CN211099612U - Multifunctional mixed type feeding pipe for horizontal screw centrifuge - Google Patents
Multifunctional mixed type feeding pipe for horizontal screw centrifuge Download PDFInfo
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- CN211099612U CN211099612U CN201921440572.6U CN201921440572U CN211099612U CN 211099612 U CN211099612 U CN 211099612U CN 201921440572 U CN201921440572 U CN 201921440572U CN 211099612 U CN211099612 U CN 211099612U
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- 238000002156 mixing Methods 0.000 claims abstract description 43
- 239000000463 material Substances 0.000 claims abstract description 38
- 230000007704 transition Effects 0.000 claims abstract description 23
- 239000008394 flocculating agent Substances 0.000 claims abstract description 15
- 238000007789 sealing Methods 0.000 claims description 35
- 239000007788 liquid Substances 0.000 claims description 24
- 238000007580 dry-mixing Methods 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 230000004323 axial length Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 description 7
- 230000009286 beneficial effect Effects 0.000 description 4
- 238000005189 flocculation Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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Abstract
The utility model provides a spiral shell centrifuge is with multi-functional mixed type inlet pipe crouches, multi-functional mixed type inlet pipe includes: a flocculating agent pipe, a feeding pipe and a material conveying pipe; the flocculant pipe includes: an inlet straight pipe section, a spiral pipe section, an outlet straight pipe section, a front mixed flow blade, a conical outlet and a spiral pipe transition section; the spiral pipe section is connected with the inlet straight pipe section through a spiral pipe transition section, the spiral pipe section is connected with one end of the outlet straight pipe section through a spiral pipe transition section, the other end of the outlet straight pipe section is connected with the large end face of the conical outlet, and double-spiral blades are welded on the side face of the outlet straight pipe section; the feed pipe includes: the device comprises a connecting flange, a front mixing pipe, a rear mixing pipe and a fishtail-shaped blade, wherein the fishtail-shaped blade is fixed in the rear mixing pipe; the material conveying pipe comprises: connecting the flange and the straight pipe; the utility model discloses can improve the mixed effect of flocculating agent and material, prevent that the spiral shell centrifuge operation in-process inlet pipe from taking place to block for sleeping in.
Description
Technical Field
The utility model belongs to the centrifuge field, concretely relates to spiral shell centrifuge for crouching uses multi-functional mixed type inlet pipe.
Background
The solid content of municipal sewage is relatively low, the particle diameter of solid-phase particles in the sewage is small, and in the process of treating sewage by using a horizontal spiral centrifugal machine, in order to improve the centrifugal separation efficiency, a flocculating agent is often added into the sewage to increase the volume of the solid-phase particles. The flocculating agent is the most widely applied medicament in the current sewage treatment, and the flocculation process is an indispensable key link in the sewage treatment process.
In order to achieve a good flocculation effect, technicians usually use a mixer to mix the sewage and the flocculant, however, in practical application, it is found that the traditional mixer has a general mixing effect, flocculation products are easy to accumulate on the mixed flow element, and blockage occurs at the mixer position after long-time operation; on the other hand, when the gas content in the material to be separated is high, the complicated flow channel of the mixer is not beneficial to gas conveying, gas resistance is easy to occur at the position of the mixer, and flow cutoff is caused when the gas content is serious, and even the normal operation of the horizontal screw centrifuge is influenced.
Therefore, under the prerequisite of guaranteeing the good mixed effect of flocculating agent and material, need improve horizontal screw centrifuge feed pipe structure, prevent that horizontal screw centrifuge from taking place to block up in the operation process inlet pipe.
SUMMERY OF THE UTILITY MODEL
In order to solve the air resistance problem of the traditional horizontal screw centrifuge mixer, the mixing effect of the material and the flocculating agent is improved, the utility model provides a horizontal screw centrifuge is with multi-functional mixed type inlet pipe.
The utility model adopts the technical proposal that:
the utility model discloses a spiral shell centrifuge for crouching includes with multi-functional mixed type inlet pipe: a flocculating agent pipe 1, a feeding pipe 2 and a material conveying pipe 3;
the flocculant pipe 1 includes: an inlet straight pipe section 11, a spiral pipe section 12, an outlet straight pipe section 13, double helical blades 14, a tapered outlet 15, a first spiral pipe transition section 16 and a second spiral pipe transition section 17; the spiral pipe section 12 is connected with the inlet straight pipe section 11 through a first spiral pipe transition section 16, the spiral pipe section 12 is connected with one end of the outlet straight pipe section 13 through a second spiral pipe transition section 17, the other end of the outlet straight pipe section 13 is connected with the large end face of the conical outlet 15, and double-spiral blades 14 are welded on the side face of the outlet straight pipe section 13;
the feed pipe 2 comprises: the mixing device comprises a first flange 21, a front mixing pipe 22a, a rear mixing pipe 22b and a fishtail-shaped blade 23, wherein the front mixing pipe 22a is connected with the rear mixing pipe 22b through threads, and the fishtail-shaped blade 23 is fixed in the rear mixing pipe 22 b; the material conveying pipe 3 includes: a second flange 31 and a straight tube 32;
the first flange 21 and the second flange 31 are provided with a flocculant pipe limiting groove A, a first sealing groove B and a flange hole C, and the flocculant pipe limiting groove A, the first sealing groove B and the flange hole C on the first flange 21 and the second flange 31 are symmetrical about the flange surface; a convex sealing ring m is arranged on the flange surface of the second flange 31, and an inward concave second sealing groove n is arranged on the flange surface of the second flange 31; during the installation, sealing washer 111 is placed in first seal groove B, sealing ring m with second seal groove n cooperation, inlet pipe 2 with material conveying pipe 3 is connected through first flange 21 and second flange 31, inlet pipe 2 material conveying pipe 3 coincides with spiral shell centrifuge's spiral pusher 4, rotary drum 5's axis, just inlet pipe 2's export is located material allotment room 6. When the first flange 21 and the second flange 31 are connected, the flocculant pipe limiting groove A is cylindrical, the first sealing groove B is annular, the central axis of the first sealing groove B coincides with the central axis of the inlet straight pipe section 11 of the flocculant pipe 1, and the sealing ring m and the second sealing groove n are annular, and the central axis of the sealing ring m coincides with the central axis of the connecting flange; the central axis of the inlet straight pipe section 11 is vertical to the horizontal ground and is limited in the flocculant pipe limiting groove A; the spiral pipe section 12, the outlet straight pipe section 13, the double-spiral blade 14, the conical outlet 15, the first spiral pipe transition section 16 and the second spiral pipe transition section 17 are all positioned in the front mixing pipe 22a of the feeding pipe 2, and the central axes of the spiral pipe section 12, the outlet straight pipe section 13, the double-spiral blade 14 and the conical outlet 15 are coincident with the axis of the feeding pipe 2;
the double-spiral blade 14 comprises a first double-spiral blade 14a and a second double-spiral blade 14b, each of which has a spiral angle of 180 degrees, the first double-spiral blade 14a is composed of two small spiral blades with the same structure, and the spiral direction of the small spiral blade of the first double-spiral blade 14a is opposite to that of the spiral pipe section 12; the second double helical blade 14b is composed of two small helical blades of the same structure, the helical direction of the small helical blade of the second double helical blade 14b is opposite to the helical direction of the small helical blade of the first double helical blade 14a, and the two small helical blades of the first double helical blade 14a and the second double helical blade 14b are different by 180 degrees with the axis of the outlet straight tube section 13 as the center of rotation; the first double-spiral blade 14a and the second double-spiral blade 14b are welded on the side surface of the outlet straight pipe section 13 through an inner spiral root e, the inlet edge of the first double-spiral blade 14a is arranged on the inlet end surface of the outlet straight pipe section 13, the inlet edge of the first double-spiral blade 14a is vertical to the axis of the inlet straight pipe section 11, the outlet edge of the first double-spiral blade 14a and the inlet edge of the second double-spiral blade 14b are on the same plane and form an included angle of 90 degrees, and the outlet edge of the second double-spiral blade 14b is arranged on the outlet end surface of the outlet straight pipe section 13; outlet straight pipe section liquid outlet holes b are formed in the side face of the outlet straight pipe section 13, are located on the inlet edge, the outlet edge and the middle position of the double-helix blade 14 and are circumferentially spaced from the blade by 90 degrees, and the diameter of a round hole of each outlet straight pipe section liquid outlet hole b is 5-10 mm; a plurality of dry mixing flow holes c are uniformly formed in the blade surface of the double-spiral blade 14 along the spiral direction; the thickness of the double-spiral blade 14 is 2 mm; FIG. 7 shows a single helical blade of a double helical blade 14 with a helical direction, the helical surface of which satisfies the equation in this coordinate system
The blades having opposite spiral directions are seated on the seatThe helicoid of the system satisfies the equation
Wherein R is the distance from any point P on the spiral surface to the original point O, β is the included angle between PO and the X axis, L1A half pitch;
the fishtail blade 23 is formed by fixing a short edge through a rectangular iron sheet, twisting another short edge by 180 degrees around a symmetry axis perpendicular to the short edge to obtain, the fishtail blade 23 comprises a first fishtail blade 23a and a second fishtail blade 23b, the twisting directions of the first fishtail blade 23a and the second fishtail blade 23b are opposite, the inlet edge of the first fishtail blade 23a is 90 degrees of included angle with the outlet edge of the second double-spiral blade 14b, the inlet edge of the first fishtail blade 23a is located on the connecting surface of the front mixing tube 22a and the rear mixing tube 22b, the distance from the inlet edge of the first fishtail blade 23a to the conical outlet 15 is D, the outlet edge of the first fishtail blade 23a is 90 degrees of included angle with the inlet edge of the second fishtail blade 23b, the thickness of the fishtail-shaped blade 23 is 2mm, a plurality of dry mixing flow holes c are formed in the surface of the fishtail-shaped blade 23, and the diameter of a circular hole of each dry mixing flow hole c is 10-20 mm; FIG. 8 is a schematic view of a spiral-oriented fishtail blade 23, whose spiral surface satisfies the equation in the coordinate system
The spiral surface of the blade with the opposite spiral direction satisfies the equation under the coordinate system
Wherein R is the distance from any point P on the spiral surface to the original point O, β is the included angle between PO and the X axis, L2A half pitch;
the number of 12 spiral turns of the spiral pipe section is twoA plurality of spiral pipe section liquid outlet holes a are arranged on the flow surface of the spiral pipe section 12 along the spiral line directionnN is the number of the spiral pipe section liquid outlet holes on the flow surface of the spiral pipe section 12, as shown in fig. 4, the angle difference between the liquid outlet holes of two circumferentially adjacent spiral pipe sections is α degrees, which is 30-90 degrees, and the liquid outlet holes a of the spiral pipe sectionsnThe diameter of the round hole is 5mm-10 mm;
the inner diameter of the feeding pipe 2 and the material conveying pipe 3 is D, the inner diameter D is determined according to the size of a horizontal screw centrifuge, the inner diameter of the flocculant pipe 1 is 0.2D, the diameter of a central spiral line of the spiral pipe section 12 is 0.5D, the distance from the central spiral line to the inner wall of the feeding pipe 2 is 0.25D, the pitch of the central spiral line is 1.5D-3D, the pipe length of a conical outlet 15 of the flocculant pipe 1 is 0.3D, the cone angle is 6-10 degrees, the axial length L1 of each blade of the double-spiral blade 14 and the fishtail-shaped blade 23 is equal to that of the blade in L2, and the lengths of the blades are both 1.5D.
The utility model discloses a theory of operation:
when in work, the flocculating agent enters the upper part and is provided with a spiral pipe section liquid outlet hole a along the spiral line directionnThe flocculating agent firstly flows out of the liquid hole a of the spiral pipe sectionnThe middle outflow direction is opposite to the flowing direction of the materials in the feeding pipe 2, meanwhile, compared with a straight pipe, the arrangement of the spiral pipe section 12 is more beneficial to the uniform conveying of the materials, the contact area of the materials flowing through the outer side of the spiral pipe section is larger, and the liquid outlet hole a of the spiral pipe sectionnThe flocculant flowing out of the mixer is more beneficial to fully mixing with the materials, which is the first mixing of the flocculant and the materials; the materials to be separated after the first mixing continuously flow forwards and are mixed with the flocculating agent flowing out of the liquid outlet hole b of the outlet straight pipe section for the second time when flowing to the flow passage area formed by the double helical blades 14 and the front mixing pipe 22 a; and finally, the flocculating agent is ejected from the conical outlet 15 of the flocculating agent pipe 1 to form a low-pressure area, the peripheral materials to be separated are sucked into the jet area and then flow into a basin formed by the fishtail-shaped blades 23 and the rear mixing pipe 22b to be mixed for the third time, and finally the materials to be separated enter a centrifugal machine to be separated.
The beneficial effects of the utility model are embodied in:
the mixing effect of the flocculating agent and the materials is improved in the third mixing process; the whole structure can ensure that gas can smoothly pass through under the working condition of high gas content of the material, and avoid gas resistance; the whole feeding pipe can be easily disassembled and assembled, and the shutdown cleaning of all elements in the feeding pipe is facilitated.
Drawings
FIG. 1 is a cross-sectional view of an embodiment of a decanter centrifuge;
FIG. 2 is a schematic view of an embodiment of a feed tube;
FIG. 3 is a schematic diagram of an embodiment of a feed flocculant pipe;
FIG. 4 is a front view of FIG. 3 taken along the X direction;
FIG. 5 is an assembled cross-sectional view of a feed tube structure according to an embodiment;
FIG. 6 is a schematic view of an embodiment of a material delivery tube and feed tube;
FIG. 7 is a schematic view of a double helical blade in one embodiment;
FIG. 8 is a schematic view of a fishtail vane in one embodiment
The reference numbers indicate 1-flocculant tube, 11-inlet straight tube section, 111-seal ring, 12-spiral tube section, 13-outlet straight tube section, 14-double spiral blade, 14 a-first double spiral blade, 14B-second double spiral blade, 15-conical outlet, 16-first spiral tube transition section, 17-second spiral tube transition section, 2-feed tube, 21-first flange, 22-mixing tube, 23-fishtail blade, 23 a-first fishtail blade, 23B-second fishtail blade, 3-material delivery tube, 31-second flange, 32-straight tube, 4-spiral pusher, 5-drum, 6-material distribution chamber, an-spiral tube section liquid outlet hole, B-outlet straight tube section liquid outlet hole, C-mixing hole, α -angle of circumferentially adjacent two liquid outlet holes, a-flocculant tube limiting groove, B-first seal groove, C-flange hole, m-seal ring, n-second seal groove, e-inner spiral blade root, D-double spiral blade inner diameter, L-single spiral blade, 2-PO axial direction included angle, P-single spiral blade length, 366335-single spiral blade.
Detailed Description
In order to show the technical solutions and advantages of the present invention in more detail, it will now be described by some relevant examples. The purpose of the present invention will be described with reference to the accompanying drawings and examples. It should be understood that the specific embodiments described herein are only for the purpose of illustrating the present invention and are not to be construed as limiting the invention, and all other embodiments that can be obtained by one of ordinary skill in the art without inventive faculty are within the scope of the invention.
With reference to the attached figures 1-8
Fig. 1 is an assembly schematic diagram of a multistage mixing air-resistance type feeding pipe and a horizontal screw centrifuge of the utility model, the multistage mixing air-resistance type feeding pipe of the utility model comprises a flocculating agent pipe 1, a feeding pipe 2 and a material conveying pipe 3;
as shown in fig. 2 and 3, the flocculant pipe 1 includes: an inlet straight pipe section 11, a spiral pipe section 12, an outlet straight pipe section 13, double helical blades 14, a tapered outlet 15, a first spiral pipe transition section 16 and a second spiral pipe transition section 17; the spiral pipe section 12 is connected with the inlet straight pipe section 11 through a first spiral pipe transition section 16, the spiral pipe section 12 is connected with one end of the outlet straight pipe section 13 through a second spiral pipe transition section 17, the other end of the outlet straight pipe section 13 is connected with the large end face of the conical outlet 15, and double-spiral blades 14 are welded on the side face of the outlet straight pipe section 13;
as shown in fig. 1, 5 and 6, the feed pipe 2 includes: the mixing device comprises a first flange 21, a front mixing pipe 22a, a rear mixing pipe 22b and a fishtail-shaped blade 23, wherein the front mixing pipe 22a is connected with the rear mixing pipe 22b through threads, and the fishtail-shaped blade 23 is fixed in the rear mixing pipe 22 b; the material conveying pipe 3 includes: a second flange 31 and a straight tube 32; flocculant pipe limiting grooves A, first sealing grooves B and flange holes C are formed in the first flange 21 and the second flange 31, and the flocculant pipe limiting grooves A, the first sealing grooves B and the flange holes C on the first flange 21 and the second flange 31 are symmetrical about the flange surface; a convex sealing ring m is arranged on the flange surface of the second flange 31, and an inward concave second sealing groove n is arranged on the flange surface of the second flange 31; during the installation, sealing washer 111 is placed in first seal groove B, sealing ring m with second seal groove n cooperation, inlet pipe 2 with material conveying pipe 3 is connected through first flange 21 and second flange 31, inlet pipe 2 material conveying pipe 3 coincides with spiral shell centrifuge's spiral pusher 4, rotary drum 5's axis, just inlet pipe 2's export is located material allotment room 6. When the first flange 21 and the second flange 31 are connected, the flocculant pipe limiting groove A is cylindrical, the first sealing groove B is annular, the central axis of the first sealing groove B coincides with the central axis of the inlet straight pipe section 11 of the flocculant pipe 1, and the sealing ring m and the second sealing groove n are annular, and the central axis of the sealing ring m coincides with the central axis of the connecting flange; the central axis of the inlet straight pipe section 11 is vertical to the horizontal ground and is limited in the flocculant pipe limiting groove A; the spiral pipe section 12, the outlet straight pipe section 13, the double-spiral blade 14, the conical outlet 15, the first spiral pipe transition section 16 and the second spiral pipe transition section 17 are all positioned in the front mixing pipe 22a of the feeding pipe 2, and the central axes of the spiral pipe section 12, the outlet straight pipe section 13, the double-spiral blade 14 and the conical outlet 15 are coincident with the axis of the feeding pipe 2;
as shown in fig. 3 and 7, the double-spiral blade 14 includes a first double-spiral blade 14a and a second double-spiral blade 14b, each of which has a spiral angle of 180 °, the first double-spiral blade 14a is composed of two small spiral blades with the same structure, and the spiral direction of the small spiral blade of the first double-spiral blade 14a is opposite to the spiral direction of the spiral pipe section 12; the second double helical blade 14b is composed of two small helical blades with the same structure, the helical direction of the small helical blade of the second double helical blade 14b is opposite to that of the small helical blade of the first double helical blade 14a, and the two small helical blades of the first double helical blade 14a and the second double helical blade 14b are different by 180 degrees by taking the axis of the outlet straight pipe section 13 as a rotation center; the first double-spiral blade 14a and the second double-spiral blade 14b are welded on the side surface of the outlet straight pipe section 13 through the inner spiral root part e, the inlet edge of the first double-spiral blade 14a is arranged on the inlet end surface of the outlet straight pipe section 13, the inlet edge of the first double-spiral blade 14a is vertical to the axis of the inlet straight pipe section 11, the outlet edge of the first double-spiral blade 14a is arranged on the same plane as the inlet edge of the second double-spiral blade 14b and forms an included angle of 90 degrees, and the outlet edge of the first double-spiral blade 14a is arranged on the same plane asThe outlet side of the second double helical blade 14b is on the outlet end face of the outlet straight tube section 13; outlet straight pipe section liquid outlet holes b are formed in the side face of the outlet straight pipe section 13, are located on the inlet edge, the outlet edge and the middle position of the double-helix blade 14 and are circumferentially spaced from the blade by 90 degrees, and the diameter of a round hole of each outlet straight pipe section liquid outlet hole b is 8 mm; a plurality of dry mixing flow holes c are uniformly formed in the blade surface of the double-spiral blade 14 along the spiral direction; the thickness of the double-spiral blade 14 is 2 mm; FIG. 7 shows a single helical blade of a double helical blade 14 with a helical direction, the helical surface of which satisfies the equation in this coordinate system
(10mm<R<50mm；0<β<Pi) of the blade, the helical surface of which in the coordinate system is opposite to the helical direction of the blade satisfies the equation
(10mm<R<50mm；0<β<Pi), wherein R is the distance from any point P on the spiral surface to the origin O, β is the included angle between PO and the X axis, L1A half pitch;
as shown in fig. 5, 6 and 8, the fishtail vane 23 is obtained by fixing a short side of a rectangular iron sheet and twisting the other short side by 180 ° around a symmetry axis perpendicular to the short side, the fishtail vane 23 includes a first fishtail vane 23a and a second fishtail vane 23b, the twisting directions of the first fishtail vane 23a and the second fishtail vane 23b are opposite, and the twisting direction of the first fishtail vane 23a is opposite to the twisting direction of the second double spiral vane 14b, the inlet edge of the first fishtail vane 23a and the outlet edge of the second double spiral vane 14b form an included angle of 90 °, the inlet edge of the first fishtail vane 23a is located on the connection surface of the front mixing pipe 22a and the rear mixing pipe 22b, and the distance from the inlet edge of the first fishtail vane 23a to the conical outlet 15 is 100mm, the inlet edge of the first fishtail vane 23a and the outlet edge of the second fishtail vane 23b form an included angle of 90 °, the thickness of the fishtail-shaped blade 23 is 2mm, and the blade surface of the fishtail-shaped blade 23 is provided withA plurality of dry mixing flow holes c are formed, and the diameter of a circular hole of each dry mixing flow hole c is 20 mm; FIG. 8 is a schematic view of a spiral-oriented fishtail blade 23, whose spiral surface satisfies the equation in the coordinate system
(0<R<50mm；0<β<Pi) of the blade, the helical surface of which in the coordinate system is opposite to the helical direction of the blade satisfies the equation
(0<R<50mm；0<β<Pi), wherein R is the distance from any point P on the spiral surface to the origin O, β is the included angle between PO and the X axis, L2A half pitch;
as shown in fig. 3 and 4, the number of spiral turns of the spiral pipe section 12 is two, and a plurality of spiral pipe section liquid outlet holes a are formed on the upstream side of the spiral pipe section 12 along the spiral line directionnN is the number of the spiral pipe section liquid outlet holes on the flow surface of the spiral pipe section 12, as shown in fig. 4, the angle difference between the liquid outlet holes of two adjacent spiral pipe sections in the circumferential direction is α ═ 90 °, and the liquid outlet holes a of the spiral pipe sectionsnThe diameter of the round hole is 8 mm;
as shown in fig. 5, the inner diameters of the feed pipe 2 and the material conveying pipe 3 are determined to be D equal to 100mm according to the size of a horizontal screw centrifuge, the inner diameter of the flocculant pipe 1 is 0.2D equal to 20mm, the diameter of the central spiral line of the spiral pipe section 12 is 0.5D equal to 50mm, the distance from the central spiral line to the inner wall of the feed pipe 2 is 0.25D equal to 25mm, the pitch of the central spiral line is 2D equal to 200mm, the length of the conical outlet 15 of the flocculant pipe 1 is 0.3D equal to 30mm, the angle of the conical outlet is 7 °, the axial lengths L1 and L2 of the single blades of the double-spiral blade 14 and the fishtail blade 23 are equal, and the lengths are both 1.5D equal to 150 mm.
Claims (3)
1. The utility model provides a spiral shell centrifuge is with multi-functional mixed type inlet pipe crouches, its characterized in that spiral shell centrifuge includes with multi-functional mixed type inlet pipe crouches: a flocculating agent pipe (1), a feeding pipe (2) and a material conveying pipe (3); the flocculant pipe (1) comprises: an inlet straight pipe section (11), a spiral pipe section (12), an outlet straight pipe section (13), a double-helix blade (14), a tapered outlet (15), a first spiral pipe transition section (16) and a second spiral pipe transition section (17); the spiral pipe section (12) is connected with the inlet straight pipe section (11) through a first spiral pipe transition section (16), the spiral pipe section (12) is connected with one end of the outlet straight pipe section (13) through a second spiral pipe transition section (17), the other end of the outlet straight pipe section (13) is connected with the large end face of the conical outlet (15), and double-spiral blades (14) are welded on the side face of the outlet straight pipe section (13); the feed pipe (2) comprises: the mixing device comprises a first flange (21), a front mixing pipe (22a), a rear mixing pipe (22b) and a fishtail-shaped blade (23), wherein the front mixing pipe (22a) is connected with the rear mixing pipe (22b) through threads, and the fishtail-shaped blade (23) is fixed in the rear mixing pipe (22 b); the material conveying pipe (3) comprises: a second flange (31) and a straight pipe (32);
flocculant pipe limiting grooves (A), first sealing grooves (B) and flange holes (C) are formed in the first flange (21) and the second flange (31), and the flocculant pipe limiting grooves (A), the first sealing grooves (B) and the flange holes (C) in the first flange (21) and the second flange (31) are symmetrical about the flange surface; a convex sealing ring (m) is arranged on the flange surface of the second flange (31), and a concave second sealing groove (n) is arranged on the flange surface of the second flange (31); during installation, a sealing ring (111) is placed in the first sealing groove (B), a sealing ring (m) is matched with the second sealing groove (n), the feeding pipe (2) is connected with the material conveying pipe (3) through a first flange (21) and a second flange (31), the axes of the feeding pipe (2) and the material conveying pipe (3) are overlapped with the axes of a spiral pusher (4) and a rotary drum (5) of a horizontal screw centrifuge, and the outlet of the feeding pipe (2) is positioned in a material distribution chamber (6); when the first flange (21) and the second flange (31) are connected, the flocculant pipe limiting groove (A) is cylindrical, the first sealing groove (B) is annular, the central axis of the first sealing groove coincides with the central axis of the inlet straight pipe section (11) of the flocculant pipe (1), the sealing ring (m) and the second sealing groove (n) are annular, and the central axis of the sealing ring coincides with the central axis of the connecting flange; the central axis of the inlet straight pipe section (11) is vertical to the horizontal ground and is limited in the flocculant pipe limiting groove (A); the spiral pipe section (12), the outlet straight pipe section (13), the double-helix blade (14), the conical outlet (15), the first spiral pipe transition section (16) and the second spiral pipe transition section (17) are all positioned in a front mixing pipe (22a) of the feeding pipe (2), and the central axes of the spiral pipe section (12), the outlet straight pipe section (13), the double-helix blade (14) and the conical outlet (15) are coincident with the axis of the feeding pipe (2);
the double-spiral blade (14) comprises a first double-spiral blade (14a) and a second double-spiral blade (14b), the spiral angle of each double-spiral blade is 180 degrees, the first double-spiral blade (14a) consists of two small spiral blades with the same structure, and the spiral direction of the small spiral blade of the first double-spiral blade (14a) is opposite to that of the spiral pipe section (12); the second double helical blade (14b) consists of two small helical blades with the same structure, the helical direction of the small helical blade of the second double helical blade (14b) is opposite to that of the small helical blade of the first double helical blade (14a), and the two small helical blades of the first double helical blade (14a) and the second double helical blade (14b) are different by 180 degrees by taking the axis of the outlet straight pipe section (13) as a rotation center; the first double-spiral blade (14a) and the second double-spiral blade (14b) are welded on the side surface of the outlet straight pipe section (13) through an inner spiral root (e), the inlet edge of the first double-spiral blade (14a) is arranged on the inlet end surface of the outlet straight pipe section (13), the inlet edge of the first double-spiral blade (14a) is perpendicular to the axis of the inlet straight pipe section (11), the outlet edge of the first double-spiral blade (14a) and the inlet edge of the second double-spiral blade (14b) are on the same plane and form an included angle of 90 degrees, and the outlet edge of the second double-spiral blade (14b) is arranged on the outlet end surface of the outlet straight pipe section (13); outlet straight pipe section liquid outlet holes (b) are formed in the side surface of the outlet straight pipe section (13), are positioned at the inlet edge, the outlet edge and the middle position of the double-helix blade (14), are circumferentially spaced by 90 degrees from the blade, and have the diameter of a round hole of 5-10 mm; a plurality of dry mixing flow holes (c) are uniformly formed in the blade surface of the double-helix blade (14) along the helix direction; the thickness of the double-spiral blade (14) is 2 mm; the helicoid of a single helical blade of a double helical blade (14) in a helical direction satisfies the equation
The spiral surface of the blade with the opposite spiral direction satisfies the equation under the coordinate system
Wherein R is the distance from any point P on the spiral surface to the original point O, β is the included angle between PO and the X axis, L1A half pitch;
the fishtail blade (23) is obtained by screwing another short side for 180 degrees around a symmetrical axis vertical to the short side through a fixed short side by a rectangular iron sheet, the fishtail blade (23) comprises a first fishtail blade (23a) and a second fishtail blade (23b), the screwing directions of the first fishtail blade (23a) and the second fishtail blade (23b) are opposite, the screwing direction of the first fishtail blade (23a) is opposite to the screwing direction of the second double-spiral blade (14b), the inlet edge of the first fishtail blade (23a) is 90 degrees of included angle with the outlet edge of the second double-spiral blade (14b), the inlet edge of the first fishtail blade (23a) is positioned on the connecting surface of the front mixing pipe (22a) and the rear mixing pipe (22b), and the distance from the inlet edge of the first fishtail blade (23a) to the conical outlet (15) is D, d is the inner diameter size of the material conveying pipe (3); the outlet edge of the first fishtail-shaped blade (23a) and the inlet edge of the second fishtail-shaped blade (23b) form an included angle of 90 degrees, the thickness of the fishtail-shaped blade (23) is 2mm, a plurality of dry mixing flow holes (c) are formed in the surface of the fishtail-shaped blade (23), and the diameter of a circular hole of each dry mixing flow hole (c) is 10-20 mm; the helicoid of a fishtail blade (23) in the spiral direction satisfies the equation
The blade with the opposite spiral direction is at the coordinateThe spiral surface of the system satisfies the equation
Wherein R is the distance from any point P on the spiral surface to the original point O, β is the included angle between PO and the X axis, L2One-half pitch.
2. The multifunctional mixed feeding pipe for the horizontal decanter centrifuge as claimed in claim 1, characterized in that: the spiral pipe section (12) has two spiral turns, and a plurality of spiral pipe section liquid outlet holes (a) are arranged on the flow-facing surface of the spiral pipe section (12) along the spiral line directionn) N is the number of the liquid outlet holes of the spiral pipe section on the flow-facing surface of the spiral pipe section (12), the angle difference between the liquid outlet holes of two adjacent spiral pipe sections in the circumferential direction is α degrees which is 30-90 degrees, and the liquid outlet holes (a) of the spiral pipe sectionsn) The diameter of the round hole is 5mm-10 mm.
3. The multifunctional mixed feeding pipe for the horizontal decanter centrifuge as claimed in claim 1, characterized in that the inner diameter of the feeding pipe (2) and the material conveying pipe (3) is D, the inner diameter of the flocculant pipe (1) is 0.2D, the diameter of the central spiral line of the spiral pipe section (12) is 0.5D, the distance from the central spiral line to the inner wall of the feeding pipe (2) is 0.25D, the pitch of the central spiral line is 1.5D-3D, the pipe length of the conical outlet (15) of the flocculant pipe (1) is 0.3D, the cone angle is 6-10 degrees, the axial lengths L1 and L2 of the single blades of the double spiral blade (14) and the fishtail blade (23) are equal, and the lengths are both 1.5D.
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| CN201921440572.6U CN211099612U (en) | 2019-08-30 | 2019-08-30 | Multifunctional mixed type feeding pipe for horizontal screw centrifuge |
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| CN201921440572.6U CN211099612U (en) | 2019-08-30 | 2019-08-30 | Multifunctional mixed type feeding pipe for horizontal screw centrifuge |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110605189A (en) * | 2019-08-30 | 2019-12-24 | 浙江工业大学 | Multifunctional mixed type feeding pipe for horizontal screw centrifuge |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110605189A (en) * | 2019-08-30 | 2019-12-24 | 浙江工业大学 | Multifunctional mixed type feeding pipe for horizontal screw centrifuge |
| CN110605189B (en) * | 2019-08-30 | 2024-05-03 | 浙江工业大学 | Multifunctional mixed type feeding pipe for horizontal decanter centrifuge |
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