CN104645787A - Self-circulation gas-liquid two-phase separation tower - Google Patents
Self-circulation gas-liquid two-phase separation tower Download PDFInfo
- Publication number
- CN104645787A CN104645787A CN201310603042.XA CN201310603042A CN104645787A CN 104645787 A CN104645787 A CN 104645787A CN 201310603042 A CN201310603042 A CN 201310603042A CN 104645787 A CN104645787 A CN 104645787A
- Authority
- CN
- China
- Prior art keywords
- liquid
- solution
- gas
- tower
- absorption
- 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
Landscapes
- Gas Separation By Absorption (AREA)
Abstract
The invention relates to a self-circulation gas-liquid two-phase separation tower and belongs to the field of paraffin machining equipment. The self-circulation gas-liquid two-phase separation tower is characterized in that the separation tower comprises a gas absorption device and a solution regeneration device, wherein a liquid exhausting opening is formed in the bottom of the gas absorption device and a liquid discharging opening is communicated with the solution regeneration device; the solution regeneration device is provided with an absorption solution circulation outlet; and the absorption solution circulation outlet is communicated with a general spraying pipe by a pipeline and a pump. When an absorption solution absorbs chlorine gas, the absorption solution is directly injected into the regeneration device to be regenerated; and the absorption solution regeneration device and an absorption tower are in an integrated structure so that the self-circulation gas-liquid two-phase separation tower is convenient to move and maintain.
Description
Technical field
The present invention relates to a kind of circulating gas-liquid two-phase laminated flow tower, belong to paraffin process equipment field.
Background technology
The preparation method of chlorinated paraffin wax comprises thermal chlorination, catalysis method and photocatalytic method three kinds at present.Upper three kinds of methods, after chlorine and paraffin react in reaction tower, will produce 2% ~ 10% unreacted chlorine, and these chlorine needs to carry out processing and absorbing in follow-up technical process, in the process processed and absorb, need a large amount of absorbing liquids.Generally, can inject regenerating unit and regenerate after absorbing liquid absorbs chlorine, regeneration of absorption solution device is separated with absorption tower, is inconvenient to move and keep in repair.
Summary of the invention
The object of this invention is to provide a kind of circulating gas-liquid two-phase laminated flow tower.
A kind of circulating gas-liquid two-phase laminated flow tower, described knockout tower comprises gas absorbing device and regenerative device of solution;
Described gas absorbing device is cylindrical-shaped tower, and be provided with at least one group of spray house steward by being provided with in tower, described spray house steward is provided with some nozzles; The bottom of described gas absorbing device is provided with liquid outlet, and liquid outlet communicates with regenerative device of solution, and described regenerative device of solution is provided with absorbing liquid loop exit, and this absorbing liquid loop exit is communicated with spray house steward by pipeline and pump.
The bottom of the preferred described gas absorbing device of circulating gas-liquid two-phase laminated flow tower of the present invention is provided with gas access.
The bottom of the preferred described regenerative device of solution of circulating gas-liquid two-phase laminated flow tower of the present invention is provided with discharge port.
The top of the preferred described gas absorbing device of circulating gas-liquid two-phase laminated flow tower of the present invention is provided with gas vent.
The present invention's preferred technical scheme is:
A kind of circulating gas-liquid two-phase laminated flow tower, described knockout tower comprises gas absorbing device and regenerative device of solution;
Described gas absorbing device is cylindrical-shaped tower, and be provided with two groups of spray house stewards by being provided with in tower, described spray house steward is provided with some nozzles.The bottom of described gas absorbing device is provided with liquid outlet, and liquid outlet 5 communicates with regenerative device of solution, and described regenerative device of solution is provided with absorbing liquid loop exit, and this absorbing liquid loop exit 3 is communicated with spray house steward by pipeline and pump.
Beneficial effect of the present invention: a kind of circulating gas-liquid two-phase laminated flow tower, described knockout tower comprises gas absorbing device and regenerative device of solution; The bottom of described gas absorbing device is provided with liquid outlet, and liquid outlet communicates with regenerative device of solution, and described regenerative device of solution is provided with absorbing liquid loop exit, and this absorbing liquid loop exit is communicated with spray house steward by pipeline and pump.Can directly inject regenerating unit to regenerate after absorbing liquid absorbs chlorine, regeneration of absorption solution device and absorption tower are structure as a whole, convenient mobile and maintenance.
Accompanying drawing explanation
Fig. 1 is a kind of schematic diagram of circulating gas-liquid two-phase laminated flow tower.
Detailed description of the invention
Following non-limiting example can make the present invention of those of ordinary skill in the art's comprehend, but does not limit the present invention in any way.
Embodiment 1
A kind of circulating gas-liquid two-phase laminated flow tower, described knockout tower comprises gas absorbing device 1 and regenerative device of solution 4; Described gas absorbing device 1 is cylindrical-shaped tower, and be provided with two groups of spray house stewards 7 by being provided with in tower, described spray house steward 7 is provided with some nozzles 4.The bottom of described gas absorbing device 1 is provided with liquid outlet 5, and liquid outlet 5 communicates with regenerative device of solution 4, and described regenerative device of solution 4 is provided with absorbing liquid loop exit 3, and this absorbing liquid loop exit 3 is communicated with spray house steward 7 by pipeline and pump 3.The bottom of described gas absorbing device 1 is provided with gas access 9.The bottom of described regenerative device of solution 4 is provided with discharge port 6.The top of described gas absorbing device 1 is provided with gas vent 8.
Claims (5)
1. a circulating gas-liquid two-phase laminated flow tower, is characterized in that: described knockout tower comprises gas absorbing device (1) and regenerative device of solution (4);
Described gas absorbing device (1) is cylindrical-shaped tower, and be provided with at least one group of spray house steward (7) by being provided with in tower, described spray house steward (7) is provided with some nozzles (4); The bottom of described gas absorbing device (1) is provided with liquid outlet (5), liquid outlet (5) communicates with regenerative device of solution (4), described regenerative device of solution (4) is provided with absorbing liquid loop exit (3), and this absorbing liquid loop exit (3) is communicated with spray house steward (7) by pipeline and pump (3).
2. knockout tower according to claim 1, is characterized in that: the bottom of described gas absorbing device (1) is provided with gas access (9).
3. knockout tower according to claim 1, is characterized in that: the bottom of described regenerative device of solution (4) is provided with discharge port (6).
4. knockout tower according to claim 1, is characterized in that: the top of described gas absorbing device (1) is provided with gas vent (8).
5. knockout tower according to claim 1, is characterized in that: described gas absorbing device (1) is cylindrical-shaped tower, and be provided with two groups of sprays house steward (7) by being provided with in tower, described spray house steward (7) is provided with some nozzles (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310603042.XA CN104645787A (en) | 2013-11-22 | 2013-11-22 | Self-circulation gas-liquid two-phase separation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310603042.XA CN104645787A (en) | 2013-11-22 | 2013-11-22 | Self-circulation gas-liquid two-phase separation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104645787A true CN104645787A (en) | 2015-05-27 |
Family
ID=53237727
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310603042.XA Pending CN104645787A (en) | 2013-11-22 | 2013-11-22 | Self-circulation gas-liquid two-phase separation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104645787A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101024603A (en) * | 2007-03-29 | 2007-08-29 | 永港伟方(北京)科技有限公司 | Methanal absorbing system |
| CN201894910U (en) * | 2010-12-08 | 2011-07-13 | 湖北江钻天祥化工有限公司 | Circulating absorption tower |
| CN202270465U (en) * | 2011-10-13 | 2012-06-13 | 惠州市东江环保技术有限公司 | Combined device for absorbing acid gas |
| CN202682825U (en) * | 2012-06-29 | 2013-01-23 | 怀化市骏源精细化工有限公司 | Acid mist recovery device of reaction kettle for producing polymeric aluminum |
| CN203108419U (en) * | 2013-01-31 | 2013-08-07 | 珠海九通水务有限公司 | Chlorine absorbing device |
-
2013
- 2013-11-22 CN CN201310603042.XA patent/CN104645787A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101024603A (en) * | 2007-03-29 | 2007-08-29 | 永港伟方(北京)科技有限公司 | Methanal absorbing system |
| CN201894910U (en) * | 2010-12-08 | 2011-07-13 | 湖北江钻天祥化工有限公司 | Circulating absorption tower |
| CN202270465U (en) * | 2011-10-13 | 2012-06-13 | 惠州市东江环保技术有限公司 | Combined device for absorbing acid gas |
| CN202682825U (en) * | 2012-06-29 | 2013-01-23 | 怀化市骏源精细化工有限公司 | Acid mist recovery device of reaction kettle for producing polymeric aluminum |
| CN203108419U (en) * | 2013-01-31 | 2013-08-07 | 珠海九通水务有限公司 | Chlorine absorbing device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103920384A (en) | Equipment for absorbing high-concentration nitric oxides by adopting normal-pressure process | |
| CN203408621U (en) | Acidic flue gas treatment system | |
| CN208436641U (en) | A kind of elution device of efficient removal tantalum niobium waste gas decomposition | |
| CN104645787A (en) | Self-circulation gas-liquid two-phase separation tower | |
| CN102743970A (en) | Processing method and processing device of production waste gas containing hydrogen sulfide | |
| CN202237714U (en) | Tail gas absorbing system | |
| CN204543953U (en) | A kind of novel absorbent tower | |
| CN204656339U (en) | A kind of desulphurization denitration absorption reaction tower | |
| CN203862115U (en) | Sulfuric acid exhaust gas washing tower | |
| CN204619719U (en) | A kind of baffling absorption tower for ammonia desulfurizing process | |
| CN204170587U (en) | A kind of device strengthening iodomethane in absorption acetate acid tail gas | |
| CN203816465U (en) | Waste gas absorption tower | |
| CN202876625U (en) | Acid and alkali-resistant absorbing tower | |
| CN203440262U (en) | Device for producing trans-1, 2-dichloroethylene with acetylene by adopting catalytic chlorination method | |
| CN206138988U (en) | Tower exhaust -gas treatment equipment | |
| CN206343058U (en) | A kind of tail gas absorber in CBS production processes | |
| CN204073795U (en) | Gas-phase alcohol recovery system in expelling water tail gas | |
| CN104645788A (en) | Cooling absorption tower for producing chlorinated paraffin | |
| CN202224031U (en) | Chilling spray equipment for purification of chemical waste gas | |
| CN204672122U (en) | A kind of novel acid mist purifying tower sprinkling equipment | |
| CN206184210U (en) | Tail gas treatment tower | |
| CN204337982U (en) | A kind of vapor absorbing apparatus | |
| CN204594284U (en) | Utilize the cooling water generating means of liquid nitrogen vaporizer cold air | |
| CN203877925U (en) | Regenerating equipment for carbon dioxide generated in ethylene oxide production | |
| CN215962868U (en) | Cooling absorption tower and sulfur-containing waste treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150527 |
|
| RJ01 | Rejection of invention patent application after publication |