 degrees, such that the mixed material does not deposit at the bottom easily and so there is no residue when supplying the mixed material. Each of the mixing and supplying barrels 102a1, 102a2, 102a3 includes a mixing module 106 for stirring and mixing the raw materials such as slurry, DI water, H2O2 or chemicals fed into the barrel to obtain the mixed material. The mixing and supplying barrels 102a1, 102a2, 102a3 include a pressure-regulating and pulsation-absorbing module (not shown in drawings) and a transfer pump set (not shown in drawings), for regulating a supplying flow and a supplying pressure of the mixed material.
(17) In addition, one or more heat exchange modules may be disposed between each mixing and supplying barrel 102a1, 102a2, 102a3 through proper pipeline arrangement to individually control the temperature of the liquid in the barrel. Each mixing and supplying barrel 102a1, 102a2, 102a3 also includes a cleaning module (not shown in drawings) with a 360-degree rotatable spray head for completely cleaning the inside of the barrel after the barrel has finished supplying the mixed material therein to prevent the next mixing from being affected by pipeline blockage or residue of the mixed material.
(18) In order to timely monitor the status and/or a property of the mixed material in each mixing and supplying barrel 102a1, 102a2, 102a3, an analysis module (not shown in drawings) utilizing particle size analyzer like particle counter or zeta potential meter, viscometer, specific gravity meter, pH meter, and conductivity meter to measure the status/property of the mixed material in the barrel may be disposed. After the measurement and analysis, the trace composition in the mixed material may be adjusted by an adjustment module (not shown in drawings) or more raw materials may be added by the feeding module 101 by transmitting a signal to the control unit 104.
(19) Each of the mixing and supplying barrels 102a1, 102a2, 102a3 may be connected to a wet nitrogen device 113. The wet nitrogen device 113 provides nitrogen having atomized pure water, wherein the wet nitrogen can reduce the metamorphism of the mixed material caused by the oxidation of the mixed material itself and, at the same time, can maintain the high humidity in the barrel through the vapor or water molecules, and thereby preventing the crystallization of the raw materials or the mixed material due to dryness, which would reduce the quality of the mixed material. Further, an exhaust module (not shown in drawings) may be disposed in each mixing and supplying barrel 102a1, 102a2, 102a3 for expelling the exhaust to maintain the pH in the mixing and supplying barrel. The exhaust module includes a filter module (not shown in drawings) that uses high efficiency particulate air filter (HEPA) to control the property and quality of the expelled exhaust to reduce air pollution in the environment.
(20) Moreover, a pressure-regulating and pulsation-absorbing module may be disposed at places in each pipeline of the material mixing and supplying system 100 for modulating the pulsation and regulating the liquid flow and the pressure in the pipeline. In addition, the mixing and supplying barrels can be blocked from external contact by disposing a choke (not shown in drawings) in the predetermined space S. Further, the material mixing and supplying system 100 can include a nitrogen supply device (not shown in drawings) for providing nitrogen to maintain a condition in the mixing and supplying barrels.
(21) Description of Work Sequence
(22) In the following embodiments and comparative examples, each system is assumed to be implemented in the predetermined space S and the unit time t is 30 minutes, and the set conditions are as such: the predetermined space S is set to be a space that accommodates a total barrel volume of 300 liters (L), and for a volume of 1/12 S, the feeding time is 1 t, the mixing time is 0.5 t, the transfer time between barrels is 1 t, and the supplying time is 4 t.
(23) It is to be noted that slurry will be used as the mixed material in the following descriptions for illustration purpose.
(24) Supplying sequence for the material mixing and supplying system of the present disclosure
(25) Since the mixing and supplying barrels 102a1, 102a2, 102a3 used by the material mixing and supplying system 100 of the present disclosure have both the mixing function and the supplying function, the time for transferring mixed material/slurry from a mixing barrel to a supplying barrel is saved. The volume of the mixing and supplying barrel according to the embodiment of the present disclosure is 100 L (⅓ S), and therefore the feeding time is 4 t, the mixing time is 2 t, the supplying time is 16 t, and the cleaning or maintenance time is 24 t. The schedule illustrated in
(26) Referring to part (A) of
(27) Now, presume that a total operation number of each mixing and supplying barrel assembly is k, then the formula for a total time T needed to achieve the set amount of slurry is: T=16 kt+6 t, wherein the number of times the assembly needed to operate to supply the predetermined space S (300 L) is 3 (k=3), then the total time is 16*3 t+6 t=54 t.
(28) Hence, the total operation number of all mixing and supplying barrels is determined by the set amount of mixed material to be supplied by the material mixing and supplying system. Moreover, the total time that the material mixing and supplying system takes to complete or finish supplying the set amount of mixed material is determined by the total operation number of all mixing and supplying barrels.
(29) First comparative system: three-barrel setup with two mixing barrels and one supplying barrel
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(31) Referring to
(32) In the first comparative system, presume that the operation number of the mixing barrel is i and the operation number of the supplying barrel is j, then the formula for a total time T needed to achieve the set amount of slurry is: T=24 jt+7.5 t, and 2 j=i; wherein the number of times the supplying barrel assembly needed to operate to supply the predetermined space S (300 L) is 2 (j=2), and the number of times the mixing barrel assembly operates is 4 (i=4). Thus, the total operation number of the mixing barrel assembly and the supplying barrel assembly is j+i=6, and the total time is 24*2 t+7.5 t=55.5 t.
(33) Second comparative system: three-barrel setup with two mixing barrels and one supplying barrel
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(35) In the second comparative system, the supply of the slurry starts when the transfer of the slurry from the mixing barrel to the supplying barrel is half-way through, by which the system start time is moved up and the assembly usage is more frequent to increase efficiency. Referring to part (A) of
(36) Presume that in the second comparative system, the operation number of the mixing barrel is i and the operation number of the supplying barrel is j, then the formula for a total time T needed to achieve the set amount of slurry is: T=16 jt+8 t, and j=i, wherein the number of times the supplying barrel assembly needed to operate to supply the predetermined space S (300 L) is 3 (j=3), and the number of times the mixing barrel assembly operates is 3 (i=3). Hence, the total operation number of the mixing barrel assembly and the supplying barrel assembly is j+i=6, and the total time is 16*3 t+8 t=56 t.
(37) Third comparative system: four-barrel setup with two mixing barrels and two supplying barrels
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(39) In the four-barrel setup of two mixing barrels and two supplying barrels, the supply of the slurry also starts when the transfer of the slurry from the mixing barrel to the supplying barrels is half-way through. As shown in part (A) of
(40) In the third comparative system, presume that the operation number of the mixing barrel is i and the operation number of the supplying barrel is j, then the formula for a total time T needed to achieve the set amount of slurry is: T=12 jt+6 t, and j=i, wherein the number of times the supplying barrel assembly needed to operate to supply the predetermined space S (300 L) is 4 (j=4), and the number of times the mixing barrel assembly operates is 4 (i=4). Therefore, the total operation number of the mixing barrel assembly and the supplying barrel assembly is j+i=8 and the total time is 12*4 t+6 t=54 t.
(41) Although the four-barrel setup of two mixing barrels and two supplying barrels is relatively stable, where even if one of the mixing barrels and one of the supplying barrels undergoes the cleaning and maintenance operation, the supply of the slurry can still be kept continuous and on-going, the smaller volume of each barrel would increase the operation number of each assembly. Table 1 below illustrates the number of times the assembly operates in different setups while providing the same amount of supply, wherein i is the operation number of the mixing barrel, j is the operation of the supplying barrel, and k is the operation number of the mixing and supplying barrel of the present disclosure.
(42) TABLE-US-00001 TABLE 1 Operation Number Supply (L) (i + j) or k 300 9000 18000 36000 108000 324000 The Present 3 90 180 360 1080 3240 Disclosure First Comparative 6 180 360 720 2160 6480 System Second Comparative 6 180 360 720 2160 6480 System Third Comparative 8 240 480 960 2880 8640 System
(43) From table 1, it can be seen that, when supplying the same amount of slurry/mixed material, the present disclosure has the lowest number of assembly operations, whereas the number of assembly operations in the three-barrel setups used by the first and the second comparative systems is twice of that of the present disclosure, and that number is even 2.67 times more than the present disclosure for the four-barrel setup used by the third comparative system.
(44) Table 2 compares the supplying time of each setup to the amount of supply and it can be observed that because the supply rate is set to be fixed, the difference between the supplying time of each setup is less significant as the amount of supply increases.
(45) TABLE-US-00002 TABLE 2 Supplying Supply (L) Time (unit: t) 300 9000 18000 36000 72000 324000 The Present 54 1446 2886 5766 11526 51846 Disclosure First Comparative 55.5 1447.5 2887.5 5767.5 11527.5 51847.5 System Second Comparative 56 1448 2888 5768 11528 51848 System Third Comparative 54 1446 2886 5766 11526 81846 System
(46) The material mixing and supplying system according to the embodiment of the present disclosure has the best setup in a limited space, and when each assembly needs cleaning or repair, the other assembly is able to supplement one another functional-wise and to provide functional redundancy, so that the supply of the mixed material is not cutoff. In addition, the number of operations by the assembly as a whole is reduced and in turn prolongs the lifecycle of the assemblies. Thus, the operation cost of the entire assembly is reduced, which increases a lifetime of the material mixing and supplying system. Furthermore, the reduced number of operations by the assembly as a whole and without transfer time between mixing and supplying barrels also reflects on a shortened total time to finish supplying a set amount of mixed material, and therefore the supplying efficiency is enhanced.
(47) The above disclosure is only the preferred embodiment of the present disclosure, and not used for limiting the scope of the present disclosure. All equivalent variations and modifications on the basis of shapes, structures, features and spirits described in claims of the present disclosure should be included in the claims of the present disclosure.