CN107952259A - A kind of high-efficiency blade formula feed distribution mechanism - Google Patents
A kind of high-efficiency blade formula feed distribution mechanism Download PDFInfo
- Publication number
- CN107952259A CN107952259A CN201711500359.5A CN201711500359A CN107952259A CN 107952259 A CN107952259 A CN 107952259A CN 201711500359 A CN201711500359 A CN 201711500359A CN 107952259 A CN107952259 A CN 107952259A
- Authority
- CN
- China
- Prior art keywords
- discharge port
- guide vane
- grid case
- distribution mechanism
- tank body
- 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.)
- Pending
Links
- 238000009826 distribution Methods 0.000 title claims abstract description 52
- 239000000463 material Substances 0.000 claims abstract description 16
- 239000006260 foam Substances 0.000 claims abstract description 10
- 238000003491 array Methods 0.000 claims abstract description 6
- 238000007599 discharging Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 32
- 239000012530 fluid Substances 0.000 abstract description 11
- 238000000926 separation method Methods 0.000 abstract description 5
- 238000010008 shearing Methods 0.000 abstract description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 230000006378 damage Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000006467 substitution reaction 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
- B01D3/06—Flash distillation
-
- 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
- B01D3/008—Liquid distribution
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses a kind of high-efficiency blade formula feed distribution mechanism, in one feed inlet of middle part vertical connection of tank body, one distribution grid case is installed in feed inlet, the middle symmetric arrays of sub-material grating box have what some involute in form were distributed to divide guide vane, the outlet of two pairs of points of guide vanes is respectively directed to the first discharge port and the second discharge port, distribution grid case and the first discharge port, wire mesh demister is equipped between second discharge port, fluid is after feed inlet entrance, shunted successively in distribution grid case by some points of guide vanes, and pass through wire mesh demister further stream and foam removal, finally exported from the first discharge port and the second discharge port, it can avoid droplets from or liquid hammer is to follow up device frontal impact, so as to reduce the generation of shearing force；Make drop more dispersed and reduce charging momentum, at utmost realize gas-liquid separation to the greatest extent, there is good practical value.
Description
Technical field
The present invention relates to a kind of feed distribution mechanism, more particularly to a kind of high-efficiency blade formula feed distribution mechanism.
Background technology
Acetic acid is very important industrial chemicals.At present, the gas-liquid separation effect of flash tank is frequent in production of acetic acid device
Greatly deviate desired value, entrained liquids mist diameter reaches grade in gas vent, and liquid hammer impact force is big, scattered uneven, leads
Cause product quality not ideal enough.It is following several that preferable gas-liquid feed distribution mechanism mainly gently redistributes realization by fluid
Function：Big degree to the greatest extent realizes gas-liquid separation；(or liquid hammer) is avoided droplets to container inner wall or feed arrangement body frontal impact,
So as to reduce the generation of shearing force, droplet distribution is prevented into more tiny mist；Reduce charging pressure drop；It is dynamic effectively to reduce charging
Amount, is uniformly distributed so as to promote gas to be formed in container section；In the presence of having liquid hammer, liquid hammer is effectively cut, is kept away
Exempt from because the interference of liquid hammer causes the big ups and downs of liquid level and destruction to foam removal element.But in actual operation, blade radian
Unreasonable with length, biserial leaf angle is unreasonable, so as to cannot meet above-mentioned performance requirement, due to the inequality of charging itself
Even property, liquid hammer have certain deviation to the impact direction of end with center line, so in the case of multiple hammering, feed arrangement
End or side can occur badly damaged, if removing feed distribution mechanism, gas-liquid mixture fluid can directly impact the charging mouth of pipe
Radially corresponding container inner wall, causes the flash tank interface overdraught rate of climb extremely uneven, under long-term working condition, epimere
Blade demister can be locally destroyed, and aggravation is destroyed with the extension of time.Therefore acetic acid and other fluid productions are engaged in
Staff wishes a kind of efficient distribution apparatus, reduces impact during product is fed, improves the production matter of product
Amount.
