CN202605897U - Gas-liquid-solid separation device - Google Patents
Gas-liquid-solid separation device Download PDFInfo
- Publication number
- CN202605897U CN202605897U CN 201220184773 CN201220184773U CN202605897U CN 202605897 U CN202605897 U CN 202605897U CN 201220184773 CN201220184773 CN 201220184773 CN 201220184773 U CN201220184773 U CN 201220184773U CN 202605897 U CN202605897 U CN 202605897U
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- solid
- solid separator
- oil
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The utility model particularly relates to a gas-liquid-solid separation device which is applied to a solid bed process coking unit. The device is characterized by comprising a gas-liquid-solid separator, one side of the gas-liquid-solid separator is provided with a flow guide tube, the flow guide tube extends to the inside of the gas-liquid-solid separator, a gas rising tube is arranged at the upper end of the gas-liquid-solid separator, and a blanking tube is arranged at the lower end of a casing. The device has the advantages of being simple in structure, low in cost, safe and reliable in performance, quick in gas-liquid-solid separation speed and good in effect. By the aid of the device, coke powder and part of the liquid in oil gas are separated from gas quickly after the oil gas enters a reactor, the foam quantity in the reactor is reduced, the device can work for a long period, and the production efficiency is improved.
Description
Technical field
The utility model is specifically related to a kind of gas-liquid solid separation device that is applicable to the solid bed process coking plant of what.
Background technology
In the reaction of the solid bed of what coking plant reaction system, residual oil, sump oil, cracking tail oil, catalytic slurry, heavy fuel wet goods heavy oil component are heated to 480-550 ℃ through heating furnace, can produce the oil gas about 500 ℃; Oil gas need be conveyed in the reactor and react; Owing to contain a spot of coke powder in the oil gas, these coke powders contact with a large amount of oil gas after getting into reactor, can produce a large amount of foams; Be unfavorable for that the device long period goes into operation, and influences production efficiency.
The utility model content
It is a kind of simple in structure that the purpose of the utility model is to provide, and performance is safe and reliable, can the Rapid Realization gas-liquid separate admittedly, reduces the gas-liquid solid separation device of the reaction back oil gas coke powder amount of carrying.
The utility model is realized through following technical scheme:
It is a kind of gas-liquid solid separation device; It is characterized in that comprising a gas-liquid-solid separator, a side of gas-liquid-solid separator is provided with mozzle, and mozzle extends to the inside of gas-liquid-solid separator; The upper end of gas-liquid-solid separator is provided with riser, and the lower end of housing is provided with tremie pipe.
A preferred version as the utility model: the inner end of mozzle is provided with guide-leaf plate.
The operation principle of the utility model is following:
The oil gas that contains coke powder gets in the gas-liquid-solid separator through mozzle; Oil gas leaves through guide-leaf plate and gas-liquid-solid separator Rapid Realization bispin flow point with certain linear speed; Can the Rapid Realization gas-liquid separate admittedly; Riser gets into the oil gas line to gas phase from the top, and solid and partially liq drop in the solid bed bioreactor of what through tremie pipe.Thereby realize reducing significantly the probability that oil gas carries coke powder.
The utlity model has simple in structure, cost is low, performance is safe and reliable, solid fast, the effective advantage of separating rate of gas-liquid.Use the utility model, after oil gas got into reactor, coke powder in the oil gas and partially liq separated with gas fast, have reduced the amount of foam in the reactor, help the device long period and go into operation, and have improved production efficiency.
Description of drawings:
Fig. 1 is the structural representation of the utility model.
Shown in figure: 1 mozzle; 2 gas-liquid-solid separators; 3 guide-leaf plates; 4 riseies; 5 tremie pipes.
The specific embodiment:
As shown in Figure 1: a side of gas-liquid-solid separator 2 is provided with mozzle 1, and mozzle 1 extends to the inside of gas-liquid-solid separator 2, and its inner end is provided with guide-leaf plate 3; The top of gas-liquid-solid separator 2 is provided with riser 4, and the bottom is provided with tremie pipe 5.
When the utility model uses; Oil gas about 500 ℃ gets into gas-liquid-solid separator 2 through mozzle 1; Oil gas leaves through guide-leaf plate 3 and gas-liquid-solid separator 2 Rapid Realization bispin flow points with certain linear speed, and gas-liquid that can Rapid Realization is separated admittedly, and riser 4 gets into the oil gas lines to gas phase from the top; Solid and partially liq drop in the solid bed bioreactor of what through tremie pipe 5, thereby realize reducing significantly the probability that oil gas carries coke powder.
Claims (2)
1. gas-liquid solid separation device; It is characterized in that comprising a gas-liquid-solid separator, a side of gas-liquid-solid separator is provided with mozzle, and mozzle extends to the inside of gas-liquid-solid separator; The upper end of gas-liquid-solid separator is provided with riser, and the lower end of housing is provided with tremie pipe.
2. gas-liquid solid separation device according to claim 1 is characterized in that the inner end of mozzle is provided with guide-leaf plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220184773 CN202605897U (en) | 2012-04-27 | 2012-04-27 | Gas-liquid-solid separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220184773 CN202605897U (en) | 2012-04-27 | 2012-04-27 | Gas-liquid-solid separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202605897U true CN202605897U (en) | 2012-12-19 |
Family
ID=47339630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220184773 Expired - Fee Related CN202605897U (en) | 2012-04-27 | 2012-04-27 | Gas-liquid-solid separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202605897U (en) |
-
2012
- 2012-04-27 CN CN 201220184773 patent/CN202605897U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202605897U (en) | Gas-liquid-solid separation device | |
| CN201930645U (en) | Spiral air-lift type steam separator | |
| CN203469506U (en) | Device for recycling waste heat of steam condensate of vacuum flash tank | |
| CN205398517U (en) | Processing apparatus behind aniline | |
| CN202724728U (en) | Methanol water fractionating tower reflowing system | |
| CN202356093U (en) | Waste heat recovery device for etherification tank | |
| CN103386286A (en) | Recyclable reaction vessel system | |
| CN203768293U (en) | Thin-layer gas collection dry distiller | |
| CN204219958U (en) | Flue gas cleaner | |
| CN204325292U (en) | New type water gas purification equipment | |
| CN204356288U (en) | A kind of weight hydrocarbon separation system | |
| CN202390379U (en) | Diesel oil hydrogenation desulfurization device | |
| CN202030682U (en) | Acylation reaction system | |
| CN203382719U (en) | Production line for cracking, distillation and regeneration of waste oil | |
| CN103396895A (en) | Method for preparing biodiesel from microalgae through ultrasonic-assisted direct ester exchange | |
| CN201719924U (en) | Simple tail gas separation device | |
| CN201855591U (en) | Oil-water separator | |
| CN203355324U (en) | Flash drum device | |
| CN203382532U (en) | Novel horizontal tower injection type deoxidization device | |
| CN203108254U (en) | Tail gas condensation and collection device applied to production of polyester resin | |
| CN203639422U (en) | Biomass gasifier | |
| CN202131293U (en) | Reaction device for synthesizing biological compound alcohol-based fuel | |
| CN201755421U (en) | Gas-liquid separator | |
| CN202116530U (en) | Reaction kettle for solid acid catalyst and pre-esterification of biodiesel and continuous recycling of carbinol | |
| CN105399056A (en) | Oxidation tower with heating device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121219 Termination date: 20200427 |