CN201197927Y - Low-voltage gas transport equipment of refinery desulfurizer - Google Patents
Low-voltage gas transport equipment of refinery desulfurizer Download PDFInfo
- Publication number
- CN201197927Y CN201197927Y CNU2008200216595U CN200820021659U CN201197927Y CN 201197927 Y CN201197927 Y CN 201197927Y CN U2008200216595 U CNU2008200216595 U CN U2008200216595U CN 200820021659 U CN200820021659 U CN 200820021659U CN 201197927 Y CN201197927 Y CN 201197927Y
- Authority
- CN
- China
- Prior art keywords
- pressure gas
- low
- low pressure
- equipment
- transfer pipeline
- 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
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model relates to low-press gas conveyer equipment for a regeneration tower of a desulfurizing installation in a refinery, belonging to the technical field of desulfurizing equipment in the refinery. The low-press gas conveyer equipment comprises a regeneration tower and an acidulous water stripping tower, wherein, a low-pressure gas conveying pipeline is arranged at the top of the regeneration tower, and a pressure control valve is arranged on the low-pressure gas conveying pipeline; a high-pressure gas conveying pipeline is arranged at the top of the acidulous water stripping tower. The low-press gas conveyer equipment is characterized in that pressurized equipment is also arranged on the low-pressure gas conveying pipeline; the high-pressure gas conveying pipeline has two branched pipelines, wherein, one branched pipeline is connected with the pressurized equipment, and the other branched pipeline is transported to a torch. The utility model utilizes the high-pressure gas of the acidulous water stripping tower as power to pressurize the low-pressure gas so as to meet the requirement for long-distance conveying of the low-pressure gas, and pipelines with smaller caliber can be adopted for conveying the low-pressure gas to save a great deal of rolled steels.
Description
Technical field
The utility model patent is to refinery's sulfur removal technology equipment technical field, is specifically related to a kind of refinery desulfurizer regenerator low pressure gas conveying equipment.
Background technology
Desulfurizer is one of important desulfurization facility of oil plant, the principle of desulfurizer is the diethanol amine doctor treatment that adopts in the wet type desulfurizing method, sulfur-bearing dry gas, liquefied gas in each cover oil refining apparatus are introduced desulfurizing tower, make itself and desulfurization solvent generation chemical reaction at low temperatures, remove sulfur dioxide and carbon dioxide in dry gas, the liquefied gas, the dry gas of output clean from sulfur and liquefied gas.Device mainly partly is made up of dry gas desulfurization, desulfuration of liquefied gas and solvent reclamation etc.Through dry gas and liquefied gas after the desulfurization processing, hydrogen sulfide content can be reduced to below the 50PPm.Because solvent reclamation partial regeneration cat head low pressure gas pressure is low, carries for long distance and brought certain difficulty, and carry the pipeline bore of low pressure gas very big.
Summary of the invention
The purpose of this utility model is for solving low pressure gas length apart from transportation problem, a kind of refinery desulfurizer regenerator low pressure gas conveying equipment is provided, its main points are to increase pressurized equipment on the low pressure gas transfer pipeline, and the high pressure gas of employing soul water stripper is as the power of pressurized equipment, after the low pressure gas pressurization, long distance is carried and can be adopted the less pipeline of bore.
The following technical scheme of the concrete employing of the utility model:
A kind of refinery desulfurizer regenerator low pressure gas conveying equipment comprises regenerator, soul water stripper, and regeneration overhead is provided with the low pressure gas transfer pipeline, and the low pressure gas transfer pipeline is provided with pressure-control valve; Soul water stripper top is provided with the high pressure gas transfer pipeline, it is characterized in that, also is provided with pressurized equipment on described low pressure gas transfer pipeline, and described high pressure gas transfer pipeline is by two branch lines, and one is connected with pressurized equipment, and one is delivered to torch.
Described pressurized equipment comprises high pressure gas import, low pressure gas import, the high pressure gas import is connected with carrier pipe, the carrier pipe front end is provided with nozzle, the low pressure gas import is arranged on the sidewall of pressurized equipment, the pressurized equipment front portion also is provided with mixing chamber, mixes the continuation conveying of pressurization back with low pressure gas from the high pressure gas that nozzle goes out.
