CN206688293U - A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid - Google Patents
A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid Download PDFInfo
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- CN206688293U CN206688293U CN201720276941.7U CN201720276941U CN206688293U CN 206688293 U CN206688293 U CN 206688293U CN 201720276941 U CN201720276941 U CN 201720276941U CN 206688293 U CN206688293 U CN 206688293U
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Abstract
The utility model discloses a kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid, including top plate, glass infuser, bottom plate, liquid level detector, top valve, double reduction reducing and primary speed-down reducing.The beneficial effects of the utility model are：The bubble trap energy is efficient and smoothly removes the bubble in bio-pharmaceuticals in fluid, liquid level detector is by fluid gas-liquid line of demarcation with digitized signal, PC or PLC is accurately sent to, the liquid level adjustment after the bubble discharge of separation, ensure that the high accuracy of bubble removing；Using multiple stage fluid deceleration reducing, the rate of flow of fluid inside device is effectively reduced, improves the stability of fluid conveying；The device is mainly used in the gas-liquid separation in the fluid delivery process in bio-pharmaceuticals, realizes that fluid conveying is steady, the device has mode of operation that can be manual, semi or fully automatic, and operating procedure is easy, can meet the needs of process characteristic.The bubble trap operation is convenient, and each component connection is flexible.
Description
Technical field
It the utility model is related to a kind of gas-liquid separator, the bubble of specially a kind of gas-liquid separation and steady rate of flow of fluid is fallen into
Trap, belong to pressure vessel and equipment applied technical field.
Background technology
During bio-pharmaceuticals, due to factors such as raw material, techniques, the material produced is flowing material, wherein containing big
The gas of amount and it is of great rarity, when putting into production, is often mingled with a small amount of bubble.In order to reduce conveying of the bubble in production equipment,
Designing a device for removing bubble removing is highly desirable.
In the prior art using structure members such as T-shaped pipeline, blind plugging pipeline and primary speed-down reducings, with reference to planar top, bottom
Portion forms the container of closing, using gravity, is automatically separated gas and liquid, realizes the function of bubble separation.But this kind of knot
Structure is there is also the possibility of secondary generation bubble, and bubble removal is inefficient, and fluid conveying is unstable, goes bubble precision low, degassing
The shortcomings of bulb apparatus operation is not easy.Therefore, the bubble of a kind of gas-liquid separation and steady rate of flow of fluid is proposed regarding to the issue above
Trap.
Utility model content
The purpose of this utility model is that to solve the above problems and provides a kind of gas-liquid separation and steady fluid stream
The bubble trap of speed.
The utility model is achieved through the following technical solutions above-mentioned purpose, a kind of gas-liquid separation and steady rate of flow of fluid
Bubble trap, including top plate, the top plate lower section sets glass infuser, and top valve, the top are set above the glass infuser
Liquid level detector is set below portion's valve, and bottom plate is set below the liquid level detector, sets two level to subtract above the bottom plate
Fast reducing, and primary speed-down reducing is set below the double reduction reducing.
Preferably, in order that more accurate, the top plate is detected in gas-liquid line of demarcation of the device convection body in glass infuser
Lower section sets several liquid level detectors.
Preferably, in order that the device is more accurate to the liquid level variation record after the bubble discharge of separation, this is made
Device removal bubble efficiency is higher, and the liquid level detector is attached to distal end PLC.
Preferably, in order that the rate of flow of fluid inside device is lower, the agitation of fluid is reduced, makes the flow of fluid in equipment
Steadily, the primary speed-down reducing and the double reduction reducing are in arc-shaped structure.
Preferably, in order that the bubble can quickly discharge from fluid, the top valve side sets out bubble mouth.
Preferably, in order that the device can lead into the fluid needed for bio-pharmaceuticals and bubble is removed to it, and go
Fluid discharge after bubble removing, the bottom plate side sets upward charging aperture and side minimum point sets discharging opening.
The beneficial effects of the utility model are：The bubble trap energy is efficiently and smoothly in removal bio-pharmaceuticals in fluid
Gas-liquid line of demarcation of the fluid in glass infuser with digitized signal, is accurately sent to PC or PLC by bubble, liquid level detector,
Liquid level adjustment after the bubble discharge of separation, in order to avoid the factor such as error signal, exterior materials is disturbed, ensure that bubble removing
High accuracy；Using multiple stage fluid deceleration reducing, the rate of flow of fluid inside device is effectively reduced, the agitation of fluid is reduced, makes to set
Flow of fluid in standby is steady, improves the stability of fluid conveying；The device is mainly used in the fluid transmission in bio-pharmaceuticals
During gas-liquid separation, realize that fluid conveying is steady, the device has mode of operation that can be manual, semi or fully automatic,
Operating procedure is easy, can meet the needs of process characteristic.The bubble trap operation is convenient, and each component connection is flexible.
Brief description of the drawings
Fig. 1 is the utility model overall structure diagram.
In figure：1st, top plate；2nd, glass infuser；3rd, bottom plate；4th, liquid level detector；5th, top valve；6th, double reduction reducing；7、
Primary speed-down reducing.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
Refer to shown in Fig. 1, the bubble trap of a kind of gas-liquid separation and steady rate of flow of fluid, including top plate 1, under top plate 1
Side sets glass infuser 2, and the top of glass infuser 2 sets top valve 5, and the lower section of top valve 5 sets liquid level detector 4, and liquid level
The lower section of detector 4 sets bottom plate 3, and the top of bottom plate 3 sets double reduction reducing 6, and the lower section of double reduction reducing 6 sets one-level to subtract
Fast reducing 7.
As a kind of technical optimization scheme of the present utility model, the lower section of top plate 1 sets several liquid level detectors 4, makes this
Gas-liquid line of demarcation detection of the device convection body in glass infuser is more accurate.
As a kind of technical optimization scheme of the present utility model, liquid level detector 4 is attached to distal end PLC, made inside device
Rate of flow of fluid it is lower, reduce the agitation of fluid, make the flow of fluid in equipment steady.
As a kind of technical optimization scheme of the present utility model, primary speed-down reducing 7 and double reduction reducing 6 are in circular arc
Shape structure, make the rate of flow of fluid inside device lower, reduce the agitation of fluid, make the flow of fluid in equipment steady.
As a kind of technical optimization scheme of the present utility model, the side of top valve 5 sets out bubble mouth, enable bubble from
Quickly discharged in fluid.
As a kind of technical optimization scheme of the present utility model, the side of bottom plate 3 sets upward charging aperture and side minimum point
Discharging opening is set, the device is led into the fluid needed for bio-pharmaceuticals and bubble is removed to it, and after removing bubble removing
Fluid discharge.
When in use, first, whole bubble trap location is fixed for the utility model, secondly, is using the bubble trap
When realized and automatically control by PC or PLC by the top valve 5 of the top of top plate 1, by glass infuser 2 be used for fluid it is temporary and
Fluid level position is observed, multiple double reduction reducings 6 are used to realize the steady logical of fluid with primary speed-down reducing 7 on bottom plate 3
Cross, discharge the bubble being wherein mixed with and meet the automatic of bio-pharmaceuticals industry standard and drain function etc., effectively reduce in device
The rate of flow of fluid in portion, the agitation of fluid is reduced, make the flow of fluid in equipment steady, the stability for improving fluid conveying passes through
Gas-liquid line of demarcation of the fluid in glass infuser 2 with digitized signal, is accurately sent to PLC, the gas of separation by liquid level detector 4
Liquid level adjustment after bubble discharge, in order to avoid the factor such as error signal, exterior materials is disturbed, ensure that the high-precision of bubble removing
Degree.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of without departing substantially from spirit or essential attributes of the present utility model, it can realize that this practicality is new in other specific forms
Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new
The scope of type limits by appended claims rather than described above, it is intended that the equivalency fallen in claim is contained
All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as limitation
Involved claim.
Moreover, it will be appreciated that although the present specification is described in terms of embodiments, not each embodiment is only wrapped
Containing an independent technical scheme, this narrating mode of specification is only that those skilled in the art should for clarity
Using specification as an entirety, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
It is appreciated that other embodiment.
Claims (6)
1. a kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid, including top plate（1）, it is characterised in that：The top plate（1）
Lower section sets glass infuser（2）, and the glass infuser（2）Top sets top valve（5）, the top valve（5）Lower section is set
Liquid level detector（4）, and the liquid level detector（4）Lower section sets bottom plate（3）, the bottom plate（3）Top sets double reduction
Reducing（6）, and the double reduction reducing（6）Lower section sets primary speed-down reducing（7）.
2. a kind of gas-liquid separation according to claim 1 and the bubble trap of steady rate of flow of fluid, it is characterised in that：It is described
Top plate（1）Lower section sets several liquid level detectors（4）.
3. a kind of gas-liquid separation according to claim 1 and the bubble trap of steady rate of flow of fluid, it is characterised in that：It is described
Liquid level detector（4）It is attached to distal end PLC.
4. a kind of gas-liquid separation according to claim 1 and the bubble trap of steady rate of flow of fluid, it is characterised in that：It is described
Primary speed-down reducing（7）With the double reduction reducing（6）It is in arc-shaped structure.
5. a kind of gas-liquid separation according to claim 1 and the bubble trap of steady rate of flow of fluid, it is characterised in that：It is described
Top valve（5）Side sets out bubble mouth.
6. a kind of gas-liquid separation according to claim 1 and the bubble trap of steady rate of flow of fluid, it is characterised in that：It is described
Bottom plate（3）Side sets upward charging aperture and side minimum point sets discharging opening.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720276941.7U CN206688293U (en) | 2017-03-21 | 2017-03-21 | A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720276941.7U CN206688293U (en) | 2017-03-21 | 2017-03-21 | A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206688293U true CN206688293U (en) | 2017-12-01 |
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ID=60443742
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720276941.7U Active CN206688293U (en) | 2017-03-21 | 2017-03-21 | A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206688293U (en) |
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2017
- 2017-03-21 CN CN201720276941.7U patent/CN206688293U/en active Active
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| GR01 | Patent grant | ||
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| CP03 | Change of name, title or address |
Address after: 200000 Building 1, No. 399, jinliu Road, Jinshan District, Shanghai Patentee after: Shanghai dongfulong Haiwei Biotechnology Co.,Ltd. Address before: 215138 No. 9, donghenggang street, Yangchenghu Town, Xiangcheng District, Suzhou City, Jiangsu Province Patentee before: SUZHOU HAIWEI BIOTECHNOLOGY CO.,LTD. |