CN200957350Y - Charging structure of liquid-membrane mass reactor - Google Patents
Charging structure of liquid-membrane mass reactor Download PDFInfo
- Publication number
- CN200957350Y CN200957350Y CN 200620108517 CN200620108517U CN200957350Y CN 200957350 Y CN200957350 Y CN 200957350Y CN 200620108517 CN200620108517 CN 200620108517 CN 200620108517 U CN200620108517 U CN 200620108517U CN 200957350 Y CN200957350 Y CN 200957350Y
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- water
- soluble liquid
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Abstract
The utility model discloses a liquid film mass transfer reactor feed structure, including an aqueous phase inlet distributed at the upper part of a crust of the reactor; the utility model is characterized in that the device also has a mixed phase inlet which is composed of oil phase and the aqueous phase. When the aqueous phase inlet is set up at the top of the reactor, then the mixed phase inlet is respectively set up at the upper profile of the reactor; on the contrary, When the mixed phase inlet is set up at the top of the reactor, then the aqueous phase inlet is set up at the upper profile of the reactor. Owing to the aqueous phase is divided into more than two ways and to enter into a capped end of the reactor, therefore, the liquid film of the aqueous phase can be formed easily and distributed evenly on the fibre so as to avoid a ditch flow and ensure the two phases have a large contact area, so the mass transfer efficiency is improved greatly.
Description
Technical field
The utility model relates to a kind of feed distribution structure of mass transfer reaction device, and this mass transfer reaction device belongs to a kind of liquid film mass transfer reaction device of extracting between immiscible two phase liquid or solution-air of can be used for.
Background technology
Liquid film mass transfer reaction device can be used for mass transfer reaction processes such as the extraction, catalysis of industries such as chemical industry, metallurgy, papermaking, environmental protection.A kind of liquid distribution to bat wool, is formed liquid film; Make another kind of liquid distribution outside this liquid film.Two kinds of liquid are in the co-flow process, and existing very big contact, mass transfer area have short mass transfer distance again, thereby improved mass transfer reaction efficient.U.S. Pat 3,977,829 adopt the fibre bundle of a kind of glass or stainless steel as the carrier that disperses liquid film; 3992156 pairs of fibre bundles of U.S. Pat adopt beam splitting to fix; Chinese patent CN022589856 adopts the fiber bundle structure of unit tubular type.But above-mentioned patented technology has all adopted water-soluble liquid phase and the independent charging of oil phase to the charging pattern of liquid, has influenced the liquid film uniform in shaping of water-soluble liquid phase, thereby makes mass-transfer efficiency reduce.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of feeding structure of liquid film mass transfer reaction device, and it improves the charging pattern of liquid film mass transfer reaction device, make aqueous solution phase film forming more evenly, improve mass-transfer efficiency and simple and practical.
The utility model solves the problems of the technologies described above the technical scheme that is adopted: a kind of feeding structure of liquid film mass transfer reaction device, it comprises the water-soluble liquid phase import that is distributed in shell of reactor top, it is characterized in that having in addition the mixing import mutually of oil phase and the mixing of water-soluble liquid phase, when water-soluble liquid phase import is arranged on the reactor head position, mix the sideway stance that the phase import is separately positioned on reactor top; When the import of mixing phase was arranged on the reactor head position, water-soluble liquid phase import was arranged on the sideway stance on reactor top.
When a water-soluble liquid phase import was arranged on the reactor head position, other 1-3 was mixed the sideway stance that the phase import is separately positioned on reactor top; When the import of mixing phase was arranged on the reactor head position, 1-3 water-soluble liquid phase import was separately positioned on the sideway stance on reactor top.
In the inlet pipeline of described mixing phase import blender is installed, inlet pipeline has water-soluble liquid phase charging aperture and oil phase charging aperture.
Described blender directly is connected with end socket.
Described import is positioned at end socket place, reactor top.
Compared with prior art, advantage of the present utility model is: water-soluble liquid phase adopts the feeding manner more than 2 tunnel, make the material that enters in the reactor distribute more even, the moulding of liquid film on fiber be easier, be more evenly distributed, guarantee that the two-phase of liquid liquid has very big contact area, improved mass-transfer efficiency greatly, and feeding structure is simple and practical, implement easily to make, cost is low.
Description of drawings
Fig. 1 is one of the utility model feeding structure schematic diagram;
Fig. 2 is two of the utility model feeding structure schematic diagram;
Fig. 3 is a reactor fusing head connection tube orientation schematic diagram among Fig. 1;
Fig. 4 is a reactor fusing head connection tube orientation schematic diagram among Fig. 2.
The specific embodiment
Embodiment describes in further detail the utility model below in conjunction with accompanying drawing.
As Fig. 1-2, a kind of liquid film mass transfer reaction device, form by shell of reactor, the first phase liquid-inlet, the second phase liquid or gas feed, filament boundling carrier, fluid separation applications jar shell, the first phase liquid outlet, the second phase liquid or critical pieces such as gas vent, the first phase liquid distributor, these all are traditional technology, see also the document in the background technology.
The first phase liquid of the present utility model is set at water-soluble liquid phase, and the second phase liquid is oil phase.
Water liquid phase import demultiplexing enters in the end socket of reactor head.
As Fig. 1,3, a kind of structure is, the top, top that water-soluble liquid phase import 1 is arranged on reactor 6 is that cat head enters.1-3 is mixed the sideway stance that phase import 2 is distributed in reactor 6 tops, in the inlet pipeline of mixing phase import 2 blender 3 is installed, and inlet pipeline has water-soluble liquid phase charging aperture 5 and oil phase charging aperture 4.And described blender 3 can directly be connected with end socket.Make like this in the water-soluble liquid phase other 1-3 road respectively with oil phase through blender 3 mix the back from reactor 6 upper cover sides 1-3 mixing mutually import 2 enter in the tower.
