CN1073683C - High-efficiency liquid chlorine gasifier capable of direct utilization of natural energy - Google Patents
High-efficiency liquid chlorine gasifier capable of direct utilization of natural energy Download PDFInfo
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- CN1073683C CN1073683C CN97119068A CN97119068A CN1073683C CN 1073683 C CN1073683 C CN 1073683C CN 97119068 A CN97119068 A CN 97119068A CN 97119068 A CN97119068 A CN 97119068A CN 1073683 C CN1073683 C CN 1073683C
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- liquid chlorine
- heating
- gasifying
- pipe
- chlorine
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Abstract
The present invention relates to a high-efficiency liquid chlorine gasifier capable of directly utilizing natural energy. A shell pipe type structure is adopted. Heating pipes are arranged in a multilayer intersection mode to form a heating gasifying pipe bundle. An array of nozzle plates is arranged on the upper part of the heating gasifying pipes. A liquid chlorine inlet is positioned on the upper part of a casing, and gasified chlorine outlet is positioned on the lower part of the casing. After led in the casing from the upper part, the liquid chlorine is evenly ejected on the heating gasifying pipes from the nozzles of the array nozzle plates and is heated and gasified into gas chlorine by the heating gasifying pipe bundle. Then, the gas chlorine is discharged from the gas outlet at the bottom of the casing. Because the gasification efficiency of the gasifier is high, rivers, streams, lakes or sea water in the nature can be directly used as energy sources to gasifying liquid chlorine. Therefore, energy consumption can be greatly reduced, and the gasification cost of the liquid chlorine can be greatly reduced.
Description
The present invention relates to a kind of gasification installation of liquid chlorine.Specifically provide the gasify vaporizer of liquid chlorine of a kind of energy that directly utilizes nature river, river, lake or seawater.
The liquid chlorine gasification device of present industrial use mainly contains two kinds, first shell pipe type liquid chlorine gasifier capable, and it is equivalent to a heat exchanger, and liquid chlorine is fed by the vaporizer bottom, is discharged by vaporizer top behind the tubulation heating and gasifying.Another kind is to be provided with the heating pipe that imports water vapor to heat with steam liquid chlorine is gasified in a jar that fills liquid chlorine.The gasification efficiency of above-mentioned this class device is low, and equipment volume is huge, and investment is big, and all needs to consume a large amount of energy, operating cost height.But, therefore still be used industrial at large because these legacy equipments are relatively simple for structure, with low content of technology.
The purpose of this invention is to provide a kind of high-efficiency liquid chlorine gasifier capable that can directly utilize the nature energy.The gasification efficiency height of this device, it can directly utilize natural river, river, lake or seawater to make liquid chlorine vaporizing as the energy, therefore can greatly reduce power consumption, reduces the liquid chlorine vaporizing cost significantly.
High-efficiency liquid chlorine gasifier capable of the present invention is still takes the shell pipe type structure, many heating pipes promptly are set in the vaporizer housing, it is characterized in that heating pipe is the heating and gasifying pipe family of arranging with the multilayer cross modal, one array nozzle plate is arranged at the superiors heating and gasifying pipe top, the liquid chlorine inlet is positioned at housing top, and the outlet of gasification chlorine is positioned at lower housing portion; After liquid chlorine feeds housing by top, evenly be injected on the heating and gasifying pipe, vertically be parallel to each other, after cross section becomes the heating pipe family heat air of cross modal to change into gas chlorine, discharge by the gas outlet of housing bottom through many rows by the nozzle of array nozzle plate; With natural water resources, for example river, river, lake or seawater in the pipeline of the heating and gasifying pipe bottom pumping into, and successively to the circulation of top tubulation, are discharged by the outlet of top heating and gasifying pipe at last by suction booster.
In vaporizer of the present invention, because the heating and gasifying tubulation is to be cross section to intersect, the tubulation family of multi-layer structure, liquid chlorine evenly is ejected on the gasifying pipe from top to bottom by array nozzle plate, contacts with the multilayer tubulation in the process that flows downward, fully carry out heat exchange, have very high gasification efficiency, so the water resources that can directly utilize nature to exist is made the energy, family heats to gasifying pipe.
The vaporizer of the invention described above, because unit gasification efficiency height, the volume of vaporizer housing can be little a lot of than the conventional gasifier volume, and according to required treatment fluid chlorine dose array nozzle plate, many exhaustizations tubulation family and housing designed.Wherein array nozzle plate is positioned at the liquid chlorine inlet down, on this plate, have the nozzle hole, the distribution in nozzle hole is corresponding with the first layer gasifying pipe, promptly open row's nozzle hole by gasifying pipe length, and open the nozzle hole of going together mutually by the radical of gasifying pipe, the pitch-row in nozzle hole, aperture and total open area are determined by the specific discharge of liquid chlorine.Under the identical situation of perforated area, reduce the gasification that the aperture helps liquid gas, but will increase the number in nozzle hole, be that 0.25～5.0mm is more suitable with the aperture generally, and the liquid chlorine by each nozzle hole ejection can be directly injected on the surface of first layer gasifying pipe row.Heating and gasifying pipe family is arranged under the array nozzle plate according to layer, the number of plies of the radical of every layer of gasifying pipe and pipe family all can be decided according to liquid gas disposal amount, the number of plies of every layer of gasifying pipe radical and gasifying pipe is many more, to help gasification more, but also can cause processing difficulties, meticulous gasifying pipe is easily stopped up by impurity in incrustation scale or the water again simultaneously, so generally adopting external diameter makes greater than the metal tube of the anti-chlorine corrosion of φ 8mm, every layer of gasifying pipe be for being no less than 4, and have the heating and gasifying pipe family of the mutual cross arrangement of cross section more than 4 layers.The intercommunication of every layer of gasifying pipe interior conduit is communicated with between each layer gasifying pipe successively, and orlop gasification pipe and suction booster are connected to water intake, and the superiors' gasification pipe links to each other with water outlet, and by pipeline communicate with the water source (or discharging).The liquid chlorine gasifier capable fabrication and processing of the invention described above all can be carried out with reference to routine techniques.
Below by drawings and Examples technology of the present invention is given to illustrate further.
Accompanying drawing 1 is the structural representation of vaporizer of the present invention along heating and gasifying pipe lateral cross section;
Accompanying drawing 2 is structure and the water cycle schematic representation of vaporizer of the present invention along heating and gasifying pipe longitudinal cross-section.
Among the figure, 1. housing; 2. array nozzle plate; 3. nozzle hole; 4. gasifying pipe; 5. suction booster; 6. liquid chlorine enters the mouth; 7. chlorine outlet; 8. waste pipe; 9. nature water source.
Vaporizer of the present invention shown in attached Fig. 1 and 2, its housing (1) is a rectangular box, following and the airtight array nozzle plate (2) that is equipped with of inner walls of the liquid chlorine inlet (6) on housing (1) top, have nozzle hole (3) on this plate, wherein accompanying drawing 1 is depicted as the nozzle hole (3) of being opened by row, accompanying drawing 2 is depicted as the nozzle hole (3) of being opened by row, under array nozzle plate (2), be arranged in order and be provided with gasifying pipe (4), and first layer gasifying pipe radical is corresponding with the nozzle hole (3) that array nozzle plate (2) is opened, liquid chlorine can be directly injected on gasifying pipe (4) surface by the nozzle hole, and every layer of gasifying pipe (4) lateral cross mutually arranged; The method for communicating of heating and gasifying pipe (4) technology routinely carries out, the water of by suction booster (5) natural water source (9) being extracted out in the accompanying drawing 2 is made thermal source and is imported by the bottom gasifying pipe, according in pipeline, flowing in a direction indicated by the arrow on the course, water is discharged through waste pipe (8) by the upper strata gasification pipe at last.Liquid chlorine is flow on the array nozzle plate (2) by the liquid chlorine inlet (6) on housing (1) top, be ejected into gasifying pipe (4) surface through nozzle hole (3), through constantly gasification of multilayer gasifying pipe (4) heating, discharge the liquid chlorine vaporizing process of finishing by the chlorine outlet of housing (1) bottom at last.As a specific embodiment, have 5 row nozzle holes (3) on the array nozzle plate (2), the pitch-row 5mm in every row's nozzle hole (3), the aperture of nozzle hole (3) is φ 0.6mm.First layer has 5 φ 20mm gasifying pipes (2) under array nozzle plate (2), form gasifying pipe family for totally 7 layers, it is 380mm that every gasifying pipe can provide the length of heat exchange part, housing (1) is airtight casing, the vaporizer material therefor all adopts stainless steel to make, and is processed into vaporizer of the present invention with reference to routine techniques.
The same specification liquid chlorine vaporizing of the Steam Heating that liquid chlorine gasifier capable of the present invention and present industrial potassium chlorate factory adopt Device (by the 6mol/ amount of vaporization of second) is compared, and its energy consumption only is the latter's 1～1.5%, and the volume of equipment is little, also Only be the latter's 1/2～1/3.
Liquid chlorine gasifier capable of the present invention also can be used for Running-water Company, and tank is supported as the water that heat is provided The source, the water inlet pipe that at this moment needs only the supercharging pump inserts tank, and drainage pipeline also imports tank, consists of water circulation System. If heating and gasifying pipe of the present invention adopts other thermal medium, for example hot water, water vapour heat supply or direct Use electric-heating-wire-heating, then the volume of gasifier can also further dwindling, and makes the high-efficient liquid chlorine of ultra-small volume Change device. At this moment also adopt corrosion-resistant noble metal to make, improve stability and the reliability of equipment.
Claims (3)
1. a high-efficiency liquid chlorine gasifier capable is to take the shell pipe type structure, it is characterized in that heating pipe is the heating and gasifying pipe family of arranging with the multilayer cross modal, one array nozzle plate is arranged at the superiors heating and gasifying pipe top, and the liquid chlorine inlet is positioned at housing top, and the outlet of gasification chlorine is positioned at lower housing portion; After liquid chlorine feeds housing by top, evenly be injected on the heating and gasifying pipe, after heating pipe family heat air changes into gas chlorine, discharge by the gas outlet of housing bottom by the nozzle of array nozzle plate.
2. according to the described high-efficiency liquid chlorine gasifier capable of claim 1, it is characterized in that the heating and gasifying pipe family that the multilayer cross modal is arranged is that many rows vertically are parallel to each other, cross section becomes the heating and gasifying pipe family of cross modal.
3. according to the described high-efficiency liquid chlorine gasifier capable of claim 1, it is characterized in that array nozzle plate is positioned at the liquid chlorine inlet down, on this plate, have the nozzle hole, the distribution in nozzle hole is corresponding with the first layer gasifying pipe, promptly open row's nozzle hole, and open the nozzle hole of going together mutually by the radical of gasifying pipe by gasifying pipe length.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97119068A CN1073683C (en) | 1997-10-22 | 1997-10-22 | High-efficiency liquid chlorine gasifier capable of direct utilization of natural energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97119068A CN1073683C (en) | 1997-10-22 | 1997-10-22 | High-efficiency liquid chlorine gasifier capable of direct utilization of natural energy |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1215137A CN1215137A (en) | 1999-04-28 |
| CN1073683C true CN1073683C (en) | 2001-10-24 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97119068A Expired - Fee Related CN1073683C (en) | 1997-10-22 | 1997-10-22 | High-efficiency liquid chlorine gasifier capable of direct utilization of natural energy |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1073683C (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101118028B (en) * | 2007-08-03 | 2011-06-22 | 自贡鸿鹤化工股份有限公司 | Liquid chlorine gasification device and gasification method |
| WO2023172306A1 (en) * | 2022-03-07 | 2023-09-14 | Mustang Sampling, Llc | Improved liquid gas sample vaporizer conditioning system and method |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104279891B (en) * | 2013-07-05 | 2018-03-30 | 黑龙江省金永科技开发有限公司 | Flow channel type seawater heat exchanger |
| CN105570668A (en) * | 2016-02-06 | 2016-05-11 | 罗涛 | Efficient safe energy-saving heat source air conveying supercharging apparatus |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5004043A (en) * | 1987-03-24 | 1991-04-02 | Tch Thermo-Consulting-Heidelberg Gmbh | Internal tubular falling film apparatus for the evaporation of liquids and for the absortion or degassing of solutions of two or more substances |
| CN1090915A (en) * | 1992-12-29 | 1994-08-17 | 普拉塞尔技术有限公司 | Cryogenic fluid vaporizer system and method |
-
1997
- 1997-10-22 CN CN97119068A patent/CN1073683C/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5004043A (en) * | 1987-03-24 | 1991-04-02 | Tch Thermo-Consulting-Heidelberg Gmbh | Internal tubular falling film apparatus for the evaporation of liquids and for the absortion or degassing of solutions of two or more substances |
| CN1090915A (en) * | 1992-12-29 | 1994-08-17 | 普拉塞尔技术有限公司 | Cryogenic fluid vaporizer system and method |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101118028B (en) * | 2007-08-03 | 2011-06-22 | 自贡鸿鹤化工股份有限公司 | Liquid chlorine gasification device and gasification method |
| WO2023172306A1 (en) * | 2022-03-07 | 2023-09-14 | Mustang Sampling, Llc | Improved liquid gas sample vaporizer conditioning system and method |
| GB2619243A (en) * | 2022-03-07 | 2023-11-29 | Mustang Sampling Llc | Improved liquid gas sample vaporizer conditioning system and method |
| US12098986B2 (en) | 2022-03-07 | 2024-09-24 | Mustang Sampling, Llc | Liquid gas sample vaporizer enclosure |
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| Publication number | Publication date |
|---|---|
| CN1215137A (en) | 1999-04-28 |
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