CN105148690A - Smoke drying treatment device - Google Patents
Smoke drying treatment device Download PDFInfo
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- CN105148690A CN105148690A CN201510550887.6A CN201510550887A CN105148690A CN 105148690 A CN105148690 A CN 105148690A CN 201510550887 A CN201510550887 A CN 201510550887A CN 105148690 A CN105148690 A CN 105148690A
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- outer tube
- membrane pipe
- pipe module
- outlet
- infiltration membrane
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Abstract
The invention relates to the field of environment protection measuring, in particular to a smoke drying treatment device. The smoke drying treatment device comprises an outer sleeve pipe with an inlet and an outlet in two ends and an osmotic membrane pipe assembly of which a part is arranged in the outer sleeve pipe; the inlet end and outlet end of the osmotic membrane pipe assembly are arranged by extending out of the outer sleeve pipe and communicated with outside, the rest part is arranged in the outer sleeve pipe, and the inlet end and outlet end of the osmotic membrane pipe assembly are respectively sealed and fixed together with head and tail end surfaces of the outer sleeve pipe; the bottom of the outer wall of the outer sleeve pipe is provided with an inlet for introducing of dry instrument gas, and the top of the outer sleeve pipe is provided with an outlet for exhausting the dry instrument gas. Therefore, the smoke drying device has following advantages that water vapor in smoke can be removed without requiring a refrigerating process, and gas to be analyzed in the smoke cannot be lost.
Description
Technical field
The present invention relates to a kind of environmental protection fields of measurement, especially relate to a kind of flue gas drying treating apparatus.
Background technology
Existing technology is all first heat for the dehumidifying of flue gas, then freeze, steam in the flue gas globule that congeals into is got rid of, but such shortcoming is, owing to there being the process of refrigeration, some exists falls with gas with analysis in the flue gas also easy process losses with freeze, has an impact to the result of measurement.
Summary of the invention
The present invention mainly solves the technical problem existing for prior art; Provide one and do not need process of refrigerastion, just the steam in flue gas can be removed, and a kind of flue gas drying treating apparatus of the gas with analysis in flue gas can not be lost.
Above-mentioned technical problem of the present invention is mainly solved by following technical proposals:
A kind of flue gas drying treating apparatus, is characterized in that, comprise the outer tube that two ends are provided with import and outlet, and the infiltration membrane pipe module in the outer tube of part setting; The entrance point of described infiltration membrane pipe module and port of export setting are stretched out outer tube two ends and are communicated with the external world, and remainder is arranged in outer tube, and the entrance point of infiltration membrane pipe module and the port of export seal fixing with outer tube head and the tail both ends of the surface respectively; Be provided with the import for passing into dry instrument gas bottom described outer tube outer wall, top is provided with the outlet of discharging for dry instrument gas.
At above-mentioned a kind of flue gas drying treating apparatus, described infiltration membrane pipe module comprises some capillary percolation film pipes, and described some capillary percolation film pipes form a cylindric infiltration membrane pipe module; These cylindric infiltration membrane pipe module two ends are fixed respectively by support ring, and cylindric infiltration membrane pipe module two ends stretch out import and the outlet of outer tube respectively; The import of described outer tube is equal with the caliber of cylindric infiltration membrane pipe module with the diameter of outlet.
Therefore, tool of the present invention has the following advantages: do not need process of refrigerastion, just the steam in flue gas can be removed, and can not lose the gas with analysis in flue gas.
Accompanying drawing explanation
Accompanying drawing 1 is a kind of principle schematic of the present invention.
Accompanying drawing 2 be of the present invention in the structural representation of cylindric infiltration membrane pipe module.
Accompanying drawing 3 is left TV structure schematic diagrames of Fig. 2.
Detailed description of the invention
Below by embodiment, and by reference to the accompanying drawings, technical scheme of the present invention is described in further detail.
Embodiment:
The present invention includes the outer tube 5 that two ends are provided with import and outlet, and the infiltration membrane pipe module in the outer tube 5 of part setting; The entrance point of described infiltration membrane pipe module and port of export setting are stretched out outer tube 5 two ends and are communicated with the external world, and remainder is arranged in outer tube 5, and the entrance point of infiltration membrane pipe module and the port of export seal fixing with outer tube 5 head and the tail both ends of the surface respectively; Be provided with the import 2 for passing into dry instrument gas bottom described outer tube 5 outer wall, top is provided with the outlet 4 of discharging for dry instrument gas.
Infiltration membrane pipe module comprises some capillary percolation film pipes 6, and described some capillary percolation film pipes 6 form a cylindric infiltration membrane pipe module; These cylindric infiltration membrane pipe module two ends are fixed respectively by support ring, and cylindric infiltration membrane pipe module two ends stretch out import and the outlet of outer tube 5 respectively; The described import of outer tube 5 is equal with the caliber of cylindric infiltration membrane pipe module with the diameter of outlet.
It should be noted that, inside pipe casing outside, remain constant temperature 20 ~ 70 degree, preferred plan is 50 °, in addition, exporting 4 by dry instrument gas feed 2 to instrument supply gas is negative-pressure gas, and high 1 to the dry flue gas 3 of flue gas water capacity through dust removal process is malleation, thus be malleation in formation outer tube, thus steam is oozed out in capillary percolation film pipe 6 to export from instrument supply gas with dry instrument gas 4 to evaporate.
Specific embodiment described herein is only to the explanation for example of the present invention's spirit.Those skilled in the art can make various amendment or supplement or adopt similar mode to substitute to described specific embodiment, but can't depart from spirit of the present invention or surmount the scope that appended claims defines.
Although more employ through terms such as the flue gas (water capacity is high) 1 of dust removal process, dry instrument gas feed 2, dry flue gas 3, instrument supply gas outlet 4, outer tube 5, capillary percolation film pipes 6, do not get rid of the possibility using other term herein.These terms are used to be only used to describe and explain essence of the present invention more easily; The restriction that they are construed to any one additional is all contrary with spirit of the present invention.
Claims (2)
1. a flue gas drying treating apparatus, is characterized in that, comprises the outer tube (5) that two ends are provided with import and outlet, and the infiltration membrane pipe module in the outer tube (5) of part setting; The entrance point of described infiltration membrane pipe module and port of export setting are stretched out outer tube (5) two ends and are communicated with the external world, remainder is arranged in outer tube (5), and the entrance point of infiltration membrane pipe module and the port of export seal fixing with outer tube (5) head and the tail both ends of the surface respectively; Be provided with the import (2) for passing into dry instrument gas bottom described outer tube (5) outer wall, top is provided with the outlet (4) of discharging for dry instrument gas.
2. a kind of flue gas drying treating apparatus according to claim 1, it is characterized in that, described infiltration membrane pipe module comprises some capillary percolation film pipes (6), described some capillary percolation film pipe (6) compositions cylindric infiltration membrane pipe module; These cylindric infiltration membrane pipe module two ends are fixed respectively by support ring, and cylindric infiltration membrane pipe module two ends stretch out import and the outlet of outer tube (5) respectively; The import of described outer tube (5) is equal with the caliber of cylindric infiltration membrane pipe module with the diameter of outlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510550887.6A CN105148690A (en) | 2015-08-31 | 2015-08-31 | Smoke drying treatment device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510550887.6A CN105148690A (en) | 2015-08-31 | 2015-08-31 | Smoke drying treatment device |
Publications (1)
Publication Number | Publication Date |
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CN105148690A true CN105148690A (en) | 2015-12-16 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201510550887.6A Pending CN105148690A (en) | 2015-08-31 | 2015-08-31 | Smoke drying treatment device |
Country Status (1)
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CN (1) | CN105148690A (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1049511A (en) * | 1989-08-17 | 1991-02-27 | 分离动力股份有限公司 | Closed loop gas dehydration process and device |
JPH0866616A (en) * | 1994-08-30 | 1996-03-12 | Koganei Corp | Dehumidifier |
DE19812960C1 (en) * | 1998-03-24 | 1999-11-04 | Kompressoren Und Druckluft Tec | Membrane drying system for compressed air |
CN2745636Y (en) * | 2004-11-19 | 2005-12-14 | 江苏江分电分析仪器有限公司 | Membrane type drier |
JP2008246374A (en) * | 2007-03-30 | 2008-10-16 | Orion Mach Co Ltd | Membrane-type drier for highly defumidified air |
JP2009142800A (en) * | 2007-12-18 | 2009-07-02 | Smc Corp | Dehumidification system and dehumidification method in booster piping |
CN103759998A (en) * | 2014-01-21 | 2014-04-30 | 北京汇丰隆生物科技发展有限公司 | Atmosphere dehumidification method and device |
CN205084594U (en) * | 2015-08-31 | 2016-03-16 | 武汉宇虹环保产业发展有限公司 | Flue gas dry processing device |
-
2015
- 2015-08-31 CN CN201510550887.6A patent/CN105148690A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1049511A (en) * | 1989-08-17 | 1991-02-27 | 分离动力股份有限公司 | Closed loop gas dehydration process and device |
JPH0866616A (en) * | 1994-08-30 | 1996-03-12 | Koganei Corp | Dehumidifier |
DE19812960C1 (en) * | 1998-03-24 | 1999-11-04 | Kompressoren Und Druckluft Tec | Membrane drying system for compressed air |
CN2745636Y (en) * | 2004-11-19 | 2005-12-14 | 江苏江分电分析仪器有限公司 | Membrane type drier |
JP2008246374A (en) * | 2007-03-30 | 2008-10-16 | Orion Mach Co Ltd | Membrane-type drier for highly defumidified air |
JP2009142800A (en) * | 2007-12-18 | 2009-07-02 | Smc Corp | Dehumidification system and dehumidification method in booster piping |
CN103759998A (en) * | 2014-01-21 | 2014-04-30 | 北京汇丰隆生物科技发展有限公司 | Atmosphere dehumidification method and device |
CN205084594U (en) * | 2015-08-31 | 2016-03-16 | 武汉宇虹环保产业发展有限公司 | Flue gas dry processing device |
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Address after: 430223 Hubei city of Wuhan province East Lake high tech Development Zone, Shiyuan Road No. 11 Applicant after: WUHAN TIANHONG ENVIRONMENTAL PROTECTION INDUSTRY CO.,LTD. Address before: 430223 Hubei city of Wuhan province East Lake high tech Development Zone, Shiyuan Road No. 11 Applicant before: WUHAN YUHONG ENVIRONMENT PROTECTION DEVELOPMENT Co.,Ltd. |
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WD01 | Invention patent application deemed withdrawn after publication | ||
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Application publication date: 20151216 |