CN109621470B - Gas-liquid separator for acrylamide methyl propane sulfonic acid distillation equipment - Google Patents
Gas-liquid separator for acrylamide methyl propane sulfonic acid distillation equipment Download PDFInfo
- Publication number
- CN109621470B CN109621470B CN201811612870.9A CN201811612870A CN109621470B CN 109621470 B CN109621470 B CN 109621470B CN 201811612870 A CN201811612870 A CN 201811612870A CN 109621470 B CN109621470 B CN 109621470B
- Authority
- CN
- China
- Prior art keywords
- liquid
- gas
- outlet
- separator
- component outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 154
- 238000004821 distillation Methods 0.000 title claims abstract description 29
- BOOMOFPAGCSKKE-UHFFFAOYSA-N butane-2-sulfonic acid;prop-2-enamide Chemical compound NC(=O)C=C.CCC(C)S(O)(=O)=O BOOMOFPAGCSKKE-UHFFFAOYSA-N 0.000 title description 3
- 238000000926 separation method Methods 0.000 claims abstract description 38
- 239000003638 chemical reducing agent Substances 0.000 claims description 5
- 230000000903 blocking effect Effects 0.000 claims description 3
- 238000003780 insertion Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims description 3
- 239000000523 sample Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 6
- 238000005192 partition Methods 0.000 abstract description 6
- 238000005086 pumping Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention relates to a gas-liquid separator which can be used in a distillation apparatus, comprising: the separator body is internally provided with a gas partition area and a liquid partition area from top to bottom; the top of the gas dividing zone is provided with a gas-liquid inlet; the side wall is provided with an exhaust port; the side wall of the separator body is sequentially provided with a light component outlet and a heavy component outlet of liquid from top to bottom. Compared with the prior art, the gas-liquid separator can be used in distillation equipment, and the separator comprises a light component outlet and a heavy component outlet of liquid, so that the liquid with different components is effectively separated; the separated liquids with different concentrations are treated by the subsequent process; therefore, at least part of heavy component liquid does not need to be repeatedly pumped and circulated back to the top, the pumping energy consumption is reduced, the gas-liquid separation efficiency is improved, and further, the continuous treatment of gas-liquid separation can be realized.
Description
Technical Field
The invention relates to the technical field of gas-liquid separation, in particular to a gas-liquid separator which can be used in distillation equipment.
Background
The gas-liquid separator utilizes the fact that the gas-liquid specific weights are different, and the mass of gas is smaller than that of liquid under the same volume. In a suddenly-expanding container, after the flow rate is reduced, fine liquid drops in the gas phase sink and are separated from the gas in the process of turning the main fluid, so that condensate recovery or gas phase purification is realized.
In the existing distillation technology, for example, on the equipment of a falling film evaporator, liquid enters a gas-liquid separation space after passing through a heat exchanger tube array; in this gas-liquid separation space, there is usually only one liquid outlet in addition to the gas outlet. On the same liquid outlet, if the liquid does not reach the concentration degree (for example, the liquid is pumped back to the heat exchanger by a pump for repeated heat exchange and evaporation until the liquid reaches a certain concentration degree, the concentrated liquid is pumped to a specified container) needs to be subjected to repeated heat exchange and evaporation. In this case, the non-volatile impurities in the liquid entering the gas-liquid separation space are repeatedly pumped back to the heat exchanger for a long time, wasting pumping capacity, and wasting heat exchange capacity; the separation cannot realize the process operation of continuously treating the concentrated solution, thereby reducing the gas-liquid separation efficiency.
Therefore, how to provide a device capable of continuously treating gas-liquid separation to improve separation efficiency is a problem to be solved by those skilled in the art.
Disclosure of Invention
In view of the above, the invention provides a gas-liquid separator which can be used in distillation equipment, and solves the technical problems that the separator in the prior art can not realize continuous treatment of concentrated solution and gas-liquid separation efficiency.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
the invention provides a gas-liquid separator for distillation equipment, comprising:
the separator body is internally provided with a gas partition area and a liquid partition area from top to bottom; the top of the gas dividing zone is provided with a gas-liquid inlet; the side wall is provided with an exhaust port; the side wall of the separator body is sequentially provided with a light component outlet and a heavy component outlet of liquid from top to bottom.
Compared with the prior art, the gas-liquid separator can be used in distillation equipment, and the separator comprises a light component outlet and a heavy component outlet of liquid, so that the liquid with different components is effectively separated; the separated liquids with different concentrations are treated by the subsequent process; therefore, at least part of heavy component liquid does not need to be repeatedly pumped and circulated back to the top, the pumping energy consumption is reduced, the gas-liquid separation efficiency is improved, and further, the continuous treatment of gas-liquid separation can be realized.
Preferably, the light component outlet is provided with an adjusting structure for adjusting the liquid level height; by adopting the scheme, the liquid level in the separator body can be adjusted, so that the quality of liquid separation is improved.
Preferably, the adjustment structure comprises: the device comprises a shell, a fixing piece, a supporting piece, a bolt and an overflow baffle;
The shell is detachable on the separator body, forms a liquid outlet space with the separator body, and is at least partially communicated with the light component outlet or used for blocking liquid; wherein the shell liquid inlet is larger than the light component outlet; and forms a shoulder with the periphery of the light component outlet; the shell is provided with a liquid outlet;
The fixing piece is welded on the side wall of the light component outlet channel and is provided with a splicing groove;
the support piece is inserted into the insertion groove; the support piece is provided with a plurality of threaded holes;
the bolts comprise a plurality of bolts which are correspondingly matched with the threaded holes, and the extending ends of the bolts are inserted into the liquid outlet channels of the light component outlets;
The overflow baffle has multiunit different sizes, and it pushes up the butt in fender shoulder department through the bolt, and can change different sizes with fender shoulder department.
The effect of adopting this scheme is: the overflow baffles with different sizes (height sizes) can be replaced according to the use requirement and are propped against the shoulder through bolts, so that the purpose of adjusting the liquid level height in the separator body is realized; when the overflow baffle is installed, firstly, the bolt is unscrewed, and the extending end of the bolt is far away from the shoulder, so that the overflow baffle can be replaced at the moment; after replacement, the bolts are screwed, and the replaced overflow baffle is propped against the baffle shoulder. According to the scheme, the height of the liquid surface of the separator body refers to the depth of the liquid surface, the separation condition of light and heavy components of the liquid can be directly influenced, and the liquid storage in the separator body is balanced as little as possible and the light and heavy components of the liquid are separated as well as possible by adjusting the height of the liquid surface, so that the liquid separation efficiency is further improved.
Preferably, the gas-liquid separator which can be used in the distillation equipment provided by the invention further comprises a valve or a reducing pipe; the valve or the reducing pipe is arranged on the heavy component outlet, and the concentration requirement of the separated liquid can be met by manually opening or closing the valve; or the pipeline length is increased through the reducer pipe, and the aim can be achieved. In the technical scheme of the invention, the plugging structure at the heavy component outlet is not limited to the mode, and the plugging structure is only provided with different component separation channels on the separator body, and the plugging structure falls into the protection scope of the invention.
Preferably, the valve may be an electromagnetic valve, the electromagnetic valve is electrically connected with a power supply, the formation of heavy components can be controlled according to the closing time of the electromagnetic valve, and then a battery valve is opened to discharge the heavy component liquid through a heavy component outlet; the on-off of the power supply can be realized through a switch; therefore, the operation intensity of personnel is reduced, the influence of human operation factors is reduced, and the separation quality and efficiency are further improved.
Preferably the separator body comprises from top to bottom a hollow cylinder and a hollow cone communicating with the cylinder; the cylinder is internally provided with a gas dividing area, and the cone is internally provided with a liquid dividing area; the light component outlet is arranged on the side wall of the cone close to the bottom of the cylinder; the heavy component outlet is arranged at the cone end of the cone. By adopting the scheme, the liquid separation area has large space, which is beneficial to separating gas under the action of gravity after gas and liquid enter, and the gas is discharged from the gas outlet; under the action of gravity, the liquid is positioned at the top or the bottom of the liquid separation zone according to the different components, and the liquid with different components is discharged through a light component outlet or a heavy component outlet; the conical liquid separation area is beneficial to converging heavy component liquid.
Preferably, the light component outlet is formed in the side wall of the cone close to the bottom of the cylinder, and the heavy component outlet is formed in the cone portion of the cone. Thereby facilitating separation of the light fraction liquid and the heavy fraction liquid. The light component outlet can be of a hole structure or a structure with a certain connecting joint.
Preferably, the exhaust port is one or more. Selected according to the specific use requirements.
The number of the light component outlets and the number of the heavy component outlets in the invention are selected according to specific use requirements, but all the same or similar schemes related to the arrangement of a plurality of liquid outlets on the separator body are within the protection scope of the invention.
Preferably, the gas-liquid separator which can be used in distillation equipment further comprises an online densimeter, wherein a probe of the online densimeter is arranged near a heavy component outlet; the on-line densimeter can adopt an MH5300 densimeter and the like, and the density value of the test liquid can be conveniently read.
Alternatively, the density signal can be converted into an electric signal, and the electric signal is obtained through a controller, and the controller is electrically connected with the electromagnetic valve and controls the electromagnetic valve to be opened or closed according to the required density requirement.
Preferably, the gas-liquid separator provided by the invention can be used in distillation equipment, and further comprises an inclined plate; the first end of the sloping plate is fixed on the separator body; the second end of the light component outlet is inclined above the light component outlet; the first ends of the two connecting pieces can be fixed on the separator body or fixed through the connecting pieces; the purpose of the scheme is that: wherein the inclined plate can block the liquid entering through the gas-liquid inlet and prevent the liquid falling near the overflow port (namely the light component outlet) from directly flowing out without separating the light component from the heavy component; further improving the liquid separation efficiency.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings that are required to be used in the embodiments or the description of the prior art will be briefly described below, and it is obvious that the drawings in the following description are only embodiments of the present invention, and that other drawings can be obtained according to the provided drawings without inventive effort for a person skilled in the art.
FIG. 1 is a perspective view of a vapor-liquid separator that may be used in a distillation apparatus in accordance with the present invention;
FIG. 2 is a schematic drawing showing a semi-cutaway perspective view of a vapor-liquid separator that may be used in a distillation apparatus in accordance with the present invention;
fig. 3 is a schematic view of a gas-liquid separator adjusting structure (a gas dividing zone and a shell are not shown) which can be used in distillation equipment.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
The embodiment of the invention discloses a gas-liquid separator which can be used in distillation equipment, and solves the technical problems that the separator in the prior art cannot realize continuous treatment of concentrated solution and gas-liquid separation efficiency.
Referring to fig. 1, the gas-liquid separator which can be used in distillation equipment provided by the invention comprises:
the separator comprises a separator body 1, wherein the separator body 1 is internally provided with a gas partition area and a liquid partition area from top to bottom; the top of the gas division area is provided with a gas-liquid inlet 11; the side wall is provided with an exhaust port 12; the side wall of the separator body is provided with a light component outlet 13 and a heavy component outlet 14 which are sequentially arranged from top to bottom.
The invention discloses a gas-liquid separator which can be used in distillation equipment, and as the separator body 1 comprises a light component outlet 13 and a heavy component outlet 14 of liquid, the liquid with different components is effectively separated; the separated liquids with different concentrations are treated by the subsequent process; therefore, at least part of heavy component liquid does not need to be repeatedly pumped and circulated back to the top, the pumping energy consumption is reduced, the gas-liquid separation efficiency is improved, and further, the continuous treatment of gas-liquid separation can be realized.
In one embodiment of the invention, an adjusting structure for adjusting the liquid level height is arranged at the light component outlet 13; whereby the liquid level in the separator body 1 can be adjusted and thus the quality of the liquid separation is improved.
Specifically, referring to fig. 3, the adjustment structure includes: the device comprises a shell 4, a fixing piece 5, a supporting piece 6, bolts and an overflow baffle 7;
The shell 4 is detachable on the separator body 1 and forms a liquid outlet space with the separator body 1, at least partially communicated with the light component outlet 13 or used for blocking liquid; wherein the liquid inlet of the housing 4 is larger than the light fraction outlet 13; and forms a shoulder with the periphery of the light component outlet 13; the shell 4 is provided with a liquid outlet;
The fixing piece 5 is welded on the side wall of the light component outlet 13 channel and is provided with a splicing groove;
The supporting piece 6 is inserted into the insertion groove; and the support 6 is provided with a plurality of threaded holes;
the bolts comprise a plurality of bolts which are correspondingly matched with the threaded holes, and the extending ends of the bolts are inserted into the liquid outlet channel of the light component outlet 13;
the overflow baffle 7 has a plurality of groups of different sizes, is propped against the shoulder through bolts, and can be replaced with the shoulder in different sizes.
According to the scheme, the overflow baffles with different sizes (height sizes) can be replaced according to the use requirement and are propped against the baffle shoulder through the bolts, so that the purpose of adjusting the liquid level height in the separator body is realized; when the overflow baffle is installed, firstly, the bolt is unscrewed, and the extending end of the bolt is far away from the shoulder, so that the overflow baffle can be replaced at the moment; after replacement, the bolts are screwed, and the replaced overflow baffle is propped against the baffle shoulder. According to the scheme, the height of the liquid surface of the separator body refers to the depth of the liquid surface, the separation condition of light and heavy components of the liquid can be directly influenced, and the liquid storage in the separator body is balanced as little as possible and the light and heavy components of the liquid are separated as well as possible by adjusting the height of the liquid surface, so that the liquid separation efficiency is further improved.
Wherein the size and the specific shape of the shell 4 are selected according to the capacity and the shape of the separator body 1; the number of the fixing members 5 may be one or more, and the shape thereof may be selected according to the structure of the separator body 1; the support 6 may be strip-like, sheet-like or columnar; the overflow baffle 7 may comprise components of various structural dimensions, which can be selected for use according to different requirements.
In the above-described embodiments, the embodiments are not particularly limited as long as the above-described arrangement of the liquid level adjustment structure on the light component outlet 13 is included, and all fall within the scope of the present invention.
More advantageously, the gas-liquid separator provided by the invention, which can be used in distillation equipment, further comprises a valve or a reducer; the valve or the reducing pipe is arranged on the heavy component outlet, and the concentration requirement of the separated liquid can be met by manually opening or closing the valve; or the pipeline length is increased through the reducer pipe, and the aim can be achieved. In the technical scheme of the invention, the plugging structure at the heavy component outlet is not limited to the mode, and the plugging structure is only provided with different component separation channels on the separator body, and the plugging structure falls into the protection scope of the invention.
The valve can be an electromagnetic valve, the electromagnetic valve is electrically connected with a power supply, the formation of heavy components can be controlled according to the closing time of the electromagnetic valve, and then a battery valve is opened to discharge heavy component liquid through a heavy component outlet 14; the on-off of the power supply can be realized through a switch; therefore, the operation intensity of personnel is reduced, the influence of human operation factors is reduced, and the separation quality and efficiency are further improved.
Advantageously, in one embodiment of the invention, the separator body 1 comprises from top to bottom a hollow cylinder and a hollow cone communicating with the cylinder; the cylinder is internally provided with a gas dividing area, and the cone is internally provided with a liquid dividing area; the light component outlet 13 is arranged on the side wall of the cone close to the bottom of the cylinder; the heavy component outlet 14 is provided at the cone end of the cone. Therefore, the liquid separation area is large in space, so that gas can be separated under the action of gravity after gas and liquid enter, and the gas is discharged from the gas outlet 12; under the action of gravity, the liquid is positioned at the top or the bottom of the liquid dividing zone according to the different components, and the liquid with different components is discharged through a light component outlet 13 or a heavy component outlet 14; the conical liquid separation area is beneficial to converging heavy component liquid.
More advantageously, the light fraction outlet 13 opens on the side wall of the cone near the bottom of the cylinder, the heavy fraction outlet 14 being located in the cone of the cone. Thereby facilitating separation of the light fraction liquid and the heavy fraction liquid. The light component outlet 13 may be a hole structure or a structure with a certain connecting joint.
In another embodiment of the present invention, the exhaust ports 12 are one or more. Selected according to the specific use requirements.
The number of the light component outlets 13 and the heavy component outlets 14 in the present invention is selected according to the specific use requirements, but the same or similar schemes involving a plurality of liquid outlets provided on the separator body should fall within the scope of the present invention.
In other embodiments of the present invention, the gas-liquid separator provided by the present invention for use in distillation apparatus further comprises an in-line densitometer having a probe mounted near heavy ends outlet 14; the on-line densimeter can adopt an MH5300 densimeter and the like, and the density value of the test liquid can be conveniently read.
Alternatively, the density signal can be converted into an electric signal, and the electric signal is obtained through a controller, and the controller is electrically connected with the electromagnetic valve and controls the electromagnetic valve to be opened or closed according to the required density requirement.
