CN109621470A - The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment - Google Patents
The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment Download PDFInfo
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- CN109621470A CN109621470A CN201811612870.9A CN201811612870A CN109621470A CN 109621470 A CN109621470 A CN 109621470A CN 201811612870 A CN201811612870 A CN 201811612870A CN 109621470 A CN109621470 A CN 109621470A
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- liquid
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- distillation equipment
- light fraction
- export
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- 239000007788 liquid Substances 0.000 title claims abstract description 152
- 238000004821 distillation Methods 0.000 title claims abstract description 33
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical group NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 title description 3
- BRXCDHOLJPJLLT-UHFFFAOYSA-N butane-2-sulfonic acid Chemical compound CCC(C)S(O)(=O)=O BRXCDHOLJPJLLT-UHFFFAOYSA-N 0.000 title description 3
- 238000000926 separation method Methods 0.000 claims abstract description 46
- 238000005215 recombination Methods 0.000 claims abstract description 23
- 230000006798 recombination Effects 0.000 claims abstract description 23
- 239000003638 chemical reducing agent Substances 0.000 claims description 7
- 230000004888 barrier function Effects 0.000 claims description 3
- 239000000523 sample Substances 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims 2
- 238000000034 method Methods 0.000 abstract description 7
- 238000005086 pumping Methods 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000470 constituent Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 230000005484 gravity Effects 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 4
- 101000911390 Homo sapiens Coagulation factor VIII Proteins 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 102000057593 human F8 Human genes 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000011344 liquid material Substances 0.000 description 2
- 229940047431 recombinate Drugs 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/02—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
Abstract
The present invention relates to the gas-liquid separators that can be used in distillation equipment, comprising: separator body is respectively the area Fen Qi and liquid separation area in separator body from top to bottom；There is gas-liquid entrance at the top of the area Fen Qi；There is exhaust outlet on side wall；The light fraction outlet and recombination sub-export of liquid are from top to bottom followed successively by separator body side wall.It can be seen via above technical scheme that compared with prior art, the present disclosure provides the gas-liquid separators that can be used in distillation equipment effectively to separate the liquid of different component since separator includes the light fraction outlet and recombination sub-export of liquid；Various concentration liquid after separation is handled by subsequent technique；Thus at least partly heavies liquid returns back to top portion without carrying out repeatedly pumping circulation, reduces pumping energy consumption, improves gas-liquid separation efficiency, and then can be realized the continuous processing of gas-liquid separation.
Description
Technical field
The present invention relates to gas and liquid separation technology fields, more particularly to can be used for the gas-liquid separation in distillation equipment
Device.
Background technique
Gas-liquid separator is to utilize gas-liquid specific gravity different, and the quality of gas is smaller than the quality of liquid under same volume.One
In the container of a sudden enlargement, after flow velocity reduces, during main fluid turns to, in gas phase subtle drop sink and with gas
Lime set recycling or gas phase purifying are realized in body separation.
Existing distillation technique, such as in the equipment of falling film evaporator, liquid is entering one after heat exchanger tube
A gas-liquid separation space；On this gas-liquid separation space, in addition to having gas vent, there is usually one liquid outlets.And
On this same liquid outlet, as liquid be not achieved enrichment (such as first liquid blowback heat exchanger is exchanged heat evaporation repeatedly with pump,
After liquid reaches certain enrichment, by concentrate pump to specified containers) need to carry out heat exchange evaporation repeatedly.In such case
Under, heat exchanger, waste pump can be pumped back to repeatedly for a long time into the fixedness impurity in the liquid of gas-liquid separation space
Capacity power causes to waste exchange capability of heat；And above-mentioned separation cannot achieve the technological operation of continuous processing concentrate, and then reduce
Gas-liquid separation efficiency.
Therefore, how to provide one kind to be capable of the device raising separative efficiency of continuous processing gas-liquid separation is those skilled in the art
The problem of member's urgent need to resolve.
