CN203615356U - Gasification system of liquefied petroleum gas - Google Patents
Gasification system of liquefied petroleum gas Download PDFInfo
- Publication number
- CN203615356U CN203615356U CN201320826716.8U CN201320826716U CN203615356U CN 203615356 U CN203615356 U CN 203615356U CN 201320826716 U CN201320826716 U CN 201320826716U CN 203615356 U CN203615356 U CN 203615356U
- Authority
- CN
- China
- Prior art keywords
- barrel
- water
- gasification
- kiln
- gasifying
- 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
- 238000002309 gasification Methods 0.000 title claims abstract description 40
- 239000003915 liquefied petroleum gas Substances 0.000 title abstract 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 70
- 239000007789 gas Substances 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 239000002918 waste heat Substances 0.000 claims abstract description 7
- 238000010521 absorption reaction Methods 0.000 claims description 25
- 230000003020 moisturizing effect Effects 0.000 claims description 19
- 239000013589 supplement Substances 0.000 claims description 12
- 238000007789 sealing Methods 0.000 claims description 5
- 230000005611 electricity Effects 0.000 abstract description 3
- 239000002737 fuel gas Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000008399 tap water Substances 0.000 abstract 1
- 235000020679 tap water Nutrition 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 2
- 238000013024 troubleshooting Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Images
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The utility model relates to the technical field of gasification systems and discloses a gasification system of liquefied petroleum gas. The gasification system comprises a gasification barrel which uses water to heat and gasify liquefied petroleum gas, then the heated and gasified liquefied petroleum gas is processed and used by a kiln, a gas delivery pipe is arranged in the gasification barrel, a heat absorbing barrel which absorbs waste heat in the kiln and then provides the waste heat to water in the gasification barrel for automatic heating is connected with the gasification barrel through a pipeline, the gasification barrel is mounted on one side above the heat absorbing barrel and located outside the kiln, a water adding port is disposed at the upper end of the gasification barrel, a water adding trough which automatically adds water to the gasification barrel when low water level and water shortage of the gasification barrel occur is connected with the water adding port through a pipeline, the water adding trough is located at a position of one side above the gasification barrel, an automatic liquid level control device is installed in the water adding trough, and the automatic liquid level control device is connected with an external tap water pipe. The gasification system of the liquefied petroleum gas has the advantages that the electricity and equipment spending is saved, failure process of equipment is reduced, normal gasification of kiln fuel gas and long-time normal operation of gasification equipment are guaranteed, and energy is saved.
Description
Technical field
The utility model relates to the technical field of gasification system, refers in particular to a kind of gasification system that utilizes using residual heat from kiln furnace to gasify to oil liquefied gas by siphon principle.
Background technology
Traditional gasification bucket is to adopt common water heater by water pump, and circulation is heated the water in gasification bucket, makes water reach the gasification temperature of oil liquefied gas, makes oil liquefied gas gasification.Water heater and the water pump of this type of gasification bucket easily break down, the bucket that causes gasifying cannot normally be worked, maintenance difficult, often need to be serviced, to guarantee the normal use of gasification bucket, and the use of water heater and water pump, all need to realize by power supply, to guarantee the normal use of equipment, once run into power failure, equipment cannot normally be worked, affect manufacturing schedule, in addition, user is in the input of equipment and the expense of electricity consumption, also need the higher cost of cost, this has increased burden in use to undoubtedly user in manpower and materials fund.
Summary of the invention
The purpose of this utility model is to overcome weak point of the prior art and gasification system that a kind of oil liquefied gas is provided, and this device can automatic water supplement, guarantees that the equipment such as kiln can normal work in 24 hours, reduces troubleshooting, saves the energy, reduces production costs.
For achieving the above object, the utility model adopts following technical scheme:
A kind of gasification system of oil liquefied gas, it comprises the gasifying barrel that a water heating and gasifying oil liquefied gas uses for kiln processing, the built-in appendix of gasifying barrel, described gasifying barrel connects a heat absorption bucket that absorbs waste heat in kiln and be supplied to the water automatic heating in gasifying barrel by pipeline, this gasifying barrel is arranged on top one side of heat absorption bucket and in kiln outside, gasifying barrel upper end is provided with water supplement port, water supplement port connects one when gasifying barrel low water level and lack of water are to the moisturizing groove of its automatic water supplement by pipeline, the position of this moisturizing groove side above gasifying barrel, the built-in liquid-level auto-control device of moisturizing groove, this liquid-level auto-control device connects an external running water pipe.
