CN106606916A - Sulfur melting steam recovery and utilization apparatus - Google Patents
Sulfur melting steam recovery and utilization apparatus Download PDFInfo
- Publication number
- CN106606916A CN106606916A CN201510700244.5A CN201510700244A CN106606916A CN 106606916 A CN106606916 A CN 106606916A CN 201510700244 A CN201510700244 A CN 201510700244A CN 106606916 A CN106606916 A CN 106606916A
- Authority
- CN
- China
- Prior art keywords
- oxygen
- water pump
- pipe
- eliminating device
- recovery tank
- 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
- 238000011084 recovery Methods 0.000 title claims abstract description 32
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 229910052717 sulfur Inorganic materials 0.000 title claims abstract description 27
- 239000011593 sulfur Substances 0.000 title claims abstract description 27
- 230000008018 melting Effects 0.000 title abstract 3
- 238000002844 melting Methods 0.000 title abstract 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 54
- 238000010612 desalination reaction Methods 0.000 claims abstract description 19
- 230000005540 biological transmission Effects 0.000 claims description 3
- 208000031481 Pathologic Constriction Diseases 0.000 claims description 2
- 210000001215 vagina Anatomy 0.000 claims description 2
- 210000003437 trachea Anatomy 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 7
- 238000001914 filtration Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000005374 membrane filtration Methods 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention discloses a sulfur melting steam recovery and utilization apparatus, which comprises a recovery cylinder, a gas inlet pipe, a gas valve, a gas conveying pipe, a deaerator, a gas return pipe, a desalination water pool, and a water pump. Compared to the apparatus in the prior art, the apparatus of the present invention has the following characteristics that the structure is simple, the function is strong, and the sulfur melting tail gas can be recovered and re-utilized so as to avoid the waste of resources and save the production cost.
Description
Technical field
The present invention relates to a kind of recycle device, more particularly to a kind of molten sulfur steam circulation recovery
Using device.
Background technology
Need to be dissolved sulfur with high-temperature steam in sulphuric acid plant, and the tail gas after molten sulfur is direct
In entering air, and steam also has higher temperature, and condenses into water after steam is cooled down,
So as to the source stream for causing water is lost, so as to serious waste resource, increase production cost, in view of more than
Defect, is necessary in fact a kind of molten sulfur steam circulation recycle device of design.
The content of the invention
The technical problem to be solved is：A kind of molten sulfur steam circulation is provided and reclaims profit
Molten sulfur tail gas is solved with device to enter cause in air the wasting of resources, increase production cost
Problem.
To solve above-mentioned technical problem, the technical scheme is that：A kind of molten sulfur steam circulation
Recycle device, including recovery tank, air inlet pipe, air valve, appendix, oxygen-eliminating device, return-air
Pipe, desalination pond, water pump, described recovery tank is located at cylinder block, described air inlet pipe position
In recovery tank left end downside, described air inlet pipe is weldingly connected with recovery tank, described air valve position
In air inlet pipe top, described air valve is connected with air inlet pipe screw thread, and described appendix is located at back
Receive at cylinder top center, described appendix is weldingly connected with recovery tank, described oxygen-eliminating device position
In appendix right-hand member, described oxygen-eliminating device is connected with gas transmission pipe screw thread, and described muffler is located at
At oxygen-eliminating device top center, described muffler is connected with oxygen-eliminating device screw thread, described desalted water
Pond is located at oxygen-eliminating device right-hand member, and described water pump is located at desalination pond left end bottom, described water pump
It is connected with desalination pond screw thread, and described water pump is connected with recovery tank and oxygen-eliminating device pipeline.
Further, described desalination pond contain shell, semi-transparent film filter, the second water pump,
Water-supply-pipe.
Further, described shell is located at oxygen-eliminating device right-hand member, and described shell is square cylinder body.
Further, described semi-transparent film filter is located at enclosure, described semi-transparent membrane filtration
Device is connected with outer casing screw.
Further, the second described pump shell right-hand member bottom, described the second water pump and shell
Screw thread is connected.
Further, described water-supply-pipe is located at the second water pump right-hand member, described water-supply-pipe and second
Water pump screw thread is connected.
