CN102688666A - Gas purifying drying tank - Google Patents
Gas purifying drying tank Download PDFInfo
- Publication number
- CN102688666A CN102688666A CN2011100760078A CN201110076007A CN102688666A CN 102688666 A CN102688666 A CN 102688666A CN 2011100760078 A CN2011100760078 A CN 2011100760078A CN 201110076007 A CN201110076007 A CN 201110076007A CN 102688666 A CN102688666 A CN 102688666A
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- jar
- disposed
- gas
- tank
- air inlet
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Abstract
The invention relates to a gas purifying drying tank which comprises a tank upper part and a tank lower part; a gas outlet is disposed at one side of the top of the tank upper part; a gas-fog separation component is disposed at the middle part of the tank upper part; a gas inlet is disposed at the bottom side of the tank lower part; an air inlet is disposed at the upper side of the gas inlet; a control valve c is disposed on the air inlet; a stainless steel filter screen is disposed at the upper side of the air inlet; a gas purifying component is disposed at the upper side of the stainless steel filter screen; a stainless steel filter screen is also disposed at the lower side of the gas inlet of the tank lower part; an inverted cone-shape water storage part is connected with the bottom of the tank lower part; a water outlet is disposed at the bottom of the water storage part; a control valve b is disposed on the water outlet; three triangular supporting legs are respectively disposed on the tank upper part and the tank lower part. The advantages of the invention are that: the desulphurization efficiency is high; a desulfurizer is reduced completely; the collected and used gas is cleaner through filtration and dehydration; no obstruction occurs; the flow resistance is low; the structure is simple and the cost is low.
Description
Technical field
The present invention relates to the clarifier field, relate in particular to a kind of gas purification drying chamber.
Background technology
Along with development of industry and agriculture, garbage disposal etc. have brought rich in natural resources all for the generation of biogas or natural gas, yet because the fermentation of biogas or natural gas the time; Also can produce certain harmful hydrogen sulfide gas; Hydrogen sulfide is a kind of hypertoxic gas, has the stench egg flavor, is strong neurotoxic substance; Get in the blood through respiratory system, bring very huge injury to human body.Hydrogen sulfide is in the operation of burning, and the generation sulfur dioxide that also can burn, sulfur dioxide are the very strong gas of kind of corrosivity; After sucking, human body can stimulate respiratory tract; Influence the normal function of respiratory system, and it is the chief component of acid rain with sulfurous acid that water combine to produce, also is more serious to environment and health effects; And meeting accelerated corrosion domestic cookers, reduction of service life.Therefore before utilization, must carry out desulfurization to biogas.
In the prior art, mainly be in airtight container, to adopt desulfurizing agent to carry out desulfurization to the sulphur removal of biogas or natural gas, desulfurizing agent commonly used is an iron oxide; Be shaped as particle; But because have impurity and water in biogas or the natural gas, the gap of easy blocking desulfurizing agent causes desulfurized effect poor.Bubbling air or oxygen is the reduction and desulfurization agent automatically, but because the reasons such as obstruction of impurity and water, desulfurizing agent can not be reduced fully, and desulfurized effect is poor, and causes corrosion and hidden danger to miscellaneous equipment.
Therefore, for the health of assurance human body and the protection of environment, be badly in need of a kind of improved technology and solve this problem.
Summary of the invention
The purpose of this invention is to provide a kind of gas purification drying chamber.
The technical scheme that the present invention adopts is:
The gas purification drying chamber comprises a jar top and a jar bottom, it is characterized in that: said jar of upper bottom is provided with external screw thread; Said jar of top, top one side is provided with the gas outlet, and middle part, said jar of top is provided with the aerosol separating component, and said jar of bottom is provided with the internal thread that matches with jar upper external thread; The bottom of said jar of bottom also is provided with internal thread, and said jar of lower base one side is provided with air inlet, and the upside of said air inlet also is provided with the air air intake; The upside of said air air intake is provided with stainless steel filtering net; The upside of said stainless steel filtering net is provided with the gas purification parts, and the said jar bottom air inlet downside that is positioned at also is provided with stainless steel filtering net, and said jar of lower base is connected with inverted taper water storage place; The top at said water storage place is provided with the external screw thread that matches with jar lower internal thread, and the bottom at said water storage place also is provided with delivery port.
Said jar top and jar bottom are equipped with the feet of three triangularity shapes.Said gas outlet is provided with by-pass valve control a, and said delivery port is provided with by-pass valve control b, also is provided with by-pass valve control c on the said air air intake, and said air inlet is provided with by-pass valve control d.
Advantage of the present invention is: desulfuration efficiency is high, fully reduction and desulfurization agent, and the gas that filtration and dehydration utilize collection is cleaner, can not stop up, and flow resistance is little; Simple in structure, cost is low, is applicable to gas cleaning drying processes such as biogas, natural gas and coal gas.
Description of drawings
Below in conjunction with the accompanying drawing and the specific embodiment the present invention is described in further detail.
Fig. 1 is a structural representation of the present invention.
Wherein: 1, jar top, 2, jar bottom, 3, the gas outlet, 4, by-pass valve control a; 5, aerosol separating component, 6, the air air intake, 7, by-pass valve control c, 8, air inlet; 9, by-pass valve control d, 10, the gas purification parts, 11, stainless steel filtering net, 12, the water storage place; 13, delivery port, 14, by-pass valve control b, 15, feet.
The specific embodiment
As shown in Figure 1, gas purification drying chamber of the present invention comprises a jar top 1 and a jar bottom 2; It is characterized in that: said jar of 1 bottom, top is provided with external screw thread, and said jar of top, top one side is provided with gas outlet 3, and said gas outlet 3 is provided with by-pass valve control a4; Said jar of 1 middle part, top is provided with aerosol separating component 5, and said jar of bottom 2 is provided with and jar internal thread that top 1 external screw thread matches, and the bottom of said jar of bottom 2 also is provided with internal thread; Said jar of lower base one side is provided with air inlet 8,, said air inlet is provided with by-pass valve control d9; The upside of said air inlet 8 also is provided with air air intake 6, also is provided with by-pass valve control c7 on the said air air intake 6, and the upside of said air air intake 6 is provided with stainless steel filtering net 11; The upside of said stainless steel filtering net 11 is provided with gas purification parts 10, and said jar bottom 2 air inlets, 8 downsides that are positioned at also are provided with stainless steel filtering net 11, and said jar of 2 bottoms, bottom are connected with inverted taper water storage place 12; The top at said water storage place 12 is provided with and jar external screw thread that bottom 2 internal threads match, and the bottom at said water storage place 12 also is provided with delivery port 13, and said delivery port 13 is provided with by-pass valve control b14; Said jar top 1 and jar bottom 2 are equipped with the feet 15 of three triangularity shapes, and desulfuration efficiency is high, fully reduction and desulfurization agent; Filtration and dehydration make the gas of collecting utilization cleaner, can not stop up, and flow resistance is little; Simple in structure, cost is low, is applicable to gas cleaning drying processes such as biogas, natural gas and coal gas.
Claims (3)
1. the gas purification drying chamber comprises a jar top and a jar bottom, it is characterized in that: said jar of upper bottom is provided with external screw thread; Said jar of top, top one side is provided with the gas outlet, and middle part, said jar of top is provided with the aerosol separating component, and said jar of bottom is provided with the internal thread that matches with jar upper external thread; The bottom of said jar of bottom also is provided with internal thread, and said jar of lower base one side is provided with air inlet, and the upside of said air inlet also is provided with the air air intake; The upside of said air air intake is provided with stainless steel filtering net; The upside of said stainless steel filtering net is provided with the gas purification parts, and the said jar bottom air inlet downside that is positioned at also is provided with stainless steel filtering net, and said jar of lower base is connected with inverted taper water storage place; The top at said water storage place is provided with the external screw thread that matches with jar lower internal thread, and the bottom at said water storage place also is provided with delivery port.
2. gas purification drying chamber according to claim 1 is characterized in that: said jar top and jar bottom are equipped with the feet of three triangularity shapes.
3. gas purification drying chamber according to claim 1 is characterized in that: said gas outlet is provided with by-pass valve control a, and said delivery port is provided with by-pass valve control b, also is provided with by-pass valve control c on the said air air intake, and said air inlet is provided with by-pass valve control d.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100760078A CN102688666A (en) | 2011-03-25 | 2011-03-25 | Gas purifying drying tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100760078A CN102688666A (en) | 2011-03-25 | 2011-03-25 | Gas purifying drying tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102688666A true CN102688666A (en) | 2012-09-26 |
Family
ID=46854499
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011100760078A Pending CN102688666A (en) | 2011-03-25 | 2011-03-25 | Gas purifying drying tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102688666A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103470953A (en) * | 2013-09-18 | 2013-12-25 | 中国石油集团西部钻探工程有限公司 | Compressed natural gas complete purification ready-packaged movable device |
| CN109612227A (en) * | 2019-01-24 | 2019-04-12 | 沈阳工程学院 | A kind of rapid drying device of gallium oxide powder |
-
2011
- 2011-03-25 CN CN2011100760078A patent/CN102688666A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103470953A (en) * | 2013-09-18 | 2013-12-25 | 中国石油集团西部钻探工程有限公司 | Compressed natural gas complete purification ready-packaged movable device |
| CN103470953B (en) * | 2013-09-18 | 2015-12-23 | 中国石油集团西部钻探工程有限公司 | Compressed natural gas complete purification fast-assembling mobile device |
| CN109612227A (en) * | 2019-01-24 | 2019-04-12 | 沈阳工程学院 | A kind of rapid drying device of gallium oxide powder |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120926 |