The content of the invention
The present invention proposes a kind of high-efficiency blade formula feed distribution mechanism, effectively handles slug flow, and ensures charging distribution
Device work steady in a long-term, uniformly guides and spreads to fluid.
In order to solve the above technical problem, the present invention provides following technical solution：
A kind of high-efficiency blade formula feed distribution mechanism of the present invention, including tank body, the first discharge port, the second discharge port, charging
Mouthful, distribution grid case and divide guide vane, the both ends of the tank body are respectively equipped with first discharge port and second discharge port,
One feed inlet of middle part vertical connection of the tank body, is provided with the distribution grid case in the feed inlet, described point
Cloth grating box is a trapezoidal babinet, in the inner cavity of the distribution grid case symmetric arrays have it is some it is described divide guide vane, if
Divide guide vane to be to be involute formula to be distributed in the sub-material grid case described in dry, the outlet of guide vane is divided described in two pairs
It is respectively directed to first discharge port and second discharge port, the sub-material grid case and first discharge port, described the
Wire mesh demister is equipped between two discharge ports.
As a preferred technical solution of the present invention, the side of the tank body is equipped with circular observation window.
As a preferred technical solution of the present invention, the feed inlet is circular channel.
As a preferred technical solution of the present invention, the avris for dividing guide vane input end is equipped with Despumation device.
As a preferred technical solution of the present invention, some spacing divided between guide vane and radian pass through accurate
CFD is simulated and calculating and setting.
As a preferred technical solution of the present invention, the tank body, the distribution grid case and it is described divide guide vane by
Kazakhstan B2 materials or 316L materials are made.
As a preferred technical solution of the present invention, the specification of the wire mesh demister is according to material balance and requirement
Calculate gained.
The present invention is rational in infrastructure, sets a tank body, pacifies in one feed inlet of middle part vertical connection of tank body, feed inlet
A trapezoidal babinet is filled as distribution grid case, symmetric arrays there are some forms of bursting at the seams to be divided in the inner cavity of distribution grid case
Cloth divides guide vane, and the outlet of two pairs of points of guide vanes is respectively directed to the first discharge port and the second discharge port, distribution grid case and
Wire mesh demister is set between one discharge port, the second discharge port, fluid is after feed inlet entrance, if the quilt in wire mesh demister successively
It is dry to divide guide vane shunting cutting, and by wire mesh demister further stream and foam removal, finally from the first discharge port and second
Exported in discharge port.
The beneficial effect that is reached of the present invention is：It can avoid droplets from or liquid hammer is to inner tank wall or follow up device body
Frontal impact, so as to reduce the generation of shearing force；Make droplet distribution into more uniformly and reduce charging momentum, so as to promote gas
Formed and be uniformly distributed in container section；Avoid charging pressure drop from reducing, in the presence of having liquid hammer, effectively cut liquid hammer,
Avoid because the interference of liquid hammer causes the big ups and downs of liquid level and destruction to foam removal element；Avoid the generation and emulsification of fine droplets
The general knowledge of liquid, lifting gas-liquid charging distributing homogeneity；Reentrainment is avoided droplets from, slug amount of flow is reduced, reduces demister
Liquid load, to the greatest extent big degree realize gas-liquid separation.
Brief description of the drawings
Attached drawing is used for providing a further understanding of the present invention, and a part for constitution instruction, the reality with the present invention
Apply example to be used to explain the present invention together, be not construed as limiting the invention.In the accompanying drawings：
Fig. 1 is the subjective structure diagram of the present invention；
The master that Fig. 2 is the present invention cuts open topology view；
Fig. 3 is the distribution grid box structure schematic diagram of the present invention；
In figure：1st, tank body；2nd, the first discharge port；3rd, the second discharge port；4th, feed inlet；5th, distribution grid case；6th, guide vane is divided
Piece；7th, wire mesh demister；8th, circular observation window.
Embodiment
The preferred embodiment of the present invention is illustrated below in conjunction with attached drawing, it will be appreciated that described herein preferred real
Apply example to be merely to illustrate and explain the present invention, be not intended to limit the present invention.
Embodiment 1
As shown in Figs. 1-3, the present invention provides a kind of high-efficiency blade formula feed distribution mechanism, including tank body 1, the first discharge port
2nd, the second discharge port 3, feed inlet 4, distribution grid case 5 and guide vane 6 is divided, the both ends of tank body 1 are respectively equipped with 2 He of the first discharge port
Second discharge port 3, one feed inlet 4 of middle part vertical connection of tank body 1, distribution grid case 5 is provided with feed inlet 4, is distributed lattice
Grid case 5 is a trapezoidal babinet, and symmetric arrays have some points of guide vanes 6, some points of guide vanes in the inner cavity of distribution grid case 5
6 in distribution grid case 5 be to be involute formula to be distributed, and the outlet of two pairs of points of guide vanes 6 is respectively directed to the first discharge port 2
With the second discharge port 3, wire mesh demister 7 is equipped between 5 and first discharge port 2 of distribution grid case, the second discharge port 3, works as fluid
After the entrance of feed inlet 4, shunted successively in distribution grid case 5 by some points of guide vanes 6, and pass through wire mesh demister 7 into one
The stream of step and foam removal, finally export from the first discharge port 2 and the second discharge port 3.
Further, the side of tank body 1 is equipped with circular observation window 8, easy to observe the mobility status of fluid.
Further, feed inlet 4 is circular channel, and size is set with specific reference to demand, to strengthen the suitable of the present invention
Ying Xing.
Further, the avris of 6 input end of guide vane is divided to be equipped with Despumation device, Despumation device uses three-level foam removal structure, the
Level-one pre-processes for vane type, and the second level is high-efficiency blade formula demister, and the third level is wire mesh demister.
Further, the spacing between some points of guide vanes 6 and radian is simulated by accurate CFD and calculating and setting, so as to right
A variety of fluids point lead.
Further, tank body 1, distribution grid case 5 and guide vane 6 is divided by being made of Kazakhstan B2 materials or 316L materials, Kazakhstan
Material or 316L material structures are firm, wearability is good, and possess good elasticity, decrease liquid hammer can be carried out in fluid impact
Impact to feed arrangement.
Further, the specification of wire mesh demister is according to material balance and requires to calculate gained, can be carried out according to demand
Installation, targetedly to flow the material with the various flow-likes of foam removal.
The present invention is rational in infrastructure, a tank body 1 is set, in one feed inlet 4 of middle part vertical connection of tank body 1, feed inlet 4
One trapezoidal babinet of middle installation is as distribution grid case 5, and symmetric arrays have some forms that burst at the seams in the inner cavity of distribution grid case 5
What is be distributed divides guide vane 6, and the outlet of two pairs of points of guide vanes 6 is respectively directed to the first discharge port 2 and the second discharge port 3, distribution
Wire mesh demister 7 is equipped between 5 and first discharge port 2 of grating box, the second discharge port 3, after fluid enters from feed inlet 4, according to
It is secondary to be shunted in distribution grid case 5 by some points of guide vanes 6, and by wire mesh demister 7 further stream and foam removal, finally
Exported from the first discharge port 2 and the second discharge port 3, (or liquid hammer) can be avoided droplets to 1 inner wall of tank body or feed arrangement
Body and follow-up equipment frontal impact, so as to reduce the generation of shearing force；Make droplet distribution into more uniformly and to reduce charging dynamic
Amount, is uniformly distributed so as to promote gas to be formed in container section；Avoid charging pressure drop from reducing, there is situation existing for liquid hammer
Under, liquid hammer is effectively cut, is avoided because the interference of liquid hammer causes the big ups and downs of liquid level and destruction to foam removal element；Avoid trickle
The generation of drop and the general knowledge of emulsion, lifting gas-liquid charging distributing homogeneity；Reentrainment is avoided droplets from, reduces slug flowing
Amount, reduces the liquid load of demister, big degree to the greatest extent realizes gas-liquid separation, therefore has good practical value.