Described gasifying barrel is arranged on kiln outside, the upper and lower side that this gasifying barrel connects heat absorption bucket one side is respectively equipped with the first input port and the first delivery outlet, upper and lower side at heat absorption bucket is respectively equipped with the second input port and the second delivery outlet, the second delivery outlet is connected by pipeline with the first input port, and the second input port is also connected by pipeline with the first delivery outlet.
The sealing of described heat absorption bucket is arranged on the inside that kiln moves back warm section.
Described liquid-level auto-control device comprises that the ball valve, of a connection running water pipe is opened or the free arm and of closing ball valve is followed the ball float that water level rises or declines, and ball float is connected with ball valve by free arm.
Described appendix is provided with two mouths of pipe that stretch out gasifying barrel, and wherein one end mouth of pipe connects oil liquefied gas by pipeline, and this appendix other end mouth of pipe is connected on kiln by pipeline.
The beneficial effects of the utility model are: it absorbs the waste heat in kiln by the water that is sealed in the heat absorption bucket in kiln, and these water are transported in gasifying barrel, make water in gasifying barrel reach the gasification temperature of oil liquefied gas, gasification oil liquefied gas, use with the processing of supply kiln, take full advantage of the heat energy producing in kiln production process, save the use of water heater arrangement, coordinate the moisturizing effect of moisturizing groove, and in conjunction with the moisturizing control of liquid-level auto-control device in moisturizing groove, equipment can be realized on the basis of automatic water supplement, also avoid water waste, save the use of common water heater and water pump, save the spending of electricity consumption and equipment, from being heated to moisturizing link, save the input of equipment, reduce the troubleshooting of equipment, both the normal gasification and the equipment for gasification that had guaranteed kiln combustion gas can normally be worked for a long time, save again the energy.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
Below in conjunction with Figure of description, the utility model is described in further detail:
As shown in Figure 1, the utility model is about a kind of gasification system of oil liquefied gas, and it comprises the gasifying barrel 1 that a heating and gasifying oil liquefied gas uses for kiln processing, the built-in appendix 2 of gasifying barrel 1.
As shown in Figure 1, gasifying barrel 1 connects a heat absorption bucket 3 by pipeline 5, heat absorption bucket 3 absorbs waste heat in kiln, and utilize siphon principle to be supplied to the water Automatic-heating in gasifying barrel 1, this gasifying barrel 1 is arranged on top one side of heat absorption bucket 3 and in kiln outside, gasifying barrel 1 upper end is provided with water supplement port 11, water supplement port 11 connects one when gasifying barrel 1 low water level and lack of water are to the moisturizing groove 4 of its automatic water supplement by pipeline 5, the position of this moisturizing groove 4 side above gasifying barrel 1, the built-in liquid-level auto-control device 6 of moisturizing groove 4, this liquid-level auto-control device 6 connects an external running water pipe, moisturizing groove 4, gasifying barrel 1 and heat absorption bucket 3(are wherein, moisturizing groove 4, gasifying barrel 1 all contains running water with heat absorption bucket 3) be set in sequence in the position of differing heights, make that height of formation is poor to each other, be full of an inverted U-shaped pipeline 5(in the liquid of higher position and be called siphon pipe) afterwards, form vacuum, be opened on lower position, under this structure, in pipe, peak liquid moves toward low level mouth of pipe place under Action of Gravity Field, under action of vacuum, the liquid of the high-order mouth of pipe is sucked into peak, discharge to the other end, form siphonage, and then at gasifying barrel 1 or heat absorption bucket 3 water levels when too low, by moisturizing groove 4 to the direct moisturizing of gasifying barrel 1 or to the 3 indirect moisturizings of heat absorption bucket, with the normal work of assurance device.
Wherein, gasifying barrel 1 preferred size is φ 60 × 80CM, the preferred φ 7.8 of thermotank × (40～45) CM, the stainless steel cask of the 304# of the about 0.5CM of wall thickness, the second input port 31 of this thermotank and the second delivery outlet 32 are sealing state, it should be noted that, gasifying barrel 1 is only the preferred version of this specific embodiment with the aforementioned selection of thermotank, user can carry out optimum selecting to size, the material etc. of gasifying barrel 1 or heat absorption bucket 3 according to needs of production, does not give from limit at this.
As shown in Figure 1, wherein, the upper and lower side that gasifying barrel 1 connects heat absorption bucket 3 one sides is respectively equipped with the first input port 12 and the first delivery outlet 13, upper and lower side at heat absorption bucket 3 is respectively equipped with the second input port 31 and the second delivery outlet 32, the second delivery outlet 32 is connected by pipeline 5 with the first input port 12, and the second input port 31 is also connected by pipeline 5 with the first delivery outlet 13.
As shown in Figure 1,3 sealings of heat absorption bucket are arranged on the inside that kiln moves back warm section, and the waste heat producing to absorb kiln, reaches gasification temperature for the water in gasifying barrel 1.
As shown in Figure 1, liquid-level auto-control device 6 comprises the ball valve 61 of a connection running water pipe, the ball float 63 that a free arm 62 and of opening or closing ball valve 61 is followed water level rising or declined, ball float 63 is connected with ball valve 61 by free arm 62, ball float 63 all floats on waterborne all the time, and in the time that the water surface goes up, ball float 63 also and then rises, ball float 63 rises and just drives free arm 62 also to rise, in the time that ball float 63 rises to certain position, free arm 62 is propped the rubber piston pad of ball valve 61, sealing water source; In the time that water level declines, ball float 63 also declines, and free arm 62 drives again piston pad to open, and then reaches the effect of automatic water supplement, and avoids water waste, saves water source.
Appendix 2 is provided with two mouths of pipe that stretch out gasifying barrel 1, and wherein one end mouth of pipe connects oil liquefied gas by pipeline, and these appendix 2 other end mouths of pipe are connected on kiln by pipeline.
The gasification system of a kind of oil liquefied gas that the utility model discloses, its operation principle is: when the water of the heat absorption bucket 3 in kiln absorbs after using residual heat from kiln furnace, when water temperature reaches 100 ℃, the water of heat absorption bucket 3 is carried toward the top of gasifying barrel 1 automatically, gasifying barrel 1 cold water is below with potential difference, and the heat absorption bucket 3 in natural pressure supply kiln, completes a do action, go round and begin again, make water in gasifying barrel 1 reach the gasification temperature of oil liquefied gas.
The above is only to preferred embodiment of the present utility model; not scope of the present utility model is limited; therefore do not departing under the prerequisite of the utility model design spirit; equivalence that the common engineers and technicians in this area do structure described in the utility model, feature and principle changes or decorates, and all should fall in the protection domain that the utility model applies for a patent.
Claims (5)
1. the gasification system of an oil liquefied gas, it comprises the gasifying barrel that a water heating and gasifying oil liquefied gas uses for kiln processing, the built-in appendix of gasifying barrel, it is characterized in that: described gasifying barrel connects a heat absorption bucket that absorbs waste heat in kiln and be supplied to the water automatic heating in gasifying barrel by pipeline, this gasifying barrel is arranged on top one side of heat absorption bucket and in kiln outside, gasifying barrel upper end is provided with water supplement port, water supplement port connects one when gasifying barrel low water level and lack of water are to the moisturizing groove of its automatic water supplement by pipeline, the position of this moisturizing groove side above gasifying barrel, the built-in liquid-level auto-control device of moisturizing groove, this liquid-level auto-control device connects an external running water pipe.
2. gasification system according to claim 1, it is characterized in that: described gasifying barrel is arranged on kiln outside, the upper and lower side that this gasifying barrel connects heat absorption bucket one side is respectively equipped with the first input port and the first delivery outlet, upper and lower side at heat absorption bucket is respectively equipped with the second input port and the second delivery outlet, the second delivery outlet is connected by pipeline with the first input port, and the second input port is also connected by pipeline with the first delivery outlet.
3. gasification system according to claim 1 and 2, is characterized in that: the sealing of described heat absorption bucket is arranged on the inside that kiln moves back warm section.