Referring to fig. 2, the gas-liquid separator provided by the invention can be used in distillation equipment, and further comprises an inclined plate 3; the first end of the sloping plate 3 is fixed on the separator body 1; the second end of which is inclined above the light component outlet 13; the first ends of the two can be fixed on the separator body 1 or fixed through a connecting piece; the purpose of the scheme is that: wherein the sloping plate 3 can block liquid entering through the gas-liquid inlet and prevent the liquid falling near the overflow port (namely the light component outlet 13) from directly flowing out without separating light components from heavy components; further improving the liquid separation efficiency.
The gas-liquid separator of the invention is not limited to be applied to acrylamide methyl propane sulfonic acid distillation equipment, and can be applied to any distillation equipment needing gas-liquid separation.
In the present specification, each embodiment is described in a progressive manner, and each embodiment is mainly described in a different point from other embodiments, and identical and similar parts between the embodiments are all enough to refer to each other. For the device disclosed in the embodiment, since it corresponds to the method disclosed in the embodiment, the description is relatively simple, and the relevant points refer to the description of the method section.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (6)
1. A gas-liquid separator usable in distillation apparatus, comprising:
the separator comprises a separator body (1), wherein the separator body (1) is internally provided with a gas separation zone and a liquid separation zone from top to bottom; the top of the gas-separating zone is provided with a gas-liquid inlet (11), and the side wall of the gas-separating zone is provided with an exhaust port (12); the side wall of the separator body (1) is sequentially provided with a light component outlet (13) and a heavy component outlet (14) of liquid from top to bottom; the separator body (1) comprises a hollow cylinder and a hollow cone communicated with the cylinder from top to bottom; the cylinder is internally provided with a gas dividing area, and the cone is internally provided with a liquid dividing area; the light component outlet (13) is formed in the side wall of the cone close to the bottom of the cylinder; the heavy component outlet (14) is arranged at the cone end of the cone;
A sloping plate (3); the first end of the sloping plate (3) is fixed on the separator body (1); the second end of which is inclined above the light component outlet (13);
An adjusting structure for adjusting the liquid level height is arranged at the light component outlet (13); the adjusting structure comprises: the device comprises a shell (4), a fixing piece (5), a supporting piece (6), bolts and an overflow baffle (7); the shell (4) is detachable on the separator body (1) and forms a liquid outlet space with the separator body (1), and the liquid outlet space is at least partially communicated with the light component outlet (13) or is used for blocking liquid; wherein the housing (4) liquid inlet is larger than the light fraction outlet (13); and forms a shoulder with the periphery of the light component outlet (13); the shell (4) is provided with a liquid outlet; the fixing piece (5) is welded on the side wall of the light component outlet (13) channel, and is provided with a splicing groove; the supporting piece (6) is inserted into the insertion groove; and the support (6) is provided with a plurality of threaded holes; the bolts comprise a plurality of bolts which are correspondingly matched with the threaded holes, and the extending ends of the bolts are inserted into the liquid outlet channel of the light component outlet (13); the overflow baffle (7) is provided with a plurality of groups of different sizes, is propped against the shoulder through the bolts, and can be replaced by the shoulder.
2. The gas-liquid separator for use in a distillation apparatus according to claim 1, further comprising a valve or a reducer; the valve or reducer is mounted on the heavy fraction outlet (14).
3. The gas-liquid separator usable in distillation apparatus as set forth in claim 2, wherein said valve is a solenoid valve; the electromagnetic valve is arranged on the heavy component outlet (14); the electromagnetic valve is characterized by further comprising a power supply, wherein the power supply is electrically connected with the electromagnetic valve, and the electromagnetic valve can be switched on and off through a switch.
4. A gas-liquid separator usable in a distillation apparatus according to any one of claims 1-3, wherein the vent (12) is one or more.
5. A gas-liquid separator usable in a distillation apparatus according to any one of claims 1-3, wherein the light fraction outlet (13) and the heavy fraction outlet (14) are each one or more.