As Fig. 2,4, another kind of structure is, mix the tip position that phase import 2 is arranged on reactor 6, water-soluble liquid phase import 1 is arranged on the sideway stance on reactor 6 tops, make a road in the water-soluble liquid phase and oil phase mix the back through blender 3 and mix import 2 mutually from of cat head and enter, the other 1-3 road in the water-soluble liquid phase enters in the tower from reactor upper cover side 1-3 water-soluble liquid phase import 1.
The course of work of the feed distribution pattern of liquid film mass transfer reaction device of the present utility model is: a part of water enters from top inlet.Another part water can 1 to 3 the tunnel advances in blender and the distributor that enters into from the side after oil phase mixes in the tower, make water uniform distribution in tower, on fiber, evenly form liquid film, guarantee that the two-phase of liquid liquid has very big contact area, has improved mass-transfer efficiency greatly.
Claims (6)
1, a kind of feeding structure of liquid film mass transfer reaction device, it comprises the water-soluble liquid phase import that is distributed in shell of reactor top, it is characterized in that having in addition the mixing import mutually of oil phase and the mixing of water-soluble liquid phase, when water-soluble liquid phase import is arranged on the reactor head position, mix the sideway stance that the phase import is separately positioned on reactor top; When the import of mixing phase was arranged on the reactor head position, water-soluble liquid phase import was arranged on the sideway stance on reactor top.
2, feeding structure according to claim 1 when it is characterized in that a described water-soluble liquid phase import is arranged on the reactor head position, has 1-3 to mix the sideway stance that the phase import is separately positioned on reactor top.
3, feeding structure according to claim 1, when it is characterized in that the import of described mixing phase is arranged on the reactor head position, 1-3 water-soluble liquid phase import is separately positioned on the sideway stance on reactor top.
4, according to claim 2 or 3 described feeding structures, it is characterized in that in the inlet pipeline of described mixing phase import blender being installed, inlet pipeline has water-soluble liquid phase charging aperture and oil phase charging aperture.
5, feeding structure according to claim 4 is characterized in that described blender directly is connected with end socket.
6, feeding structure according to claim 5 is characterized in that described import is positioned at end socket place, reactor top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620108517 CN200957350Y (en) | 2006-10-11 | 2006-10-11 | Charging structure of liquid-membrane mass reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620108517 CN200957350Y (en) | 2006-10-11 | 2006-10-11 | Charging structure of liquid-membrane mass reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200957350Y true CN200957350Y (en) | 2007-10-10 |
Family
ID=38784224
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620108517 Expired - Lifetime CN200957350Y (en) | 2006-10-11 | 2006-10-11 | Charging structure of liquid-membrane mass reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200957350Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102408913A (en) * | 2010-09-26 | 2012-04-11 | 刘宽 | Light hydrocarbon sweetening process utilizing alkali liquor by stages |
| CN102757809A (en) * | 2012-08-03 | 2012-10-31 | 宁波中一石化科技有限公司 | Mercaptan removal and lye regeneration device and method for gasoline light fractions |
| CN101780375B (en) * | 2008-04-30 | 2013-09-18 | 赛尔格有限责任公司 | A contained liquid membrane contactor and a method of manufacturing the same |
-
2006
- 2006-10-11 CN CN 200620108517 patent/CN200957350Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101780375B (en) * | 2008-04-30 | 2013-09-18 | 赛尔格有限责任公司 | A contained liquid membrane contactor and a method of manufacturing the same |
| CN102408913A (en) * | 2010-09-26 | 2012-04-11 | 刘宽 | Light hydrocarbon sweetening process utilizing alkali liquor by stages |
| CN102408913B (en) * | 2010-09-26 | 2014-03-12 | 刘宽 | Light hydrocarbon sweetening process utilizing alkali liquor by stages |
| CN102757809A (en) * | 2012-08-03 | 2012-10-31 | 宁波中一石化科技有限公司 | Mercaptan removal and lye regeneration device and method for gasoline light fractions |
| CN102757809B (en) * | 2012-08-03 | 2015-03-18 | 宁波中一石化科技有限公司 | Mercaptan removal and lye regeneration device and method for gasoline light fractions |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Charging structure of liquid-membrane mass reactor Effective date of registration: 20120814 Granted publication date: 20071010 Pledgee: China Co truction Bank Corp Ningbo national hi tech Zone sub branch Pledgor: Ningbo Zhongyi Petrochemical Technology Co., Ltd. Registration number: 2012990000445 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20130809 Granted publication date: 20071010 Pledgee: China Co truction Bank Corp Ningbo national hi tech Zone sub branch Pledgor: Ningbo Zhongyi Petrochemical Technology Co., Ltd. Registration number: 2012990000445 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 315040 No. 1558 Jiangnan Road, Zhejiang, Ningbo Patentee after: NINGBO ZHONGYI PETROCHEMICAL TECHNOLOGY CO., LTD. Address before: 315040 No. 1558 Jiangnan Road, Zhejiang, Ningbo Patentee before: Ningbo Zhongyi Petrochemical Technology Co., Ltd. |
|
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 315040, Zhejiang, Ningbo province National hi tech Zone Lingyun road 1177 Lingyun Industrial Park, building 10, north 2 floor Patentee after: NINGBO ZHONGYI PETROCHEMICAL TECHNOLOGY CO., LTD. Address before: 315040 No. 1558 Jiangnan Road, Zhejiang, Ningbo Patentee before: NINGBO ZHONGYI PETROCHEMICAL TECHNOLOGY CO., LTD. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20071010 |
|
| EXPY | Termination of patent right or utility model |