4. gasification system according to claim 1, it is characterized in that: described liquid-level auto-control device comprises that the ball valve, of a connection running water pipe is opened or the free arm and of closing ball valve is followed the ball float that water level rises or declines, and ball float is connected with ball valve by free arm.
5. gasification system according to claim 1, is characterized in that: described appendix is provided with two mouths of pipe that stretch out gasifying barrel, and wherein one end mouth of pipe connects oil liquefied gas by pipeline, and this appendix other end mouth of pipe is connected on kiln by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320826716.8U CN203615356U (en) | 2013-12-16 | 2013-12-16 | Gasification system of liquefied petroleum gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320826716.8U CN203615356U (en) | 2013-12-16 | 2013-12-16 | Gasification system of liquefied petroleum gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203615356U true CN203615356U (en) | 2014-05-28 |
Family
ID=50767998
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320826716.8U Expired - Fee Related CN203615356U (en) | 2013-12-16 | 2013-12-16 | Gasification system of liquefied petroleum gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203615356U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114277450A (en) * | 2021-12-27 | 2022-04-05 | 黄瑞轮 | Intelligent vacuum infiltration device |
| CN117250999A (en) * | 2023-10-26 | 2023-12-19 | 广州环投增城环保能源有限公司 | An automatic water level control device and slag extractor for a waste incineration power plant |
-
2013
- 2013-12-16 CN CN201320826716.8U patent/CN203615356U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114277450A (en) * | 2021-12-27 | 2022-04-05 | 黄瑞轮 | Intelligent vacuum infiltration device |
| CN117250999A (en) * | 2023-10-26 | 2023-12-19 | 广州环投增城环保能源有限公司 | An automatic water level control device and slag extractor for a waste incineration power plant |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203615356U (en) | Gasification system of liquefied petroleum gas | |
| CN205710579U (en) | A kind of coke oven coke oven uprising tube automatic water-replenishing device | |
| CN203940237U (en) | Intelligent Double anti-leakage gas drainer | |
| CN203336226U (en) | Torch water-sealed tank liquid level pressure maintaining device | |
| CN201569739U (en) | Water hinge leakage circulating and recovering device | |
| CN203687009U (en) | Automatic water replenishing device of boiler water seal tank | |
| CN204005263U (en) | Anti-leakage gas drainage device | |
| CN202382459U (en) | Hydraulic suction closing type automatic water feeder for solar water heater | |
| CN203010573U (en) | Condensate water recovery device | |
| CN201934729U (en) | Gas check water seal valve | |
| CN201575304U (en) | Water cyclical utilization device for coal gas standpipe water seal | |
| CN204849936U (en) | Modified water heater cold water recycle in earlier stage device | |
| CN209068161U (en) | A kind of screw type wet gas cabinet of the water-saving freeze proof sealing water circulation system of band | |
| CN104154774A (en) | Condenser circulating water system capable of automatically exhausting air | |
| CN203052188U (en) | Self-control adjustment steam trap | |
| CN202580640U (en) | Leakage-free coal gas drainer | |
| CN202517326U (en) | Lubricating oil distribution device | |
| CN202531988U (en) | Float valve | |
| CN202625391U (en) | Thermal power plant adjacent furnace negative pressure powder bin emptying device | |
| CN201412826Y (en) | Pump-less self-pressure water filling boiler | |
| CN205444294U (en) | Simple and easy two ball -cock assembly water saving fixtures | |
| CN202692022U (en) | Overflow water seal device for low-temperature deaerator | |
| CN203216074U (en) | Water filling controller for solar water heaters | |
| CN204100589U (en) | The device of cold water in a kind of the automatic recovery hot water pipeline | |
| CN204202427U (en) | One can self-bleeding condenser circulation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20161024 Address after: 521000 Guangdong city of Chaozhou province Chaozhou Avenue North on the left Patentee after: Chaozhou Daxin Arts & Crafts Co., Ltd. Address before: 521031 Guangdong province Chaozhou Fengxi District Huai de Feng Dong Lu Ceramic Research Institute dormitory building 4, room 809 Patentee before: Wu Junjie |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140528 Termination date: 20181216 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |