CN209108650U - A kind of sulphur separator - Google Patents
A kind of sulphur separator Download PDFInfo
- Publication number
- CN209108650U CN209108650U CN201821648680.8U CN201821648680U CN209108650U CN 209108650 U CN209108650 U CN 209108650U CN 201821648680 U CN201821648680 U CN 201821648680U CN 209108650 U CN209108650 U CN 209108650U
- Authority
- CN
- China
- Prior art keywords
- sulphur
- helix tube
- bottom end
- runner
- separator box
- 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
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model discloses a kind of sulphur separators, including water pipe, the middle position of the water pipe is connected with water pump, and cooling cylinder is fixed on the right side of water pump, the inside of the cooling cylinder is equipped with helix tube, and the top of helix tube is provided with gas outlet, the bottom end of the helix tube is fixedly installed with air inlet, and the bottom end of air inlet is connected with the top of separator box, the inside left of the separator box is fixed with baffle, the inside left bottom end of the separator box is provided with gas access, and the top of gas access is connected with skewback, the helical structure that the utility model passes through helix tube, the Process Gas in sulphur separator is set thoroughly to condense, improve the separative efficiency of sulphur, condensed water is set to recycle trickling by water pump, reduce the waste of condensed water, liquid-state sulfur quick separating is enable by separator box simultaneously, Furthermore the deimpurity efficiency of liquid-state sulfur is improved by flusher, meets use demand.
Description
Technical field
The utility model relates to separator technical field, specially a kind of sulphur separator.
Background technique
Sulfur Gas Fields Gas Purification Factory can all be related to selexol process during handling natural gas and to de-
Sulphur out carries out Sulfur Recovery Procedure Gas, concrete technology flow process are as follows: and sour gas passes through burning forming process gas in combustion furnace,
The Process Gas for leaving acid gas burner enters waste heat boiler and carries out energy regenerating, and the Process Gas after having recycled energy enters one
Grade sulfur condenser is condensed, and the gaseous state sulphur in condenser internal procedure gas, which condenses out, to form liquid-state sulfur, then passes through
It crosses Sulphur sealer and enters molten sulfur sulphur tank.
Process Gas condensation at present in the actual production process in sulphur separator is not thorough enough, reduces point of sulphur
From efficiency, and condensed water needs continuous trickling that could cause the waste of condensed water, while mistake to Process Gas rapid condensation
Journey gas and condensed liquid-state sulfur position are not easy to the separation of liquid-state sulfur, furthermore the deimpurity effect of liquid-state sulfur at one
Rate is lower, and it is impossible to meet use demands.
Utility model content
The purpose of this utility model is to provide a kind of sulphur separators, to solve mistake mentioned above in the background art
The condensation of journey gas not enough thoroughly, the problem of being not easy to separation and liquid-state sulfur deimpurity low efficiency of liquid-state sulfur.
To achieve the above object, the utility model provides the following technical solutions: a kind of sulphur separator, including water pipe,
The middle position of the water pipe is connected with water pump, and cooling cylinder is fixed on the right side of water pump, the inside installation of the cooling cylinder
There is helix tube, and the top of helix tube is provided with gas outlet, the bottom end of the helix tube is fixedly installed with air inlet, and air inlet
Bottom end be connected with the top of separator box, the inside left of the separator box is fixed with baffle, and the inside of the separator box is left
Side bottom end is provided with gas access, and the top of gas access is connected with skewback, the inner right side bottom end peace of the separator box
Equipped with outlet, and the bottom end exported is provided with flusher, is connected with driving wheel on the right side of the flusher, and driving wheel
Top is connected with the output end of motor, and sealing ring is provided on the left of the driving wheel, and the bottom end of the flusher is fixed
There is carbon disulfide solution, the left side top of the separator box is fixed with control button.
Preferably, the flusher includes turntable, runner, connecting rod, communicating pipe, nozzle and belt, the turntable
Internal to be uniformly equipped with runner, and the surface of runner is connected with connecting rod, the connecting rod is internally provided with communicating pipe, described
The surface of connecting rod is uniformly fixed with nozzle, and the runner is coated with belt.
Preferably, the helix tube is three groups of helical form hollow structures, and gas outlet is socketed in inside the top of helix tube, and
Air inlet is socketed in the bottom inner portion of helix tube.
Preferably, the runner has three groups, and runner forms triangular structure, and the length between every two groups of runners is greater than company
The length of extension bar.
Preferably, the runner forms rotational structure by belt, and belt and driving wheel group are at rotational structure.
Preferably, the nozzle structure different for three groups of four directions, and the direction of two groups of nozzles and another group
Nozzle it is contrary.
Compared with prior art, the utility model has the beneficial effects that the spiral that the sulphur separator passes through helix tube
Structure enables the Process Gas in sulphur separator thoroughly to condense, and improves the separative efficiency of sulphur, makes to condense by water pump
Water energy enough recycles trickling, reduces the waste of condensed water, while making Process Gas and condensed liquid-state sulfur point by separator box
Work is clear, liquid-state sulfur can quick separating, the deimpurity efficiency of liquid-state sulfur is furthermore improved by flusher, is met
Use demand.
(1) device increases the contact area of Process Gas and condensed water by the helical structure of helix tube, makes sulphur point
It can thoroughly be condensed from the Process Gas in device, improve the separative efficiency of sulphur, condensed water recycle stream is enable by water pump
It drops down, reduces the waste of condensed water.
(2) device passes through separator box inner chamfer plate and baffle efficient combination, Process Gas and condensed liquid-state sulfur
Position is not together, and the division of labor is clear, and liquid-state sulfur being capable of quick separating.
(3) device enables liquid-state sulfur to spray the different directions to the inside of carbon disulfide solution by flusher,
The contact area of liquid-state sulfur Yu carbon disulfide solution is increased, the deimpurity efficiency of liquid-state sulfur is improved, meets use
Demand.
Detailed description of the invention
Fig. 1 is that the structure of the utility model faces diagrammatic cross-section；
Fig. 2 is the structure schematic top plan view of helix tube and gas outlet；
Fig. 3 is that the structure of flusher looks up diagrammatic cross-section.
In figure: 1, water pipe；2, water pump；3, cooling cylinder；4, helix tube；5, gas outlet；6, air inlet；7, it exports；8, it sprays
Device；801, turntable；802, runner；803, connecting rod；804, communicating pipe；805, nozzle；806, belt；9, motor；10, it is driven
Wheel；11, sealing ring；12, carbon disulfide solution；13, gas access；14, separator box；15, skewback；16, baffle；17, it controls
Button.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Fig. 1-3 is please referred to, a kind of embodiment provided by the utility model: a kind of sulphur separator, including water pipe 1, water
The middle position of pipe 1 is connected with water pump 2, and the right side of water pump 2 is fixed with cooling cylinder 3, and the inside of cooling cylinder 3 is equipped with spiral
Pipe 4, and the top of helix tube 4 is provided with gas outlet 5, it is preferred that helix tube 4 is three groups of helical form hollow structures, 5 sets of gas outlet
It connects inside the top of helix tube 4, and air inlet 6 is socketed in the bottom inner portion of helix tube 4, by the helical structure of helix tube 4,
The contact area of Process Gas and condensed water is increased, so that the Process Gas in sulphur separator is thoroughly condensed, improves sulphur
The separative efficiency of sulphur enables condensed water to recycle trickling by water pump 2, reduces the waste of condensed water, and the bottom end of helix tube 4 is solid
Dingan County is equipped with air inlet 6, and the bottom end of air inlet 6 is connected with the top of separator box 14, and the inside left of separator box 14 is fixed
There is baffle 16, the inside left bottom end of separator box 14 is provided with gas access 13, and the top of gas access 13 is connected with inclined-plane
The left side top of plate 15, the separator box 14 is fixed with control button 17.
The inner right side bottom end of separator box 14 is equipped with outlet 7, and the bottom end of outlet 7 is provided with flusher 8, preferably
, flusher 8 includes turntable 801, runner 802, connecting rod 803, communicating pipe 804, nozzle 805 and belt 806, turntable 801
Inside runner 802 is uniformly installed, and the surface of runner 802 is connected with connecting rod 803, it is preferred that runner 802 has three groups,
Runner 802 forms triangular structure, and the length between every two groups of runners 802 is greater than the length of connecting rod 803, it is preferred that turns
Wheel 802 forms rotational structure by belt 806, and belt 806 and driving wheel 10 form rotational structure, and runner 802 drives
Connecting rod 803 and nozzle 805 rotate, and three groups of runners 802 can cover bigger area, improve the efficiency of reaction, connecting rod 803
Be internally provided with communicating pipe 804, the surface of connecting rod 803 is uniformly fixed with nozzle 805, it is preferred that nozzle 805 be three group four
The different structure in a direction, and the direction of two groups of nozzles 805 is contrary with another group of nozzle 805, different directions
When nozzle 805 rotates, so that liquid-state sulfur is sprayed to the different directions inside carbon disulfide solution 12, increase reaction surface
Product, runner 802 are coated with belt 806, so that liquid-state sulfur is sprayed to carbon disulfide solution 12 by flusher 8
Internal different directions, increase the contact area of liquid-state sulfur Yu carbon disulfide solution 12, improve liquid-state sulfur except impurity
Efficiency, the right side of flusher 8 is connected with driving wheel 10, and the top of driving wheel 10 is connected with the output end of motor 9, pass
The left side of driving wheel 10 is provided with sealing ring 11, and sealing ring 11, which blocks air and enters, to be reduced air and influence on reaction bring,
The bottom end of flusher 8 is fixed with carbon disulfide solution 12.
Working principle: in use, operation control button 17 is powered by external power supply to whole device, Process Gas passes through gas
Body entrance 13 enters separator box 14, air inlet 6 is entered between skewback 15 and the gap of baffle 16, from the inside of helix tube 4
By the condensed water inside helix tube 4 condenses Process Gas, uses the condensate water circulatory inside water pipe 1 by water pump 2, mistake
Sulphur condensation in journey gas is flowed out at liquefaction sulphur from the bottom end of air inlet 6, and uncooled Process Gas is discharged from gas outlet 5, liquid
Change sulphur by baffle 16 and skewback 15, baffle 16 enters gas access with the structure barrier of skewback 15 liquefaction sulphur
13, it flows downward from the top of outlet 7, by the helical structure of helix tube 4, increases the contact surface of Process Gas and condensed water
Product, enables the Process Gas in sulphur separator thoroughly to condense, improves the separative efficiency of sulphur, make to condense by water pump 2
Water energy enough recycles trickling, reduces the waste of condensed water, while by skewback 15 and 16 efficient combination of baffle, Process Gas with it is cold
Liquid-state sulfur position after solidifying is not together, and the division of labor is clear, and liquid-state sulfur being capable of quick separating.
Outlet 7 is by the way that in 804 flow nozzle 805 of communicating pipe, the rotation of motor 9 drives driving wheel 10 to rotate, and 10 turns of driving wheel
Dynamic to drive three groups of runners 802 to rotate by belt 806, runner 802 drives nozzle 805 to rotate, and the nozzle 805 of different directions is turning
Liquid-state sulfur is sprayed to the different directions inside carbon disulfide solution 12 during dynamic, increases liquid-state sulfur and carbon disulfide
The contact area of solution 12 improves reaction efficiency, and liquid-state sulfur is dissolved in carbon disulfide solution 12, and impurity does not dissolve in curing
Carbon solution 12 is precipitated, and is improved the deimpurity efficiency of liquid-state sulfur, is improved the purity of sulphur, meet use demand.
It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and
And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this is practical new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this is practical new
The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing for the equivalent requirements of the claims will be fallen in
All changes in justice and range are embraced therein.It should not treat any reference in the claims as limiting
Related claim.
Claims (6)
1. a kind of sulphur separator, including water pipe (1), it is characterised in that: the middle position of the water pipe (1) is connected with water
It pumps (2), and is fixed with cooling cylinder (3) on the right side of water pump (2), the inside of the cooling cylinder (3) is equipped with helix tube (4), and spiral shell
The top of coil (4) is provided with gas outlet (5), and the bottom end of the helix tube (4) is fixedly installed with air inlet (6), and air inlet
(6) bottom end is connected with the top of separator box (14), and the inside left of the separator box (14) is fixed with baffle (16), described
The inside left bottom end of separator box (14) is provided with gas access (13), and the top of gas access (13) is connected with skewback
(15), the inner right side bottom end of the separator box (14) is equipped with outlet (7), and the bottom end for exporting (7) is provided with flusher
(8), it is connected with driving wheel (10) on the right side of the flusher (8), and the output end on the top of driving wheel (10) and motor (9)
It is connected, is provided with sealing ring (11) on the left of the driving wheel (10), the bottom end of the flusher (8) is fixed with curing
The left side top of carbon solution (12), the separator box (14) is fixed with control button (17).
2. a kind of sulphur separator according to claim 1, it is characterised in that: the flusher (8) includes turntable
(801), runner (802), connecting rod (803), communicating pipe (804), nozzle (805) and belt (806), the turntable (801)
Inside is uniformly equipped with runner (802), and the surface of runner (802) is connected with connecting rod (803), the connecting rod (803)
It is internally provided with communicating pipe (804), the surface of the connecting rod (803) is uniformly fixed with nozzle (805), the runner (802)
Be coated with belt (806).
3. a kind of sulphur separator according to claim 1, it is characterised in that: the helix tube (4) is three groups of spirals
Shape hollow structure, gas outlet (5) are socketed in inside the top of helix tube (4), and air inlet (6) is socketed in the bottom of helix tube (4)
End is internal.
4. a kind of sulphur separator according to claim 2, it is characterised in that: the runner (802) has three groups, runner
(802) triangular structure is formed, and the length between every two groups of runners (802) is greater than the length of connecting rod (803).
5. a kind of sulphur separator according to claim 2, it is characterised in that: the runner (802) passes through belt
(806) rotational structure is formed, and belt (806) and driving wheel (10) form rotational structure.
6. a kind of sulphur separator according to claim 2, it is characterised in that: the nozzle (805) is three groups four
The different structure in direction, and the direction of two groups of nozzles (805) is contrary with another group of nozzle (805).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821648680.8U CN209108650U (en) | 2018-10-11 | 2018-10-11 | A kind of sulphur separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821648680.8U CN209108650U (en) | 2018-10-11 | 2018-10-11 | A kind of sulphur separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209108650U true CN209108650U (en) | 2019-07-16 |
Family
ID=67200541
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821648680.8U Expired - Fee Related CN209108650U (en) | 2018-10-11 | 2018-10-11 | A kind of sulphur separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209108650U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112588074A (en) * | 2020-12-24 | 2021-04-02 | 扬州康龙环保工程有限公司 | Sulfur separation device |
| CN112604484A (en) * | 2020-12-24 | 2021-04-06 | 扬州康龙环保工程有限公司 | Neutralization reaction device for sulfur-containing acidic fluid |
| CN114105104A (en) * | 2021-12-27 | 2022-03-01 | 扬州康龙环保工程有限公司 | Coking sulfur purification device |
-
2018
- 2018-10-11 CN CN201821648680.8U patent/CN209108650U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112588074A (en) * | 2020-12-24 | 2021-04-02 | 扬州康龙环保工程有限公司 | Sulfur separation device |
| CN112604484A (en) * | 2020-12-24 | 2021-04-06 | 扬州康龙环保工程有限公司 | Neutralization reaction device for sulfur-containing acidic fluid |
| CN114105104A (en) * | 2021-12-27 | 2022-03-01 | 扬州康龙环保工程有限公司 | Coking sulfur purification device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209108650U (en) | A kind of sulphur separator | |
| CN100534587C (en) | Sintering smoke wet method sulphur removing and dust removing technology | |
| CN103252161B (en) | Renewable organic amine circulation desulfurization purification tower and renewable organic amine circulation desulfurization technology | |
| CN105617847B (en) | A kind of eddy flow coupling depth desulfurization reinforced module | |
| CN104084330A (en) | Two-stage atomizing nozzle for efficiently atomizing and nucleating desulfurization waste water in thermal power plant | |
| CN203002194U (en) | Turbulent ball turbocharged composite desulphurization dedusting tower | |
| CN1689968A (en) | Production method of refined sulfuric acid and production equipment thereof | |
| CN205576244U (en) | A smelt flue gas quench tower for dry process receipts arsenic | |
| CN102580504A (en) | Novel ammonia desulphurization absorption device | |
| CN206881311U (en) | Demisting separator | |
| CN202506306U (en) | Novel ammonia process desulfurization absorption device | |
| CN206980436U (en) | A kind of eddy flow phase transformation sieving flue gas desulfurization complementary energy reclaims integrated reactor | |
| CN1903414A (en) | Phosphorous ore, lime double circulation desulphurization and dust-removing process, and equipment therefor | |
| CN106943850A (en) | A kind of multi-functional subregion ammonia desulfuration equipment | |
| CN202161911U (en) | Flue gas treatment equipment | |
| CN206809915U (en) | A kind of pneumatic combined demisting separator of flat board | |
| CN103557436B (en) | A kind of desulphurization denitration activated coke regeneration gas cooling device and delivery method | |
| CN215479739U (en) | Venturi absorber tube for absorbing sulfur trioxide in sulfuric acid and plant for producing sulfuric acid | |
| CN103341274B (en) | In heat-engine plant wet desulfurization fume, moisture reclaims and gypsum rain controlling device and method | |
| CN208406113U (en) | A kind of calcination rotary kiln tail gas pre-concentration spent acid device | |
| CN113230831A (en) | System and method for washing, arsenic removal and purification of nonferrous smelting flue gas through adiabatic evaporation and cooling | |
| CN103030117B (en) | Recovering technology for waste acid | |
| CN108889098B (en) | Energy-saving ammonia process modified by gypsum-process desulfurization device | |
| CN102887486A (en) | Refined sulfuric acid absorption tower | |
| CN206817447U (en) | The dead steam recovery system of sulfuric acid apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190716 Termination date: 20211011 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |