CN205145645U - Hypergravity revolving bed device and hypergravity rectification plant who constitutes thereof - Google Patents
Hypergravity revolving bed device and hypergravity rectification plant who constitutes thereof Download PDFInfo
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- CN205145645U CN205145645U CN201520949627.1U CN201520949627U CN205145645U CN 205145645 U CN205145645 U CN 205145645U CN 201520949627 U CN201520949627 U CN 201520949627U CN 205145645 U CN205145645 U CN 205145645U
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- swinging bed
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Abstract
The utility model provides a hypergravity revolving bed device, includes casing, motor, carousel, filler, the carousel is installed on the swivel mount that sets up in the casing, the motor is installed on the casing, the main shaft and the carousel coaxial coupling of motor, the filler is installed on the carousel, install hollow boss on the casing, boss bottom opening communicates with the casing is inside. Hypergravity revolving bed device is small, the energy consumption low, and the passing through liquids sprays sends liquid into inside, has increaseed liquid distributor's decentralization, and what the fluid power of loseing one's temper was enough more abundant contacting and exchanging. Utilizing the sieve to tackle the liquid that sprays out, having avoided effectively having improved the distribution efficiency of liquid because the action of gravity leads to the fact liquid to assemble in the bottom of inside, what the fluid power of loseing one's temper was enough more abundant contacting and exchanging.
Description
Technical field
The utility model design oil-gas-liquid liquefied oil gas separation technology field specifically, is the hypergravity rectifying device of a kind of hypergravity swinging bed device and composition thereof.
Background technology
The Main Ingredients and Appearance of liquefied petroleum gas (being called for short LPG) is propane, normal butane, iso-butane, and also containing a small amount of ethane and carbon five, carbon six alkane, wherein the molar content of propane is more than 60%, and the molar content of normal butane, iso-butane is more than 25%.If using liquefied petroleum gas as fuel, its value is not high, so wish by carrying out rectifying separation to LPG, obtains the higher propane of added value and butane.Nowadays conventional method uses rectifying column to carry out rectifying separation in time.
Rectifying is a kind of process of caloic simultaneous interpretation, utilizes the difference of material to be separated component boiling point to carry out lock out operation, obtains the product of high-quality.In the industry such as chemical industry, oil vapor treatment, separation equipment has consequence, and its efficiency, energy consumption etc. have vital impact to the performance of final products.Utilize rectifying column to carry out rectifying separation, although treating capacity is large, because the feature such as enhancing efficiency narrow space, energy consumption are high, bulky, cause high energy consumption, large investment, large volume conflict with high product quality.
Utility model content
The deficiency that the utility model exists for above-mentioned prior art, devises the hypergravity rectifying device of a kind of hypergravity swinging bed device and composition thereof.
Hypergravity swinging bed device of the present utility model, comprise housing, motor, rotating disk, filler, described rotating disk is arranged on the swivel base of setting in housing, described motor is arranged on housing, the main shaft of described motor is coaxially connected with rotating disk, described filler is arranged on rotating disk, described housing is provided with the boss of hollow, and described boss bottom opening is also communicated with enclosure interior.
Be provided with the rotor inner edge of tubular in described housing, top, described rotor inner edge is connected with boss, and bottom contacts with rotating disk.
Described housing is provided with air inlet and liquid outlet.
Described boss is provided with inlet and gas outlet, described inlet is connected with feed tube, and described feed tube extend into the inside of rotor inner edge, and described feed tube bottom end seal, sidewall is provided with nozzle.
Preferably, be provided with wire mesh demister in described boss, described inlet and gas outlet are all positioned at the top of wire mesh demister.
Preferably, described rotor inner edge inwall is provided with sieve plate, and described sieve plate is provided with sieve aperture.
Preferably, be inclined upwardly inside described sieve plate installation.
Preferably, described sieve plate is installed multiple from top to bottom, and the width of described sieve plate increases from top to bottom gradually.
A kind of hypergravity rectifying device, comprise hypergravity swinging bed device, condenser and reboiler, described hypergravity swinging bed device is provided with two.
The inlet of described first hypergravity swinging bed device is connected with the first feed tube, and gas outlet is connected with the first escape pipe, and air inlet is connected with the first air inlet pipe, and liquid outlet is connected with the first drain pipe.
The inlet of described second hypergravity swinging bed device is connected with the second feed tube, and gas outlet is connected with the second escape pipe, and air inlet is connected with the second air inlet pipe, and liquid outlet is connected with the second drain pipe.
Described second air inlet pipe is all connected with the first feed tube with the second drain pipe, described first escape pipe is connected with the second air inlet pipe, described first air inlet pipe is all connected with reboiler with the first drain pipe, described second escape pipe is all connected with condenser with the second feed tube, described first drain pipe is connected with the first output pipe, and described condenser is connected with the second output pipe.
The beneficial effects of the utility model are: hypergravity swinging bed device volume is little, energy consumption is low, by liquid spray, liquid are sent to inside, increase the decentralization of liquid distribution, enable gas-liquid carry out more fully contacting and exchanging.Utilize sieve plate to tackle the liquid sprayed out, efficiently avoid because Action of Gravity Field causes liquid at the congregate of inside, improve the distribution efficiency of liquid, enable gas-liquid carry out more fully contacting and exchanging.Sieve plate is obliquely installed, and more effectively can tackle liquid.Sieve plate is multistage setting from top to bottom, improves its Intercepting effect to liquid.The wire mesh demister installed effectively can prevent liquid foam entrainment, avoids being entrained with liquid in the gas of discharging.
Hypergravity rectifying device carries out rectifying and carries heating up in a steamer by two hypergravity swinging bed devices respectively, and can be separated gas phase, liquid phase, gas-liquid two-phase, mass-and heat-transfer is effective, more effectively can complete distillation process.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of hypergravity swinging bed device;
Accompanying drawing 2 is the structural representation of hypergravity rectifying device.
Detailed description of the invention
In order to understand structure of the present utility model, feature and other object further, the appended preferred embodiment of existing combination is described in detail as follows, and illustrated preferred embodiment is only for illustration of the technical solution of the utility model, and non-limiting the utility model.
Detailed description of the invention of the present utility model is as follows:
Embodiment one:
As shown in Figure 1, this hypergravity swinging bed device comprises housing 1, motor 2, rotating disk 3, filler 4.
Rotating disk 3 is arranged on the swivel base 5 of setting in housing 1, and motor 2 is arranged on housing 1, and the main shaft 6 of motor 2 is coaxially connected with rotating disk 3, and filler 4 is arranged on rotating disk 3.
Housing 1 is provided with the boss 7 of hollow, boss 7 bottom opening is also communicated with housing 1 inside.
Be provided with the rotor inner edge 8 of tubular in housing 1, top, rotor inner edge 8 is connected with boss 7, and bottom contacts with rotating disk 3.
Housing 1 is provided with air inlet 9 and liquid outlet 10.
Boss 7 is provided with inlet 11 and gas outlet 12, inlet 11 is connected with feed tube 13, and feed tube 13 extend into the inside of rotor inner edge 8, and feed tube 13 bottom end seal, sidewall is provided with nozzle 14.
Liquid phase enters in feed tube 13 by inlet 11, sprays, spray to rotor inner edge 8 from the nozzle 14 of feed tube 13.Motor 2 drives the filler 4 on rotating disk 3 and rotating disk 3 to rotate, and produce hypergravity effect, liquid enters into filler 4 and is drawn into drop, liquid film, brin.Gas phase enters into housing by air inlet 9, and assemble in housing 1, after reaching certain pressure, pressure forces gas to enter into the inside of rotor inner edge 8 through filler 4.Gas in the process of filler 4, be drawn in filler drop, liquid film, brin liquid surface contact, carry out mass-and heat-transfer.The liquid and gas completing mass-and heat-transfer are discharged from liquid outlet 10 and gas outlet 12 respectively.
Embodiment two:
Embodiment two forms substantially identical with the structure of embodiment one, and difference is:
Be provided with wire mesh demister 15 in boss 7, inlet 11 and gas outlet 12 are all positioned at the top of wire mesh demister 15.Wire mesh demister 15 stops the opening of whole boss 7, has made the gas phase of mass-and heat-transfer by must, through wire mesh demister 15, make wire mesh demister 15 effectively can prevent liquid foam entrainment during gas outlet 12, avoids being entrained with liquid in the gas of discharging.
Embodiment three:
Embodiment three forms substantially identical with the structure of embodiment one, and difference is:
Rotor inner edge 8 inwall is provided with sieve plate 16, and sieve plate 16 is provided with sieve aperture.Sieve plate 16 is corresponding with nozzle 14, the liquid phase sprayed by nozzle 14 is flowed downward after being sprayed onto rotor inner edge 8 inwall, then tackled by sieve plate 16, slowly flowed downward again by sieve aperture by the liquid phase that sieve plate 16 is tackled, efficiently avoid because Action of Gravity Field causes liquid at the congregate of inside, improve the distribution efficiency of liquid.
Embodiment four:
Embodiment four forms substantially identical with the structure of embodiment three, and difference is:
Be inclined upwardly inside sieve plate 16 installation, and sieve plate 16 is installed multiple from top to bottom, and the width of sieve plate 16 increases from top to bottom gradually.
Sieve plate 16 is obliquely installed, and more effectively can tackle liquid.Sieve plate 16 is multistage setting from top to bottom, improves its Intercepting effect to liquid.
Embodiment five:
As shown in Figure 2, this hypergravity rectifying device comprises the hypergravity swinging bed device described in embodiment one and condenser 21 and reboiler 22, and hypergravity swinging bed device is provided with two.
The inlet of the first hypergravity swinging bed device 23 is connected with the first feed tube 31, and gas outlet is connected with the first escape pipe 32, and air inlet is connected with the first air inlet pipe 33, and liquid outlet is connected with the first drain pipe 34.
The inlet of the second hypergravity swinging bed device 24 is connected with the second feed tube 35, and gas outlet is connected with the second escape pipe 36, and air inlet is connected with the second air inlet pipe 37, and liquid outlet is connected with the second drain pipe 38.
Second air inlet pipe 37 is all connected with the first feed tube 31 with the second drain pipe 38, first escape pipe 32 is connected with the second air inlet pipe 37, first air inlet pipe 33 is all connected with reboiler 22 with the first drain pipe 34, second escape pipe 36 is all connected with condenser 21 with the second feed tube 35, first drain pipe 34 is connected with the first output pipe 41, and condenser 21 is connected with the second output pipe 42.
First hypergravity swinging bed device 23 is as stripping section, and the second hypergravity swinging bed device 24 is as rectifying section, and the first hypergravity swinging bed device 23 and the second hypergravity swinging bed device 24 carry out hypergravity rectifying to the material entered.
The LPG carrying out rectifying separation is needed first to send into the first feed tube 31 of hypergravity rectifying device.
When the LPG entered is gas-liquid two-phase, liquid phase wherein enters into the first hypergravity swinging bed device 23 by the first feed tube 31, and gas phase then enters into the second hypergravity swinging bed device 24 by the second air inlet pipe 37 be connected with the first feed tube 31; When the LPG entered is gas phase, LPG enters into the second hypergravity swinging bed device 24 by the second air inlet pipe 37 be connected with the first feed tube 31; When the LPG entered is liquid phase, LPG enters into the first hypergravity swinging bed device 23 by the first feed tube 31.
The gaseous phase materials entered by the second air inlet pipe 37 with put forward the gas phase of heating up in a steamer from the first escape pipe 32 through the first hypergravity swinging bed device 23 and converge, together enter the second hypergravity swinging bed device 24 as rectifying section.
By the gas phase of the second escape pipe 36 through the second hypergravity swinging bed device 24 rectifying, after condenser 21 cools, become liquid phase, a part is back in the second hypergravity swinging bed device 24 by the second feed tube 35; Another part is as product---propane, discharge from the second output pipe 42.
The liquid phase flowed out by the second hypergravity swinging bed device 24 second drain pipe 38 is converged with the liquid phase of the LPG entered from the first feed tube 31, enters into the first hypergravity swinging bed device 23 and carries out carrying heating up in a steamer.
By the liquid phase that the first hypergravity swinging bed device 23 first liquid outlet 34 flows out, a part is as bottom product---butane, discharged by the first output pipe 41; Another part becomes gas phase by reboiler 22, enters the first hypergravity swinging bed device 23 by the first air inlet pipe 33.
Said process forms a complete LPG distillation process.
Claims (6)
1. a hypergravity swinging bed device, comprise housing (1), motor (2), rotating disk (3), filler (4), described rotating disk (3) is arranged on the swivel base (5) of setting in housing (1), described motor (2) is arranged on housing (1), the main shaft (6) of described motor (2) is coaxially connected with rotating disk (3), described filler (4) is arranged on rotating disk (3), it is characterized in that, described housing (1) is provided with the boss (7) of hollow, described boss (7) bottom opening is also communicated with housing (1) inside,
Be provided with the rotor inner edge (8) of tubular in described housing (1), described rotor inner edge (8) top is connected with boss (7), and bottom contacts with rotating disk (3);
Described housing (1) is provided with air inlet (9) and liquid outlet (10);
Described boss (7) is provided with inlet (11) and gas outlet (12), described inlet (11) is connected with feed tube (13), described feed tube (13) extend into the inside of rotor inner edge (8), described feed tube (13) bottom end seal, sidewall is provided with nozzle (14).
2. hypergravity swinging bed device according to claim 1, it is characterized in that, be provided with wire mesh demister (15) in described boss (7), described inlet (11) and gas outlet (12) are all positioned at the top of wire mesh demister (15).
3. hypergravity swinging bed device according to claim 1, it is characterized in that, described rotor inner edge (8) inwall is provided with sieve plate (16), and described sieve plate (16) is provided with sieve aperture.
4. hypergravity swinging bed device according to claim 3, is characterized in that, described sieve plate (16) inner side is inclined upwardly installation.
5. hypergravity swinging bed device according to claim 3 or 4, is characterized in that, described sieve plate (16) is installed multiple from top to bottom, and the width of described sieve plate (16) increases from top to bottom gradually.
6. a hypergravity rectifying device, is characterized in that, comprise hypergravity swinging bed device described in claim 1, condenser (21) and reboiler (22), described hypergravity swinging bed device is provided with two,
The inlet of described first hypergravity swinging bed device (23) is connected with the first feed tube (31), gas outlet is connected with the first escape pipe (32), air inlet is connected with the first air inlet pipe (33), and liquid outlet is connected with the first drain pipe (34);
The inlet of described second hypergravity swinging bed device (24) is connected with the second feed tube (35), gas outlet is connected with the second escape pipe (36), air inlet is connected with the second air inlet pipe (37), and liquid outlet is connected with the second drain pipe (38);
Described second air inlet pipe (37) is all connected with the first feed tube (31) with the second drain pipe (38), described first escape pipe (32) is connected with the second air inlet pipe (37), described first air inlet pipe (33) is all connected with reboiler (22) with the first drain pipe (34), described second escape pipe (36) is all connected with condenser (21) with the second feed tube (35), described first drain pipe (34) is connected with the first output pipe (41), and described condenser (21) is connected with the second output pipe (42).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520949627.1U CN205145645U (en) | 2015-11-24 | 2015-11-24 | Hypergravity revolving bed device and hypergravity rectification plant who constitutes thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520949627.1U CN205145645U (en) | 2015-11-24 | 2015-11-24 | Hypergravity revolving bed device and hypergravity rectification plant who constitutes thereof |
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| CN205145645U true CN205145645U (en) | 2016-04-13 |
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| CN201520949627.1U Active CN205145645U (en) | 2015-11-24 | 2015-11-24 | Hypergravity revolving bed device and hypergravity rectification plant who constitutes thereof |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854461A (en) * | 2016-04-18 | 2016-08-17 | 中国石油化工股份有限公司 | Dish type gas decontamination device |
| CN106943763A (en) * | 2017-03-29 | 2017-07-14 | 河南省化工研究所有限责任公司 | A kind of rectifier unit that waste liquid commercial recovery system is produced suitable for coal-ethylene glycol |
| CN108640330A (en) * | 2018-04-18 | 2018-10-12 | 中北大学 | Hypergravity strengthening extraction-catalysis O3/Ti4+Handle the method and device of high nitrobenzene waste water |
| CN109603720A (en) * | 2019-01-08 | 2019-04-12 | 北京化工大学 | Hypergravity oxidation reactor device and application |
| CN110152336A (en) * | 2019-05-21 | 2019-08-23 | 大湾环保科技惠州有限公司 | A kind of hypergravity bed |
-
2015
- 2015-11-24 CN CN201520949627.1U patent/CN205145645U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854461A (en) * | 2016-04-18 | 2016-08-17 | 中国石油化工股份有限公司 | Dish type gas decontamination device |
| CN106943763A (en) * | 2017-03-29 | 2017-07-14 | 河南省化工研究所有限责任公司 | A kind of rectifier unit that waste liquid commercial recovery system is produced suitable for coal-ethylene glycol |
| CN108640330A (en) * | 2018-04-18 | 2018-10-12 | 中北大学 | Hypergravity strengthening extraction-catalysis O3/Ti4+Handle the method and device of high nitrobenzene waste water |
| CN108640330B (en) * | 2018-04-18 | 2021-08-17 | 中北大学 | Supergravity enhanced extraction-catalysis of O3/Ti4+Method and device for treating high-concentration nitrobenzene wastewater |
| CN109603720A (en) * | 2019-01-08 | 2019-04-12 | 北京化工大学 | Hypergravity oxidation reactor device and application |
| CN109603720B (en) * | 2019-01-08 | 2021-03-26 | 北京化工大学 | Hypergravity oxidation reactor device and application |
| CN110152336A (en) * | 2019-05-21 | 2019-08-23 | 大湾环保科技惠州有限公司 | A kind of hypergravity bed |
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Legal Events
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20181207 Address after: 610041 No.1-16, No.88, No.5 Jitai Road, Chengdu High-tech Zone, Sichuan Province Patentee after: Sichuan Jerry Heng RI Natural Gas Engineering Co., Ltd. Address before: 264000 No. 9 Jierui Road, Laishan District, Yantai City, Shandong Province Patentee before: JEREH OIL & GAS ENGINEERING CORPORATION |