CN104084322A - Particle separation device - Google Patents
Particle separation device Download PDFInfo
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- CN104084322A CN104084322A CN201410328659.XA CN201410328659A CN104084322A CN 104084322 A CN104084322 A CN 104084322A CN 201410328659 A CN201410328659 A CN 201410328659A CN 104084322 A CN104084322 A CN 104084322A
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Abstract
The invention provides a particle separation device which comprises a separation cylinder and a cover, wherein the cover is connected with the top end of the separation cylinder; an inlet is formed in the top side wall of the separation cylinder and is communicated with a vapor-liquid-solid feeding pipe; a particle outlet is formed at the lower end of the separation cylinder; an outlet is formed in the middle of the cover and is communicated with a vapor-liquid outlet pipe; the cover is connected with an isolation component; the isolation component comprises a cylindrical hollow supporting body and a disc; one end of the supporting body is connected with the cover and the other end of the supporting body is connected with the disc; a plurality of through holes with diameter of 1.5mm are formed in the disc; the supporting body is communicated with the outlet of the cover; a spiral guiding plate is arranged on the inner wall of the separation cylinder. According to the device, inert solid particles in a vapor-liquid-solid three-phase mixed material can be effectively separated from feed liquid. The disc with the through holes with diameter of 1.5mm is arranged at the top of the device, so that few particles are effectively prevented from escaping from the upward side of the particle separation device and then the sufficient separation of solid particles in the feed liquid is realized.
Description
Technical field
The present invention relates to a kind of particle separating device.
Background technology
Chinese medicine, food, chemical field, in process of production, when feed liquid is the state of the solid three-phase mixing of vapour-liquid, the feed liquid that often the solid three-phase of vapour-liquid need to be mixed is carried out separation, due to the small volume of solid particle, lightweight, exist part solid particle and be mixed in vapour-liquid, with vapour-liquid trend, not segregative problem.In addition, consider the raising of productivity effect, should guarantee, under the prerequisite of separated validity, production cost to be controlled to reduced levels.
Summary of the invention
The object of this invention is to provide a kind of particle separating device, can be effectively that the solid particle in feed liquid is separated, while needing the feed liquid of the solid three-phase mixing of vapour-liquid to carry out separation in solution prior art, small volume due to solid particle, existing part solid particle is mixed in vapour-liquid, with vapour-liquid trend, not segregative problem.
Technical solution of the present invention is:
A kind of particle separating device, comprise separated cylindrical shell and lid, lid is connected to the top of separated cylindrical shell, the top sidewall of separated cylindrical shell is provided with import, import is communicated with the solid feed pipe of vapour-liquid, the low side of separated cylindrical shell is provided with particle discharging opening, the middle part of lid is provided with outlet, outlet is communicated with vapour-liquid delivery line, lid is connected with barrier assembly, barrier assembly comprises supporter and the disk of tubular hollow, one end of supporter is connected on lid, the other end clutch disk of supporter, disk has the through hole of some diameter 1.5mm, supporter is communicated with the outlet of lid, the inwall of separated cylindrical shell is provided with spiral stock guide.
Further, separated cylindrical shell comprises cylinder top, the tapered lower portion that is communicated with setting, and separated cylindrical shell, supporter, vapour-liquid delivery line arrange with one heart.
Further, the sidewall of supporter arranges the through hole of some diameter 1.5mm.
Further, the solid feed pipe of described vapour-liquid is communicated with evaporimeter, and described vapour-liquid delivery line is communicated with vapour liquid separator.
Further, the diameter of vapour-liquid delivery line is separated barrel diameter 1/4.
The invention has the beneficial effects as follows: this kind of particle separating device can, by the inert solid particle in the solid three-phase composite material of vapour-liquid, carry out separation effectively from feed liquid.The solid feed liquid of vapour-liquid, by after vaporization chamber, is sent into particle separating device, and solid particle is subject to centrifugal inertial force effect to be thrown toward wall, with lower eddy flow, is down to the cone outlet at the end, by bottom, is discharged; Vapour-liquid becomes the inward eddy of rising, from the vapour-liquid delivery line at top, discharges.Top is provided with the apertured disc of 1.5mm, effectively prevents that minority particle is from the effusion of particle separator top, thereby has realized the abundant separation of solids in feed liquid.This kind of particle separating device, cost is low, and reasonable in design is beneficial to production and application.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of the present invention;
Wherein: the separated cylindrical shell of 1-, 2-lid, the solid feed pipe of 3-vapour-liquid, 4-vapour-liquid delivery line, 5-supporter, 6-disk, 7-spiral stock guide.
The specific embodiment
Below in conjunction with accompanying drawing, describe the preferred embodiments of the present invention in detail.
Embodiment
A kind of particle separating device, as shown in Figure 1, comprise separated cylindrical shell 1 and lid 2, lid 2 is connected to the top of separated cylindrical shell 1, the top sidewall of separated cylindrical shell 1 is provided with import, import is communicated with the solid feed pipe 3 of vapour-liquid, the low side of separated cylindrical shell 1 is provided with particle discharging opening, the middle part of lid 2 is provided with outlet, outlet is communicated with vapour-liquid delivery line 4, lid 2 is connected with barrier assembly, barrier assembly comprises supporter 5 and the disk 6 of tubular hollow, one end of supporter 5 is connected on lid 2, the other end clutch disk 6 of supporter 5, disk 6 has the through hole of some diameter 1.5mm, supporter 5 is communicated with the outlet of lid 2, the inwall of separated cylindrical shell 1 is provided with spiral stock guide 7.
Between evaporator heating chamber and vapour liquid separator, be provided with particle separator, for inert solid particle is separated from feed liquid.The equipment body of particle separator is also comprised of circular cone two parts, as shown in Figure 1.The solid three-phase mixture of vapour-liquid with particle enters separated cylindrical shell 1 through the solid feed pipe 3 of vapour-liquid, along spiral stock guide 7, makes spiralling downwards, and solid particle is subject to centrifugal inertial force effect to be thrown toward wall, with lower eddy flow, is down to the cone outlet at the end, by bottom, is discharged; Vapour-liquid becomes the inward eddy of rising, from the vapour-liquid delivery line 4 at top, discharges.There is a gas column in negative pressure at internal layer eddy flow center, and gas phase is discharged thus.Separated cylindrical shell 1 top flange place is provided with the apertured disc 6 that aperture is 1.5mm, to prevent that minority particle from, from the effusion of particle separator top, improving the separative efficiency of particle.
Separated cylindrical shell 1 comprises cylinder top, the tapered lower portion that is communicated with setting, and separated cylindrical shell 1, supporter 5, vapour-liquid delivery line 4 arrange with one heart, are beneficial to the derivation of vapour-liquid.Simultaneously, the diameter of vapour-liquid delivery line 4 be separated cylindrical shell 1 diameter be preferably 1/4, blast pipe diameter is less, Particle Phase separative efficiency is larger, but when blast pipe diameter is reduced to certain amplitude, the amplitude that efficiency improves reduces, after productive experiment, improve the diameter of vapour-liquid delivery line 4, be more conducive to the raising of separative efficiency.
The diameter of supporter 5, disk 6 is 1/2 of separated cylindrical shell 1 diameter.Particle discharging opening is located at the below of disk 6.The sidewall of supporter 5 arranges the through hole of some diameter 1.5mm, makes vapour-liquid when deriving more quickly, the particle in separated vapour-liquid.
The solid feed pipe 3 of vapour-liquid is communicated with evaporimeter, after first the feed liquid that the solid three-phase of vapour-liquid mixes heats via evaporimeter, vapour-liquid is had with solids and differ larger state, can guarantee the separation of the particle of particle separating device.Vapour-liquid delivery line 4 is communicated with vapour liquid separator, carries out next step vapor-liquid separation according to Production requirement.
Claims (5)
1. a particle separating device, it is characterized in that: comprise separated cylindrical shell (1) and lid (2), lid (2) is connected to the top of separated cylindrical shell (1), the top sidewall of separated cylindrical shell (1) is provided with import, import is communicated with the solid feed pipe (3) of vapour-liquid, the low side of separated cylindrical shell (1) is provided with particle discharging opening, the middle part of lid (2) is provided with outlet, outlet is communicated with vapour-liquid delivery line (4), lid (2) is connected with barrier assembly, barrier assembly comprises supporter (5) and the disk (6) of tubular hollow, one end of supporter (5) is connected on lid (2), the other end clutch disk (6) of supporter (5), disk (6) has the through hole of some diameter 1.5mm, supporter (5) is communicated with the outlet of lid (2), the inwall of separated cylindrical shell (1) is provided with spiral stock guide (7).
2. particle separating device as claimed in claim 1, is characterized in that: described separated cylindrical shell (1) comprises cylinder top, the tapered lower portion that is communicated with setting, and separated cylindrical shell (1), supporter (5), vapour-liquid delivery line (4) arrange with one heart.
3. particle separating device as claimed in claim 2, is characterized in that: the sidewall of described supporter (5) arranges the through hole of some diameter 1.5mm.
4. the particle separating device as described in claim 1-3 any one, is characterized in that: the solid feed pipe (3) of described vapour-liquid is communicated with evaporimeter, and described vapour-liquid delivery line (4) is communicated with vapour liquid separator.
5. particle separating device as claimed in claim 4, is characterized in that: the diameter of vapour-liquid delivery line (4) is 1/4 of separated cylindrical shell (1) diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410328659.XA CN104084322A (en) | 2014-07-11 | 2014-07-11 | Particle separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410328659.XA CN104084322A (en) | 2014-07-11 | 2014-07-11 | Particle separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104084322A true CN104084322A (en) | 2014-10-08 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410328659.XA Pending CN104084322A (en) | 2014-07-11 | 2014-07-11 | Particle separation device |
Country Status (1)
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| CN (1) | CN104084322A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104525392A (en) * | 2014-12-10 | 2015-04-22 | 华北电力大学 | Cyclone separator with gradually enlarged inlet, flow guide plate and dustproof screen and experiment system |
| CN113577810A (en) * | 2021-06-24 | 2021-11-02 | 安徽佳先功能助剂股份有限公司 | High vacuum molecular distillation device for concentrating and crystallizing in dibenzoyl methane production |
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| CN202667015U (en) * | 2012-05-30 | 2013-01-16 | 郭丰亮 | Cyclone dust extractor with continuous spiral ribs on inner wall |
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| CN203972161U (en) * | 2014-07-11 | 2014-12-03 | 江苏华泰重工装备有限公司 | Particle separating device |
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2014
- 2014-07-11 CN CN201410328659.XA patent/CN104084322A/en active Pending
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| CN88100109A (en) * | 1988-01-11 | 1988-08-10 | 王宝瑞 | Produce bean curd new technology and equipment thereof fast |
| EP0371531B1 (en) * | 1988-12-01 | 1993-04-28 | METALLGESELLSCHAFT Aktiengesellschaft | Filter bed combined with a centrifugal separator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104525392A (en) * | 2014-12-10 | 2015-04-22 | 华北电力大学 | Cyclone separator with gradually enlarged inlet, flow guide plate and dustproof screen and experiment system |
| CN113577810A (en) * | 2021-06-24 | 2021-11-02 | 安徽佳先功能助剂股份有限公司 | High vacuum molecular distillation device for concentrating and crystallizing in dibenzoyl methane production |
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| C06 | Publication | ||
| PB01 | Publication | ||
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| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20141008 |