CN108479388A - Intensive compressed air purification system - Google Patents
Intensive compressed air purification system Download PDFInfo
- Publication number
- CN108479388A CN108479388A CN201810578452.6A CN201810578452A CN108479388A CN 108479388 A CN108479388 A CN 108479388A CN 201810578452 A CN201810578452 A CN 201810578452A CN 108479388 A CN108479388 A CN 108479388A
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- air inlet
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- reaction tube
- inlet pipe
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- 238000004887 air purification Methods 0.000 title claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 70
- 238000010438 heat treatment Methods 0.000 claims abstract description 26
- 230000002687 intercalation Effects 0.000 claims abstract description 7
- 238000009830 intercalation Methods 0.000 claims abstract description 7
- 238000003780 insertion Methods 0.000 claims description 12
- 230000037431 insertion Effects 0.000 claims description 12
- 230000000903 blocking effect Effects 0.000 claims description 11
- 239000003054 catalyst Substances 0.000 claims description 9
- 239000011490 mineral wool Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 3
- 238000000746 purification Methods 0.000 abstract description 9
- 238000012423 maintenance Methods 0.000 abstract description 7
- 230000009975 flexible effect Effects 0.000 abstract description 5
- 230000000694 effects Effects 0.000 description 8
- 239000000919 ceramic Substances 0.000 description 6
- 238000013461 design Methods 0.000 description 6
- 229910052573 porcelain Inorganic materials 0.000 description 5
- 238000007906 compression Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 230000006835 compression Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 2
- 230000003111 delayed effect Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 206010053615 Thermal burn Diseases 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/88—Handling or mounting catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/06—Polluted air
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses a kind of intensive compressed air purification systems, including babinet and the preheating heat exchanger and reactor that are arranged in babinet, it is provided with compressed air inlet and compressed air outlet on the outer wall of the babinet, pre-heating intaking mouth, preheating gas outlet, heat exchange air inlet and heat exchange gas outlet are equipped on the preheating heat exchanger, the reactor includes reaction tube and the coaxially air inlet pipe and an air outlet pipe in intercalation reaction cylinder；The compressed air inlet and pre-heating intaking mouth, the outer end of preheating gas outlet and air inlet pipe, escape pipe outer end and heat exchange air inlet and heat exchange gas outlet and compressed air outlet between connected by connecting pipe.Using intensive compressed air purification system provided by the invention, simple and compact, compact, using flexible is good purification, efficient, and use cost is cheap, and service life is long, and maintenance cost is low, can sustainedly and stably provide the clean compressed air of oil-free.
Description
Technical field
The invention belongs to air compressor technical fields, and in particular to a kind of intensive style compressed air purification system.
Background technology
It is high to the quality requirements of compressed air in special industries such as electronics, food, medicine, this lubricated type air compressor machine without
Method meets quality requirement of these industries to compressed air.Contain although traditional oil-free air compressor can control compressed air oil
Amount, but manufacturing cost is high, and service life also only has oil lubricating type air compressor half, not only extremely uneconomical, and in work
Industry production area itself just contains greasy dirt in air, even if oilless air compressor can control compression process and not bring oil, compressed air into
Oil content also can be due to air oil-containing itself far more than standard.
Occur the compressed air cleaner using catalysis oxidation as technological core currently on the market, can realize oil removing, kill
Bacterium, purified compressed air in cooling procedure caused by condensate liquid, no Residual oil, can direct emission, can be entire work
The air source of factory is purified.It is that only a or two a end station wants the cleanliness factor of compressed air now with a kind of demand
It asks, other stations have no demand, and therefore, existing compressed air purification system seems and impracticable not only ties in such a scenario
Structure is complicated, and equipment pipe connection length, equipment volume is big, and acquisition cost is higher, and integrated low, it is difficult to transport, using flexible
Property is poor.
Invention content
In order to solve the above technical problems, the present invention provides a kind of intensive compressed air purification system, have it is simple in structure,
Device is small and exquisite, using flexible, good purification, efficient, and use cost is cheap, and service life is long, the low feature of maintenance cost,
The clean compressed air of oil-free can be sustainedly and stably provided.