Finally it should be noted that：It these are only the preferred embodiment of the present invention, be not intended to limit the invention, although
The present invention is described in detail with reference to the foregoing embodiments, for those skilled in the art, it still can be right
Technical solution described in foregoing embodiments is modified, or carries out equivalent substitution to which part technical characteristic.It is all
Within the spirit and principles in the present invention, any modification, equivalent replacement, improvement and so on, should be included in the protection of the present invention
Within the scope of.
Claims (7)
1. a kind of high-efficiency blade formula feed distribution mechanism, including tank body (1), the first discharge port (2), the second discharge port (3), charging
Mouthful (4), distribution grid case (5) and divide guide vane (6), it is characterised in that the both ends of the tank body (1) are respectively equipped with described first
Discharge port (2) and second discharge port (3), the feed inlet (4) of middle part vertical connection one of the tank body (1) are described
The distribution grid case (5) is installed, the distribution grid case (5) is a trapezoidal babinet, the distribution in feed inlet (4)
In the inner cavity of grating box (5) symmetric arrays have it is some it is described divide guide vane (6), it is some described to divide guide vane (6) in the distribution
It is to be involute formula to be distributed in grating box (5), divides the outlet of guide vane (6) to be respectively directed to described first described in two pairs and go out
Material mouth (2) and second discharge port (3), the distribution grid case (5) and first discharge port (2), second discharging
Wire mesh demister (7) is equipped between mouth (3).
2. a kind of high-efficiency blade formula feed distribution mechanism according to claim 1, it is characterised in that the tank body (1)
Side is equipped with circular observation window (8).
A kind of 3. high-efficiency blade formula feed distribution mechanism according to claim 1, it is characterised in that the feed inlet (4)
It is circular channel.
4. a kind of high-efficiency blade formula feed distribution mechanism according to claim 1, it is characterised in that described to divide guide vane
(6) avris of input end is equipped with Despumation device.
5. a kind of high-efficiency blade formula feed distribution mechanism according to claim 1, it is characterised in that divide guide vane described in some
Spacing between piece (6) and radian is simulated by accurate CFD and calculating and setting.
6. a kind of high-efficiency blade formula feed distribution mechanism according to claim 1, it is characterised in that the tank body (1), institute
State distribution grid case (5) and described divide guide vane (6) to be made of Kazakhstan B2 materials or 316L materials.
7. a kind of high-efficiency blade formula feed distribution mechanism according to claim 1, it is characterised in that (7) silk screen removes
The specification of foam device is according to material balance and requires to calculate gained.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711500359.5A CN107952259A (en) | 2017-12-29 | 2017-12-29 | A kind of high-efficiency blade formula feed distribution mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711500359.5A CN107952259A (en) | 2017-12-29 | 2017-12-29 | A kind of high-efficiency blade formula feed distribution mechanism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107952259A true CN107952259A (en) | 2018-04-24 |
Family
ID=61956104
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711500359.5A Pending CN107952259A (en) | 2017-12-29 | 2017-12-29 | A kind of high-efficiency blade formula feed distribution mechanism |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107952259A (en) |
Citations (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1517510A (en) * | 1975-09-26 | 1978-07-12 | Atomic Energy Authority Uk | Multistage distillation plant |
| CN1158270A (en) * | 1995-10-20 | 1997-09-03 | 法国石油研究所 | Dispensers for individually filling and/or discharging fluids |
| US6007055A (en) * | 1997-12-29 | 1999-12-28 | Schifftner; Kenneth C. | Gas and liquid contact apparatus |
| CA2476961A1 (en) * | 2002-02-21 | 2003-08-28 | Shell Internationale Research Maatschappij B.V. | Apparatus and method for treating a fluid |
| CA2610878A1 (en) * | 2002-10-03 | 2004-04-15 | York International Corporation | Compressor systems for use with smokeless lubricant |
| US20040104493A1 (en) * | 1997-11-19 | 2004-06-03 | Buchanan John Scott | Vapor/liquid contacting cyclone with secondary vanes |
| US20050116364A1 (en) * | 2003-10-24 | 2005-06-02 | Gardner Nelson C. | Spinning impingement multiphase contacting device |
| WO2006106582A1 (en) * | 2005-03-31 | 2006-10-12 | Hitachi Zosen Corporation | Multi-stage flash evaporator |
| US20070175746A1 (en) * | 2006-02-01 | 2007-08-02 | Exxonmobil Research And Engineering Company | Distillation tower baffle |
| US20080257147A1 (en) * | 2005-12-06 | 2008-10-23 | Johnson Matthey Plc | Gas Distributor |
| US20100162891A1 (en) * | 2008-12-31 | 2010-07-01 | Zhanping Xu | Vapor-liquid contacting in co-current contacting apparatuses |
| CN102049149A (en) * | 2009-10-27 | 2011-05-11 | 中国石油化工股份有限公司 | Tower feeding distributor |
| CN102309864A (en) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | Distillation tower feeding distributor |
| WO2014015906A1 (en) * | 2012-07-26 | 2014-01-30 | Fmc Separation Systems, Bv | Inlet device for separator |
| CN203525664U (en) * | 2013-11-13 | 2014-04-09 | 上海协升化工科技有限公司北京协升圣华分公司 | Multiple-blade feeding distributor |
| CN203763912U (en) * | 2014-03-31 | 2014-08-13 | 华东理工大学 | Three-phase separation device |
| US9643105B1 (en) * | 2016-12-01 | 2017-05-09 | Worthington Industries, Inc. | Inlet diverter |
| CN106621431A (en) * | 2016-12-30 | 2017-05-10 | 深圳市危险废物处理站有限公司 | Organic waste liquid evaporation separator and method for treating organic waste liquid |
| CN206214914U (en) * | 2016-11-28 | 2017-06-06 | 西安长庆科技工程有限责任公司 | A kind of spiral-flow type gas-liquid separation device |
| WO2017190852A1 (en) * | 2016-05-02 | 2017-11-09 | Fmc Separation Systems, Bv | Fluid inlet device for use in gas liquid separators |
| CN208065816U (en) * | 2017-12-29 | 2018-11-09 | 上海协升化工科技有限公司 | A kind of high-efficiency blade formula feed distribution mechanism |
-
2017
- 2017-12-29 CN CN201711500359.5A patent/CN107952259A/en active Pending
Patent Citations (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1517510A (en) * | 1975-09-26 | 1978-07-12 | Atomic Energy Authority Uk | Multistage distillation plant |
| CN1158270A (en) * | 1995-10-20 | 1997-09-03 | 法国石油研究所 | Dispensers for individually filling and/or discharging fluids |
| US20040104493A1 (en) * | 1997-11-19 | 2004-06-03 | Buchanan John Scott | Vapor/liquid contacting cyclone with secondary vanes |
| US6007055A (en) * | 1997-12-29 | 1999-12-28 | Schifftner; Kenneth C. | Gas and liquid contact apparatus |
| CA2476961A1 (en) * | 2002-02-21 | 2003-08-28 | Shell Internationale Research Maatschappij B.V. | Apparatus and method for treating a fluid |
| CA2610878A1 (en) * | 2002-10-03 | 2004-04-15 | York International Corporation | Compressor systems for use with smokeless lubricant |
| US20050116364A1 (en) * | 2003-10-24 | 2005-06-02 | Gardner Nelson C. | Spinning impingement multiphase contacting device |
| WO2006106582A1 (en) * | 2005-03-31 | 2006-10-12 | Hitachi Zosen Corporation | Multi-stage flash evaporator |
| US20080257147A1 (en) * | 2005-12-06 | 2008-10-23 | Johnson Matthey Plc | Gas Distributor |
| US20070175746A1 (en) * | 2006-02-01 | 2007-08-02 | Exxonmobil Research And Engineering Company | Distillation tower baffle |
| US20100162891A1 (en) * | 2008-12-31 | 2010-07-01 | Zhanping Xu | Vapor-liquid contacting in co-current contacting apparatuses |
| CN102049149A (en) * | 2009-10-27 | 2011-05-11 | 中国石油化工股份有限公司 | Tower feeding distributor |
| CN102309864A (en) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | Distillation tower feeding distributor |
| WO2014015906A1 (en) * | 2012-07-26 | 2014-01-30 | Fmc Separation Systems, Bv | Inlet device for separator |
| CN203525664U (en) * | 2013-11-13 | 2014-04-09 | 上海协升化工科技有限公司北京协升圣华分公司 | Multiple-blade feeding distributor |
| CN203763912U (en) * | 2014-03-31 | 2014-08-13 | 华东理工大学 | Three-phase separation device |
| WO2017190852A1 (en) * | 2016-05-02 | 2017-11-09 | Fmc Separation Systems, Bv | Fluid inlet device for use in gas liquid separators |
| CN206214914U (en) * | 2016-11-28 | 2017-06-06 | 西安长庆科技工程有限责任公司 | A kind of spiral-flow type gas-liquid separation device |
| US9643105B1 (en) * | 2016-12-01 | 2017-05-09 | Worthington Industries, Inc. | Inlet diverter |
| CN106621431A (en) * | 2016-12-30 | 2017-05-10 | 深圳市危险废物处理站有限公司 | Organic waste liquid evaporation separator and method for treating organic waste liquid |
| CN208065816U (en) * | 2017-12-29 | 2018-11-09 | 上海协升化工科技有限公司 | A kind of high-efficiency blade formula feed distribution mechanism |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204051086U (en) | A kind of oil and gas separation device | |
| CN104474741B (en) | A kind of orientation poly-Liquid liquid Separation device | |
| EP2850253A1 (en) | Elongate continuous flow controller with web-shaped or string-shaped flow restrictor | |
| CN208065816U (en) | A kind of high-efficiency blade formula feed distribution mechanism | |
| CN204387342U (en) | A kind of filling valve | |
| CN107952259A (en) | A kind of high-efficiency blade formula feed distribution mechanism | |
| CN107191176A (en) | A kind of oil gas supercharging device | |
| EP3204167A1 (en) | Pneumatic atomizing nozzle | |
| CN103252192B (en) | Flotation agent feed system based on fall type coal paste preprocessor | |
| CN107158808A (en) | A kind of crude oil dewatering treater | |
| AT511466B1 (en) | FLUID MIXER | |
| EP3156121A1 (en) | Mixer | |
| CN218206630U (en) | Pressure reduction control device for oil and gas field drilling equipment | |
| DE2214435C3 (en) | Wet separator for dusty gases or air | |
| CN203777811U (en) | High-efficiency gas-liquid separator | |
| CN105311979A (en) | High-flow liquid-powder mixing device | |
| CN106523839B (en) | The method for reducing pressure piping large flow fluid pressure using pipeline depressurization device | |
| CN211215819U (en) | Slug flow separator | |
| CN204805184U (en) | Loader hydraulic tank structure | |
| CN204107354U (en) | A kind of flue gas mixing arrangement | |
| CN206544898U (en) | A kind of filling apparatus of syrup | |
| CN112774259A (en) | Oil-gas mixture's separator | |
| CN207245959U (en) | Oil mist separator | |
| DE1806897A1 (en) | Dosing device | |
| CN203183816U (en) | Novel liquid-separating tank |
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 | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180424 |
|
| RJ01 | Rejection of invention patent application after publication |