6. A gas-liquid separator usable in a distillation apparatus according to any one of claims 1-3, further comprising an in-line densitometer, the probe of which is mounted near the heavy fraction outlet (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811612870.9A CN109621470B (en) | 2018-12-27 | 2018-12-27 | Gas-liquid separator for acrylamide methyl propane sulfonic acid distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811612870.9A CN109621470B (en) | 2018-12-27 | 2018-12-27 | Gas-liquid separator for acrylamide methyl propane sulfonic acid distillation equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109621470A CN109621470A (en) | 2019-04-16 |
| CN109621470B true CN109621470B (en) | 2024-05-28 |
Family
ID=66078370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811612870.9A Active CN109621470B (en) | 2018-12-27 | 2018-12-27 | Gas-liquid separator for acrylamide methyl propane sulfonic acid distillation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109621470B (en) |
Families Citing this family (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 |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB320986A (en) * | 1928-08-17 | 1929-10-31 | Frank Pink | Apparatus for separating liquids of different densities |
| CN202376859U (en) * | 2011-12-23 | 2012-08-15 | 青岛京润石化设计研究院有限公司 | Gas-liquid separator |
| CN204073512U (en) * | 2014-08-18 | 2015-01-07 | 上海高桥捷派克石化工程建设有限公司 | A kind of experimental rig solution-air-liquid three phase separator |
| CN104888560A (en) * | 2015-04-23 | 2015-09-09 | 刘洋 | Efficient separator using swirling flow effect to carry out gas-liquid separation |
| CN105597378A (en) * | 2016-03-18 | 2016-05-25 | 西安交通大学 | Gas, liquid and light-weight oil triphase separating device |
| RU2612741C1 (en) * | 2015-10-13 | 2017-03-13 | Публичное акционерное общество "Татнефть" имени В.Д. Шашина | Liquid-gas separator |
| 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 |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7931719B2 (en) * | 2007-12-03 | 2011-04-26 | National Tank Company | Revolution vortex tube gas/liquids separator |
-
2018
- 2018-12-27 CN CN201811612870.9A patent/CN109621470B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB320986A (en) * | 1928-08-17 | 1929-10-31 | Frank Pink | Apparatus for separating liquids of different densities |
| CN202376859U (en) * | 2011-12-23 | 2012-08-15 | 青岛京润石化设计研究院有限公司 | Gas-liquid separator |
| CN204073512U (en) * | 2014-08-18 | 2015-01-07 | 上海高桥捷派克石化工程建设有限公司 | A kind of experimental rig solution-air-liquid three phase separator |
| CN104888560A (en) * | 2015-04-23 | 2015-09-09 | 刘洋 | Efficient separator using swirling flow effect to carry out gas-liquid separation |
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109621470A (en) | 2019-04-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR102336726B1 (en) | Apparatus for removing scale from cooling water using water-jet | |
| JP2016117051A (en) | Scale removal device, water heater and scale removal method | |
| KR101596181B1 (en) | A plate evaporator of the falling film type, and a plate evaporator apparatus having such a plate evaporator arranged in a housing | |
| CN109621470B (en) | Gas-liquid separator for acrylamide methyl propane sulfonic acid distillation equipment | |
| EP1809965A4 (en) | Wastewater heat recovery device and method | |
| RU2765477C2 (en) | Separation device | |
| CN203663472U (en) | Efficient falling film evaporator | |
| CN208166956U (en) | A kind of waste oil dewatering system of combining ultrasonic wave and cyclone | |
| US20170274305A1 (en) | Wastewater treatment apparatus and system for oil and gas production wells | |
| JP5632866B2 (en) | Seawater desalination system and energy recovery device | |
| CN209662648U (en) | The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment | |
| KR100487872B1 (en) | Structure of cold and hot water purifier | |
| CN207680101U (en) | Oil water separator | |
| CN208786092U (en) | A kind of hydrogen peroxide oxidation exhaust treatment system | |
| CN203745423U (en) | Ultrasonic detection device | |
| RU2354433C1 (en) | Separator | |
| RU198457U1 (en) | FILM HEAT AND MASS EXCHANGE UNIT | |
| WO2006042421A1 (en) | Apparatus and method for processing fluids from oil wells | |
| KR101998796B1 (en) | Apparatus for removing scale | |
| RU2547750C1 (en) | Method of technical oil purification | |
| RU2236889C1 (en) | Entrainment separator | |
| RU2206734C1 (en) | Method of degassing and dehydration of oil and separator for method embodiment | |
| KR200376056Y1 (en) | Forced circulation evaporator | |
| CN110697952B (en) | Electrochemical water treatment system | |
| CN207943980U (en) | Filtering oily sewage oil removing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |