CN102284385A - Built-in cyclone separator device - Google Patents

Built-in cyclone separator device Download PDF

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Publication number
CN102284385A
CN102284385A CN2011102051038A CN201110205103A CN102284385A CN 102284385 A CN102284385 A CN 102284385A CN 2011102051038 A CN2011102051038 A CN 2011102051038A CN 201110205103 A CN201110205103 A CN 201110205103A CN 102284385 A CN102284385 A CN 102284385A
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CN
China
Prior art keywords
cyclone separator
return pipe
crystallizing evaporator
built
barrel
Prior art date
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Application number
CN2011102051038A
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Chinese (zh)
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CN102284385B (en
Inventor
杭文甫
杭新健
杨士鑫
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WUXI RONGFENG BIOLOGICAL ENGINEERING Co Ltd
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WUXI RONGFENG BIOLOGICAL ENGINEERING Co Ltd
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Priority to CN 201110205103 priority Critical patent/CN102284385B/en
Publication of CN102284385A publication Critical patent/CN102284385A/en
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Publication of CN102284385B publication Critical patent/CN102284385B/en
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Abstract

The invention relates to a built-in cyclone separator device, which belongs to the technical field of mechanical equipment manufacturing and comprises a liquid return pipe, a lower cone, a barrel, an air return pipe, a helical plate, a flush pipe and a fixing plate, wherein the air return pipe is arranged in the barrel; the helical plate is arranged between the air return pipe and the barrel; the flush pipe is connected with the air return plate; the lower end of the barrel is provided with the lower cone; the lower cone and the liquid return pipe are welded; the upper end of the barrel is fixedly connected with the fixing plate; and the fixing plate and the upper seal head of a crystallizing evaporator are welded and fixed. The built-in cyclone separator device is capable of reducing the manufacturing cost of a whole crystallizing evaporator system and saving the space of the plant arrangement of the whole crystallizing evaporator system and has low manufacturing cost; the flowing direction of airflow is controlled through the guide action of the helical plate; the accumulation of liquid in the liquid return pipe can be avoided, and moreover, the temperature of the liquid is consistent with that of the crystallizing evaporator, thus, material crystallization caused by temperature drop is avoided, and a separator can also be washed at irregular time through the annular flush pipe, thereby, the blockage of the liquid return pipe is avoided.

Description

Built-in cyclone separator means
Technical field
The present invention relates to a kind of vapor-liquid separating device, specifically be used for the vapor-liquid separation of crystallizing evaporator system, belong to biofermentation, chemical mechanical equipment manufacturing technology field.
Background technology
The effect of cyclone separator in the crystallizing evaporator system is the material of carrying secretly in the separated secondary steam.In traditional prior art, cyclone separator generally all is the outside that is placed on crystallizing evaporator, can take the space that entire equipment is arranged usually; Simultaneously,, to thicken during the design of separator tank skin, make whole cost of manufacture to promote because whole system is the negative pressure operation; Cyclone separator generally all arranges in a high position, when heavier, needs to give the separator designs support to bear deadweight as this body weight of separator; Crystallizing evaporator has crystal and produces, and makes cyclone separator liquid back pipe (U type pipe) stop up easily, promptly uses hot water also to be difficult to clean, and loses separating effect.
Summary of the invention
The objective of the invention is to overcome above-mentioned weak point, thereby a kind of built-in cyclone separator means is provided, the space that can reduce whole evaporation and crystallization system is arranged, reduces the cost of whole workshop and cyclone separator body, solves the liquid back pipe blocking problem.
According to technical scheme provided by the invention, built-in cyclone separator means comprises liquid back pipe, lower cone, cylindrical shell, muffler, spiral plate, jet water spout and fixed head, be provided with muffler in the described cylindrical shell, between muffler and cylindrical shell, be furnished with spiral plate, jet water spout is connected with muffler, and described cylindrical shell lower end is provided with lower cone, and lower cone and liquid back pipe are welded to connect, the fixedly connected fixed head in described cylindrical shell upper end, fixed head and the welding of crystallizing evaporator upper cover are fixing.
Described liquid back pipe is a straight tube.The spiral angle of described spiral plate is: between 30 ° to 45 °
Described jet water spout is annular jet water spout.
The present invention is simple, compact and reasonable for structure; Can reduce the cost of whole crystallizing evaporator system, save the space that whole crystallizing evaporator system workshop is arranged, cost of manufacture is cheap; Control the flow direction of air-flow by the guide effect of spiral plate; Simultaneously, because liquid back pipe is straight tube, avoided liquid accumulating in liquid back pipe, and temperature is consistent with crystallizing evaporator, avoided causing the material crystallization because of temperature drop, again can be by jet water spout not timing separator is cleaned, thus avoided the obstruction of liquid back pipe; Liquid back pipe outlet design is avoided air-flow to form short circuit in liquid back pipe and is reduced separating effect when crystallizing evaporator moves below the liquid level.
Description of drawings
Fig. 1 is a structural front view of the present invention.
Fig. 2 is a structure vertical view of the present invention.
The specific embodiment
 
Embodiment during following the present invention incites somebody to action in conjunction with the accompanying drawings is further described:
As shown in Figure 1, comprising: liquid back pipe 1, lower cone 2, cylindrical shell 3, muffler 4, spiral plate 5, jet water spout 6 and fixed head 7 etc.
Be provided with muffler 4 in the cylindrical shell 3 of the present invention, be furnished with spiral plate 5 between muffler 4 and cylindrical shell 3, the spiral angle of described spiral plate 5 is: between 30 ° to 45 °, jet water spout 6 is connected with muffler 4, and described jet water spout 6 is annular jet water spout.Described cylindrical shell 3 lower ends are provided with lower cone 2, and lower cone 2 is welded to connect with liquid back pipe 1, and described liquid back pipe 1 is a straight tube.The fixedly connected fixed head 7 in described cylindrical shell 3 upper ends, fixed head 7 is fixing with the welding of crystallizing evaporator upper cover.
The present invention determines the diameter of muffler 4 and the cylindrical shell clearance distance to crystallizing evaporator upper cover (top) according to the evaporation capacity (indirect steam vapour amount) of crystallizing evaporator, and then the diameter of definite cylindrical shell 3, determine the angle of spiral plate 5 according to the indirect steam flow velocity.After whole cyclone separator completes separately, jet water spout 6 and crystallizing evaporator upper cover preformed hole are welded to connect finish earlier, again muffler 4 and crystallizing evaporator top preformed hole are implemented to be welded to connect; In welding process, to keep whole cyclone separator vertical with the angle of evaporative crystallization, fixing by 3 fixed heads 7 then with the welding of crystallizing evaporator upper cover.At last liquid back pipe 1 and cone 2 are welded to connect.
The operation principle of the present invention and the course of work:
No matter be which kind of material, in the crystallizing evaporator evaporation process, always carry a certain amount of material secretly in the indirect steam and escape outward.By cyclone separator the time, the first gap by cyclone separator and crystallizing evaporator of indirect steam enters revolves the branch separator, enter then between muffler 4 and the cylindrical shell 3, then according to the angle rotational flow of spiral plate 5, produce centrifugal force, make the heavier material of proportion flow down, be back to crystallizing evaporator by liquid back pipe then along cylindrical shell and cone inwall.Indirect steam then can flow to next body or the condenser of imitating by muffler.
Crucial effect is played in the setting of the present invention spiral plate and angle thereof in work, reach the flows at angles of forcing indirect steam to envision by it according to design, in the whole flow process of air-flow, the centrifugal force that produces with the fluid separation applications of carrying secretly in the air-flow to the separator inwall, thereby flow to liquid back pipe along inwall, gas is then overflowed from muffler fast, produces certain centrifugal force, thereby has reached the purpose that makes gas and fluid separation applications.Simultaneously be provided with annular jet water spout, can be used to clean whole separator by external hot water on separator top.
Points for attention of the present invention:
1, to polish whole cyclone separator, reduce the material wall cling phenomenon.2, regularly by jet water spout to the cleaning of washing by water of cyclone separator inside.When 3, whole crystallizing evaporator is shut down maintenance, check whether liquid back pipe has clogging.

Claims (4)

1. built-in cyclone separator means, it is characterized in that: comprise liquid back pipe (1), lower cone (2), cylindrical shell (3), muffler (4), spiral plate (5), jet water spout (6) and fixed head (7), be provided with muffler (4) in the described cylindrical shell (3), between muffler (4) and cylindrical shell (3), be furnished with spiral plate (5), jet water spout (6) is connected with muffler (4), described cylindrical shell (3) lower end is provided with lower cone (2), lower cone (2) is connected with liquid back pipe (1), described cylindrical shell (3) upper end fixedly connected fixed head (7), fixed head (7) is fixing with the welding of crystallizing evaporator upper cover.
2. built-in cyclone separator means as claimed in claim 1 is characterized in that: described liquid back pipe (1) is a straight tube.
3. built-in cyclone separator means as claimed in claim 1 is characterized in that: the spiral angle of described spiral plate (5) is: 30 ° to 45 °.
4. built-in cyclone separator means as claimed in claim 1 is characterized in that: described jet water spout (6) is annular jet water spout.
CN 201110205103 2011-07-21 2011-07-21 Built-in cyclone separator device Active CN102284385B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201110205103 CN102284385B (en) 2011-07-21 2011-07-21 Built-in cyclone separator device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201110205103 CN102284385B (en) 2011-07-21 2011-07-21 Built-in cyclone separator device

Publications (2)

Publication Number Publication Date
CN102284385A true CN102284385A (en) 2011-12-21
CN102284385B CN102284385B (en) 2013-04-10

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Family Applications (1)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1565318A (en) * 1925-04-06 1925-12-15 Ernest F Fisher Separator
BE824428A (en) * 1974-01-16 1975-07-16 DEVICE FOR THE SEPARATION OF POLLUTANTS FROM GASES
US4559068A (en) * 1983-08-25 1985-12-17 Tetra Pak International Ab Arrangement for the separation of particles
JP2002022102A (en) * 2000-07-12 2002-01-23 Shinei Kk Clean steam generating device
CN201701781U (en) * 2010-06-08 2011-01-12 河北工业大学 Vacuum flash evaporation mould
CN202155273U (en) * 2011-07-21 2012-03-07 无锡荣丰生物工程有限公司 Built-in cyclone separator device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1565318A (en) * 1925-04-06 1925-12-15 Ernest F Fisher Separator
BE824428A (en) * 1974-01-16 1975-07-16 DEVICE FOR THE SEPARATION OF POLLUTANTS FROM GASES
US4559068A (en) * 1983-08-25 1985-12-17 Tetra Pak International Ab Arrangement for the separation of particles
JP2002022102A (en) * 2000-07-12 2002-01-23 Shinei Kk Clean steam generating device
CN201701781U (en) * 2010-06-08 2011-01-12 河北工业大学 Vacuum flash evaporation mould
CN202155273U (en) * 2011-07-21 2012-03-07 无锡荣丰生物工程有限公司 Built-in cyclone separator device

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Denomination of invention: Built-in cyclone separator device

Effective date of registration: 20140211

Granted publication date: 20130410

Pledgee: Agricultural Bank of China Limited by Share Ltd Wuxi science and Technology Branch

Pledgor: Wuxi Rongfeng Biological Engineering Co., Ltd.

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Pledgor: Wuxi Rongfeng Biological Engineering Co., Ltd.

Registration number: 2014990000097

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Denomination of invention: Built-in cyclone separator device

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Pledgee: Agricultural Bank of China, Limited by Share Ltd, Wuxi, Binhu branch

Pledgor: Wuxi Rongfeng Biological Engineering Co., Ltd.

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Pledgee: Agricultural Bank of China Limited by Share Ltd. Wuxi Binhu branch

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Denomination of invention: Built in cyclone separator

Effective date of registration: 20210325

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Pledgee: Agricultural Bank of China Limited by Share Ltd. Wuxi Binhu branch

Pledgor: WUXI RONGFENG BIOENGINEERING Co.,Ltd.

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