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Pneumatic Conveying cyclone

And the types of choices
    Cyclone is to be sent to materials from a separate gas-flow device. Separator and dust in essence can be said to belong to the same type of equipment, different separator is mainly used to transport the materials separation, and the dust was mainly pneumatic conveying system for recovery of dust or gas purifying conveying to protect the gas source Machinery and reduce environmental pollution. 
     According to the principle of the role and structure characteristics of the separator are positive displacement, centrifugal, inertia and so on several combined. The choice of type size usually depends on the material and air flow. For example, a dedicated bulk grain terminal in the port and grain processing enterprises in the use of pneumatic conveying equipment, the use of most of the volume and type centrifuge. 
     Separator of the requirements are: high efficiency separation, should ensure that the materials were shipped overwhelming majority of the (powdery material) or all of the (granular materials) from the two-phase flow can be separated; stable conditions for transmission can be a little There are changes (such as wind or the volume mixing ratio changes), but also a stable separation capability; structure is simple and compact size, light weight; small pressure loss; easy to wear and tear of the site to replace the demolition, inspection, maintenance and convenience. In addition, it must be transparent part of the (window) in order to observe the internal state. 
     Sending smoke and pressure-delivery system can use the same structure of the separator. However, due to smoking-delivery system separator pressure lower than atmospheric pressure, the leakage would greatly reduce the efficiency of separation and therefore the need for better air tightness of the discharge-matching, so that the materials were ranked in the process of unloading a quantity of gas leakage Kept to the minimum.

Volume-separator
Volume-separator is one of the most commonly used by self-separation settlement to the separation of granular materials, sometimes called the settler. 
     1. Typical volume-separator its principle role is tha……Click here to regist or click here contact us.
     2. Damping-volume separator for discharge in the middle, which is outside the framework of the activities and composition of the frame. Activities through a frame and take over the arc discharge board, ……Click here to regist or click here contact us.

Centrifugal separator    

Centrifugal separator, also known as cyclone, he is using the rotary gas-flow generated by the centrifugal force would be material (or dust) from the air in a separate device. Because of its simple structure, low investment and small footprint, easy operation and maintenance, and high separation efficiency, pressure loss, and so on the merits of smaller, so small and medium-sized pneumatic conveying system was widely used. In addition to the separation of materials used to it, can also be used as a dust collector. 
     1. And the working principle of air movement 
    (1) How it works: the structure of the cyclone. When the gas-flow by cutting through the entrance to the separator, along the outer wall from top to bottom for the rotation, this rotation down from the outside as the air vortex, arrived outside the vortex at the bottom of the cone, turn on , Up along the axis of rotation, the final discharge from the exhaust pipe. This bottom-up into the air inside the vortex. The downward spiral outside and inside the upward spiral direction of rotation is the same. Airflow for rotation, the solid particles in the centrifugal effect of the move to the outer wall, reached the outer wall of solid particles in the air down the rotation and gravity to promote the role of the co-cone along the wall under the whereabouts of nesting into the exhaust port. 
    (2) air flow inside the cyclone movement: the movement of gas inside the cyclone is actually very complex three-dimensional gas-solid turbulent campaign. Gas rate of three-dimensional movement, that is tangential, axial and radial velocity. 
     1) tangential velocity vt. The trap dust particles and separation played a leading role. The dust concentration in the gas cut the rate to the role of the next. So that the dust from the outside, centrifugal settlement. 
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     4) vortex. It is the speed of axial and radial velocity pose. Separation of performance, in particular the impact of higher separation efficiency. Eddy common are: 
     ① short-circuit flow. Separator cap, with the outer wall of the exhaust pipe between the cylinder wall, as the axial and radial velocity of the existence of speed, and the formation of the local eddy current (also known as short-circuit flow). It folder with a considerable number of fine dust particles along the exhaust pipe on the external surface of decline, with the increase in central air escaping from the exhaust pipe, affected the efficiency of the dust. 
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2. Particle size and critical theory of separation 
    (1) the critical size: Strictly speaking, most of the separation process has the connotation of classification.……Click here to regist or click here contact us.
    (2) balance of separation theory: analysis to determine the critical size classification of a variety of theories, in order to balance the separation of theory and practice in line compared with the theory that: ……Click here to regist or click here contact us.
    4. Cyclone impact on the performance factor
    (1) of imports of wind speed: With the grade is the size of imports and reduce the rate of increase, that is, high-efficiency dust. However, the pace of imports also not be too big, too easy to make the speed of airflow in the separator (particularly in its part of the cone) of turbulence intensity exercise increases, it will reduce the efficiency of separation. 
    ◎(2) D-diameter cylinder and exhaust pipe diameter dp: the smaller the diameter of the cyclone, dc50 also the smaller the particle size classification, the higher the efficiency of the precipitator. Therefore, the best cyclone a diameter of no more than 1m. If a larger air volume, two or more smaller diameter separator used in parallel. Reduce the exhaust pipe diameter, will help improve the efficiency of the dust. However, the exhaust pipe of diameter can not get too small, too large in order to avoid resistance. 
    (3) of the cyclone cylinder and the cone height: dust to increase the cylinder and a high cone, appears to be on the increase in the direct sense of the dust in the air inside the rotating ring, the dust in favor of separation. In fact due to an increase in the vortex of the next rotation of traction outside of the vortex, so that the air outside the vortex in the next rotation in the process of some of the dust Cuanjin continuous airflow inside the vortex, the cylinder and the cone had a high degree of Great little or no practical significance. Practice shows that in some of the cone, as the cross-section decreased continuously, reached the outer wall of dust gradually reduce the distance, and the flow of tangential velocity increasing, which is separated from the dust as well. Therefore, most modern and efficient dust collector is a long cone. 
    (4) of the lower part of the dust-tight: I expected more platoon tight, the lower the rate of leakage, dust, the better the effect, when the leakage rate of 5%, the separation efficiency by 90% to 50%; leakage rate 15% drop in efficiency have become more intense.  

    (5) the physical properties of materials: the separation of its effects is also greater. The greater size and density of materials, centrifugal force is greater, the higher the separation efficiency; otherwise, the lower the efficiency of separation. ◎
     5. Cyclone of several commonly used under-rotating centrifuge technology parameters table. Away from the upper part of spiral-shaped cylinder, gas-flow guide to a certain pitch down rotation to avoid the vortex ring and the gray generation. This separator import wind speed usually 10 ~ 17m / s, and the drag coefficient separator has little to do in diameter, often taking (ζ = 5.7. External rotation type centrifuge technology parameters table. Imports for the shell-and-vortex, Drag coefficient with a diameter of about separator. Rotation-type centrifuge technology parameters table. Cylinder with its import-lateral tangent, was not at the top of the spiral and a high degree of smaller size, structure is relatively simple, easy to manufacture, However, resistance to a greater separation (dust) and less efficient.

Under the spin-centrifuge (dust) 

Imports
at speed
/m.s-1
Diameter cylinder
 
D/min
250 300 350 400 450 500 550 600 650 700 800 900 1000
Import area/m2 0.0063 0.0091 0.0124 0.0162 0.0204 0.0253 0.0306 0.0364 0.0427 0.0496 0.0648 0.0820 0.1012
Pressure loss / pa Air Flow/m3.h-1
10 350 230 330 445 585 735 910 1100 1310 1540 1790 2335 2950 3645
11 400 250 360 490 640 810 1000 1210 1440 1690 1965 2570 3245 4010
12 500 270 395 535 700 880 1095 1320 1570 1845 2145 2800 3540 4375
13 590 295 425 580 760 955 1185 1430 1700 2000 2320 3035 3840 4740
14 680 320 460 625 815 1030 1275 1540 1835 2150 2500 3270 4135 5105
15 800 340 490 670 875 1100 1370 1650 1965 2305 2680 3500 4430 5470
16 900 365 525 715 935 1175 1460 1760 2100 2460 2860 3785 4125 5835
17 1000 385 555 760 990 1250 1550 1870 2230 2615 3040 3970 5020 6200

External rotation-type centrifuge (dust)  

Imports at speed/m.s-1 Diameter cylinder D/min 250 300 350 400 450 500 550 600
Drag coefficient ζ 9.6 9.9 10.2 10.6 10.9 11.2 11.6 11.9
Import area/m2 0.0063 0.0090 0.0123 0.0160 0.0203 0.0250 0.0303 0.0360
9 Air Flow/m3.h-1 200 290 400 520 655 810 980 1165
Pressure Loss/pa 480 490 510 530 540 560 580 590
10 Air Flow/m3.h-1 225 325 440 575 730 900 1090 1295
Pressure Loss/pa 590 610 630 650 670 690 710 730
11 Air Flow/m3.h-1 250 355 485 635 800 990 1200 1425
Pressure Loss/pa 710 730 760 790 810 830 860 880
12 Air Flow/m3.h-1 270 390 530 690 875 1080 1310 1555
Pressure Loss/pa 850 870 900 930 960 990 1020 1050
13 Air Flow/m3.h-1 290 420 575 750 950 1170 1415 1685
Pressure Loss/pa 990 1020 1050 1090 1130 1160 1200 1230
14 Air Flow/m3.h-1 315 455 620 805 1020 1260 1525 1815
Pressure Loss/pa 1050 1090 1220 1270 1310 1350 1390 1430

External rotation-type centrifuge (dust)  

Imports at speed/m.s-1 Diameter cylinder D/min 300 350 400 450 500 550 600 650 700 800
Drag coefficient ζ 10 10.6 11.5 12.0 12.6 13.3 14.0 14.6 15.3 16.5
Import area/m2 0.0112 0.0153 0.0200 0.0253 0.0312 0.0378 0.0450 0.0528 0.0612 0.0800
9 Air Flow/m3.h-1 320 440 575 730 900 1090 1295 1520 1760 2300
Pressure Loss/pa 390 420 450 470 490 520 550 570 600 650
10 Air Flow/m3.h-1 360 495 650 820 1010 1225 1460 1710 1985 2590
Pressure Loss/pa 500 530 570 600 630 660 700 730 760 820
11 Air Flow/m3.h-1 405 550 720 910 1120 1360 1620 1900 2205 2280
Pressure Loss/pa 610 650 700 740 770 810 860 890 940 1010
12 Air Flow/m3.h-1 445 605 790 1000 1235 1500 1780 2090 2425 3170
Pressure Loss/pa 740 790 850 890 930 990 1040 1080 1130 1220
13 Air Flow/m3.h-1 185 660 865 1090 1350 1630 1945 2280 2640 3450
Pressure Loss/pa 380 930 1010 1060 1110 1170 1230 1280 1350 1450
14 Air Flow/m3.h-1 252 715 935 1185 1460 1770 2105 2470 2614 3456
Pressure Loss/pa 1030 1100 1190 1240 1300 1380 1450 1510 1350 1450

Inertial-separator
    The use of campaign materials to the inertia of the particles flow in separated from the device into inertia separator, as shown. When the gas-flow through the pipe, the direction of air currents and sudden changes in speed, due to the inertia of material particles than the large inertia of the gas molecules to hundreds of thousands of times, and it is very kinetic energy of the material particles from the air will be separated , Set into the hopper, and the discharge port unloaded, dust and air flow through pipe while exports from the separator in the discharge. 
     In the separator-hopper, air pressure and is expected to lose control of the same pressure. In the smoke-delivery system, in order to reduce the outside air from leaking into the discharge port Department, must be installed on the lower part of its special valves or lock-valve atresia. 
     Another chart shows the inertial separator. Into the air along with the widening of the material is expected to take over, some of the lost speed, due to inertia and the role of settlement along the outer wall of room-shaped curve downward slide, and after discharge from the discharge hole (Gray) unloading device, smaller The materials from particles into the air to guide the settlement of the greater part of the room section, lost more speed in the grid-blinds to block the land down under. Dust and air through the exhaust emitted by the grill. Separator for the fine grade material can be used to fly free of fiber, wire, fabric, and so porous to replace the grille shutters.

Combined separator 
   Separator is a modular structure in the form of two different separator combination of the materials separation device. Its characteristics are due to the adoption of two-stage separation, separation more efficient, more compact structure, also the general role of both dust. Volume on the ground as shown in Figure centrifugal separator and a combination of the separation device. Gas-flow from the cut to take over the import into the cylinder, because there is a substantial rate of decrease, the vast majority of the material particles will be down to land by discharging unloading device. Lighter particles and dust from the inside rotation for the air entrainment up into the centrifugal separator, in its most isolated by the discharge unloading device. The dust concentration in the exhaust air flow through the introduction of the next level in the dust collector for further purification. 
     Map shows the volume-separator has built-in cone-settlement of the separation device. 
     The photo shows inertia - centrifugal separator. The vast majority of coarse particles from the isolated part of the inertia, and the smaller and most of the dust grains through part of the centrifugal separation. In addition, the centrifuges could Shunt is also part of a whirlwind two centrifugal separators. 
     Grain processing enterprises in the pneumatic conveying equipment, regular use of modular separator to the separation of grain and light impurities. Map shows the back wind-separator, the course of their work are: gas-flow into the separator before by a longer slow down the spread of pipe, and then to slow the pace of rise and cover the arc (wall James Emery) to less than 30 ° tangent of the angle of friction collision. In the arc-shaped duct, the wind speed remained at 10m / s or so, so that material can continue to move into the settlement movement and the room and fall into the hopper in the deposit. Back to the air duct flow. When the material in the hopper keep up to a certain weight, the pressure to open automatic doors. Grains fall particle cloud sentence drip board. In the on-board mobility, food grains and light impurities can be automatically graded and returned to the air drop together. At this point back from the duct to the air, since the bottom up through the grain and grain to the light impurities away. Set to the whereabouts of food grain hopper, the door pressure by the discharge. With a light impurities in the air, the duct upward arc into the settlement room, so that the light impurities and air separation. Air and dust from the air duct aspiration. Light impurities are set to the whereabouts of the hopper, and then discharged by the discharge device. This separator has a more reasonable population wind elections, and its own settlement with light impurities room, so will be able to better food grain, light impurities, dust and other materials were collected. The separation of light impurities in the efficiency of more than 80%. This separator is characterized by: the structure of the complex, more material consumption.

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