Summary of the invention
In view of this, overcoming and dividing in the prior art the present invention provides the gas-liquid separator that can be used in distillation equipment
It cannot achieve continuous processing concentrate from device, the technical issues of gas-liquid separation efficiency.
To achieve the goals above, the present invention adopts the following technical scheme:
The gas-liquid separator provided by the invention that can be used in distillation equipment, comprising:
Separator body is respectively the area Fen Qi and liquid separation area in separator body from top to bottom；There is gas at the top of the area Fen Qi
Liquid entrance；There is exhaust outlet on side wall；Light fraction outlet and the recombination of liquid are from top to bottom followed successively by separator body side wall
Sub-export.
It can be seen via above technical scheme that compared with prior art, the present disclosure provides can be used for distillation equipment
In gas-liquid separator, due to separator include liquid light fraction outlet and recombination sub-export, effectively by different component
Liquid is separated；Various concentration liquid after separation is handled by subsequent technique；Thus at least partly heavies liquid is not necessarily to
It carries out repeatedly pumping circulation to return back to top portion, reduces pumping energy consumption, improve gas-liquid separation efficiency, and then can be realized gas-liquid separation
Continuous processing.
Preferably, the adjustment structure for adjusting liquid level is provided at light fraction outlet；Using this scheme due to dividing
It is adjustable from the intrinsic liquid level of device, therefore improve the quality of liquid separation.
Preferably, adjustment structure includes: shell, fixing piece, supporting element, bolt and overflow baffle；
Shell forms one with separator body and goes out liquid space detachably in separator body, at least partly and gently
Component outlet or liquid barrier；Wherein, shell liquid import is greater than light fraction outlet；And it is formed with light fraction outlet side
Shoulder block；There is liquid outlet on shell；
Fixing piece is welded on the side wall in light fraction outlet channel, has inserting groove thereon；
Supporting element is plugged in inserting groove；And there are multiple threaded holes on supporting element；
Bolt include it is multiple, with threaded hole corresponding matching, extension end be inserted into light fraction outlet liquid outlet channel on；
Overflow baffle has multiple groups difference size, by bolt press be connected at shoulder block, and at shoulder block it is replaceable not
Same size.
Using the effect of this scheme are as follows: the overflow baffle for replacing different sizes (height dimension) according to the usage requirement passes through
Bolt press is connected at shoulder block, realizes the purpose for adjusting liquid level in separator body；Wherein, when installation, first unscrew spiral shell
Bolt, the extension end of bolt far from shoulder block at, overflow baffle can be replaced at this time；After replacement, bolt is tightened, by the overflow after replacement
Baffle presses at shoulder block.Separator body liquid level refers to the depth of liquid level in this programme, can directly affect that liquid is light, recombination
Point separation situation, the present invention by regulating liquid surface height, make in separator body liquid material stock few as far as possible and liquid gently, heavy constituent
Reach equilibrium state between separation is good as far as possible, further improves liquid separative efficiency.
Preferably, the gas-liquid separator provided by the invention that can be used in distillation equipment further includes valve or reducer pipe；Valve
Door or reducer pipe are installed in recombination sub-export, and the concentration of liquid is wanted after can reach separation by manually opening or closing valve
It asks；Or length of pipe is increased by reducer pipe, it is equally reached above-mentioned purpose.In technical solution of the present invention, sub-export is recombinated
Place's plugging structure is not limited to aforesaid way, as long as should all fall into have different component split tunnels in separator body
In protection scope of the present invention.
Preferably, above-mentioned valve can be solenoid valve, and solenoid valve is electrically connected with the power supply, can be closed according to solenoid valve
Time control heavy constituent formation, then open battery valve, by heavies liquid through recombination sub-export release；The on-off of power supply
It can be realized by switch；The manipulation strength of personnel is reduced with this, reducing manual operation factor influences, and then improves disintegrate-quality
And efficiency.