To achieve the above object, technical solution of the present invention is as follows：
A kind of intensive style compressed air purification system, is characterized by：Including babinet and it is arranged at pre- in babinet
Heat exchanger and reactor are provided with compressed air inlet and compressed air outlet on the outer wall of the babinet, described pre-
Heat exchanger is equipped with pre-heating intaking mouth, preheating gas outlet, heat exchange air inlet and heat exchange gas outlet, and the reactor includes reaction
Cylinder and the coaxially air inlet pipe and an air outlet pipe in intercalation reaction cylinder；The compressed air inlet and pre-heating intaking mouth preheat out
The outer end of gas port and air inlet pipe, escape pipe outer end and heat exchange air inlet and heat exchange gas outlet and compressed air outlet between
It is connected by connecting pipe.
Using the above structure, compressed air to be clean accesses compressed air inlet, after preheated heat exchanger preheating from into
Tracheae is introduced into reaction tube, is cleaned in reaction tube, and purified compressed air introduces preheating heat exchanger through escape pipe and carries out
The compressed air of heat exchange, purification after cooling is exported from compressed air outlet；Pass through the air inlet pipe and an air outlet pipe of coaxial arrangement
Structure design, not only ensure that the clean-up effect and efficiency to compressed air, but also enormously simplify air inlet pipe and an air outlet pipe anti-
The structure outside cylinder is answered, manufacturing cost is reduced, reduces space hold, the connection of preheating heat exchanger and reactor is made more to step up
It gathers, Miniaturization Design can be completed, preheating heat exchanger and reactor are integrated in a small-sized babinet, single terminal end is met
The use demand of station, using flexible, purchase and maintenance cost are cheap, long lifespan；Meanwhile heat exchange design in, not merely with
Preheating heat exchanger preheats compressed air to be clean, moreover, by the design being sleeved on outside escape pipe in air inlet pipe, it can
Secondary preheating is carried out using the hot-air in escape pipe, the pre- thermal efficiency greatly improved, effectively reduce energy consumption, improve purification
Efficiency.
As preferred：It is sleeved in air inlet pipe outside the escape pipe, and is stayed between the inner wall of escape pipe and the outer wall of air inlet pipe
There is gap, from one end intercalation reaction cylinder of reaction tube, the insertion end of the air inlet pipe extends to the air inlet pipe and an air outlet pipe
The other end of reaction tube, the end of the escape pipe insertion end is close to one end that the reaction tube is connect with escape pipe.Using folding
The purifying paths design for returning formula, not only ensure that purification efficiency, but also improve clean-up effect.
As preferred：The escape pipe includes the branch pipe for being responsible for and being arranged on supervisor's outer wall and communicating therewith, institute
It states air inlet pipe to be threaded through on supervisor, the outer end of the supervisor is provided with the envelope for blocking gap between supervisor and air inlet pipe
Blocking component, the branch pipe is between reaction tube and blocking component.Using the above structure, it can be achieved that compressed air is in reaction tube
The same end passes in and out, and preheating heat exchanger is placed and reactor top, the connection of preheating gas outlet and air inlet pipe and heat exchange air inlet
It is realized with the same side that is connected to of escape pipe, greatly reduces the length of the connecting pipe between reactor and preheating heat exchanger,
To play the left and right reduced system pressure drop and reduce manufacturing cost.
As preferred：The blocking component includes pipe cap, seal member and the support element for being used to support seal member, described
Support element is located on supervisor's inner wall other than branch pipe, the seal member from the outer end of supervisor be embedded in, and be sleeved on outside into
On tracheae, the pipe cap is mounted on the outer end of supervisor, for compressing the seal member.Using the above structure, simple in structure
Reliably, it can effectively ensure that the air-tightness between inlet/outlet pipe, while easy to disassemble, be conducive to repair and maintenance.
As preferred：The babinet includes outer housing and is arranged in outer housing and is used to support the shell branch of outer housing
Frame, the preheating heat exchanger are fixedly mounted on by heat exchanger bracing frame in shell holder, and the reaction tube passes through reaction tube branch
Frame is fixedly mounted in shell holder.Using the above structure, shell holder can not only be provided with outer housing the support of effect, and
And it is easily installed fixed preheating heat exchanger and reactor.
As preferred：Heat-insulated rock wool is filled in the babinet, which coats the preheating heat exchanger and reaction
Cylinder.Using the above structure, the effect kept the temperature to preheating heat exchanger and reactor has delayed scattering and disappearing for heat.
As preferred：It is provided with electric cabinet in the babinet, which is located at the outside of heat-insulated rock wool, described automatically controlled
The shell of case is made of heat-barrier material.Using the above structure, heat shielding is both carried out to electric cabinet by heat-insulated rock wool, by passing through
Itself shell carries out heat shielding, ensure that the normal work of electric cabinet.
As preferred：The inside of the reaction tube is divided into apex cavity area, reaction zone, heating zone and bottom from top to bottom
Cavity zone is filled with catalyst in the reaction zone, and heat medium is provided in the heating zone, and the air inlet pipe is inserted into
The end at end is located in the bottom cavity area, and the end of the escape pipe insertion end is located in the apex cavity area.More than
The compressed air of structure, oil-containing is sent from air inlet pipe to the bottom of reaction tube, heating zone is first passed through after turning back from bottom to top, external
Ceramic heat circle and accumulation of heat porcelain ball under the action of heating reach reaction temperature, subsequently into reaction zone catalyst work
With lower generation oxidation reaction, the clean compressed air of oil is entirely free of after purification from the discharge of the escape pipe on top, ensure that net
Change efficiency and clean-up effect.
As preferred：The reaction tube outer cover be equipped with heater, the heater at least covering part reaction zone and
Part heating zone.Using the above structure, compressed air to be clean can be made to be rapidly achieved reaction temperature, ensure that empty to compression
The clean-up effect and efficiency of gas.
As preferred：The reaction tube includes cylinder and lid closes the cover in the cylinder upper end, the air inlet pipe and goes out
Tracheae is downwardly into from cover in reaction tube, and the insertion end of the air inlet pipe close to the bottom of cylinder, insert by the escape pipe
Enter end close to cover.Using the above structure, not only easy to repair, maintenance or inside reactor device had been replaced, but also used down into upper
The purifying paths design for going out Zigzag type, while ensure that purification efficiency, improves clean-up effect.
Compared with prior art, the beneficial effects of the invention are as follows：
Using intensive compressed air purification system provided by the invention, structure novel, it is easy to accomplish, simple and compact, body
Small and exquisite, the using flexible of product, good purification, efficient, use cost is cheap, and service life is long, and maintenance cost is low, can continue
The clean compressed air of oil-free is steadily provided.
Description of the drawings
Fig. 1 is the structural diagram of the present invention；
Fig. 2 is the structural schematic diagram of reactor；
Fig. 3 is the structural schematic diagram that reactor removes catalyst and heat medium.
Specific implementation mode
The invention will be further described with attached drawing with reference to embodiments.
As shown in Figure 1, a kind of intensive style compressed air purification system, including babinet 300 and be arranged in babinet 300
Preheating heat exchanger 400 and reactor, compressed air inlet 310 and compressed air are provided on the outer wall of the babinet 300
Outlet 320 is equipped with pre-heating intaking mouth 410, preheating gas outlet 420,430 and of heat exchange air inlet on the preheating heat exchanger 400
Exchange heat gas outlet 440, and the reactor includes reaction tube 100 and coaxially the air inlet pipe 210 in intercalation reaction cylinder 100 and goes out
Tracheae 220.The compressed air inlet 310 and pre-heating intaking mouth 410, preheating gas outlet 420 and air inlet pipe 210 outer end, go out
Pass through connection between the outer end and heat exchange air inlet 430 and heat exchange gas outlet 440 and compressed air outlet 320 of tracheae 220
Pipeline 500 connects.
The compressed air of oil-containing accesses compressed air inlet 310, and preheated heat exchanger 400 draws after preheating from air inlet pipe 210
Enter in reaction tube, first heated in reaction tube, then by catalysis oxidation, purified compressed air introduces pre- through escape pipe 220
Heat exchanger 400 carries out heat exchange, and the compressed air of purification after cooling is exported from compressed air outlet 320.
Fig. 1 is referred to, the babinet 300 includes outer housing 301 and setting in outer housing 301 and is used to support shell
The shell holder 302 of body 301, the shell holder 302 are tower structure, the inner wall of support housing body 301.
Further, the preheating heat exchanger 400 is located at the top of reactor, makes preheating gas outlet 420 and heat exchange air inlet
Mouthfuls 430 with the air inlet pipe 210 of reactor and 220 distance of escape pipe closer to, to keep the structure of complete equipment compacter, volume
It is more compact.To ensure that the reliability of the installation of preheating heat exchanger 400, the preheating heat exchanger 400 pass through heat exchanger bracing frame 303
It is fixedly mounted in shell holder 302, the heat exchanger bracing frame 303 is trabeation, is fixed on shell holder 302
Top, the preheating heat exchanger 400 are fixed in heat exchanger bracing frame 303, make the preheating gas outlet of heat exchanger bracing frame 303
420 are located at the surface of air inlet pipe 210, can shorten the length of connecting pipe 500, keep overall structure compacter, volume is more
Add small and exquisite.
The reaction tube 100 is fixedly mounted on by multiple reaction tube stents 304 in shell holder 302.It is simple in structure, surely
It is fixed reliable.
Further, heat-insulated rock wool 700 is filled in the babinet 300, which coats the pre-heating heat-exchanging
Device 400 and reaction tube 100.To the effect that preheating heat exchanger 400 and reactor are kept the temperature, scattering and disappearing for heat is delayed.Also, institute
It states and is provided with electric cabinet 600 in babinet 300, which is located at the outside of heat-insulated rock wool 700, the shell of the electric cabinet 600
Body is made of heat-barrier material, both heat shielding is carried out to electric cabinet 600 by heat-insulated rock wool 700, by being carried out by itself shell
Heat shielding ensure that the normal work of electric cabinet 600.Further, the electric cabinet 600 is preferably provided inside babinet 300
The top in space keeps surrounding environment temperature relatively low, improves the reliable of electric cabinet 600 far from the big reactor of calorific value
Property.
Fig. 1~Fig. 3 is referred to, the reactor includes reaction tube 100, which includes cylinder 100a and lid
Close the cover 100b in the upper ends cylinder 100a.It is equipped on the cover 100b sleeved into escape pipe 200, this is sleeved
Include air inlet pipe 210 and the escape pipe 220 that is sleeved on outside in air inlet pipe 210 into escape pipe 200, the outer wall of the air inlet pipe 210 with go out
There are gaps between the inner wall of tracheae 220, and the air inlet pipe 210 and escape pipe 220 are from cover 100b intercalation reactions cylinder 100
In, close to the top of 100 inner cavity of reaction tube, upper end is pierced by the cover 100b, the air inlet pipe for the lower end of the escape pipe 220
210 lower end is pierced by close to the bottom of 100 inner cavity of reaction tube, upper end from the upper end of the escape pipe 220.Compression to be clean is empty
Gas imports the bottom of cylinder 100a through air inlet pipe 210, is flowed up in cylinder 100a, and be cleaned, and purified compression is empty
Gas enters the gap between air inlet pipe 210 and escape pipe 220, and is exported from escape pipe 220.It is pointed out that air inlet pipe 210
Being inserted into from 100 bottom of reaction tube with escape pipe 220 can also implement, and the above mounting means, which turns around, can be realized.
Fig. 1 and Fig. 2 are referred to, the escape pipe 220 includes the branch be responsible for 221 and be arranged on 221 outer wall of the supervisor
Pipe 222, the branch pipe 222 are connected to supervisor 221.The air inlet pipe 210 is threaded through on supervisor 221, in the outer end of the supervisor 221
Portion is provided with the blocking component 230 for blocking gap between supervisor 221 and air inlet pipe 210, and the branch pipe 222 is located at reaction tube
Between 100 top and blocking component 230.
Fig. 2 is referred to, the blocking component 230 is including pipe cap 231, seal member 232 and is used to support seal member 232
Support element 233, the support element 233 is located on 221 inner wall of the supervisor of the top of branch pipe 222, the seal member 232 from
The outer end insertion of supervisor 221, and be sleeved on outside in air inlet pipe 210, the pipe cap 231 is mounted on the outer end of supervisor 221, is used for
The seal member 232 is compressed, which is graphite packing.
The reaction zone 101 being distributed up and down and heating are formed between the inner wall and the outer wall of air inlet pipe 210 of the reaction tube 100
Area 102 is filled with catalyst 105 in the reaction zone 101, and heat medium 106 is provided in the heating zone 102, should
Heat medium 106 is porcelain ball, which is filled in heating zone 102.Heater is housed in the outer cover of the reaction tube 100
107, which is ceramic heat circle, the ceramic heat circle covered section reaction zone 101 and part heating zone 102, energy
Enough porcelain balls and catalyst 105 are heated.It is heated using ceramic heat circle, heat transfer is fast, and generate heat uniform and the operation is stable, can carry
For stable heating environment, temperature does not leak when ceramic heat circle heats, external touch non-scald on hand, work circumstances safe it is reliable and
Electric energy is saved, in addition the installation, maintenance of ceramic heat circle is convenient, and service life is long.
Fig. 2 is referred to, the supporting screening plate 108 being horizontally mounted, 109 and of exhaust screen are provided in the reaction tube 100
It is vented pressing plate 110, the inside of reaction tube 100 is divided into apex cavity area 104, reaction zone 101, heating zone 102 from top to bottom
It is located in the bottom cavity area 103 with the end in bottom cavity area 103,210 insertion end of the air inlet pipe, the escape pipe 220
The end of insertion end is located in the apex cavity area 104.Wherein, supporting screening plate 108 is located at heating zone 102 and bottom cavity area
Between 103, it is used to support porcelain ball, exhaust screen 109 is used to support catalyst between reaction zone 101 and heating zone 102
105, exhaust pressing plate 110 is between apex cavity area 104 and reaction zone 101, for being compacted catalyst 105.
Refer to Fig. 1 and Fig. 2, blowdown valve 112 be installed in the bottom of the reaction tube 100, the blowdown valve 112 with react
The inside connection of cylinder 100, discharges pollutants for concentrating.Multiple thermocouples are provided on the outer wall of the reaction tube 100 to survey
Prospect hole 113, the thermocouple assay hole 113 are connected to the inside of reaction tube 100, for monitor in reaction zone 101 catalyst and
The temperature of porcelain ball in heating zone 102.
Finally, it should be noted that foregoing description is only the preferred embodiment of the present invention, the ordinary skill people of this field
Member under the inspiration of the present invention, without prejudice to the purpose of the present invention and the claims, can make table as multiple types
Show, such transformation is each fallen within protection scope of the present invention.
Claims (10)
1. a kind of intensive style compressed air purification system, it is characterised in that：Including babinet (300) and it is arranged at babinet
(300) preheating heat exchanger (400) in and reactor, compressed air inlet is provided on the outer wall of the babinet (300)
(310) and compressed air outlet (320) pre-heating intaking mouth (410), preheating outlet, are equipped on the preheating heat exchanger (400)
It mouthful (420), heat exchange air inlet (430) and exchanges heat gas outlet (440), the reactor includes reaction tube (100) and coaxially
Air inlet pipe (210) in intercalation reaction cylinder (100) and escape pipe (220)；
The compressed air inlet (310) and pre-heating intaking mouth (410), preheating gas outlet (420) and air inlet pipe (210) outside
End, escape pipe (220) outer end and heat exchange air inlet (430) and heat exchange gas outlet (440) and compressed air outlet (320) it
Between pass through connecting pipe (500) connect.
2. intensive style compressed air purification system according to claim 1, it is characterised in that：The escape pipe (220) is outside
It is sleeved in air inlet pipe (210), and there are gap, the air inlets between the inner wall of escape pipe (220) and the outer wall of air inlet pipe (210)
(210) and escape pipe (220) are managed from one end intercalation reaction cylinder (100) of reaction tube (100), the air inlet pipe (210) is inserted
Enter the other end that end extends to reaction tube (100), the end of escape pipe (220) insertion end is close to the reaction tube (100)
The one end being connect with escape pipe (220).
3. intensive style compressed air purification system according to claim 2, it is characterised in that：Escape pipe (220) packet
The branch pipe (222) for including supervisor (221) and being arranged on supervisor (221) outer wall and communicating therewith, the air inlet pipe (210) are worn
Be located on supervisor (221), the outer end of the supervisor (221) be provided with for block supervisor (221) and air inlet pipe (210) it
Between gap blocking component (230), the branch pipe (222) is located between reaction tube (100) and blocking component (230).
4. intensive style compressed air purification system according to claim 3, it is characterised in that：The blocking component (230)
Including pipe cap (231), seal member (232) and the support element (233) for being used to support seal member (232), the support element
(233) it is located on the supervisor (221) inner wall other than branch pipe (222), the seal member (232) is outside supervisor (221)
End is embedded in, and is sleeved on outside in air inlet pipe (210), and the pipe cap (231) is mounted on the outer end of supervisor (221), for compressing
The seal member (232).
5. intensive style compressed air purification system according to claim 1, it is characterised in that：The babinet (300) includes
Outer housing (301) and the shell holder (302) for being arranged in outer housing (301) and being used to support outer housing (301), it is described pre-
Heat exchanger (400) is fixedly mounted on by heat exchanger bracing frame (303) in shell holder (302), and the reaction tube (100) is logical
Reaction tube stent (304) is crossed to be fixedly mounted in shell holder (302).
6. intensive style compressed air purification system according to claim 1, it is characterised in that：It is filled out in the babinet (300)
Filled with heat-insulated rock wool (700), which coats the preheating heat exchanger (400) and reaction tube (100).
7. intensive style compressed air purification system according to claim 6, it is characterised in that：In the babinet (300)
It is provided with electric cabinet (600), which is located at the outside of heat-insulated rock wool (700), the shell of the electric cabinet (600)
It is made of heat-barrier material.
8. intensive style compressed air purification system according to claim 1, it is characterised in that：The reaction tube (100)
Inside is divided into apex cavity area (104), reaction zone (101), heating zone (102) and bottom cavity area (103) from top to bottom,
It is filled with catalyst (105) in the reaction zone (101), heat medium (106), institute are provided in the heating zone (102)
The end for stating air inlet pipe (210) insertion end is located in the bottom cavity area (103), the end of escape pipe (220) insertion end
In the apex cavity area (104).
9. intensive style compressed air purification system according to claim 8, it is characterised in that：In the reaction tube (100)
Outer cover be equipped with heater (107), the heater (107) at least covering part reaction zone (101) and part heating zone
(102)。
10. intensive style compressed air purification system according to claim 1, it is characterised in that：Reaction tube (100) packet
It includes cylinder (100a) and covers the cover (100b) closed in the upper end cylinder (100a), the air inlet pipe (210) and escape pipe
(220) it is downwardly into reaction tube (100) from cover (100b), the insertion end of the air inlet pipe (210) is close to cylinder
The bottom of (100a), the insertion end of the escape pipe (220) is close to cover (100b).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810578452.6A CN108479388A (en) | 2018-06-05 | 2018-06-05 | Intensive compressed air purification system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810578452.6A CN108479388A (en) | 2018-06-05 | 2018-06-05 | Intensive compressed air purification system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108479388A true CN108479388A (en) | 2018-09-04 |
Family
ID=63342307
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810578452.6A Pending CN108479388A (en) | 2018-06-05 | 2018-06-05 | Intensive compressed air purification system |
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| CN (1) | CN108479388A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109692569A (en) * | 2019-02-21 | 2019-04-30 | 重庆鲍斯净化设备科技有限公司 | Hydrocarbon remover, detection system and its detection method in gas source |
| CN114288853A (en) * | 2022-02-11 | 2022-04-08 | 重庆鲍斯净化设备科技有限公司 | Compressed air oil removal and purification system |
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| CN106268304A (en) * | 2016-09-20 | 2017-01-04 | 重庆鲍斯可燃气工程有限公司 | Compressed air purification system and using method thereof |
| CN208542031U (en) * | 2018-06-05 | 2019-02-26 | 重庆鲍斯可燃气工程有限公司 | The compressed air purification system of high integration |
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2018
- 2018-06-05 CN CN201810578452.6A patent/CN108479388A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104998491A (en) * | 2015-07-23 | 2015-10-28 | 北京石油化工工程有限公司 | High pressure hot separator for suspension bed hydrogenation |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109692569A (en) * | 2019-02-21 | 2019-04-30 | 重庆鲍斯净化设备科技有限公司 | Hydrocarbon remover, detection system and its detection method in gas source |
| CN109692569B (en) * | 2019-02-21 | 2024-04-23 | 重庆鲍斯净化设备科技有限公司 | Hydrocarbon remover in gas source, detection system and detection method thereof |
| CN114288853A (en) * | 2022-02-11 | 2022-04-08 | 重庆鲍斯净化设备科技有限公司 | Compressed air oil removal and purification system |
| CN114288853B (en) * | 2022-02-11 | 2024-05-14 | 重庆鲍斯净化设备科技有限公司 | Compressed air deoiling and purifying system |
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Country or region after: China Address after: Building 4, No. 8 Jiangxia Road, Nan'an District, Chongqing, 400072 Applicant after: CHONGQING BAOSI PURIFICATION EQUIPMENT TECHNOLOGY Co.,Ltd. Address before: Building 4, No. 8 Jiangxia Road, Nan'an District, Chongqing, 401336 Applicant before: CHONGQING BAOSI FLAMMABLE GAS ENGINEERING Co.,Ltd. Country or region before: China |