CN102068868A - High-efficiency gas-liquid separator - Google Patents
High-efficiency gas-liquid separator Download PDFInfo
- Publication number
- CN102068868A CN102068868A CN 201010580867 CN201010580867A CN102068868A CN 102068868 A CN102068868 A CN 102068868A CN 201010580867 CN201010580867 CN 201010580867 CN 201010580867 A CN201010580867 A CN 201010580867A CN 102068868 A CN102068868 A CN 102068868A
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- gas
- urceolus
- inner core
- moisture
- inner barrel
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Abstract
The invention discloses a high-efficiency gas-liquid separator, which consists of an inner barrel and an outer barrel sleeved together, and is characterized in that: the top of the inner barrel is a conical closed body, the lateral wall of the inner barrel is provided with a wire mesh support framework, and the lower end of the inner barrel has a dewatered gas outlet; and the outer barrel is sleeved outside the inner barrel, a gas distributor and a filter layer are arranged between the outer barrel shell and the inner barrel, the upper part of the outer barrel shell is conical and has a moisture feeding port, the lower part of the outer barrel shell is formed into a conical bottom plate, a drain outlet is formed along the outer wall, and the moisture-containing gas booster is arranged on the exterior of the outer barrel. The high-efficiency gas-liquid separator has the advantages that: the flow speed of the furnace gas can be improved by increasing furnace gas pressure on the premise of flow area unchanged; gas is uniformly distributed by the gas distributor in the separator to pass through the filter material ; the device has a simple structure and is convenient to process; compared with the traditional electric defroster, the separator saves electricity; the manufacturing cost is low, no particular material is used, and the selection range of the filter material is wide; and the gas-liquid separator is applicable to industrial furnace gas.
Description
Technical field
The invention belongs to the improvement of the gas-liquid separation device and the gas-liquid separating method of industrial gasses preparation process.
Background technology
At present, the method of sulfuric acid industry gas preparation process gas-liquid separation is varied, the gas purifying technique that for example prepares sulfuric acid process at troilite, in order to remove the redundant moisture that shaped Venturi dedusting is brought into, add electrostatic precipitator in the venturi back, be used to remove bulky grain, large diameter moisture, acid mist among the roaster furnace gas.Further furnace gas is carried out drying with industrial sulphuric acid more afterwards.This demist separate mode need provide the high-voltage electrostatic field to consume a large amount of electric energy, just can reach the effect of demist, dehydration.The gas-liquid separator that uses in the Chinese patent ZL200620071193.0 flue-gas dust-removing and desulfurization device adopts ceramic hollow ball body wall face that through hole is set, and it is simple in structure, and is little to flue gas resistance, can carry out gas-liquid separation.But for removing the bulky grain in the roaster furnace gas, large diameter moisture, acid mist, the ancillary method of still needing.
Summary of the invention
The present invention is the further improvement to existing technology, and necessary gas moisture content isolation field, enough filter areas are provided, and the furnace gas that makes band water is by the high speed Brownian movement, is captured at the filter material surface of necessity, reaches the purpose of divided gas flow moisture.
The technical scheme that the present invention addresses the above problem employing is: a kind of high efficient gas and liquid separation equipment, inner core and urceolus by suit are formed, the tapered obturator in inner core top, the inner core sidewall is provided with the woven wire support frame, the inner core lower end is the dehydrated air outlet, the urceolus housing is sleeved on the inner core outside, be provided with gas distributor and filter material layer between urceolus and the inner core, urceolus housing top is tapered, be provided with moisture gas feed mouth, the tapered base plate of urceolus lower housing portion is provided with the discharging tube outlet along outer wall, and the urceolus outside is provided with moisture gas pressurized device.
Aforesaid high efficient gas and liquid separation equipment, its filter material layer is a mineral wool, rock wool, glass fibre.
Aforesaid high efficient gas and liquid separation equipment, its moisture gas pressurized device is an air pump, but supercharging 100Pa.
Advantage of the present invention is: increase furnace gas pressure, improve the flow velocity of furnace gas under the constant prerequisite of circulation area.Reach gas at the inner using gases distributor of separation equipment and pass through filtrate inner evenly distribution of separation equipment.Use the little woven wire of resistance as the skeleton that supports filtrate.In time draw the liquid (moisture) that separates and prevent that secondary from bringing in the middle of the furnace gas.Device structure is simple, is convenient to processing and fabricating.With traditional electrostatic precipitator relatively can saves energy.Cheap, need not special material, the filtrate range of choice is bigger.
The present invention is applicable to the gas-liquid separation equipment when containing bulky grain, large diameter moisture, acid mist in the industrial furnace gas.
Description of drawings
Below in conjunction with drawings and Examples, the present invention is further described.
Fig. 1 is a kind of organigram of high efficient gas and liquid separation equipment
Among the figure, 1-inner core, 2-woven wire support frame, the outlet of 3-dehydrated air, 4-urceolus housing, 5-gas distributor, 6-filter material layer, the moisture gas feed mouth of 7-, the outlet of 8-discharging tube, the moisture gas pressurized device of 9-
The specific embodiment
As seen from Figure 1, a kind of high efficient gas and liquid separation equipment, inner core and urceolus by suit are formed, the tapered obturator in inner core 1 top, the inner core sidewall is provided with woven wire support frame 2, the inner core lower end is dehydrated air outlet 3, urceolus housing 4 is sleeved on the inner core outside, be provided with gas distributor 5 and filter material layer 6 between urceolus and the inner core, urceolus housing top is tapered, is provided with moisture gas feed mouth 7, the tapered base plate of urceolus lower housing portion, be provided with discharging tube outlet 8 along outer wall, the urceolus outside is provided with moisture gas pressurized device 9.
Using method of the present invention is, the furnace gas (industrial gasses) that contains bulky grain major diameter moisture enters gas separator inside from top, makes the evenly cross section by gas separator of gas by the gas inside distribution apparatus, and then enters in the filtrate.The furnace gas (industrial gasses) that flows in the filtrate inner high speed passes through collision, and the particle diameter increase is captured by filtrate.The moisture following current is drawn by discharging tube after accumulating to the bottom, and the furnace gas behind the disengaging moisture is discharged by the bottom exhaust outlet by filter screen and entered into next operation.
High efficient gas and liquid separation equipment of the present invention can pass through prefabricated finished product, installs then.But, be used to carry the blower fan outlet pressure of furnace gas should improve more than the 100pa at least according to the actual conditions and the plant bulk size of filling filtrate.
Claims (3)
1. high efficient gas and liquid separation equipment, inner core and urceolus by suit are formed, it is characterized in that, the tapered obturator in inner core top, the inner core sidewall is provided with the woven wire support frame, the inner core lower end is the dehydrated air outlet, the urceolus housing is sleeved on the inner core outside, be provided with gas distributor and filter material layer between urceolus and the inner core, urceolus housing top is tapered, is provided with moisture gas feed mouth, the tapered base plate of urceolus lower housing portion, be provided with the discharging tube outlet along outer wall, the urceolus outside is provided with moisture gas pressurized device.
2. high efficient gas and liquid separation equipment as claimed in claim 1 is characterized in that filter material layer is a mineral wool, rock wool, glass fibre.
3. high efficient gas and liquid separation equipment as claimed in claim 1 is characterized in that, but the air pump that its moisture gas pressurized device is supercharging 100Pa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010580867 CN102068868A (en) | 2010-12-03 | 2010-12-03 | High-efficiency gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010580867 CN102068868A (en) | 2010-12-03 | 2010-12-03 | High-efficiency gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102068868A true CN102068868A (en) | 2011-05-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010580867 Pending CN102068868A (en) | 2010-12-03 | 2010-12-03 | High-efficiency gas-liquid separator |
Country Status (1)
| Country | Link |
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| CN (1) | CN102068868A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582101A (en) * | 2016-12-19 | 2017-04-26 | 芜湖万向新元环保科技有限公司 | Three-stage filter system |
| CN106861339A (en) * | 2017-03-22 | 2017-06-20 | 溧阳市英创机电技术有限公司 | A kind of multiphase flow separation equipment |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2064677U (en) * | 1989-06-17 | 1990-10-31 | 梁喜武 | Gas-liquid separator |
| CN2499585Y (en) * | 2001-10-19 | 2002-07-10 | 艾买尔江·买买提 | Environment protection device for reclaiming waste gas |
| CN1383925A (en) * | 2002-03-05 | 2002-12-11 | 高根树 | Axial-flow type coupled filtering centrifuger |
| CN201015718Y (en) * | 2007-02-27 | 2008-02-06 | 王银昌 | Separator for water and vapor |
| CN201534030U (en) * | 2009-05-14 | 2010-07-28 | 颜晓琼 | Oil gas filtering and separating device |
-
2010
- 2010-12-03 CN CN 201010580867 patent/CN102068868A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2064677U (en) * | 1989-06-17 | 1990-10-31 | 梁喜武 | Gas-liquid separator |
| CN2499585Y (en) * | 2001-10-19 | 2002-07-10 | 艾买尔江·买买提 | Environment protection device for reclaiming waste gas |
| CN1383925A (en) * | 2002-03-05 | 2002-12-11 | 高根树 | Axial-flow type coupled filtering centrifuger |
| CN201015718Y (en) * | 2007-02-27 | 2008-02-06 | 王银昌 | Separator for water and vapor |
| CN201534030U (en) * | 2009-05-14 | 2010-07-28 | 颜晓琼 | Oil gas filtering and separating device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582101A (en) * | 2016-12-19 | 2017-04-26 | 芜湖万向新元环保科技有限公司 | Three-stage filter system |
| CN106861339A (en) * | 2017-03-22 | 2017-06-20 | 溧阳市英创机电技术有限公司 | A kind of multiphase flow separation equipment |
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| AD01 | Patent right deemed abandoned |
Effective date of abandoning: 20110525 |
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| C20 | Patent right or utility model deemed to be abandoned or is abandoned |