CN106268536A - Reactor for compressed air purification system - Google Patents

Reactor for compressed air purification system Download PDF

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Publication number
CN106268536A
CN106268536A CN201610834730.0A CN201610834730A CN106268536A CN 106268536 A CN106268536 A CN 106268536A CN 201610834730 A CN201610834730 A CN 201610834730A CN 106268536 A CN106268536 A CN 106268536A
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CN
China
Prior art keywords
cylinder
compressed air
reactor
purification system
air purification
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610834730.0A
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Chinese (zh)
Inventor
瞿赠名
代吉雨
涂巧灵
樊孟
张世伟
杜泳川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Baosi Flammable Gas Engineering Co Ltd
Original Assignee
Chongqing Baosi Flammable Gas Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by Chongqing Baosi Flammable Gas Engineering Co Ltd filed Critical Chongqing Baosi Flammable Gas Engineering Co Ltd
Priority to CN201610834730.0A priority Critical patent/CN106268536A/en
Publication of CN106268536A publication Critical patent/CN106268536A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0242Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical
    • B01J8/025Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical in a cylindrical shaped bed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8668Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/88Handling or mounting catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0285Heating or cooling the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0292Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds with stationary packing material in the bed, e.g. bricks, wire rings, baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132Tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00884Means for supporting the bed of particles, e.g. grids, bars, perforated plates

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The invention discloses a kind of reactor for compressed air purification system, including cylinder and the bung assembly that is fastened on this cylinder, the stage casing of described inner barrel is the reaction zone for loading catalyst filling, it is provided with compressed air inlet on cylinder above described reaction zone, it is provided with compressed air outlet on the cylinder of lower section, the bottom of described cylinder being provided with sewage draining exit, is provided with and adds heat pipe on this cylinder, this heating part adding heat pipe is positioned at reaction zone.Use above structure, can the most in all case purify the compressed air of oil-free, disclosure satisfy that all trades and professions strict demand to Compressed Air degree, and the impact of the factors such as purification efficiency and working life air oil content, ambient temperature and humidity the most by compression, has purified treatment ability strong, and clean-up effect is reliable and stable, service life is long, the feature of operation and maintenance low cost, the water of discharge does not pollutes the environment, and has high practicality and market value.

Description

Reactor for compressed air purification system
Technical field
The invention belongs to pneumatic plant technical field, be specifically related to a kind of reaction for compressed air purification system Device.
Background technology
Air compressor is the basic product of the modernization of industry, and air compressor is suffered from needing widely by all trades and professions Asking, along with living standard and the raising of scientific and technological level, the compressed air quality that air compressor is produced by people requires the most more to come The highest.
Especially in the industry such as medical treatment and food, compressed-air actuated degree of purification is required higher, it is desirable to compressed air is absolute Oil-free, without granulometric impurity and be dried.And in the compressed air that provided of existing oil lubricating type air compressor oil content is significantly Exceed standard, it is impossible to meet prescription, raw material and product and production process etc. are polluted, and the oil in compressed air exists The organic acid formed after high-temperature gasification can corrode air compressor, brings harm to compressed air source unit and pneumatic system.On market Oil-free air compressor manufacturing cost is high, and only has oil lubricating type air compressor half service life, the most uneconomical.Cause This, occur in that for purifying the compressed-air actuated cleaning system that air compressor machine provides in recent years, and these cleaning systems be all to use Being mechanically decoupled filtration reactor and lyophilization, carry out the mode of activated carbon filtration the most again, this purification style is not only Parts are various, and structure is complicated, and purification efficiency is low.At present, the filtration of any a compressed air purification system on market Reactor all exists that filter efficiency is low, service life is short, need the problems such as frequent maintenance, and the mistake of these filtration reactors Filter not sufficiently effective, it is impossible to the clean compressed air of complete oil-free is provided, thus all trades and professions cannot be met to compressed-air actuated matter Amount requirement, solving problem above becomes the task of top priority.
Summary of the invention
For solving above technical problem, the present invention provides a kind of reactor for compressed air purification system, its structure Simple and reliable, disposal ability is strong, and service life is long, and maintenance cost is low, using the teaching of the invention it is possible to provide oil-free, the compression of cleaning without granulometric impurity Air.
For achieving the above object, technical solution of the present invention is as follows:
A kind of reactor for compressed air purification system, it is characterized by: includes cylinder and is fastened on this cylinder On bung assembly, the stage casing of described inner barrel is the reaction zone for loading catalyst filling, above described reaction zone Cylinder on be provided with compressed air inlet, the cylinder of lower section is provided with compressed air outlet, sets in the bottom of described cylinder Being equipped with sewage draining exit, be provided with and add heat pipe on this cylinder, this heating part adding heat pipe is positioned at reaction zone.
Using above structure, simple and reliable, the compressed air of oil-containing is filled out at catalyst from the reacted district of compressed air inlet There is oxidation reaction under the effect of material, after purification, discharge the clean compressed air of complete oil-free from compressed air outlet;This The bright compressed air that can the most in all case purify oil-free, it is possible to meet all trades and professions clean to compressed air The strict demand of cleanliness, and purification efficiency and working life air oil content, ambient temperature the most by compression in rated range With the impact of the factor such as humidity, having purified treatment ability strong, clean-up effect is reliable and stable, and service life is long, operation and maintenance The feature of low cost, and discharge water do not pollute the environment, there is high practicality and market value.
As preferably: be provided with the supporting construction for supporting catalyst filling in the bottom of described reaction zone, this support is tied Structure includes bracer, the gripper shoe being placed on this bracer that are arranged on described cylinder inboard wall and is arranged on this gripper shoe top The exhaust screen of the upper and lower laid out in parallel of at least two-layer, be equipped with at least one of which first described in adjacent two layers between exhaust screen Porcelain ball.Use above structure, it is possible to effectively support catalyst filling, it is ensured that the integrally-built stability in reaction zone.
As preferably: be provided with the compressing structure for being compacted catalyst filling at the top of described reaction zone, this compression is tied Structure includes the air inlet screen of at least upper and lower laid out in parallel of two-layer, is being provided with the second porcelain ball described in adjacent two layers between air inlet screen, Being provided with pressing plate on the top of the described air inlet screen being positioned at top, this pressing plate is connected by fixation kit and described cylinder are fixing. Use above structure, it is possible to be compacted catalyst filling tightly, prevent between the granule of catalyst filling occur play and mutual Friction, effectively slow down catalyst filling efflorescence, improves the service life of catalyst filling so that in compressed air, hydro carbons is miscellaneous Matter catalytic oxidation be able to safe efficient, persistently carry out.
As preferably: described fixation kit includes the first nut that the first bolt, the second bolt and the first bolt adapt And the second nut adapted with the second bolt, described first bolt be placed through after the described air inlet screen at top and pressing plate Its end is welded with the second nut, and this second bolt abuts with described cylinder through the second nut, the axis of this second bolt and The axis of described first bolt is vertical.Using above structure, the described air inlet screen and the pressing plate that are pointed to top carry out spacing, enter One step ensure that the compactness of catalyst filling.
As preferably: be provided with at least one temperature testing organization on described cylinder.Use above structure, examined by temperature Survey mechanism and monitor the temperature in cylinder in real time, add the caloric value of heat pipe with regulation, make reactor temperature be maintained at set point In, it is ensured that the catalytic oxidation even running of oil in compressed air.
As preferably: described temperature testing organization includes being welded on the cushion cap on described cylinder lateral wall and through this cushion cap The thermocouple of the described catalyst filling of rear insertion, this thermocouple is fixedly mounted on described cushion cap by connecting black box.Adopt Using above structure, thermocouple can be firmly fixed in sidewall of reactor, with low cost and can bear higher system pressure.
As preferably: described connection black box includes the cutting ferrule being set on described thermocouple, this cutting ferrule and cushion cap it Between connected by fittings body, this fittings body respectively with cutting ferrule and cushion cap threaded engagement, described thermocouple is arranged with sealing copper The collar, this sealing copper sheathing ring interference is fitted in first conical surface of described cutting ferrule and second conical surface of fittings body.Use above knot Structure, it is ensured that the air-tightness of cylinder.
As preferably: described bung assembly includes being set in the flange of described cylinder upper end and being arranged on the upper of this flange Portion the blind flange adapted with it, be provided with gasket seal between flange and blind flange, same on the top of described blind flange Axle is provided with gland, is provided with the annular protrusion downwardly extended along its axis in the center of this gland lower surface, in described method Orchid covers and is provided with the counterbore adapted with this annular protrusion, between described flange and blind flange and described gland and blind flange it Between all connected by fastening bolt.Use above structure, it is ensured that the air-tightness of cylinder, high temperature resistant, high pressure, and easy accessibility, Service life is long.
As preferably: described in add heat pipe and be positioned at the part in described catalyst filling twist, its upper end is through described heavy Hole passes gland, and interference is pressed with graphite packing in described counterbore.Above structure, graphite packing is used to have extremely strong close Envelope ability, the most high temperature resistant, high pressure, corrosion-resistant;And add the heating part of heat pipe twist, can effectively increase heating surface Long-pending, heating power, makes system realize heating safely and fast.
As preferably: be provided with two on described cylinder and install journal stirrup.Use above structure, by installing journal stirrup to whole Reactor is securely fixed.
Compared with prior art, the invention has the beneficial effects as follows:
Use the reactor for compressed air purification system that the present invention provides, simple in construction, reliable, it is easy to accomplish, Can the most in all case purify the compressed air of oil-free, it is possible to meet all trades and professions to Compressed Air Degree strict demand, and in rated range purification efficiency and working life air oil content the most by compression, ambient temperature and The impact of the factors such as humidity, has purified treatment ability strong, and clean-up effect is reliable and stable, and service life is long, and operation and maintenance becomes This low feature, the water of discharge does not pollutes the environment, and has high practicality and market value.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention;
Fig. 2 is the enlarged drawing in Fig. 1 at A;
Fig. 3 is the enlarged drawing in Fig. 1 at B;
Fig. 4 is the enlarged drawing in Fig. 1 at C;
Fig. 5 is the top view of Fig. 1;
Fig. 6 is cushion cap, connects the black box installation diagram with thermocouple.
Detailed description of the invention
Below in conjunction with embodiment and accompanying drawing, the invention will be further described.
As it is shown in figure 1, a kind of reactor for compressed air purification system, including cylinder 1, this cylinder 1 fastens There is the bung assembly 2 for sealed cylinder 1, the outer wall of cylinder 1 is provided with two relative installation journal stirrups 8.In described cylinder 1 The stage casing in portion is the reaction zone 3 for loading catalyst filling 31, and the cylinder 1 above described reaction zone 3 is provided with compression Air intlet 12, the cylinder 1 of lower section is provided with compressed air outlet 11, and the bottom of described cylinder 1 is provided with sewage draining exit 13, Being provided with on described cylinder 1 and add heat pipe 4, this heating part 41 adding heat pipe 4 is positioned at reaction zone 3, i.e. this heating part 41 In described catalyst filling 31, and twist, it is effectively increased the efficiency of heating surface.Wherein, catalyst filling 31 uses oxidation Catalyst, makes the micro oil in compressed air that oxidation reaction quickly to occur under the effect of catalyst filling 31, generates titanium dioxide Carbon and water, completely eliminate the Hydrocarbon in compressed air and carbon monoxide, finally discharge nothing from compressed air outlet 11 Oil, the compressed air being dried.
Referring to Fig. 1, Fig. 2 and Fig. 5, described bung assembly 2 includes being set in the flange 21 of described cylinder 1 upper end and setting Put at the top of this flange 21 blind flange 22 that adapts with it, by fastening bolt 24 between this flange 21 and blind flange 22 Connect, and between blind flange 22 and flange 21, be provided with gasket seal 25, it is ensured that the air-tightness in cylinder 1.At described flange The top of lid 22 is coaxially arranged with gland 23, is provided with, in the center of this gland 23 lower surface, the ring downwardly extended along its axis Shape projection 231, is provided with the counterbore 221 adapted with this annular protrusion 231, flange 21 and blind flange 22 on described blind flange 22 Between and gland 23 and blind flange 22 between all connected by fastening bolt 24.
Referring to Fig. 1 and Fig. 2, the top adding heat pipe 4 passes gland 23, and interference in counterbore 221 through described counterbore 221 Being pressed with graphite packing, graphite packing has an extremely strong sealability, and the most high temperature resistant, high pressure is corrosion-resistant, it is ensured that cylinder 1 Air-tightness.
Refer to Fig. 1 and Fig. 4, be provided with the supporting construction for supporting catalyst filling 31 in the bottom of described reaction zone 3 6, this supporting construction 6 includes the bracer 64 being welded on described cylinder 1 inwall, is provided with gripper shoe on this bracer 64 61, the exhaust screen 62 of the upper and lower laid out in parallel of two-layer it is provided with on this gripper shoe 61 top, every layer of exhaust screen 62 is at least laminated with One drainage screen, the shape of exhaust screen 62 adapts with the interior shape of described cylinder 1, exhaust screen described in two-layer 62 it Between lay one layer of first porcelain ball 63, the described exhaust screen 62 being positioned at top abuts with described catalyst filling 31, makes this support Structure 6 provides effective support to catalyst filling 31.
Referring to Fig. 1 and Fig. 3, be provided with compressing structure 7 at the top of described reaction zone 3, this compressing structure 7 includes that two-layer is used In the air inlet screen 71 of compacting catalyst filling 31, every layer of air inlet screen 71 is at least laminated with a drainage screen, air inlet screen 71 with The interior shape of described cylinder 1 adapts, and is provided with the second porcelain ball 72 of certain altitude, position between air inlet screen described in two-layer 71 Described air inlet screen 71 in bottom abuts with described catalyst filling 31, on the top of the described air inlet screen 71 being positioned at top Being provided with pressing plate 73, this pressing plate 73 is connected by fixation kit 74 is fixing with described cylinder 1, and described fixation kit 74 includes the first spiral shell The first nut 742 that bolt the 741, second bolt 743 and the first bolt 741 adapt and with the second bolt 743 adapt second Nut 744, described first bolt 741 is welded with in its end after being placed through the described air inlet screen 71 at top and pressing plate 73 Two nuts 744, described first nut 742 coordinates on described air inlet screen 71 and pressing plate 73 that the first bolt 741 is fixed on top, Described second bolt 743 abuts with described cylinder 1 after the second nut 744, the axis of this second bolt 743 and described first The axis of bolt 741 is vertical.First the first bolt 741 is passed air inlet screen 71 and pressing plate 73 during use, then use First nut 742 is tightened, then use the second bolt 743 through the second bolt 743 being welded on the first bolt 741, and with Cylinder 1 abuts, and makes air inlet screen 71 and pressing plate 73 fix, and the most tightly compacted catalyst filling 31 prevents catalyst filling 31 Granule between there is play and phase mutual friction, effectively slow down the efflorescence of catalyst filling 31, improve catalyst filling 31 Service life.
Refer to Fig. 1 and Fig. 6, the sidewall of described cylinder 1 is provided with multiple temperature testing organization 5, this temperature detector Structure 5 is evenly distributed on the sidewall of reaction zone 3 of cylinder 1.Described temperature testing organization 5 includes being welded on described cylinder 1 sidewall On cushion cap 51 and through inserting the thermocouple 52 of described catalyst filling 31 after this cushion cap 51, this thermocouple 52 is by connecting Black box 53 is fixedly mounted on described cushion cap 51.Described connection black box 53 includes being set on described thermocouple 52 Cutting ferrule 531, is connected by fittings body 532 between this cutting ferrule 531 and cushion cap 51, this fittings body 532 respectively with cutting ferrule 531 and cushion cap 51 threaded engagement, are arranged with sealing copper sheathing ring 533 on described thermocouple 52, and this sealing copper sheathing ring 533 interference is fitted in described In first conical surface of cutting ferrule 531 and fittings body 532 second conical surface, not only thermocouple 52 is fixed, also maintains cylinder 1 Air-tightness, simultaneously high temperature high voltage resistant.
The work process of the present invention is as follows:
The thermocouple 52 of temperature testing organization 5 detects the temperature of catalyst filling 31 in real time, and testing result is converted to The signal of telecommunication passes to controller, and controller controls to add the caloric value of heat pipe 4, so that temperature stabilization is at set point in reaction zone In;Compressed air is downwardly into reaction zone 3 after compressed air inlet 12 enters in cylinder 1, in the effect of catalyst filling 31 Under, the micro oil generation oxidation reaction in compressed air generates carbon dioxide and water, the clean oil-free compressed air after purification Discharge from compressed air outlet 11.
It is last it should be noted that foregoing description is only the preferred embodiments of the present invention, the ordinary skill people of this area Member, under the enlightenment of the present invention, on the premise of present inventive concept and claim, can make table as multiple types Show, within such conversion each falls within protection scope of the present invention.

Claims (10)

1. the reactor for compressed air purification system, it is characterised in that: include cylinder (1) and be fastened on this cylinder (1) the bung assembly (2) on, the stage casing of described cylinder (1) inside is the reaction zone (3) being used for loading catalyst filling (31), The cylinder (1) of described reaction zone (3) top is provided with compressed air inlet (12), the cylinder (1) of lower section is provided with pressure Contracting air outlet slit (11), is provided with sewage draining exit (13) in the bottom of described cylinder (1), is provided with and adds heat pipe on this cylinder (1) (4), this heating part (41) adding heat pipe (4) is positioned at reaction zone (3).
Reactor for compressed air purification system the most according to claim 1, it is characterised in that: in described reaction zone (3) bottom is provided with the supporting construction (6) for supporting catalyst filling (31), and this supporting construction (6) includes being arranged on described Propping up bracer (64), the gripper shoe (61) being placed on this bracer (64) and being arranged on this gripper shoe (61) on cylinder (1) inwall The exhaust screen (62) of the upper and lower laid out in parallel of at least two-layer on top, is equipped with between exhaust screen described in adjacent two layers (62) At least one of which the first porcelain ball (63).
Reactor for compressed air purification system the most according to claim 1 and 2, it is characterised in that: described instead The top answering district (3) is provided with the compressing structure (7) for being compacted catalyst filling (31), and this compressing structure (7) includes at least two The air inlet screen (71) of layer laid out in parallel up and down, is provided with the second porcelain ball (72) between air inlet screen described in adjacent two layers (71), Being provided with pressing plate (73) on the top of the described air inlet screen (71) being positioned at top, this pressing plate (73) passes through fixation kit (74) and institute State the fixing connection of cylinder (1).
Reactor for compressed air purification system the most according to claim 3, it is characterised in that: described fixation kit (74) include the first nut (742) that the first bolt (741), the second bolt (743) and the first bolt (741) adapt and with The second nut (744) that second bolt (743) adapts, described first bolt (741) is placed through the described air inlet filter at top Be welded with the second nut (744) after net (71) and pressing plate (73) in its end, this second bolt (743) passes the second nut (744) abut with described cylinder (1) afterwards.
Reactor for compressed air purification system the most according to claim 1, it is characterised in that: at described cylinder (1) at least one temperature testing organization (5) it is provided with.
Reactor for compressed air purification system the most according to claim 5, it is characterised in that: described temperature detection Mechanism (5) includes the cushion cap (51) being welded on described cylinder (1) sidewall and inserts described catalysis afterwards through this cushion cap (51) The thermocouple (52) of agent filler (31), this thermocouple (52) is fixedly mounted on described cushion cap (51) by connecting black box (53) On.
Reactor for compressed air purification system the most according to claim 6, it is characterised in that: described connection seals Assembly (53) includes the cutting ferrule (531) being set on described thermocouple (52), by connecing between this cutting ferrule (531) and cushion cap (51) Head body (532) connect, this fittings body (532) respectively with cutting ferrule (531) and cushion cap (51) threaded engagement, in described thermocouple (52) On be arranged with sealing copper sheathing ring (533), this sealing copper sheathing ring (533) interference be fitted in described cutting ferrule (531) first conical surface and In second conical surface of fittings body (532).
Reactor for compressed air purification system the most according to claim 1, it is characterised in that: described bung assembly (2) include the flange (21) being set in described cylinder (1) upper end and be arranged on the top of this flange (21) and adapt with it Blind flange (22), between this blind flange (22) and flange (21), be provided with gasket seal (25), at described blind flange (22) Top is coaxially arranged with gland (23), is provided with, in the center of this gland (23) lower surface, the annular downwardly extended along its axis Protruding (231), are provided with the counterbore (221) adapted with this annular protrusion (231), described flange on described blind flange (22) (21) and all connected by fastening bolt (24) between blind flange (22) and between described gland (23) and blind flange (22).
Reactor for compressed air purification system the most according to claim 8, it is characterised in that add heat pipe described in: (4) being positioned at the part in described catalyst filling (31) twist, its upper end passes gland (23) through described counterbore (221), And interference is pressed with graphite packing in described counterbore (221).
Reactor for compressed air purification system the most according to claim 1, it is characterised in that: at described cylinder (1) it is provided with two and journal stirrup (8) is installed.
CN201610834730.0A 2016-09-20 2016-09-20 Reactor for compressed air purification system Pending CN106268536A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108816039A (en) * 2018-06-05 2018-11-16 重庆鲍斯可燃气工程有限公司 Catalytic reactor for compressed air purification system
CN109663545A (en) * 2018-12-24 2019-04-23 大连理工大学 A kind of big flux heat exchange fixed bed reactors of winding tubular type

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5182086A (en) * 1986-04-30 1993-01-26 Henderson Charles A Oil vapor extraction system
EP1504806A2 (en) * 2003-08-08 2005-02-09 Columbus Filter GmbH Gas purification device
US7033549B1 (en) * 1999-04-16 2006-04-25 Volvo Lastvagnar Ab Air compression arrangement for vehicles
CN101206144A (en) * 2007-12-20 2008-06-25 吴加伦 High pressure thermojunction of gasification furnace
CN201807276U (en) * 2010-10-18 2011-04-27 黄应力 Simple drier of compressed air
KR20130120595A (en) * 2012-04-26 2013-11-05 한국에어로(주) Apparatus for eliminating oil of compressed air
CN204395649U (en) * 2014-12-19 2015-06-17 青岛金海诺交通装备有限公司 Energy-conservation single-cylinder type compressed air cleaner
CN105347343A (en) * 2015-11-18 2016-02-24 聊城鲁西聚碳酸酯有限公司 Phosgene production device and method

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5182086A (en) * 1986-04-30 1993-01-26 Henderson Charles A Oil vapor extraction system
US7033549B1 (en) * 1999-04-16 2006-04-25 Volvo Lastvagnar Ab Air compression arrangement for vehicles
EP1504806A2 (en) * 2003-08-08 2005-02-09 Columbus Filter GmbH Gas purification device
CN101206144A (en) * 2007-12-20 2008-06-25 吴加伦 High pressure thermojunction of gasification furnace
CN201807276U (en) * 2010-10-18 2011-04-27 黄应力 Simple drier of compressed air
KR20130120595A (en) * 2012-04-26 2013-11-05 한국에어로(주) Apparatus for eliminating oil of compressed air
CN204395649U (en) * 2014-12-19 2015-06-17 青岛金海诺交通装备有限公司 Energy-conservation single-cylinder type compressed air cleaner
CN105347343A (en) * 2015-11-18 2016-02-24 聊城鲁西聚碳酸酯有限公司 Phosgene production device and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108816039A (en) * 2018-06-05 2018-11-16 重庆鲍斯可燃气工程有限公司 Catalytic reactor for compressed air purification system
CN109663545A (en) * 2018-12-24 2019-04-23 大连理工大学 A kind of big flux heat exchange fixed bed reactors of winding tubular type

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