CN204275745U - The multistage dehumidifying filter of integral type ammonia - Google Patents
The multistage dehumidifying filter of integral type ammonia Download PDFInfo
- Publication number
- CN204275745U CN204275745U CN201420724463.8U CN201420724463U CN204275745U CN 204275745 U CN204275745 U CN 204275745U CN 201420724463 U CN201420724463 U CN 201420724463U CN 204275745 U CN204275745 U CN 204275745U
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- housing
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- ammonia
- integral type
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- Filtering Of Dispersed Particles In Gases (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Drying Of Gases (AREA)
Abstract
The utility model discloses the multistage dehumidifying filter of a kind of integral type ammonia, comprise the hollow housing with bottom ammonia entrance and upper end ammonia outlet be arranged on bracing frame, characterized by further comprising the cyclonic separation assembly, gas-liquid separation assembly, charcoal absorption assembly and point dirt filter assemblies that are set in turn in enclosure interior from bottom to top; Compared with prior art, filtration at different levels is integrated in one by the utility model, while guarantee function at different levels, reduces equipment investment and place waste.
Description
Technical field
The utility model relates to separation equipment technical field, particularly the multistage dehumidifying filter of a kind of integral type ammonia.
Background technology
Manufacture in the liquid ammonia gasification process of ammonia at chemical industry, the impurity existed in gas after must removing liquid ammonia gasification and moisture, in the traditional handicraft of current use, ammonia dehumidifying dehydration, removal impurity need multi-stage separation container to form train, namely cause equipment investment too high, take many production sites again.
Utility model content
The utility model provides a kind of integral type ammonia multistage dehumidifying filter, there is in order to solve in prior art the problem that equipment investment is high, place is wasted.
The utility model method comprises: provide a kind of integral type ammonia multistage dehumidifying filter, comprise the hollow housing with bottom ammonia entrance and upper end ammonia outlet be arranged on bracing frame, also comprise the cyclonic separation assembly, gas-liquid separation assembly, charcoal absorption assembly and point dirt filter assemblies that are set in turn in enclosure interior from bottom to top; Wherein
Described cyclonic separation assembly comprises tangential admission cyclone pipe, baffle plate is revolved in central drain pipe, swirl vane, resistance; Tangential admission cyclone pipe is connected with central drain pipe, and swirl vane is fixedly installed on central drain pipe upper end, and resistance is revolved baffle plate and is fixedly installed on central drain pipe lower end;
Described gas-liquid separation assembly comprises horizontal stainless steel gas-liquid separate mesh, condensate tank, drainage pipe; Described condensate tank is positioned in inner walls and arranges ringwise below stainless steel gas-liquid separate mesh, and is connected to housing bottom by drainage pipe;
Described charcoal absorption assembly comprises active carbon hygroscopic agent;
Described point of dirt filter assemblies is included in the filter cartridge seat of horizontally set on housing, and is arranged at the multiple microfiltration cores in described filter cartridge seat;
Ammonia entrance is passed through after tangential admission cyclone pipe cyclonic separation containing wet ammonia, liquid drains into housing bottom through central drain pipe, gas forms centrifugal effect by rotating at stainless steel gas-liquid separate mesh interior orientation after swirl vane, complete secondary gas-liquid separation, liquid drains into housing bottom through condensate pipe and drainage pipe, and gas has been discharged dehumidifying and the purification of gas after the dehumidifying of active carbon hygroscopic agent and microfiltration core removing impurity by ammonia outlet.
Described housing bottom is provided with a sewage draining exit.
Described housing upper is provided with a differential manometer mouth.
Compactor is provided with between described gas-liquid separation assembly and charcoal absorption assembly.
Described resistance is revolved baffle plate and is set to two panels and right-angled intersection composition.
Described case top adopts ellipsoidal head, and described housing bottom adopts conical head.
Described housing comprises the sub-housing of multistage, passes through Flange joint between described sub-housing.
Described housing comprises by the first sub-housing of Flange joint, the second sub-housing, the 3rd sub-housing and the 4th sub-housing; Described ammonia outlet is arranged on the first sub-housing, described point of dirt filter assemblies is arranged on described second sub-enclosure interior, described charcoal absorption assembly is arranged on described 3rd sub-enclosure interior, described gas-liquid separation assembly and cyclonic separation assembly are arranged on described 4th sub-enclosure interior, and described ammonia entrance is arranged on described 4th sub-housing.