Compared with prior art, the molten sulfur steam circulation recycle device, is first turned on air valve,
So that molten sulfur tail gas is entered in recovery tank by air inlet pipe, steam passes through gas transmission in recovery tank
In pipe input oxygen-eliminating device, and steam condensation Cheng Shuihou can be accumulated in recovery tank bottom, and enter and remove
Steam in oxygen device is removed by oxygen-eliminating device and pass through after oxygen in devaporation muffler directly by steam
In conveying melt back sulfur equipment, and some vapor can be accumulated in oxygen-eliminating device in the water that oxygen-eliminating device is condensed into
Bottom, then the water of recovery tank and oxygen-eliminating device bottom is pumped in desalination pond by water pump, pass through
Semi-transparent film filter by water filtration, so as to the salt in water be filtered so that through semi-transparent membrane filtration
Salt is not contained in the water of device, the water after filtration is pumped in water-supply-pipe by the second water pump, then by defeated
Water is transmitted back to firing equipment and is heated into steam and is being conveyed to molten sulfur equipment, the apparatus structure by water pipe
Simply, it is powerful, molten sulfur tail gas recycle can be re-used, so as to avoid the wasting of resources,
Production cost is saved.
Description of the drawings
Fig. 1 is the front view of molten sulfur steam circulation recycle device
Fig. 2 is the sectional view in desalination pond
The air inlet pipe 2 of recovery tank 1
The appendix 4 of air valve 3
The muffler 6 of oxygen-eliminating device 5
The water pump 8 of desalination pond 7
The semi-transparent film filter 702 of shell 701
The water-supply-pipe 704 of second water pump 703
Specific embodiment
Hereinafter, various specific details are elaborated, to provide to constituting described embodiment
The thorough understanding of the concept on basis.However, it will be apparent to those skilled in the art that institute
The embodiment of description can be in the case of without some or all in these specific details
To put into practice.In other cases, well-known process step is not specifically described.
As shown in Figure 1 and Figure 2, including recovery tank 1, air inlet pipe 2, air valve 3, appendix 4,
Oxygen-eliminating device 5, muffler 6, desalination pond 7, water pump 8, shell 701, semi-transparent film filter
702nd, the second water pump 703, water-supply-pipe 704, described recovery tank 1 is located at cylinder block, institute
The air inlet pipe 2 stated is located at the left end of recovery tank 1 downside, and described air inlet pipe 2 is welded with recovery tank 1
Connect connected, described air valve 3 is located at the top of air inlet pipe 2, described air valve 3 and air inlet pipe 2
Screw thread is connected, and described appendix 4 is located at the top center of recovery tank 2, described appendix
4 are weldingly connected with recovery tank 2, and described oxygen-eliminating device 5 is located at the right-hand member of appendix 4, described
Oxygen-eliminating device 5 is connected with the stricture of vagina of appendix spiral shell 4, and described muffler 6 is located in the top of oxygen-eliminating device 5
At the heart, described muffler 6 is connected with the screw thread of oxygen-eliminating device 5, and described desalination pond 7 is located at
The right-hand member of oxygen-eliminating device 5, described water pump 8 is located at the left end bottom of desalination pond 7, described water pump
8 are connected with the screw thread of desalination pond 7, and described water pump 8 and recovery tank 1 and oxygen-eliminating device pipe 5
Road is connected, described desalination pond 1 contain shell 701, semi-transparent film filter 702, the
Two water pumps 703, water-supply-pipe 704, described shell 701 is located at the right-hand member of oxygen-eliminating device 5, described
Shell 701 be square cylinder body, described semi-transparent film filter 702 is located inside shell 701,
Described semi-transparent film filter 702 is connected with the screw thread of shell 701, the second described water pump 703
The right-hand member bottom of shell 701, the second described water pump 703 is connected with the screw thread of shell 701, described
Water-supply-pipe 704 be located at the right-hand member of the second water pump 703, the described water pump of water-supply-pipe 704 and second
703 screw threads are connected, and the molten sulfur steam circulation recycle device is first turned on air valve 3, makes
Sulfur tail gas must be melted to enter in recovery tank 1 by air inlet pipe 2,1 steam passes through in recovery tank
In the input oxygen-eliminating device 5 of appendix 4, and steam condensation Cheng Shuihou can be accumulated in the bottom of recovery tank 1,
And enter in oxygen-eliminating device 5 steam and removed in devaporation after oxygen by muffler by oxygen-eliminating device 5
6 directly convey steam in melt back sulfur equipment, and the water that some vapor is condensed in oxygen-eliminating device 5
Can be accumulated in the bottom of oxygen-eliminating device 5, then by water pump 8 by recovery tank 1 and the bottom of oxygen-eliminating device 5
Water is pumped in desalination pond 7, by semi-transparent film filter 702 by water filtration, so as to by water
Salt filter so that do not contain salt through in the water of semi-transparent film filter 702, the water after filtration
Pumped in water-supply-pipe 704 by the second water pump 703, then water is transmitted back to by water-supply-pipe 704 plus
Hot equipment is heated into steam and is being conveyed to molten sulfur equipment, and wherein shell 701 is storage steam cooling
The water of condensation, and shell 701 is the installation of the water pump 703 of semi-transparent film filter 702 and second
Carrier.
Embodiment described above is only that the preferred embodiment of the present invention is described, and
It is non-that the spirit and scope of the present invention are defined.In the premise without departing from design concept of the present invention
Under, various modifications and improvement that this area ordinary person makes to technical scheme,
Protection scope of the present invention should be dropped into.
Claims (6)
1. a kind of molten sulfur steam circulation recycle device, it is characterised in that including recovery tank, enter
Trachea, air valve, appendix, oxygen-eliminating device, muffler, desalination pond, water pump, described returns
Receive cylinder and be located at cylinder block, described air inlet pipe is located at recovery tank left end downside, described air inlet
Pipe is weldingly connected with recovery tank, and described air valve is located at the top of air inlet pipe, described air valve with enter
Gas-pipe thread is connected, and described appendix is located at recovery tank top center, described appendix
Be weldingly connected with recovery tank, described oxygen-eliminating device is located at appendix right-hand member, described oxygen-eliminating device with
Gas transmission pipe screw thread is connected, and described muffler is located at oxygen-eliminating device top center, described return-air
Pipe is connected with oxygen-eliminating device screw thread, and described desalination pond is located at oxygen-eliminating device right-hand member, described water pump
Positioned at desalination pond left end bottom, described water pump is connected with desalination pond screw thread, and described
Water pump is connected with recovery tank and oxygen-eliminating device pipeline.
2. a kind of molten sulfur steam circulation recycle device as claimed in claim 1, its feature
It is that described desalination pond contains shell, semi-transparent film filter, the second water pump, water-supply-pipe.
3. a kind of molten sulfur steam circulation recycle device as claimed in claim 2, it is special
It is that described shell is located at oxygen-eliminating device right-hand member to levy, and described shell is square cylinder body.
4. a kind of molten sulfur steam circulation recycle device as claimed in claim 3, it is special
It is that described semi-transparent film filter is located at enclosure to levy, described semi-transparent film filter with it is outer
Shell screw thread is connected.
5. a kind of molten sulfur steam circulation recycle device as claimed in claim 4, it is special
It is the second described pump shell right-hand member bottom to levy, described the second water pump and outer casing screw phase
Even.
6. a kind of molten sulfur steam circulation recycle device as claimed in claim 5, it is special
It is that described water-supply-pipe is located at the second water pump right-hand member to levy, described water-supply-pipe and the second water pump spiral shell
Stricture of vagina is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510700244.5A CN106606916A (en) | 2015-10-26 | 2015-10-26 | Sulfur melting steam recovery and utilization apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510700244.5A CN106606916A (en) | 2015-10-26 | 2015-10-26 | Sulfur melting steam recovery and utilization apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106606916A true CN106606916A (en) | 2017-05-03 |
Family
ID=58613383
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510700244.5A Pending CN106606916A (en) | 2015-10-26 | 2015-10-26 | Sulfur melting steam recovery and utilization apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106606916A (en) |
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| CN104989607A (en) * | 2015-06-08 | 2015-10-21 | 青海中控太阳能发电有限公司 | Steam power generation system for solar thermal power generation and pipe warming method of system |
| CN205216499U (en) * | 2015-10-26 | 2016-05-11 | 安徽华尔泰化工股份有限公司 | Melt sulphur steam circulation recycle device |
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2015
- 2015-10-26 CN CN201510700244.5A patent/CN106606916A/en active Pending
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| CN201507917U (en) * | 2009-09-25 | 2010-06-16 | 湖北华强化工集团有限公司 | Exhaust recovery device of deaerator |
| CN101660463A (en) * | 2009-09-25 | 2010-03-03 | 中能纪（北京）国际科技有限公司 | Waste heat utilization and emission reduction device used for tail gas of oil drilling power combustion engine |
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| CN202470683U (en) * | 2011-12-28 | 2012-10-03 | 奎克化学（中国）有限公司 | Steam condensate water recycling device for drying room |
| CN202546730U (en) * | 2012-04-01 | 2012-11-21 | 浙江航民股份有限公司 | Atmospheric deoxidation system capable of recovering exhaust steam |
| CN103787279A (en) * | 2012-11-01 | 2014-05-14 | 天津渤大硫酸工业有限公司 | Molten sulfur exhausted steam recovering device and application method thereof |
| CN103499089A (en) * | 2013-09-25 | 2014-01-08 | 济南澳海炭素有限公司 | Exhaust steam recycling heating device for waste heat power generation deaerator |
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| PB01 | Publication | ||
| PB01 | Publication | ||
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Application publication date: 20170503 |