For the ease of control, the preferred scheme of the utility model is as follows:
Between pressurized equipment and control valve, be provided with flowmeter on the low pressure gas transfer pipeline, be respectively equipped with temperature control valve, high pressure draught control valve on two branch lines of high pressure gas transfer pipeline.
Compared with prior art, the utlity model has following beneficial effect: 1) after the low pressure gas supercharging, can satisfy the requirement that long distance is carried, but also can adopt the little pipeline of bore, can save great deal of steel; 2) pressurized equipment of the present utility model can produce swabbing action to low pressure gas, and the discharging of low pressure gas is more prone to; 3) flow of the utility model low pressure gas is controlled the amount that high pressure gas is advanced supercharging equipment by control valve, and unnecessary high pressure gas can reach the purpose of control regeneration overhead temperature by the control valve torch of setting fire.
Description of drawings
Fig. 1 is a prior art desulfurizer regenerator low pressure gas conveying equipment annexation schematic diagram;
Fig. 2 is the utility model desulfurizer regenerator low pressure gas conveying equipment annexation schematic diagram;
Fig. 3 is the structural representation of the utility model pressurized equipment.
Among the figure, 1 is soul water stripper top temperature control valve, 2 is the regeneration overhead pressure-control valve, and 3 for advancing pressurized equipment high pressure draught control valve, and 4 is soul water stripper, 5 is regenerator, 6 for pressurized equipment, 6-1 are that high pressure gas import, 6-2 are that carrier pipe, 6-3 are that nozzle, 6-4 are the low pressure gas import, and 6-5 is a mixing chamber, and 7 is flowmeter, 8 is the low pressure gas transfer pipeline, and 9 is the high pressure gas transfer pipeline.
The specific embodiment
Embodiment
As shown in Figure 2, a kind of refinery desulfurizer regenerator low pressure gas conveying equipment, comprise regenerator 5, soul water stripper 4, regenerator 5 cats head are provided with low pressure gas transfer pipeline 8, low pressure gas transfer pipeline 8 is provided with regeneration overhead pressure-control valve 2, on transfer pipeline 8, also be provided with pressurized equipment 6, be provided with flowmeter 7 between pressurized equipment 6 and the pressure-control valve 2; Soul water stripper 4 cats head are provided with high pressure gas transfer pipeline 9, and high pressure gas transfer pipeline 9 has two branch lines, and one is connected with pressurized equipment 6, which is provided with high pressure draught control valve 3, and another is delivered to torch, which is provided with tower top temperature control valve 1.
As shown in Figure 3, described pressurized equipment 6 comprises high pressure gas import 6-1, low pressure gas import 6-4, and high pressure gas import 6-1 is connected with carrier pipe 6-2, and carrier pipe 6-2 front end is provided with nozzle 6-3, low pressure gas import 6-4 is arranged on the sidewall of pressurized equipment 6, and the pressurized equipment front portion also is provided with mixing chamber 6-5.
The utility model by regulate, metering low pressure gas flow, can control flow as the high pressure gas of power, simultaneously, the surplus of the high pressure gas torch that reduces internal heat can guarantee the pressure and temperature of soul water stripper 4 like this.
Comparative Examples
As shown in Figure 1, the low pressure gas conveying equipment of prior art is: the low pressure gas of regenerator 5 is by pipeline 8, and soul water stripper 4 is carried by 9 fens two-way of high pressure gas pipeline.Because the gas pressure of low pressure gas is low, the therefore general bigger pipeline of bore that adopts is carried.
Claims (3)
1. refinery's desulfurizer regenerator low pressure gas conveying equipment comprises regenerator, soul water stripper, and regeneration overhead is provided with the low pressure gas transfer pipeline, and the low pressure gas transfer pipeline is provided with pressure-control valve; Soul water stripper top is provided with the high pressure gas transfer pipeline, it is characterized in that also be provided with pressurized equipment on described low pressure gas transfer pipeline, described high pressure gas transfer pipeline has two branch lines, and one is connected with pressurized equipment, and one is delivered to torch.
2. refinery according to claim 1 desulfurizer regenerator low pressure gas conveying equipment, it is characterized in that, described pressurized equipment comprises high pressure gas import, low pressure gas import, the high pressure gas import is connected with carrier pipe, front end is provided with nozzle, the low pressure gas import is arranged on the sidewall of pressurized equipment, and the pressurized equipment front portion also is provided with mixing chamber.
3. refinery according to claim 1 desulfurizer regenerator low pressure gas conveying equipment, it is characterized in that, between pressurized equipment and pressure-control valve, be provided with flowmeter on the low pressure gas transfer pipeline, be respectively equipped with temperature control valve, high pressure draught control valve on two branch lines of high pressure gas transfer pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200216595U CN201197927Y (en) | 2008-04-30 | 2008-04-30 | Low-voltage gas transport equipment of refinery desulfurizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200216595U CN201197927Y (en) | 2008-04-30 | 2008-04-30 | Low-voltage gas transport equipment of refinery desulfurizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201197927Y true CN201197927Y (en) | 2009-02-25 |
Family
ID=40449082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200216595U Expired - Fee Related CN201197927Y (en) | 2008-04-30 | 2008-04-30 | Low-voltage gas transport equipment of refinery desulfurizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201197927Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101554564B (en) * | 2009-05-06 | 2012-01-11 | 山东金诚石化集团有限公司 | Method and device for preventing flare gas compressor and pipeline from being blocked and incrusted with salt |
-
2008
- 2008-04-30 CN CNU2008200216595U patent/CN201197927Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101554564B (en) * | 2009-05-06 | 2012-01-11 | 山东金诚石化集团有限公司 | Method and device for preventing flare gas compressor and pipeline from being blocked and incrusted with salt |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101670231B (en) | Device and process for converting calcium process desulfurization into temperature difference crystallizing ammonia process desulfurization | |
| CN104888599B (en) | Spray drying desulfurizer used for cement plant and process method | |
| CN205127729U (en) | Novel wet flue gas desulfurization system supplies thick liquid device | |
| CN102720947B (en) | Liquid ammonia gasifying system and gasifying process thereof | |
| CN102548642A (en) | Process for sulfur removal from refinery off gas | |
| CN102844275A (en) | Integrated process for treating refinery waste water, containing ammonia and hydrogen sulphide, and refinery exhaust acid gas containing hydrogen sulphide | |
| CN201197927Y (en) | Low-voltage gas transport equipment of refinery desulfurizer | |
| CN105457478A (en) | Cement kiln smoke ammonia desulfurization system and method | |
| CN109054893B (en) | System for hydrogen purification and wax oil hydrogenation coupling in coal hydrogen production | |
| CN104119946A (en) | Catalytic cracking flue gas desulfurization and acid gas treatment process | |
| CN104745238A (en) | Improved alkali source system of desulfurization process of coking plant | |
| CN109276982A (en) | A kind of method of fuel gas anaerobic organism desulfurization | |
| CN106335876A (en) | Purification device for sulfur-containing conversion gases | |
| CN209144092U (en) | Nitrogen fertilizer plant's energy-saving natural gas desulphurization system | |
| CN206599546U (en) | Anaerobic integrated methane gas bio-desulfurization device | |
| CN203382730U (en) | Negative pressure desulfurization equipment for coke oven gas | |
| CN100425324C (en) | Top-push decreasing gas desulfurization at normal-pressure and apparatus thereof | |
| CN112852504A (en) | System and process for prolonging service life of blast furnace gas fine desulfurization reactant | |
| CN208266129U (en) | Top of Vacuum Tower gas circulation desulfurizing device | |
| CN206666473U (en) | Coke oven gas desulfurization hydro-conversion system | |
| CN209872642U (en) | Synthetic ammonia low transformation gas technology condensate purification treatment system | |
| CN215138548U (en) | Ammonia spraying and desulfurizing device for dry quenching flue gas | |
| CN204569839U (en) | A kind of high nitrogen low-sulfur raw material oil hydrogenation emission-reducing system | |
| CN109251771B (en) | Process and device for desulfurization and decyanation by catalyst method | |
| CN202465605U (en) | Condensate oil desulfurizing and deodorizing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090225 |