The utility model beneficial effect is as follows:
A, separation container at different levels are integrated, reduce the waste in equipment investment and place;
B, tower body adopt multisection type flange arrangement, and the consumptive material of fillter section at different levels can independently regenerate or change, and assembling and dismounting are flexibly and easily;
C, according to different user's requirements, with identical structural shape, plurality of specifications can be manufactured, be applicable to different gas treatment amount, different operating pressure, different pipeline diameter.
D, the utility model, except being specially suitable for ammonia dehumidifying, can be used for dehumidifying and the purification of other gases equally.
Accompanying drawing explanation
Fig. 1 is the multistage dehumidifying filter structure schematic representation of integral type ammonia;
Fig. 2 is integral type ammonia multistage dehumidifying filtration device structure top view;
Fig. 3 is that baffle arrangement schematic diagram is revolved in the multistage dehumidifying filter resistance of integral type ammonia.
In figure, the title of each numeral and alphabetical designation respectively: 1-housing, the sub-housing of 101-first, the sub-housing of 102-second, the sub-housing of 103-the 3rd, the sub-housing of 104-the 4th, 2-filter cartridge seat, 3-microfiltration core, 4-active carbon hygroscopic agent, 5-compactor, 6-stainless steel gas-liquid separate mesh, 7-condensate tank, 8 swirl vanes, 9-drainage pipe, 10-tangential admission cyclone pipe, 11-central drain pipe, 12-resistance revolves baffle plate, 13-foot-supporting frame, 14-ellipse head, 15-conical head, N1-ammonia entrance, N2-ammonia outlet, N3-differential manometer mouth.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model content is described further, but concrete form of implementation of the present utility model is not limited in following embodiment.
For achieving the above object and adopt technical solution be such: the multistage dehumidifying filter of the integral type ammonia provided, comprise the hollow housing 1 with bottom ammonia entrance N1 and upper end ammonia outlet N2 be arranged on bracing frame 13, also comprise the cyclonic separation assembly, gas-liquid separation assembly, charcoal absorption assembly and point dirt filter assemblies that are set in turn in housing 1 inside from bottom to top; Wherein cyclonic separation assembly comprises tangential admission cyclone pipe 10, central drain pipe 11, swirl vane 8 and resistance and revolves baffle plate 12, its air inlet of tangential admission cyclone pipe 10 is connected with ammonia entrance N1, its liquid outlet is connected the bottom blow-down mouth N3 place passing to housing 1 with central drain pipe 11, central drain pipe 11 is vertically fixedly installed on housing 1 lower central position, swirl vane 8 fixes the horizontal upper end at central drain pipe 11, and swirl vane is arranged to fan leaf sheet; The lower end that baffle plate 12 is fixedly installed on central drain pipe 11 is revolved in resistance, and preferably resistance is revolved baffle plate 12 and is set to two panels and vertical right-angled intersection composition, effectively blocks the flowing of housing lower end gas, prevents the liquid of housing bottom to pass again; Wherein gas-liquid separation assembly comprises horizontal stainless steel gas-liquid separate mesh 6, condensate tank 7, drainage pipe 9; Condensate tank 7 is arranged ringwise, being positioned at the below with stainless steel gas-liquid separate mesh 6 on housing 1 inwall, and arranging with swirl vane isoplanar, can be connected to bottom housing 1 according to user's request by arranging one or more drainage pipe 9; Charcoal absorption assembly comprises active carbon hygroscopic agent 4, for the removal moisture drying of ammonia after gas-liquid separation; The filter cartridge seat 2 of dividing dirt filter assemblies to be included in horizontally set on housing 1 and the multiple microfiltration cores 3 be arranged in filter cartridge seat 2, can trap and filter out the magazines such as the dust oil droplet of 0.01-1 micron; Bottom housing 1, be provided with a sewage draining exit N3 simultaneously, in order to discharge the liquid filtering and obtain, be provided with a differential manometer mouth N4 on housing 1 top, in order to the air pressure size in monitor force container casing 1.
A kind of preferred embodiment that the present embodiment provides is between gas-liquid separation assembly and charcoal absorption assembly, arrange compactor 5, for being fixed gas-liquid separation assembly and charcoal absorption assembly; Preferably the top of housing 1 adopts ellipsoidal head 14, and be convenient to the discharge of dehumidifying ammonia, adopt conical head 15 bottom housing 1, the liquid being convenient to gas dehumidification is discharged from housing 1 bottom blow-down mouth 13; Ammonia entrance is arranged on housing tangent plane position.
In addition, can independently regenerate to make the consumptive material of each assembly of this filter or be convenient to change, preferably housing 1 be made up of the sub-housing of multistage, passes through Flange joint between sub-housing; According to the actual requirement that ammonia dehumidifying in Chemical Manufacture is filtered, more preferably housing 1 is made up of four parts, comprises by the sub-housing 102 of the first sub-housing 101, second of Flange joint, the 3rd sub-housing 103 and the 4th sub-housing 104 respectively; Ammonia outlet is arranged on the first sub-housing, dirt filter assemblies is divided to be arranged on described second sub-enclosure interior, charcoal absorption assembly is arranged on described 3rd sub-enclosure interior, gas-liquid separation assembly and cyclonic separation assembly are arranged on described 4th sub-enclosure interior, and ammonia entrance is arranged on described 4th sub-housing.
Operation principle of the present utility model is such: pass into containing before wet ammonia, check each filter assemblies, close leakage fluid dram N3, tangential admission cyclone pipe 10 is entered by the ammonia entrance N1 tangentially arranged with housing 1 containing wet ammonia, after tangential admission cyclone pipe 10 carries out cyclonic separation, complete first time gas-liquid separation, the liquid of separation drains into the bottom blow-down mouth N3 place of housing 1 by central drain pipe 11; The gas be simultaneously separated is by after swirl vane 8, gas forms the air-flow of high speed directional-rotation in housing 1, produce centrifugal effect, when passing through in stainless steel gas-liquid separate mesh 6, the large moisture of quality under the influence of centrifugal force, to the motion of housing 1 inwall direction, after stainless steel gas-liquid separate mesh 6 stops, flow into condensate tank 7 along housing 1 inwall; The ammonia of lightweight moves under the influence of centrifugal force and enters charcoal absorption assembly by stainless steel gas-liquid separate mesh 6 in the middle part of housing 1, complete secondary gas-liquid separation, liquid drains into housing bottom sewage draining exit 13 place through condensate tank 7 and drainage pipe 9, gas dehumidifies through active carbon hygroscopic agent 4 and is discharged by ammonia outlet N2 after microfiltration core 3 dedusting, completes the dehumidifying containing wet ammonia and purification.After having operated containing wet ammonia dehumidifying dehydration, removal impurity, open leakage fluid dram N3, discharged the liquid in housing 1, independence regeneration or replacing can have been carried out according to the consumptive material of need of production to each sub-housing inner filtration assembly simultaneously.
The multistage dehumidifying filter of this integral type ammonia, according to user's requirement, with identical structural shape, can manufacture plurality of specifications, is applicable to different gas treatment amount, different operating pressures, different pipeline diameters; Except being specially applicable to ammonia dehumidifying dehydration, the removal of impurity, be applicable to dehumidifying and the purification of gas gas equally.
Obviously, those skilled in the art can carry out various change and modification to the utility model and not depart from spirit and scope of the present utility model.Like this, if these amendments of the present utility model and modification belong within the scope of the utility model claim and equivalent technologies thereof, then the utility model is also intended to comprise these change and modification.
Claims (8)
1. the multistage dehumidifying filter of integral type ammonia, comprise the hollow housing with bottom ammonia entrance and upper end ammonia outlet be arranged on bracing frame, characterized by further comprising the cyclonic separation assembly, gas-liquid separation assembly, charcoal absorption assembly and point dirt filter assemblies that are set in turn in enclosure interior from bottom to top; Wherein
Described cyclonic separation assembly comprises tangential admission cyclone pipe, baffle plate is revolved in central drain pipe, swirl vane, resistance, tangential admission cyclone pipe is connected with central drain pipe, swirl vane is fixedly installed on central drain pipe upper end, and resistance is revolved baffle plate and is fixedly installed on central drain pipe lower end;
Described gas-liquid separation assembly comprises horizontal stainless steel gas-liquid separate mesh, condensate tank, drainage pipe; Described condensate tank is positioned in inner walls and arranges ringwise below stainless steel gas-liquid separate mesh, and is connected to housing bottom by drainage pipe;
Described charcoal absorption assembly comprises active carbon hygroscopic agent;
Described point of dirt filter assemblies is included in the filter cartridge seat of horizontally set on housing, and is arranged at the multiple microfiltration cores in described filter cartridge seat;
Ammonia entrance is passed through after tangential admission cyclone pipe cyclonic separation containing wet ammonia, liquid drains into housing bottom through central drain pipe, gas forms centrifugal effect by rotating at stainless steel gas-liquid separate mesh interior orientation after swirl vane, complete secondary gas-liquid separation, liquid drains into housing bottom through condensate pipe and drainage pipe, and gas has been discharged dehumidifying and the purification of gas after the dehumidifying of active carbon hygroscopic agent and microfiltration core removing impurity by ammonia outlet.
2. the multistage dehumidifying filter of integral type ammonia according to claim 1, it is characterized in that, described housing bottom is provided with a sewage draining exit.
3. the multistage dehumidifying filter of integral type ammonia according to claim 1, is characterized in that, described housing upper is provided with a differential manometer mouth.
4. the multistage dehumidifying filter of integral type ammonia according to claim 1, is characterized in that, is provided with compactor between described gas-liquid separation assembly and charcoal absorption assembly.
5. the multistage dehumidifying filter of integral type ammonia according to claim 1, is characterized in that, described resistance is revolved baffle plate and is set to two panels and right-angled intersection composition.
6. the multistage dehumidifying filter of integral type ammonia according to claim 1, is characterized in that, described case top adopts ellipsoidal head, and described housing bottom adopts conical head.
7. the multistage dehumidifying filter of integral type ammonia according to claim 1, is characterized in that, described housing comprises the sub-housing of multistage, passes through Flange joint between described sub-housing.
8. the multistage dehumidifying filter of the integral type ammonia according to claim 1 ~ 7 any one, is characterized in that, described housing comprises by the first sub-housing of Flange joint, the second sub-housing, the 3rd sub-housing and the 4th sub-housing; Described ammonia outlet is arranged on the first sub-housing, described point of dirt filter assemblies is arranged on described second sub-enclosure interior, described charcoal absorption assembly is arranged on described 3rd sub-enclosure interior, described gas-liquid separation assembly and cyclonic separation assembly are arranged on described 4th sub-enclosure interior, and described ammonia entrance is arranged on described 4th sub-housing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420724463.8U CN204275745U (en) | 2014-11-26 | 2014-11-26 | The multistage dehumidifying filter of integral type ammonia |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420724463.8U CN204275745U (en) | 2014-11-26 | 2014-11-26 | The multistage dehumidifying filter of integral type ammonia |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204275745U true CN204275745U (en) | 2015-04-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420724463.8U Expired - Fee Related CN204275745U (en) | 2014-11-26 | 2014-11-26 | The multistage dehumidifying filter of integral type ammonia |
Country Status (1)
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| CN (1) | CN204275745U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104971553A (en) * | 2015-07-21 | 2015-10-14 | 中国科学院广州能源研究所 | Multi-level composite efficient gas-liquid separation device |
| CN105435613A (en) * | 2015-12-17 | 2016-03-30 | 江苏新奇环保有限公司 | Exhaust gas processing device |
| AT517269A3 (en) * | 2015-06-12 | 2017-11-15 | Frick Adolf | Flue gas filter system |
| CN109569165A (en) * | 2019-01-18 | 2019-04-05 | 安徽沃特普尔节能科技有限公司 | A kind of reciprocal device for filtering other ions in ammonia |
-
2014
- 2014-11-26 CN CN201420724463.8U patent/CN204275745U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT517269A3 (en) * | 2015-06-12 | 2017-11-15 | Frick Adolf | Flue gas filter system |
| AT517269B1 (en) * | 2015-06-12 | 2017-11-15 | Frick Adolf | Flue gas filter system |
| CN104971553A (en) * | 2015-07-21 | 2015-10-14 | 中国科学院广州能源研究所 | Multi-level composite efficient gas-liquid separation device |
| CN105435613A (en) * | 2015-12-17 | 2016-03-30 | 江苏新奇环保有限公司 | Exhaust gas processing device |
| CN109569165A (en) * | 2019-01-18 | 2019-04-05 | 安徽沃特普尔节能科技有限公司 | A kind of reciprocal device for filtering other ions in ammonia |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150422 Termination date: 20171126 |