The hollow cone that be preferably separated device ontology from top to down include hollow cylinder and is connected to cylindrical body；Cylinder
In vivo it is the area Fen Qi, is liquid separation area in cone；Light fraction outlet is opened on the side wall of the cone of cylinder bottom；
Recombinate the tapered end that sub-export is set to cone.Using this scheme, liquid separation area space is big, after being conducive to gas-liquid entrance, makees in gravity
With lower separation gas, gas is excluded by exhaust outlet；Liquid under the effect of gravity, be not in together according to component liquid separation area top or
The liquid of bottom, different component is excluded by light fraction outlet or recombination sub-export；The liquid separation area of cone is conducive to convergence weight
Component fluids.
Preferably, light fraction outlet is opened on the side wall of the cone of cylinder bottom, and recombination sub-export is located at
Cone tapering.Thus facilitate separation light component liquid and heavies liquid.Wherein light fraction outlet can be hole class formation,
It can be for certain jointing structure.
Preferably, exhaust outlet is one or more.It is selected according to specific use.
Wherein, light fraction outlet and recombination sub-export number are selected according to specifically used in the present invention, but only
The same or similar scheme for being related to being provided with multiple liquid outlets on separator body should all fall into protection of the invention
Range.
Preferably, the gas-liquid separator provided by the invention that can be used in distillation equipment, further includes on-line densimeter, online
The probe of densitometer is installed on heavy constituent near exit；On-line densimeter can be using MH5300 densitometer etc., can be very convenient
Reading test liquid density value.
It is selectable, it can also be obtained by controller, controller electrically connects using density signal is changed into electric signal
Solenoid valve is connect, and density requirements control solenoid valve as needed opens or closes.
Preferably, the gas-liquid separator provided by the invention that can be used in distillation equipment, further includes inclined plate；Inclined plate first end
It is fixed in separator body；Its second end favours above light fraction outlet；Its first end can between stationary separator ontology
On, or fixed by connector；Using the purpose of this scheme: its middle swash plate can stop the liquid entered by gas-liquid entrance,
It prevents from falling in the liquid of overflow port (i.e. light fraction outlet) nearby to have little time the separation of weight component and flow directly out；It further increases
Liquid separative efficiency.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
The embodiment of invention for those of ordinary skill in the art without creative efforts, can also basis
The attached drawing of offer obtains other attached drawings.
Fig. 1 attached drawing is the gas-liquid separator perspective view provided by the invention that can be used in distillation equipment；
Fig. 2 attached drawing is the gas-liquid separator half-sectional perspective view provided by the invention that can be used in distillation equipment；
Fig. 3 attached drawing is that the schematic diagram of the gas-liquid separator adjustment structure provided by the invention that can be used in distillation equipment (divides
Gas area, shell are not shown).
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
The embodiment of the invention discloses the gas-liquid separator that can be used in distillation equipment, separator in the prior art is overcome
It cannot achieve continuous processing concentrate, the technical issues of gas-liquid separation efficiency.
Referring to attached drawing 1, the gas-liquid separator provided by the invention that can be used in distillation equipment, comprising:
Separator body 1 is respectively the area Fen Qi and liquid separation area in separator body 1 from top to bottom；Have at the top of the area Fen Qi
Gas-liquid entrance 11；There is exhaust outlet 12 on side wall；The light fraction outlet of liquid is from top to bottom followed successively by separator body side wall
13 and recombination sub-export 14.
The present invention discloses the gas-liquid separator that can be used in distillation equipment of offer, since separator body 1 includes liquid
Light fraction outlet 13 and recombination sub-export 14, effectively the liquid of different component is separated；Various concentration after separation
Liquid is handled by subsequent technique；Thus at least partly heavies liquid returns back to top portion without carrying out repeatedly pumping circulation, reduces
Energy consumption is pumped, improves gas-liquid separation efficiency, and then can be realized the continuous processing of gas-liquid separation.
In one embodiment of the invention, the adjusting knot for adjusting liquid level is provided at light fraction outlet 13
Structure；Thus the liquid level in separator body 1 is adjustable, therefore improves the quality of liquid separation.
Specifically, adjustment structure includes: shell 4, fixing piece 5, supporting element 6, bolt and overflow baffle referring to attached drawing 3
7；
Shell 4 forms one with separator body 1 and goes out liquid space detachably in separator body 1, at least partly with
The connection of light fraction outlet 13 or liquid barrier；Wherein, the liquid-inlet of shell 4 is greater than light fraction outlet 13；And go out with light component
13 sides of mouth form shoulder block；There is liquid outlet on shell 4；
Fixing piece 5 is welded on the side wall in 13 channel of light fraction outlet, has inserting groove thereon；
Supporting element 6 is plugged in inserting groove；And there are multiple threaded holes on supporting element 6；
Bolt include it is multiple, with threaded hole corresponding matching, extension end be inserted into light fraction outlet 13 liquid outlet channel on；
Overflow baffle 7 has multiple groups difference size, by bolt press be connected at shoulder block, and at shoulder block it is replaceable not
Same size.
The overflow baffle that above scheme replaces different sizes (height dimension) according to the usage requirement is supported by bolt press
It is connected at shoulder block, realizes the purpose for adjusting liquid level in separator body；Wherein, it when installation, first loosers a bolt, bolt is stretched
Outlet far from shoulder block at, overflow baffle can be replaced at this time；After replacement, tighten bolt, by after replacement overflow baffle press in
At shoulder block.Separator body liquid level refers to the depth of liquid level in this programme, can directly affect that liquid is light, separation feelings of heavy constituent
Condition, the present invention by regulating liquid surface height, make in separator body liquid material stock it is few as far as possible with liquid gently, that heavy constituent separates is good as far as possible
Between reach equilibrium state, further improve liquid separative efficiency.
Wherein, the size of shell 4, concrete shape are selected according to the capacity and shape of separator body 1；Fixing piece 5 can be with
For one or more, shape can be according to the structure choice of separator body 1；Supporting element 6 can be strip, sheet or column；
Overflow baffle 7 may include the component of various structures size, can select to use according to different needs.
In above scheme, it is specifically not limited to the above-mentioned embodiment enumerated, as long as comprising above-mentioned on light fraction outlet 13
Setting liquid level adjustment structure should all be fallen within the scope of protection of the present invention.
It should further be appreciated that the gas-liquid separator provided by the invention that can be used in distillation equipment, further includes valve or variable diameter
Pipe；Valve or reducer pipe be installed on recombination sub-export on, by manually open or close valve can reach separation after liquid it is dense
Degree requires；Or length of pipe is increased by reducer pipe, it is equally reached above-mentioned purpose.In technical solution of the present invention, heavy constituent
Exit plugging structure is not limited to aforesaid way, as long as to have different component split tunnels in separator body, it should all
It falls within the scope of protection of the present invention.
Above-mentioned valve can be solenoid valve, and solenoid valve is electrically connected with the power supply, the time that can be closed according to solenoid valve
The formation for controlling heavy constituent, then opens battery valve, and heavies liquid is released through recombinating sub-export 14；The on-off of power supply can be with
It is realized by switch；The manipulation strength of personnel is reduced with this, reducing manual operation factor influences, and then improves disintegrate-quality and effect
Rate.
Advantageously, in one embodiment of the invention, separator body 1 include from top to down hollow cylinder and with
The hollow cone of cylindrical body connection；The area cylindrical body Nei Weifenqi, interior cone is liquid separation area；Light fraction outlet 13, which is opened in, to be leaned on
On the side wall of the cone of nearly cylinder bottom；Recombinate the tapered end that sub-export 14 is set to cone.Liquid separation area space is big as a result,
After being conducive to gas-liquid entrance, gas is separated under the effect of gravity, gas is excluded by exhaust outlet 12；Liquid under the effect of gravity, root
The top or bottom in liquid separation area it are not in together according to component, the liquid of different component passes through light fraction outlet 13 or recombination sub-export 14
It excludes；The liquid separation area of cone is conducive to converge heavies liquid.
It should further be appreciated that light fraction outlet 13 is opened on the side wall of the cone of cylinder bottom, recombination is separated
Mouth 14 is located at cone tapering.Thus facilitate separation light component liquid and heavies liquid.Wherein light fraction outlet 13 can be
Hole class formation, or there is certain jointing structure.
In another embodiment of the present invention, exhaust outlet 12 is one or more.It needs to carry out according to specific use
Selection.
Wherein, light fraction outlet 13 and recombination 14 numbers of sub-export are selected according to specifically used in the present invention,
But as long as the same or similar scheme for being related to being provided with multiple liquid outlets on separator body should all fall into of the invention
Protection scope.
In other embodiments of the invention, the gas-liquid separator provided by the invention that can be used in distillation equipment, also
Including on-line densimeter, the probe of on-line densimeter is installed near recombination sub-export 14；On-line densimeter can use
MH5300 densitometer etc. can very easily read the density value of test liquid.
It is selectable, it can also be obtained by controller, controller electrically connects using density signal is changed into electric signal
Solenoid valve is connect, and density requirements control solenoid valve as needed opens or closes.
Referring to attached drawing 2, the gas-liquid separator provided by the invention that can be used in distillation equipment further includes inclined plate 3；Inclined plate 3
First end is fixed in separator body 1；Its second end favours 13 top of light fraction outlet；Its first end can between fixed point
It is fixed from device ontology 1, or by connector；Using the purpose of this scheme: its middle swash plate 3 can stop by gas-liquid entrance into
The liquid entered prevents from falling in the liquid of overflow port (i.e. light fraction outlet 13) nearby and has little time the separation of weight component and directly flow
Out；Further improve liquid separative efficiency.
Gas-liquid separator of the invention is not limited to be applied in acrylamide group methyl propane sulfonic acid distillation equipment, Ke Yiying
It uses in any distillation equipment for needing gas-liquid separation.
Each embodiment in this specification is described in a progressive manner, the highlights of each of the examples are with other
The difference of embodiment, the same or similar parts in each embodiment may refer to each other.For device disclosed in embodiment
For, since it is corresponded to the methods disclosed in the examples, so being described relatively simple, related place is said referring to method part
It is bright.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention.
Various modifications to these embodiments will be readily apparent to those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, of the invention
It is not intended to be limited to the embodiments shown herein, and is to fit to and the principles and novel features disclosed herein phase one
The widest scope of cause.
Claims (10)
1. the gas-liquid separator that can be used in distillation equipment characterized by comprising
Separator body (1), the interior separator body (1) is respectively the area Fen Qi and liquid separation area from top to bottom；The area Fen Qi
Top has gas-liquid entrance (11), has exhaust outlet (12) on side wall；On separator body (1) side wall from top to bottom successively
Light fraction outlet (13) and recombination sub-export (14) equipped with liquid.
2. the gas-liquid separator according to claim 1 that can be used in distillation equipment, which is characterized in that the light component goes out
The adjustment structure for adjusting liquid level is provided at mouth (13).
3. the gas-liquid separator according to claim 2 that can be used in distillation equipment, which is characterized in that the adjustment structure
It include: shell (4), fixing piece (5), supporting element (6), bolt and overflow baffle (7)；
The shell (4) forms one with the separator body (1) and goes out liquid detachably on the separator body (1)
Space, the liquid space out is at least partly connected to the light fraction outlet (13) or liquid barrier；Wherein, the shell (4)
Liquid-inlet is greater than the light fraction outlet (13)；And shoulder block is formed with the light fraction outlet (13) side；The shell (4)
It is upper that there is liquid outlet；
The fixing piece (5) is welded on the side wall in the light fraction outlet (13) channel, has inserting groove thereon；
The supporting element (6) is plugged in the inserting groove；And there are multiple threaded holes on the supporting element (6)；
The bolt include it is multiple, with the threaded hole corresponding matching, the light fraction outlet (13) is inserted into extension end
On liquid outlet channel；
The overflow baffle (7) has multiple groups difference size, by the bolt press be connected at the shoulder block, and with it is described
Replaceable difference size at shoulder block.
4. the gas-liquid separator according to claim 1 that can be used in distillation equipment, which is characterized in that further include valve or
Reducer pipe；The valve or reducer pipe are installed on the recombination sub-export (14).
5. the gas-liquid separator according to claim 4 that can be used in distillation equipment, which is characterized in that the valve is electricity
Magnet valve；The solenoid valve is installed on the recombination sub-export (14)；
It further include power supply, the power supply and the solenoid valve are electrically connected, by switching the convertible solenoid valve and the electricity
The switching in source.
6. the gas-liquid separator according to claim 1 that can be used in distillation equipment, which is characterized in that the separator sheet
Body (1) is from top to down including hollow cylinder and the hollow cone being connected to the cylindrical body；It is to divide gas in the cylindrical body
Area, the interior cone is liquid separation area；The light fraction outlet (13) is opened in the circular cone close to the cylinder bottom
On the side wall of body；Recombination sub-export (14) is set to the tapered end of the cone.
7. the gas-liquid separator according to claim 1-6 that can be used in distillation equipment, which is characterized in that described
Exhaust outlet (12) is one or more.
8. the gas-liquid separator according to claim 1-6 that can be used in distillation equipment, which is characterized in that described
Light fraction outlet (13) and the recombination sub-export (14) are one or more.
9. the gas-liquid separator according to claim 1-6 that can be used in distillation equipment, which is characterized in that also wrap
On-line densimeter is included, the probe of the on-line densimeter is installed near the recombination sub-export (14).
10. the gas-liquid separator according to claim 1-6 that can be used in distillation equipment, which is characterized in that also
Including inclined plate (3)；Inclined plate (3) first end is fixed on the separator body (1)；Its second end favours described light group
Above sub-export (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811612870.9A CN109621470A (en) | 2018-12-27 | 2018-12-27 | The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811612870.9A CN109621470A (en) | 2018-12-27 | 2018-12-27 | The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment |
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| Publication Number | Publication Date |
|---|---|
| CN109621470A true CN109621470A (en) | 2019-04-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811612870.9A Pending CN109621470A (en) | 2018-12-27 | 2018-12-27 | The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113264564A (en) * | 2021-05-18 | 2021-08-17 | 国能朗新明环保科技有限公司南京分公司 | Wastewater zero discharge system based on high-efficiency concentration and spray drying integrated treatment |
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| RU2612741C1 (en) * | 2015-10-13 | 2017-03-13 | Публичное акционерное общество "Татнефть" имени В.Д. Шашина | Liquid-gas separator |
| CN105597378A (en) * | 2016-03-18 | 2016-05-25 | 西安交通大学 | Gas, liquid and light-weight oil triphase separating device |
| CN207193204U (en) * | 2017-09-25 | 2018-04-06 | 神华集团有限责任公司 | Coal carries out the device of liquefaction reaction and the system of DCL/Direct coal liquefaction production oil product |
| CN209662648U (en) * | 2018-12-27 | 2019-11-22 | 合肥艾普拉斯环保科技有限公司 | The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment |
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| CN113264564A (en) * | 2021-05-18 | 2021-08-17 | 国能朗新明环保科技有限公司南京分公司 | Wastewater zero discharge system based on high-efficiency concentration and spray drying integrated treatment |
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